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Publisher: Society of Petroleum Engineers (SPE)
Paper presented at the SPE/IATMI Asia Pacific Oil & Gas Conference and Exhibition, October 10–12, 2023
Paper Number: SPE-215275-MS
... for a ‘finite energy gas lift system’ – using gas produced from a deeper, high-pressure reservoir through a previously idle well as gas supply to the gas lift headers. This required installation of a new flowline to connect the well directly to the gas lift headers. Success of the implemented ‘finite energy...
B.. Al-Shammari, N. M. Rane, S. F. Desai, A. A. Al-Rabah, M.. Pandey, S.. Shankhdhar, R.. Chacko, R.. Jagannathan
Paper presented at the SPE/IATMI Asia Pacific Oil & Gas Conference and Exhibition, October 17–19, 2017
Paper Number: SPE-186205-MS
... collaboration center. The results are shown as new optimized set points for choke or header changesto achieve facility production targets. The new set points can be automatically passed on to the SCADA system for implementation after quick validation by the stakeholders. The paper provides new insights...
Paper presented at the SPE Asia Pacific Oil & Gas Conference and Exhibition, October 25–27, 2016
Paper Number: SPE-182226-MS
... and studied flowline network model in-house using a commercial steady-state multiphase flow simulator for the wells connecting to one of Kuwait companys' Gathering Centre (GC). GC-XY was considered as its eight headers are ranging between high and low pressure headers, and receiving production from several...
Paper presented at the Asia Pacific Oil and Gas Conference & Exhibition, August 4–6, 2009
Paper Number: SPE-124276-MS
... availability, potential weight limitation, tapping point where the platform pipeline header will be connected to the LPS and lastly wellhead connection type. This information will determine the design module sizes and crossover connections required. As with any new operation, the Hazop and Hazid study...
Paper presented at the SPE Asia Pacific Oil and Gas Conference, November 7–10, 1994
Paper Number: SPE-28771-MS
... of process options. System capacity was evaluated against predicted Longford Plant flare rates and profile distribution. The optimally sized unit has a nominal flare gas capacity of 200 std km3/d and will process around 70% of the flare header volumes. The system consists of one train of three compression...
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