AT7325B - Process for the production of tannin extract from sulphite cellulose liquors. - Google Patents
Process for the production of tannin extract from sulphite cellulose liquors.Info
- Publication number
- AT7325B AT7325B AT7325DA AT7325B AT 7325 B AT7325 B AT 7325B AT 7325D A AT7325D A AT 7325DA AT 7325 B AT7325 B AT 7325B
- Authority
- AT
- Austria
- Prior art keywords
- production
- tannin extract
- sulphite cellulose
- acid
- desc
- Prior art date
Links
- 239000000284 extract Substances 0.000 title claims description 3
- 238000000034 method Methods 0.000 title claims description 3
- 238000004519 manufacturing process Methods 0.000 title description 2
- 235000018553 tannin Nutrition 0.000 title description 2
- 229920001864 tannin Polymers 0.000 title description 2
- 239000001648 tannin Substances 0.000 title description 2
- 229920002678 cellulose Polymers 0.000 title 1
- 239000001913 cellulose Substances 0.000 title 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 title 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 4
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 4
- 238000001704 evaporation Methods 0.000 claims description 4
- 239000004571 lime Substances 0.000 claims description 4
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 claims description 3
- 230000008020 evaporation Effects 0.000 claims description 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims 1
- 238000000354 decomposition reaction Methods 0.000 claims 1
- 238000001556 precipitation Methods 0.000 claims 1
- 229910021653 sulphate ion Inorganic materials 0.000 claims 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- 239000002253 acid Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 241000272476 Gyps Species 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000007524 organic acids Chemical group 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000003891 oxalate salts Chemical class 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Description
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der gebundenen schweigen Säure und Essigsäure erforderlich erscheint, dann wird durch längere Zeit, etwa eine Stunde lang, bei gewöhnlicher Temperatur, eventuell unter Kühlung damit die Temperatur von 300 C nicht überschritten wird, ausgerührt.
Wesentlich erscheint hiebei, dass der Säurezusatz ausreichen muss, die gebundene schweflige Säure und Essigsäure möglichst vollständig freizumachen.
Naturgemäss kann man den Säurezusatz entsprechend vergrössern, wenn man den übrigen gelösten, zumeist an organische Säuren gebundenen Kalk unlöslich ausfällen will ; aber dieser letztere Zweck lässt sich auch durch Anwendung von löslichen Salzen, wie Sulfaten, Phosphaten, Oxalaten etc., die durch Wechselumsetzung unlösliche Kalkverbindungen liefern, erreichen.
Nach dem Ausrühren wird der ausgeschiedene, krystallinische Gyps mittelst Filter- pressen oder ähnlichen Vorrichtungen getrennt und die Flüssigkeit hierauf in Vacuumapparaten in einer oder mehreren Phasen bis zur gewünschten Concentration eingedampft.
Arbeitet man in einer Phase, dann macht sich die Abscheidung des krystallinischen Gypses bei fortschreitender Concentration durch starkes Stossen der Flüssigkeit und intensives Inkrustieren der Heizröhren sehr unangenehm bemerkbar ; es empfiehlt sich daher die Concentration mindestens in zwei Phasen zu bewerkstelligen, indem man zunächst angenähert auf die Dichte von 16-180 Beaumé eindampft, den ausgeschiedenen Gyps mittels Filterpressen trennt und hierauf das weitere Verkochen der Flüssigkeit im Vacuum auf die Endconcentration fortsetzt.
PATENT-AKSPRÜCHE :
1. Verfahren zur Gewinnung von Gerbstoff-Extracten mit 28-30p Beaumé aus Sulfit-Oelluloselaugen durch Eindampfen im Vacuum in einer oder mehreren Phasen. dadurch gekennzeichnet, dass diese Lauge vor ihrer Eindampfung mit Zinkstaub und mindestens soviel Schwefelsäure oder einer anderen stärkeren Säure, als zum Freimachen der in den Laugen enthaltenen gebundenen schwefligen Säure und Essigsäure erforderlich ist unter längerem Ausrühren behandelt werden.
**WARNUNG** Ende DESC Feld kannt Anfang CLMS uberlappen**.
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the bound silent acid and acetic acid appear necessary, then it is stirred for a long time, about an hour, at ordinary temperature, possibly with cooling so that the temperature of 300 ° C. is not exceeded.
It appears essential here that the addition of acid must be sufficient to liberate the bound sulfurous acid and acetic acid as completely as possible.
Naturally, you can increase the acid addition accordingly if you want to insoluble precipitate the remaining dissolved lime, which is mostly bound to organic acids; but this latter purpose can also be achieved by using soluble salts, such as sulfates, phosphates, oxalates, etc., which, through alternating conversion, yield insoluble lime compounds.
After stirring, the precipitated, crystalline gypsum is separated by means of filter presses or similar devices and the liquid is then evaporated in vacuum apparatus in one or more phases to the desired concentration.
If one works in one phase, then the deposition of the crystalline gypsum makes itself very unpleasantly noticeable as the concentration progresses through strong pushing of the liquid and intensive incrustation of the heating tubes; It is therefore advisable to achieve the concentration in at least two phases by first evaporating to a density of 16-180 Beaumé, separating the excreted gyps using filter presses and then continuing to boil the liquid in a vacuum to the final concentration.
PATENT CLAIMS:
1. Process for the production of tannin extracts with 28-30p Beaumé from sulphite-oil-liquor by evaporation in a vacuum in one or more phases. characterized in that this lye, prior to its evaporation, is treated with zinc dust and at least as much sulfuric acid or another stronger acid as is required to free the bound sulfurous acid and acetic acid contained in the lyes, with prolonged stirring.
** WARNING ** End of DESC field may overlap beginning of CLMS **.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT7325T | 1901-06-25 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT7325B true AT7325B (en) | 1902-04-25 |
Family
ID=3498334
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT7325D AT7325B (en) | 1901-06-25 | 1901-06-25 | Process for the production of tannin extract from sulphite cellulose liquors. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT7325B (en) |
-
1901
- 1901-06-25 AT AT7325D patent/AT7325B/en active
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