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Home My WebLink AboutDAQ-2024-0104711 DAQC-963-24 Site ID 10676 (B4) MEMORANDUM TO: STACK TEST FILE – HOLCIM – Utelite Plant THROUGH: Harold Burge, Major Source Compliance Section Manager FROM: Robert Sirrine, Environmental Scientist DATE: September 24, 2024 SUBJECT: Contact: Carsten Mortensen (801-467-2800) Contractor: TETCO Location: SR 32 West of Rockport Reservoir, Summit County, Utah Source: Kiln #1 and #3 FRS Site ID #: UT0000004904300001 Permit #: 4300001004 dated May 24, 2023, revised May 24, 2023 Action Code: 3A Subject: Review of Stack Test Reports received August 9, 2024 On August 9, 2024, the Utah Division of Air Quality (DAQ) received test reports for the Holcim – Utelite Kilns #1 and #3. Testing was performed on July 10, 2024, to demonstrate compliance with the PM10 emission limits found in Permit Conditions II.B.2.a, and II.B.3.a. The DAQ-calculated test results are: Source Test Date RM/Pollutant DAQ Result Source Result Limit Kiln #1 7/10-11/24 201A/PM10 0.585 lbs/hr 0.58 lbs/hr 3.34 lbs/hr 0.006 gr/dscf 0.006 gr/dscf 0.024 gr/dscf Kiln #3 7/10-11/24 201A/PM10 0.74 lbs/hr 0.74 lbs/hr 3.34 lbs/hr 0.006 gr/dscf 0.006 gr/dscf 0.024 gr/dscf DEVIATIONS: None noted. CONCLUSION: The stack testing reports should be considered acceptable. Measured emissions appeared to be within limits at the time of testing. RECOMMENDATION: Holcim – Utelite Plant Kilns #1 and #3 should be considered to have been in compliance with the PM10 emission limits at the time of testing. HPV: No. ATTACHMENT: Stack testing reports for Kilns #1 and #3 received August 9, 2024 DAQ generated excel spreadsheets g!1 HoLcrM August 8,2024 Mr. Harold Burge Utah Division of Air Quality 195 North 1950 West P.O. Box 144820 salt Lake city, UT 84114-4820 UTAH DEPARTMENT OF ENVIRONMENTAL QUALITY AUG - rq '.:t)4 land deti,lued DIVISION OF AIH OIJAI !T" RE: Stack Test, No. 1 Bag House, Title V Operating Permit No. 4300001004 Dear Mr. Burge Enclosed is a copy of the PMro Particulate Compliance Test, conducted in accordance with sections ll.B.2.a.loftheOperatingPermit. TestingwasdoneattheHolcim,UtelitePlantonJulyl0&Ju|y1.1.,2024. I certify that; a) Testing was conducted while the source was operating at the rate and or conditions required b) by the approval order, operating permit or federal regulations. During testing, the source combusted fuels, used raw materials, and maintained process conditions that represented normal operations and was operated under other relevant conditions specified by the Executive Secretary. Based on information and belief formed after reasonable inquiry, to the best of my knowledge the information found in the report is true, accurate and complete. c) lf you have any questions, please call. Operations Manager Holcim-US, Utelite Plant Holcim US, 6375 W Three Mile Canyon Road, Phone 801 -467 -2800, www. holcim-us. com Coalville, UT 84017 I I T T T T T T T I I T T -]]fi[bTpARTMENT oF erlviiouuglrnu ounUT AUG - I 2024 DIVISION OF AIR OUALITY PMIO PARTICULATE COMPLIANCE TEST CONDUCTED FOR UTELITE CORPORAI"ION KILN #I BAGHOUSE July l0-l1,2024 by: TETCO 391 East 620 South American Fork, UT 84003 Phone:801 492-9106 Fax:801 492-9107 I Frepared for: I ffi[:::rporation I Coalville, UT 84017 I r,r;i;"ffi" T T CERTIFICATION OF REPORT INTEGRITY Technical Emissions Testing Company (TETCO) certifies that this report represents the truth as well as can be derived by the methods employed. Every effort was made to obtain accurate and representative data and to comply with procedures set forth in the Federal Register. Michael McNamara Reviewer: Date: Dean. Kitchen Reviewer: Date: T I T TABLE OF CONTENTS Perge Introduction Test Purpose.............. ......,..........1 Test l,ocation. 1'ype of Process. ...................1 Test Dates ............. "..1 Pollutants Tested....... .................1 Test Participants........ .................1 Methods Applied..... ................... i Principle of EPA Method 2014........ ...........2 Discussion of Errors or lrregularities.......... ...................2 Quality Assurance. .....................2 Summary of Results Emission Results...... ..................1 Process Data.......... .....................3 Allowable Emissions ................._j Dcscription of Collected Samples. ...............3 Cyclone Cut Rate and Isokinetics............ ......................:i Sourcc Operation I)rocess Clontrol Devices Operation .............-5 Process Representativeness..... .....................5 Sampling and Analysis Procedures Sarnpling Port Location............. ..................6 Sampling Point Location........... ...................(r Sanrpling Train Description .......6 Sampling and Analytical Procedures........,.. ..................7 Quality Assurance ......................7 Appendices A: Complete Results and Sample CalculationsB: Raw Field Data C: Laboratory Data and Chain of CustodyD: Facility Schematic Representation. Production ar-rd Control Equipment DataE: Calibration Procedures and ResultsF: Related Correspondence T T ! I I T T I ! llt T I Table I II III IV Irigure t,IST OF ]-ABLES Paqe Measured PMro Emissions......... ........................3 Cyclone Cut Rate and Isokinetics............ ..........4 Sample Point Location............ .........6 Complete Results Appenclix A LIST OF- FIGURES Schematic Representation of Facility ................./\ppendix t) Schematic of Method 201A1202 Sanipling T'rain......... ....... Appt:ndix E t T I T T T I I T T I I I I I I I I T INTRODUCTION Test Purpose This test was conducted to determine the PMro particulate emissions from the baghouse serving Kiln # l. Emissions are expressed in grains per dry standard cubic foot and pounds per hour. The results are used to determine compliance with the facility Title V Operating Permit, Permit No. 4300001004. Test Location. Tvpe of Process The facility is located south of Wanship, Utah. The process consists of firing calcine shale as it passes through a rotary drum and expands to a less dense material. The expanded material is used in the construction industry as a lightweight aggregate. A schematic of representation of the Kiln #l exhaust stack is given as Figure I in Appendix D. Test Dates Three test runs were completed July l0-11, 2024. Pollutants Tested The tests were a gravimetric determination of PMro particulate in accordance with EPA Method20lA and202 found in 40 CFR 51 Appendix M. Method 202 for condensable particulate matter (CPM) is for informational purposes and not for compliance. Test Participants Test Facility State Agency TETCO Alex Judd Robert Sirrine Mike McNamara Dave Vernon Xaun Dang Jerimiah Opthof Methods Applied EPA Methods 201,4' and202 were used for each of the tests. T T I Princirral of EPA Method 201A A gas sample is extracted at a constant flow rate through an in-stack sizing device. which separates particulate matter (PM) greater than PMro from particulate nlatter lcss than PMro. Variations fiom sampling conditions are maintained within well delrned limits. 'fhe particulate mass is detenrrined gravirnetrically after removal of uncombined water. A schematic of the sampling train is given as Figure 2 in Appendix E. Discussion of Errors of Irregularities There were no errors or irregularities. Quality Assurance 1'esting procedurcs and sample recovery techniques were according to those outlined in the Federal Register and the Quulity, Assuruncc lTundfuxtk.for Air Pollution lvlcusurcmerrt Sv.stcm.t'. I I T T T t I I I I T T t T I I T t I T I T T T t t T t T T t SUMMARY OF RESULTS Emission Results l'able I presents the compliance test results. P-rocess D_eta The process was operated according to standard procedures. All pertinent process data was available lbr recording by agency personnel. Baghouse AP readings are included on the daily log sheet fbr Kiln # l. in Appendix D. Allowable Emissions The allowable PMro concentration for this source is 0.024 grldscf. The allowable PMrg emission rate for the Kiln # I Baghouse is 3.34 lb/hr. Description of Collected Samples The sample filters for all three test runs were lightly discolored with gray colorcd particLrlate. The front washes were all clear in appearance. Cvclone Cut Rate and Isokinetics The Federal Register specifies that tests for PMro using EPA Method 20lA shall either not exceed +1p of 10p and the measured flow rates (AP's) shall not exceed the calculated Ap -) TABLE I Measured PMro Emissions 0.0062 0.00ss 0.00s5 I I T T T I I T I T I I t I T t T T T maximum or AP minimum, or one AP may exceed the AP tnaximum or rninimum if the isokinetics remain within +20oh of 100%. The cyclone cut rates. isokinetics. and number of AP's which exceeded the allowable range arc shown in Table Il. TABLE II Cut Rate and Isokinetics Run ##pts <APnrin or )APnra. 1 2 J 0 0 0 % lsokinetic 9.96 10.13 9.91 t07 103 107 SOURCE OPE,RATION Process Control Devices Operation All process control devices were operated nonnally. Baghouse AP readings are found on the daily log sheet for Kiln #l in Appendix D. Process Rerrresentativeness Tlic facility was operated normally. Production data is found in Appendix D. I T I T I I T I I I I T I I T I I T I SAMPLING AND ANALYSIS PROCEDURES Samplinq Port Location The stack inside diarneter is 47 inches. Poft location is depicted in Figure l. 1-he ports arc iocatcd I 1.5 dianteters (45 feet) downstrearn fiom the last disturbancc and 8.4 diarrieters (ii tect) upstream fiom the next distllrbancc. There are two samplc ports with inside diameters ol sir inches. Samrrling Point Location 'fable Ill shows the sarnpling point distance from the insiclc wall according to Fil'}A Method l. Each point is markecl and identified with a glass tapc wrapping and numbered. l'hersc lroints arc determined by measr"rring the distance liom the inside wall ancl adding the rclerencc (port) measurement. TABLE III Sam Point Location Distance (inches) fiom lnside Wall I 2 -) ,|t 5 6 2.07 6.ti6 13.91 33.0e 40.11 44.93 Samnling Train Description 'fo determine the actual emission rates fbr this stack, 40 CFR 51, Appendix M. and202 were fbllowed. All sampling trains were made of inert materials, (i.e., Teflon. Stainlc'ss Steel. prevenl intcrfcrence of the sampled gas and particulate. l'hc stack analyzer used to conducl Methods 20lA and202 is constructccl to ntcet tlre T t specifications outlined in the CFR. The temperature sensors are K-type thennocouples. Heater. vacuum and pitot line connections have been designed to be interchangeable with all units used by the tester. The probe liner was of Teflon. A sarnpling train sketch is found in Figure 2 in Appendix E. Sample boxes were prepared fbr testing by fbllowing the prescribed procedure outlinecl in Method 201A and202. Samnling and Analvtical Procedures All test sampling and analytical procedures employed were as specified in 40 CFR 60 Appendix A and 40 CFR 5l Appendix M. Qualitl' Assurance All equipment set-up, sampling procedures, sample rccovery and equipment calihrations werc carried out according to the procedures specified in 40 CFR 60,40 CFR 5l and the Quulitv Assurunce Handbook./or Air Pollulion Meus'urentent Syslems. I T I T I T I T t t t t T T I T I I t I I I APPENDIX Complete Results and Sample Calculations Raw Field Data Laboratory Data and Chain of Custody Facility Schematic Representation, Production and Control Equipment Data Calibration Procedures and Results Re lated Correspondence APPENDIX A Complete Results Nomenclature Sample Equations A cr tnl tn T t I I T T t t T I T T I t T I I I I TNBI,II IV COMPI-EII: RtrStJl.TS PM r(, PnRTtC'UI-A-rE MA rrEIt KIt,N I BNCHOI.JSF- Synrbol Date []rlter # llcgin I:nd Irb,, ,\l.l Vrn '1 ," Ahead b, ,,np,, ./,11r,.n.,,,.,, ,/.^t, lr ('f I)u ('or o: N. & ('o Vttt.,j Ilw. xd M,i M. '%t lt QsS't Qst i'c' Nrc (' l).,, l)t" C'r I)io- r 7. T PC lrhn lr. () 4,, Mpu r,,, Mrrr,,,,, M.,ru, CPM t,,,, Crpul,,,,, C..rn, FiRp1111,11 1..:R>pM l0 (l [:R"r,n Dolc _llnle Tesr Bc!]m l irnc'l lsl t-nd.'d Mctcr BrronLlnc Pressurc Orficc Prcssurc Drop lvlcrer ( i|bralroil \' ,:iclor Volumc 6as Sxmpled--Meler Condrtors A\:j l\4clcr'fernperJturc Arc r\r(:x lllocled b\ Srnrple I ranr Sric[ ( ros5 Ssrtrnrxl Arcx Probc Bk)ckgc fnclur li,r I'Ml 5 Sq Roor Velocrt\ ltcssure ( orerdd for hl' Sq Ro(!l V.lftll\ Hcad ( r\ rnsurcd) Sq R(xn Vclocrt\ llcad (adt lor blocltrlc rl'il('ccrsi^ ) WcIlhr \Villcr (i)llt'.lcd Durxlkil r)l Tr\l Pilot lirbc ( ocllicrcnr No//le Drinlcrer volumc ", ( irlrn Dro\rdc Volunlc ". ()\\gcn Volunrc'1, Nrlrogcn Md ( arhon Mrrno\rde voluilc C$ Simplcd (Slindxrd) Volunc Wnler Vanor I racl(n H.,O rn Stxcl Cs F'ractron of Dn Cas Molccular WI Dn Cas ivolccular Wt Slacl Cas Pcrccnl lsoknclrc (;N slrcxnr viscosit\ D^ Cns SnmDlc Rile Srnrp[rU liale Reynolds Ntrmbcr ( unrilllhanl ( orrcetron tncktr , PM: 5 P['ll0(ull'ornt PN'll i (il |,otril. (ondrlrt,n llurll lr Re'-cstrnratcd ( unnnrlilanr ( orr*tron ljJckrr PMI s ( u1 Pod ( ondilron Burll ln Rrlrool D5l)/DslLl (0,99<Z< l.0l) r\rlj Strcl Tcmpcraturc Strcl ( ros\ Scclrontl Arca slrcl Slatc Prcssure Simpl(' Pon lJaftrmctrrc Pr6surc Strcl Prcs\urc StacL Cas Vollnrcrrc lrlotr Rile lStd) i\{'csurrd Stacl (;a$ Volurclnc l_lo\ Rate {Aclual} Mcsurr'd velGtt\ ol'Slucl Cs Meourcd MGs ol P\'llll.(, l,r(tculalc Viss ol >PM I r) ll I'arlrculilc Mrss ol-(ondensrbles Concenlrauon ofl,M lt) l) Pilruculntc ('oilccnlrot,on ol >PMI0 o Parlrculxlc ( onccn[alron ol Condcnsrbles HmrslroD Ralc ol'PM I () ll Ptnrculale Emrssiur Rile o[>PM lo {r Pantculatc [:mrssroil Rale of( ondulsrbles Dintensions Run # I Run #2 &I]-{J 1n0t2024 7/t v2024 7fi l/2024rtq0 49 t 4q?i4:40 8:15 t)..15 15:41 9:16 10:48 Description ln llg Abs ln Il.o drntcnstonles! 24.10 0.-16() 0.994 25 26.1 99.1 17.(x) t7-14.e 0.009tt 0 4869 ().4{i2 t 0482t (r3.7 60.25 0.713 0.21 5() 6.70 ll.l() 80.t0 t9. I l9 3.004 0. |.16 0.864 29 60 28.02 106 7 220.t 0.3 r7 0.64ti 2288.6 Ll()8 9.96 L39 l.l t3 2.39 0 99tt '7.7 2.0 50.8 0.0062 0 00t6 0.04 r0 0,6-j-1 0.1 64 4.1 75 24.05 0 360 0.994 23 277 li6.-l 17 00 173.1.(, 0.()()9li 0.49t7 0.4889 0.4lill9 6.i.6 58 75 {t.769 0.1150 650 I -r. l0 80.40 17.994 2 999 0. l4-1 0.8-s 7 19.5() ?7 91 roi 2 220 7 0.306 0.616 2212.4 L r09 10. 13 2.47 r.lll 147 0.q99 24.05 0 160 ().994 25.-+26 96..1 17.(x) t7i{ q 0.(x)efi 0..l8lt.l 0.t836 ()..tt{-16 67.Ii 61.00 0.77 3 0.2.150 l). i0 12.n0 80.70 t9.302 .i. t 97 0. lrl2 0.85tt 29 55 ?7 91 I07.;l l2 I ..1 0.:i I6 0 65q 2277.7 1 il0 9.9 t 2..ttt 1 il5 2 lli () 99[i Root ln ll,0 Rool lD ll,o R1)oi l[ ll.0 Granl" lUrnulcs Drlrensronlesr lnchr'r Pcrrrnt Pcrcurl l,cracnt dscl 5cl- F-rJCnoo [:rncton lb/lhnx)l lh,lbrnol l'erc$l tnltroDotsc dsclrl Drm(.N!onl!'ss f)rDrcnsronlcss Sq Ft hr HrO ln Hg Abs ln llg ,\bs dsclin clrrr lpnl millrgmms nrlLgranrs nrllrBrtrilrs tr, dscl gr / dscl' rr i dscl' lb/hr lb/hr tb,,hr .,\ \/(; 2118.2 293.1 29(r.5 2t)2-B r2.018 I2.048 I? 04n-0.220 -0.120 -{t 220 24.04 21.99 23.9e 24 024 23 971 23 e71 l.l9Er'01 l.l9l:+()4 l.lltlr+().1 l.llltl+0{ 2.4-1t'.+04 2.471:+04 l.46lt+04 2.{58+0.1 2.01E+01 ?.()sFr0l 2.()41:+0-l 2.0JU+03 6..1 ?2 62.7 0 0055 0.00 t 9 0.0538 0.558 0.192 5.464 (r.9 2t 5li ;t 0.005-s 0.0057 0.00 | 7 0.0017 0.0467 0.0{71 0 5.i7 0.5tt25 0. t6q 0.t752 1.7 13 4.7812 t T Method 20lA 1202 Nomenclature percent isokinetic stack cross-sectional area (li'') see r/aP runit heat value (British thennal unit) 'liaction of watcr in stack gas concentration ol condensibles ( grain/dscf) concentration of coarse part icLrlate ( gr/dsc t) percent cart'ron dioxide in the stack gas pitot tube coefficient (0.84) concentration of PM r0 particLllale (gr/dscl) equivalent stack diameter (inches) oril'ice pressure drop (inclrcs I IlO) olillce pressure (inches l{,O) oril'ice pressurc head (inclres H,O) needed lbr cl,ckrnc florv rate nozzle d iameter ( i nches) stack flolv pressure diffbrential (inches H20) -50o,'o effective cutofT diarnetcr of parlicle ( pr) dianreter of the stack (t'eet) pcrcent excess air ernissiorr rate ol condensibles (lb/hr) emission rate olcoarse palticulate (lb/hr) ernission rate per rnrnBtu or torr of tuel etc. ernissiorr rate of PM ',, particulate (lbrhr) emission rate of compound which replaces x lengtli of rectangular stack (inches) thor,rsand [Jtu rnass of condensibles (mi I I i grarns) rnass of coarse particulate (rnilligrarns) nrolecular weight of stack gas. dry basis (lbilb-nrol) rnillion Btu rnass ol PM,o particulate (milligrarns) rnolectrlar weight of stack gas, wet basis (lb/lb-nrol) gas viscosily ( rnicropoisc) t 9,bt .. A' -' ASAP Btu - B*"= C.p'u - L.,,rt COr = (',, t'\ t'\lI0 D.,, AII .\l l.^. , \lld , [),, lP= DPs. '= D. '- t,A =' Fir.n,, El'.u,, -= 8R,,,,,,8,, ERprr Io - ERr : L- nrBtu '' M.n,,,l = M.,,,t =' Ma= mnrBtu '= Mlvro - M,- Its -- T t T T t t T T I T t M*",,, ,- rnolecular rveight ol'gas species (lbilh-rnol ) N, - percent nitrogen in tlre stack gas O, " percent oxygen in the stack gas VAP - average of the square roots o1-,AP (rnay also be referred to as ASAP) {APr : squarc root of AP at point I o1'the clrrrent test. Method 20lA ./AP,' .