Attachment C_ EFGS May 2014.pdf

ENVIRONMENTAL

FINAL GOVERNING STANDARDS

SPAIN

MAY 2014

CNREURAFSWA Environmental

PSC 817 Box 108

FPO AE 09622-0108

+39 081 568-2886

SPAIN Revalidations and Updates

May 2014 Spain FGS i

Revision 0

Revalidations and Updates

IAW DODI 4715.5, paragraph 6.3.6.

Action Date Posted By

Full Revision May 2014 CNREURAFSWA

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SPAIN Table of Contents

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Chapters Page

1 Overview 1-1

2 Air Emissions 2-1

3 Drinking Water 3-1

4 Wastewater 4-1

5 Hazardous Material 5-1

6 Hazardous Waste 6-1

7 Solid Waste 7-1

8 Medical Waste 8-1

9 Petroleum, Oil, & Lubricants 9-1

10 [Reserved] 10-1

11 Pesticides 11-1

12 Historic & Cultural Resources 12-1

13 Natural Resources & Endangered Species 13-1

14 Polychlorinated Biphenyls 14-1

15 Asbestos 15-1

16 [Reserved] 16-1

17 Lead-Based Paint 17-1

18 Spill Prevention & Response Planning 18-1

19 Underground Storage Tanks 19-1

Appendices

Appendix A List of Hazardous Substances & Materials

Appendix B.1 Characteristics of Hazardous Waste

Appendix B.2 Waste Disposal Activities

Appendix B.3 Waste Recovery Activities

Appendix C Determination of Worst Case Discharge Planning Volume

Addendums

Addendum 1 EU List of Hazardous Materials

Addendum 2 European List of Wastes

SPAIN - 1 Overview

May 2014 Spain FGS 1-1

C1. CHAPTER 1

OVERVIEW

C1.1. PURPOSE

The primary purpose of these Final Governing Standards (FGS) is to provide environmental compliance criteria at United States (U.S.) Department of Defense (DoD) installations in Spain.

This document implements DoD Instruction 4715.5, “Management of Environmental

Compliance at Overseas Installations,” dated 22 April 1996, and is based upon DoD 4715.05-G, “Overseas Environmental Baseline Guidance Document” (OEBGD), dated 1 May 2007.

C1.2. APPLICABILITY

C1.2.1. These FGS provide environmental compliance criteria applicable to actions for

DoD Components at installations located in Spain.

C1.2.2. These FGS represent minimum criteria; DoD Components may impose additional criteria provided those policies and directives do not directly conflict with these FGS.

C1.2.3. Activities and installations shall notify the Environmental Executive Agent (EEA) of any directly conflicting DoD Component policies or directives they discover prior to imposing criteria more protective than provided in these FGS.

C1.2.4. Other than required authorizations for certain activities, DoD Components shall not enter into agreements with Spanish authorities at any level that establishes a criterion for compliance with an environmental criterion different than provided in these FGS without the prior written approval of the EEA.

C1.3. EXEMPTIONS

C1.3.1. These FGS do not apply to:

C1.3.1.1. DoD installations that do not have more than de minimis potential to affect the natural environment (e.g., offices whose operations are primarily administrative, including defense attaché offices, security assistance offices, foreign buying offices, and other similar organizations), or for which the DoD Components exercise control only on a temporary or intermittent basis.

C1.3.1.2. Leased, joint use, and similar facilities to the extent that the DoD does not control the instrumentality or operation that a criterion seeks to regulate.

C1.3.1.3. Operations of U.S. military vessels or the operations of U.S. military aircraft, or off-installation operational and training deployments. Off-installation operational

May 2014 Spain FGS 1-2 deployments include cases of hostilities, contingency operations in hazardous areas, and when

U.S. forces are operating as part of a multi-national force not under full control of the United

States. Such excepted operations and deployments shall be conducted in accordance with applicable international agreements, other DoD Directives (DoDDs) and DoD Instructions

(DoDIs), and environmental annexes incorporated into operation plans or operation orders.

However, these FGS apply to support functions for U.S. military vessels and U.S. military aircraft provided by the DoD Components, including management or disposal of off-loaded waste or material.

C1.3.1.4. Facilities and activities associated with the Naval Nuclear Propulsion

Program, which are covered under Executive Order (E.O.) 12344 “Naval Nuclear Propulsion

Program,” and conducted pursuant to 42 United States Code (U.S.C.) 7158.

C1.3.1.5. The determination or conduct of remediation to correct environmental problems caused by the Department of Defense's past activities, conducted in accordance with

DoD Instruction (DoDI) 4715.8, “Environmental Remediation Overseas.”

C1.3.1.6. Environmental analyses conducted under E.O. 12114, “Environmental Effects

Abroad of Major Federal Actions.”

C1.4. DEFINITIONS

For purposes of these FGS, unless otherwise indicated, the following definitions apply:

C1.4.1. Criteria and Management Practices. Particular substantive provisions of the

OEBGD that are used by the EEA to develop these FGS.

C1.4.2. Existing Facility. Any facility and/or building, source, or project in use or under construction before 1 October 1994, unless it is subsequently substantially modified.

C1.4.3. Final Governing Standards. A comprehensive set of country-specific substantive provisions, typically technical limitations on effluent, discharges, etc., or a specific management practice.

C1.4.4. Host Nation. Throughout this document the term “host nation” refers to Spain.

C1.4.5. Local National. A DoD employee hired under Spanish employment conditions, including local subcontractors’ employees.

C1.4.6. New Facility. Any facility and/or building, source, or project with a construction start date on or after 1 October 1994, or a pre-existing facility that has been substantially modified since 1 October 1994.

C1.4.7. Substantial Modification. Any modification to a facility and/or building the cost of which exceeds $1 million, regardless of funding source.

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C1.5. ADDITIONAL INFORMATION

C1.5.1. The DoD Components shall establish and implement an environmental audit program to ensure that overseas installations assess compliance with these FGS at least once every 3 years at all major installations.

C1.5.2. DoDI 4715.4, “Pollution Prevention,” implements policy, assigns responsibility, and prescribes procedures for implementation of pollution prevention programs throughout the

DoD. As a matter of DoD policy, DoDI 4715.4 shall be consulted for particular requirements that apply to activities outside the United States. Pollution prevention shall be considered in developing the criteria and management practices for these FGS. Where economically advantageous and consistent with mission requirements, pollution prevention shall be the preferred means for attaining compliance with these FGS.

