TY - JOUR
T1 - Recovery of liquid CO2 from cleaning solutions without phase change using ultrafiltration and microfiltration membranes
AU - Photinon, K.
AU - Boddu, A.
AU - Ilias, Shamsuddin
PY - 2003/1/1
Y1 - 2003/1/1
N2 - Recovery of liquid and supercritical fluid (SCF) CO2 in the application of CO2 as processing solvent in extraction, chemical, and biochemical reactions is an important issue. Membrane-based separation may provide an option in recovering CO2 in liquid and/or SCF phase without expensive, energy intensive recompression. The potential application of microporous inorganic membranes in separating liquid CO2 without phase change was investigated. A high-pressure membrane filtration unit was designed, built, and tested. Microporous stainless steel (0.2 μm) and ceramic (0.02 μm, and 1000 Dalton) tubular elements were retrofitted into in-house designed, high-pressure housings to test the functionality of the system using Triton X-100 solute in liquid CO2 as feed. In-house designed fiberoptic cells coupled with a UV-VIS spectrophotometer was used for on-line measurement of solute Triton X-100 in the feed and permeate streams. The fiberoptic cell coupled with UV-VIS spectrophotometer was capable of providing on-line concentration measurement of Triton X-100 at operating pressures up to 100 bar. Two different path-length fiberoptic cells, 5.0 mm and 0.5 mm, were designed and built to cover a wide range of solute concentrations. Membrane filtration experiments with ceramic membranes showed that 1000-Dalton membrane offered a solute rejectivity of about 80%. The coarse ceramic membrane (0.02 μm) had a lower rejectivity, which was about 55%. The 0.2-μm stainless steel membrane provided very little solute rejectivity.
AB - Recovery of liquid and supercritical fluid (SCF) CO2 in the application of CO2 as processing solvent in extraction, chemical, and biochemical reactions is an important issue. Membrane-based separation may provide an option in recovering CO2 in liquid and/or SCF phase without expensive, energy intensive recompression. The potential application of microporous inorganic membranes in separating liquid CO2 without phase change was investigated. A high-pressure membrane filtration unit was designed, built, and tested. Microporous stainless steel (0.2 μm) and ceramic (0.02 μm, and 1000 Dalton) tubular elements were retrofitted into in-house designed, high-pressure housings to test the functionality of the system using Triton X-100 solute in liquid CO2 as feed. In-house designed fiberoptic cells coupled with a UV-VIS spectrophotometer was used for on-line measurement of solute Triton X-100 in the feed and permeate streams. The fiberoptic cell coupled with UV-VIS spectrophotometer was capable of providing on-line concentration measurement of Triton X-100 at operating pressures up to 100 bar. Two different path-length fiberoptic cells, 5.0 mm and 0.5 mm, were designed and built to cover a wide range of solute concentrations. Membrane filtration experiments with ceramic membranes showed that 1000-Dalton membrane offered a solute rejectivity of about 80%. The coarse ceramic membrane (0.02 μm) had a lower rejectivity, which was about 55%. The 0.2-μm stainless steel membrane provided very little solute rejectivity.
KW - Crossflow ultrafiltration and microfiltration
KW - Liquid and supercritical CO2
KW - Membrane-based separations
KW - Separation with phase change
KW - Triton X-100 surfactant
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U2 - 10.1081/SS-120022580
DO - 10.1081/SS-120022580
M3 - Conference article
SN - 0149-6395
VL - 38
SP - 2951
EP - 2962
JO - Separation Science and Technology (Philadelphia)
JF - Separation Science and Technology (Philadelphia)
IS - 12-13
ER -