CN1398659A - Biochemical iron-alkali solution catalyzing process for desulfurizing gas - Google Patents
Biochemical iron-alkali solution catalyzing process for desulfurizing gas Download PDFInfo
- Publication number
- CN1398659A CN1398659A CN02130605A CN02130605A CN1398659A CN 1398659 A CN1398659 A CN 1398659A CN 02130605 A CN02130605 A CN 02130605A CN 02130605 A CN02130605 A CN 02130605A CN 1398659 A CN1398659 A CN 1398659A
- Authority
- CN
- China
- Prior art keywords
- iron
- alkali solution
- gas
- biochemical
- desulfurizing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000003513 alkali Substances 0.000 title claims abstract description 137
- 238000000034 method Methods 0.000 title claims abstract description 92
- 230000008569 process Effects 0.000 title claims description 69
- 230000003009 desulfurizing effect Effects 0.000 title claims description 55
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 336
- 229910052742 iron Inorganic materials 0.000 claims abstract description 183
- 241001148470 aerobic bacillus Species 0.000 claims abstract description 62
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 58
- -1 ferrous compound Chemical class 0.000 claims abstract description 48
- 239000011593 sulfur Substances 0.000 claims abstract description 35
- 229910052717 sulfur Inorganic materials 0.000 claims abstract description 35
- 230000008929 regeneration Effects 0.000 claims abstract description 23
- 238000011069 regeneration method Methods 0.000 claims abstract description 23
- 230000003647 oxidation Effects 0.000 claims abstract description 12
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 12
- 238000010521 absorption reaction Methods 0.000 claims abstract description 11
- 125000001741 organic sulfur group Chemical group 0.000 claims abstract description 11
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000007789 gas Substances 0.000 claims description 110
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 58
- 238000006477 desulfuration reaction Methods 0.000 claims description 33
- 150000008442 polyphenolic compounds Chemical class 0.000 claims description 31
- 235000013824 polyphenols Nutrition 0.000 claims description 31
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 30
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 28
- 230000023556 desulfurization Effects 0.000 claims description 26
- 239000000203 mixture Substances 0.000 claims description 25
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims description 24
- 150000002506 iron compounds Chemical class 0.000 claims description 24
- JVXHQHGWBAHSSF-UHFFFAOYSA-L 2-[2-[bis(carboxylatomethyl)amino]ethyl-(carboxylatomethyl)amino]acetate;hydron;iron(2+) Chemical compound [H+].[H+].[Fe+2].[O-]C(=O)CN(CC([O-])=O)CCN(CC([O-])=O)CC([O-])=O JVXHQHGWBAHSSF-UHFFFAOYSA-L 0.000 claims description 22
- 241000726221 Gemma Species 0.000 claims description 21
- 235000018553 tannin Nutrition 0.000 claims description 21
- 239000001648 tannin Substances 0.000 claims description 21
- 229920001864 tannin Polymers 0.000 claims description 21
- 150000001299 aldehydes Chemical class 0.000 claims description 19
- 239000005864 Sulphur Substances 0.000 claims description 18
- 239000000463 material Substances 0.000 claims description 18
- 241000894006 Bacteria Species 0.000 claims description 17
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 claims description 16
- 125000003118 aryl group Chemical group 0.000 claims description 16
- 150000001875 compounds Chemical class 0.000 claims description 16
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 16
- 229910021529 ammonia Inorganic materials 0.000 claims description 15
- ZRNHBOAYYNHVOY-UHFFFAOYSA-K 2-hydroxybenzoate;iron(3+) Chemical class [Fe+3].OC1=CC=CC=C1C([O-])=O.OC1=CC=CC=C1C([O-])=O.OC1=CC=CC=C1C([O-])=O ZRNHBOAYYNHVOY-UHFFFAOYSA-K 0.000 claims description 14
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 14
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 12
- 239000008280 blood Substances 0.000 claims description 12
- 210000004369 blood Anatomy 0.000 claims description 12
- 241000283690 Bos taurus Species 0.000 claims description 10
- 239000000126 substance Substances 0.000 claims description 10
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 claims description 8
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 claims description 8
- 239000002912 waste gas Substances 0.000 claims description 7
- AZQWKYJCGOJGHM-UHFFFAOYSA-N 1,4-benzoquinone Chemical compound O=C1C=CC(=O)C=C1 AZQWKYJCGOJGHM-UHFFFAOYSA-N 0.000 claims description 6
- 241000193830 Bacillus <bacterium> Species 0.000 claims description 6
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 6
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 claims description 6
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 6
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 claims description 6
- 239000013522 chelant Substances 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 6
- MUVQKFGNPGZBII-UHFFFAOYSA-N 1-anthrol Chemical compound C1=CC=C2C=C3C(O)=CC=CC3=CC2=C1 MUVQKFGNPGZBII-UHFFFAOYSA-N 0.000 claims description 4
- 241000422409 Alkalibacterium Species 0.000 claims description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 4
- MWPLVEDNUUSJAV-UHFFFAOYSA-N anthracene Chemical compound C1=CC=CC2=CC3=CC=CC=C3C=C21 MWPLVEDNUUSJAV-UHFFFAOYSA-N 0.000 claims description 4
- PYKYMHQGRFAEBM-UHFFFAOYSA-N anthraquinone Natural products CCC(=O)c1c(O)c2C(=O)C3C(C=CC=C3O)C(=O)c2cc1CC(=O)OC PYKYMHQGRFAEBM-UHFFFAOYSA-N 0.000 claims description 4
- 150000004056 anthraquinones Chemical class 0.000 claims description 4
- 238000005516 engineering process Methods 0.000 claims description 4
- 239000000284 extract Substances 0.000 claims description 4
- LNTHITQWFMADLM-UHFFFAOYSA-N gallic acid Chemical compound OC(=O)C1=CC(O)=C(O)C(O)=C1 LNTHITQWFMADLM-UHFFFAOYSA-N 0.000 claims description 4
- 125000005842 heteroatom Chemical group 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 4
- 239000011591 potassium Substances 0.000 claims description 4
- 229910052700 potassium Inorganic materials 0.000 claims description 4
- WQGWDDDVZFFDIG-UHFFFAOYSA-N pyrogallol Chemical compound OC1=CC=CC(O)=C1O WQGWDDDVZFFDIG-UHFFFAOYSA-N 0.000 claims description 4
- 150000004053 quinones Chemical class 0.000 claims description 4
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 claims description 4
- 239000006227 byproduct Substances 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 3
- MEIRRNXMZYDVDW-MQQKCMAXSA-N (2E,4E)-2,4-hexadien-1-ol Chemical compound C\C=C\C=C\CO MEIRRNXMZYDVDW-MQQKCMAXSA-N 0.000 claims description 2
- CBEYZWBXIPZYNH-UHFFFAOYSA-J 1,5-dihydroxypentan-3-yl phosphate;2,3-dihydroxypropyl phosphate;iron(2+) Chemical compound [Fe+2].[Fe+2].OCC(O)COP([O-])([O-])=O.OCCC(CCO)OP([O-])([O-])=O CBEYZWBXIPZYNH-UHFFFAOYSA-J 0.000 claims description 2
- KBPZVLXARDTGGD-UHFFFAOYSA-N 2,3-dihydroxybutanedioic acid;iron Chemical compound [Fe].OC(=O)C(O)C(O)C(O)=O KBPZVLXARDTGGD-UHFFFAOYSA-N 0.000 claims description 2
- DEQJBORXLQWRGV-UHFFFAOYSA-N 2-hydroxypropanoic acid;iron Chemical compound [Fe].CC(O)C(O)=O.CC(O)C(O)=O DEQJBORXLQWRGV-UHFFFAOYSA-N 0.000 claims description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 2
- 241000203069 Archaea Species 0.000 claims description 2
- KRKNYBCHXYNGOX-UHFFFAOYSA-K Citrate Chemical compound [O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O KRKNYBCHXYNGOX-UHFFFAOYSA-K 0.000 claims description 2
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 claims description 2
- 102000008857 Ferritin Human genes 0.000 claims description 2
- 108050000784 Ferritin Proteins 0.000 claims description 2
- 238000008416 Ferritin Methods 0.000 claims description 2
- PMVSDNDAUGGCCE-TYYBGVCCSA-L Ferrous fumarate Chemical compound [Fe+2].[O-]C(=O)\C=C\C([O-])=O PMVSDNDAUGGCCE-TYYBGVCCSA-L 0.000 claims description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
- 229930192627 Naphthoquinone Natural products 0.000 claims description 2
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 2
- NMKMOHFZXZFDFP-UHFFFAOYSA-N anthracene-1,2,3,4-tetrol Chemical compound C1=CC=CC2=CC3=C(O)C(O)=C(O)C(O)=C3C=C21 NMKMOHFZXZFDFP-UHFFFAOYSA-N 0.000 claims description 2
- KNCZUXHSQJQWIB-UHFFFAOYSA-N anthracene-1,4,9,10-tetrone Chemical compound O=C1C2=CC=CC=C2C(=O)C2=C1C(=O)C=CC2=O KNCZUXHSQJQWIB-UHFFFAOYSA-N 0.000 claims description 2
- NUZWLKWWNNJHPT-UHFFFAOYSA-N anthralin Chemical compound C1C2=CC=CC(O)=C2C(=O)C2=C1C=CC=C2O NUZWLKWWNNJHPT-UHFFFAOYSA-N 0.000 claims description 2
- YYXHRUSBEPGBCD-UHFFFAOYSA-N azanylidyneiron Chemical compound [N].[Fe] YYXHRUSBEPGBCD-UHFFFAOYSA-N 0.000 claims description 2
- 150000004054 benzoquinones Chemical class 0.000 claims description 2
- CHYQSXLXQCXPAA-UHFFFAOYSA-H butanedioate;iron(3+) Chemical compound [Fe+3].[Fe+3].[O-]C(=O)CCC([O-])=O.[O-]C(=O)CCC([O-])=O.[O-]C(=O)CCC([O-])=O CHYQSXLXQCXPAA-UHFFFAOYSA-H 0.000 claims description 2
- 150000001735 carboxylic acids Chemical class 0.000 claims description 2
- NKQPRNDTEUZYKT-UHFFFAOYSA-N cyclohex-5-ene-1,2,3,4-tetrone Chemical compound O=C1C=CC(=O)C(=O)C1=O NKQPRNDTEUZYKT-UHFFFAOYSA-N 0.000 claims description 2
