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Nonhalogenated VOC's:
Acetone, Styrene, etc.

Nonhalogenated VOC's in Air Emissions / Off-Gases
Three technologies that are most commonly used to treat nonhalogenated VOC's in air emissions/off-gases are:

Carbon Adsorption


Carbon Absorption Diagram.

Carbon adsorption is a remediation technology in which pollutants are removed from air by physical adsorption onto the carbon grain. Carbon is "activated" for this purpose by processing the carbon to create porous particles with a large internal surface area (300 to 2,500 square meters per gram of carbon) that attracts and adsorbs organic molecules as well as certain metal and other inorganic molecules.

Commercial grades of activated carbon are available for specific use in vapour-phase applications. The granular form of activated carbon is typically used in packed beds through which the contaminated air flows until the concentration of contaminants in the effluent from the carbon bed exceeds an acceptable level. Granular activated carbon systems typically consist of one or more vessels filled with carbon connected in series and/or parallel operating under atmospheric, negative, or positive pressure. The carbon can then be regenerated in place, regenerated at an off-site regeneration facility, or disposed of, depending upon economic considerations.

Catalytic Oxidation


Catalytic Oxidation Diagram.

Catalytic oxidation is an alternative for the treatment of VOC's in air streams resulting from remedial operations. VOC's are thermally destroyed at temperatures typically ranging from 200°C to 600°C by using a solid catalyst.

First, the contaminated air is directly preheated (electrically or, more frequently, using natural gas or propane) to reach a temperature necessary to initiate the catalytic oxidation of the VOC's. Then the preheated VOC-laden air is passed through a bed of solid catalysts where the VOC's are rapidly oxidised. In most cases, the process can be enhanced to reduce auxiliary fuel costs by using an air-to-air heat exchanger to transfer heat from the exhaust gases to the incoming contaminated air. Typically, about 50% of the heat of the exhaust gases is recovered. Depending on VOC concentrations, the recovered heat may be sufficient to sustain oxidation without additional fuel. Catalyst systems used to oxidise VOC's typically use metal oxides such as nickel oxide, copper oxide, manganese dioxide, or chromium oxide. Metals such as platinum and palladium may also be used. However, in a majority of remedial applications, non-precious metals (e.g., nickel, copper, or chromium) are used. Most commercially available catalysts are proprietary.

Thermal Oxidation


Thermal Oxidation Diagram.

Thermal oxidation equipment is used for destroying contaminants in the exhaust gas from air strippers and SVE systems.

Thermal oxidation units are typically single chamber, refractory-lined oxidisers equipped with a propane or natural gas burner and a stack. Lightweight ceramic blanket refractory is used because many of these units are mounted on skids or trailers. Thermal oxidisers are often equipped with heat exchangers where combustion gas is used to preheat the incoming contaminated gas. Operating temperatures range from 700°C to 1000°C, and gas residence times are typically 1 second or less.
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MEL LTD, Environmental remediation contractors, Newmillerdam Business Park, Wakefield, WF2 6QW, England, UK.
Tel: 01924 251101 Fax: 01924 240448 Email: mail@melltd.com

MEL (Ireland) LTD, 45 Aughrim Street, Dublin 7, Ireland Tel: 00353 1 8685398 Fax: 00353 1 8685412. Also at; 28 Campsie Industrial Estate, McLean Road, Londonderry BT47 3XX, Tel: 02871 865869 Fax: 02871 860942