DE535473C - Process for converting high-boiling to low-boiling hydrocarbons - Google Patents

Process for converting high-boiling to low-boiling hydrocarbons

Info

Publication number
DE535473C
DE535473C DEI32326D DEI0032326D DE535473C DE 535473 C DE535473 C DE 535473C DE I32326 D DEI32326 D DE I32326D DE I0032326 D DEI0032326 D DE I0032326D DE 535473 C DE535473 C DE 535473C
Authority
DE
Germany
Prior art keywords
boiling
parts
hydrocarbons
acids
low
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
DEI32326D
Other languages
German (de)
Inventor
Dr Ernst Galle
Dr Gerhardt Hofmann
Dr Walter Rosinsky
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.)
IG Farbenindustrie AG
Original Assignee
IG Farbenindustrie AG
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 IG Farbenindustrie AG filed Critical IG Farbenindustrie AG
Priority to DEI32326D priority Critical patent/DE535473C/en
Priority to GB33580/27D priority patent/GB311789A/en
Priority to US301688A priority patent/US1923571A/en
Priority to FR660559D priority patent/FR660559A/en
Application granted granted Critical
Publication of DE535473C publication Critical patent/DE535473C/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/06Catalytic processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/04Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing carboxylic acids or their salts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/26Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/04Thermal processes
    • 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/08Halides
    • 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12Inorganic carriers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

Verfahren zur Umwandlung hochsiedender in niedrigsiedende Kohlenwasserstoffe Es hat sich gezeigt, daß man die Spaltung von höhersiedenden Kohlenwasserstofen mit vorzüglichen Ausbeuten an niedrigsiedenden Kohlenwasserstoffen ausführen kann, wenn man auf naphthensäurefreie hochsiedende Ausgangsmaterialien, z. B. naphthensäurefreie Mineralöle, Teere, Hydrierungsprodukte von Kohle, ölen oder Teeren u. dgl., oder Destil:-lätions- und Umwandlungsprodukte dieser Ausgangsstoffe Katalysatoren vom Typ komplexer Ansolvosäuren (Liebigs Annalen, Band 455, S. 227 bis 253) oder deren Komponenten, also Verbindungen oder Mischungen organischer Säuren oder deren Derivaten, wie z. B. Oxysäuren, Säureamide u. a., mit anorganischen Salzen, bei Temperaturen oberhalb 3oo° einwirken läßt.Process for converting high-boiling to low-boiling hydrocarbons It has been shown that the cleavage of higher-boiling hydrocarbons can perform with excellent yields of low-boiling hydrocarbons, if you rely on naphthenic acid-free high-boiling starting materials, e.g. B. naphthenic acid-free Mineral oils, tars, hydrogenation products of coal, oils or tars and the like, or Destil: -lätions- and conversion products of these starting materials catalysts from Type of complex ansolvo acids (Liebigs Annalen, Volume 455, pp. 227 to 253) or their Components, i.e. compounds or mixtures of organic acids or their derivatives, such as B. Oxyacids, acid amides and others, with inorganic salts, at temperatures lets act above 300 °.

Es ist zwar bekannt, Gemische von organischen Säuren und anorganischen Salzen als Zusätze bei der Spaltung von Kohlenwasserstoffen zu verwenden; doch gelangen diese Mischungen in sehr großer Menge und bei Temperaturen von etwa 2oo° zur Anwendung, bei denen Ansolvosäuren noch gar nicht wirksam sind. Der große Vorzug der Ansolvosäuren gegenüber den bei den bekannten Verfahren vorhandenen undefinierten Gemischen liegt in ihrer besonderen Spaltfähigkeit, die darauf beruht, daß die Komplexsäuren eine erhöhte H-Ionenkonzentration gegenüber den Einzelkomponenten aufweisen, die in bestimmten Mischungsverhältnissen der Komponenten noch besonders ausgeprägt ist. Diesem Umstand ist es zu danken, daß, sie schon in geringer Menge ausgezeichnet wirksam sind. Es hat sich gezeigt, daß, sämtliche Ansolvosäuren in dieser Weise als Krackkatalysatoren mit Vorteil anwendbar sind.Although it is known, mixtures of organic acids and inorganic To use salts as additives in the splitting of hydrocarbons; get there these mixtures are used in very large quantities and at temperatures of around 2oo °, where Ansolvo acids are not yet effective. The great advantage of the Ansolvo acids compared to the undefined mixtures present in the known processes in their special cleavage ability, which is based on the fact that the complex acids a have increased H-ion concentration compared to the individual components that are present in certain Mixing ratios of the components is still particularly pronounced. This circumstance It is to be thanked that, even in small amounts, they are extremely effective. It it has been found that all ansolvo acids act as cracking catalysts in this way are applicable with advantage.

