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HomeMy WebLinkAboutDRC-2016-006718 - 0901a0688062ca30ENERGY FUELS Energy Fuels Resources (LISA) Inc. 225 Union Blvd. Suite 600 Lakewood, CO, US, 80228 303 974 2140 www.energvfuels.com DRC- 20i6- 00671Q busses; t May 2’2016 MAY - 4 2016 Sent VIA OVERNIGHT DELIVERY Mr. Scott Anderson Director Division of Waste Management and Radiation Control Utah Department of Environmental Quality 195 North 1950 West P.O. Box 144880 Salt Lake City, UT 84114-4820 Re: Transmittal of Revised Spill Prevention, Control and Countermeasures Pan (“SPCC”) and Revised Stormwater Best Management Practices Plan (“SWBMPP”) for White Mesa Uranium Mill Dear Mr. Anderson: This letter transmits Energy Fuels Resources (USA) Inc.’s (“EFRI’s”) proposed revisions to the White Mesa Mill SPCC and SWBMPP. These revisions include changes made to: 1. Update personnel and contact information. 2. Correct typographical errors. For ease of review we have provided both redline/strikeout (text only) and clean versions (text and all tables and figures) of each document. If you should have any questions regarding these plans please contact me. Yours very truly, Energy Fuels Resources (USA) Inc. Kathy Weinel Quality Assurance Manager CC: David C. Frydenlund Harold R. Roberts David E. Turk Logan Shumway Scott Bakken REDLINE WHITE MESA MILL SPILL PREVENTION, CONTROL, AND COUNTERMEASURES PLAN FOR CHEMICALS AND PETROLEUM PRODUCTS May 2,2016 Energy Fuels Resources (USA) Inc. WHITE MESA MILL 6425 S. HWY 191 BLANDING, UT 84511 ENERGY FUELS Contents 1.0 OBJECTIVE.................................................................................................................................1 2.0 RESPONSIBILITIES.................................................................................................................24 3.0 DRAINAGE BASINS, PATHWAYS, AND DIVERSIONS........................................................32 4.1 Basin A1............................................................................................................................32 4.2 Basin A2............................................................................................................................32 4.3 Basin B1............................................................................................................................32 4.4 Basin B2............................................................................................................................32 4.5 Basin B3............................................................................................................................32 4.6 Basin C..............................................................................................................................32 4.7 Basin D..............................................................................................................................43 4.8 Basin E..............................................................................................................................43 4.9 Basin F..............................................................................................................................43 5.0 POTENTIAL CHEMICAL SPILL SOURCES AND SPILL CONTAINMENT..........................43 5.1 Reagent Tanks (Tank list included in Table 2.0).............................................................43 5.2 Ammonia...........................................................................................................................43 5.3 Ammonia Meta-Vanadate................................................................................................43 5.4 Caustic Storage (Sodium Hydroxide)...............................................................................53 5.5 Sodium Carbonate (Soda Ash)........................................................................................54 5.6 Sodium Chlorate............................................................................................................... 54 5.7 Sulfuric Acid.....................................................................................................................54 5.8 Vanadium Pentoxide........................................................................................................64 5.9 Kerosene (Organic)..........................................................................................................65 5.10 Used/Waste Oil................................................................................................................. 65 6.0 POTENTIAL PETROLEUM SOURCES AND CONTAINMENT.............................................65 6.1 Petroleum Tanks..............................................................................................................65 6.1.1 Diesel.........................................................................................................................65 6.2 Aboveground Fuel Pump Tanks.......................................................................................65 6.2.1 Diesel.........................................................................................................................66 6.2.2 Unleaded Gasoline...................................................................................................75 6.2.3 PumpStation.............................................................................................................75 6.2.4 Truck Unloading........................................................................................................75 7.0 SPILL DISCOVERY AND REMEDIAL ACTION.....................................................................75 8.0 SPILL INCIDENT NOTIFICATION...........................................................................................97 8.1 External Notification............................................................................................................93 8.2 Internal Notification.............................................................................................................93 9.0 RECORDS AND REPORTS...................................................................................................108 10.0 SPILL REPORTING REQUIREMENTS..............................................................................119 11.0 PERSONNEL TRAINING AND SPILL PREVENTION PROCEDURES............................JM9 11.1 Training Records............................................................................................................119 11.2 Monitoring Reports.........................................................................................................119 12.0 REVISION.............................................................................................................................119 13.0 MILL MANAGER APPROVAL............................................................................................1240 14.0 CERTIFICATION BY REGISTERED PROFESSIONAL ENGINEER...............................1240 15.0 SUMMARY...........................................................................................................................1344 WHITE MESA MILL SPILL PREVENTION, CONTROL, AND COUNTERMEASURES PLAN FOR CHEMICALS AND PETROLEUM PRODUCTS 1.0 OBJECTIVE The objective of the Spill Prevention, Control, and Countermeasures (SPCC) Plan is to serve as a site-specific guideline for the prevention of and response to chemical and petroleum spills. The plan outlines spill potentials, containment areas, and drainage characteristics of the White Mesa Mill site. The plan addresses chemical spill prevention, spill potentials, spill discovery, and spill notification procedures. Spills are reportable if the spill leaves the site. Ammonia is the only chemical (as vapor) that has the potential to leave the site. In addition, chemical and petroleum spills will be reported in accordance with applicable laws and regulations. 1.1 Plan Organization This SPCC is organized as follows: Section 1,0 Objective Section 2 Responsibilities Section 3.0 Drainage Basins, Pathways, and Diversions Section 4 Description of Basins Section 5.0 Potential Chemical Spill Sources and Spill Containment Section 6.0 Potential Petroleum Spill Sources and Containment Section 7.0 Spill Discovery and Remedial Action Section 8.0 Spill Incident Notification Section 9.0 Records and Reports Section 10.0 Spill Reporting Requirements Section 11.0 Personnel Training and Spill Prevention Procedures Section 12.0 Revision Section 13.0 Mill Manager Approval Section 14,0 Certification by Registered Professional Engineer Section 15.0 Summary Tables: Table 1.0 is the Energy Fuels Resources (USA) Inc. (EFRI) personnel responsible for implementing this SPCC. Table 2.0 lists the reagent tanks and their respective capacities. Table 3.0 lists the laboratory chemicals, their amounts, and their reportable quantities. Table 4,0 lists the reagent vard/small quantity chemicals. Table 5.0 lists the chemicals in the reagent yard, their amounts, and their reportable quantities. Table 6.0 lists the petroleum products and solvents on site. 1 Figures: Figure lih shows the Mill Site Layout,_shows a map of the mill site including the locations of the chemical tanks on-site. Figure 2 shows the basins and drainage ditch areas for the mMill sSite. Figure 3 shows the organization chart for Mill Operations. Table 1.0 is an organization chart for Mill operations. Table 2.0 liste-the- reagent tanks and their-respective capacities. Table 3.0 lists the laboratory chemicals, their amounts, and their reportable quantities. Table 4.0 lists the operations chemicals-—Table 5.0 lists the chemicals in the reagent yard, their amounts; -and their reportable quantities. Table 6.0 lists the petroleum-pfoducts-and solvents en-sker 2.0 RESPONSIBILITIES Personnel responsible for spill prevention and follow-up spill reporting are included on Table 1 which is included in the Tables Tab of this SPCC. Person in charge of facility responsible for spill prevention: Mr. Dan Hillsten, Mill Manager 6-125 South Highway 191 Blanding, UT 84511 (435) 678 2221 (work) -------(435)979 3041 (home) Person4n- eharge-of follow-up spill-reporting: Mr. David Turk, EH&S Manager 6425 South Highway 191 Blanding, UT 84511 (435) 678 2221 (work) (435) 678 7802 (home) 2 3.0 DRAINAGE BASINS, PATHWAYS, AND DIVERSIONS The main drainage pathways are illustrated in Figure 2. The map shows drainage basin boundaries, flow paths, constructed diversion ditches, tailing cells, the spillway between Cell 2 and 3, dikes, berms, and other relevant features. The White Mesa Mill is a “zero” discharge facility for process liquid wastes. The mill area has been designed to ensure that all spills or leaks from tanks will drain toward the lined tailing eefcmanagement system. The tailings cellsmanagement system, in turn, are-is operated with sufficient freeboard (minimum of three feet) to withstand 100% of the PMP (Probable Maximum Precipitation). This allows for a maximum of 10 inches of rain at any given time. Precipitation and unexpected spills from the mill site are contained within their prospective drainage basins. Overflow ultimately drains into one of the four lined tailings cellsthe tailings management system. 4.1 Basin A1 Basin A1 is north of Cell 1-f and Diversion Ditch No. 1. The basin contains 23 tributary acres, all of which drain into Westwater Creek. 4.2 Basin A2 Basin A2 contains all of Cell 1-1 including an area south of the Diversion Ditch No. 1. The basin covers 84 acres. Any overflow from this basin would be contained within Cell 14. 4.3 Basin B1 Basin B1 is north of the mill area. The basin contains 45.4 tributary acres. Overflow from this basin drains into a flood retention area by flowing through Diversion Ditch No. 2. Diversion Ditch No. 2 drains into Westwater Creek. 4.4 Basin B2 Basin B2 is northeast of the mill area and contains only 2.6 tributary acres. Overflow from this basin would drain into Diversion Ditch No. 3. Diversion Ditch No. 3 ultimately drains into Diversion Ditch No. 2. 4.5 Basin B3 Basin B3 contains most of the mill area, buildings, ore stockpiles, process storage tanks, retention ponds, spill containment structures, pipelines, and roadways. The normal direction of flow in this basin is from the northwest to the southwest. Any overflow from this basin would drain into Cell 14. The basin contains 64 acres. This basin has sufficient freeboard to withstand 100% of the PMP (Probable Maximum Precipitation). This allows 10 inches of rain for any given storm event. 4.6 Basin C 3 Basin C contains all of Cell 2. The basin consists of 80.7 acres. Areas in this basin include earth stockpiles and the heavy equipment shop. The direction of flow in this basin is to the southwest. All overflows in this basin is channeled along the southern edge of the basin. Overflow then flows into Cell 3 via the spillway from Cell 2 to Cell 3. 4.7 Basin D Basin D contains all of Cell 3. This basin consists of 78.3 acres including a portion of the slopes of the topsoil stockpile and random stockpile. The basin contains all flows, including those caused by the PMFP. 4.8 Basin E Basin E contains Cell 4A and consists of 40 acres. All anticipated flows including those caused by the PMFP will be contained within the basin and will flow directly into Cell 4A. 4.9 Basin F Basin F wvH-contains Cell 4B, and consists of 40 acres. All anticipated flows including those caused by the PMP will be contained within the basin and will flow directly into Cell 4B.if and when constructed. The area consists of 44 acres at a relatively low elevation. Direction of flow in ■this-basln4s~tewafds the southwest. 