KR20010014690A - 카보닐 및 질소를 갖는 유기 화합물로 이루어진수소화처리 촉매의 황화방법 - Google Patents
카보닐 및 질소를 갖는 유기 화합물로 이루어진수소화처리 촉매의 황화방법 Download PDFInfo
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- B01J31/1805—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing nitrogen
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/20—Sulfiding
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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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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J31/2208—Oxygen, e.g. acetylacetonates
- B01J31/2226—Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
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- 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
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- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S502/00—Catalyst, solid sorbent, or support therefor: product or process of making
- Y10S502/506—Method of making inorganic composition utilizing organic compound, except formic, acetic, or oxalic acid or salt thereof
- Y10S502/509—Nitrogen containing organic compound
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- Y10S502/506—Method of making inorganic composition utilizing organic compound, except formic, acetic, or oxalic acid or salt thereof
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- 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
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Abstract
Description
공급물 | 진공 기체 오일 |
질소(ASTM D-4629)(ppmwt) | 1271 |
황(ASTM D-4294)(wt.%) | 1.29 |
밀도 15℃(g/ml) | 0.9217 |
Dist.(℃)(ASTM D 1160) | |
IBP | 259 |
5vol.% | 326 |
10vol.% | 358 |
30vol.% | 415 |
50vol.% | 450 |
70vol.% | 485 |
90vol.% | 536 |
95vol.% | 559 |
FBP | 587 |
온도(℃) | 360 |
압력(bar) | 70 |
H2/오일(Nl/l) | 400 |
LHSV(h-1) | 1.2 |
촉매 1 | 촉매 2 | 대조촉매 1 | |
RVA HDN | 103 | 118 | 100 |
Claims (12)
- 수소화처리 촉매는 트리옥시드로 계산하여 22wt.%의 몰리브덴, 옥시드로 계산하여 4wt.%의 코발트, P2O5로 계산하여 3wt.%의 인과 6족 및 8족 금속의 전체 몰량의 0.6배의 EDTA를 갖는 알루미나 수화물 담체로 이루어진 촉매가 아니라는 조건하에서, 수소화처리 촉매가 황화단계를 거치고, 수소화처리 촉매는 적어도 50wt.%의 알루미나를 갖는 담체로 이루어지고, 상기 촉매는 적어도 하나의 수소화 금속 성분과 적어도 하나의 공유결합된 질소원자 및 적어도 하나의 카보닐성분을 갖는 유기 화합물로 이루어지며, 유기 화합물과 전체 수소화 금속 함량사이의 몰비는 적어도 0.01:1인 것을 특징으로 하는 황화 수소화처리 촉매의 제조방법.
- 제 1 항에 있어서,상기 유기 화합물은 적어도 두개의 질소원자 및 적어도 두개의 카보닐 성분으로 이루어진 것을 특징으로 하는 제조방법.
- 제 1 항 또는 제 2 항에 있어서,적어도 하나의 카보닐 성분이 카복실기내에 존재하는 것을 특징으로 하는 제조방법.
- 제 1 항 내지 제 3 항 중 어느 한 항에 있어서,적어도 하나의 질소원자가 적어도 두개의 탄소원자와 공유결합하는 것을 특징으로 하는 제조방법.
