DE972001C - Process for removing sodium and vanadium from crude petroleum or petroleum products - Google Patents
Process for removing sodium and vanadium from crude petroleum or petroleum productsInfo
- Publication number
- DE972001C DE972001C DEA18203A DEA0018203A DE972001C DE 972001 C DE972001 C DE 972001C DE A18203 A DEA18203 A DE A18203A DE A0018203 A DEA0018203 A DE A0018203A DE 972001 C DE972001 C DE 972001C
- Authority
- DE
- Germany
- Prior art keywords
- petroleum
- vanadium
- sodium
- crude
- bauxite
- 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
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C
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)
Description
AUSGEGEBEN AM 6. MAI 1959ISSUED MAY 6, 1959
BIBUOTHSKBIBUOTHSK
PATENTSCHRIFTPATENT LETTERING
KLASSE 23b GRUPPE 1o5 INTERNAT. KLASSE CIOg CLASS 23b GROUP 1o5 INTERNAT. CLASS CIOg
A 18203 IVc I 23bA 18203 IVc I 23b
Frederick William Bertram Porter und Roy Purdy Northcott, Sunbury-on-Thames, Middlesex (Großbritannien)Frederick William Bertram Porter and Roy Purdy Northcott, Sunbury-on-Thames, Middlesex (Great Britain)
sind als Erfinder genannt wordenhave been named as inventors
The British Petroleum Company Limited, LondonThe British Petroleum Company Limited, London
Verfahren zur Entfernung von Natrium und Vanadium aus rohem Erdöl oder ErdölproduktenMethod of removing sodium and vanadium from crude petroleum or petroleum products
Zusatz zum Patent 970 697Addendum to patent 970 697
Patentiert im Gebiet der Bundesrepublik Deutschland vom 14. Juni 1953
Das Hauptpatent hat angefangen am 13. Januar 1952
Patentanmeldung bekanntgemacbt am 30. August 1956Patented in the territory of the Federal Republic of Germany on June 14, 1953 The main patent started on January 13, 1952
Patent application announced on August 30, 1956
Patenterteilung bekanntgemacht am 23. April 1959
Die Priorität der Anmeldung in Großbritannien vom 18. Juni 1952 ist in Anspruch genommenPatent issued April 23, 1959
The priority of the application in Great Britain of June 18, 1952 has been claimed
Gegenstand des Patents 970 697 ist ein Verfahren zur Entfernung von Natrium und Vanadium aus rohem Erdöl oder Erdölprodukten, bei denen das rohe Erdöl oder die Erdölprodukte mit Bauxit in Gegenwart von Wasserstoff unter solchen zwischen 311 und 4270 liegenden Temperaturen, vorzugsweise bei 415 °, und solchen zwischen 57 und 71 kg/cm2 liegenden Drücken, vorzugsweise bei 71 kg/cm2, behandelt werden, daß Natrium und Vanadium vom Bauxit festgehalten werden.The subject of patent 970 697 is a process for the removal of sodium and vanadium from crude petroleum or petroleum products, in which the crude petroleum or petroleum products with bauxite in the presence of hydrogen below temperatures between 311 and 427 0 , preferably at 415 °, and such pressures lying between 57 and 71 kg / cm 2 , preferably at 71 kg / cm 2 , are treated that sodium and vanadium are retained by the bauxite.
Es wurde nun gefunden, daß man 'an Stelle von Bauxit das rohe Erdöl oder die Erdölprodukte mitIt has now been found that crude oil or petroleum products can be used instead of bauxite
einem aus Fullererde bestehenden Kontaktmaterial behandeln kann und das behandelte öl gegebenenfalls anschließend einer Hydrierungszone zur Entfernung organisch gebundenen Schwefels zuführen kann.can treat a contact material consisting of fuller's earth and the treated oil, if necessary can then feed a hydrogenation zone to remove organically bound sulfur.
Vorzugsweise wird unter folgenden Bedingungen gearbeitet:It is preferable to work under the following conditions:
Raumströmungsgeschwindigkeit 0,5 bis 2 V/V/Std.Room flow rate 0.5 to 2 V / V / hour.
