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U.S. Department of Energy
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A novel liquid membrane technique for removal of SO sub 2 /NO sub x from flue gas

Technical Report ·
DOI:https://doi.org/10.2172/7073737· OSTI ID:7073737
The objective of this project is to measure the permeability coefficients of SO{sub 2}, CO{sub 2}, NO, O{sub 2} and N{sub 2} through a variety of immobilized liquid membranes using simulated flue gas mixtures, select the promising liquid membranes, study the extent of flue gas purification achieved in a novel microporous hollow-fiber-contained liquid membrane (HFCLM) permeator using selected membrane liquids, and determine the stability and reliability of this novel permeator for different operational modes. The simulated flue gas mixture to be used for the project should have a composition of around CO{sub 2} 12%, N{sub 2} 74%, O{sub 2} 1.8%, H{sub 2}O 12%, NO 0.045% and SO{sub 2} 0.5%. The ultimate target for purification is simultaneous 90% reduction of SO{sub 2} and NO. A SO{sub 2}/CO{sub 2} selectivity in the range of 50--200 is desirable along with high SO{sub 2} and NO flux. Measurements are to be made primarily at 25{degree}C with one measurement at 70{degree}C for the selected liquid membranes. Membranes tested include solutions of NaHSO{sub 3}, Na{sub 2}SO{sub 3}, Fe{sup 2+} EDTA and Fe{sup 3+} EDTA. 33 refs., 17 figs., 35 tabs.
Research Organization:
Stevens Inst. of Tech., Hoboken, NJ (USA). Dept. of Chemistry and Chemical Engineering
Sponsoring Organization:
DOE/FE
DOE Contract Number:
AC22-87PC79853
OSTI ID:
7073737
Report Number(s):
DOE/PC/79853-T1; ON: DE90013757
Country of Publication:
United States
Language:
English