Agenda packet — Industry City Council, February 12, 2026 (part 57 of 59)

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MARICI BATTERY ENERGY STORAGE SYSTEM FACILITY INITIAL STUDY / MITIGATED

NEGATIVE DECLARATION

CITY OF INDUSTRY

APPENDIX
PlaceWorks
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MARICI BATTERY ENERGY STORAGE SYSTEM FACILITY INITIAL STUDY / MITIGATED

NEGATIVE DECLARATION

CITY OF INDUSTRY

APPENDIX
DECEMBER 2025

APPENDIX K

REVISED SOIL AND GROUNDWATER

MANAGEMENT PLAN

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MARICI BATTERY ENERGY STORAGE SYSTEM FACILITY INITIAL STUDY / MITIGATED

NEGATIVE DECLARATION

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APPENDIX
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Revised Soil and
Groundwater
Management Plan
September 2025
Marici Project LLC
16207, 16233, and 16253 Gale Avenue
City of Industry, California 91475
Prepared For:

Marici Project LLC
11801 Domain Blvd. Suite 450
Austin, Texas 78758
Prepared By:

TRC
6 Executive Circle, Suite 200
Irvine, California 92614
Prepared by:

Jose Maldonado
Project Manager
Reviewed and Approved by:

John Trompeter, PG, CHG
Principal Hydrogeologist
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Marici Project LLC September 2025
Revised Soil and Groundwater Management Plan i

TABLE OF CONTENTS
ACRONYM LIST ........................................................................................................................II SOIL AND GROUNDWATER MANAGEMENT PLAN (SGMP) REFERENCE GUIDE ..............III

1.0 INTRODUCTION.............................................................................................................1

2.0 SITE DESCRIPTION.......................................................................................................1

3.0 BACKGROUND..............................................................................................................1

4.0 EXCAVATED SOIL CHARACTERISTICS ......................................................................3

5.0 NOTIFICATIONS AND PRE-EXCAVATION ACTIVITIES...............................................4

5.1 General Notifications...........................................................................................................4

5.2 Notifications for Impacted Soil ............................................................................................4

5.3 Worker Education and Safety .............................................................................................5

6.0 POTENTIAL IMPACTED SOILS.....................................................................................5

7.0 POTENTIAL EXPOSURE PATHWAYS AND RECEPTORS...........................................6

8.0 SOIL MANAGEMENT.....................................................................................................6

8.1 Soil Excavation Parameters................................................................................................6

8.2 Waste Minimization/management.......................................................................................6

8.3 Changed Conditions and Soil Stockpiling...........................................................................7

8.4 Waste Characterization and Disposal.................................................................................7

9.0 GROUNDWATER AND STORMWATER MANAGEMENT .............................................7

9.1 Permits ................................................................................................................................8

9.2 Sampling and Testing Groundwater or Stormwater............................................................8

10.0 ADDITIONAL PROJECT CONTROLS............................................................................9

10.1 Dust Control Measures .......................................................................................................9

10.2 Stormwater Quality Controls ...............................................................................................9

11.0 DOCUMENTATION ........................................................................................................9

12.0 LIMITATIONS ...............................................................................................................10

13.0 REFERENCES..............................................................................................................11

APPENDICES
A Exhibit 1 – Vicinity Map
Exhibit 2 – Site Diagram
B San Gabriel Valley Regional Groundwater Plume Maps
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Marici Project LLC September 2025
Revised Soil and Groundwater Management Plan ii
Acronym List
AST Aboveground storage tank
BER Business Environmental Risk
BESS Battery Energy Storage System
BMPs Best management practices
CAM-17 Metals California Administrative Manual metals
COCs Contaminants of concern
EPA Environmental Protection Agency
ESA Environmental Site Assessment
GC General Contractor
HAZWOPER Hazardous Waste Operators and Emergency Response HASP Health and Safety Plan
NPDES National Pollutants Discharge Elimination Permit System OCPs Organochlorine pesticides
OSHA Occupational Safety and Health Administration
PCBs Polychlorinated Biphenyls
PCE Perchloroethylene
PPE Personal protective equipment
PRP Potential responsible party
pVEC Potential vapor encroachment condition
REC Recognized environmental condition
SCAQMD South Coast Air Quality Management District
SGMP Soil and Groundwater Management Plan
STLC Soluble Threshold Limit Concentration
SWPPP Stormwater Pollution Prevention Plan
TBD To be determined
TCE Trichloroethylene
TCLP Toxicity Characteristic Leaching Procedure
TPH Total petroleum hydrocarbons
UST Underground storage tank
VEC Vapor encroachment conditions
VOCs Volatile organic compounds
WET Waste Extraction Test
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Marici Project LLC September 2025
Revised Soil and Groundwater Management Plan iii
Soil and Groundwater Management Plan (SGMP) Reference Guide Site Description
Project Name: Marici Project LLC
Project Location:
16207,16233, and 16253 Gale Avenue
City of Industry, California 91475
Owner Contacts
Owner: Marici Project LLC
Primary Contact:

Alex Evers, Operations Manager
Mobile: (626) 437-3346
Email: [email protected]
Alternate Contact:

Nate Moore, Vice President of Operations and Maintenance Mobile: (775) 545-2078
Email: [email protected]
Contractor Contacts
General Contractor (GC) To be determined
Environmental
Professional (EP) To be determined
California Certified
Laboratory To be determined
Relevant Permits/Agency Notification Requirements
Confined Space
Entry Permit
Required if qualified/trained personnel will be entering an excavation deeper than four feet, or if entering a structure with limited ingress/egress and the potential for hazardous
atmosphere.

South Coast Air Quality
Management District
(SCAQMD)
The contractor to confirm that no permit and no notification is required. Best management practices (BMPs) need to be
implemented for effective dust control management (confining generated dust to the boundaries of the Property). Any impacted or potentially impacted soils should be covered and/or
containerized and handled as indicated herein.

County of Los Angeles
Public Health –
Environmental Health
Permits are required for soil borings deeper than 10 feet or that extend into groundwater.

State Water Resources
Control Board (Water
Board)
Stormwater Pollution Prevention Plan (SWPPP) and Construction Stormwater General Permit Order 2022-0057-DWQ coverage are required for construction activities; clearing, demolition, grading, excavation, and other land disturbance activities.

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Marici Project LLC September 2025
Revised Soil and Groundwater Management Plan iv
Potential Disposal/Recycling Facilities
Non-Hazardous Soil Soil Safe, Adelanto, CA
Hazardous Soil CWM Kettleman Hills Landfill, Kettleman City, CA Non-RCRA Hazardous
Soil and Groundwater
TBD based on confirmation of compliance status to accept waste at the time of disposal. Potential facilities include:
• World Oil Recycling, Compton, CA
• Chiquita Canyon Landfill, Castaic, CA
• Simi Valley Landfill and Recycling Center, Simi Valley, CA • Azusa Land Reclamation (owned by Waste Management,
Inc.), Azusa, CA
• Clean Harbors Buttonwillow Landfill Facility, Buttonwillow, CA Potential Waste Transportation
Registered Waste Hauler Belshire Environmental SVCS, Inc.

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Marici Project LLC September 2025
Revised Soil and Groundwater Management Plan 1

1.0 Introduction
TRC has prepared this Revised Soil and Groundwater Management Plan (SGMP) to provide background information on environmental site conditions and best management practices (BMPs) for use in the event impacted soil or excavation water is encountered during construction of the Marici Project LLC. The project consists of demolition of existing site features and development of a Battery Energy Storage System (BESS). The project will be developed on parcels comprising 16207, 16233, and 16253 Gale Avenue in the City of Industry, California (Site). A Vicinity Map showing the Site location, and a Site Diagram showing an aerial photograph with the existing site features are included as Exhibits 1 and 2 in Appendix A, respectively.

2.0 Site Description
Site Name Marici Project LLC
Site
Location/Address
16207,16233, and 16253 Gale Avenue
City of Industry, California 91475
Los Angeles County Assessor Identification Numbers: 8242-016-033, 8242-016-034, 8242-016-036, 8242-016-044, and 8242-016-061 Site Description
The Site occupies approximately 9.2 acres that is primarily occupied by building improvements, asphalt-paved parking areas and driveways, concrete-paved loading docks, landscaping, and utilities.

On-site operations include metal fabricating, food product warehousing, distribution, electronics, transportation services, and administrative business activities (Terracon, 2024, 2025a, 2025b).

Refer to Appendix A which includes Exhibit 1 Vicinity Map showing the Site location and Exhibit 2 Site Diagram showing an aerial photograph with existing developed conditions.

3.0 Background
The background information regarding the Site is primarily sourced from the five (5) previous Phase I Environmental Site Assessments [ESAs]) and two limited site investigations listed in the References. The Project addresses identified in this SGMP are those documented for the parcels on tax assessor records.

Current and historic land uses at the Site have included agricultural, industrial, and commercial activities, as follows:
• As early as 1894, the area of the Site and surrounding properties consisted of undeveloped and/or agricultural land through approximately the mid-1960s. • By 1970, the eastern portion of the Site (16253 Gale Avenue) appeared as a Christmas tree farm with small structures/sheds in the east-central portion of the Site. • By 1976, in the western portion of the Site (16233 Gale Avenue), the existing industrial building used for metal fabrication appeared to be developed. • In the western portion of the Site (16207 Gale Avenue):

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Marici Project LLC September 2025
Revised Soil and Groundwater Management Plan 2
o From 1970-2009, a stainless-steel commercial appliance manufacturer operated at the Site.
o From 2009-2022, an auto and tent parts warehouse facility operated at the Site. o From 2009-2020, a computer numeric control (CNC) machine shop operated at the Site.
• By 2000, the eastern portion of the Site was developed with the existing multi-tenant logistical warehousing and fulfillment facility.
• Current operations include administrative business activities, warehousing, distribution, electronics, metal fabricating, and transportation services.

Immediately adjacent to the Site, land uses have included railroad, utility, and residential, as follows:
• By 1927, Union Pacific Railroad appeared developed north of the Site. • By 1964:
o The Southern California Edison Walnut Substation appeared developed east of the Site.
o Residential neighborhoods appeared developed south of the Site. • Land uses at the adjoining properties have remained consistent to the present.

