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.Info
- 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
Links
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims description 16
- 238000000855 fermentation Methods 0.000 title claims description 9
- 230000004151 fermentation Effects 0.000 title claims description 9
- 229910021529 ammonia Inorganic materials 0.000 title claims description 8
- 238000000034 method Methods 0.000 title claims description 6
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- 239000000126 substance Substances 0.000 title claims 3
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 title claims 2
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 claims description 14
- 150000001408 amides Chemical class 0.000 claims description 3
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 2
- DCXYFEDJOCDNAF-UHFFFAOYSA-N Asparagine Natural products OC(=O)C(N)CC(N)=O DCXYFEDJOCDNAF-UHFFFAOYSA-N 0.000 claims 1
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 claims 1
- DCXYFEDJOCDNAF-REOHCLBHSA-N L-asparagine Chemical compound OC(=O)[C@@H](N)CC(N)=O DCXYFEDJOCDNAF-REOHCLBHSA-N 0.000 claims 1
- WHUUTDBJXJRKMK-VKHMYHEASA-N L-glutamic acid Chemical compound OC(=O)[C@@H](N)CCC(O)=O WHUUTDBJXJRKMK-VKHMYHEASA-N 0.000 claims 1
- 235000009582 asparagine Nutrition 0.000 claims 1
- 229960001230 asparagine Drugs 0.000 claims 1
- 239000006227 byproduct Substances 0.000 claims 1
- 235000013922 glutamic acid Nutrition 0.000 claims 1
- 239000004220 glutamic acid Substances 0.000 claims 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 235000013379 molasses Nutrition 0.000 description 3
- 235000016068 Berberis vulgaris Nutrition 0.000 description 2
- 241000335053 Beta vulgaris Species 0.000 description 2
- 229940041514 candida albicans extract Drugs 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 239000004458 spent grain Substances 0.000 description 2
- 239000012138 yeast extract Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- YYRMJZQKEFZXMX-UHFFFAOYSA-N calcium;phosphoric acid Chemical compound [Ca+2].OP(O)(O)=O.OP(O)(O)=O YYRMJZQKEFZXMX-UHFFFAOYSA-N 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 235000012015 potatoes Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002426 superphosphate Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
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**.
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EMI1.1
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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
EMI2.1
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.
EMI2.7
** WARNING ** End of DESC field may overlap beginning of CLMS **.
Claims (1)
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 |
Family
ID=3550454
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. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT34348B (en) |
-
1907
- 1907-09-12 AT AT34348D patent/AT34348B/en active
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