首页> 外国专利> METHOD FOR AUTOMATICALLY MAINTAINING THE TEMPERATURE REGIME OF TECHNOLOGICAL PROCESSES OF LOW-TEMPERATURE GAS SEPARATION INSTALLATION BY TURBO EXPANDING UNIT IN THE CONDITIONS OF NORTH OF RUSSIAN FEDERATION

METHOD FOR AUTOMATICALLY MAINTAINING THE TEMPERATURE REGIME OF TECHNOLOGICAL PROCESSES OF LOW-TEMPERATURE GAS SEPARATION INSTALLATION BY TURBO EXPANDING UNIT IN THE CONDITIONS OF NORTH OF RUSSIAN FEDERATION

机译:在俄罗斯联邦北方的条件下,涡轮增压单位自动维护低温气体分离装置技术过程温度制度

摘要

FIELD: gas industry. ;SUBSTANCE: invention relates to the field of production and preparation of gas and gas condensate for long-distance transport, in particular to the automatic maintenance of the temperature regime of the technological processes of the low-temperature gas separation installation during the period when the cooling of the extracted gas is carried out by turbo expander units (TEU) in the conditions of the North of the Russian Federation. The method includes preliminary purification of the extracted gas-liquid mixture from mechanical impurities, separation of a mixture of unstable gas condensate (UGC) and an aqueous solution of an inhibitor (ASI) in a separator of the first reduction stage. The partially purified extracted mixture is directed from the output of the separator of the first stage of reduction through the flow control valve (CV) of the extracted gas-condensate mixture and divided into two streams, which are fed for pre-cooling to the input of the first sections of recuperative heat exchangers hereinafter referred to as “gas-gas” “gas-condensate” HE. Both streams, after leaving the first sections of the HE, are combined and fed to the input of the TEU turbine equipped with a rotor speed sensor. Then the cooled extracted gas-liquid mixture is fed into a low-temperature gas separator equipped with a temperature sensor, in which it is finally divided into dried cold gas and a mixture of UGC and ASI. The cold dried gas coming out of the low-temperature separator is divided into two streams. One of them is fed to the input of the second section of the “gas-gas” HE, and the second to the bypass of this section, equipped with a gas flow CV, which changes the flow ratio of these cooled gas flows. Then these gas flows are combined and fed to the input of the TEU compressor. A mixture of UGC and ASI from the lower part of the low-temperature separator is fed to the entrance of the second section of the “gas-condensate” HE and then to the working fluid, from which the separated UGC is sent to the MCP, ASI for regeneration, and the flow of the separated gas, weathering gas from the working fluid is transported for disposal or compressed and fed to the main gas pipeline (MGP). Automatic temperature maintenance in a low-temperature separator is carried out using proportional-integral-differentiating regulators (PID regulators). To obtain the set temperature T in a low-temperature separator, the automated process control system supplies a single value of its setpoint signal to the SP input of the PID controllers that control the operation mode of “gas-gas” or “gas-condensate” HE and the PID controller that determines the setpoint of the required speed of rotation of the TEU rotor, which is required to be maintained. At the same time, the automated process control system sends a signal of the actual temperature T value from the temperature sensor in the low-temperature separator to the PV feedback input of the same PID controllers. The automated control system also sets the order of switching on/off these three PID controllers. The PID controller, which generates the signal of the setpoint of the rotation speed of the TEU rotor, feeds it from its CV output to the input of the SP task of the PID controller, which directly controls the rotation speed of the TEU rotor. ;EFFECT: invention provides the maximum use of the refrigeration produced at the installation for automatic maintenance of the temperature regime in a low-temperature separator in compliance with technological norms and restrictions provided for by its technological regulations. ;5 cl, 2 dwg
机译:领域:天然气工业。物质:发明领域涉及用于长距离运输的气体和气体冷凝物的生产和制备领域,特别是在期间的高温气体分离装置的技术过程的自动维护提取的气体的冷却通过俄罗斯联邦北部的涡轮扩展器单元(TEU)进行。该方法包括从机械杂质的萃取的气液混合物的初步纯化,不稳定的气体冷凝物(UGC)的混合物和抑制剂(ASI)的水溶液中的第一减少阶段的分离器中的含水溶液。部分纯化的提取混合物通过提取的气体冷凝物混合物的流量控制阀(CV)的第一阶段的第一阶段的分离器的输出引导,并将其分成两条流,其供给用于输入预先冷却在下文中,恢复热交换器的第一部分称为“气体”“气体冷凝物”。在离开他的第一部分之后,两条流被组合并馈送到配备有转子速度传感器的Teu涡轮机的输入。然后将冷却的萃取的气液混合物加入配备有温度传感器的低温气体分离器中,其中最终分为干燥的冷气和UGC和ASI的混合物。从低温分离器出来的冷水气体被分成两条流。其中一个被馈送到“气体气体”的第二部分的输入,并且第二部分到该部分的旁路,配备有气流CV,其改变了这些冷却气体流的流量比。然后将这些气体流合并并馈送到TEU压缩机的输入。从低温分离器的下部的UGC和ASI的混合物被送入“气凝酯”的第二部分的入口,然后将分离的UGC发送到MCP的工作流体的入口处,用于再生的ASI,以及分离气体的流动,从工作流体的风化气体被输送以进行处理或压缩并进料到主气管道(MGP)。使用比例整体区分调节器(PID调节器)进行低温分离器中的自动温度维护。为了在低温分离器中获得设定温度T,自动化过程控制系统将其设定点信号的单个值提供给控制“气体气体”或“气体冷凝物”的操作模式的PID控制器的SP输入。 “他和PID控制器,用于确定TEU转子所需旋转速度的设定点,这是需要维护的。同时,自动化过程控制系统从低温分离器中的温度传感器发送实际温度T值的信号,到相同PID控制器的PV反馈输入。自动控制系统还设置开启/关闭这三个PID控制器的顺序。 PID控制器产生TEU转子的转速的设定点的信号,将其从其CV输出供给到PID控制器的SP任务的输入,这直接控制TEU转子的旋转速度。 ;效果:发明提供了在安装装置中产生的制造的最大利用,以符合其技术法规提供的技术规范和限制的低温分离器中的温度调节。 ; 5 cl,2 dwg

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