CA2295917C - Procede de reduction de l'indice d'acidite total du petrole brut - Google Patents
Procede de reduction de l'indice d'acidite total du petrole brut Download PDFInfo
- Publication number
- CA2295917C CA2295917C CA002295917A CA2295917A CA2295917C CA 2295917 C CA2295917 C CA 2295917C CA 002295917 A CA002295917 A CA 002295917A CA 2295917 A CA2295917 A CA 2295917A CA 2295917 C CA2295917 C CA 2295917C
- Authority
- CA
- Canada
- Prior art keywords
- oil
- petroleum feed
- metal
- water
- petroleum
- 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 - Lifetime
Links
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
-
- 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
- C10G45/16—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 suspended in the oil, e.g. slurries
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
La présente invention concerne un procédé de réduction de la quantité d'acides carboxyliques dans les alimentations en pétrole consistant à (a) ajouter d'abord à cette alimentation un agent catalytique renfermant un composé d'un métal pouvant se dissoudre ou se disperser dans le pétrole, ce composé étant sélectionné dans le groupe constitué par les métaux des groupes VB, VIB, VIIB et VIII, et la quantité de métal dans l'alimentation précitée étant d'au moins 5 wppm; puis,(b) chauffer l'alimentation avec ledit agent catalytique dans un réacteur à une température d'environ 400 à environ 800 DEG F (environ 204,44 à environ 426,67 DEG C), sous une pression d'hydrogène de 15 psig à 1000 psig (204,75 à 6996,33 kPa); et enfin, (c) balayer le réacteur contenant l'alimentation et l'agent catalytique avec un gaz renfermant de l'hydrogène à une vitesse suffisante pour maintenir la pression partielle de l'eau de constitution et du dioxyde de carbone en dessous de 50 psia (environ 344,75 kPa)
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US92044797A | 1997-08-29 | 1997-08-29 | |
| US08/920,447 | 1997-08-29 | ||
| US09/072,764 US5914030A (en) | 1997-08-29 | 1998-05-05 | Process for reducing total acid number of crude oil |
| US09/072,764 | 1998-05-05 | ||
| PCT/US1998/018041 WO1999010453A1 (fr) | 1997-08-29 | 1998-08-28 | Procede de reduction de l'indice d'acidite total du petrole brut |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2295917A1 CA2295917A1 (fr) | 1999-03-04 |
| CA2295917C true CA2295917C (fr) | 2005-06-07 |
Family
ID=26753711
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002295917A Expired - Lifetime CA2295917C (fr) | 1997-08-29 | 1998-08-28 | Procede de reduction de l'indice d'acidite total du petrole brut |
Country Status (12)
| Country | Link |
|---|---|
| EP (1) | EP1062302B1 (fr) |
| JP (1) | JP4283988B2 (fr) |
| CN (1) | CN1105769C (fr) |
| AU (1) | AU733884B2 (fr) |
| BR (1) | BR9811387A (fr) |
| CA (1) | CA2295917C (fr) |
| DE (1) | DE69804026T2 (fr) |
| DK (1) | DK1062302T3 (fr) |
| ID (1) | ID24702A (fr) |
| NO (1) | NO20000948D0 (fr) |
| RU (1) | RU2184762C2 (fr) |
| WO (1) | WO1999010453A1 (fr) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1922290B (zh) * | 2003-12-19 | 2010-06-16 | 国际壳牌研究有限公司 | 生产原油产品的系统和方法 |
| NL1027750C2 (nl) * | 2003-12-19 | 2006-07-13 | Shell Int Research | Systemen, methoden en katalysatoren voor het produceren van een ruwe-oliehoudend product. |
| KR101898289B1 (ko) * | 2011-01-10 | 2018-09-13 | 에스케이이노베이션 주식회사 | 탄화수소류 유분 내의 유기산을 저감하는 방법 |
| US10195588B1 (en) * | 2017-11-28 | 2019-02-05 | Uop Llc | Process for making and using iron and molybdenum catalyst for slurry hydrocracking |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2921023A (en) * | 1957-05-14 | 1960-01-12 | Pure Oil Co | Removal of naphthenic acids by hydrogenation with a molybdenum oxidesilica alumina catalyst |
| NO303837B1 (no) * | 1994-08-29 | 1998-09-07 | Norske Stats Oljeselskap | FremgangsmÕte for Õ fjerne hovedsakelig naftensyrer fra en hydrokarbonolje |
| DK0809683T3 (da) * | 1995-02-17 | 2002-03-04 | Exxonmobil Res & Eng Co | Termisk dekomponering af naphtensyrer |
-
1998
- 1998-08-28 DK DK98942321T patent/DK1062302T3/da active
- 1998-08-28 CN CN98808614A patent/CN1105769C/zh not_active Expired - Fee Related
- 1998-08-28 DE DE69804026T patent/DE69804026T2/de not_active Expired - Lifetime
- 1998-08-28 ID IDW20000596A patent/ID24702A/id unknown
- 1998-08-28 WO PCT/US1998/018041 patent/WO1999010453A1/fr not_active Ceased
- 1998-08-28 CA CA002295917A patent/CA2295917C/fr not_active Expired - Lifetime
- 1998-08-28 BR BR9811387-9A patent/BR9811387A/pt not_active IP Right Cessation
- 1998-08-28 RU RU2000104874A patent/RU2184762C2/ru active
- 1998-08-28 EP EP98942321A patent/EP1062302B1/fr not_active Expired - Lifetime
- 1998-08-28 AU AU90404/98A patent/AU733884B2/en not_active Ceased
- 1998-08-28 JP JP2000507762A patent/JP4283988B2/ja not_active Expired - Fee Related
-
2000
- 2000-02-25 NO NO20000948A patent/NO20000948D0/no not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| DE69804026D1 (de) | 2002-04-04 |
| CN1268968A (zh) | 2000-10-04 |
| NO20000948L (no) | 2000-02-25 |
| AU733884B2 (en) | 2001-05-31 |
| RU2184762C2 (ru) | 2002-07-10 |
| JP2001514300A (ja) | 2001-09-11 |
| EP1062302A1 (fr) | 2000-12-27 |
| WO1999010453A1 (fr) | 1999-03-04 |
| NO20000948D0 (no) | 2000-02-25 |
| ID24702A (id) | 2000-08-03 |
| CA2295917A1 (fr) | 1999-03-04 |
| BR9811387A (pt) | 2000-08-29 |
| CN1105769C (zh) | 2003-04-16 |
| AU9040498A (en) | 1999-03-16 |
| JP4283988B2 (ja) | 2009-06-24 |
| EP1062302B1 (fr) | 2002-02-27 |
| DK1062302T3 (da) | 2002-04-02 |
| DE69804026T2 (de) | 2002-10-31 |
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| CA2295917C (fr) | Procede de reduction de l'indice d'acidite total du petrole brut | |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| MKEX | Expiry |
Effective date: 20180828 |