= square root of AP at point I of the previor-rs traverse, Method 20 lA {AP',,,.. = averoge of the square roots of AP fiorn the previous traverse. Method 20 lA Pb,, =- absolute lraronretric pressure at the dr1 gas rneter (inches Hg) Pbn - absolute barornetric pressure at the sample location (inches Flg) P., - stack static pressure (inches I-l.O) P, : absolute stack pressure (inches Hg) P,,,, - absolute pressure at standard conditions \29.92 inches Hg.) pls = number of'traverse points during the test (rninimum of 6. maximum ol' l2)0 - time of test (rrrinr,rtes) T I T I T T T T 0r : 0,, = Q,: Q,: Q,. : Qr.' -- Q* '= R*0" : Il,ni,, : T,,, : T'= T.ra = Tr .= Vm= Vfflrr.t -= Vn,iu = w= W1'u. -- X,r = Method 20lA 1202 Nomenclature sample time (duration in minutes) at first sample point for Method 20lA sample time (duration in minutes) at sample point "n" fbr Method 20lA stack gas volumetric flow rate (acfm) stack gas volumetric flow rate (dscfm) actual gas flow rate through the cyclone (acfm) predicted actual gas flow rate through the cyclone (acfin) wet stack gas std. volunretric flow (ftr/nrin" wscfin) multiplier for V,, mr-rltiplier tbr V,, meter temperature (oF) stack temperature ("F) absolute ternperature at standard conditions (528'R) see 0 sarnple volurne (ft3) at meter conditions volume standard (dscf), sarnple volume adj usted to 68"F and 29 .92 inches l'lg. nraximum allowed nozzle velocity (fps) rninimum allowed nozzle velocity (fps) target nozzle velocity (fps) velocity of stack gas (fpm) volume water vapor (scfl at 68"F and 29.92 inches Hg. width of rectangular stack (inches) weight of the condensed water collected (grams) liaction of dry gas rneter cal ibration Y-factor (di nrension less ) t T T T Method 20lA 1202 Sample Equations 7ol : Vtn.,6'(T, + 460)' 1039 / (0'V.' P,'Xl' D,r) 4. : lDsr I 4). n B*, = V* / (Vm.,,' +V*) C.pr, - M.pr.0.0 1543/Vmr14 C"ur. = M.,,r,. 0.01543 /Vmr,,1 Cpr,rrt, -- Mu1r,r, .0.01543 / Vm.1,1 D"n = 2.L.Wi (L+W) AHd = [Q,.',. Xd. P./(T, +460)]2. [(Tn, + 460) - M.r. 1.083. AH(,,,/ Pb,,,] Dpio -, 0.15625 . [(T, * 460) / (M- . P.)]t"0"' . (p, / Q,.)"'nn' Ap,u., : 1.3686. l0-4. P,. M.. Vn,,"2 / [(T,+460). cpr] Ap,,,,, = 1.3686. l0-1. P,. M.. vn,iul / [(T. + 460). Cp2] EA =. (9/oor - 0.5 %CO) 1t0.264 %Nr - (%Or - 0.5 %CO)l Er.p,,, = C.r,n,. Qr. 0.00857 [JI'.,-r, : C.,,* . Q, .0.00857 FlRn,n,131,, = ER/(rnrnBtu /hr) ERpn,', ' CuM|o. Q-. 0.00857 M4 : CO3 .0.44 + Or . 0.32 + N, .0.28 M, == (Mu . Xu) + ( 18 . B*,) lk .- [51.05 + 0.207. (]',-r 460)+ 3.24-10'5. (T, -r460): + 0.53147 -o/oO:-74.143 P. - P['r,,+(PG/13.6) 0, = 1rilP,'/./AP'.".;. (0,"., i pts) Qn = V,'A, 0,, : 0r . r/AP,, /./APl Q, ' Qo . X,r . P,. Tuo / [(T, + 460)' P.rd] Q.. - [(T',+460). P,r.r/(Tuu. P,)] . [(Vrnu6 + V*)/e] Q..' = p, . 0.002837 . [(Tr +460) / (M. . P.)]n t"'" Q,, = Q./Xa R,,u, = 0.4457 + i[0.-soso + (0.2603 . {Q,.' . 1., / V,,' ')] R,,i,, : 0.2457 + ![0.:OZZ - (0.2603 . iQ*"' . pr, / V,,r 5;1 V,uo, - Vr.Rn,u* V,n,u - V',' Rr,i,, Vr.r'r,,,1 = Vrn.Y. T,td .(Pb,,,+ AH / 13.6)/[P"0.(T,,,+ 460)] V, : 3.056 . Q..'/ Dn2 v, =- 85.49 . 60 . Cp. ilP . { 11t, + 460) / (P.. M-)l V* = Wt*..0.0471-5 X6 = l-B*. T I I I I T t . B*,.i . l0'' I I I I T I t T I I APPENDIX B Preliminary Velocity Traverse and Sampling Point Location Data Particulate Field Data Sheets Preliminary Facility Utelite co Stack ldentification Kiln #l Baghouse Exhaust Barometric Pressure Estimated Moisture (Bw") l0 N Sample Heighr from Ground 60 feet N Stack Dia. 47" Ports arc 33' ,,onr rra--F- Reference: 6" Upstream from next disturbance I)ownstream from last disturbance Comments: Averages: TS AP Z Flow Ts ZFlow AP Traverse Point Percent Diameter Distance From: A r-E . PoI--rrtsfl---rlElFIDReference 44 2.07 8.07 2 14.6 6.86 12.86 -ta,.,lj J 29.6 I3.9r 19.91 i$c.: 4 70.4 33.09 39.09 ;8(; : ") 5 8s.4 40.14 46.14 |,b 6 95.6 44.93 50.93 KEY:> oE^ .= [ ;=vdPo r o >FOG =6Eoo"oo ) cEooo- o GOo- . .= 6 o Yo e<c> '= - 6a c-co. . () : -E.E c Fl 0)o tl i oNIo_oEt- 6o_ c=o_E(J E!aI!sEoEooo-,r ,$ar IIIII io l 3 lcld cO D P .E € -EL6 '. : t-lul==t t r- l I =l iq l -l -l ZI E^gAL TI=T. I FC)o IIIIII _tol fl(s l . Clxl LU I rlal .. flol -c lol (0 l co lEIYlE:u: iO /oqEC TTTaC 9l6tolol =lol5l IIlu s T; t uE f f : ll =, = = o n ii ; l l u' | | :! i] :l ll , l ; i l l , L I $+ 5- Q ) E: s : E 3 t e- i E .E . q + - f o x uv > i ' EI s -{ 3 t< Olo I c.l . EI !,: . l a -- l u n "l < 2' l sl e =l E lLl5 ,1 , "1 , ' l ; l= o lo o lu d Ill t r , I= E q | ;y & otr - . 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Lo-E9>oI (o l (o -l * gg92oo&r IIlI -l-l fO o'-IetoLi-+E,! oF cq I r+ l |r ) s (o N APPENDIX C Sample Recovery Particulate Analysis Condensible Particulate Matter Analysis Gas Analysis Data (ORSAT) Chain of Custody C ['ac i I ity Stack Idcrrti licaliotr Kiln # I)atc: Mctiurd:20 tn /202 tllflIcElt$ Itiltcr Nunrber: Irinal tgt Inirial rgl Nct rgi -our-lLitcdcsllCIlien Purgc stirrl l)rrrsc crtd+ ml I I-0 addctl Srrtttltlc [],rx lmninger Numfrer lnitiuls Inilral Volrunc of lrqrrrrl (I l;O) rn wcigh and tliscnrd T T T T T T T T t T I I T T T t T I I t}utt-i\liltts lrihcl Nuntbcr: Sarnplc lhx I)rlr[c stirrl Pur!.c cnd rll I 1"0 addccl Imoinger Numbcr Initial Volrrrnc ollrqrrid (l lr()) in irrrlingers. trnl) I nitialr I lcxnnc rvcigh & arrall'zc ucigh arttl disc ntPt}('I.RS lriltcr Nrrnrbcr: I:inal tg) lrritial rgr t.\ct (gt nrn llltcr dcscrintiorr I)rrl1lc starl S:rnrplc llor lmninser Number I nili:rh nrl I I.0 acldcd 490 I I I t I T T t I T I I T T I T T t t Facilitl: Stack ltlcnti licatiort : lriltcr Nunrbcr': Urelite Rinse Vol. I'iltcr & I)M|,6 > l)lvlr,, [)atc: l lll)1202.1 Ilrrrr: Sanrplc Bor: nrl nrl Kilrt # I Blanks & Rinses Filter > PMro Wash n cctonc lJlank ('orrcction 0.(XXXX) g/ I 0()rr I 60.8792 0.12 r7 0.1215 s b b I 2() 2() ( til'lljRIn liinull: Irinai.: [;irral,111;: 0.1 2 1 (r g l)rilveight: 0. I I67 g Nct 0.(X)49 ! Net 4.9 mg [:inal,111;: 60.li820 g lnitial,ryl;: frtl*;,lZ g (iloss: 0.002[l !r lllank: 0.000t) g Nct 0.0028 Net 2.8 F-irral,ry6: 60.7626 g lnitialor,,;: (r0.7606 g (iross: 0.0020 []lartk: 0.0000 Nct Nel I'M,,, 0.0020 .1.9 n1g 2.tl nr_q ---Jt--^e I)atc: ill6/2024 'l intc: l)nt.,-7i?DIIJ- tinrc: t)rrtc: 7/16/2024 .l irnc: ll:(X) t)r,.,-7ilDIIt ti,,'.,-tJJtr,- [)atc: Ill1612l\)3 'l irnc: Dut.,ll7l?DDl- t i,nc: Datc: 7l1612(124 l inrc: ti:0() l),,t.'lTEEEi- 1i,,,", l+'l)rt I)N{ (lnlirlnration Onll ) t,L,,lr, 7.7 ntlt t'M,,, f.0 rlt!: Total 9,7 nrg l)irt,:: 7/ l-j/2-l l)rrrc: 7ll6124 PM11y Wash l:inirl ,: l)itral": lnitial,: I n itia ll: llcakcr N unrhcr: 60.88 t9 60.8820 (r0.8'792 E mg Final ,: l'inal.: I nitiirl , : lnit ial,: 60.7624 60.7628 60.760,1 c b mg (r0.7608 llcakcr N tlttbcr: BESULTS l:rlter (Ivl ) I)N4r,, Wilsh (M,) Total I-ab l'cchnrcrau: MikclVlcNarnala l.ah l-cchnrcian l)can Kitchcn l,J:(X) 4.2 1J 75 t I I I I I I I I I T T I I t t I t T I:lcilitr': LJtelite [)ate: l ll I120?1 llrrrr: ) Sarnplc llor: l-) Stlck lrlcrrtillcation: Kiln # I l:iltcr Nurnbcr 491 BIanks & Rinses Filter FM11, Wash > PMro Wash Acct()nc Illank C'orrection 0.0000() gi l(X)nrl Rinsc Vol. lriltcr'& ['M,,, -ltt ' l)Nl !, ().1 t99 g Finally,;: g Prcwcight: 0. I lgti s 0.1 156 c Nct 0.(X)-12 !r Nct il.2 mg 62.5277 --]0 nrl rnI [ , lrllll2l\ ilt_______:i_'" ____r lrinal,: l:inal.:0.I t97 I:inul,: ltinll": lnitial,: Initia l1: ltirral 1: l'inal.: lrritial,: Initial.: 62.52'76 b Final.r1.,: 62.5277 g Initial.ry,,: (r2.5255 g ( iloss: 0.0()22 U Illank: 0.0000 g Nct 0.(X)22 tr Net 2.2 nrg lrinal,lyl;: 62.054tt g lnilialn"l;: 62.0526 g (iross: 0.0022 !r Lllank: 0.0000 g Nct _0.9922_8 Net 2.2 nrg PM,,, l)atc: 7/ 16i202.1 'l irnc: lt:00t)"t.,li6EIlI- 1i,,,., l-l'o,t [)atc: I lll612023 'l inrc: I),,t"'lTTilDDf tir,c: t>atc: 7/1612021 l inrc: lt:(X) D,,t"'-7fir2EJ- 1 i,,,.,-lJil- [)M 1 I nlirnnatiorr ( )rrly') 62.525,t 62.5256 Ilcakcr Nurlhc:r': 62.0548 (r2.054ti s62.052'l 62.0525 Bcirker Nunrbcr: RESULTS l tltcr(Mr) I'M,,, Wash (M,) Total 2.2 6.4 ntg nl8 mg lrM,,, l'M,,, 'I otel Mikc McNanrara [-rh lcchnician: Dean Kitchcn 6.4 nlg n1g ntg 11 li.6 7ll612.l lo 4{) mg -3"0 I I T I T I T T t I T T I T I T T T T l:acil it1': Stack ldcntillcation: [:ilter Nunrbcr: [Jtelite l)alc: 7ll I l2n4 l{urr: -_ -j Sarrplc llor: Il Kilrr # I Blanks & Rinses Filter , PM,,, Wash l;inall: l:irra l.: 492 Acct()nc lllank ('orrcctron 0.0(XX)0 g/ l(X)rnl 57.78Ul 62.2047 0.1 I 12 (). il 12 u s s c c I-'inal.,,y6: l)rewcight: Rinsc Vol. l:iltcr & I)N4,,, .. l,N4r,, rnI rnI PM,1, Wash l;inirl,: lti nrtl": Initiirl,: I rritial,: lJcakcl Nrrnrhcr 5 7.7 ri06 Nct (0.0010) g Net (.].0) mg l:irral-ru.,;: 57.7806 B lnitialny,,;: 51 .7707 g (irrss: 0.(X)99 I lllank: 0.0000 g Nct _ 0.9099_ S Net 9.9 mg l-'inal.nu,1;: 62.2068 g Ini{ial,rr,,: 62.201'l g (iross: 0.(X)2 I Illank: ().()000 N"t -lfoou t Net 2.1 PM,,, nlg nr8 mg Datc: '7/1612021 l inrt: I)nt.,-TIZDIJJ- tinre t)atc: 7/ l61202.1 l irnr:: ll:(X) t),rt.,-i,fiDll]- I i,,,,',--1.fiil- Datc: I ll1612()23 I inre : D,,t",ll7iJZIJ3- [ir,c: I)arc: 7il61102.1 'l'inrc: Dut.'1G.EEI- t i,r,:. I)M 1 Intirrrnation ()nlr') l'M1,, (r.9 ntt l>Mr , 2.1 tnq Total_!0 __ mg I)irte: .l5lli{J l)atc: .l-5.lti() 5 ,-.11011 57.7706 I'inal,: I- ina l": lrritirrl,: I n itia l.: 6).2069 62.206(r 62.20,17 Bcakcr NLtrnbcr: BESUTTS I-rltcr (Mr) l)Mf , Wosh (Mi) 'I'ota I 9.9 6.9 [.ab lcchnician. Mike McNurrtala I-uh lcchniciln. [)can Kitchcrr l.t:(X) -. I * t ll l , l I ,r , l cc I .i =l rl ' - tt . - tl - ud Eu=f,.=JEUcIil!CULCJ rJE.Zoz!*2.:€'aEEaL-uq6oo EIEL -:€-- i3)Uo3.!(,zgFC.CoCLU2a C EI\ oa octro il H E ;. E o.E-o=C ca <. c- t cc J al C? :tal coF- :f ,a{oor- . t+a{o'l \o :f ,c. l \o -+ol e1tr - -+claa=r- :t6l .. l -fat:\o 00r-r nal .. !N inra6I^i a. l (". . !N c' l Vt.!6l ra.lra1t Ui (\ Tui t €r *cle.l lta. l a. l tfi!t".1N 5a{clc. t cla. t alFI al ll ] ! 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L 2 _ od. d)E-.9(!scc==ij- : . €;c (,.9c01c =ao OI J d) OI .- c t € E, 3 , 8 CJ O - =E t r cc o or ) lr r "l - cl Scl. .2 ! .. ! * UU _ = =' = cE u E.9or ),ozCa ct i2Up:a= c0E2.L'cs.n ;C 5t )Eo-(,Uaa :tCIOrOJoa)=.. ;;co,!cu!o5a ... ; ')c- -! ,a)doO).J ,& )i6l6lq)z ITTITTtTIItTIIIItIT 1 1' F.a C) (do (,(!o sl=lGoE!"a()F )oJ.Joo6l:' :=O(! Ir .I6lC'2 TTTITTITTTITItTTTtI d)CiD.:o[,FJ 6dEZ2.o::.:.:s:oF-nJo.:t-fi3LI-ro lsga -, L -:€-: iooo'a )ao0id(,zut4)FEcOii0)oo- It=;'. =(!oEoEo6a Cd c0ooLc- \oE'1 -_;() 0)Foa :; l c=-- i0)d. o'Fao o; <f N oo sf, :f ,a. . l cor- - *j -€F- :f ,alct .i -N\o .?.Joor- :i 'a!oo -l-6lol +ol o\€r\ ooon.. i <falan ?ra JFI6l cncl (- I cl c. l ?a ) ra.l t\. 1 r- \o t- F- €t.lal o.Et .1al o\=(\ IN \o=talal 3=tatal raVJ!?al6l tfio FI :z6Loo0)d. E=6 OJ .EFq,o :; E tr j o*. oE'i(J(!o € t € '+ c. i =f,o.loaF- <tC.l oo=t- - $c!at $CI \o .tal ooa- :i l -aloo:lF- 'falol -. fal \o €6r\ r-.lal o\ c'. 1c\ 6rAnal ooal6t c. l c. l o\ ra6t .I o\ F- o.+alct ca$ctcl o\ .+qt\ €t'. -<fa. ici 6F-=f.!a{ €or-=e.!a. l th =a. t a.9o- .Eoo!()o-6(n (, .9U .>o:2 ,(n0) co oo b D o, -N E v a- c. t =E ' 6 E, E D = () o - -- E=a i r EE o ho b o or -o . l 5 s- bl ? 7 ' t , le . e B 0) 0 ) - -- ' a 6G o qJEo(nooLo.;C E.9oooE.=IrELts o-Uo=b,o :t t0)oco bJ ;; . . i -c l - E -- h I 3l s , B () ( ) - ?. > Eaa iio oJ ) c, 5J ) OI ) U v- c I Et u .1 0 .g ' , oo - ?? - i= = ' = 5'J -- ' .9or l OJz.;--Eoa b02. l,=oFa 31 3 l i CC 6Jo uGo (.)Eon)LJI.9oC)F-ocoJ CcCCOoa)=IIg-c()()F-od soEE.!1a tr=_:C) o.Foo ()CIc) I € 6l sfnt@a- -l.Ja'l \o $al 6iI() '?oo t- -uJL'1 =f ,c- clol aaCJct ?o ". 46l c.. t a. l r-clc. l a. l6l N aJ i' -f .! al o an ila)L! =*\vod. C)EFoL. l C)o1)o ?6 a. t wc\ l oor- .f ,GIa] ti -a. t \o (]qJo T\oa. l a.)F- c. lol \oc1c. l 6?oe.Ial r. lci oo\oo. l c. t FT?a ) a- l C. l Vt +. ! cl o E(. )OIad.U9&. =0) oE'i()o (, oo CI O .fc!oor- $alcl $c\ od t-*fr-6l cl r- a- r- 6r- oo t- - oot- - €Ir - c. lal cl nnc l .. 1 o na. t a. l a. l (\a- l c.lcl ola.l a.lN c'-oC)o-: zc0 +toJ ItL() :zOU c0 c0 br - a. i -E vv O l E, E = () o - }B E G6 r .- . - o Lr - !- > a) c t ) u. .< .< .: - .. t -a vv O I diUPE o > o( J _ ?? . e cd ( 6 E o, J d) = 5) EO^ 6 -: 66 Y 6 o- E d (d 2 = 6 3 2 J7 . z 6d / c -o s- = = 60 . ; .9 co 8 dUx6J=Z (JoF atal=rtCt;o.;o,q =C,o=oa )tr()(Jo.=u:i1':'6tr tro!q, lrr-. 1c. lo2- ITtTItTTTTTtITtTITI sl s l I 0ia uo (J?.=(qoc;'-O4)F-aJ COZoa-: i;Oo.a|_-cc6J .9-oGE,. 1(n =JC o\ -- - iC) 0) tr(. )- a)€O o O=f , OIe. l =rsoo=t- - atcloo-a- <ta\ .. l \o '$c. t \c OCcdIu-r =t o/JOF.c:Ea r-o\F- O9alc.. l atot \oa. l6l c. l6tal cl a l GI o. .l _, 3 6U!(f -c.2LL =-:o (fF0)o ()o6) & + a. l <rNoo=r- $a!@F- sf, (- . l ('l -c(- l a)c()(J =i-al F- . a. l (. ' . l t-otot t-a{al Ir -\o.1o. l r-at(\ 6l(\ l € r; cr (. l o o.T6d.(,(, -o \ (]d O=FO(€o OJCO 6 :l - O?c\ l sa. l ooF- =Ja. l oo-r- <i-ata.l \o a. . l \o O ota o.r- a! -l ^t € o\ lf a. l o c. . l al - o. l al olc{ t\N (.. l cj .' l (\ t ItaoLo7)o= ItoJ +.=dJdc.) co or ) cr J c, ,i -- { *- , -- a \ - l v, v 5 , PI ! I , t s c) 0 ) * -? = ;a i i o qJ aJ q. -- c l - = OJ , .l D .: I ' , (, ) ru - -? . 2 -= -= ' 7 o0 bn = cI l . a -a a6 y ? q? * q cC 2 = c € E. z * 2 d (6 / d 'o a' = = 6G . - UU U UI(B 0) Ir .(,bnq,LLJ6lalO2 IIItTITTITTTITtTTTt Plant Analytical Method FRYRITE Date 'l'est No. Cas Bag No. Anrbient Temp Operator Date Test No. Cas Bag No. Ambient Tenrp Operator Date Cas [lag 11s. --:-l-:l- Anrbient Ternp Operator Gas RUN Averagc Net Volunre I )J Actual Reeding Net Actual Reading Nrt Actuel Reading Nel CO, O, (Net is Actual 02 Reading Minus Actual lO. Readine). N2 (Net is 100 Minus Actual 02 Reading). ,..i1.1.',!ii.i : 1:; ' $:tj,#."I', Gas RUN Average Net Volunre 2 ,) Acturl Reading Net ,\ctual Rerdinc Nct ,\ctunl Rerding Nel CO, 0t Or (Net is Actual O1 Reading Minus Actual CO, Readins). N, (Net is 100 Minus Actual O. Reading).ffi ffi Gas RUN Averagc Net Volumc I 2 -) Actual Rcadins Net Actu{l Rcading Nc(Actual Reading Net CO, O2 (Net is Actual O, Reading Minus Actual 30, Reading). (. \2 (Net is 100 Minus {ctual O" Reading). *; aJ@ttalr:--,ii*.*ffi#:rii"ltI*4i&&!q;1,* CO is ntx meastrred. as it has thc same molecular rvciglrt as N1 a7)=oL) f.:-OJ o ()Gn LJ {: , : rT]tl '6(- )0) a=()C) (J() !c0 'cq.,o.a c0r3L'lJo4J oUNE -oo.c -! ioaoE 0. ) (J IrI,lrlllllrIlIl llItl trTT a0>, ?)0fr l5a ,u0)==aCJ -o=OJa4)d(_ ) .J -+)a-l,)U--I.-c!-rI(. ) -o!)cri .=62 .2() .CoJ]=CUFFo'o(Jo;C)C63E(J0.)c-Es= IIT1iIl -+ r- 6C ) L_l- . o. -i t L! =E6 .9 oU^ \a .lo { ^c , .l i ,. . - *€AvUFfE I F' l (Joz ra l e / A se u e x a H 0u o l a J t es u r 5 ry qc t u : ) tO S p : as u r u pu e t1 c 1 e 3 ug r 1 1 is u r U ?p tl r t e ) lo u e d o r d o s l )s u r N si l r n \ a l l ? au o l a l r v I es u r u T qr l e J o. H -i re l l l c wd I JA T I J ht r d *t qs E l A lu o r c as J u o qs P A A lu o u eu r c -t qs E A lu o J J cq 'i ) 'o J o( l6< -i 0. ) (s ! .t ()oa t?a. -i'. t ?t :- ' . '] .Y \-t i ''L:r Figure l. Facility Schematic Representation Production and Control Equipment Data APPE,NDIX D I ] l\ TI Ill Ill t T T t I T T I I T \11 a .. oc J 9- . LI - & l 6E n L L 1 - .a : a Y c x a *u - t s ., 0 ) ( J q o . - dE d a ( J i . - . o A9 = b H E E E oi: e o l u ES E r y , + V _ b == a : ! = > - c at J L q = , U _ = E. A E i 5 . Z F A = il - q i = o ! j z= c ,- G a :: .- e- o E U t 7 , F= 7 ] : E d i .= , Y = 9 E , - r i= ? A a 9r t r o J - ' ,i X o U oa Y J-Y' -' " E -n ! .|-- ) ,. . -q ; AgI >. -: : U II :: I ; !:;U ,, f 6 <) l' (- l ( g tlII / ttsI ,, r , 1 C) I hI J .d lml *lcl \l l EdEC) !a(,5 -tE( t' . , J ll r i -a - ) tr t bv )F{ JA \ (JoU()+- ) cF { T- f(. )srl E. 'orI IIll I I t T t I T t I T I I T T I I I T t UTELITE DAILY KILN REPORT 5:00 PM 6:00 PM 5:00 AM END OF END OF DAY SHIFT TONNAGE NIGHT SHIFT TONNAGE oares T rtr-'(i/ FEED TAN K RATE TPH BH DP GAS SETTI NG BH TEMP ID FAN AMPS KILN EXIT TEMP COAL MILL EXIT TEMP COAL MILL AMPS COAL SETTING day/date 7:00 AM 8:00 AM t;,,,ft .t )'t : 9:00 AM f'.,l- '-:.-' I f I i I 10:00 AM ljtr/L]-1 11:00 AM 0,r' L2:00 AM li''I 1:00 PM ,II N 2:00 PM lt,.l! r,:Lr -'1 3:00 PM :i ;.rl ,! 4:00 PM 1 "ii I 1 7:00 PM I t. ,)1-\i. r ii l 8:00 PM 'r.'it "r -'/it -)- 9:00 PM . ) _-:- 10:00 PM , 11:00 PM I r''I ( 12:00 PM It . t114-t **'.'( dayldate 1:00 AM 2:00 AM I.t-1 3:00 AM 1 t, /r'L l-i 4:00 AM :''t .,, ,- ''/.,1 !- ,.,, ). ,5:00 AM DAY SHIFT: Thurs thru Tues: (12 hr shifts) 7am to 7pm; Burner: 51t.1 i 4 (circle one) Wed: (6 hr shifts) 7am-1pm & 1pm to 7pm KILN OPERATION KILN OPERATION ..1 Gas on:Gas off: Reason: Gas on:Gas off: Reason: Gas on:Gas off: Reason: Feed in:Feed out: Feed in:Feed out: "?ct: Lt TANKS: Silver Rus Coarse Problems, Goncerns or Events: NIGHT SHIFT Thurs thru Tues: (12hr shifts) 7pm to 7am; Wed: (5 hr shifts) 7 pm-1am & 1am to 7am Utilitv Hand: -f,e ,.,. -ro Gas on;Gas off: Reason: Gas on:Gas off: Reason: Gas on:Gas off: Reason: Feed in:Feed out: Feed in:Feed out: TANKS:i o'. aL\ '1"i Silver 5',riC L!"j Orange Rus Coarse Problems, Concerns or Events: Bin Vent: t t T T T I t I I I t I I T I t I T I UTELITE DAILY KILN REPORT KILN ,,/\\o' 3 4 END OF DAY SHIFT TONNAGE END OF NIGHT SHIFT TONNAGE FEED rANK RATE TPH BH DP GAS SETTING BH TEMP ID FAN AMPS KILN EXIT TEMP COAL MILL EXIT TEMP COAL MILL AMPS COAL SETTING day/date 7:00 AM lt i\,": 'l u,a t"tI:t1-i-. '4q -7 r'7i. ':*,t;luct '!/rl -?,. . i tl 8:00 AM 'l,.1 u5 ; J- -t-- li ')rtl t-;7 ",ri I I!.|'; ti' 9:00 AM li,, i,,o 1t 14. 5 o{+3ti ;i1..,i 't^,t 'l 10:00 AM 1.,'!,,{,,A 'l . !!.,,r.{JJ LI, ')tQ .iz '1.\t'., I,.1 .,j . .1..