Synthesis method for highly selective 2-methylallyl chloride and synthesis reactor thereof

US11407698B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11407698-B2
Application numberUS-201816759931-A
CountryUS
Kind codeB2
Filing dateOct 10, 2018
Priority dateJan 29, 2018
Publication dateAug 9, 2022
Grant dateAug 9, 2022

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

The present invention relates to a synthesis method and synthesis reactor of high-selectivity 2-methylallyl chloride by taking isobutylene and chlorine gas as raw materials and performing a gas-phase chlorination reaction in a microchannel reactor with a cooling surface. The isobutylene and the chlorine gas are reacted in a T-shaped microchannel reactor, and the mixing speed is extremely fast. Meanwhile, the huge heat exchange area per unit volume can ensure that the reaction proceeds stably at a substantially constant temperature and has good controllability. Therefore, side reactions caused by excessive local temperature can be effectively suppressed, the reaction selectivity is high, and no coking phenomenon occurs.

First claim

Opening claim text (preview).

The invention claimed is: 1. A synthesis reactor assembly for producing high-selectivity 2-methyl-3-chloroallyl, comprising: an isobutylene supply having isobutylene; a chlorine gas supply having chlorine gas; a plurality of synthesis reactors arranged side-by-side, each synthesis reactor comprising: a synthesis reaction tube fluidly coupled with an isobutylene inlet tube configured to receive the isobutylene from the isobutylene supply and fluidly coupled with a chlorine gas inlet tube configured to receive chlorine gas from the chlorine gas supply; wherein the isobutylene inlet tube, the chlorine gas inlet tube, and the synthesis reaction tube are connected in tee form; wherein the isobutylene inlet tube and the chlorine gas inlet tube are in a U-shape, and an upper end of the synthesis reaction tube is connected to the U-shape to form the tee form; and wherein the isobutylene inlet tube, the chlorine gas inlet tube, and the synthesis reaction tube have a diameter of 0.2-0.5 mm, respectively; a cooling jacket wrapped around the plurality of synthesis reactors arranged side-by-side; and a cooling surface of each synthesis reactor has a heat exchange area of 8000-20000 m 2 /m 3 based on an actual reaction volume of each synthesis reactor. 2. The synthesis reactor assembly for producing high-selectivity 2-methyl-3-chloroallyl of claim 1 , comprising: isobutylene in each isobutylene inlet tube; and chlorine gas in each chlorine gas inlet tube. 3. A method for synthesizing high-selectivity 2-methyl-3-chloroallyl, comprising: providing the synthesis reactor assembly of claim 1 ; feeding isobutylene from the isobutylene supply through each isobutylene inlet tube and chlorine gas from the chlorine gas supply through each chlorine gas inlet tube; mixing the isobutylene and the chlorine gas at each tee form to produce a mixture of isobutylene and chlorine gas; and performing a gas-phase chlorination reaction of the mixture of isobutylene and chlorine gas in each synthesis reaction tube to produce 2-methyl-3-chloroallyl. 4. The method according to claim 3 , wherein an excess amount of isobutylene is added in the chlorination reaction. 5. The method according to claim 4 , wherein a molar ratio of the isobutylene to the chlorine gas is 1.005˜1.02:1. 6. The method according to claim 3 , wherein the chlorination reaction temperature is 0˜30° C. and the chlorination reaction residence time is 0.1˜1 second.

Assignees

Inventors

Classifications

  • Heat exchange · CPC title

  • Tubular reactors · CPC title

  • One or more tube-shaped elements · CPC title

  • C07C17/10Primary

    of hydrogen atoms (combined with addition of halogens to unsaturated hydrocarbons C07C17/06) · CPC title

  • Fouling of the reactor or the process equipment · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US11407698B2 cover?
The present invention relates to a synthesis method and synthesis reactor of high-selectivity 2-methylallyl chloride by taking isobutylene and chlorine gas as raw materials and performing a gas-phase chlorination reaction in a microchannel reactor with a cooling surface. The isobutylene and the chlorine gas are reacted in a T-shaped microchannel reactor, and the mixing speed is extremely fast. …
Who is the assignee on this patent?
Univ Zhejiang, Zhejiang Huangma Tech Co Ltd
What technology area does this patent fall under?
Primary CPC classification C07C17/10. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Aug 09 2022 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 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).