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鼓泡

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The photocatalytic oxidation performance and kinetics of the simulated organic wastewater in a circulating slurry photocatalytic reactor was investigated.The effects of operation conditions, such as dosage of photocatalyst, illumination time, initial benzamide concentration, pH value, anions and cations in wastewater, on the photocatalytic oxidation performance were discussed.

采用循环式浆态光催化反应器对苯甲酰胺模拟废水光催化氧化特性和动力学进行了研究,系统地考察了操作条件对模拟污染物光催化降解的影响,并与搅拌式和鼓泡床式浆态光催化反应器中苯甲酰胺的降解效果进行对比。

A detailed description of the heat transfer and mass transfer during ammonia-water bubble absorption in air-cooled vertical finned tube is presented.

详细描述了垂直风冷翅片管吸收器中氨水鼓泡吸收的传热和传质过程。

It had been found that when the relative molecular weight changed, the properties changed also. When the relative molecular weight of PESA is in the range 800 to 1000, the scale inhibitions are best. When the relative molecular weight of PESA is lower than 700 or higher than 1000, the scale inhibition becomes worse.

采用鼓泡法研究了PESA的阻垢性能与其相对分子质量的关系,发现当PESA相对分子质量变化时,其性能变化相当大,当相对分子质量在800~1000范围时,钙离子稳定浓度达到120 mgL1以上;当相对分子质量低于700或高于1000时,阻垢性能变差。

The effects of the reaction temperature , time ,pressure and air flow on the vield of o - toluic acid were evaluated on a medium sized Semi - coninuous bubbling bed reartor.

在中型半连续鼓泡床反应器上,评价了反应温度、反应压力、空气流量以及反应时间对邻甲苯甲酸单程收率的影响。

Preparation of o toluic acid from o xylene over cobalt naphthenate catalyst in the presence ofair in liquid phase oxidation is presented.

对采用空气作氧化剂,环烷酸钴作催化剂,由邻二甲苯液相氧化制备邻甲基苯甲酸的反应条件,在中型半连续鼓泡床反应器上,评价了反应温度、反应压力、空气流量以及反应时间对产物邻甲基苯甲酸单程质量收率的影响。

Using bubble oxygenator, ecc time more than 180minutes , pressure before the artery filter higher than 240 mmhg and haematocrit in the first blood gas analysis more than 27% were significantly different.

使用鼓泡肺,ecc时间大于180 min,及泵压大于240 mmhg组,术中第一次血气分析血球压积大于27%三组,p.05,有显著差异。

According to this investigation based on absorption of CO〓 with dilute Na〓CO〓 solution in tubes with K-type and H-type static mixing elements, an external loop ALR with K-type static mixing elements was constructed and tested in the pilot scale as the reactor for replacing the traditional carbonating tower of chemical plant.

在实验室对K型、H型和O型反应器进行了稀纯碱溶液吸收混合气中的二氧化碳的研究基础上,又在工厂进行了K型气升式外环流反应器用于氨水吸收混合气中的二氧化碳生产碳酸氢铵的实验,以取代现在普遍使用的鼓泡式碳化塔。

The effects of gas sparging, gas flow rate, liquid flow rate and transmembrane pressure on the solvent flux and separation factor were examined during ultrafiltration of xylanases.

研究了木聚糖酶和β-木糖苷酶的超滤分离过程中,气体鼓泡的作用、气体流量、液相流量和操作压强对溶剂透过率和分离因数的影响。

The optimal gas flow rate was from 25 to 50 mL/min. The solvent flux increased linearly with transmembrane pressure and the separation factor was almost constant under experimental conditions with gas sparging.

适宜的空气流量为25~50 mL/min;在气体鼓泡的情况下,溶剂透过率随操作压强线性地增加,而分离因数不受操作压强影响。

Experimental results showed that gas sparging could increase permeate flux and improve the efficiency of fractionation during the ultrafiltraion of xylanases. The lower the liquid flow rate, or the higher transmembrane pressure, the more pronounced the enhancement in the ultrafiltration efficency.

结果发现,通入少量的空气即能显著改善溶剂透过率和分离因数,这种改善效果与操作条件相关,液相进料速度较低、操作压强较高时,气体鼓泡所产生的效果较为明显。

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