KR970704518A - 저매크로기공 잔유 전화촉매(low macropore resid conversion catalyst) - Google Patents
저매크로기공 잔유 전화촉매(low macropore resid conversion catalyst) Download PDFInfo
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- KR970704518A KR970704518A KR1019970700531A KR19970700531A KR970704518A KR 970704518 A KR970704518 A KR 970704518A KR 1019970700531 A KR1019970700531 A KR 1019970700531A KR 19970700531 A KR19970700531 A KR 19970700531A KR 970704518 A KR970704518 A KR 970704518A
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- pore diameter
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- alumina support
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- 239000003054 catalyst Substances 0.000 title claims abstract 19
- 238000006243 chemical reaction Methods 0.000 title 1
- 239000011148 porous material Substances 0.000 claims abstract 52
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract 16
- 229910052751 metal Inorganic materials 0.000 claims abstract 6
- 239000002184 metal Substances 0.000 claims abstract 6
- 150000002739 metals Chemical class 0.000 claims abstract 4
- 238000000034 method Methods 0.000 claims abstract 4
- 239000000295 fuel oil Substances 0.000 claims abstract 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims 4
- 239000007787 solid Substances 0.000 claims 4
- 150000003568 thioethers Chemical class 0.000 claims 4
- 239000002253 acid Substances 0.000 claims 3
- 229910021472 group 8 element Inorganic materials 0.000 claims 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims 2
- 239000007864 aqueous solution Substances 0.000 claims 2
- 229910017052 cobalt Inorganic materials 0.000 claims 2
- 239000010941 cobalt Substances 0.000 claims 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims 2
- 229910052750 molybdenum Inorganic materials 0.000 claims 2
- 239000011733 molybdenum Substances 0.000 claims 2
- 229910052759 nickel Inorganic materials 0.000 claims 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims 1
- 230000002378 acidificating effect Effects 0.000 claims 1
- 238000006477 desulfuration reaction Methods 0.000 claims 1
- 230000023556 desulfurization Effects 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 claims 1
- 230000003472 neutralizing effect Effects 0.000 claims 1
- 150000002815 nickel Chemical class 0.000 claims 1
- 229910017604 nitric acid Inorganic materials 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 150000002902 organometallic compounds Chemical class 0.000 claims 1
- 238000007493 shaping process Methods 0.000 claims 1
- 239000000243 solution Substances 0.000 claims 1
- 150000002736 metal compounds Chemical class 0.000 abstract 1
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- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
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- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- 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
-
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- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J35/00—Catalysts, in general, characterised by their form or physical properties
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- B01J35/64—Pore diameter
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- 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
- B01J35/651—50-500 nm
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
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- 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
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- B01J35/635—0.5-1.0 ml/g
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- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J35/67—Pore distribution monomodal
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- Thermal Sciences (AREA)
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
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Abstract
금속을 함유하는 중유 공급원료의 수소첨가탈황법을 위한 촉매의 제법 및 촉매의 사용법 및 개선된 수명 및 금속 용량을 갖는 촉매에 관한 것이다. 촉매는 기공부피의 70부피%가 기공직경이 140A 내지 220A인 알루미나를 포함하는 지지체상에 ⅥB족 및 Ⅷ족 금속 또는 금속화합물을 포함한다.
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
Claims (19)
- 입자밀도가 1.0g/㎠이고 기공부피가 0.5 내지 1.1㎠/g의 범위에 있는 것을 포함하며, 여기서 적어도 기공 부피의 약 70%는 기공직경이 140 내지 220A 범위이고, 기공부피의 5% 이하는 기공직경이 약 500A 이상이고 기공부피의 2% 이하는 기공직경이 약 1000A 이상이며 알루미나 지지체의 기공이 170A 이상의 피크 가공 직경을 갖는 수소첨가탈황촉매에 관한 알루미나 지지체.
- 제1항에 있어서, 적어도 약 기공부피의 45%는 기공직경이 170 내지 220A 범위이고, 알루미나 지지체의 기공이 170 내지 220A 범위의 파크 기공 직경을 갖는 알루미나 지지체.
- 제1항에 있어서, 적어도 약 기공부피의 25%는 기공직경이 180 내지 220A 범위의 직경이고, 알루미나 지지체의 기공이 180 내지 220A 범위의 파크 가공 직경을 갖는 알루미나 지지체.
