Code of Federal Regulations (alpha)

CFR /  Title 40  /  Part 268  /  Sec. 268.42 Treatment standards expressed as specified technologies.

Note: For the requirements previously found in this section in Table 2--Technology-Based Standards By RCRA Waste Code, and Table 3--Technology-Based Standards for Specific Radioactive Hazardous Mixed Waste, refer to Sec. 268.40.

(a) The following wastes in the table in Sec. 268.40 ``Treatment Standards for Hazardous Wastes,'' for which standards are expressed as a treatment method rather than a concentration level, must be treated using the technology or technologies specified in the table entitled ``Technology Codes and Description of Technology-Based Standards'' in this section.

Table 1--Technology Codes and Description of Technology-Based Standards------------------------------------------------------------------------

Technology code Description of technology-based standards------------------------------------------------------------------------ADGAS: Venting of compressed gases into an absorbing or

reacting media (i.e., solid or liquid)--venting

can be accomplished through physical release

utilizing valves/piping; physical penetration

of the container; and/or penetration through

detonation.AMLGM: Amalgamation of liquid, elemental mercury

contaminated with radioactive materials

utilizing inorganic reagents such as copper,

zinc, nickel, gold, and sulfur that result in a

nonliquid, semi-solid amalgam and thereby

reducing potential emissions of elemental

mercury vapors to the air.BIODG: Biodegradation of organics or non-metallic

inorganics (i.e., degradable inorganics that

contain the elements of phosphorus, nitrogen,

and sulfur) in units operated under either

aerobic or anaerobic conditions such that a

surrogate compound or indicator parameter has

been substantially reduced in concentration in

the residuals (e.g., Total Organic Carbon can

often be used as an indicator parameter for the

biodegradation of many organic constituents

that cannot be directly analyzed in wastewater

residues).CARBN: Carbon adsorption (granulated or powdered) of

non-metallic inorganics, organo-metallics, and/

or organic constituents, operated such that a

surrogate compound or indicator parameter has

not undergone breakthrough (e.g., Total Organic

Carbon can often be used as an indicator

parameter for the adsorption of many organic

constituents that cannot be directly analyzed

in wastewater residues). Breakthrough occurs

when the carbon has become saturated with the

constituent (or indicator parameter) and

substantial change in adsorption rate

associated with that constituent occurs.CHOXD: Chemical or electrolytic oxidation utilizing the

following oxidation reagents (or waste

reagents) or combinations of reagents: (1)

Hypochlorite (e.g., bleach); (2) chlorine; (3)

chlorine dioxide; (4) ozone or UV (ultraviolet

light) assisted ozone; (5) peroxides; (6)

persulfates; (7) perchlorates; (8)

permangantes; and/or (9) other oxidizing

reagents of equivalent efficiency, performed in

units operated such that a surrogate compound

or indicator parameter has been substantially

reduced in concentration in the residuals

(e.g., Total Organic Carbon can often be used

as an indicator parameter for the oxidation of

many organic constituents that cannot be

directly analyzed in wastewater residues).

Chemical oxidation specifically includes what

is commonly referred to as alkaline

chlorination.CHRED: Chemical reduction utilizing the following

reducing reagents (or waste reagents) or

combinations of reagents: (1) Sulfur dioxide;

(2) sodium, potassium, or alkali salts or

sulfites, bisulfites, metabisulfites, and

polyethylene glycols (e.g., NaPEG and KPEG);

(3) sodium hydrosulfide; (4) ferrous salts; and/

or (5) other reducing reagents of equivalent

efficiency, performed in units operated such

that a surrogate compound or indicator

parameter has been substantially reduced in

concentration in the residuals (e.g., Total

Organic Halogens can often be used as an

indicator parameter for the reduction of many

halogenated organic constituents that cannot be

directly analyzed in wastewater residues).

Chemical reduction is commonly used for the

reduction of hexavalent chromium to the

trivalent state.CMBST: High temperature organic destruction

technologies, such as combustion in

incinerators, boilers, or industrial furnaces

operated in accordance with the applicable

requirements of 40 CFR part 264, subpart O, or

40 CFR part 265, subpart O, or 40 CFR part 266,

subpart H, and in other units operated in

accordance with applicable technical operating

requirements; and certain non-combustive

technologies, such as the Catalytic Extraction

Process.DEACT: Deactivation to remove the hazardous

characteristics of a waste due to its

ignitability, corrosivity, and/or reactivity.FSUBS: Fuel substitution in units operated in

accordance with applicable technical operating

requirements.HLVIT: Vitrification of high level mixed radioactive

wastes in units in compliance with all

applicable radioactive protection requirements

under control of the Nuclear Regulatory

Commission.IMERC: Incineration of wastes containing organics and

mercury in units operated in accordance with

the technical operating requirements of 40 CFR

part 264 subpart 0 and part 265 subpart 0. All

wastewater and nonwastewater residues derived

from this process must then comply with the

corresponding treatment standards per waste

code with consideration of any applicable

subcategories (e.g., High or Low Mercury

Subcategories).INCIN: Incineration in units operated in accordance

with the technical operating requirements of 40

CFR part 264 subpart 0 and part 265 subpart 0.LLEXT: Liquid-liquid extraction (often referred to as

solvent extraction) of organics from liquid

wastes into an immiscible solvent for which the

hazardous constituents have a greater solvent

affinity, resulting in an extract high in

organics that must undergo either incineration,

reuse as a fuel, or other recovery/reuse and a

raffinate (extracted liquid waste)

proportionately low in organics that must

undergo further treatment as specified in the

standard.

