CN111686819A - Copper-containing catalyst and preparation method thereof - Google Patents
Copper-containing catalyst and preparation method thereof Download PDFInfo
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- CN111686819A CN111686819A CN201910182541.3A CN201910182541A CN111686819A CN 111686819 A CN111686819 A CN 111686819A CN 201910182541 A CN201910182541 A CN 201910182541A CN 111686819 A CN111686819 A CN 111686819A
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- 239000003054 catalyst Substances 0.000 title claims abstract description 136
- 239000010949 copper Substances 0.000 title claims abstract description 112
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 82
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 75
- 238000002360 preparation method Methods 0.000 title abstract description 26
- 238000000034 method Methods 0.000 claims abstract description 45
- 229910052751 metal Inorganic materials 0.000 claims abstract description 23
- 239000002184 metal Substances 0.000 claims abstract description 23
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 12
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 9
- 229910052593 corundum Inorganic materials 0.000 claims abstract description 9
- -1 phosphonic acid compound Chemical class 0.000 claims abstract description 9
- 229910001845 yogo sapphire Inorganic materials 0.000 claims abstract description 9
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims abstract description 7
- 229920000642 polymer Polymers 0.000 claims abstract description 7
- 239000006259 organic additive Substances 0.000 claims abstract 4
- 230000032683 aging Effects 0.000 claims description 77
- 238000006243 chemical reaction Methods 0.000 claims description 57
- 239000011259 mixed solution Substances 0.000 claims description 57
- 239000002002 slurry Substances 0.000 claims description 56
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 40
- 239000012752 auxiliary agent Substances 0.000 claims description 32
- 239000000243 solution Substances 0.000 claims description 30
- 239000011701 zinc Substances 0.000 claims description 30
- 229910052782 aluminium Inorganic materials 0.000 claims description 24
- 229910052725 zinc Inorganic materials 0.000 claims description 24
- 239000000463 material Substances 0.000 claims description 23
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 20
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 20
- 238000001035 drying Methods 0.000 claims description 19
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical class [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 17
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 13
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 13
- 150000001879 copper Chemical class 0.000 claims description 11
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims description 8
- 150000003751 zinc Chemical class 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 229940120146 EDTMP Drugs 0.000 claims description 4
- 229920002125 Sokalan® Polymers 0.000 claims description 4
- 239000007864 aqueous solution Substances 0.000 claims description 4
- NFDRPXJGHKJRLJ-UHFFFAOYSA-N edtmp Chemical compound OP(O)(=O)CN(CP(O)(O)=O)CCN(CP(O)(O)=O)CP(O)(O)=O NFDRPXJGHKJRLJ-UHFFFAOYSA-N 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 239000004584 polyacrylic acid Substances 0.000 claims description 4
- 229920001444 polymaleic acid Polymers 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 4
- BAERPNBPLZWCES-UHFFFAOYSA-N (2-hydroxy-1-phosphonoethyl)phosphonic acid Chemical compound OCC(P(O)(O)=O)P(O)(O)=O BAERPNBPLZWCES-UHFFFAOYSA-N 0.000 claims description 3
- 229920002845 Poly(methacrylic acid) Polymers 0.000 claims description 3
- 229920000805 Polyaspartic acid Polymers 0.000 claims description 3
- YDONNITUKPKTIG-UHFFFAOYSA-N [Nitrilotris(methylene)]trisphosphonic acid Chemical compound OP(O)(=O)CN(CP(O)(O)=O)CP(O)(O)=O YDONNITUKPKTIG-UHFFFAOYSA-N 0.000 claims description 3
- 108010064470 polyaspartate Proteins 0.000 claims description 3
- 229920001529 polyepoxysuccinic acid Polymers 0.000 claims description 3
- 230000009467 reduction Effects 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- JSYPRLVDJYQMAI-ODZAUARKSA-N (z)-but-2-enedioic acid;prop-2-enoic acid Chemical compound OC(=O)C=C.OC(=O)\C=C/C(O)=O JSYPRLVDJYQMAI-ODZAUARKSA-N 0.000 claims description 2
- IQEKRNXJPCBUAT-UHFFFAOYSA-N 2-[hydroperoxy(hydroxy)phosphoryl]acetic acid Chemical compound OOP(O)(=O)CC(O)=O IQEKRNXJPCBUAT-UHFFFAOYSA-N 0.000 claims description 2
- 229920002126 Acrylic acid copolymer Polymers 0.000 claims description 2
- 239000001273 butane Substances 0.000 claims description 2
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 claims description 2
- 229920001577 copolymer Polymers 0.000 claims description 2
- 229940090960 diethylenetriamine pentamethylene phosphonic acid Drugs 0.000 claims description 2
- DUYCTCQXNHFCSJ-UHFFFAOYSA-N dtpmp Chemical compound OP(=O)(O)CN(CP(O)(O)=O)CCN(CP(O)(=O)O)CCN(CP(O)(O)=O)CP(O)(O)=O DUYCTCQXNHFCSJ-UHFFFAOYSA-N 0.000 claims description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 2
- 239000007790 solid phase Substances 0.000 claims description 2
- 150000005846 sugar alcohols Polymers 0.000 claims description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 82
- 230000000694 effects Effects 0.000 abstract description 20
- 230000002195 synergetic effect Effects 0.000 abstract description 14
- 238000003786 synthesis reaction Methods 0.000 abstract description 10
- 230000015572 biosynthetic process Effects 0.000 abstract description 7
- 238000000975 co-precipitation Methods 0.000 abstract description 5
- 230000006872 improvement Effects 0.000 abstract description 3
- 238000009827 uniform distribution Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 49
- 239000008367 deionised water Substances 0.000 description 35
- 229910021641 deionized water Inorganic materials 0.000 description 35
- 238000003756 stirring Methods 0.000 description 26
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 22
- 239000000203 mixture Substances 0.000 description 22
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 21
- 239000012065 filter cake Substances 0.000 description 19
- 238000005406 washing Methods 0.000 description 18
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 15
- 238000002156 mixing Methods 0.000 description 15
- 239000011148 porous material Substances 0.000 description 15
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 13
- 239000006185 dispersion Substances 0.000 description 13
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 12
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 12
- 238000009826 distribution Methods 0.000 description 12
- 238000001914 filtration Methods 0.000 description 12
- 239000002244 precipitate Substances 0.000 description 12
- 238000001556 precipitation Methods 0.000 description 12
- 239000010439 graphite Substances 0.000 description 10
- 229910002804 graphite Inorganic materials 0.000 description 10
- 229910002092 carbon dioxide Inorganic materials 0.000 description 8
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- 238000003825 pressing Methods 0.000 description 7
- 230000008569 process Effects 0.000 description 7
- CDQSJQSWAWPGKG-UHFFFAOYSA-N butane-1,1-diol Chemical compound CCCC(O)O CDQSJQSWAWPGKG-UHFFFAOYSA-N 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- CQRYARSYNCAZFO-UHFFFAOYSA-N salicyl alcohol Chemical compound OCC1=CC=CC=C1O CQRYARSYNCAZFO-UHFFFAOYSA-N 0.000 description 6
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Inorganic materials [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 description 6
- 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 description 5
- 229910052708 sodium Inorganic materials 0.000 description 5
- 239000011734 sodium Substances 0.000 description 5
