CH107191A - Process for increasing the porosity of decolorizing carbons. - Google Patents
Process for increasing the porosity of decolorizing carbons.Info
- Publication number
- CH107191A CH107191A CH107191DA CH107191A CH 107191 A CH107191 A CH 107191A CH 107191D A CH107191D A CH 107191DA CH 107191 A CH107191 A CH 107191A
- Authority
- CH
- Switzerland
- Prior art keywords
- porosity
- increasing
- oxygen
- coal
- combustion
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 10
- 239000000126 substance Substances 0.000 claims description 7
- 239000003610 charcoal Substances 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 238000002485 combustion reaction Methods 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 239000008246 gaseous mixture Substances 0.000 claims description 2
- 230000003647 oxidation Effects 0.000 claims description 2
- 238000007254 oxidation reaction Methods 0.000 claims description 2
- 239000003245 coal Substances 0.000 description 9
- 239000007789 gas Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
Verfahren zur Erhöhung der Porosität von Entfär bungskohlen. Die Wirksamkeit einer Entfärbungskohle beruht bekanntlich auf ihrem Adsorptions- vermögen, das einerseits durch die Ober flächenaktivität im Sinne des Gibbs'schen Theorems, anderseits durch Kapillaritäts erscheinungen infolge der Porosität der Kohleteilchen bedingt ist.
Die Verfahren zur Herstellung von Kohlen mit hoher Ober flächenaktivität beruhen im allgemeinen darauf, dass man organische Stoffe bei höhe rer Temperatur, zumeist in Gegenwart von alkalischen Stoffen, wie Hydroxyden, Kar bonaten, Sulfiden u. a., der Alkalien oder Erdalkalien, oder von sauren Stoffen, wie Säuren, oder bei höherer Temperatur sauer wirkenden Stoffen, wie Chloriden, Sulfaten, Phosphaten des Ammoniums, Aluminiums, Zinks, Eisens und dergleichen, unter Vermei dung von Luftzutritt erhitzt.
Um die bei der Verkohlung auftretenden Destillations- organe schnell abzuführen, leitet man viel fach während des Verkohlungsvorganges Gase oder Dämpfe, wie Wasserdampf, Koh lendioxyd, Stickstoff, Chlor u. a. durch die Masse hindurch. Man hat in einzelnen Fäl len die Oberflächenaktivität der. Kohle, namentlich zwecks Wiederbelebung gebrauch ter Kohle, auch dadurch zu erhöhen gesucht, dass man die Kohle auf 200 bis 400 , even tuell unter Zutritt von Luft, erhitzt hat oder gelöste Oxydationsmittel auf die Kohle hat einwirken lassen.
Gegenstand der Erfindung ist ein Ver fahren, durch welches eine besonders hohe Porosität der Kohle erzielt wird. Es geht von fertiggebildeter Adsorptionskohle be liebiger Herkunft und Herstellung aus und besteht darin, dass man über die auf über 500 erhitzte Kohle längere Zeit hindurch ein aus Sauerstoff und aus mindestens einem die Verbrennung verhinderndem gasförmigen Stoff, zum Beispiel einem Gas oder Dampf, bestehendes Gemisch leitet, dessen Sauer stoffgehalt derart niedrig gewählt ist,
dass die durch denselben bedingte Oxydation der Kohlenstof fteilchen erst nach völliger Durch dringung des Kohlenstoffgerüstes durch das Gemisch allmählich und ohne sichtbare Verbrennungserscheinungen erfolgt.
Die Durchführung des vorliegenden Ver fahrens geschieht zweckmässig in der Weise, dass in einem geschlossenen, auf über<B>500'</B> erhitzten, die Kohle enthaltenden Raum das Gas- oder Dampfgemiseli langsam hindurch geleitet wird, wobei man lediglich darauf zu achten hat, dass während dieses Vorganges an der glühenden Kohle keine sichtbaren Verbrennungs- bezw. Feuererscheinungen be merkbar sind. In diesem Falle müsste die Konzentration des Sauerstoffes vermindert werden. Als Ausgangsmaterial kann man ,jede beliebige Entfärbungskohle, zum Bei spiel Holzkohle, Tierkohle u. a., anwenden.
Zur Bereitung des gasförmigen Gemisches wird man nicht reinen Sauerstoff, sondern zweckmässigerweise Luft verwenden; als Ver dünnungsgase oder -dämpfe eignen sich alle die Verbrennung verhindernden, sauerstoff freien oder sauerstoffarmen Gase oder D,impfe, zum Beispiel Abgase von Feuerun- en. Generatoren, Kalköfen usw.
