AT55446B - Process for the recovery of the sodium salts in the form of bicarbonate in black liquors from the soda cellulose production, which have been freed from organic substances which can be precipitated with carbon dioxide. - Google Patents
Process for the recovery of the sodium salts in the form of bicarbonate in black liquors from the soda cellulose production, which have been freed from organic substances which can be precipitated with carbon dioxide.Info
- Publication number
- AT55446B AT55446B AT55446DA AT55446B AT 55446 B AT55446 B AT 55446B AT 55446D A AT55446D A AT 55446DA AT 55446 B AT55446 B AT 55446B
- Authority
- AT
- Austria
- Prior art keywords
- bicarbonate
- freed
- precipitated
- recovery
- carbon dioxide
- Prior art date
Links
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 title claims description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title description 7
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 title description 6
- 238000000034 method Methods 0.000 title description 5
- 239000000126 substance Substances 0.000 title description 5
- 239000001569 carbon dioxide Substances 0.000 title description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 title description 3
- 239000001913 cellulose Substances 0.000 title description 3
- 229920002678 cellulose Polymers 0.000 title description 3
- 238000011084 recovery Methods 0.000 title description 3
- 238000004519 manufacturing process Methods 0.000 title description 2
- 159000000000 sodium salts Chemical class 0.000 title description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 6
- 150000003839 salts Chemical class 0.000 claims description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 3
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 3
- 229910021529 ammonia Inorganic materials 0.000 claims description 3
- 239000004571 lime Substances 0.000 claims description 3
- 150000007524 organic acids Chemical group 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 claims description 2
- RSWGJHLUYNHPMX-UHFFFAOYSA-N 1,4a-dimethyl-7-propan-2-yl-2,3,4,4b,5,6,10,10a-octahydrophenanthrene-1-carboxylic acid Chemical compound C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims 1
- 239000000706 filtrate Substances 0.000 claims 1
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 6
- 235000002639 sodium chloride Nutrition 0.000 description 5
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 3
- GBAOBIBJACZTNA-UHFFFAOYSA-L calcium sulfite Chemical compound [Ca+2].[O-]S([O-])=O GBAOBIBJACZTNA-UHFFFAOYSA-L 0.000 description 3
- 235000010261 calcium sulphite Nutrition 0.000 description 3
- 239000004310 lactic acid Substances 0.000 description 3
- 235000014655 lactic acid Nutrition 0.000 description 3
- 238000000197 pyrolysis Methods 0.000 description 3
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 3
- 229910001948 sodium oxide Inorganic materials 0.000 description 3
- 239000006188 syrup Substances 0.000 description 3
- 235000020357 syrup Nutrition 0.000 description 3
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 235000019253 formic acid Nutrition 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000000052 vinegar Substances 0.000 description 2
- 235000021419 vinegar Nutrition 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000004295 calcium sulphite Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
Description
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Natürlich kann man auch nach Konzentrieren der ganzen Lösung dieselbe der trockenen Destillation unterziehen, und zwar mit oder ohne Zusatz von Kalk und in Gegenwart oder Abwesenheit von überhitztem Wasserdampf, wobei Alkohol, Azeton usw. in Mischung gewonnen wird. Die Lösung kann auch zur Freimachung der organischen Säuren durch stärkere Säuren sauer gemacht werden. Unter den letzteren ist zweckmässig erst Schwefeldioxyd zu verwenden, durch welches etwa die Hälfte der ganzen Menge Kalk als unlösliches Kalziumsulfit gefällt wird. Die Reaktion findet am besten bei erhöhter Temperatur statt, um die Bildung von saurem Kalziumsulfit zu vermeiden. Hiedurch wird der Essig freigemacht und kann, wenn erwünscht, direkt abdestilliert werden.
Wenn der Essig abdestilliert worden ist, kann die Ameisensäure durch eine stärkere Säure, wie z. B. Schwefelsäure, freigemacht und dann abdestilliert werden.
Ein anderer Weg des Verfahrens besteht darin, erst das Kalziumsulfit zu entfernen und
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Die sirupartigen Stoffe können dann durch Filtrieren oder Pressen mit oder ohne Zusatz von Wasser oder einem anderen geeigneten Lösungsmittel direkt von der Salzmenge abgeschieden werden. Der so erhaltene Sirup kann durch trockene Destillation weiter verarbeitet werden.