- WRMNZCZEMHIOCP-UHFFFAOYSA-N 2-phenylethanol Chemical compound OCCC1=CC=CC=C1 WRMNZCZEMHIOCP-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- GTTSNKDQDACYLV-UHFFFAOYSA-N Trihydroxybutane Chemical compound CCCC(O)(O)O GTTSNKDQDACYLV-UHFFFAOYSA-N 0.000 description 4
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 4
- 238000005984 hydrogenation reaction Methods 0.000 description 4
- 238000010335 hydrothermal treatment Methods 0.000 description 4
- 239000012266 salt solution Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 3
- 229910002651 NO3 Inorganic materials 0.000 description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- TVZPLCNGKSPOJA-UHFFFAOYSA-N copper zinc Chemical compound [Cu].[Zn] TVZPLCNGKSPOJA-UHFFFAOYSA-N 0.000 description 3
- 230000000977 initiatory effect Effects 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000011268 mixed slurry Substances 0.000 description 3
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate group Chemical group [N+](=O)([O-])[O-] NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000012716 precipitator Substances 0.000 description 3
- 230000002194 synthesizing effect Effects 0.000 description 3
- VPTUPAVOBUEXMZ-UHFFFAOYSA-N (1-hydroxy-2-phosphonoethyl)phosphonic acid Chemical compound OP(=O)(O)C(O)CP(O)(O)=O VPTUPAVOBUEXMZ-UHFFFAOYSA-N 0.000 description 2
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 2
- KJJPLEZQSCZCKE-UHFFFAOYSA-N 2-aminopropane-1,3-diol Chemical compound OCC(N)CO KJJPLEZQSCZCKE-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 2
- HDYRYUINDGQKMC-UHFFFAOYSA-M acetyloxyaluminum;dihydrate Chemical compound O.O.CC(=O)O[Al] HDYRYUINDGQKMC-UHFFFAOYSA-M 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 229910000329 aluminium sulfate Inorganic materials 0.000 description 2
- 229940009827 aluminum acetate Drugs 0.000 description 2
- 238000004873 anchoring Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 150000002191 fatty alcohols Chemical class 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000012066 reaction slurry Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 229910052726 zirconium Inorganic materials 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 229910000611 Zinc aluminium Inorganic materials 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- JRBRVDCKNXZZGH-UHFFFAOYSA-N alumane;copper Chemical compound [AlH3].[Cu] JRBRVDCKNXZZGH-UHFFFAOYSA-N 0.000 description 1
- HXFVOUUOTHJFPX-UHFFFAOYSA-N alumane;zinc Chemical compound [AlH3].[Zn] HXFVOUUOTHJFPX-UHFFFAOYSA-N 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000013064 chemical raw material Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 229940116318 copper carbonate Drugs 0.000 description 1
- GEZOTWYUIKXWOA-UHFFFAOYSA-L copper;carbonate Chemical compound [Cu+2].[O-]C([O-])=O GEZOTWYUIKXWOA-UHFFFAOYSA-L 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007123 defense Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- HPNMFZURTQLUMO-UHFFFAOYSA-N diethylamine Chemical compound CCNCC HPNMFZURTQLUMO-UHFFFAOYSA-N 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 230000008570 general process Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 235000019359 magnesium stearate Nutrition 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 239000012702 metal oxide precursor Substances 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
- 229910052596 spinel Inorganic materials 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 150000003752 zinc compounds Chemical class 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
- B01J31/28—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of the platinum group metals, iron group metals or copper
-
- B01J35/394—
-
- B01J35/613—
-
- B01J35/615—
-
- B01J35/633—
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/153—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the catalyst used
- C07C29/154—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the catalyst used containing copper, silver, gold, or compounds thereof
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Abstract
The invention discloses a copper-containing catalyst and a preparation method thereof, wherein the preparation method comprises the following steps of: CuO 15-60%, ZnO 10-35%, Al2O310-35 percent of organic additive, 2-25 percent of organic additive; the organic assistant is organic assistant P1 and organic assistant P2, the organic assistant P1 is organic phosphonic acid compound and/or carboxylic acid polymer, and the organic assistant P2 is organic alcohol. The copper-containing catalyst is prepared by a coprecipitation method. The copper-containing catalyst has the advantages of uniform distribution of active metal copper, good synergistic effect, large number of active metal active centers, and improvement of the activity, selectivity and thermal stability of the methanol synthesis catalyst and the service life of the catalyst.
Description
Technical Field
The invention relates to a preparation method of a copper-containing catalyst, in particular to a copper-containing catalyst with high activity, high selectivity and good heat resistance and a preparation method thereof.
Background
Methanol is increasingly regarded as a basic chemical raw material and a new energy source, is widely applied to organic synthesis, dye, fuel, medicine, coating and national defense industries, and along with the continuous increase of the demand and the production capacity of methanol along with the development of the industries in recent years, the position of methanol in national economy is more important, so that the production technology and the catalyst performance of the methanol are required to be further improved in order to further promote the development of the methanol industry.
Industrially, methanol generally contains H2、CO、CO2The synthesis gas of (a) is produced under conditions of pressure, temperature and presence of a catalyst. At present, methanol is synthesized by adopting a medium-pressure and low-pressure gas phase method in the world, and the used catalyst is basically mixed oxide of copper, zinc and aluminum. CuO, ZnO and Al in synthetic methanol catalyst2O3The three components have different functions, CuO is used as a main active component, ZnO and Al2O3Is an auxiliary agent. The addition of ZnO can make the catalyst form Cu/Zn synergetics, greatly raise activity and selectivity of catalyst, Al2O3Not only plays a role of a framework in the catalyst, but also can disperse active components in the catalyst to enable CO to be generated2The adsorption and conversion rate are improved, and a proper amount of Al is added into the copper-based catalyst2O3Can improve catalyst CO2Selectivity of synthesizing methanol by hydrogenation.
Cu/ZnO/Al2O3The activity of the catalyst is closely related to the distribution and the morphology of metals, and when the composition and the content of the catalyst are not changed, the Cu-ZnO synergistic effect and the Cu dispersibility in the catalyst play an important role in the catalytic activity and the selectivity. The catalytic theory considers that the Cu/ZnO catalyst has double active points, the oxygen vacancy on ZnO also has important influence on the catalytic performance of the catalyst (Cu-ZnO synergistic effect), the number of the oxygen vacancy is increased, the interaction between Cu and ZnO is enhanced, and the conversion rate of carbon monoxide and the selectivity of methanol are increased. The dispersion performance and oxygen vacancy of the Cu/ZnO catalyst are closely related to the composition and preparation method of the catalyst, and how to improve the dispersion degree of active components of the catalyst in the preparation process of the catalyst, thereby achieving the synergistic effect of improving the Cu-ZnO catalyst and increasing the reaction active centerThe object of (2) is to improve both the activity and selectivity of the catalyst, and has become the focus of research on copper-based catalysts.
