GB1410924A - Hydrocarbon conversion process - Google Patents
Hydrocarbon conversion processInfo
- Publication number
- GB1410924A GB1410924A GB5954771A GB5954771A GB1410924A GB 1410924 A GB1410924 A GB 1410924A GB 5954771 A GB5954771 A GB 5954771A GB 5954771 A GB5954771 A GB 5954771A GB 1410924 A GB1410924 A GB 1410924A
- Authority
- GB
- United Kingdom
- Prior art keywords
- hydrodesulphurization
- bar
- catalyst
- catalytic
- dec
- 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.)
- Expired
Links
- 239000004215 Carbon black (E152) Substances 0.000 title 1
- 238000006243 chemical reaction Methods 0.000 title 1
- 229930195733 hydrocarbon Natural products 0.000 title 1
- 150000002430 hydrocarbons Chemical class 0.000 title 1
- 238000000034 method Methods 0.000 title 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 abstract 5
- 239000003921 oil Substances 0.000 abstract 4
- 239000011148 porous material Substances 0.000 abstract 4
- 239000003054 catalyst Substances 0.000 abstract 3
- 239000002245 particle Substances 0.000 abstract 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 2
- 230000003197 catalytic effect Effects 0.000 abstract 2
- 229910052739 hydrogen Inorganic materials 0.000 abstract 2
- 239000001257 hydrogen Substances 0.000 abstract 2
- 229910052759 nickel Inorganic materials 0.000 abstract 2
- 229910052720 vanadium Inorganic materials 0.000 abstract 2
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 abstract 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 abstract 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
- C10G45/14—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
-
- 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
-
- 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
-
- 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
- B01J35/64—Pore diameter
- B01J35/643—Pore diameter less than 2 nm
-
- 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
-
- 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
- B01J35/66—Pore distribution
- B01J35/67—Pore distribution monomodal
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
1410924 Catalytic hydrodesulphurization of residual oils SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ BV 20 Dec 1972 [22 Dec 1971 (2)] 59547/71 and 59548/71 Heading C5E The catalytic hydrodesulphurization with catalyst replenishment of residual oils is carried out using a catalyst having a pore volume above 0À30 ml./g. and which is in the form either of particles less than 10% of the pore volume of which is present in pores of diameter above 100 nm., said particles having a specific average pore diameter (p, measured in nm.) and specific average particle diameter (d, measured in mm.) that: (a) if the oil has a total vanadium plus nickel content of at most 120 p.p.m. wt. then 0À025 Î P H2 # p/(d)<SP>0À6</SP> # 0À1ÎP H2 -5À0, the hydrogen partial pressure P H2 being at least 70 bar; or (b) if the oil has a total vanadium plus nickel content above 120 p.p.m. then 4À5 > p/(d)<SP>0À6</SP> > 14À0 and the hydrogen partial pressure P H2 being at least 50 bar. The hydrodesulphurization can be carried out at 300-475 C. and 50-200 bar using a catalyst containing Ni and/or Co together with Mo and/or W on a support such as alumina or silica-alumina. The hydrodesulphurization can be preceded by a demetallization by catalytic hydrogenation.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB5954771A GB1410924A (en) | 1971-12-22 | 1971-12-22 | Hydrocarbon conversion process |
CA155,291A CA981615A (en) | 1971-12-22 | 1972-10-31 | Hydrocarbon conversion process |
NL7216877A NL7216877A (en) | 1971-12-22 | 1972-12-13 | |
FR7245433A FR2164741B1 (en) | 1971-12-22 | 1972-12-20 | |
DE2262410A DE2262410A1 (en) | 1971-12-22 | 1972-12-20 | METHOD FOR CATALYTIC HYDRATING DESULFURIZATION WITH CATALYST FILLING |
JP12733672A JPS5628956B2 (en) | 1971-12-22 | 1972-12-20 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB5954771A GB1410924A (en) | 1971-12-22 | 1971-12-22 | Hydrocarbon conversion process |
GB5954871 | 1971-12-22 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1410924A true GB1410924A (en) | 1975-10-22 |
Family
ID=26267794
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5954771A Expired GB1410924A (en) | 1971-12-22 | 1971-12-22 | Hydrocarbon conversion process |
Country Status (6)
Country | Link |
---|---|
JP (1) | JPS5628956B2 (en) |
CA (1) | CA981615A (en) |
DE (1) | DE2262410A1 (en) |
FR (1) | FR2164741B1 (en) |
GB (1) | GB1410924A (en) |
NL (1) | NL7216877A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA1217756A (en) * | 1983-08-10 | 1987-02-10 | Hri, Inc. | Demetallization catalyst and process for metals- containing hydrocarbon feedstocks |
JPS6078746U (en) * | 1983-11-04 | 1985-06-01 | 日本クラウンコルク株式会社 | Cap device for liquid containers |
-
1971
- 1971-12-22 GB GB5954771A patent/GB1410924A/en not_active Expired
-
1972
- 1972-10-31 CA CA155,291A patent/CA981615A/en not_active Expired
- 1972-12-13 NL NL7216877A patent/NL7216877A/xx not_active Application Discontinuation
- 1972-12-20 FR FR7245433A patent/FR2164741B1/fr not_active Expired
- 1972-12-20 DE DE2262410A patent/DE2262410A1/en not_active Withdrawn
- 1972-12-20 JP JP12733672A patent/JPS5628956B2/ja not_active Expired
Also Published As
Publication number | Publication date |
---|---|
FR2164741B1 (en) | 1975-11-07 |
NL7216877A (en) | 1973-06-26 |
CA981615A (en) | 1976-01-13 |
JPS4870705A (en) | 1973-09-25 |
JPS5628956B2 (en) | 1981-07-04 |
FR2164741A1 (en) | 1973-08-03 |
DE2262410A1 (en) | 1973-06-28 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PCNP | Patent ceased through non-payment of renewal fee |