RU2000124672A - REMOVAL OF NAPHTHENIC ACIDS FROM OIL RAW MATERIALS AND DISTILLATES - Google Patents
REMOVAL OF NAPHTHENIC ACIDS FROM OIL RAW MATERIALS AND DISTILLATESInfo
- Publication number
- RU2000124672A RU2000124672A RU2000124672/04A RU2000124672A RU2000124672A RU 2000124672 A RU2000124672 A RU 2000124672A RU 2000124672/04 A RU2000124672/04 A RU 2000124672/04A RU 2000124672 A RU2000124672 A RU 2000124672A RU 2000124672 A RU2000124672 A RU 2000124672A
- Authority
- RU
- Russia
- Prior art keywords
- specified
- organic acids
- water
- ethoxylated amine
- amine
- Prior art date
Links
- 239000002253 acid Substances 0.000 title claims 6
- 239000002994 raw material Substances 0.000 title claims 4
- 150000007513 acids Chemical class 0.000 title claims 2
- 150000001412 amines Chemical class 0.000 claims 13
- 238000000034 method Methods 0.000 claims 11
- 150000007524 organic acids Chemical class 0.000 claims 10
- 235000005985 organic acids Nutrition 0.000 claims 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 8
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims 5
- 229910001385 heavy metal Inorganic materials 0.000 claims 5
- 229910052717 sulfur Inorganic materials 0.000 claims 5
- 239000011593 sulfur Substances 0.000 claims 5
- 229910052500 inorganic mineral Inorganic materials 0.000 claims 4
- 239000011707 mineral Substances 0.000 claims 4
- 150000003839 salts Chemical class 0.000 claims 4
- -1 amine salt Chemical class 0.000 claims 3
- 239000001569 carbon dioxide Substances 0.000 claims 3
- 229910002092 carbon dioxide Inorganic materials 0.000 claims 3
- 239000003921 oil Substances 0.000 claims 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims 2
- 239000010779 crude oil Substances 0.000 claims 2
- 239000000839 emulsion Substances 0.000 claims 2
- 239000006260 foam Substances 0.000 claims 2
- 239000003208 petroleum Substances 0.000 claims 2
- 238000000926 separation method Methods 0.000 claims 2
- 239000004215 Carbon black (E152) Substances 0.000 claims 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims 1
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 238000007664 blowing Methods 0.000 claims 1
- 238000011033 desalting Methods 0.000 claims 1
- 229930195733 hydrocarbon Natural products 0.000 claims 1
- 125000001183 hydrocarbyl group Chemical group 0.000 claims 1
- 150000007529 inorganic bases Chemical class 0.000 claims 1
- 239000010410 layer Substances 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 125000005608 naphthenic acid group Chemical group 0.000 claims 1
- 239000007764 o/w emulsion Substances 0.000 claims 1
Claims (1)
а) обработки исходного нефтяного сырья, содержащего органические кислоты, тяжелые металлы и серу, этоксилированным амином и водой в количествах, при условиях, в течение времени и при температуре, достаточных для образования эмульсии соли амина типа вода в масле, причем указанный этоксилированный амин имеет следующую формулу:
где m равно от 1 до 10, a R - углеводород С3 - С6,
б) разделения указанной эмульсии с операции а) на несколько слоев, причем один из этих слоев содержит обработанное нефтяное сырье с пониженным количеством органических кислот, тяжелых металлов и серы,
в) извлечения указанного слоя с операции б), содержащего указанное обработанное нефтяное сырье с пониженным количеством органических кислот, тяжелых металлов и серы, и слоев, содержащих воду и соль этоксилированного амина
2. Способ по п. 1, отличающийся тем, что указанную воду добавляют одновременно с указанным этоксилированным амином или после него.1. The method of removal of organic acids, heavy metals and sulfur from the source of crude oil, including operations
a) processing the original petroleum feedstock containing organic acids, heavy metals and sulfur, with an ethoxylated amine and water in amounts, under conditions, for a time and at a temperature sufficient to form an emulsion of the water-in-oil amine salt, the ethoxylated amine having the following formula:
where m is from 1 to 10, a R is a hydrocarbon With 3 - C 6 ,
b) separating said emulsion from operation a) into several layers, and one of these layers contains treated oil feedstock with a reduced amount of organic acids, heavy metals and sulfur,
C) removing the specified layer from operation b), containing the specified processed oil with a reduced amount of organic acids, heavy metals and sulfur, and layers containing water and a salt of ethoxylated amine
2. The method according to p. 1, characterized in that the specified water is added simultaneously with the specified ethoxylated amine or after it.
