CN1421264A - Absorbing liquid for eliminating sulfide from gas mixture - Google Patents

Absorbing liquid for eliminating sulfide from gas mixture Download PDF

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Publication number
CN1421264A
CN1421264A CN 02148499 CN02148499A CN1421264A CN 1421264 A CN1421264 A CN 1421264A CN 02148499 CN02148499 CN 02148499 CN 02148499 A CN02148499 A CN 02148499A CN 1421264 A CN1421264 A CN 1421264A
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absorption liquid
methyl
liquid according
sterically hindered
concentration
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CN 02148499
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CN1219579C (en
Inventor
毛松柏
朱道平
肖红
丁雅萍
陆建刚
叶宁
黄晓燕
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Jiangsu Landian Environmental Protection Co ltd
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Research Institute of Nanjing Chemical Industry Group Co Ltd
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Abstract

The present invention belongs to gas producing technology. The absorbing liquid for eliminating sulfide from gas mixture includes main absorbent comprising steric hindrance amine and N-methyl diethanolamine; cosolvent of one or several of sulfolane, N-methyl pyrrolidine, polyglycol dialkyl ether, morpholine and its derivative; catalyst of one or several of C2-C12 alkanolamine, piperazine and its derivative, quinoline, urea and metal phthalocyanine complex. Using the absorbing liquid can eliminate H2S, COS, mercaptan, thioether and other sulfide in less steps.

Description

From admixture of gas, remove the absorption liquid of sulfide
Technical field
The invention belongs to the gas purification technique field, be specifically related to from admixture of gas, remove H 2The absorption liquid of S, COS, mercaptan, thioether sulfides.
Background technology
Usually contain H in the process gas flows such as natural gas, refinery gas, synthesis gas 2S, COS, mercaptan, thioether sulfides must remove them before further utilizing.The alkanolamine method is to remove H 2The method that acid gas impurities such as S are the most frequently used.As; US4,551,158; US4,553,984; US4,537,753; CA1291321; CA1295810; DE1904428; US4,775,519 grades all are to be the sulfur method of host with N methyldiethanol amine (MDEA).But said method is organic sulfide removal effectively.
US3,716,620 propose to add iodine in amine aqueous solution removes H 2S and mercaptan.
US4,808,765 propose to remove H in the unstripped gas with MDEA and diisopropanolamine (DIPA) (DIPA) mixed solution 2S and COS.
US5,589,149 propose to remove mercaptan in the unstripped gas with the mixed solution of amine aqueous solution and polyethylene glycol alkyl ether.
DE19933301 proposes to remove H with MDEA and piperazine 2S and mercaptan.
DE19947845 proposes with MDEA and removes H 2S and COS.
Said method all fails with amine aqueous solution organic sulfur and inorganic sulfur to be removed simultaneously, thereby also need increase other desulfurizer.
Summary of the invention
The objective of the invention is to, propose a kind of novel solution, it is compared with traditional sulfur method, can be simultaneously with H 2S, COS, mercaptan, thioether sulfides remove, thereby have reduced treatment process, make sulfur method more economical.
Absorption liquid of the present invention comprises (1) main absorbent, is made up of sterically hindered amines (I) and N methyldiethanol amine (II); (2) cosolvent (III) is made up of in the following material one or more: sulfolane, N-methyl pyrrolidone, polyethylene glycol dialkyl ether, morpholine and derivative thereof; (3) catalyst (IV) is made up of in the following material one or more: C 2~C 12Alkyl chain alcohol amine, piperazine and derivative thereof, quinoline compound, urea, metallo phthalocyanine.Specific as follows:
1, the aqueous solution with sterically hindered amines (I) and N methyldiethanol amine (II) is main absorber.Its concentration is 10~70% (wt), but is preferably 30~50% (wt).Component (II) is 0.5~4: 4.5~1 with the mol proportioning of component (I), but is preferably 1~2: 3~2.Component (I) can be a kind of single sterically hindered amines, also can be the mixture of several sterically hindered amines.The sterically hindered amines of indication of the present invention is to have one or more alcamine compounds with non-linear carbochain of sterically hindered structure on nitrogen-atoms, comprising: 2-piperidines ethanol (2-piperidineethanol), 2-(2-tert-butylamine base) propoxyl group ethanol (2-(2-teriarybutylamino) propoxyethanol), 2-amino-2-methyl-1-propanol (2-amino-2-methyl-1-propanol), tert-butylamine base diethanol amine (teriarybutyldiethanolamine), (1-methyl isophthalic acid-second Propylamino) ethoxy ethanol ((1-methyl-1-ethylpropylamino) ethoxyethanol), 2-isopropylamine base-1-propyl alcohol (2-isopropylamino-1-propanol), tert-butylamine base oxethyl ethanol (teriarybutylaminoethoxyethanol), tert-butylamine base ethanol (teriarybutylaminoethanol), 3-tert-butylamine base n-butanol (3-teriarybutylamino-n-butanol) etc.
2, the concentration of cosolvent (III) is 5~60% (wt), but is preferably 10~30% (wt).Described morpholine derivative comprises methyl morpholine, formyl-morpholine, acetyl group morpholine; The polyethylene glycol dialkyl ether comprises NHD, polyethylene glycol diethyl ether.
3, the concentration of catalyst (IV) is 0.1~10% (wt), but is preferably 1~5% (wt).Described alkyl chain alcohol amine is: monoethanolamine, diethanol amine, triethanolamine, diglycolamine, diisopropanolamine (DIPA), methyl-ethanolamine; Bridged piperazine derivatives is an alkyl piperazine; Quinoline compound; Metallo phthalocyanine comprises sulfonated phthalocyanine cobalt, poly-phthalocyanine cobalt, quaternary ammonium alkalization phthalocyanine cobalt and FePC.
Specific embodiment embodiment one:
Absorption liquid is formed: main absorbent bulky amine (I) 15%, MDEA (II) 25%, cosolvent (III) N-methyl pyrrolidone etc. 10%, catalyst (IV) piperazine etc. 3%, unstripped gas is formed: N 280.5%, CO 216.5%, H 2S 3.0%, mercaptan 487mg/m 3Absorb in 40 ℃ of normal pressures, the mercaptan removal efficiency is: 90.6%.Embodiment two:
Absorption liquid is formed: main absorbent bulky amine (I) 25%, MDEA (II) 15%, cosolvent (III) formyl-morpholine etc. 5%, catalyst (IV) monoethanolamine etc. 3%, unstripped gas is formed: N 272.1%, CO 223.3%, H 2S 3.6%, thioether 538mg/m 3Absorb in 40 ℃ of monoethanolamine normal pressures, the thioether removal efficiency is: 76.8%.Embodiment three:
Absorption liquid is formed: main absorbent bulky amine (I) 15%, MDEA (II) 40%, cosolvent (III) N-methyl pyrrolidone etc. 5%, catalyst (IV) piperazine etc. 3%, unstripped gas is semiwater gas (N 221.8%, CO 28.0%, CO 28.5%, H 240.0%, O 20.4%, CH 41.3%, COS 136mg/m 3), 0.5MPa absorbs, 40 ℃ of tower top temperatures, and the COS removal efficiency is: 95.2%.Embodiment four:
Absorption liquid is: main absorbent bulky amine (I) 5%, MDEA (II) 15%, cosolvent (III) sulfolane 10%, catalyst (IV) diethanol amine etc. 5%, unstripped gas adopt conversion gas (N 216.98%, CO 228.43%, CO 1.20%, H 252.38%, CH 41.01%), allocates mercaptan 2132mg/m into 3, 0.5MPa absorbs, 40 ℃ of tower top temperatures, and the mercaptan removal efficiency is: 71.2%.

