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US4096235A Expired / Lapsed US ⏱️ 0.0 years remaining

Process of producing magnesia with sulfuric acid recycle

Assignee: GEA Group AG
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Filing: 1976-10-13
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Granted: 1978-06-20
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Expires: 1996-10-13
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Abstract

Abstract This invention relates to a process of producing magnesia from magnesium-containing carbonate ores, which comprises leaching with sulfuric acid, subsequently neutralizing the solution with magnesia, separating the undissolved impurities, crystallizing magnesium sulfate under pressure and above 150° C so the crystals have from 1.5 to 4 moles of water per magnesium sulfate molecule and thermally decomposing the latter to form magnesia and SO 2 , recovering sulfuric acid from the sulfur dioxide produced in the decomposing steps and recycling the sulfuric acid to the leaching stage.

Inventors

  • 👤 Harry Edward Cross
  • 👤 Wolfgang Krieger
  • 👤 Eberhard Anschutz
  • 👤 Lothar Reh
  • 👤 Martin Hirsch

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 10:40
CPC Classifications
C; C01; C01F; C01F5/00; C01F5/02; C01F5/06; C01F5/12; C01F5/40

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 214 words
Process for producing magnesia from magnesium-containing carbonate ores which comprises: (a) leaching said ore with sulfuric acid; (b) neutralizing the solution from (a) with magnesia and separating undissolved impurities; (c) crystallizing magnesium sulfate from the solution from (b) under superatmospheric pressure and at temperatures above 150° C; (d) separating and cooling the magnesium sulfate crystals so that they contain 1.5-4 mols of water of crystallization and thereby have a crystal fineness suitable for decomposition in the fluidized bed reaction zone of step (f); (e) dehydrating and/or heating the crystals from (d) in a suspension-type heat-exchanger with exhaust gases from the fluidized-bed reaction zone of step (f); (f) feeding the crystals from (e) after separation to a fluidized bed reaction zone where they are decomposed to form magnesia and sulfur dioxide, the heat required for the decomposition reaction being generated by approximately a stoichiometric combustion of fuel charged into the fluidized bed reaction zone; (g) removing magnesia from the fluidized bed reaction zone and feeding same to a multi-stage fluidized-bed cooler operated with air as a fluidized gas; (h) feeding fluidized air from the fluidized bed cooler to the fluidized bed reaction zone of step (f); (i) converting the sulfur dioxide produced in step (f) into sulfuric acid and recycling same to leaching step (a).
Claim 2
Dependent Claim 214 words
Process for producing magnesia from magnesium-containing carbonate ores which comprises: (a) leaching said ore with sulfuric acid; (b) neutralizing the solution from (a) with magnesia and separating undissolved impurities; (c) crystallizing magnesium sulfate from the solution from (b) under superatmospheric pressure and at temperatures above 150° C; (d) separating and cooling the magnesium sulfate crystals so that they contain 1.5-4 mols of water of crystallization and thereby have a crystal fineness suitable for decomposition in the fluidized bed reaction zone of step (f); (e) dehydrating and/or heating the crystals from (d) in a suspension-type heat-exchanger with exhaust gases from the fluidized-bed reaction zone of step (f); (f) feeding the crystals from (e) after separation to a fluidized bed reaction zone where they are decomposed to form magnesia and sulfur dioxide, the heat required for the decomposition reaction being generated by approximately a stoichiometric combustion of fuel charged into the fluidized bed reaction zone; (g) removing magnesia from the fluidized bed reaction zone and feeding same to a multi-stage fluidized-bed cooler operated with air as a fluidized gas; (h) feeding fluidized air from the fluidized bed cooler to the fluidized bed reaction zone of step (f); (i) converting the sulfur dioxide produced in step (f) into sulfuric acid and recycling same to leaching step (a).
Claim 3
Dependent Claim 47 words
Process of claim 1 wherein magnesium sulfate is decomposed in step (f) in an expanded fluidized bed having a mean fractional voidage of ε>0.7, the solids are separated in a recycling cyclone and a major portion of the solids are recycled into the fluidized bed reaction zone.
Claim 4
Dependent Claim 45 words
Process of claim 2 wherein a portion of the fluidizing air is fed to the reaction zone as secondary air above the inlet for the fluidizing air and fuel is charged to the reaction zone between the inlets for the fluidizing air and secondary air.
Claim 5
Dependent Claim 21 words
Process of claim 3 wherein the ratio of fluidizing air to secondary air is 1 : 2 to 5 : 1.
Claim 6
Dependent Claim 24 words
Process of claim 1 wherein sulfur losses in the process are compensated for by adding sulfur containing substances to the fluidized bed reaction zone.

References Cited (Backward Citations)

US3579616A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-06-19 1981-12-19 1982-06-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-06-19 1985-12-19 1986-06-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-06-19 1989-12-19 1990-06-20 $7700.00 Window Closed / Lapsed

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