At present, Cu/ZnO/Al2O3The synthesis method of the catalyst comprises a precipitation method, an impregnation method and a sol-gel method, and in general, in industry, a coprecipitation method (including a parallel flow method, a reverse addition method and a forward addition coprecipitation method) is firstly used for generating mixed basic carbonate of copper and zinc, then aluminum hydroxide is added in the pulping process, and the generated pulp is washed by water, dried, roasted and tabletted to form. At present, the improvement of catalyst preparation is generally in the aspects of adding auxiliary agents, selecting carriers, investigating different preparation methods, optimizing reaction conditions and the like, and the problems of poor thermal stability, low selectivity and short service life of a copper-based catalyst are solved by changing the proportion and the dispersion degree of catalyst components and the size of crystal grains, increasing the number of active sites in the catalyst, optimizing the synergistic effect of the active components and the auxiliary agents and increasing the specific surface area of the catalyst to improve the activity of the catalyst. The catalyst has different preparation methods, different dispersity of the obtained copper, different synergistic effect between the metal active center copper and the auxiliary agent, and larger difference of the performance of the obtained catalyst.
CN107185543 discloses a catalyst for synthesizing methanol by carbon dioxide hydrogenation, the catalyst is a mixture of Cu and ZnO in filiform or cylindrical form, soluble zinc salt and mineralizer are dissolved in deionized water, the solution is kept at 60-150 ℃ for 1-6 h in a high-pressure reaction kettle, and then is slowly cooled to room temperature to obtain white precipitate, and ZnO in different forms is obtained after drying; adding soluble copper salt and prepared ZnO into deionized water, adding a reducing agent for reaction, washing and drying to obtain the Cu/ZnO catalyst.
CN 1660490A discloses a preparation method of a methanol synthesis catalyst, and a small amount of surfactant OP is added in the preparation process of a coprecipitation method. CN 101733109A copper-based methanol synthesis catalyst is prepared by adding an auxiliary agent (one or more of ethylene glycol, diethylamine, glycerol, magnesium stearate, and activated carbon) during precipitation. In the method, the organic reagent is added in the precipitation process to improve the Cu-ZnO synergistic effect, but the improvement of the dispersion of the catalyst metal by the organic reagent is limited, and the Cu-ZnO synergistic effect is not obviously improved.
CN101327431 discloses a preparation method of a synthetic methanol catalyst, which comprises the steps of firstly preparing a copper-zinc coprecipitate, secondly preparing a zinc-aluminum coprecipitate with a spinel structure, thirdly preparing a copper-aluminum coprecipitate, then mixing and aging the three coprecipitates, then washing, drying, roasting, adding graphite tablets into the roasted material, and thus obtaining the synthetic methanol catalyst. The method mainly aims to improve the dispersibility of the active component copper, the auxiliary agent zinc and the carrier aluminum, but the method is complex, and precipitates prepared by three-step precipitation are mixed, so that the composition and the structure of the product are uneven, and the performance of the catalyst is influenced.
CN103801302A discloses a preparation method of a copper-zinc-containing catalyst. Introducing CO into soluble salt solution A containing zinc2Gas, reacting to generate zinc compound deposit. Introducing CO into the sodium metaaluminate solution2Gas to generate aluminum-containing precipitate, aging under stirring, adding basic copper carbonate during aging, washing, filtering, drying, roasting, tabletting and forming to obtain the copper-containing catalyst. The method improves the surface area of the catalyst, but the pore structure is not concentrated, and the material obtained by precipitation has poor cohesiveness and is not easy to be tabletted and molded.
CN103172607 discloses a copper-based catalyst for synthesizing methanol by carbon dioxide hydrogenation, a preparation method and an application thereof, wherein a precipitation solution containing zinc, aluminum and zirconium is firstly generated, a copper-containing salt solution is added into the precipitation solution, and after Cu in the precipitation solution is precipitated, aging, washing, drying and roasting are carried out to obtain the copper-containing catalyst. The method still adopts the conventional process conditions in the preparation process, improves the distribution of the active metal of the catalyst only by adding zirconium and adopting polyvinylpyrrolidone and polyethylene glycol as stabilizing agents, but does not obviously increase the number of active centers.
CN201610773534.7 discloses a preparation method of a synthetic methanol catalyst, which comprises the steps of adding a sodium metaaluminate alkaline solution and a soluble salt solution containing Cu into a reaction tank filled with purified water in a concurrent flow manner to carry out gelling reaction to generate slurry I, then dropwise adding the sodium metaaluminate alkaline solution into a soluble salt solution containing Zn to carry out gelling reaction to generate slurry II, uniformly mixing the slurry I and the slurry II, carrying out aging and filtering to obtain a material, carrying out hydrothermal treatment on the obtained material by using water vapor, adding urea during the hydrothermal treatment, and then washing, filtering, drying, roasting, tabletting and forming to obtain the catalyst. Although the content of active metal copper in the surface phase of the catalyst prepared by the method is high, the synergistic effect of copper and zinc in the catalyst is reduced under the action of water vapor pressure and the impact of water molecules.
The method changes the copper-based catalyst preparation process or adds the auxiliary agent on the basis of the copper-based catalyst preparation process to change the copper dispersibility on the reduced catalyst and improve the activity of the catalyst, but in the process of improving the copper component dispersibility, other physicochemical properties of the catalyst are influenced, and the effect of improving the active component dispersibility is not obvious.
Disclosure of Invention
In view of the above-mentioned deficiencies in the prior art, the present invention provides a copper-containing catalyst and a method for preparing the same. The active metal copper and the auxiliary agent zinc of the copper-containing catalyst are uniformly distributed, have good synergistic effect and large active metal active center quantity, and improve the activity, selectivity and thermal stability of the methanol synthesis catalyst and the service life of the catalyst.
The copper-containing catalyst of the invention comprises the following components by weight: CuO 15-60%, preferably 20-55%, ZnO 10-35%, preferably 15-30%, Al2O310 to 35 percent, preferably 7 to 28 percent, and 2 to 25 percent, preferably 3 to 15 percent of organic auxiliary agent; the organic auxiliary agents are organic auxiliary agent P1 and organic auxiliary agent P2. The organic assistant P1 is organic phosphonic acid compound and/or carboxylic acid polymer, and the organic assistant P2 is organic alcohol.
Based on the weight of the catalyst, the content of the organic assistant P1 is 2wt% -15 wt%, preferably 2wt% -8 wt%, and the content of the organic assistant P2 is 2wt% -11 wt%, preferably 2wt% -7 wt%.
The organic phosphonic acid compound is selected from one or more of ethylenediamine tetramethylene phosphonic acid, hydroxyethylene diphosphonic acid, polyalcohol phosphonate ester, polyaminopolyether methylene phosphonic acid, 1,2, 4-tricarboxylic acid-2-phosphonic butane, hydroxyphosphonoacetic acid, aminotrimethylene phosphonic acid and diethylenetriamine pentamethylene phosphonic acid, and is preferably selected from one or more of ethylenediamine tetramethylene phosphonic acid, hydroxyethylene diphosphonic acid or aminotrimethylene phosphonic acid.
The molecular weight of the carboxylic acid polymer is 400-5000, and the carboxylic acid polymer is selected from one or more of polyacrylic acid, polymethacrylic acid, polymaleic acid, polyaspartic acid, polyepoxysuccinic acid, acrylic acid-hydroxypropyl acrylate copolymer or maleic acid-acrylic acid copolymer, and preferably one or more of polyacrylic acid, polymethacrylic acid, polymaleic acid, polyaspartic acid or polyepoxysuccinic acid.
