AT79018B - Process and device for the extraction of by-products in the production of mixed gas through the alternating action of oxygen and water vapor on all types of fuels. - Google Patents

Process and device for the extraction of by-products in the production of mixed gas through the alternating action of oxygen and water vapor on all types of fuels.

Info

Publication number
AT79018B
AT79018B AT79018DA AT79018B AT 79018 B AT79018 B AT 79018B AT 79018D A AT79018D A AT 79018DA AT 79018 B AT79018 B AT 79018B
Authority
AT
Austria
Prior art keywords
fuels
extraction
oxygen
water vapor
products
Prior art date
Application number
Other languages
German (de)
Inventor
Oskar Simmersbach
Friedrich Sommer
Original Assignee
Oskar Simmersbach
Friedrich Sommer
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 Oskar Simmersbach, Friedrich Sommer filed Critical Oskar Simmersbach
Application granted granted Critical
Publication of AT79018B publication Critical patent/AT79018B/en

Links

Description

  

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   dationsp@@@@e erheblich   abgekürzt werden, wobei gleichzeitig ein stickstoffarmes, reiches Gas    entstehu.''an nderen   Gase kann man zusetzen, um sie zu beseitigen, z. B. Abgase der Ammoniakfabriken   odt.     u   sie zu regenerieren, z. B. Verbrennungsgase. 



   Endlich ist es möglich, dem Brennstoff vor der Vergasung Kalziumverbindungen zuzusetzen. 



  Dieser Zusatz wirkt dadurch erhöhend auf die Ammoniakausbeute, dass er btickstoffhaltige   Verbindungen unter Freiwerden von Ammoniak zersetzt oder die Zersetzung des Wasserdampfes unter Bildung chemisch wirksamen Wasserstoffes (in statu nascendi) befördert.   



    Auf der Zeichnung ist ein Ausführungsbeispiel eines für das "erfahren bestimmten Generators dargestellt. Der Generator hat zwei Zonen 1 und II, welche in der beschriebenen Weise abwechselnd mit Dampf und Luft behandelt werden. Die Grenzen der Zonen sind durch strichpunktierte Linien angedeutet. Der Generator a wird durch eine Bes@@@kungsvorrichtung b mit Brennstoff versorgt. Er hat eine Anzahl von Düsen c und d mit angeschlossenen Leitungen e und f, durch welche abwechselnd Dampf oder Luft zugeführt wird. Das erzeugte Gas entweicht   
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  Am Boden des Generators sitzt eine Haube   i zum   Austragen der Asche, welche durch eingeblasene kleine Dampfmengen gekühlt wird. Im Notfalle kann diese Haube auch zur   Zuführung   
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   müssen.   



     Zunächst   werden die beiden Zonen   1   und II mit Luft angeblasen, bis die ganze   Beschickung   gluh Dann bläst man durch die Düsen c an Stelle der Luft Dampf in die obere Zone II ein, wahrend die Luftzufuhr in der unteren   Zone I fortdauert.   Die Zone II erzeugt also jetzt Wasser- 
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 Temperatur Generatorgas erzeugt. Sobald der Stickstoffgehalt der Brennstoffoberfläche in   Zne II verbraucht   ist, leitet man durch die Düsen c Luft in die Zone   II,   während jetzt der Zene I durch die Düsen d Dampf zugeführt wird, so dass jetzt diese Wassergas und Ammomak. 



  (l'Zone II dagegen Generatorgas liefert. Die Gase ziehen gemeinsam durch die Öffnungen g   111 he Hauptleitung/t ab.   
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   dationsp @@@@ e can be shortened considerably, at the same time a nitrogen-poor, rich gas is produced. '' Other gases can be added to eliminate them, e.g. B. exhaust gases from ammonia factories odt. u to regenerate them, e.g. B. Combustion gases.



   It is finally possible to add calcium compounds to the fuel before gasification.



  This addition increases the ammonia yield by decomposing nitrogenous compounds with the release of ammonia or by promoting the decomposition of water vapor with the formation of chemically active hydrogen (in statu nascendi).



    The drawing shows an exemplary embodiment of a generator intended for the "experienced". The generator has two zones 1 and II, which are treated alternately with steam and air in the manner described. The boundaries of the zones are indicated by dot-dash lines. The generator a is supplied with fuel by a filling device B. It has a number of nozzles c and d with connected lines e and f, through which steam or air is alternately fed in. The gas produced escapes
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  At the bottom of the generator there is a hood i for discharging the ash, which is cooled by small amounts of steam blown in. In an emergency this hood can also be used for feeding
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   have to.



     First, the two zones 1 and II are blown with air until the entire charge is glowing.Then, instead of air, steam is blown into the upper zone II through the nozzles c, while the air supply in the lower zone I continues. Zone II is now generating water
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 Generated temperature generator gas. As soon as the nitrogen content of the fuel surface in Zne II is used up, air is passed through the nozzles c into zone II, while steam is now fed to zone I through the nozzles d, so that water gas and ammomak are now produced.



  (Zone II, on the other hand, supplies generator gas. The gases withdraw together through the openings g 111 he main line / t.
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AT79018D 1915-10-07 1917-01-11 Process and device for the extraction of by-products in the production of mixed gas through the alternating action of oxygen and water vapor on all types of fuels. AT79018B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE79018X 1915-10-07

Publications (1)

Publication Number Publication Date
AT79018B true AT79018B (en) 1919-11-10

Family

ID=5638451

Family Applications (1)

Application Number Title Priority Date Filing Date
AT79018D AT79018B (en) 1915-10-07 1917-01-11 Process and device for the extraction of by-products in the production of mixed gas through the alternating action of oxygen and water vapor on all types of fuels.

Country Status (1)

Country Link
AT (1) AT79018B (en)

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