AT48194B - Device for the distillation of oils of the petroleum, tar u. Like. Industry under high vacuum. - Google Patents

Device for the distillation of oils of the petroleum, tar u. Like. Industry under high vacuum.

Info

Publication number
AT48194B
AT48194B AT48194DA AT48194B AT 48194 B AT48194 B AT 48194B AT 48194D A AT48194D A AT 48194DA AT 48194 B AT48194 B AT 48194B
Authority
AT
Austria
Prior art keywords
distillation
tar
petroleum
oils
high vacuum
Prior art date
Application number
Other languages
German (de)
Inventor
Philipp Porges
Leopold Dr Singer
Leo Steinschneider
Original Assignee
Philipp Porges
Leopold Dr Singer
Leo Steinschneider
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 Philipp Porges, Leopold Dr Singer, Leo Steinschneider filed Critical Philipp Porges
Application granted granted Critical
Publication of AT48194B publication Critical patent/AT48194B/en

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
    • C10G7/00—Distillation of hydrocarbon oils
    • C10G7/06—Vacuum distillation

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)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

  

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 EMI1.1 
 
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 die bauliche Schwierigkeit unvermeidlich ist, die   Destillationsanlage ungcmoin   hoch aufstellen zu   müssen,   um den Austritt noch über Erdniveau anordnen zu können. Die Unterbauten für die Destillieranlage werden dadurch ungemein kostspielig, die Hinaufschaffung des Brennmaterials und die Bedienung höchst unvorteilhaft. 



   Der Gegenstand der vorliegenden Erfindung behebt die obenangeführten Mängel vollständig. Auf der beiliegenden Zeichnung ist schematisch eine Destillieranlage für hohes Vakuum dargestellt, deren Einrichtung den Gegenstand vorliegender Erfindung bildet. Aus der Destillierblase D gelangen die   Dcstillatdämpfe   durch ein System von   Luftkiihl-Dephlegmatoren A   und B beliebiger Einrichtung zum Röhrenkühler K und von da aus zum hochstehenden Kondensator C. Die in den Dephlegmatoren A und B kondensierten Destillate gelangen zu den   Röhrenkühlem   0 und von da aus durch Rohre ra zu Sammelgefässen S, welche zur Regulierung ihres Flüssigkeitsstandes vorteilhaft mit einer Schwimmervorrichtung versehen werden können.

   Die im Röhrenkühler K gebildeten flüssigen Destillate können eventuell direkt zu einem solchen Sammelgefäss 8 gelangen. Aus den   Gefässen 8 gelangen   die auf diese Weise gesammelten einzelnen flüssigen Fraktionen mittels eines Fallrohres r4 zu entsprechend tief   gestellten Fraktionspumpen   p, so zwar. dass jede einzelne Fraktion ihre eigene Pumpe erhält. Diese Pumpen drücken die gebildeten Fraktionen durch separate Druckrohre r5 in die höherstehende Receiving box E (Empfangskasten). Die nichtkondensierbaren Gase werden aus dem   hochstehenden   Kondensator ('mittels 
 EMI2.1 
 entsprechend hohes Fallrohr r6 zum Abflusskanal abgeleitet. 



   Während nun bei den Anlagen für geringes Vakuum das Kondensat nach Verlassen des Kühlers und Passieren eines entsprechenden   Flüssigkeitssyphons frei zur Receiving   box auslaufen kann. da eine dem   Vakuum   entsprechend geringe Flüssigkeitshöhe in dem   Htandrohr r4   bereits 
 EMI2.2 
 für das Vakuum notwendigen   Gefälles   werden durch diese Anordnung vermieden und es   braucht   in diesem Falle bloss der   barometrische   Kondensator hochgestellt zu werden.



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 the structural difficulty is inevitable that the distillation plant has to be set up high in order to be able to arrange the outlet above ground level. This makes the substructures for the distillation system extremely expensive, and the transportation of the fuel and operation extremely disadvantageous.



   The object of the present invention completely overcomes the above deficiencies. In the accompanying drawing, a distillation system for high vacuum is shown schematically, the device of which forms the subject of the present invention. From the still D, the distillate vapors pass through a system of air cooler dephlegmators A and B of any device to the tube cooler K and from there to the upright condenser C. The distillates condensed in the dephlegmators A and B reach the tube coolers 0 and from there through Pipes ra to collecting vessels S, which can advantageously be provided with a float device to regulate their liquid level.

   The liquid distillates formed in the tube cooler K can possibly reach such a collecting vessel 8 directly. From the vessels 8, the individual liquid fractions collected in this way pass by means of a downpipe r4 to fraction pumps p, which are appropriately positioned lower down. that every single faction has its own pump. These pumps push the fractions formed through separate pressure pipes r5 into the higher-standing receiving box E (receiving box). The non-condensable gases are released from the upright condenser ('by means of
 EMI2.1
 correspondingly high downpipe r6 diverted to the drainage channel.



   Whereas with the systems for low vacuum the condensate can flow freely to the receiving box after leaving the cooler and passing a corresponding liquid siphon. there is already a liquid level in the hand pipe r4 corresponding to the vacuum
 EMI2.2
 The gradient required for the vacuum is avoided by this arrangement and in this case only the barometric condenser needs to be turned up.

Claims (1)

PATENT-ANSPRUCH : EMI2.3 PATENT CLAIM: EMI2.3
AT48194D 1907-12-19 1907-12-19 Device for the distillation of oils of the petroleum, tar u. Like. Industry under high vacuum. AT48194B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT48194T 1907-12-19

Publications (1)

Publication Number Publication Date
AT48194B true AT48194B (en) 1911-05-26

Family

ID=3568715

Family Applications (1)

Application Number Title Priority Date Filing Date
AT48194D AT48194B (en) 1907-12-19 1907-12-19 Device for the distillation of oils of the petroleum, tar u. Like. Industry under high vacuum.

Country Status (1)

Country Link
AT (1) AT48194B (en)

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