Temperatur 400 bis 430°Temperature 400 to 430 °
Druck 35 bis 105 atPressure 35 to 105 at
rückgeführte Wasserstoffmenge 180 bis 1800 m3/m8 Recirculated amount of hydrogen 180 to 1800 m 3 / m 8
909 504/13909 504/13
Es wurde gefunden, daß bei der Hydrofinierung von rohem Erdöl und Erdölrückständen unter Verwendung eines aus Kobalt- und Molybdänoxyden auf einem Aluminiumoxydträger bestehenden Katalysators beträchtliche Mengen Vanadium und Natrium vom Katalysator aufgenommen werden und dadurch die Katalysatoraktivität während des Betriebes ständig abnimmt und bei einer Regeneration in üblicher Weise nicht voll wiederhergestellt werden kann. Gemäß derIt has been found that in the hydrofining of crude petroleum and petroleum residues using a catalyst consisting of cobalt and molybdenum oxides on an alumina support is considerable Amounts of vanadium and sodium are absorbed by the catalyst and thereby the catalyst activity is constant during operation decreases and cannot be fully restored during regeneration in the usual way. According to the
ίο Erfindung wird dagegen in einem kontinuierlichen Verfahren das Vanadium und/oder Natrium enthaltende Erdöl zunächst mit Fullererde behandelt und darin in einer Hydrierungszone von organisch gebundenem.,,. Schwefel befreit.ίο Invention, on the other hand, is ongoing Process the vanadium and / or sodium containing petroleum first treated with fuller's earth and therein in a hydrogenation zone of organically bound. ,,. Sulfur free.
Nachstehend wird die Anwendung des Verfahrens gemäß der Erfindung auf die Behandlung eines Erdölrückstandes gegeben.The application of the method according to the invention to the treatment of a petroleum residue will now be described given.
Entfernung von Natrium und Vanadium aus einem Erdölrückstand, der durch Abtreiben von 47% flüchtiger Stoffe aus einem Kuwaitöl erhalten wurde.Removal of sodium and vanadium from a petroleum residue, which by stripping 47% volatiles obtained from a Kuwait oil.
BetriebsbedingungenOperating conditions
Ausgangsöl Kuwait 53 Volumprozent Rückstand Raumströmungsgeschwindigkeit iV/V/Std.Starting oil Kuwait 53 volume percent residue space velocity IV / V / hour
Temperatur '. 4160 CTemperature '. 416 0 C
Druck 70 atPressure 70 at
rückgeführte Wasserstoffmenge 720 m3/m3 recirculated amount of hydrogen 720 m 3 / m 3
Flußrichtung aufwärtsDirection of flow upwards
Betriebsdauer 50 StundenOperating time 50 hours
Erzielte ErgebnisseResults achieved
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB15307/52A GB735521A (en) | 1952-06-18 | 1952-06-18 | Improvements relating to the removal of vanadium and/or sodium from petroleum and hydrocarbons of petroleum origin |
Publications (1)
Publication Number | Publication Date |
---|---|
DE972001C true DE972001C (en) | 1959-05-06 |
Family
ID=10056761
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEA18203A Expired DE972001C (en) | 1952-06-18 | 1953-06-14 | Process for removing sodium and vanadium from crude petroleum or petroleum products |
Country Status (4)
Country | Link |
---|---|
US (1) | US2766183A (en) |
BE (1) | BE520662A (en) |
DE (1) | DE972001C (en) |
GB (1) | GB735521A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE550052A (en) * | 1954-12-10 | |||
US2945803A (en) * | 1958-04-14 | 1960-07-19 | Gulf Research Development Co | Process for hydrogen treatment and catalytic cracking of petroleum hydrocarbons |
US3546103A (en) * | 1969-02-03 | 1970-12-08 | Exxon Research Engineering Co | Hydrogenation catalysts on charcoal in guard chamber for removing metals from petroleum residua |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2116061A (en) * | 1929-10-26 | 1938-05-03 | Standard Ig Co | Purification of mineral oils, tars, their distillation products, and the like |
GB345738A (en) * | 1930-01-23 | 1931-04-02 | Ig Farbenindustrie Ag | Improvements in the purification of mineral oils, tars, their distillation products and the like |
US2340922A (en) * | 1941-04-15 | 1944-02-08 | Atlantic Refining Co | Desulphurization of hydrocarbon oils |
-
0
- BE BE520662D patent/BE520662A/xx unknown
-
1952
- 1952-06-18 GB GB15307/52A patent/GB735521A/en not_active Expired
-
1953
- 1953-06-14 DE DEA18203A patent/DE972001C/en not_active Expired
- 1953-06-16 US US362145A patent/US2766183A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
GB735521A (en) | 1955-08-24 |
US2766183A (en) | 1956-10-09 |
BE520662A (en) |
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