US280172A - Hubert grotjven - Google Patents

Hubert grotjven Download PDF

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US280172A
US280172A US280172DA US280172A US 280172 A US280172 A US 280172A US 280172D A US280172D A US 280172DA US 280172 A US280172 A US 280172A
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strontium
potassium
sulphide
carbonate
coelestin
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/18Carbonates
    • C01F11/186Strontium or barium carbonate
    • C01F11/188Barium carbonate

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  • the mixture for said process is preferably made in the following proportions one hundred and ninety to two hundred kilograms of powdered coelestin, equal to two atoms of sulphate of strontium two hundred and two to two hundred and five kilograms of the crystallized double salt of potassium and magnesium, equal to one atom of y and superheated air.
  • a crucible of the dimensions mentioned holds eight liters,and contains the above stand ard mixture, with five kilograms of coelestin. In the upper part of the sides of each crucible,
  • This sulphide mass is composed of magnesia, hydrated oxide of strontium, sulphide of strontium, and sulphide of potassium, and is directly poured from the cooled crucibles into the extractionvessels, whereby exposure to air is avoided as much as possible.
  • These extraction-vessels are closed, and preferably round, and each is provided with an agitator and a steam-coil for boiling the mass.
  • the lixiviation in a boiling state, is continued by decantation and repeated pouring on of fresh water until the filtered fluid will only show traces of oxide of strontium. I prefer to combine seven of such ves- 'sels, so as to obtain continuous lixiviation and concentrated filtrates.
  • I claim as my invention The method herein specified of manufacturing carbonate of strontium, consisting, first, in mixing powdered coelestin with a double sulphate of potassium and magnesium and powdered carbon or coal, in the proportions men tioned, or nearly in those proportions; sec ond, furnacing this mixture, under exclusion of air, for its conversion into sulphide of strontium, hydrated oxide of strontium, sulphide of potassium, and magnesium in cylinders or crucibles within a furnace; third, the lixiviation of the furnaced mass with water, under exclusion of air, for gaining asolution ofhydrated oxide of strontium, sulphide of strontium, and simple.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Description

