Methods and systems to form propylene chlorohydrin from dichloropropane using Lewis acid

US10590054B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10590054-B2
Application numberUS-201916424878-A
CountryUS
Kind codeB2
Filing dateMay 29, 2019
Priority dateMay 30, 2018
Publication dateMar 17, 2020
Grant dateMar 17, 2020

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

There are provided methods and systems to form propylene chlorohydrin by hydrolysis of dichloropropane in presence of Lewis acid and to further form propylene oxide from the propylene chlorohydrin.

First claim

Opening claim text (preview).

What is claimed is: 1. A method to form propylene chlorohydrin (PCH), comprising: hydrolyzing dichloropropane (DCP) to PCH in an aqueous solution comprising Lewis acid. 2. The method of claim 1 , wherein the Lewis acid is selected from the group consisting of silicon chloride; germanium chloride; tin chloride; boron chloride; aluminum chloride; gallium chloride; indium chloride; thallium chloride; phosphorus chloride; antimony chloride; arsenic chloride; copper chloride; zinc chloride; titanium chloride; vanadium chloride; chromium chloride; managanese chloride; iron chloride; cobalt chloride; nickel chloride; lanthanide chloride; and triflates. 3. The method of claim 1 , wherein the Lewis acid is selected from the group consisting of BCl 3 ; AlCl 3 ; GaCl 3 ; InCl 3 ; TlCl 3 ; CuCl 2 ; ZnCl 2 ; TiCl 3 ; TiCl 4 ; and LaCl 3 . 4. The method of claim 1 , wherein the Lewis acid is AlCl 3 ; GaCl 3 ; CuCl 2 ; or ZnCl 2 . 5. The method of claim 1 , wherein the Lewis acid is in a concentration in a range of about 0.1-6 mol/kg of the solution. 6. The method of claim 1 , wherein the aqueous solution further comprises HCl. 7. The method of claim 6 , wherein the HCl is a combination of the other HCl added to the hydrolysis step and the HCl co-produced during the hydrolysis step. 8. The method of claim 7 , wherein the HCl is in a concentration of between about 1-20 wt % HCl. 9. The method of claim 1 , wherein the aqueous solution further comprises one or more chloride salts. 10. The method of claim 9 , wherein the one or more chloride salts are alkali metal chloride and/or alkaline earth metal chloride. 11. The method of claim 10 , wherein the one or more chloride salts are sodium chloride, lithium chloride, potassium chloride, calcium chloride, magnesium chloride, barium chloride, strontium chloride, or combination thereof. 12. The method of claim 10 , wherein the one or more chloride salts are in a concentration between about 1-30 wt %. 13. The method of claim 1 , wherein concentration of the DCP in the hydrolysis reaction is between about 10-95% by volume. 14. The method of claim 1 , further comprising carrying out the hydrolysis in reaction conditions selected from temperature between 20° C.-200° C., pressure between 0-350 psig, residence time of less than two hours, and combinations thereof. 15. The method of claim 1 , wherein the hydrolysis results in PCH formed with selectivity of between 10-95 wt % and/or STY of more than 0.01. 16. The method of claim 1 , further comprising after hydrolysis, transferring the solution comprising PCH and DCP to epoxidation; and epoxidizing the PCH with a base to form PO in presence of the DCP. 17. A system to form PCH, comprising: a hydrolysis reactor comprising DCP in an aqueous solution comprising Lewis acid, wherein the reactor is configured to hydrolyze the DCP to PCH. 18. The system of claim 17 , wherein the Lewis acid is selected from the group consisting of silicon chloride; germanium chloride; tin chloride; boron chloride; aluminum chloride; gallium chloride; indium chloride; thallium chloride; phosphorus chloride; antimony chloride; arsenic chloride; copper chloride; zinc chloride; titanium chloride; vanadium chloride; chromium chloride; managanese chloride; iron chloride; cobalt chloride; nickel chloride; lanthanide chloride; and triflates. 19. The system of claim 17 , wherein the Lewis acid is AlCl 3 ; GaCl 3 ; CuCl 2 ; or ZnCl 2 . 20. The system of claim 17 , wherein the aqueous solution further comprises HCl. 21. The system of claim 17 , wherein the aqueous solution further comprises one or more chloride salts. 22. The system of claim 21 , wherein the one or more chloride salts are alkali metal chloride and/or alkaline earth metal chloride.

Assignees

Inventors

Classifications

  • C07C29/09Primary

    by hydrolysis · CPC title

  • the halogen not being fluorine · CPC title

  • C07C29/124Primary

    of halides · CPC title

  • to unsaturated hydrocarbons · CPC title

  • by simultaneous introduction of -OH groups and halogens · CPC title

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What does patent US10590054B2 cover?
There are provided methods and systems to form propylene chlorohydrin by hydrolysis of dichloropropane in presence of Lewis acid and to further form propylene oxide from the propylene chlorohydrin.
Who is the assignee on this patent?
Calera Corp
What technology area does this patent fall under?
Primary CPC classification C07C29/09. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Mar 17 2020 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 12 related publications on this page (citations in our corpus or others sharing the same primary CPC).