5.0 POTENTIAL CHEMICAL SPILL SOURCES AND SPILL CONTAINMENT 5.1 Reagent Tanks (Tank list included in Table 2.0) 5.2 Ammonia The ammonia storage tanks consist of two tanks with a capacity of 31,409 gallons each. The tanks are located southeast of the Mill building. Daily monitoring of the tanks for leaks and routine integrity inspections will be conducted to minimize the hazard associated with ammonia. The reportable quantity for an ammonia spill is 7 gallons. Ammonia spills should be treated as gaseous. Ammonia vapors will be monitored closely to minimize the hazard associated with inhalation. If vapors are detected, efforts will be made to stop or repair the leak expeditiously. Ammonia is the only chemical (as vapor) that has the potential to leave the site. i Meta-Vanadate Ammonium meta-vanadate is present in the vanadium precipitation area of the Mill building as the process solutions move through the circuit to produce the vanadium end product. Spills would be contained in the process sump within the vanadium precipitation area. The reportable spill quantity for ammonium meta-vanadate is 1,000 pounds.Ammonia meta vanadate is present in the SX building as the process solutions move through the circuit to produce the vanadium-end-produetr -Spills-would be contained in the process sump within the SX building. The reportable spill quantity for ammonia meta vanadate is 1,000 pounds. 4 5.4 Caustic Storage (Sodium Hydroxide) The caustic storage tank is located on a splash pad on the northwest comer of the SX building. The tank has a capacity of 19,904 gallons. The tank supports are mounted on a concrete curbed catchment pad which directs spills into the sand filter sump in the northwest comer of the SX building. The reportable spill quantity for sodium hydroxide is 85 gallons. 5.5 Sodium Carbonate (Soda Ash) The soda ash solution tank has a capacity of 16,921 gallons and is located in-outside the northeast comer of the SX building. Spills from the soda ash solution tank are contained in the North SX impound and run to Cell 1. The smaller soda ash shift tank has a capacity of 8,530 gallons and is located in the SX building. Spills will be diverted into the boiler area, and would ultimately drain into Cell 1-f. There is no reportable spill quantity associated with sodium carbonate. 5.6 Sodium Chlorate Sodium chlorate tanks consist of three fiberglass tanks located within a dike east of the SX building. Tank maximum volumes of the three tanks are 16,075. 21,057 and 28,788 gallons. Daily monitoring of the tanks for leaks and integrity inspections will be conducted to minimize the hazard associated with sodium chlorate.Sodium chlorate tanks consist of two fiberglass tanks located within a dike east of the SX building. The larger tank-is-used for dilution-purposes and has a maximum capacity of 17,700 gallons. The smaller tank serves as a storage tank and has a capacity of 10,500 gallons. Daily monitoring-oTthe-tanks for leaks and integrity inspections will be conducted to minimize the hazard ■ass<reiated-wlth-sedium chlorate. Sodium chlorate that has dried and solidified becomes even more of a safety hazard due to its extremely flammable nature. The reportable spill quantity for sodium chlorate is 400 gallons. 5.7 Sulfuric Acid The sulfuric acid storage tanks consist of one large tank with the capacity of 1,600,000 gallons and twe-one smaller tanks with capacities a capacity of 269.16011,000 gallons-eaeh. The large tank is located in the northwest comer of mill area basin B3 and is primarily used for acid storage and unloading. The tank support for the large tank is on a mound above a depression which would contain a significant spill. All flows resulting would be channeled to Cell IT. The tank is equipped with a high level audible alarm which sounds prior to tank overflows. A concrete spill catchment with a sump in the back provides added containment around the base of the tank. However, the catchment basin would not be able to handle a major tank failure such as a tank rupture. The resulting overflow would flow towards Cell 1- I. The twe-smaller storage tanks are-is located within an equal voltime-spifl ■ containment dike east of the millon the north side of the SX building. The tanks are not presently in use, but are-isequipped with ahigh level audible alarms. The reportable spill quantity for sulfuric acid is 65 gallons. 5 5.8 Vanadium Pentoxide Vanadium pentoxide is produced when vanadium is processed through the drying and fusing circuits and is not present in the vanadium circuit until after the deammoniator. Efforts will be made to minimize leaks or line breaks that may occur in processes in the circuit that contain vanadium pentoxide. Special care will be taken in the transportation of this chemical. The reportable spill quantity for vanadium pentoxide is 1000 pounds. 5.9 Kerosene (Organic) The kerosene storage area is located in the central mill yard and has a combined capacity of 10,152 gallons in three tanks. Any overflow from these three tanks would flow around the south side of the SX building and then into Cell 14. These tanks have drain valves which remain locked unless personnel are supervising draining operations. The reportable spill quantity for kerosene is 100 gallons. 5.10 Used/Waste Oil Used/ Waste oil for parts washing is located north of the maintenance shop in a tank and has a capacity of 5,000 gallons. The tank is contained within a concrete containment system. Ultimate disposal of the uUsed oil is to an EPA permitted oil rccvolerwill be disposed of on site. Any oil escaping the concrete containment system will be cleaned up. Soil contaminated with used oil will be excavated and disposed of in Cell 2 the Cell currently used for the disposal of solid Mill wastes. 6.0 POTENTIAL PETROLEUM SOURCES AND CONTAINMENT 6.1 Petroleum Tanks 6.1.1 Diesel There are two diesel storage tanks located north of the mill building. The tanks have capacities of 250 gallons each. One of the diesel tanks is for the emergency generator. The other tank is located in the pumphouse on an elevated stand. Spillage from either tank would ultimately flow into Cell 14. The reportable spill quantity for diesel is 100 gallons. The spill is also reportable if the spill has the potential for reaching any nearby surface waters or ground waters. 6.2 Aboveground Fuel Pump Tanks 6.2.1 Diesel The diesel tank is located on the east boundary of Basin B3 and has a capacity of 6,000 gallons. The tank is contained within a concrete catchment pad. The reportable spill quantity for diesel is 100 gallons. A diesel spill is also reportable if the spill has the potential for reaching any surface waters or ground waters. 6 6.2.2 Unleaded Gasoline The unleaded gasoline tank is located next to the diesel tank. The unleaded gasoline tank has a capacity of 3,000 gallons and is contained within the same containment system as the diesel tank. Spills having the potential for reaching any surface waters or ground waters will need to be reported. The reportable spill quantity for unleaded gasoline is 100 gallons. 6.2.3 Pump Station Both the diesel and the unleaded gasoline tanks will be used for refueling company vehicles used around the mill site. The pump station is equipped with an emergency shut-off device in case of overflow during fueling. In addition, the station is also equipped with a piston leak detector and emergency vent. Check valves are present along with a tank monitor console with a leak detection system. The catchment is able to handle a complete failure of one tank. However, if both tanks failed the concrete catchment pad would not be able to contain the spill. In this case, a temporary berm would need to be constructed. Absorbent diapers or floor sweep would be used in an effort to limit and contain the spill. The soil would have to be cleaned up and placed in the Cell currently used for the disposal of solid Mill wastesthe authorized dump in Cell 2. 6.2.4 Truck Unloading In the event of a truck accident resulting in an overturned vehicle in the mill area, proper reporting and containment procedures will be followed when warranted, such as when oil or diesel fuel is spilled. Proper clean-up procedures will be followed to minimize or limit the spill. The spill may be temporarily bermed or localized with absorbent compounds. Any soils contaminated with diesel fuel or oil will be cleaned up and placed in the Cell currently used for the disposal of solid Mill wastesCeU-3. 7.0 SPILL DISCOVERY AND REMEDIAL ACTION Once a chemical or petroleum spill has been detected, it is important to take measures to limit additional spillage and contain the spill that has already occurred. Chemical or petroleum spills will be handled as follows: • The Shift Foreman will direct efforts to shut down systems, if possible, to limit further release. • The Shift Foreman will also secure help if operators are requiring additional assistance to contain the spill. • The Shift Foreman is also obligated to initiate reporting procedures. • Once control measures have begun and personal danger is minimized, the Shift Foreman will notify the Production Superintendent, Maintenance Superintendent, or Mill Manager. • The Production or Maintenance Superintendent will notify the Mill Manager, who in turn will notify the EH&S Manager and/or the Environmental Coordinator. • The Mill Manager will assess the spill and related damage and direct remedial actions. The corrective actions may include repairs, clean-up, disposal, and 7 company notifications. Government notifications may be necessary in some cases. If a major spill continues uncontrolled, these alternatives will be considered: 1. Construct soil dikes or a pit using heavy equipment. 2. Construct a diversion channel into an existing pond. 3. Start pumping the spill into an existing tank or pond. 4. Plan further clean-up and decontamination measures. 8.0 SPILL INCIDENT NOTIFICATION 8.1 External Notification For chemical and petroleum spills that leave the site, the following agencies should be notified: 1. EPA National Response Center 1-800-424-8802 2. US Nuclear Regulatory Commission 301-816-5100 3. State of Utah 801-538-7200 In case of a tailings dam failure, contact the following agencies: 1. US Nuclear Regulatory Commission 301-816-5100 2. State of Utah, Natural Resources 801-538-7200 8.2 Internal Notification Internal reporting requirements for incidents, spills, and significant spills are as follows: Report Immediately Event Criteria: 1. Release of toxic or hazardous substances 2. Fire, explosions, and accidents 3. Government investigations, information requests, or enforcement actions 4. Private actions or claims (corporate or employee) 5. Deviations from corporate policies or government requirements by management Which have or could result in the following: 1. Death, serious injury, or adverse health effects 2. Property damage exceeding $1,000,000 3. Government investigation or enforcement action which limits operations or assesses penalties of $100,000 or more 4. Publicity resulted or anticipated 5. Substantial media coverage Report at the Beginning of the Next Day Event Criteria: 1. Was reported to a government agency as required by law 2. Worker (employee or contractor) recordable injury or illness associated with a release 3. Community impact-reported or awareness 4. Publicity resulted or anticipated 5. Release exceeding 5,000 pounds of process material, waste, or by-product 9 In the event of a spill requiring reporting, the Mill Manager is required to call the Quality Assurance Manager, the Executive Vice President and Chief Operating Officer, or the President and Chief Executive Officer. The spill will first be reported to the Shift Foreman. The Shift Foreman will then report the spill to the Mill Superintendent, Maintenance Superintendent, or Mill Manager. The Mill or Maintenance Superintendent will report to the Mill Manager. The EH&S Manager and the Quality Assurance Manager will be contacted by the Mill Manager. Name Title Home Phone Mill Personnel: Dan HillstenLoean Shumwav Mill Manager (435) 939459-98783044 David Turk EH&S Manager 3803 Garrin Palmer Mill Environmental Compliance Coordinator Scot ChristensenThayne Holt Production Superintendent -1783 (435) 038459-9786- (435) 459-9463 (435) Wade Hancock Maintenance Superintendent (435) 678-2753 David Lyman---------------Mill Foreman-----------------------------------------(435) 678 3202 Thayne Holt----------------Mill Foreman-----------------------------------------(435) 979 3557 Denver Lakewood Personnel: Stephen P. Antony President and Chief Executive Officer (303) 974-2142 Harold R. Roberts Executive Vice President and Chief Operating OfficerConventional Operations (303) 389-4160 Scott BakkenSr. Director, Regulatory Affairs(303) 389-4132 Kathy Weinel Quality Assurance Manager (303)389-4134 In the event the next person in the chain-of-command cannot be reached, then proceed up the chain-of-command to the next level. Figure 3.0 shows the organizational chart for the mill site. 9.0 RECORDS AND REPORTS 10 The following reports and records are to be maintained in Central File by the Environmental Coordinator-Department for inspection and review for a minimum of thfee-five years: 1. Record of site monitoring inspections a. Daily Tailings Inspection Data b. Weekly Tailings Inspection and Survey c. Monthly Tailings Inspection, Pipeline thickness d. Quarterly Tailings Inspection 2. Tank to soil potential measurements 3. Annual bulk oil and fuel tank visual inspections 4. Tank and pipeline thickness tests 5. Quarterly and annual PCB transformer inspections (if transformer contains PCBs) 6. Tank supports and foundation inspections 7. Spill Incident reports 8. Latest revision of SPCC plan 10.0 SPILL REPORTING REQUIREMENTS 1. Report to applicable government agency as required by laws and regulations 2. Report any recordable injury or illness associated with the release 3. Fulfill any communication requirements for community awareness of spill impacts 4. Report release of 5,000 pounds or more of any process material or waste product 11.0 PERSONNEL TRAINING AND SPILL PREVENTION PROCEDURES All new employees are instructed on spills at the time they are employed and trained. They are briefed on chemical and petroleum spill prevention and control. They are informed that leaks in piping, valves, and sudden discharges from tanks should be reported immediately. Abnormal flows from ditches or impoundments are of immediate concern. In addition, a safety meeting is presented annually by the Environmental Coordinator to review the SPCC plan. 11.1 Training Records Employee training records on chemical and petroleum spill prevention are maintained in the general safety training files. 