(BAT) Reference Document for the Production of Chlor-alkali ...

(BAT) Reference Document for the Production of Chlor-alkali ... (BAT) Reference Document for the Production of Chlor-alkali ...

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Chapter 4 Cross-media effects If the contaminated soil is removed, additional emissions may result from the mobilisation of pollutants and additional soil is required to substitute the confined soil. Raw materials and energy are used for the confinement. Technical considerations relevant to applicability Some containment techniques are restricted by existing buildings and underground equipment. The removal of soil can be difficult if the contamination is present at some depth and/or in the in the presence of an aquifer [ 245, Euro Chlor 2009 ]. Economics Containment techniques are more economical than decontamination techniques. The total costs for site remediation in Rheinfelden (Germany) including incineration of the soil fraction with the heaviest PCDD/PCDF contamination amounted to EUR 24 million. A complete decontamination was considered to be not economical due to the elevated costs and the fact that the risk of ground water contamination with PCDDs/PCDFs could be excluded [ 240, Otto et al. 2006 ]. Driving force for implementation The driving forces for implementation of this technique include: environmental legislation; reduction of costs. Example plants Mercury cell chlor-alkali plant in Skutskär (Sweden), in operation from 1949 – 1977 [ 75, COM 2001 ], [ 278, Verberne and Maxson 2000 ]; Mercury cell chlor-alkali plant in Pavlodar (Kazakhstan), put into operation in 1975, chlorine capacity 100 kt/yr [ 262, Ilyushchenko et al. 2008 ]; Mercury and diaphragm cell chlor-alkali plant in Rheinfelden (Germany), put into operation in 1890 [ 240, Otto et al. 2006 ]. {Please TWG provide more examples.} Reference Literature [ 75, COM 2001 ], [ 240, Otto et al. 2006 ], [ 244, Hinton and Veiga 2001 ], [ 245, Euro Chlor 2009 ], [ 262, Ilyushchenko et al. 2008 ], [ 278, Verberne and Maxson 2000 ] 4.5.4 Decontamination 4.5.4.1 Overview Decontamination is frequently carried out by excavation of the soil and ex-situ treatment, either on site of off site, while in-situ treatment is less frequently applied. WORKING DRAFT IN PROGRESS Excavated contaminated soil is waste according to the Waste Framework Directive. It falls under chapter 17 05 of the European List of Waste. Depending on the properties, the excavated contaminated soil may fulfil the criteria for hazardous waste [ 145, Decision 2000/532/EC 2000 ], [ 269, Waste Framework Directive 98/EC 2008 ]. Ex-situ techniques for decontamination are therefore described in the Waste Treatments Industries BREF (e.g. immobilisation, thermal desorption, vapour extraction, solvent extraction, soil washing) [ 267, COM 2006 ] and the Waste Incineration BREF (e.g. incineration, mercury abatement, PCDD/PCDF abatement) [ 268, COM 2006 ]. The techniques described in 260 December 2011 TB/EIPPCB/CAK_Draft_1

Chapter 4 Sections 4.5.4.2 and 4.5.4.3 constitute specific examples of waste treatments relevant for contaminated chlor-alkali sites. Table 4.24 summarises potential techniques for the decontamination of mercury-contaminated soils. Table 4.24: Potential techniques for the decontamination of mercury-contaminated soils Technique Description Thermal desorption is an ex-situ physical technique to remove mercury from the contaminated medium. Heat is supplied under reduced pressure to the contaminated Thermal soil or waste, volatilising mercury. The off-gas is treated by condensation to desorption generate liquid elemental mercury. The off-gas may require further treatment also depending on the presence of other pollutants. The technique has been used at full scale including chlor-alkali sites (see Section 4.5.4.2). Vapour extraction is based on in-situ volatilisation of mercury by applying vacuum Vapour and heat followed by treatment of the exhaust gases. The technique has been used at extraction full scale, but not at chlor-alkali sites. Soil washing is an ex-situ technique that takes advantage of the behavior of mercury to preferentially adsorb onto fine particles. The contaminated soil is suspended in a wash solution and the fine particles are separated from the suspension, thereby Soil washing reducing the contaminant concentration in the remaining soil. The extraction of and extraction mercury from the fine particles fraction can be based on desorption of adsorbed species, oxidation of metallic mercury, complexation and dissolution (e.g. by using acids). The technique has been used at full scale including chlor-alkali sites (see Section 4.5.4.3). Solidification and stabilisation are ex-situ techniques which reduce the mobility of hazardous substances and contaminants in the environment through both physical and chemical means. This technique physically binds or encloses contaminants within a stabilised mass and chemically reduces the hazard potential by converting Solidification the contaminants into less soluble, mobile, or toxic forms. Amalgamation is and stabilisation typically used to immobilise elemental mercury and is often combined with encapsulation to prevent volatisation of mercury from the amalgam. The technique has been used at full scale including chlor-alkali sites. Soluble mercury may be immobilised in-situ by precipitation as mercury sulphide. Vitrification is a high-temperature treatment designed to immobilise contaminants ex-situ or in-situ by incorporating them in the vitrified end product, which is chemically durable and leach resistant. The primary residue generated by this technique is typically glass cullet or aggregate. Secondary residues generated are air Vitrification emissions, scrubber liquor, carbon filters, and used hood panels. This technique may also cause contaminants to volatilise or undergo thermal destruction, thereby reducing their concentration in the soil. The technique has been used at full scale, but not at chlor-alkali sites. Source: [ 244, Hinton and Veiga 2001 ], [ 245, Euro Chlor 2009 ], [ 266, US EPA 2007 ] Techniques for treating mercury-contaminated waste water arising during decontamination are described in Section 4.1.3.1 and in the CWW and WT BREFs [ 124, COM 2011 ], [ 267, COM 2006 ]. Techniques for treating mercury-containing waste gases arising during decontamination are described in Section 4.1.3.1 and in the WT and WI BREFs [ 267, COM 2006 ], [ 268, COM 2006 ]. WORKING DRAFT IN PROGRESS 4.5.4.2 Thermal desorption Description This technique consists in heating excavated soil (on site or off site) to volatilise mercury and other organic compounds (e.g. PCDDs/PCDFs and halogenated organic compounds) with subsequent treatment of the resulting waste gases. TB/EIPPCB/CAK_Draft_1 December 2011 261

