发明名称 FLOW CONTROL SYSTEM WITH BUILD-DOWN SYSTEM FLOW MONITORING
摘要 To provide a flow control system with build-down system flow monitoring that realizes flow monitoring close to real-time monitoring by combining build-down system flow rate measurement with the upstream side of the flow control system without using a thermal type flow sensor by effectively utilizing high pressure fluctuation resistance characteristics of the flow control system, and can be significantly downsized and reduced in cost.
申请公布号 US2015136248(A1) 申请公布日期 2015.05.21
申请号 US201314404418 申请日期 2013.04.15
申请人 FUJIKIN INCORPORATED 发明人 Nagase Masaaki;Hidaka Atsushi;Nishino Kouji;Ikeda Nobukazu
分类号 G05D7/06 主分类号 G05D7/06
代理机构 代理人
主权项 1. A flow control system with build-down system flow monitoring comprising: an upstream side valve AV that opens/closes distribution of a gas from a gas supply source having a desired gas supply pressure; a flow control system with supply pressure fluctuation resistance connected to the downstream side of the upstream side valve AV; a build-down capacity BC being an internal volume of a passage communicatively connecting the outlet side of the upstream side valve AV and the inlet side of the flow control system; a temperature detection sensor T arranged to detect the temperature of a gas distributed inside the passage forming the build-down capacity BC; a pressure sensor P arranged to detect the pressure of the gas distributed inside the passage forming the build-down capacity BC; and a monitoring flow rate arithmetic and control unit CPb operably connected to control opening and closing of the upstream side valve AV, and arranged to compute and output a monitoring flow rate Q by a build-down system by dropping the gas pressure to a set lower limit pressure value by closing the upstream side valve AV after a predetermined time oft seconds after setting the gas pressure inside the build-down capacity BC to a set upper limit pressure value by opening the upstream side valve AV, wherein the monitoring flow rate Q is computed by the following equation:Q=1000760×60×273(273+T)×V×ΔPΔt wherein T is a gas temperature (° C.), V is a build-down capacity BC (1), ΔP is a pressure drop range (set upper limit pressure value−set lower limit pressure value) (Torr), Δt is a time (sec) from closing to opening of the upstream side valve AV.
地址 Osaka JP
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