11.2 Monitoring Reports Shift logs shall provide a checklist for inspection items. 12.0 REVISION This procedure is to be reviewed by the mill staff and a registered professional engineer at least once every three years, and updated when circumstances warrant a revision. 11 13.0 MILL MANAGER APPROVAL I hereby certify that I have reviewed the foregoing chemical and petroleum product SPCC plan, that I am familiar with the Energy Fuels Resources (USA) Inc. White Mesa Mill facilities, and attest that this SPCC plan has been prepared in accordance with the Standard Operating Procedures currently in effect. E)an HillstenLogan Shumway Mill Manager 14.0 CERTIFICATION BY REGISTERED PROFESSIONAL ENGINEER I hereby certify that I have reviewed the foregoing chemical and petroleum product SPCC plan, that I am familiar with the Energy Fuels Resources (USA) Inc. White Mesa Mill facilities, and attest that this SPCC plan has been prepared in accordance with good engineering practices. Harold R. Roberts Registered Professional Engineer State of Utah No. 165838 12 15.0 SUMMARY Chemical and petroleum spills will be reported in accordance with applicable laws and regulations. Spills that leave the property need to be reported immediately. Each spill will be assessed and reported as required by the applicable regulations. Reportable quantities are shown in the attached tables.Below ■-is a table listing the specific reportable quantities associated with the major chemical and petroleum products on site. CHEMICAL REPORTABLE QUANTITY (RQ) AMMONIA AMY SODIUM HYDROXIDE SODA ASH SODIUM CHLORATE SULFURIC AG© VANADIUM PENTOXIDE KEROSENE ©& PROPANE DIE-SEL--& UNLEADED FUEL 100 POUNDS Ne------Reportable Quantity 400 GALLONS 1,000 POUNDS 1000 POUNDS 100 GALLONS Ne------Reportable Quantity Ne------Reportable Quantity 100 GALLONS f Formatted: Body Text Indent, Justified I Formatted: Body Text Indent, Justified ( Formatted: Body Text Indent, Justified ( Formatted: Body Text Indent, Justified f Formatted: Body Text Indent, Justified ( Formatted: Body Text Indent, Justified f Formatted: Body Text Indent, Justified I Formatted: Body Text Indent, Justified [ Formatted: Body Text Indent, Justified (Formatted: Body Text Indent, Justified ^Formatted: Body Text Indent, Justified ( Formatted: Body Text Indent, Justified 13 TABLES FIGURES CLEAN WHITE MESA MILL SPILL PREVENTION, CONTROL, AND COUNTERMEASURES PLAN FOR CHEMICALS AND PETROLEUM PRODUCTS May 2,2016 Energy Fuels Resources (USA) Inc. WHITE MESA MILL 6425 S. HWY 191 BLANDING, UT 84511 ENERGYFUELS Contents 1.0 OBJECTIVE.........................................................................................................................................................................1 2.0 RESPONSIBILITIES......................................................................................................................................................2 3.0 DRAINAGE BASINS, PATHWAYS, AND DIVERSIONS...........................................................................2 4.1 Basin A1....................................................................................................................................................................2 4.2 Basin A2....................................................................................................................................................................2 4.3 Basin B1....................................................................................................................................................................2 4.4 Basin B2....................................................................................................................................................................2 4.5 Basin B3....................................................................................................................................................................3 4.6 Basin C......................................................................................................................................................................3 4.7 Basin D.......................................................................................................................................................................3 4.8 Basin E.......................................................................................................................................................................3 4.9 Basin F.......................................................................................................................................................................3 5.0 POTENTIAL CHEMICAL SPILL SOURCES AND SPILL CONTAINMENT....................................3 5.1 Reagent Tanks (Tank list included in Table 2.0).................................................................................3 5.2 Ammonia...................................................................................................................................................................3 5.3 Ammonia Meta-Vanadate................................................................................................................................4 5.4 Caustic Storage (Sodium Hydroxide)........................................................................................................4 5.5 Sodium Carbonate (Soda Ash).....................................................................................................................4 5.6 Sodium Chlorate...................................................................................................................................................4 5.7 Sulfuric Acid.............................................................................................................................................................4 5.8 Vanadium Pentoxide...........................................................................................................................................5 5.9 Kerosene (Organic)..............................................................................................................................................5 5.10 Used/Waste Oil........................................................................................................................................................5 6.0 POTENTIAL PETROLEUM SOURCES AND CONTAINMENT.............................................................5 6.1 Petroleum Tanks...................................................................................................................................................5 6.1.1 Diesel................................................................................................................................................................5 6.2 Aboveground Fuel Pump Tanks...................................................................................................................5 6.2.1 Diesel................................................................................................................................................................5 6.2.2 Unleaded Gasoline....................................................................................................................................6 6.2.3 Pump Station................................................................................................................................................6 6.2.4 Truck Unloading...........................................................................................................................................6 7.0 SPILL DISCOVERY AND REMEDIAL ACTION.............................................................................................6 8.0 SPILL INCIDENT NOTIFICATION.........................................................................................................................7 8.1 External Notification................................................................................................................................................7 8.2 Internal Notification..................................................................................................................................................7 9.0 RECORDS AND REPORTS.....................................................................................................................................9 10.0 SPILL REPORTING REQUIREMENTS.............................................................................................................9 11.0 PERSONNEL TRAINING AND SPILL PREVENTION PROCEDURES..........................................9 11.1 Training Records..................................................................................................................................................9 11.2 Monitoring Reports...............................................................................................................................................9 12.0 REVISION..........................................................................................................................................................................9 13.0 MILL MANAGER APPROVAL..............................................................................................................................10 14.0 CERTIFICATION BY REGISTERED PROFESSIONAL ENGINEER.............................................10 15.0 SUMMARY......................................................................................................................................................................11 WHITE MESA MILL SPILL PREVENTION, CONTROL, AND COUNTERMEASURES PLAN FOR CHEMICALS AND PETROLEUM PRODUCTS 1.0 OBJECTIVE The objective of the Spill Prevention, Control, and Countermeasures (SPCC) Plan is to serve as a site-specific guideline for the prevention of and response to chemical and petroleum spills. The plan outlines spill potentials, containment areas, and drainage characteristics of the White Mesa Mill site. The plan addresses chemical spill prevention, spill potentials, spill discovery, and spill notification procedures. Spills are reportable if the spill leaves the site. Ammonia is the only chemical (as vapor) that has the potential to leave the site. In addition, chemical and petroleum spills will be reported in accordance with applicable laws and regulations. 1.1 Plan Organization This SPCC is organized as follows: Section 1.0 Objective Section 2 Responsibilities Section 3.0 Drainage Basins, Pathways, and Diversions Section 4 Description of Basins Section 5.0 Potential Chemical Spill Sources and Spill Containment Section 6.0 Potential Petroleum Spill Sources and Containment Section 7.0 Spill Discovery and Remedial Action Section 8.0 Spill Incident Notification Section 9.0 Records and Reports Section 10.0 Spill Reporting Requirements Section 11.0 Personnel Training and Spill Prevention Procedures Section 12.0 Revision Section 13.0 Mill Manager Approval Section 14.0 Certification by Registered Professional Engineer Section 15.0 Summary Tables: Table 1.0 is the Energy Fuels Resources (USA) Inc. (EFRI) personnel responsible for implementing this SPCC. Table 2.0 lists the reagent tanks and their respective capacities. Table 3.0 lists the laboratory chemicals, their amounts, and their reportable quantities. Table 4.0 lists the reagent yard/small quantity chemicals. Table 5.0 lists the chemicals in the reagent yard, their amounts, and their reportable quantities. Table 6.0 lists the petroleum products and solvents on site. 1 Figures: Figure 1 shows the Mill Site Layout, shows the mill site including the locations of the chemical tanks on-site. Figure 2 shows the basins and drainage ditch areas for the Mill Site. Figure 3 shows the organization chart for Mill Operations. 2.0 RESPONSIBILITIES Personnel responsible for spill prevention and follow-up spill reporting are included on Table 1 which is included in the Tables Tab of this SPCC. 3.0 DRAINAGE BASINS, PATHWAYS, AND DIVERSIONS The main drainage pathways are illustrated in Figure 2. The map shows drainage basin boundaries, flow paths, constructed diversion ditches, tailing cells, the spillway between Cell 2 and 3, dikes, berms, and other relevant features. The White Mesa Mill is a “zero” discharge facility for process liquid wastes. The mill area has been designed to ensure that all spills or leaks from tanks will drain toward the lined tailing management system. The management system, in turn, is operated with sufficient freeboard (minimum of three feet) to withstand 100% of the PMP (Probable Maximum Precipitation). This allows for a maximum of 10 inches of rain at any given time. Precipitation and unexpected spills from the mill site are contained within their prospective drainage basins. Overflow ultimately drains into the tailings management system. 4.1 Basin A1 Basin A1 is north of Cell 1 and Diversion Ditch No. 1. The basin contains 23 tributary acres, all of which drain into Westwater Creek. 4.2 Basin A2 Basin A2 contains all of Cell 1 including an area south of the Diversion Ditch No. 1. The basin covers 84 acres. Any overflow from this basin would be contained within Cell 1. 4.3 Basin B1 Basin B1 is north of the mill area. The basin contains 45.4 tributary acres. Overflow from this basin drains into a flood retention area by flowing through Diversion Ditch No. 2. Diversion Ditch No. 2 drains into Westwater Creek. 4.4 Basin B2 Basin B2 is northeast of the mill area and contains only 2.6 tributary acres. Overflow from this basin would drain into Diversion Ditch No. 3. Diversion Ditch No. 3 ultimately drains into Diversion Ditch No. 2. 2 4.5 Basin B3 Basin B3 contains most of the mill area, buildings, ore stockpiles, process storage tanks, retention ponds, spill containment structures, pipelines, and roadways. The normal direction of flow in this basin is from the northwest to the southwest. Any overflow from this basin would drain into Cell 1. The basin contains 64 acres. This basin has sufficient freeboard to withstand 100% of the PMP (Probable Maximum Precipitation). This allows 10 inches of rain for any given storm event. 