Dynamic simulation of the low-temperature separation process in order to determine the capacity of the plant

Ibragimova A.T. at_ibragimova@tnnc.rosneft.ru “Tyumen petroleum research center” LLC
Mezentseva Т.A. “Tyumen petroleum research center” LLC
DOI: 10.24412/2076-6785-2023-8-94-98

Abstract
The article deals with the dynamic modeling of the low-temperature separation unit of the integrated gas and condensate treatment plant in HYSYS software. The aim of the study is to optimize the operating mode of the low-temperature separation unit (LTS). A simulation dynamic model of the LTS process has been created in the software. Real-time modeling of the devices was carried out, the dependencies of the throughput of each element under a given technological mode were investigated. As a result, the potential of increasing the productivity of the investigated installation by 17 % of the actual operating mode was determined.

Materials and methods
The materials used are field information, method: dynamic modeling.

Keywords
dynamic modeling, gas extraction, gas treatment, low-temperature separation, three-phase separator, choke, gas condensate, forecasting
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