C1.5.3. Laboratory analyses necessary to implement these FGS would normally be conducted in a laboratory that has been certified by a U.S. or host nation regulatory authority for the applicable test method. In the absence of a certified laboratory, analyses may also be conducted at a laboratory that has an established reliable record of quality assurance compliance with standards for the applicable test method that are generally recognized by appropriate industry or scientific organizations.

C1.5.4. Unless otherwise specified, all record keeping requirements, including assessments, inspection records, logs, manifests, notices, forms, and formats, are described in

DoD 8910.1-M, “DoD Procedures for Management of Information Requirements.”

C1.5.5. These FGS do not create any rights or obligations enforceable against the United

States, the DoD, or any of its components, nor does it create any standard of care or practice for individuals. Although these FGS refer to DoDDs and DoDIs, it is intended only to coordinate the requirements of those directives/instructions as required to implement the policies found in

DoDI 4715.5. These FGS do not change other DoD or service directives/instructions, or alter

DoD or service policies.

C1.5.6. References to websites that are not controlled by the DoD are intended for informational purposes, solely to facilitate compliance with the existing FGS in this document.

Any other requirement, standard or criteria listed in the website shall not be incorporated by references as a Final Governing Standard. Reference to the website does not establish any obligation to comply with other requirements, standards, or criteria listed in the website.

Referenced websites that are not under the control of the DoD may be changed at any time without notice to the DoD.

C1.6. WAIVERS

C1.6.1. If compliance with an FGS criteria at a particular installations or facilities would seriously impair operations, adversely affect relations with Spanish authorities, or require substantial expenditure of funds at an installation that has been identified for closure or at an installation that has been identified for a realignment that would remove the requirement, a DoD

Component may ask the EEA to waive the particular criteria. See DoD Instruction 4715.5, May 2014 Spain FGS 1-4

Management of Environmental Compliance at Overseas Installations, and EUCOM Compliance

Instruction (ECI) 4804.01, Environmental Security, for complete waiver procedures.

C1.7. AUTHORIZATIONS AND REPORTING

C1.7.1. The Spanish Base Commander is the formal representative of the installation and serves as the liaison with host nation authorities. Any formal interaction or interaction of common (U.S. and Spanish) interest with Spanish authorities shall be conducted with the cognizance of the Spanish Base Commander.

C1.7.2. The DoD Components shall not directly obtain authorizations (including, but not limited to licenses and permits) from Spanish authorities. If an authorization is required, DoD

Components will assist the Spanish Base Commander by providing reports, records or otherwise helping him/her with their liaison duties.

C1.7.3. If the Spanish Base Commander obtains an authorization on behalf of the DoD

Component and the authorization requires a more protective criteria than prescribed in the FGS, the criteria in the authorization shall be the compliance criteria. However, if an authorization allows a less protective criteria, then the FGS will be the compliance criteria unless a waiver is obtained.

C1.7.4. If the installation at issue does not fall under the responsibility of a Spanish Base

Commander, the DoD installation may request clarification from the EEA via the chain of command.

C1.7.5. Contractors performing work for DoD must comply with all Spanish laws and regulations including obtaining all necessary licenses, permits, and/or authorizations.

Notwithstanding the use of contracts, DoD Components and agencies are required to comply with these FGS unless exempted under Section C1.3, Exemptions.

C1.7.6. Certificates obtained from appropriate Spanish authorities (e.g., tank tightness testing) do not fall within the definition of an authorization for which the SBC has responsibility.

Request for such services shall be forwarded directly to the appropriate organizations without involving the SBC.

C1.7.7. Access to Installations & Information by Spanish Authorities. Inspections and non-routine requests for information by Spanish authorities shall be coordinated with the SBC and reported to the EEA via the Component chain-of-command. To the maximum extent possible, U.S. military personnel shall lead the review of DoD Component activities by Spanish authorities during the inspection.

C1.8. LEGAL PROTECTIONS FOR U.S. FORCES EMPLOYEES

C1.8.1. Legal protections afforded DoD personnel investigated or charged by a host nation with alleged offenses arising out of any act or omission done in the performance of official duty vary depending upon the status of the individual under the NATO Status of Forces

Agreement (SOFA) and other applicable international agreements. In general, there is a greater

May 2014 Spain FGS 1-5 ability for the U.S. to assert a primary right to exercise criminal jurisdiction over a military service member of the force as opposed to a member of the civilian component. There is no such right with respect to local national employees. Accordingly, military service members shall assume responsibility under these FGS in lieu of DoD civilians or local national employees where non-compliance may result in a host nation enforcement action.

C1.8.2. Installations, activities, and personnel shall immediately contact their servicing legal office when faced with possible or actual host nation enforcement actions in order to maximize protections afforded to DoD personnel under the NATO SOFA, bilateral agreements, U.S. and DoD regulations, and to secure legal representation for the subjects of the enforcement action (including local national employees). Installations will report possible or actual Spanish enforcement actions to the EEA via their chain-of-command.

C1.8.3. If the host nation authorities seek to question a DoD employee regarding his or her official duties, a representative from installation legal shall accompany the employee. The installation legal representative shall clarify with the host nation authorities whether the employee is questioned as a suspect or a witness, and the employee advised accordingly. It may not be readily apparent whether the host nation legal proceeding is criminal or administrative in nature. This point shall be clarified as soon as possible since different procedures may apply depending on the answer. Installations will report interview by Spanish authorities to the EEA via their chain-of-command.

C1.9. ENVIRONMENTAL EXECUTIVE AGENT

C1.9.1. The EEA for these FGS is the Commander, Navy Region Europe Africa

Southwest Asia. Any questions or comments pertaining to these FGS shall be sent to:

Commander, Navy Region Europe Africa Southwest Asia

PSC 817 Box 108

FPO AE 09622

DSN Voice (314) 626-2886

DSN FAX (314) 626-2878

Commercial +39 081-568-2886

SPAIN - 2 Air Emissions

May 2014 Spain FGS 2-1

C2. CHAPTER 2

AIR EMISSIONS

C2.1. SCOPE

This Chapter contains standards for air emissions sources. Criteria addressing open burning of solid waste are contained in Chapter 7, “Solid Waste.” Criteria addressing asbestos are contained in Chapter 15, “Asbestos.”

C2.2. DEFINITIONS

C2.2.1. Coal Refuse. Waste products from coal mining, cleaning, and coal preparation operations (e.g., culm and gob) containing coal, matrix material, clay, and other organic and inorganic material.