Das vorliegende Verfahren wird bei gewöhnlichem oder zweckmäßig bei erhöhtem Druck durchgeführt, wobei Rühren der Reaktionsmasse vorteilhaft ist.The present method is usually or conveniently at carried out under elevated pressure, stirring the reaction mass is advantageous.

Auch kann man in Gegenwart von Wasserstoff oder wasserstoffabgebenden Gasen arbeiten.It is also possible in the presence of hydrogen or a hydrogen donor Gases work.

Beispiel i ioo Teile einer von Zoo. bis 35o° siedenden Dünnteerfraktion werden mit 5 Teilen einer a-Naphthoesäure-Zinntetrachlorid-Doppelverbindung bei 35o bis 400° und einem Druck von io at behandelt. Von den erhaltenen Spaltprodukten sieden 41,2 Teile, bezogen auf das Ausgangsmaterial, unterhalb 2oo°.Example i ioo parts one from zoo. up to 35o ° boiling thin tar fraction are with 5 parts of an α-naphthoic acid-tin tetrachloride double compound 35o to 400 ° and a pressure of io at treated. From the fission products obtained 41.2 parts, based on the starting material, boil below 200 °.

Statt der Doppelverbindung kann. man auch die beiden Komponenten in veränderlichen molekularen Verhältnissen zusetzen. Arbeitet man bei niedrigeren Temperaturen, etwa Zoo bis 25o°, dann bilden sich nur 2 bis 3% bis 2oo° siedende Produkte. Beispiel a ioo Teile eines gereinigten Generatordickteeres werden in Gegenwart von 5 Teilen einer i - Naphtholcarbonsäure - Aluminiumchlorid-Doppelverbindung (oder ihren Bestandteilen wie im vorigen Beispiel) in einem mit -Monel:-blech ausgekleideten Autoklaven auf etwa 38o bis q.20° erhitzt. Von den gewonnenen Produkten sieden, bezogen auf das Ausgangsmaterial, 33,5 Teile bis zoo°. ' Beispiel 3 ioo Teile eines entbenzinierten Genera<tordickteeres werden mit 3 Teilen einer ölsäure-Zinkchlorid-Doppelverbindung (oder ihren Bestandteilen, s. Beispiel i) in einem Rührautoklaven bei 35o° und a5 at behandelt, wobei man 35 Teile von bis 2oo' siedenden Produkten erhält. -Beispiel q.Instead of the double connection can. you can also use the two components in subject to changing molecular conditions. One works at lower Temperatures, about zoo up to 25o °, then only 2 to 3% to 2oo ° are boiling Products. Example a 100 parts of a cleaned generator oil are in the presence of 5 parts of an i - naphtholecarboxylic acid - aluminum chloride double compound (or its components as in the previous example) in a sheet lined with Monel: Autoclave heated to around 38o to 20 °. Boil from the obtained products, based on the starting material, 33.5 parts up to zoo °. 'Example 3 ioo parts of a Gasoline-free genera <tordickeeres are made with 3 parts of an oleic acid-zinc chloride double compound (or its components, see example i) in a stirred autoclave at 35o ° and a5 treated at, whereby 35 parts of up to 2oo 'boiling products are obtained. -Example q.

