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Based on PVT and sand packed tube, the high pressure characteristics such as viscosity, expansion coefficient and minimum miscibility pressure were measured for mixture of crude oil and carbon dioxide, and the oil and gas production during multi contact experiments under constant and declined pressure was investigated, Lastly, the production performance of sand packed tube similar to low permeable reservoir.

通过PVT筒和填砂管气液平衡等模拟实验,测定原油与CO2体系的黏度、膨胀因数和最小混相压力等高压物性参数,研究了恒压和降压下5次CO2接触过程中原油和气体的产量变化,并对比研究模拟特低渗填砂管与PVT筒CO2吞吐实验的开采动态。

ResultsThe best packed method was trituration and the best packed preparation conditions were as follows:β-CD :volatile oil=10g:1ml,adding 3 times water,triturating 3 hours.

结果优选出的包合方法为研磨法,最佳包合工艺条件为:βCD与挥发油的投料比为10 g∶1 ml,加3倍量水,研磨3 h。

Especially for structured packed columns, which are boomingly used, due to the poor self-distributivity resulted from the lower pressure drop of the structured packing, and the more sensitivity to gas distribution, the influence of gas distribution for structured packed columns is more severe.

特别是目前逐渐被广泛应用的规整填料塔,由于其阻力小,对气体得自分布性能较差,同时有对气体的分布较为敏感,所以气体分布状况会对整个精馏塔的分离效率有较大的影响。

Finally, SO2 removal efficiency empirical equation in the scope of experimental condition is gained from the result of uniform experiments by means of stepwise regression analysis.3. Under the basis of the experimental results in lab, crossflow packed-bed absorber for additional experiment is designed according to experience. The dimension of packed-bed absorber is fixed and flooding gas speed of absorber is checkouted. At the same time, calandria liquid distributor is designed. The efficiency of flue gas desulfurization by scrap iron is investigated in the additional equipment. Under th

为了更好的掌握脱硫工艺的过程规律,根据脱硫工艺涉及的Fe浓度范围,选用NaHso3作为反应物质,全面研究10一6M、阵扭l:IM范围内Fe液相催化氧化s反应动力学,将Fe浓度分为两个范围对实验结果加以讨论,确定HSO3一和Fe的反应级数,调查离子强度和温度对反应速率常数的影响;并结合研究者提出的自由基机理和反应历程,分析反应机理,解释动力学规律。

Notice the packed cell volume from the centesis fluid exceeds the packed cell volume taken from the peripheral vein.

注意的穿刺液红细胞压积从超过红细胞压积静脉抽取周边。

If the packed cell volume of centesis fluid exceeds the peripheral packed cell volume, very likely there is either a splenic, hepatic or renal parenchymal laceration.

如果细胞体积包装穿刺液超过了周边红细胞压积,很可能有一个或脾,肝,肾实质裂伤。

ZG rotating bed consists of mono-or multi-rotors.Gas and liquid flow zigzag through the rotors countercurrently and carry out mass transfer.In ZG rotating bed,gas and liquid contact intensively,and the mass transfer rate can be increased greatly.It is a breakthrough for traditional plate and packed columns.ZGrotating bed of 1.5 meter high can achieve the separation ability which traditional plate of packed columns of 15 meters high can achieve.

该设备由一个或多个高速旋转的转子组成,气液以逆向折流方式流经转子,进行接触传质,1.5米高的ZG系列超重力精馏机相当于15米高的常用精馏塔,是对传统的板式塔、填料塔的重大突破,由国家级专家组鉴定,产品达到国际先进水平(专利号:ZL011343214)。

There are some midst matters in wastewater, for removal of these matters the electrolyze time should exceed 30 min. The experimental results show that the bipolar packed bed cell has best treatment efficiency of phenol wastewater under condition that voltage is 10V, electrolyses time is 30 min, and velocity of flow is 1.03 cm/min.Basic on the study on treating of phenol wastewater, this paper carry on a research on treating of circuitry board film wastewater by bipolar packed bed cell.

本文在以上处理苯酚废水研究的基础上,论文研究了BPBC处理两种不同浓度得脱膜废水,试验结果表明,对于浓度较高的酸化气浮-光酚顿的出水,在外加氧化剂双氧水后,最佳处理工艺:槽电压8V,实际电解时间60min,双氧水的投加量为1倍理论药量,pH值为3,COD的去除率达到60%;在酸化气浮过程采用酸铜废液调节pH值将会降低COD的去除率。

It could be found with can packed or cup packed on street vendors and aluminum foil packaging starfruit juice is sold in the convenience stores.

杨桃汁通常可在路边摊贩买到,有罐装及杯装的形式,一般便利商店亦可买到铝箔包装的杨桃汁。

A uniform mixture of silicon powder (granularity≤0.044 mm) and polyvinyl alcohol solution (PVA,5 wt%) in response to a certain proportion was prepared.After sieving,prilling and vibration,the mixture was packed.Effects of the vibration frequency (14~50 Hz) and time (10~230 s) on packed density of powder were studied.

摘 要:将Si粉(粒度≤0.044 mm)和聚乙烯醇水溶液(聚乙烯醇质量分数为5%)按一定比例混匀,过筛造粒后,振动装料,研究了振动频率(14~50 Hz)和振动时间(10~230 s)对粉料填充密度的影响。

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