Process and plant for thermal decomposition of aluminium chloride hydrate into aluminium oxide

Patent metadata

Field	Value
Publication number	US-2022177321-A1
Application number	US-202117542779-A
Country	US
Kind code	A1
Filing date	Dec 6, 2021
Priority date	Jun 7, 2019
Publication date	Jun 9, 2022
Grant date	—

Abstract

A process and its relating plant for thermal conversion of aluminum chloride hydrate into aluminum oxide and gaseous hydrogen chloride. In a first step, aluminum chloride hydrate is fed into a decomposition reactor where it is heated to a temperature between 120 and 400° C. Afterwards, the partially decomposed aluminum chloride hydrate is finally calcined to aluminum oxide at a temperature between 850 and 1200° C. in a second reactor. The aluminum chloride hydrate is admixed with aluminum oxide in an intensive mixer with a mass ratio between 1:1 and 10:1 aluminum chloride hydrate to aluminum oxide for using a fluidized bed reactor as a decomposition reactor.

First claim

1 .- 16 . (canceled)

17 . A process for thermal conversion of aluminum chloride hydrate into aluminum oxide and gaseous hydrogen chloride by partially decomposing the aluminum chloride hydrate into a decomposition reactor by heating to a temperature between 120 and 400° C. and then calcining the partially decomposed aluminum chloride hydrate in the calcining reactor to aluminum oxide at a temperature between 850 and 1200° C., wherein the aluminum chloride hydrate is admixed with aluminum oxide in an intensive mixer with a mass ratio between 1:1 and 10:1 aluminum chloride hydrate to aluminum oxide and that the resulting mixture is fed into the decomposition reactor which is a fluidized bed reactor.

18 . The process according to claim 17 , wherein at least parts of the aluminum oxide from the calcination is recirculated into the decomposition.

19 . The process according to claim 18 , wherein the recirculated aluminum oxide features a temperature between 600 and 1100° C. into the decomposition reactor.

20 . The process according to claim 17 , wherein at least parts of the aluminum oxide from the decomposition is recirculated into the decomposition.

21 . The process according to claim 20 , wherein the recirculated aluminum oxide for the admixing in the mixer has a temperature below 100° C.

22 . The process according to claim 17 , wherein the aluminum chloride hydrate is passed through a lump breaker and/or a dryer before being fed into the mixer.

23 . The process according to claim 17 , wherein the calcination takes part in a fluidized bed/or a rotary kiln.

24 . The process according to claim 17 , wherein decomposition and/or calcination take/s in a circulating fluidized bed.

25 . The process according to claim 17 , wherein steam and/or air is added to the decomposition and/or air and/or a fuel is added to the calcination.

26 . The process according to claim 17 , wherein the off-gases are passed separately from the decomposition and the calcination to an off-gas treatment.

27 . The process according to claim 26 , wherein the off-gas treatment contains a quenching step and/or a scrubbing step and/or an absorption step.

28 . The process according to claim 17 , wherein the mixing is performed in a mixer with knifes and/or ploughshares and/or paddles.

29 . The process according to claim 28 , wherein the knifes rotate at least twice as fast as the ploughshares.

30 . The process according to claim 17 , wherein the residence time in the mixer is more than one minute.

Assignees

• Metso Outotec Finland Oy

Inventors

• Von Garnier Agnes
• Perander Linus
• Schneider Günter
• Sturm Peter

Classifications

• C01B7/035

  Preparation of hydrogen chloride from chlorides · CPC title

• B01J8/38

  with fluidised bed containing a rotatable device or being subject to rotation {or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it} · CPC title

• C01F7/306 Primary

  Thermal decomposition of hydrated chlorides, e.g. of aluminium trichloride hexahydrate · CPC title

• Y02E60/36

  Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title