- 11:00 AM iiu:,ii'i.r).',j .h-7 r, i1 -i Ita;,'t !iLt I)li I ,l ll 12:00 AM 1:00 PM 2:00 PM 3:00 PM 4:00 PM 5:00 PM 6:00 PM 7:00 PM 8:00 PM 9:00 PM 1O:00 PM t1:00 PM 12:00 PM day/date 1:00 AM 2:00 AM 3:00 AM 4:00 AM 5:00 AM 5:00 AM KILN OPERATION KILN DAY SHIFT: Thurs thru Tues: (12 hr shifts)7am to 7pm; Burner: | - .., Wed: (6 hr shifts) 7am-1pm & 1pm to 7pm i7 t'4 (circle one) KILN OPERATION Utilitv Hand: Gas on:Gas off: Reason: Gas on:Gas off: Reason: Gas on:Gas off: Reason: Feed in:Feed out: Feed in:Feed out: TANKS: Silver Oranqe Coarse Problems, Concerns or Events: NIGHT SHIFT Thurs thru Tues: (12hr shifts) 7pm to 7am; Wed: (6 hr shifts) 7 pm-1am & 1am to 7am Utilitv Hand: Gas on:Gas off: Reason: Gas on:Gas off: Reason: Gas on:Gas off: Reason: Feed in:Feed out: Feed in:Feed out: TANKS: Silver Orange Coarse Problems, Concerns or Events: Bin Vent: I T T T T I T T I I T APPENDIX E Calibration of the console dry gas meter(s), pitot tubes, nozzles diameters, and temperature sensors were carried out in accordance with the procedures outlincd in the Quality Assurance Handbook. The appropriate calibration data are presented in the following pages. The nozzle calibrations are recorded on the first page of the field data sheets. Figure 2 Schen-ratic of Method20lAl202 Sampling-l'rain Meter Box Calibration Data and Calculations Forms Post-test Dry Gas Meter Calibration Data Forms Type S Pitot Tube Inspection Data Salnple Box 'femperature Serrsor Calibration F'ilter Balance Calibration EJ0 fC /t r ,> f -a c? o =s r-=: ' oo G, le l3o:Eat tgEt IL TTTtITITTtItIIIIttT .C$1-F(f ,Co-E(oU)NONrOC. l -( fo.C0)ooFoEogoU) c. ioL:l.9LL du I 5s I) 6-OA Ea ' oE ,o () ' : f , 1 ,D - E j3 ,, (i ii f \O tJ PA rcUS troGq3Eol .h o- ot t(\: 0 i \ aqcOJEcoo al9l \lol 5 ol 6 l N ! 6 1 6 1 6 1 6 1 6 1 6 l 6l o l o l o l F l s l o l F l o l Fl @ l 6 l @ l 6 i @ l 6 l b l 6 l -l ;l -l il -l - l -l -l - l $l 5l hl 3l 31 31 31 5l gl sl 8l 3l ol 6 l o l 6 l o l o l o l 6 1 6 1 6 1 6 1 6 l ol o l dl c j l c i l ;l ; l ; l ol c i l ci l ol qQ q 9o l q IcoaUaU(t:FcUL=!ts rl o z F o U0udulG F Er il Fl -l - ur o^ \ .2 ,. , 1) ot h U NI. g g .i l ,' d -\ - / i1 EnnoFC)uzIFEo=ot]UFu=a>olrolt l(,tu [[ noo o 6r r t 6 l > 6 r r r 6 r > N r o r b r > -l @l o l < @ l t s l 6l < @l ol o l { Nl G t o t t t o t 6 t 6 t o t o l ql nl ". I al ut l q l ql F: l .,! l Fl t s l t l i l o l 6 1 6 1 6 l t l {l o t @ l @ l o t i t 6 t 6 l E t dl 6 l E l E I 6 1 6 l d l o l F l ts l 6 l F l 6 l o l N l o l o l ts l ol N l o l $ l i l o l F l 6 l N l il l i l l + l { l d l d l r i l u i l +l c,9,todccooO f- : gr j_! ^ 6 i2 t) o S- ! 9 -a ? a 6 eB i E tz v J or - . ^ a 69 - o Or ; :c = E 3E P * sr u 6 (9 o E R Ou ) , r* o P 5 oQ ! -t a : + a XD ; ] E ii u o o 6- t oo o i 61 5 ': N l n Eb :oot a Zor$ ooE-E ^t tl ci ,t l @o o o o o 6 @ o rid o i d r i c j @ ! F Nt s F N t s F F F E EH ; l" l " . l " l HT ff i f f i f f i 0vc!, bO6 cOuo9o6oa--:6v !l oog39 ll rr F6 Gco$Oox =,s5ooi=: ; -4 d, JE>Lo6ooo5 -+ E o? o9z !E o6 = EQ O <to )Es r @ E= zP j o6 8 < "' A dr - 9 o ^, i <. : > o6 - @i6 9 l'l 8. E f; 3 F o o i i = 5= F E O aa 9 uE y +* o (, 6 9 =: . e =F > d Noci d oF F,N qo .! ! c 1 ri , L ll-r t.- ', - t i !\l +l :l{; {: - ,t :.l i f - . , ,l .lot')ir ,; N tr t r t r o2H= c- o5E uF EFUz NN N F Nts F ts o FoN F ts N N ts d c o e @ Na ts F Nts oF F @ o N N ts N F Fqcca oc1 tstso Fqo oI@o n eN @N oaN ci qN -i oHH o6O-u=u^ q8E -U^r o =osigB >UsB to IUdfooUEr9dFU=oGm -s" q gR Jgts2 dE zl dl . i_ : l o(EL-c lEC)Io(L$c\ lo6t oocEoclioooEogo6s oo - q cE f g! o6; ! s v6o* o IO O 6 n ='i -= a I 66 0 E '= o 6 = e EP a - U B -0 c - 9 Y o or - o - E6 P 5 ! U aA a t 6 ' 3 -0 . E =? -9 5 o t l :p 6 g t 5: E E H o; o - - G 6 60 g o -b o 9 t 9 o 6J ! b . - o o: f , c o !v ts -o c ' = ! ;i r o : = 6 o: tr G = 3: 6 F 6b E 9 . 6 6o 5 6 E E P: 3 E sE E e s 90 0 > o =!o ! b =o i 3 o E8 : f r 8 OO l d - ) O Ot t c ( . oLuIltd.ooFao(96fzItoJ()tUJFUJ=U' (,tror, ,ooIUJ= !tTTITttItITITIITII oFzE=gf,oum; EE ] {{ JJet r uuFEE3 tra.oJd NE l_ l 5 l$ l lr l lr [ - E l - ; l I I St gt I l - l o l :: ii { <L Fg3 g =rHr ,U = @l 6l Ol -t - t ;t otolci l ol @ l @ l N l @l @ l 6 l @ l ot 6 1 6 1 6 t cjl dl ct l dl u@(xouaTUtrfFtruq=UF F3ozozU(uBd ni l IE I U U* 'L :- - . ; Pl u O . i l -. X '- 2 t; EiltroF(JuzotrtoJ(.1tY . UJFuEo(,uoutoEu, n mf] - n ll l t mm o! @ t ot .? l c? l cl l !l r l r l I- ; t J- i l" l . l . l I- J : T J I 6 1 6 l o l I N I 6 l E l Ljl ; l ; l t- l - t - l :3 : ff i f f i f f i lo l(9 ol o l 6 l > 3l Pl F l < NI N I N I ol o l ; l co=pcoodpcaoaoE. e ooo> o .t o 5E ! r: U o ot r E o! - o 4- . -y c tf o?6 --: .ib c l id - -h t o 3E b G{ - r o oo V ii l { q 3, " , , O : Y L oF I !xnp I(=tloI c€!cooEoEc11 ir aa r^ >E96> - XT o iE UO> r o" - t rP o, 6H : =d j 9o P -+ E X= ql ;o - 6U ; o- o o9 > OU a@ ; O r- o oot j6zI G!5o i pBGi i -a c -- 9 oaOoo.5=; P€EE6P a6 = eQ 6 a_ r t s io , - <. 2 s, s ? n 9E g dE 9 99 ot s Jft<- : > o i6 . 9 o. 9 * uo E A e € oa G i 4. > () : ( J a +e ru P P (r 6 ! 6P - " pt s > dd d ei - :. : -. {' c, i ,; , I *i I .i l r ,I .tli \, I+k ri - . '- i . i .:i N aZH=3 E' uE oF o F o6 @o @ o @oq oNd o\ cc( ort tr n t r T HE3e H< - EE A@=c <{e6 a !ss9 reo troGLsEoooo. I -dqg3*E Fz oFzU=gfoU E=utr)ooudaIgFUoe.6 oocEP,.Eoo (r , o uJ I () E tr r E o) o r s X' E B ii : a J1 0 * E , E H tv t s =h F bE o cl a € E I g; o b :J / ;5 o Ee F s = L O X Oy = 4- 3 d o > O i$ 6 o t .. d E = io E ol i 6 Ef i E E f ; o; o -E - 6 6o g( 9 q :o ! 2 9 d r = X. Y -- E gE E : ; J- l o E = E ^< g; e E; L, E gl - d F i. a XE s" E lu 6 . e i . g r E F !* E f , p UJ E E; !E = q9 o . s g I 6 0 1 6 o =o g hD 6 sE : fi E EO FN o s rO ITtT m; l I sl $l t_ L : l {i d JJfr f r e, F ru=E IE l" l ls l la l ls l H i i l Ll = i i l = E: !E E <rf; r FI ooIFut= I t Tvpe S Pitot 1'uhc lnspection l)ata Pitot lirbc ldcntillcation : 'l'cchn ician: 5 I (i-2[)atc: Dr t ryr I M. McNamara T I I t T t T T I T I I t T t I T D,=0.375 rn. Pl -0.410 in Pr = 0.470 in u.1 < 10" r1r = 0:<l0o 0:= ls Pt-p'"r ls 1.05. D, S l'n& P,, :i I 50.1), ' Ycs 1'es ,,4 p,/^l l_/ ! --: L__-_--- \\t\ [], ' 5o [], t j" 0r = 0, '' 2" 0.t) l(r in. 5 in. 0, +- -l 0 0(r5/. < 0.125 in. /. - W <0.0.1 12-s in W > 3 inchcs 7. > -l/4 inch lin l)robc C()ntinuitv L'lreck Ycs I lcat Chcck 248 Ycs r cmpcralure Sourcc ( Mcdiunr) lcnlDcruture ertrperaturc Dif}'crcncc ("1,) KCtCreItce ("F') ,) ("1') Probc AIR 65 64 I Stack AIR 64 63 I IC'II WA'I'ER 3-.]3l 0 BOtL WAl'tlR 204 204 0 stLt('oNti oil -;----...-*--o II r Y>3inchcs Y= I l/2 in. l lrc pitot tubc nrcots the specilicatrorrs tor a calihratioll lhclor ol'0.t141) Yos t t T T t T T I I T t I T T I I t I T 'l y'pe S Pitot 'l'ube lnspection Duta Pitot'lirbc ldr:nti tlcation: 'l-cchn i,:ian 0.i75 M. McNarnara Ycs tn u1 tn0 426 Is Po=Pn't ls l.{)5.D, < P^&P,, < 1.50.D, 1 Ycs Pa=o 426 /i la I )-{l'l,\ .J Pe= tr1 < lOn d1 - c, < l0o crl - {}r':5" lt, - lj:' 5" 0: = Z < 0. I 25 in. 7.'= 0 0?9 Ws003125in. W= 0.015 in In 1o -T W > 3 inchcs /. > )/4 inch W = (r.75 in 7.= I rn Y= 1 l/1 irr Thc pitot tubc mccts thc spccillcations lirr a calibration tactor ol'0.8.11 Yes 'l'emperaturc Scnsor CalibrationRelbrence. Omcga CL35l24 Continuity Chcck I lcat Chcck 248 =C,;()c) r. i\)o,1 )Isia-t)>/ . .- , ^= u co Ec i cJ _ c m O - Y rr Y -S J 4 o- .: l i- , I a c) - = J ^ ! - .P E a qr+ - il - _. s C '\ J -+ :.- : Jlt * - '- = l l r L .S g U9 D^ ^ - .l ri Ya bJ J r; CF l Udue9' = -u =l -l 0J 4f n' O U !l ^h -= : : '= ^q t g '- ; -: } l < "- bo Nr ^ U U .: a4 ) 6- U u r i i, br ( J t h 6 il il 55 '. = ' E q -A cr , C:j L! J!! v LJ r- ) q)a a- ) gH c e !v . r F n ^ C. ; rl "- - / ?; c J L (J =C) -- o cS f- H. r l< '( ) o-E()Fa0) e :? E E r i = q vvpv gE 4, E -O L < X L! 0 ) v (U P \/* 9X u Ht r ( J (u d r, x o l- t \, / -c gq. ) o) EE l )F .1a. l co GLEZ()a.: z2"o\q $c. lUa. l aa (a ) O:t€F):zL^dro cl ,!F_ iciol \ctr i;dJ i l'o aE>. ;<. lr J o aY t=a- aAvUFri t' l TIITIIITITITITTITIT Fo(cqJbo (Bc) cd0) LJ ! r: Y ? o I v ca .J - oo I- - \( ) \O r- . F - r- - O\ O\ oo oq o q oo <' ra c- ) ,. ? ,r ? vl U.;OJo4).J(J ()F' o. 6\ O Zf - )i -br CJ a -q ) E aA 'a = i? a A--+,o!r r ) F€ -r tr - ts i F(Ia AI .lt)GL-.--6€ (, ) -o)FI-I-l)F. i -I-I.-70) ---t' r *JIr J t.-A- aa Ezooo':!! g E AC rv . - F 6 A (J t J i -! .r ; 0 J .L L() E !; L F l i li6E0)F aana.] =fc. l \oc. . l c.) -ll\, ,3 ir - ^! = r' ;=a lLD -r a=. .9 cr :- o '->= 4J LJ - . z P !p ; o LC ' u7 ) \ <t a - ^ \; U L( ) - c rY t o- s tr Y 02 <t c- | 'J . di h! O _ UE AL u- 6a -' h a - il x ^, E - lr . 9 - Ji l CT ^ I L C CJ o ^ '- o u- .l j 7 ct ri i C* =CY( c ue .J '- -c -u y 1t n.t ilb u O - C - {1 5 rr . = E .o ' J ( J c. . ) 1 ) LL 4q o a , a: . ) i U' ( J 6 . t lr l l b5 '; ' t q< € C LL -a - a, -o O \r s: ==UU Ia (h() ca o,qia a = ;9 u o_ - :. = r\ = v jj !. ' / o E- ;i d . . iJ h EL ? qo . ) v .c ] c r i L F '! s\ . 1 (B -. c aA v l- J \ / *d (. ) u ElcF c.9.;'lJooio ;- lr f'- Ft (- - \\ \ cr . ct \ oo oo o o oo -- ^ . - - *f , . f , $ v] v l '1 o\oqO.9cdit ) !(JbI !() {|h!F ?t ) 6f - :r - c. lJ U+J t r 9io) .1 i \- -a-a = ir a /Alr l l- l+- )oFE - r- - &d . Fta *(\ l \o(\ l ?aFI.-*- )CE li-.--cqU-q)A4 Ia--l-F' lE-Li .-'-0) --F- l *i*- ) .lnr AvU3f; r 13 II!TTITITIIIITttTII Of€ico . ij cl !ltr - \@iO6t\.Lr l E h-<. tr l a .a ^, a, a6 I T t I I I I I t I I I I I T I I I T TETCO Sample Box Temperature Sensor Calibration Darc ll2l21 Calibratur'Xuan N. Dane Rclercncc: Onrega Ct,35 llA 0 0 0 -l 0 -l 0 o I 0 a 0 -l 0 o 0 0 0 t init ll)'I'hcrmocouple l,ocation 'fcmpcraturc Sou rce (Nledium) I'emncraturc 'l cmpcraturc l)ifl'crcncc ("r) Ilel'crencc ('l') Sensor ("r) A Oven (3)Watcr 33 33 0 Watcr 203 201 -) Oven (4)watcr i3 _,i -{0 Waler 203 201 _) B Oven (3)Watcrr'-) -,0 Wirtcr 203 202 I Oven (4)Watcr -i -i .J.J Watcr 20-l 201 -l C Oven (3)Watcr 33 il 0 Watcr 203 20i 0 Ovcn (,1)Watcr J_1 33 Watcr 203 203 () D Ovcn (3)Watcr 33 ,1 0 Watcr 203 203 0 Oven (4)watcr -]3 -) -l Watcr 203 203 0 E Oven (3)Watcr 33 0 Water 203 203 () Oven (4)water JJ .1-j Water 203 203 0 F Oven watcr 33 33 0 Watcr 20-1 20?-l G Overr Watcr l3 0 Watcr 203 202 -l H Oven Watcr 33 0 Watcr 203 203 0 0 lrnpingcr Out A Impingcr Out B ftnpinger Out D lmpingcr Out E Impingcr Out F Impin-eer Out C lntpinger Out H lmpinger Out I lmpinger Out J t t T I I t T T t t T I I t T T T T I TETCO Annual Balance Calibration Check Date 1123124 Denver lnstruments, ModelA-250, SN 8045284Balance Weights Used Troemner Weight Set, sN 98-115146 Technician Certified Weight orams Measured Weight orams Difference qrams 0.1 000 0.1 000 0.0000 0.5000 0.5000 0.0000 1.0000 1.0000 0.0000 10.0000 10.0000 0.0000 50.0000 50.0001 -0.0001 100.0000 100.0000 0.0000 120.0000 120.0001 -0.0001 150.0000 150.0000 0.0000 Michael McNamara APPENDIX F Tlre testing protocol and other correspondence related to the tests are included here. t T T T T t T T T T T T T T t I T T T State of Utah SPENCERJ. COX Covennr DEIDRE I{ENDERSON Lic.Uaa* Gownor Deparfinent of Environmental Quality Kiubcrly D- Shellcy Exctulit+Dir*w DrvrsroN oF AtRQUALTry Boacc C' Bird Dlrcctor June 28, 2024 DAQC-636-24 Site ID 10676 (84) Dave Vernon Holcim Utelite Plant P.O. Box 387 Coalville, Utah 84017 Dear Mr. Vernon: Re: Holcim SWR,lnc. Utelite Plant -Kilns #l and #3 * Protocol Review and Test Date Con{irmation - Summit Couuty The testing protocol for the Holcim Kilns #l and #3 received June 6, 2024, has becn reviewed and found acceptable. The agreed upon test date is the week of July 8,2A24. Acceptance of a protocol does not relieve the ownerloperator and the testing contractor from strict adhsrence to all applicable EPA Be*rods, Utah Division of Air Quality (DAQ) policies, Utah Air Quality Rules (UAQR), and methods approved by the director. Any deviation from EPA methods, DAQ policies, UAQR, and methods approved by the director must be addressed separately and express written consent given prior to commencement of testing. The DAQ requires that all test reports include a statement signed by a responsible official certi$ing &at: A. Testirg was conducted wbile the source was operating at the rase an&or conditions specified in the applicable approval order, operating permig or federal regulation. B. During tcsting, the source combusted firels, used raw materials, and maintained process conditions representative ofnormal operations, and operated under such other relevant conditions specified by the director. C. Based on information and belief formed after reasonable inquiry, the statements and information contained in the report are true, accurat€, and complete. t95 tffi 1950 W.r{'Sslr L.k! City, IrfM.it"g Ad&Bs: P.O. Box 1448!0 . Srlr Lrkc CrB, Uf E4l ld4820Tohehac (801 ) 536-{000 . Prx (80t ) 5364099 . T.D.D. {80 I } 90t-39TE w.b1.aah"gvv Pdnrod oa t00ki, rclclcd Fpdr t T I T I T I t I I T T I T I I T T t DAQC{36}4 rucz 1 i :. L :t,: r-iJ iridi':r{: r i i l;:il{ -J i;;.;. i.;, i: , 1.,3';1 ,; r; "i t $It $ $inoomty, !. fll{{ i Robfit $nriqo, Euytr-omoqbl Su.icotict DiYibhDd,Aft^Y,ry R$$ oc: $mit CountyHqalth UWerUrm.* --lgrcL_1,"-.'i .;1: .:il,p..r l t' r, t i'r i 1." t',. .':. zi.:'tl'; t r iii COMPLIANCE PMro EMISSION TESTING PROTOCOL HOLCIM UTELITE, COALVILLE UTAH KILN #I AND KILN #3 PROJECT ORGANIZATION AND RESPONSIBILITY The tbllowing personnel are presently anticipated to be involved in the testing prourarn. Thc tJtah Division of Air Quality (UDAQ) and EPA may have their orvn personnel to obsclve all phases irrcluding the process. Company Holcirn [.ltelite Plant P.O. Box 387 Coalville. Utah 84017 .r't-.-fco 391 East 620 South American Fork^ tjtah 84003 Contacts Dave Vernon Alex Judd (80 r ) 467-2800 (80r ) 467-2800I I t T T I T I T Dean Kitchen 80l-492-9106 l)uring these tests only lJolcim personnel listed above or assigrred pcrsonnel liorn the opcrating departrnent are authorized to answer or obtain answers to pertinerrt questions on the proccss corrditions or the test protoccll. PRO.IECT pESCRTPTTON ANp METHOpS AppLrEp- The sources to be tested are the baghouse exhausts of Kiln #l and Kiln #3. at the Ilolcinr lbcilitl, located south of Wanship. Utah. l'his test will be conducted to demonstratc cornpliance witlr the lacility's Title V Operating Perrnit nurnber 4300001004. Tcsting procedures rvill includc accumulating process and production data as well as testing fbr PMrg emissions using EPA Method 201A. Condensable particulate matter (CPM) will be measured according to EPA Method 202 and is not for compliance, but informational purposes only. Tesling will consist of three test runs. TEST SCHEDULE It is planned to cornplete alltesting the week of July 8.2024. The tcsting c,rew will arrive and set up and start testing on.luly 9tl'and continue until all testing has been cornpletcd. A pretest meeting can be scheduled il'requested by l-lolcirn or DAQ. TEST PROCEDURES T T I I I I Three test runs will be conducted on each kilnl for PMro emissions. 'festirrg will fbllow [:Pr\ Metlrods 20lA and 202 as specified in 40 CFR 5 I Appendix M. EPA Methods20lAl202. The following specific items will be followed for Methods20lAl202: l. 'fheKiln#lstackinsidediameteris4Tinches. Therearetwoportsavailablefortesting that meet the upstrearn/downstream requirements o1'Method l. The ports are localecl 45 lbet downstream and 33 feet upstream lrorn any florv disturbancc. A total of l2 points will be sampled, six per port. Minirnum target sarnpling tirne will be 60 rninutes. The stack llow rvill deterrnine the dwell time at cach point and actual test tirrie. 'l'he Kiln 3 stack inside diameter is 46.5 inchcs. Thc're are trvo porls available that mcct thc upstrcam/downstream requirements ol-Method l. '['he ports are located 45 {Lct dorvnstream and 35 feet upstream from any {low disturbance. A total ot'12 points will be sampled. six per port. Minirnum target sarnpling tirne will be 60 rninutes. I-he stack llorv rvill detcrntinc thc dwell time at each point and actual test 2. EPA Method 2 will be used to determine gas stream velocity. Calibration data lbr tlre type "S" pitot tubes are included with this protocol. Dual inclined/r,ertical rnanonreters rvithgraduatiorrsin0.0l inchesofwaterwill beuscd.'l'heabsenceol'cyclorricllorvwill be checked during the prelirninary run. 3. A barometerwill be used to measurethe barometric pressure. lt is perioclically chcckercl against a mercury barometer. Prior to testing it will be checked to assurc an acourate barornetric pressure. 4. An integratcd sanrple of the flue gas will be taken liom the exhaust linc after thc dry gas nreter orifice during each test run and analyz-ed at the test's completion by Fyritc to detennine the gas stream molecular weight. 5. The probe liners will be borosilicate glass or'l-eflon. 