Die nach dem vorliegenden Verfahren her gestellten Produkte unterscheiden sieh von dem Ausgangsmaterial durch ihr wesentlich höheres Aufnahmevermögen gegenüber Ga sen, Dämpfen oder gelösten Stoffen.
Process for increasing the porosity of decolorizing carbon. As is well known, the effectiveness of decolorizing charcoal is based on its adsorption capacity, which is conditioned on the one hand by the surface activity in the sense of Gibbs' theorem and on the other by capillarity phenomena due to the porosity of the charcoal particles.
The process for the production of coals with high surface activity are generally based on the fact that organic substances at higher temperature, mostly in the presence of alkaline substances such as hydroxides, carbonates, sulfides and the like. a., of alkalis or alkaline earths, or of acidic substances such as acids, or substances that have an acidic effect at a higher temperature, such as chlorides, sulfates, phosphates of ammonium, aluminum, zinc, iron and the like, are heated with avoidance of air.
In order to quickly remove the distillation organs that occur during the charring process, gases or vapors such as water vapor, carbon dioxide, nitrogen, chlorine and the like are passed many times during the charring process. a. through the crowd. In individual cases one has the surface activity of the. Coal, especially for the purpose of revitalizing used coal, sought to be increased by heating the coal to 200 to 400, possibly with the admission of air, or by letting dissolved oxidizing agents act on the coal.
The invention relates to a process by which a particularly high porosity of the coal is achieved. It is based on fully formed adsorption coal of any origin and manufacture and consists in passing a mixture of oxygen and at least one gaseous substance that prevents combustion, for example a gas or steam, over the coal heated to over 500 for a longer period of time whose oxygen content is so low that
that the oxidation of the carbon particles caused by the same takes place gradually and without visible signs of combustion only after the carbon structure has completely penetrated the mixture.
The present process is expediently carried out in such a way that the gas or steam parchment is slowly passed through in a closed space which is heated to over 500 'and contains the coal, whereby one merely needs to be careful has that during this process no visible burns or burns on the glowing coal. Fire phenomena are noticeable. In this case the concentration of oxygen would have to be reduced. The starting material can be any decolorizing charcoal, for example charcoal, animal charcoal and the like. a., apply.
For the preparation of the gaseous mixture one will not use pure oxygen, but expediently air; all oxygen-free or low-oxygen gases or gases that prevent combustion are suitable as dilution gases or vapors, for example exhaust gases from fires. Generators, lime kilns, etc.
The products produced by the present process differ from the starting material in that they have a significantly higher absorption capacity for gases, vapors or dissolved substances.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS107191X | 1922-08-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CH107191A true CH107191A (en) | 1924-10-01 |
Family
ID=5448893
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CH107191D CH107191A (en) | 1922-08-19 | 1923-08-16 | Process for increasing the porosity of decolorizing carbons. |
Country Status (1)
| Country | Link |
|---|---|
| CH (1) | CH107191A (en) |
-
1923
- 1923-08-16 CH CH107191D patent/CH107191A/en unknown
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CH107191A (en) | Process for increasing the porosity of decolorizing carbons. | |
| DE1669318A1 (en) | Process for removing sulfur dioxide from gases containing sulfur dioxide and means therefor | |
| DE2157537A1 (en) | Process for the safe handling of low molecular weight acetylene hydrocarbons | |
| DE520381C (en) | Active coal production | |
| AT98710B (en) | Process for increasing the porosity of decolorizing carbons. | |
| DE909453C (en) | Process for the production of reactive coal from hard coal | |
| DE482175C (en) | Active coal production | |
| AT115411B (en) | Process for activating carbon for absorption and decolorization purposes. | |
| DE636997C (en) | Process for the production of weather-resistant briquettes from strongly swelling brown coal | |
| DE934944C (en) | Process for the production of active charcoal | |
| DE892583C (en) | Method of making fire-starters | |
| DE918196C (en) | Mass for producing colored smoke | |
| DE502040C (en) | Active coal production | |
| DE512387C (en) | Process for the production of primary tar and light oils | |
| DE447757C (en) | Process for the oxidation of hydrogen sulfide contained in gases to sulfur | |
| DE945088C (en) | Process for the production of activated carbon | |
| DE555003C (en) | Production of hydrogen | |
| DE817590C (en) | Process for producing high quality fuel | |
| DE490355C (en) | Process for the preservation of hydrocyanic acid | |
| DE857086C (en) | Activated carbon carbon electrode and process for its manufacture | |
| DE88614C (en) | ||
| DE692958C (en) | Process for the production of fertilizers suitable for spreading | |
| DE567083C (en) | Process for the production of olefin-rich gases from bituminous coals | |
| DE389160C (en) | Process for the production of solid alkali hypochlorite | |
| AT83478B (en) | The manufacture and assembly of briquettes for the smoked goods industry. |