Pipeline transport of oil with strongly temperature-dependent viscosity

被引：0
|
作者：
Strand, B [1 ]
Djuve, SM [1 ]
机构：
[1] Norsk Hydro ASA, Stabekk, Norway
来源：
2ND NORTH AMERICAN CONFERENCE ON MULTIPHASE TECHNOLOGY | 2000年 / 40期
关键词：
D O I：
暂无
中图分类号：
TE [石油、天然气工业];
学科分类号：
0820 ;
摘要：
A method is described to estimate the temperature and pressure drop in a pipeline flowing an oil with strongly temperature dependent viscosity. Results of an analysis with this method are compared to results obtained with a standard steady state, one dimensional, single phase pipeline simulation tool. It is demonstrated how failure to account for radial variations in liquid viscosity may cause the pipeline pressure drop to be grossly underpredicted. The method is illustrated by example of a planned 220 km long North Sea subsea oil export pipeline.
引用
收藏
页码：17 / 33
页数：17
相关论文
共 50 条
12345