6. I)reparation and clean-up by the contractor will be performed in the contractor's testing trailer. Laboratory work and analysis will be done by the testing conlractor as soori as possible after all tests have been completed at 391 East 620 South. Arnerican Fork, Utah. 7.Uack hall-will be determined by EPA Method202. EPA klethod 202 analysis will bc fbllowed as in the method. If plant maintenance or operating problems arise during the test. the test rnay be sbpped. This determination will be rnade by the Holcim Corporation representatives or operatiug personnel in consultation with agency representatives 8. I I T t I T T T T I T I I T I T T I T 9. Current calibration data is subrnitted in Appendix B of this protocol. Any equiplnent calibration that fall past due prior to the test date will be recalibrated prior to use. OPERATIONAL DATA AND INSTRUMENTATION Pcrtinent operating data rvill be made available by t{olcirn upon request by agency personnel. TE,ST AREA The test area slrall include the control room" stack and associatcd areas. and thc alea arorrrd thc contractor's testing trailer for preparation. and clean-up. TEST SITE A sketch oi"the source is included with this protoco[. ACCESS TO SAMPLE SITE T'he site is accessed via stairs and ladders. POTENTIAL HAZARDS Moving Equipment Yes I'{ot Equipnrent Yes Chernical Other No No ESTIMATES OF TESTING PARAMETERS The volumetric flow ratc. rnoisturc and stack tenrperatures are similar for both stacks. Volumetric FIow Rate 12.000 dcfin Moisture l4oh Temperature 325'F OUALITY ASSURANCE I I T I T t I T All testing and analysis in these compliance tests will be conducted according to Methods 20lA and 202 and appropriate sections of the EPA Quali4t -As.surant:e Hantlbook.for Air Pollutiort L[e a :nrrem en I Sy,stent,s Vo I u me I I I. REPORTTNG The emissions test report will be prepared by the testing contractor according to EPA Quality' Assurance Guidelines. l'he contractor will furnish several copies of the test repoft to l-lolcirn.'l'his report rvill be submitted within 30 days following the completion of the tests. EPA Method 202 rvill be included in the written report for inforrnational purposes only. Complete copies of raw data, calculations and summary of test will be included in reports. All process and production data will be recorded and retained for inspection and <;opying by DAQ and EPA. t I t t I I T I Appendix A Facility Schematics ooc> ) Ub . r - t r - - .! Z S r E . c - l i. i . c d = ) . ; 1: 3 = ; ; E Z i E_ E 5 i r z ; = z ? 6, = z d = 6 ' t r =i . X l L - 1 = ca ; ! : E ; =- = 3 9= = 2 6 i ; .E / c U L t L E- ' r : i u n :j- ] 9f o K \ u Ch : : ui ; UU -7 ). . _eoU i: c) 6o l ' do .^ // / q)aE' J +l - nl - . i.:€!':'5=o=U) l+ ,!I1.\,'tEala)al) u- I = E; E E - I 9 t- ! = : 13 ! . . . b E E ; Y!O J =E 6 r P . : 9 . " 4 =7= ! 6 = t r zE z - 5 ! E2 4f o " 6 , o = -j ! c : 7 ' i . =- : = ^c s . , d ; - +. = E r E I r l -t 5E : ' h l i gE c K \ 0;iC- a , = v, a .4 , =' r i a o o3Q - a' 'J l' ;- j i1 . .J o o // / (- i !<Fd {- JFTLi (J al- E l \J r\\J()#rp ( ()+J ) ,t Ja:i +t ' ;o.;C!6a tNt- l_ " _ L Appendix B Calibration Data nf bl ql j Hl 'l - . UT ct z'\ { 'o . 6 ol ; !l F l Y o o l i ' S- ; !l<, ; Ia sl rl :l E l :l 3 : l E l El El gI l H {l i l d ff i ff i HE ff i .c e r l ff i f f i f f i qtcl riat -ldl ol 6 l * l o l o l N l Nl 6 l d l N I 6 l F l 6l o l E l 6 1 6 l N l al ! l ol rl c l 6{ il s l 6 l b l b l e l I] El Et : gl Ht ff l : Bl fl fl : :l Pl Il Il rl il El rl El oo 0 0 0 0 o@ o 6 a @ c.-jEc OO 5- -E > U a- , x n , h + 3g u, 99 ; o" Y b o I ,: ; q c q -o , t o 9 O C /', :FU D or : X; e ' : o I a +i d =- ) , . 1 c Y o- d i ;i ;; ts r - v ii =; i o 0 ; D j r :i #i . [ i l ilo 6 Y i n ' o < =d , . :- = o u3 I o< < 3' " " c a Y q fu F -O>- :ng !€oI c3EcopoECo6oDeo(,oEo:o5!oo-eEoooE6i, i2I;lir . l :l\|4i,t,l .(l. =€6€o- 5 iPEg >5 <5 4 o6oSO: U sL - o a= <E o o= E i! e@E - : 9E r <D G GE 9 @ -E u- - 6m e A q€ o 6 E a 5E E* e uP P -t ooE p 2- o 6Z = >F > i6 0 € o o .lq r c ! q 6 l q q q q q q e ts9 i 'I -, Ir" l _ Il- "- l B alal4tUIalul (1 2 fl -EIdlul IL=lt ! UI Y ts t f i lElulu N +- o3p igP6Hi BE 6@si CO<f>6>UEg E&o o(!€(!C)Ioo-t(\ Io$t III 5@gR*E oiO= d- o5EUt r N N N NN F N h F F ts I- J ; I ff+i d JJaa UUfi h ts a 9u =o trdo6 ll E l. l o l+ l l= l l' [ s l l ] ll - l " l ti i i i <F Fq3 E =rHs FE = oc6o6aoD.9ad -i1 oo ! 6 o- o i: o o G o =. . E i X o d '= o 6 = v EP r 3 " o- o V fi E = _ 6 -.1 E, ; 5 i I i- o - ! =o o o - i; , = n : s -9 t e E o Pe = z Pt = * u = -= ; u o; c - E 6 6( ) g O i; g r p 9 o r 6: = E - o o: f, c o E= : ! J ot E o = 9? - r c E it o = b c !* E E p !; - 6 : d,Q o ) : o p ft 6 > 6 >o o ! E ::6 0 ! N'U C F I U dr o l i o Ad E i E v, lr l9ILtoJoFd.c)o-afzoFttr lJottuFuJEat ,oEoar)ooxFUIE It tr t r t r I I T I T t T I ! T t I T T I I T T T Date: Dr t/1612024 'l'vpo S Pitot Tube Inspection Data Pitot l ube ldentrfication: Technician: 0 375 M. McNanrara D,=ls l)1: I)n ? Is I 05. D, < P^& Pr < I 50. D,'i Yes Ycs Pr=0.4'76 -r 1 d\ irlll As,)T-),\ -/ _/v -,/.----<.r\ \_)\/ tr. Ps=0.4't6 u, < 10" o. < 10" llr<f 0,t5" dt - cl: - 0r= 0:= )o 0' t" 7. < 0.125 in. Z =0.002 , .:=?.,=t - -- -\ -'- -'-w < 0 03125 in 0.004 W > 3 inchcs Z.> 3/4 inch 7=I tn. in. l-- - --"-- i---- ,-.-- l ..-' Tffil- *O \'> 3 inchcs Y.= -1 l/2 in. l'he pitot tubc nrccls thc specilications lbr a calibratlon faotor of0.84? Ycs Sensor (lalibration Heat Check 24tl ICE WATF,R I T I t T T T T T T T T T T I t I T T Datc Dr t/t6t2024 Type S Pitot Tube Inspection Data Pitot Tubc ldcntification:-51 c-2 M. McNamara I),=0 37s ls P.r = P, 't Is l0j.I), < P^&l)r, < 150.D,? Ycs Ycs Po=0.470 tn. in.t-;l l"l-\t Ps=0.470 <r, < l0o ct1 < l0o 0, '5o 0, '5o dt = ct: =I 9r= 2 0:= 3 Z<0.125in 7.=0.065 W < 0.03 125 in. W - 0.016 in W > 3 inchcs /,> 314 ittclt 7 ---" ln in -_-_-.,.J\o-- | ' qJ,:*- mmr- -:il Uirlffi I ----.------y > 3 inchcs y = -t t/2 in lhc pitot tubc rrccts thc spccifications l'or a calibration l'actor of 0.84'l Yes Contiuuity Check IC]E WATER BOII- WA ER sil.tcoNri orr I I T I T t I T t I I t I T T I I T t TETCO Sample Box Temperature Sensor Calibration Ovc:n (3) Oven (4) Ovcn (3) Ovcn (3) Ovcn (4) ()vcn (3) Oven (4) Oven (3) Oven (4) Datc. ll2lA Calbrator Xuan N. Danc Rcferorrce: OnlcPa ('L35 I2n Itnit lD Tcmpcrature Dil'ferencc ("f ) -I () 1 o 0 0 () -t -l 0 0 0 0 -l -l 0jj 0 0 -2 0 -l 0 0 0 0 hnpingcr Out A In:pinger Out I) Impingcr Out h. Impinger Out F' lmpingcr Out C Impinger Out H lmpinger Out I hnpinger Out K I T T T I I I T I T T T T I T T t I T TETCO Annual Balance Calibration Check Dale 1123124 Denver lnstruments, ModelA-250, SN 8045284 Weights Used Troemner Weight Set, sN 98-115146 Technician Cedified Weight qrams Measured Weight orams Difference qrams 0.1 000 0.1 000 0.0000 0.5000 0.5000 0.0000 1.0000 1.0000 0.0000 10.0000 10.0000 0.0000 50.0000 50.0001 -0.0001 100.0000 100.0000 0.0000 120.0000 120.0001 -0.0001 150.0000 150.0000 0.0000 Michael McNamara =-o.. :UOJa.i 'oOJ>0 1 .- C<j o-U -l >.r e 3p i 4) - o a (f - < ,5 € <t I u1 o= .3 E ra v 6r * - ll - = ^E =, \ J = f i 9 | E = EL L = '= a (r P n. : d d e= ir , .: : c- B v:al e (J .: : 6a '( ) ! 41 ) U -. u u !th v * g4l s ? 55 -' J O ar t s c J U ;-L !6q U U '( x j7 Ur ( J 6 6 il il 83 '5 ' . = -n r- -o - . o UU c)a ao () c , - :c B o 0 t & !v r - F ^ 9 >r . <- / -; 6 - ) -i J v!J -- o cg l< lJ r Li '( ) o. dFC)F(hq) : | *: E ! J d ) su d t_ E 4, EA li d ) v (g € Eq ) * h E 9 t- . 1 \,d eu C)F aO.1a. . l ca E(nz.J(.) -vE2, o\o\ *d i c. l \oe. . l c.) ra ) .$€F3I:r ==c . atoa l ;: -+ =r tr - iN\oLI);r l, r )u't ra '- = a'; i kJ o9. Y a6AvUFE]Fr TtITTTIIIItTItIIItT qil0) -o=o,Et0)(JboL0) Eo.;C)a E (J ! rr : YJ o I v .n $ o o I- - \O \O \\ \ C C, . oO o9 € o g t. i c n E.9'td.)o6)bIdLqJ 6Ho . 6\ OUf - EOFt r 9tOEPE .A U, = fEa-i)+)0r0)>> t"Io ITlF t lo.-ir )63LA-.r i --U-()aIAI-l-Fr -tJa:.-7q)A t- --Fr+) rL , .l!r ca t c. ) c?rnr\ l CJEZ3aCJ=o':I .< fNa. l c. ).9 E AC rv F Ao t ! " v d: 0 J &U.C ) A : S FU ^FG)F O=o.. =()4) (aal-oa l: ., 9 (] _ o- L .> ) O;(s ( , o- ._ | 1) d. E rt a .. : C il l rr l .=u!o'=6J 0.' t) q J o- o- =E ooOU u0 ) I: J OJ '; ' E==L, U qlid) .od)0)bO,u<t coLoa OJ -5 lu n as b q il x -? n dJ 1ou - c)a I rl ') .i l o dl s ' - <l - =ta B;q jqi . U r( J il ll J1 S -5 - I \J LJ ^ :, : . ; IJ Y ' n : i ija = q . , e -- - 0J ^{ ) i .= v O c - ;i d . E I" L : .U L0 ) v (g e \/ E 9 t !E A J (E i t aA v l- l vd i) u Clc=F a() ca CAq tit: /FU- l2l a/ al -lu/ q)a0F( f ) ar - :r - A\ J r\vbt r CJ s -o t a'a = pl to l- lFI{- )FE Fr t f- &d FIa c.9.;(.) ;c ;; tt__ r O F- r - F- r- r - r- . -^ ^ . ^ ' o. o . oo co oo oo AA - I .f , <f , < f c'td.) c_ )OI (J tI.tra r ) tI-.l--U-q) j-IaI--Frot-.-'-0)E-l-Fr i)+l o-Alr l vUF.Hi- tTIttTTtITTITIIT!TI if,6-tan l I, i i- lAa/)(\\c= = !. E Ir ) . &uaa C HoLcrM UTAH DEPAHTMENT OF Ei.|VIROI'IMENTAL AIAUTf August 9,2024 Mr. Harold Burge Utah Division of Air Quality 195 North 1950 West P.O. Box L44820 Salt Lake City, UT 84174-4820 AUG flan rt DtvrsloN - 9 ?t,24 lst;{{t!*, RE: Stack Test, No. 3 Bag House, Title V Operating Permit No. 4300001004 Dear Mr. Burge Enclosed is a copy of the PMro Particulate Compliance Test, conducted in accordance with sections 11.8.3.a.1 of the Operating Permit. Testing was done at the Holcim, Utelite Plant on July 70,2024. I certify that; a) Testing was conducted while the source was operating at the rate and or conditions required b) by the approval order, operating permit or federal regulations. During testing, the source combusted fuels, used raw materials, and maintained process conditions that represented normal operations and was operated under other relevant conditions specified by the Executive Secretary. Based on information and belief formed after reasonable inquiry, to the best of my knowledge the information found in the report is true, accurate and complete. c) lf you have any questions, please call. Operations Manager Holcim-US, Utelite Plant Holcim US, 6375 W Three Mile Canyon Road, Phone 801 -467 -2800, www. holcim-us.com Coalville, UT 84017 I t T I T I T I I t I t I T I I I T I AH DEPARTMENf OF DIVISION OFAIR QUALITY 2024 liv PMIO PARTICULATE COMPLIANCE TEST CONDUCTED FOR UTELITE CORPORATION KILN #3 BAGHOUSE July 10,,2024 by: TETCO 391 East 620 South American Fork, UT 84003 Phone: 801 492-9106 Fax:801 492-9107 Prepared for: Utelite Corporation P O Box 387 Coalville, UT 840t7 Date of report: July 24,2024 CERTIFICATION OF REPORT INTEGRITY Technical Emissions Testing Company (TETCO) certifies that this report represents the truth as well as can be derived by the methods employed. Every effort was made to obtain accurate and representative data and to comply with procedures set forth in the Federal Register. Mike McNamara 1' l. :i /i I i I .- . Dean Kitchen Reviewer: Date: Reviewer: Date: T t TABLE OF CONTENTS Page Introduction Test Purpose.............. .................1 Test Location, Type of Process. ...................1 Test Dates .................1 Pollutants Tested ........................1 Test Participants........ .................1 Methods Applied..... ...................2 Principle of EPA Method 2014........ ...........2 Discussion of Errors or lrregularities......... ....................2 Quality Assurance. .....................2 Summary of Results Emission Results...... ..................3 Process Data.......... .....................3 Allowable Emissions .................i Description of Collected Samples. ...............3 Cyclone Cut Rate and Isokinetics.......... ........................3 Source Operation Process Control Devices Operation .............5 Process Representativeness...... ."................."5 Sampling and Analysis Procedures Sampling Port Location............. ..................6 Sampling Point Location........... ...................6 Sarnpling Train Description .......6 Sampling and Analytical Procedures........... ..................7 Quality Assurance ......................7 Appendices A: Complete Results and Sample CalculationsB: Raw Field Data C: Laboratory Data and Chain of CustodyD: Raw Production and Control Equipment Data E: Calibration Procedures and Results F: Related Correspondence t I lll T T T Table I II III IV LIST OF TABLES Page Measured PMro Emissions......... ........................3 Cyclone Cut Rate and Isokinetics............ ..........,1 Sample Point Location........... ..........6 Complete Results ..... .....Appendix A LIST OF FIGURES Figure I 2 Schematic Representation of Facility Appendix D Schematic of Method 201A1202 Sampling Train ........ ........ Appendix Il lv T T I I t T T T T T I t I t T I T t I INTRODUCTION Test Purrrose This test was conducted to determine the PMro particulate emissions from the baghouse serving Kiln # 3. Emissions are expressed in grains per dry standard cubic fbot and pounds per hour. The results are used to determine compliance with the facility Title V Operating Perrnit. Permit No. 4300001004. Test Location. Tvrre of Process The facility is located south of Wanship, Utah. The process consists o1- firing calcine shale as it passes through a rotary drum and expands to a less dense material. The expanded material is used in the construction industry as a lightweight aggregate. A schematic of representation of the Kiln #3 exhaust stack is given as Figure I in Appenclix D. Test Dates Three test runs were completed July 10.2024. Pollutants Tested The tests were a gravimetric determination of PMro particulate in accordance with EPA Method 201A. Method 202 for condensible particulate matter (CPM) was also completed burt is lor informational purposes and not for compliance. Test Participants Test Facility Dave Vernon Alex Judd State Agency TET'CO Robert Sinine Mike McNarnara Xaun Dang Jerinliah Opthof' I I Methods Apptied t EPA Methods 201A and202 were used for each of the tests. t Principal of EPA Method 201A A gas sample is extracted at a constant flow rate through an in-stack sizing device, which separates I particulate matter (PM) greater than PMro from particulate matter less than PMro. VariationsI from sampling conditions are maintained within well defined limits. The particulate mass is determined gravimetrically after removal of uncombined water. I A schematic of the sampling train is given as Figure 2 in Appendix E. t Discussion of Errors of Irresularities I There were no errors or irregularities. I Oualitv Assurance r Testing procedures and sample recovery techniques were according to those outlined in the I Federal Register and the Quality Assurance Handbookfor Air Pollution Measurement Systems. T I T t I T T T T I I T T t T t T T T T T t T T t t t T SUMMARY OF RESULTS Emission Results Table I presents the compliance test results. Process Data The process was operated according to standard procedures. All pertinent process data was available for recording by agency personnel. Baghouse AP readings are included on the daily log sheet for Kiln # 3, in Appendix D. Allowable Emissions The allowable PMro concentration for this source is 0.024 grldscf. The allowable PMro emission rate for the Kiln # 3 Baghouse is 3.34 lb/tr. Description of Collected Samples The sample filters for all three test mns were lightly discolored with tan colored particulate. The front washes were all clear in appearance. Cvclone Cut Rate and Isokinetics The Federal Register specifies that tests for PMro using EPA Method 20lA shall either not exceed + I p of lOp and the measured flow rates (AP's) shall not exceed the calculated AP maximum or Ap minimum, or one AP may exceed the AP maximum or minimum if the isokinetics remain within +20%o of 100%. TABLE I. Measured PMro Emissions T I T T T T T T I T T T I I T T I T t The cyclone cut rates, isokinetics and number of AP 's which exceeded the allowable range are shown in Table II. clone Cut Rate and Isokinetics #pts <AP.in or >APmax 0 0 0 4 Cyclone Cut Rate 10.28 9.89 9.91 T I souRCE .PERATT.N t Process Control Devices Operation I All process control devices were operated normally. Baghor;se AP readings are fbund on ther daily log sheet for Kiln #3 in Appendix D. I Process Representativeness I Thc facility was operated normally. Production data is found in Appendix D. I t t T I T I t t I T ts T T I SAMPLING AND ANALYSIS PROCEDURES Sampling Port Location The stack inside diameter is 46.5 inches. Port location is depicted in Figure 1. The ports are located 1 1.5 diameters (45 feet) downstream from the last disturbance and 8.4 diameters (35 fbet) upstream from the next disturbance. There are two sample ports with inside diameters of six inches. Samnlins Point Location Table III shows the sampling point distance from the inside wall according to EPA Method L Each point is marked and identified with a glass tape wrapping and numbered. These points are determined by measuring the distance liom the inside wall and adding the ret-ereng6r (port) mcasurement. I T T T t T I TABLE III. Sam Point Location Distance (inches) from Sample Point I I 2 1J 4 5 6 2.05 6.79 13.76 32.74 39.71 44.45 I T I Samnling Train Description To determine the actual emission rates for this stack. 