Patent US540265A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4100254A Expired / Lapsed US ⏱️ 0.0 years remaining

Industrial process of preparing magnesia of high purity

Assignee: Veitscher Magnesitwerke AG
•
Filing: 1976-11-18
•
Granted: 1978-07-11
•
Expires: 1996-11-18
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract In an industrial process of preparing high-purity magnesia from an impure magnesium-containing starting material, wherein the starting material is dissolved in HCl and the resultant acidic solution is subjected to a multistep treatment for precipitating the impurities out of the solution, the precipitate is separated from the residual purified magnesium chloride solution, and the magnesium chloride is thermally decomposed to obtain magnesia, the purified magnesium chloride solution is first concentrated and sulfate ions are then added thereto to precipitate calcium ions from the concentrated solution as calcium sulfate.

Inventors

  • 👤 Helmut Grohmann
  • 👤 Michael Grill

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 23:48
CPC Classifications
C; C01; C01F; C01F11/00; C01F11/46; C01D; C01D5/00; C01D5/06; C01F5/00; C01F5/02; C01F5/06; C01F5/10; C01P; C01P2006/00; C01P2006/80

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 207 words
In an industrial process of preparing magnesia of high purity from a magnesium-containing starting material containing impurities which comprises (a) dissolving the starting material in aqueous hydrochloric acid to produce an acidic solution of the starting material, and (b) subjecting the acidic solution of the starting material to a multi-step treatment wherein the impurities are precipitated from the solution and the precipitate is separated from the residual purified solution, said multi-step treatment comprising (1) a first step in the purification treatment including precipitating impurities as hydroxides and separating the precipitate from the residual magnesium chloride solution, and (2) a second treatment step including precipitating calcium present in the magnesium chloride solution by adding sulfate ions containing material and separating the precipitate, said calcium originating from the starting material and/or from material added for promotion of precipitation during the first step of the treatment, and (c) thermally decomposing the magnesium chloride in the purified solution to obtain magnesia, and recovering the magnesia, the improvement of first concentrating the magnesium chloride solution in the second treatment step to a content of more than 350 grams MgCl 2 /liter and then adding thereto the sulfate ions containing material to precipitate the calcium ions from the concentrated solution as calcium sulfate.
Claim 2
Dependent Claim 207 words
In an industrial process of preparing magnesia of high purity from a magnesium-containing starting material containing impurities which comprises (a) dissolving the starting material in aqueous hydrochloric acid to produce an acidic solution of the starting material, and (b) subjecting the acidic solution of the starting material to a multi-step treatment wherein the impurities are precipitated from the solution and the precipitate is separated from the residual purified solution, said multi-step treatment comprising (1) a first step in the purification treatment including precipitating impurities as hydroxides and separating the precipitate from the residual magnesium chloride solution, and (2) a second treatment step including precipitating calcium present in the magnesium chloride solution by adding sulfate ions containing material and separating the precipitate, said calcium originating from the starting material and/or from material added for promotion of precipitation during the first step of the treatment, and (c) thermally decomposing the magnesium chloride in the purified solution to obtain magnesia, and recovering the magnesia, the improvement of first concentrating the magnesium chloride solution in the second treatment step to a content of more than 350 grams MgCl 2 /liter and then adding thereto the sulfate ions containing material to precipitate the calcium ions from the concentrated solution as calcium sulfate.
Claim 3
Dependent Claim 20 words
In the industrial process of claim 1, the step of adding magnesia to the solution during the second treatment step.
Claim 4
Dependent Claim 30 words
In the industrial process of claim 2, the magnesia added to the solution during the second treatment step is taken from the magnesia obtained by thermally decomposing the magnesium chloride.
Claim 5
Dependent Claim 47 words
In the industrial process of claim 3, magnesia obtained by thermally decomposing the magnesium chloride is carried by flue gases generated by the thermal decomposition, the magnesia is separated from the flue gases, and the separated magnesia is added to the solution during the second treatment step.
Claim 6
Dependent Claim 29 words
In the industrial process of claim 1, the step of heating the purified chloride solution in the second treatment step to a temperature of about 60° to 120° C.
Claim 7
Dependent Claim 26 words
In the industrial process of claim 5 the step of heating the purified chloride solution in the second treatment step to a temperature about 100° C.
Claim 8
Dependent Claim 26 words
In the industrial process of claim 1, the step of adding the sulfate ions to the purified magnesium chloride solution in the form of magnesium sulfate.
Claim 9
Dependent Claim 26 words
In the industrial process of claim 1, the step of adding the sulfate ions to the purified magnesium chloride solution in the form of sulfuric acid.
Claim 10
Dependent Claim 32 words
In the industrial process of claim 1, the step of adding the sulfate ions to the purified magnesium chloride solution in the form of a sulfur-containing substance derived from heating waste gases.
Claim 11
Dependent Claim 39 words
In the industrial process of claim 1, the purified magnesium chloride solution is concentrated in the second treatment step to a content of more than 380 g MgCl 2 /liter of the solution before the sulfate ions are added.

References Cited (Backward Citations)

US1090125A Cited
US3341290A Cited
US3980753A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-07-10 1982-01-09 1982-07-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-07-10 1986-01-09 1986-07-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-07-10 1990-01-09 1990-07-11 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag