AT92474B - Process for pretreating the sulphite liquor for fermentation. - Google Patents
Process for pretreating the sulphite liquor for fermentation.Info
- Publication number
- AT92474B AT92474B AT92474DA AT92474B AT 92474 B AT92474 B AT 92474B AT 92474D A AT92474D A AT 92474DA AT 92474 B AT92474 B AT 92474B
- Authority
- AT
- Austria
- Prior art keywords
- fermentation
- acid
- waste liquor
- pretreating
- liquor
- Prior art date
Links
- 238000000855 fermentation Methods 0.000 title claims description 8
- 230000004151 fermentation Effects 0.000 title claims description 8
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 title claims description 6
- 238000000034 method Methods 0.000 title claims description 5
- 239000002699 waste material Substances 0.000 claims description 10
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 8
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 claims description 6
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 4
- 230000002378 acidificating effect Effects 0.000 claims description 4
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 4
- 239000001099 ammonium carbonate Substances 0.000 claims description 4
- 235000012501 ammonium carbonate Nutrition 0.000 claims description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 2
- 150000008043 acidic salts Chemical class 0.000 claims 1
- 230000007935 neutral effect Effects 0.000 claims 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 229910019142 PO4 Inorganic materials 0.000 description 5
- 235000021317 phosphate Nutrition 0.000 description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 3
- 235000011941 Tilia x europaea Nutrition 0.000 description 3
- 239000004571 lime Substances 0.000 description 3
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229940043430 calcium compound Drugs 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- -1 sulphonic acid calcium compounds Chemical class 0.000 description 2
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 description 1
- 239000004254 Ammonium phosphate Substances 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 235000012538 ammonium bicarbonate Nutrition 0.000 description 1
- 229910000148 ammonium phosphate Inorganic materials 0.000 description 1
- 235000019289 ammonium phosphates Nutrition 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 239000001166 ammonium sulphate Substances 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 159000000007 calcium salts Chemical class 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
- 238000000354 decomposition reaction Methods 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 239000002426 superphosphate Substances 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Fertilizers (AREA)
- Removal Of Specific Substances (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Description
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Verfahren zur Vorbehandlung der Sulfitablauge für die Vergärung.
Bei den bisher gebräuchlichen Aufbereitungsverfahren der Sulfitablauge für Zwecke der Vergärung des in ihr enthaltenen Zuckers zu Alkohol wurde die vorhandene freie Säure bekanntlich mit Kalk abgestumpft, wodurch grosse Mengen von wertlosem Gips entstanden, dessen Aussüssen und Beseitigung oft grosse Schwierigkeiten macht.
Da überdies nach der solcherart erfolgten Entfernung der freien Säure noch beträchtliche Mengen von organischen sulfensauren Kalziumverbindungen in den Ablaugen enthalten bleiben, die bei der Weiterverarbeitung der letzteren freie schweflige Säure abspalten, so wurden diese organischen Verbindungen vielfach durch Versetzen der Ablaugen mit Salzsäure, Schwefelsäure oder mit geeigneten organischen Säuren zersetzt und die hiebei frei gewordene schweflige Säure wieder mit Kalk neutralisiert, wodurch eine neuerliche unerwünschte Vermehrung an Kalziumsalzen
EMI1.1
in der Ablauge verbleiben und dann die Gärung gewiss nicht fördern, oder aber-wenn sie unlöslich sind - ihrerseits wieder die Bildung grosser Mengen von lästigen Niederschlägen veranlassen.
Die Erfindung betrifft nun ein Verfahren zur Aufbereitung von Sulfitablauge für die Vergärung, welche die genannten Nachteile dadurch vermeidet, dass die in der Ablauge enthaltenen organischen sulfensauren Verbindungen mittels Phosphorsäure oder saurer Phosphate zersetzt werden und die so behandelte Ablauge zwecks Austreibens sowohl der in Freiheit gesetzten, als auch der schon vorhanden gewesene freien schwefligen Säure unter gleichzeitiger Konzentrierung der Einwirkung von Wärme ausgesetzt wird.
Die praktisch schwefligsäurefrei gewordene Ablauge wird schliesslich zweckmässig mittels Ammonkarbonats oder Ammonbikarbonats neutralisiert, wobei etwa vorhandene freie Schwefelsäure die Bildung von Ammonsulfat veranlasst, während vorhandene Phosphorsäure oder Phosphate Ammonphosphat geben, beides höchst wertvolle Hefel1ährstoffe, die den Verlauf der nachher durchzuführenden Vergärung auf das günstigste beeinflussen. Die bei der Zersetzung der organischen sulfensauren Kalziumverbindungen mittels Phosphorsäure oder saurer Phosphate niederfallende Kalziumphosphatmenge ist ganz unvergleichlich geringer, als die beim blossen Neutralisieren der Ablauge mit Kalk nach vorhergehenden Lüften ausfallende Gipsmenge.