40 CFR 51, Appendix M. Methods 20 I A and 202 were fbllowed.I I T t All sampling trains were made of inert materials, (i.e., Teflon, Stainless Steel, glass, etc.) to prevent interference of the sampled gas and particulate. The stack analyzer used to conduct Methods 201A and 202 is constructed to meet the specifications outlined in the CFR. The temperature sensors are K{ype thermocouples. I.leater, vacuum and pitot line connections have been designed to be interchangeable with all units used by the tester. The probe liner was of Teflon. A sampling train sketch is found in Figure 2 in Appendix E. t T Sample boxes \ryere prepared for testing by tbllowing the prescribed procedure outlined in Method 20lA and202. Sampling and Analytical Procedures All test sampling and analytical procedures employed were as specified in 40 CF'R 60 Appendix A and 40 CFR 5l Appendix M. Qualitv Assurance All equipment set-up, sampling procedures, sample recovery and equipment calibrations were carried out according to the procedures specified in 40 CFR 60, 40 CFR 5l and the Quulit.t, Assurunce l{undbook /br Air I'ollulion lvleasuremenl S1,stems. APPENDIX Complete Results and Sample Calculations Raw Field Data Laboratory Data and Chain of Custody Raw Production Data Calibration Procedures and Results Related Correspondence APPENDIX A Complete Results Nomenclature Sample Equations A TABI,E IV COMPI,ETE RBSULTS PM IO PARTICUI,ATE MATTER Kiln #3 BACI IOUSE Compl.te Resuhts I Symbol Date Filter # Begin Lnd Pb,, AH Y Vm T'. Ahcad A" bf iAp,, iAp."u.ur"6 .iap wr",. Tr cp D, Coz o2 N2&CO VITl.td Bw. xd Md Ms Yol u QsS'f QsCyc Nre C Dso Drn Cr Dso-r Z T" As Pc Pb, P. Q. QO Mpuro o M>pruto o M"o. Cpuro o C>puro u C"r. ERp",o n ERrpv'o n ER"r- Description Dimensions ln Hg Abs ln HrO dimensronless cf ,n' tn' Root ln H2O Rool In HzO Rool ln HrO Crms Mlnutes Drmensronless lnchcs Perccnl Perccnl PercenL dscf scf Fracllon Fracton lb/lbmol lb/lbmol Percent mrcroporse dscfm Drmensronlss mlcrons mtcrons I)rmensronless mtcrons DimeNronless I Sq Fl ln HrO In Hg Abs ln HB Abs dsc[m c[n) fp- mrlliBrms mrllgrm mrlIgrms 8r / dscf gr / dscf gr / dscf lb/hr lb/hr lb/hr Run#[ Run#2'7/t0t24 7il0t24487 488 8:45 10:26 24.10 24.10 0 350 0.3900.994 0.99424.288 26 272 87.5 95.3 17 00 17.00 t698.2 t698.2 0.0100 0.0 r00 0 5685 0 s598 0 5628 0 ss42 0 5628 0.5542 474 544 59.00 60.25 0 769 0 773 0.2r60 02r80 4.20 4.20 14.80 14.50 8l .00 81 30 18.773 20.024 2.235 2 566 0 106 0.1 t4 0 894 0.886 29.26 29.25 28.07 27 97 r 03.9 r08 7 218 3 2t8.6 0.3 18 0 3320.608 0.6452241.6 2349.5l.106 l.106 10 28 9.89 2.s0 2 35t.106 r.l 13 2.50 2.34 r.000 0.997 2648 269 6 l 1.793 fi.793 -0.270 -0 270 24.05 24.05 24.030 24 030 1.42E+04 1.39E+04 2.718+04 2.70E+04 2.30E+03 2.298+03 Run #3 7/t0/24 489 l2:10 l3: l4 24.t0 0.400 0.994 26 642 99.9 17 00 t698.2 0.0 100 0.5s48 0.5492 0.5492 s0.3 60.00 0 769 0.21 60 4.00 14.90 81.10 20.139 2.372 0.r05 0.895 29.24 28.05 tt22 218.4 0.336 0.641 2359.2 r.106 9.91 2.35 1,n2 234 0 997 AVG 264.8 266.4 I L793 -0 270 24.05 24.030 1.39E+04 1.40E+04 2658+04 2.698+04 2258+03 2.28E+03 6.0 2.5 23.0 0.0046 0.0019 0 0r76 0.546 0.228 2.093 Date Time Tesl Begm Trme Test Ended Meler B&ometflc Pr6sure Orifice Pr6sure Drop Met€r Calbraton Y [&1or Volume C6 Smpled--Meter Condrlions Atg Meler'Iemperalure Are Area Blocked bv Smple Tran Stack Cross S4nona.l Area Probe BlochSe Factor for PM2 5 Sq Root Velocrty Pr6sure Corected [o, bf Sq Rool Velocily Head ( 6 m6ured) Sq Rool Veloci& Had (ad, lor blocka8e tlnecss6.) Weighl Waler Collecled Duraton ofTesl Pilot Tube Coeflicrenl Nozle Dreeter Volume o/o Cdbon Diorde Volume 7o Oxy8en Volume 70 Nrtrogm ed Cubon Mono\ide Volume G6 Smpled (Standild) volume Water Vapor Frelion H2O rn Srli C6 Fr&lion of f)N G6 Molcculd Wl Dry G6 Moleculd Wl Slack Gd Percenl lsohnetic 06 stred viscosrty Dry Cs Smple Rate Samplmg Rate Rcynolds Numb.r CMmghm Cordtion Facror rg PM2.5 PM l0 Cul Pornl PM2.5 Cut Potnr. Condrtion Built In Re-6nmaled Cmrnghm Correction Faclor PM2.5 Cut Pornt. Conditron Burlt ln Rarioof Dso/D50-l (0.99S2S l.0l) Avg Stek Temperalure Stack Cross S@tonal Area Shck Static Prssure Smple Pod Buomelric Preslure Stack Pressurc SI&k C6 Volumelnc Flor\ Rare (Std) M6ured Skl C6 Volumetnc Flow Rate (Actual) Mesured Vel@rty of Srk C6 M6ured M6s of PM 10.0 Pdiculate M6s of >PMl0 0 PMiculalc MN of Conde6ibles Concfilrauon of PM l0 O PMicullte Concenranon of>PMl0 0 Pdiculare Concentrabon of Condensibl6 Emrssion Rde of PM l0 0 Pffrculare Emission Rale of >PM I0l) Pfirculate Emrssron Rate of Condensibl6 0.0058 0 0080 0.0037 0 0030 0.0238 0.0167 0.709 0.9ss0.450 0 3s82.897 1.993 T t T T T 7.t 4.5 29.0 10.4 3.9 zt.7 0.0061 0.0029 0.0194 0.7368 0.3451 2.3277 t I T t T t T I T T I T T T I I T I T %t= A, '= ASAP . BtLr ' B,,, = C.p,, = C.n,. = Co: = Cn= Lptrtto - D",, AH .- At-l@ Al-16 = D,, = AP -. DP;o = D.= EA= Ef"p,,, = Efr,r. '- Li11,,,,,,111u = ERt'r'' rn = EI{\ - L= rnBtu = M.u,,d = M.,,rt = Ma -- nilnBtu - M,lrro = Mr= Irs = Method 201A I 202 Nomenclature percent isokinetic stack cross-sectional area (11i) See lAP Lrnit heat value (British thennal unit) fl'action of water in stack gas concentration of condensibles (grain/dscll concentration of coarse particu late ( gr/dscl) perce,rt carbon dioxide in the stack gas pitot tLrbe coefficient (0.84) concentration of PM r0 particulate (grldsct) equivalent stack diarneter (inches) orillce pressure drop (inclres H2O) oriflce pressure (inches H,O) orifice prcssure head (inches ll,O) needed fbr cyclone llorv late nozzle d iameter ( inches) stack flow pressure ditferential (inches HrO) 50% effective cr-rtoff diarneter of particle ([r) clianreter of thc stack (f-eet) percent excess air emission rate of condensibles (lb/hr) ernission rate of coarse particulatc (lb/hr) emission rate per mnlBtll or tt-rn of fuel ctc. emission rate of PM 1s particulate (lb/hr) emission rate of compound which replaces x length of rectangular stack (inches) thousand BtLr mass of condensibles (rn i I ligrarns) mass of coarse particulate (rnilliglarns) molecular weight o1'stack gas. dry basis (lb/lb-rnol) million BtLr rrass of PM,6 parlicLrlate (rnilligrarns) molecular weight of stack gas. wet basis (lb/lb-nrol) gas viscosity (rnicropoise) M,,s,,, .-- rllolecular weight of gas specics (lb/lb-rnol) N, : percent nitrogen in the stack gas O, = pcrcent oxygen in tlre stack gas r/Ap = average of the square roots of AP (rnay also be referred to as ASAP) .i4fr, - square root olAP at point I of the current test. Method 20 lA r/Af ,' .. square root of AP at point I of the previous traverse, Methocl 20 lA VAP'.'" = averoge of the square roots o1'AP tiorn the previous traverse. Method 20 lA Pbn, = absolute barometric pressure at the dly gas meter (inches Hg) Pb, = absolute barometric pressure at the sample location (inches Hg) P,' = stack static pressure (inches HlO) P. = absolute stack pressure (inches Hg) P,,., = absolute pressure at standard condilions (29.92 inches Hg.) pts : number of traverse points during tlre test (minirnum of 6, maximurn of l2) e = time of test (minutes) I I Method 20lA 1202 Nomenclature I 0, : sample time (duration in minutes) at first sample point for Method 20lA I t = :::ii*;:lnxi:lilffi [a#i;-''" p'irr"n"ror Me'1h'd 20rA Q,. : actual gas flow rate through the cyclone (acfrn) I Q..' : predicted actual gas flow rate through tlre cyclone (acfm)I Q* : wet stack gas std. volumetric flow 1ftr/min, wscfm) I [::: : Hi::iH[:l: T,,, : Ineter temPerature ("F; I ,: r;ffii:ffi;:[i,:lstandardconditionsls2s,,R; Tt = seeO I Vm = sample volume (ftr) at meter conditions I Vln,,6 : volume standard (dscO, sample volune adjusted to 68"F and29.92 inches tlg. V,u,, : maximum allowed nozzle velocity (fps) I vi,,i" : minimum allowed nozzlevelocity (fps) y'n = target noz.z.le velocity (fps) I J; : lllli"S;ff:ffi:lT,T],68,,F and 2e e2 inches Hg W : width of rectangular stack (inches) I *l: : ff:?[:"]h";::""0 water corrected (grams) Y : meter calibration Y-factor (dimensionless) T T T I T I t T T T T I o/ol A. B,o, C.0,, C"o* Cprl o D.u AHa DPtu AP,u. APn'in EA Er.p,, Er.u^ ERn,u,t),,, ERp*u M,t M. lrs P, 0l Q, 0,, Q, Q*. Qr.' Q* R.ot R,i, Vn,o" V,niu Vl11rrd X,l Method 20lA 1202 Sample Equations : vln.rd . (T, + 460) . 1039 / (e . v". P.. X6 . D,,2) = lDsr I 4). n : Y*l(Vrn",o+V*): M"n,n . 0.01543 / Vmr,6 -- M.o.* . 0.01543 / Vmr,6: Mpuro . 0.01543 / Vm.,6 = 2.L.W/(L+W) = [Q,.'. Xo. P,i (T,+460)]r. [(T,, +460).Md. 1.083.aH,,,j/ Pb,,,] - 0. I5625 . [(T. + 460) / (M, . p,)]o'uo' . (p, / e,.)"'0"': 1.36g6. l0-4. p, - M, - V,uu*2 / [(T,+460). C,,2] : 1.3686. l0-4. p,. M,. Vn,in2 / [(T"+ 460). Cp2] = (%% - 0.s %co) t10.264 %N2 - (%or - 0.s %co)l: c.pn, . Q.. 0.00857 - C.,r,, . Q..0.00857: ER / (mrnBtu / hr) = CpNrro . Q.. 0.00857: co: .0.44 + 02 . 0.32 + N: .0.28 = (Mo.Xu)+(18.8,,) T T t t I I [51.05+0.207.(T.+460)+3.24.10't.(T,+460):+0.53t47.o/o}1-74.143.8*.].t0-,' Pbe+(Pc 113.6) I : 1r/ne,'/ !ap',u"). (0,"., / pts) = V..A, - or . r/aP,, / r/AP,: Qn . X,r . P,. T.ra / [(T. + 460) . Psrd]: [('t, + 460). P",6 / (T,,a . P,)] . [(Vmu.r + V*) / 0]: F, . 0.002837 . [(T, +460) / (M, . P,)]0 "0": Q,/X.r = 0.4457 + ![0.5690 + (0.2603 . Je,.' . t4 / v,r s)] : 0.2457 + i[0.3072 - (0.2603 . iQ,.' . ]r, / Vu' ')l: V, ' R,.u* : Vn' Rn,in: Vm. Y. T.ta. (Pb,n +AH/ 13.6)/ [Pua. (T,, +,160)] : 3.056 . qr.'/ Dnl: 8-s.49. 60. Cp../Ap. {11t. +460)/(p,. M.)l: Wt*..0.04715: I -B*. T I I t I I t T I I T APPENDI* B I Preliminary Velocity Traverse and Sampling Point Location Data I Particulate Field Data Sheets T I T t I T I T T I I I T TB t N B Stack Dia. Ports are Ports are .1(r.5 Reference: 6 35',Upstream from next disturbance Downstream from last disturbance45', Preliminary calculated Comments: Averages: T, Lt"o ZFlow ' ri I AP KEY:> r/ap Ts ZFlow AP Stack ldentification Kiln #3 Baghouse Date .' .' r.1 r .'-.\ Barometric Pressure Static Pressure (P6) - . L;* in H2O Estimated Moisture (Bw.) 12 o/o Sample Height from Ground 50 feet Traverse Point Percent Diameter Distance From:Ports ID Reference A B C D E F 4.4 2.05 8.05 a',,f,3 j.) 1L 14.6 6.71)12.79 ,y1"Y1 -)29.6 13.76 19.76 4 70.4 i2.74 38.74 5 85.4 3().71 ,t5.71 -.^ :, ,.Jr 6 95.6 11.45 50.45 L;t' ,'5 . C)E.6=3= uoPo r }EO6 =aCO-F '6 oo0 ) --GO o coo- . oY v!c>=o E- !a=GFO oNIo_oE-EEU T c uE ,1 , t= II,lI i'= 7,13l oaII -" =- ll r :l . l . , l 'l " l l sl aa ,' Cl l = l I -' -l e ii I l? : : i l s i i l" * 3 ' ' r i . ZE :l ; ' l l ' i l ' l , l E z F l o P + E- c / ! ; ' t l 9 7 2 H Z = i< ! tl < .q ) -; A c A .l u " >- 6L TT !!oootGe= ! , 7 ," q > o ^ . -. O .\ Y !Y * v L e - :F >_ t r _ -E ; =t - o>a oL ' l - l -l - ,iI 1 -lI 'l;L i 21 = ! FOo Co a:l(t r -Cxulo{)loEo)oco(f):ltcYIIcj ., 1 ,l :6 i- N luli o-oO0)=(Drlzs II c3=2!6EoEarocio$c c22!-cEaE6o--lcoa :^ l l ?,etro"l I nl6l IEE,dc5 co <l _ _O v (f) N q)Eo - :<673=Edpc : >E EaEO -fo"o- 0) _!GO o rc o 9o ,:6 l Es :ou-c>o:o: i F (- ) ONro-OE.F : t1ll 'l ' l =Go- o- E .= Cl, E E!oo c Z7 o t" , ' r > o n r :a p ( J E >_ c _ >i . : = 0)>6OL r c= !\ tt -E r -: l . I r{ t 't ' l z- - = 1 j Y:E=* t fL .l su !YI , I' l l ' i l , l ; , o = I H 2 -U E ,l , l ,t " l -o l ?: o- l = 6 Nl + f rl Y i- i IL ; lx : lt . r * I ", . t _ = .l 2 -t- t '\ AJ -t .O -a F()a at tr l (U t -c lXI uJ l or l .h l llol _c lol (o l co l co l +t lslYl iI -.1 I o-==a tI!C IIIIIlol () l0) l . .= lqlrl IT"Ti ao ? r-33 =--2!sEaE-aaLT ,st:ad -E=2!aEo=o:-lEotu a> rl N l ( f ) l v l r o l (o ro s (f, C\ j 0)tr ^3: !do^ . o >E OGE A l+-CCo -lAo ) _cGOo. - o GO o- . .= 6 U 5@ .a o u-c> ' c-o:oa C O^ FU c6E.Q o.r UE oi - Ff , =0 i o,6O Lr l L- bI r E :l , I ,l l i -l - l : l * . " 1 - -l ll == = . | 'l ' r = = ? zt sl Ee r r l r r l Sl E: il t i I l l: : l E . ' r i ll i lr , o* ,i _. !- . i e, l ;, l :l ,l i, l .l : J , l -' * 2 -4 r- f ! , e e @ E u. . l P t a - z + i = : n .i < .E , c + C ., = \ l L l U 2. 2 C 1 '* <L Z cn=2EstrocE=oalf ,.to a-,2!aEoaa-) I ro l-loa I =ioIZ9ftsonl.l 6t*lE,saE CD alo-Cxtu(l)oo-Co)oco(o:t t=YaIU? c!=-: TTTTTjTTtTt T i I= i I_ i 1 ,1 , lp a lu L ltJ - a ll = E a IL +' > - = I! IIII.t-l;, : aF()o c- Lr ) -l Nlc v ) I $l to l (o s c.) N ? IIIIIIIJololel -t(D l rlan 1! T,Ti TI o =ctrL c=EL! l Eo X X X X X X X x X X X X !cc.6q rJ .i a!:r !=a o- ? o- .a "a l! F @-c O f, l t: o Sarnple Recovery Particulate Analysis Condensible Particulate Matter Analysis Gas Analysis Data (ORSAT) Chain of Custody APPENDIX C C Facilitr: IJtclitc Stack ldcntiljcation: Kiln # I Datc: Mcthocl:l() lAi 202 IIIPINGIIRS l'iltcr Nunrbcr: Final rg) Initial ts) Nct (s) -un-lLXerdcserptiur i< l)urgc start Purgc cnd i. ml I1"0 atldcd r .. Sanrplc llox I n il ials I lexanc liquid (l I,O) ir irrpingcrs. (rnl) T T t I T I T T T I I I t I t I T T T IMPINCjIB.S lrihcr Nurnbcr: Irinal 1g1 lnitial 1g1 Nct (gr *#suaelelluau Purucstan i,:'-----s- l'urgc cnd nrl l l,0 addcd r , Run: l-- 'fotrl t*,___ J '.' . 'i RINSES tlro Acetonc Sanrplc Box: D I ni(ia ls (hl,()1 in rnrpingcrs, (ntl) ' .i )L .r-t 5t .-t, ir .l IMTTNCERS Filtcr Nunrbcr: Iz ' .-. Finallc) Initial (gt Nct (g) prn-fiXeldexriptiop l)urgcstart ''" ' I'urgeend ,.- l-:,i nrl H,0 addcd 'l:.. Run: t Total 1gy Sanrplc Box: I nitials lnitial Volurnc of liquid (l{:O) irr RINSES H2O tcctone I lexane t T T T T t T T I I t T I T I T I I lfacility: Stack Idcnti llcatiorr : lriltcr Nunrhcr: LJrel ite I)ate : 1ll0l20?-4 [{un: Sarrrplc 13or: Kiln #3 Illanks & Rinses Filter PM,,, Wash > PlvIro Wash I ( omnrcnts: 487 Acctonc lllank Corrcction 0.(X)(XX) gi l(X)ml Rinse Vol. []iltcr & l)lvl r() 'I'M,., I,Mr, 7.1 ntg 't'V,,, '1.5 nrg Total I 1.6 mg l) I llc,c shilll l)c nt lcasi b hrs bctuccrr rrcri:hrngs l-ab "[cchnician: Mikc McNanrara l.ab 'lechnicran: [)can Kitchcn ( l(l l l lili\ io ntl nr! l:inal ,: Irinal":0. r 202 [)irrul,r1,.;: 0.1203 g l)rcrvcight: 0. I 155 g Net 0.0048 g Net ,{.8 mg 60.8932 19.9407 0. r 203 () 5 t, 0.(n2l _q 60.893 r Iinaloyu: (r0.t1932 g lnitialny6: 60.1t909 g DaLc: 7l16l?021 l'inre : Dur.,l7lr,nd2.l I inrc: DaLc: 7ll(t12024 'l irttc: 8:00 D.r.",7iTM Iin,.,llJxt- Date: 61712024 'l inrc:Dut.,?frilIEf tirrc: l)ate: i 11612021 'l'irnc: tl:tX) Datc:7lEilff I in'., -il,rttr PM ( lnftrrnration ()nly ) l:inul^u,,: .19.9409 g lnitial,rr,,;: +,f .rXra g (iloss: 0.00,15 g t3lanli: 0.0(X)0 g Ncr __0.00a1_ 9 Net ,1.5 mg Irinal,: lrinalz: Initial,: lnitial.: I:'inul,: I;ina l.: lnitiall: I n itial,: (r0.Iil909 (lloss: Blank: Nct Net 60.tt90tl 0.0023 s 0.0000 g 2.3 mg Ileakcr Nunrbcr: 49.9,1 l0 ,19.9364 49.9363 Ilcakcl Nunrbcr: BESUTIS I'M"r lrilrcr (M | ) 4.8 mg I)M1,, Wash tV.i 2.3 mg Total_LL_ mg ( ritcria | ) \!crglrts ilrc | 0 5 rtrg ofcach other. or within l'!o ol thc nel \\ught l)aLc: 1 I l5/21 Dlrtc: _ 7/16/24 40 -l( ) 3.9 tt0 I T T T T I T t I Facilirr,: [Jtelite Date: I1l,012024 flun: 2 Sanrplc []ox: t) Stack Idcntilication: Iriltcr Numhcr: Kiln #3 488 Acctonc [Jlank Corrcction 0.(X)000 g/l00rnl Rinse Vol. Irilter & I)M,,, :, pl\yl lr ml rnl Blanks & Rinses Filter t c'onr1.rcr)ts: (lR I l trltlr\ PM11y Wash I'inal,: Ijinal.: lnitial ,: I n itia l.: []cakcl Nunrbcr: 'PM,n lrirral,: Wash lrinal": Initial,: lnitiall: Bcakcl Nr-rrnber: 6 | .9033 62.t971 0.r 194 0.1 194 e b c g I:inal,: l'inal,: Finalqy6: 0.1 194 g Prcwcight: 0.1 144 g Net 0.0050 g Net 5.0 mg lrinalny,l: 61 .90tt8 g lnitialnr,',-?]EI-g Cross: 0.005.1 I tllank: 0.0000 g Nct 0.0054 g: Net lrinalnu,,: 62.1971 S Initial,ry,;: CrZ.trl:Z g D.nrc: 711612024',Iirrrc:D,",1iTffif, rirnc: l)atc 7 16,2024 I inrc: tJ:00 I)"t.,lrGDI]r Ii,r,c' ll:(x) Dlttc: 61712024 -[ inrt: Date: 7ll6l?(t24t-ti.",1iiffi Dittc: 61712024 I)ot",?llDEf PM (lnlirrmation Onlyl PMr,, I().4 mt .1,M,,, li.9 rrtg 'l'otal_LL1__ mg t)ate: 7/l-512-l l)atc: 7ll6121 6 L90ti9 61.9086 6 t .9034 62.1971 62.1932 (r2.193 I Cross: g lllank: g Nct Nel Plvt r,) 0.0039 g 0.0000 g 0.0039 g 8l I RESutrs T tiiltcr (M r ) PMr, Wrsh (Mr) Total 5.0 mg ---11- nrg ----l!'4- *e (-lt(eiln tlWcrglilinrc to5rnAol cachotlrcr.or r!rlhrr l9"of lhcnttwerght l) lherc5hnlltrcatlcail 6lrfst)el$ecrrrvctultrtrcs Lah'lcchnician: MikcMcNamaraI I T I T I T I-ab Icohnician. Dearr Kitchen I Faciliry: Utelite I )ate:1il(\12024 Stack Idcnti lication: l:iltcr Nurnbcr: Kiln #3 I{ trn: Sarnplc []ox:I 489 Blanks & R.inses Filter Acctonc lJlank Corrcction 0.00(X)0 gi l00ml Rinse Vol. I:iltcr & PM,,, > I)N1 1,1 l0 rnl nrlI30 ( l{l I i:ltlr\ l:inal, I:irral. 0 t 1.59 g [--inaln1,r,: 0.I 159 g l'rewciqht: 0. I 153 gt0.1 I 59 Nct 0.0006 u Net 0.6 mgtPM,u Wash l'inal1: Ii nal.: Initial,: In it ial.: 62.87 r5 g ltinal,.r,,,: 62.ti715 g Initial.ru,,: 62.ti66 I g (iross: 0.(X)54 g Blank: 0.0000 g l)trrr::7/16l?024 l-inrt:: 8:0() 62.87 t5 Drrt"'.7lGili T (r2.ll(16 I l)atc: 6t712024 '[ ir]lc t)ut.,7,rlTD6il Iirnc62.8(160 Ncl 0.00i4 r I Net 5.4 mg Beakcr Nr.rntbcr:82 r PM,u Wash l:inal1: l" ina l-: Initial, : ln itial": 60.6705 <t s liinalnyl;: 60.6705 g Initialnu,,: 60.6680 -0. Datc:7116120?1 ltrrtr,liitfizl l'irne : t{:00 T 60.6705 (iross: lllank: Nct Net PM r, 0.6 0.0025 c 60.66'79 0.0000 g ().0()25 g I)atc l)atc 61712O24 I irnc: 6ln/2(lA 'l'inrc:t 60.6680 2.-5 rng T Bcaker Nuntbcr: RESUTTS I'}lVl (lntirrnration Orrll ) t;illcr(Mr) I)M,,, Wash (M1) 'I'otal r11g r1'lg mg l'lvl ,,, ,,M,,, (i.0 nlg T 5.1 2.5 lng 6.0 Totnl ll.5 mg ll I lterc slrall I)cxt iur!t () hrs hctrvccn wcrrhlrlr( ortrrncnts: T T l.ah'l'cchnicinn: Mikc: McNarnara l)atc: 7/l 5i2021 I)atc: 711612024[.ab'l'cchnician: [)ean Kitc,hcn T T I I T I -o \ (, oEFoo +' o*( n E=Td. t)E't :U(€ oo a. l 6t =a. l€r- iN(\\o =! - c. l \o {'cl00F tota.{=\o -d '6l .a\o =l00F- c. lcl oc-+c.la. l 6ractFI oot- -a. l c. la'l @a.l .. !c{ 6N6lN alal \o alFI F-coF- €$.1a. t oo:1 . (. !c! &!f ,q6l F-olcl atcl €.. 1a: t ra(\ { 6t al& E-- io& oF(J tJ il ! EEr o 6 q,ctrC)u O6 c. l oo ol -s6looF- s(\c. t \o $N\o <taloor- 'tclot tcl\o caoo l- r F-+\oc'tc. { €.tcl a. t €+\0.lFI ao$c]N catc'l c. l inN r-6I U F.6t \ooor raF- 'cl c. . l dl l- . .c\al FI rra{N6t otc{ a. t c. l a. l 6I NmFI .. !N N t- .N a{ \6t d. E6& oEL:o il H ... :(.)& E.Fo! 6 (\ O$ c.t $6l rcr- . .+c. t(\ $N\o ?..l@r- :t6lc. . t \o at- a\oor\ ct r- .clol t- .F\c.l c. { o\r-.laa cla. l cl<+c]ol ra!l.!FI rat'. . \dN \o r, ) t- -viN €c- r-GICtl a\ .. ' l 6.1 at ]- . {a ).ial o. a. J .16l o\olalol o\a{a.: ".1 ia6l t N o\ 6a :t ro.E.Eoo.JcEU) o-(i .EC!5( ItF,!()co br ) bo ot or ) b 0 hI ,- i ,- l .. , -N - g vJ al =: ' 6 ls , E B () 0 J - >> € cg c i E cc o ) o0E>.E(do0d=.LE == F = h [ t b 5 t E =E = A o E; ? 2 < ^: v^ ! 9 - -T > Q L EP Z Z a €. = , , i > S <d d, 1 .L 2 CE > ' L -! , 5 E d, o0E'=ouLiiE!oE o.Oo.Eo,o It'ai)vCq() o0 0 0 0I bo 5 0 0I aE.9(dol),-oz:: .E-oE q,E-i'Uo?iE hl)ErU:l6u.;E o/)Ez)o?.EE -6 1 -q vv bl == ' 6 lg , E B (J c ) - BI E cd ( g r CC o -N - E vv hI := ' 6 PE o > ar ( , - >> E c6 . d r CE :: ; a 9J - c. l -c -- b{ :: ' 6Er 3 , > aJ o - Bi . E (6 6 t r Ec o 3l 3 l ! C;L uduEo:lOU6:qEl)C) l--c -t r r .v .o tt s== c! c 0 :E :E oo EELL f (,(g6EZo2CJt'-.;o6J?