DE405058C - Process for the recovery of the amount of liquid and gas escaping from pulp digesters - Google Patents
Process for the recovery of the amount of liquid and gas escaping from pulp digestersInfo
- Publication number
- DE405058C DE405058C DEA40956D DEA0040956D DE405058C DE 405058 C DE405058 C DE 405058C DE A40956 D DEA40956 D DE A40956D DE A0040956 D DEA0040956 D DE A0040956D DE 405058 C DE405058 C DE 405058C
- Authority
- DE
- Germany
- Prior art keywords
- liquid
- recovery
- amount
- gas escaping
- pulp digesters
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C11/00—Regeneration of pulp liquors or effluent waste waters
- D21C11/06—Treatment of pulp gases; Recovery of the heat content of the gases; Treatment of gases arising from various sources in pulp and paper mills; Regeneration of gaseous SO2, e.g. arising from liquors containing sulfur compounds
Landscapes
- Paper (AREA)
Description
Verfahren zur Wiedergewinnung der beim Abgasen von Zellstoffkochern übertretenden Flüssigkeits- und Gasmengen. Es ist bekannt, die schweflige Säure und den Wärmeinhalt der Kocherabgase dadurch nutzbar zu machen, daß man die Abgase in geschlossene Druckbehälter einleitet, die mit einer wässerigen Lösung von doppelschwefelsaurem Kalk beschickt sind, von der die Gase aufgenommen werden. Diese mit SO. angereicherte Lauge wird dann in warmem Zustand zur Füllung neuer Kocher verwendet.Process for the recovery of waste gas from pulp digesters Overflowing liquid and gas quantities. It is known to have sulphurous acid and to make the heat content of the cooker exhaust gases usable by the fact that the exhaust gases in closed pressure vessel, which is filled with an aqueous solution of double sulfuric acid Lime are charged, from which the gases are absorbed. This with SO. enriched Lye is then used in a warm state to fill new cookers.
Nach dem neuen Verfahren werden dagegen die Abgase unter Ersparung aller Zwischenbehälter unmittelbar in einen anderen unter vollem Betriebsdruck stehenden Zellstoffkocher übergeführt. Zu diesem Zweck werden sie mittels Pumpe, Injektor oder durch ein anderes Beförderungsmittel in den zweiten Kocher gedrückt und dadurch sowohl Säuregehalt als Wärmeinhalt unmittelbar verwertet.According to the new process, on the other hand, the exhaust gases are reduced all intermediate containers directly into another one under full operating pressure Pulp digester transferred. For this purpose, they are pumped, injected or pushed into and through the second digester by some other means of conveyance both acidity and heat content are used directly.
Hat man auch früher schon aus Zellstoffkochern entweichende schwefligsaure Dämpfe unmittelbar einem zweiten Kocher zugeführt, so war doch der zweite Kocher in diesen. Fällen entweder gar nicht angeheizt, oder er stand nicht unter vollem Kochdruck. Infolgedessen war man in der Ausnutzung der Anlage beschränkt, während bei dem neuen Verfahren der zweite in Betracht kommende Kocher unter vollem Betriebsdruck steht. Die Kosten für einen oder mehrere geschlossene Zwischenbehälter werden damit erspart.Sulfuric acid escaping from cellulose digesters has also been found in the past If vapors were fed directly to a second cooker, that was the second cooker in these. Cases either not fueled at all or he was not under full Cooking pressure. As a result, one was limited in the use of the facility while in the new process the second digester under consideration under full operating pressure stands. The costs for one or more closed intermediate containers are thus saved.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEA40956D DE405058C (en) | 1923-11-09 | 1923-11-09 | Process for the recovery of the amount of liquid and gas escaping from pulp digesters |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEA40956D DE405058C (en) | 1923-11-09 | 1923-11-09 | Process for the recovery of the amount of liquid and gas escaping from pulp digesters |
Publications (1)
Publication Number | Publication Date |
---|---|
DE405058C true DE405058C (en) | 1924-10-24 |
Family
ID=6932247
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEA40956D Expired DE405058C (en) | 1923-11-09 | 1923-11-09 | Process for the recovery of the amount of liquid and gas escaping from pulp digesters |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE405058C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1089256B (en) * | 1953-05-07 | 1960-09-15 | Gustaf Haglund | Process and plant for the production of cellulose by boiling wood with bisulfite liquor |
-
1923
- 1923-11-09 DE DEA40956D patent/DE405058C/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1089256B (en) * | 1953-05-07 | 1960-09-15 | Gustaf Haglund | Process and plant for the production of cellulose by boiling wood with bisulfite liquor |
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