ioo Teile Paraffin (Fp: 41 bis q.3°) werden mit i Teil einer Ameisensäure-Aluminiumchlorid-Doppelverbindung (oder deren Komponenten, s. Beispiel i) auf ¢0o bis q.q.o° und 3o at erhitzt, wobei gg Teile überdestillieren, von denen 7 5 .Teile bis 2oo' und weiter a¢Teile bis 36o° sieden, Beispiel 5 iooTeile eines oberhalb von 2oo' siedenden Mineralöles werden mit 5 Teilen einer a'- Naphthoesäure - Antimonpentachlorid-Doppelverbindung (oder ihrer Komponenten wie in Beispiel i) unter einem Wasserstoffdruck von 5o at bis, ¢2o° erhitzt. Von den erhaltenen Spaltprodukten sieden,. bezogen auf das Ausgangsmaterial, ¢5 Teile unterhalb zoo°.100 parts of paraffin (melting point 41 to 3 °) are combined with 1 part of a formic acid-aluminum chloride double compound (or their components, see Example i) heated to ¢ 0o to q.q.o ° and 3o at, with Distill over gg parts, of which 7 5 parts up to 2oo 'and further a ¢ parts up to Boiling 360 °, example 5 100 parts of a mineral oil boiling above 200 ' with 5 parts of a'-naphthoic acid - antimony pentachloride double compound (or its components as in example i) under a hydrogen pressure of 50 at to, ¢ 20 ° heated. Boil from the cleavage products obtained. based on the starting material, ¢ 5 parts below zoo °.

Claims (1)

PATENTANSPRUCH: Verfahren zur Umwandlung höhersiedender in niedrigsiedende Kohlenwasserstoffe in Gegenwart organischer - Säuren und anorganischer Salze, dadurch gekennzeichnet, daß man auf naphthensäurefreie Ausgangsstoffe, wie naphthensäurefreie Mineralöle, Teere, Hydrierungsprodukte von Kohle u. dgl., oder deren Destillations-oder Umwandlungsprodukte Verbindungen oder Mischungen organischer Säuren oder deren Derivate mit anorganischen Salzen vom Typus der Ansolvosäuren bei Temperaturen oberhalb 300°, zweckmäßig bei erhöhtem Druck und gegebenenfalls in-Gegenwart von Wasserstoff oder wasserstoffabgebenden Gasen, einwirken läßt.PATENT CLAIM: Process for converting higher boiling to lower boiling ones Hydrocarbons in the presence of organic - acids and inorganic salts, thereby characterized in that one uses naphthenic acid-free starting materials, such as naphthenic acid-free Mineral oils, tars, hydrogenation products of coal and the like, or their distillation or Conversion products Compounds or mixtures of organic acids or their derivatives with inorganic salts of the Ansolvo acid type at temperatures above 300 °, expediently at elevated pressure and optionally in the presence of hydrogen or hydrogen-releasing gases.
DEI32326D 1927-10-03 1927-10-03 Process for converting high-boiling to low-boiling hydrocarbons Expired DE535473C (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
DEI32326D DE535473C (en) 1927-10-03 1927-10-03 Process for converting high-boiling to low-boiling hydrocarbons
GB33580/27D GB311789A (en) 1927-10-03 1927-12-14 Improvements in the conversion of hydrocarbons of high boiling point into those of low boiling point
US301688A US1923571A (en) 1927-10-03 1928-08-23 Conversion of hydrocarbons of high boiling point into those of low boiling point
FR660559D FR660559A (en) 1927-10-03 1928-09-18 Process for the conversion of high boiling point hydrocarbons to low boiling point hydrocarbons

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEI32326D DE535473C (en) 1927-10-03 1927-10-03 Process for converting high-boiling to low-boiling hydrocarbons

Publications (1)

Publication Number Publication Date
DE535473C true DE535473C (en) 1931-10-10

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ID=7188101

Family Applications (1)

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DEI32326D Expired DE535473C (en) 1927-10-03 1927-10-03 Process for converting high-boiling to low-boiling hydrocarbons

Country Status (4)

Country Link
US (1) US1923571A (en)
DE (1) DE535473C (en)
FR (1) FR660559A (en)
GB (1) GB311789A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5814407B2 (en) * 1976-05-10 1983-03-18 ライオン株式会社 Method for producing catalyst for olefin polymerization
US4504378A (en) * 1983-02-18 1985-03-12 Marathon Oil Company Sodium tetrachloroaluminate catalyzed process for the molecular weight reduction of liquid hydrocarbons

Also Published As

Publication number Publication date
FR660559A (en) 1929-07-12
US1923571A (en) 1933-08-22
GB311789A (en) 1929-05-14

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