Table 1.1	Magnitude and pathway of toxic releases into the environment in the United States and the State of Illinois in 1989 (USEPA Toxic Release Inventory, 1991).
Table 1.2	USEPA VOC categories based on vapor pressure (USEPA Control Technology Guideline Series, 1991).
Table 1.3	TVOC and acetone sources, pathways, exposure and human health effects (National Institute for Occupational Safety and Health Guide to Chemical Hazards, 1990).
Table 1.4	Primary categories of industrial sources emitting HAPs.
Table 1.5	Control devices commercially available for VOC removal from effluent gas streams (Ruddy and Carroll, 1993).
Table 1.6	Applicability of VOC control technologies to specific VOC categories (Moretti and Mukhopadhyay, 1993).
Table 3.1	Industrial gas adsorption separation processes (Keller, 1983).
Table 3.2	Industrial TVOC emissions that may be recovered efficiently by ACFC sorption.
Table 3.3	Commercial adsorbents that are commonly used in gas separation and purification (Noll, 1991).
Table 3.4	Experimental constants for use in the Wagner equation (Reid et al., 1977).
Table 3.5	Refrigerant selection based on temperature.
Table 3.6	Theoretical removal efficiencies for three refrigerants, Acetone and two TVOCs with a 10% by volume inlet gas stream.
Table 3.7	List of commercially available activated carbon fiber and cloth (Suzuki, 1994).
Table 3.8	Physical properties of Kynol ACC-5092 (Foster, 1992).
Table 3.9	Physical characteristics of KynolTM ACC-5092-20 30.
Table 4.1	Summary of acetone adsorption breakthrough tests with ACFC-fixed bed.
Table 4.2	Summary of acetone adsorption breakthrough tests with ACFC packed-bed.
Table 4.3	Summary of MEK adsorption breakthrough tests with ACFC fixed-bed.
Table 4.4	DA and DR parameters for adsorption of acetone and MEK with ACC-5092-20.
Table 4.5	K and ts coefficients for the BTC dynamic model.
Table 4.6	Summary of regeneration tests for desorption of acetone from ACFC-fixed bed
Table 4.7	Summary of regeneration tests for desorption of MEK from ACFC-fixed bed
Table 4.8	Percent impurities analyzed relative to acetone abundance for acetone blank sample
Table 4.9	Percent impurities analyzed relative to acetone abundance for adsorption/ desorption/condensation acetone sample
Table 5.1	Mass transfer/thermodynamic model results for scale-up condenser design
Table 5.2	Activated Carbon Fiber Cloth (ACFC Fixed Bed Adsorber and cryogenic condenser for Toxic Volatile Organic Compounds (TVOC)
Table 5.3	Break-even analysis for Scenario II
Table 5.4	Mass transfer/thermodynamic model results for scale-up condenser design
Table 5.5	Shell-and-tube capital cost analysis for an 8 ft tube length, 14 BWG fixed tubesheet condenser with 262 ft2 surface area. Derived cost factors from USEPAb, (Carmichael, 1996)
Table 5.6	Shell-and-tube annual cost analysis for an 8 ft tube length, 14 BWG fixed tubesheet condenser with 262 ft2 surface area. Derived cost factors from USEPAb, 1991)