5. Способ по п. 1, отличающийся тем, что указанные операции а) и б) выполняют в течение времени, составляющего от 1 мин до 1 ч.4. The method according to p. 1, characterized in that the ethoxylated amine is 0.15 - 3.0 molar equivalents based on the amount of organic acids
5. The method according to p. 1, characterized in that said operations a) and b) are performed for a time of from 1 minute to 1 hour.
где m равно 1 - 10, a R - С3 - С6, в контактной колонне, в течение времени и при температуре, достаточных для образования неустойчивой эмульсии типа масло в воде.7. The method according to p. 1, characterized in that it is carried out at the wellhead, and the specified raw materials contained in the full flow from the specified wellhead, the method includes passing the specified full stream to the separator to obtain a gas flow, flow of raw materials, containing naphthenic acids, and a stream of water, contacting, in a countercurrent, the said source of crude oil with said stream of water in the presence of an ethoxylated amine in quantities, for a time and at a temperature sufficient to produce salt and amine, and the specified ethoxylated amine has the following formula
where m is 1 - 10, a R - C 3 - C 6 , in the contact column, for a time and at a temperature sufficient to form an unstable oil-in-water emulsion.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/049,466 US5961821A (en) | 1998-03-27 | 1998-03-27 | Removal of naphthenic acids in crude oils and distillates |
| US09/049,466 | 1998-03-27 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| RU2000124672A true RU2000124672A (en) | 2002-08-10 |
| RU2208622C2 RU2208622C2 (en) | 2003-07-20 |
Family
ID=21959969
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| RU2000124672/04A RU2208622C2 (en) | 1998-03-27 | 1999-03-19 | Removal of naphthenic acids from oil feedstock and distillates |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US5961821A (en) |
| EP (1) | EP1068280B1 (en) |
| JP (1) | JP2002509980A (en) |
| CN (1) | CN1295607A (en) |
| AU (1) | AU745496B2 (en) |
| BR (1) | BR9909116A (en) |
| CA (1) | CA2323051A1 (en) |
| DE (1) | DE69900846T2 (en) |
| DK (1) | DK1068280T3 (en) |
| ES (1) | ES2172318T3 (en) |
| NO (1) | NO325473B1 (en) |
| RU (1) | RU2208622C2 (en) |
| WO (1) | WO1999050376A1 (en) |
Families Citing this family (38)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6536523B1 (en) | 1997-01-14 | 2003-03-25 | Aqua Pure Ventures Inc. | Water treatment process for thermal heavy oil recovery |
| US6096196A (en) * | 1998-03-27 | 2000-08-01 | Exxon Research And Engineering Co. | Removal of naphthenic acids in crude oils and distillates |
| AUPQ363299A0 (en) | 1999-10-25 | 1999-11-18 | Silverbrook Research Pty Ltd | Paper based information inter face |
| US6531055B1 (en) * | 2000-04-18 | 2003-03-11 | Exxonmobil Research And Engineering Company | Method for reducing the naphthenic acid content of crude oil and fractions |
| US6372123B1 (en) | 2000-06-26 | 2002-04-16 | Colt Engineering Corporation | Method of removing water and contaminants from crude oil containing same |
| GB0031337D0 (en) * | 2000-12-21 | 2001-02-07 | Bp Exploration Operating | Process for deacidfying crude oil |
| FR2825369B1 (en) * | 2001-06-01 | 2005-04-15 | Elf Antar France | PROCESS FOR PROCESSING RAW OIL WITH HIGH ORGANIC ACIDITY |