UNITED- STATES PATENT OFFICE.
UBERT GROUVEN, or LEIPSIO, SAXONY, eERMAivYf MANUFACTURE OF STRONTIIIUM CARBONATEI SPECIFICATION forming part of Letters Patent No. 280,172, dated June 26, 1883.
Application filed May 1, 1883.
T at whom it may concern:
Be it known that I, HUBERT GRoUvEN, of Leipsic, Kingdom of Saxony, German Empire, have invented an Improvement in'the Manufacture of Carbonate of Strontium, of which the following is a specification.
The perfect reduction of coelestin or sulphate of strontium into sulphide of strontium by means of carbon requires a degree of white heat which will destroy the crucible, so that it can only be used once. Moreover, the decomposition of sulphideof strontium by carbonic acid is difficult and only partial, and hence the sulphide of strontium, or the cheap sulphate in the form of coelestin, has never been used successfully in the manufacture of strontia on a commercial scale. I remove the'difficulties by introducing sulphide of potassium into the process. Sulphide of potassium,being a body which, at a glowing heat, considerably surpasses the reducing-power of carbon, will, in connection or combination with carbon, completely reduce the coelestin at a comparal tively low temperature.
I have ascertained that, in connection with sulphide of potassium, the sulphide of strondered coelestin with finely-powdered crystallized double salt of sulphate of potassium and magnesium. These areheated to incandescence in connection with carbon, and the double salt will be reduced first, and at a comparatively low temperature, into oxide ofmagnesium and sulphide of potassium. The latter, which is easily fusible, will act on the adjacent molecules of coelestin. I have found that the mixture for said process is preferably made in the following proportions one hundred and ninety to two hundred kilograms of powdered coelestin, equal to two atoms of sulphate of strontium two hundred and two to two hundred and five kilograms of the crystallized double salt of potassium and magnesium, equal to one atom of y and superheated air.
(N0 Specimens.)
sulphate of potassium and magnesium; one
hundred and kilograms of powdered coal,
(gas -coal;) ten to fifteen kilograms of sulphate of potassium residuum of the preceding process. These materials must be finely pow dered and very intimately mixed and ground and eight hundred millimeters height, which crucibles are suspended in rows in the top of a crucible furnace heated by generator-gases 7 After each furnacing, lasting about two hours and a half, one series of incandescent crucibles is removed from the top of the furnace and replaced by a new series freshly charged.
, A crucible of the dimensions mentioned holds eight liters,and contains the above stand ard mixture, with five kilograms of coelestin. In the upper part of the sides of each crucible,
' but below the top of the furnace, several holes are provided, each ten millimeters in diameter, through which the carbonic-oxide gas and sulphureted hydrogen gas, developing in abundance during the furnacing process, will es cape, and will burn in the oven, thereby help ing to heat it. Outside the oven the crucible is closed, during the furnaeing, with a loose cover, which may be easily made gastight with clay in the well-known manner. This very important desulphurati'on of the contents of the crucibles, which is indicated by the abovementioned abundant development of sulphureted-hydrogen gas, depends upon the six to seven kilograms of hydrogen contained in the )owdered coal, steadily and slowly set free from t 1e same during the furuacing process. The temperature in the oven must not be above the melting-point of copper. The crucibles will stand such a heat well, especially if made of the best Scotch iron, and will be but slowly destroyed. The inside of them is not corroded at all by the above-named mixture, which, during the furnacing, is not melted, but simply forms into a lump, which, on turning over the crucible, will at once fall out and show a soft flesh-color mass. This mass, which, for convenience, I will call sulphide mass, if furhundred and ten millimeters internal diameter 4 naced properly, will weigh about two hundred and fifty kilograms. It should dissolve entirely in diluted hydrochloric acid, and should contain neither sulphuric acid nor any white particles of undecomposed coelestin. This sulphide mass is composed of magnesia, hydrated oxide of strontium, sulphide of strontium, and sulphide of potassium, and is directly poured from the cooled crucibles into the extractionvessels, whereby exposure to air is avoided as much as possible. These extraction-vessels are closed, and preferably round, and each is provided with an agitator and a steam-coil for boiling the mass. The lixiviation, in a boiling state, is continued by decantation and repeated pouring on of fresh water until the filtered fluid will only show traces of oxide of strontium. I prefer to combine seven of such ves- 'sels, so as to obtain continuous lixiviation and concentrated filtrates. These filtrates are clear, nearly colorless, and, if cooled down, more than one-half of the strontium .will be separated in large crystals, as hydrate of strontia. This ox ide, however, will prove to be polluted with a small quantity of sulphide of strontium, for
which reason I prefer not to separate the oxide,
but to convert it, in connection with the motherlye, into carbonate of strontium. This conversion of the solution of strontium and sulphide of potassium into carbonate of strontium and carbonate of potassium is obtained by introducing carbonic acid at boiling-point,
so that the result will be, 011 the one hand, a
heavy sediment of carbonate of strontia, and, on the other hand, a ten per cent. solution of carbonate of potash. The development of sulphuretedhydrogen gas, which is enormous at the start, diminishes gradually after a few hours continuance of this operation. This i11- troduction of carbonic acid may be stopped as soon as a strip of paper moistened with a solution of acetate of lead willnot indicate any trace of hydrosulphureted hydrogen in the escaping vapors. The carbonic acid to be used must be free from any oxygen gas or smoke, and the perfectly-pure carbonic acid obtained by acting with superheated steam upon limestone is to be preferred. The precipitated carbonate of strontium is to be separated from the potash solution by a filter-press, and may easily be lixiviated, so as to leave it as awhite coke. It
contains ninety-nine per cent. of carbonate of strontium and only very littlesulphide of iron. The potash solution, after evaporation, roasting, and redissolving in a minimum of cold water, whereby small quantities of' oxide of iron and sulphate of potassium are left, will give a potash of ninety-eight per cent. if the double sulphate of potassium and magnesium employed has been nearly free of chlorides. The small portion of sulphate of potassium thus left is added to the next mixture for the crucible, and, re-entering into the process, is not lost. According to the process described, I gain from each one hundred kilograms of coelestin about sixty-six kilograms of car bonate of strontium and twenty-eight kilo grams of carbonate of potassium. The latter will cover about two-thirds of the entire cost of manufacturing, and therefore the manufacture of the carbonate of strontium is made uncommonly cheap.
I claim as my invention The method herein specified of manufacturing carbonate of strontium, consisting, first, in mixing powdered coelestin with a double sulphate of potassium and magnesium and powdered carbon or coal, in the proportions men tioned, or nearly in those proportions; sec ond, furnacing this mixture, under exclusion of air, for its conversion into sulphide of strontium, hydrated oxide of strontium, sulphide of potassium, and magnesium in cylinders or crucibles within a furnace; third, the lixiviation of the furnaced mass with water, under exclusion of air, for gaining asolution ofhydrated oxide of strontium, sulphide of strontium, and simple. sulphide of potassium; fourth, the evaporation of this solution, at the same time introducing carbonic-acid gas till the development of sulphureted-hydrogen gas stops, and separation of the precipitated strontium carbonate from the potassium carbonate-left in the solution. I
In testimony whereof I have hereunto set my hand, this 27th day of March, 1883, in the presence of two subscribing witnesses.
HUBERT GROUVEN.
lVitnesses:
\VILHELM VVREsoHtiTTER, GEoRG RICHTER.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4666688A (en) * 1986-02-03 1987-05-19 Excel-Mineral Company, Inc. Method for recovery and conversion of strontium sulfate to strontium carbonate from low and medium grade celestite ores

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4666688A (en) * 1986-02-03 1987-05-19 Excel-Mineral Company, Inc. Method for recovery and conversion of strontium sulfate to strontium carbonate from low and medium grade celestite ores

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