AT34348B - Process for the production of ammonia from organic nitrogenous substances by fermentation. - Google Patents

Process for the production of ammonia from organic nitrogenous substances by fermentation.

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Publication number
AT34348B
AT34348B AT34348DA AT34348B AT 34348 B AT34348 B AT 34348B AT 34348D A AT34348D A AT 34348DA AT 34348 B AT34348 B AT 34348B
Authority
AT
Austria
Prior art keywords
fermentation
ammonia
production
butyric acid
organic nitrogenous
Prior art date
Application number
Other languages
German (de)
Inventor
Jean Dr Effront
Original Assignee
Jean Dr Effront
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 Jean Dr Effront filed Critical Jean Dr Effront
Application granted granted Critical
Publication of AT34348B publication Critical patent/AT34348B/en

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Description

  

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   In diesem Fall soU für die erste Kultur die zugesetzte Menge von Hefeextrakt po berechnet werden, dass dadurch 0.1-0.2 g Gesamtstickstoff in jeden Liter Flüssigkeit hineingebracht wird. 



  [n den folgenden Operationen werden die Dosen von Hefenextrakt allmählich erhöht, bis man ichliesslich ein Verhältnis von 4-6 9 Stickstoff pro Liter erreicht. 



  Die Akklimatisation kann auch, obwohl nicht so leicht durch sukzessive Züchtungen in   
 EMI2.1 
 



   Die auf eine dieser Arten akklimatisierten Buttersäurebakterien lassen sich leicht in   Brennereischlempe (Melassen, Rüben, Getreide, Kartoffel usw. ), sowie in die Abfälle der Zucker-   fabrikation einführen. Man erzielt bei dieser Gärung neben einer ansehnlichen Ausbeute an Buttersäure auch eine   Überführung   von über 90% des Gesamtstickstoffes in Ammoniak. 



   Zur praktischen   Ausführung   des Verfahrens mit Melassenschlempe. empfiehlt es sich auf folgende Weise vorzugehen :
Die Melassenschlempe (Rückstand der Destillation) wird auf die Dichte von 6-70 Ball. 
 EMI2.2 
 reichen ; nach Zugabe von 20-50   9   Superphosphat und 30-60   9   Aluminiumsulfat pro Hektoliter, wird diese Schlempe auf die Temperatur von   38-420 ('gebracht   und der   Buttersäuregärung   unterworfen. 



   Das Anstellen der Schlempe wird vorzugsweise mit schon zu Amiden akklimatisierten Buttersäurefermenten ausgeführt. Während der ersten 24 Stunden wird Luft durch die Masse geführt, wobei während der ganzen Zeit die Alkalinität der   Flüssigkeit   stets zwischen 1. 5-2 g pro Liter zu halten ist. Unter guten Verhältnissen dauert die Gärung etwa drei Tage.

   Lässt man vom Moment, wo'90% des Stickstoffes in Ammoniak   übergegangen sind.   die Gärung noch   4-5 Stunden   weiter gehen, so erhält mau das Maximum der Ausbeute. 
 EMI2.3 
 Anstellen der Gärung in der folgenden Operation aufbewahrt ; der restliche Teil der   abgegorenen   Flüssigkeit wird mit 2-3   9 Hchlempekohle   pro Liter versetzt und der Destillation unterworfen, um das Ammoniak zu trennen, welches dann auf bekanntem Wege aufgefangen und verwertet wird. 
 EMI2.4 
 Kalk anstatt der rohen Schlempekohle angewandt. 



   Bei der Verarbeitung der Getreideschlempe empfiehlt es sich, die aus den   DestiUierapparaten     kommende   Schlempe durch Filterpressen zu filtrieren, um die Treber zu trennen. Die aus den 
 EMI2.5 
   schlempe.   



   Bei der   Trennung   des Ammoniaks aus derartig behandelten Schlempen und besonders aus den Getreide- und Rübenschlempen sind sehr günstige Resultate erreicht worden durch den   sogenannten..     Kestnerschen   Atomisator", einen Apparat. welcher wegen des in demselben entstehenden Luftzuges das   Ammoniak gut aus der Flüssigkeit   treibt. 
 EMI2.6 
 mässig geringer ist. denn es gehen nur   45-50%   des Gesamtstickstoffes in Ammoniak über. 



   Die Erhöhung der Ausbeute ist jedoch durch eine besondere Vorbehandlung der von den Trebern befreiten Schlempe möglich ; vorzugsweise verfährt man wie folgt :   Die nitrierte Schlempe wird   bei einer Temperatur von 400 C mit   Bierhefe im Verhältnis   
 EMI2.7 
 

**WARNUNG** Ende DESC Feld kannt Anfang CLMS uberlappen**.



   <Desc / Clms Page number 1>
 
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   In this case, the added amount of yeast extract po for the first culture should be calculated by bringing 0.1-0.2 g total nitrogen into each liter of liquid.