C2.2.2. Cold Cleaning Machine. Any device or piece of equipment that contains and/or uses liquid solvent, into which parts are placed to remove soil and other contaminants from the surfaces of the parts or to dry the parts. Cleaning machines that contain and use heated, nonboiling solvent to clean the parts are classified as cold cleaning machines.

C2.2.3. Fossil Fuel. Natural gas, petroleum, coal, and any form of solid, liquid, or gaseous fuel derived from such material for the purpose of creating useful heat.

C2.2.4. Fluorinated Gases (F-gases). Family of man-made gases used in a range of industrial applications as substitute for ozone-depleting substances. F-gases are considered greenhouse gases. They include the following groups: Chlorofluorocarbons (CFC), Halons, Hydrobromofluorocarbons (HBFC), Hydrochlorofluorocarbons (HCFC), Bromochloromethane

(BCM), hydrofluorocarbons (HFCs), Perfluorocarbons (PFCs) and Sulfur Hexafluoride (SF6).

C2.2.5. Freeboard Ratio. The ratio of the solvent cleaning machine freeboard height to the smaller interior dimension (length, width, or diameter) of the solvent cleaning machine.

C2.2.6. Hydrofluorocarbon (HFC). A compound consisting of hydrogen, fluorine, and carbon often used as a replacement for Ozone-Depleting Substances (ODS).

C2.2.7. Incinerator. A stationary or mobile unit dedicated to the thermal treatment of waste (including municipal waste combustion units) with or without recovery of the combustion heat generated. This includes the incineration by oxidation of waste as well as other thermal treatment processes such as pyrolysis, gasification or plasma processes in so far as the substances resulting from the treatment are subsequently incinerated.

C2.2.7.1. Co-incinerator. A stationary or mobile unit which uses waste as a fuel source and where energy generation or production is the main purpose.

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C2.2.7.2. Existing Incinerator or Co-incinerator Plant. An incinerator or co-incinerator authorized before 14 June 2003 and in operation before 29 December 2003.

C2.2.8. Motor Vehicle. Any commercially available vehicle that is not adapted to military use which is self-propelled and designed for transporting persons or property on a street or highway, including but not limited to, passenger cars, light duty vehicles, and heavy duty vehicles.

C2.2.9. Municipal Solid Waste (MSW). Any waste produced in housing or commercial units, offices, and services, and any other waste classified as non-hazardous that may be comparable to waste produced by those activities. Similar wastes generated at industrial facilities are also considered municipal wastes. Municipal waste also includes waste from cleaning operations of public roads, green areas, recreational areas and beaches, as well as furniture, household electrical and electronic equipment, abandoned vehicles and wastes proceeding from minor household remodeling.

C2.2.10. Municipal Waste Combustion (MWC) Units. Any equipment that combusts solid, liquid, or gasified municipal solid waste (MSW) including, but not limited to, field-erected

MWC units (with or without heat recovery), modular MWC units (starved-air or excess-air), boilers (for example, steam generating units), furnaces (whether suspension-fired, grate-fired, mass-fired, air curtain incinerators, or fluidized bed-fired), and pyrolysis/combustion units.

Municipal waste combustion units do NOT include pyrolysis or MWC units located at a plastics or rubber recycling unit, cement kilns that combust MSW, internal combustion engines, gas turbines, or other combustion devices that combust landfill gases collected by landfill gas collection systems.

C2.2.11. Ozone-Depleting Substances (ODS). Those substances listed in Table 2.8.

C2.2.12. Perfluorocarbon (PFC). A compound consisting solely of carbon and fluorine often used as a replacement for ODS.

C2.2.13. Process Heater. A device that is primarily used to heat a material to initiate or promote a chemical reaction in which the material participates as a reactant or catalyst.

C2.2.14. Pyrolysis. The endothermic gasification of hospital waste and/or medical/infectious waste using external energy.

C2.2.15. Stack. Any point in a source covered by criteria contained in C2.3.1., C2.3.2., C2.3.3., C2.3.4., or C2.3.5. designed to emit pollutants.

C2.2.16. Steam/Hot Water Generating Unit. A device that combusts any fuel and produces steam or heats water or any other heat transfer medium. This definition does not include nuclear steam generators or process heaters.

C2.2.17. Substantially-Modified. Any modification to a facility/building, the cost of which exceeds $1 million, regardless of funding source.

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C2.2.18. Volatile Organic Compound (VOC). Any organic compound having a vapor pressure ≥ 0.01 kPa at a temperature of 293.15 K , or having a corresponding volatility under the particular conditions of use.

C2.2.19. Vapor Cleaning Machine. A batch or in-line solvent cleaning machine that boils liquid solvent which generates solvent vapor that is used as a part of the cleaning or drying cycle.

C2.2.20. Vehicle Fluff. Vehicle scraps and parts from a scrap vehicle after it has been stripped for recycling.

C2.3. CRITERIA

C2.3.1. Steam/Hot Water Generating Units. Installations that operate steam/hot water generating units shall provide sufficient information to the Spanish Base Commander for authorization prior to their use (see Chapter 1 for the process).

C2.3.1.1. Installations that operate steam/hot water-generating units shall maintain an inventory that includes information on the units, emitted pollutants, any exceedances of emission limits, types of emission controls, and inspection records. This inventory shall be maintained for

≥ 10 years.

C2.3.1.2. Additionally, steam/hot water generating units with a rated thermal input > 20

MW (except hazardous or municipal waste incinerators) shall provide sufficient information to the Spanish Base Commander for a greenhouse gas emissions authorization (see Chapter 1 for the process).

C2.3.1.3. The following standards apply to units that commenced construction and/or operation on or after 1 October 1994 or that were substantially modified since 1 October 1994.

C2.3.1.4. Air Emission Standards. The following criteria apply to steam/hot water generating units as indicated below:

C2.3.1.4.1. Steam/hot water generating units and associated emissions controls, if applicable, must be designed to meet the emission standards for specific-sized units shown in

Tables 2.1, 2.2, and 2.3 at all times, except during periods of start up, shut down, malfunction, or when emergency conditions exist.

C2.3.1.4.2. For units combusting liquid or solid fossil fuels, fuel sulfur content

(weight %) and higher heating value will be measured and recorded for each new shipment of fuel. Use these data to calculate sulfur dioxide (SO2) emissions and document compliance with the SO2 limits in Tables 2.1, 2.2, and 2.3. Alternatively, install a properly calibrated and maintained continuous emissions monitoring system to measure the flue gas for SO2, NOX, PM and either oxygen (O2) or carbon dioxide (CO2).