- 제1항에 있어서, 기공부피의 약 20% 이하는 기공직경이 70 내지 130A 범위인 알루미나 지지체.
- 제1항에 있어서, 기공부피의 약65% 이하는 기공직경이 110 내지 190A 범위인 알루미나 지지체.
- 제1항에 있어서, 기공부피의 약 2%이하는 기공직경이 500A 이상이고, 기공부피의 약 1% 이하는 기공직경이 1000A 이상인 알루미나 지지체.
- 제6항에 있어서, 기공부피의 약 1% 이하는 기공직경이 500A 이상이고, 기공부피의 약 0.5% 이하는 기공직경이 1000A 이상인 알루미나 지지체.
- 제3항에 있어서, 기공부피의 2% 이하는 기공직경이 500A 이상이고, 기공부피의 약 0.5% 이하는 기공직경이 1000A 이상인 알루미나 지지체.
- 제7항에 있어서, 기공부피의 2% 이하는 기공직경이 300A 이상인 알루미나 지지체.
- 제8항에 있어서, 기공부피의 2% 이하는 기공직경이 300A 이상인 알루미나 지지체.
- 제1항의 알루미나 지지체, ⅥB족 원소의 금속, 산화물 및 황화물로부터 선택된 ⅥB족 성분 및 Ⅷ족 원소의 금속, 산화물 및 황화물로부터 선택된 Ⅷ족 성분을 포함하는 중유의 수소첨가탈황 촉매.
- 제11항에 있어서, 촉매 기공 부피의 적어도 약 70%는 기공직경이 140 내지 220A 이고, 촉매 기공 부피의 5% 이하는 기공직경이 500A 이상이고, 촉매 기공 부피의 2% 이하는 기공직경이 1000A 이상이고, 촉매 기공이 170A 피크 기공 직경을 갖는 촉매.
- 제12항에 있어서, 촉매 기공 부피의 적어도 약 45%는 기공직경이 170 내지 220A이고, 촉매의 기공이 170 내지 220A의 피크 기공 직경을 갖는 촉매.
- 제11항에 있어서, 코발트, 니켈 및 몰리브덴의 금속, 산화물 및 황화물로부터 선택된 ⅥB족 성분 및 Ⅷ족 성분을 갖는 촉매.
- 제14항에 있어서, 약 2% 내지 약 4% 니켈 및 약 7% 내지 약 9% 몰리브덴을 함유하는 촉매.
- 제15항에 있어서, 알루미나 지지체를 코발트 또는 니켈 염 및 헤테로폴리몰리브덴산의 용액과 함침시켜 제조되는 촉매.
- 5분 이하의 질산 겔화 값을 갖는 알파-알루미나 일수화물을 포함하는 고체를 약 pH3.0 내지 3.5까지의 산성 수용액에 혼합시켜 처리하고; 산 1당량당 약 0.9내지 1.1 당량 범위의 염기를 함유하는 질소 염기 수용액에 처리된 고체에 적어도 일부의 부가된 산을 부가시켜 중화시키고; 중화되었거나 부분적으로 중화된 고체를 성형화하고 건조시키며; 적어도 1600℉(871℃)의 온도에서 성형화된 고체를 하소시키는 것을 특징으로 하는 방법을 사용하여 제조된 제1항의 알루미나 지지체.
- 수소첨가탈황조건 및 수소기체의 존재하의 중유를 제11항의 촉매와 접촉시켜 이루어진 유기금속 화합물을 포함하는 중유의 수소첨가탈황법.