4.6 Basin C Basin C contains all of Cell 2. The basin consists of 80.7 acres. Areas in this basin include earth stockpiles and the heavy equipment shop. The direction of flow in this basin is to the southwest. All overflows in this basin is channeled along the southern edge of the basin. Overflow then flows into Cell 3 via the spillway from Cell 2 to Cell 3. 4.7 Basin D Basin D contains all of Cell 3. This basin consists of 78.3 acres including a portion of the slopes of the topsoil stockpile and random stockpile. The basin contains all flows, including those caused by the PMP. 4.8 Basin E Basin E contains Cell 4A and consists of 40 acres. All anticipated flows including those caused by the PMP will be contained within the basin and will flow directly into Cell 4A. 4.9 Basin F Basin F contains Cell 4B, and consists of 40 acres. All anticipated flows including those caused by the PMP will be contained within the basin and will flow directly into Cell 4B. 5.0 POTENTIAL CHEMICAL SPILL SOURCES AND SPILL CONTAINMENT 5.1 Reagent Tanks (Tank list included in Table 2.0) 5.2 Ammonia The ammonia storage tanks consist of two tanks with a capacity of 31,409 gallons each. The tanks are located southeast of the Mill building. Daily monitoring of the tanks for leaks and routine integrity inspections will be conducted to minimize the hazard associated with ammonia. The reportable quantity for an ammonia spill is 7 gallons. Ammonia spills should be treated as gaseous. Ammonia vapors will be monitored closely to minimize the hazard associated with inhalation. If vapors are detected, efforts will be made to stop or repair the leak expeditiously. Ammonia is the only chemical (as vapor) that has the potential to leave the site. 3 5.3 Ammonium Meta-Vanadate Ammonium meta-vanadate is present in the vanadium precipitation area of the Mill building as the process solutions move through the circuit to produce the vanadium end product. Spills would be contained in the process sump within the vanadium precipitation area. The reportable spill quantity for ammonium meta-vanadate is 1,000 pounds. 5.4 Caustic Storage (Sodium Hydroxide) The caustic storage tank is located on a splash pad on the northwest comer of the SX building. The tank has a capacity of 19,904 gallons. The tank supports are mounted on a concrete curbed catchment pad which directs spills into the sand filter sump in the northwest comer of the SX building. The reportable spill quantity for sodium hydroxide is 85 gallons. 5.5 Sodium Carbonate (Soda Ash) The soda ash solution tank has a capacity of 16,921 gallons and is located outside the northeast corner of the SX building. Spills from the soda ash solution tank are contained in the North SX impound and ran to Cell 1. The smaller soda ash shift tank has a capacity of 8,530 gallons and is located in the SX building. Spills will be diverted into the boiler area, and would ultimately drain into Cell 1. There is no reportable spill quantity associated with sodium carbonate. 5.6 Sodium Chlorate Sodium chlorate tanks consist of three fiberglass tanks located within a dike east of the SX building. Tank maximum volumes of the three tanks are 16,075, 21,057 and 28,788 gallons. Daily monitoring of the tanks for leaks and integrity inspections will be conducted to minimize the hazard associated with sodium chlorate. Sodium chlorate that has dried and solidified becomes even more of a safety hazard due to its extremely flammable nature. The reportable spill quantity for sodium chlorate is 400 gallons. 5.7 Sulfuric Acid The sulfuric acid storage tanks consist of one large tank with the capacity of 1,600,000 gallons and one smaller tank with a capacity of 11,000 gallons. The large tank is located in the northwest corner of mill area basin B3 and is primarily used for acid storage and unloading. The tank support for the large tank is on a mound above a depression which would contain a significant spill. All flows resulting would be channeled to Cell 1. The tank is equipped with a high level audible alarm which sounds prior to tank overflows. A concrete spill catchment with a sump in the back provides added containment around the base of the tank. However, the catchment basin would not be able to handle a major tank failure such as a tank rupture. The resulting overflow would flow towards Cell 1. The smaller storage tank is located on the north side of the SX building. The tank is equipped with a high level audible alarm. 4 The reportable spill quantity for sulfuric acid is 65 gallons. 5.8 Vanadium Pentoxide Vanadium pentoxide is produced when vanadium is processed through the drying and fusing circuits and is not present in the vanadium circuit until after the deammoniator. Efforts will be made to minimize leaks or line breaks that may occur in processes in the circuit that contain vanadium pentoxide. Special care will be taken in the transportation of this chemical. The reportable spill quantity for vanadium pentoxide is 1000 pounds. 5.9 Kerosene (Organic) The kerosene storage area is located in the central mill yard and has a combined capacity of 10,152 gallons in three tanks. Any overflow from these three tanks would flow around the south side of the SX building and then into Cell 1. These tanks have drain valves which remain locked unless personnel are supervising draining operations. The reportable spill quantity for kerosene is 100 gallons. 5.10 Used/Waste Oil Used/ Waste oil for parts washing is located north of the maintenance shop in a tank and has a capacity of 5,000 gallons. The tank is contained within a concrete containment system. Used oil will be disposed of on site. Any oil escaping the concrete containment system will be cleaned up. Soil contaminated with used oil will be excavated and disposed of in the Cell currently used for the disposal of solid Mill wastes. 6.0 POTENTIAL PETROLEUM SOURCES AND CONTAINMENT 6.1 Petroleum Tanks 6.1.1 Diesel There are two diesel storage tanks located north of the mill building. The tanks have capacities of 250 gallons each. One of the diesel tanks is for the emergency generator. The other tank is located in the pumphouse on an elevated stand. Spillage from either tank would ultimately flow into Cell 1. The reportable spill quantity for diesel is 100 gallons. The spill is also reportable if the spill has the potential for reaching any nearby surface waters or ground waters. 6.2 Aboveground Fuel Pump Tanks 6.2.1 Diesel The diesel tank is located on the east boundary of Basin B3 and has a capacity of 6,000 gallons. The tank is contained within a concrete catchment pad. The reportable spill quantity for diesel is 100 gallons. A diesel spill is also reportable if the spill has the potential for reaching any surface waters or ground waters. 5 6.2.2 Unleaded Gasoline The unleaded gasoline tank is located next to the diesel tank. The unleaded gasoline tank has a capacity of 3,000 gallons and is contained within the same containment system as the diesel tank. Spills having the potential for reaching any surface waters or ground waters will need to be reported. The reportable spill quantity for unleaded gasoline is 100 gallons. 6.2.3 Pump Station Both the diesel and the unleaded gasoline tanks will be used for refueling company vehicles used around the mill site. The pump station is equipped with an emergency shut-off device in case of overflow during fueling. In addition, the station is also equipped with a piston leak detector and emergency vent. Check valves are present along with a tank monitor console with a leak detection system. The catchment is able to handle a complete failure of one tank. However, if both tanks failed the concrete catchment pad would not be able to contain the spill. In this case, a temporary berm would need to be constructed. Absorbent diapers or floor sweep would be used in an effort to limit and contain the spill. The soil would have to be cleaned up and placed in the Cell currently used for the disposal of solid Mill wastes. 6.2.4 Truck Unloading In the event of a truck accident resulting in an overturned vehicle in the mill area, proper reporting and containment procedures will be followed when warranted, such as when oil or diesel fuel is spilled. Proper clean-up procedures will be followed to minimize or limit the spill. The spill may be temporarily bermed or localized with absorbent compounds. Any soils contaminated with diesel fuel or oil will be cleaned up and placed in the Cell currently used for the disposal of solid Mill wastes. 7.0 SPILL DISCOVERY AND REMEDIAL ACTION Once a chemical or petroleum spill has been detected, it is important to take measures to limit additional spillage and contain the spill that has already occurred. Chemical or petroleum spills will be handled as follows: • The Shift Foreman will direct efforts to shut down systems, if possible, to limit further release. • The Shift Foreman will also secure help if operators are requiring additional assistance to contain the spill. • The Shift Foreman is also obligated to initiate reporting procedures. • Once control measures have begun and personal danger is minimized, the Shift Foreman will notify the Production Superintendent, Maintenance Superintendent, or Mill Manager. • The Production or Maintenance Superintendent will notify the Mill Manager, who in turn will notify the EH&S Manager and/or the Environmental Coordinator. • The Mill Manager will assess the spill and related damage and direct remedial actions. The corrective actions may include repairs, clean-up, disposal, and 6 company notifications. Government notifications may be necessary in some cases. If a major spill continues uncontrolled, these alternatives will be considered: 1. Construct soil dikes or a pit using heavy equipment. 2. Construct a diversion channel into an existing pond. 3. Start pumping the spill into an existing tank or pond. 4. Plan further clean-up and decontamination measures. 8.0 SPILL INCIDENT NOTIFICATION 8.1 External Notification For chemical and petroleum spills that leave the site, the following agencies should be notified: 1. EPA National Response Center 1 -800-424-8802 2. US Nuclear Regulatory Commission 301-816-5100 3. State of Utah 801-538-7200 In case of a tailings dam failure, contact the following agencies: 1. US Nuclear Regulatory Commission 301-816-5100 2. State of Utah, Natural Resources 801-538-7200 8.2 Internal Notification Internal reporting requirements for incidents, spills, and significant spills are as follows: Report Immediately Event Criteria: 1. Release of toxic or hazardous substances 2. Fire, explosions, and accidents 3. Government investigations, information requests, or enforcement actions 4. Private actions or claims (corporate or employee) 5. Deviations from corporate policies or government requirements by management Which have or could result in the following: 1. Death, serious injury, or adverse health effects 2. Property damage exceeding $1,000,000 3. Government investigation or enforcement action which limits operations or assesses penalties of $100,000 or more 4. Publicity resulted or anticipated 5. Substantial media coverage 7 Report at the Beginning of the Next Day Event Criteria: 1. Was reported to a government agency as required by law 2. Worker (employee or contractor) recordable injury or illness associated with a release 3. Community impact-reported or awareness 4. Publicity resulted or anticipated 5. Release exceeding 5,000 pounds of process material, waste, or by-product In the event of a spill requiring reporting, the Mill Manager is required to call the Quality Assurance Manager, the Executive Vice President and Chief Operating Officer, or the President and Chief Executive Officer. The spill will first be reported to the Shift Foreman. The Shift Foreman will then report the spill to the Mill Superintendent, Maintenance Superintendent, or Mill Manager. The Mill or Maintenance Superintendent will report to the Mill Manager. The EH&S Manager and the Quality Assurance Manager will be contacted by the Mill Manager. Name Mill Personnel: Logan Shumway David Turk Garrin Palmer Thayne Holt Wade Hancock Lakewood Personnel: Stephen P. Antony Harold R. Roberts Scott Bakken Kathy Weinel Title Mill Manager EH&S Manager Mill Environmental Compliance Coordinator Production Superintendent Maintenance Superintendent President and Chief Executive Officer Executive Vice President Conventional Operations Sr. Director, Regulatory Affairs Quality Assurance Manager Home Phone (435) 459-9878 (435) 459-9786 (435) 459-9463 (435) 459-1783 (435) 678-2753 (303) 974-2142 (303) 389-4160 (303) 389-4132 (303) 389-4134 In the event the next person in the chain-of-command cannot be reached, then proceed up the chain-of-command to the next level. Figure 3.0 shows the organizational chart for the mill site. 8 9.0 RECORDS AND REPORTS The following reports and records are to be maintained in Central File by the Environmental Department for inspection and review for a minimum of five years: 1. Record of site monitoring inspections a. Daily Tailings Inspection Data b. Weekly Tailings Inspection and Survey c. Monthly Tailings Inspection, Pipeline thickness d. Quarterly Tailings Inspection 2. Tank to soil potential measurements 3. Annual bulk oil and fuel tank visual inspections 4. Tank and pipeline thickness tests 5. Quarterly and annual PCB transformer inspections (if transformer contains PCBs) 6. Tank supports and foundation inspections 7. Spill Incident reports 8. Latest revision of SPCC plan 10.0 SPILL REPORTING REQUIREMENTS 1. Report to applicable government agency as required by laws and regulations 2. Report any recordable injury or illness associated with the release 3. Fulfill any communication requirements for community awareness of spill impacts 4. Report release of 5,000 pounds or more of any process material or waste product 11.0 PERSONNEL TRAINING AND SPILL PREVENTION PROCEDURES All new employees are instructed on spills at the time they are employed and trained. They are briefed on chemical and petroleum spill prevention and control. They are informed that leaks in piping, valves, and sudden discharges from tanks should be reported immediately. Abnormal flows from ditches or impoundments are of immediate concern. In addition, a safety meeting is presented annually by the Environmental Coordinator to review the SPCC plan. 11.1 Training Records Employee training records on chemical and petroleum spill prevention are maintained in the general safety training files. 