C2.3.1.5. Air Emissions Monitoring. Steam/hot water generating units subject to NOX, SO2 and PM standards in Tables 2.1, 2.2, and 2.3 shall have a properly calibrated and maintained continuous emissions monitoring system (CEMS) to measure the flue gas as follows:

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C2.3.1.5.1. For units with a maximum design heat input capacity > 30 million Btu/hr:

Opacity, except that CEMS is not required where gaseous or distillate fuels are the only fuels combusted.

C2.3.1.5.2. For fossil fuel fired units with a maximum design heat input capacity >

100 million Btu/hr: NOX and either O2 or CO2.

C2.3.1.6. Testing of Emission Controls. Periodic testing shall be performed in order to verify the effectiveness of the emission prevention and control measures and compliance with the emission limit values.

C2.3.2. Incinerators. Installations that operate an incinerator for waste treatment (municipal waste, sludge, hazardous waste, or medical waste) shall provide sufficient information to the

Spanish Base Commander for authorization (see Chapter 1 for the process). The following criteria apply to the combustion of all types of waste. Refer to Chapter 6, “Hazardous Waste,” for additional information regarding hazardous waste disposal and incineration.

C2.3.2.1. Waste Incinerator. Each waste incinerator shall meet the emission limits specified in Tables 2.4 and 2.5.

C2.3.2.2. Waste Co-incinerator. Each waste co-incinerator shall meet the emission limits, specified in Tables 2.6 and 2.7.

C2.3.2.3. Monitoring Requirements. All waste incinerators and co-incinerators shall be subject to continuous measurements of the following parameters: NOX, CO, particulate matter, TOC, HCl, HF, SO2.

C2.3.2.4. Sewage Sludge Incinerators. All sewage sludge incinerators that commenced construction on or after 1 October 1994 or that were substantially modified since 1 October 1994 and that burn > 1 ton per day (tpd) of sewage sludge or > 10% sewage sludge, must also be designed to meet a particulate emission limit of 0.65 g/kg dry sludge (1.30 lb/ton dry sludge) and an opacity limit of 20% at all times, except during periods of start up, shut down, malfunction, or when emergency conditions exist.

C2.3.2.5. Medical Waste Incinerators (MWI). The following standards apply to all units. These requirements do not apply to any portable units (field deployable), pyrolysis units, or units that burn only pathological, low-level radioactive waste, or chemotherapeutic waste.

Refer to Chapter 8, “Medical Waste,” for other requirements pertaining to medical waste management.

C2.3.2.5.1. All MWI must be designed and operated according to the following standards:

C2.3.2.5.1.1. Unit design: dual chamber.

C2.3.2.5.1.2. Minimum temperature in primary chamber: 1562-1600°F.

C2.3.2.5.1.3. Minimum temperature in secondary chamber: 1800-

2200°F.

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C2.3.2.5.1.4. Flue gas temperature and internal combustion chamber for waste containing >1% of halogenated substances (expressed as chlorine): 1,100°C (2,012 °F).

C2.3.2.5.1.5. Minimum residence time in the secondary chamber: 2 seconds.

C2.3.2.5.1.6. Incinerator operators must be trained in accordance with applicable Service requirements.

C2.3.2.5.2. Each incinerator shall be equipped with auxiliary burners that are automatically activated when the flue gas temperature drops below 850 °C (1562 F) or 1,100 °C

(2,012 F) depending on the waste stream.

C2.3.3. Perchloroethylene (PCE) Dry Cleaning Machines. The following requirements apply to all dry cleaning machines. These criteria do not apply to coin-operated machines.

C2.3.3.1. Emissions from PCE dry cleaning machines installed before 1 October 1994 that use > 2000 gallons per year of PCE (installation wide) in dry cleaning operations, must be controlled with a refrigerated condenser, unless a carbon absorber was already installed. The temperature of the refrigerated condenser must be maintained at ≤ 45 ºF.

C2.3.3.2. All PCE dry cleaning systems installed on or after 1 October 1994 must be of the dry-to-dry design with emissions controlled by a refrigerated condenser. The temperature of the refrigerated condenser must be maintained at ≤ 45 ºF. Dry cleaning machines and control devices must be operated according to manufacturer recommendations.

C2.3.3.3. The total VOCs emission limit for dry cleaning machines shall be ≤ 20 g/kg of cleaned and dried product.

C2.3.3.4. Dry cleaning machines releasing > 10 kg/h (22.05 lb/h) of total organic carbon

(TOC) at the final point of discharge shall be equipped with continuously monitoring equipment.

C2.3.4. Chromium Electroplating and Chromium Anodizing Tanks. Electroplating and anodizing tanks must comply with one of the three methods below for controlling chromium emissions. Implement one of the following methods that is most appropriate to suit local conditions:

C2.3.4.1. Option 1: Limit chromium emissions in the ventilation exhaust to 0.015 milligrams per dry standard cubic meter (mg/dscm). Control devices/methods must be operated according to manufacturer recommendations.

C2.3.4.2. Option 2: Use chemical tank additives to prevent surface tension of the electroplating or anodizing bath from exceeding 45 dynes per centimeter (cm) as measured by a stalagmometer or 35 dynes/cm as measured by a tensiometer. Measure the surface tension prior to the first initiation of electric current on a given day and every 4 hours thereafter.

C2.3.4.3. Option 3: Limit chromium emissions to the maximum allowable mass emission rate (MAMER) calculated using the following equation: MAMER = ETSA x K x 0.015 mg/dscm, where: MAMER = the alternative emission rate for enclosed hard chromium

May 2014 Spain FGS 2-6 electroplating tanks in mg/hr; ETSA = the hard chromium electroplating tank surface area in square feet (ft ); K = a conversion factor, 425 dscm/(ft

-hr). Option 3 is ONLY applicable to hard chrome electroplating tanks equipped with an enclosing hood and ventilated at half the rate or less than that of an open surface tank of the same surface area.

C2.3.5. Halogenated Solvent Cleaning Machines. These requirements apply to all solvent cleaning machines that use solvent which contains > 5% by weight: methylene chloride (CAS

No. 75-09-2), perchloroethylene (CAS No. 127-18-4), trichloroethylene (CAS No. 79-01-6), 1,1,1-trichloroethane (CAS No. 71-55-6), carbon tetrachloride (CAS No. 56-23-5), chloroform

(CAS No. 67-66-3), or any combination of these halogenated solvents.

