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HomeMy WebLinkAboutDAQ-2024-0069891 DAQC-277-24 Site ID 10007 (B5) MEMORANDUM TO: CEM FILE – HOLCIM THROUGH: Harold Burge, Major Source Compliance Section Manager FROM: Rob Leishman, Environmental Scientist DATE: March 19, 2024 SUBJECT: Source: Kiln Contact: Clint Badger – 801-829-2122 Mark Miller – 972-221-4646 Location: Devil’s Slide, Morgan County, UT Test Contractor: Holcim In-House Staff FRS ID#: UT0000004902900001 Permit/AO#: Title V operating permit 2900001004 dated November 18, 2021 Last revised March 25, 2022 Subject: Review of RA/PST Protocol dated March 18, 2024 On March 18, 2024, DAQ received a protocol for a RA/PST (relative accuracy/performance specification test) of the Holcim Portland Cement Kiln at Devil’s Slide, Morgan County, UT. Testing will be performed on May 2, 2024, to determine the relative accuracy of the HCL monitoring systems. PROTOCOL CONDITIONS: 1. Test Method EPA PS 15 - Measurement of Gaseous Hydrogen Chloride Emissions at Portland Cement Kilns by Fourier Transform Infrared (FTIR) Spectroscopy, analyte spiking procedure: OK DEVIATIONS: No deviations noted. CONCLUSION: The protocol appears to be acceptable. RECOMMENDATION: Send attached protocol review and test date confirmation notice. 1 8 2 Holcim (US) Inc. 6055 E. Croydon Rd. Morgan, Utah 84050 Phone 801 829 6821 www.holcim.com/us Sent via email March 18, 2024 Bryce C. Bird, Director Utah Division of Air Quality 195 North 1950 West Salt Lake City, UT 84116 Re: HCl Performance Test Notification for Holcim (US), lnc.'s Devil's Slide Cement Manufacturing Plant in Morgan, UT Dear Mr. Bird, Holcim (US) Inc. ("Holcim") owns and operates a Portland cement manufacturing plant located in Morgan, UT. The Devil's Slide Plant operates under Utah Division of Air Quality issued Title V Permit, No. 2900001004. The Plant is subject to the National Emission Standards for Hazardous Air Pollutants for the Portland Cement Industry ("Portland Cement NESHAP"), 40 C.F.R. Part 63, Subpart LLL, and is a major source of HAPs. Holcim will perform testing and evaluation of the ABB ACF5000 FTIR to meet the HCl continuous emission monitoring requirements in Subpart LLL. This site-specific HCl CEMS performance evaluation test plan is prepared to satisfy the requirements of 40 CFR 63, Subpart A §63.8(e) for the required monitor performance test (i.e., “performance evaluation”). The performance evaluation will follow the requirements in EPA Performance Specification 15 for FTIR-based CEMS. Spike testing will be completed as outlined in the protocol with an example of previous spike test showing run times from each subsequent calibration of 12 spikes as attachment A. The test is currently scheduled to be conducted May 2, 2024 by Holcim Devil’s Slide Plant personnel. If you should have any questions or need additional information, please contact me at 702.358.7280 or by email at mark.miller@holcim.com. Sincerely, Mark Miller Mark Miller Environmental Director Enclosure test protocol and attachment A Site-Specific HCl CEMS Performance Evaluation Test Plan for Holcim (US) Inc. Devil’s Slide Plant Holcim (US) Inc. (“Holcim”) owns and operates a Portland cement manufacturing plant located in Morgan, Utah. The Devil’s Slide plant is subject to the National Emission Standards for Hazardous Air Pollutants for the Portland Cement Industry (“Portland Cement NESHAP”), 40 CFR Part 63, Subpart LLL, and is a major source of HAPs. The Devil’s Slide plant will perform testing and evaluation of the ABB ACF5000 FTIR to meet the HCl continuous emission monitoring requirements in Subpart LLL. This site- specific HCl CEMS performance evaluation test plan is prepared to satisfy the requirements of 40CFR63, Subpart A §63.8(e) for the required monitor performance test (i.e., “performance evaluation”). The performance evaluation will follow the requirements in EPA Performance Specification 15 for FTIR-based CEMS. Schedule The performance evaluation is expected to be conducted on May 2nd, 2024, starting at 10:00 A.M. Holcim will notify UDAQ as soon as practical of any scheduling changes