- 제 1 항 내지 제 4 항 중 어느 한 항에 있어서,상기 유기 화합물은 하기 화학식 1의 화합물인 것을 특징으로 하는 제조방법.(화학식 1)(R1R2)N-R3-N(R1'R2')(상기 화학식 1에서, R1, R2, R1' 및 R2'는 카보닐, 카복시, 에스테르, 에테르, 아미노 또는 아미도에서 선택된 하나 또는 그 이상의 기로 선택적으로 치환된 10개 미만의 탄소원자를 갖는 알킬, 알케닐 및 알릴에서 각각 선택되고, R3은 -O- 또는 -NR4-가 끼여있는 10개미만의 탄소원자를 갖는 알킬렌기이고, R4는 상기에 R1에서 기술된 것과 같은 기에서 선택되며, R3 알킬렌기는 카보닐, 카르복실, 에스테르, 에테르, 아미노 또는 아미도에서 선택된 하나 이상의 기로 치환될 수 있고, 단 화학식 1의 유기 화합물은 적어도 하나의 카보닐 성분으로 이루어진다)
- 제 5 항에 있어서,상기 R1, R2, R1' 및 R2'중 적어도 두개는 -R5-COOX이고, 여기서, R5는 1-4개의 탄소원자를 갖는 알킬렌기이고, X는 수소 또는 다른 양이온이며, X가 다가 양이온이라면, 하나의 X는 둘 또는 그 이상의 -R5-COO기에 부착될 수 있는 것을 특징으로 하는 제조방법.
- 제 1 항 내지 제 6 항 중 어느 한 항에 있어서,상기 황화가 엑스-시추(ex-situ)에서 실시되는 것을 특징으로 하는 제조방법.
- 제 1 항 내지 제 7 항 중 어느 한 항에 있어서,상기 황화가 선택적 스파이크 탄화수소 공급물로 인-시추(in-situ)에서 실시되는 것을 특징으로 하는 제조방법.
- 제 1 항 내지 제 8 항 중 어느 한 항에 있어서,1. 적어도 하나의 수소화 금속 성분과 적어도 50wt%의 알루미나로 이루어진 촉매 담체를 혼합하고,2. 상기 수소화 금속 성분과의 혼합 전에, 동시에 또는 이어서 유기 화합물과 촉매 담체를 혼합하고,3. 충분히 낮은 온도에서 수소화 금속 성분 및 유기 화합물로 이루어진 담체를 선택적으로 건조시켜서, 전체 수소화 금속 함량에 대한 유기 화합물의 몰비를 적어도 0.01:1로 유지시키는 단계로 상기 수소화처리 촉매를 제조하는 것을 특징으로 하는 제조방법.
- 제 1 항 내지 제 9 항 중 어느 한 항에 있어서,상기 알루미나가 전이 알루미나로 이루어진 것을 특징으로 하는 제조방법.
- 탄화수소 공급물이 수소화처리 조건하에서 제 1 항 내지 제 10 항 중 어느 한 항의 제조방법에 의해 수득된 촉매와 접촉하는 것을 특징으로 하는 탄화수소 공급물의 수소화처리방법.
- 제 11 항에 있어서,상기 탄화수소 공급물은 S로 계산하여 적어도 0.2wt.%의 황을 함유하는 것을 특징으로 하는 방법.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12825699P | 1999-04-08 | 1999-04-08 | |
EP99201051 | 1999-04-08 | ||
US60/128,256 | 1999-04-08 | ||
EP99201051.2 | 1999-04-08 |
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Publication Number | Publication Date |
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KR20010014690A true KR20010014690A (ko) | 2001-02-26 |
KR100653505B1 KR100653505B1 (ko) | 2006-12-04 |
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Application Number | Title | Priority Date | Filing Date |
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KR1020000017830A KR100653505B1 (ko) | 1999-04-08 | 2000-04-06 | 카르보닐 및 질소를 포함하는 유기 화합물을 포함하는 수소화처리 촉매의 황화 방법 |
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US (1) | US6540908B1 (ko) |
EP (1) | EP1043069B1 (ko) |
JP (1) | JP4187383B2 (ko) |
KR (1) | KR100653505B1 (ko) |
AT (1) | ATE296163T1 (ko) |
DE (1) | DE60020292T2 (ko) |
SG (1) | SG83201A1 (ko) |
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US6923904B1 (en) * | 1999-04-02 | 2005-08-02 | Akso Nobel N.V. | Process for effecting ultra-deep HDS of hydrocarbon feedstocks |
ES2244457T3 (es) | 1999-07-05 | 2005-12-16 | Albemarle Netherlands B.V. | Procedimiento para regenerar catalizadores que contienen aditivos. |
US6872678B2 (en) * | 2000-04-11 | 2005-03-29 | Akzo Nobel N.V. | Process for activating a catalyst containing an S-containing additive |