C2.3.5.1. All cold cleaning machines (remote reservoir and immersion tanks) must be covered when not in use. Additionally, immersion type cold cleaning machines must have either a 1-inch water layer or a freeboard ratio of ≥ 0.75.

C2.3.5.2. All vapor cleaning machines (vapor degreasers) must incorporate design and work practices which minimize the direct release of halogenated solvent to the atmosphere.

When the mass flow of the sum of the halogenated organic solvents (as specified in C2.3.5) is ≥

100 g/h (0.22 lb/h), the emission shall not exceed 20 mg/Nm

C2.3.6. Units Containing ODS Listed In Table 2.8. The following criteria apply to direct atmospheric emissions of ODS listed in Table 2.8.

C2.3.6.1. Except as allowed in C2.3.6.2 and C2.3.6.3, use of the following ODSs, as listed in Table 2.8, is prohibited. Running an existing system without maintenance (e.g., using a refrigerator) would not be classified as use.

C2.3.6.2. Halons shall only be used for critical uses as specified in Table 2.9.

C2.3.6.3. The use of ODSs shall be allowed:

C2.3.6.3.1. In essential laboratory and analytical uses.

C2.3.6.3.2. As halon substitutes in existing fire protection systems specified in Table

2.9 under the following conditions:

C2.3.6.3.2.1. Original halons shall be replaced with the same type of halon.

C2.3.6.3.2.2. Original halons contained in such fire protection systems shall be replaced completely;

C2.3.6.4. Refrigerant Recovery/Recycling. All repairs, including leak repairs or services to appliances, industrial process refrigeration units, air conditioning units, or motor vehicle air conditioners, must be performed using commercially available refrigerant recovery/recycling equipment operated by trained personnel. Refrigerant technicians shall be trained in proper recovery/recycling procedures, leak detection, safety, shipping, and disposal in accordance with recognized industry standards or Spanish equivalent.

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C2.3.6.4.1. Recovery Requirements for ODSs. ODSs identified in Table 2.8 shall be recovered as follows using equipment operated by trained personnel:

C2.3.6.4.1.1. Repaired equipment containing ≥ 3 kg (6.6 lbs) of refrigerating fluid charge shall be checked annually for leaks.

C2.3.6.4.1.2. Where methyl bromide is used in soil fumigation, the use of virtually impermeable films for a sufficient time, or other techniques ensuring the same level of environmental protection must be used. All practicable precautionary measures must be taken to prevent and minimize leakage of methyl bromide from fumigation installations and operations.

C2.3.6.4.1.3. Halons and other ODSs recovered shall be returned to the DLA

Defense Reserve (located in Germersheim Germany; Zevenaar Netherlands; and Richmond, Virginia) for reprocessing in accordance with the established DoD ODS turn-in procedures

(dated September 2012).

C2.3.6.4.2. Use of HCFCs as Refrigerants. Reclaimed or recycled HCFCs may be used until 31 December 2014 for the maintenance and servicing of existing refrigeration, air conditioning, and heat pump equipment provided they have been recovered from such equipment. These uses are prohibited after 31 December 2014.

C2.3.6.5. Refrigerant Venting Prohibition. Any class I or II ODS, HFC, and PFC refrigerant (identified in Table 2.8) shall not be intentionally released in the course of maintaining, servicing, repairing, or disposing of appliances, industrial process refrigeration units, air conditioning units, or motor vehicle air conditioners. De minimis releases associated with good faith attempts to recycle or recover ODS, HFC, and PFC refrigerants are not subject to this prohibition.

C2.3.6.6. Refrigerant Leak Monitoring and Repair. Monitor and repair refrigeration equipment for ODS leakage in accordance with the following criteria and repair, if found to be leaking.

C2.3.6.7. Installations containing ODS refrigerant. The following precautionary measures shall be taken to prevent leakage of ODSs included in Table 2.8:

C2.3.6.7.1. All precautionary measures practicable shall be taken to prevent and minimize any leakage and emissions of ODSs.

C2.3.6.7.2. Units containing fluorinated refrigerants with fluid charge of ≥ 300 kg shall be equipped with a leak detection system.

C2.3.6.7.3. When operating refrigeration, air conditioning or heat pump equipment, or fire protection systems that contain ODSs, the stationary equipment or systems shall be checked for leakage at the following frequency:

May 2014 Spain FGS 2-8

Fluid charge of controlled substance Frequency

≥ 3 kg and < 30 kg 12 months

≥ 30 kg and < 300 kg 6 months

≥ 300 kg 3 months

C2.3.6.7.4. Any detected leakage from the above specified equipment or from any other equipment relying on ODSs shall be repaired within 14 days. The equipment or system shall be checked for leakage within 1 month after a leak has been repaired to ensure its effectiveness.

C2.3.6.8. Unit Maintenance. Installation, maintenance and dismantling of refrigeration units shall only be performed by qualified personnel certified in accordance with a recognized

U.S. certification body and/or the Spanish equivalent.

C2.3.6.9. Unit Labeling. All refrigeration units shall be placarded with the following information:

C2.3.6.9.1. Name and address of the installation company;

C2.3.6.9.2. Model and serial number of the equipment;

C2.3.6.9.3. Year of manufacture;

C2.3.6.9.4. Date of the next periodic inspection;

C2.3.6.9.5. Type of refrigerant;

C2.3.6.9.6. Fluid charge, expressed in kg;

C2.3.6.9.7. Allowable maximum pressure, expressed in bar; and

C2.3.6.9.8. CE or UL seal of approval.

C2.3.6.9.9. Additionally, units containing fluorinated greenhouse gas refrigerants shall be labeled with the chemical name of the refrigerant and its quantity.

C2.3.6.10. Refrigerant Inventory. DoD installations shall maintain an inventory of all refrigeration units that includes information on the manufacturer and type of unit installed, name of the installation company, date of the first and subsequent periodic inspections, and monitoring and repair records.

C2.3.7. Fluorinated Gases.

C2.3.7.1. Installation, handling and maintenance of the following equipment containing fluorinated gases shall be performed by personnel certified in accordance with a recognized U.S.

certification body and/or Spanish equivalent:

C2.3.7.1.1. Refrigeration or air conditioning equipment;

May 2014 Spain FGS 2-9

C2.3.7.1.2. Air conditioning systems in motor vehicles; and

C2.3.7.1.3. Fire protection systems that use fluorinated gas as an extinguishing agent.