or delays. Holcim Contacts Questions or comments about the test program should be directed to: Clinton Badger Environmental Manager Holcim (US) Inc. 801-829-2122 clinton.badger@holcim.com Test Services Holcim will provide the necessary performance evaluation services. Devil’s Slide Plant personnel will conduct the performance evaluation. These individuals have extensive experience working with CEMS and HCl emission measurements at the Devil’s Slide plant. Objectives and Approach The objective of this test program is to demonstrate that the ABB ACF5000 HCl CEMS meets the applicable requirements of Performance Specification 15 (PS 15) for FTIR- based CEMS. If successful, this will complete the requirements for the monitor performance test (i.e., “performance evaluation”). The monitor can continue to be used to acquire HCl emissions data to demonstrate compliance with the emission limitation and will be subject to ongoing quality assurance requirements in 40CFR60, Appendix F, Procedure 1. Subpart LLL, §63.1350(l)(1) states: “(1) If you monitor compliance with the HCl emissions limit by operating an HCl CEMS, you must do so in accordance with Performance Specification 15 (PS 15) of appendix B to part 60 of this chapter, or, upon promulgation, in accordance with any other performance specification for HCl CEMS in appendix B to part 60 of this chapter. You must operate, maintain, and quality assure a HCl CEMS installed and certified under PS 15 according to the quality assurance requirements in Procedure 1 of appendix F to part 60 of this chapter except that the Relative Accuracy Test Audit requirements of Procedure 1 must be replaced with the validation requirements and criteria of sections 11.1.1 and 12.0 of PS 15.” The above referenced Section 11.1.1 and calculations in Section 12.0 of PS 15 require that the performance of the CEMS be validated by conducting analyte spikes (also known as “dynamic spikes”) rather than by the more traditional method of acquiring independent effluent measurements and calculating the relative accuracy. In addition, PS 15 does not include a 7-day zero and upscale calibration drift test. However, it does require injection and analysis of a calibration transfer standard (CTS) on each day of the test program and it requires that the monitor response agree within ± 5% of the CTS value. CO2 tri blend gas will be used as the CTS gas. The CTS gas may include other constituents such as SO2 or NO. Analyte Spiking Procedure HCL spike test will consist of 12 sequential up and down analyte spikes which will typically be conducted over a 2.0 hour period with 2 minutes between spikes. Holcim has provided an example of typical spike sequencing as attachment A. Analyte spiking is the quantitative addition of a known amount of calibration gas into the effluent gas stream. The exact concentration of the calibration spike gas is determined by directly analyzing the calibration gas by the FTIR (or using the tag value if trusted). The calibration gas is then spiked into the CEMS probe immediately upstream of the particulate matter filter (similar to a normal CEMS system calibration.) The difference between analyte spiking and system calibrations is that only a fraction of the total flow is injected into the effluent stream instead of conducting a “probe flood” or similar procedure that results in 100% calibration gas in the analyzer cell. Spike gas is introduced at a rate of no greater than 10% of the total sample flow rate: i.e., 10:1 dilution so that the sample gas matrix remains mostly unchanged. (The native effluent concentrations are diluted by the introduction of the spike gas.) For example if the total system flow is 10 ppm, then the spike flow can be no greater than 1 lpm. Dynamic spikes that introduce less spike gas than 10:1 (e.g., 15/1 and 20/1) are also acceptable. The nominal HCl concentration of the spike gas cylinder will be between 40 and 70 ppm. The spike gas will also contain about 330 ppm N 2O ppm as a tracer to determine spike flow to total flow rate according to equation 3.2 below. The goal is to quantitatively add approximately 4 