Recovery of calcium carbonate and hydrogen sulfide from waste calcium sulfide

被引:21
作者
Brooks, MW
Lynn, S
机构
[1] UNIV CALIF BERKELEY,DEPT CHEM ENGN,BERKELEY,CA 94720
[2] UNIV CALIF BERKELEY,LAWRENCE BERKELEY LAB,BERKELEY,CA 94720
关键词
D O I
10.1021/ie970151j
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The removal of H2S from hot coal gas using a limestone-based sorbent generates a large quantity of calcium sulfide waste (e.g., 67 tons/day from the gasification of 1000 tons/day of 3% S coal) that cannot be landfilled because of potential H2S evolution and sulfide leaching. In the process proposed here, the CaS is dissolved by reaction with H2S complexed with aqueous methyldiethanolamine (MDEA) or other alkanolamines. In the second step, the highly soluble Ca(HS)(2) reacts readily with CO2, also complexed with aqueous MDEA, to precipitate pure CaCO3 of uniform crystal size and to form MDEA-complexed H2S in solution. The solution from step 2 is split-half is recycled to step 1 and half is sent to a stripper to recover H2S and from there to a column where the needed CO2 is absorbed from a combustion gas.
引用
收藏
页码:4236 / 4242
页数:7
相关论文
共 13 条
[1]  
BISWAS SC, 1976, FERT TECHNOL, V13, P255
[2]  
BROOKS MW, 1995, THESIS U CALIFORNIA
[3]  
*BRYAN RES ENG, 1995, TSWEET SIM PROGR VER
[4]  
FENOUIL LA, 1995, IND ENG CHEM RES, V34, P2324, DOI 10.1021/ie00046a014
[5]   STUDY OF CALCIUM-BASED SORBENTS FOR HIGH-TEMPERATURE H2S REMOVAL .2. KINETICS OF H2S SORPTION BY CALCINED LIMESTONE [J].
FENOUIL, LA ;
LYNN, S .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (07) :2334-2342
[6]  
JEFFERY GH, 1989, VOGELS TXB QUANTITAT, P389
[7]  
KEAIRNS DL, 1974, ENV ASPECTS FUEL CON
[8]  
Perry RE., 1984, PERRYS CHEM ENG HDB, V6th
[9]  
SCHWERDTFEGER K, 1993, ERDOL KOHLE ERDGAS P, V46, P103
[10]  
Siedell A., 1940, Solubilities of Inorganic and Metal Organic Compounds