- 150000005205 dihydroxybenzenes Chemical class 0.000 claims description 2
- OXLBLZDGMWMXSM-UHFFFAOYSA-N dioxido(dioxo)chromium;iron(3+) Chemical compound [Fe+3].[Fe+3].[O-][Cr]([O-])(=O)=O.[O-][Cr]([O-])(=O)=O.[O-][Cr]([O-])(=O)=O OXLBLZDGMWMXSM-UHFFFAOYSA-N 0.000 claims description 2
- XPPKVPWEQAFLFU-UHFFFAOYSA-N diphosphoric acid Chemical compound OP(O)(=O)OP(O)(O)=O XPPKVPWEQAFLFU-UHFFFAOYSA-N 0.000 claims description 2
- UZVGFAUPMODEBR-UHFFFAOYSA-L disodium;9,10-dioxoanthracene-1,2-disulfonate Chemical compound [Na+].[Na+].C1=CC=C2C(=O)C3=C(S([O-])(=O)=O)C(S(=O)(=O)[O-])=CC=C3C(=O)C2=C1 UZVGFAUPMODEBR-UHFFFAOYSA-L 0.000 claims description 2
- 239000000975 dye Substances 0.000 claims description 2
- 229960002413 ferric citrate Drugs 0.000 claims description 2
- VEPSWGHMGZQCIN-UHFFFAOYSA-H ferric oxalate Chemical compound [Fe+3].[Fe+3].[O-]C(=O)C([O-])=O.[O-]C(=O)C([O-])=O.[O-]C(=O)C([O-])=O VEPSWGHMGZQCIN-UHFFFAOYSA-H 0.000 claims description 2
- KTWOOEGAPBSYNW-UHFFFAOYSA-N ferrocene Chemical compound [Fe+2].C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 KTWOOEGAPBSYNW-UHFFFAOYSA-N 0.000 claims description 2
- 239000011773 ferrous fumarate Substances 0.000 claims description 2
- 235000002332 ferrous fumarate Nutrition 0.000 claims description 2
- 229960000225 ferrous fumarate Drugs 0.000 claims description 2
- 235000013925 ferrous lactate Nutrition 0.000 claims description 2
- 239000004225 ferrous lactate Substances 0.000 claims description 2
- 229940037907 ferrous lactate Drugs 0.000 claims description 2
- 239000000835 fiber Substances 0.000 claims description 2
- 235000004515 gallic acid Nutrition 0.000 claims description 2
- 229940074391 gallic acid Drugs 0.000 claims description 2
- BTIJJDXEELBZFS-QDUVMHSLSA-K hemin Chemical compound CC1=C(CCC(O)=O)C(C=C2C(CCC(O)=O)=C(C)\C(N2[Fe](Cl)N23)=C\4)=N\C1=C/C2=C(C)C(C=C)=C3\C=C/1C(C)=C(C=C)C/4=N\1 BTIJJDXEELBZFS-QDUVMHSLSA-K 0.000 claims description 2
- 229940025294 hemin Drugs 0.000 claims description 2
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 claims description 2
- XHQSLVIGPHXVAK-UHFFFAOYSA-K iron(3+);octadecanoate Chemical compound [Fe+3].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XHQSLVIGPHXVAK-UHFFFAOYSA-K 0.000 claims description 2
- JCDAAXRCMMPNBO-UHFFFAOYSA-N iron(3+);oxygen(2-);titanium(4+) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[Ti+4].[Ti+4].[Fe+3].[Fe+3] JCDAAXRCMMPNBO-UHFFFAOYSA-N 0.000 claims description 2
- BMWMWYBEJWFCJI-UHFFFAOYSA-K iron(3+);trioxido(oxo)-$l^{5}-arsane Chemical compound [Fe+3].[O-][As]([O-])([O-])=O BMWMWYBEJWFCJI-UHFFFAOYSA-K 0.000 claims description 2
- NPFOYSMITVOQOS-UHFFFAOYSA-K iron(III) citrate Chemical compound [Fe+3].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NPFOYSMITVOQOS-UHFFFAOYSA-K 0.000 claims description 2
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 claims description 2
- VLAPMBHFAWRUQP-UHFFFAOYSA-L molybdic acid Chemical compound O[Mo](O)(=O)=O VLAPMBHFAWRUQP-UHFFFAOYSA-L 0.000 claims description 2
- 150000002762 monocarboxylic acid derivatives Chemical class 0.000 claims description 2
- HZVGIXIRNANSHU-UHFFFAOYSA-N naphthalene-1,2,3,4-tetrone Chemical compound C1=CC=C2C(=O)C(=O)C(=O)C(=O)C2=C1 HZVGIXIRNANSHU-UHFFFAOYSA-N 0.000 claims description 2
- NCIAGQNZQHYKGR-UHFFFAOYSA-N naphthalene-1,2,3-triol Chemical compound C1=CC=C2C(O)=C(O)C(O)=CC2=C1 NCIAGQNZQHYKGR-UHFFFAOYSA-N 0.000 claims description 2
- 150000004780 naphthols Chemical class 0.000 claims description 2
- 150000002791 naphthoquinones Chemical class 0.000 claims description 2
- 239000003345 natural gas Substances 0.000 claims description 2
- 235000006408 oxalic acid Nutrition 0.000 claims description 2
- 229940072033 potash Drugs 0.000 claims description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 2
- 235000015320 potassium carbonate Nutrition 0.000 claims description 2
- 229910000160 potassium phosphate Inorganic materials 0.000 claims description 2
- 235000011009 potassium phosphates Nutrition 0.000 claims description 2
- GVPLVOGUVQAPNJ-UHFFFAOYSA-M potassium;hydron;trioxido(oxo)-$l^{5}-arsane Chemical compound [K+].O[As](O)([O-])=O GVPLVOGUVQAPNJ-UHFFFAOYSA-M 0.000 claims description 2
- 102000004169 proteins and genes Human genes 0.000 claims description 2
- 108090000623 proteins and genes Proteins 0.000 claims description 2
- 229940005657 pyrophosphoric acid Drugs 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- 239000011734 sodium Substances 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- 229910001415 sodium ion Inorganic materials 0.000 claims description 2
- 239000001488 sodium phosphate Substances 0.000 claims description 2
- 229910000162 sodium phosphate Inorganic materials 0.000 claims description 2
- FPUYSDUWYZEIMA-UHFFFAOYSA-L sodium;iron(2+);oxalate Chemical compound [Na+].[Fe+2].[O-]C(=O)C([O-])=O FPUYSDUWYZEIMA-UHFFFAOYSA-L 0.000 claims description 2
- WUUHFRRPHJEEKV-UHFFFAOYSA-N tripotassium borate Chemical compound [K+].[K+].[K+].[O-]B([O-])[O-] WUUHFRRPHJEEKV-UHFFFAOYSA-N 0.000 claims description 2
- BYGOPQKDHGXNCD-UHFFFAOYSA-N tripotassium;iron(3+);hexacyanide Chemical compound [K+].[K+].[K+].[Fe+3].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] BYGOPQKDHGXNCD-UHFFFAOYSA-N 0.000 claims description 2
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 claims description 2
- 229910000859 α-Fe Inorganic materials 0.000 claims description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims 2
- 150000002989 phenols Chemical class 0.000 abstract description 6
- 230000003197 catalytic effect Effects 0.000 abstract description 5
- 239000000243 solution Substances 0.000 description 128
- 239000000276 potassium ferrocyanide Substances 0.000 description 20
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 17
- 230000000694 effects Effects 0.000 description 17
- XOGGUFAVLNCTRS-UHFFFAOYSA-N tetrapotassium;iron(2+);hexacyanide Chemical compound [K+].[K+].[K+].[K+].[Fe+2].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] XOGGUFAVLNCTRS-UHFFFAOYSA-N 0.000 description 16
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 15
- 229910001447 ferric ion Inorganic materials 0.000 description 15
- 150000005208 1,4-dihydroxybenzenes Chemical class 0.000 description 13
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 13
- 229910001448 ferrous ion Inorganic materials 0.000 description 13
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 8
- 229910002092 carbon dioxide Inorganic materials 0.000 description 8
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 7
- 239000001569 carbon dioxide Substances 0.000 description 7
- 229960004424 carbon dioxide Drugs 0.000 description 7
- 239000003054 catalyst Substances 0.000 description 7
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 7
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 7
- 230000007423 decrease Effects 0.000 description 5
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 125000004122 cyclic group Chemical group 0.000 description 4
- 239000006260 foam Substances 0.000 description 4
- 238000009472 formulation Methods 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 4
- 229910021506 iron(II) hydroxide Inorganic materials 0.000 description 4
- VLYFRFHWUBBLRR-UHFFFAOYSA-L potassium;sodium;carbonate Chemical compound [Na+].[K+].[O-]C([O-])=O VLYFRFHWUBBLRR-UHFFFAOYSA-L 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 238000010926 purge Methods 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 238000009395 breeding Methods 0.000 description 3
- 230000001488 breeding effect Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000005262 decarbonization Methods 0.000 description 3
- 230000006837 decompression Effects 0.000 description 3
- 238000007255 decyanation reaction Methods 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 235000014413 iron hydroxide Nutrition 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000012797 qualification Methods 0.000 description 3
- 230000001172 regenerating effect Effects 0.000 description 3
- 230000008439 repair process Effects 0.000 description 3
- RMVRSNDYEFQCLF-UHFFFAOYSA-N thiophenol Chemical compound SC1=CC=CC=C1 RMVRSNDYEFQCLF-UHFFFAOYSA-N 0.000 description 3
- 239000004277 Ferrous carbonate Substances 0.000 description 2
- 206010028980 Neoplasm Diseases 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 201000011510 cancer Diseases 0.000 description 2
- 230000000536 complexating effect Effects 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- RAQDACVRFCEPDA-UHFFFAOYSA-L ferrous carbonate Chemical compound [Fe+2].[O-]C([O-])=O RAQDACVRFCEPDA-UHFFFAOYSA-L 0.000 description 2
- 235000019268 ferrous carbonate Nutrition 0.000 description 2
- 229960004652 ferrous carbonate Drugs 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910000015 iron(II) carbonate Inorganic materials 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 231100000572 poisoning Toxicity 0.000 description 2
- 230000000607 poisoning effect Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 1
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 description 1
- AZSYUHSAQICHNK-UHFFFAOYSA-N [C]=O.[S] Chemical compound [C]=O.[S] AZSYUHSAQICHNK-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 208000030303 breathing problems Diseases 0.000 description 1