DE60144149D1 (de) * | 2000-07-12 | 2011-04-14 | Albemarle Netherlands Bv | Ein auf einem brennbaren bindemittel basierender mischmetallkatalysator |
FR2841798B1 (fr) * | 2002-07-03 | 2005-03-04 | Inst Francais Du Petrole | Catalyseur d'hydrotraitement contenant un compose organique azote et son utilisation |
JP2004344754A (ja) * | 2003-05-21 | 2004-12-09 | National Institute Of Advanced Industrial & Technology | 炭化水素の水素化処理触媒組成物の製造方法 |
JP2005000873A (ja) * | 2003-06-13 | 2005-01-06 | Catalysts & Chem Ind Co Ltd | 炭化水素の水素化処理触媒組成物の製造方法 |
JP4370124B2 (ja) * | 2003-06-27 | 2009-11-25 | 日揮触媒化成株式会社 | 水素化処理触媒組成物 |
EP1660232B1 (fr) * | 2003-08-08 | 2009-07-22 | Total Raffinage Marketing | Catalyseur d'hydrotraitement et/ou d'hydrocraquage d'hydrocarbures et sa preparation |
WO2005070542A1 (en) | 2004-01-20 | 2005-08-04 | Shell Internationale Research Maatschappij B.V. | A method of restoring catalytic activity of a spent hydrotreating catalyst, the resulting restored catalyst, and a method of hydroprocessing |
DK1718408T3 (en) * | 2004-01-20 | 2016-09-19 | Shell Int Research | PROCEDURE FOR THE RECOVERY OF CATALYTIC ACTIVITY FOR A USED HYDROGEN TREATMENT CATALYST |
JP4444690B2 (ja) * | 2004-02-26 | 2010-03-31 | 株式会社ジャパンエナジー | 水素化処理触媒前駆体およびその製造方法並びに精製炭化水素油の製造方法 |
JP4472556B2 (ja) * | 2004-03-26 | 2010-06-02 | コスモ石油株式会社 | 炭化水素油の水素化処理触媒及びその製造方法並びに炭化水素油の水素化処理方法 |
US10941353B2 (en) | 2004-04-28 | 2021-03-09 | Hydrocarbon Technology & Innovation, Llc | Methods and mixing systems for introducing catalyst precursor into heavy oil feedstock |
CA2564346C (en) | 2004-04-28 | 2016-03-22 | Headwaters Heavy Oil, Llc | Ebullated bed hydroprocessing methods and systems and methods of upgrading an existing ebullated bed system |
FR2880823B1 (fr) * | 2005-01-20 | 2008-02-22 | Total France Sa | Catalyseur d'hydrotraitement, son procede de preparation et et son utilisation |
US7670984B2 (en) | 2006-01-06 | 2010-03-02 | Headwaters Technology Innovation, Llc | Hydrocarbon-soluble molybdenum catalyst precursors and methods for making same |
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- 2000-03-23 EP EP00201039A patent/EP1043069B1/en not_active Revoked
- 2000-03-30 SG SG200001772A patent/SG83201A1/en unknown
- 2000-03-31 US US09/540,402 patent/US6540908B1/en not_active Expired - Lifetime
- 2000-04-06 KR KR1020000017830A patent/KR100653505B1/ko active IP Right Grant
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JP2000325797A (ja) | 2000-11-28 |
EP1043069B1 (en) | 2005-05-25 |
SG83201A1 (en) | 2001-09-18 |
EP1043069A1 (en) | 2000-10-11 |
JP4187383B2 (ja) | 2008-11-26 |
KR100653505B1 (ko) | 2006-12-04 |
DE60020292D1 (de) | 2005-06-30 |
ATE296163T1 (de) | 2005-06-15 |
US6540908B1 (en) | 2003-04-01 |
DE60020292T2 (de) | 2006-05-04 |
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