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A method and system for separating hydrogen from catalytic cracking dry gas

A catalytic cracking and separation method technology, applied in the field of hydrogen separation in catalytic cracking dry gas, can solve the problem that hydrogen is not widely used, reduce the requirements of operating space and operating procedures, reduce energy consumption, and save investment. Effect

Active Publication Date: 2018-06-29
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Summary
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  • Description
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AI Technical Summary

Problems solved by technology

Due to limited field operation space and energy consumption of gas compressors, hydrate separation technology has not been widely used in the separation of hydrogen in catalytic cracking dry gas.

Method used

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  • A method and system for separating hydrogen from catalytic cracking dry gas
  • A method and system for separating hydrogen from catalytic cracking dry gas

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Experimental program
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Effect test

Embodiment 1

[0039] Hydrate working fluid is tetrabutylammonium bromide (English abbreviation: TBAB), and its concentration is 10wt%;

[0040] The composition of catalytic cracking dry gas is shown in Table 1 below:

[0041] Table 1 Composition of catalytic cracking dry gas

[0042] composition

[0043] use as figure 1 The process flow and figure 2 For the specific process, please refer to the description of the above separation method, and the process parameters involved are as follows:

[0044] 1) The pressure of catalytic cracking dry gas is 1.6MPa.

[0045] 2) When the hydrate working fluid enters the hydration reactor, the temperature is 8°C and the pressure is 5MPa.

[0046] 3) The pressure of the hydrate working fluid passing through the throat section of the hydration reactor is 1.2MPa.

[0047] 4) The fluid formed by the hydrate working liquid and the hydrogen in the catalytic cracking dry gas has a pressure of 4.5 MPa in the stable section of the hydration reactor...

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Abstract

The invention provides a separation method of hydrogen from catalytic cracking dry gas and a system therefor. The separation method includes the steps of: performing a hydration reaction to the catalytic cracking dry gas and collecting hydrogen-rich gas. A hydration reactor for the hydration reaction includes the following structures: a chamber, in the flowing direction of a hydrate working fluid, of the hydration reactor comprises an inlet section, a throat pipe section and a stable section, wherein the flowing area of the throat pipe section is less than those in both the inlet section and the stable section. An air inlet is arranged on the side wall, which is relative to the throat pipe section, of the chamber of the hydration reactor. The separation method is free of a step of compressing and pressurizing the catalytic cracking dry gas in a process of separating the hydrogen from the catalytic cracking dry gas through a hydrate separation method in the prior art, so that the separation method is reliable in operation and has strong practical industrial application aviliability.

Description

technical field [0001] The invention relates to a method for separating hydrogen from catalytic cracking dry gas and a system thereof, belonging to the technical field of chemical industry. Background technique [0002] Since catalytic cracking dry gas contains a large amount of hydrogen and ethylene, their comprehensive utilization can save millions of tons of ethylene cracking raw materials and hydrogen production raw materials every year, and has billions of economic benefits. In recent years, many researchers have done a lot of research on the separation and recovery of hydrogen and ethylene in catalytic cracking dry gas. The existing methods for separating hydrogen and ethylene in catalytic cracking dry gas include cryogenic separation, absorption separation, membrane Separation method and hydrate separation method. However, the above methods have different defects, which restrict the recovery of hydrogen and ethylene in the catalytic cracking dry gas. [0003] For ex...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B3/52
Inventor 郭绪强陈光进
Owner CHINA UNIV OF PETROLEUM (BEIJING)
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