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- PCHPORCSPXIHLZ-UHFFFAOYSA-N diphenhydramine hydrochloride Chemical compound [Cl-].C=1C=CC=CC=1C(OCC[NH+](C)C)C1=CC=CC=C1 PCHPORCSPXIHLZ-UHFFFAOYSA-N 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 206010025482 malaise Diseases 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 150000002898 organic sulfur compounds Chemical class 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 230000009719 regenerative response Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 208000017520 skin disease Diseases 0.000 description 1
- 239000001632 sodium acetate Substances 0.000 description 1
- 235000017281 sodium acetate Nutrition 0.000 description 1
- HXJUTPCZVOIRIF-UHFFFAOYSA-N sulfolane Chemical compound O=S1(=O)CCCC1 HXJUTPCZVOIRIF-UHFFFAOYSA-N 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulfur dioxide Inorganic materials O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 1
- 238000005987 sulfurization reaction Methods 0.000 description 1
- 239000004291 sulphur dioxide Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Gas Separation By Absorption (AREA)
Abstract
A biochemical iron-alkali solution catalytic method is used to elimiante organic and/or inorganic sulfur from sulfur-contained gas, and the iron-alkali solution is compounded with aerobic spores and/or aerobic bacteria, ferrous compound, alkali matter, phenols and water. The used iron-alkali solution with absorbed organic sulfur and/or inorganic sulfur regenerated by air oxidation under the catalysis of iron ion and phenols for reuse, while coproducing sulfur. The insoluble ferrous compound produced during the absorption and regeneration is decomposed of by aerobic bacteria, and the produced iron ion is returned to the iron-alkali solution to maintain the unchanged iron ion concentration.
Description
Technical field
The present invention relates to the purification method of waste gas or industrial gasses, the especially a kind of raw material of industry gas of organic sulfur and/or inorganic sulfur or purification method of waste gas of containing.
Background technology
Because the fast development of industry, the raw material of industry gas of sulfur-bearing and the consumption and the discharge capacity of waste gas are increasing.The exhaust gas discharging of sulfur-bearing has caused the serious environmental pollution, for example, the formation of acid rain, the acidizing corrosion of building, and synergy causes cancer, breathing problem and skin disease etc., direct harm humans health.
The raw material of industry gas of sulfur-bearing is very harmful to industrial production, for example, cause the equipment heavy corrosion, poisoning casualty accident etc., especially even more serious to the harm of ammonia synthesizing industry, for example, cause that transformation catalyst, synthetic ammonia catalyst poisoning lose activity, copper loss increases, [referring to the Jiang Shengjie work, " synthetic ammonia engineering " (second volume), Beijing, Chemical Industry Press of CNPC publishes, 1976], product quality descends, phenomenons such as product blackout, and wherein hydrogen sulfide have the title of ammonia synthesizing industry " cancer cell ".Therefore, development and research desulfur technology seem urgent and important day by day.
Up to now, all kinds of gases were seldom handled through desulfurization before entering atmosphere, even through handling, its content is still than higher.Existing hydramine method, A.D.A. method, G-V method, aqueous slkali method, weak aqua ammonia method, tannin extract method, and doctor treatment such as sulfolane process, mainly be as elementary doctor treatment, the hydrogen sulfide that removes in the raw material of industry gas [is seen F.C.Riesenfeld, A.L.Kohl, Shen Yusheng translates, " gas purification ", Beijing, Chinese architecture publishing house, 1982], and generally be not used for removing the hydrogen sulfide of general gas, mainly be because these sulfur method cost height, seriously corroded, effect is undesirable, organic sulfur remove rate variance.The cushioning liquid method of the acetic acid of present ferrous hydroxide, sodium acetate and ammonia [is seen 1998 " chemical industry journals ", 49 (1), P48-58], the wet desulphurization method of the aqueous solution of the alkaline matter that contains iron ion of iron-alkali solution catalyzing gas decarbonization, desulfuration and decyanation method [seeing Chinese patent ZL99100596.1] has the ability that removes multiple sulphur, and the gas sweetening effect to low sulfur content is more effective than traditional gas wet desulphurization method, and the total sulfur content in gas is less than 300mg/m
3The time, the total sulfur content in the gas can be reduced to 3mg/m
3Below.But, we find the poor stability of these iron ions in alkaline solution, can produce a large amount of iron hydroxides or ferrous hydroxide precipitation, simultaneously, when the gas of this iron-aqueous slkali and sulfur compound contacts, also can produce a large amount of iron sulfide or ferrous sulfide precipitation, cause that iron ion content reduces rapidly in the solution, desulfurized effect reduces rapidly, and causes phenomenons such as desulfurizing tower obstruction, and is unwell to the gas sweetening of high sulfur content.
Summary of the invention
The purpose of this invention is to provide a kind of aerobic bacteria that contains, biochemical iron-the alkali solution catalyzing process for desulfurizing gas of the alkaline substance solution of iron ion and aldehydes matter (calling process for desulfurizing gas of the present invention in the following text), make it can remove organic sulfur and/or the inorganic sulfur that contains in the gas, simultaneously, the iron ion that can guarantee various forms stably exists in solution, the deposit of the iron content of the various forms of unlikely generation, thereby strengthen the stability of iron-aqueous slkali, overcome the weak point of iron-alkali solution catalyzing gas decarbonization, desulfuration and decyanation method [seeing Chinese patent ZL99100596.1], enable to be used for the desulfurization of high sulfur content gas, be not subjected to the interference of other harmful components in the gas.
Biochemical iron-aqueous slkali of the present invention is by aerobic bacteria gemma and/or aerobic bacteria, iron compound, alkaline matter, aldehydes matter and water are formulated, in process for desulfurizing gas of the present invention, at first, remove organic sulfur and/or inorganic sulfur in the sulfurous gas with biochemical iron alkali solution, secondly, the biochemical iron alkali solution that has absorbed organic sulfur and/or inorganic sulfur is under the common catalysis of iron ion and aldehydes matter, regenerate with air oxidation, and by-product sulphur, biochemical iron alkali solution after the regeneration recycles, wherein absorb in the process of organic sulfur and/or inorganic sulfur at biochemical iron alkali solution, and in the process of biochemical iron alkali solution regeneration, the amounts of insoluble iron compound that produces is decomposed by aerobic bacteria, decomposes the iron ion that produces and returns biochemical iron alkali solution, makes the iron concentration in the biochemical iron alkali solution keep stable.
Process for desulfurizing gas of the present invention does not have specific (special) requirements to the total sulfur content in the sulfurous gas before the desulfurization, and still, in order to reach the higher desulfuration effect, total sulfur content is less than 90% (volume ratio) in the preferred sulfurous gas.
In process for desulfurizing gas of the present invention, process conditions are not had strict restriction, but preferably adopt normal pressure to absorb or pressurizing absorption, the normal pressure regeneration technology absorbs temperature and is preferably 25～90 ℃, and regeneration temperature is preferably 25～120 ℃.
The preferred group of described biochemical iron-aqueous slkali becomes: total Na ion concentration≤10mol/L, total iron concentration 〉=0.00001mol/L, aldehydes matter concentration 〉=0.00008mol/L, 4≤pH≤12, and a certain amount of aerobic bacteria gemma and/or aerobic bacteria, the content of aerobic bacteria gemma and/or aerobic bacteria can not done concrete qualification, because aerobic bacteria gemma and/or aerobic bacteria can be grown up in the desulfurization operation process gradually, ripe, breeding and decline.Sulfur content is less than 300mg/m in gas
3The time, do not need often in biochemical iron alkali solution, to add aerobic bacteria gemma and/or aerobic bacteria, as long as in the biochemical iron alkali solution aerobic bacteria gemma and/or aerobic bacteria are arranged.
Alkaline matter described in the present invention comprises sodium carbonate, sodium acid carbonate, ammonia, potash, saleratus, sodium phosphate, potassium phosphate, Boratex, potassium borate, natrium arsenicum, Macquer's salt or alcamines, or two or more mixture wherein.Be preferably sodium carbonate, sodium acid carbonate and ammonia.
