CN106905997B - Catalyst used in series connection type boiling bed hydrogenation treatment process of inferior heavy oil - Google Patents
Catalyst used in series connection type boiling bed hydrogenation treatment process of inferior heavy oil Download PDFInfo
- Publication number
- CN106905997B CN106905997B CN201710240112.8A CN201710240112A CN106905997B CN 106905997 B CN106905997 B CN 106905997B CN 201710240112 A CN201710240112 A CN 201710240112A CN 106905997 B CN106905997 B CN 106905997B
- Authority
- CN
- China
- Prior art keywords
- catalyst
- hydrotreating catalyst
- aluminium hydroxide
- spherical
- hydroxide powder
- 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 184
- 239000000295 fuel oil Substances 0.000 title claims abstract description 36
- 238000009835 boiling Methods 0.000 title claims abstract description 29
- 238000000034 method Methods 0.000 title claims abstract description 29
- 230000008569 process Effects 0.000 title claims abstract description 20
- 238000005984 hydrogenation reaction Methods 0.000 title claims description 25
- 239000003921 oil Substances 0.000 claims abstract description 37
- 239000002245 particle Substances 0.000 claims abstract description 24
- 238000005299 abrasion Methods 0.000 claims abstract description 12
- 239000000843 powder Substances 0.000 claims description 65
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims description 61
- 229910021502 aluminium hydroxide Inorganic materials 0.000 claims description 61
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 54
- 239000000243 solution Substances 0.000 claims description 44
- 239000011324 bead Substances 0.000 claims description 42
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 40
- 229910052719 titanium Inorganic materials 0.000 claims description 40
- 239000010936 titanium Substances 0.000 claims description 40
- 229910052746 lanthanum Inorganic materials 0.000 claims description 39
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical group [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 claims description 39
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 38
- 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 30
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 28
- 229910052759 nickel Inorganic materials 0.000 claims description 28
- 230000003647 oxidation Effects 0.000 claims description 21
- 238000007254 oxidation reaction Methods 0.000 claims description 21
- 239000007864 aqueous solution Substances 0.000 claims description 20
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 19
- 239000002253 acid Substances 0.000 claims description 15
- 229910052750 molybdenum Inorganic materials 0.000 claims description 15
- 239000011733 molybdenum Substances 0.000 claims description 14
- 229910000480 nickel oxide Inorganic materials 0.000 claims description 14
- 238000002360 preparation method Methods 0.000 claims description 14
- 239000007787 solid Substances 0.000 claims description 14
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 claims description 13
- 239000011148 porous material Substances 0.000 claims description 13
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 11
- 239000000377 silicon dioxide Substances 0.000 claims description 11
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 10
- 239000012535 impurity Substances 0.000 claims description 10
- 229910017604 nitric acid Inorganic materials 0.000 claims description 10
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 9
- 230000002378 acidificating effect Effects 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 9
- 230000000149 penetrating effect Effects 0.000 claims description 9
- 229910052698 phosphorus Inorganic materials 0.000 claims description 9
- 239000011574 phosphorus Substances 0.000 claims description 9
- 239000007921 spray Substances 0.000 claims description 9
- 230000033764 rhythmic process Effects 0.000 claims description 8
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 8
- 239000000470 constituent Substances 0.000 claims description 6
- 230000000694 effects Effects 0.000 claims description 5
- 238000005516 engineering process Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- 229910052761 rare earth metal Inorganic materials 0.000 claims description 5
- 239000011280 coal tar Substances 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 4
