DE1189032B - Process for the flotative production of high-percentage potassium chlorine from kainite-containing potash crude salts - Google Patents
Process for the flotative production of high-percentage potassium chlorine from kainite-containing potash crude saltsInfo
- Publication number
- DE1189032B DE1189032B DEW37225A DEW0037225A DE1189032B DE 1189032 B DE1189032 B DE 1189032B DE W37225 A DEW37225 A DE W37225A DE W0037225 A DEW0037225 A DE W0037225A DE 1189032 B DE1189032 B DE 1189032B
- Authority
- DE
- Germany
- Prior art keywords
- kainite
- flotative
- production
- potassium chlorine
- flotation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/01—Organic compounds containing nitrogen
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/02—Collectors
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2203/00—Specified materials treated by the flotation agents; specified applications
- B03D2203/02—Ores
- B03D2203/04—Non-sulfide ores
- B03D2203/10—Potassium ores
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
Verfahren zur flotativen Herstellung von hochprozentigem Chlorkalium aus kainithaltigen Kalirohsalzen Nach dem kanadischen Patent 612 295 und dem italienischen Patent 573 817 ist es bekannt, Kainit aus Kainitmineralen mit primären Fettsäureaminen unter Benutzung einer aus den Komponenten KCl, NaCI, MgS04 und MgClp, bestehenden Lauge, die in dieser Zusammensetzung innerhalb des Existenzgebietes von Sylvin des quinären, an KCl und NaCI gesättigten Systems liegt, insbesondere mit Hartsalzlauge mit etwa 100 bis 250 g MgCl, und weniger als etwa 100 g MgS04 pro Liter zu flotieren. Bei dieser Flotation wird der im Rohkainit vorhandene Sylvin jedoch mit ausgeschwommen. Das Patent 1 175 172 betrifft ein Verfahren zur flotativen Herstellung von hochprozentigem Chlorkalium aus kainithaltigen Kalirohsalzen, welches dadurch gekennzeichnet ist, daß der Sylvinflotation eine Kainitflotation mit geringen Mengen bekannter sylvinselektiver Sammler bzw. Sammlerschäumer, wie primären aliphatischen Fettaminen, im Gemisch mit nicht oder kaum auf KCl ansprechenden kationenaktiven Verbindungen, wie sekundären oder substituierten primären Aminen, insbesondere Methyldodecylamin, Dimethylhexylamin, Dicyclohexylamin, oder Gemischen dieser Stoffe vorausgeht.Process for the flotative production of high percentage potassium chlorine from cainite crude potash salts According to Canadian patent 612 295 and the Italian one In patent 573 817 it is known to produce kainite from kainite minerals with primary fatty acid amines using one consisting of the components KCl, NaCl, MgS04 and MgClp Lye, which in this composition is within the area of existence of Sylvin des quinary system, saturated with KCl and NaCl, in particular with hard salt liquor to float with about 100 to 250 g of MgCl, and less than about 100 g of MgSO4 per liter. With this flotation, however, the sylvine present in the raw kainite is also floated out. Patent 1,175,172 relates to a process for the flotative production of high-proof liquor Potassium chlorine from kainite-containing potash salts, which is characterized by that the sylvine flotation a kainite flotation with small amounts of known sylvine selective Collectors or collector foams, such as primary aliphatic fatty amines, in a mixture with cation-active compounds that do not respond or hardly respond to KCl, such as secondary ones or substituted primary amines, especially methyldodecylamine, dimethylhexylamine, Precedes dicyclohexylamine, or mixtures of these substances.
