IP Library Granted Patent US 10,029,966
Granted Patent B2
US 10,029,966 · App. 15/268,456 · Granted Jul 24, 2018

Method and reaction equipment for preparing dimethyl ether and olefin from methanol

Inventors: Shuai Hu (Shanghai, CN); Xin Jin (Shanghai, CN)
Assignees: CHINA PETROLEUM & CHEMICAL CORPORATION; SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY SINOPEC
C07C41/09B01J8/0453B01J8/0457B01J8/0492B01J8/0496B01J8/065C07C1/20B01J2208/00256B01J2208/00548B01J2208/027Y02P20/52
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Quick Facts
Patent No.
US 10,029,966
App. No.
15/268,456
Granted
Jul 24, 2018
Kind
B2
Abstract

The present invention relates to a method for preparing dimethyl ether from methanol which is carried out in a reaction device arranged with a plurality of catalyst bed layers connected in series, and comprises: dividing the reactant stream that contains methanol into n substreams, and feeding these different substreams into the reaction device through top feed ports or side feed ports between the catalyst bed layers of the reaction device for methanol-to-dimethyl ether reaction; wherein, the temperature T1 of the substream fed into the first catalyst bed layer is controlled within the following range: 290−50K1≤T1≤150K1 2 −271K1+397.5; where, 1>K1≥0.5, and T1 is in unit of ° C.

Claims (34)

1. A method for preparing dimethyl ether from methanol carried out in a reaction device arranged with a plurality of catalyst bed layers connected in series, which method comprising:

dividing a reactant stream containing methanol into n substreams, n being an integer greater than 2, and feeding the n substreams into the reaction device through top feed port or side feed ports between catalyst bed layers of the reaction device to undergo a methanol-to-dimethyl ether reaction;

wherein, according to flow directions of the reactant stream, the n substreams each have a flow rate F1˜Fn, respectively, allocation proportions Ki of the reactant in the substreams are Fi/F0, F0 being the sum of F1˜Fn, i being an integer in the range of 1˜n, and n being an integer greater than 2, and

wherein the substream fed into the first catalyst bed layer has a temperature T1 that is controlled within the following range:

290−50 K 1≤ T 1≤150 K 1 2 −271 K 1+397.5

where 1>K1≥0.5, and T1 is in unit of ° C.

2. The method for preparing dimethyl ether from methanol according to claim 1 , wherein 2≤n≤8.

3. The method for preparing dimethyl ether from methanol according to claim 1 , wherein 0.95≥K1≥0.6.

4. The method for preparing dimethyl ether from methanol according to claim 1 , wherein 1>K1≥0.6.

5. The method for preparing dimethyl ether from methanol according to claim 1 , wherein the allocation proportion Ki of the reactant in the substream i

Ki

(

1

-

i

=

1

i

-

1

K

i

)

×

50

%

,

wherein i≠1.

6. The method for preparing dimethyl ether from methanol according to claim 1 , wherein the number of the catalyst bed layers is greater than or equal to n.

7. The method for preparing dimethyl ether from methanol according to claim 1 , wherein the reaction device comprises one or more fixed bed reactors, with said a plurality of catalyst bed layers arranged in the one or more fixed bed reactors.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 20, 2016
From: HU, SHUAI; JIN, XIN
To: CHINA PETROLEUM & CHEMICAL CORPORATION; SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY SINOPEC
Reel/Frame 039801/0614 →
Priority Claims (1)
CN 2015 1 0537517 · Nov 17, 2015 · national
Continuity (1)
Related Publication 20170137357A1 · May 18, 2017