C2.3.7.2. ODS Fire Suppression Agent (Halon) Venting Prohibition. Halons shall not be intentionally released into the environment while testing, maintaining, servicing, repairing, or disposing of halon-containing equipment or using such equipment for technician training. Halon uses authorized in C2.3.6.2 are exempt from the venting prohibition in the following situations:

C2.3.7.2.1. De minimis releases associated with good faith attempts to recycle or recover halons (i.e., release of residual halon contained in fully discharged total flooding fire extinguishing systems).

C2.3.7.2.2. Emergency releases for the legitimate purpose of fire extinguishing, explosion inertion, or other emergency applications for which the equipment or systems were designed.

C2.3.7.2.3. Releases during the testing of fire extinguishing systems if each of the following is true: systems or equipment employing suitable alternative fire extinguishing agents are not available; release of extinguishing agent is essential to demonstrate equipment functionality; failure of system or equipment would pose great risk to human safety or the environment; and, a simulant agent (i.e., substitute product that can perform the same function) cannot be used.

C2.3.8. Motor Vehicles. This criteria applies to DoD-owned motor vehicles as defined in paragraph C2.2.8.

C2.3.8.1. All vehicles shall be inspected as follows to ensure that no tampering with the factory-installed emission control equipment has occurred:

Vehicle Age Inspection Frequency

0-4 years every 2 years after 4 years annually

C2.3.8.2. CO emission limits for idling gasoline-fueled vehicles that were manufactured in Europe shall not exceed 5% by volume (at 15-20º C (59-68 º F) and 750-760 mm Hg). Motor vehicles manufactured in Europe and equipped with diesel engines shall not exceed the following opacity limits:

Engine Horsepower Opacity Limit (Absolute Units)

> 200 2.1

>100 and <200 2.4

< 100 2.8

1. The opacity limits are based on measures made at a minimum motor temperature of 60C (140 ºF).

C2.3.8.3. Use only unleaded gasoline in vehicles that are designed for this fuel.

May 2014 Spain FGS 2-10

C2.3.9. Stack Heights. Hg is the good engineering practice stack height necessary to minimize downwash of stack emissions due to aerodynamic influences from nearby structures.

C2.3.9.1. Stacks shall be designed and constructed to heights at least equal to the largest

Hg calculated from either of the following two criteria:

C2.3.9.1.1. Hg = H +1.5L, where H is the height of the nearby structure measured from the ground level elevation at the base of the stack, and L is the lesser of height or projected width of the nearby structure(s). A structure is determined to be nearby when the stack is located within 5L of the structure envelope but not > 0.8 km (0.5 mile). This calculation shall be performed for each structure nearby the stack being studied to determine the greatest Hg.

C2.3.9.1.2. Hg is the height demonstrated by a fluid model or a field study, which ensures that the emissions from a stack do not result in ground-level concentrations of any air pollutant related to the combustion activities above the permitted limit values as a result of atmospheric downwash, wakes, or eddy effects created by the source itself, nearby structures, or nearby terrain features ≥ 40% in excess of the maximum ground-level concentrations of any air pollutant experienced in the absence of such atmospheric downwash, wakes, or eddy effects. For purposes of this paragraph, “nearby” means ≤ 0.8 km (0.5 mile), except that the portion of a terrain feature may be considered to be nearby which falls within a distance of up to 10 times the maximum height (Ht) of the feature, not to exceed 2 miles if such feature achieves a height (Ht)

0.8 km from the stack that is ≥ 40% of the good engineering practice stack height determined by the formula provided in C2.3.9.1.1. of this part or 26 meters, whichever is greater, as measured from the ground-level elevation at the base of the stack. The height of the structure or terrain feature is measured from the ground-level elevation at the base of the stack.

C2.3.10. Fuel Composition. The composition of fuels allowed for use in Spain is specified in the following table:

Parameter Units Diesel Fuel Fuel Oil

Minimum Maximum Minimum Maximum

Density at

15C kg/m

820 845 720 775

Viscosity at

40C mm

/s 2.00 4.50 --- ---

Total sulfur content mg/kg --- 10 --- 10

Total lead content g/l --- --- --- 0.005

Water mg/kg --- 200 --- ---

C2.3.10.1. The presence of the metallic additive in fuel is limited to 6 mg of manganese per liter as of 1 January 2011, and 2 mg of manganese per liter as of 1 January 2014.

May 2014 Spain FGS 2-11

Table 2.1. Emission Limits for Power Plants with Energy-Generating Potential < 50 MW

Fuel Source

Emission Limits

Opacity (1)

SO2

(mg/Nm

Particulate Matter

(mg/Nm

Liquid fuels 20 5,500 200

Solid fuel (anthracite coal) 20 2,400 400

Solid fuel (lignite coal) 20 9,000 400 Notes:

1. The limits shall not exceed 40% opacity or more than one 2-minute period per hour.

2. The units of mg/Nm are at normal physical conditions of 0ºC and 0.1013 Mpa.

These emission limits apply to the activities subjected to notification (group C).

Table 2.2. Emission Limits for Industrial Combustion Facilities

(Steam/Heat Generating Units, Excluding Thermal Plants)

Fuel Source

Emission Limits

Opacity (1)

SO2

(mg/Nm

CO

(ppm)

Gas oil or domestic fuel oil 20 1,700 1,445

Heavy #1 fuel oil 40 4,200 1,445

Heavy #2 fuel oil 50 6,800 1,445 Notes:

1. The limits shall not be exceeded more than three times per day, with each period lasting < 10 minutes.

2. The units of mg/Nm are at normal physical conditions of 0ºC (32 ºF) and 0.1013 Mpa.

These emission limits apply to the activities subjected to notification (group C).

