DE928116C - Process for the refined hydrogenation of paraffins which are difficult to refine - Google Patents

Process for the refined hydrogenation of paraffins which are difficult to refine

Info

Publication number
DE928116C
DE928116C DER10716A DER0010716A DE928116C DE 928116 C DE928116 C DE 928116C DE R10716 A DER10716 A DE R10716A DE R0010716 A DER0010716 A DE R0010716A DE 928116 C DE928116 C DE 928116C
Authority
DE
Germany
Prior art keywords
atmospheres
hydrogenation
water
paraffins
refine
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
DER10716A
Other languages
German (de)
Inventor
Robert Lueben
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.)
Ruhrchemie AG
Original Assignee
Ruhrchemie 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 Ruhrchemie AG filed Critical Ruhrchemie AG
Priority to DER10716A priority Critical patent/DE928116C/en
Application granted granted Critical
Publication of DE928116C publication Critical patent/DE928116C/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
    • C10G73/00Recovery or refining of mineral waxes, e.g. montan wax
    • C10G73/42Refining of petroleum waxes
    • C10G73/44Refining of petroleum waxes in the presence of hydrogen or hydrogen-generating compounds

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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

Es ist bekannt, Hartwachse, vorzugsweise solche, die bei der katalytischen Kohlenoxydhydrierung gebildet werden und oberhalb 3800 sieden, durch Hydrierung an geeigneten Katalysatoren, die vorzugsweise Metalle der 8. Gruppe des Periodischen Systems bzw. Kupfer neben Aktivatoren, wie z. B. MgO, enthalten, zu farblosen, farbstabilen Paraffinen zu raffinieren. Dabei wird im allgemeinen im kontinuierlichen Verfahren an fest angeordneten Katalysatoren bei Temperaturen von 200 bis 2600, vorzugsweise 2500, und Drücken von 10 bis 120 atü, vorzugsweise von 75 atü, gearbeitet. Das Ende der Hydrierung ist in etwa 1 bis 4 Stunden, vorzugsweise in 2 Stunden, erreicht. In manchen Fällen erhält man jedoch auch bei Anwendung hoher Drücke. während der Hydrierung, bekpielsweise von 120 atü, nur gefärbte Produkte, die wenig transparent bleiben und sich bei der Weiterverarbeitung verfärben.It is known that hard waxes, preferably those that are formed in the catalytic hydrogenation of carbohydrates and boil above 380 0 , by hydrogenation over suitable catalysts, which are preferably metals from Group 8 of the Periodic Table or copper in addition to activators, such as. B. MgO contain to refine to colorless, color-stable paraffins. In general, the continuous process is carried out over fixed catalysts at temperatures from 200 to 260 ° , preferably 250 ° , and pressures from 10 to 120 atmospheres, preferably 75 atmospheres. The end of the hydrogenation is reached in about 1 to 4 hours, preferably in 2 hours. However, in some cases high pressures are also obtained. during the hydrogenation, for example from 120 atmospheres, only colored products that remain not very transparent and discolor during further processing.

Es wurde gefunden, daß die Hydrierung der Hartwachse der katalytischen Kohlenoxydhydricrung zu transparenten, farblosen, farbstabilen Hartwachsen führt, wenn man die durch Hydrierung zu raffinierenden Produkte zunächst einer Wasservoxbehandlung bei einer Temperatur, die oberhalb des Schmelzpunktes des Produktes liegt, bei der die störendem Bestandteile; von Wasser gelöst werden, vorzugsweise bei 200°, und dem entsprechenden Dampfdruck im Rühr autoklav 1 bis 3 Stunden unterwirft. Das Wasser und eine etwaIt has been found that the hydrogenation of the hard waxes is the result of catalytic hydrocarbons leads to transparent, colorless, color-stable hard waxes if they are hydrogenated Products to be refined first undergo a water vox treatment at a temperature that is above the melting point of the product at which the interfering components; dissolved by water are, preferably at 200 °, and the corresponding steam pressure in the stirrer autoclave 1 to Subjected for 3 hours. The water and one about

entstandene dünne Emulsionssdhicht werden danach vom Einsatzprodukt abgetrennt und letzteres in bekannter Weise an geeigneten Hydrierkatalysatoren, die vorzugsweise Metalle der 8. Gruppe des Periodischen Systems, gegebenenfalls auch Kupfer neben Aktivatoren, wie z. B. Magnesiumoxyd, enthalten, hydriert, wobei Drücke von io bis 120 atü, vorzugsweise 75 atü, H2 + N2 entsprechend einem Wasserstoffpartialdruck von 56 atü, angewandt werden.The resulting thin emulsion layer is then separated off from the feedstock and the latter in a known manner on suitable hydrogenation catalysts, which are preferably metals of group 8 of the Periodic Table, optionally also copper in addition to activators, such as. B. magnesium oxide, contain, hydrogenated, with pressures of 10 to 120 atmospheres, preferably 75 atmospheres, H 2 + N 2 corresponding to a hydrogen partial pressure of 56 atmospheres, are used.

Beispielexample

Ein braunes Fischer-Tropsch-Hartwachs aus der zweiten Synthesestufe mit einem Siedepunkt oberhalb 4600 wurde bei 2500 und 75 atü H2 + N2 = 56 atü H2 am Nickel-Magnesiumoxyd-Kieselgur-Katalysator 5 Stunden hydriert. Das^hydirierte Produkt war zwar aufgehellt, blieb jedoch wenig transparent und im durchfallenden Licht braun.A brown Fischer-Tropsch hard wax from the second synthesis stage with a boiling point above 460 ° was hydrogenated at 250 ° and 75 atm. H 2 + N 2 = 56 atm. H 2 over a nickel-magnesium oxide-diatomaceous earth catalyst for 5 hours. The hydrated product was indeed lightened, but remained less transparent and brown in the transmitted light.

