AT80445B - Process for removing odorous substances from Processes for removing odorous substances from waste gases from pulp production. s waste gases from pulp production. - Google Patents
Process for removing odorous substances from Processes for removing odorous substances from waste gases from pulp production. s waste gases from pulp production.Info
- Publication number
- AT80445B AT80445B AT80445DA AT80445B AT 80445 B AT80445 B AT 80445B AT 80445D A AT80445D A AT 80445DA AT 80445 B AT80445 B AT 80445B
- Authority
- AT
- Austria
- Prior art keywords
- odorous substances
- waste gases
- pulp production
- wood
- removing odorous
- Prior art date
Links
- 239000000126 substance Substances 0.000 title claims description 11
- 238000000034 method Methods 0.000 title claims description 5
- 238000004519 manufacturing process Methods 0.000 title description 6
- 239000002912 waste gas Substances 0.000 title description 4
- 239000002023 wood Substances 0.000 claims description 15
- 239000007789 gas Substances 0.000 claims description 14
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 9
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 4
- 239000000460 chlorine Substances 0.000 claims description 4
- 230000001590 oxidative effect Effects 0.000 claims description 4
- 229910052801 chlorine Inorganic materials 0.000 claims description 3
- 241000589614 Pseudomonas stutzeri Species 0.000 claims description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 239000007800 oxidant agent Substances 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 230000006378 damage Effects 0.000 description 3
- 235000019645 odor Nutrition 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical class S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 229910001902 chlorine oxide Inorganic materials 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000004868 gas analysis Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000035943 smell Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
Description
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Verfahren zur Beseitigung der riechenden Stoffe aus Abgasen der Zellstoff-Fabrikation.
In der Fabrikation von Holz-und Stroh-oder Espartozellstoff hat man zur Zerstörung der übelriechenden Gase oxydierende Mittel, wie wässrige Lösungen, z. B. von Chlorkalk oder Salpetersäure, ferner auch oxydierende Mittel in Gasform, wie z. B. Stickoxyde, vorgeschlagen.
Zu einer Lösung des für die Zellstoffabrikatioll hochwichtigen Geruchproblems haben diese Vorschläge nicht geführt. Vermutlich sind es der grosse Feuchtigkeitsgehalt der Abgase einerseits und die ausserordentlich grosse Verdünnung der Riechstoffe andrerseits, die eine glatte Oxydation
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von Wasserstoffspuren in kohlenoxyd-und methanhaltigen Gasen sich gestaltet, selbst wenn, wie in der Gasanalyse, ausserordentlich hoher Sauerstoffüberschuss vorhanden ist. Um die Oxydation der riechenden Stoffe in den Zellstoffabgasen zu erzwingen, erscheint es daher zweckmässig, die Geruchstoffe auf irgendeine Weise anzureichern und dann erst die Oxydation vorzunehmen.
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Gerüche an sich zu ziehen und festzuhalten. Nach Erreichung der Sättigungsgrenze kann das Holz z.
B. in einer Natronzellstoffabrik dem gewöhnlichen Kochgut beigegeben, in einer Strohzellstoffabrik durch Verbrennung unter dem Dampfkessel verwertet werden. Man kann aber auch durch Anwendung von geeigneten Oxydationsmitteln die vom Holz festgehaltenen riechenden Bestandteile zerstören und nach der Zerstörung das Holz o. dgl. wiederholt zur Adsorption von Gerüchen nutzbar machen.
Hat man beispielsweise die riechenden mercaptan-und sulfidhaltigen Abgase der Sulfatzellstoffabriken mittels Holzklein geruchlos gemacht, so kann die endgültige Zerstörung der
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bewirkt werden. Man kann auch diese oxydierenden Gase schon vor der Adsorption im Holz dem Abgasstrom beimengen. Für den Fall. dass der unter Umständen sehr hohe Wassergehalt der Abgase störend bei der Anreicherung und Oxydation der Riechstoffe wirkt, muss man das Wasser durch Kühlung der Abgase vor dem Überleiten über das Holz teilweise entfernen. Entsprechend den, dem Gewicht nach sehr geringen Mercaptanmengen genügen ausserordentlich kleine Mengen von Chlor oder Stickoxyden zur Oxydation der Mercaptane und Sulfide. Eine tief greifende Zerstörung der Holzsubstanz wird daher nicht herbeigeführt.