The organic auxiliary agent P2 is selected from organic alcohol with 3-10 carbon atoms, the organic alcohol is one or more of fatty alcohol, butanetriol, glycerol, diethylene glycol, butanediol, ethylene glycol, propylene glycol, salicyl alcohol, 2-amino-1, 3-propanediol and phenethyl alcohol, and is preferably butanetriol, glycerol, diethylene glycol, butanediol, ethylene glycol, propylene glycol or salicyl alcohol.
The specific surface area of the copper-containing catalyst is 100-550 m2The pore volume is 0.20 to 0.80 ml/g.
The specific surface area of metallic copper in the reduced copper-containing catalyst is 35-120 m2Preferably 40 to 100 m/g2(ii) in terms of/g. The dispersion degree of the metallic copper is 13 to 45 percent, and preferably 18 to 40 percent.
The preparation method of the copper-containing catalyst comprises the following steps: (1) carrying out parallel flow gelling reaction on the mixed solution A and ammonia water to obtain slurry I, and then aging; (2) dropwise adding the mixed solution B and a sodium carbonate solution into the aged slurry I obtained in the step (1) in a parallel flow manner, carrying out gelling reaction to obtain slurry II, and then aging; (3) carrying out solid-liquid separation on the material obtained in the step (2), and drying and forming a solid phase to obtain a catalyst; wherein the mixed solution A is an aqueous solution containing soluble copper salt, soluble zinc salt and soluble aluminum salt, and the mixed solution B is an aqueous solution containing soluble copper salt and soluble aluminum salt; wherein the organic assistant P1 is added in the step (1), and the organic assistant P2 is added in the step (2).
In the method of the present invention, the organic auxiliary agent P1 in step (1) may be added alone in parallel, or may be added during the preparation of the mixed solution a, preferably during the preparation of the mixed solution a. The organic auxiliary agent P2 added in step (2) can be added separately and concurrently, or can be added when preparing the mixed solution B, preferably when preparing the mixed solution B.
In the method, the dosage of the organic auxiliary agent P1 added in the step (1) accounts for 10-90% of the total dosage of the organic auxiliary agent, and preferably 40-70%; in the step (2), the amount of the added organic auxiliary agent P2 is 10-90% of the total amount of the organic auxiliary agent, preferably 30-60%.
In the method, when the organic assistant P1 is added in the step (1), the adding amount of the organic assistant P1 is 5-120 g/L, preferably 20-100 g/L, based on the volume of the mixed solution A; when the organic assistant P2 is added in the step (2), the addition amount of the organic assistant P2 is 2-50 g/L, preferably 4-40 g/L based on the volume of the mixed solution B.
In the mixed solution A in the step (1), the concentration of the soluble copper salt is Cu2+1.0 to 5.0mol/L, preferably 1.5 to 4.0mol/L, and the concentration of the soluble zinc salt is Zn2+0.5 to 6.0mol/L, preferably 1.0 to 4.0mol/L, and the concentration of the soluble aluminum salt is Al3+The amount of the compound is 1.0 to 6.0mol/L, preferably 1.2 to 5.0 mol/L. The copper content in the mixed solution A is 40-80%, preferably 55-75% of the copper content in the catalyst. The aluminum content in the mixed solution A is 45-85%, preferably 55-80% of the aluminum content in the catalyst. The soluble copper salt is nitrate and/or acetate containing copper, the soluble zinc salt is nitrate and/or acetate containing zinc, and the soluble aluminum salt is one or more selected from aluminum nitrate, aluminum sulfate, aluminum chloride or aluminum acetate.
The weight concentration of the ammonia water in the step (1) is 5-15%.
The gelling reaction in the step (1) is generally carried out in a reaction tank, and the gelling reaction conditions are as follows: the reaction temperature is 30-80 ℃, preferably 40-70 ℃, the reaction time is 0.2-2.0 hours, preferably 0.5-1.5 hours, and the pH value is 6.0-9.0, preferably 6.5-8.5.
The aging conditions of the slurry I in the step (1) are as follows: the aging temperature is 40-90 ℃, preferably 50-80 ℃, the pH value is 6.0-8.0, preferably 6.5-7.5, and the aging time is 0.2-1.0 hour, preferably 0.3-0.8 hour. The aging is carried out under stirring, the preferred stirring conditions being as follows: the stirring speed is 100-300 rpm, preferably 150-250 rpm.
In the mixed solution B in the step (2), the concentration of the soluble copper salt is Cu2+0.5 to 4.0mol/L, preferably 1.0 to 3.0mol/L, and the concentration of the soluble aluminum salt is Al3+The amount of the compound is 0.5 to 5.0mol/L, preferably 1.0 to 3.5 mol/L. The soluble copper salt is nitrate and/or acetate containing copper, and the soluble aluminum salt is one or more selected from aluminum nitrate, aluminum sulfate, aluminum chloride or aluminum acetate. The copper content in the mixed solution B is 20-60% of the copper content in the catalyst, and preferably 25-45%; the aluminum content in the mixed solution B is 15-55%, preferably 20-45% of the aluminum content in the catalyst.
In the reaction material in the step (2), the molar ratio of the amount of the sodium carbonate to the total amount of copper and zinc is 0.5-4.0, preferably 1.0-3.0.
The gelling reaction conditions in the step (2) are as follows: the reaction temperature is 30-90 ℃, preferably 40-80 ℃, the reaction time is 1.5-4.0 hours, preferably 1.5-3.5 hours, the pH value is 8.5-12.0, preferably 9.0-11.0, and the pH value is at least 1.0 higher than that of the gelling reaction in the step (1), preferably at least 1.5 higher.
The aging conditions of the slurry II in the step (2) are as follows: the aging temperature is 40-90 ℃, preferably 50-80 ℃, the aging time is 1.5-6.0 hours, preferably 2.0-5.0 hours, the pH value is 7.5-11.0, preferably 8.0-10.0, and the pH value is at least 0.5 higher than the pH value aged in the step (1), preferably at least 1.0 higher. The aging is carried out under stirring, the preferred stirring conditions being as follows: the stirring speed is 300-500 rpm, preferably 300-450 rpm.
The solid-liquid separation process in the step (3) generally comprises conventional washing and filtering processes, wherein the washing process generally adopts organic alcohol solution washing (the same as the organic alcohol used in the step (2)), and the washing temperature is controlled to be 30-80 ℃, and is preferably 35-65 ℃. The number of washing is 1 to 5, preferably 2 to 4. The carbon number of the organic alcohol is 3-10, the organic alcohol is one or more of fatty alcohol, butanetriol, glycerol, diethylene glycol, butanediol, ethylene glycol, propylene glycol, salicyl alcohol, 2-amino-1, 3-propanediol and phenethyl alcohol, and the organic alcohol is preferably butanetriol, glycerol, diethylene glycol, butanediol, ethylene glycol, propylene glycol and salicyl alcohol. The organic alcohol solution has a weight concentration of 2-30 g/L, preferably 3-25 g/L.
The drying temperature in the step (3) is 50-120 ℃, preferably 60-110 ℃, and the drying time is 2-36 hours, preferably 4-26 hours.