  In the following operations the doses of yeast extract are gradually increased until a ratio of 4-6 9 nitrogen per liter is finally achieved.



  Acclimatization can also, although not so easily, through successive breeding in
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   The butyric acid bacteria acclimatized in one of these ways can easily be introduced into distillery mash (molasses, beets, grain, potatoes, etc.), as well as into the waste from sugar production. This fermentation not only achieves a substantial yield of butyric acid, but also converts over 90% of the total nitrogen into ammonia.



   For the practical execution of the process with molasses stillage. it is recommended to proceed in the following way:
The molasses liquor (residue of the distillation) is adjusted to a density of 6-70 ball.
 EMI2.2
 pass ; After adding 20-50 9 superphosphate and 30-60 9 aluminum sulfate per hectolitre, this stillage is brought to a temperature of 38-420 ('and subjected to butyric acid fermentation.



   The vinasse is preferably made with butyric acid ferments that have already acclimated to amides. During the first 24 hours, air is passed through the mass, the alkalinity of the liquid must always be kept between 1.5-2 g per liter during the entire time. In good conditions, fermentation takes about three days.

   Leaving aside the moment when 90% of the nitrogen has been converted into ammonia. the fermentation go on for 4-5 hours, so the maximum yield is obtained.
 EMI2.3
 Instead of fermentation kept in the following operation; The remaining part of the fermented liquid is mixed with 2-3 9 Hchlempekohle per liter and subjected to distillation in order to separate the ammonia, which is then collected and used in a known way.
 EMI2.4
 Lime used instead of raw coal.



   When processing the grain mash, it is advisable to filter the mash from the stills through filter presses in order to separate the spent grains. The ones from the
 EMI2.5
   stillage.



   In the separation of ammonia from such treated liquors, and especially from grain and beet liquors, very favorable results have been achieved by the so-called "Kestner atomizer", an apparatus which drives the ammonia well out of the liquid because of the draft in it.
 EMI2.6
 is moderately lower. because only 45-50% of the total nitrogen is converted into ammonia.



   However, the yield can be increased by a special pretreatment of the stillage freed from the spent grains; The preferred procedure is as follows: The nitrated stillage is mixed with brewer's yeast at a temperature of 400 C.
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** WARNING ** End of DESC field may overlap beginning of CLMS **.

 

Claims (1)

PATENT-ANSPRUCEE : l. Verfahren zur Gewinnung von Ammoniak aus organischen stickstoffhaltigen Stoffen. gekennzeichnet durch deren Vergärung mittels Buttersäurefermenten. <Desc/Clms Page number 3> PATENT CLAIMS: l. Process for the production of ammonia from organic nitrogenous substances. characterized by their fermentation using butyric ferments. <Desc / Clms Page number 3> 2. Zur Ausführung des im Anspruch 1 gekennzeichneten Verfahrens bei Behandlung von Brennereischlempe oder Rückständen der Zuckerfabrikation die Durchführung der Buttersäure- gärung bei einer konstanten Alkalinität, entsprechend 1-2 9 Na OH pro Liter. 2. To carry out the method characterized in claim 1 when treating distillery mash or residues from sugar production, the butyric acid fermentation is carried out at a constant alkalinity, corresponding to 1-2 9 Na OH per liter. 3. Zur Ausführung des im Anspruch l gekennzeichneten Verfahrens, die Akklimatisation der Buttersäurefermente an amidhaltige Stoffe, in der Weise, dass die Buttersäuregärung in Gegenwart von allmählich gesteigerten Mengen von Amiden, wie Glutaminsäure, Asparagin oder dg). oder von Produkten der Selbstverdauung der Hefe durchgeführt wird. 3. To carry out the process characterized in claim l, the acclimatization of the butyric acid ferments to amide-containing substances in such a way that the butyric acid fermentation in the presence of gradually increased amounts of amides, such as glutamic acid, asparagine or dg). or by products of the self-digestion of yeast.
AT34348D 1907-09-12 1907-09-12 Process for the production of ammonia from organic nitrogenous substances by fermentation. AT34348B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT34348T 1907-09-12

Publications (1)

Publication Number Publication Date
AT34348B true AT34348B (en) 1908-09-10

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Family Applications (1)

Application Number Title Priority Date Filing Date
AT34348D AT34348B (en) 1907-09-12 1907-09-12 Process for the production of ammonia from organic nitrogenous substances by fermentation.

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AT (1) AT34348B (en)

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