Aldehydes matter described in the present invention comprises single phenol, polyphenol, uniquinones material or many quinones substances, or two or more mixture wherein.
Wherein single phenol is the material that only contains a hydroxyl on the aromatic rings, and aromatic rings can be one or more.There is not hetero atom in the aromatic rings of hydroxyl, in other aromatic rings hetero atom can be arranged, in addition, can there be other any substituted radical other position that described single phenol hydroxyl-removal replaces outside the position, described single phenol is preferably the above fragrant phenol in phenol, naphthols, anthrol, Fourth Ring or Fourth Ring, or two or more mixture wherein.
Wherein said polyphenol is the material that contains two or more hydroxyls on the aromatic rings, and aromatic rings can be one or more.There is not hetero atom in the aromatic rings of hydroxyl, in other aromatic rings hetero atom can be arranged, in addition, can there be other any substituted radicals other position that described polyphenol hydroxyl-removal replaces outside the position, and the hydroxyl on the described polyphenol can replace on same aromatic rings, also can on different aromatic rings, replace, described polyphenol is preferably dihydroxy benzenes, the benzene of trihydroxy benzene or three above hydroxyls, dihydroxy naphthlene, the naphthalene of trihydroxynaphthalene or three above hydroxyls, anthraline, the anthrol of trihydroxy anthrol or three above hydroxyls, the fragrant polyphenol that Fourth Ring or Fourth Ring are above, gallic acid, tannin, tannin extract or Tea Polyphenols, or two or more mixture wherein.
Wherein said uniquinones material comprises the fragrant quinone that benzoquinones, naphthoquinones, anthraquinone, Fourth Ring or Fourth Ring are above, or two or more mixture wherein.
Wherein said many quinones substances comprise the fragrant diquinone that benzene diquinone or diquinone above benzene, naphthalene diquinone or diquinone above naphthalene, anthradiquinone or diquinone above anthracene, Fourth Ring or Fourth Ring are above or diquinone is above or anthraquinone disulfonic acid sodium salt etc., or two or more mixture wherein.Experiment confirm, the action effect of different types of aldehydes matter are the same substantially.
Iron compound of the present invention comprises organoiron compound and/or inorganic iron compound.
Wherein, complex compound and/or chelate that complex compound that complex compound that it is the compound that closes with carbon-iron (C-Fe) bond that the form that described organoiron compound exists has between organism and the iron, nitrogen-iron (N-Fe) bond is closed and/or chelate, oxygen-iron (O-Fe) bond are closed and/or chelate, sulphur-iron (S-Fe) bond are closed, or two or more mixture wherein.Described organoiron compound comprises blood bovine, ferroheme, hemin, siderophillin, ferritin, Mo-Fe protein, rich blood iron, ferrous fumarate, tartaric acid iron, ferric stearate, ferrodextranum, ironic citrate, ferric citrate, ferric glycerophosphate, praseodynium iron, carbonyl iron, EDTA iron, anthraquinone (two) sulfonic acid iron, sorbic alcohol iron, ferrous lactate, ferric succinate, oxalic acid high ferro ammonium, ferric oxalate, sodium oxalate iron, iron octoate, the sulfonic acid ferric salicylate, monocarboxylic acid class iron, two carboxylic acids iron, multi-carboxylic acid's iron or ferrocene and derivative thereof, or two or more mixture wherein.
Wherein, the inorganic iron compound comprises oxidation (Asia) iron, hydroxide (Asia) iron, carbonic acid (Asia) iron, pyrophosphoric acid (Asia) iron, (height) ferrite, perferrite, the red prussiate of soda (potassium), yellow sodium prussiate (potassium), phosphoric acid (Asia) iron, iron titanate, barba hispanica, molybdic acid (Asia) iron, molybdenumization (Asia) iron, tungstenization (Asia) iron, wolframic acid (Asia) iron, ferric vandate, (height) mangaic acid iron, (weight) ferric chromate, (partially) aluminic acid (Asia) iron or ferric arsenate etc., or two or more mixture wherein.
When the iron compound that uses is EDTA iron, sulfonic acid ferric salicylate, oxidation (Asia) iron, hydroxide (Asia) iron or carbonic acid (Asia) iron, preferably add another kind of beyond self or more than one other iron compound mixes use with it.
When the iron compound that uses was a kind of inorganic iron compound, the organoiron compound that preferably adds one or more mixed use with it.
Aerobic bacteria of the present invention is preferably the aerobic bacteria of common thiophilicity.
Wherein, the aerobic bacteria of described common thiophilicity comprise have a liking for alkali bacterium, alkaline-resisting bacterium, knot bacillus, bacillus, thermophilic acidophilic alkali bacterium, hyperthermophile, superthermal bacterium, chemolithotrophic bacteria, Alkaliphilic bacillus, have a liking for salt and have a liking for alkali ancient bacterium, halophilic archaea, have a liking for the ancient bacterium of alkali, sulfur-oxidizing bacteria or basophilla sulfur-oxidizing bacteria, or two or more mixture wherein.
In process for desulfurizing gas of the present invention, aerobic bacteria directly can be added in the biochemical iron alkali solution, also the gemma of this aerobic bacteria directly can be added in the biochemical iron alkali solution, the gemma of aerobic bacteria can grow up to into bacterium gradually in sweetening process.
Iron ion of the present invention is divalence, trivalent or iron ion more at high price.
Catalyst of the present invention is iron ion and aldehydes matter, and aerobic bacteria can guarantee the stability of the iron concentration of the various forms in the biochemical iron alkali solution, can also assist simultaneously iron ion to reduce COS, CS in the solution significantly
2, HS
-Or S
2-Deng the concentration of material, the desulfurization purifying degree of gas is significantly improved.
Because the present invention is with the aqueous solution (i.e. " biochemical iron alkali solution ") of the alkaline matter that contains aerobic bacteria, iron ion and aldehydes matter (ion that comprises ferrous ion and ferric ion or other valence state), absorbs organic sulfur and/or inorganic sulfur in the sulfurous gas.Simultaneously, the insoluble molysite such as iron hydroxide, ferrous hydroxide, iron oxide, ferrous oxide, iron sulfide and ferrous sulfide that in absorption and regenerative process, produce, decomposed by aerobic bacteria, decomposing the iron ion that produces returns in the biochemical iron alkali solution, guarantee the stability of various form iron concentrations in the solution, biochemical iron alkali solution is under the common catalysis of aldehydes matter and iron ion, when regenerating with air oxidation, by-product sulphur, the biochemical iron alkali solution of regenerating recycles.Sweetening process has mainly been utilized the variability of the valence state of iron ion, and the enantiotropy of the quinone phenol of aldehydes matter reaches the purpose of desulfurization; Experiment shows, the total content size of the iron ion of the various forms in the biochemical iron alkali solution is determining the desulphurizing ability and the desulfurized effect of biochemical iron alkali solution, little with the type and the kind relation of part in the complexing iron, part can only influence the content size of the iron ion in the biochemical iron alkali solution, can not influence desulfurized effect; Because, form under the identical situation at other, and iron concentration is also identical, and just the concentration of part is not simultaneously, the desulfurized effect of this biochemistry iron alkali solution differs very little, therefore, only represent that with total iron concentration iron compound concentration gets final product in the biochemical iron alkali solution, there is no need to represent with certain concrete sharp iron compound concentration; Experiment confirm, the action effect of different types of aldehydes matter is also close; Therefore, statement for convenience, below only with DDS represent organoferric part, aldehydes matter only with hydroquinones represent, aerobic bacteria represents with ⊙, so basic principle of the present invention is as follows:
When gas contacted with biochemical iron alkali solution, following absorption reaction took place:
CS in more than reacting
2, COS, R-SH,
Be respectively carbon disulfide, the sulphur carbonoxide, mercaptan and thiophenol, they belong to volatility organic sulfur compounds.
Absorbed the aqueous solution (being biochemical iron alkali solution) of the biochemical alkaline matter that contains iron ion of sulphur and carbon dioxide, be designated hereinafter simply as " rich solution "." rich solution " under the common catalysis of aldehydes matter and iron ion, with air oxidation regeneration, regenerative response is as follows:
" rich solution " after air oxidation regeneration is transformed into " lean solution ", and " lean solution " recycles.
Owing in absorption and regenerative process, can produce insoluble molysite such as iron hydroxide, ferrous hydroxide, iron oxide, ferrous oxide, iron sulfide and ferrous sulfide, aerobic bacteria can decompose the amounts of insoluble iron salt that generates, the iron ion that decomposes generation is returned in the biochemical iron alkali solution, guarantee the stability of various form iron concentrations in the solution, its mechanism is as follows:
In order to realize above-mentioned basic principle, designed two kinds of production procedures by the compositing range of gas with various: first kind is that normal pressure absorbs, atmospheric air regeneration flow process; Second kind is pressurizing absorption, decompression, atmospheric air oxidation regeneration flow process.
