Study effect of initiators on performance of copolymer used as pour point depressant for Diamond crude oil, Blocks 01 and 02, offshore Vietnam

Authors

  • Dao Viet Than School of Chemical Engineering, Hanoi University of Science and Technology, Vietnam Author
  • Thai Hong Chuong DMC-Drilling Fluids and Well Services, DMC Coporation, Vietnam Author
  • Dao Quoc Tuy School of Chemical Engineering, Hanoi University of Science and Technology Author
  • Bui Dac Trung DMC-Drilling Fluids and Well Services, DMC Coporation, Vietnam Author

DOI:

https://doi.org/10.51316/jca.2020.067

Keywords:

Pour point depressant, Diamond crude oil, Copolymerization

Abstract

Diamond oil field is located in Blocks 01&02 Offshore Vietnam. Crude oil from Diamond Well Head Platform (WHP) is evacuated to FPSO via 20km - 10” subsea flexible pipeline. The lowest seabed temperature in the field is 22˚C, while pour point temperature of this crude oil is very high (36˚C) due to high parafin content (about 25% by weight). So studying to synthesize a copolymer use to reduce pour point temperature of this oil is very important. The copolymer must have ability to reduce pour point temperature of the crude oil from 36˚C to 21˚C

The synthesis process occurred via copolymerization of acrylate, methacrylate and vinyl acetate monomers using free radical polymerization method in Solvent 100 as a solvent. There are many factors which affect copolymerization reaction and therefore they will impact on the structure and performance of the said copolymer. One of the most important factor is a ratio of initiator to monomer in the reaction.

Therfore the aim of this research is to choose an appropriated ratio of initiator to produce a copolymer which can reduce pour point temperature of Diamond crude oil from 36˚C to 21˚C at dosage of 1.750ppmv 

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References

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Published

31-12-2020

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How to Cite

Study effect of initiators on performance of copolymer used as pour point depressant for Diamond crude oil, Blocks 01 and 02, offshore Vietnam. (2020). Vietnam Journal of Catalysis and Adsorption, 9(4), 36-41. https://doi.org/10.51316/jca.2020.067

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