Wenn erwünscht, können die Kaliumsalze der sirupartigen Stoffe bereits vor dem Abdestillieren der Ameisensäure einer solchen trockenen Destillation unterzogen werden. Wenn die sirupartigen
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werden, wodurch der Sirup gezwungen wird, Wasser und Kohlensäure abzugeben und in eine harzartige Form überzugehen ; dieses gilt indessen nicht von der Milchsäure, die ein in Wasser schwerlösliches Anhydrid bildet. Der so verharzte Sirup kann durch Waschen mit zweckmässig erwärmtem Wasser unter Druck von der Salzmenge und der Milchsäure freigemacht werden, wobei die Salze und die Milchsäure gelöst werden und verwertet werden können, während das Harz ungelöst bleibt.
Beim Fällen von Natriumbikarbonat muss selbstverständlich darauf geachtet
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Verfahrens zum Regenerieren von Natriumkarbonat aus Schwarzlaugen soll dasselbe natürlich gleichzeitig direkt auf neue Mengen Kochsalz verwendet werden, um gleichzeitig zur Deckung aller Verluste von Natriumoxyd beim Kochen zellulosehaltiger Stoffe eine wohlfeile Lösung von Natriumkarbona t herzustellen.
In allen Operationen, die in diesem Prozesse zur Wiedergewinnung von Natriumoxyd aus Schwarzlauge oder zur gleichzeitigen Gewinnung von Natriumoxyd aus Natriumchlorid aus-
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PATENT-ANSPRÜCHE :
1. Verfahren zur Gewinnung der in Schwarzlaugen der Natronzellulosefabrikation, die von mit Kohlensäure fällbaren organischen Stoffen befreit worden sind, befindlichen Natriumsalze in der Form von Bikarbonat, dadurch gekennzeichnet, dass die Lauge bei zur Fällung von Bikarbonat geeigneter Temperatur (20 bis 400 C) mit Ammoniak und Kohlensäure behandelt wird.
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Of course, after the whole solution has been concentrated, it can also be subjected to dry distillation, with or without the addition of lime and in the presence or absence of superheated steam, with alcohol, acetone, etc. being obtained as a mixture. The solution can also be made acidic with stronger acids to liberate the organic acids. Among the latter, it is advisable to use sulfur dioxide first, through which about half of the total amount of lime is precipitated as insoluble calcium sulphite. The reaction is best done at an elevated temperature to avoid the formation of acidic calcium sulfite. This frees the vinegar and can, if desired, be distilled off directly.
When the vinegar has been distilled off, the formic acid can be replaced by a stronger acid such as. B. sulfuric acid, cleared and then distilled off.
Another way of the process is to first remove the calcium sulfite and
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The syrupy substances can then be separated off directly from the amount of salt by filtering or pressing with or without the addition of water or another suitable solvent. The syrup obtained in this way can be processed further by dry distillation.
If desired, the potassium salts of the syrupy substances can be subjected to such a dry distillation even before the formic acid is distilled off. When the syrupy
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which forces the syrup to give off water and carbonic acid and turn into a resinous form; However, this does not apply to lactic acid, which forms an anhydride that is sparingly soluble in water. The syrup resinified in this way can be freed from the amount of salt and lactic acid by washing it with appropriately heated water under pressure, whereby the salts and lactic acid can be dissolved and utilized while the resin remains undissolved.
Of course, care must be taken when felling sodium bicarbonate
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The process for regenerating sodium carbonate from black liquors should of course be used at the same time directly on new quantities of table salt, in order to simultaneously produce an inexpensive solution of sodium carbonate to cover all losses of sodium oxide when boiling cellulose-containing substances.
In all operations involved in this process for the recovery of sodium oxide from black liquor or for the simultaneous recovery of sodium oxide from sodium chloride
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PATENT CLAIMS:
1. A method for obtaining the sodium salts in the form of bicarbonate in black liquors from the soda cellulose production, which have been freed from organic substances that can be precipitated with carbon dioxide, characterized in that the liquor at a temperature suitable for precipitation of bicarbonate (20 to 400 C) with Ammonia and carbon dioxide is treated.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE55446X | 1910-02-14 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT55446B true AT55446B (en) | 1912-09-25 |
Family
ID=20266702
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT55446D AT55446B (en) | 1910-02-14 | 1911-02-11 | Process for the recovery of the sodium salts in the form of bicarbonate in black liquors from the soda cellulose production, which have been freed from organic substances which can be precipitated with carbon dioxide. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT55446B (en) |
-
1911
- 1911-02-11 AT AT55446D patent/AT55446B/en active
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