摘要
实验研究了固相分数为8.2%~23.1%的CO2水合物浆在内径为8 mm的圆管中的流动特性。结果发现水合物浆在管内的流动压降随着流速的增加而增大。当流速低于0.60 m·s-1时,浆体流变指数小于1,且随着固相体积分数的增大而减小,CO2水合物浆为H-B流体,其表观黏度随着流速的增大而减小,呈剪切变稀特性。剪切速率为600 s-1时,CO2水合物浆的表观黏度为8.5~10.6 mPa·s。实验得到了CO2水合物浆的流变特征参数及其流变方程,可为CO2水合物浆的流动及其应用研究提供理论指导。
An experimental setup was established to produce CO2 hydrate slurry by cooling after CO2 injection in precooled water. The flow characteristics of CO2 hydrate slurry with 8.2%-23.1%(vol) in a 8 mm straight stainless steel circular tube were studied in a dynamic loop. The pressure drops of CO2 hydrate slurry were measured and it increased with the increase of flow rate. The flow of CO2 hydrate slurry presente non-Newtonian behavior. At flow rate v<0.60 m·s-1, behavior index n<1 and decreased with the increase of solid fraction. CO2 hydrate slurry behaved as a Herschel-Bulkley fluid. Apparent viscosity decreased with the increase of shear rate, showing shear-thinning characteristics. Apparent viscosity of CO2 hydrate slurry was from 8.5 mPa·s to 10.6 mPa·s at shearing rate of 600 s-1. The rheological parameters and equations were determined, providing the guide for the research of CO2 hydrate slurry flow properties and its application.
出处
《化工学报》
EI
CAS
CSCD
北大核心
2014年第2期550-554,共5页
CIESC Journal
基金
国家自然科学基金项目(50706028)
上海市教委科研创新项目(12YZ106)~~
关键词
二氧化碳
水合物浆
流动
压降
黏度
carbon dioxide
hydrate slurry
flow
pressure drop
viscosity