11.2 Monitoring Reports Shift logs shall provide a checklist for inspection items. 12.0 REVISION This procedure is to be reviewed by the mill staff and a registered professional engineer at least once every three years, and updated when circumstances warrant a revision. 9 13.0 MILL MANAGER APPROVAL I hereby certify that I have reviewed the foregoing chemical and petroleum product SPCC plan, that I am familiar with the Energy Fuels Resources (USA) Inc. White Mesa Mill facilities, and attest that this SPCC plan has been prepared in accordance with the Standard Operating Procedures currently in effect. 14.0 CERTIFICATION BY REGISTERED PROFESSIONAL ENGINEER I hereby certify that I have reviewed the foregoing chemical and petroleum product SPCC hite Mesa Mill Logan Shumway Mill Manager :ordance with good 10 15.0 SUMMARY Chemical and petroleum spills will be reported in accordance with applicable laws and regulations. Spills that leave the property need to be reported immediately. Each spill will be assessed and reported as required by the applicable regulations. Reportable quantities are shown in the attached tables. 11 TABLES TABLE 1.0 __________________RESPONSIBILITIES________________ Person in charge of facility responsible for spill prevention: Logan Shumway 6425 South Highway 191 Blanding, UT 84511 (435) 678-4119 (work) (435) 459-9878 (home) Person in charge of follow-up spill reporting: David Turk 6425 South Highway 191 Blanding, UT 84511 (435) 678-4113 (work) (435) 459-9786 (cell)___________________________________ TABLE 2.0 REAGENT TANK LIST QUANTITY REAGENT CAPACITY (GAL) AMMONIUM SULFATE 24,366 DIESEL 250 KEROSENE 10,152 USED/WASTE OIL 5,000 DIESEL 6,000 UNLEADED 3,000 PROPANE 30,000 LNG 30,000 AMMONIA 31,409 SODIUM HYDROXIDE 19,904 SODA ASH SOLUTION 16,921 SODA ASH SHIFT 8,530 SODIUM CHLORATE 16,075 SODIUM CHLORATE 21,057 SODIUM CHLORATE 28,788 SULFURIC ACID 1,600,000 SULFURIC ACID 11,000 TABLE 3.0 LABORATORY CHEMICAL INVENTORY LIST1 Chemical in Lab RQ2 Quantity In Stock Aluminum nitrate 2,270 kg 1.8 kg Ammonium carbonate 2,270 kg 11-3 kg Ammonium bifluoride 45.4 kg 2.27 kg Ammonium chloride 2,270 kg 2,27 kg Ammonium oxalate 2,270 kg 6.8 kg Ammonium thiocyanate 2,270 kg 7.8 kg Antimony potassium tartrate 45.4 kg 0.454 kg n-Butyl acetate 2,270 kg 4 L Calcium acetate 4.54 kg 0.454 kg Cyclohexane 454 kg 24 L Ferric chloride 454 kg 6.810 kg Ferric nitrate 454 kg 0.454 kg Ferrous ammonium sulfate 454 kg 0.57 kg Ferrous sulfate 454 kg 0.454 kg Lead nitrate 4.54 kg 2.7 kg Potassium chromate 4.54 kg 0.114 kg Sodium hydrosulfide 2,270 kg 1.0 kg Sodium nitrite 45.4 kg 2.5 kg Sodium phosphate tribasic 2,270 kg 1.4 kg Zinc acetate 454 kg 0.91 kg Chemical in Volatiles and Flammables Lockers (A,B,C)RQ2 Quantity In Stock Chloroform 4.54 kg 1L Formaldehyde 45.4 kg <1L of 37% solution Nitrobenzene 454 kg 12 L Toluene 454 kg 12 L Chemical in Acid Shed RQ2 Quantity In Stock Hydrochloric acid 2,270 kg 58 gal Nitric acid 454 kg 5 L Phosphoric acid 2,270 kg 10 L Sulfuric acid 454 kg 25 L Hydrofluoric Acid 45.4 kg 1 L Ammonium hydroxide 454 kg 18 L 1. This list identifies chemicals which are regulated as hazardous substances under the Federal Water Pollution Control Act 40 CFR Part 117. The lab also stores small quantities of other materials that are not hazardous substances per the above regulation. 2. Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3: “Reportable Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act.” TABLE 4.0 REAGENT YARD/SMALL QUANTITIY CHEMICALS LIST 1 CHEMICAL RQ2 QUANTITY IN STORAGE COMPOUND Acetic Acid, Glacial 1000 lbs 4 gal Ammonium Hydroxide 1000 lbs 5L Ferrous Sulfate Heptahydrate 1,000 lbs 5 kg (1 libs) Hydrochloric Acid 5,000 lbs 60 gal of 40% solution Nitric Acid 1,000 lbs 10 L Potassium Permanganate 0.1 N 32 gal 5 kg (11 lbs) Silver Nitrate 1 lb 2.6 kg Trichloroethylene 1001b 2 L 1. This list identifies chemicals which are regulated as hazardous substances under the Federal Water Pollution Control Act 40 CFR Part 117. Materials in this list are stored in a locked storage compound near the bulk storage tank area. The Mill also stores small quantities of other materials that are not hazardous substances per the above regulation. 2. Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3: “Reportable Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act.” TABLE 5.0 REAGENT YARD AND BULK CHEMICALS LIST1 REAGENT RQ QUANTITY ON SITE Sulfuric Acid 1,000 lbs 2,719,680 lbs Floe #301 None 0 lbs Hyperfloc 102 None 1,500 lbs Ammonia - East Tank 100 lbs 113,600 lbs Ammonia - West Tank 100 lbs 93,720 lbs Kerosene 100 gal approx. 5,100 gal Salt (Bags)None 19,600 lbs Ammonium Hydrogendifluoride None 20,450 lbs Soda Ash Dense (Bag)None 2,000 lbs Phosphoric Acid 5,000 lbs 6,300 lbs Hydrogen Peroxide None 3,600 gal Polyox None 560 lbs Millsperse None 1,410 lbs Nalco TX760 None 9 barrels Nalco 7200 None 1,590 lbs Tributyl phosphate None 9,450 lbs Distillates None 110 gal Diesel 100 gal approx. 6,000 gal Gasoline 100 gal approx. 3,000 Alamine 336 drums None 0 lbs Floe 109 None 7,750 lbs Floe 208 None 1,500 lbs Floe 904 None 1,500 lbs Hyperfloc 624 None 4,230 lbs Salt (Bulk solids)None Total of 70,000 lbs Salt (Bulk solutions)None on site in all forms Caustic Soda 1,000 lbs 24,000 lbs in 40% solution Ammonium Sulfate None 21,300 lbs Sodium Chlorate None 66,000 gal Alamine 335 Bulk None 310 lbs Alamine 310 Bulk None 0 lbs Isodecanol None 0 lbs Vanadium Pentoxide 1,000 lbs 500,000 lbs Yellowcake None < 10,000 lbs 1. This list identifies the bulk chemicals and the chemicals in the reagent yard whether or not they are regulated as hazardous substances under the Federal Water Pollution Control Act 40 CFR Part 117. 2. Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3: “Reportable Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act.” 3. Vanadium Pentoxide and Yellowcake, the Mill’s products, are not stored in the Reagent Yard itself, but are present in closed containers in the Mill Building and/or Mill Yard. TABLE 6.0 PETROLEUM PRODUCTS AND SOLVENTS LIST1 2 PRODUCT RQ QUANTITY IN WAREHOUSE Lubricating Oils in 55 gallon drums 100 gal 1,540 gallons Transmission Oils 100 gal 0 gallons Dielectric fluids 5 gallons Antifreeze None 55 gallons Greases 1,787 lbs Water Soluble Oils 100 gal 30 gallons Xylene (mixed isomers)100 lbs 0 gallons Lacquer thinner 0 gallons Acetone None 55 gallons Methyl Ethyl Ketone None 55 gallons Toluene 1000 lbs 0 gallons Varsol Solvent (2% trimethyl benzene in petroleum distillates)100 gal 0 gallons Resin None 10 gallons Epoxy Paints None 55 gallons Epoxy Catalyst None 30 gallons Oil Base paints None 15 gallons Paint thinners None 0 gallons Other paints None 20 gallons 1. This list includes all solvents and petroleum-based products in the Mill warehouse 2. Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3: “Reportable Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act.” FIGURES LNG 3C ACID TANK 5 □o WATE w /SUBST, ORE 8 A GRIZZLYol□OLD DECONTAMINATIONo PAD AMMONIUM SULFATE QQQ o\>MILL ATER > BUILDING 5 O 'I A. ypi0 SAMPLE PLANTO □j SODA AMMONIAOOQO AS—r~ "i fo\\ N E c SALT yf~Q ) III; 00 kerosi ... i o e> i □ ENE SHOPSX BUILDING o ooool FUEL ISLAND^ ^ 5646 □ Ot) oo , ° .SODIUM CHLORATE □ooDlIl ALTERNATE - i, FEED / Jj CIRCUIT , „ ■5640 ■CDy o 5 c'tf JcDRYREAGENT Storage <o9^d3 CONTSC TIONPEL *-?E l REAGENT YARD 100 50 0(?)200IOC 2 SCALE IN FEET ^ --y—Ta « .8« Energy Fuels Resources (US/ 225 Union Blvd. Suite 60C Lakewood, CO 80228 i Energy FuelsTRUCK SHOP WHITE MESA MILLREVISIONS County: gan Juan State: UtahDateBy Location\WVA 10-11 GM Figure 1 MILL SITE LAYOUT 5-14 DLS 4-16 RE , 20Q0 | Drafted ByScale: 1 "=200 Date: May 12 Mill Site Layout 4.28.16.dwg Figure 11 n} <? <oI? a S § S'po y iV.a-.-f.l J\mi\COJwAo 5 wCO ^ men a2:^Y,* ® 4 COlU < <M t CO LU CO Qj CC -10 3 d < O 2 2 E a: r- SX - -"■Co .22 •§ £ CD c cb 3 2* U_ <0 xD■r\z A 5 ycmB)CM o1112 Q w0 <<Xs<CO s -YA tro 5s*a CM * **>3*. 000. ner >-—5^ d.0 80 * o ^ J -•■ V..1UJ 1/.< 2 COaCM -7 CNQ<Fl0o\<0 LL W 0<2■MQ CO co CM CD W O K CO ~X UJX ™ CQ Q CD > (D C C<00V O * ■ r LU >■<1 CD C35 O OO CD "c/> ’CO%P <rjr>5 ro cair,i <- CD C13ro > >CM5* d co a a a§aco f-Sd1 f ,7^0.<<0 /a coV"- .. J LU/. ;V? nJ t r *i '.. '/• v\ » M /0. ' i- * %§kte,< o z <Xw *»A * \ *. *—,t-.j S3 * 'f 4>Q K. ■T0 “ fo*•* X /<>f\ *._/ V ■»’.XXm “T\i 0 U ST Y U <p*2r io X ,'r 1r ) -if XU o*A'60-3-r £ sjn^AsC3M0\TSwWlW«n\^>oiwnVft Figure 3 Energy Fuels Resources (USA) Inc. White Mesa Mill Organizational Structure President & CEO Executive VP Conventional Operations Sr. Director Regulatory Affairs Mill Manager Manager, Environmental Health and Safety and RSO Quality Assurance Manager Mill Operations Personnel Radiation Technicians Environmental Technicians Safety Supervisor REDLINE STORMWATER BEST MANAGEMENT PRACTICES PLAN for White Mesa Uranium Mill 6425 South Highway 191 P.0. Box 809 Blanding, Utah May 2, 2016 Prepared by: Energy Fuels Resources (USA) Inc. 105047th Street, Suite 950 Denver. CO 80265225 Union Blvd., Suite 600 Lakewood. CO 80228 Best Management Practices Plan TABLE OF CONTENTS 1.0 INTRODUCTION/PURPOSE...................................................................................................................................2 2.0 SCOPE........................................................................................................................................................................3 3.0 RESPONSIBILITY....................................................................................................................................................4 4.0 BEST MANAGEMENT PRACTICES.....................................................................................................................5 4.1 General Management Practices Applicable to All Areas............................................................................5 4.1.1 Keep Potential Pollutants from Contact with Soil, and Surface Water:.............................................5 4.1.2 Keep Potential Pollutants from Contact with Precipitation.................................................................5 4.1.3 Keep Paved Areas from Becoming Pollutant Sources........................................................................5 4.1.4 Inspection and Maintenance of Diversion Ditches and Drainage Channels within the Process and Reagent Storage Area.....................................................................................................................5 4.1.5 Recycle Fluids Whenever Possible:......................................................................................................5 4.2 Management Practices for Process and Laboratory Areas.........................................................................6 4.2.1 Clean Up Spills Properly.....................................................................................................................6 4.2.2 Protect Materials Stored Outdoors.......................................................................................................6 4.2.3 Management..........................................................................................................................................6 4.2.4 Materials Management.........................................................................................................................6 4.3 Management Practices for Maintenance Activities....................................................................................7 4.3.1 Keep a Clean Dry Shop........................................................................................................................7 4.3.2 Manage Vehicle Fluids........................................................................................................................7 4.3.3 Use Controls During Paint Removal...................................................................................................7 4.3.4 Use Controls During Paint Application and Cleanup..........................................................................7 4.4 Management Practices for Ore Pad, Tailings Area, and Heavy Equipment...............................................8 4.4.1 Wash Down Vehicles and Equipment in Proper Areas.......................................................................8 4.4.2 Manage Stockpiles to Prevent Windbome Contamination.................................................................8 4.4.3 Keep Earthmoving Activities from Becoming Pollutant Sources.......................................................8 Figures Figure 1: White Mesa Mill Site Layout.....................................................................................................................1847 Figure_2: White Mesa Mill Site Drainage Basins.....................................................................................................1948 Figure 3: Energy Fuels Resources (USA) Inc.- White Mesa Mill Management Organization Chart.....................2128 Figure 4: Energy Fuels Resources (USA) Inc.