to 7 ppm of HCl with the stack gas effluent and then examine the CEMS response to determine if the sampling and analytical systems are able to produce reliable HCl monitoring data. The specific procedure is as follows: Analyze the spike gas cylinder directly with the FTIR. Name the response values as the cylinder reference value (i.e., “tag value”) for both HCl and N 2O concentrations. Alternately, use the gas supplier provided tag value if it is a known and trusted value. Obtain stable sequential spectra while sampling stack gas only while the process is operating at stable conditions and name this as unspiked sample number 1. Begin injecting HCl spike gas at a 10:1 ratio1 or less until stable readings are obtained. (ACF5000 values are updated approximately every 35 seconds and are the result of the co-addition of x FTIR scans. VIM DAS compiles 1-minute averages but is not synchronized to ACF5000 analysis cycles.) Collect several sequential measurements and name the initial final stable response as spiked sample number 1. Collect an additional independent value (separated by 1 or more 1-minute VIM DAS averages) and name this as spiked sample 2. Shut the spike off and allow the measurements to stabilize back to unspiked effluent only (“baseline”) concentration. Then, record two independent baseline stable values as unspiked sample numbers 2 and 3. Repeat this series of spiked and unspiked samples until there are twelve sets of spiked and unspiked effluent measurements. Variations in the effluent concentrations of either HCl or the tracer gas N2O during the analyte spike procedures can adversely affect the results. It is important to conduct these tests during operating periods when variability of these concentrations is low. In the event that excess variations in the HCl or N2O concentrations are observed, it may be necessary to discard affected spike runs and conduct additional runs. Sulfur hexafluoride (SF6) is often used for FTIR analyzers as a tracer because SF6 has a large infrared absorption, is easily measured at low concentrations (especially for liquid nitrogen cooled MCT detectors) and is not present in the effluent. 5 ppm of SF6 is a good cylinder concentration for some FTIRs. However, ABB prefers use of N2O as a tracer since it was already a compound included in their TUV certified analysis routines. The concentration of N2O in the cylinder must be significantly higher due to the weaker N2O absorption characteristics. In addition, the calculations of spike recovery must take into account that there is a low level of N2O present in the effluent samples at most cement kilns. ABB previously submitted documentation and procedures supporting the N2O spike procedure to Holcim. These documents are available upon request. Jim Peeler of EMI derived HCl spike recovery calculations for the use of N2O as a tracer during the Holicm 2012 HCl CEMS Field Evaluation. These procedures were validated during the Holcim 2012 study and also used during the Holcim 2015 evaluation of the ABB ACF5000 CEMS. The dilution factor calculation when the tracer gas is present in the effluent samples is now included in the Performance Specification 18, Appendix A “Standard Addition Procedures” as equation A3. The HCl spike recovery calculations for systems that also measure N2O as used in the previous Holcim studies and now found in PS18, Appendix A are as follows: 1 Adjust the spike gas flow rate to provide a spiked N2O, value to a level of 0.1 (10%) or less of the direct analysis value of N2O. For example, if a direct analysis is 330 ppm N2O, then adjust the spike gas flow rate until the observed stable value of the spiked effluent N2O measurement is about 33 ppm plus the native N2O concentration. Dilution Factor: 𝐷𝐷𝐷𝐷𝐷𝐷𝐷𝐷 = � N2OObserved − N2ONative � N2OBottle − N2ONative N2OObserved − N2ONative CExpected = CNative �1 − N2O Bottle − N2O � Native N2OObserved − N2ONative + CSpike Gas � N2O Bottle − N2O � Native Where: CExpected = HCl expected concentration response for dynamic spike (i.e., analyte spike) based on the sum of the diluted native concentration and spike addition CNative = HCl concentration present in the sample gas without spike added N2OObserved = Concentration of N2O observed during dynamic spike gas injection concurrent with stable spiked HCl response N2ONative = N2O concentration in the sample gas without spike added N2OBottle = Concentration of N2O in spike gas determined from direct analysis of the spike gas CSpike Gas = HCl concentration of spike gas as determined from direct analysis of the spike gas The definition of the dilution factor above is the reciprocal (i.e., 1/DF) as defined in PS 15. Calculate the amount of added HCl in the spiked gas: Cs = Dir HCl/DF in PS15 Eq. 5 is therefore modified to be: Cs = Dir HCl*DF Calculate the Bias: B = Sm – Mm – Cs Where: Sm= mean of average of spiked samples Mn = mean of average of unspiked samples Calculate the Standard Deviations: Calculate the standard deviation and RSD of the spiked samples (and unspiked sample) differences. Where: Di2 = the difference between spiked and unspiked sample pairs; S1-S2 and U1-U2 RSD = Sds/Sm Calculate the CF: CF = 1/(1 + B ) Cs Calculate the composite standard deviation of the combined differences: SD = �Sds2 + Sdu2 Determine If Bias is Statistically Significant – Compare t = 2.201 B t = SD Spreadsheet calculations have been developed for these calculations. Data Quality Objectives The data quality objectives are: • Demonstrate acceptable CTS gas analysis results for each day of the test program where the ACF5000 response is within ± %5 of the gas value. • Acquire a minimum of 12 valid spiked and unspiked pairs of samples where the spike gas flow rate is 10% or less of the total sample flow rate as determined by the N2 O tracer concentration and the measurements are not adversely affected by temporal variations in the effluent concentrations • RSD < 50% for the spiked (and unspiked) paired differences • If the apparent bias is determined to be statistically significant, the bias correction factor (CF) shall be between 0.7 and 1.3 CEMS Description and Quality Assurance An ABB ACF5000 FTIR-based CEMS will be evaluated to determine its ongoing ability to acquire accurate and precise HCl effluent measurements. The CEMS is a full extractive (i.e., non-dilution) measurement system. It consists of an M&C sample probe with provisions for injecting calibration gases and spike gases upstream of the PM filter, approximately 96 feet of heated sample line (also containing calibration gas lines and communications) and the ABB FTIR analyzer. The sample lines and analyzer gas cell are maintained at 180°C (356°F), while the sample probe and PM filter may be operated at a higher temperature of ~230°C. The ABB sample probe acquires samples from the stack at the same level used for all stack sampling activities and a point approximately 1 meter from the stack wall. RATAs of SO2, NO, O2 and CO2 CEMS have been performed at this location for many years and there is no evidence of gas concentration stratification and no reason to expect that such stratification is present. The ACF5000 will communicate with the VIM DAS that is used to record all emission monitoring data. All effluent measurements that are used to determine the ACF5000 performance will be acquired from the VIM DAS records. Due to delays and technical problems encountered by NIST and EPA, NIST Traceable HCl calibration gases with an uncertainty of ≤5% are not available. HCl calibration gases with nominal concentrations of 40 and 70 ppm HCl and 330 ppm N2O will be used. These gases are being certified in accordance with a broadly applicable EPA approved alternate method designated Alt-114 which was based on an alternative method request and supporting information submitted to EPA by Air Liquide. EPA’s approval is contained in a letter from Steffan Johnson, Group Leader, Measurement Technology Group, OAQPS, dated Feb. 22, 2016. The designation of these gases are HCl GMACS and are certified by Air Liquide (now Airgas) by dual interlocking gravimetric and classical gas analysis methods, each with a total combined uncertainty of <5%. Additional information regarding the HCl GMACS and an example certificate