1) Filling rate
填充率
1.
Under the condition of DO of 4 to 5 mg/L in HSMBR and HRT of 4 h,the COD removal rate is 75%,62% and 56% respectively when the carrier filling rate.
在HSMBR中的溶解氧浓度为4～5mg/L、HRT为4h的条件下,当填料填充率分别为45%、20%和0时,系统对COD的去除率分别为75%、62%和56%;对NH3-N的去除率>90%;膜清洗周期分别为40、36和24d。
2.
The elongation and filling rate have been selected and the tensional coefficient has been calibrated systematically on the bases of the rolling law.
根据轧制规律,选用合理的延伸系数和填充率,系统地校核了张力系数,减少了断锭堆料事故,改善和提高了铝杆的力学性能,延长了轧辊使用寿命,降低了产品的制造成本。
3.
In order to model the estimation for the over-sample and sub-pixel imaging considering the detector s filling rate,the detector pixel spread function is derived adversely by the sub-pixel arithmetic.
针对探测器存在填充率时过采样和亚像元成像质量评价问题,利用亚像元算法反演线阵探测器像元扩散函数,发现较过采样成像不仅能在1/m微扫描作用下减小采样间隔,还能使探测器矩形窗口压缩m倍。
2) filling ratio
填充率
1.
Preparation of SiO_2 ordered macroporous materials with high filling ratio
高骨架填充率的SiO_2有序大孔材料的制备
2.
2% mixing moisture, 6r/min mixing drum rotating speed, 13% filling ratio,and 7min mixing time, it is ensured that the +3mm fraction in sintering mix over 85%.
2 % ,混合机转速 6 r/m in,填充率 13% ,混合时间 7min时 ,即可保证混合料中大于3mm部分在 85 %以
3.
For a single edgree of freedom(SDOF) non-obstructive particle damping(NOPD) system,the influences of factors such as particle filling ratio,particle material type,vibration direction and cavity shape etc on the structural damping characteristics are experimentally investigated.
针对非阻塞性微颗粒阻尼(NOPD)单自由度体系,通过实验研究颗粒填充率、颗粒材料类型、振动方向以及空腔形状等因素对结构阻尼特性的影响,并根据实验数据对阻尼特性进行了拟合分析。
3) Filling fraction
填充率
1.
Numerical result shows that the width of the lowest band gap increases (decreases) with increasing the filling fraction (lattice constant); The center frequency of the lowest gapwas about independent of the cylinder radius, but gets lower with increasing lattice constant.
结果表明,当填充率(晶格常数)增大时,最低禁带宽度增大(减小);最低禁带中心频率基本不受散射体半径的影响,但随晶格常数的增大而降低。
2.
There will be not only one gap in the photonic band structure in the case of incidence along the direction,it is shown that the middle frequency v of pseudo-gaps including the first gap and the third gap will increase when the filling fraction of the background dielectric medium inside the opal voids ff decreases, and that v will increase when the sintering factor.
应用平面波展开法分析了三维反蛋白石结构光子晶体的带隙性质;计算了沿[111]方向入射时其赝带隙(第一、第三赝带)中心频率分别与填隙材料在模板中填充率ff、模板煅烧因子sf的关系曲线:随ff的减小,v增大;随sf的增大,v随之增大,非理想状态下,ff<100%、sf>1,因此较理想态发生蓝移;由此提出了求解平均填充率ffev与平均煅烧因子sfev的计算框图。
4) media-filling rate
填料填充率
1.
The influence of air-water ratio,HRT(hydraulic retention time),media-filling rate for biological contact oxidation tank and dosage of flocculating agent,surface loading for flotation tank on pollutants removal was studied.
开展了生物接触氧化/气浮工艺处理微污染源水的中试研究(规模为20 m3/h),考察了生物接触氧化池的气水比、水力停留时间、悬浮生物填料填充率和气浮池混凝剂投加量、表面负荷对污染物去除效果的影响。
5) filling ratio
充填率
1.
As a result,the manipulate conditions were determined of the steel ball medium filling ratio and original ratio,grinding production and concentration,and compared with the energy saving on several type mill.
4m加长非标型球磨机的基本参数,确定了钢球充填率、原始配比、给矿速度、磨矿浓度等操作条件,并对耗能进行了对比,指出下一步应改进之处。
6) packing fraction
充填率
1.
Some concrete suggestions for increases of packing fraction and rotating speed are presented, the rotating speed is 11.
提出增加充填率和加快转速的具体措施。
2.
18 m×3 m ball mill with double chambers(the front chamber for steel shot and the rear for steel roll), overfall type, packing fraction of 35%～40% and productive capacity of 3 t/h phosphate rock was retrefitted into the one with double chambers, overfall type through grating, packing fraction of 55%～60% and productive capacity of 6 t/h.
8m×3m双仓磨机处理磷矿石,按溢流磨机标准装填磨料时,进料仓装钢球,出料仓装钢棒,磨料综合充填率35%～40%,处理磷矿量3t/h左右。
补充资料：填充离子交换树脂的电渗析器、电渗析填充床等
分子式：
CAS号：
性质：又称填充离子交换树脂的电渗析器、电渗析填充床等。这是将离子交换树脂充填入电渗析器隔室中，将电渗析与离子交换树脂结合一起的一种脱盐方法。这种装置可以提高脱盐室的电导，并能有效地防止极化沉淀以制备高纯水。但其结构比较复杂，拆装不便。其工作原理为：将H+，OH-型阳、阴树脂予混后填充入电渗析器脱盐室。在直流电场作用下，阴、阳树脂与溶液中的阴、阳离子进行交换。之后，由于电解再生，树脂分别又转为H+，OH-型，解吸的阴、阳离子分别通过阴、阳膜进入浓缩隔室。
CAS号：
性质：又称填充离子交换树脂的电渗析器、电渗析填充床等。这是将离子交换树脂充填入电渗析器隔室中，将电渗析与离子交换树脂结合一起的一种脱盐方法。这种装置可以提高脱盐室的电导，并能有效地防止极化沉淀以制备高纯水。但其结构比较复杂，拆装不便。其工作原理为：将H+，OH-型阳、阴树脂予混后填充入电渗析器脱盐室。在直流电场作用下，阴、阳树脂与溶液中的阴、阳离子进行交换。之后，由于电解再生，树脂分别又转为H+，OH-型，解吸的阴、阳离子分别通过阴、阳膜进入浓缩隔室。
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