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major factor affecting
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  主要因素
     1. Pressure is the major factor affecting the solubility of kiwifruit seed oil in supercritical CO2. The transforming pressure for extracting kiwifruit seed oil by supercritical CO2 extraction is approximately 27.8Mpa.
     1.压力是影响猕猴桃籽油在超临界CO2 中溶解度的最主要因素。 超临界CO2 萃取猕猴桃籽油的转变压力约为27.8MPa。
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     In seedling stage, the average daily temperature (AT) was the major factor affecting NAR and CGR. In the range of 12~26℃ of AT, At rises, which is favourable for NAR and CGR rising.
     苗期日均温(AT)是影响NAR,CGR的主要因素,AT在12~26℃范围内,提高温度,可提高NAR和CGR;
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     The multivariate linear regression analysis revealed that ET-1 and ACE were major factor affecting PI.
     多元回归分析显示ET-1和ACE可能是影响PI的主要因素
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     The results show that the major factor affecting the desulfurizing capability of M/VACF is not its specific surface area and pore structure,but the kind of loaded metal.
     结果表明,M/VACF的比表面积和孔结构不是影响M/VACF脱硫性能的主要因素,负载金属的种类是影响M/VACF脱硫性能的主要因素
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     In the case of multivalent metal ion,the major factor affecting strongly the phase behavior is the hydrophobicity of metal HDEHP complex. 
     在多价金属离子的情况下,强烈影响微乳体系相行为的主要因素是金属-HDEHP络合物的亲油性。
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  “major factor affecting”译为未确定词的双语例句
     Lead and zinc loading was the major factor affecting the PbO-ZnO/Ti-PILC catalytic activity in the transesterification reaction. The highest yield of DPC is 21.8% (over 15wt% PbO-ZnO/Ti-PILC catalyst).
     酯交换合成DPC反应中,铅、锌负载量对PbO-ZnO/Ti-PILC的活性有较大影响,15wt%PbO-ZnO/Ti-PILC催化性能最好,DPC收率为21.8%。
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     Y d=1.7459+0.4108x 1+0.0975x 2+0.9025x 4+0.3442x 5+0.0834x2 1+0.3060x2 4-0.2623x2 5.The models showed that percentage of fodder water is the major factor affecting the growing speed of T.
     Y死 =1 .745 9+0 .41 0 8x1+ 0 .0 975 x2 + 0 .90 2 5 x4 + 0 .3442 x5+ 0 .0 834x21+ 0 .30 60 x24 - 0 .2 62 3x25。
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     Results Vision was≥0.5 in 45 eyes (76%) 3 months after the operation; it was≥0.5 in 46 eyes (79%) and≥1.0 in 11 eyes (19%) 6 months after the operation. The major factor affecting postoperative vision is progressive pathological changes of fun-dus.
     结果术后3月视力≥0.5者45眼(76%),术后6月视力≥0.5者46眼(79%),≥1.0者11眼(19%),影响术后视力恢复的主要原因为高度进行性近视眼底病变。
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     The results show that the oxidation of the substrate surface is the major factor affecting the mobility of the epitaxial layer.
     结果表明 ,衬底表面氧化是影响外延层迁移率的重要因素
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     Land degradation (LD) has become the major factor affecting and constraining the socio-economic development and environmental rehabilitation and conservation in the northwestern region (NWR) of China.
     土地退化已成为我国西北地区社会经济发展和生态环境保护的制约因素。
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  相似匹配句对
     Motivation is the major factor of learning process.
     动机是学习过程的核心。
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     tumor recurrence was the major factor of death;
     肿瘤复发是死亡的主要原因 ;
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     Gene expression was the major factor affecting gene transfer.
     影响基因转移的一个主要因素是细胞的基因表达。
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     Study on the Major Affecting Factor of Prepressing Property of Plywood
     影响胶合板板坯预压性能主导因素的研究
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     Temperature is the major factor affecting maize growth duration.
     气温是影响玉米生育期长短的主要因子,日均温与生育期的相关系数r_(鲁玉10)=-0.954~(**),r_(农大108)=-0.995~(**)都达极显著水平。
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  major factor affecting
Another major factor affecting fiber morphology and size distribution is the relative humidity.
      
Of the component concentrations, the major factor affecting the rate of uraninite dissolution is the oxidant concentration.
      
The size of the matrix precipitates was the major factor affecting the atmospheric SCC resistance when GBPs were larger than a critical size that could nucleate hydrogen bubbles.
      
The effect of agglomerates on sintering and microstructural development was studied and it was found that the agglomerate content in compacts was a major factor affecting the microstructure development and the sintered densities.
      
Significant short-term outcome predictors have been identified, and they often allude to the level of psychological distress as a major factor affecting outcome.
      
