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Simultaneous stripping and solvent extraction for the recovery of ammonia and acid gases from wastewaters

Technical Report ·
OSTI ID:7128127
A processing approach is proposed which has the potential for reducing energy requirements for the recovery of ammonia and acid gases (e.g. CO/sub 2/ and H/sub 2/S) from wastewaters. Two separation processes, solvent extraction and steam stripping, are carried out simultaneously. One process preferentially removes the acid gases, the other the basic gas (NH/sub 3/). The key to the process is the identification of a suitable solvent for one of the components. No common solvents were found to be effective for extraction of either CO/sub 2/ or H/sub 2/S at the usual pH of such wastewaters. Only liquid cation exchangers were found to be suitable extractants for ammonia. Solvents containing an acid of intermediate strength, di-2-ethylhexyl phosphoric acid (D2EHPA) have more favorable properties. Diluent choice affected the properties of D2EHPA-containing solvents. Batch experiments comparing solvent extraction/stripping with stripping alone confirmed that the former resulted in increased CO/sub 2/ volatility and served to isolate NH/sub 3/ from CO/sub 2/. Analysis of the overall economics of the process indicates that costs for replenishment of D2EHPA due to aqueous solubility losses and for the energy to regenerate the solvent are dominant. An improved extractant is needed if this approach is to offer economical advantages over other established approaches for recovering and isolating ammonia from such water streams.
Research Organization:
Lawrence Berkeley Lab., CA (USA)
DOE Contract Number:
AC03-76SF00098
OSTI ID:
7128127
Report Number(s):
LBL-17740; ON: DE84011816
Country of Publication:
United States
Language:
English