of analysis are available upon request. Compressed HCl calibration gases will be introduced to the ACF5000 using Silconert Treated dual stage low volume stainless steel regulators and HCl Gas Delivery Panel Prototype VI and Nitrogen Purge & Purification Panel acquired from Air Liquide. These devices allow the gas regulators and gas delivery panel to be completely purged with ultra-dry nitrogen prior to and after the introduction of HCl mixtures to greatly reduce the potential for internal corrosion and/or HCl losses and to reduce the time required to achieve stable HCl responses from the ACF5000. After the performance certification of the ACF5000 for the measurement of HCl concentrations is successfully completed, the Devil’s Slide plant will continue to operate the HCl CEMS in accordance with the requirements of 40 CFR 60, Appendix F, Procedure 1. The span value of the HCl CEMS will be 20 ppm. Daily zero checks will be performed by injection of zero gas and daily upscale calibration checks will be performed using an internal gas cell. Quarterly cylinder gas audits will be performed using HCl GMACS compressed gases at 20-30% of span and 50-60% of span. In accordance with the explicit requirements of §63.1350(l)(1), dynamic spike evaluations will be performed annually. Run Date time Action HCl Cylinder [ppm] HCl FTIR [ppm] N2O Cylinder [ppm] N2O FTIR [ppm] HCl Expected [ppm] % Recovery (all) Cs = HCl Added [ppm] HCl Change [ppm] % Recovery (Change) DF Spike 1 Up 11/4/2022 12:22 PM baseline 0.26 0.8 11/4/2022 12:13 PM spike response 40.2 3.90 333.0 33.2 4.16 93.9%3.92 3.67 93.5%9.8% Spike 2 Down 11/4/2022 12:24 PM baseline 0.20 0.9 11/4/2022 12:16 PM spike response 40.2 4.04 333.0 31.8 3.92 103.0%3.74 3.86 103.2%9.3% Spike 3 Up 11/4/2022 12:46 PM baseline 0.35 0.9 11/4/2022 12:37 PM spike response 40.2 4.72 333.0 36.2 4.59 102.9%4.27 4.41 103.1%10.6% Spike 4 Down 11/4/2022 12:48 PM baseline 0.25 0.7 11/4/2022 12:40 PM spike response 40.2 4.32 333.0 33.9 4.24 101.9%4.02 4.09 102.0%10.0% Spike 5 Up 11/4/2022 13:06 PM baseline 0.40 1.0 11/4/2022 12:57 PM spike response 40.2 3.89 333.0 30.0 3.88 100.3%3.51 3.52 100.4%8.7% Spike 6 Down 11/4/2022 13:10 PM baseline 0.23 0.7 11/4/2022 12:59 PM spike response 40.2 4.13 333.0 32.0 3.99 103.4%3.79 3.92 103.6%9.4% Spike 7 Up 11/4/2022 13:32 PM baseline 0.26 0.6 11/4/2022 13:19 PM spike response 40.2 4.80 333.0 36.6 4.59 104.7%4.35 4.57 104.9%10.8% Spike 8 Down 11/4/2022 13:35 PM baseline 0.21 0.7 11/4/2022 13:22 PM spike response 40.2 4.53 333.0 34.0 4.22 107.4%4.03 4.34 107.8%10.0% Spike 9 Up 11/4/2022 13:53 PM baseline 0.30 0.6 11/4/2022 13:44 PM spike response 40.2 4.01 333.0 30.8 3.93 102.2%3.65 3.74 102.3%9.1% Spike 10 Down 11/4/2022 13:56 PM baseline 0.24 0.5 11/4/2022 13:46 PM spike response 40.2 4.08 333.0 31.1 3.92 104.1%3.70 3.86 104.4%9.2% Spike 11 Up 11/4/2022 14:25 PM baseline 0.32 0.8 11/4/2022 14:12 PM spike response 40.2 4.76 333.0 36.1 4.56 104.4%4.27 4.47 104.7%10.6% Spike 12 Down 11/4/2022 14:42 PM baseline 0.37 0.7 11/4/2022 14:16 PM spike response 40.2 4.57 333.0 34.9 4.47 102.3%4.14 4.24 102.4%10.3% Mean 102.5%3.95 102.7% Spike No.Spiked Response Sn-S(n-1)Sdi*Sdi Unspiked Response Un-U(n-1)Udi*Udi Cs (HCl Added, ppm) 1 3.90 0.26 3.92 2 4.04 0.14 0.020 0.20 -0.06 0.004 3.74 3 4.72 0.35 4.27 4 4.32 -0.40 0.160 0.25 -0.10 0.010 4.02 5 3.89 0.40 3.51 6 4.13 0.24 0.058 0.23 -0.17 0.029 3.79 7 4.80 0.26 4.35 8 4.53 -0.27 0.073 0.21 -0.05 0.003 4.03 9 4.01 0.30 3.65 10 4.08 0.07 0.005 0.24 -0.06 0.004 3.70 11 4.76 0.32 4.27 12 4.57 -0.19 0.036 0.37 0.05 0.003 4.14 Mean Sm 4.31 Mean Mm 0.28 Mean Cs 3.95 SDs 0.171 SDu 0.065 RSDs 3.97%RSDu 23.1% Composite SD 0.18 Composite RSD 23.4%Precision Acceptable RSD < 50% Bias = Sm-Mm-Cs (ppm)0.08 Statistically Significance Test t 0.441 Bias Not Statisticaly Significant if t < 2.201 Bias is not statistically significant Correction Factor CF 0.980 Correction Factor Is Not Required Table 1: Dynamic Spike Results for Holcim (US), Inc. Devil's Slide ACF5000 CEMS Analysis from VIM DAS Data ASTM D 6348 Method 321 Table 2: PS 15 Calculations for Devil's Slide ACF 5000 HCl CEMS