Overall, based on the Phase I ESAs (Terracon, 2025a and 2025b) performed for the properties at the Site, the following conclusions regarding environmental conditions of concern have been identified:
• The Site is located within the San Gabriel Valley, Puente Valley Operable Unit (Area 4) Superfund project, which includes regional groundwater that is impacted by halogenated solvents including trichloroethylene (TCE) and perchloroethylene (PCE) above applicable regulatory screening levels. Based on the regional plume maps in November 2020 showing PCE concentrations in shallow groundwater, it appears the plume is mostly located north/northeast of the Site and extends underneath the Site in the vicinity of Gale Avenue (see Figure 14 prepared by Tetra Tech in Appendix B). Based on review of the Environmental Protection Agency (EPA) and Regional Water Board records, the Site was not reported as a contributor to the plume (Terracon, 2024) and the Site was not listed as a potential responsible party (PRP; Partner, 2017). Relative to the Site, this Superfund project represents a recognized environmental condition (REC) and potential vapor encroachment condition (pVEC) due to the anticipated shallow depth of groundwater in the Site vicinity (Terracon, 2024, 2025a, 2025b). • The off-site adjoining SCE Walnut Substation located east of the Site was identified as a potential source for halogenated solvent impacts to shallow groundwater beneath the Site based on the generated waste streams identified (including halogenated solvents), the close proximity to the Site, and the shallow depth to groundwater (approximately 19 feet below grade [fbg]). The off-site SCE Walnut Substation represents a REC to the Site (Terracon, 2024).
• For the 16207 Gale Avenue property, the former stainless-steel commercial appliance manufacturer represents a REC to the Site based on the longevity of industrial operations (approximately 39 years), lack of information concerning waste streams, and K-7

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Marici Project LLC September 2025
Revised Soil and Groundwater Management Plan 3
the likely use of petroleum and solvents/chemicals as part of the historical operations (Terracon, 2025a).
• For the 16233 Gale Avenue property, the Metal Cutting Service facility represents a REC to the Site based on longevity of business operations (approximately 49 years), the likely use of petroleum and solvents/chemicals as part of the current and historical operations at the Site, and the potential release of hazardous substances (Terracon, 2025b). • Polychlorinated biphenyls (PCBs) were identified offsite (SCE Walnut Substation). The Phase I ESAs concluded they do not represent a REC for the Site. • Organochlorine pesticides (OCPs) from historic agricultural land use are not identified as a REC for the Site.

Limited site investigations (LSIs) were performed at the properties in February 2025, and were reported in Terracon, 2025c and 2025d listed in the References. The objective of the LSIs were to assess the presence of chemicals commonly associated with the RECs identified in the Phase I ESAs. The laboratory results of soil and soil vapor samples collected and analyzed for the LSIs are summarized as follows:
• Soil – TPH and VOCs: Volatile organic compounds (VOCs), total petroleum hydrocarbons gasoline range organics, (TPH-GRO), TPH diesel range organics (TPHDRO) were not detected above laboratory reporting limits (RLs). Motor oil range organics (TPH-MORO) were detected above the RL for one (1) sample, but it was below its residential and commercials environmental screening levels (ESLs). All other samples were below the RLs for each constituent analyzed.
• Soil – Metals: Metals were not detected above the laboratory RLs with the exception of arsenic, barium, chromium, cobalt, copper, lead, nickel, vanadium, and zinc. The concentrations of the metals listed above are within the range of naturally occurring “background” concentrations, and were below residential, commercial, and construction worker ESLs; except two (2) soil sample results for arsenic above ESLs but below the Department of Toxic Substances Control (DTSC) established regional “background” concentrations for Southern California.
• Soil Gas – TPH and VOCs: Concentrations of 1,3-butadiene, benzene, ethylbenzene, tetrachloroethene (PCE), trichloroethene (TCE), and 1,1,2,2-tetrachloroethane (TCA) were above either residential or commercial ESLs or both. It is noted that concentrations of VOCs in soil gas are generally increasing with depth, which supports that the regional VOC groundwater plume may be a likely source.

4.0 Excavated Soil Characteristics
While no impacted soils have been identified onsite, during excavation and grading, there is a potential to encounter unknown impacted soils, for example, when buildings, foundations or paving are removed or underlying soils are excavated. Based on the identified RECs, potential constituents of concern (COCs) could include total petroleum hydrocarbons (TPH) and volatile organic compounds (VOCs). If excavated, impacted soils may result in the generation of waste that would require management and additional precautions during construction.

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Marici Project LLC September 2025
Revised Soil and Groundwater Management Plan 4
The groundwater in the Site vicinity is anticipated to be encountered at depths ranging from approximately 21 to 26 fbg (Terracon Geotechnical Report, December 2024). Based on the maximum depth of the proposed excavation activities (up to 10 fbg), groundwater is not anticipated to be encountered at the Project Site during routine earthwork. However, geotechnical exploration soil borings and/or deep foundations for the interconnection support poles have the potential to encounter groundwater, which is further described in Section 9.0.

1. RCRA Hazardous Waste – excavated soil with representative chemical concentrations exceeding Federal criteria when analyzed by Toxicity Characteristic Leaching Procedure (TCLP). Based on the available data, soil excavated from the Project Site is not anticipated to fall under this category.

2. Non-RCRA [California] Hazardous Waste – excavated soil with representative chemical concentrations exceeding State criteria when analyzed by Waste Extraction Test (WET) methods, Soluble Threshold Limit Concentration (STLC), but not exceeding Federal criteria. Based on the available data, soil excavated from the Project Site is not anticipated to fall under this category.

3. Non-hazardous Waste – excavated soil with representative chemical concentrations less than State and Federal criteria. Previously undocumented, localized area(s) of soil excavated from the Project Site may fall under this category.

4. Non-impacted Soil – soil does not have chemical impacts that would require special handling or off-site disposal. It is anticipated that the vast majority of the soil excavated from the Project Site will fall under this category.

5.0 Notifications and Pre-Excavation Activities

5.1 General Notifications
The GC is responsible for all necessary permits and notifications to regulatory and permitting agencies associated with the project work. BMPs should be implemented by the GC to ensure compliance with the approved SWPPP and dust control plan.

5.2 Notifications for Impacted Soil
The Owner will require the General Contractor (GC) and its subcontractors to instruct and train workers to be cognizant of the potential for encountering soil contaminated by past activities and to implement measures consistent with this plan.

The Owner shall be immediately notified of any discovery of potentially impacted soil or unanticipated underground feature such as an underground storage tank (UST), septic pit, hydraulic lift component, clarifier, or other unknown feature which is suspected to potentially contain or have in the past contained hazardous substances.

In the event of any indication of impacted soil is observed (i.e., odors, staining, debris, etc.) during an excavation or other work that exposes soil, the Foreman shall immediately notify the K-9

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Revised Soil and Groundwater Management Plan 5
Owner and the Owner shall promptly obtain recommendations from a qualified environmental professional regarding any additional characterization/sampling and remedial activities that should be conducted.

The immediate notification to the Owner for reporting discoveries shall be to:
• Primary Contact: Alex Evers, Operations Manager
Mobile: (626) 437-3346
E-mail: [email protected]
• Alternate Contact: Nate Moore, Vice President of Operations and Maintenance Mobile: (775) 545-2078
E-mail: [email protected]

5.3 Worker Education and Safety
This Revised SGMP provides information that will help to support compliance with employer obligations such as employee right-to-know, worker safety, and other regulatory programs while providing general guidelines for reducing the potential for exposure if impacted soils are encountered. However, each employer remains responsible for the health and safety of its own workers. This Revised SGMP is not intended for direct, unmodified use by employers to protect workers. Rather, it intends to provide general considerations and procedures for modification and incorporation by employers into their existing worker safety programs. The GC and environmental consultant must inform and educate their respective workers and subcontractors to be alert for new or undiscovered conditions that could potentially pose risk.

The GC, environmental consultant, and their subcontractors are required to develop and implement independent Health and Safety Plans (HASPs) during all phases of work. The HASP should be prepared by a qualified person experienced in the health and safety risks associated with the identified COCs in accordance with the Federal Occupational Safety and Health Administration (OSHA) Hazardous Waste Operators and Emergency Response (HAZWOPER) standard (29 CFR 1910.120) and Cal-OSHA standard (8 CCR 5192). The HASP should specify administrative and engineering controls and require applicable personal protective equipment (PPE) for worker safety during each stage of the Project.

6.0 Potential Impacted Soils
Based on the findings from the previous Phase I ESAs and the LSIs performed in 2025, which are summarized in Section 3.0 above, construction workers have the potential to be exposed to soil (TPH-MORO) and/or soil gas (VOCs including PCE and TCE) with concentrations that could represent a health hazard (See Exhibit 2). From the LSI results, metal concentrations in soil (particularly arsenic) are below DTSC accepted regional background levels.

The environmental consultant shall be onsite when substantive grading or excavations are occurring in soils not previously disturbed by project construction. The GC and environmental consultant shall implement procedures and practices to ensure that their respective workers are trained to be continually observant for potential impacted soils. The Owner, or the GC and K-10

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Revised Soil and Groundwater Management Plan 6
environmental consultant at the Owner’s direction, shall provide for active, periodic field oversight including:
• Screening exposed and excavated soils:
o Using visual indicators and instrumentation (e.g., calibrated photoionization detector) to identify potentially TPH- and VOC-impacted soils. o Based on visual indicators or instrumentation, potential collection of select soil samples for laboratory analysis for contaminants of concern (COCs) including TPH, VOCs, and any additional profile testing that may be required by waste disposal facilities, using EPA approved methods. At a minimum, this testing would include profiling of removed soil waste that will be transported for off-site disposal.
• Excavation, separation, and documentation of potentially impacted soils. • If appropriate, collection of select samples for laboratory analysis (as indicated above) from:
o Soils remaining where impacted soils have been removed. o Impacted soils designated for reuse, additional sampling, and/or for off-site disposal.
• Coordination and facilitation of waste profiling, transportation, and disposal.

7.0 Potential Exposure Pathways and Receptors
Exposure pathways are identified as:
• Inhalation of dust or vapors that could be generated from impacted soil. • Dermal contact with impacted soil during excavation activities. • Dermal contact or ingestion of groundwater.

The GC, environmental consultant, and Subcontractor HASPs and BMPs should include hazard assessment and mitigation measures to eliminate or minimize potential exposure pathways.

8.0 Soil Management

8.1 Soil Excavation Parameters
Nearly all of the project site will be graded, and most excavations will be less than 10 feet deep.

Two electric tie-line support poles will require deep excavations or borings.

8.2 Waste Minimization/management
If impacted soil is encountered, it should be removed and segregated in a manner to minimize over-excavation or mixing with clean soil. Impacted soils should be removed from the Site frequently to minimize the potential for contact between stormwater and any impacted soils identified during excavation. Excavation in areas where impacted soil is encountered should be protected from stormwater run-on by clean soil berms or other diversionary features to direct K-11

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Revised Soil and Groundwater Management Plan 7
water away from any exposed impacted soils. Other BMP measures such as covering impacted soils with plastic shall be implemented to prevent or minimize stormwater contact with impacted soils.

8.3 Changed Conditions and Soil Stockpiling
The GC and subcontractors should be aware of the regulatory implications of improper management or disposal of contaminated soils. If changed conditions are encountered (i.e., petroleum hydrocarbons, USTs, or obviously impacted soils), the excavated impacted soil shall be stockpiled separately on plastic sheeting under the direction of the environmental consultant, covered with plastic sheeting, and secured with fiber rolls or equivalent until they can be properly evaluated. See Section 5.2 for notifications. Workers in physical contact with obviously impacted environmental media should have OSHA HAZWOPER training consistent with 29 CFR 1910.120.

