The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Dec. 01, 2020

Filed:

Jan. 19, 2017
Applicant:

Purac Biochem Bv, Gorinchem, NL;

Inventors:

Johannes Jeichienus De Vries, Gorinchem, NL;

Raymon Frediansyah, Gorinchem, NL;

Assignee:

PURAC BIOCHEM BV, Gorinchem, NL;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01F 5/00 (2006.01); C01F 5/30 (2006.01); C01B 7/03 (2006.01); C01F 5/10 (2006.01); C07C 51/02 (2006.01); B01D 1/26 (2006.01); B01D 1/28 (2006.01); C12P 7/40 (2006.01); C12P 7/42 (2006.01); C12P 7/44 (2006.01); C12P 7/46 (2006.01); C12P 7/48 (2006.01); C12P 7/52 (2006.01); C12P 7/56 (2006.01); C12P 17/04 (2006.01);
U.S. Cl.
CPC ...
C01F 5/30 (2013.01); B01D 1/26 (2013.01); B01D 1/28 (2013.01); C01B 7/035 (2013.01); C01F 5/10 (2013.01); C07C 51/02 (2013.01); C12P 7/40 (2013.01); C12P 7/42 (2013.01); C12P 7/44 (2013.01); C12P 7/46 (2013.01); C12P 7/48 (2013.01); C12P 7/52 (2013.01); C12P 7/56 (2013.01); C12P 17/04 (2013.01);
Abstract

Magnesium chloride solutions including providing aqueous magnesium chloride solution with magnesium chloride concentration of 10-30 wt. % to concentration step where water is evaporated, resulting in concentrated magnesium chloride solution with magnesium chloride concentration of 30-50 wt. %, wherein concentration step is carried out in one or more stages, wherein at least one of the stages is conducted at elevated pressure, withdrawing concentrated magnesium chloride solution from concentration step, and providing it to thermohydrolysis reactor of at least 300° C., withdrawing MgO from thermohydrolysis reactor in solid form, and withdrawing a HCl containing gas stream of at least 300° C. from thermohydrolysis reactor, providing the HCl-containing gas stream of at least 300° C. to cooling step, where HCl-containing gas stream is contacted with cooling liquid, withdrawing HCl-containing gas stream below 150° C. from cooling step, circulating cooling liquid through heat exchanger where energy is transferred to heating liquid which circulates from heat exchanger to concentration step.


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