-_od-iAJE,i :a.) :t ro @aaE-Eo'c ,cooI!UzuFTo-ca:Zcuooa 3 alF-.(,ooFtrt.;(.) .;Ca Dtroo- JoooIt! lr6L(EJ6l6lq,2 IITITIIItTITTIITtTT =l = l r cq U €rlaao-o()ootr l ()7. cooFU-v ,(!ou()OJ -l-o- -lSIFl ,lq/(nUd(,F:t lvooO'o,, yo(h )Foo. :lo(J .=6));'5(o cl I6l(\o ITITIITTtITTTTttITI ()l)IcdA/ LJ.: ._ )uF-. odJ CE!(dtr7.OCJ=oqJFCd J -+ > ,a ,t t= Eoo =s rJ . LL coooL o\Ef()& It)E't r0)Cn IJ ;! a-o. \oE.L'-. . :u& o.EFoGo oo \t 6t O O@ <t ct wc. l€F- . .fc{oo l- - $c. t a.. l +C\ \o $a. l ooF- +c. too t- - =lctN <- c, t o\ooF. ooc. t .. i $.!N 'crat\6l C.l c. ]N c]C.l ?ara6rc.t Ir - \o r- o\F\ €+cjcl \o.f ,al c. t a\ot..1N .t r .. 1cl :?lf(- lal V)ra!e. !N r, . ) 6l -v ,dqL()o()& EJr oC)d" oF{)(BL.J :; n E6d (, 't r4)Cdo @ t N O€ o'+ c. . l :f ,c!oor- . +c. l ooF' $a.lN\o sc. l $c\ l oor- . .fC. l ooF-- $c. lot \o a{ oo€r- r-c.!6l o.n6t 6ra(NN oo .. . !6l Na{ o\ rf )(\ei t o\ \o o\ oo\r- aao\+c'lN o. !+olN fao\ i.!6t €l'-tf ,o. lCJ ooF-<f , c. l .J €F- . *l r.lN ora rf ,6t ooo.o0)o0.,o-Ea Uo(dCI 6) I()m ,{ -{ .- t -G l - E vv of == ' d EE , F 6) 0 ) - dd E o E.9cgboo(B O0 ) - - , T J XE = ^ o BS E + < A: i .: i l r = b r : E E y7 3. y 2 Z a !. : r > : Y d A 4 'L Z (J = 2 ' i , t' . H E d EB,9rtg0o6fr .Eo U.9(!olo r0) -vcnoco -o J - C vv dF= C ) 38 , > () u - (d c u r o -G l - C va / h I .9 p .s o , (, 0J - ?- . =cE ' e tt O E>.9dar )o0)zooE E4UFiieELoF,oE lr tl =i cJ l ^J ;l ; -l = Nl F - Iui i oo oEou 0)oVC60)o;.s.9oq)F-oJ CdEdzo2CJ*z.;.9.9oOJF-o6J o1'Ic!EOIa E-. :0)& ()E't :oo oCOxC)J € c. l O vNooF- tNN\o va\o 0, )dx(.) :l@F-a vF- cla\ \ooc!N \or. l e. l 6l c!al r-Oc. l 6l f.lal 6l a. l \o ^r * + c'l GI - CNU(. ) iI E6d, oi:o(uo ()o6)o OC; N <f,Noor- - <ra. tN\o rfc. ) \o o()o $\oc. l o, r- o, \oanc. !al \oc. t c. !N 6\ot. tc!N \o\ocf )clc.l €\ocnc. l c. l i' - . \orac. !cl t) \oo\ +o ! No 0)OIdoUU& EJ- to 6& (.)E't :0,)(!o L()> € N sa.looF-- !f ,a. t o. l \o v(. l o6 r-+tLr-oa. l No\ r- . F-- o\F- o\r- @t- . oor- €r- . NN a. t n na l NC ; c. lc! c. iN (\a\ .. ]6l nN 6l (\ l *!.9oo()oJ(nc0 J LOJ -vcd0)co bo bo ot -N t v i, b/C = =' d EI g , B 0) o - >> g dc d r r- r - 0) l& l ! > bo o o oI - c. l -c vv O, .s o . 9 p , c) o - -? . =do t r .= .= te C ) ,6 ^6 . : qd y 6 6d r a (! 2 = d =J :2 -v , = 2 d (O r ' d ; co i < : r 'A (B . = ar - a .i c O o ) Jc- t iLo6 xCn cac.t e.. l F- ..:6)CUooFcJ;o6dotE() 'ooa :)o)loo(,) .=Ef,>.=()cd lJ . Ir(Eo6,o! q)oh. .\ talo IIIIITTITIItTITITtI Pl = l s ooEoI ()cBo ()CNo (. )()Vd0);CBo(J()F-oCdJ IBHao(6z(. )0) I;.g(.)oF-o(cJ (JLC!hla E6d o.Et-c)dLJ o(\ ,x() oo t N O .i fNoot- - .sNoot' sNN\o .+c. l cn\o 0)odx() I $@r-aJa F-o' r- \oc. la.l \o(-. 1a. l al6l al@c' l c. l o. c.1N \oai .I cn o\ (\ l *c i U)U() .2I! E6 (., .EFC'Cga (,)oq, 6 O$ N O vNoo t- - .d -ot@F* sc. lN\o $ol \o q)o0)o cf)t\ool \oF- \oc. ) .. 1c{ Ot- -C'nc! r-(- ).lal c-\oc!a. l r-c!c' l o\ \o?a l .Ic. i c.)m <. .a r. r c'i NO (.)OI ccoUUd, E()d, C)E't :q)o L() O@ $ c! s(\cot- - sc!@r- Nc{ <f ,N\o LOJ NU) o\ t- - .. l c. l 6. 1 C\cIo.l alNat 00cl(\ o,clGt o\alFI ra Oc. l oOoc ) al o oooLoC)o-:Zco oJ *()J()c0 - C. t -C vv C U : =' 6 EE } o0 ) - >> E -_ : - cc d r cc .- . ; o -a \ E vv E U .9 1 . S o , oo - d( d E o0 oJ J 7 ol ,6 .6 -a qd Y 6 A- * A c6 2 = ( n E -, 2 * E (6 c U / c 6 E 6* = '; Hp ,9 6 3 p -vc0 6 x6J fr€!q,)ooCEc,GJ(\a(tl0)2 ITtTITTTIIIITIITTTI I I Location Analytical Method_FRYRITE_ I D.,"_-.,;,,...+_ Test No. , l ^,:fi:ff,),";OPerator ..,tri". T t I I T T T t T T I Gas RUN Average Ne( Volume 2 3 Acturl Rcading Net Actuel Rending Nct Acturl Reeding Net CO, 147 L.r 1Z lj,,tL- O, (Net is Actual 03 Reading Minus Actual CO2 Reading).)\. t,I q.o iq.t, N2 (Net is 100 Minus Actual 02 Reading). Gas RUN Average Net Volume I 2 J Acturl Rearding Net Actual Reeding Nct Acturl Rerdins Net CO,ll ^!i (- rlL1 'l - Ir --irl-Lrt ,] 02 (Net is Actual 02 Reading Minus Actual lO" Readine). i 'i,)I I tl, i-, (a '; \2 (Net is I00 Minus Actual02 Reading). Gas RAN Average Net Volume 2 3 Aclual Rcnding Nct Actual Rerding Net Actufll Rerding Net CO,-,\c L{..t '{.o '1 L)-t.;i O, (Net is Actual O" Reading Minus Actual CO. Reading). 11.1 l,t. 1 lrt.'1 'j .- N2 (Net is 100 Minus Actual 02 Reading). C0 is not measured, as it has thc same molecular weight as N2 c0 'o(.) (1 )(.)() EO(JC) t)0)d, es u r u T, q3 l u J to s p as u l u pu e rl J l u J zo z H cs u r u T r{ r l e J lo u s d o r d o s l rs r ' n l l sa u 0 x a l J ?9 os u r x ? r{ 3 1 € f , oz qs P / A lu o r c es J u o EE(" )()o(J rf ,() tao0) l)ao(. ,d. l- J()otr(( ,a ,c()cd .9;oo()UFFoo0) .:()E(JLh()o.Ecg0 -IJo:,a-)UcF ( tI.-G--U =r 6C ) L--o tcrC€ .o a u. ^ bO (, 6l .t i \c -Em= -r fC) a'=?= !aoQo. - .2 T, tdr, l o (J ( . ) a= (J(.) AvUt- l FdE' i TtITTTITIITtTIIItIT T T APPENDIX D Figure 1. Facility Schematic Representation Raw Production and Control Equipment Data T I I I I I I T D ,Ja,) )sA) ac :1 . . o ?3U oot>u!t!.J a'-)LLotl ) E 6 E E = l. E Z ;- o ei t u c T . 6 A =- Z 3 E Y E 6 EE + - € ' A ! r EP E E E E I EF E - r ! Bb+2 2 oi _ ; oec- O n q( ) 6 O l' = Hl i ii i5di -r(- l .lal ct ::r .. o ir ' .: f ^l TNt C)acbJ l a. )+tV;.96o.;U;os(n t- l F. {o o1 { -| Jdt- <ccU(. ) Irp { pr ( ()+J ) ITIIIItIITIIIIttTtI T I T I T T I T T T I t T T t T t T I UTELITE DAILY KILN REPORT KILN 1 5:00 PM 6:00 PM 5:00 AM 4 END OF END OF DAY SHIFT TONNAGE NIGHT SHIFT TONNAGE FEED TANK RATE TPH BH DP GA5 SETTI NG BH TEMP ID FAN AMPS KILN EXIT TEMP COAL MILL EXIT TEMP COAL MILL AMPS COAL SETTING d ay7 d ate 7:00 AM lu l.'-- .,' I .tl ')1; 8:00 AM ti I l 9:00 AM V(-'7 t':: t0:00 AM ?'- ,|)'^t i - 1*i t:: 11:00 AM ..., "i I 12:00 AM 1 '),.'|I 1:00 PM )I 2:00 PM a,1 t | -1 3:00 PM I 4:00 PM ttl 'tl I1l:, l"l I 7:00 PM :',, 11. :l IiBrq**;:ti {.,v;!r 8:00 PM ^r+r7'l'-.-ai . .xJ , 9:00 PM I - i-'ii 10:00 PM 7r l: '2, 11:00 PM .,*.,i| 12:00 PM day/ciate 1:00 AM rt 2:00 AM 3:00 AM A / ".1. 4:00 AM .1. , ,,:- l_ {'- t,{,1 6:00 AM KILN OPERATION KILN 1 (3 4 (circle one) DAY SHIFT: Thurs thru Tues: (12 hr shifts) Burner: t' ,',,,i{-,' 7am to 7pm; Wed: (6 hr shifts) 7am-Ipm & 1pm to 7pm Utilitv Hand: Gas on:Gas off:Reason:Aft:nf -. KILN OPERATION Gas on:Gas off:Reason: Gas on:Gas off:Reason: Feed in:Feed out: Feed in:Feed out: TANKS: Silver 0 1-.t-jt;0,'1" Orange 0 r I 0.+"{f' . -..) Rusty Coarse Problems, Concerns or Events: NIGHT SHIFT Thurs thru Tues: (12hr shifts) 7pm to 7am: Wed: (6 hr shifts) 7 pm-1am & lam to 7am 11 ,,Utility Hand: i Gas on:Gas off:Reason: Gas on:Gas off:Reason: Gas on:Gas off:Reason: Feed in:Feed out: Feed in:Feed out: i'. i?11 - {, r TANKS 5'.* ";r,t4 Silver Orange Rusty Coarse Problems, Concerns or Events Bin Vent: I I APPENDIX E I Calibration of the console dry gas meter(s). pitot tubes. nozzles diameters. and temperature sensors were carried out in accordance with the procedures outlined in the Quality Assurance I Handbook. The appropriate calibration data are presented in the fbllowing pages. -fhe nozzler calibrations are recorded on the first page of the field data sheets. t Figure 2 Schematic of Method 201A1202 Sampling Train I [:Tl"i;i1;*'.J,:t?Ah,il:,:"1'Jl?l?:'i:'''Type S Pitot Tube lnspection Data I iiHBff;l"Jffil1lile Sensorcaribration E .C(oLt- -o)CoE(gaNoNoNEo.C0)oC) (sE0) .Co(t )o. ioLl.9LL ,x o / o + fi s coEoo :Fu= .: o. o)dqroc l o;E( / r P Efd l t; EfLEg 6Coo I Fa t l ? *\ il r re Oq - l= ( F \ . n ] - f i .\ \ TA . J I I , '\ . \( -- lH -: . - \: U \ J ' i E fl Y. - ' o t l l ; = g -" - < r o . t t " g a rf l 1 1 + ) [i i 1 't i l -i 5 \- t ' u ' v l l t r" z { = ( 1 i j . , ul !oo!c!. aB tl l l - 9t () E-rrIuIL q7 od IIc alt ofoaoEoEF tTITTTIITITTTIItTTT ugozuqUft:dUzu e Sr l g gi l r l El r l : l nf ; lE l "l ; Hl r - U5 ao ,^ot d u Nl - (9 ci l -. ' s\ , ul?, , :f sl s l El i l 3l g: l : l El il sl El E *l , J l { l noaoF()LzoFdd)JL)duFrlEoU(,e.U [[ [ oo o 6l -l 6l> o l { l 6 l > N t 6 1 6 l > El 3l 3 l < 3 l El gl < 3l 31 3l < :l : l 3 l il s l S ;l ; l i l slcil \l ;l @l o t r l o l o t t s l xl 6 1 6 l N I o l -l ol 6 l N l 6 1 6 l E l rl r l 6 l -l Al d l il d l @ l qi l dl +l oo o € 8 6 o6 @ @ n N c3Ec!!ToIE9- d ._ ; : r'. l l i; 9 r:. cL * fi - 3 q 3, , , ,, o' - l 3 6c> I:. IE !(, il co5c!oPO o- + o- . i o! - o OL E ,> U =" - (D o u oo , -9 ; qJ - 2 6: (, off o: o@ ; *, . - { or , , ' n'dz ff i f f i f f i aq u l ff i f f i f f i tr t r t r E6!;e tj6a=6H5! -66o o- 5 <E o o- 2 h oh =oE 3 (i -Y O 4, 1 P U E ' : .t 6oz p 6E . =F > q <ri nq r .! a^ :J o2U= d-@5EUt r N N F F ts N -d o S! ! :E@ 6€ O-H< - xH2i E tr qs3 (O>6>qLO gxo I=Un:UdtItFu=oEo dEoR JEEz 3E " l_ : l ocsooE.q l3- ;E 6 o. * ) Y o_ o xP ! o " r: ii X o o -- 6 = o E^ e : E = .r o ; , - e -E B, i > ij f r a - . ; r . +3 E e B e O= = - :E : = u = -= ; u o; o- E 6 60 g (, EE S e c o: = E = o o: f c o !u F'_ ,^ Y - c o 3; ! E E - o- - C 6 b. = E 6 o o= 6. E =o ; 9 c 6 00 i J o p a; > 6 ;! 9 h € x! m 4 = 6t i . P 3 o Ol dj O at E c t coGi=(!oIoLt(\o$l auJ(J lJ -aoJC)FE.oozafzoFtmJotUJFul=aotolooo-FtuE TIITIttTTIIItIITTTt eFzqEcfoU r- I - ] Ui l +i i JJs< dGBUTFUU+u Eto) T- - l e llFtt a Ir l o lE l t: l le l rl ;l I ls l B l ll - l . l i i i it- q3 E =Cil r .U = Ergl >= EI>l- 6l F l N l ololdl ot 6 t @ l N l @l o l o l @l ol o l o l o l ol o l o l ol LadazUot!tfl-trucEUF FfozUOzNtxUUE -t o @l o Fl-dl >E lox 6I r-;o#ll, l ff i [ I r o HE M [ T ce!co t) i-6'6 ! ;E h *v a '7 0- - tr , i o u il r 3C @ ., @ .'- 6 H 5 g' ' H ,. 4 - -; D -'Y 4 i; ; u o c, - o -- : o': o o: 5 o = E 6 EP = i o o P e -t r b I o *h I o- ; :t ' 3F E o. q 6 !; J6 v 6! o tr - : s 3. E e o< < 6or l il i r_ d J56c>9 II E Io -a , ,i oI concoopoDcqoooOooojC'o-fof,c!DoooooEoooo0Efailn, i j *l4i .- : \|\i !q " ? q ^l-: : ri i l: IK,:+ =6?E5a -6 €>6>E oaOoqd i E6a3SP a- ; Eq o o: t s zo - ^ ir D hE 9E g kB e dE 9 o ". : :i * ' <= > od - o 8. 9 <: H uE q E e= o: E t x> () =o tr go =d a6. - - I= E z* 6 @E t =F > qo o dd u i N o ff i f f i f f i tr [ I EilgoF(JIzotrum=oE,ulFu=U)4odorlJot]U lo lo ilo ol o l o r > ol 6 l t s l < .! l c l l cll !i ! l ! l ol D l ts l .? l nl nl {l r l i l c F @F o F oa o o @ oo @ €q =EOco= a2H= (- oSEUt r F<U. zEioi62 - JOiH@@O-H3 xu -U5r o tr q 4: .E+ >6>u r9 IEo UdC(JtFUEoul0JJEEuuooe. t s UU FOEg rao)oFe o(Etrooooo- ii ' i tTTTTIITTTTTItIIITt -degRd[ J zl t; l .L : l oFzU=Lfou t d+ 96 5 =[HE FE = oocgPEgooo AouJ gou IL X U di l e E oi E * JY b o (J O 5 F F iU O 6 FO G = U t E 9: 3e o b 3 ' l r ;6 ai q. 9 E €= = ;E t s S " A B , f r E : . { ' :r Eg E eE A *E H i E a E ot - l go H !- = Y -c 6 3' E E 5: o!v t- i m gE E€ \J = 3: OE d. 6 aE 9E Iu fr o i. q . E F i* E E p Ul ti F : oE E q eE eg 9 G o > d a Eo g hp 6 sE : fi E oo t x o tro FN o e rl )ooIFTU= T I I I T T I I t T t T t I I I I t T 1'ype S Pitot'lirhe lnspection Data Pitot I uhe Identillcation:5l C-,1 'l'cchn ician 0 .375 M. McNamara I),=Is Pn = Pr, 'r Is 1.05.D, s Pn&Pr, < l.i().D,? Ycs Pr-0..126 l'n =0 426 c;< lOn 0r= c7< 10" 0:-2" 0, t5" 0:<5" l) | - lrr -t" z ---------+ll<-----;l Z<0 t25in 0 029 ----'sy--t ": r' ,z/- J s W < 0.()3125 rn( -'---- t -l w: 00t5 in ----lJ-- - i.,''r\ i ai-'..:;l-c|=- i' lTffiI i W > 3 inches 7, > 311 ]rrch W = 6.75 in 7.= I it f,'- -; -:---Q[rlffiffi-l- r , Yzrirrr:hcs Y._ i r/2 in The pitot (ube rneets the specifications lbr a calibration lactor of().841 Yes Continuity Checl ICL WAl'ER BOIL WA ER stLtCoNE oil- Dif'lerence I T T T t I I I T T t T I I I T T T T Ut6/2021 Tvpe S Pitot Tuhe InsDection Data Pitot Tubc ldentification:5l c-2 'l'echnician 0.375 M. McNanrara PA P8 tn. Is in. ls P,r = l)B ? 1.05 . D, I l'r& Prr S 1.50. t),'l Yes Yes Pr=0.470 t-"1 ["1 P 0 470 c1 <l0o 0r = u7 < lOn ct: = ln I 0, '5o 0,'5o 9r = 0:=J Z<0. l2-sin. 7 =0.065 W <0.0.1 125 in.0.0 l6 -i- L- -........_- ':______La;1..\.i*:i__:S:-cF--nHrffil i W>linches W: 7-> 314 inch 7.-: 5in lin l'hc pitot tubc nrccts the spu"cilications lbr a calibration thotor ol'0.114? Yes Contrnuity ('heck ICE WATER ca lr . (€Lzo0, ll€z. gE G C !u . i F Ao > r i " ! d; 0 ) L !; : - Iv- l 9 l- I J i L{ LO J o. tHoF cOct )r)o, l sc{ \o(\c. t =oo(.iaC. iE.EC)>d ) io-( JY> , ()Fa. z, <t r 4 .) \ t- = 6c n -( s \, u N-fr t r rr OC Pl r r! O- c C) eH' t 0J 0.) qgo- o- F=U( ) C) 0 J oc ) CCoo (€ c g -o -. o EE r* / L) oAD (l)a aL!m r( r " € t 'i t ?LJ_ O tr - + LJ t4 ll a c ll . t €l>: lA. l .r : l I Jl d ; <l - : .U ts;? i,.. i , f ll l lhd -4 . D, \J (J E EA E H ri 5 J? oo . E g, E Er i H !o - ) v Ct r e \ ) -t J o *H E 9 .i C. h / r v i- l -v EE E E] JF v)C) co o\q tr ) o.g0)cEU\J 6- ir '. = ^o Ea o- ; E rr Y ? o .a $ o o F- \O \O F- I ' - t- - od c i O\ O\ oo oo o o oo $c o c a O c. l ca<)-{ llC) -oo o\ \o\- oU o(60lo0. )bo() LG) ItaC)F c{ ca C)H' or b\ o Zf - g\ , -I.-)r I .+ J rt s (a {iIo-e)+iac) t' rA-ltt+) !r nF€&i F- (!0 -Io.-+.GLA-, !---U-c)-It-I--F- l 1,-I.--0, ) ---Fr+.o{i a .l0i \JUtrHFl TTITTTtITITTTIIIItt o$ooF3d.oc l ;- -f =rE- ta-- ac'lgl -oo .3 ; (ll /<.OE a= ld o .: a ., aYc! ! ai co oEzoE(JTo g E Ga rv F 6 ^o r - J < < / t: d J =! l i s-(- ) v t s 0. ) ^ . o c d E- I J r ! L6 ) tc)F cn.1rnc{ $c\ \oc. l c- l qilyoo, r - _o c o 4 '. E =ocu €' r _a j '; =ue 4J lJ 5 o-; q) -s <- ? L.J -^ A L( J - o m c - : { - d- l - r( . J - .9 < a' t ,5 d: ' '; s r O E -a a* U- as (/ ) ur - ll X -: E =r ( . : y E 3 n x E cC ^ ( ! C 'i h r r O .J LA , P e ' t !v i O{ t tr r C-Hc s o -- = (J !H' = ar O (J TI ; ;l qe O - O - -+ l s a EE -o o o eG q J 4 J f,^ L L q. 4 D 7 ) Qr q J a a il il b5 '. = '. = q< ( ! € 't l L lJ ( J = = G( cUU (ua a() co o\q orn 5a x = 3E E * r a t EU ts E E #, Ei q. vLr d ) v (E I \) E 9 i HE O . ) q d- c 6 xc ) l- i \ / * EU EI !4F oo = OO A tt__ r o F* r* a' - c- i - - Ir - o\ o o o oq o 9 oq $$ \ f , ,. ? vl vl oo o o.Oo.E()o4)o/dLo q)E0F tf J Af - Zf * Qr U Ubt r .- .i 9i \J I -\ -*q ) t a ,- ^ 'o = ima=+J.F E -f -ts o l >> FrIa st\ t \oN?aaIo.-t)-l.\ lLi -o--6U-o-HAI--E- l -tJ-L.- f\-,.c)s-l-F+. +. ) .-Er AvUF( rdF TTITTTTIITITTTTIITI O-f ,ooL.)j ot -- 6P. " aol ti. lo,aEa=<.OD FI o .l l o 9= ai I t T I I t I I T t T T t I t I t I I T'81'CO Sarnple Box Temperature Sensor Calibration l)are I l2l?4 Calibrator:Xuan N. Dane Rcfcrencc. Onrega CL35 l24 tinit lD cnlporfltu rc l)ilfcrcncc ("r') -2 ."> -l -2 E -l -l l -l 'l'hcrmocouple l,ocation 'l'emperature Sou rce ( l\lcdium) Ovcn (4) Ovcn (.1) Oven (4) Ovcn (3) Ovcn (4) Ovcn (.i) Impingcr Out B lmpinger Out C) Impinger Out D lmpinger Out l: Impingcr C)ut F Ilnpinger Out J T I I T T T I T T T I I I T T I T t T TETCO Annual Balance Calibration Check Dale 1123124 Denver lnstruments, ModelA-250, SN 8045284Balance Weights Used Troemner Weight Set, sN 98-115146 Technician Certified Weight orams Measured Weight qrams Difference orams 0.1 000 0.1 000 0.0000 0.5000 0.5000 0.0000 1.0000 1.0000 0.0000 10.0000 10.0000 0.0000 50.0000 50.0001 -0.0001 100.0000 100.0000 0.0000 120.0000 '120.0001 -0.0001 150.0000 150.0000 0.0000 Michael McNamara t T APPENDIX F I The testing protocol and other correspondence related to the tests are included here. T I I T T t T I I I I T I T IF T T T T T t I I I I I T I T T T T I T T State of Utatr SPENCEA, J, COX Goscnor DEIDREfiENDSRSON Lictttwrt Ctovs*or Departnent of Environmental Qualiry Kimbdy D"Shelley Ero*ttw Dirscur DrvrsloN 0F ArR QUALITy B4acc C. Bitd Diwator June 28, 2024 DAQC-636-24 Site ID 10676 (84) Dave Vernon Holcim Utelite Plant P.O. Box 387 Coalville, Utah 84017 DearMr. Vernon: Re: Holcim SWR,luc. Utelite Plant *Kilns #l and #3 * Protocol Review and Test Date Con{irmation * Summit Couaty The testing protocol for the Holcim Kilns #l and #3 received June 6, 2024, has been reviewed and found acceptable. The agreedupon test &te is the week of Juty 8,2024. Acceptance of a protocol does not rclieve the owner/operator and the testing contrdctor from strict adherence to all applicable EPA nnethods, Utah Division of Air Quality (DAQ) policies, Utah Air Quality Rules (UAQR), and methods approved by the director. Any dcviation from EPA mcthods, DAQ policies, UAQR, and methods approved by the director must be addressed separately and express written consent given prior to commencement of testing. The DAQ requires that all test re,ports include a statement signed by a responsible official ce.rtifying &at: A. Tcsting was conductcd white the source was opcmting at thc ran and/or conditions specified in the appticable approval order, operating permig or federal regulation. B. During testing, &e source combusted fuels, used raw matsrials, and maintained process conditions reprcsentative of normal operations, and operated under such other relevant conditions specified by the director. C. Based on information and belief formed after reasonable inquiry, the statements and information contained in the report are true, accurate, and complete. 195 Nor& l9i0 W;rr. S* Lrl$ City, UTllriling Addrcss: P.O. Box 144820, Sah Lr&c City, UT g4l l4,lg20 ?e!+honc t80t ) 536-d{D0 . trx {80t } 536-4099 . T.D.D. (80I } 903-3s?S fiw_doq.atuh ge frriDred on loot" rFdycl.d Br I I T I I I T I I I T t T T I I I I T DAS{36?4 Fage2 If you tarrc any qrrc$ioa calt mc d (SOl) 232-5345* omnim'e di Samaely, Robc{t S-ffiie Eedn'monul $qldi$' Divibioot$*bAulity .:t.. i',' ...;.i RS:rh crc: $@rit CounryI{ealth nemsmt "***_JE[SQ__"*ti , !-: , i . I .r1 rai^,, ,yi'1 ;r,r';1.i.,r1.jt, l" -,,, "'i ,f"i:.irl.;iir * '.'l ,rir{f: .