The copper-containing catalyst of the invention is applied to catalytic hydrogenation reaction, such as methanol synthesis reaction of synthesis gas, condensation hydrogenation reaction of aldehyde and the like; the method is applied to methanol synthesis reaction, and the general process conditions are as follows: the reaction temperature is 210-320 ℃, and preferably 230-280 ℃; the pressure is 2-10 MPa, preferably 2-7 MPa; the volume airspeed is 2000-15000 h-1Preferably 4000 to 12000h-1。
Compared with the prior art, the catalyst prepared by the method has the advantages of more dispersed active metal, good synergistic effect among Cu-ZnO, high activity, high selectivity and heat resistance.
The method comprises the steps of firstly carrying out co-current flow and coprecipitation reaction on a mixed solution containing part of Cu, Al and Zn and ammonia water, carrying out primary aging on the Cu, Zn and Al and the mixed slurry to generate a primary precipitate containing Cu, Zn and Al oxides, then adding the residual mixed solution of Cu and Al and a sodium carbonate solution into the aged slurry in a co-current flow manner, then carrying out deep aging to prepare a mixed precipitate of copper, zinc and aluminum, and finally preparing the copper-zinc catalyst. The first precipitation is carried out under the condition that part of Cu, Al and Zn are used as a precipitator in ammonia water and P1 added with an organic auxiliary agent, active metal and the organic auxiliary agent P1 are chelated to form a macromolecular reticular complex, so that the metal of the precipitate containing Cu, Zn and Al after the first primary aging is orderly combined and the particle size of the precipitate is uniform, the second precipitation is carried out under the condition that part of Cu and Al are used as a precipitator in sodium carbonate and P2 added with the organic auxiliary agent, so that the subsequent addition of the active metal is uniformly deposited on the previous precipitate, and through the regulation and control of the preparation steps and the preparation conditions, in the process of the growth of the mixed precipitate particles of copper, zinc and aluminum, the active metal in the metal oxide precursor deposited previously has certain anchoring effect on the active metal deposited later, different active metals are orderly deposited in the catalyst, the growth speed of the metal oxide particles and the mutual contact probability between the active metals are controlled, the dispersion degree of copper is improved, the Cu-ZnO synergistic effect is increased, the primary precipitation takes an ammonia water solution as a precipitator, so that the precipitation process is more moderate, the precipitate slurry after the primary aging is a stable system, and the anchoring effect on the active metal deposited later is facilitated. The change of the preparation conditions improves the dispersion degree of copper in the catalyst, the density of active centers is improved, and the selectivity and the thermal stability of methanol are also obviously improved.
In addition, in the reduction process of the catalyst, the organic auxiliary agent in the catalyst is beneficial to the dispersion of copper, and the dispersion degree of metal copper is further improved.
Detailed Description
The embodiments and effects of the present invention are further illustrated by the following examples. In the present invention, the specific surface area, pore volume and pore distribution are measured by a low-temperature liquid nitrogen adsorption method, and the specific surface area (S) of the catalyst metal Cu after reduction is measuredCu) And degree of dispersion (D)Cu) By using N2Determined by O-chemisorption. v% is volume fraction and wt% is mass fraction.
Example 1
Adding Cu (NO)3)2·3H2O、Zn(NO3)2·6H2O、AlCl3·6H2Dissolving O in deionized water, adding ethylenediamine tetramethylene phosphonic acid, mixing to obtain working solution A, copper (Cu)2+) Zinc (Zn) at a concentration of 2.8mol/L2+) Aluminum ion (Al) with a concentration of 2.5mol/L3+) The concentration is 3.6mol/L, and the ethylene diamine tetraacetic acid isThe concentration by weight of the methylphosphonic acid is 70 g/L. Adding Cu (NO)3)2·3H2O and AlCl3·6H2Dissolving O in deionized water, adding ethylene glycol, mixing to obtain working solution B, copper (Cu)2+) Concentration of 1.8mol/L, aluminum ion (Al)3+) The concentration is 2.0mol/L, and the weight concentration of the ethylene glycol is 20 g/L. Adding deionized water into a reaction tank, adding 10wt% ammonia water and the mixed solution A into the reaction tank in parallel, wherein the gelling temperature is 62 ℃, the gelling pH value is 7.5, and the gelling time is 1.0 hour to obtain slurry I. And ageing the slurry I under stirring, wherein the stirring speed is 210 rpm, the ageing temperature is 75 ℃, the pH value is 7.2, and the ageing time is 0.6 hour. After the aging is finished, adding the mixed solution B and a sodium carbonate solution into the aged slurry I in a cocurrent manner, wherein the molar ratio of the amount of sodium carbonate to the total amount of copper and zinc is 2.0, the gelling temperature is 60 ℃, the pH value is 9.5, and the gelling time is 2.0 hours, so as to obtain slurry II, aging the slurry II under the stirring condition, wherein the stirring speed is 405 r/m, the aging temperature is 72 ℃, the pH value is 8.9, and the aging time is 3.0 hours, filtering the aged slurry II, washing a filter cake for 3 times by using an ethylene glycol solution (the weight concentration is 15 g/L), drying the filter cake for 15 hours at 100 ℃, adding a proper amount of graphite into the dried material, and pressing the dried material into a sheet to obtain the catalyst A. The composition, pore distribution and main properties are shown in table 1.
Example 2
Cu (NO) was added in the amount shown in Table 1 according to the catalyst B in example 13)2·3H2O、Zn(NO3)2·6H2O and AlCl3·6H2Dissolving O in deionized water, adding hydroxyethylidene diphosphonic acid, mixing to obtain mixed solution A, and adding Cu (NO)3)2·3H2O and Al (NO)3)3·9H2Dissolving O in deionized water, adding butanediol, and mixing to obtain mixed solution B. Adding deionized water into a reaction tank, adding ammonia water with the weight concentration of 9wt% and the mixed solution A into the reaction tank in a concurrent flow manner, wherein the gelling temperature is 52 ℃, the gelling pH value is 7.4, and the gelling time is 0.8 hour to obtain slurry I. The slurry I was aged with stirring,the stirring speed is 180 r/min, the aging temperature is 76 ℃, the aging pH value is 6.9, and the aging time is 0.7 hour. After the aging is finished, adding the mixed solution B and a sodium carbonate solution into the slurry I in a cocurrent manner, wherein the molar ratio of the amount of sodium carbonate to the total amount of copper and zinc is 2.1, the gelling temperature is 60 ℃, the pH value is 9.3, the gelling time is 2.6 hours, so as to obtain slurry II, aging the slurry II under the stirring condition, the stirring speed is 430 revolutions/minute, the aging temperature is 72 ℃, the aging pH value is 8.8, and the aging time is 3.9 hours, filtering the aged slurry II, washing a filter cake for 2 times by using a butanediol solution (the weight concentration is 15 g/L), drying the filter cake for 16 hours at 80 ℃, adding a proper amount of graphite into the dried material, and pressing the dried material into a sheet by using water, so as to obtain the catalyst B. The composition, pore distribution and main properties are shown in table 1.
