AT31275B - Process for the production of high-percentage potash from stillage coal. - Google Patents
Process for the production of high-percentage potash from stillage coal.Info
- Publication number
- AT31275B AT31275B AT31275DA AT31275B AT 31275 B AT31275 B AT 31275B AT 31275D A AT31275D A AT 31275DA AT 31275 B AT31275 B AT 31275B
- Authority
- AT
- Austria
- Prior art keywords
- sep
- stillage
- production
- coal
- percentage
- Prior art date
Links
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 title claims description 7
- 235000015320 potassium carbonate Nutrition 0.000 title claims description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 title claims description 5
- 229940072033 potash Drugs 0.000 title claims description 5
- 238000004519 manufacturing process Methods 0.000 title claims 2
- 238000000034 method Methods 0.000 title claims 2
- 239000003245 coal Substances 0.000 title 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 5
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 2
- 239000003610 charcoal Substances 0.000 claims 2
- 238000002386 leaching Methods 0.000 claims 1
- 229910052700 potassium Inorganic materials 0.000 claims 1
- 239000011591 potassium Substances 0.000 claims 1
- 150000003109 potassium Chemical class 0.000 claims 1
- 150000003839 salts Chemical class 0.000 claims 1
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 6
- 239000001103 potassium chloride Substances 0.000 description 3
- 235000011164 potassium chloride Nutrition 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 230000029142 excretion Effects 0.000 description 1
- 235000017550 sodium carbonate Nutrition 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)
- Sawing (AREA)
- Confectionery (AREA)
Description
<Desc/Clms Page number 1>
EMI1.1
EMI1.2
EMI1.3
<tb>
<tb>
K2@O3. <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> 98#5 <SEP> bis <SEP> 99#4%
<tb> Na2CO3 <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> 1#2 <SEP> # <SEP> 0#4%
<tb> A'r/.......... <SEP> o.. <SEP> o-2"
<tb>
EMI1.4
EMI1.5
<tb>
<tb>
Wasser <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> 19 <SEP> %
<tb> kohlensaures <SEP> Kali <SEP> 71 <SEP> ()
<tb> kohlensaurs <SEP> Natron.... <SEP> O''o
<tb> Chlorkalium <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> . <SEP> 9#4%
<tb>
<Desc/Clms Page number 2>
Dieselbe kann behufs Ausscheidung des Chlorkaliums auf 520 Bé. verdünnt und gekühlt werden, wobei das Chlorkalium auskriställisiert. Die davon abgetrennte Lauge kann wieder, wie beschrieben, auf hochprozentige Pottasche verarbeitet werden oder dient direkt zur Herstellung einer Pottasche von über 90% Gehalt an kohlensaurem Kali.
<Desc / Clms Page number 1>
EMI1.1
EMI1.2
EMI1.3
<tb>
<tb>
K2 @ O3. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP> 98 # 5 <SEP> to <SEP> 99 # 4%
<tb> Na2CO3 <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP> 1 # 2 <SEP> # <SEP> 0 # 4%
<tb> A'r / .......... <SEP> o .. <SEP> o-2 "
<tb>
EMI1.4
EMI1.5
<tb>
<tb>
Water <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP> 19 <SEP>%
<tb> carbonate <SEP> potash <SEP> 71 <SEP> ()
<tb> carbonated <SEP> soda .... <SEP> O''o
<tb> Potassium Chloride <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP>. <SEP> 9 # 4%
<tb>
<Desc / Clms Page number 2>
The same can be done for the excretion of potassium chloride to 520 Be. be diluted and cooled, whereby the potassium chloride crystallizes out. The lye separated from it can be reprocessed into high-percentage potash, as described, or is used directly to produce potash with a carbonate of potash content of over 90%.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT31275T | 1905-09-25 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT31275B true AT31275B (en) | 1908-01-10 |
Family
ID=3545710
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT31275D AT31275B (en) | 1905-09-25 | 1905-09-25 | Process for the production of high-percentage potash from stillage coal. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT31275B (en) |
-
1905
- 1905-09-25 AT AT31275D patent/AT31275B/en active
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