—Corporate Management Organizational-Chart...........................2322 Tables TABLE 1.0: White Mesa Mill Management Personnel Responsible for Implementing This BMPP.....................1148 TABLE 2.0: REAGENT YARD LIST......................................................................................................................1244 TABLE 3.0: LABORATORY CHEMICAL INVENTORY LIST 1.......................................................................13H TABLE 4.0: REAGENT YARD/SMALL QUANTITY CHEMICALS LIST 1.....................................................1448 TABLE 5.0: REAGENT YARD/BULK CHEMICALS LIST 1.............................................................................1544 TABLE 6.0: PETROLEUM PRODUCTS AND SOLVENTS LIST 1...................................................................1648 Page 1 Best Management Practices Plan Revision 1.5: September 2Q120ctober 2()15Mav 2016 1.0 INTRODUCTION/PURPOSE Energy Fuels Resources (USA) Inc. ("EFRI") operates the White Mesa Uranium Mill ("the “Mill”) in Blanding, Utah. The Mill is a net water consumer, and is a zero-discharge facility with respect to water effluents. That is, no water leaves the Mill site because the Mill has: • no outfalls to public stormwater systems, • no surface runoff to public stormwater systems, • no discharges to publicly owned treatment works ("POTWs"), and • no discharges to surface water bodies. The State of Utah issued Groundwater Discharge Permit No. UGW370004 to EFRI on March 8, 2005. As a part of compliance with the Permit, EFRI is required to submit a Stormwater Best Management Practices Plan ("BMPP") to the Executive- Seeretar-vDirector of the Division of Waste Management and Radiation Control (“DWMRC”). Utah Department of Environmental Quality. This BMPP presents operational and management practices to minimize or prevent spills of chemicals or hazardous materials, which could result in contaminated surface water effluents potentially impacting surface waters or ground waters through runoff or discharge connections to stormwater or surface water drainage routes. Although the Mill, by design, cannot directly impact stormwater, surface water, or groundwater, the Mill implements these practices in a good faith effort to minimize all sources of pollution at the site. Page 2 Best Management Practices Plan Revision 1.5: September 2012Oetober 2015Mav 2016 2.0 SCOPE This BMPP identifies practices to prevent spills of chemicals and hazardous materials used in process operations, laboratory operations, and maintenance activities, and minimize spread of particulates from stockpiles and tailings management areas at the Mill. Storage of ores and alternate feeds on the ore pad, and containment of tailings in the Mill tailings impoundment system are not considered "spills" for the purposes of this BMPP. The Mill site was constructed with an overall grade and diversion ditch system designed to channel all surface mnoff, including precipitation equivalent to a Probable Maximum Precipitation/Probable Maximum Flood ("PMP/PMF") storm event, to the tailings management system. In addition, Mill tailings, all other process effluents, all solid waste and debris (except used oil and recyclable materials), and spilled materials that cannot be recovered for reuse are transferred to one or more of the tailings cellstailings management impoundments in accordance with the Mill's NRC licenseRadioactive Materials License (“RML”) #UT1900479 conditions. All of the process and laboratory building sinks, sumps, and floor drains are tied to the transfer lines to the tailings impoundments. A site map of the Mill is provided in Figure 1. A sketch of the site drainage basins is provided in Figure 2. As a result, unlike other industrial facilities, whose spill management programs focus on minimizing the introduction of chemical and solid waste and wastewater into the process sewers and storm drains, the Mill is permitted by RML NRG-lieense-to manage some spills via draining or wash down to the process sewers, and ultimately the tailings management system. However, as good environmental management practice, the Mill attempts to minimize: 1. the number and size of material spills, and 2. the amount of unrecovered spilled material and wash water that enters the process sewers after a spill cleanup. Section 4.0 itemizes the practices in place at the Mill to meet these objectives. This BMPP addresses the management of stormwater, and the prevention of spills of chemicals and hazardous materials, at the Mill site. Detailed requirements and methods for management, recordkeeping, and documentation of hazardous material spills are addressed separately in the EFRI White Mesa Mill Spill Prevention, Control and Countermeasures ("SPCC") Plan, the Emergency Response Plan ("ERP")-, and the housekeeping procedures incorporated in the White Mesa Mill Standard Operating Procedures ("SOPs"). Page 3 Best Management Practices Plan Revision 1.5: September2Q ISOctoher 2015Mav 2016 3.0 RESPONSIBILITY All Mill personnel are responsible for implementation of the practices in this BMPP. EFRI White Mesa Mill management is responsible for providing the facilities or equipment necessary to implement the practices in this BMPP. The EFRI Corporate Management and Mill Management Organization is presented in Figure 3. The EFR Corporate Management Organization is presented-in Figure A. An updated spill prevention and control notification list is provided in Table 1. Page 4 Best Management Practices Plan Revision 1.5: September 2012Qctober 2015Mav 2016 4.0 BEST MANAGEMENT PRACTICES A summary list and inventory of all liquid and solid materials managed at the Mill is provided in Tables 2 through 5. 4.1 General Management Practices Applicable to All Areas 4.1.1 Keep Potential Pollutants from Contact with Soil, and Surface Water: • Store hazardous materials and other potential pollutants in appropriate containers. • Label the containers. • Keep the containers covered when not in use. 4.1.2 Keep Potential Pollutants from Contact with Precipitation • Store bulk materials in covered tanks or drums. • Store jars, bottle, or similar small containers in buildings or under covered areas. • Replace or repair broken dumpsters and bins. • Keep dumpster lids and large container covers closed when not in use (to keep precipitation out). 4.1.3 Keep Paved Areas from Becoming Pollutant Sources • Sweep paved areas regularly, and dispose of debris in the solid waste dumpsters or tailings area as appropriate. 4.1.4 Inspection and Maintenance of Diversion Ditches and Drainage Channels within the Process and Reagent Storage Area • • Diversion ditches, drainage channels and surface water control structures in and around the Mill area will be inspected at least monthly in accordance with the regularly scheduled inspections required by Groundwater Discharge Permit No. UGW370004, and by product Materials License #UT1900479the RML. Areas requiring maintenance or repair, such as excessive vegetative growth, channel erosion or pooling of surface water runoff, will be reported to site management and maintenance departments for necessary action to repair damage or perform reconstruction in order for the control feature to perform as intended. Status of maintenance or repairs will be documented during follow up inspections and additional action taken if necessary. 4.1.5 Recycle Fluids Whenever Possible: • When possible, select automotive fluids, solvents, and cleaners that can be recycled or reclaimed • When possible, select consumable materials from suppliers who will reclaim empty containers. • Keep spent fluids in properly labeled, covered containers until they are picked up for recycle or transferred to the tailings areamanagement system for disposal. Page 5 Best Management Practices Plan Revision 1.5: September 2012Qctober 2015Mav 2016 4.2.1 Clean Up Spills Properly • Clean up spills with dry cleanup methods (absorbents, sweeping, collection drums) instead of water whenever possible. ___________________ • Clean spills of stored reagents or other chemicals immediately after discovery. •* ( Formatted: Indent: Left: 0" • (Groundwater Discharge Permit No. UGW370004, Section I.D.lO.c.) • Recover and re-use spilled material whenever possible. • Keep supplies of rags, sorbent materials (such as cat litter), spill collection drums, and personnel protective equipment ("PPE") near the areas where they may be needed for spill response. • If spills must be washed down, use the minimum amount of water needed for effective cleanup. 4.2.2 Protect Materials Stored Outdoors • If drummed feeds or products must be stored outdoors, store them in covered or diked areas when possible. • If drummed chemicals must be stored outdoors, store them in covered or diked areas when possible. • Make sure drums and containers stored outdoors are in good condition and secured against wind or leakage. Place any damaged containers into an overpack drum or second container. 4.2.3 Management • When possible, recycle and reuse water from flushing and pressure testing equipment. When possible, wipe down the outsides of containers instead of rinsing them off in the sink. • When possible, wipe down counters and work surfaces instead of hosing or rinsing them off to sinks and drain 4.2.4 Materials Management • Purchase and inventory the smallest amount of laboratory reagent necessary. • -Do not stock more of a reagent than will be used up before its expiration date. • All new construction of reagent storage facilities will include secondary containment which shall control and prevent any contact of spilled reagents, or otherwise released • reagent or product, with the ground surface. (Groundwater Discharge Permit No. • UGW370004, Section I.D.3.g.) 4.2 Management Practices for Process and Laboratory Areas Page 6 Best Management Practices Plan Revision 1.5: September-2&l-3Qetober SOl-SMav 2016 4.3.1 Keep a Clean Dry Shop • Sweep or vacuum shop floors regularly. • Designate specific areas indoors for parts cleaning, and use cleaners and solvents only in those areas. • Clean up spills promptly. Don't let minor spills spread. • Keep supplies of rags, collection containers, and sorbent material near each work area where they are needed. • Store bulk fluids, waste fluids, and batteries in an area with secondary containment (double drum, drip pan) to capture leakage and contain spills. 4.3.2 Manage Vehicle Fluids • Drain fluids from leaking or wrecked/damaged vehicles and equipment as soon as possible. Use drip pans or plastic tarps to prevent spillage and spread of fluids. • Promptly contain and transfer drained fluids to appropriate storage area for reuse, recycle, -or disposal. • Recycle automotive fluids, if possible, when their useful life is finished. 4.3.3 Use Controls During Paint Removal • Use drop cloths and sheeting to prevent windbome contamination from paint chips and sandblasting dust. • Collect, contain, and transfer, as soon as possible, accumulated dusts and paint chips to a disposal location in the tailings area authorized to accept waste materials from maintenance or construction activities. 4.3.4 Use Controls During Paint Application and Cleanup • Mix and use the right amount of paint for the job. Use up one container before opening a second one. • Recycle or reuse leftover paint whenever possible. • Never clean brushes or rinse or drain paint containers on the ground (paved or unpaved). • Clean brushes and containers only at sinks and stations that drain to the process sewer to the tailings management system. • Paint out bmshes to the extent possible before water washing (water-based paint) or solvent rinsing (oil-based paint). • Filter and reuse thinners and solvent whenever possible). Contain solids and unusable excess liquids for transfer to the tailings areamanagement system. 4.3 Management Practices for Maintenance Activities Page 7 Best Management Practices Plan Revision 1.5: September 20120ctober 20 PS-Mav 2016 Detailed instructions for ore unloading, dust suppression, and tailings management are provided in the Mill SOPs. 4.4.1 Wash Down Vehicles and Equipment in Proper Areas • Wash down trucks, trailers, and other heavy equipment only in areas designated for this purpose (such as wash down pad areas and tile-truck'wash stationdecontamination pads). • At the truck wash-station decontamination pads, make sure the water collection and recycling system is working before turning on water sprays. 4.4.2 Manage Stockpiles to Prevent Windborne Contamination • Water spray the ore pad and unpaved areas at appropriate frequency in accordance with Mill SOPs. • Water spray stockpiles as required by opacity standards or weather conditions. • Don't over-water. Keep surfaces moist but minimize runoff water. 4.4.3 Keep Earthmoving Activities from Becoming -Pollutant Sources • Schedule excavation, grading, and other earthmoving activities when extreme dryness and high winds will not be a factor (to prevent the need for excessive dust suppression). • Remove existing vegetation only when absolutely necessary. •Seed or plant temporary vegetation for erosion control on slopes. 4.4 Management Practices for Ore Pad, Tailings Area, and Heavy Equipment Page 8 Best-Management Practices Plan Revision 1 .^-September 2012Qctober 2944 Page 9 TABLES Page 10 TABDRl White- Mesa Mill Management Personnel Responsible for Implementing This BMPP Mill-Staff Personnel ¥itle Work Phene Home Phene/ Other Contact Number Dan HillstenLogan V nn mil m\ i jJlTUTliW uy Thayne Holt Mill Manager Maintenance Superintendent Mi-H-Superintendent 135 678 11051119 135 678 1166 435-678 4130 Cell:-135 97459 30119878 43-5-678-2753 Gellr-4-35 -979 04-10 435 459 1783 David E. Turk Manager, Environment, 435-6-78-41-13 Health and Safety Garrin-Palmer Mill Environmental 135 678 1115 Compliance Coordinator 435 678 7802 Gell:-435 459-9786 Cell:-435 459 9463 Personnel Corporate-Management Staff Title Work Phene Harold R. Roberts David C. Frydenlund President and Chief 30-3 974- 2142 Operating Officer Executive Vice 303 389 1160 President Conventional Operations Sr. Vice President 303 389 1130 Regulatory-Affairs-and General Counsel Home Phone / Other Contact 1\IiiiviKn»«nuinucr Cell: 303 378 8254 Cell: 303 902 2870 303 221 0098 Cell: 303 808 6648 Jo Ann TischlerKathv Weinel-----------------Director. ComplianceOualitv Assurane-e-Manager--------303 389 11321134------------Cell: 303 501489 92269182 Page 11 TABLE 2 REAGENT YARD LIST QUANTITY (LBS) STORAGE TANKS (GALLONS) AMMONIUM SULFATE(BUL-K) SULFATE(BAGS) ANHYDROUS AMMONIA TRIDEOYLALGOHQL DIESEL FUEL GRINDING BALLS KEROSENE POLOX PROPANE SALT (BAGS) SALT (BULK) SODA ASH (BAGS) SODA ASH (BULK) SODIUM CHLORATE SODIUM HYDROXIDE SULFURIC ACID 5-1,000 26,000 107,920 4E430 72,000 ■\ 3/|/] 1 n 9KfiIVjUUv/ 09.280 0 39.280 84,100 101,128 0 4.801838.440840 2 4 + 2 UNLEADED GASOUNE USED OIL 4 4 4 4 4 4 4 4 42 4 4 24,366 31,409 25Q 64)0© 10,315 10,095 25,589 13,763 18,864 16,921 8^30 46,-924 22,561 29,940 19,905 1.394405.439 3.000 5.000 Page 12 TABLE 3.0 LABORATORY CHEMICAL INVENTORY LIST4 Chemical In Lab RQ Quantity in Stock Aluminum-nitrate Ammonium bifluoride Ammonium chloride Ammonium oxalate Ammonium thiocyanate Antimony potassiumdatrate n-8utyl acetate Cyclohexane 454 Ferrous ammonium suifate Potassium chromate Sodium nitrite Sodium phosphate tribasic Zinc acetate 2270 kg 45.4 kg 2270 kg 227-Q-kg 2270 kg 45.4 kg 2270 kg kg 24 454 kg 454-k§ 4.54 kg 45.4 kg 2270kg /| j^g 4=8-kg 2.27 kg 2.27 kg 6=8-kg 7r8-k§ 0=454 44= L 6.81 kg 0 57 Q. ~] 1 /| fcg 2=54<g 4=4 Q=94-kg Chemical, in Volatiles and Flammables Lockers 4A.B.C) RQ Quantity in Stock Chloroform 4-54-kg 8-4= Formaldehyde 45.4 kg <1L of 37% solution Nitrobenzene 454 kg 42-4= Toluene 454 kg 424= Chemical in Acid Shed RQ Quantity in-Stock Chloroform 4.54 kg 55 gal Flydrochloric acid 2,270 kg 58 gal Nitrate acid 454 kg 54= Phosphoric Acid 2,270 kg 404= Sulfuric acid 454 kg 254= Hydrofluoric-acid 45:4 kg 4-4= Ammonium hydroxide 454 kg 484= 1. This list identifies chemicals which are regulated as hazardous-substances under the Federal Water Pollution Control Act 40 CFR Part 117. The lab also stores small quantities of other materials that-are not hazardous substances per the above regulation. 