Example 3
Cu (NO) was added in the amount shown in Table 1 according to the catalyst C in example 13)2·3H2O、Zn(NO3)2·6H2O and Al (NO)3)3·9H2Dissolving O in deionized water, adding polymaleic acid (molecular weight is 500) and hydroxyethylidene diphosphonic acid, mixing to obtain mixed solution A, and adding Cu (NO)3)2·3H2O and Al (NO)3)3·9H2Dissolving O in deionized water, adding salicyl alcohol, and mixing to obtain mixed solution B. Adding deionized water into a reaction tank, adding ammonia water with the weight concentration of 12wt% and the mixed solution A into the reaction tank in parallel, wherein the gelling temperature is 50 ℃, the pH value is 7.8, and the gelling time is 1.1 hours to obtain slurry I. And ageing the slurry I under stirring, wherein the stirring speed is 230 rpm, the ageing temperature is 76 ℃, the ageing pH value is 7.3, and the ageing time is 0.5 hour. After the aging is finished, adding the mixed solution B and a sodium carbonate solution into the slurry I in a cocurrent manner, wherein the molar ratio of the amount of sodium carbonate to the total amount of copper and zinc is 2.6, the gelling temperature is 57 ℃, the gelling pH value is 9.6, the gelling time is 2.9 hours, obtaining slurry II, aging the slurry II under the stirring condition, the stirring speed is 420 r/min, the aging temperature is 75 ℃, the aging pH value is 9.6, the aging time is 4.0 hours, filtering the aged slurry II, washing a filter cake for 2 times by using a salicylic alcohol solution (the weight concentration is 18 g/L),and drying the filter cake at 95 ℃ for 10 hours, adding a proper amount of graphite into the dried material, and pressing the dried material into sheets by water to obtain the catalyst C. The composition, pore distribution and main properties are shown in table 1.
Example 4
Cu (NO) was added in the amount shown in Table 1 according to the method of example 1, based on the catalyst D composition3)2·3H2O、Zn(NO3)2·6H2O and Al2(SO4)3·18H2Dissolving O in deionized water, adding polyacrylic acid (molecular weight is 3000) and ethylenediamine tetramethylene phosphonic acid, mixing to obtain mixed solution A, and adding Cu (NO)3)2·3H2O and Al2(SO4)3·18H2Dissolving O in deionized water, adding glycerol, and mixing to obtain mixed solution B. Adding deionized water into a reaction tank, adding 14wt% ammonia water and the mixed solution A into the reaction tank in parallel, wherein the gelling temperature is 50 ℃, the pH value is 7.3, and the gelling time is 1.1 h, so as to obtain slurry I. And ageing the slurry I under stirring, wherein the stirring speed is 220 rpm, the ageing temperature is 76 ℃, the ageing pH value is 6.8, and the ageing time is 0.6 hour. After aging, adding the mixed solution B and a sodium carbonate solution into the slurry I in a cocurrent manner, controlling the molar ratio of the amount of sodium carbonate to the total amount of copper and zinc to be 2.2, the gelling temperature to be 46 ℃, the gelling pH value to be 10.0 and the gelling time to be 3.8 hours to obtain slurry II, aging the slurry II under stirring conditions, controlling the stirring speed to be 425 revolutions per minute, the aging temperature to be 74 ℃, controlling the pH value to be 9.5 and the aging time to be 3.5 hours, filtering the aged slurry II, washing a filter cake for 2 times by using a glycerol solution (the weight concentration is 14 g/L), drying the filter cake for 16 hours at 90 ℃, adding a proper amount of graphite into the dried material and pressing the dried material into a sheet to obtain a catalyst D. The composition, pore distribution and main properties are shown in table 1.
Comparative example 1
Mixing Cu (NO) according to the component content of the catalyst E in the table 13)2·3H2O、Zn(NO3)2·6H2O and AlCl3·6H2Dissolving O in deionized water to prepare a mixed solution. Adding deionized water into a reaction tank, and mixingAnd (3) adding the combined solution and a sodium carbonate solution into a reaction tank in a concurrent flow manner, wherein the molar ratio of the amount of sodium carbonate to the total amount of copper and zinc is 2.0, the gelling temperature is 60 ℃, the gelling time is 3 hours, and the reaction pH value is 7.6, so as to obtain reaction slurry. Aging the slurry under the condition of stirring, wherein the aging pH value is 7.8, the aging temperature is 75 ℃, the aging time is 3.7 hours, filtering the aged slurry, washing a filter cake for 3 times by deionized water, drying the filter cake for 10 hours at 100 ℃, roasting for 3 hours at 360 ℃, adding a proper amount of graphite into the roasted material, and pressing the mixture into sheets by water to obtain the catalyst E. The composition, pore distribution and main properties are shown in table 1.
Comparative example 2
Mixing Cu (NO) according to the component content of the catalyst F in the table 13)2·3H2O、Zn(NO3)2·6H2O and AlCl3·6H2Dissolving O in deionized water to prepare a mixed solution. Adding deionized water into a reaction tank, adding 10wt% ammonia water and the mixed solution into the reaction tank in parallel, wherein the gelling temperature is 60 ℃, the gelling time is 3 hours, and the reaction pH value is 7.6, so as to obtain reaction slurry. Aging the slurry under the condition of stirring, wherein the aging pH value is 7.8, the aging temperature is 75 ℃, the aging time is 3.7 hours, filtering the aged slurry, washing a filter cake for 3 times by deionized water, drying the filter cake for 10 hours at 100 ℃, roasting for 3 hours at 360 ℃, adding a proper amount of graphite into the roasted material, and pressing the mixture into sheets by water to obtain the catalyst F. The composition, pore distribution and main properties are shown in table 1.
Comparative example 3
Mixing Cu (NO) according to the component content of the catalyst G in the table 13)2·3H2O and AlCl3·6H2Dissolving O in deionized water to prepare solution A. Adding Zn (NO)3)2·6H2O and AlCl3·6H2Dissolving O in deionized water to prepare solution B. Adding deionized water into a reaction tank 1, adding 10wt% ammonia water and the solution A into the reaction tank 1 in parallel, wherein the gelling temperature is 60 ℃, the gelling pH value is 7.5, and the gelling time is 1.0 hour to obtain slurry I. Adding deionized water into a reaction tank 2, and adding 10wt% ammonia water and the solution B in parallelPutting the mixture into a reaction tank 2, wherein the gelling temperature is 60 ℃, the gelling pH value is 9.2, and the gelling time is 2.0 hours, so as to obtain slurry II, mixing the slurry I and the slurry II, aging the mixed slurry under the condition of stirring, wherein the aging pH value is 7.8, the aging temperature is 75 ℃, the aging time is 3.7 hours, filtering the aged slurry, washing a filter cake with deionized water for 3 times, drying the filter cake at 100 ℃ for 10 hours, roasting at 360 ℃ for 3 hours, adding a proper amount of graphite and water pressure into the roasted material to form sheets, so as to obtain a catalyst G. The composition, pore distribution and main properties are shown in table 1.