Carbanion in the biochemical iron alkali solution of first kind of flow process, bicarbonate ion, the concrete concentration of ferrous ion and ferric ion there is no need to stipulate exactly, because a large amount of carbon dioxide changes biochemical iron alkali solution in absorption process, carbanion in the biochemical iron alkali solution almost all is transformed into bicarbonate ion, when regeneration, discharge carbon dioxide in the biochemical iron alkali solution, bicarbonate ion wherein resolves into carbon dioxide and carbanion, and promptly the concentration of carbanion in the cyclic process of biochemical iron alkali solution and bicarbonate ion changes; Biochemical iron alkali solution is when air regenesis, ferrous ion is oxidized to ferric ion, when absorbing sulphur, ferric ion is reduced into elemental sulfur with sulphion, simultaneously, ferric ion is transformed into ferrous ion, promptly the concentration of ferrous ion in the cyclic process of biochemical iron alkali solution and ferric ion changes, but the summation of ferrous ion and ferric ion concentration is greater than 0.00001mol/L in the biochemical iron alkali solution, aldehydes matter concentration is greater than 0.00008mol/L, 4≤pH≤12, the content of aerobic bacteria gemma and/or aerobic bacteria can not done concrete qualification, because aerobic bacteria gemma and aerobic bacteria can be grown up in the desulfurization operation process gradually, ripe, breeding and decline; If sulfur content is less than 300mg/m in gas
3The time, as long as have aerobic bacteria gemma and/or aerobic bacteria in the original biochemical iron alkali solution, just can often in biochemical iron alkali solution, not add aerobic bacteria gemma and/or aerobic bacteria.
Carbanion in the biochemical iron alkali solution of second kind of flow process, bicarbonate ion, the concrete concentration of ferrous ion and ferric ion there is no need to stipulate exactly, because a large amount of carbon dioxide changes biochemical iron alkali solution in absorption process, carbanion in the biochemical iron alkali solution almost all is transformed into bicarbonate ion, and contain a large amount of free carbon dioxides, the concentration of the carbanion in the at this moment biochemical iron alkali solution is almost nil, when decompression and regeneration, discharge carbon dioxide in the biochemical iron alkali solution, bicarbonate ion wherein resolves into carbon dioxide and carbanion, and promptly the concentration of carbanion in the cyclic process of biochemical iron alkali solution and bicarbonate ion is marked change; Biochemical iron alkali solution is when air regenesis, ferrous ion is oxidized to ferric ion, when absorbing sulphur, ferric ion is reduced into elemental sulfur with sulphion, simultaneously, ferric ion is transformed into ferrous ion, promptly the concentration of ferrous ion in the cyclic process of biochemical iron alkali solution and ferric ion is marked change, but ferrous ion and ferric ion concentration summation are greater than 0.00001mol/L in the biochemical iron alkali solution, aldehydes matter concentration is greater than 0.00008mol/L, 4≤pH≤12, the content of aerobic bacteria gemma and/or aerobic bacteria can not done concrete qualification, because aerobic bacteria gemma and aerobic bacteria can be grown up in the desulfurization operation process gradually, ripe, breeding and decline; If sulfur content is less than 300mg/m in gas
3The time, as long as have aerobic bacteria gemma and/or aerobic bacteria in the original biochemical iron alkali solution, just can often in biochemical iron alkali solution, not add aerobic bacteria gemma and/or aerobic bacteria.
Owing to contain the ferrous ion and the ferric ion of higher concentration in the biochemical iron alkali solution of the present invention, from Chemical Kinetics and thermodynamics and chemical reaction equilibrium point of theory, can reduce the reaction speed that fe is oxidized to ferrous ion or ferric ion effectively, promptly alleviated the corrosivity of biochemical iron alkali solution, prolonged the service life of equipment equipment.
The present invention compares with iron-alkali solution catalyzing gas decarbonization, desulfuration and decyanation method, have following advantage: 1. iron-alkali solution catalyzing only is useful for the low sulfur content gas sweetening, and the biochemical iron alkali solution catalysis method of indication of the present invention both can be used for the low sulfur content gas sweetening also can be used for the high sulfur content gas sweetening; 2. iron-alkali solution catalyzing can produce insoluble molysite precipitation in whole desulfurization and regenerative process, and the biochemical iron alkali solution catalysis method of indication of the present invention can not produce insoluble molysite precipitation basically; 3. on the basis of iron-alkali solution catalyzing, the desulfuration solution internal circulating load of the biochemical iron alkali solution catalysis method of indication of the present invention can also reduce significantly; 4. iron-alkali solution catalyzing can not be used for the desulfurization of high sulfur content gas, otherwise can produce a large amount of insoluble precipitates, cause many trouble phenomenons such as stifled tower and stopping production, the insoluble precipitate amount that produces during the biochemical iron alkali solution catalytic desulfurizing of indication of the present invention seldom can not cause phenomenons such as stifled tower and stopping production; 5. iron-alkali solution catalyzing desulfurization purifying degree is lower than the biochemical iron alkali solution catalytic desulfurizing degree of purification of the present invention indication, and the method for indication of the present invention can be reduced to 0.1mg/m with the total sulfur content in the gas
3Below.
Biochemical iron-alkali solution catalyzing process for desulfurizing gas of the present invention has the wide industrial purposes, can use it for the desulfurization of gases such as other raw material of industry gas of the semiwater gas of natural gas, oven gas, town gas, synthetic ammonia and conversion gas, the synthetic waste gas in dyestuff factory, chemical fibre factory's blowdown gas, Crouse's (Cross) tail gas and sulfur-bearing or waste gas.
Description of drawings
Fig. 1 is that the normal pressure of embodiment one absorbs, the schematic diagram of atmospheric air regeneration flow process.
Fig. 2 is the pressurizing absorption of embodiment two, decompression, the schematic diagram of atmospheric air oxidation regeneration flow process.
The specific embodiment
Describe biochemical iron-alkali solution catalyzing process for desulfurizing gas of the present invention below in conjunction with specific embodiment, described embodiment is for the present invention is described better, and can not be interpreted as it is restriction to claim of the present invention.
Embodiment one as shown in Figure 1, wherein, (1) desulfurizing tower, (2) regenerative pump, (3) jet regeneration tank, (4) lean solution groove, (5) desulfur pump, (6) geosyncline, (7) geosyncline pump, (8) sulfurous gas, (9) Purge gas, (10) rich solution, (11) lean solution, (12) air, drop a hint (13), (14) sulphur foam, materials such as (15) alkaline matter and catalyst, (16) steam.
Referring to Fig. 1, gas (8) enters from desulfurizing tower (1) bottom, and lean solution (11) counter current contacting; Sulphur in the gas (8) is absorbed by lean solution (11), and gas (8) is transformed into Purge gas (9) and discharges from desulfurizing tower (1) top; The lean solution (11) that has absorbed sulphur is transformed into rich solution (10) in purifying column (1) bottom; Rich solution (10) is reproduced pump (2) and extracts out from desulfurizing tower (1) bottom, and pressurization, enter jet regeneration tank (3), air self-suction (12) and rich solution (10) are mixed in jet regeneration tank (3), sulphion in the rich solution (10) etc. is changed into elemental sulfur by Catalytic Oxygen, forms sulphur foam (14) desulfuration sulphur recycle section; Air (12) becomes drop a hint (13) and is discharged into the external world; Rich solution (10) through air regenesis is transformed into lean solution (11), flows in the lean solution groove (4), and lean solution (11) is desulfurized pump (5) and delivers to again in the desulfurizing tower (1), removes to absorb the sulphur in the gas (8); Material such as alkaline matter and catalyst (15) at first is added in the geosyncline (6), adds lean solution (11) or water again, uses steam (16) heating then, and stirs, and after dissolving or stirring, sends in the lean solution groove (4) with geosyncline pump (7).
Embodiment two as shown in Figure 2, wherein, (17) desulfurizing tower, (18) jet regeneration tank, (19) lean solution groove, (20) desulfur pump, (21) geosyncline pump, (22) geosyncline, (23) sulfurous gas, (24) Purge gas, materials such as (25) alkaline matter and catalyst, (26) steam, (27) air, drop a hint (28), (29) sulphur foam, (30) rich solution, (31) lean solution.
Referring to Fig. 2, gas (23) enters from desulfurizing tower (17) bottom, and lean solution (31) counter current contacting; Sulphur in the gas (23) is absorbed by lean solution (31), and gas (23) is transformed into Purge gas (24) and discharges from desulfurizing tower (17) top; The lean solution (31) that has absorbed sulphur is transformed into rich solution (30) in desulfurizing tower (17) bottom; Rich solution (30) flows out from desulfurizing tower (17) bottom, enters jet regeneration tank (18), air self-suction (27), in jet regeneration tank (18), and rich solution (30) is mixed, and the sulphion in the rich solution (30) etc. is changed into elemental sulfur by Catalytic Oxygen, forms sulphur foam (29) desulfuration sulphur recycle section; Air (27) becomes drop a hint (28) and is discharged into the external world; Rich solution (30) through air regenesis is transformed into lean solution (31), flows in the lean solution groove (19), and lean solution (31) is desulfurized pump (20) and delivers to again in the desulfurizing tower (17), removes to absorb the sulphur in the gas (23); Material such as alkaline matter and catalyst (25) at first is added in the geosyncline (22), adds lean solution (31) or water again, uses steam (26) heating then, and stirs, and after dissolving or stirring, sends in the lean solution groove (19) with geosyncline pump (21).
At identical sulfurous gas composition, flow, under the situation of identical biochemical iron alkali solution internal circulating load, utilize above technological process, the biochemical iron alkali solution that is made into different material, carry out desulfurization, the total content size of finding the iron ion of the various forms in the biochemical iron alkali solution is determining the desulphurizing ability and the desulfurized effect of biochemical iron alkali solution, little with the type and the kind relation of part in the complexing iron, part can only influence the content size of the iron ion in the biochemical iron alkali solution, can not influence desulfurized effect; Because, form under the identical situation at other, and iron concentration is also identical, and just the concentration of part not simultaneously, the desulfurized effect of this biochemistry iron alkali solution differs very little, therefore, only represent that with total iron concentration iron compound concentration gets final product in the biochemical iron alkali solution, there is no need to represent, illustrate that simultaneously what work in the sweetening process is iron ion with certain concrete iron compound concentration, rather than the part in the iron compound, experimental result is shown in table one, table two, table three, table four.Simultaneously, in the desulfurization process, we measure the variation of total iron ion content in the biochemical iron alkali solution, it is more stable that discovery has added the content of total iron ion in the biochemical iron alkali solution of aerobic bacteria, decrease speed is slower, on the contrary, does not add the content instability of total iron ion in the iron alkali solution of aerobic bacteria, decrease speed is very fast, and experimental result as shown in Table 5.
