Method and apparatus for producing inorganic powder using chemical vapor synthesis
US-2025100050-A1 · Mar 27, 2025 · US
US11591233B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11591233-B2 |
| Application number | US-202117542779-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 6, 2021 |
| Priority date | Jun 7, 2019 |
| Publication date | Feb 28, 2023 |
| Grant date | Feb 28, 2023 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The invention relates to 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.
Opening claim text (preview).
The invention claimed is: 1. A process for thermal conversion of aluminum chloride hydrate into aluminum oxide and gaseous hydrogen chloride by partially decomposing the aluminum chloride hydrate in a decomposition reactor by heating to a temperature between 120 and 400° C. and then calcining the partially decomposed aluminum chloride hydrate in a calcining reactor to aluminum oxide at a temperature between 850 and 1200° C., wherein the aluminum chloride hydrate is admixed with aluminum oxide in a 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. 2. The process according to claim 1 , wherein at least parts of the aluminum oxide from the calcination is recirculated in the decomposition reactor. 3. The process according to claim 2 , wherein the recirculated aluminum oxide features a temperature between 600 and 1100° C. in the decomposition reactor. 4. The process according to claim 1 , wherein at least parts of the aluminum oxide from the decomposition is recirculated in the decomposition reactor. 5. The process according to claim 4 , wherein the recirculated aluminum oxide for the admixing in the mixer has a temperature below 100° C. 6. The process according to claim 1 , wherein the aluminum chloride hydrate is passed through a lump breaker and/or a dryer before being fed into the mixer. 7. The process according to claim 1 , wherein the calcination takes part in a fluidized bed/or a rotary kiln. 8. The process according to claim 1 , wherein the decomposition and/or the calcination occur in a circulating fluidized bed. 9. The process according to claim 1 , wherein steam and/or air is added to the decomposition and/or air and/or a fuel is added to the calcination. 10. The process according to claim 1 , wherein off-gases are passed separately from the decomposition and the calcination to an off-gas treatment. 11. The process according to claim 10 , wherein the off-gas treatment contains a quenching step and/or a scrubbing step and/or an absorption step. 12. The process according to claim 1 , wherein the mixing is performed in the mixer with knifes and/or ploughshares and/or paddles. 13. The process according to claim 12 , wherein the knifes rotate at least twice as fast as the ploughshares. 14. The process according to claim 1 , wherein the residence time in the mixer is more than one minute.
Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title
Preparation of hydrogen chloride from chlorides · CPC title
Thermal decomposition of hydrated chlorides, e.g. of aluminium trichloride hexahydrate · CPC title
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
Related publications grouped by family.
Answers are generated from the same data shown on this page.