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Shutdown gas ethane pipeline restart system and method

A technology of restarting and ethane, applied in the pipeline system, gas/liquid distribution and storage, mechanical equipment, etc., can solve the problems of easy generation of liquid ethane, increase pipeline investment, waste ethane products, etc., and achieve investment saving , reduce waste, improve the effect of operating pressure

Pending Publication Date: 2019-02-19
CHINA PETROLEUM ENG & CONSTR +1
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  • Claims
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AI Technical Summary

Problems solved by technology

Although these two methods can avoid the formation of liquid ethane in the pipeline during the shutdown process, there are certain deficiencies: in the first method, the pipeline adopts the low-pressure transportation method. Amplification has the problem of large pipe diameter, which increases pipeline investment; in the second method, the pressure relief during stoppage not only wastes a certain amount of ethane product, but also increases the pipeline pressure after the medium is filled in the restart process. Also prone to liquid ethane, causing low temperature problems

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  • Shutdown gas ethane pipeline restart system and method

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Embodiment Construction

[0028] A gaseous ethane pipeline stop and restart system, such as figure 1 As shown, including: upstream main line ball valve 100, upstream main line bypass regulating valve 101, flow transmitter 102, temperature transmitter 103, pressure transmitter 104, main line pipeline 1, temperature transmitter 2, pressure transmitter 3. Downstream main line ball valve 4, downstream main line regulating valve 5, post-valve flow transmitter 6, post-valve pressure transmitter 19, post-valve temperature transmitter 20, bypass ball valve 7, bypass primary control valve 8, Bypass branch 9 / 18, bypass electric heating branch pipe 10 / 11 / 12 / 13, bypass temperature transmitter 14 / 15 / 16 / 17, reserved pressure stabilizer interface 21, downstream main line ball valve 23, bypass Secondary regulating valve 22 .

[0029] Among them, the upstream main line ball valve 100, the upstream main line bypass regulating valve 101, the flow transmitter 102, the temperature transmitter 103, the pressure transmitter...

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Abstract

The invention discloses a shutdown gas ethane pipeline restart system and method. The system comprises a main line start point valve group and temperature, pressure and flow detection system, a main line tail end valve group and temperature, pressure and flow detection system and a main line tail end bypass valve group and tracing pipeline system. By means of the shutdown gas ethane pipeline restart system, operation pressure is provided by an ethane pipeline, it is allowed that liquid ethane is formed in a pipeline, and the pipe diameter is reduced; in the restart process, when gas ethane enters the upstream, ethane is exhausted through a bypass to control the ethane gas emission, heat is exchanged between new ethane and accumulated ethane, and accumulated liquid ethane is slowly gasifiedby reducing pipeline pressure within a small range; in the restart process, by means of the bypass stainless steel valve group and tracing pipeline system, throttled ethane is prevented from producing low-temperature influences on the pipeline system, the temperature is further improved at a certain degree, and throttled ethane is prevented from producing low-temperature influence on the downstream system; and in the restart process, ethane continuously exhausted in the start process can enter the downstream system.

Description

technical field [0001] The invention relates to a system and a method for restarting after the gaseous ethane pipeline is stopped and restarted. Background technique [0002] In recent years, the market demand for ethylene has become increasingly strong, and the traditional raw material naphtha cannot be met in time, and ethane is also a good ethylene raw material, so refineries have a large demand for ethane. With the advent of the shale gas revolution in the United States, a large amount of ethane can be exported and supplied to refineries after extraction; at the same time, the domestic light hydrocarbon recovery process is becoming more and more mature, and self-produced ethane can also supplement the raw material gap of refineries. Therefore, there is a huge demand for supporting the construction of ethane pipelines from the ethane source to the refinery. Ethane products, as a class of natural gas accessory products with a lighter molar mass, have a high saturated vapo...

Claims

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Application Information

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IPC IPC(8): F17D1/04F17D3/01F17D5/00
CPCF17D1/04F17D3/01F17D5/00
Inventor 陈俊文谌贵宇李国军汤晓勇缪晖边云燕祝疆余洋王晓玉代卿张双蕾郭翔宇彭洋姜炜杨轶杨帆郭艳林王磊
Owner CHINA PETROLEUM ENG & CONSTR
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