2r.—Reportable Quantities are those identified in 40 CFR Part t17-Table~417:3f ''Reportable Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act." Page 13 TABLE 4.0 REAGENT YARD/SMALL QUANTITY CHEMICALS LIST 4 CHEMICAL« lunimnc-----------------------------------------RQ' STORAGE Acetic Acid, Glacial 4,000 lbs A1 HaiAmmonium Hydroxide 1,000 lbs Calcium Hypochlorite 404bs kg (4.4 lbs) Chlorine 464bs 0 |[-)g Ferrous Sulfate Heptahydrate 1,000 lbs 5 kg (11 lbs) Hydrochloric 5=000 lbs 60 gal oMO%-solutioft Nitric Acid 1 non ihrt jWUU I uo 404= Potassium Permanganate 0.1 -N 32-dal 5 kg (11 lbs) Sodium-Hypoohlerite-5.5%1 on lh^2 kg (11 lbs) of 6.5% solution Silver Nitrato 44b Q | fog Trichloroethylene 4004b 24= 1. This list identifies chemicals whicb are regulated as hazardous substances under the-Federal Water Pollution Control Act 40 CFR Part 117, Materials in this list are stored in a locked storage compound near the bulk storage tank area. The Mill also stores small quantities of other materials that are not hazardous substances per the above regulation^ 2. Reportable Quantities-are those identified in40-GFR Part 147-Table 117.3: "Reportable Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act:" Page 14 TABLE 5.0 REAGENT YARD/BULK CHEMICALS LIST* REAGENT Sulfuric Acid RQi 1,000 lbs QUANTITY IN REAGENT YARD IMDOQ.OOO-tbs Hyperfloe 102 Ammonia - East Tank Ammonia—Westfank Kerosene Salt (Bags) None 400-lbs 100 lbs mo mli uu uaiNone 1,500 lbs Q [fog 105,000 lbs 500 n.nl Soda Ash Dense (Bag)None 50,000 lbs Polyox None 490 lbs Tributyl phosphate MnnpI 1WI I w Diesel Gasoline Alamine 336 drums 100 gal 100 gal MonorwTTv7 Approx. 3300 gal Approx. 6000 gal 8,250 gal Salt(Bulk Solids) Saft(Bulk Solutions) Caustic Soda Ammonium Sulfate Sodium Chlorate MnnpI IWI I Ks MnnprtunU 1,000 lbs Mnnp None 9-QOQ-gal 16.000 lbs 460r000lbs 350.000 lbs Isodecanol Vanadium-Pentoxide3 Yellowcake3 Ammonia Meta Vanadate Boo-655 Floe 712 MnnpFrUTTUNone 1000 lbs MnnprtxTnu-1000 lbs Q Hjg 30.000 lbs <-100,000 lbs 0 ||jo 21.000 lbs 1,250 lbs -T—This list identifies all chemicals in the reagent yard-whether-or-not-they are -regulated as hazardous substances under the Federal Water Pollution Control Act 40 CFR Part 117. 2-.—Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3: "Reportable Quantities of Hazardous Substances Designated-Porsuant to-Section 311 of the Clean Water Act." &—Vanadium Pentoxide and Yellowcake, the Mill's products, are not stored in the Reagent Yard-itself; but-are present in-otosed-containers in the Mill Building and/or Mill Yard Page 15 TABLE 6.0 PETROLEUM PRODUCTS AND SOLVENTS LIST4 PRODUCT RQ QUANTITY IN WAREHOUSE Lubricating Oils in 55 gallon drums Transmission Oils Water-Soluble-Oils Xylene (mixed isomers) Tnil ipnp Varsol Solvent (3%—trimethyl—benzene—in—petroleum distillates) 100 gal 100 gal 100-gal 100 gal 1000-gal 100 gal 1,510 gallons 110 gallons 110 gallons 0 gallons 0 gallons 0 gallons T—This list includes all solvents-and petroleum-based products in the Mill warehouse petroleum and chemical storage aisles. S-.—Reportable Quantities are those identified in 10 CFR Part 4-4-7 Table 117.3: "Reportable Quantities of-Hazardous Substances Designated Pursuant-to-Seetion 311 of the Clean Water-Act." Page 16 FIGURES Page 17 Figure 1 White Mesa Mill Mill Site Layout Figure 2 Mill Site Drainage Basins Page-17 Figure 3 White Mesa Mill Mill-Management Organization Chart Figuf-e-3 Energy Fuels -Resoarees (USA) Inc. White Mesn Mill Management Organizational Structure President & CEO Executive VP and Chief Operating Officer Sr. VP Regulatory Affairs & General Counsel Director, Compliance Mill Manager Manager, Environment, Health, and Safety Mill Safety Mill Environmental Compliance Coordinator Mill Environmental Monitoring Coordinator Mi Radiation Safety Officer Safety TechnicianRadiation Technician Mill Operations Personnel Page 17 Pa g e 17 Figure 4 White Mesa Mill Energy Fuels Resources (USA) Inc- Organizational Structure Figure 4 Energy Fuels Resources (USA) Inc. Organizational Structure President & CEO Executive VP and Chief Operating Officer Sr. VP Regulatory Affairs & General Counsel Mill Manager Manager, Environment, Health, and Safety Director, Compliance Page 17 Page 17 Page 17 Page 17 — CLEAN STORMWATER BEST MANAGEMENT PRACTICES PLAN for White Mesa Uranium Mill 6425 South Highway 191 P.0. Box 809 Blanding, Utah May 2, 2016 Prepared by: Energy Fuels Resources (USA) Inc. 225 Union Blvd., Suite 600 Lakewood, CO 80228 Best Management Practices Plan Revision 1.5: May 2016 TABLE OF CONTENTS 1.0 INTRODUCTION/PURPOSE.............................................................................................2 2.0 SCOPE................................................................................................................................3 3.0 RESPONSIBILITY.............................................................................................................4 4.0 BEST MANAGEMENT PRACTICES...............................................................................5 4.1 General Management Practices Applicable to All Areas......................................5 4.1.1 Keep Potential Pollutants from Contact with Soil, and Surface Water:........5 4.1.2 Keep Potential Pollutants from Contact with Precipitation............................5 4.1.3 Keep Paved Areas from Becoming Pollutant Sources.....................................5 4.1.4 Inspection and Maintenance of Diversion Ditches and Drainage Channels within the Process and Reagent Storage Area..............................................................5 4.1.5 Recycle Fluids Whenever Possible:.....................................................................5 4.2 Management Practices for Process and Laboratory Areas..................................6 4.2.1 Clean Up Spills Properly.....................................................................................6 4.2.2 Protect Materials Stored Outdoors.....................................................................6 4.2.3 Management.........................................................................................................6 4.2.4 Materials Management......................................................................................6 4.3 Management Practices for Maintenance Activities...............................................7 4.3.1 Keep a Clean Dry Shop........................................................................................7 4.3.2 Manage Vehicle Fluids.........................................................................................7 4.3.3 Use Controls During Paint Removal.................................................................7 4.3.4 Use Controls During Paint Application and Cleanup.......................................7 4.4 Management Practices for Ore Pad, Tailings Area, and Heavy Equipment.......8 4.4.1 Wash Down Vehicles and Equipment in Proper Areas...................................8 4.4.2 Manage Stockpiles to Prevent Windborne Contamination.............................8 4.4.3 Keep Earthmoving Activities from Becoming Pollutant Sources...................8 Figures Figure 1: White Mesa Mill Site Layout Figure 2: White Mesa Mill Site Drainage Basins Figure 3: Energy Fuels Resources (USA) Inc.- White Mesa Mill Management Organization Chart Tables TABLE 1.0: White Mesa Mill Management Personnel Responsible for Implementing This BMPP TABLE 2.0: REAGENT YARD LIST TABLE 3.0: LABORATORY CHEMICAL INVENTORY LIST TABLE 4.0: REAGENT YARD/SMALL QUANTITY CHEMICALS LIST TABLE 5.0: REAGENT YARD/BULK CHEMICALS LIST TABLE 6.0: PETROLEUM PRODUCTS AND SOLVENTS LIST Page 1 Best Management Practices Plan Revision 1.5: May 2016 1.0 INTRODUCTION/PURPOSE Energy Fuels Resources (USA) Inc. ("EFRI") operates the White Mesa Uranium Mill (the “Mill”) in Blanding, Utah. The Mill is a net water consumer, and is a zero-discharge facility with respect to water effluents. That is, no water leaves the Mill site because the Mill has: • no outfalls to public stormwater systems, • no surface runoff to public stormwater systems, • no discharges to publicly owned treatment works ("POTWs"), and • no discharges to surface water bodies. The State of Utah issued Groundwater Discharge Permit No. UGW370004 to EFRI on March 8, 2005. As a part of compliance with the Permit, EFRI is required to submit a Stormwater Best Management Practices Plan ("BMPP") to the Director of the Division of Waste Management and Radiation Control (“DWMRC”), Utah Department of Environmental Quality. This BMPP presents operational and management practices to minimize or prevent spills of chemicals or hazardous materials, which could result in contaminated surface water effluents potentially impacting surface waters or ground waters through runoff or discharge connections to stormwater or surface water drainage routes. Although the Mill, by design, cannot directly impact stormwater, surface water, or groundwater, the Mill implements these practices in a good faith effort to minimize all sources of pollution at the site. Page 2 Best Management Practices Plan Revision 1.5: May 2016 2.0 SCOPE This BMPP identifies practices to prevent spills of chemicals and hazardous materials used in process operations, laboratory operations, and maintenance activities, and minimize spread of particulates from stockpiles and tailings management areas at the Mill. Storage of ores and alternate feeds on the ore pad, and containment of tailings in the Mill tailings impoundment system are not considered "spills" for the purposes of this BMPP. The Mill site was constructed with an overall grade and diversion ditch system designed to channel all surface runoff, including precipitation equivalent to a Probable Maximum Precipitation/Probable Maximum Flood ("PMP/PMF") storm event, to the tailings management system. In addition, Mill tailings, all other process effluents, all solid waste and debris (except used oil and recyclable materials), and spilled materials that cannot be recovered for reuse are transferred to one or more of the tailings management impoundments in accordance with the Mill's Radioactive Materials License (“RML”) #UT1900479 conditions. All of the process and laboratory building sinks, sumps, and floor drains are tied to the transfer lines to the tailings impoundments. A site map of the Mill is provided in Figure 1. A sketch of the site drainage basins is provided in Figure 2. As a result, unlike other industrial facilities, whose spill management programs focus on minimizing the introduction of chemical and solid waste and wastewater into the process sewers and storm drains, the Mill is permitted by RML to manage some spills via draining or wash down to the process sewers, and ultimately the tailings management system. However, as good environmental management practice, the Mill attempts to minimize: 1. the number and size of material spills, and 2. the amount of unrecovered spilled material and wash water that enters the process sewers after a spill cleanup. Section 4.0 itemizes the practices in place at the Mill to meet these objectives. This BMPP addresses the management of stormwater, and the prevention of spills of chemicals and hazardous materials, at the Mill site. Detailed requirements and methods for management, recordkeeping, and documentation of hazardous material spills are addressed separately in the EFRI White Mesa Mill Spill Prevention, Control and Countermeasures ("SPCC") Plan, the Emergency Response Plan ("ERP"), and the housekeeping procedures incorporated in the White Mesa Mill Standard Operating Procedures ("SOPs"). Page 3 Best Management Practices Plan Revision 1.5: May 2016 3.0 RESPONSIBILITY All Mill personnel are responsible for implementation of the practices in this BMPP. EFRI White Mesa Mill management is responsible for providing the facilities or equipment necessary to implement the practices in this BMPP. The EFRI Corporate Management and Mill Management Organization is presented in Figure 3. An updated spill prevention and control notification list is provided in Table 1. Page 4 Best Management Practices Plan Revision 1.5: May 2016 4.0 BEST MANAGEMENT PRACTICES A summary list and inventory of all liquid and solid materials managed at the Mill is provided in Tables 2 through 5. 4.1 General Management Practices Applicable to All Areas 4.1.1 Keep Potential Pollutants from Contact with Soil, and Surface Water: • Store hazardous materials and other potential pollutants in appropriate containers. • Label the containers. • Keep the containers covered when not in use. 4.1.2 Keep Potential Pollutants from Contact with Precipitation • Store bulk materials in covered tanks or drums. • Store jars, bottle, or similar small containers in buildings or under covered areas. • Replace or repair broken dumpsters and bins. • Keep dumpster lids and large container covers closed when not in use (to keep precipitation out). 