If chemical odors, stained or saturated soils, a sheen on water collected in excavations, detected concentrations of COCs from laboratory analysis of select soil samples, or other evidence of potential chemical contamination is encountered during excavation activities, work in the area of the discovery shall cease immediately and the Owner shall be notified. See Section 5.2 for notifications.

8.4 Waste Characterization and Disposal
If impacted soils are identified, the impacted soil shall be characterized as needed to determine which of the waste categories in Section 4.0 it fits in. If off-site disposal is required characterization will also be required by the receiving facility. Based on historical knowledge of the Site and vicinity, if impacted soils are encountered, typical waste profiling parameters, may include TPH carbon chain by EPA Method 8015M and VOCs by EPA Method 8260B. If impacted soil is excavated, proper classification is the responsibility of the Generator, which will be the Owner unless otherwise dictated by contract or state law. All impacted soil characterization and results as well as manifesting shall be coordinated with the Owner.

Only an authorized transporter can transport soils offsite. Transport and shipping documentation shall be coordinated with the Owner. Receiving facilities must be licensed to receive the types and concentrations of COCs in the soil shipment. Some licensed disposal/recycling facilities and waste transporters are listed in the SGMP Reference Guide. The listed facilities are not intended to be limiting.

9.0 Groundwater and Stormwater Management
If either groundwater or stormwater that has contacted impacted soils is handled during construction, management measures in this plan must be adhered to. The groundwater in the Site vicinity is anticipated to be at depths of approximately 21 to 26 fbg. Groundwater is not expected to be encountered during construction except potentially for construction of the deep foundations for the electric tie-line support poles, and potentially in borings if additional geotechnical drilling is conducted. If stormwater collects in any excavation during construction, it should be visually inspected for evidence of sheen or other indication of COC presence such as visually impacted soil in the excavation wall. If groundwater or storm water that has come in K-12

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Revised Soil and Groundwater Management Plan 8
contact with potentially impacted soils is to be removed from an excavation, the water shall be managed as potentially contaminated and evaluated through chemical analysis prior to discharge and/or off-site disposal. Samples shall be collected by a qualified person and characterization shall be coordinated with the Owner.

Produced and/or captured groundwater or stormwater that has contacted impacted soils shall be containerized in suitable portable aboveground storage tanks (ASTs) compatible with the potential COCs and properly secured to prevent unsafe exposure, contact with stormwater, or discharge to the surface, storm drains, or waterways. Secondary containment of the containerized water shall be established for volumes greater than 100 gallons and shall have a capacity of 110 percent (%) of the total volume of the containers, regardless of actual volume stored in the containers. Additional BMPs such as regular inspection of the containers and secondary containment and proper labeling shall be maintained.

9.1 Permits
Discharge of untested and/or untreated groundwater or potentially impacted stormwater to the ground surface, storm drain, or sanitary sewer system is prohibited. It is the responsibility of the GC, and/or its subcontractors to obtain the necessary permit and equipment to conduct any dewatering and discharging activities that might be needed and to ensure that required characterization (e.g., laboratory analysis of COCs using EPA-approved methods) of such water occurs under the direction of the environmental consultant. Impacted water must be managed in accordance with applicable waste regulations. Impacted water may be shipped off-site by a licensed hauler to a permitted treatment facility or treated on-site and discharged under a valid permit. Water generated may be temporarily stored on-site in ASTs, as described above, pending necessary permitting, testing, and/or treatment. Some licensed disposal/recycling facilities and waste transporters are identified in the SGMP Reference Guide. The listed options are not intended to be limiting.

Project construction will need to occur under the State Water Resources Control Board Construction General Permit Order 2022-0057-DWQ, adopted September 8, 2022, effective September 1, 2023.

9.2 Sampling and Testing Groundwater or Stormwater
If either groundwater or stormwater that has contacted impacted soils must be handled, the GC will ensure that sampling and testing occur in accordance with applicable regulations as directed by the environmental consultant. All sampling shall be conducted by qualified personnel.

Samples shall be collected in laboratory-provided pre-cleaned, EPA-approved sample containers, transported to an accredited laboratory in a cooler with ice, and shipped with chainof-custody documentation. Based on the known potential chemicals of concern, if groundwater is pumped, samples shall be collected and analyzed pursuant to regulatory permit requirements, and may include TPH by EPA Method 8015M and VOCs by EPA Method 8260B. Additional sampling and analysis may be required for waste characterization or discharge to local sanitary sewer system and/or storm drain according to applicable permit requirements, such as general chemistry, pH, and temperature.

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Revised Soil and Groundwater Management Plan 9

10.0 Additional Project Controls
The following additional control measures, or measures with similar of greater effectiveness, shall be implemented to limit the potential for worker or public exposure to impacted soils, if present.

10.1 Dust Control Measures
The GC will be responsible for controlling dust in accordance with SCAQMD requirements. A Dust Control Permit and a Dust Mitigation Plan may be required. Supplemental permits may also be needed for activities such as (but not limited to) stockpiling, backfilling, or crushing, etc.

A complete list of the necessary supplemental permits typically is available on the SCAQMD web as follows:
http://www.aqmd.gov/home/regulations/ceqa/air-quality-analysis-handbook/mitigationmeasures-and-control-efficiencies/fugitive-dust.

The GC will be responsible for the preparation of and adherence to the Dust Mitigation Plan, as well as adhering to other pertinent requirements referenced.

10.2 Stormwater Quality Controls
Project construction will require coverage under State Water Resources Control Board Construction General Permit Order 2022-0057-DWQ for storm water discharges from construction sites. The Owner will hold the General Permit and will require the GC to comply with the permit and with the SWPPP required by the permit. The SWPPP will be prepared by a Qualified SWPPP Developer and will include BMPs to prevent stormwater contact with potential contaminants site-wide. The SWPPP will be complementary to this Revised SGMP, and the GC and subcontractor work and environmental consultant directives will be required to follow applicable BMPs from both if impacted soil or groundwater is managed.

11.0 Documentation
Upon completion of Site excavation activities and receipt of any necessary laboratory analytical results and waste manifest documentation, the GC and/or environmental consultant shall prepare a report that will include:
• Field Logs or Activities Summaries and photo-documentation related to any encounters of impacted soil or water.
• Tabulated summary of samples taken.
• Laboratory results for testing of soil and groundwater samples, and characterization of wastes, if any.
• Site map indicating sample locations and limits of contamination encountered, if any. • Waste profile forms, if any.
• Waste manifests for soil and water transported off-site for disposal and/or recycling, if any.

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Revised Soil and Groundwater Management Plan 10

12.0 Limitations
This Revised SGMP has been developed to inform the GC, environmental consultant, and subcontractors of the potential for encountering contaminated soil or water during excavation activities at the Site. If encountered, impacted soil or water could contain COCs at concentrations that could present a health hazard to construction personnel via dermal contact, inhalation of dust or vapors, or accidental ingestion. The measures herein are intended to inform the GC, environmental consultant, and subcontractors of the potential for impacted soil or groundwater to be encountered and to provide general guidance and project-specific requirements for management of impacted soil, stormwater that has contacted impacted soil, or groundwater. It is not intended to fulfill any GC, environmental consultant, or subcontractor obligation for worker health and safety, waste management, or environmental protection. The GC, environmental consultant, and its subcontractors engaged in activities at the project are responsible for conducting Site activities in accordance with all applicable federal, state, and local environmental and safety regulations. Additionally, since there are no known impacted soils on the Project site and this plan is primarily oriented toward the discovery of currently unknown conditions, this plan should be updated during construction in the event any such need is identified.

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Revised Soil and Groundwater Management Plan 11

13.0 References
Partner Engineering and Science, Inc. (Partner), 2017, Phase I Environmental Site Assessment Report, prepared for Morgan Stanley Mortgage Capital Holdings, LLC, for the property located at 16253-16293 East Gale Avenue, City of Industry, Los Angeles County, California 91475; dated December.

Terracon Consultants, Inc. (Terracon) 2023, Phase I Environmental Site Assessment Report, prepared for Aypa Power Development, LLC, for the Marici - City of Industry Battery Energy Storage System (BESS) Project located at 16253-16293 East Gale Avenue, City of Industry, Los Angeles County, California 91475; dated November 1 (Revised November 21).

Terracon Consultants, Inc.(Terracon) 2024, Phase I Environmental Site Assessment Report, prepared for Aypa Power Development, LLC, for the Marici - City of Industry Battery Energy Storage System (BESS) Project located at 16253-16293 East Gale Avenue, City of Industry, Los Angeles County, California 91475; dated August 23.

Terracon Consultants, Inc.(Terracon) 2025a, Phase I Environmental Site Assessment Report, prepared for Aypa Power Development, LLC, for the Marici - City of Industry Battery Energy Storage System (BESS) – 16233 Gale Avenue Project located at 16233 and 16235 Gale Avenue, City of Industry, Los Angeles County, California 91475; dated January 7.

Terracon Consultants, Inc.(Terracon) 2025b, Phase I Environmental Site Assessment Report, prepared for Aypa Power Development, LLC, for the Marici - City of Industry Battery Energy Storage System (BESS) – 16207 Gale Avenue Project located at 16207 and 16209 Gale Avenue, City of Industry, Los Angeles County, California 91475; dated January 27.

Terracon Consultants, Inc.(Terracon) 2025c, Limited Site Investigation Report, prepared for Aypa Power Development, LLC, for the Marici - City of Industry Battery Energy Storage System (BESS) – 16207 Gale Avenue Project located at 16207 and 16209 Gale Avenue, City of Industry, Los Angeles County, California 91475; dated March 26.

Terracon Consultants, Inc.(Terracon) 2025d, Limited Site Investigation Report, prepared for Aypa Power Development, LLC, for the Marici - City of Industry Battery Energy Storage System (BESS) – 16233 Gale Avenue Project located at 16233 and 16235 Gale Avenue, City of Industry, Los Angeles County, California 91475; dated March 26.

