GB366971A - Improvements in treating mineral salts - Google Patents

Improvements in treating mineral salts

Info

Publication number
GB366971A
GB366971A GB3340530A GB3340530A GB366971A GB 366971 A GB366971 A GB 366971A GB 3340530 A GB3340530 A GB 3340530A GB 3340530 A GB3340530 A GB 3340530A GB 366971 A GB366971 A GB 366971A
Authority
GB
United Kingdom
Prior art keywords
mass
dehydrated
chloride
furnace
stage
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.)
Expired
Application number
GB3340530A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to GB3340530A priority Critical patent/GB366971A/en
Publication of GB366971A publication Critical patent/GB366971A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F5/00Compounds of magnesium
    • C01F5/26Magnesium halides
    • C01F5/30Chlorides
    • C01F5/305Dehydrating ammonium or alkali magnesium chlorides, e.g. carnalite

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Seasonings (AREA)

Abstract

<PICT:0366971/III/1> Magnesium chloride, either alone or mixed with sodium chloride, potassium chloride or ammonium chloride, and also in the form of double salts such as carnallite or ammonium carnallite, is dehydrated in two stages. In the first stage, the compounds are partially dehydrated by introducing them continuously or intermittently into the upper end of a drying apparatus through which they descend while a current of hot air is passed upwardly through the mass, and the dehydrated products are continuously or intermittently removed from the lower end of the apparatus, e.g. by a mechanical grate. In the second stage, the partially dehydrated products are similarly treated by a countercurrent of hot hydrochloric acid gas to obtain the anhydrous salt, the temperatures in both stages being so regulated that the desired degree of dehydration is obtained in the lower part of the furnace and the upper portion of the mass is not heated to the fusion or sintering point. No external heating is used in either stage. For the preparation of the dihydrate, the temperature at the bottom of the mass ranges from 140-160 DEG C., and for the tetrahydrate 120-140 DEG C., while the temperature of the exit gases is 60-80 DEG C. In the preparation of the anhydrous salt, the temperatures are 450-550 DEG C. and 150-250 DEG C. respectively. A suitable apparatus is shown in the Figure, wherein the salt is fed down through the furnace a, which may have an enamel or ceramic lining, in counter-current to the drying agent which is forced in through the opening d after passing through a heater p. The dehydrated material is removed by a rotating grate b and falls into a tapping chamber g closed by valves h<1>, h<2>. Thermometers t<1>, t<2>, t<3> are used to regulate the temperature of the drying agent and of the mass. The inlet for the drying agent may be arranged above the grate, and provision may be made for evacuating the apparatus or rinsing with indifferent gases to remove the air contained in the mass before the drying commences. When preparing the anhydrous salt, the hydrogen chloride issuing from the apparatus is dried, reheated and recycled through the furnace, any losses being made up from a suitable supply.
GB3340530A 1930-11-06 1930-11-06 Improvements in treating mineral salts Expired GB366971A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB3340530A GB366971A (en) 1930-11-06 1930-11-06 Improvements in treating mineral salts

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB3340530A GB366971A (en) 1930-11-06 1930-11-06 Improvements in treating mineral salts

Publications (1)

Publication Number Publication Date
GB366971A true GB366971A (en) 1932-02-08

Family

ID=10352509

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3340530A Expired GB366971A (en) 1930-11-06 1930-11-06 Improvements in treating mineral salts

Country Status (1)

Country Link
GB (1) GB366971A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE748089C (en) * 1936-02-22 1944-10-26 Hans Grothe Dr Ing Process for the production of fine-grained, anhydrous and low-oxide magnesium chloride

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE748089C (en) * 1936-02-22 1944-10-26 Hans Grothe Dr Ing Process for the production of fine-grained, anhydrous and low-oxide magnesium chloride

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