AT34873B - Process for the preparation of high-percentage potash from still coal or the like. - Google Patents
Process for the preparation of high-percentage potash from still coal or the like.Info
- Publication number
- AT34873B AT34873B AT34873DA AT34873B AT 34873 B AT34873 B AT 34873B AT 34873D A AT34873D A AT 34873DA AT 34873 B AT34873 B AT 34873B
- Authority
- AT
- Austria
- Prior art keywords
- carbonic acid
- preparation
- bicarbonate
- potash
- percentage
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 5
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 title claims description 4
- 229940072033 potash Drugs 0.000 title claims description 4
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 title claims description 4
- 235000015320 potassium carbonate Nutrition 0.000 title claims description 4
- 238000002360 preparation method Methods 0.000 title claims description 3
- 239000003245 coal Substances 0.000 title description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims description 13
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 7
- 235000015497 potassium bicarbonate Nutrition 0.000 claims description 6
- 229910000028 potassium bicarbonate Inorganic materials 0.000 claims description 6
- 239000011736 potassium bicarbonate Substances 0.000 claims description 6
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 claims description 6
- 229910000030 sodium bicarbonate Inorganic materials 0.000 claims description 4
- 235000017557 sodium bicarbonate Nutrition 0.000 claims description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims description 2
- 239000002244 precipitate Substances 0.000 claims description 2
- 239000006227 byproduct Substances 0.000 claims 1
- 230000008030 elimination Effects 0.000 claims 1
- 238000003379 elimination reaction Methods 0.000 claims 1
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 claims 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 4
- 150000003839 salts Chemical group 0.000 description 3
- 238000001354 calcination Methods 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- GXCLVBGFBYZDAG-UHFFFAOYSA-N N-[2-(1H-indol-3-yl)ethyl]-N-methylprop-2-en-1-amine Chemical class CN(CCC1=CNC2=C1C=CC=C2)CC=C GXCLVBGFBYZDAG-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000029142 excretion Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- VLYFRFHWUBBLRR-UHFFFAOYSA-L potassium;sodium;carbonate Chemical compound [Na+].[K+].[O-]C([O-])=O VLYFRFHWUBBLRR-UHFFFAOYSA-L 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- UIIMBOGNXHQVGW-UHFFFAOYSA-N sodium;hydron;carbonate Chemical compound [Na+].OC(O)=O UIIMBOGNXHQVGW-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
<Desc/Clms Page number 1>
Verfahren zur Darstellung hochprozentiger Pottasche aus Schlempekohle oder dgl.
EMI1.1
von mindestens 40 Bé. und Temperatur von etwa 40-50 C mit Kohlensäure eventuell unter Druck behandelt wird, wobei aus der entsprechend gekühlten Flüssigkeit Kaliumbikarbonat ausfällt.
EMI1.2
zurückbleibende Lauge sodann entsprechend stark eingedampft, das Natriumbikarbonat durch Erhitzen in Karbonat verwandelt und die rückbleibende Lösung neuerdings mit Kohlensäure behandelt, wobei ein weiterer Teil des Kalis als Bikarbonat ausfällt. Bei den bekannten Löslichkeitsverhältnissen von Natrium- und Kaliumbikarbonat in Wasser,
wäre bei der Behandlung einer Kaliumnatriumkarbonatlösung mit Kohlensäure eher ein Ausfallen von Natriumbikarbonat als von Kaliumbikarbonat zu erwarten. Bei der in Betracht kommenden, aus Schlempekohle dargestellten Lauge werden jedoch die Löslichkeitsverhältnisse der Bikarbonate durch die Anwesenheit von Chloriden und Sulfaten wesentlich beeinflusst, weiters wird dem Verfahren gemäss durch das Einhalten bestimmter Konzentration. Temperatur und Einleitungsdauer von Kohlensäure ein Zustand herbeigeführt, wobei die Lösung nie mit Natriumbikarbonat gesättigt ist, so dass ein Ausfallen dieses Malzes vermieden wird. Die nähere Durchführung des Verfahrens wird aus dem angeführten Beispiel klar.
Ausgangsprodukt sei beispielsweise eine Lauge von folgender Zusammensetzung des Salzgehaltes :
EMI1.3
In die auf zirka 45"C erwärmte Lauge wird hierauf unter Druck (0'2-1-5 Atm. ) in ge- eigneten Apparaten Kohlensäure eingeleitet. Zufolge der auftretenden Reaktionswärme ist eine Kühlung auf eine Temperatur von 25-45 C notwendig. Während dieser Operation scheidet sich ein Kaliumbikarbonat von hoher Reinheit aus und der Salzgehalt der Lösung sinkt. Hat derselbe 39 Bé. erreicht, wird die Einleitung von Kohlensäure unterbrochen, das ausgeschiedene Salz abgenutscht.
Dasselbe kann als solches (Bikarbonat) oder als Karbonat nach vorhergegangenem Kalzinieren verwendet werden.
EMI1.4
EMI1.5
EMI1.6
<Desc/Clms Page number 2>
EMI2.1
folgenden Abkühlen dieser Lösung scheidet sich das schwerlösliche Kaliumbikarbonat aus. Bei einer Temperatur von zirka 70 C wird neuerdings COg so lange eingeleitet, bis die Konzentration der Lauge 39-41 Be. erreicht hat. Hiebei werden wieder 30-38% der Trockensubstanz der Ursprungslauge als hochprozentige Pottasche gewonnen.