In Fortentwicklung dieses Verfahrens wurde nun gefunden, daß für die Abtrennung des Kainits Tallölfettamin als besonders preiswertes Mittel geeignet ist, wie das folgende Beispiel zeigt: Ein Gemisch aus 51 °/o Kainit, 43 °/o Steinsalz und 2,5 °/o Kieserit, aufgemahlen auf eine Korngröße von weniger als 0,5 mm, ergibt mit Tallölaminacetat, ; Handelsprodukt Delamat der Firma Herkules Powder, folgende Konzentrate mit rund 90°/oiger Kainitausbeute: a) in einer Lauge des KCl-Existenzgebietes des quinären Systems ozeanischer Salze (KCI, NaCI-gesättigt, 120 g pro Liter MgCl2): 85°/a Kainit, 10 °/o NaCI und 5 % Kieserit; b) in einer Lauge, die an KC1 und NaCI gesättigt ist und im Liter 340 g MgCl, enthält: 89 °/o Kainit, 8 °/o NaCI und 3 °/o Kieserit.As a further development of this process, it has now been found that tall oil fatty amine is a particularly inexpensive means of separating off the kainite, as the following example shows: A mixture of 51% kainite, 43% rock salt and 2.5% kieserite , ground to a grain size of less than 0.5 mm, yields with tall oil amine acetate,; Commercial product Delamat from Herkules Powder, the following concentrates with around 90% kainite yield: a) in a lye from the KCl area of existence of the quinary system of oceanic salts (KCl, NaCl-saturated, 120 g per liter MgCl2): 85 ° / a kainite , 10% NaCl and 5% kieserite; b) in a lye which is saturated in KCl and NaCl and contains 340 g MgCl per liter: 89% kainite, 8% NaCl and 3% kieserite.
Tallölamin bietet also den Vorteil, daß aus Rohsalzen, die neben Kainit noch freien Sylvin enthalten, dieser kaum oder nur in geringer Menge mit in das Flotationskonzentrat des Kainits gelangt. Dies liegt , offenbar an dem Gehalt des Tallölamins an Dehydroabietylamin, das sogenannte Rosin-Amin. Es wird also ein Rückstand erhalten, in dem sich praktisch der Sylvin befindet, beispielsweise bei der Flotation in der Lauge der Zusammensetzung b). Die Abtrennung des Sylvins aus dem Rückstand, insbesondere von Steinsalz, kann dann in bekannter Weise in einer Verfahrensstufe erfolgen.Tall oil amine thus offers the advantage of being made from crude salts, in addition to kainite still contain free sylvin, hardly any or only a small amount of this in the Flotation concentrate of the kainite arrives. This is apparently due to the content of the Tallölamins to dehydroabietylamine, the so-called rosin amine. So it will be a backlog obtained, in which practically the sylvin is, for example in flotation in the liquor of composition b). The separation of Sylvins from the residue, in particular rock salt, can then in a known manner in one process stage take place.
Bei der Flotation eines kainithaltigen Kalirohsalzes wurde mit 250 g/Tonne Delamin, Handelsprodukt des Tallölamins, welches als Hydrochlorid nach Neutralisation mit verdünnter Salzsäure verwendet wurde, ein Konzentrat aus 93 °/o Kainit, 4 °/o Sylvin und 3 °/o NaCI bei einer Ausbeute von 89 °/o an Kainit und ein Rückstand mit 5 °/o Kainit, 45 °/o Sylvin und 50 °/o Steinsalz erhalten.In the flotation of a kainite crude potash salt, 250 g / ton Delamin, commercial product of tall oil amine, which is the hydrochloride after neutralization with dilute hydrochloric acid was used, a concentrate of 93% kainite, 4% Sylvine and 3% NaCl with a yield of 89% kainite and a residue Preserved with 5% kainite, 45% sylvin and 50% rock salt.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEW37225A DE1189032B (en) | 1964-07-23 | 1964-07-23 | Process for the flotative production of high-percentage potassium chlorine from kainite-containing potash crude salts |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEW37225A DE1189032B (en) | 1964-07-23 | 1964-07-23 | Process for the flotative production of high-percentage potassium chlorine from kainite-containing potash crude salts |
Publications (1)
Publication Number | Publication Date |
---|---|
DE1189032B true DE1189032B (en) | 1965-03-18 |
Family
ID=7601417
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEW37225A Pending DE1189032B (en) | 1964-07-23 | 1964-07-23 | Process for the flotative production of high-percentage potassium chlorine from kainite-containing potash crude salts |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE1189032B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102014017645A1 (en) * | 2014-12-01 | 2016-06-02 | K+S Aktiengesellschaft | Process for the selective flotation of kainite from mineral mixtures using sulfated fatty acids as a collector reagent |
-
1964
- 1964-07-23 DE DEW37225A patent/DE1189032B/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102014017645A1 (en) * | 2014-12-01 | 2016-06-02 | K+S Aktiengesellschaft | Process for the selective flotation of kainite from mineral mixtures using sulfated fatty acids as a collector reagent |
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