MACRO: Macroencapsulation with surface coating

materials such as polymeric organics (e.g.,

resins and plastics) or with a jacket of inert

inorganic materials to substantially reduce

surface exposure to potential leaching media.

Macroencapsulation specifically does not

include any material that would be classified

as a tank or container according to 40 CFR

260.10.NEUTR: Neutralization with the following reagents (or

waste reagents) or combinations of reagents:

(1) Acids; (2) bases; or (3) water (including

wastewaters) resulting in a pH greater than 2

but less than 12.5 as measured in the aqueous

residuals.NLDBR: No land disposal based on recycling.POLYM: Formation of complex high-molecular weight

solids through polymerization of monomers in

high-TOC D001 non-wastewaters which are

chemical components in the manufacture of

plastics.PRECP: Chemical precipitation of metals and other

inorganics as insoluble precipitates of oxides,

hydroxides, carbonates, sulfides, sulfates,

chlorides, fluorides, or phosphates. The

following reagents (or waste reagents) are

typically used alone or in combination: (1)

Lime (i.e., containing oxides and/or hydroxides

of calcium and/or magnesium; (2) caustic (i.e.,

sodium and/or potassium hydroxides; (3) soda

ash (i.e., sodium carbonate); (4) sodium

sulfide; (5) ferric sulfate or ferric chloride;

(6) alum; or (7) sodium sulfate. Additional

floculating, coagulation or similar reagents/

processes that enhance sludge dewatering

characteristics are not precluded from use.RBERY: Thermal recovery of Beryllium.RCGAS: Recovery/reuse of compressed gases including

techniques such as reprocessing of the gases

for reuse/resale; filtering/adsorption of

impurities; remixing for direct reuse or

resale; and use of the gas as a fuel source.RCORR: Recovery of acids or bases utilizing one or more

of the following recovery technologies: (1)

Distillation (i.e., thermal concentration); (2)

ion exchange; (3) resin or solid adsorption;

(4) reverse osmosis; and/or (5) incineration

for the recovery of acid--Note: this does not

preclude the use of other physical phase

separation or concentration techniques such as

decantation, filtration (including

ultrafiltration), and centrifugation, when used

in conjunction with the above listed recovery

technologies.RLEAD: Thermal recovery of lead in secondary lead

smelters.RMERC: Retorting or roasting in a thermal processing

unit capable of volatilizing mercury and

subsequently condensing the volatilized mercury

for recovery. The retorting or roasting unit

(or facility) must be subject to one or more of

the following: (a) a National Emissions

Standard for Hazardous Air Pollutants (NESHAP)

for mercury; (b) a Best Available Control

Technology (BACT) or a Lowest Achievable

Emission Rate (LAER) standard for mercury

imposed pursuant to a Prevention of Significant

Deterioration (PSD) permit; or (c) a state

permit that establishes emission limitations

(within meaning of section 302 of the Clean Air

Act) for mercury. All wastewater and

nonwastewater residues derived from this

process must then comply with the corresponding

treatment standards per waste code with

consideration of any applicable subcategories

(e.g., High or Low Mercury Subcategories).RMETL: Recovery of metals or inorganics utilizing one

or more of the following direct physical/

removal technologies: (1) Ion exchange; (2)

resin or solid (i.e., zeolites) adsorption; (3)

reverse osmosis; (4) chelation/solvent

extraction; (5) freeze crystalization; (6)

ultrafiltration and/or (7) simple precipitation

(i.e., crystalization)--Note: This does not

preclude the use of other physical phase

separation or concentration techniques such as

decantation, filtration (including

ultrafiltration), and centrifugation, when used

in conjunction with the above listed recovery

technologies.RORGS: Recovery of organics utilizing one or more of

the following technologies: (1) Distillation;

(2) thin film evaporation; (3) steam stripping;

(4) carbon adsorption; (5) critical fluid

extraction; (6) liquid-liquid extraction; (7)

precipitation/crystalization (including freeze

crystallization); or (8) chemical phase

separation techniques (i.e., addition of acids,

bases, demulsifiers, or similar chemicals);--

Note: this does not preclude the use of other

physical phase separation techniques such as a

decantation, filtration (including

ultrafiltration), and centrifugation, when used

in conjunction with the above listed recovery

technologies.RTHRM: Thermal recovery of metals or inorganics from

nonwastewaters in units identified as

industrial furnaces according to 40 CFR 260.10

(1), (6), (7), (11), and (12) under the

definition of ``industrial furnaces''.RZINC: Resmelting in high temperature metal recovery

units for the purpose of recovery of zinc.STABL: Stabilization with the following reagents (or

waste reagents) or combinations of reagents:

