CN115518644B - 一种渣油加氢脱金属催化剂的制备方法 - Google Patents
一种渣油加氢脱金属催化剂的制备方法 Download PDFInfo
- Publication number
- CN115518644B CN115518644B CN202110708835.2A CN202110708835A CN115518644B CN 115518644 B CN115518644 B CN 115518644B CN 202110708835 A CN202110708835 A CN 202110708835A CN 115518644 B CN115518644 B CN 115518644B
- Authority
- CN
- China
- Prior art keywords
- aging
- water
- high polymer
- solution
- soluble high
- 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.)
- Active
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 52
- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 40
- 230000032683 aging Effects 0.000 claims abstract description 39
- 239000000243 solution Substances 0.000 claims abstract description 33
- 229910052751 metal Inorganic materials 0.000 claims abstract description 30
- 239000002184 metal Substances 0.000 claims abstract description 30
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000012266 salt solution Substances 0.000 claims abstract description 22
- 229920000642 polymer Polymers 0.000 claims abstract description 19
- 238000001035 drying Methods 0.000 claims abstract description 18
- VXAUWWUXCIMFIM-UHFFFAOYSA-M aluminum;oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Al+3] VXAUWWUXCIMFIM-UHFFFAOYSA-M 0.000 claims abstract description 16
- 230000002378 acidificating effect Effects 0.000 claims abstract description 11
- 238000006386 neutralization reaction Methods 0.000 claims abstract description 11
- 239000002002 slurry Substances 0.000 claims abstract description 11
- 239000011148 porous material Substances 0.000 claims abstract description 10
- 238000005406 washing Methods 0.000 claims abstract description 6
- 238000004898 kneading Methods 0.000 claims abstract description 5
- 238000001914 filtration Methods 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 17
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 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 7
- 229910052708 sodium Inorganic materials 0.000 claims description 7
- 239000011734 sodium Substances 0.000 claims description 7
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims description 6
- 239000002202 Polyethylene glycol Substances 0.000 claims description 6
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 6
- 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 claims description 6
- 229920001223 polyethylene glycol Polymers 0.000 claims description 6
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 229920000609 methyl cellulose Polymers 0.000 claims description 5
- 239000001923 methylcellulose Substances 0.000 claims description 5
- 235000010981 methylcellulose Nutrition 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 5
- 239000001301 oxygen Substances 0.000 claims description 5
- 229920002401 polyacrylamide Polymers 0.000 claims description 4
- 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 claims description 2
- WPUINVXKIPAAHK-UHFFFAOYSA-N aluminum;potassium;oxygen(2-) Chemical compound [O-2].[O-2].[Al+3].[K+] WPUINVXKIPAAHK-UHFFFAOYSA-N 0.000 claims description 2
- 238000000465 moulding Methods 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 12
- 239000002253 acid Substances 0.000 abstract description 9
- 238000006477 desulfuration reaction Methods 0.000 abstract description 5
- 230000023556 desulfurization Effects 0.000 abstract description 5
- 230000000052 comparative effect Effects 0.000 description 11
- 239000003921 oil Substances 0.000 description 11
- 238000011156 evaluation Methods 0.000 description 9
- 229910052799 carbon Inorganic materials 0.000 description 6