Das gleiche Produkt wurde mit 30% Wasser bei 2oo° 2 Stunden lang im Rührautoklav bei einem Wasserdampfpartialdruck von etwa 16 atü behandelt. Nach Abtrennen des Wassers wurde das Produkt 2 Stunden bei den sonst gleichen Bedingungen hydriert, wobei man ein transparentes, farbloses, farbstabiles Hartwachs erhielt.The same product was treated with 30% water at 2oo ° for 2 hours in a stirred autoclave treated with a water vapor partial pressure of about 16 atü. After separating the water, the Product hydrogenated for 2 hours under the otherwise identical conditions, using a transparent, colorless, color-stable hard wax was obtained.

Claims (1)

PATENTANSPRUCH:PATENT CLAIM: Verfahren z,ur raffinierenden Hydrierung schwer raffinierbarer Paraffine, vorzugsweise von Hartwachs aus der katalytischen Kohlenoxydhydrierung, dadurch gekennzeichnet, daß man die zu raffinierenden Produkte zunächst einer Vorbehandlung mit Wasser bei einer ■ Temperatur, die über dem Schmelzpunkt des Produktes liegt und bei der die störenden Bestandteile von Wasser gelöst werden, vorzugsweise bei 2oo°, und dem entsprechenden Dampfdruck 1 bis 3 Stunden unterwirft, das Wasser mit den darin gelösten störenden Bestandteilen vom Einsatzprodukt abtrennt und letzteres in bekannter Weise an geeigneten Hydrierkatalysatoren, die vorzugsweise Metalle der 8. Gruppe des Periodischen Systems, gegebenenfalls auch Kupfer neben Aktivatoren, wie z. B. Magnesiumoxyd, enthalten, hydriert, wobei- Drücke von 10 bis 120 atü, vorzugsweise 75 atü, H2 + N2 entsprechend einem Wasserstoffpartialdruck von 56 atü, angewandt werden.Process for refining hydrogenation of paraffins which are difficult to refine, preferably hard wax from catalytic carbon dioxide hydrogenation, characterized in that the products to be refined are first pretreated with water at a temperature which is above the melting point of the product and at which the interfering components are dissolved by water, preferably at 2oo °, and subjected to the corresponding vapor pressure for 1 to 3 hours, the water with the disruptive constituents dissolved therein is separated from the starting product and the latter is in a known manner on suitable hydrogenation catalysts, preferably metals of group 8 of the Periodic Table , optionally also copper in addition to activators, such as. B. magnesium oxide, contain, hydrogenated, pressures of 10 to 120 atmospheres, preferably 75 atmospheres, H 2 + N 2 corresponding to a hydrogen partial pressure of 56 atmospheres, are used. 1 509507 5.551 509507 5.55
DER10716A 1953-01-15 1953-01-16 Process for the refined hydrogenation of paraffins which are difficult to refine Expired DE928116C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DER10716A DE928116C (en) 1953-01-15 1953-01-16 Process for the refined hydrogenation of paraffins which are difficult to refine

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE2761871X 1953-01-15
DER10716A DE928116C (en) 1953-01-15 1953-01-16 Process for the refined hydrogenation of paraffins which are difficult to refine

Publications (1)

Publication Number Publication Date
DE928116C true DE928116C (en) 1955-05-23

Family

ID=25991128

Family Applications (1)

Application Number Title Priority Date Filing Date
DER10716A Expired DE928116C (en) 1953-01-15 1953-01-16 Process for the refined hydrogenation of paraffins which are difficult to refine

Country Status (1)

Country Link
DE (1) DE928116C (en)

Similar Documents

Publication Publication Date Title
DE68902700T2 (en) METHOD FOR PRODUCING SYNTHETIC LUBRICANT OIL BY OLEFINOLIGOMERISATION.
US2163563A (en) Method of reclaiming mineral oils
DE1443763A1 (en) Process for the production of aromatics or cracked products
DE933826C (en) Process for the production of gasoline and possibly diesel oil from crude oil
DE928116C (en) Process for the refined hydrogenation of paraffins which are difficult to refine
DE685595C (en) Process for refining gasoline
DE927593C (en) Process for cleaning, in particular lightening, of completely or partially saturated hydrocarbons by hydrogenating their hydrogenatable accompanying substances
DE2831328C2 (en)
DE843849C (en) Process for the preparation of oxygen-containing compounds
DE939278C (en) Process for the desulphurization of crude oils by catalytic pressure hydrogenation
DE700434C (en)
DE935080C (en) Process to increase the yield and improve the quality of shale oil smoldering paraffins
DE535723C (en) Process for liquefying coal
DE725600C (en) Process for the catalytic pressure hydrogenation of high-boiling liquid or fusible hydrocarbon oils containing asphalt and / or resins
DE1119844B (en) Process for the production of alkenes
DE547536C (en) Process for liquefying coal
DE689360C (en)
DE829344C (en) Process for the production of low-boiling hydrocarbons
DE879442C (en) Process for the separation of olefins from cracked products
US2307675A (en) Process for the production of ozokeritelike substances
DE928060C (en) Process to increase the yield and improve the quality of Schieferoelschwelparaffin
DE895763C (en) Process for carrying out the olefin polymerization with substances containing metal halides
DE561714C (en) Process for the production of unsaturated hydrocarbons
DE954692C (en) Process for the alkylation and hydrogenation refining of benzene hydrocarbons
DE708432C (en) Process for processing lignite pressure extracts