Thermal decomposition of magnesium chloride

Patent metadata

Field	Value
Publication number	US-2022235383-A1
Application number	US-202217717319-A
Country	US
Kind code	A1
Filing date	Apr 11, 2022
Priority date	Apr 1, 2014
Publication date	Jul 28, 2022
Grant date	—

Abstract

A method for conversion of magnesium chloride into magnesium oxide and HCl includes the steps of providing a magnesium chloride compound to a thermohydrolysis reactor, the reactor being at a temperature of at least 300° C., withdrawing MgO from the thermohydrolysis reactor in solid form, and withdrawing an HCl containing gas stream from the thermohydrolysis reactor. The magnesium chloride compound provided to the thermohydrolysis reactor may be a solid magnesium chloride compound which comprises at least 60 wt. % of MgCl2.4H2O.

First claim

1 . Method for conversion of magnesium chloride into magnesium oxide and HCl, comprising the steps of
providing a magnesium chloride compound to a thermohydrolysis reactor, the reactor being at a temperature of at least 300° C., withdrawing magnesium oxide from the thermohydrolysis reactor in solid form, and withdrawing a HCl-containing gas stream from the thermohydrolysis reactor, wherein the magnesium chloride compound provided to the thermohydrolysis reactor is a solid magnesium chloride compound which comprises:
at least 50 wt. % of MgCl 2 .4H 2 O; and,
less than 30 wt. % of magnesium chloride hexahydrate.

2 . The method according to claim 1 , wherein the magnesium chloride compound comprises less than 20 wt. % of magnesium chloride hexahydrate.

3 . The method according to claim 1 , wherein the magnesium chloride compound comprises less than 10 wt. % of magnesium chloride hexahydrate.

4 . The method according to claim 1 , wherein the magnesium chloride compound comprises less than 40 wt. % of the total of magnesium chloride anhydrate, magnesium chloride monohydrate, and magnesium chloride dehydrate.

5 . The method according to claim 1 , wherein the thermohydrolysis reactor is at a temperature of at least 350° C. and/or at a temperature below 1000° C.

6 . The method according to claim 1 , wherein the thermohydrolysis is carried out in the presence of a gas stream.

7 . The method according to claim 1 , wherein the thermohydrolysis reactor is a tube reactor wherein the magnesium chloride compound enters the reactor at or near one end of the reactor, further indicated as the feed end, and product magnesium oxide is withdrawn at or near the other end of the reactor, further indicated as the product end, while a gas stream enters the reactor at or near the product end, and a gas stream comprising HCl is withdrawn at or near the feed end.

8 . The method according to claim 1 further comprising steps of:
subjecting a magnesium chloride solution to a drying step at a temperature of 100-160° C. to form a magnesium chloride compound comprising at least 50 wt. % of MgCl 2 .4H 2 O and less than 30 wt. % of magnesium chloride hexahydrate;
providing said magnesium chloride compound to a thermohydrolysis reactor, the reactor being at a temperature of at least 300° C.; and,
withdrawing magnesium oxide from the thermohydrolysis reactor in solid form, and withdrawing a HCl-containing gas stream from the thermohydrolysis reactor.

9 . The method according to claim 8 , wherein the drying step is carried out at a temperature of 110-160° C.

10 . The method according to claim 8 , wherein the drying step is carried out in the presence of HCl.

11 . The method according to claim 10 , wherein the HCl present in the drying step is provided by providing the HCl-containing gas stream derived from the thermohydrolysis reactor to the drying step.

12 . The method according to claim 1 further comprising steps of
subjecting a carbon source to a fermentation step to form a carboxylic acid, which fermentation step comprises the steps of fermenting a carbon source by means of a micro-organism in a fermentation broth to form carboxylic acid and neutralizing at least part of the carboxylic acid by adding a magnesium base selected from magnesium oxide and magnesium hydroxide, thereby obtaining a magnesium carboxylate,
subjecting the magnesium carboxylate to an acidification step wherein the magnesium carboxylate is contacted with HCl in an aqueous environment to form an aqueous mixture comprising carboxylic acid and magnesium chloride,
subjecting the aqueous mixture comprising carboxylic acid and magnesium chloride to a separation step, to form an effluent comprising carboxylic acid and a magnesium chloride solution,
subjecting the magnesium chloride solution to a drying step at a temperature of 100-160° C. to form a magnesium chloride compound comprising at least 50 wt. % of MgCl 2 .4H 2 O and less than 30 wt. % of magnesium chloride hexahydrate,
providing said magnesium chloride compound to a thermohydrolysis reactor, the reactor being at a temperature of at least 300° C.,
withdrawing magnesium oxide from the thermohydrolysis reactor in solid form, and
withdrawing a HCl-containing gas stream from the thermohydrolysis reactor.

13 . The method according to claim 12 further comprising a step of recycling the magnesium oxide withdrawn from the thermohydrolysis reactor at least in part to the fermentation step.

14 . The method according to claim 12 , wherein the HCl-containing gas stream derived from the thermohydrolysis reactor is provided to the drying step.

15 . The method according to claim 14 further comprising a step of recycling the HCl-containing gas stream derived from the drying step at least in part to the acidification step.

16 . The method according to claim 12 , wherein the separated carboxylic acid is selected from the group consisting of mono, di- and tricarboxylic acids having at least two but no more than 6 carbon atoms (C2-C6 carboxylic acid).

17 . The method according to claim 12 , wherein the separated carboxylic acid is selected from the group consisting of: lactic acid; succinic acid; propionic acid; 3-hydroxypropionic acid; 2-, 3-, and 4-hydroxybutyric acid; citric acid; fumaric acid; itaconic acid; adipic acid; acrylic acid; levulinic acid; maleic acid; 2,5-furandicarboxylic acid; mandelic acid; malic acid; and, tartaric acid.

18 . Method for conversion of magnesium chloride into magnesium oxide and HCl, comprising the steps of
providing a magnesium chloride compound to a thermohydrolysis reactor, the reactor being at a temperature of at least 300° C., withdrawing MgO from the thermohydrolysis reactor in solid form, and withdrawing a HCl containing gas stream from the thermohydrolysis reactor, wherein the magnesium chloride compound provided to the thermohydrolysis reactor is a solid magnesium chloride compound which comprises: MgCl 2 .4H 2 O; and less than 30 wt. % of magnesium chloride hexahydrate.

Assignees

• Purac Biochem Bv

Inventors

• De Haan André Banier
• Bokhove Jeroen
• Laksmana Fesia Lestari

Classifications

• C01F5/10 Primary

  by thermal decomposition of magnesium chloride with water vapour · CPC title

• B01J8/067

  Heating or cooling the reactor (B01J8/062 takes precedence) · CPC title

• C01B7/035

  Preparation of hydrogen chloride from chlorides · CPC title

• C12P7/40 Primary

  containing a carboxyl group {including Peroxycarboxylic acids} · CPC title

• C01B7/03

  Preparation from chlorides · CPC title