Chapter 4<br />

Sections 4.5.4.2 and 4.5.4.3 constitute specific examples <strong>of</strong> waste treatments relevant <strong>for</strong><br />

contaminated chlor-<strong>alkali</strong> sites.<br />

Table 4.24 summarises potential techniques <strong>for</strong> <strong>the</strong> decontamination <strong>of</strong> mercury-contaminated<br />

soils.<br />

Table 4.24: Potential techniques <strong>for</strong> <strong>the</strong> decontamination <strong>of</strong> mercury-contaminated soils<br />

Technique Description<br />

Thermal desorption is an ex-situ physical technique to remove mercury from <strong>the</strong><br />

contaminated medium. Heat is supplied under reduced pressure to <strong>the</strong> contaminated<br />

Thermal soil or waste, volatilising mercury. The <strong>of</strong>f-gas is treated by condensation to<br />

desorption generate liquid elemental mercury. The <strong>of</strong>f-gas may require fur<strong>the</strong>r treatment also<br />

depending on <strong>the</strong> presence <strong>of</strong> o<strong>the</strong>r pollutants. The technique has been used at full<br />

scale including chlor-<strong>alkali</strong> sites (see Section 4.5.4.2).<br />

Vapour extraction is based on in-situ volatilisation <strong>of</strong> mercury by applying vacuum<br />

Vapour<br />

and heat followed by treatment <strong>of</strong> <strong>the</strong> exhaust gases. The technique has been used at<br />

extraction<br />

full scale, but not at chlor-<strong>alkali</strong> sites.<br />

Soil washing is an ex-situ technique that takes advantage <strong>of</strong> <strong>the</strong> behavior <strong>of</strong> mercury<br />

to preferentially adsorb onto fine particles. The contaminated soil is suspended in a<br />

wash solution and <strong>the</strong> fine particles are separated from <strong>the</strong> suspension, <strong>the</strong>reby<br />

Soil washing reducing <strong>the</strong> contaminant concentration in <strong>the</strong> remaining soil. The extraction <strong>of</strong><br />

and extraction mercury from <strong>the</strong> fine particles fraction can be based on desorption <strong>of</strong> adsorbed<br />

species, oxidation <strong>of</strong> metallic mercury, complexation and dissolution (e.g. by using<br />

acids). The technique has been used at full scale including chlor-<strong>alkali</strong> sites (see<br />

Section 4.5.4.3).<br />

Solidification and stabilisation are ex-situ techniques which reduce <strong>the</strong> mobility <strong>of</strong><br />

hazardous substances and contaminants in <strong>the</strong> environment through both physical<br />

and chemical means. This technique physically binds or encloses contaminants<br />

within a stabilised mass and chemically reduces <strong>the</strong> hazard potential by converting<br />

Solidification<br />

<strong>the</strong> contaminants into less soluble, mobile, or toxic <strong>for</strong>ms. Amalgamation is<br />

and stabilisation<br />

typically used to immobilise elemental mercury and is <strong>of</strong>ten combined with<br />

encapsulation to prevent volatisation <strong>of</strong> mercury from <strong>the</strong> amalgam. The technique<br />

has been used at full scale including chlor-<strong>alkali</strong> sites. Soluble mercury may be<br />

immobilised in-situ by precipitation as mercury sulphide.<br />

Vitrification is a high-temperature treatment designed to immobilise contaminants<br />

ex-situ or in-situ by incorporating <strong>the</strong>m in <strong>the</strong> vitrified end product, which is<br />

chemically durable and leach resistant. The primary residue generated by this<br />

technique is typically glass cullet or aggregate. Secondary residues generated are air<br />

Vitrification<br />

emissions, scrubber liquor, carbon filters, and used hood panels. This technique<br />

may also cause contaminants to volatilise or undergo <strong>the</strong>rmal destruction, <strong>the</strong>reby<br />

reducing <strong>the</strong>ir concentration in <strong>the</strong> soil. The technique has been used at full scale,<br />

but not at chlor-<strong>alkali</strong> sites.<br />

Source: [ 244, Hinton and Veiga 2001 ], [ 245, Euro <strong>Chlor</strong> 2009 ], [ 266, US EPA 2007 ]<br />

Techniques <strong>for</strong> treating mercury-contaminated waste water arising during decontamination are<br />

described in Section 4.1.3.1 and in <strong>the</strong> CWW and WT BREFs [ 124, COM 2011 ], [ 267, COM<br />

2006 ]. Techniques <strong>for</strong> treating mercury-containing waste gases arising during decontamination<br />

are described in Section 4.1.3.1 and in <strong>the</strong> WT and WI BREFs [ 267, COM 2006 ], [ 268, COM<br />

2006 ].<br />

WORKING DRAFT IN PROGRESS<br />

4.5.4.2 Thermal desorption<br />

Description<br />

This technique consists in heating excavated soil (on site or <strong>of</strong>f site) to volatilise mercury and<br />

o<strong>the</strong>r organic compounds (e.g. PCDDs/PCDFs and halogenated organic compounds) with<br />

subsequent treatment <strong>of</strong> <strong>the</strong> resulting waste gases.<br />

TB/EIPPCB/CAK_Draft_1 December 2011 261

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