Comparative example 4
Mixing Cu (NO) according to the component content of catalyst H in the table 13)2·3H2O and AlCl3·6H2Dissolving O in deionized water to obtain mixed solution A, and dissolving Zn (NO)3)2·6H2O and AlCl3·6H2Dissolving O in deionized water to prepare a mixed solution B, adding the deionized water into a reaction tank 1, adding the mixed solution A and a sodium carbonate solution into the reaction tank in a cocurrent manner, wherein the molar ratio of the amount of sodium carbonate to the total amount of copper and zinc is 2.0, the gelling temperature is 60 ℃, the gelling pH value is 7.5, and the gelling time is 1.0 hour, thus obtaining slurry I. Adding deionized water into a reaction tank 2, adding a mixed solution B and a sodium carbonate solution into the reaction tank 2 in a cocurrent manner, wherein the molar ratio of the amount of sodium carbonate to the total amount of copper and zinc is 2.0, the gelling temperature is 60 ℃, the gelling pH value is 9.2, and the gelling time is 2.0 hours, so as to obtain a slurry II, mixing the slurry I and the slurry II, aging the mixed slurry under stirring, wherein the aging pH value is 7.8, the aging temperature is 75 ℃, the aging time is 3.7 hours, filtering the aged slurry, washing a filter cake for 3 times by using the deionized water, drying the filter cake for 10 hours at 100 ℃, roasting for 3 hours at 360 ℃, adding a proper amount of graphite into the roasted material, and pressing the mixture into sheets by using water, so as to obtain a catalyst H. The composition, pore distribution and main properties are shown in table 1.
Comparative example 5
Mixing Cu (NO) according to the component content ratio of catalyst I in Table 13)2·3H2O、Zn(NO3)2·6H2O and AlCl3·6H2Dissolving O in deionized water to prepare a mixed solution A. Adding Cu (NO)3)2·3H2O and AlCl3·6H2Dissolving O in deionized water to prepare a mixed solution B. Adding deionized water into a reaction tank, adding 10wt% ammonia water and the mixed solution A into the reaction tank in parallel, wherein the gelling temperature is 60 ℃, the gelling pH value is 7.5, and the gelling time is 1.0 hour to obtain slurry I. Adding the mixed solution B and a sodium carbonate solution into slurry I which is not aged in a cocurrent manner, wherein the molar ratio of the amount of sodium carbonate to the total amount of copper and zinc is 2.0, the gelling temperature is 60 ℃, the pH value is 9.2, the gelling time is 2.0 hours, so as to obtain slurry II, aging the slurry II under the condition of stirring, the aging temperature is 75 ℃, the aging pH value is 7.8, and the aging time is 3.7 hours, filtering the aged slurry, washing a filter cake for 3 times by using deionized water, drying the filter cake at 100 ℃ for 10 hours, roasting at 360 ℃ for 3 hours, adding a proper amount of graphite into the roasted material, pressing the roasted material into sheets by using water, and thus obtaining the catalyst I. The composition, pore distribution and main properties are shown in table 1.
Comparative example 6
Reference J, having the same composition as the catalyst of example 1, was prepared according to the method disclosed in CN201610773534.7, by the following procedure:
cu (NO) with the catalyst composition of example 13)2·3H2Dissolving O in deionized water to prepare solution A. Adding Zn (NO)3)2·6H2Dissolving O in deionized water to prepare a mixed solution B. Adding deionized water into the reaction tank, and adding sodium metaaluminate solution (containing Al)2O342 g/L) and the mixed solution A are added into a reaction tank in parallel, the gelling temperature is 60 ℃, the gelling pH value is 7.5, and the gelling time is 1.0 hour, thus obtaining slurry I. Sodium metaaluminate solution (containing Al)2O342 g/L) is added into the solution B under stirring, the gelling temperature is kept at 60 ℃, the pH value is controlled at 7.5 when the gelling is finished, and the gelling time is controlled at 2 hours, thereby generating zinc and aluminum containing precipitate slurry II. The two types of slurry containing precipitates were mixed. The aging is started under the condition of stirring, the pH value is 7.8 during the aging, the temperature is 75 ℃, the aging is carried out for 3.7 hours, the materials are filtered after the aging, the filter cake is subjected to hydrothermal treatment under the water vapor containing urea, and the conditions of the hydrothermal treatment are as follows: molar ratio of urea to total amount of active metal atomsThe ratio of the catalyst to the catalyst is 7:1, the temperature is 230 ℃, the pressure is 6.0MPa, the processing time is 4 hours, the filter cake is washed by deionized water for 3 times, the filter cake is dried for 10 hours at 100 ℃, roasted for 3 hours at 360 ℃, and a proper amount of graphite and water are added into the roasted material to press the material into sheets, so that the catalyst J is obtained. The composition, pore distribution and main properties are shown in table 1.
Example 5
Grinding the synthetic methanol catalyst to 16-40 mesh, and using low concentration hydrogen (H) before use2/N2And (vol) = 3/97) reducing the mixed gas of hydrogen and nitrogen for 16-25 h, wherein the maximum reduction temperature is 210 ℃. The activity of the catalyst was evaluated on a miniature fixed bed reactor. The loading of the catalyst is 5ml, and the composition of the raw material gas is CO/H2/CO2/N2=12/70/6/12 (volume ratio), reaction pressure is 5.0MPa, space velocity is 10000h-1The reaction temperature was 250 ℃ and CO were measured2The conversion of (a) is the initial activity of the catalyst. Then the catalyst is heat treated for 5h at 440 ℃ in the synthetic atmosphere, and then the temperature is reduced to 250 ℃ for measuring CO and CO2The conversion of (b) is activity after heat treatment, i.e., heat resistance. The product was analyzed by gas chromatography to give a space-time yield of g.mL of methanol-1·h-1I.e., grams of methanol produced per milliliter of catalyst per hour, the results are shown in table 2.
As can be seen from tables 1 and 2, the catalyst of the present invention has good metal dispersion, thereby improving the synergistic effect between Cu and ZnO catalysts, and has high activity and selectivity, and as can be seen from the test results, the catalyst of the present invention for methanol synthesis has high activity, heat resistance and excellent selectivity.