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Revised Soil and Groundwater Management Plan
Attachment A: Exhibit 1 – Vicinity Map
Exhibit 2 – Site Diagram
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NV
AZ
UT

PROPERTY BOUNDARY
DATE:

APPROVED BY:

CHECKED BY:

DRAWN BY: PROJ. NO.:

FILE:

TITLE:

PROJECT:

MARICI_EXHIBITS
COORDINATE SYSTEM: NAD 1983 STATEPLANE CALIFORNIA V FIPS 0405 FEET; MAP ROTATION: 0 -- SAVED BY: RCOLLINS ON 5/19/2025, 16:09:03 PM; FILE PATH: T:\1-PROJECTS\AYPA_POWER\604109.1PPL_SGMP\2-APRX\MARICI_EXHIBITS.APRX; LAYOUT NAME: EXHIBIT 1 – VICINITY MAP MAY 2025
13810 SE EASTGATE WAY
SUITE 440
BELLEVUE, WA 98005
PHONE: 425.395.0010
F
1:24,000 1" = 2,000'
0 1,000 2,000
FEET
BASE MAP: USGS 7.5' QUADRANGLES : BALDWIN PARK(34117-A8) DATA SOURCES: TRC
J. TROMPETER
J. MALDONADO
R. COLLINS
EXHIBIT 1
604109.1PPL.0000

VICINITY MAP

AYPA POWER DEVELOMENT LLC

MARICI - CITY OF INDUSTRY BESS
16253-16293 GALE AVENUE

LOS ANGELES COUNTY, CALIFORNIA
SITE
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NV
AZ
UT
Union Pacific RR
Union Pacific RR
Gale Ave
Ward Way
Fo
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Gale Ave
Folger S t
D
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(918 SOUTH STIMPSON AVENUE)
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16211 GALE
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16235 GALE
AVENUE
16233 GALE
AVENUE
16253-16293 GALE AVENUE

SCE WALNUT SUBSTATION
(16333 GALE AVENUE)

EMPTY DISPOSAL

BIN STORAGE AREA METAL CUTTING SERVICE

RESIDENTIAL NEIGHBORHOOD

GLENELDER ELEMENTARY
SCHOOL
(16234 FOLGER STREET)
%
B-1
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B-3
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LEGEND

PROPERTY BOUNDARY
U+
BORING LOCATIONS FROM 2023 TERRACON
GEOTECHNICAL INVESTIGATION (LA235125)

D SOLID WASTE DISPOSAL BINS

T TRANSFORMER (PAD MOUNT)

S SUMP/PUMP

STORM CURB INLET
% ANTICIPATED GROUNDWATER FLOW DIRECTION
DATE:

APPROVED BY:

CHECKED BY:

DRAWN BY: PROJ. NO.:

FILE:

TITLE:

PROJECT:

MARICI_EXHIBITS
COORDINATE SYSTEM: NAD 1983 STATEPLANE CALIFORNIA V FIPS 0405 FEET; MAP ROTATION: 0 -- SAVED BY: RCOLLINS ON 5/19/2025, 14:22:30 PM; FILE PATH: T:\1-PROJECTS\AYPA_POWER\604109.1PPL_SGMP\2-APRX\MARICI_EXHIBITS.APRX; LAYOUT NAME: EXHIBIT 2 – SITE DIAGRAM MAY 2025
13810 SE EASTGATE WAY
SUITE 440
BELLEVUE, WA 98005
PHONE: 425.395.0010
F
1:2,400 1" = 200'
0 100 200
FEET
BASE MAP: GOOGLE SATELLITE IMAGERY
DATA SOURCES: TRC
J. TROMPETER
J. MALDONADO
R. COLLINS
EXHIBIT 2
604109.1PPL.0000

SITE DIAGRAM

AYPA POWER DEVELOMENT LLC

MARICI - CITY OF INDUSTRY BESS
16253-16293 GALE AVENUE
DRAFT

LOS ANGELES COUNTY, CALIFORNIA
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Revised Soil and Groundwater Management Plan
Attachment B: San Gabriel Valley Regional Groundwater Plume Maps K-20

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6 Third Five-Year Review for San Gabriel Valley Area 4 Superfund Site Source: EPA, 2021.

Figure 2. Detailed Map of San Gabriel Valley Area 4
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p-SlnGabn IVa.lley(Ar 4),Puen VIJ yOpera. lHt
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Third Five-Year Review for San Gabriel Valley Area 4 Superfund Site 7 Source: EPA, 2021.

Figure 3. San Gabriel Groundwater Basin
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T M
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City of Industry, California
PCE Iso-concentration Map
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T IT L E:

L O CAT IO N:

APPRO V ED

DRAFT ED
PRO JECT #
DAT E

FIGU RE
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NS = Not Sa m pled (in sufficien t wa ter level/ In oprea b le extra ction well) ?@ Groun dwa ter Mon itorin g Well
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MARICI BATTERY ENERGY STORAGE SYSTEM FACILITY INITIAL STUDY / MITIGATED

NEGATIVE DECLARATION

CITY OF INDUSTRY

APPENDIX
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MARICI BATTERY ENERGY STORAGE SYSTEM FACILITY INITIAL STUDY / MITIGATED

NEGATIVE DECLARATION

CITY OF INDUSTRY

APPENDIX
OCTOBER 2025

APPENDIX L

HAZARDOUS MATERIALS AND SAFETY

MEMORANDUM

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NEGATIVE DECLARATION

CITY OF INDUSTRY

APPENDIX
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ATTACHMENT K
Hazardous Materials and Safety
Memorandum
L-1

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L-2

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1 MEMORANDUM
To: Geoff Forner, Aypa Power Development LLC
From: Joe Stenger and Chris Andrews, TRC
Date: February 5, 2025
Re: Hazardous Materials Safety Requirements, Marici Project, City of Industry, CA TRC Project No. 604109
The Marici Project is a planned 400-megawatt battery energy storage system (BESS) to be constructed on an approximately six-acre parcel in City of Industry, California. The project will utilize lithium-ion battery energy storage technology with batteries in purpose-built outdoor containers to store energy from the grid and discharge it back into the grid when needed. The battery energy storage operation does not generate electricity and does not generate any emissions to air, land, or water. Operation of lithium-Ion battery energy storage facilities require few hazardous materials. Hazardous materials expected to be needed include mineral oil, coolant and refrigerant. In addition, the backup generator will have a fuel tank and lubricating oil. Lithium-ion batteries also contain hazardous materials and spent or damaged batteries can fall under hazardous or universal waste management regulations.

This memorandum has been prepared to identify applicable regulations and consensus standards applicable to BESSs for use and storage of hazardous materials, fire prevention and protection, safety, and emergency response preparedness. These requirements will need to be integrated in Project planning and execution to comply with existing regulations and standards. Key regulatory requirements include, but are not limited to, the following as further described below:
• Federal and State requirements for Hazardous Chemical Inventory Reporting and Emergency Response Planning;
• Federal and State requirements for preventing spills; • Federal and State requirements for employers to protect worker health and safety; • Federal and State requirements for management of hazardous waste; • National Fire Protection Association (NFPA) 855 standards for Battery Energy Storage Systems; • State requirements for BESS Emergency Planning;
• State and local fire authority requirements; and
• Water quality protection requirements.

Hazardous Chemical Inventory Reporting and Emergency Response Planning Section 311 in the Federal Emergency Planning and Community Right-to-Know Act (EPCRA) requires facilities that have hazardous chemicals to report the presence of such chemicals onsite to the State and local emergency planning committees (LEPC) if the chemicals are present above threshold quantities. In California, these requirements and additional hazardous material reporting requirements are implemented through California Code of Regulations(CCR) Title 19 Division 5, Chapter 1 (Section 5030.1 et seq). Under these regulations, the project will be required to maintain an inventory of all hazardous materials onsite in a quantity equal to or greater than 500 pounds, 55 gallons, or 200 cubic feet (STP) for gas or exceeding any federal threshold planning quantity in 40 CFR Part 355. The inventory will need to be submitted to Certified L-3

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2 Unified Program Agency and the local fire authority via online filing and must be updated annually and within 30 days of changes. The hazardous materials inventory must identify all hazardous materials onsite above threshold quantities and provide common and chemical name, Chemical Abstract Service Number, map location, quantity stored, type of container, largest container quantity, storage temperature and pressure information and hazardous properties. The inventory is designed to provide emergency response agencies with the information needed to be prepared for prompt and appropriate response to a potential hazardous materials incident. The submittal also must include emergency response plans and procedures including immediate notification of local emergency response personnel and procedures for mitigation, prevention, and abatement of hazards to persons, property or the environment. Title 19 Division 5 Chapter 1 regulations also require a training program including initial and annual refresher training for safe handling of hazardous materials, procedures for coordination with local emergency response agencies, use of onsite emergency response equipment and supplies. Such training helps to minimize the potential for hazardous materials incidents and to ensure prompt and appropriate response in the event of an incident.

Oil Spill Prevention and Preparedness
Oil-filled transformers will be subject to Code of Federal Regulations Title 40 Part 112 and California Health and Safety Code Chapter 6.67 requirements for development and implementation of a Spill Prevention Control and Countermeasures Plan (SPCC) including secondary containment for aboveground bulk oil storage containers, routine inspections for oil containment integrity and ensuring collected stormwater is oil-free before it is released, and contingency planning for prompt and appropriate response to a potential release. SPCC requirements would also apply to a back-up generator fuel tank and if a temporary bulk fuel tank is provided onsite during construction. The requirements in these regulations are designed to minimize the potential for an oil spill from equipment to impact waters.

Federal and State Occupational Safety and Health
Federal and State OSHA regulations require that all employees be informed and trained on hazardous materials in their work area at the time of their assignments. These are comprehensive regulations designed to protect worker health and safety and by doing so helping to minimize the potential for a hazardous material incident and ensure training for prompt and proper response to a potential hazardous materials incident. CCR 5194 requires manufacturers or importers to classify the hazard of chemicals that they produce or import and requires all employers to provide information to employees about the hazards of chemicals to which they may be exposed. A written hazard communication program must be maintained at the workplace including a list of hazardous chemicals, a Safety Data Sheet for each hazardous chemicals, comprehensive labeling and communication procedures for hazardous chemicals, training methods, and precautionary procedures to protect employees during normal operations and in the event of an emergency.

Comprehensive training and precautionary procedures required by these regulations help to minimize the chance of a hazardous chemical spill or other human error hazardous chemical event. CalOSHA General Industry Safety Orders (Section 3220 et seq.) includes standard specifications for an Emergency Action Plan that employers must develop to keep employees safe from fire and other emergencies. Required components include redundant alarm systems, emergency reporting, procedures for emergency evacuation and continued operation of critical elements, emergency contacts, and training.

Hazardous Waste Requirements
The Project may generate small quantities of hazardous waste subject to regulation under CCR Title 22, Division 4.5 and would be expected to meet the criteria for Small Quantity Generator. State regulations in CCR Title 22 Division 4.5 require facilities generating hazardous waste to have preparedness and prevention measures in place for emergency response minimizing the potential for a release of hazardous L-4

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3 waste and to support prompt and appropriate response in the event of an incident including internal communications or alarm systems, fire control, spill control and decontamination equipment, fire suppression water systems, and posted emergency information. Hazardous waste Generators are required to ensure that employees are trained and knowledgeable on emergency procedures and to attempt to make arrangement with local emergency responder appropriate for the wastes managed.

National Fire Protection Association (NFPA) 855 – Battery Energy Storage Systems The 2023 revisions to NFPA 855 are designed specifically to mitigate risks of fire and explosion for battery energy storage systems. The NFPA 855 requirements are incorporated in the International Building Code (IBC) requirements applicable to the Project via California Building Code. The NFPA 855 also requires and outlines the requirements for the following:
• Permits
• Hazard Mitigation Analysis (HMA)
• Fire Risk Assessment (FRA).
• Emergency response plan (ERP)
• Inspection, testing and maintenance of fire protection systems.

