DE515911C - Process for smoldering fine-grained or dusty bituminous substances - Google Patents

Process for smoldering fine-grained or dusty bituminous substances

Info

Publication number
DE515911C
DE515911C DET30936D DET0030936D DE515911C DE 515911 C DE515911 C DE 515911C DE T30936 D DET30936 D DE T30936D DE T0030936 D DET0030936 D DE T0030936D DE 515911 C DE515911 C DE 515911C
Authority
DE
Germany
Prior art keywords
smoldering
dusty
grained
fine
bituminous substances
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
DET30936D
Other languages
German (de)
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.)
KOHLENVEREDLUNG AKT GES
Original Assignee
KOHLENVEREDLUNG AKT GES
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 KOHLENVEREDLUNG AKT GES filed Critical KOHLENVEREDLUNG AKT GES
Priority to DET30936D priority Critical patent/DE515911C/en
Application granted granted Critical
Publication of DE515911C publication Critical patent/DE515911C/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C10B49/04Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
    • C10B49/08Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated in dispersed form

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Furnace Details (AREA)

Description

Verfahren zum Schwelen von feinkörnigen oder staubförmigen bituminösen Stoffen Bei den bisher für die Tieftemperaturschwelerei mit unmittelbarer Beheizung angewandten Verfahren waren Heizgastemperaturen von höchstens 5oo bis 6oo ° zulässig. Vereinzelt wurden auch Heizgastemperaturen bis 8oo ° C vorgeschlagen. Wurde z. B. das Schwelgut in stückiger Form derart verschwelt, daß das Heizgas zwischen den einzelnen Stücken hindurchtrat, so konnte eine höhere Temperatur aus dem Grunde nicht angewandt werden, weil die größeren Kohlenstücke an der Oberfläche beinahe die Heizgastemperatur annahmen, während der Kern noch verhältnismäßig kalt blieb. Hierbei ergab sich der Nachteil, daß sich die im Kern des Kohlenstückes entstehenden, nach außen entweichenden Teerdämpfe bei ihrem Durchgang durch die hocherhitzte Randschicht der einzelnen Stücke zersetzten.Process for smoldering fine-grained or dusty bituminous Fabrics For those previously used for low-temperature delicatessen with direct heating The methods used allowed hot gas temperatures of no more than 5oo to 6oo °. In some cases, heating gas temperatures of up to 8oo ° C have also been suggested. Was z. B. the Schwelgut in lump form so carbonized that the heating gas between the individual pieces passed through, a higher temperature could from the bottom cannot be used because the larger pieces of coal on the surface are almost assumed the hot gas temperature while the core remained relatively cold. This resulted in the disadvantage that the resulting in the core of the coal piece, tar vapors escaping to the outside as they pass through the highly heated surface layer of the individual pieces decomposed.

Soweit Temperaturen in der Nähe von 8oo ° oder darüber zur Behandlung bituminösen Materials durch Spülgase vorgeschlagen wurden, handelte es sich nicht um Verschwelung, d. h. schonende Destillation mit Teergewinnung, sondern um Hochtemperatur-Destillationsverfahren zur Gewinnung von Koks, wobei auf die möglichste Erhaltung der teerigen Bestandteile kein Wert gelegt wurde. Demgegenüber hat der Erfinder erkannt, daß bei geeigneter Betriebsführung und insbesondere Abkürzung der Dauer der Einwirkung der heißen Gase auf das Ausgangsgut auch die Temperaturen der Heizgase für die Durchführung von Schwelverfahren, d. h. schonender Destillation, wesentlich höher gehalten werden können, als man bisher für derartige Verfahren zulässig erachtete.As far as temperatures in the vicinity of 8oo ° or above for treatment bituminous material were suggested by purge gases, it was not about smoldering, d. H. gentle distillation with tar extraction, but rather high-temperature distillation processes for the production of coke, with the greatest possible preservation of the tarry components no value was placed. In contrast, the inventor has recognized that with a suitable Operational management and in particular shortening the duration of exposure to the hot gases on the starting material also the temperatures of the heating gases for the implementation of Smoldering process, d. H. gentle distillation, are kept much higher than was previously considered admissible for such proceedings.