- DDTIGTPWGISMKL-UHFFFAOYSA-N molybdenum nickel Chemical compound [Ni].[Mo] DDTIGTPWGISMKL-UHFFFAOYSA-N 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000000295 fuel oil Substances 0.000 description 4
- 238000005984 hydrogenation reaction Methods 0.000 description 4
- 229920003169 water-soluble polymer Polymers 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- RGHNJXZEOKUKBD-UHFFFAOYSA-N D-gluconic acid Natural products OCC(O)C(O)C(O)C(O)C(O)=O RGHNJXZEOKUKBD-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 2
- RGHNJXZEOKUKBD-SQOUGZDYSA-N Gluconic acid Natural products OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C(O)=O RGHNJXZEOKUKBD-SQOUGZDYSA-N 0.000 description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 239000012752 auxiliary agent Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000004202 carbamide Substances 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 235000012208 gluconic acid Nutrition 0.000 description 2
- 239000000174 gluconic acid Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910000476 molybdenum oxide Inorganic materials 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 229910000480 nickel oxide Inorganic materials 0.000 description 2
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 description 2
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- CKQGJVKHBSPKST-UHFFFAOYSA-N [Ni].P#[Mo] Chemical compound [Ni].P#[Mo] CKQGJVKHBSPKST-UHFFFAOYSA-N 0.000 description 1
- 239000002671 adjuvant Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 229910052596 spinel Inorganic materials 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/88—Molybdenum
- B01J23/883—Molybdenum and nickel
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/635—0.5-1.0 ml/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/638—Pore volume more than 1.0 ml/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
- C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
- C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
-
- 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
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/202—Heteroatoms content, i.e. S, N, O, P
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/205—Metal content
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/04—Diesel oil
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Catalysts (AREA)
Abstract
Description
反应条件 | |
温度,℃ | 405 |
压力,MPa, | 16 |
空速,h-1 | 0.5 |
氢油体积比 | 800 |
原料 | 中东渣油 |
S,wt% | 2.98 |
Ni,µg/g | 32.5 |
V,µg/g | 59.6 |
实施例1 | 实施例2 | 实施例3 | 实施例4 | 实施例5 | 比较例1 | 比较例2 | 比较例3 | |
催化剂编号 | A | B | C | D | E | F | G | H |
比表面积,m2/g | 216 | 210 | 205 | 192 | 202 | 141 | 111 | 163 |
孔容,mL/g | 0.95 | 0.92 | 0.96 | 1.02 | 0.98 | 0.71 | 0.68 | 0.45 |
可几孔径,nm | 20 | 20 | 20 | 22 | 20 | 17 | 22 | 9 |
MoO3,% | 13.1 | 13.2 | 6.8 | 16.7 | 13.2 | 13.3 | 13.2 | 13.3 |
NiO,% | 3.2 | 3.3 | 3.4 | 4.2 | 3.2 | 3.2 | 3.1 | 3.1 |
酸性质 | ||||||||
150-250℃,mL/g | 6.741 | 6.626 | 6.726 | 6.787 | 6.426 | 5.24 | 5.421 | 6.341 |
250-400℃,mL/g | 3.123 | 3.233 | 3.216 | 3.31 | 3.116 | 2.568 | 2.089 | 2.865 |
400-500℃,mL/g | 1.072 | 1.072 | 1.052 | 1.062 | 1.006 | 0.552 | 0.465 | 0.645 |
总酸量,mL/g | 10.936 | 10.931 | 10.994 | 11.159 | 10.548 | 8.36 | 7.975 | 9.851 |
评价试验结果 | ||||||||
脱硫率,wt% | 83.9 | 83.7 | 81.6 | 86.5 | 83.4 | 77.5 | 73.8 | 63.5 |
脱金属率,wt% | 89.2 | 90.3 | 86.5 | 91.8 | 89.6 | 84.5 | 85.2 | 60.2 |
柴油收率,wt% | 13.9 | 13.6 | 14.6 | 15.8 | 14.0 | 7.9 | 7.3 | 5.8 |
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110708835.2A CN115518644B (zh) | 2021-06-25 | 2021-06-25 | 一种渣油加氢脱金属催化剂的制备方法 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110708835.2A CN115518644B (zh) | 2021-06-25 | 2021-06-25 | 一种渣油加氢脱金属催化剂的制备方法 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115518644A CN115518644A (zh) | 2022-12-27 |