May 2014 Spain FGS 2-12

Table 2.3. Emission Limit Values

(for new installations with a power capacity of >50 MW authorized after 27 November 2002)

Pollutant

Thermal input

50 to100 MW 100 to 300

MW

> 300 MW

Solid fuels (mg/Nm ) (O2 content 6 %)

SO2:

General case

Biomass

NOX :

Biomass

Particulate matter

50 30 30

Opacity (%) 20

Liquid fuels (mg/Nm ) (O2 content 3 %)

SO2 850 400 to 200

(linear decrease)

NOX 400 200 200

Particulate matter

50 30 30

Opacity (%) 20

Gaseous fuels (mg/Nm ) (O2 content 3 %)

SO2 35

NOX :

Natural gas

Other gases

Particulate matter

May 2014 Spain FGS 2-13

Table 2.4. Emission Limit Values for Waste Incinerators

(daily average values)

Pollutant Emission Standards

Particulate matter 10 mg/m

Gaseous and vaporous organic substances, expressed as total organic carbon

10 mg/m

Hydrogen chloride (HCl) 10 mg/m

Hydrogen fluoride (HF) 1 mg/m

Sulfur dioxide (SO2) 50 mg/m

Nitrogen monoxide (NO) and nitrogen dioxide (NO2) expressed as nitrogen dioxide for existing incineration plants with a nominal capacity exceeding 6 tonnes per hour or new incineration plants

200 mg/m

Nitrogen monoxide (NO) and nitrogen dioxide

(NO2), expressed as nitrogen dioxide for existing incineration plants with a nominal capacity of ≤6 tonnes per hour

400 mg/m

Table 2.5. Heavy Metals Emission Limit Values for Waste Incinerators

(All average values over the sample period of a minimum of 30 minutes and a maximum of 8 hours)

Pollutant Total emission limit value

Cadmium and its compounds, expressed as cadmium

(Cd)

Total 0.05 mg/m

Total 0.1

Thallium and its compounds, expressed as thallium (Tl)

Mercury and its compounds, expressed as mercury (Hg) 0.05

0.1 mg/m

Antimony and its compounds, expressed as antimony

(Sb)

Total 0.5

Total 1

Arsenic and its compounds, expressed as arsenic (As)

Lead and its compounds, expressed as lead (Pb)

Chromium and its compounds, expressed as chromium

(Cr)

Cobalt and its compounds, expressed as cobalt (Co)

Copper and its compounds, expressed as copper (Cu)

Manganese and its compounds, expressed as manganese

(Mn)

Nickel and its compounds, expressed as nickel (Ni)

Vanadium and its compounds, expressed as vanadium

(V)

May 2014 Spain FGS 2-14

Table 2.6. Emission Limit Values for Waste Co-incinerators

(daily average values)

Pollutant < 50

MW

50 to100 MW 100 to 300 MW > 300 MW

Solid fuels (mg/m ) (O2 content 6 %)

SO2:

Indigenous fuels or rate of desulphurization

≥ 90 %

850 to 200

(linear decrease from 100 to 300

MW)

≥ 92 %

≥ 95 %

NOX 400 300 200

Particulate matter

50 50 30 30

Biomass (mg/m ) (O2 content 6 %)

SO2 200 200 200

NOX 350 300 300

Particulate matter

50 50 30 30

Liquid fuels (mg/m ) (O2 content 3 %)

SO2 850 850 to 200

(linear decrease from 100 to 300

MW)

NOX 400 300 200

Particulate matter

50 50 300 30

Table 2.7. Heavy Metals Emission Limit Values for Waste Co-incinerators

Pollutant Total emission limit value

Cd + Tl 0.05 mg/m

Hg 0.05 mg/m

Sb + As + Pb + Cr + Co + Cu + Mn + Ni + V 0.5 mg/m

Dioxins and furans 0.1 mg/m

May 2014 Spain FGS 2-15

Table 2.8. Ozone Depleting Substances

Molecular

Formula Common Name CAS Number

Chemical Name

Chlorofluorocarbons (CFCs)

CFCl3 CFC – 11 75-69-4 Trichlorofluoromethane

CF2Cl2 CFC – 12 75-71-8 Dichlorodifluoromethane

C2F3Cl3 CFC – 113 76-13-1 Trichlorotrifluoroethane

C2F4Cl2 CFC – 114 76-14-2 Dichlorotetrafluoroethane

C2F5Cl CFC – 115 76-15-3 Chloropentafluoroethane

Other Fully Halogenated Chlorofluorocarbons

CF3Cl CFC – 13 75-72-9 Chlorotrifluoromethane

C2FCl5 CFC – 111 354-56-3 Pentachlorofluoroethane

C2F2Cl4 CFC – 112 76-12-0 Tetrachlorodifluoroethane

C3FCl7 CFC – 211 422-78-6 Heptachlorofluoropropane

C3F2Cl6 CFC – 212 3182-26-1 Hexachlorodifluoropropane

C3F3Cl5 CFC – 213 2354-06-5 Pentachlorotrifluoropropane

C3F4Cl4 CFC – 214 29255-31-0 Tetrachlorotetrafluoropropa ne

C3F5Cl3 CFC – 215 4259-43-2 Trichloropentafluoropropane

C3F6Cl2 CFC – 216 661-97-2 Dichlorohexafluoropropane

C3F7Cl CFC – 217 422-86-6 Chloroheptafluoropropane

Halons

CF2BrCl Halon – 1211 353-59-3 Bromochlorodifluoromethan e

CF3Br Halon – 1301 75-63-8 Bromotrifluoromethane

C2F4Br2 Halon – 2402 124-73-2 Dibromotetrafluoroethane

Carbon Tetrachloride

CCl4 Carbon

Tetrachloride

56-23-5 Carbon Tetrachloride

1,1,1-trichloroethane

C2H3Cl3 Methyl Chloroform 71-55-6 1,1,1-trichloroethane

Methyl Bromide

CH3Br Methyl Bromide 74-83-9 Methyl Bromide

Hydrobromofluorocarbons

CHFBr2 N/A Dibromofluoromethane

CHF2Br HBFC-22B1 Bromodifluoromethane

CH2FBr N/A Bromofluoromethane

C2HFBr4 N/A Tetrabromofluoroethane

C2HF2Br3 N/A Tribromodifluoroethane

May 2014 Spain FGS 2-16

Molecular

Formula Common Name CAS Number

Chemical Name

C2HF3Br2 N/A Dibromotrifluoroethane

C2HF4Br N/A Bromotetrafluoroethane

C2H2FBr3 N/A Tribromofluoroethane

C2H2F2Br2 N/A Dibromodifluoroethane

C2H2F3Br N/A Bromotrifluoroethane

C2H3FBr2 N/A Dibromofluoroethane

C2H3F2Br N/A Bromodifluoroethane

C2H4FBr N/A Bromofluoroethane

C3HFBr6 N/A Hexabromofluoropropane

C3HF2Br5 N/A Pentabromodifluoropropane

C3HF3Br4 N/A Tetrabromotrifluoropropane

C3HF4Br3 N/A Tribromotetrafluoropropane

C3HF5Br2 N/A Dibromopentafluoropropane

C3HF6Br N/A Bromohexafluoropropane

C3H2FBr5 N/A Pentabromofluoropropane

C3H2F2Br4 N/A Tetrabromodifluoropropane

C3H2F3Br3 N/A Tribromotrifluoropropane

C3H2F4Br2 N/A Dibromotetrafluoropropane

C3H2F5Br N/A Bromopentafluoropropane

C3H3FBr4 N/A Tetrabromofluoropropane

C3H3F2Br3 N/A Tribromodifluoropropane

C3H3F3Br2 N/A Dibromotrifluoropropane

C3H3F4Br N/A Bromotetrafluoropropane

C3H4FBr3 N/A Tribromofluoropropane

C3H4F2Br2 N/A Dibromodifluoropropane

C3H4F3Br N/A Bromotrifluoropropane

C3H5FBr2 N/A Dibromofluoropropane

C3H5F2Br N/A Bromodifluoropropane

C3H6FBr N/A Bromofluoropropane

Hydrochlorofluorocarbons (HCFCs)