- 239000003208 petroleum Substances 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 3
- -1 siliceous Substances 0.000 claims description 3
- 150000002739 metals Chemical class 0.000 claims description 2
- 239000000428 dust Substances 0.000 claims 1
- 229940098458 powder spray Drugs 0.000 claims 1
- 238000004231 fluid catalytic cracking Methods 0.000 abstract description 8
- 230000007547 defect Effects 0.000 abstract 1
- 238000012545 processing Methods 0.000 description 15
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 12
- 239000002994 raw material Substances 0.000 description 11
- 239000000126 substance Substances 0.000 description 10
- 239000000084 colloidal system Substances 0.000 description 9
- 238000011156 evaluation Methods 0.000 description 9
- 239000001257 hydrogen Substances 0.000 description 9
- 229910052739 hydrogen Inorganic materials 0.000 description 9
- 229910021645 metal ion Inorganic materials 0.000 description 8
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 230000003197 catalytic effect Effects 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 229910000476 molybdenum oxide Inorganic materials 0.000 description 6
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 241000772415 Neovison vison Species 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 239000005864 Sulphur Substances 0.000 description 4
- 238000006555 catalytic reaction Methods 0.000 description 4
- 229910000008 nickel(II) carbonate Inorganic materials 0.000 description 4
- ZULUUIKRFGGGTL-UHFFFAOYSA-L nickel(ii) carbonate Chemical compound [Ni+2].[O-]C([O-])=O ZULUUIKRFGGGTL-UHFFFAOYSA-L 0.000 description 4
- XYOVOXDWRFGKEX-UHFFFAOYSA-N azepine Chemical compound N1C=CC=CC=C1 XYOVOXDWRFGKEX-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 229910052681 coesite Inorganic materials 0.000 description 3
- 229910052906 cristobalite Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- JKQOBWVOAYFWKG-UHFFFAOYSA-N molybdenum trioxide Inorganic materials O=[Mo](=O)=O JKQOBWVOAYFWKG-UHFFFAOYSA-N 0.000 description 3
- 229910052682 stishovite Inorganic materials 0.000 description 3
- 229910052905 tridymite Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229910017318 Mo—Ni Inorganic materials 0.000 description 2
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 2
- XFBXDGLHUSUNMG-UHFFFAOYSA-N alumane;hydrate Chemical compound O.[AlH3] XFBXDGLHUSUNMG-UHFFFAOYSA-N 0.000 description 2
- 239000004411 aluminium Substances 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 description 2
- 229940010552 ammonium molybdate Drugs 0.000 description 2
- 235000018660 ammonium molybdate Nutrition 0.000 description 2
- 239000011609 ammonium molybdate Substances 0.000 description 2
- 239000011260 aqueous acid Substances 0.000 description 2
- FYDKNKUEBJQCCN-UHFFFAOYSA-N lanthanum(3+);trinitrate Chemical compound [La+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O FYDKNKUEBJQCCN-UHFFFAOYSA-N 0.000 description 2
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 2
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 description 2
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 description 2
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- WURBVZBTWMNKQT-UHFFFAOYSA-N 1-(4-chlorophenoxy)-3,3-dimethyl-1-(1,2,4-triazol-1-yl)butan-2-one Chemical compound C1=NC=NN1C(C(=O)C(C)(C)C)OC1=CC=C(Cl)C=C1 WURBVZBTWMNKQT-UHFFFAOYSA-N 0.000 description 1
- 239000004254 Ammonium phosphate Substances 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 229910017313 Mo—Co Inorganic materials 0.000 description 1
- 229910003978 SiClx Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910000148 ammonium phosphate Inorganic materials 0.000 description 1
- 235000019289 ammonium phosphates Nutrition 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000006253 efflorescence Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000003837 high-temperature calcination Methods 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- JLRJWBUSTKIQQH-UHFFFAOYSA-K lanthanum(3+);triacetate Chemical compound [La+3].CC([O-])=O.CC([O-])=O.CC([O-])=O JLRJWBUSTKIQQH-UHFFFAOYSA-K 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000009703 powder rolling Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000001141 propulsive effect Effects 0.000 description 1
- 206010037844 rash Diseases 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 229910000162 sodium phosphate Inorganic materials 0.000 description 1
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
Classifications
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
- B01J27/19—Molybdenum
-
- 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
-
- 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
- C10G45/14—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 with moving solid particles
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
Description
Catalyst | Spherical pre-hydrotreating catalyst -1 | Spherical main hydrotreating catalyst -1 |
Particle size range, mm | 0.82-0.90 | 0.82-0.90 |
Breaking strength, N/ grains | 8.2 | 9.2 |
Abrasion, wt% | 0.25 | 0.11 |
La wt% | 0.025 | - |
SiO2Wt% | - | 1.5 |
P2O5Wt% | - | 2.7 |
TiO2Wt% | - | 2.6 |
NiO wt% | 1.2 | 2.6 |
MoO3Wt% | 8.3 | 18.2 |
Catalyst | Spherical pre-hydrotreating catalyst -3 | Spherical main hydrotreating catalyst -3 |
Particle size range, mm | 0.90-0.95 | 0.90-0.95 |
Breaking strength, N/ grains | 9.8 | 12.1 |
Abrasion, wt% | 0.08 | 0.06 |
La wt% | 0.041 | - |
SiO2Wt% | - | 2.5 |
TiO2Wt% | - | 4.1 |
P2O5Wt% | - | 3.8 |
NiO wt% | 2.2 | 3.6 |
MoO3Wt% | 10.5 | 20.5 |
Catalyst | Spherical pre-hydrotreating catalyst -4 | Spherical main hydrotreating catalyst -4 |
Particle size range, mm | 0.95-1.00 | 0.95-1.00 |
Breaking strength, N/ grains | 10.2 | 12.8 |
Abrasion, wt% | 0.07 | 0.02 |
La wt% | 0.044 | - |
SiO2Wt% | - | 3.0 |
TiO2Wt% | - | 5.8 |
P2O5Wt% | - | 4.2 |
NiO wt% | 2.5 | 4.2 |
MoO3Wt% | 11.5 | 21.1 |
Claims (4)
- A kind of 1. catalyst that tandem inferior heavy oil boiling bed hydrogenation handling process uses, it is characterised in that:Including spherical Pre-hydrotreating catalyst and spherical main hydrotreating catalyst, inferior heavy oil is first in spherical pre-hydrotreating catalyst Effect is lower to react, and is then reacted in the presence of spherical main hydrotreating catalyst, the diameter of spherical pre-hydrotreating catalyst For 0.82-1.15mm, abrasion are less than 0.3wt%, and breaking strength is more than 8.0N/ grains;Spherical main hydrotreating catalyst it is a diameter of 0.82-1.15mm, abrasion are less than 0.2wt%, and breaking strength is more than 9.0N/ grains;Spherical pre-hydrotreating catalyst is mounted in pre- hydrogenation Handle in fluidized bed reactor, spherical main hydrotreating catalyst is mounted in main hydrotreating fluidized bed reactor, at pre- hydrogenation Reason fluidized bed reactor is used in series with main hydrotreating fluidized bed reactor;Described spherical pre-hydrotreating catalyst uses the alumina globule containing rare earth element as carrier, loads nickel element and molybdenum Element is active component, and rare earth element is lanthanum element, and the content of lanthanum element is 0.02-0.06wt%;In terms of oxide, nickel oxide Content is 1.0-3.5wt%, and oxidation molybdenum content is 8.0-15.0wt%;Described spherical pre-hydrotreating catalyst is prepared using bonding-acidifying-spin ball making process, is comprised the following steps that:(1)At room temperature, aluminium hydroxide powder is placed in the rotary drum of bowling machine, the aluminium hydroxide powder spray under rotation into rotary drum Enter aluminum nitrate solution and the diluted nitric acid aqueous solution containing lanthanum element, aluminium hydroxide powder made of above-mentioned aluminium hydroxide powder to exist Microballoon is formed in the presence of aluminum nitrate solution and diluted nitric acid aqueous solution, the dust technology with aluminum nitrate solution and containing lanthanum element is molten The continuous penetrating of liquid, the amount of the aluminium hydroxide powder of microballoon adhesion gradually increases, in the presence of solid bowl centrifuges power, the body of microballoon Product becomes larger, and forms the bead of aluminium hydroxide powder containing lanthanum, controls the size of solid bowl centrifuges power and sprays into aluminum nitrate solution and contain The speed rhythm of the diluted nitric acid aqueous solution of lanthanum element, produce the bead of aluminium hydroxide powder containing lanthanum of required particle diameter;(2)The bead of aluminium hydroxide powder containing lanthanum is transferred