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Simulation on venting process and valve opening control method for gas trunk pipelines
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作者 Li-Li Zuo An-Tai Jin +3 位作者 Qian Chen Qin-Long Dong Yuan-Xin Li Si-Rui Zhao 《Petroleum Science》 SCIE CAS CSCD 2022年第6期3016-3028,共13页
Determining the venting time of a gas trunk pipeline segment provides an important basis for formulating an emergency plan in the advent of unexpected accidents.As the natural gas venting process corresponds to the tr... Determining the venting time of a gas trunk pipeline segment provides an important basis for formulating an emergency plan in the advent of unexpected accidents.As the natural gas venting process corresponds to the transient flow,it is necessary to establish a transient hydraulic-thermal simulation model in order to determine the venting time.In this paper,based on two kinds of venting scenarios in which there is only one venting point in the venting system of a gas trunk pipeline segment—namely,where the venting point is either at one of the two ends or at the junction of two gas trunk pipeline segments—transient hydraulic-thermal simulation models are established.The models consist of gas flow governing equations,the gas state equation,gas physical property equations,initial conditions,and appropriate boundary conditions.The implicit central difference method is used to discretize the gas flow partial differential equations,and the trust-region-dogleg algorithm is used to solve the equations corresponding to each time step,in order to dynamically simulate the whole venting process.The judgment condition for the end of the venting process is that the average pressure of gas trunk pipeline segment is less than 0.11 MPa(actual pressure).Comparing the simulation results of the proposed model with those of the OLGA software and real operational data,we find that the venting time error is less than 10%.On this basis,a venting valve opening control principle is proposed,which prevents the venting noise from exceeded the specified noise value(85 d B)in the venting design of domestic gas pipeline projects.The established calculation model for venting time(dynamic simulation model)for a gas trunk pipeline segment and the proposed opening control principle of venting valve provide reference for the optimal operation of gas pipeline venting systems. 展开更多
关键词 gas pipeline Venting time Transient simulation Implicit central difference method valve opening control Method
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连续重整装置低负荷下待生剂提升问题的分析与解决
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作者 王添 孙伟 +3 位作者 沈博 徐耀东 董庆 董涛 《炼油技术与工程》 CAS 2021年第3期17-19,24,共4页
某企业连续重整装置在低负荷运行时待生催化剂(待生剂)提升操作发生变化,在反吹时甚至出现了提升中断的情况。深入分析原因发现,由于低负荷下反应系统压力下降,再生系统的分离料斗没有相应的降压方式,导致二次气控制阀开度增大、待生剂... 某企业连续重整装置在低负荷运行时待生催化剂(待生剂)提升操作发生变化,在反吹时甚至出现了提升中断的情况。深入分析原因发现,由于低负荷下反应系统压力下降,再生系统的分离料斗没有相应的降压方式,导致二次气控制阀开度增大、待生剂流动"逆压差"升高,由15 kPa升至25 kPa,从而使待生剂在立管内流动不畅,甚至在反吹后流动中断。从控制分离料斗压力和二次气控制阀开度的角度来解决问题。综合考虑措施的可行性和实际操作难度,使用分离料斗泄压手阀手动泄压来降低分离料斗压力,使待生剂流动"逆压差"维持在15 kPa,反吹时及时开大手阀泄压,有效地解决了问题。 展开更多
关键词 连续重整装置 低负荷 待生剂提升 二次气控制阀开度 分离料斗压力
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