- 제18항에 있어서, 촉매 기공 부피의 약 45%가 기공직경이 170 내지 220A이고, 기공부피의 약 1%이하가 기공직경이 500A 이상이고, 기공부피의 약 0.5% 이하가 약 기공직경이 1000A 이상이고,촉매의 기공이 170내지 220A의 피크 기공 직경을 갖는 방법.※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US28267394A | 1994-07-29 | 1994-07-29 | |
US08/282,673 | 1994-07-29 | ||
US08/477,440 | 1995-06-07 | ||
US08/477,440 US5817454A (en) | 1995-06-07 | 1995-06-07 | Portable apparatus and method for detection of methylxanthine chemical species |
PCT/US1995/008828 WO1996004073A1 (en) | 1994-07-29 | 1995-07-14 | Low macropore resid conversion catalyst |
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Publication Number | Publication Date |
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KR970704518A true KR970704518A (ko) | 1997-09-06 |
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Application Number | Title | Priority Date | Filing Date |
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KR1019970700531A KR970704518A (ko) | 1994-07-29 | 1995-07-14 | 저매크로기공 잔유 전화촉매(low macropore resid conversion catalyst) |
Country Status (12)
Country | Link |
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EP (1) | EP0804288B1 (ko) |
JP (1) | JP3838660B2 (ko) |
KR (1) | KR970704518A (ko) |
CN (1) | CN1078822C (ko) |
AT (1) | ATE269159T1 (ko) |
AU (1) | AU3098095A (ko) |
CA (1) | CA2194974A1 (ko) |
CZ (1) | CZ4497A3 (ko) |
DE (1) | DE69533173D1 (ko) |
FI (1) | FI970356A0 (ko) |
SK (1) | SK10797A3 (ko) |
WO (1) | WO1996004073A1 (ko) |
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CN100415374C (zh) * | 2005-03-11 | 2008-09-03 | 石油大学(北京) | 大孔加氢催化剂及其制备方法 |
CN101152631B (zh) * | 2006-09-29 | 2011-04-20 | 中国石油化工股份有限公司 | 一种选择性加氢脱硫催化剂及其制备方法 |
CN104646072B (zh) * | 2013-11-20 | 2017-06-20 | 中国石油化工股份有限公司 | 一种加氢处理催化剂载体的制备方法 |
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FR3022157B1 (fr) * | 2014-06-13 | 2017-09-01 | Ifp Energies Now | Catalyseur bimodal a phase active comalaxee, son procede de preparation et son utilisation en hydrotraitement de residus |
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GB1584706A (en) * | 1977-06-21 | 1981-02-18 | Exxon Research Engineering Co | Hydrotreating catalyst and process utilizing the same |
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US5215955A (en) * | 1991-10-02 | 1993-06-01 | Chevron Research And Technology Company | Resid catalyst with high metals capacity |
US5223472A (en) * | 1992-04-14 | 1993-06-29 | Union Oil Company Of California | Demetallation catalyst |
-
1995
- 1995-07-14 DE DE69533173T patent/DE69533173D1/de not_active Expired - Fee Related
- 1995-07-14 WO PCT/US1995/008828 patent/WO1996004073A1/en active IP Right Grant
- 1995-07-14 CA CA002194974A patent/CA2194974A1/en not_active Abandoned
- 1995-07-14 EP EP95926685A patent/EP0804288B1/en not_active Expired - Lifetime
- 1995-07-14 CN CN95194329A patent/CN1078822C/zh not_active Expired - Fee Related
- 1995-07-14 KR KR1019970700531A patent/KR970704518A/ko not_active Application Discontinuation
- 1995-07-14 AU AU30980/95A patent/AU3098095A/en not_active Abandoned
- 1995-07-14 CZ CZ9744A patent/CZ4497A3/cs unknown
- 1995-07-14 AT AT95926685T patent/ATE269159T1/de not_active IP Right Cessation
- 1995-07-14 JP JP50652796A patent/JP3838660B2/ja not_active Expired - Fee Related
- 1995-07-14 SK SK107-97A patent/SK10797A3/sk unknown
-
1997
- 1997-01-28 FI FI970356A patent/FI970356A0/fi unknown
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ATE269159T1 (de) | 2004-07-15 |
DE69533173D1 (de) | 2004-07-22 |
JP2001520567A (ja) | 2001-10-30 |
WO1996004073A1 (en) | 1996-02-15 |
JP3838660B2 (ja) | 2006-10-25 |
CN1154668A (zh) | 1997-07-16 |
SK10797A3 (en) | 1997-07-09 |
FI970356A (fi) | 1997-01-28 |
CZ4497A3 (en) | 1997-11-12 |
EP0804288A1 (en) | 1997-11-05 |
CA2194974A1 (en) | 1996-02-15 |
AU3098095A (en) | 1996-03-04 |
EP0804288B1 (en) | 2004-06-16 |
CN1078822C (zh) | 2002-02-06 |
FI970356A0 (fi) | 1997-01-28 |
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