Hi. I am a process/operation engineer. I post this thread to find answers from instrument guys regarding installation philosophy on SDV. Recently, I've been designing a new gas injection line. Since our well will no longer produce oil, we planned to rigged down the 2" gas lift line and reuse the available SDV for the new gas injection line. This gas injection line however, will accommodate much higher gas flow at higher pressure, thus was sized as 3" line. Therefore, reducers will be fitted in order to install the reused SDV. Through some calculations, the gas velocity through the line and SDV is acceptable. My concern then will be: is it technically acceptable to configured SDV with reducers? I've been through many P&IDs and noticed that usually SDVs were installed directly with the line without any blockage/reducers. Are there any design standards that prohibit such configuration?? Thanks.



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