CHFCl2 HCFC – 21 Dichlorofluoromethane

CHF2Cl HCFC – 22 Chlorodifluoromethane

CH2FCl HCFC – 31 Chlorofluoromethane

C2HFCl4 HCFC – 121 Tetrachlorofluoroethane

C2HF2Cl3 HCFC – 122 Trichlorodifluoroethane

C2HF3Cl2 HCFC – 123 Dichlorotrifluoroethane

C2HF4Cl HCFC – 124 Chlorotetrafluoroethane

C2H2FCl3 HCFC – 131 Trichlorofluoroethane

C2H2F2Cl2 HCFC – 132 Dichlorodifluoroethane

C2H2F3Cl HCFC – 133 Chlorotrifluoroethane

C2H3FCl2 HCFC – 141 Dichlorofluoroethane

CH3CFCl2 HCFC – 141b 1,1-dichloro-1-fluoroethane

May 2014 Spain FGS 2-17

Molecular

Formula Common Name CAS Number

Chemical Name

C2H3F2Cl HCFC – 142 Chlorodifluoroethane

CH3CF2Cl HCFC – 142b 1-chloro-1,1-difluoroethane

C2H4FCl HCFC – 151 Chlorofluoroethane

C3HFCl6 HCFC – 221 Hexachlorofluoropropane

C3HF2Cl5 HCFC – 222 Pentachlorodifluoropropane

C3HF3Cl4 HCFC – 223 Tetrachlorotrifluoropropane

C3HF4Cl3 HCFC – 224 Trichlorotetrafluoropropane

C3HF5Cl2 HCFC – 225 Dichloropentafluoropropane

CF3CF2CHCl2 HCFC – 225ca 3,3-dichloro-1,1,1,2,2-pentafluoropropane

CF2ClCF2CHCl

F

HCFC – 225cb 1,3-dichloro-1,1,2,2,3-pentafluoropropane

C3HF6Cl HCFC – 226 Chlorohexafluoropropane

C3H2FCl5 HCFC – 231 Pentachlorofluoropropane

C3H2F2Cl4 HCFC – 232 Tetrachlorodifluoropropane

C3H2F3Cl3 HCFC – 233 Trichlorotrifluoropropane

C3H2F4Cl2 HCFC – 234 Dichlorotetrafluoropropane

C3H2F5Cl HCFC – 235 Chloropentafluoropropane

C3H3FCl4 HCFC – 241 Tetrachlorofluoropropane

C3H3F2Cl3 HCFC – 242 Trichlorodifluoropropane

C3H3F3Cl2 HCFC – 243 Dichlorotrifluoropropane

C3H3F4Cl HCFC – 244 Chlorotetrafluoropropane

C3H4FCl3 HCFC – 251 Trichlorofluoropropane

C3H4F2Cl2 HCFC – 252 Dichlorodifluoropropane

C3H4F3Cl HCFC – 253 Chlorotrifluoropropane

C3H5FCl2 HCFC – 261 Dichlorofluoropropane

C3H5F2Cl HCFC – 262 Chlorodifluoropropane

C3H6FCl HCFC – 271 Chlorofluoropropane

Bromochloromethane

CH2BrCl BCM Bromochloromethane

Dibromodifluoromethane

CBr2F2 Halon-1202 Dibromodifluoromethane Note:

1. The American Chemical Society’s Chemical Abstracts Service number.

May 2014 Spain FGS 2-18

Table 2.9. Critical Uses of Halon

Application Cut-off date

(31

December of the stated year)

End date

(31

December of the stated year)

Category of equipment or facility

Purpose Type of extinguisher

Type of

Halon

On military ground vehicles

For the protection of engine compartments

Fixed system

2010 2035

For the protection of crew compartments

Fixed system

2011 2040

Portable extinguisher

2011 2020

On ship military surface ships

For the protection of normally occupied machinery spaces

Fixed system

2010 2040

For the protection of normally unoccupied engine spaces

Fixed system

2010 2035

For the protection of normally unoccupied electrical compartments

Fixed system

2010 2030

For the protection of command centers

Fixed system 1301 2010 2030

For the protection of fuel pump rooms

Fixed system 1301 2010 2030

For the protection of flammable liquid storage compartments

Fixed system

2010 2030

For the protection of aircraft in hangars and maintenance areas

Portable extinguisher

2010 2016

On military submarines

For the protection of machinery spaces

Fixed system 1301 2010 2040

For the protection Fixed system 1301 2010 2040

May 2014 Spain FGS 2-19

Application Cut-off date

(31

December of the stated year)

End date

(31

December of the stated year)

Category of equipment or facility

Purpose Type of extinguisher

Type of

Halon of command centers

For the protection of diesel generator spaces

Fixed system 1301 2010 2040

For the protection of electrical compartments

Fixed system 1301 2010 2040

On aircraft

For the protection of normally unoccupied cargo compartments

Fixed system

2018 2040

For the protection of cabins and crew compartments

Portable extinguisher

2014 2025

For the protection of engine nacelles and auxiliary power units

Fixed system

2014 2040

For the inerting of fuel tanks Fixed system

2011 2040

For the protection of lavatory waste receptacles

Fixed system

2011 2020

For the protection of dry bays Fixed system

2011 2040

In oil, gas and petrochemicals facilities

For the protection of spaces where flammable liquid or gas could be released

Fixed system

2010 2020

On commercial cargo ships

For the inerting of normally occupied spaces where flammable liquid or gas could be released

Fixed system

1994 2016

In land-based command and

For the protection of normally Fixed system

2010 2025

May 2014 Spain FGS 2-20

Application Cut-off date

(31

December of the stated year)

End date

(31

December of the stated year)

Category of equipment or facility

Purpose Type of…