AT52958B - Process for the simultaneous preparation of chlorammonium and sulphites of barium, strontium, calcium, magnesium and zinc. - Google Patents
Process for the simultaneous preparation of chlorammonium and sulphites of barium, strontium, calcium, magnesium and zinc.Info
- Publication number
- AT52958B AT52958B AT52958DA AT52958B AT 52958 B AT52958 B AT 52958B AT 52958D A AT52958D A AT 52958DA AT 52958 B AT52958 B AT 52958B
- Authority
- AT
- Austria
- Prior art keywords
- sulphites
- magnesium
- zinc
- calcium
- strontium
- Prior art date
Links
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical class OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 title claims description 7
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title claims description 5
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 title claims description 4
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims description 4
- 229910052788 barium Inorganic materials 0.000 title claims description 4
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 title claims description 4
- 229910052749 magnesium Inorganic materials 0.000 title claims description 4
- 239000011777 magnesium Substances 0.000 title claims description 4
- 229910052712 strontium Inorganic materials 0.000 title claims description 4
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 title claims description 4
- 239000011701 zinc Substances 0.000 title claims description 4
- 229910052725 zinc Inorganic materials 0.000 title claims description 4
- 229910052791 calcium Inorganic materials 0.000 title claims description 3
- 239000011575 calcium Substances 0.000 title claims description 3
- 238000000034 method Methods 0.000 title claims description 3
- QDHHCQZDFGDHMP-UHFFFAOYSA-N Chloramine Chemical compound ClN QDHHCQZDFGDHMP-UHFFFAOYSA-N 0.000 title claims 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 4
- PQUCIEFHOVEZAU-UHFFFAOYSA-N Diammonium sulfite Chemical compound [NH4+].[NH4+].[O-]S([O-])=O PQUCIEFHOVEZAU-UHFFFAOYSA-N 0.000 claims description 2
- 229910021529 ammonia Inorganic materials 0.000 claims description 2
- 150000003841 chloride salts Chemical class 0.000 claims description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims 2
- 239000000725 suspension Substances 0.000 claims 2
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims 2
- 229960005069 calcium Drugs 0.000 claims 1
- 239000001110 calcium chloride Substances 0.000 claims 1
- 235000011148 calcium chloride Nutrition 0.000 claims 1
- 229960002713 calcium chloride Drugs 0.000 claims 1
- 229910001628 calcium chloride Inorganic materials 0.000 claims 1
- 235000011147 magnesium chloride Nutrition 0.000 claims 1
- 229960002337 magnesium chloride Drugs 0.000 claims 1
- 229910001629 magnesium chloride Inorganic materials 0.000 claims 1
- 229940091250 magnesium supplement Drugs 0.000 claims 1
- 239000011780 sodium chloride Substances 0.000 claims 1
- 239000011592 zinc chloride Substances 0.000 claims 1
- 235000005074 zinc chloride Nutrition 0.000 claims 1
- 229960001939 zinc chloride Drugs 0.000 claims 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical class [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- HSYFJDYGOJKZCL-UHFFFAOYSA-L zinc;sulfite Chemical compound [Zn+2].[O-]S([O-])=O HSYFJDYGOJKZCL-UHFFFAOYSA-L 0.000 description 1
Landscapes
- Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Description
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Die zirka 90 bis 950 C messende Flüssigkeit wird in der Hitze von dem ausgeschiedenen Sulfit getrennt und durch Abkühlung zur Kristallisation gebracht ; die Mutterlauge von dem nunmehr auskristallisierten Salmiak wird für einen neuen Ansatz verwendet. Die ausgeschiedenen Sulfite werden mit heissem Wasser bzw. heissen ungesättigten Waschlaugen, eventuell systematisch, gewaschen und vom Salmiak befreit.
Die Sulfite des Bariums, Strontiums, Kalizum und Magnesiums sind in heissgesättigter Salmiaklösung praktisch unlöslich ; dagegen ist das Zinksulfit in der letzteren teilweise löslich und lässt sich bei den oben erwähnten Mengenverhältnissen nur zu etwa zwei Drittel der Theorie als Präzipitat gewinnen.
Bisher waren die vorteilhaftesten Bedingungen zur gleichzeitigen Herstellung von kristallisationsfähigen Salmiaklösungen und feinkristallinischen sulfiten durch Umsetzung von Ammonsulfat mit den Chloriden des Bariums, Strontiums, Kalziums, Magnesiums und Zinks nicht bekannt. Erst unsere Beobachtung, dass die bei der Bildung des Ammoniumsulfits entwickelte Reaktionswärme eine derartige ist, dass man hochkonzentrierte kristallisationsfähige Salmiaklösungen erhalten kann, ohne Lösungen eindampfen zu müssen, weiters, dass man hiebei gleich- zeitig n'ine, oxyd-und karbonatfreie Sulfite der alkalischen Erden, der Magnesia und des Zinks in feinkristallinsicher Form gewinnen kann, macht den Prozess zu einem rationellen und ökonomischen.
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The liquid, measuring around 90 to 950 C, is separated from the precipitated sulfite in the heat and crystallized by cooling; the mother liquor from the salmiac which has now crystallized out is used for a new approach. The precipitated sulfites are washed with hot water or hot unsaturated washing liquors, possibly systematically, and freed from ammonia.
The sulphites of barium, strontium, potassium and magnesium are practically insoluble in hot saturated ammonium solution; on the other hand, the zinc sulfite is partially soluble in the latter and can only be obtained as a precipitate to about two thirds of the theory given the proportions mentioned above.
So far, the most advantageous conditions for the simultaneous production of crystallizable ammonia solutions and finely crystalline sulfites by reacting ammonium sulfate with the chlorides of barium, strontium, calcium, magnesium and zinc were not known. It was not until our observation that the heat of reaction developed during the formation of ammonium sulfite is such that highly concentrated crystallizable ammonium solutions can be obtained without having to evaporate solutions, further that one can simultaneously obtain no oxide and carbonate-free sulfites of the alkaline Earth, which can extract magnesia and zinc in fine-crystalline form, makes the process a rational and economical one.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT52958D AT52958B (en) | 1909-04-14 | 1911-03-13 | Process for the simultaneous preparation of chlorammonium and sulphites of barium, strontium, calcium, magnesium and zinc. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT41934T | 1909-04-14 | ||
| AT52958D AT52958B (en) | 1909-04-14 | 1911-03-13 | Process for the simultaneous preparation of chlorammonium and sulphites of barium, strontium, calcium, magnesium and zinc. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT52958B true AT52958B (en) | 1912-04-10 |
Family
ID=25600912
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT52958D AT52958B (en) | 1909-04-14 | 1911-03-13 | Process for the simultaneous preparation of chlorammonium and sulphites of barium, strontium, calcium, magnesium and zinc. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT52958B (en) |
-
1911
- 1911-03-13 AT AT52958D patent/AT52958B/en active
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