化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2014年
2期
550-554
,共5页
刘妮%戴海凤%余宏毅%由龙涛
劉妮%戴海鳳%餘宏毅%由龍濤
류니%대해봉%여굉의%유룡도
二氧化碳%水合物浆%流动%压降%黏度
二氧化碳%水閤物漿%流動%壓降%黏度
이양화탄%수합물장%류동%압강%점도
carbon dioxide%hydrate slurry%flow%pressure drop%viscosity
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。
實驗研究瞭固相分數為8.2%~23.1%的CO2水閤物漿在內徑為8 mm的圓管中的流動特性。結果髮現水閤物漿在管內的流動壓降隨著流速的增加而增大。噹流速低于0.60 m·s-1時,漿體流變指數小于1,且隨著固相體積分數的增大而減小,CO2水閤物漿為H-B流體,其錶觀黏度隨著流速的增大而減小,呈剪切變稀特性。剪切速率為600 s-1時,CO2水閤物漿的錶觀黏度為8.5~10.6 mPa·s。實驗得到瞭CO2水閤物漿的流變特徵參數及其流變方程,可為CO2水閤物漿的流動及其應用研究提供理論指導。
실험연구료고상분수위8.2%~23.1%적CO2수합물장재내경위8 mm적원관중적류동특성。결과발현수합물장재관내적류동압강수착류속적증가이증대。당류속저우0.60 m·s-1시,장체류변지수소우1,차수착고상체적분수적증대이감소,CO2수합물장위H-B류체,기표관점도수착류속적증대이감소,정전절변희특성。전절속솔위600 s-1시,CO2수합물장적표관점도위8.5~10.6 mPa·s。실험득도료CO2수합물장적류변특정삼수급기류변방정,가위CO2수합물장적류동급기응용연구제공이론지도。
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.