#tJ; i:r1t1 ' i,i,*i, .,,".1E":i;*):.,{+i,r rti I .}t4r]li:rl T COMPLIANCE PMIO EMISSION TESTING PROTOCOL HOLCIM UTELITE, COALVILLE UTAH KILN #I AND KILN #3 PRO.IECT ORGANTZATION AND RESPONSIBILITY 'fhc lbllowing personnel are presently anticipated to be involved in the testing prourarn. I'he Utah l)ivision of n ir Quality (UDAQ) and EPA may have their own pcrsonnel to obscrve all phases irrcluding the process. Company I-lolcinr IJtel ite Plant P.0. Box 387 Cloalville. Utah 84017 TETCO 391 East 620 South American Fork. tjtah 84003 Contacts Dave Vcrnon Alex Judd (80 r ) 467-2800 (80 r ) 167-2800T I t T t I T t t Dean Kitchen 801-492-9106 During these tests only Holcirn personnel listed above or assigned personnel liorl the operating department are authorized to answer or obtain answers to pertinent questions on the process coiiditions or the test protocol. PROJECT DESCRIPTION AND METHODS-APPLIED l'he sources to be tested are the baghousc exhausts of Kiln # I and Kiln #3. at the I lolcirl lacility krcated south of'Wanship, Utah. This test will be conducted to demorrstrate cornpliancc wil.h the tacility's -l'itle V Operating Perrnit number.1300001004. Testing procedures will include accurnulating process and production data as well as lesting lbr [,N4ro emissior-ts using LPA Method 201A. Condcnsable particulate rnatter (CPM) will be measured accordirrg to Ill)A Method 202 and is rrot for compliancc. but infbrmational purposcs only. Tcsting rvill consist ol three test runs. TEST SCHEDULE It is planned to complete all testing the week of July 8,2021. 'fhe testing crew will arrivc and set up and starl testing on July 9tl'and continue until all testing has been conrpletecl. A pretest nieeting can be scheduled if reqLrested by Holcim or DAQ. TEST PROCEDURES ') 1. 5. 6. 7. 8. t T T t t I t T t t T T T t T t t I T Three test runs rvill be conducted on each kiln I Methods 201 A and 202 as specitied in 40 CFR EPA Methods20lAl202. for PMro emissions. Testing will tbllow EPA 5l Appendix M. The following specific items rvill be followed for Methods 201A1202: | . The Kiln # I stack inside diameter is 47 inches. There are two ports available lor testing that rneet the upstream/downstream requirements of Method l. 'fhe ports are located 45 f'eet downstream and 33 feet upstream from any flow disturbance. A total of l2 points will be sampled, six per port. Minimum target sampling tinre will be 60 minutes. The stack flow will determine the dwell time at each point and actual test tirne. The Kiln 3 stack inside diameter is 46.5 inches. There are two ports availahle that meet the upstrearn/downstream requirernents of Method l. 'fhe porls arc located 45 l-eet downstreamand35feetupstreamfromanyflowdisturbance. Atotal of l2poiritsrvill be sampled, six per port. Minimum target sarnpling time will be 60 minutes. 'fhe stack flow will deterrnirre the dwell time at each point and actual test EPA Method 2 will be used to determine gas stream velocity. Calibration data fbr the type "S" pitot tubes are included with this protocol. Dual inclined/vertical manometcrs with graduations in 0.01 inches of water will be used. 'fhe absence ol'cyclonic florv lvill be checked during the preliminary run. A barometer will be used to measure the barometric pressure. lt is poriodically checkecl against a mercury barometer. Prior to testing it will be checked to assure an accurate barometric pressure. An integrated sample of the flue gas will be taken fionr the exhaust line after the dr,"- gas rneter orifice during each test run and analyzed at the test's completion by Fyrite to determine the gas stream molecular weight. 1'he probe liners will be borosilicate glass or Teflon. Preparation and clean-up by the contractor will be performed in the contractor's testing trailer. Laboratory work and analysis will be done by the testing contractor as soon as possibleafterall testshavebeencompletedat39l East620South.AmcricanFork.tJtalr. Back half will be determined by EPA Method202. EPA Method202 analysis will be followed as in the method. If plant maintenance or operating problerns arise during the test. the test may be stopped. This determination will be made by the Holcim Corporation representatives or operating personnel in consultation with agency representatives t t I t I t T T T T I T I T I I I T I 9. Current calibration data is submitted in Appendix B of this protocol. Any equipment calibration that fall past due prior to the test date will be recalibrated prior to use. OPBRATIONAL DATA AND INSTRUMENTATION Pertinent operating data will be made available by Holcirn upon request by agency personnel. TE,ST AREA The test area shall include the control room, stack and associated areas, and the area around the contractor's testing trailer for preparation. and clean-up. TEST SITE A sketclr of the source is included with this protocol. ACCESS TO SAMPLE SITE The site is accessed via stairs and ladders. POTENTIAL HAZARDS Moving Equiprnent Yes ['lot Equiprnent Yes Chemical No Other No ESTIMATES OF TESTING PARAMETERS The volumetric flow rate. moisture and stack ternperatures are sinrilar for both stacks. Volumetric Flow Rate 12,000 dcfnrMoisture l1%Temperature 325'F OUALITY ASSURANCE T t All testing and analysis in these cornpliance tests will be conducted according to Methods 201 A and202 and appropriate sections of the EPA Qualitlt A.t,rurunce Hantlltook./itr,lir Pollutiorr Measurement Syslem.s Volume III. REPORTING The emissions test report will be prepared by the testing contractor according to EPA Quality Assurance Guidelines. The contractor will furnish several copies of the test repoft to Holcim. This report will be submitted within 30 days following the cornpletion o1'the tests. EPA Method 202 will be included in the written repoft for informational purposes only. Complete copies of raw data. calculations and summary of test will be included in reports. All process and production data will be recorded and retained for inspection and copying by DAQ and EPA. T T T I I t Appendix A I Facility Schematics ouo_o?Ei,'afi|,or l l! 6 : ?, \ L E & 6 & z o. ,E s oo E o - = ti : r i . s 8 = r a i El i s i b F E r Yr O q Es 6 o E ; + P E =E ? = -6 a . Y c l r o t r : E E ? Z = E 2 oE H E i ; , EE + 1 : E n l ! .: . - t = 9 E u erkE ; a , Y , " P3 o t i !L U U i7 3 )r c J36 E , E- O n 6" , o O 1' a6.. p d^ ci i rn ^l .. 1 F. -i f ir t .: r i- , -l tiaJ C)aEI J +h tr y ' a'5o'5coJocn -l t- ' (cFi .PCC I t- , iocQ()+J rF 1 tr i c. ) -l - ) ;) tr=. . -9o*Q \t t = =. . a Zc oO .)?, c 3cau!EastJ 'J 1=!€il-6ibb,J L! oo ; i E F & 6 .E i o. ,a ! oo E o = a; q r j . S c = : J -a = a ' L E E : d E E. 1 : E s r. E ; i! E -a E g 6 = 6 - 7 E? , E i 5 . - 2 F E . E =' o i a o - o H A =e ' G - q . = () t r x E i i , ;E q , , i 6 i ; r ,: . s E ! E r r : F E g 6 E g3 0 a 9L O u ao Y=s 6 36 2 c- o a Nt ' - ,, a) t' i5 E - .. i do .. i a. t ^l OC-ir- i .la. t \5*: r + c. i TJ. C)abj l C$ en+hMC.;6o.E(]I:loa -l lr (c rf irl . JdL{ccU() .l - ) rf iFiO{- ) ) o TTTIITItIITTIIIItIT Appendix B Calibration Data ol @ l N l o l @ r 6 1 6 r o l 6 r g 3l E !l _E I =l !l 5l _q l T 3l :l oG-c t(!oIoo-$$to(\ t ill noo o bl F l s l > s l ? r o l > N l o r 6 r > 5l sl 3l < sl 51 3l < El Bl S l < ql . ! l ol el r? l ql el \ l .! l ts l N l + l < l s l @ { s l b l {l Tt Pl 3 l xl Rl 3l 5l @l 6 l N I 6 l o l Nl !l ? l o l r l 6 l Nl vl s i l @ l u i l "t l il s" q gp*E JEEz to o o N @ F@ O .t ! , I r . ! a n q o r q u@ 6 ri q \ e Ea N q q +: ,S r I hf,zzEt n-hI U Ui eA ol ii ut s l . _ ' o o l -" fl \- , u< ,,a :ra gi l g f l s l :l :l : l El fl l l f l p] -E l 33 ff i H i l f f i a:! -- o !o>EvS;ou oi u E 3i rl I L- - c ; -; : o _o A I 6 E , . F t ! r " " -o l .. i ; H r: o[ '- e 9 - - o ,,, 6 0 (J 't -. L o- n ' 9 d t- + 2 3E ' 2 ll m- A F: oo r F= o :" ^ a a' o< t < B, , O aY L or : 2 cd6c>qns n6O(,o c.aEcoEDcoi:ECoooo;, i U oo6Io, -s&o, ,EJ i5i;n HT Hf i Tf r al u :Eo6Ei 8E -U6E tr qE= CO<f>6>Uc9 Ia :l1i /l . i,] .. 1 {. I ., 1:<Il o2u- - r- o1g UF - =6:ra1€4P>t s L1 U' €E?c 6! i;6P o- B<E c 2t * @a = z- 2 5 OE B <. D ; Gr : 9 e -i- o- - 6i 2 -9 3 E P€ Oo a J9 : < E4 =+ e rr r 8E (9 'E i = fF > ff i f f i f f i eFU=trfoU I- J ; I ui l ii id )Jad . UUa>UU9u EEoJ NE ll 5 t; t l6 l t= l l* l F l E l I I -l ol Il - l . l ,i L i {g6 E a4$r 'u ut4IdFU=odo cooCooE6a;Eoo , q f ='6o- o I O O 6! = ti Eo o FO d = u E9 : 3 a sE : = f , -t r i o t ,2 . 6 a a ' -6 d ; g lo E o li e O= E - .r E ! u r a E: E E T o; 6 - C 6 6( ) S o Eo Q 9 o ft B E E : o o: f c ., = O ' - - - o: tr N = f -- o E : ! E . i : 6 D f , o c eE H i o -o > : C i t r - , u 6 ,6 E e o oi r T > i 6 E!J 6 9 -E - . o E ;3 ; 9 t 3 OO f . - ) O @t t - E t oLr J()LLE.oJoFao(9z-a n:lzoFtoJoxuFUJEu)od.or.( )ooIFulE N N N N N l tr t r t r I T t I I T I I T T T I I I t T T I T [)ate Dr Type S Pitot Tube Inspection Data Pitot -I'ubc ldenrillcation: l'echn ician M. McNamara D,= 0.-175 in. Is ['1 = Pe ? Is 1.05.D, S P^&Pr1 S 150.D, 'l Yes Yes P^=0,176 in. [t le)tt Pn=0.476 in u1 <l0o 0r = o2<l0o d:= )i) 0-j -/[--1 \p, "+l l+-[ -------------7--+-l []r < 5n {}, '5n ljr = l): -t" 7. < 0.125 itr 7. :0.002 ...-..-I W < 0.03 125 in. W = 0.004 W>3inchcs W= 7.> 314 inch /.= 5 in. I in.lGffiI If" -i.- ' -:t- ---Q [ -trffi l- .. \, > r inchcs y = .] r/2 in I'he pitot tubc nrcets the specilicalions lirr a calibration laclor ol'0.114? Ycs 'l r:mpcraturr; Scnsor Cal ibrationRel'erence: C)mega CL.l5 l2A llmt Check 2:llt BOIL WA'TER I I I T T I T T T T t t T I I I t I T l^6t2021 Tyrre S Pitot Tube Inspcction Data l)itot fube Identillcation:5tc-2 Dr .j=- .:*-Zllf"^tf r. ..-- - _**_f ," I 'l echnician: 0._175 M. McNanrara D,=ls p. = [,s ,) Is 1 05 . D, < I)n& Pr < 1 50.I), 1 P 0 4'70 l"l 0.470 a1 < l0o ur - n2 < l0' Ctt= r(lI l' ,ri s, -ri)| -,'F---<-. --\a \{0, 0, '5n 0,'5" []r =' 0:=J 7. <0.125 in. 7..,0 065 ----rJ':+r --J-l:w <003t25in W > 3 inches ' Z>311 inclt W -. 0.016 in --l-..:L:.-' t./'. i: T _j__._1.__iF-==*.-.-[:iilffi] I lin ;]-:--r -; il.tlmr -O { Y --Jtncllcs Y= 3 ll2 rn 'Ihc pitot tubc rnccts the spccifications tbr a calibration factor ol'0.8.1? Yes l'omporaturc Scnsor Cal ibrationIlelbrence: Omega Cl.35l2A Continuiw Check l lcat Chock 248 I('E WATER IX)lt_wAtLR stLl( oNL. oI, T I I I TETCO Sample Box Temperature Sensor Calibration I I T T I t T T T T I I T I I t>arc I 12/24 ('alibraror Xuan N. Dang Rclbrcncc OrncgaCl,35l2A -2 0 -l 0 0 0 0 Llnit It)Thermocouple Location I-emperaturc Source (Medium) 'femperature 'fcmperatu re Diffcrcncc ("1.) Reference ("1') Scnsor ("t.) A Oven (3)Waler 33 33 0 Watcr 203 20r a Oven (4)water 3i 33 Water 203 20t 1 B Oven (3)Water 33 33 0 Watcr 203 202 .l Oven (4)waler -i -1 0 Watcr 203 20t _) C Ovcn (3)Waler J-1 0 Watcr 203 20 0 Ovcn (4)walcr 33 33 Watcr 203 203 0 D Ovun (3)Water .,J J-)0 Watcr 20:l 203 0 Ovcn (4)watcr i3 -).) Watcr 20:i 203 0 E Oven (-j)Watcr ., 1 33 0 Watcr 203 203 0 Oven (4)water -) -l 33 0 Water 203 203 0 F Oven Water 33 33 Watcr 203 202 -I G Oven Water 33 33 0 Water 203 ?02 -l H Ovcn Water 33 33 0 Water 203 203 0 0 0 0 -l 0 -l 0 0 I 0 Impinger Out C lrnpingcr Out D Irnpinger Out I:) lmpinger Out (i hnpinger Out I Impinger Out K T I I t Batance Weiohts UsedI T T T T TETCO Annual Balance Calibration Check Dale 1123124 Denver lnstruments, Model4-250, SN 8045284 Troemner Weight Set, sN 98-'115146 I Technician Michaet McNamara Certified Weight qrams Measured Weight qrams Difference qrams 0.1 000 0.1 000 0.0000 0.5000 0.5000 0.0000 1.0000 1.0000 0.0000 10.0000 10.0000 0.0000 50.0000 50.0001 -0.0001 100.0000 100.0000 0.0000 120.0000 120.000'1 -0.0001 150.0000 150.0000 0.0000 Uo'ao() rAc.. i 'oo(J>6 J .Cio -uXl r =U o Eo I C) - o a O - - '( r - t 1 t t s1 o= JA u - .i cs (, rr j G ll ,. t r o = C. \ J + : : .9 r c, Z .a - + > '; I uv dJ r ^ '- o L i - E= 50 ,;' i ^i(-) ! U, = .l J E 40 c ) -. 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Id . 9= a- o Source Information Division of Air Quality Compliance Demonstration Referance Method 201 & 201A for PM10 Source Information Company Name Holcim Utelite Company Contact:Carsten Mortensen Contact Phone No.801-467-2800 Stack Designation:Kiln #1 Test & Review Dates Test Date: 7/10-11/24 Review Date: 9/23/2024 Observer: Robert Sirrine Reviewer:Robert Sirrine Particulate Emission Limits lbs/MMBTU lbs/hr gr/dscf 0.000 3.340 0.024 Front Half Emission Rates lbs/MMBTU lbs/hr gr/dscf 0.59 0.006 Total (Front & Back Half) Emission Rates lbs/MMBTU lbs/hr gr/dscf 0.762335345 0.007462594 Test Information Stack I.D. inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn Target Time 47.00 12.048 0.9940 1.607 0.773 24.1 -0.22 0.235 60 Contractor Information Contracting Company: TETCO Contact: Dean Kitchen Phone No.: 801-768-0973 Project No.: Circular 10100 9780 9860 9190 8710 8710 8710 10540 10640 11950 320 10610 10200 10390 1970 1800 1910 1420 1040 1190 1250 F factor usedF factors for Coal, Oil, and Gas Anthrocite 2 Lignite Natural Propane Butane COAL OIL GAS Bituminous 2 Fd Fw Fc scf/MMBtu scf/MMBtu scf/MMBtu O2 CO2 lbs/MMBtu Page 1 Summary Division of Air Quality Reference Methods 201 & 201A - TSP Compliance Demonstration of Holcim Utelite - Kiln #1 Testing Results Lab Data - grams collected Test Date 7/10-11/24 7/10-11/24 7/10-11/24 7/10-11/24 Lab Data Cyclone Catch Filter Back Run 1 Run 2 Run 3 Run 4 Run 1 0.0028 0.004900 0.00200 As ft^2 12.05 12.05 12.05 12.05 Run 2 0.0022 0.004200 0.00220 Pbar 24.10 24.10 24.10 24.10 Run 3 0.0069 0.000000 0.0021 Pq (static)-0.22 -0.22 -0.22 -0.22 Run 4 Ps 24.08 24.08 24.08 24.08 Avg. Ts F 288.20 293.60 296.00 Holcim Utelite Kiln #1 CO2 - FCO2 6.70 6.50 6.50 0.00 Front Half Emissions Summary O2 13.20 13.10 12.80 0.00 Run 1 Run 2 Run 3 Run 4 Avg. N2+C 80.10 80.40 80.70 100.00 gr./dscf 0.00622 0.00549 0.00551 0.00574 Md 29.60 29.56 29.55 28.00 lbs/hr 0.636 0.562 0.558 0.58533 Mw 28.03 27.92 27.92 lbs/MMbtu Y 0.9940 0.9940 0.9940 0.9940 Cp 0.77 0.77 0.77 0.77 Particulate Emission Limits Front Half Emission Rates Vm cf 25.264 23.277 25.426 0.000 lbs/MMBTU lbs/hr gr/dscf lbs/MMBTU lbs/hr gr/dscf Vlc 63.700 63.600 67.800 0.000 3.340 0.024 0.59 0.005736922 AVG. Tm F 99.00 87.04 96.41 Vm cf 25.264 23.277 25.426 0 Holcim Utelite Kiln #1 Vm std 19.119 18.000 19.331 #VALUE!Total Emissions Summary w/back half condensable Vw std 3.000 2.990 3.190 Run 1 Run 2 Run 3 Run 4 Avg. Bws 13.50% 14.20% 14.10% #VALUE! gr./dscf 0.00783 0.0074 0.0072 0.0075 S Bws 99.90% 99.90% 99.90% #VALUE! lbs/hr 0.8024 0.7560 0.7286 0.7623 Avg. Sqrt Dlp 0.48 0.49 0.48 0.50 lbs/MMbtu Vs 33.661 34.198 33.888 scfm wet 13820.29 13940.05 13769.73 #VALUE!Particulate Emission Limits Total Emission Rates acfm 24333.53 24721.54 24497.26 lbs/MMBTU lbs/hr gr/dscf lbs/MMBTU lbs/hr gr/dscf Qsd dscfh 717273 717634 709692 3.340 0.024 0.762335345 0.007462594 Qs ft3/min 0.646521 0.650992 0.653159 #VALUE! % Isokinetic 106.18 104.23 107.17 Test Quality Parameters Viscostiy 221.07 221.87 222.40 Run 1 Run 2 Run 3 Run 4 D50 9.99 9.99 9.99 Outlying Dlp's 0.00 0.00 0.00 % Isokinetic 106.17 104.23 107.16 D50 Outlying Dlp's % Isokinetic Status Run 1 Passed Passed Passed Acceptable Run Run 2 Passed Passed Passed Acceptable Run Run 3 Passed Passed Passed Acceptable Run Run 4 Page 1 Run 1 Holcim Utelite Test Date 7/10-11/24 Imp. Liquid Collected in grams Run No. 1 - RM 201A - Pre-test velocity traverse:Wt. (Final)Wt. (Tare)lc Port 1 Port 2 Port 3 Port 4 371.0 336.0 35.0 Point No.∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'623.2 615.7 7.5 1 617.3 607.9 9.4 2 962.2 950.4 11.8 3 0.0 ∆P1 Avg. Sqrt ∆P No. Sample Points t1 in min. Ts avg -50oF Avg. Ts oF Ts avg +50oF 0.25 0.49663265 12 5.05 Ts oF 238.20 288.20 338.20 ∆H 0.55 0.51 0.48 ∆ = delta, i.e., delta P would be ∆P Stack I.D. (inches)As ft^2 Pbar Pq (static) Ps CO2 % O2 % N2+C Md lb/lb mole Mw lb/lb mole Stack Saturation 47.00 12.05 24.10 -0.22 24.08 6.70 13.20 80.10 29.60 28.03 4.7907 Y ∆H@ Cp 201A Cp 2 Dn An Vm cf Vm std Vlc Vw std Bws S Bws 0.9940 1.607 0.77 0.235 3.01E-04 25.264 19.119 63.70 3.000 0.1350 0.9990 Avg. Sqrt ∆p Vs ft/sec Avg. ∆h Avg. Tm F scfm wet acfm Qsd dscfh Qs (final) ft3/min µs Viscosity Run Time (act) Target Time 0.4838 33.66 0.360 99.00 13,820 24,334 7.17E+05 0.646520678 221.07 60.25 60 Sample Point No.Dn used Sampling End Time (Min.Sec.) Actual Dwell Time (Min.Sec.) Desired Dwell Time (Min.Sec.) Stack Temp. Ts F Velocity Head ∆P ∆h D50 Dry Gas Meter Temp. tm F (in) tm F (out) Status Pmin & Pmax 1 - ∆P t1 0.235 5.15 5.15 5.15 295 0.25 0.36 9.990 88 86 Passed 2 - ∆P tn 0.235 10.15 5.00 5.15 294 0.25 0.36 9.990 87 89 Passed 3 - ∆P tn 0.235 15.15 5.00 5.00 295 0.24 0.36 9.990 88 96 Passed 4 - ∆P tn 0.235 20.00 4.45 4.30 296 0.20 0.36 9.990 89 101 Passed 5 - ∆P tn 0.235 24.45 4.45 4.30 296 0.20 0.36 9.990 91 105 Passed 6 - ∆P tn 0.235 29.15 4.30 4.30 295 0.19 0.36 9.990 92 103 Passed 7 - ∆P tn 0.235 34.30 5.15 5.15 267 0.26 0.36 9.990 95 106 Passed 8 - ∆P tn 0.235 40.00 5.30 5.30 263 0.28 0.36 9.990 96 112 Passed 9 - ∆P tn 0.235 45.30 5.30 5.30 288 0.28 0.36 9.990 97 110 Passed 10 - ∆P tn 0.235 50.30 5.00 5.00 290 0.24 0.36 9.990 99 114 Passed 11 - ∆P tn 0.235 55.30 5.00 4.45 290 0.22 0.36 9.990 99 116 Passed 12 - ∆P tn 0.235 60.15 4.45 4.45 290 0.21 0.36 9.990 100 117 Passed 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 Run Acceptance Results. D50 9.9900 Passed Sampling Points outside of Pmin & Pmax 0.00 Passed % Isokinetic 106.2 Passed The results are acceptabel if two conditions are met: A. D50 is between 9.0 µm & 11.0 µm.  