Table one, 25 ℃ the time, the desulfurized effect (aerobic bacteria is arranged) of different formulations, the different biochemical iron alkali solutions of forming
| Formula material | Total iron ion content (g/L) | Phenols content (g/L) | Total alkalinity (g/L) is in sodium carbonate | The PH value | Hydrogen sulfide content (mg/m before the desulfurization 3) | Desulfurization after cure hydrogen content (mg/m 3) |
| Sodium carbonate blood bovine hydroquinones | ?0.1 | 0.2 | 35 | 8.5 | ?1000 | 0 |
| Sodium carbonate EDTA iron hydroquinones | ?0.1 | 0.2 | 35 | 8.5 | ?1000 | 0.5 |
| Sodium carbonate potassium ferrocyanide hydroquinones | ?0.1 | 0.2 | 35 | 8.5 | ?1000 | 1 |
| Sodium carbonate, ammonia, blood bovine, potassium ferrocyanide, iron oxide, hydroquinones, tannin | ?0.1 | 0.1 0.1 (tannin) | 35 | 8.5 | ?1000 | 0 |
| Sodium carbonate, ethylenediamine, EDTA iron, potassium ferrocyanide, sulfonic acid ferric salicylate, Tea Polyphenols, tannin | ?0.1 | (0.1 Tea Polyphenols) 0.1 (tannin) | 35 | 8.5 | ?1000 | 1.5 |
| Sodium carbonate, natrium arsenicum, EDTA iron, potassium ferrocyanide, ferroheme, Tea Polyphenols, ADA | ?0.1 | (0.1 Tea Polyphenols) 0.1 (ADA) | 35 | 8.5 | ?1000 | 1 |
Table two, 35 ℃ the time, the desulfurized effect (aerobic bacteria is arranged) of different formulations, the different biochemical iron alkali solutions of forming
| Formula material | Total iron ion content (g/L) | Phenols content (g/L) | Total alkalinity (g/L) is in sodium carbonate | The PH value | Hydrogen sulfide content (mg/m before the desulfurization 3) | Desulfurization after cure hydrogen content (mg/m 3) |
| Sodium carbonate blood bovine hydroquinones | ?0.1 | 0.4 | 25 | 8.1 | ?5000 | 50 |
| Sodium carbonate EDTA iron hydroquinones | ?0.1 | 0.4 | 25 | 8.1 | ?5000 | 51.5 |
| Sodium carbonate potassium ferrocyanide hydroquinones | ?0.1 | 0.4 | 25 | 8.1 | ?5000 | 48.5 |
| Sodium carbonate, ammonia, blood bovine, potassium ferrocyanide, iron oxide, hydroquinones, tannin | ?0.1 | 0.2 0.2 (tannin) | 25 | 8.1 | ?5000 | 48 |
| Sodium carbonate, ethylenediamine, EDTA iron, potassium ferrocyanide, sulfonic acid ferric salicylate, Tea Polyphenols, tannin | ?0.1 | (0.2 Tea Polyphenols) 0.2 (tannin) | 25 | 8.1 | ?5000 | 49.5 |
| Sodium carbonate, natrium arsenicum, EDTA iron, potassium ferrocyanide, ferroheme, Tea Polyphenols, ADA | ?0.1 | (0.2 Tea Polyphenols) 0.2 (ADA) | 25 | 8.5 | ?5000 | 49 |
Table three, 45 ℃ the time, the desulfurized effect (aerobic bacteria is arranged) of different formulations, the different biochemical iron alkali solutions of forming
| Formula material | Total iron ion content (g/L) | Phenols content (g/L) | Total alkalinity (g/L) is in sodium carbonate | The PH value | Hydrogen sulfide content (mg/m before the desulfurization 3) | Desulfurization after cure hydrogen content (mg/m 3) |
| Sodium carbonate blood bovine hydroquinones | ?0.9 | ?0.4 | 25 | ?8.0 | ?10000 | ?0 |
| Sodium carbonate EDTA iron hydroquinones | ?0.9 | ?0.4 | 25 | ?8.0 | ?10000 | ?0.5 |
| Sodium carbonate potassium ferrocyanide hydroquinones | ?0.9 | ?0.4 | 25 | ?8.0 | ?10000 | ?1.5 |
| Sodium carbonate, ammonia, blood bovine, potassium ferrocyanide, iron oxide, hydroquinones, tannin | ?0.9 | 0.2 0.2 (tannin) | 25 | ?8.0 | ?10000 | ?1 |
| Sodium carbonate, ethylenediamine, EDTA iron, potassium ferrocyanide, sulfonic acid ferric salicylate, Tea Polyphenols, tannin | ?0.9 | (0.2 Tea Polyphenols) 0.2 (tannin) | 25 | ?8.0 | ?10000 | ?0.5 |
| Sodium carbonate, natrium arsenicum, EDTA iron, potassium ferrocyanide, ferroheme, Tea Polyphenols, ADA | ?0.9 | (0.2 Tea Polyphenols) 0.2 (ADA) | 25 | ?8.0 | ?10000 | ?0 |
Table four, 55 ℃ the time, the desulfurized effect (aerobic bacteria is arranged) of different formulations, the different biochemical iron alkali solutions of forming
| Formula material | Total iron ion content (g/L) | Phenols content (g/L) | Total alkalinity (g/L) is in sodium carbonate | The PH value | Hydrogen sulfide content (mg/m before the desulfurization 3) | Desulfurization after cure hydrogen content (mg/m 3) |
| Sodium carbonate blood bovine hydroquinones | ?0.9 | ?0.2 | 25 | ?8.0 | ?10000 | ?0 |
| Sodium carbonate EDTA iron hydroquinones | ?0.9 | ?0.2 | 25 | ?8.0 | ?10000 | ?1.5 |
| Sodium carbonate potassium ferrocyanide hydroquinones | ?0.9 | ?0.2 | 25 | ?8.0 | ?10000 | ?0.5 |
| Sodium carbonate, ammonia, blood bovine, potassium ferrocyanide, iron oxide, hydroquinones, tannin | ?0.9 | 0.1 0.1 (tannin) | 25 | ?8.0 | ?10000 | ?0 |
| Sodium carbonate, ethylenediamine, EDTA iron, potassium ferrocyanide, sulfonic acid ferric salicylate, Tea Polyphenols, tannin | ?0.9 | (0.1 Tea Polyphenols) 0.1 (tannin) | 25 | ?8.0 | ?10000 | ?0 |
| Sodium carbonate, natrium arsenicum, EDTA iron, potassium ferrocyanide, ferroheme, Tea Polyphenols, ADA | ?0.9 | (0.1 Tea Polyphenols) 0.1 (ADA) | 25 | ?8.0 | ?10000 | ?0 |
Table five, 45 ℃ the time, biochemical iron alkali solution and the iron alkali solution iron ion stability in the desulfurization operation process
| Iron compound type in biochemical iron alkali solution and the iron alkali solution | The bacterium existence | Desulfurization during different running time in biochemical iron alkali solution and the iron alkali solution total iron content (g/L) change | ||||||||
| Initial concentration | One day | Two days | Three days | Four days | Five days | Six days | Seven days | Eight days | ||
| Ferroheme | Have | 1.00 | ?1.00 | ?0.99 | ?0.97 | ?0.96 | ?0.94 | ?0.92 | ?0.90 | ?0.91 |
| Do not have | 1.00 | ?0.95 | ?0.85 | ?0.74 | ?0.63 | ?0.55 | ?0.36 | ?0.29 | ?0.17 | |
| EDTA iron | Have | 1.00 | ?0.99 | ?0.97 | ?0.95 | ?0.93 | ?0.91 | ?0.89 | ?0.87 | ?0.80 |
| Do not have | 1.00 | ?0.89 | ?0.79 | ?0.69 | ?0.6 | ?0.5 | ?0.3 | ?0.12 | ?0.03 | |
| The sulfonic acid ferric salicylate | Have | 1.00 | ?0.90 | ?0.88 | ?0.85 | ?0.83 | ?0.80 | ?0.76 | ?0.70 | ?0.65 |
| Do not have | 1.00 | ?0.80 | ?0.75 | ?0.68 | ?0.57 | ?0.41 | ?0.29 | ?0.11 | ?0.01 | |
| Potassium ferrocyanide | Have | 1.00 | ?0.99 | ?0.98 | ?0.96 | ?0.96 | ?0.94 | ?0.94 | ?0.93 | ?0.93 |
| Do not have | 1.00 | ?0.90 | ?0.81 | ?0.69 | ?0.61 | ?0.51 | ?0.31 | ?0.19 | ?0.10 | |
| Ferroheme EDTA iron | Have | 1.00 | ?1.00 | ?0.98 | ?0.98 | ?0.97 | ?0.97 | ?0.97 | ?0.92 | ?0.91 |
| Do not have | 1.00 | ?0.91 | ?0.80 | ?0.69 | ?0.60 | ?0.50 | ?0.29 | ?0.20 | ?0.09 | |
| Ferroheme, EDTA iron, sulfonic acid ferric salicylate | Have | 1.00 | ?1.00 | ?0.99 | ?0.99 | ?0.96 | ?0.96 | ?0.92 | ?0.90 | ?0.90 |
| Do not have | 1.00 | ?0.89 | ?0.81 | ?0.71 | ?0.59 | ?0.51 | ?0.32 | ?0.21 | ?0.10 | |
| EDTA iron, sulfonic acid ferric salicylate, iron oxide | Have | 1.00 | ?0.98 | ?0.98 | ?0.97 | ?0.95 | ?0.93 | ?0.91 | ?0.89 | ?0.86 |
| Do not have | 1.00 | ?0.90 | ?0.80 | ?0.71 | ?0.61 | ?0.50 | ?0.31 | ?0.20 | ?0.11 | |
| Ferroheme, sulfonic acid ferric salicylate, iron oxide | Have | 1.00 | ?1.00 | ?0.99 | ?0.98 | ?0.97 | ?0.97 | ?0.96 | ?0.92 | ?0.90 |
| Do not have | 1.00 | ?0.92 | ?0.82 | ?0.72 | ?0.58 | ?0.48 | ?0.32 | ?0.22 | ?0.1 | |
| EDTA iron, potassium ferrocyanide, ferrous carbonate | Have | 1.00 | ?0.99 | ?0.99 | ?0.97 | ?0.96 | ?0.94 | ?0.95 | ?0.93 | ?0.92 |
| Do not have | 1.00 | ?0.89 | ?0.79 | ?0.70 | ?0.61 | ?0.51 | ?0.31 | ?0.21 | ?0.1 | |
| EDTA iron, potassium ferrocyanide, ferrous carbonate, ferroheme | Have | 1.00 | ?1.00 | ?0.99 | ?0.98 | ?0.97 | ?0.96 | ?0.97 | ?0.93 | ?0.92 |
| Do not have | 1.00 | ?0.92 | ?0.81 | ?0.71 | ?0.62 | ?0.52 | ?0.29 | ?0.22 | ?0.12 | |
| Potassium ferrocyanide, iron oxide, ferroheme, sulfonic acid ferric salicylate | Have | 1.00 | ?1.00 | ?0.99 | ?0.98 | ?0.98 | ?0.97 | ?0.96 | ?0.94 | ?0.92 |
| Do not have | 1.00 | ?0.91 | ?0.82 | ?0.69 | ?0.61 | ?0.51 | ?0.31 | ?0.21 | ?0.09 | |
| Ferroheme, sulfonic acid ferric salicylate | Have | 1.00 | ?1.00 | ?0.99 | ?0.99 | ?0.95 | ?0.96 | ?0.94 | ?0.92 | ?0.90 |
| Do not have | 1.00 | ?0.92 | ?0.79 | ?0.71 | ?0.61 | ?0.49 | ?0.31 | ?0.19 | ?0.11 | |
Claims (31)