Claims (8)

1, a kind of absorption liquid that from admixture of gas, removes sulfide, it is characterized in that it mainly comprises (1) main absorbent, the aqueous solution of forming by sterically hindered amines (I) and N methyldiethanol amine (II), its concentration is 10~70% (wt), and component (II) is 0.5~4: 4.5~1 with the mol proportioning of component (I); (2) cosolvent, its concentration are 5~60% (wt), are made up of in the following material one or more: sulfolane, N-methyl pyrrolidone, polyethylene glycol dialkyl ether, morpholine and derivative thereof; (3) catalyst, its concentration are 0.1~10% (wt), are made up of in the following material one or more: C 2~C 12Alkyl chain alcohol amine, piperazine and derivative thereof, quinoline compound, urea, metallo phthalocyanine.
2, absorption liquid according to claim 1, it is characterized in that component (I) can be a kind of single sterically hindered amines, it also can be the mixture of several sterically hindered amines, the sterically hindered amines of indication is to have one or more alcamine compounds with non-linear carbochain of sterically hindered structure on nitrogen-atoms, comprising: 2-piperidines ethanol (2-piperidineethanol), 2-(2-tert-butylamine base) propoxyl group ethanol (2-(2-teriarybutylamino) propoxyethanol), 2-amino-2-methyl-1-propanol (2-amino-2-methyl-1-propanol), tert-butylamine base diethanol amine (teriarybutyldiethanolamine), (1-methyl isophthalic acid-second Propylamino) ethoxy ethanol ((1-methyl-1-ethylpropylamino) ethoxyethanol), tert-butylamine base oxethyl ethanol (teriarybutyl-aminoethoxyethanol), 2-isopropylamine base-1-propyl alcohol (2-isopropylamino-1-propanol), tert-butylamine base ethanol (teriarybutylaminoethanol), 3-tert-butylamine base n-butanol (3-teriarybutyl-amino-n-butanol) etc.
3, absorption liquid according to claim 1, the concentration that it is characterized in that main absorbent sterically hindered amines (I) and N methyldiethanol amine (II) is 30~50% (wt).
4, absorption liquid according to claim 1 is characterized in that the component (II) and the mol proportioning of component (I) are 1~2: 3~2.
5, absorption liquid according to claim 1, the concentration that it is characterized in that cosolvent (III) are 10~30% (wt).
6, absorption liquid according to claim 1 is characterized in that described morpholine derivative comprises methyl morpholine, formyl-morpholine, acetyl group morpholine; The polyethylene glycol dialkyl ether comprises NHD, polyethylene glycol diethyl ether.
7, absorption liquid according to claim 1, the concentration that it is characterized in that catalyst (IV) are 1~5% (wt).
8, absorption liquid according to claim 1 is characterized in that described alkyl chain alcohol amine is: monoethanolamine, diethanol amine, triethanolamine, diglycolamine, diisopropanolamine (DIPA), methyl-ethanolamine; Bridged piperazine derivatives is an alkyl piperazine; Quinoline compound; Metallo phthalocyanine comprises sulfonated phthalocyanine cobalt, poly-phthalocyanine cobalt, quaternary ammonium alkalization phthalocyanine cobalt and FePC.
CN 02148499 2002-12-11 2002-12-11 Absorbing liquid for eliminating sulfide from gas mixture Expired - Lifetime CN1219579C (en)

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