Refinery mixed dry gas recovery system and recovery method

A refinery mixed dry gas and recovery system technology, applied in chemical instruments and methods, gas mixture processing, hydrocarbons, etc., can solve the problems of limited process applicability, low recovery rate, large investment, etc., to avoid Adverse effects, strong applicability, and the effect of less total dosage

Active Publication Date: 2015-04-29
CHINA PETROLEUM & CHEM CORP +1
View PDF9 Cites 41 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0014] In order to solve the problems of how to centrally recover and utilize saturated dry gas and unsaturated dry gas, as well as existing processes such as large investment, high energy consumption, low recovery rate, and limited process applicability, the invention provides a refinery mixing Dry gas recovery system and method

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Refinery mixed dry gas recovery system and recovery method
  • Refinery mixed dry gas recovery system and recovery method
  • Refinery mixed dry gas recovery system and recovery method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment

[0063] Such as figure 1 As shown, a refinery mixed dry gas recovery system includes: an absorption tower, a desorption tower, a purification device, a rough fractionation tower, a gasoline absorption tower and a gasoline desorption tower;

[0064] The compressor is connected to the heat exchanger and then connected to the absorption tower. The top of the absorption tower is connected to the gasoline absorption tower, and the bottom of the absorption tower is connected to the desorption tower; The top is connected to the upper part of the absorption tower, and the bottom of the gasoline desorption tower is connected to the upper part of the gasoline absorption tower. A reboiler is installed at the bottom of the absorption tower.

[0065] The dry gas composition is shown in Table 1,

[0066] Table 1

[0067]

[0068]

[0069] Refinery dry gas includes PSA stripping gas, light hydrocarbon dry gas and FCC dry gas, of which PSA stripping gas and light hydrocarbon dry gas ...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention discloses a refinery mixed dry gas recovery system and a recovery method. The system comprises an absorption tower, a desorption tower, a rough separation tower, a purification device, a gasoline absorption tower and a gasoline desorption tower, wherein a compressor is connected with a heat exchanger and then is connected with the absorption tower, the top of the absorption tower is connected with the gasoline absorption tower, and the bottom of the absorption tower is connected with the desorption tower; the top of the desorption tower is connected with the purification device and then is connected with the rough separation tower, the bottom of the gasoline absorption tower is connected with the gasoline desorption tower, the top of the gasoline desorption tower is connected with the upper part of the absorption tower, and the bottom of the gasoline desorption tower is connected with the upper part of the gasoline absorption tower. According to the recovery system, a C2 component is recovered from dry gas through one set of absorption-desorption, a tower top gas phase of the desorption tower enters the rough separation tower, and an entrained absorbent is recovered through another set of absorption-desorption; ethylene-rich gas is recovered from the tower top of the rough separation tower and is delivered to an ethylene unit demethanizer, and ethane-rich gas is recovered from a reactor of the rough separation tower and is delivered to an ethylene unit cracking furnace. According to the recovery method disclosed by the invention, the flow is simple, the recovery rate is high, saturated hydrocarbons and unsaturated hydrocarbons are treated separately, and the operation of an ethylene unit is hardly affected.

Description

technical field [0001] The invention relates to the field of dry gas treatment, and more specifically relates to a refinery dry gas recovery system and recovery method. Background technique [0002] Refinery dry gas mainly comes from the secondary processing of crude oil, such as catalytic cracking, thermal cracking, delayed coking, hydrocracking, etc. At present, most refineries in my country still burn the refinery dry gas as fuel gas, which has low utilization value and causes great waste of resources and environmental pollution. [0003] Generally, the content of ethylene in catalytic dry gas is high, which belongs to unsaturated dry gas. Saturated dry gas usually comes from PSA desorption gas, light hydrocarbon dry gas, hydrogenation dry gas, reforming dry gas, etc. Ethane and propane in saturated dry gas The content is relatively high, while the content of ethylene and propylene is very low. Therefore, the composition and application of enriched gas after recovery of...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): C07C7/11C07C7/00C07C11/04C07C9/06C10G70/06C10G70/00
Inventor 刘智信过良李琰李东风程建民廖丽华罗淑娟王婧王宇飞康锴
Owner CHINA PETROLEUM & CHEM CORP
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products