Containers would be spaced in accordance with NFPA 855 requirements that are designed to minimize risk of a fire spreading to adjacent containers so that if a fire occurs, it can be isolated. NFPA 855 also would require comprehensive safety planning submittals to the local fire authority having jurisdiction including results of bench-scale fire and explosion testing by the manufacturer and hazard mitigation analysis for the specific type of battery used, and an Emergency Response Plan designed to ensure well-planned, prompt, safe, and appropriate response in the event of an emergency. These submittals would be made to the Fire Department after the specific equipment is selected and prior to issuance of building permits. NFPA 855 mandates initial and annual refresher emergency response training for facility staff. The Project should coordinate with the Fire Department during construction and operations to facilitate site-specific Fire Department staff training.

State Requirements for BESS Emergency Planning
California SB 38, passed in 2023, requires BESS facilities to develop Emergency Response and Emergency Action Plans that:
• Establish response procedures for an equipment malfunction or failure; • Provide for the safety of surrounding residents, neighboring properties, emergency responders, and the environment through procedures established in consultation with local emergency management agencies; and
• Establish notification and communication procedures between the facility and local emergency management agencies.

The Los Angeles County Fire Department is the Certified Unified Program Agency (CUPA) in the City of Industry and has jurisdiction for permitting the battery energy storage under NFPA 855 and will require the information needed for consistency with SB 30 and other emergency planning requirements for BESS prior to operations.

State and Local Fire Authority Requirements
The project will be required to comply with State building and fire code requirements and Los Angeles County Fire Code. Los Angeles County Fire Code adopts the California Fire Code and International Fire Code by reference. These codes include comprehensive regulations regarding all conditions affecting the L-5

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4 safety of fire fighters and emergency responders during emergency operations and required fire hydrant systems, water supply, fire equipment access, combustible materials controls, flammable liquid storage controls, and other requirements for fire and explosion prevention (LACFC Title 32, Section 101.2). Los Angeles County Fire Code section 1207 contains safety requirements specifically for energy storage systems and requires that project proponents obtain both a construction permit and an operating permit for lithium-ion energy storage systems of 20 kWh or more. Additional BESS design standards are under development by Los Angeles County Fire Department and the fire department will be responsible for fire safety plan reviews and inspections and will enforce the fire code. The Fire Departments authority over permitting and enforcement authority for the Fire Code, SB 38, CCR Title 19, and NFPA 855 will ensure integrated emergency prevention and emergency response planning and preparation across each of these requirements and that such measures are satisfied prior to operations.

Water Quality Protection Requirements
The Clean Water Act is implemented in California through the Porter Cologne Water Quality Control Act and both State and federal regulations include requirements designed to ensure that hazardous materials do not pose a threat to water quality. During construction, the project will need to comply with the State General Permit for stormwater discharges from construction sites as described further below. During operations, the project will need to implement and maintain engineering and other best management practices required under the Los Angeles County Municipal Separate Storm Sewer System (MS4) permit as described further below.

Construction NPDES
Because construction will disturb more than one acre, the Project will be required to apply for and comply with the State General Permit for stormwater discharges from construction sites. For coverage under the permit, the Project will need to submit a Storm Water Pollution Prevention Plan (SWPPP) with best management practices to be implemented to prevent stormwater pollution. Construction best management practices include storage and use of hazardous materials under safeguards to prevent releases to soil or water. Precipitation or runoff contact with hazardous materials must be prevented through engineering and other best management practices. The Regional Water Quality Control Board has jurisdiction for review of SWPPPs and implemented BMPs and will acknowledge coverage under the State General Permit upon demonstration of an appropriate SWPPP and other permit registration documents.

Operations MS4 Compliance
Operations requirements for the project also include best management practices for prevention of stormwater pollution. These measures include proper waste management to prevent contact with runoff, and storage and handling hazardous materials following measures to prevent spills or other releases that could be contacted by precipitation or runoff.

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MARICI BATTERY ENERGY STORAGE SYSTEM FACILITY INITIAL STUDY / MITIGATED

NEGATIVE DECLARATION

CITY OF INDUSTRY

APPENDIX
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MARICI BATTERY ENERGY STORAGE SYSTEM FACILITY INITIAL STUDY / MITIGATED

NEGATIVE DECLARATION

CITY OF INDUSTRY

APPENDIX
DECEMBER 2025

APPENDIX M

PLUME STUDY

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MARICI BATTERY ENERGY STORAGE SYSTEM FACILITY INITIAL STUDY / MITIGATED

NEGATIVE DECLARATION

CITY OF INDUSTRY

APPENDIX
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Marici
Plume Study
HD-24045-Marici-Plume-1.3
August 14, 2025
Prepared for:

Marici Project LLC
By:

Anna Jensen
Erik Archibald, Ph.D. P.E.

Kevin Marr, Ph.D. P.E.

Hazard Dynamics LLC
PO Box 1967
Pflugerville, TX 78691 USA
This report is confidential and contains proprietary information.

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Contents
1 Executive Summary 2
2 Introduction 3
3 Background on Lithium-Ion ESS Toxicity Hazards 3

3.1 Toxicity Hazards . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3

3.2 Toxic Gases of Interest . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4 4 Site and System Descriptions 5

4.1 Site Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5

4.1.1 Typical Wind Conditions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6

4.2 Energy Storage System Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7 5 UL 9540A Test Results 10

5.1 Cell Test . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11

5.2 Module Test . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12

5.3 Unit Test . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15 6 Fire and Toxicity Modeling 17

6.1 Model Setup . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 19

6.2 Plume Toxicity Results . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 19

6.3 Flammable Gas Plume . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 27 7 Emergency Response Considerations 29
8 Conclusion 31
9 Limitations 34
References 36
A Appendix 37
B Revisions 37
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1 Executive Summary
A plume study was conducted for the Marici BESS (battery energy storage system) site to determine toxicity and flammability hazards posed to nearby areas during possible battery failure scenarios. The study considers toxic species that can be released by Li-ion batteries during thermal failures. Accumulation of flammable battery vent gas outside a failing BESS enclosure is also considered. Computational fluid dynamics (CFD) models were utilized to simulate plumes resulting from theoretical battery failure scenarios. The modeled scenarios considered (1) a nonfire scenario in which battery vent gas is released, (2) a small fire scenario, and (3) a large fire scenario. Low and high wind conditions were evaluated based on nearby meteorological data.

Based on the modeled scenarios, toxic gas species concentrations 2 m (6.6 ft) from ground level and flammable gas accumulation surrounding the BESS enclosure were estimated using Fire Dynamics Simulator (FDS), which is a CFD software developed by the National Institute of Standards and Technology (NIST) for fire modeling. This software has also been extensively validated for gas dispersion. A summary of the findings of the study is as follows:
• The large fire, high wind condition was found to result in the highest battery plume concentrations 2 m (6.6 ft) above ground level for much of the modeled distance downwind of the enclosures. The modeled average carbon monoxide concentrations may cause serious health effects (exceed the AEGL-2 level) up to approximately 5.8 m (19 ft) from the unit in a large fire scenario with high winds. The 99th percentile wind speed of 15 mph was used to model the high wind scenarios for the Marici site. For first responders who may be operating within this region, guidance for appropriate personal protective equipment (PPE) can be found in relevant Emergency Response Protocol (ERP) documents. • Modeled carbon monoxide levels may exceed the AEGL-2 limit (150 ppm) at 2 m (6.6 ft) above ground level beyond the masonry wall in high wind conditions in areas where the wall is less than 5.8 m (19 ft) from the BESS enclosures. Concentrations at the AEGL-2 level may cause serious health effects.
• The high-wind gas release scenarios (with no fire) resulted in the greatest modeled distances for the OSHA PEL (8-hour average) and EPA NAAQ (1-hr) levels of carbon monoxide.

The worst-case distances were 42 ft and 50 ft, respectively. • Modeled unit gas release scenarios with an active NFPA 69 ventilation system did not result in flammable regions of battery vent gas outside the enclosure. The ventilation system diluted the gas such that it remained below the lower flammability limit (LFL). • Over 600 houses are located within a half-mile of the Marici site. The nearest residential property is 111 ft away from the BESS enclosure at the edge of the site. At these distances, CO levels are expected to be below the EPA NAAQ (1-hr) level of 35 ppm. • Hydrogen fluoride (HF) levels were not evaluated as HF was not measured during the UL 9540A testing for this system. HF has been measured in laboratory-scale battery thermal runaway tests; however, the range of reported measurements is wide. Thus, hydrogen fluoride may be a risk, but the exact magnitude of this risk is unknown. Hydrogen fluoride is highly reactive with a range of materials including metals and various organic compounds. It is unclear whether substantial HF concentrations persist at a distance away from larger module, rack, and ESS scales. HF can also be emitted from the combustion of plastic components in the ESS, such as wiring insulation and module or rack enclosure casings. Although these plastics are commonly fire-retarded, fire-retardant plastics can be overwhelmed if the severity of the fire is sufficiently large. Similar fire-retardant plastics are commonly found in non-battery applications and may pose similar emission hazards during fire conditions.

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• Other toxic organic gases, such as volatile organic compounds (VOCs) make up only trace amounts of the battery vent gas. VOC release quantities are too small to exceed hazardous levels at any distance from the unit.

Note that this Executive Summary does not contain all of Hazard Dynamics’ technical evaluations, analyses, conclusions, and recommendations. Hence, the main body of this report is at all times the controlling document.
2 Introduction
This report describes the results of a plume dispersion study conducted for the Marici battery energy storage system (BESS), which is being built in City of Industry, California. The Marici site uses the Sungrow PowerTitan 2.0 for lithium-ion battery energy storage. The purpose of a plume study is to identify and quantify potential risks associated with toxic and flammable gases produced by a battery energy storage system (BESS) under abnormal conditions.

Where appropriate data is unavailable, reasonable engineering assumptions will bemade. These assumptions will be drawn from the available body of technical literature. This analysis was conducted using a set of probable worst-case scenarios based upon available test data such as UL 9540A reports and includes up to a fully-involved fire in a single unit.

This report will first provide background on the toxicity hazards of lithium-ion battery systems.

Next, it will review the details of the Marici site as well as the energy storage system itself. Finally, the report will evaluate possible toxic and flammable gas scenarios and their consequences.