in magazine from the rotary drum of bowling machine, 100-120 DEG C of temperature in drying box 3-4 hours are dried under the conditions of degree, dried bead is fitted into saggar, in roaster at a temperature of 850-950 DEG C, is calcined 2.5- After 3.5 hours, lanthanum containing alumina bead carrier is produced;(3)Lanthanum containing alumina bead carrier is loaded in the rotary drum of spray-stain machine, rotate the acid that spray-stain contains nickel, molybdenum element at room temperature The property aqueous solution, the lanthanum containing alumina bead carrier that spray-stain has nickel, molybdenum element is placed in drying box, 110-120 DEG C of temperature conditionss Under, 4-5 hours are dried, are then transferred in saggar, 450-550 DEG C of roasting 3-4 hour, produce spherical pre-hydrotreating catalyst;Described spherical main hydrotreating catalyst uses the alumina globule of siliceous, titanium, P elements as carrier, loads nickel element It is active component with molybdenum element, in terms of oxide, silica content 1.0-5.0wt%, titanium oxide content 2.0-7.0wt%, Oxidation phosphorus content is 2.5-5.5wt%, nickel oxide content 2.5-5.5wt%;Oxidation molybdenum content is 18.0-24.0wt%;Described spherical main hydrotreating catalyst is prepared using bonding-acidifying-spin ball making process, is comprised the following steps that:(1)At room temperature, siliceous, titanium aluminium hydroxide powder is placed in the rotary drum of bowling machine, under rotation into rotary drum it is siliceous, The aluminium hydroxide powder of titanium sprays into made of above-mentioned aluminium hydroxide powder aluminum nitrate solution and the diluted acid containing P elements is water-soluble Liquid, siliceous, titanium aluminium hydroxide powder form microballoon in the presence of aluminum nitrate solution and dilute acid solution containing P elements, The continuous penetrating of dilute acid solution with aluminum nitrate solution and containing P elements, siliceous, titanium the aluminium hydroxide of microballoon adhesion The amount of powder gradually increases, and in the presence of solid bowl centrifuges power, the volume of microballoon becomes larger, and forms siliceous, titanium, P elements Aluminium hydroxide powder bead, control the size of solid bowl centrifuges power and spray into aluminum nitrate solution and the dilute acid solution containing P elements Speed rhythm, produce needed for the siliceous of particle diameter, titanium, the aluminium hydroxide powder bead of P elements;(2)The aluminium hydroxide powder bead of siliceous, titanium, P elements is transferred in magazine from the rotary drum of bowling machine, in drying box 3-4 hours are dried under 100-120 DEG C of temperature conditionss, dried bead is fitted into saggar, 550-650 DEG C of temperature in roaster Under, after being calcined 2.5-3.5 hours, produce the alumina globule carrier of siliceous, titanium, P elements;(3)The alumina globule carrier of siliceous, titanium, P elements is loaded in the rotary drum of spray-stain machine, rotate spray-stain at room temperature and contain The acidic aqueous solution of nickel, molybdenum element, by spray-stain have nickel, the siliceous of molybdenum element, titanium, P elements alumina globule carrier be placed in it is dry In dry case, under 110-120 DEG C of temperature conditionss, 4-5 hours are dried, are then transferred to 450-550 DEG C of roasting 3-4 hour in saggar, i.e., Obtain spherical main hydrotreating catalyst.
- 2. the catalyst that tandem inferior heavy oil boiling bed hydrogenation handling process according to claim 1 uses, it is special Sign is:Described inferior heavy oil is petroleum residual oil component oil inferior, the high temperature inferior that metals content impurity is less than 400ppm The inferior heavy oil that the heavy constituent of coal tar is oily or petroleum residual oil component inferior and the heavy constituent of high temperature coal-tar inferior reconcile into.
- 3. the catalyst that tandem inferior heavy oil boiling bed hydrogenation handling process according to claim 1 uses, it is special Sign is:The preparation process of spherical pre-hydrotreating catalyst(1)In, the specific surface area of described aluminium hydroxide powder is 240- 300m2/ g, pore volume 0.75-0.90mL/g.
