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利用孔板与均速管组合在线测量汽—水两相流双参数,解决了稠油热采中同时测量蒸汽流量与干度的难题。其工作程序用Mcs-51单片机汇编语言编制而成,主程序由初始化、数据采集处理,热物理参数生成、汽—水两相流量、干度、质量流量、热量计算以及累计运算等模块组成。通过在现场进行标定;干度用化验CI^-法进行标定,流量用锅炉入口的涡轮流量计标定。经胜利和新疆两油田进行的大量试验可知,该仪表测量水蒸汽流量和干度其均方差皆小于7%,满足了工业应用要求。 相似文献
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阐述了煤矿管道瓦斯流量计量技术的发展现状,分析了孔板流量计、涡街流量计、皮托管流量计、旋进漩涡流量计、V锥流量计的优缺点;针对瓦斯流量测量准确度受气体中的杂质和瓦斯体积分数变化影响的问题,提出了解决办法;建议煤矿瓦斯抽放管网中的主管、干管、支管采用V锥流量计,汇流管以及各评价单元采用多点采样的插入式流量计;指出煤矿管道瓦斯流量计量应根据不同的现场状况、工况条件及测量需求选择相应的流量计。 相似文献
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基于彩色多普勒成像的近测等速面(PISA)算法是临床评价二尖瓣中心返流严重程度的一种常用方法,但对于偏心返流却存在极大低估。针对这一现状,从返流角度和湍流强度两个方面,对传统PISA算法的有效返流瓣口面积(EROA)进行修正。为比较首先用传统PISA算法的EROA对具有不同程度偏心返流的20例患者进行分级,结果误差较大;用改进PISA算法的EROA分级效果良好。对比实时三维超声测得的数据表明修改后的PISA算法相关性更好。 相似文献
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A. M. Lali A. S. Khare J. B. Joshi A. C. Eapen S. M. Rao V. N. Yelgaonkar R. L. Ajmera 《加拿大化工杂志》1988,66(2):182-191
Two phase flow in a horizontal pipe, with orifice plates placed at regular intervals as obstructions, was studied for the effect of phase velocities on flow patterns, fractional phase hold-ups, pressure drop and liquid phase axial dispersion. Radioactive technetium-99m (as an aqueous solution of sodium pertechnatate) was used as tracer. A pulse injection technique with two point measurements was employed. Three different orifice diameters were used (8 mm, 16 mm, and 20 mm) in a pipe diameter of 32 mm. The orifice spacing was 500 mm in all cases. Superficial gas (air) velocity was varied over a range from 0.02 m/s to 1.0 m/s and superficial liquid (water) velocity from 0.03 m/s to 0.85 m/s. Different flow patterns under different flow conditions were identified and a generalised flow map is presented. Variations in hold-ups and pressure drop with flow patterns have been explained. Rational correlations have been developed for fractional phase hold-ups and pressure drop. A preliminary comparison of two phase gas-liquid flow in a horizontal pipe with orifice obstructions (to be called orifice pipe reactor), as a gas-liquid contacting device, is made with a conventional bubble column reactor. Recommendations have been made for future work. 相似文献
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Global hydrodynamic characteristics, liquid mixing and gas‐liquid mass transfer for a 63 L split‐rectangular airlift reactor were studied. Correlations for gas holdup and overall liquid circulation velocity were derived for the air‐water system as a function of the specific power input; these were compared to data and correlations for reactor volumes between 4.7 L and 4600 L. A partial recirculation of small bubbles in the riser was observed when Ugr > 0.03 m/s, which was attributed to the use of a single‐orifice nozzle as the gas phase distributor. The dimensionless mixing time and the overall axial dispersion coefficient were nearly constant for the range of gas flow rates studied. However, values of KL/dB were greater than those reported in previous studies and this is caused by the partial recirculation of the gas phase in the riser. While scale effects remain slight, the use of a gas distributor favouring this partial recirculation seems adequate for mass transfer in split‐rectangular airlift reactors. 相似文献
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Polysulfone (PSf) asymmetric hollow‐fiber membranes, which have a dense outer layer but a loose inner layer, were tentatively fabricated by coextrusion through a triple‐orifice spinneret and a dry/wet‐phase inversion process. Two simple polymer dopes were tailored, respectively, for the dense outer layer and the porous inner layer according to the principles of the phase‐inversion process. By adjusting the ratio of the inner/outer extrusion rate, the hollow‐fiber membranes with various thicknesses of outer layers were achieved. The morphology of the hollow‐fiber membranes was exhibited and the processing conditions and the water permeability of the membrane were investigated. © 2004 Wiley Periodicals, Inc. J Appl Polym Sci 94: 259–266, 2004 相似文献
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大流量水电站的消能设计历来都是非常复杂和困难的.在1:60溢流坝表、中泄水孔断面模型上对密松水电站泄水建筑物的布置方案进行了泄流能力、流速流态、压力分布等相关水力学问题的试验研究,并通过10多个方案的比较优化,提出了基本可行的泄水建筑物体型和消力池型式.研究成果表明:表孔取消宽尾墩,采用跌坎式消力池方案,可有效降低底流消能时的池底板流速,同时消除宽尾墩形成的水翅击打两侧导墙现象,达到了较满意的消能效果.试验成果对该工程设计提供了较好的参考方案,并对类似工程有很好的启发借鉴作用. 相似文献