Die vorliegende Erfindung beruht auf der Erkenntnis, daß es bei dem an sich bekannten Verfahren, das Schwelgut schwebend in einem Heizgasstrom zu schwelen, möglich ist, mit den Temperaturen der Heizgase weit höher zu gehen, als das bisher der Fall war. Die Schwelgutteilchen sind so klein, daß nennenswerte Temperaturunterschiede zwischen Außenfläche und Kern nicht vorhanden sein können. Die Heizgastemperatur kann also gegenüber der bisher zulässigen wesentlich gesteigert werden, ohne daß Zersetzungserscheinungen eintreten.The present invention is based on the finding that it is in the known methods of smoldering the smoldering material while floating in a flow of heating gas, it is possible to go much higher with the temperatures of the heating gases than before was the case. The Schwelgutteilchen are so small that there are significant temperature differences cannot exist between the outer surface and the core. The heating gas temperature can therefore be increased significantly compared to the previously permissible without Signs of decomposition occur.

Zu Beginn des Schwelvorganges wird, wie bekannt, aus dem Schwelgut zunächst das Wasser ausgetrieben, ein Vorgang, der nach eingehenden Versuchen den größten Teil der zum Schwelen überhaupt erforderlichen Wärmemenge beansprucht. Während dieser Zeit bleibt die Temperatur der Staubteilchen auf der dem Druck im Ofen entsprechenden Siedetemperatur des Wassers stehen, um nach vollendeter Wasserverdampfung weiter zu steigen. Bis zum Beginn des Entweichens der Teerdämpfe haben sich die Heizgase aber bereits so weit abgekühlt, daß eine Zersetzung der Teerdämpfe beim Vermischen mit den Heizgasen nicht mehr zu befürchten ist. In Erkenntnis dieser Vorgänge sollen nach dem vorliegenden Verfahren für die Tieftemperaturschwelung, also zur Gewinnung von Urteer und Halbkoks, Anfangstemperaturen der Heizgase von über 8oo ° C angewandt werden. Durch diese hohen Temperaturen wird das Wärmegefälle der Heizgase gegenüber der Schwelguttemperatur erheblich vergrößert, so daß die Schwelzeit auf wenige Sekunden verkürzt wird.As is known, at the beginning of the smoldering process, the smoldering material becomes first expelled the water, a process that, after careful experiments, the most of the amount of heat required for smoldering. While During this time, the temperature of the dust particles remains at the temperature corresponding to the pressure in the oven Stand at the boiling point of the water to continue after the water has evaporated to rise. By the time the tar vapors begin to escape, the heating gases have settled but already cooled so far that a decomposition of the tar vapors when mixing is no longer to be feared with the heating gases. In recognition of this According to the present procedure for low-temperature depletion, processes should So for the extraction of tar and semi-coke, starting temperatures of the heating gases from above 8oo ° C can be used. The heat gradient is caused by these high temperatures the heating gases increased considerably compared to the temperature of the smoldering material, so that the The smoldering time is shortened to a few seconds.

Claims (1)

PATENTANrrtPIZUCFI: Verfahren zum Schwelen von feinkörnigen oder staubfQrmigen bituminösen Stoffen, die im Heizgas schwebend erhalten werden, dadurch gekennzeichnet, daß der Wärmegrad der Verblasegase, die das Gut durch den Heizraum tragen, beim Beginn der Schwelung oberhalb 8oo ° C liegt.PATENTANrrtPIZUCFI: Process for smoldering fine-grained or dusty bituminous substances that are obtained floating in the heating gas, characterized in that that the degree of warmth of the blown gases that carry the goods through the boiler room The beginning of the swelling is above 800 ° C.
DET30936D 1924-03-18 1924-03-18 Process for smoldering fine-grained or dusty bituminous substances Expired DE515911C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DET30936D DE515911C (en) 1924-03-18 1924-03-18 Process for smoldering fine-grained or dusty bituminous substances

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DET30936D DE515911C (en) 1924-03-18 1924-03-18 Process for smoldering fine-grained or dusty bituminous substances

Publications (1)

Publication Number Publication Date
DE515911C true DE515911C (en) 1931-01-15

Family

ID=7555949

Family Applications (1)

Application Number Title Priority Date Filing Date
DET30936D Expired DE515911C (en) 1924-03-18 1924-03-18 Process for smoldering fine-grained or dusty bituminous substances

Country Status (1)

Country Link
DE (1) DE515911C (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1106289B (en) * 1954-02-20 1961-05-10 Steinmueller Gmbh L & C Method and device for degassing coal dust
DE1106290B (en) * 1954-02-20 1961-05-10 Steinmueller Gmbh L & C Process for degassing coal dust

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1106289B (en) * 1954-02-20 1961-05-10 Steinmueller Gmbh L & C Method and device for degassing coal dust
DE1106290B (en) * 1954-02-20 1961-05-10 Steinmueller Gmbh L & C Process for degassing coal dust

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