2012
DOI: 10.1007/s10553-012-0385-5
|View full text |Cite
|
Sign up to set email alerts
|

Study of deposition behavior in small-diameter gathering pipelines for water-cut oil

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
2

Citation Types

0
10
0

Year Published

2015
2015
2023
2023

Publication Types

Select...
9

Relationship

2
7

Authors

Journals

citations
Cited by 15 publications
(10 citation statements)
references
References 1 publication
0
10
0
Order By: Relevance
“…In this paper, the waxy crude oil in the Daqing oilfield was selected. 20 The multiphase system mainly includes oil, paraffin, asphaltene, and water, and the phase transition point was 65.2% (the water cut corresponds to the transition point from W/O emulsion to O/W emulsion). The WAT was 345.15 K. The peak wax precipitation point was 295.15 K. The minimum temperature at which the oil acts as a Newtonian fluid was 315.15 K. The oil pour point was 310.15 K. The weight percent of each component in the multiphase system is shown in Table 1.…”
Section: Simulation Methodologymentioning
confidence: 99%
See 1 more Smart Citation
“…In this paper, the waxy crude oil in the Daqing oilfield was selected. 20 The multiphase system mainly includes oil, paraffin, asphaltene, and water, and the phase transition point was 65.2% (the water cut corresponds to the transition point from W/O emulsion to O/W emulsion). The WAT was 345.15 K. The peak wax precipitation point was 295.15 K. The minimum temperature at which the oil acts as a Newtonian fluid was 315.15 K. The oil pour point was 310.15 K. The weight percent of each component in the multiphase system is shown in Table 1.…”
Section: Simulation Methodologymentioning
confidence: 99%
“…In this paper, the waxy crude oil in the Daqing oilfield was selected . The multiphase system mainly includes oil, paraffin, asphaltene, and water, and the phase transition point was 65.2% (the water cut corresponds to the transition point from W/O emulsion to O/W emulsion).…”
Section: Simulation Methodologymentioning
confidence: 99%
“…The world demand for crude oil has increased from 6.0ˆ10 7 barrels (bbls) per day to 8.4ˆ10 7 barrels per day in the last 20 years [1]. It is well known that pipelines as a mean of transporting crude oil from the producing field to the treatment station or the refinery are the least expensive, the most effective and environmentally convenient and have been widely used in the gathering process at the oilfield and for downstream fuel supply [2,3]. The pressure drop loss in the pipeline must be lowered to decrease the pump power to push the oil economically for a long distance [4].…”
Section: Introductionmentioning
confidence: 99%
“…In this paper, the waxy crude oil in Daqing oilfield was selected; a multiphase system mainly including oil, paraffin, asphaltene, and water was employed. The wax appearance temperature was 325.15 K. The peak wax precipitation point was 295.15 K. The minimum temperature at which the oil acts as a Newtonian fluid was 315.15 K. The oil pour point was 310.15 K. The weight percent of each component in the multiphase system is shown in Table .…”
Section: Simulation Methodologymentioning
confidence: 99%