- 4. the catalyst that tandem inferior heavy oil boiling bed hydrogenation handling process according to claim 1 uses, it is special Sign is:The preparation process of spherical main hydrotreating catalyst(1)In, the ratio table of described siliceous, titanium aluminium hydroxide powder Area is 300-380m2/ g, pore volume 0.90-1.20mL/g.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710240112.8A CN106905997B (en) | 2017-04-13 | 2017-04-13 | Catalyst used in series connection type boiling bed hydrogenation treatment process of inferior heavy oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710240112.8A CN106905997B (en) | 2017-04-13 | 2017-04-13 | Catalyst used in series connection type boiling bed hydrogenation treatment process of inferior heavy oil |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106905997A CN106905997A (en) | 2017-06-30 |
CN106905997B true CN106905997B (en) | 2017-12-05 |
Family
ID=59209452
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710240112.8A Active CN106905997B (en) | 2017-04-13 | 2017-04-13 | Catalyst used in series connection type boiling bed hydrogenation treatment process of inferior heavy oil |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106905997B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110028984A (en) * | 2019-04-26 | 2019-07-19 | 河南百优福生物能源有限公司 | Biomass pyrolysis liquid hydrogenation deoxidation oil hydrocracking catalyst and its preparation method and application |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102453547A (en) * | 2010-10-15 | 2012-05-16 | 中国石油化工股份有限公司 | Heavy oil lightweight combination process |
-
2017
- 2017-04-13 CN CN201710240112.8A patent/CN106905997B/en active Active
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102453547A (en) * | 2010-10-15 | 2012-05-16 | 中国石油化工股份有限公司 | Heavy oil lightweight combination process |
Also Published As
Publication number | Publication date |
---|---|
CN106905997A (en) | 2017-06-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN1307290C (en) | Hydro processing of hydrocarbon using a mixture of catalysts | |
CN103773429A (en) | Residual oil hydrotreating method | |
CN104383922B (en) | A kind of heavy-oil hydrogenation ferrum-based catalyst and application thereof | |
CN106179414B (en) | A kind of sulfurized hydrogenation catalyst for refining and preparation method thereof | |
CN109894155A (en) | It is a kind of for the catalyst carrier of residual hydrocracking, catalyst and its preparation method | |
CN103769179A (en) | Preparation method of residual oil hydro-treatment catalyst | |
CN105749922A (en) | Preparation method of heavy oil hydrotreating catalyst and heavy oil hydrotreating catalyst prepared by preparation method and use of heavy oil hydrotreating catalyst | |
CN106905997B (en) | Catalyst used in series connection type boiling bed hydrogenation treatment process of inferior heavy oil | |
CN111100680A (en) | Catalyst grading method and residual oil hydrotreating method | |
WO2023232122A1 (en) | Hydrodesulfurization catalyst for heavy oil, and preparation method therefor | |
JPS5998736A (en) | Preparation of hydrotreating catalyst of hydrocarbon oil | |
US10676680B2 (en) | Catalyst for the hydrotreatment of a heavy hydrocarbon feedstock | |
CN106622308B (en) | Hydrobon catalyst and its preparation method and application | |
TW201807177A (en) | An ebullated bed process for high conversion of heavy hydrocarbons with a low sediment yield | |
JPH06200261A (en) | Hydroconversion and catalyst used for it | |
CN103100391A (en) | Preparation method of eggshell hydrogenation catalyst | |
CN106179388B (en) | A kind of preparation method of hydrotreating catalyst | |
CN101260319B (en) | Vulcanization method for hydrogenation catalyst | |
CN106807420A (en) | A kind of catalyst and preparation method for petroleum naphtha hydrogenation dearsenification | |
CN111100676A (en) | Catalyst grading method and application thereof in residual oil hydrotreating method | |
CN111375419A (en) | Hydrogenation catalyst and preparation method thereof | |
CN107282073A (en) | Catalyst, preparation method and the composite catalyst of catalytic hydroprocessing thermal cracking | |
CN109897664A (en) | A kind of hydrotreating method of acid-containing raw oil | |
CN106622268A (en) | Slurry reactor hydrogenation catalyst and preparation method thereof | |
CN110180585A (en) | A kind of gasoline hydrogenation treatment catalyst and preparation method thereof |
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 | ||
CB03 | Change of inventor or designer information |
Inventor after: Wan Feng Inventor before: Wan Huiyi Inventor before: Wan Chao Inventor before: Wan Xuebing |
|
CB03 | Change of inventor or designer information | ||
TA01 | Transfer of patent application right |
Effective date of registration: 20170926 Address after: Linzi District Street Jixia Huai Xing Cun 255400 Shandong city of Zibo Province Applicant after: Zibo Taiguang Chemical Co., Ltd. Address before: 255400 No. 6 Wang Zhu Road, Linzi District, Shandong, Zibo Applicant before: Zibo Taitong Catalytic Technology Co., Ltd. |
|
TA01 | Transfer of patent application right | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20220513 Address after: 266100 room 1015, building 49, No. 101, Shenzhen road, Laoshan District, Qingdao, Shandong Province Patentee after: QINGDAO HUIYIMING CATALYSIS NEW MATERIAL TECHNOLOGY Co.,Ltd. Address before: 255400 huaihang village, Jixia street, Linzi District, Zibo City, Shandong Province Patentee before: Zibo Taiguang Chemical Co.,Ltd. |
|
TR01 | Transfer of patent right |