Zusammensetzung der Ausscheidung :
EMI2.2
Die'restierende Mutterlauge kommt zu neuerlichen teilweisen Sulfat-, Chlorid-. Sodaabscheidung und kann dann wieder zur Karbonation Verwendung finden.
Zusammensetzung der Restlaugentrockensubstanz :
EMI2.3
Durch vorstehendes Verfahren werden somit durch zweimalige Karbonation derselben
EMI2.4
Als Kohlensäurequellen können Kalkofenkohlensäure, Gärungskohlensäure (der hiedurch eine neue technische Verwertung geboten wird), ferner die bei der Kalzinierung des Bikarbonates gewinnbare Kohlensäure dienen.
<Desc / Clms Page number 1>
Process for the preparation of high-percentage potash from still coal or the like.
EMI1.1
of at least 40 Bé. and a temperature of about 40-50 C is treated with carbonic acid, possibly under pressure, with potassium bicarbonate precipitating from the appropriately cooled liquid.
EMI1.2
The lye that remains is then evaporated accordingly, the sodium bicarbonate is converted into carbonate by heating and the remaining solution is recently treated with carbonic acid, with another part of the potassium precipitating as bicarbonate. With the known solubility ratios of sodium and potassium bicarbonate in water,
If a potassium sodium carbonate solution is treated with carbonic acid, precipitation of sodium bicarbonate rather than potassium bicarbonate would be expected. In the case of the lye that comes under consideration, produced from coal stillage, however, the solubility ratios of the bicarbonates are significantly influenced by the presence of chlorides and sulphates; Temperature and duration of the introduction of carbonic acid brought about a state in which the solution is never saturated with sodium bicarbonate, so that precipitation of this malt is avoided. The detailed implementation of the procedure is clear from the example given.
The starting product is, for example, a lye with the following composition of salt content:
EMI1.3
In the caustic solution, heated to about 45 ° C., carbonic acid is then introduced under pressure (0.2-1-5 atm.) In suitable apparatus. As a result of the heat of reaction that occurs, cooling to a temperature of 25-45 ° C. is necessary During this operation, a high-purity potassium bicarbonate precipitates and the salt content of the solution drops. When it reaches 39 Bé., the introduction of carbonic acid is interrupted and the precipitated salt is sucked off.
The same can be used as such (bicarbonate) or as carbonate after previous calcination.
EMI1.4
EMI1.5
EMI1.6
<Desc / Clms Page number 2>
EMI2.1
the sparingly soluble potassium bicarbonate separates out when this solution cools down. At a temperature of around 70 C, COg has recently been introduced until the concentration of the lye 39-41 Be. has reached. In doing so, 30-38% of the dry matter of the original liquor is recovered as high-percentage potash.
Composition of the excretion:
EMI2.2
The residual mother liquor comes to renewed partial sulfate, chloride. Soda separation and can then be used again for carbonation.
Composition of the residual liquor dry substance:
EMI2.3
The above method thus carbonates the same twice
EMI2.4
Lime-kiln carbonic acid, fermentation carbonic acid (which is offered by a new technical utilization), furthermore the carbonic acid obtainable during the calcination of the bicarbonate can serve as carbonic acid sources.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT34873T | 1906-10-08 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT34873B true AT34873B (en) | 1908-10-26 |
Family
ID=3551191
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT34873D AT34873B (en) | 1906-10-08 | 1906-10-08 | Process for the preparation of high-percentage potash from still coal or the like. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT34873B (en) |
-
1906
- 1906-10-08 AT AT34873D patent/AT34873B/en active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| AT34873B (en) | Process for the preparation of high-percentage potash from still coal or the like. | |
| DE2914662A1 (en) | METHOD FOR PRODUCING MAGNESIUM OXIDE FROM AN AQUEOUS MAGNESIUM SULFATE SOLUTION | |
| DE210273C (en) | ||
| DE815645C (en) | Process for the production of phenols or phenolates | |
| DE299752C (en) | ||
| DE592496C (en) | Process for the decomposition of multiple salts consisting of alkali sulphates and calcium sulphate | |
| DE874900C (en) | Process for the production of alumina | |
| DE590158C (en) | Process for the production of potash | |
| DE630145C (en) | Process for the production of inorganic and organic salts of alkali or alkaline earth metals | |
| US1303177A (en) | Process of producing ligno tanning material from waste sulfite liquors | |
| DE28067C (en) | Process for the production of hydrogen sulfide from calcium sulfhydrate liquors by heating | |
| AT236988B (en) | Process for the production of ammonium chloride | |
| AT154567B (en) | Process for the production of magnesium compounds, in particular magnesium chloride. | |
| DE572802C (en) | Production of caustic potash or potash and potash nitrate | |
| AT117067B (en) | Process for the preparation of solid ammonium formate. | |
| DE575247C (en) | Production of soda and potash with simultaneous extraction of chlorammonium | |
| DE25218C (en) | Innovations in the process patented under No. 15385 for the production of strontian sugar from molasses and syrups | |
| DE570471C (en) | Production of potash with by-production of ammonia or ammonium sulphate | |
| DE573429C (en) | Process for the production of potassium nitrate | |
| DE406363C (en) | Process for the preparation of potassium sulfate from carnallite and Epsom salt | |
| DE555929C (en) | Process for the production of alkali hydroxide from alkali bicarbonate or carbonate | |
| DE957390C (en) | Process for the production of succinic acid dinitrile | |
| DE557619C (en) | Production of soda, chlorammon, sodium nitrate and hydrochloric acid from sodium chloride | |
| DE734217C (en) | Process for the extraction of pure clay | |
| AT113103B (en) | Process for converting lead sulfate into lead carbonate. |