This analysis relies on the following information:
• Plans for the Marici site [1]
• Specifications for the PowerTitan 2.0 system [2]
• UL 9540A Cell test report for cell model L173F314, CSA Group – Kunshan Branch report number 80184345 dated 11/17/2023 [3]
• UL 9540A Module test report for module model P1044AL-AHA, TUVRheinland (Shanghai) Co., Ltd. report number CN23P68X 001 dated 12/16/2023 [4] • UL 9540A Unit test report for unit model applies to various R0417BL and R0835BL unit configurations, TUVRheinland (Shanghai) Co., Ltd. report number CN23JPBV 001 dated 12/16/2023 [5]
• CFD Heat Flux Modeling Report and NFPA 69 CFD Analysis for the Sungrow PowerTitan

2.0 [6] [7]
3 Background on Lithium-Ion ESS Toxicity Hazards

3.1 Toxicity Hazards
Toxicity hazards may exist alone or in combination with fire and explosion hazards. A significant amount of the gas released during thermal runaway is carbon monoxide (CO), which is toxic. Depending on the conditions, the combustion of battery gases may burn off some carbon monoxide or create additional carbon monoxide from partially reacted hydrocarbons. Smaller amounts of other toxic gases may also be released depending on the cell, whether the gases burn, and if water or other suppression agents are added. Experiments show that lithium-ion cells in thermal runaway may release hydrogen fluoride (HF), hydrogen chloride (HCl), hydrogen cyanide (HCN), nitrogen dioxide (NO2), sulfur dioxide (SO2), and other gases [8]. When the August 14, 2025 3
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gases burn, some of the toxic components may be consumed, although others may be generated. Smoke from many fires, including battery fires, is considered hazardous. Smoke typically includes asphyxiant gases, irritant toxic gases, and particulate matter. The introduction of water to a fire may change the composition of the smoke and can create water runoff, which may also contain hazardous substances. The use of other fire suppression agents may also alter the toxic release profile [9].

3.2 Toxic Gases of Interest
Abuse and failure of lithium-ion cells may result in gas production inside of the cells. When enough gas is produced, a safety vent may open, or the cell package may rupture. The gas mixture released is flammable and toxic and is primarily made up of carbon monoxide (CO), carbon dioxide (CO2), hydrogen (H2), and an assortment of hydrocarbons. If ignited, the combustion of these gases can lead to a fire or an explosion.

When a lithium-ion cell is exposed to high temperatures such as those due to fire exposure or propagating thermal runaway, it produces toxic compounds. Plastic contained in the battery system may contribute to these toxic combustion products. Such products may include carbon monoxide (CO), nitrogen oxides (NOx), sulfur dioxide (SO2), hydrogen chloride (HCl), and hydrogen fluoride (HF). The quantity of HF produced is related to the electrolyte solvent and the chemical reactions initiated. CO2, H2, and CH4 are asphyxiant gases, or gases that can cause unconsciousness or death by suffocation because they displace oxygen in the air [8]. CO blocks the transport of oxygen by sticking to the hemoglobin in red blood cells. Poisoning by CO is often the major cause of death related to fire in which burns are not present [10]. Hydrogen cyanide (HCN) obstructs the function of mitochondria so that oxygen cannot be absorbed into the cells. Irritant gases include HF, HCl, SO2, and NO2. These gases have a toxic and irritating effect that can be significant even at very low concentrations. HCl is corrosive, highly irritating, and can cause severe injury to the respiratory tract if inhaled. SO2 is extremely irritating and can form sulfurous acid when in contact with moisture. NO2 and NO are especially irritating to the respiratory tract and lungs even at low concentrations. None of these irritants can be absorbed through the skin. HF, on the other hand, is not only severely irritating to the respiratory tract but can also penetrate skin and other tissues as the fluoride ion. When HF comes into contact with moisture, it can form hydrofluoric acid [11].

In evaluating harmful levels of toxic gases, it is helpful to reference levels known as IDLH (immediately dangerous to life or health) and AEGLs (acute exposure guideline levels). According to the Code of Federal Regulations, IDLH is defined as a concentration of any toxic, corrosive, or asphyxiant substance that poses an immediate threat to life, would cause irreversible or delayed adverse health effects, or would interfere with an individual’s ability to escape from a dangerous atmosphere [11]. IDLH values were developed to address occupational exposures to chemicals and to help protect workers from acute or short-term exposures to high concentrations of some airborne chemicals that could result in undesirable health outcomes [12]. The AEGLs were developed by the EPA to define the health effects of a once-in-a-lifetime exposure to airborne chemicals. AEGLs are used by emergency responders when dealing with major chemical leaks, spills, or other exposures. AEGL concentrations are provided for different exposure times and health effect levels. Level 1 is discomfort or irritation, Level 2 is the onset of irreversible or serious health effects, and Level 3 describes life-threatening health effects [13]. Toxic gases related to battery energy storage systems along with their IDLH, AEGL-2, and AEGL-1 concentrations are shown in Table 1. The AEGL values presented in the table are based on an exposure time of 30 minutes, which is characteristic of how long someone evacuating might be exposed to a substance.

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Table 1: Toxic chemicals that can be present during battery failure and concentrations of interest. The AEGL values shown are for a 30-minute exposure. (NR = Not recommended due to insufficient data) Chemical IDLH (ppm) AEGL-3 (ppm) AEGL-2 (ppm) AEGL-1 (ppm) Carbon Monoxide (CO) 1,200 600 150 NR
Carbon Dioxide (CO2) 40,000 NR NR NR
Hydrogen Chloride (HCl) 50 210 43 1.8
Hydrogen Cyanide (HCN) 50 21 10 2.5
Hydrogen Fluoride (HF) 30 62 34 1
Nitrogen Dioxide (NO2) 13 25 15 0.50
Nitric Oxide (NO) 100 NR NR NR
Sulfur Dioxide (SO2) 100 30 0.75 0.20
Benzene (C6H6) 500 5,600 1,100 73
Toluene (C6H5CH3) 500 5,200 760 67
4 Site and System Descriptions

4.1 Site Description
The Marici project is a lithium-ion BESS facility that will be located in City of Industry, California.

The site will be about 17 miles east of downtown Los Angeles. The location of the site can be seen in Figure 1.

Figure 1: A map showing the location of the Marici site. This image was taken from Google Maps 2025.

The Marici project includes lithium-ion battery energy storage equipment made by Sungrow.

Over 600 houses are located within a half-mile of the Marici site. The nearest residential property is 111 ft away from the BESS enclosure at the edge of the site. The site and its close surroundings are shown in Figure 2. Nearby exposures and their approximate distances from the BESS are also shown in Figure 2.

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Figure 2: A satellite view of the Marici site location and its surroundings with the site drawing overlaid. The distances shown are measured from the nearest BESS enclosure. This image was taken from Google Earth 2025.

4.1.1 Typical Wind Conditions
In case of a toxic gas release, it is expected that the impacted area would be downwind of the site. The closest weather station for historical data is the San Gabriel Valley Airport site. According to historical wind information from 1985-2024, the prevailing winds generally come from the south-southwest (see Figure 3). The average wind speed is 6.9 mph or 3.08 m/s. Peak wind speeds may exceed 20 mph or 8.9 m/s approximately 0.284% of the time. Conditions are calm

20.1% of the time [14]. Because only a small percentage of winds exceed 20 mph, wind data was further analyzed to find the 99th percentile wind speed for use in the plume model. This wind speed was found to be 15 mph or 6.7 m/s.

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Figure 3: The wind rose for the San Gabriel Valley Airport weather station, which is the closest available station to the Marici site. This image was taken from the Iowa State University Iowa Environmental Mesonet website [14].

4.2 Energy Storage System Description
The Marici project uses modular outdoor-rated PowerTitan 2.0 battery units made by Sungrow.

These units contain lithium-ion batteries installed in racks inside the enclosure. Each enclosure contains 6 racks with 8 modules each, for a total of 48 liquid-cooled battery modules. A PCS is underneath each rack [6]. The PowerTitan 2.0 includes a vent panel, heat and smoke detectors, a sound beacon, ventilation system, and flammable gas detector [2]. A PowerTitan 2.0 enclosure is shown in Figure 4.

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Figure 4: An image of a Sungrow PowerTitan 2.0 battery storage system [2] [5].

The PowerTitan 2.0 enclosures include an NFPA 69 ventilation system to expel battery vent gas in case of cell failure. This system is designed to prevent an explosive atmosphere. An inlet louver is located on the left side of the enclosure near the bottom, and an exhaust fan is located on top of the enclosure near the right side (see Figure 5). The exhaust fan activates upon detection of hydrogen gas and expels air and vent gas at a rate of 750 m3/h [7].

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Figure 5: The configuration of the NFPA 69 ventilation system on the PowerTitan 2.0 enclosure [7].

The Marici site will consist of 480 enclosures [1]. The site also includes power conversion systems and other equipment. Figure 6 shows the planned layout of the site.

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Figure 6: An engineering drawing indicating the planned layout of the Marici site, including the battery enclosures, power conversion systems, and other equipment [1].
5 UL 9540A Test Results
This analysis is based on test data from UL 9540A cell, module, and unit test results. During this testing, a cell is forced into thermal runaway while the outcome is observed. Gases released from the battery or batteries during thermal runaway are captured and analyzed for select chemical species. Depending on the outcome of cell-level testing, additional testing at the module level and full unit level may also be required. For this plume analysis, UL 9540A data from cell-level [3], module-level [4], and unit-level [5] testing was reviewed. The results of these tests are described in Sections 5.1-5.3.

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Since UL 9540A is primarily concerned with fire and explosion hazards, typical UL 9540A gas measurements are focused on major combustible gases and combustion products, such as hydrogen, carbon monoxide, carbon dioxide, and various hydrocarbons. Typically, carbon monoxide is the most significant toxicity hazard among the measured gases due to a comparatively low IDLH value and relative abundance in most battery gas. The UL 9540A test report for the CALB Group Co., Ltd. cells indicates that 192 L of gas was captured from a single cell. Of the gas captured, 13.924% by volume was carbon monoxide. This information, along with the remaining composition information, is listed in Table 3.

Cell-level gas composition information is collected by failing an individual cell inside of a sealed pressure vessel that is filled with an inert gas to prevent combustion. This method allows for the capture of the entire volume of emitted gas. Gas compositions from cell experiments are usually measured using a gas chromatograph (GC), which is typically more accurate than measurements taken from exhaust hoods during module and unit testing.

5.1 Cell Test
The system under consideration is comprised of CALB Group Co., Ltd. L173F314 cells, which are 314 Ahr lithium-ion LFP cells [3]. This cell was tested using the UL 9540A method. The results are given in the CSA Group – Kunshan Branch report 80184345 dated 11/17/2023. Figure 7 shows a cell during testing.

Figure 7: A CALB Group Co., Ltd. L173F314 cell during testing. This image was taken from the UL 9540A cell-level test report [3].

For UL 9540A testing, the L173F314 cells were heated until failure occurred. Cell details and results from UL 9540A testing are provided in Table 2.

The UL 9540A cell report showed that the cells go into thermal runaway and release a mixture of flammable gases when heated externally until failure. The vent gas composition from the UL 9540A cell report is listed in Table 3.

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Table 2: Key cell properties from the UL 9540A cell test [3].

Parameter Value
Cell Manufacturer CALB Group Co., Ltd.

Cell Model L173F314
Cell Chemistry LFP
Cell Nominal Voltage 3.2 V
Cell Capacity 314 Ahr
Volume of Gas Released 192 L
Lower Flammability Limit (LFL) at ambient temperature 6.2% Lower Flammability Limit (LFL) at venting temperature 5.6% Burning Velocity (Su) 63.8 cm/s
Maximum Pressure (Pmax) 0.68 MPa
Table 3: The gas composition from the UL 9540A cell test [3]. Model Volume Percent will be addressed in Section 6 later in this document.