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The flow pattern of pulp in currently used gravity slime concentrators except centrifugal separator belongs to laminar type. The travelling velocity of single particle sliding along an inclined surface in laminar flow may be calculated by the theoretical formula, and consequently it is known that the major factors affecting the separating efficiency of particles are the thickness of flow film, the slope of inclined surface and the coefficient of friction between particles and inclined surface. In practice,...

The flow pattern of pulp in currently used gravity slime concentrators except centrifugal separator belongs to laminar type. The travelling velocity of single particle sliding along an inclined surface in laminar flow may be calculated by the theoretical formula, and consequently it is known that the major factors affecting the separating efficiency of particles are the thickness of flow film, the slope of inclined surface and the coefficient of friction between particles and inclined surface. In practice, however, a mass movement of particles really takes place there and the acting force which causes particles maintaining in suspension is the shear stress between particles involved and not the eddy movement at all. Previous concepts proposed for the stratification of pulp in slime concentrator are considered to be not complete. According to the general role of pulp movement and the characteristics of slime flow film, in this paper the author proposes that the pulp in slime concentrator may be divided into four layers, i.e. turbulent layer, suspension layer, transportation layer and sedimentation layer, and explains the mechanism of each layer. A low efficiency of slime sluice of fixed type is due to inadequacy of loosing at trasportation layer and the packing of sedimentation layer. The process of slime concentration may be improved by the application of a shaking force to the bed of a concentrator.

现有矿泥重选设备,除离心选矿机外,矿浆流态都属层流。运用层流理论公式可求出单个矿粒的移动速度,同时得知流膜厚度、底面的坡度和摩擦系数是影响矿粒分选好坏的重要因素。当粒群在层流流膜中运动时,促使矿粒悬浮的不是水流的紊动作用而是颗粒与颗粒间的切应力。过去提出的一些矿浆分层概念都不够全面。本文根据泥沙运动的一般规律及结合矿泥流膜的特点,将矿浆分成扰动层、悬移层、推移层和沉积层,并阐明各层的作用。指出下部推移层的松散不足和沉积层压紧是固定式矿泥溜槽效率低的原因。利用摇动可以强化矿泥分选过程。

Rotational accuracy of spindle in an aerostatic spindle system The paper analyses the major factors affecting the spindle runout and axial play in an aerostatic spindle system and proposes the way to improve the spindle rotating accuracy, which is interested in aerostatic bearing applications.

本文着重分析了影响空气静压轴系主轴径向晃动和轴向窜动的主要因素,提出了提高主轴运转精度的途径。对应用静压空气轴承有一定的参考。

Saturated air solar still is a new distillation device utilizing mainly solar energy,simple in structure and suits for obtaining higher fresh water production under various operating conditions.The experiment studied first for the profile of evaporation velocity under steady state and different heating temperatures for sea water.An equation for profile D=f(t0) was obtained as:It was found that heating temperature is the major factor affecting production,with 46.2℃ as a turning point.The evaporation is...

Saturated air solar still is a new distillation device utilizing mainly solar energy,simple in structure and suits for obtaining higher fresh water production under various operating conditions.The experiment studied first for the profile of evaporation velocity under steady state and different heating temperatures for sea water.An equation for profile D=f(t0) was obtained as:It was found that heating temperature is the major factor affecting production,with 46.2℃ as a turning point.The evaporation is accelerated rapidly at the temperatures above this point.Theoretical analyses and experiments proved that liquidgas phase flow ratio byweight should meet the heating temperature of water.Maximum increase of production and lower heat consumption could be achieved only when higher ratio- 3.0 at typical solar radiation.

研究得到了太阳能空气饱和蒸馏器在稳态情况下和不同海水加热温度下的蒸发速度实验式:lgD=7.062+3.446t_0海水加热温度是影响淡水产量的主要因素,以46.2℃为转折,超过此温度,蒸发速度急促增加。液-气两相重量流量比(W/G),必须与海水加热温度相适应。温度较高,(W/G)值也应较大,这样才能最大限度地提高产水量和降低产水的耗热量。当t_0=96℃时,(W/G)_(最佳)=12;当(W/G)=11时,t_(0最佳)=90℃。在一般太阳辐射条件下,t_0=60℃,(W/G)=1.67—3.0时,热耗值最低。过多地通入空气是空气饱和蒸馏器动力消耗较大的重要原因。在适当工况下进行操作,所需空气量较小。这样,不但产水量高、热耗值低、系统阻力减少,而且能耗大幅度降低。 模拟试验表明:太阳能空气饱和蒸馏器在太阳辐射日总量4500〔千卡/米~2〕时,每平方米集热器面积,每日可产淡水5—7公斤,所需翅片冷凝器换热面积为0.21〔米~2/时·公斤淡水〕。

 
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