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Absorption stabilization process and system

An absorption stabilization system and absorption stabilization technology, applied in the petroleum industry, gas mixture processing, hydrocarbon oil treatment products, etc., can solve problems such as economic losses, and achieve the effects of reducing process energy consumption, reducing circulation, and reducing demand

Active Publication Date: 2019-03-19
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] At present, the distillation range of diesel oil in my country is 180°C to 360°C, and the final boiling point of gasoline is 205°C. Therefore, there is a problem that a certain amount of gasoline is entrained in diesel oil. Due to the low value of diesel oil, the value of gasoline is high, so low-value diesel oil Carrying some high-quality gasoline will undoubtedly cause certain economic losses

Method used

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Examples

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Effect test

Embodiment 1

[0046] Taking a 500,000-ton / year FCC-type catalytic cracking unit absorption stabilization system in China as an example, the ASPEN PLUS process simulation software is used to simulate the process of the present invention, and catalytic diesel is used as the absorbent. The key process parameters are as follows: the outlet of the rich gas compressor The pressure is 1.4 MPa, the operating temperature of the desorption gas balance tank is 40 °C, the absorption tower bottom liquid entering the desorption gas balance tank accounts for 40 wt% of the total liquid phase output at the bottom of the absorption tower, the operating temperature of the rich gas balance tank is 40 °C, and the rich gas balance tank is The liquid-phase heat exchange in the gas balance tank reaches 80°C and enters the desorption tower. The absorption tower is equipped with an intercooler and the return tower temperature is 35°C. The ethane content in the deethanized gasoline at the bottom of the desorption tower...

Embodiment 2

[0048]Compared with Example 1, the difference is that the mixture of 1-butyl-3-methylimidazolium hexafluoroborate and sodium acetate (sodium acetate is 5wt%) is used as absorbent, and the key process parameters are as follows: The outlet pressure of the compressor is 1.4 MPa, the operating temperature of the desorption gas balance tank is 40 ℃, the absorption tower bottom liquid entering the desorption gas balance tank accounts for 40wt% of the total liquid phase output at the bottom of the absorption tower, and the operating temperature of the rich gas balance tank is 40 ℃ , the rich gas balance tank liquid-phase heat exchange to 80 ℃ enters the desorption tower, the absorption tower is equipped with an intercooler and the return temperature of the tower is 35 ℃, the ethane content in the deethanized gasoline at the bottom of the desorption tower is 0.1wt%, and the absorption amount of light gasoline is supplemented 12 t / h. The internal circulation of the absorbent is 30 t / h,...

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Abstract

The invention provides an absorption-stabilization technology and system. The system comprises a gas-liquid balance tank, a rich gas compressor, a rich gas balance tank, an absorption tower, a desorption tower, a stabilization tower, a re-absorption tower, a regeneration tank, a desorption gas balance tank and a vacuum pump. The invention further provides the absorption-stabilization technology utilizing the absorption-stabilization system. By adopting the absorption-stabilization technology and system, provided by the invention, the concentration of liquefied gas in dry gas is greatly reduced; and meanwhile, the yield of catalytic gasoline and the liquefied gas can be improved and the energy consumption of the system is greatly reduced.

Description

technical field [0001] The invention relates to the petroleum refining industry, in particular to a process and a system for stabilizing the absorption of devices such as catalytic cracking and delayed coking. Background technique [0002] The absorption stabilization system is the post-treatment process of the catalytic cracking unit and the delayed coking unit in the petroleum refining industry. Its purpose is to use the principle of absorption and rectification to separate the rich gas and naphtha in the oil-gas separation tank at the top of the fractionation tower into dry gas ( C 2 Below), liquefied petroleum gas (C 3 、C 4 ) and stable gasoline with qualified vapor pressure. The optimization of the unit and process flow of the absorption stabilization system plays a very important role in the energy saving and efficiency enhancement of catalytic cracking and delayed coking units. [0003] At present, the absorption-stabilization process flow of most refineries is: t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G70/04C10G70/06
CPCC10G70/041C10G70/06C10G2400/02C10G2400/04
Inventor 高明薄德臣张英张龙陈建兵
Owner CHINA PETROLEUM & CHEM CORP
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