DE431923C - Process for obtaining benzene from gases - Google Patents

Process for obtaining benzene from gases

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Publication number
DE431923C
DE431923C DEH86131D DEH0086131D DE431923C DE 431923 C DE431923 C DE 431923C DE H86131 D DEH86131 D DE H86131D DE H0086131 D DEH0086131 D DE H0086131D DE 431923 C DE431923 C DE 431923C
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DE
Germany
Prior art keywords
benzene
gases
washing oil
oil
washing
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
DEH86131D
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German (de)
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Individual
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Individual
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Publication date
Application filed by Individual filed Critical Individual
Priority to DEH86131D priority Critical patent/DE431923C/en
Application granted granted Critical
Publication of DE431923C publication Critical patent/DE431923C/en
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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00Purifying combustible gases containing carbon monoxide
    • C10K1/08Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
    • C10K1/16Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with non-aqueous liquids
    • C10K1/18Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with non-aqueous liquids hydrocarbon oils
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10CWORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
    • C10C1/00Working-up tar
    • C10C1/04Working-up tar by distillation
    • C10C1/08Winning of aromatic fractions
    • C10C1/10Winning of aromatic fractions benzene fraction light fraction
    • 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
    • C10G5/00Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas
    • C10G5/06Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas by cooling or compressing

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Materials Engineering (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

Verfahren zur Gewinnung des Benzols aus Gasen. Das bisher üblichste Großverfahren zur Gewinnung des Benzols aus Gasen, insbesondere aus den Steinkohlendestillationsgasen, ist sehr umständlich und erfordert eine äußerst kostspielige Anlage in Gestalt von etwa 20M hohen Benzolwaschern, welche bei dem bisherigen Verfahren unumgänglich sind, weil das Waschöl, ein zwischen 195 bis 3oo° C bis 93 Prozent übergehendes Teeröl, bereits in frischem Zustand verhältnismäßig dickflüssig und träge absorbierend ist und sich diese Eigenschaften mit der Dauer des Gebrauchs des Waschöls noch erheblich verschlechtern; trotzdem verbleiben auch bei sorgfältigst betriebenen Anlagen noch 3 bis q. g Benzol im Kubikmeter Destillationsgas. Ferner gestaltet sich bisher auch die Abtreibung des Benzols aus dem Waschöl infolge der Dickflüssigkeit des letzteren verhältnismäßig umständlich, denn hierzu ist eine Vorwärmung des mit Benzol gesättigten Waschöls und eine Abtreibung des Benzols mit direktem Dampf erforderlich.Process for obtaining benzene from gases. The most common so far Large-scale processes for the production of benzene from gases, especially from the coal distillation gases, is very cumbersome and requires extremely expensive equipment in the form of about 20M high benzene washers, which were inevitable in the previous process are because the washing oil, between 195 to 300 ° C to 93 percent Tar oil, even when fresh, is relatively thick and sluggishly absorbent is and these properties increase significantly with the duration of the use of the washing oil worsen; nevertheless still remain even with the most carefully operated systems 3 to q. g of benzene in the cubic meter of distillation gas. Furthermore, so far, too the removal of benzene from the washing oil as a result of the viscosity of the latter relatively cumbersome, because this is a preheating of the with benzene saturated washing oil and an abortion of benzene with direct steam is required.

Man hat zwar das Benzol auch schon in Tauchwaschern ausgewaschen, jedoch, vermutlich infolge der oben angegebenem, Eigenschaften des verwendeten Waschöls, mit einem sehr trägen Erfolg, welcher dieses Verfahren für den Großbetrieb unanwendbar macht.The benzene has already been washed out in immersion washers, however, presumably due to the properties of the washing oil used, as stated above, with very sluggish success, which made this procedure inapplicable for large-scale operations power.