TABLE 1 catalyst composition and Properties
| Catalyst numbering | A | B | C | D |
| CuO，wt% | 55 | 50 | 46 | 52 |
| ZnO，wt% | 27 | 22 | 25 | 20 |
| Organic auxiliary agent P1 wt% | 5 | 6 | 7 | 6 |
| Organic auxiliary agent P2 wt% | 3 | 4 | 5 | 5 |
| Al2O3，wt% | Balance of | Balance of | Balance of | Balance of |
| Specific surface area, m2/g | 172 | 170 | 167 | 168 |
| Pore volume, mL/g | 0.394 | 0.385 | 0.378 | 0.371 |
TABLE 1
| Catalyst numbering | E | F | G | H | I | J |
| CuO，wt% | 55 | 55 | 55 | 55 | 55 | 55 |
| ZnO，wt% | 27 | 27 | 27 | 27 | 27 | 27 |
| Organic auxiliary agent P1 wt% | - | - | - | - | - | - |
| Organic auxiliary agent P2 wt% | - | - | - | - | - | - |
| Al2O3，wt% | 18 | 18 | 18 | 18 | 18 | 18 |
| Specific surface area, m2/g | 90 | 85 | 96 | 101 | 94 | 172 |
| Pore volume, mL/g | 0.189 | 0.176 | 0.198 | 0.209 | 0.194 | 0.394 |
TABLE 2 degree of dispersion and specific surface area of metallic copper
| Catalyst and process for preparing same | SCu/m2·g-1 | DCu，% |
| A | 62.1 | 29.8 |
| B | 61.4 | 29.3 |
| C | 60.5 | 29.0 |
| D | 60.2 | 28.8 |
| E | 28.5 | 10.2 |
| F | 25.1 | 9.6 |
| G | 25.8 | 9.7 |
| H | 30.1 | 11.1 |
| I | 29.0 | 10.8 |
| J | 49.3 | 15.9 |
SCuIs the specific surface area of copper, DCuIs degree of dispersion of copper
TABLE 3 evaluation of catalyst Activity and Heat resistance test results
| Catalyst and process for preparing same | Initial activity,% of | Initial activity,% of | Activity after heat resistance,% | Activity after heat resistance,% | Methanol space-time yield, (g. mL)-1·h-1） | Methanol selectivity,% of |
| CO | CO2 | CO | CO2 | |||
| A | 95.82 | 87.37 | 89.13 | 79.67 | 4.87 | 97.83 |
| B | 95.71 | 87.25 | 89.05 | 79.59 | 4.80 | 97.74 |
| C | 95.64 | 87.13 | 88.96 | 79.52 | 4.73 | 97.65 |
| D | 95.51 | 87.04 | 88.87 | 79.46 | 4.65 | 97.58 |
| E | 78.89 | 76.12 | 67.15 | 60.02 | 1.86 | 80.74 |
| F | 78.15 | 76.01 | 66.74 | 59.56 | 1.80 | 80.02 |
| G | 78.97 | 76.26 | 67.31 | 60.08 | 1.90 | 80.93 |
| H | 79.56 | 76.54 | 67.58 | 60.13 | 1.88 | 80.81 |
| I | 78.91 | 76.39 | 67.42 | 60.09 | 1.92 | 80.98 |
| J | 92.35 | 83.48 | 85.85 | 74.59 | 3.05 | 96.05 |
Claims (18)
1. A copper-containing catalyst characterized by: based on the weight of the catalyst, the catalyst comprises the following components: CuO 15-60%, ZnO 10-35%, Al2O310-35 percent of organic additive, 2-25 percent of organic additive; the organic assistant is organic assistant P1 and organic assistant P2, the organic assistant P1 is organic phosphonic acid compound and/or carboxylic acid polymer, and the organic assistant P2 is organic alcohol.
2. The copper-containing catalyst of claim 1, wherein: based on the weight of the catalyst, the content of the organic assistant P1 is 2wt% -15 wt%, and the content of the organic assistant P2 is 2wt% -11 wt%.
3. The copper-containing catalyst of claim 1, wherein: the organic phosphonic acid compound is selected from one or more of ethylenediamine tetramethylene phosphonic acid, hydroxyethylidene diphosphonic acid, polyalcohol phosphonate ester, polyaminopolyether methylene phosphonic acid, 1,2, 4-tricarboxylic acid-2-phosphonic butane, hydroxyphosphonoacetic acid, aminotrimethylene phosphonic acid or diethylenetriamine pentamethylene phosphonic acid; the molecular weight of the carboxylic acid polymer is 400-5000, and the carboxylic acid polymer is selected from one or more of polyacrylic acid, polymethacrylic acid, polymaleic acid, polyaspartic acid, polyepoxysuccinic acid, acrylic acid-hydroxypropyl acrylate copolymer or maleic acid-acrylic acid copolymer.
4. The copper-containing catalyst of claim 1, wherein: the organic auxiliary agent P2 is selected from organic alcohol with 3-10 carbon atoms.
5. The copper-containing catalyst of claim 1, wherein: the specific surface area of metallic copper in the copper-containing catalyst after reduction is 35-120 m2The dispersity of the metal copper is 13-45 percent.
6. A process for preparing a copper-containing catalyst according to any one of claims 1 to 5, characterized by comprising: (1) carrying out parallel flow gelling reaction on the mixed solution A and ammonia water to obtain slurry I, and then aging; (2) dropwise adding the mixed solution B and a sodium carbonate solution into the aged slurry I obtained in the step (1) in a parallel flow manner, carrying out gelling reaction to obtain slurry II, and then aging; (3) carrying out solid-liquid separation on the material obtained in the step (2), and drying and forming a solid phase to obtain a catalyst; wherein the mixed solution A is an aqueous solution containing soluble copper salt, soluble zinc salt and soluble aluminum salt, and the mixed solution B is an aqueous solution containing soluble copper salt and soluble aluminum salt; wherein the organic assistant P1 is added in the step (1), and the organic assistant P2 is added in the step (2).
7. The method of claim 6, wherein: in the step (1), the organic auxiliary agent P1 is independently added in a parallel flow manner or is added when the mixed solution A is prepared; the organic auxiliary agent P2 is added in the step (2) and is added separately or added when the mixed solution B is prepared.
8. The method of claim 6, wherein: the dosage of the organic auxiliary agent P1 added in the step (1) accounts for 10-90% of the total dosage of the organic auxiliary agent.
9. The method of claim 6, wherein: when the organic assistant P1 is added in the step (1), the adding amount of the organic assistant P1 is 5-120 g/L based on the volume of the mixed solution A; when the organic assistant P2 is added in the step (2), the addition amount of the organic assistant P2 is 2-50 g/L based on the volume of the mixed solution B.
10. The method of claim 6, wherein: in the mixed solution A in the step (1), the concentration of the soluble copper salt is Cu2+Calculated as 1.0-5.0 mol/L, and the concentration of soluble zinc salt is Zn2+0.5 to 6.0mol/L in terms of Al, and a concentration of soluble aluminum salt3+The amount is 1.0-6.0 mol/L; the copper content in the mixed solution A is 40-80% of the copper content in the catalyst, and the aluminum content in the mixed solution A is 45-85% of the aluminum content in the catalyst.
11. The method of claim 6, wherein: the gelling reaction conditions in the step (1) are as follows: the reaction temperature is 30-80 ℃, the reaction time is 0.2-2.0 hours, and the pH value is 6.0-9.0.
12. The method of claim 6, wherein: the aging conditions of the slurry I in the step (1) are as follows: the aging temperature is 40-90 ℃, the pH value is 6.0-8.0, and the aging time is 0.2-1.0 hour.
13. The method of claim 6, wherein: in the mixed solution B in the step (2), the concentration of the soluble copper salt is Cu2+0.5 to 4.0mol/L in terms of Al, and a concentration of soluble aluminum salt3+The amount is 0.5-5.0 mol/L; the copper content in the mixed solution B is 20-60% of the copper content in the catalyst, and the aluminum content in the mixed solution B is 15-55% of the aluminum content in the catalyst.
14. The method of claim 6, wherein: in the reaction material in the step (2), the molar ratio of the amount of the sodium carbonate to the total amount of copper and zinc is 0.5-4.0.
15. The method of claim 6, wherein: the gelling reaction conditions in the step (2) are as follows: the reaction temperature is 30-90 ℃, the reaction time is 1.5-4.0 hours, the pH value is 8.5-12.0, and the pH value is at least 1.0 higher than that of the gelling reaction in the step (1).
16. The method of claim 6, wherein: the aging conditions of the slurry II in the step (2) are as follows: the aging temperature is 40-90 ℃, the aging time is 1.5-6.0 hours, and the pH value is 7.5-11.0 which is at least 0.5 higher than the pH value of the aging in the step (1).
17. The method of claim 6, wherein: and (3) drying at 50-120 ℃ for 2-36 hours.
18. Use of a copper-containing catalyst according to any one of claims 1 to 5 in a catalytic hydrogenation reaction.
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