A gas-solid short contact time reaction device and its application

A technology of contact time and reaction device, which is applied in the direction of climate sustainability, bulk chemical production, condensation hydrocarbon production with dehydrocarbons, etc. Solve problems such as single means, achieve the effects of reducing gas-solid contact time, improving energy utilization rate, and reducing wear

Active Publication Date: 2022-04-12
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the depth of methane oxidation is only regulated by means of oxygen graded intake, and the control method is single, and the fluidization zone is directly connected to the riser, so the matching between fluidization states is difficult to control, and it is easy to cause large fluctuations in product composition and large bed pressure drop

Method used

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  • A gas-solid short contact time reaction device and its application
  • A gas-solid short contact time reaction device and its application
  • A gas-solid short contact time reaction device and its application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0067] This embodiment provides a figure 1 The reaction device with short gas-solid contact time shown includes a riser reactor 1 , a settling reactor 2 , a gas-solid separator 3 and a feeding device 4 .

[0068] The riser reactor 1 is installed at the bottom of the settling reactor 2, and the discharge port of the riser reactor 1 is higher than the bottom discharge port of the settling reactor 2;

[0069] The gas-solid separator 3 is used for the separation of product gas and catalyst particles in the product of the settling reactor 2;

[0070] The feeding device 4 collects the catalyst particles transported by the bottom outlet and the catalyst particles obtained by the gas-solid separator 3, and returns the collected catalyst particles to the bottom of the riser;

[0071] The bottom of the riser is provided with a feed gas inlet pipe 11 .

[0072] A flow control device 5 is provided on the return material pipeline connecting the bottom discharge port and the return materi...

Embodiment 2

[0076] This embodiment provides a figure 2 The reaction device with short gas-solid contact time shown includes a riser reactor 1 , a settling reactor 2 , a gas-solid separator 3 and a feeding device 4 .

[0077] The riser reactor 1 is installed at the bottom of the settling reactor 2, and the discharge port of the riser reactor 1 is higher than the bottom discharge port of the settling reactor 2;

[0078] The gas-solid separator 3 is used for the separation of product gas and catalyst particles in the product of the settling reactor 2;

[0079] The feeding device 4 collects the catalyst particles transported by the bottom outlet and the catalyst particles obtained by the gas-solid separator 3, and returns the collected catalyst particles to the bottom of the riser;

[0080] The bottom of the riser is provided with a feed gas inlet pipe 11 .

[0081] Four oxygen distributors 7 are evenly arranged in the riser.

[0082] A flow control device 5 is provided on the return mate...

Embodiment 3

[0087] This embodiment provides a image 3 The reaction device with short gas-solid contact time shown includes a riser reactor 1 , a settling reactor 2 , a gas-solid separator 3 and a feeding device 4 .

[0088] The riser reactor 1 is installed at the bottom of the settling reactor 2, and the discharge port of the riser reactor 1 is higher than the bottom discharge port of the settling reactor 2;

[0089] The gas-solid separator 3 is used for the separation of product gas and catalyst particles in the product of the settling reactor 2;

[0090] The feeding device 4 collects the catalyst particles transported by the bottom outlet and the catalyst particles obtained by the gas-solid separator 3, and returns the collected catalyst particles to the bottom of the riser;

[0091] The bottom of the riser is provided with a feed gas inlet pipe 11 .

[0092] Four oxygen distributors 7 are evenly arranged in the riser.

[0093] A flow control device 5 is provided on the return mater...

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Abstract

The invention belongs to a reaction device with short gas-solid contact time and its application. The reaction device includes a riser reactor, a settling reactor, a gas-solid separator and a feeding device; the riser reactor is installed in the settling At the bottom of the reactor, the discharge port of the riser reactor is higher than the bottom discharge port of the settling reactor; the gas-solid separator is used for the separation of product gas and catalyst particles; the return device collects the bottom discharge port of the settling reactor The transported catalyst particles and the catalyst particles obtained by the gas-solid separator are returned to the bottom of the riser; the bottom of the riser is provided with a feed gas inlet pipe. The present invention realizes short-term contact between the catalyst particles and the gas through the riser reactor, avoiding the deep oxidation of target products such as ethylene, and at the same time, the catalyst particles carry the reaction heat and perform heat exchange outside the reactor, so that the temperature of the hot spot in the reactor is reduced , which is conducive to improving the selectivity of the target product.

Description

technical field [0001] The invention belongs to the technical field of reaction engineering, and relates to a reaction device and its application, in particular to a reaction device with short gas-solid contact time and its application. Background technique [0002] Ethylene is the basic raw material for synthetic plastics, synthetic fibers, synthetic rubber, medicine, dyes, pesticides, new chemical materials and daily chemical products, and is the most widely used basic organic chemical raw material. At present, ethylene is mainly obtained in two ways, one is through direct cracking of petroleum raw materials such as crude oil and oilfield gas; the other is through further steam pyrolysis of naphtha, a relatively light hydrocarbon mixture obtained from petroleum refining. With the increasing shortage of petroleum resources and the increasing demand for ethylene, opening up a new route for ethylene production has become a research hotspot at home and abroad. [0003] In 198...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/00B01J8/08C07C2/84C07C11/04
CPCB01J8/0035B01J8/007B01J8/085B01J8/087C07C2/84C07C11/04Y02P20/50Y02P20/52Y02P20/584
Inventor 刘姣张战国岳君容崔彦斌许光文
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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