CN115518644B true CN115518644B (zh) | 2024-01-09 |
Family
ID=84694358
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110708835.2A Active CN115518644B (zh) | 2021-06-25 | 2021-06-25 | 一种渣油加氢脱金属催化剂的制备方法 |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115518644B (zh) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004010797A (ja) * | 2002-06-07 | 2004-01-15 | Idemitsu Kosan Co Ltd | 燃料電池用燃料油及びその製造方法 |
CN1952055A (zh) * | 2005-10-19 | 2007-04-25 | 中国石油化工股份有限公司 | 一种烃类加氢处理催化剂的制备方法 |
CN102309994A (zh) * | 2010-07-07 | 2012-01-11 | 中国石油化工股份有限公司 | 一种氧化铝载体的制备方法 |
CN103785397A (zh) * | 2012-11-01 | 2014-05-14 | 中国石油化工股份有限公司 | 一种加氢脱残炭催化剂及其制备方法 |
CN103801312A (zh) * | 2012-11-08 | 2014-05-21 | 中国石油化工股份有限公司 | 一种加氢处理催化剂的制备方法 |
CN105582951A (zh) * | 2014-10-22 | 2016-05-18 | 中国石油化工股份有限公司 | 一种含碱土金属加氢脱金属催化剂的制备方法 |
CN112742425A (zh) * | 2019-10-29 | 2021-05-04 | 中国石油化工股份有限公司 | 一种加氢催化剂及其制备方法 |
-
2021
- 2021-06-25 CN CN202110708835.2A patent/CN115518644B/zh active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004010797A (ja) * | 2002-06-07 | 2004-01-15 | Idemitsu Kosan Co Ltd | 燃料電池用燃料油及びその製造方法 |
CN1952055A (zh) * | 2005-10-19 | 2007-04-25 | 中国石油化工股份有限公司 | 一种烃类加氢处理催化剂的制备方法 |
CN102309994A (zh) * | 2010-07-07 | 2012-01-11 | 中国石油化工股份有限公司 | 一种氧化铝载体的制备方法 |
CN103785397A (zh) * | 2012-11-01 | 2014-05-14 | 中国石油化工股份有限公司 | 一种加氢脱残炭催化剂及其制备方法 |
CN103801312A (zh) * | 2012-11-08 | 2014-05-21 | 中国石油化工股份有限公司 | 一种加氢处理催化剂的制备方法 |
CN105582951A (zh) * | 2014-10-22 | 2016-05-18 | 中国石油化工股份有限公司 | 一种含碱土金属加氢脱金属催化剂的制备方法 |
CN112742425A (zh) * | 2019-10-29 | 2021-05-04 | 中国石油化工股份有限公司 | 一种加氢催化剂及其制备方法 |
Non-Patent Citations (1)
Title |
---|
劣质蜡油加氢处理催化剂载体的制备;于婷婷;《中国优秀硕士学位论文全文数据库工程科技Ⅰ辑》(第1期);24-40 * |
Also Published As
Publication number | Publication date |
---|---|
CN115518644A (zh) | 2022-12-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109718797A (zh) | 一种加氢处理催化剂的制备方法 | |
EP2969185B1 (en) | Novel resid hydrotreating catalyst | |
CN109364957B (zh) | 一种超深度脱硫催化剂及其制备方法和应用 | |
CN110404523B (zh) | 一种改性氧化铝载体、加氢脱硫催化剂和应用 | |
JPWO2015053087A1 (ja) | 重質炭化水素油の水素化処理触媒、重質炭化水素油の水素化処理触媒の製造方法、及び重質炭化水素油の水素化処理方法 | |
CN112742425B (zh) | 一种加氢催化剂及其制备方法 | |
CN109718798A (zh) | 加氢处理催化剂的制备方法 | |
CN103801312B (zh) | 一种加氢处理催化剂的制备方法 | |
CN115518644B (zh) | 一种渣油加氢脱金属催化剂的制备方法 | |
CN111135857B (zh) | 还原型催化剂的制备方法及其用途 | |
CN103801346A (zh) | 一种制备加氢处理催化剂的方法 | |
CN107961773B (zh) | 一种加氢脱硫催化剂及其制备方法和硫化态加氢脱硫催化剂的制备方法 | |
CN105709802A (zh) | 一种高金属分散度加氢裂化催化剂及其制备方法 | |
CN111195522A (zh) | 一种渣油加氢脱金属催化剂及其制备方法 | |
CN111195525A (zh) | 一种渣油加氢脱硫催化剂及其制备方法 | |
CN115518663B (zh) | 一种渣油加氢裂化催化剂的制备方法 | |
CN103785405A (zh) | 一种加氢脱金属催化剂及其制备方法 | |
CN117000276A (zh) | 一种加氢脱硫催化剂及其制备方法 | |
CN116060056B (zh) | 一种渣油加氢脱金属催化剂及其制备方法和应用 | |
CN115518645B (zh) | 加氢脱金属催化剂及其制法和回收利用 | |
CN115254083A (zh) | 一种铝锆复合载体的制备方法、包含该载体的馏分油加氢精制催化剂 | |
CN113019407B (zh) | 加氢处理催化剂及其制备方法和应用 | |
CN113019406B (zh) | 一种制备加氢处理催化剂的方法 | |
CN115518693B (zh) | 一种加氢脱金属催化剂及其制备方法和回收利用 | |
CN113019445B (zh) | 改性加氢处理催化剂载体、催化剂及其制备方法和应用 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
TA01 | Transfer of patent application right | ||
TA01 | Transfer of patent application right |
Effective date of registration: 20231203 Address after: 100728 No. 22 North Main Street, Chaoyang District, Beijing, Chaoyangmen Applicant after: CHINA PETROLEUM & CHEMICAL Corp. Applicant after: Sinopec (Dalian) Petrochemical Research Institute Co.,Ltd. Address before: 100728 No. 22 North Main Street, Chaoyang District, Beijing, Chaoyangmen Applicant before: CHINA PETROLEUM & CHEMICAL Corp. Applicant before: DALIAN RESEARCH INSTITUTE OF PETROLEUM AND PETROCHEMICALS, SINOPEC Corp. |
|
GR01 | Patent grant | ||
GR01 | Patent grant |