If D50 is less than 9.0 reject the results and repeat the test. B. One of the following conditions must also be met:That no sampling points are outside Pmin and Pmax or 1. No sampling points are outside the Pmin and Pmax or 2. Isokinetics sampling is betwee 80 percent & 120 percent and no more than one sampling point is outside ∆Pmin and ∆Pmax. Acceptable Run Acceptable Run Test Run Completed Acceptable Run Acceptable Run Page 1 Run 2 Holcim Utelite Test Date 7/10-11/24 Imp. Liquid Collected in grams Run No. 2 - RM 201A - Pre-test velocity traverse:Wt. (Final)Wt. (Tare)lc Port 1 Port 2 Port 3 Port 4 414.3 363.8 50.5 Point No.∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'619.8 616.2 3.6 1 607.5 604.6 2.9 2 963.6 957.0 6.6 3 0.0 ∆P1 Avg. Sqrt ∆P No. Sample Points t1 in min. Ts avg -50oF Avg. Ts oF Ts avg +50oF 0.17 0.4804869 12 4.20 Ts oF 243.60 293.60 343.60 ∆H 0.54 0.51 0.48 ∆ = delta, i.e., delta P would be ∆P Stack I.D. (inches)As ft^2 Pbar Pq (static) Ps CO2 % O2 % N2+C Md lb/lb mole Mw lb/lb mole Stack Saturation 47.00 12.05 24.10 -0.22 24.08 6.50 13.10 80.40 29.56 27.92 5.2109 Y ∆H@ Cp 201A Cp 2 Dn An Vm cf Vm std Vlc Vw std Bws S Bws 0.9940 1.607 0.77 0.233 2.96E-04 23.277 18.000 63.60 2.990 0.1420 0.9990 Avg. Sqrt ∆p Vs ft/sec Avg. ∆h Avg. Tm F scfm wet acfm Qsd dscfh Qs (final) ft3/min µs Viscosity Run Time (act) Target Time 0.4913 34.20 0.360 87.04 13,940 24,722 7.18E+05 0.6509922 221.87 58.75 60 Sample Point No.Dn used Sampling End Time (Min.Sec.) Actual Dwell Time (Min.Sec.) Desired Dwell Time (Min.Sec.) Stack Temp. Ts F Velocity Head ∆P ∆h D50 Dry Gas Meter Temp. tm F (in) tm F (out) Status Pmin & Pmax 1 - ∆P t1 0.235 4.00 4.00 5.00 293 0.17 0.36 9.990 75 73 Passed 2 - ∆P tn 0.235 9.00 5.00 5.00 293 0.25 0.36 9.990 76 79 Passed3 - ∆P tn 0.235 14.15 5.15 5.15 292 0.28 0.36 9.990 73 86 Passed 4 - ∆P tn 0.235 19.15 5.00 5.15 293 0.27 0.36 9.990 74 86 Passed 5 - ∆P tn 0.235 24.00 4.45 4.45 295 0.22 0.36 9.990 78 93 Passed 6 - ∆P tn 0.235 28.45 4.45 4.45 295 0.23 0.36 9.990 79 97 Passed 7 - ∆P tn 0.235 33.30 4.45 4.45 292 0.22 0.36 9.990 83 93 Passed 8 - ∆P tn 0.235 38.30 5.00 5.00 290 0.24 0.36 9.990 83 97 Passed 9 - ∆P tn 0.235 43.45 5.15 5.15 297 0.28 0.36 9.990 85 102 Passed 10 - ∆P tn 0.235 49.00 5.15 5.15 297 0.28 0.36 9.990 86 103 Passed 11 - ∆P tn 0.235 54.00 5.00 5.00 294 0.25 0.36 9.990 88 105 Passed 12 - ∆P tn 0.235 58.45 4.45 4.45 293 0.22 0.36 9.990 88 107 Passed 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 Run Acceptance Results. D50 9.9900 Passed Sampling Points outside of Pmin & Pmax 0.00 Passed % Isokinetic 104.2 Passed The results are acceptabel if two conditions are met: A. D50 is between 9.0 µm & 11.0 µm.  If D50 is less than 9.0 reject the results and repeat the test. B. One of the following conditions must also be met:That no sampling points are outside Pmin and Pmax or 1. No sampling points are outside the Pmin and Pmax or 2. Isokinetics sampling is betwee 80 percent & 120 percent and no more than one sampling point is outside ∆Pmin and ∆Pmax. Acceptable Run Acceptable Run Test Run Completed Acceptable Run Acceptable Run Page 1 Run 3 Holcim Utelite Test Date 7/10-11/24 Imp. Liquid Collected in grams Run No. 3 - RM 201A - Pre-test velocity traverse:Wt. (Final)Wt. (Tare)lc Port 1 Port 2 Port 3 Port 4 416.5 373.5 43.0 Point No.∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'610.7 605.5 5.2 1 596.2 586.0 10.2 2 974.2 964.8 9.4 3 0.0 ∆P1 Avg. Sqrt ∆P No. Sample Points t1 in min. Ts avg -50oF Avg. Ts oF Ts avg +50oF 0.17 0.4870254 12 4.30 Ts oF 246.00 296.00 346.00 ∆H 0.55 0.51 0.48 ∆ = delta, i.e., delta P would be ∆P Stack I.D. (inches)As ft^2 Pbar Pq (static) Ps CO2 % O2 % N2+C Md lb/lb mole Mw lb/lb mole Stack Saturation 47.00 12.05 24.10 -0.22 24.08 6.50 12.80 80.70 29.55 27.92 5.4070 Y ∆H@ Cp 201A Cp 2 Dn An Vm cf Vm std Vlc Vw std Bws S Bws 0.9940 1.607 0.77 0.235 3.01E-04 25.426 19.331 67.80 3.190 0.1410 0.9990 Avg. Sqrt ∆p Vs ft/sec Avg. ∆h Avg. Tm F scfm wet acfm Qsd dscfh Qs (final) ft3/min µs Viscosity Run Time (act) Target Time 0.4836 33.89 0.360 96.41 13,770 24,497 7.10E+05 0.6531595 222.40 61.00 60 Sample Point No.Dn used Sampling End Time (Min.Sec.) Actual Dwell Time (Min.Sec.) Desired Dwell Time (Min.Sec.) Stack Temp. Ts F Velocity Head ∆P ∆h D50 Dry Gas Meter Temp. tm F (in) tm F (out) Status Pmin & Pmax 1 - ∆P t1 0.235 4.15 4.15 5.15 288 0.17 0.36 9.990 86 87 Passed 2 - ∆P tn 0.235 9.45 5.30 5.15 288 0.27 0.36 9.990 85 88 Passed3 - ∆P tn 0.235 15.15 5.30 5.30 292 0.28 0.36 9.990 85 95 Passed 4 - ∆P tn 0.235 20.15 5.00 4.45 300 0.22 0.36 9.990 86 99 Passed 5 - ∆P tn 0.235 25.00 4.45 4.45 301 0.21 0.36 9.990 87 103 Passed 6 - ∆P tn 0.235 30.00 5.00 5.00 301 0.23 0.36 9.990 88 106 Passed 7 - ∆P tn 0.235 35.30 5.30 5.15 289 0.27 0.36 9.990 91 105 Passed 8 - ∆P tn 0.235 14.00 -21.70 5.15 299 0.27 0.36 9.990 91 107 Passed 9 - ∆P tn 0.235 46.15 32.15 5.15 299 0.25 0.36 9.990 92 110 Passed 10 - ∆P tn 0.235 51.15 5.00 5.00 298 0.23 0.36 9.990 93 112 Passed 11 - ∆P tn 0.235 56.15 5.00 4.45 300 0.22 0.36 9.990 94 114 Passed 12 - ∆P tn 0.235 61.00 4.45 4.30 298 0.20 0.36 9.990 95 115 Passed 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 Run Acceptance Results. D50 9.9900 Passed Sampling Points outside of Pmin & Pmax 0.00 Passed % Isokinetic 107.2 Passed The results are acceptabel if two conditions are met: A. D50 is between 9.0 µm & 11.0 µm.  If D50 is less than 9.0 reject the results and repeat the test. B. One of the following conditions must also be met:That no sampling points are outside Pmin and Pmax or 1. No sampling points are outside the Pmin and Pmax or 2. Isokinetics sampling is betwee 80 percent & 120 percent and no more than one sampling point is outside ∆Pmin and ∆Pmax. Acceptable Run Acceptable Run Test Run Completed Acceptable Run Acceptable Run Page 1 Source Information Division of Air Quality Compliance Demonstration Referance Method 201 & 201A for PM10 Source Information Company Name Holcim Utelite Company Contact:Carsten Mortensen Contact Phone No.801-467-2800 Stack Designation:Kiln #3 Test & Review Dates Test Date: 7/10/2024 Review Date: 9/23/2024 Observer: Robert Sirrine Reviewer:Robert Sirrine Particulate Emission Limits lbs/MMBTU lbs/hr gr/dscf 0.000 3.340 0.024 Front Half Emission Rates lbs/MMBTU lbs/hr gr/dscf 0.74 0.006 Total (Front & Back Half) Emission Rates lbs/MMBTU lbs/hr gr/dscf 1.084693486 0.00902737 Test Information Stack I.D. inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn Target Time 46.50 11.793 0.9940 1.607 0.769 24.1 -0.27 0.216 60 Contractor Information Contracting Company: TETCO Contact: Dean Kitchen Phone No.: 801-768-0973 Project No.: Circular 10100 9780 9860 9190 8710 8710 8710 10540 10640 11950 320 10610 10200 10390 1970 1800 1910 1420 1040 1190 1250 F factor usedF factors for Coal, Oil, and Gas Anthrocite 2 Lignite Natural Propane Butane COAL OIL GAS Bituminous 2 Fd Fw Fc scf/MMBtu scf/MMBtu scf/MMBtu O2 CO2 lbs/MMBtu Page 1 Summary Division of Air Quality Reference Methods 201 & 201A - TSP Compliance Demonstration of Holcim Utelite - Kiln #3 Testing Results Lab Data - grams collected Test Date 7/10/2024 7/10/2024 7/10/2024 7/10/2024 Lab Data Cyclone Catch Filter Back Run 1 Run 2 Run 3 Run 4 Run 1 0.0023 0.004800 0.00450 As ft^2 11.79 11.79 11.79 11.79 Run 2 0.0054 0.005000 0.00390 Pbar 24.10 24.10 24.10 24.10 Run 3 0.0054 0.000600 0.0025 Pq (static)-0.27 -0.27 -0.27 -0.27 Run 4 Ps 24.08 24.08 24.08 24.08 Avg. Ts F 264.80 262.80 264.80 Holcim Utelite Kiln #3 CO2 - FCO2 4.20 4.20 4.00 0.00 Front Half Emissions Summary O2 14.80 14.50 14.90 0.00 Run 1 Run 2 Run 3 Run 4 Avg. N2+C 81.00 81.30 81.10 100.00 gr./dscf 0.00584 0.00802 0.00460 0.00615 Md 29.26 29.25 29.24 28.00 lbs/hr 0.71 0.96 0.54 0.738 Mw 28.07 27.98 28.05 lbs/MMbtu Y 0.9940 0.9940 0.9940 0.9940 Cp 0.77 0.77 0.77 0.77 Particulate Emission Limits Front Half Emission Rates Vm cf 24.288 26.272 26.642 0.000 lbs/MMBTU lbs/hr gr/dscf lbs/MMBTU lbs/hr gr/dscf Vlc 47.400 54.400 50.300 0.000 3.340 0.024 0.74 0.006152463 AVG. Tm F 87.66 95.25 99.87 Vm cf 24.288 26.272 26.642 0 Holcim Utelite Kiln #3 Vm std 18.760 20.018 20.133 #VALUE!Total Emissions Summary w/back half condensable Vw std 2.230 2.560 2.370 Run 1 Run 2 Run 3 Run 4 Avg. Bws 10.60% 11.30% 10.50% #VALUE! gr./dscf 0.00954 0.0110 0.0065 0.0090 S Bws 99.90% 99.90% 99.90% #VALUE! lbs/hr 1.1625 1.3211 0.7705 1.0847 Avg. Sqrt Dlp 0.56 0.55 0.55 0.51 lbs/MMbtu Vs 38.316 37.882 37.151 scfm wet 15895.78 15758.96 15412.29 #VALUE!Particulate Emission Limits Total Emission Rates acfm 27112.54 26805.01 26287.87 lbs/MMBTU lbs/hr gr/dscf lbs/MMBTU lbs/hr gr/dscf Qsd dscfh 852650 838692 827640 3.340 0.024 1.084693486 0.00902737 Qs ft3/min 0.631649 0.628286 0.632130 #VALUE! % Isokinetic 103.70 108.14 112.74 Test Quality Parameters Viscostiy 218.11 216.92 218.23 Run 1 Run 2 Run 3 Run 4 D50 9.99 9.99 9.99 Outlying Dlp's 0.00 0.00 0.00 % Isokinetic 103.69 108.14 112.73 D50 Outlying Dlp's % Isokinetic Status Run 1 Passed Passed Passed Acceptable Run Run 2 Passed Passed Passed Acceptable Run Run 3 Passed Passed Passed Acceptable Run Run 4 Page 1 Run 1 Holcim Utelite Test Date 7/10/2024 Imp. Liquid Collected in grams Run No. 1 - RM 201A - Pre-test velocity traverse:Wt. (Final)Wt. (Tare)lc Port 1 Port 2 Port 3 Port 4 383.9 353.2 30.7 Point No.∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'616.2 613.4 2.8 1 607.9 601.2 6.7 2 950.4 943.2 7.2 3 0.0 ∆P1 Avg. Sqrt ∆P No. Sample Points t1 in min. Ts avg -50oF Avg. Ts oF Ts avg +50oF 0.26 0.583614384 12 4.29 Ts oF 214.80 264.80 314.80 ∆H 0.57 0.53 0.5 ∆ = delta, i.e., delta P would be ∆P Stack I.D. (inches)As ft^2 Pbar Pq (static) Ps CO2 % O2 % N2+C Md lb/lb mole Mw lb/lb mole Stack Saturation 46.50 11.79 24.10 -0.27 24.08 4.20 14.80 81.00 29.26 28.07 3.2756 Y ∆H@ Cp 201A Cp 2 Dn An Vm cf Vm std Vlc Vw std Bws S Bws 0.9940 1.607 0.77 0.216 2.54E-04 24.288 18.760 47.40 2.230 0.1060 0.9990 Avg. Sqrt ∆p Vs ft/sec Avg. ∆h Avg. Tm F scfm wet acfm Qsd dscfh Qs (final) ft3/min µs Viscosity Run Time (act) Target Time 0.5628 38.32 0.350 87.66 15,896 27,113 8.53E+05 0.631649377 218.11 59.00 60 Sample Point No.Dn used Sampling End Time (Min.Sec.) Actual Dwell Time (Min.Sec.) Desired Dwell Time (Min.Sec.) Stack Temp. Ts F Velocity Head ∆P ∆h D50 Dry Gas Meter Temp. tm F (in) tm F (out) Status Pmin & Pmax 1 - ∆P t1 0.216 4.30 4.30 4.30 266 0.26 0.35 9.990 74 74 Passed 2 - ∆P tn 0.216 10.00 5.30 5.15 265 0.39 0.35 9.990 74 77 Passed 3 - ∆P tn 0.216 15.15 5.15 5.15 268 0.38 0.35 9.990 75 82 Passed 4 - ∆P tn 0.216 20.15 5.00 5.00 265 0.34 0.35 9.990 77 84 Passed 5 - ∆P tn 0.216 25.15 5.00 4.45 266 0.33 0.35 9.990 79 93 Passed 6 - ∆P tn 0.216 30.30 5.15 5.00 264 0.35 0.35 9.990 80 98 Passed 7 - ∆P tn 0.216 34.30 4.00 3.45 261 0.21 0.35 9.990 84 99 Passed 8 - ∆P tn 0.216 38.46 4.15 4.15 261 0.25 0.35 9.990 84 99 Passed 9 - ∆P tn 0.216 43.30 4.44 4.30 269 0.29 0.35 9.990 86 104 Passed 10 - ∆P tn 0.216 48.30 5.00 4.45 268 0.32 0.35 9.990 87 104 Passed 11 - ∆P tn 0.216 53.45 5.15 5.00 262 0.36 0.35 9.990 87 106 Passed 12 - ∆P tn 0.216 59.00 5.15 5.00 263 0.35 0.35 9.990 89 108 Passed 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 Run Acceptance Results. D50 9.9900 Passed Sampling Points outside of Pmin & Pmax 0.00 Passed % Isokinetic 103.7 Passed The results are acceptabel if two conditions are met: A. D50 is between 9.0 µm & 11.0 µm.  If D50 is less than 9.0 reject the results and repeat the test. B. One of the following conditions must also be met:That no sampling points are outside Pmin and Pmax or 1. No sampling points are outside the Pmin and Pmax or 2. Isokinetics sampling is betwee 80 percent & 120 percent and no more than one sampling point is outside ∆Pmin and ∆Pmax. Acceptable Run Acceptable Run Test Run Completed Acceptable Run Acceptable Run Page 1 Run 2 Holcim Utelite Test Date 7/10/2024 Imp. Liquid Collected in grams Run No. 2 - RM 201A - Pre-test velocity traverse:Wt. (Final)Wt. (Tare)lc Port 1 Port 2 Port 3 Port 4 406.0 360.8 45.2 Point No.∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'598.1 595.2 2.9 1 604.6 604.0 0.6 2 957.0 951.3 5.7 3 0.0 ∆P1 Avg. Sqrt ∆P No. Sample Points t1 in min. Ts avg -50oF Avg. Ts oF Ts avg +50oF 0.33 0.5914468 12 4.87 Ts oF 212.80 262.80 312.80 ∆H 0.56 0.52 0.49 ∆ = delta, i.e., delta P would be ∆P Stack I.D. (inches)As ft^2 Pbar Pq (static) Ps CO2 % O2 % N2+C Md lb/lb mole Mw lb/lb mole Stack Saturation 46.50 11.79 24.10 -0.27 24.08 4.20 14.50 81.30 29.25 27.98 3.1669 Y ∆H@ Cp 201A Cp 2 Dn An Vm cf Vm std Vlc Vw std Bws S Bws 0.9940 1.607 0.77 0.218 2.59E-04 26.272 20.018 54.40 2.560 0.1130 0.9990 Avg. Sqrt ∆p Vs ft/sec Avg. ∆h Avg. Tm F scfm wet acfm Qsd dscfh Qs (final) ft3/min µs Viscosity Run Time (act) Target Time 0.5542 37.88 0.390 95.25 15,759 26,805 8.39E+05 0.6282862 216.92 60.25 60 Sample Point No.Dn used Sampling End Time (Min.Sec.) Actual Dwell Time (Min.Sec.) Desired Dwell Time (Min.Sec.) Stack Temp. Ts F Velocity Head ∆P ∆h D50 Dry Gas Meter Temp. tm F (in) tm F (out) Status Pmin & Pmax 1 - ∆P t1 0.218 5.15 5.15 4.30 258 0.33 0.39 9.990 84 84 Passed 2 - ∆P tn 0.218 10.45 5.30 5.00 255 0.35 0.39 9.990 84 88 Passed3 - ∆P tn 0.218 16.15 5.30 5.15 262 0.37 0.39 9.990 84 93 Passed 4 - ∆P tn 0.218 21.45 5.30 5.00 265 0.36 0.39 9.990 85 99 Passed 5 - ∆P tn 0.218 27.00 5.15 5.00 260 0.34 0.39 9.990 87 104 Passed 6 - ∆P tn 0.218 32.00 5.00 4.45 266 0.31 0.39 9.990 88 106 Passed 7 - ∆P tn 0.218 39.00 7.00 3.45 268 0.20 0.39 9.990 91 100 Passed 8 - ∆P tn 0.218 40.00 1.00 3.45 268 0.20 0.39 9.990 91 105 Passed 9 - ∆P tn 0.218 44.30 4.30 4.15 264 0.26 0.39 9.990 91 108 Passed 10 - ∆P tn 0.218 49.30 5.00 4.45 264 0.31 0.39 9.990 92 110 Passed 11 - ∆P tn 0.218 54.45 5.15 5.00 264 0.34 0.39 9.990 93 112 Passed 12 - ∆P tn 0.218 60.15 5.30 5.00 260 0.35 0.39 9.990 94 113 Passed 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 Run Acceptance Results. D50 9.9900 Passed Sampling Points outside of Pmin & Pmax 0.00 Passed % Isokinetic 108.1 Passed The results are acceptabel if two conditions are met: A. D50 is between 9.0 µm & 11.0 µm.  If D50 is less than 9.0 reject the results and repeat the test. B. One of the following conditions must also be met:That no sampling points are outside Pmin and Pmax or 1. No sampling points are outside the Pmin and Pmax or 2. Isokinetics sampling is betwee 80 percent & 120 percent and no more than one sampling point is outside ∆Pmin and ∆Pmax. Acceptable Run Acceptable Run Test Run Completed Acceptable Run Acceptable Run Page 1 Run 3 Holcim Utelite Test Date 7/10/2024 Imp. Liquid Collected in grams Run No. 3 - RM 201A - Pre-test velocity traverse:Wt. (Final)Wt. (Tare)lc Port 1 Port 2 Port 3 Port 4 410.1 371.8 38.3 Point No.∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'∆P'sqrt ∆P'606.0 603.7 2.3 1 586.0 582.8 3.2 2 969.8 963.3 6.5 3 0.0 ∆P1 Avg. Sqrt ∆P No. Sample Points t1 in min. Ts avg -50oF Avg. Ts oF Ts avg +50oF 0.29 0.5592823 12 4.81 Ts oF 214.80 264.80 314.80 ∆H 0.58 0.54 0.5 ∆ = delta, i.e., delta P would be ∆P Stack I.D. (inches)As ft^2 Pbar Pq (static) Ps CO2 % O2 % N2+C Md lb/lb mole Mw lb/lb mole Stack Saturation 46.50 11.79 24.10 -0.27 24.08 4.00 14.90 81.10 29.24 28.05 3.2756 Y ∆H@ Cp 201A Cp 2 Dn An Vm cf Vm std Vlc Vw std Bws S Bws 0.9940 1.607 0.77 0.216 2.54E-04 26.642 20.133 50.30 2.370 0.1050 0.9990 Avg. Sqrt ∆p Vs ft/sec Avg. ∆h Avg. Tm F scfm wet acfm Qsd dscfh Qs (final) ft3/min µs Viscosity Run Time (act) Target Time 0.5455 37.15 0.400 99.87 15,412 26,288 8.28E+05 0.6321298 218.23 60.00 60 Sample Point No.Dn used Sampling End Time (Min.Sec.) Actual Dwell Time (Min.Sec.) Desired Dwell Time (Min.Sec.) Stack Temp. Ts F Velocity Head ∆P ∆h D50 Dry Gas Meter Temp. tm F (in) tm F (out) Status Pmin & Pmax 1 - ∆P t1 0.216 4.45 4.45 4.45 265 0.29 0.40 9.990 89 88 Passed 2 - ∆P tn 0.216 10.00 5.15 4.45 260 0.30 0.40 9.990 89 91 Passed3 - ∆P tn 0.216 15.15 5.15 5.15 263 0.35 0.40 9.990 89 98 Passed 4 - ∆P tn 0.216 20.30 5.15 5.00 267 0.34 0.40 9.990 91 106 Passed 5 - ∆P tn 0.216 25.30 5.00 5.00 266 0.32 0.40 9.990 91 108 Passed 6 - ∆P tn 0.26 30.30 5.00 4.45 264 0.30 0.40 9.990 93 111 Passed 7 - ∆P tn 0.216 34.30 4.00 3.45 262 0.19 0.40 9.990 96 104 Passed 8 - ∆P tn 0.216 40.15 5.45 4.30 261 0.28 0.40 9.990 96 107 Passed 9 - ∆P tn 0.216 45.00 4.45 4.30 269 0.27 0.40 9.990 96 110 Passed 10 - ∆P tn 0.216 49.45 4.45 4.45 272 0.29 0.40 9.990 97 114 Passed 11 - ∆P tn 0.216 55.00 5.15 5.00 264 0.34 0.40 9.990 99 117 Passed 12 - ∆P tn 0.216 60.00 5.00 5.00 265 0.32 0.40 9.990 99 118 Passed 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 12.00 Run Acceptance Results. D50 9.9900 Passed Sampling Points outside of Pmin & Pmax 0.00 Passed % Isokinetic 112.7 Passed The results are acceptabel if two conditions are met: A. D50 is between 9.0 µm & 11.0 µm.  If D50 is less than 9.0 reject the results and repeat the test. B. One of the following conditions must also be met:That no sampling points are outside Pmin and Pmax or 1. No sampling points are outside the Pmin and Pmax or 2. Isokinetics sampling is betwee 80 percent & 120 percent and no more than one sampling point is outside ∆Pmin and ∆Pmax. Acceptable Run Acceptable Run Test Run Completed Acceptable Run Acceptable Run Page 1