(1) Portland cement; or (2) lime/pozzolans

(e.g., fly ash and cement kiln dust)--this does

not preclude the addition of reagents (e.g.,

iron salts, silicates, and clays) designed to

enhance the set/cure time and/or compressive

strength, or to overall reduce the leachability

of the metal or inorganic.SSTRP: Steam stripping of organics from liquid wastes

utilizing direct application of steam to the

wastes operated such that liquid and vapor flow

rates, as well as temperature and pressure

ranges, have been optimized, monitored, and

maintained. These operating parameters are

dependent upon the design parameters of the

unit, such as the number of separation stages

and the internal column design, thus, resulting

in a condensed extract high in organics that

must undergo either incineration, reuse as a

fuel, or other recovery/reuse and an extracted

wastewater that must undergo further treatment

as specified in the standard.VTD: Vacuum thermal desorption of low-level

radioactive hazardous mixed waste in units in

compliance with all applicable radioactive

protection requirements under control of the

Nuclear Regulatory Commission.WETOX: Wet air oxidation performed in units operated

such that a surrogate compound or indicator

parameter has been substantially reduced in

concentration in the residuals (e.g., Total

Organic Carbon can often be used as an

indicator parameter for the oxidation of many

organic constituents that cannot be directly

analyzed in wastewater residues).

WTRRX: Controlled reaction with water for highly

reactive inorganic or organic chemicals with

precautionary controls for protection of

workers from potential violent reactions as

well as precautionary controls for potential

emissions of toxic/ignitable levels of gases

released during the reaction.------------------------------------------------------------------------Note 1: When a combination of these technologies (i.e., a treatment

train) is specified as a single treatment standard, the order of

application is specified in Sec. 268.42, Table 2 by indicating the

five letter technology code that must be applied first, then the

designation ``fb.'' (an abbreviation for ``followed by''), then the

five letter technology code for the technology that must be applied

next, and so on.Note 2: When more than one technology (or treatment train) are specified

as alternative treatment standards, the five letter technology codes

(or the treatment trains) are separated by a semicolon (;) with the

last technology preceded by the word ``OR''. This indicates that any

one of these BDAT technologies or treatment trains can be used for

compliance with the standard.

(b) Any person may submit an application to the Administrator demonstrating that an alternative treatment method can achieve a measure of performance equivalent to that achieved by methods specified in paragraphs (a), (c), and (d) of this section for wastes or specified in Table 1 of Sec. 268.45 for hazardous debris. The applicant must submit information demonstrating that his treatment method is in compliance with federal, state, and local requirements and is protective of human health and the environment. On the basis of such information and any other available information, the Administrator may approve the use of the alternative treatment method if he finds that the alternative treatment method provides a measure of performance equivalent to that achieved by methods specified in paragraphs (a), (c), and (d) of this section for wastes or in Table 1 of Sec. 268.45 for hazardous debris. Any approval must be stated in writing and may contain such provisions and conditions as the Administrator deems appropriate. The person to whom such approval is issued must comply with all limitations contained in such a determination.

(c) As an alternative to the otherwise applicable subpart D treatment standards, lab packs are eligible for land disposal provided the following requirements are met:

(1) The lab packs comply with the applicable provisions of 40 CFR 264.316 and 40 CFR 265.316;

(2) The lab pack does not contain any of the wastes listed in Appendix IV to part 268;

(3) The lab packs are incinerated in accordance with the requirements of 40 CFR part 264, subpart O or 40 CFR part 265, subpart O; and

(4) Any incinerator residues from lab packs containing D004, D005, D006, D007, D008, D010, and D011 are treated in compliance with the applicable treatment standards specified for such wastes in subpart D of this part.

(d) Radioactive hazardous mixed wastes are subject to the treatment standards in Sec. 268.40. Where treatment standards are specified for radioactive mixed wastes in the Table of Treatment Standards, those treatment standards will govern. Where there is no specific treatment standard for radioactive mixed waste, the treatment standard for the hazardous waste (as designated by EPA waste code) applies. Hazardous debris containing radioactive waste is subject to the treatment standards specified in Sec. 268.45. [51 FR 40642, Nov. 7, 1986, as amended at 52 FR 25790, July 8, 1987; 55 FR 22692, June 1, 1990; 56 FR 3884, Jan. 31, 1991; 57 FR 8089, Mar. 6, 1992; 57 FR 37273, Aug. 18, 1992; 58 FR 29885, May 24, 1993; 59 FR 31552, June 20, 1994; 59 FR 48103, Sept. 19, 1994; 60 FR 302, Jan. 3, 1995; 61 FR 15654, Apr. 8, 1996; 62 FR 26025, May 12, 1997; 63 FR 28738, May 26, 1998; 71 FR 40278, July 14, 2006; 73 FR 27767, May 14, 2008]