Application of Mechanical and Electrical Equipment in a Natural Gas Processing Plant

Author(s):  
R. P. Lang ◽  
B. B. McCullough

In 1984 the Northwest Pipeline Corporation purchased and installed equipment for their Ignacio, Colorado, gas processing plant to extract ethane and heavier hydrocarbons from the gas arriving at their pipeline system from various natural gas producing sources. In addition to the basic turbo-expander required to achieve the very low gas temperatures in the process, the equipment includes gas turbine driven compressors, heat recovery steam generators, and a steam turbine driven electric power generator. This paper reviews the process itself, the various mechanical and electrical equipment involved, and some of the control system utilized to tie it all together.

Energies ◽  
2021 ◽  
Vol 14 (23) ◽  
pp. 8036
Author(s):  
Ruud Weijermars ◽  
Miao Jin ◽  
Nur Iman Khamidy

This study provides a workflow and preliminary estimations of the estimated ultimate recovery (EUR) volumes for natural gas and condensate liquids in the Tuwaiq Mountain Formation, the principal target in the Jafurah Field development project in Saudi Arabia. The strategic need for the field development is reviewed and the field characteristics are outlined based on public data sources complemented with data from analogous reservoirs. The target zone in the Jafurah Basin is a carbonaceous shale, being developed with up to 10,000-ft-long multistage-fractured laterals with 30 ft perforation cluster spacing and an assumed typical 1250 ft well spacing. The field will come on stream in 2024, when the gas-gathering pipeline system, natural gas processing plant, and underground gas storage facilities will all be in place. The range of uncertainties in the key reservoir parameters is taken into account to estimate preliminary EUR volumes (P90, P50, and P10) for both gas and condensates. Based on the present and prior EUR estimations, it can be concluded that the Jafurah Basin comprises one of the largest unconventional field development projects outside of North America.


2020 ◽  
Author(s):  
Jessica Narku-Tetteh ◽  
Pailin M Muchan ◽  
Teeradet Supap ◽  
Raphael Idem

2019 ◽  
Vol 1386 ◽  
pp. 012101
Author(s):  
C Agón-León ◽  
J A Sanabria-Cala ◽  
G R Conde-Rodríguez ◽  
D Laverde-Cataño ◽  
D Y Peña-Ballesteros ◽  
...  

2016 ◽  
Vol 30 (12) ◽  
pp. 10236-10243 ◽  
Author(s):  
Mohamed F. Ezzeldin ◽  
Zuzana Gajdosechova ◽  
Mohamed B. Masod ◽  
Tamer Zaki ◽  
Jörg Feldmann ◽  
...  

Author(s):  
C. F. Gee

The development of the cryogenic turbo-expander type plant as applied to natural gas processing for the recovery of ethane and heavier hydrocarbons is traced briefly. Integration of a large gas fired turbine into this process for a marine installation is discussed. Design considerations are outlined and operating experience is reviewed.


Author(s):  
Sandeep Nayak ◽  
Erol Ozkirbas ◽  
Reinhard Radermacher

This paper describes the modeling of a 27 MW combined cycle cogeneration plant with 10,000 tons chilled water central cooling facility. The cogeneration plant is designed to provide heating, cooling and electricity from a single fuel source viz., natural gas, though the gas turbines do have an inbuilt dual fuel combustion system. The topping cycle of the combined cycle cogeneration plant consists of two gas turbines each producing 11 MW of electric power at full load. The energy of the exhaust gases from these gas turbines is then utilized to generate steam in two heat recovery steam generators. The heat recovery steam generators are duct fired using natural gas to meet the peak steam load. In the bottoming part of the combined cycle, the steam from the heat recovery steam generators is expanded in a backpressure steam turbine to supply steam to the campus at about 963 kPa, generating an additional 5.5 MW of electric power in this process. There is no condenser wherein the campus acts as a sink for the steam. The central cooling facility is designed to supply 10,000 tons of chilled water out of which 3800 tons is supplied by two steam driven centrifugal chillers, which utilize a part of the steam supplied to the campus and the remaining by the centrifugal electric chillers. The combined cycle cogeneration plant along with the central chilled watercooling facility is modeled in a commercially available flexible cogeneration software package. The model is built based on the design data available from design manuals of gas turbines, heat recovery steam generators, backpressure steam turbine and centrifugal chillers. A parametric study is also done on the model to study the effect of different parameters like fuel flow rate, temperature etc on the output of the turbine and efficiency of the plant. Modeling of the inlet air-cooling of the gas turbine using an absorption chiller and electric chiller is also presented. Finally the paper discusses these results.


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