Name Formula Experimental Model
Volume Percent Volume Percent
Carbon Monoxide CO 13.924 13.924
Carbon Dioxide CO2 27.237 27.237
Hydrogen H2 44.925 44.925
Methane CH4 6.421 6.421
Acetylene C2H2 0.339 0
Ethylene C2H4 3.827 3.827
Ethane C2H6 0.996 0.996
Propylene C3H6 1.227 0
Propane C3H8 0.322 2.670
C4 Total C4H10 0.651 0
C5 Total C5H12 0.131 0

5.2 Module Test
The CALB Group Co., Ltd. cells are located inside of module model P1044AL-AHA. A module was also tested using the UL 9540A method, and the results can be found in TUVRheinland (Shanghai) Co., Ltd. test report CN23P68X 001 dated 12/16/2023. Each module contains 104 cells in a 104S configuration [4]. Multiple thermocouples were attached for testing as seen in Figure

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Figure 8: A module prepared for the UL 9540A test. This image was taken from the UL 9540A module-level test report [4].

Heaters were placed between cells 2, 3, and 4 in submodule 1, which was chosen due to its central location within the module. A diagram of the module construction is shown in Figure 9, and the locations of the thermocouples and initiating cells and can be seen in Figure 10. The temperature time history for the test is shown in Figure 11.

Figure 9: A diagram of the P1044AL-AHA module. This image was taken from the UL 9540A module-level test report [4].

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Figure 10: A diagram of the module setup for the UL 9540A test. This image was taken from the UL 9540A module-level test report [4].

Figure 11: The temperature time history for the initiating cell from the UL 9540A module test. This image taken was from the UL 9540A module-level test report [4].

The initiating cells were heated until thermal runaway occurred. The three initiating cells went into thermal runaway and propagated to two other cells, making five cells in total that failed in thermal runaway [4]. Sparks, flying debris, and external flaming were not observed during the test. Figure 12 shows the module after the test.

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Figure 12: The module after the UL 9540A test. This image was taken from the UL 9540A module-level test report [4].

5.3 Unit Test
The UL 9540A unit test applies to various R0417BL and R0835BL unit configurations and is described in TUVRheinland (Shanghai) Co., Ltd. report CN23JPBV 001 dated 12/16/2023. In this test, a unit comprised of four modules was tested. The unit contained 416 individual cells [5]. The initiating module was configured identically to the module test. This module was then inserted into a full unit, which was placed in proximity to walls and target units. The configuration of the initiating unit is shown in Figure 13, a diagram of the test setup is shown in Figure 14, and a picture of the initiating unit is shown in Figure 15.

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Figure 13: The initiating unit with the initiating module, target modules, and target unit labeled. This image was taken from the UL 9540A unit-level test report [5].

Figure 14: A diagram of the unit test setup. This image was taken from the UL 9540A unit-level test report [5].

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Figure 15: A picture of the initiating unit. This image was taken from the UL 9540A unit-level test report [5].

Thermal runaway was initiated by activating the heaters on cells 2, 3, and 4 in submodule 1 in the initiating module. Once thermal runaway began, the power to the heaters was disconnected.

The three initiating cells went into thermal runaway and propagated to two other cells, making a total of five failed cells inside the initiating module [5]. Thermal runaway did not propagate outside of the initiating module. Flaming, sparks, and flying debris were not observed. 6 Fire and Toxicity Modeling
Hazard Dynamics used data from the UL 9540A test reports to conduct plume modeling for a number of different failure scenarios. These models included cases of varying wind conditions, differing levels of failure severity, and with or without burning. Each scenario assumes a steadystate release and was modeled for 300 seconds.

Two different heat release rates (HRR) were used to represent two different sizes of fire. The large HRR of 34.8 MW represents a full enclosure burning. This value was calculated using cell and module information from the UL 9540A cell and module tests [4] [3]. In calculating the peak HRR used for the model, it was assumed that all cells and modules burned over the course of two hours (half an hour ramp up, steady burn for an hour, and half an hour ramp down). Flaming propagation between adjacent enclosures was not modeled as available UL 9540A test data did not demonstrate propagation between modules inside of a unit or between units. The small HRR of 2.2 MW was taken from the Heat Flux Analysis for the PowerTitan 2.0 system [6]. This HRR was used to evaluate the consequences of a smaller fire in which the entire enclosure does not burn. The modeled scenarios are shown in Table 4. The wind speeds used in the models will be discussed in Section 6.1.

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Table 4: Marici fire plume model scenarios.

Name Wind Speed Mass Release Rate HRR
(m/s) (kg/s) (MW)
Small Fire, Low Wind 1.5 0.147 2.2
Small Fire, High Wind 6.7 0.147 2.2
Large Fire, Low Wind 1.5 2.32 34.8
Large Fire, High Wind 6.7 2.32 34.8
The non-fire scenarios model the release of lithium-ion battery vent gas in the absence of burning. Multiple battery vent gas release scenarios were used to model varying levels of thermal runaway propagation. These scenarios include the average module gas release based on the UL 9540A module test, the peak module gas release rate, the maximum gas release rate the NFPA 69 ventilation system can handle before the exhaust exceeds 25% LFL of the battery gases, a gas release rate representative of the failure of a string of batteries, and a gas release rate representative of a full unit failure. These scenarios are summarized in Table 5. Two scenarios consider the average module vent gas release with and without an active ventilation system. For these scenarios, a gas release rate of 0.000387 kg/s was calculated using the overall time cells entered into thermal runaway during the module-level test, the amount of gas released by a single cell during the cell-level test, and the number of cells failed during the module-level test [4] [3]. The calculation can be found in the appendix of this report. This gas release rate approximates the average release rate expected from five cells failing at different times as demonstrated in the module-level test. The peak module gas release rate for the module was taken from the gas release rate profile in the NFPA 69 report by TUV Rheinland [7]. This gas release rate profile shows that the cell failures in the UL 9540A module test did not overlap. Therefore, the highest instantaneous release from one cell was used to represent a worst-case module failure. This peak rate was also used to assess larger failures of a string and a unit. The string failure scenario assumes that two modules are failing at the same time, and the unit failure scenario assumes that four modules fail at the same time. While other modules in a string or unit may also fail, it is unlikely that they would all fail at the same time. Finally, the 25% LFL gas release scenarios were based on the NFPA 69 ventilation system flow rate of 750 m3/h and an LFL of 6.2% [7] [3].

Table 5: Marici battery vent gas plume model scenarios.

Name Wind Speed Mass Release Rate
(m/s) (kg/s)
Average module gas release, no ventilation 1.5 0.000387 Average module gas release, NFPA 69 ventilation 1.5 0.000387 Peak module gas release, NFPA 69 ventilation 1.5 .0015
Peak module gas release, NFPA 69 ventilation 6.7 .0015
25% LFL release, NFPA 69 ventilation 1.5 .00273
25% LFL release, NFPA 69 ventilation 6.7 .00273
String gas release, NFPA 69 ventilation 1.5 .0030
String gas release, NFPA 69 ventilation 6.7 .0030
Unit gas release, NFPA 69 ventilation 1.5 .0060
Unit gas release, NFPA 69 ventilation 6.7 .0060
For modeling purposes, the most significant components which account for more than 95% of the gas are modeled in the non-fire gas release mixture, while minor hydrocarbon elements are approximated as propane. The volume percents used in the model can be found in column four of Table 3.

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6.1 Model Setup
Computational fluid dynamics (CFD) models of possible toxic and flammable plumes were created using Fire Dynamics Simulator (FDS) version 6.9.1. Fire Dynamics Simulator is a CFD software developed by the National Institute of Standards and Technology (NIST) for fire modeling.

The code solves the Navier-Stokes equations using a large-eddy-simulation (LES) approach and is mainly intended for low-speed flows with an emphasis on smoke and heat transport from fires. The code has been extensively validated for a variety of scenarios involving fire, smoke, gas dispersion, and other transport phenomenon. For toxic plume modeling, the model uses grid sizes ranging from 0.25 m (9.8 in) to 2 m (6.6 ft) to capture both the flow near the source (starting 2 m from the enclosure) as well as the dispersion over a large flat downwind area up to 320 m (1050 ft) away from the source as shown in Figure 16. For flammable plume modeling, a smaller, more refined mesh was used, as the flammable region is expected to impact only the near-field region immediately around the BESS enclosure. The refined mesh for these models extends 5 m (16.4 ft) from the enclosure and uses a 0.1 m grid size.

Figure 16: The toxic plume model with the grid displayed. The grid varies in size from 0.25 m near the unit to 2 m starting 40 m away from the unit. The model for flammable plume modeling only includes the portion of the model immediately around the enclosure with a mesh size of 0.1 m.

The EPA Risk Management Program recommends using a wind speed of 1.5 m/s (3.4 mph) and atmospheric stability class F conditions (stable atmosphere) for worst-case plume analysis for accidental chemical releases [15]. This wind speed was used in the model as well as the 99th percentile wind speed for the Marici site, which is roughly 6.7 m/s or 15 mph (see Figure 3). High wind speeds may act to partially overcome the upward tendency of a fire plume. The results presented here approximate worst-case results based on the wind speeds modeled and using stable atmospheric conditions with an Obukhov length of 350 meters. Because the Marici site is in a suburban area, a closed Davenport-Wieringa roughness length of 1.0 m was used.

The wind speeds used in the models are intended to be worst-case. Therefore, results from other wind speeds are expected to be bounded by the wind speeds used. Likewise, modeling a stable atmosphere, in which released gases would tend to stay near ground-level, is considered worst-case. Stable conditions may include fog, because the stability prevents vertical movement of the moist air near the ground. The moisture in fog conditions is not expected to make a plume resulting from battery vent gas release or a fire any worse. Rain during a BESS failure incident is expected to result in a less severe plume than modeled because the falling water could encourage mixing and dispersion over a wider area.

6.2 Plume Toxicity Results
Results were collected for battery vent gas concentrations (non-fire scenarios) and combustion product concentrations (fire scenarios). The gas concentration of interest was the concentration at 2 m (6.6 ft) above ground level. This corresponds to the concentration that people would experience when standing on level ground near an incident. Figure 17 shows the average vent gas concentrations, and Figure 18 shows the average combustion product gas concentrations August 14, 2025 19
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at 2 m (6.6 ft) above ground level at different distances downwind of the unit. Figure 17 shows that vent gas concentrations remain relatively low even near the enclosure and diminish significantly away from the enclosure in scenarios without fire. For the scenarios with fire, overall combustion product concentrations at 2 m (6.6 ft) above ground level remain low with wind speeds of 1.5 m/s (3.4 mph). However, the fire scenarios with high winds speeds result in high combustion product concentrations near the enclosure. These concentrations drop quickly away from the burning enclosure. The modeled high wind speed was 6.7 m/s (15 mph), which is the 99th percentile wind speed at the Marici site. However, since toxic gases are only a fraction of the total battery vent gas or combustion products, toxic gas concentrations would be a fraction of these values.

