NEW DEVELOPMENT OF THE TEALARC NATURAL GAS LIQUEFACTION PROCESS

1977 ◽  
Vol 17 (1) ◽  
pp. 128
Author(s):  
Jean-Pierre Dufresne ◽  
Joseph Gauberthier ◽  
Rene Schlatter

Technip has experience in the LNG field obtained through the design and erection of two base load natural gas liquefaction plants in Algeria and the process licensing of 13 peak-shaving units mainly in North America.Through its operating experience of base-load plants and the research and development studies performed, Technip has improved the Tealarc liquefaction process with regard to the main criteria: efficiency, reliability, flexibility, simplicity and has also adopted the Tealarc process to the use of centrifugal compressors. In this case the Tealarc process is split into two different cycles, the first Tealarc cycle called "Precooling cycle" is used to partially condense the cryogenic fluid of the second Tealarc cycle called "Liquefaction cycle" which performs the condensation of the natural gas and the subcooling of LNG.This arrangement of the precooled Tealarc process allows the realisation of large capacity liquefaction trains while satisfying the limitation of the centrifugal compressorIn 1976 French and Italian experience in the LNG process sector were combined through a permanent joint-venture between Technip and Snam Progetti.

2013 ◽  
Vol 391 ◽  
pp. 352-357
Author(s):  
Lei Zhang ◽  
Li Xin Che ◽  
Sheng Shan Bi ◽  
Hui Shi Wang ◽  
Jiang Tao Wu ◽  
...  

With the increased utilization of natural gas, there has been an increase in the research on peak-shaving natural gas liquefaction technologies. The NGE-MR natural gas liquefaction process, which precools natural gas with the cold energy generated by high pressure natural gas pipeline pressure energy recovery, is a promising technical candidate for peak-shaving LNG facilities. In this study, the effect of high pressure of the mixed refrigerant cycle (MRC) on the performance of the NGE-MR liquefaction process is analyzed under a fixed MRC pressure ratio. The result shows that for a certain mixed refrigerant composition, there is a corresponding optimal high pressure of the MRC, under which the minimum specific power of the liquefaction process could be obtained. The minimum specific power should be regarded as the evaluating indicator to represent the performance of the mixed refrigerant composition. Finally, the effect of mixed refrigerant composition on the performance of the NGE-MR liquefaction process is analyzed and the optimal operating conditions for the NGE-MR liquefaction process are obtained. As a result, the required specific power at the optimal operating conditions is less than 0.23 kW·h·kg-1 and is decreased by about 24% compared with the specific power of C3-MR natural gas liquefaction process.


2007 ◽  
Vol 2 (04) ◽  
pp. 1-7 ◽  
Author(s):  
David Wood ◽  
Saeid Mokhatab ◽  
Michael John Economides

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