| DE10217469C1 (en) * | 2002-04-19 | 2003-09-25 | Clariant Gmbh | Desulfurization of crude oil fractionation products, e.g. petrol, kerosene, diesel fuel, gas oil and fuel oil, involves extraction with (poly)alkylene glycol, alkanolamine or derivative |
| BR0202552B1 (en) * | 2002-07-05 | 2012-10-30 | process of reducing naphthenic acidity in petroleum. | |
| CA2455011C (en) | 2004-01-09 | 2011-04-05 | Suncor Energy Inc. | Bituminous froth inline steam injection processing |
| CA2455149C (en) * | 2004-01-22 | 2006-04-11 | Suncor Energy Inc. | In-line hydrotreatment process for low tan synthetic crude oil production from oil sand |
| CN1298813C (en) * | 2005-04-29 | 2007-02-07 | 清华大学 | Process for treating oil by alkali washing |
| CN101058745B (en) * | 2007-05-16 | 2011-09-07 | 中国科学院过程工程研究所 | Removal and recovery of naphthenic acid in oil based on ion switch principle |
| US7960520B2 (en) | 2007-06-15 | 2011-06-14 | Uop Llc | Conversion of lignocellulosic biomass to chemicals and fuels |
| US8013195B2 (en) * | 2007-06-15 | 2011-09-06 | Uop Llc | Enhancing conversion of lignocellulosic biomass |
| US8158842B2 (en) * | 2007-06-15 | 2012-04-17 | Uop Llc | Production of chemicals from pyrolysis oil |
| WO2008155333A1 (en) * | 2007-06-20 | 2008-12-24 | Akzo Nobel N.V. | A method for preventing the formation of calcium carboxylate deposits in the dewatering process for crude oil/water streams |
| US20090301936A1 (en) * | 2008-05-15 | 2009-12-10 | Desmond Smith | Composition and use thereof |
| US20100000910A1 (en) * | 2008-07-03 | 2010-01-07 | Chevron U.S.A. Inc. | System and method for separating a trace element from a liquid hydrocarbon feed |
| NL2002958C2 (en) * | 2008-06-03 | 2010-10-13 | Chevron Usa Inc | System and method for separating a trace element from a liquid hydrocarbon feed. |
| US8608949B2 (en) * | 2009-12-30 | 2013-12-17 | Uop Llc | Process for removing metals from vacuum gas oil |
| US8608943B2 (en) * | 2009-12-30 | 2013-12-17 | Uop Llc | Process for removing nitrogen from vacuum gas oil |
| US8608950B2 (en) * | 2009-12-30 | 2013-12-17 | Uop Llc | Process for removing metals from resid |
| US8580107B2 (en) * | 2009-12-30 | 2013-11-12 | Uop Llc | Process for removing sulfur from vacuum gas oil |
| US8608951B2 (en) * | 2009-12-30 | 2013-12-17 | Uop Llc | Process for removing metals from crude oil |
| US8608952B2 (en) * | 2009-12-30 | 2013-12-17 | Uop Llc | Process for de-acidifying hydrocarbons |
| WO2011116059A1 (en) * | 2010-03-16 | 2011-09-22 | Saudi Arabian Oil Company | System and process for integrated oxidative desulfurization, desalting and deasphalting of hydrocarbon feedstocks |
| US8790508B2 (en) | 2010-09-29 | 2014-07-29 | Saudi Arabian Oil Company | Integrated deasphalting and oxidative removal of heteroatom hydrocarbon compounds from liquid hydrocarbon feedstocks |
| JP6072790B2 (en) | 2011-07-29 | 2017-02-01 | サウジ アラビアン オイル カンパニー | Method for reducing total acid number in petroleum refinery feedstock |
| US8574427B2 (en) | 2011-12-15 | 2013-11-05 | Uop Llc | Process for removing refractory nitrogen compounds from vacuum gas oil |
| EP2628780A1 (en) | 2012-02-17 | 2013-08-21 | Reliance Industries Limited | A solvent extraction process for removal of naphthenic acids and calcium from low asphaltic crude oil |
| BR112014028452A2 (en) | 2012-05-16 | 2018-05-29 | Chevron Usa Inc | process, method, and system for removing heavy metals from fluids. |
