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 products

Info

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
Application number
DEA18203A
Other languages
German (de)
Inventor
Roy Purdy Northcott
Frederick William Betra Porter
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BP PLC
Original Assignee
BP PLC
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by BP PLC filed Critical BP PLC
Application granted granted Critical
Publication of DE972001C publication Critical patent/DE972001C/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02Refining 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
    • C10G45/04Refining 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/107Atmospheric 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

BUNDESREPUBLIK DEUTSCHLANDFEDERAL REPUBLIC OF GERMANY DEUTSCHES PATENTAMTGERMAN PATENT OFFICE

AUSGEGEBEN AM 6. MAI 1959ISSUED MAY 6, 1959

BIBUOTHSKBIBUOTHSK

DES DEUTSCHESOF GERMAN PATENTAMTESPATENT OFFICE

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 1956
Patented 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 genommen
Patent 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.

Beispielexample

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

GrobkörnigeCoarse-grained Behandeltes ÖlTreated oil FullererdeFuller's earth Gesamtmenge,Total quantity, AusgangsölStarting oil währendwhile 50 Stunden50 hours 41,041.0 erhaltenobtain Vanadium, mg/kg..Vanadium, mg / kg .. 39,039.0 27,027.0 Natrium, mg/kg ...Sodium, mg / kg ... 33,033.0 Schwefel, GewichtsSulfur, weight 3,893.89 prozent percent 3,243.24 Spezifisches Gewicht,Specific weight, 0,9580.958 I5,56/I5,56O I5.56 / I5.56 O 0,9400.940

Claims (1)

PATENTANSPRUCH:PATENT CLAIM: Verfahren zur Entfernung von Natrium und Vanadium aus rohem Erdöl oder Erdölprodukten durch Behandlung von rohem Erdöl oder Erdölprodukten mit Bauxit in Gegenwart von Wasserstoff unter solchen zwischen 371 und 4270, vorzugsweise bei 415 °, liegenden Temperaturen und solchen zwischen 57 und 71 kg/cm2, vorzugsweise bei 71 kg/cm2, liegenden Drücken, wobei Natrium und Vanadium vom Bauxit festgehalten werden, nach Patent 970 697, dadurch gekennzeichnet, daß man an Stelle von Bauxit mit einem aus Fullererde bestehenden Kontaktmaterial behandelt und das behandelte Öl gegebenenfalls anschließend einer Hydrierungszone zur Entfernung organisch gebundenen Schwefels zuführt.Process for removing sodium and vanadium from crude petroleum or petroleum products by treating crude petroleum or petroleum products with bauxite in the presence of hydrogen at temperatures between 371 and 427 0 , preferably at 415 °, and temperatures between 57 and 71 kg / cm 2 , preferably at 71 kg / cm 2 , with sodium and vanadium being retained by the bauxite, according to Patent 970 697, characterized in that instead of bauxite, treatment is carried out with a contact material consisting of fuller's earth and the treated oil optionally then a hydrogenation zone supplies organically bound sulfur to remove. © 609 616/439-8.56 (909 504/13 4.59)© 609 616 / 439-8.56 (909 504/13 4.59)
DEA18203A 1952-06-18 1953-06-14 Process for removing sodium and vanadium from crude petroleum or petroleum products Expired DE972001C (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Also Published As

Publication number Publication date
US2766183A (en) 1956-10-09
BE520662A (en)
GB735521A (en) 1955-08-24

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