1. biochemical iron-alkali solution catalyzing process for desulfurizing gas, it is characterized in that, remove organic sulfur and/or inorganic sulfur in the sulfurous gas with iron alkali solution, wherein iron alkali solution is by aerobic bacteria gemma and/or aerobic bacteria, iron compound, alkaline matter, aldehydes matter and water are formulated, the iron alkali solution that has absorbed organic sulfur and/or inorganic sulfur is under the common catalysis of iron ion and aldehydes matter, regenerate with air oxidation, and by-product sulphur, iron alkali solution after the regeneration recycles, wherein absorb in the process of organic sulfur and/or inorganic sulfur at iron alkali solution, and in the process of iron alkali solution regeneration, the amounts of insoluble iron compound that produces is decomposed by aerobic bacteria, decompose the iron ion that produces and return iron alkali solution, make the iron concentration in the iron alkali solution keep stable.
2. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 1 is characterized in that, before the desulfurization, total sulfur content is less than 90% (volume ratio) in the preferred sulfurous gas.
3. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 1 or 2 is characterized in that, described method preferably adopts normal pressure to absorb or pressurizing absorption the normal pressure regeneration technology.
4. as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of claim 1-3, it is characterized in that the absorption temperature of described method is preferably 25～90 ℃, regeneration temperature is preferably 25～120 ℃.
5. as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of claim 1-4, it is characterized in that, the preferred group of described iron alkali solution becomes: total Na ion concentration≤10mol/L, total iron concentration 〉=0.00001mol/L, aldehydes matter concentration 〉=0.00008mol/L, 4≤pH≤12, and a certain amount of aerobic bacteria gemma and/or aerobic bacteria.
6. as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 1-5, it is characterized in that sulfur content is less than 300mg/m in gas
3The time, do not need often in iron alkali solution, to add aerobic bacteria gemma and/or aerobic bacteria.
7. as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 1-6, it is characterized in that, described alkaline matter comprises sodium carbonate, sodium acid carbonate, ammonia, potash, saleratus, sodium phosphate, potassium phosphate, Boratex, potassium borate, natrium arsenicum, Macquer's salt or alcamines, or two or more mixture wherein.
8. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 7 is characterized in that described alkaline matter is preferably sodium carbonate, sodium acid carbonate or ammonia.
9. as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 1-6, it is characterized in that described aldehydes matter comprises single phenol, polyphenol, uniquinones material or many quinones substances, or two or more mixture wherein.
10. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 9 is characterized in that, described single phenol is preferably the material that only contains a hydroxyl on the aromatic rings, and aromatic rings can be one or more.
11. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 10 is characterized in that, described single phenol is preferably the above fragrant phenol in phenol, naphthols, anthrol, Fourth Ring or Fourth Ring, or two or more mixture wherein.
12., it is characterized in that described single phenol is preferably in the aromatic rings of hydroxyl does not have hetero atom, in other aromatic rings hetero atom can be arranged as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 10-11.
13., it is characterized in that can there be other any substituted radical other position that described single phenol hydroxyl-removal replaces outside the position as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 10-12.
14. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 9 is characterized in that described polyphenol is preferably the material that contains two or more hydroxyls on the aromatic rings, aromatic rings can be one or more.
15. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 14, it is characterized in that, described polyphenol is preferably above fragrant polyphenol, gallic acid, tannin, tannin extract or the Tea Polyphenols in anthrol, Fourth Ring or Fourth Ring of naphthalene, anthraline, trihydroxy anthrol or three above hydroxyls of benzene, dihydroxy naphthlene, trihydroxynaphthalene or three above hydroxyls of dihydroxy benzenes, trihydroxy benzene or three above hydroxyls, or two or more mixture wherein.
16, as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 14-15, it is characterized in that not having hetero atom in the aromatic rings of the preferred wherein hydroxyl of described polyphenol, in other aromatic rings hetero atom can be arranged.
As the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 14-16, it is characterized in that 17, can there be other any substituted radicals other position that described polyphenol hydroxyl-removal replaces outside the position.
18., it is characterized in that the hydroxyl on the described polyphenol can replace as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 14-17 on same aromatic rings, also can on different aromatic rings, replace.
19. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 9 is characterized in that, described uniquinones material comprises the fragrant quinone that benzoquinones, naphthoquinones, anthraquinone, Fourth Ring or Fourth Ring are above, or two or more mixture wherein.
20. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 9, it is characterized in that, described many quinones substances comprise the fragrant diquinone that benzene diquinone or diquinone above benzene, naphthalene diquinone or diquinone above naphthalene, anthradiquinone or diquinone above anthracene, Fourth Ring or Fourth Ring are above or diquinone is above or anthraquinone disulfonic acid sodium salt etc., or two or more mixture wherein.
21., it is characterized in that described iron compound comprises organoiron compound and/or inorganic iron compound as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 1-6.
22. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 21, it is characterized in that, complex compound and/or chelate that complex compound that complex compound that it is the compound that closes with carbon-iron (C-Fe) bond that the form that described organoiron compound exists has between organism and the iron, nitrogen-iron (N-Fe) bond is closed and/or chelate, oxygen-iron (O-Fe) bond are closed and/or chelate, sulphur-iron (S-Fe) bond are closed, or two or more mixture wherein.
23. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 22, it is characterized in that, described organoiron compound comprises blood bovine, ferroheme, hemin, siderophillin, ferritin, Mo-Fe protein, rich blood iron, ferrous fumarate, tartaric acid iron, ferric stearate, ferrodextranum, ironic citrate, ferric citrate, ferric glycerophosphate, praseodynium iron, carbonyl iron, EDTA iron, anthraquinone (two) sulfonic acid iron, sorbic alcohol iron, ferrous lactate, ferric succinate, oxalic acid high ferro ammonium, ferric oxalate, sodium oxalate iron, iron octoate, the sulfonic acid ferric salicylate, monocarboxylic acid class iron, two carboxylic acids iron, multi-carboxylic acid's iron or ferrocene and derivative thereof, or two or more mixture wherein.
24. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 21, it is characterized in that, the inorganic iron compound comprises oxidation (Asia) iron, hydroxide (Asia) iron, carbonic acid (Asia) iron, pyrophosphoric acid (Asia) iron, (height) ferrite, perferrite, the red prussiate of soda (potassium), yellow sodium prussiate (potassium), phosphoric acid (Asia) iron, iron titanate, barba hispanica, molybdic acid (Asia) iron, molybdenumization (Asia) iron, tungstenization (Asia) iron, wolframic acid (Asia) iron, ferric vandate, (height) mangaic acid iron, (weight) ferric chromate, (partially) aluminic acid (Asia) iron or ferric arsenate etc., or two or more mixture wherein.
25. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 21, it is characterized in that, when the iron compound that uses is EDTA iron, sulfonic acid ferric salicylate, oxidation (Asia) iron, hydroxide (Asia) iron or carbonic acid (Asia) iron, preferably add another kind of beyond self or more than one other iron compound mixes use with it.
26. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 21 is characterized in that, when the iron compound that uses was a kind of inorganic iron compound, the organoiron compound that preferably adds one or more mixed use with it.
27., it is characterized in that described aerobic bacteria is preferably the aerobic bacteria of common thiophilicity as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 1-6.
28. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 27, it is characterized in that, the aerobic bacteria of described common thiophilicity comprise have a liking for alkali bacterium, alkaline-resisting bacterium, knot bacillus, bacillus, thermophilic acidophilic alkali bacterium, hyperthermophile, superthermal bacterium, chemolithotrophic bacteria, Alkaliphilic bacillus, have a liking for salt and have a liking for alkali ancient bacterium, halophilic archaea, have a liking for the ancient bacterium of alkali, sulfur-oxidizing bacteria or basophilla sulfur-oxidizing bacteria, or two or more mixture wherein.
29. as the described biochemical iron-alkali solution catalyzing process for desulfurizing gas of one of claim 1-6, it is characterized in that, can directly add aerobic bacteria in the iron alkali solution, also the gemma of this aerobic bacteria directly can be added in the iron alkali solution, the gemma of aerobic bacteria can grow up to into bacterium gradually in sweetening process.
30. biochemical iron-alkali solution catalyzing process for desulfurizing gas as claimed in claim 1 is characterized in that, described iron ion is divalence, trivalent or iron ion more at high price.
31., can use it for the desulfurization of gases such as other raw material of industry gas of the semiwater gas of natural gas, oven gas, town gas, synthetic ammonia and conversion gas, the synthetic waste gas in dyestuff factory, chemical fibre factory's blowdown gas, Crouse's (Cross) tail gas and sulfur-bearing or waste gas as the purposes of one of claim 1-30 described biochemical iron-alkali solution catalyzing process for desulfurizing gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021306052A CN1158133C (en) | 2002-09-09 | 2002-09-09 | Biochemical iron-alkali solution catalyzing process for desulfurizing gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021306052A CN1158133C (en) | 2002-09-09 | 2002-09-09 | Biochemical iron-alkali solution catalyzing process for desulfurizing gas |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1398659A true CN1398659A (en) | 2003-02-26 |
| CN1158133C CN1158133C (en) | 2004-07-21 |
Family
ID=4746414
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB021306052A Expired - Lifetime CN1158133C (en) | 2002-09-09 | 2002-09-09 | Biochemical iron-alkali solution catalyzing process for desulfurizing gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1158133C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015035878A1 (en) | 2013-09-10 | 2015-03-19 | 北京博源恒升高科技有限公司 | Method for removing sox from gas using modified polyethylene glycol |
| WO2015055104A1 (en) | 2013-10-15 | 2015-04-23 | 北京博源恒升高科技有限公司 | METHOD FOR REMOVAL OF SOx FROM GAS USING COMPOUND AMINE ALCOHOL SOLUTION |
| WO2015085879A1 (en) | 2013-12-12 | 2015-06-18 | 北京博源恒升高科技有限公司 | Method for removing sox from gas using polyol complex solution |
| US9815017B2 (en) | 2013-12-12 | 2017-11-14 | Beijing Boyuan Hengsheng High-Technology Co., Ltd. | Method for removing SOx from gas using ethylene glycol composite solution |
| CN110437906A (en) * | 2019-09-04 | 2019-11-12 | 北京盈和瑞环境科技股份有限公司 | A kind of Complexing Iron biological desulfurization process |
-
2002
- 2002-09-09 CN CNB021306052A patent/CN1158133C/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015035878A1 (en) | 2013-09-10 | 2015-03-19 | 北京博源恒升高科技有限公司 | Method for removing sox from gas using modified polyethylene glycol |
| US9795917B2 (en) | 2013-09-10 | 2017-10-24 | Beijing Boyuan Hengsheng High-Technology Co., Ltd | Method for removing SOx from gas with modified polyethylene glycol |
| WO2015055104A1 (en) | 2013-10-15 | 2015-04-23 | 北京博源恒升高科技有限公司 | METHOD FOR REMOVAL OF SOx FROM GAS USING COMPOUND AMINE ALCOHOL SOLUTION |
| KR20160070129A (en) | 2013-10-15 | 2016-06-17 | 베이징 보위안 헝셩 하이-테크놀로지 컴퍼니 리미티드 | METHOD FOR REMOVAL OF SOx FROM GAS USING COMPOUND AMINE ALCOHOL SOLUTION |
| US9999852B2 (en) | 2013-10-15 | 2018-06-19 | Beijing Boyuan Hengsheng High-Technology Co., Ltd | Method for removing SOx from gas with compound alcohol-amine solution |
| WO2015085879A1 (en) | 2013-12-12 | 2015-06-18 | 北京博源恒升高科技有限公司 | Method for removing sox from gas using polyol complex solution |
| US9815017B2 (en) | 2013-12-12 | 2017-11-14 | Beijing Boyuan Hengsheng High-Technology Co., Ltd. | Method for removing SOx from gas using ethylene glycol composite solution |
| US10207218B2 (en) | 2013-12-12 | 2019-02-19 | Beijing Boyuan Hengsheng High-Technology Co., Ltd | Method for removing SOx from gas using polyol composite solution |
| CN110437906A (en) * | 2019-09-04 | 2019-11-12 | 北京盈和瑞环境科技股份有限公司 | A kind of Complexing Iron biological desulfurization process |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1158133C (en) | 2004-07-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104249995B (en) | Reduce sulfur recovery facility SO 2the method of emission concentration | |
| CN102151476B (en) | Method for removing hydrogen sulfide in gas phase through oxidization under high gravity field | |
| CN106310890B (en) | A kind of method of bioanalysis removing sour gas | |
| CN103254957B (en) | Device and method for removing hydrogen sulfide out of methane by utilizing collagenous fiber/polyester composite material to load Fe(III) | |
| Lu et al. | Enhanced biological removal of NOx from flue gas in a biofilter by Fe (II) Cit/Fe (II) EDTA absorption | |
| CN108160067B (en) | Sewage deodorization catalyst and preparation method and application thereof | |
| CN101352653B (en) | Low-temperature micro-oxygen purification method for removing harmful gas in yellow phosphorus tail gas | |
| CN111151294B (en) | Peroxide catalytic oxidation catalyst and method for treating propylene oxide and styrene co-production wastewater by using same | |
| CN107537293A (en) | A kind of closed cycle bacterial desulfurization and the method for reclaiming elemental sulfur | |
| CN104249996B (en) | Reduce sulfur recovery facility SO 2the technique of emission concentration | |
| CN1158133C (en) | Biochemical iron-alkali solution catalyzing process for desulfurizing gas | |
| Liu et al. | An innovative approach to oxidative removal of hydrogen sulfide using the solution of peroxo heteropolyacid | |
| CN109095589A (en) | The composition of dioxanes and its application in a kind of degradation water body | |
| CN104525097B (en) | A kind of Ce Ni bimetallics load the preparation method of meerschaum adsorption catalyst | |
| CN101143746A (en) | Method for processing sulfur-containing waste lye | |
| KR101774443B1 (en) | Liquid-form catalyst compositions for the removal of hydrogen sulfide from biogas | |
| CN102218260B (en) | Absorbent used for removing sulfides in malodorous gases | |
| CN205730825U (en) | A kind of device utilizing microorganism removing hydrogen sulfide in methane | |
| CN1092994C (en) | Gas decarbonization, desulfuration and decyanation technology by Fe-alkalisolution catalyst method | |
| CN1554467A (en) | Removing sulfide from CO2 enriched gas by complex iron method | |
| CN113996345B (en) | Desulfurization catalyst, blast furnace gas desulfurization system and desulfurization method | |
| CN101574607A (en) | Adsorbent for selectively removing low-concentration sulfur dioxide from gas containing carbon dioxide | |
| CN205730824U (en) | A kind of device utilizing microorganism directly to remove hydrogen sulfide in methane | |
| CN211886237U (en) | High-efficient biological enzyme exhaust treatment device | |
| CN113683178A (en) | Method for removing formaldehyde in wastewater by catalytic oxidation method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Yongfeng Boyuan Industrial Co.,Ltd. Assignor: Wei Xionghui Contract record no.: 2010360000026 Denomination of invention: Biochemical iron-alkali solution catalyzing process for desulfurizing gas Granted publication date: 20040721 License type: Exclusive License Open date: 20030226 Record date: 20100625 |
|
| EC01 | Cancellation of recordation of patent licensing contract |
Assignee: Yongfeng Boyuan Industrial Co.,Ltd. Assignor: Wei Xionghui Contract record no.: 2010360000026 Date of cancellation: 20100721 |
|
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Beijing Boyuan Hengsheng High-Technology Co.,Ltd. Assignor: Wei Xionghui Contract record no.: 2010110000100 Denomination of invention: Biochemical iron-alkali solution catalyzing process for desulfurizing gas Granted publication date: 20040721 License type: Exclusive License Open date: 20030226 Record date: 20100728 |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20200108 Address after: 100871 No. 411, apartment 16, weixiuyuan, Peking University, Haidian District, Beijing Co-patentee after: YONGFENG BOYUAN INDUSTRY CO.,LTD. JIANGXI PROVINCE Patentee after: Wei Xionghui Address before: 100871 Department of Applied Chemistry, School of chemistry and molecular engineering, Peking University, Haidian District, Beijing Patentee before: Wei Xionghui |
|
| TR01 | Transfer of patent right | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20040721 |