Figure 17: The average battery vent gas concentration versus the downwind distance for different gas release model scenarios.

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Figure 18: The average combustion products concentration versus the downwind distance for different fire model scenarios.

The trajectory of the battery vent gas coming out of the enclosure in scenarios without burning depends on the size of gas release, whether the ventilation system is active, and the wind speed.

Figure 19 shows an average module gas release with no ventilation, while Figure 20 shows an average module gas release with ventilation. Because the exhaust fan is on top of the enclosure, it lofts the battery gas upward when activated. This results in much of the battery gas being above the 2 m (6.6 ft) level and more rapid mixing of the battery gas with the surrounding air.

Figure 19: The model for an average module gas release scenario with no ventilation and low wind speeds. X_BATTERYGAS is the concentration of battery vent gas in ppm. The distances shown are measured from the front of the enclosure.

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Figure 20: The model for an average module gas release scenario with ventilation and low wind speeds. X_BATTERYGAS is the concentration of battery vent gas in ppm. The distances shown are measured from the front of the enclosure.

The speed of the wind also affects the path and mixing of the battery vent gas expelled from the enclosure. Figure 21 shows a unit gas release under high wind conditions. In this scenario, the vent gas is lower to the ground and disperses more quickly than the low wind unit gas release scenario shown in Figure 22.

Figure 21: The model for a unit gas release scenario with ventilation and high wind speeds. X_BATTERYGAS is the concentration of battery vent gas in ppm. The distances shown are measured from the front of the enclosure.

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Figure 22: The model for a unit gas release scenario with ventilation and low wind speeds. X_BATTERYGAS is the concentration of battery vent gas in ppm. The distances shown are measured from the front of the enclosure.

The fire scenarios with greater wind speeds resulted in higher concentrations of combustion products 2 m (6.6 ft) above ground level. The heat from fire conditions makes gases more buoyant such that they rise away from the ground. In most common wind conditions, fire product concentrations are low at ground level. However, under conditions of high wind, this buoyant effect may be partially overcome. The scenarios with both fire and high winds yielded the highest gas concentrations at the greatest distances. Figure 23 shows the model with a full unit fire at high wind speeds. This figure shows that the hot combustion products do not rise immediately due to high wind conditions, but they do rise gradually. Additionally, mixing occurs as the combustion products move away from the enclosure. In contrast, Figure 24 shows that the combustion products rise immediately under low wind conditions.

Figure 23: The model of a full unit fire with high wind conditions. In this scenario, the combustion products do not rise immediately due to high wind conditions, but they do rise over time while also mixing with air. X_PRODUCTS is the concentration of combustion products in ppm. The distances shown are measured from the front of the enclosure.

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Figure 24: The model of a full unit fire with low wind conditions. In this scenario, the combustion products rise immediately and stay elevated for long distances.

X_PRODUCTS is the concentration of combustion products in ppm. The distances shown are measured from the front of the enclosure.

Figure 25 shows that for a smaller fire with high winds, the combustion products stay near ground level for some distance before mixing occurs. In low wind conditions, combustion products for a small fire also rise but to a lesser degree than for a large fire scenario as shown in Figure

26. Figure 25: The model of a small fire with high wind conditions. In this scenario, the buoyant effects of the hot gas are partially overcome by the high wind such that the combustion products stay near ground level until mixing occurs. X_PRODUCTS is the concentration of combustion products in ppm. The distances shown are measured from the front of the enclosure.

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Figure 26: The model of a small fire with low wind conditions. In this scenario, combustion products rise to a lesser degree than in the large fire scenario. X_PRODUCTS is the concentration of combustion products in ppm. The distances shown are measured from the front of the enclosure.

Although multiple toxic gases may be components of battery vent gas, carbon monoxide (CO) is generally the most abundant toxic gas of concern that is regularly reported as part of UL 9540A testing. The UL 9540A cell test report for the PowerTitan 2.0 listed the carbon monoxide concentration as being 13.924%. This value was used to quantify the amount of carbon monoxide in the non-fire scenario. However, it is unclear what concentration of carbon monoxide may persist through a fire. Carbon monoxide concentration in burned gas is likely to be much lower than in the battery gas, as CO is flammable. Carbon monoxide due to incomplete combustion from the fire can also vary depending on the burning environment. Consequently, Hazard Dynamics estimated what amount of carbon monoxide might be present during a fire event using knowledge from work with many battery systems. The CO production was assumed to be 2% of the combustion products. This estimation was based on the measured combustion product concentration from the FDS models. The average carbon monoxide concentration over the 300 m (984 ft) model domain for the gas release scenarios and the fire scenarios are shown in Figure 27 and Figure 28, respectively.

Many different toxicity levels exist for carbon monoxide. The IDLH (Immediately Dangerous to Life and Health) level, the AEGL-3 (life-threatening health effects) level, and the AEGL-2 (serious health effects) level for a 30-minute exposure were discussed in Section 3.2. The EPA does not provide an AEGL-1 (temporary irritation) concentration for carbon monoxide. The IDLH and AEGL levels were created for short-term exposure to chemicals. Other toxicity levels were created to address long-term exposure. The OSHA Permissible Exposure Limits (PELs) were created to protect workers against health effects resulting from exposure to hazardous chemicals.

Additionally, the EPA National Ambient Air Quality Standards (NAAQs) were created to protect public health from chemical exposure. Table 6 shows the concentration levels for various carbon monoxide toxicity levels as well as the worst-case distance modeled above the toxicity level.

The large fire, high wind scenario was the only scenario with carbon monoxide concentrations that exceeded the IDLH and AEGL levels at 2 m (6.6 ft) above ground level. The unit gas release scenario with high winds resulted in the worst-case distances for the OSHA PEL and EPA NAAQ (1-hr) levels at 2 m (6.6 ft) above ground level. The fire scenarios with low wind remained below all reported toxicity levels at 2 m (6.6 ft) above ground level at all modeled distances.

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Figure 27: Average carbon monoxide concentrations as a function of distance for different battery vent gas release scenarios. The high wind speed modeled was 6.7 m/s (15 mph), which is the 99th percentile wind speed for the Marici site.

Figure 28: Average carbon monoxide concentrations as a function of distance for different combustion product release scenarios. The high wind speed modeled was

6.7 m/s (15 mph), which is the 99th percentile wind speed for the Marici site.

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Table 6: Toxicity levels and worst-case modeled distances for carbon monoxide at 2 m (6.6 ft) above ground level.

Toxicity Level for CO Concentration (ppm) Worst-Case Modeled Distance IDLH 1200 13 ft
AEGL-3 (30-minute) 600 15 ft
AEGL-2 (30-minute) 150 19 ft
OSHA PEL (8-hour average) 50 42 ft
EPA NAAQ (1-hour) 35 50 ft
Hydrogen fluoride (HF) is an acutely toxic gas species whose presence has been reported in some battery failure cases. Due to the high toxicity of hydrogen fluoride at quite low concentrations, it is of growing concern for safety analyses of lithium-ion battery systems. It is well accepted by researchers that a lithium-ion cell can generate HF during thermal runaway. However, HF measurements from large-scale fire tests of ESS are not publicly available. In large-scale ESS fires, hydrogen fluoride production is most likely dominated by the burning of fire-retardant plastics in battery systems rather than by the actual cells. HF generated from the cells can also react with other components such as the module casing or rack structure. In general, the publicly available data on hydrogen fluoride in battery failures remains limited, and the reported quantities vary widely. Amounts of hydrogen fluoride between 0 L/Wh and 0.24 L/Wh have been reported [8]. This indicates that HF could represent a significant percentage of the produced gas or not be present in significant amounts. The manner in which this value depends on cell chemistry, state of charge, or other factors is not well understood. Hydrogen fluoride is highly reactive with a range of materials including metals and various organic compounds. It is unclear whether substantial HF concentrations persist at a distance away from larger module, rack, and ESS scales. Hydrogen fluoride can be emitted from combustion of plastic components in the ESS, such as wiring insulation and module or rack enclosure casings. Although these plastics are commonly fire-retarded, fire-retardant plastics can be overwhelmed if the severity of the fire is sufficiently large. Such fire-retardant plastics are commonly found in nonbattery applications and may pose similar emission hazards during fire conditions. While some testing laboratories will provide HF data, it is not currently required by UL 9540A or other standards currently in use in the United States. Hydrogen fluoride data was not provided for the PowerTitan 2.0 system. It is recommended that additional fire testing be performed in order to quantify what levels of hydrogen fluoride may exist for the PowerTitan 2.0.

Typically, hydrocarbons such as benzene and toluene are the only toxic gas concentrations other than carbon monoxide that are measured as part of the UL 9540A testing process. These do not present significant toxicity hazards compared to carbon monoxide and hydrogen fluoride, as their concentrations in battery gas are usually orders of magnitude less while having generally higher AEGL concentrations than CO and HF. For the CALB Group Co., Ltd. cells, the benzene and toluene concentrations were not reported.

6.3 Flammable Gas Plume
Several thermal runaway (TR) scenarios were considered for the flammable gas plume analysis:
(1) Average TR of a single module, (2) Peak TR of a single module, (3) TR of a string of modules, and (4) TR of a BESS unit. The details of the scenarios can be found in Table 5. The average module thermal runaway scenario without ventilation resulted in a flammable region (battery vent gas concentration above LFL) that extended less than .1 m (4 in) vertically only directly over the exhaust fan (see Figure 29). The same gas release with ventilation did not result in a flammable region due to the dilution of battery gas resulting from air being mixed in by the exhaust fan.

Next, the unit gas release cases were run as bounding scenarios. Neither the low wind nor the high wind unit gas release scenario resulted in the formation of a flammable cloud outside of the enclosure. Again, the battery gas was sufficiently diluted by the NFPA 69 ventilation system August 14, 2025 27
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such that the concentration of battery vent gas did not exceed LFL outside of the enclosure.

Because the unit gas release scenarios did not result in a flammable cloud outside of the enclosure due to the active ventilation system diluting the gas, the active ventilation system will also prevent formation of flammable gas clouds during module and string release scenarios.

However, steady-state analyses, as considered here, are unable to quantify formation of smaller regions of flammable gas that can form due to intermittent or unsteady flow conditions. To qualitatively evaluate formation of these types of flammable gas clouds, battery gas concentrations at 1/2-LFL and 1/4-LFL were also evaluated. The worst-case regions for the unit gas release scenarios are shown in Figure 30. These results are also shown in Table 7. Since the flammable gas cloud is less far reaching than the toxic gas cloud, appropriate setbacks will be dictated by toxic gas plume results.

Figure 29: The worst-case battery vent gas regions for LFL, 1/2-LFL, and 1/4-LFL for an average module gas release without ventilation.

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Industry City CouncilFebruary 12, 2026

Industry City Council
February 12, 2026