Weiters bietet der Phosphatniederschlag den Vorteil, dass er kristallinisch ist, sich dadurch leichter aussüssen lässt und überdies ein wertvolles Düngemittel darstellt.
Die praktische Durchführung des vorliegenden Verfahrens kann zweckmässig in nachstehender Weise erfolgen :
Die Sulfitablauge wird nach Verlassen des Kochers mit der erforderlichen Menge eines sauren Phosphates, z. B. gewöhnliches Superphosphat, in geringem Überschuss versetzt, sodann zwecks Verjagung der schwefligen Säure unter gleichzeitiger Konzentrierung der Lauge entsprechend erwärmt, was z. B. vorteilhaft unter Anwendung von Rieseltürmen erfolgen kann, durch welche die Lauge im Gegenstrom zu inerten heissen Gasen oder möglichst sauerstoffarmen heissen Gasgemischen hindurchgeschickt wird. Sobald die Lauge praktisch schwefligsäurefrei gemacht worden ist. erfolgt ihre Neutralisierung mit Ammonkarbonat, welcher man zweckmässig eine Lüftung der so behandelten Lauge in einem Rieselturm folgen lassen kann.
In der dann auf die Gärtemperatur gebrachten Lauge kann die Gärung mit akklimatisierten Heferassen sofort eingeleitet werden.
**WARNUNG** Ende DESC Feld kannt Anfang CLMS uberlappen**.
<Desc / Clms Page number 1>
Process for pretreating the sulphite liquor for fermentation.
In the previously customary processing methods of the sulphite waste liquor for the purpose of fermenting the sugar contained in it to alcohol, the free acid present was blunted with lime, which resulted in large amounts of worthless gypsum, which often caused great difficulties to be removed and removed.
Since, after the free acid has been removed in this way, the waste liquors still contain considerable amounts of organic sulphonic acid calcium compounds, which split off free sulphurous acid when the latter is further processed, so these organic compounds were often made by adding hydrochloric acid, sulfuric acid or with suitable organic acids are decomposed and the sulphurous acid which has been liberated is neutralized again with lime, which leads to a renewed and undesirable increase in calcium salts
EMI1.1
remain in the waste liquor and then certainly do not promote fermentation, or else - if they are insoluble - in turn cause the formation of large amounts of troublesome precipitates.
The invention now relates to a method for processing sulphite waste liquor for fermentation, which avoids the disadvantages mentioned by the fact that the organic sulphate compounds contained in the waste liquor are decomposed by means of phosphoric acid or acidic phosphates and the waste liquor treated in this way is used to drive off both the released, as well as the already existing free sulphurous acid is exposed to the action of heat with simultaneous concentration.
The waste liquor, which has become practically free of sulfuric acid, is finally neutralized using ammonium carbonate or ammonium bicarbonate, with any free sulfuric acid that may be present causing the formation of ammonium sulphate, while any phosphoric acid or phosphates that are present give ammonium phosphate, both of which are extremely valuable nutrients, which have the most favorable effect on the course of the subsequent fermentation. The amount of calcium phosphate precipitating during the decomposition of the organic sulphonate calcium compounds by means of phosphoric acid or acidic phosphates is incomparably less than the amount of gypsum that precipitates when the waste liquor is simply neutralized with lime after previous ventilation.
Furthermore, the phosphate precipitate has the advantage that it is crystalline, making it easier to drain and, moreover, it is a valuable fertilizer.
The practical implementation of the present procedure can expediently take place in the following manner:
The sulphite liquor is after leaving the digester with the required amount of an acidic phosphate, z. B. ordinary superphosphate, added in a small excess, then heated accordingly to drive away the sulfurous acid while concentrating the alkali, which z. B. can advantageously be carried out using trickle towers through which the liquor is sent in countercurrent to inert hot gases or as low-oxygen hot gas mixtures as possible. As soon as the lye has been made practically sulfurous acid-free. it is neutralized with ammonium carbonate, which can expediently be followed by aeration of the alkali treated in this way in a trickle tower.
In the lye, which is then brought to the fermentation temperature, fermentation can be started immediately with acclimated yeast races.
** WARNING ** End of DESC field may overlap beginning of CLMS **.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT92474T | 1921-08-22 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT92474B true AT92474B (en) | 1923-05-11 |
Family
ID=3612480
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT92474D AT92474B (en) | 1921-08-22 | 1921-08-22 | Process for pretreating the sulphite liquor for fermentation. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT92474B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE750578C (en) * | 1941-08-20 | 1945-01-23 | Ig Farbenindustrie Ag | Method for breeding yeast and yeast-like fungi in waste liquors from the digestion of cellulose-containing substances and their pulp |
-
1921
- 1921-08-22 AT AT92474D patent/AT92474B/en active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE750578C (en) * | 1941-08-20 | 1945-01-23 | Ig Farbenindustrie Ag | Method for breeding yeast and yeast-like fungi in waste liquors from the digestion of cellulose-containing substances and their pulp |
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