4.1.3 Keep Paved Areas from Becoming Pollutant Sources • Sweep paved areas regularly, and dispose of debris in the solid waste dumpsters or tailings area as appropriate. 4.1.4 Inspection and Maintenance of Diversion Ditches and Drainage Channels within the Process and Reagent Storage Area • • Diversion ditches, drainage channels and surface water control structures in and around the Mill area will be inspected at least monthly in accordance with the regularly scheduled inspections required by Groundwater Discharge Permit No. UGW370004, and the RML. Areas requiring maintenance or repair, such as excessive vegetative growth, channel erosion or pooling of surface water runoff, will be reported to site management and maintenance departments for necessary action to repair damage or perform reconstruction in order for the control feature to perform as intended. Status of maintenance or repairs will be documented during follow up inspections and additional action taken if necessary. 4.1.5 Recycle Fluids Whenever Possible: • When possible, select automotive fluids, solvents, and cleaners that can be recycled or reclaimed • When possible, select consumable materials from suppliers who will reclaim empty containers. • Keep spent fluids in properly labeled, covered containers until they are picked up for recycle or transferred to the tailings management system for disposal. Page 5 Best Management Practices Plan Revision 1.5: May 2016 4.2.1 Clean Up Spills Properly • Clean up spills with dry cleanup methods (absorbents, sweeping, collection drums) instead of water whenever possible. • Clean spills of stored reagents or other chemicals immediately after discovery. • (Groundwater Discharge Permit No. UGW370004, Section I.D.10.C.) • Recover and re-use spilled material whenever possible. • Keep supplies of rags, sorbent materials (such as cat litter), spill collection drums, and personnel protective equipment ("PPE") near the areas where they may be needed for spill response. • If spills must be washed down, use the minimum amount of water needed for effective cleanup. 4.2.2 Protect Materials Stored Outdoors • If drummed feeds or products must be stored outdoors, store them in covered or diked areas when possible. • If drummed chemicals must be stored outdoors, store them in covered or diked areas when possible. • Make sure drums and containers stored outdoors are in good condition and secured against wind or leakage. Place any damaged containers into an overpack drum or second container. 4.2.3 Management • When possible, recycle and reuse water from flushing and pressure testing equipment. When possible, wipe down the outsides of containers instead of rinsing them off in the sink. • When possible, wipe down counters and work surfaces instead of hosing or rinsing them off to sinks and drain 4.2.4 Materials Management • Purchase and inventory the smallest amount of laboratory reagent necessary. • Do not stock more of a reagent than will be used up before its expiration date. • All new construction of reagent storage facilities will include secondary containment which shall control and prevent any contact of spilled reagents, or otherwise released • reagent or product, with the ground surface. (Groundwater Discharge Permit No. • UGW370004, Section I.D.3.g.) 4.2 Management Practices for Process and Laboratory Areas Page 6 Best Management Practices Plan Revision 1.5: May 2016 4.3.1 Keep a Clean Dry Shop • Sweep or vacuum shop floors regularly. • Designate specific areas indoors for parts cleaning, and use cleaners and solvents only in those areas. • Clean up spills promptly. Don't let minor spills spread. • Keep supplies of rags, collection containers, and sorbent material near each work area where they are needed. • Store bulk fluids, waste fluids, and batteries in an area with secondary containment (double drum, drip pan) to capture leakage and contain spills. 4.3.2 Manage Vehicle Fluids • Drain fluids from leaking or wrecked/damaged vehicles and equipment as soon as possible. Use drip pans or plastic tarps to prevent spillage and spread of fluids. • Promptly contain and transfer drained fluids to appropriate storage area for reuse, recycle, or disposal. • Recycle automotive fluids, if possible, when their useful life is finished. 4.3.3 Use Controls During Paint Removal • Use drop cloths and sheeting to prevent windbome contamination from paint chips and sandblasting dust. • Collect, contain, and transfer, as soon as possible, accumulated dusts and paint chips to a disposal location in the tailings area authorized to accept waste materials from maintenance or construction activities. 4.3.4 Use Controls During Paint Application and Cleanup • Mix and use the right amount of paint for the job. Use up one container before opening a second one. • Recycle or reuse leftover paint whenever possible. • Never clean brushes or rinse or drain paint containers on the ground (paved or unpaved). • Clean bmshes and containers only at sinks and stations that drain to the process sewer to the tailings management system. • Paint out brushes to the extent possible before water washing (water-based paint) or solvent rinsing (oil-based paint). • Filter and reuse thinners and solvent whenever possible). Contain solids and unusable excess liquids for transfer to the tailings management system. 4.3 Management Practices for Maintenance Activities Page 7 Detailed instructions for ore unloading, dust suppression, and tailings management are provided in the Mill SOPs. 4.4.1 Wash Down Vehicles and Equipment in Proper Areas • Wash down trucks, trailers, and other heavy equipment only in areas designated for this purpose (such as wash down pad areas and decontamination pads). • At the decontamination pads, make sure the water collection and recycling system is working before turning on water sprays. 4.4.2 Manage Stockpiles to Prevent Windborne Contamination • Water spray the ore pad and unpaved areas at appropriate frequency in accordance with Mill SOPs. • Water spray stockpiles as required by opacity standards or weather conditions. • Don't over-water. Keep surfaces moist but minimize runoff water. 4.4.3 Keep Earthmoving Activities from Becoming Pollutant Sources • Schedule excavation, grading, and other earthmoving activities when extreme dryness and high winds will not be a factor (to prevent the need for excessive dust suppression). • Remove existing vegetation only when absolutely necessary. • Seed or plant temporary vegetation for erosion control on slopes. 4.4 Management Practices for Ore Pad, Tailings Area, and Heavy Equipment Page 8 TABLES TABLE 1.0 RESPONSIBILITIES Person in charge of facility responsible for spill prevention: Logan Shumway _______________ 6425 South Highway 191 B landing, UT 84511 (435) 678-4119 (work) (435) 459-9878 (home) Person in charge of follow-up spill reporting: David Turk 6425 South Highway 191 Blanding,UT 84511 (435) 678-4113 (work) (435) 459-9786 (cell) TABLE 2.0 REAGENT TANK LIST QUANTITY REAGENT AMMONIUM SULFATE DIESEL KEROSENE USED/WASTE OIL DIESEL UNLEADED PROPANE LNG AMMONIA SODIUM HYDROXIDE SODA ASH SOLUTION SODA ASH SHIFT SODIUM CHLORATE SODIUM CHLORATE SODIUM CHLORATE SULFURIC ACID SULFURIC ACID CAPACITY (GAL) 24,366 250 10,152 5,000 6,000 3,000 30,000 30,000 31,409 19,904 16,921 8,530 16,075 21,057 28,788 1,600,000 11,000 TABLE 3.0 LABORATORY CHEMICAL INVENTORY LIST1 Chemical in Lab RQ2 Quantity In Stock Aluminum nitrate 2,270 kg 1.8 kg Ammonium carbonate 2,270 kg 11-3 kg Ammonium bifluoride 45.4 kg 2,27 kg Ammonium chloride 2,270 kg 2.21 kg Ammonium oxalate 2,270 kg 6-8 kg Ammonium thiocyanate 2,270 kg 7.8 kg Antimony potassium tartrate 45.4 kg 0.454 kg n-Butyl acetate 2,270 kg 4 L Calcium acetate 4.54 kg 0.454 kg Cyclohexane 454 kg 24 L Ferric chloride 454 kg 6.810 kg Ferric nitrate 454 kg 0.454 kg Ferrous ammonium sulfate 454 kg 0.57 kg Ferrous sulfate 454 kg 0.454 kg Lead nitrate 4.54 kg 2.7 kg Potassium chromate 4.54 kg 0.114 kg Sodium hydrosulfide 2,270 kg 1.0 kg Sodium nitrite 45.4 kg 2.5 kg Sodium phosphate tribasic 2,270 kg 1.4 kg Zinc acetate 454 kg 0.91 kg Chemical in Volatiles and Flammables Lockers (A,B,C)RQ2 Quantity In Stock Chloroform 4,54 kg 1L Formaldehyde 45.4 kg <1L of 37% solution Nitrobenzene 454 kg 12 L Toluene 454 kg 12 L Chemical in Acid Shed RQ2 Quantity In Stock Hydrochloric acid 2,270 kg 58 gal Nitric acid 454 kg 5 L Phosphoric acid 2,270 kg 10 L Sulfuric acid 454 kg 25 L Hydrofluoric Acid 45.4 kg 1L Ammonium hydroxide 454 kg 18 L 1. This list identifies chemicals which are regulated as hazardous substances under the Federal Water Pollution Control Act 40 CFR Part 117. The lab also stores small quantities of other materials that are not hazardous substances per the above regulation. 2. Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3: “Reportable Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act.” TABLE 4.0 REAGENT YARD/SMALL QUANTITIY CHEMICALS LIST 1 CHEMICAL RQ2 QUANTITY IN STORAGE COMPOUND Acetic Acid, Glacial 1000 lbs 4 gal Ammonium Hydroxide 1000 lbs 5L Ferrous Sulfate Heptahydrate 1,000 lbs 5 kg (1 libs) Hydrochloric Acid 5,000 lbs 60 gal of 40% solution Nitric Acid 1,000 lbs 10 L Potassium Permanganate 0.1 N 32 gal 5 kg (11 lbs) Silver Nitrate 1 lb 2.6 kg T richloroethy lene 100 lb 2 L 1. This list identifies chemicals which are regulated as hazardous substances under the Federal Water Pollution Control Act 40 CFR Part 117. Materials in this list are stored in a locked storage compound near the bulk storage tank area. The Mill also stores small quantities of other materials that are not hazardous substances per the above regulation. 2. Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3: “Reportable Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act.” TABLE 5.0 REAGENT YARD AND BULK CHEMICALS LIST1 REAGENT Sulfuric Acid Floe #301 Hyperfloe 102 Ammonia - East Tank Ammonia - West Tank Kerosene Salt (Bags) Ammonium Hydrogendifluoride Soda Ash Dense (Bag) Phosphoric Acid Hydrogen Peroxide Polyox Millsperse Nalco TX760 Nalco 7200 Tributyl phosphate Distillates Diesel Gasoline Alamine 336 drums Floe 109 Floe 208 Floe 904 Hyperfloe 624 Salt (Bulk solids) Salt (Bulk solutions) Caustic Soda Ammonium Sulfate Sodium Chlorate Alamine 335 Bulk Alamine 310 Bulk Isodecanol Vanadium Pentoxide Yellowcake RQ 1,000 lbs None None 100 lbs 100 lbs 100 gal None None None 5,000 lbs None None None None None None None 100 gal 100 gal None None None None None None None 1,000 lbs None None None None None 1,000 lbs None QUANTITY ON SITE 2,719,680 lbs 0 lbs 1,500 lbs 113,600 lbs 93,720 lbs approx. 5,100 gal 19,600 lbs 20,450 lbs 2,000 lbs 6,300 lbs 3,600 gal 560 lbs 1,410 lbs 9 barrels 1,590 lbs 9,450 lbs 110 gal approx. 6,000 gal approx. 3,000 0 lbs 7,750 lbs 1,500 lbs 1,500 lbs 4,230 lbs Total of 70,000 lbs on site in all forms 24,000 lbs in 40% solution 21,300 lbs 66,000 gal 310 lbs 0 lbs 0 lbs 500,000 lbs < 10,000 lbs 1. This list identifies the bulk chemicals and the chemicals in the reagent yard whether or not they are regulated as hazardous substances under the Federal Water Pollution Control Act 40 CFR Part 117. 2. Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3: “Reportable Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act.” 3. Vanadium Pentoxide and Yellowcake, the Mill’s products, are not stored in the Reagent Yard itself, but are present in closed containers in the Mill Building and/or Mill Yard. TABLE 6.0 PETROLEUM PRODUCTS AND SOLVENTS LIST1 PRODUCT RQ QUANTITY IN WAREHOUSE Lubricating Oils in 55 gallon drums 100 gal 1,540 gallons Transmission Oils 100 gal 0 gallons Dielectric fluids 5 gallons Antifreeze None 55 gallons Greases 1,787 lbs Water Soluble Oils 100 gal 30 gallons Xylene (mixed isomers)100 lbs 0 gallons Lacquer thinner 0 gallons Acetone None 55 gallons Methyl Ethyl Ketone None 55 gallons Toluene 1000 lbs 0 gallons Varsol Solvent (2% trimethyl benzene in petroleum distillates)100 gal 0 gallons Resin None 10 gallons Epoxy Paints None 55 gallons Epoxy Catalyst None 30 gallons Oil Base paints None 15 gallons Paint thinners None 0 gallons Other paints None 20 gallons 1. This list includes all solvents and petroleum-based products in the Mill warehouse 2. Reportable Quantities are those identified in 40 CFR Part 117 Table 117.3: “Reportable Quantities of Hazardous Substances Designated Pursuant to Section 311 of the Clean Water Act.” FIGURES LNG ACID TANK)/ □ Q WATE 2J <0SUBSTiATIO OREQ ¥■GRIO□OLD DECONTAMINATION PAD C3AMMON UM SULFATE qQQ.MILL , °°U Ol W ES ATER BUILDING /0 SODA \'SAMPLE PLANTO □ OO CjQ^Sfctp^ ammoniaAU a dBOILE L[S'SALT J n~Q □CP Oc KEROSENE 10 g> i CP ° SHOPsxBUILDINGo oooo □ ot>: □ o°o □ FUEpISLAN OO O . ALTERNATE / - lEEED / )j ,CIRCUIT (to SODIUM CHLORATE a <oDRY-REAGENT 2>5sf\sc PEC INATORALx HOOFFICE l YARDREAGENT 4© 2 J.\___D___J 4S •8®V' TRUCK SHOP SOIOP y 100 50 0 SCALE IN FEET Energy Fuels Energy Fuels Resources (USA) Inc. 225 Union Blvd. Suite 600 Lakewood, CO 80228 REVISIONS Date 10-11 5-14 4-16 By WHITE MESA MILL County: San Juan State:Utah Location: Figure 1 MILL SITE LAYOUT Scale: y=200' | Date: May 12,2000 [ Drafted By: p.siedd Mill Site Layout 4.28.16.dwg Figure 11 r X1 ^ r s—0) CMS ^ § r £C?£D fit* of %[i cooO 2 w co ~ __• aj cn o: c 8 jo.2 s CDS p ,=0 JeU-w.3 .CD CM ZZ<°£J 2 COX• 0 <'s\z b co LLICO UJCO CEo ."*ij CDaUJ/20 =; <0 <w<<'V2>cr 5§coQ uCmX C Q OCX)rsn rrI1o^■f Oo IO X CD n co B Ml■ .s UJ <Z2u '<\CO \D \ *%■ <3 < r zoo <co CO LL co*■MTVQ CD co C-JCO CD <0 K CD<UJ CDCD0U,-n - 0 0 D)ob o <<D O CD<5o<- /2'Z-<Q_X.cvi: i QCO K CO CO QO.<ICOQ . x.Xr r*-* * «% v »^*v"—^ * >:.v- xxX r CO 0 < o/2 <sISs' s ^r^- V \ r v sJK ^x «* X AT-v■V X co §T 4 Q \LLIZVLJJ Z <\I .zroQ Z Q. :v0^7 r =J* # y--m mnFIFrz n!»iVofco\rjnvtvin\vso'v!==o’n\-M Figure 3 Energy Fuels Resources (USA) Inc. White Mesa Mill Organizational Structure President & CEO Executive VP Conventional Operations Sr. Director Regulatory Affairs Mill Manager Manager, Environmental Health and Safety and RSO u Quality Assurance Manager Mill Operations Personnel Radiation Technicians Environmental Technicians Safety Supervisor