GB940146A - Process for upgrading heavy hydrocarbon oils - Google Patents
Process for upgrading heavy hydrocarbon oilsInfo
- Publication number
- GB940146A GB940146A GB18404/61A GB1840461A GB940146A GB 940146 A GB940146 A GB 940146A GB 18404/61 A GB18404/61 A GB 18404/61A GB 1840461 A GB1840461 A GB 1840461A GB 940146 A GB940146 A GB 940146A
- Authority
- GB
- United Kingdom
- Prior art keywords
- magma
- oil
- water
- reaction product
- liquid phase
- 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
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
- C10G19/00—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment
- C10G19/067—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment with molten alkaline material
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)
Abstract
Heavy hydrocarbon oils containing metal compounds and/or heteroatomic compounds of sulphur and nitrogen as contaminants are upgraded in a process which comprises contacting the oil in the liquid phase at temperatures within the range of the temperature of incipient cracking and the temperature at which extensive thermal decomposition (as defined) would occur, but in any case in the range 375-475 DEG C., for a contact time of at least 1 minute and at a pressure of at least 14 kg/cm.2 gauge, with a magma, the essential component of which is sodium and/or potassium hydroxide containing not more than 30% wt. of water, the weight ratio of alkali metal hydroxide to hydrocarbon oil being at least 0.025 : 1, and separating from the resulting mixture an oil phase having a substantially reduced content of contaminants. A preferred magma comprises the carbonate, sulphide, and hydroxide of sodium and/or potassium. A preferred process comprises the steps of (1) mixing the oil and magma, (2) cooling to above the solidification temperature of the magma, (3) adding water, (4) recovering from the mixture a vaporous phase comprising normally gaseous oil reaction product, an upper liquid phase comprising normally liquid reaction product, a lower liquid phase comprising reacted magma and water, and possibly a layer of emulsion of magma and oil reaction product, from between the interfaces of the two other liquid layers, which emulsion is recycled to step (1), (5) mixing the recovered upper liquid layer with water, and (6) recovering from this mixture a lower liquid layer of water containing magma removed from the reaction product, which may be recycled to step (3) of the process, and an upper liquid phase comprising the oil freed from magma and having a substantially reduced content of contaminants.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US30878A US3051645A (en) | 1960-05-23 | 1960-05-23 | Upgrading heavy hydrocarbon oils |
Publications (1)
Publication Number | Publication Date |
---|---|
GB940146A true GB940146A (en) | 1963-10-23 |
Family
ID=21856480
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB18404/61A Expired GB940146A (en) | 1960-05-23 | 1961-05-19 | Process for upgrading heavy hydrocarbon oils |
Country Status (4)
Country | Link |
---|---|
US (1) | US3051645A (en) |
DE (1) | DE1470628A1 (en) |
GB (1) | GB940146A (en) |
NL (1) | NL264945A (en) |
Families Citing this family (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3129165A (en) * | 1960-05-09 | 1964-04-14 | Shell Oil Co | Refining of steam-cracked gasolines with molten salt |
US3354081A (en) * | 1965-09-01 | 1967-11-21 | Exxon Research Engineering Co | Process for desulfurization employing k2s |
US3440164A (en) * | 1965-09-03 | 1969-04-22 | Exxon Research Engineering Co | Process for desulfurizing vacuum distilled fractions |
US4224139A (en) * | 1979-04-16 | 1980-09-23 | Phillips Petroleum Company | Treatment of sulfur-containing lubricating oil to increase resistance to oxidation |
US7444305B2 (en) * | 2001-02-15 | 2008-10-28 | Mass Connections, Inc. | Methods of coordinating products and service demonstrations |
US7745369B2 (en) | 2003-12-19 | 2010-06-29 | Shell Oil Company | Method and catalyst for producing a crude product with minimal hydrogen uptake |
US8025791B2 (en) | 2003-12-19 | 2011-09-27 | Shell Oil Company | Systems and methods of producing a crude product |
US7628908B2 (en) | 2003-12-19 | 2009-12-08 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
TW200602591A (en) * | 2004-07-08 | 2006-01-16 | hong-yang Chen | Gas supply device by gasifying burnable liquid |
BRPI0609416A2 (en) | 2005-04-11 | 2011-10-11 | Shell Int Research | method to produce a gross product |
RU2424275C2 (en) | 2005-04-11 | 2011-07-20 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Procedure for production of semi-finished product with reduced content of micro-carbon residue and catalyst for its implementation |
US20080083650A1 (en) | 2006-10-06 | 2008-04-10 | Bhan Opinder K | Methods for producing a crude product |
US8778173B2 (en) * | 2008-12-18 | 2014-07-15 | Exxonmobil Research And Engineering Company | Process for producing a high stability desulfurized heavy oils stream |
US8696890B2 (en) * | 2009-12-18 | 2014-04-15 | Exxonmobil Research And Engineering Company | Desulfurization process using alkali metal reagent |
US8404106B2 (en) * | 2009-12-18 | 2013-03-26 | Exxonmobil Research And Engineering Company | Regeneration of alkali metal reagent |
US8613852B2 (en) * | 2009-12-18 | 2013-12-24 | Exxonmobil Research And Engineering Company | Process for producing a high stability desulfurized heavy oils stream |
US8894845B2 (en) | 2011-12-07 | 2014-11-25 | Exxonmobil Research And Engineering Company | Alkali metal hydroprocessing of heavy oils with enhanced removal of coke products |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1506661A (en) * | 1922-02-16 | 1924-08-26 | Pannier Bros Stamp Co | Type member for printing stamps |
US2020661A (en) * | 1923-06-20 | 1935-11-12 | Phillips Petroleum Co | Process for treating hydrocarbon oils |
US2110403A (en) * | 1935-06-10 | 1938-03-08 | Shell Dev | Separating h2s and mercaptans from hydrocarbons |
US2471108A (en) * | 1947-06-06 | 1949-05-24 | Standard Oil Dev Co | Treatment of sulfur containing hydrocarbons |
US2581117A (en) * | 1949-12-16 | 1952-01-01 | Standard Oil Dev Co | Treatment of cracked naphthas with a hypochlorite followed by an alkali sulfide |
US2950245A (en) * | 1958-03-24 | 1960-08-23 | Alfred M Thomsen | Method of processing mineral oils with alkali metals or their compounds |
-
0
- NL NL264945D patent/NL264945A/xx unknown
-
1960
- 1960-05-23 US US30878A patent/US3051645A/en not_active Expired - Lifetime
-
1961
- 1961-05-19 GB GB18404/61A patent/GB940146A/en not_active Expired
- 1961-05-20 DE DE19611470628 patent/DE1470628A1/en active Pending
Also Published As
Publication number | Publication date |
---|---|
NL264945A (en) | |
DE1470628A1 (en) | 1969-03-13 |
US3051645A (en) | 1962-08-28 |
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