| WO2013173586A1 (en) | 2012-05-16 | 2013-11-21 | Chevron U.S.A. Inc. | Process, method, and system for removing mercury from fluids |
| US9447675B2 (en) | 2012-05-16 | 2016-09-20 | Chevron U.S.A. Inc. | In-situ method and system for removing heavy metals from produced fluids |
| EP2850155B1 (en) | 2012-05-16 | 2018-04-04 | Chevron U.S.A., Inc. | Process for removing mercury from fluids |
| US9023196B2 (en) | 2013-03-14 | 2015-05-05 | Chevron U.S.A. Inc. | Process, method, and system for removing heavy metals from fluids |
| US9234141B2 (en) | 2013-03-14 | 2016-01-12 | Chevron U.S.A. Inc. | Process, method, and system for removing heavy metals from oily solids |
| US9169445B2 (en) | 2013-03-14 | 2015-10-27 | Chevron U.S.A. Inc. | Process, method, and system for removing heavy metals from oily solids |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2424158A (en) * | 1944-09-20 | 1947-07-15 | Standard Oil Dev Co | Process of refining a petroleum oil containing naphthenic acids |
| US4420414A (en) * | 1983-04-11 | 1983-12-13 | Texaco Inc. | Corrosion inhibition system |
| US4737265A (en) * | 1983-12-06 | 1988-04-12 | Exxon Research & Engineering Co. | Water based demulsifier formulation and process for its use in dewatering and desalting crude hydrocarbon oils |
| GB8431013D0 (en) * | 1984-12-07 | 1985-01-16 | British Petroleum Co Plc | Desalting crude oil |
| FR2576032B1 (en) * | 1985-01-17 | 1987-02-06 | Elf France | HOMOGENEOUS AND STABLE COMPOSITION OF ASPHALTENIC LIQUID HYDROCARBONS AND AT LEAST ONE ADDITIVE USABLE IN PARTICULAR AS FUEL INDUSTRIAL |
| US4752381A (en) * | 1987-05-18 | 1988-06-21 | Nalco Chemical Company | Upgrading petroleum and petroleum fractions |
| CA2133270C (en) * | 1994-03-03 | 1999-07-20 | Jerry J. Weers | Quaternary ammonium hydroxides as mercaptan scavengers |
| RU2095393C1 (en) * | 1994-06-28 | 1997-11-10 | Всероссийский научно-исследовательский институт углеводородного сырья | Method of demercaptanizaion of crude oil and gas condensate |
| US5582792A (en) * | 1995-08-24 | 1996-12-10 | Petrolite Corporation | Corrosion inhibition by ethoxylated fatty amine salts of maleated unsaturated acids |
| US5792420A (en) * | 1997-05-13 | 1998-08-11 | Halliburton Energy Services, Inc. | Metal corrosion inhibitor for use in aqueous acid solutions |
-
1998
- 1998-03-27 US US09/049,466 patent/US5961821A/en not_active Expired - Lifetime
-
1999
- 1999-03-19 CN CN99804502.0A patent/CN1295607A/en active Pending
- 1999-03-19 EP EP99914955A patent/EP1068280B1/en not_active Expired - Lifetime
- 1999-03-19 DK DK99914955T patent/DK1068280T3/en active
- 1999-03-19 AU AU33584/99A patent/AU745496B2/en not_active Ceased
- 1999-03-19 BR BR9909116-0A patent/BR9909116A/en not_active Application Discontinuation
- 1999-03-19 DE DE69900846T patent/DE69900846T2/en not_active Expired - Fee Related
- 1999-03-19 ES ES99914955T patent/ES2172318T3/en not_active Expired - Lifetime
- 1999-03-19 WO PCT/US1999/006078 patent/WO1999050376A1/en not_active Ceased
- 1999-03-19 CA CA002323051A patent/CA2323051A1/en not_active Abandoned
- 1999-03-19 RU RU2000124672/04A patent/RU2208622C2/en active
- 1999-03-19 JP JP2000541265A patent/JP2002509980A/en active Pending
-
2000
- 2000-09-26 NO NO20004806A patent/NO325473B1/en not_active IP Right Cessation
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