Ohnehin is an und für sich ein mit Chlor vorbehandeltes Holz für alkalischen Aufschluss gut geeignet. Derartiges chlorhaltiges Holz kann daher ohne weiters im Betrieb der Natronzellstoffabriken Verwendung zur Zellstoffherstellung finden, gegebenenfalls nachdem es mehrfach zur Geruchsbeseitigung gedient hat.
An Stelle der gasförmigen Oxydationsmittel kann man auch zur Zerstörung der im Holz aufgefangenen riechenden Stoffe wässrige Lösungen der oxydierenden Mittel anwenden.
PATENT-ANSPRÜCHE : i. Verfahren zur Beseitigung der riechenden Stoffe. aus Abgasen der Zellstoffabrikation, dadurch gekennzeichnet, dass man in den Strom der riechenden Gase zerkleinertes Holz, Sägemehl oder andere Abfälle pflanzlicher, holzartiger Natur einschaltet.
**WARNUNG** Ende DESC Feld kannt Anfang CLMS uberlappen**.
<Desc / Clms Page number 1>
Process for the elimination of odorous substances from exhaust gases from pulp production.
In the manufacture of wood and straw or esparto pulp, oxidizing agents such as aqueous solutions, e.g. B. of chlorinated lime or nitric acid, also oxidizing agents in gaseous form, such as. B. nitrogen oxides suggested.
These proposals have not led to a solution to the odor problem, which is very important for the pulp mill. Presumably it is the high moisture content of the exhaust gases on the one hand and the extraordinarily great dilution of the odorous substances on the other hand that causes a smooth oxidation
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traces of hydrogen in gases containing carbon oxide and methane arise even if, as in gas analysis, there is an extraordinarily high excess of oxygen. In order to force the oxidation of the odorous substances in the pulp waste gases, it therefore seems advisable to enrich the odorous substances in some way and only then to carry out the oxidation.
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To attract and hold smells. After reaching the saturation limit, the wood can z.
B. in a soda pulp factory added to the usual food, can be recovered in a straw pulp factory by incineration under the steam boiler. But you can also destroy the odorous constituents held by the wood by using suitable oxidizing agents and after the destruction make the wood or the like repeatedly usable for the adsorption of odors.
For example, if the odorous mercaptan and sulfide-containing exhaust gases from the sulfate pulp mills have been made odorless by means of small pieces of wood, the final destruction of the
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be effected. These oxidizing gases can also be added to the exhaust gas flow before they are adsorbed in the wood. In the case. Because the possibly very high water content of the exhaust gases has a disruptive effect on the enrichment and oxidation of the odorous substances, the water must be partially removed by cooling the exhaust gases before passing it over the wood. Corresponding to the very small amounts of mercaptans by weight, extremely small amounts of chlorine or nitrogen oxides are sufficient to oxidize the mercaptans and sulfides. A profound destruction of the wood substance is therefore not brought about.
In any case, wood pretreated with chlorine is well suited for alkaline digestion. Such chlorine-containing wood can therefore easily be used in the operation of the soda pulp mills for pulp production, possibly after it has served several times to remove odors.
Instead of the gaseous oxidizing agents, aqueous solutions of the oxidizing agents can also be used to destroy the odorous substances trapped in the wood.
PATENT CLAIMS: i. Procedure for removing the odorous substances. from waste gases from pulp production, characterized in that shredded wood, sawdust or other waste of a vegetable, woody nature is switched into the stream of odorous gases.
** WARNING ** End of DESC field may overlap beginning of CLMS **.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE80445X | 1917-07-30 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT80445B true AT80445B (en) | 1920-04-10 |
Family
ID=5639095
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT80445D AT80445B (en) | 1917-07-30 | 1918-09-27 | Process for removing odorous substances from Processes for removing odorous substances from waste gases from pulp production. s waste gases from pulp production. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT80445B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2664964A (en) * | 1947-07-16 | 1954-01-05 | Asplund Arne Johan Arthur | Fibrous filter sheet for gases |
-
1918
- 1918-09-27 AT AT80445D patent/AT80445B/en active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2664964A (en) * | 1947-07-16 | 1954-01-05 | Asplund Arne Johan Arthur | Fibrous filter sheet for gases |
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