Das Verfahren gemäß der Erfindung kennzeichnet sich demgegenüber dadurch, daß anstatt eines zwischen 195 bis 300° oder auch zwischen 23o bis 25o° zu 90 Prozent übergehenden-Teeröls ein zwischen r8o bis 220'C bis 9o Prozent aus dem Benzolvorprodukt übergehendes Öl als Waschöl in Tauchwaschern verwendet und aus diesen das Benzol in DestilIationsblasen ohne direkte Dampfzufuhr ausgetrieben wird. Es hat sich nämlich ergeben, daß ein derartiges Waschöl weit absorptionsfähiger ist als die bisher verwendeten Waschöle, und daß sich eine erheblich weitergehende Benzolauswaschung als bisher und mit großen und infolgedessen auch für den Großbetrieb geeigneten Stundenleistungen sowie infolge der großen Dünnflüssigkeit dieses Öls auch ohne erheblichen Zeitaufwand in ununterbrochenem Arbeitsgang in Tauchwaschern durchführen läßt, und daß ferner zur Wiedergewinnung des Benzols aus diesem Waschöl die bisher notwendige Zuhilfenahme unmittelbar durch das Waschöl getriebenen Dampfes unnötig ist.The method according to the invention is characterized in contrast, the fact that instead of from 195 to 300 °, or between 23o to 25o ° to 90 percent over continuous-creosote one to 220'C to 9o percent from the Benzolvorprodukt on going between r8o oil as a washing oil in Tauchwaschern used and from these the benzene is expelled in distillation bubbles without direct steam supply. It has been shown that such a washing oil is far more absorbent than the washing oils used previously, and that a considerably more extensive benzene leaching than before and with large hourly outputs and consequently also suitable for large-scale operations as well as without considerable expenditure of time due to the high degree of fluidity of this oil can be carried out in an uninterrupted operation in immersion washers, and that, furthermore, to recover the benzene from this washing oil, the previously necessary assistance directly driven by the washing oil steam is unnecessary.

Das Verfahren gestaltet sich demnach etwa wie folgt: Das benzolhaltige Gas, also bei- spielsweise das durch die Ammoniakfabrik gegangene Destillationsgas, wird in einen Tauchwascher a geleitet, in welchem das Gas mittels einer Tauchglocke b durch das Waschöl fein verteilt hindurchgeleitet wird und bei c wieder entweicht. Das mit Benzolöl gesättigte Waschöl läuft, zweckmäßig in unmiterbrochenem Betrieb, unten von dem Wascher a zu einem Sammelbehälter d, von welchem es durch eine Pumpe e zu einer mit Dampf o. dgl. beheizten Destillationsblase f gedrückt wird, deren Temperatur, wie üblich, bis auf etwa z8o° gesteigert wird. Das aus der Blase gegebenenfalls direkt fraktioniert abgetriebene Benzol gelangt durch einen Kühler i in die Vorproduktenbehälter f. Das abgetriebene Waschöl wird in die Pfannen g gedrückt, wo es geküblr und das Naphthalin ausgeschieden wird, und fließt durch einen Rückkühler h in das Waschgefäß a zurück.The process is roughly as follows: The gas containing benzene, i.e. two For example, the distillation gas that has passed through the ammonia factory is fed into an immersion washer a, in which the gas is finely distributed through the washing oil by means of an immersion bell b and escapes again at c. The washing oil saturated with benzene oil runs, expediently in uninterrupted operation, from the washer a to a collecting tank d, from which it is pressed by a pump e to a steam or the like heated distillation vessel f, the temperature of which, as usual, is up to is increased to about z8o °. The benzene, which may be directly fractionated from the bladder, passes through a cooler i into the preliminary product container f. The removed washing oil is pressed into the pans g, where it is cooled and the naphthalene is eliminated, and flows back through a recooler h into the washing container a.

Beispielsweise konnte mit einem derartigen Waschöl und mittels eines einzigen Tauchwasch ers eine nahezu restlose Benz<>lauswaschung aus 3oo coo cbm Steinkohlendestillationsgasen in 2.1 Stunden erzielt werden.For example, with such a washing oil and by means of a The only immersion washer was an almost complete Benz <> lauswaschung from 3oo coo cbm Hard coal distillation gases can be achieved in 2.1 hours.

Claims (1)

PATENT-ANSPRLTCIi: Verfahren zur Gewinnung des Benzols aus Gasen i:@ Tauchwaschern, dadurch ge. kennzeichnet, daß als Waschöl ein aus dem Benzolvorprodukt zwischen :8o bis 22o' C gewonnenes Öl dient und daß das von ihm aufgenommene Benzol in DestilIationsblasen ohne direkte Dampfzufuhr ausgetrieben wird.PATENT-ANSPRLTCIi: Process for the production of benzene from gases i: @ Dip washers, thereby ge. indicates that a washing oil from the benzene precursor between: 8o to 22o 'C obtained oil is used and that the benzene absorbed by it is expelled in distillation stills without direct steam supply.
DEH86131D 1921-07-03 1921-07-03 Process for obtaining benzene from gases Expired DE431923C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEH86131D DE431923C (en) 1921-07-03 1921-07-03 Process for obtaining benzene from gases

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEH86131D DE431923C (en) 1921-07-03 1921-07-03 Process for obtaining benzene from gases

Publications (1)

Publication Number Publication Date
DE431923C true DE431923C (en) 1926-07-23

Family

ID=7164594

Family Applications (1)

Application Number Title Priority Date Filing Date
DEH86131D Expired DE431923C (en) 1921-07-03 1921-07-03 Process for obtaining benzene from gases

Country Status (1)

Country Link
DE (1) DE431923C (en)

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