1) impinging stream-rotating packed bed
撞击流-旋转填料床
1.
The percentage of making emulsion in impinging stream-rotating packed bed, the phenol removal efficiency in rotating packed bed and the effects of the way of transmembrane pressure and the membrane pore size on the demulsification process by inorganic microporous membrane were studied.
实验研究了对所采用的制乳设备——撞击流-旋转填料床对制乳率,提取设备——旋转填料床对脱酚率和破乳设备——无机微孔膜外压内抽式膜法破乳的重要参数如透过压方式、膜孔径等对膜通量和破乳率的影响。
2.
The percentage of making emulsion in impinging stream-rotating packed bed,the phenol removal efficiency in rotating packed bed and the effect of the way of transmembrane pressure and the membrane pore size on the demulsification process by inorganic microporous membrane were studied.
对所采用的制乳设备———撞击流-旋转填料床对制乳率、提取设备———旋转填料床对脱酚率、破乳设备———无机微孔膜法破乳的重要参数(如透过压方式、膜孔径等对膜通量和破乳率的影响)进行了研究。
2) impinging steam-rotating packed bed
撞击流-旋转填料床
1.
Ultrafine β-Cu powder was synthesized by high gravity reactive precipitation method from(CuSO_4·5H_2O) and β-H using impinging steam-rotating packed bed.
以五水硫酸铜和2,4-二羟基苯甲酸为原料,利用撞击流-旋转填料床合成了热敏性材料2,4-二羟基苯甲酸铜(β-Cu)粉体,研究了制备过程中撞击初速、转速、浓度、温度、陈化时间和干燥方式对粉体粒径的影响。
3) Impinging stream-rotating packed bed
撞击流旋转填料床
1.
The optimum condition was determined about making emulsion liquid membrane by impinging stream-rotating packed bed and treating phenolic effluent by rotating packed bed.
采用了煤油 Span80 石蜡 氢氧化钠组成的液膜体系,研究了利用撞击流旋转填料床制备乳化液膜并用旋转填料床进行含酚废水处理的最适宜工艺条件,讨论了制乳转速、水乳比、Span80用量、NaOH溶液浓度、提取流量对提取率的影响。
4) impinging stream rotating packed bed reactor
撞击流-旋转填料床反应器
5) rotating packed bed
旋转填料床
1.
Research on treatment of ammonia in phosphate tail gas by rotating packed bed;
旋转填料床净化磷肥尾气中的氨气
2.
Experimental studies on ozone oxidative treatment of dye wastewater in a rotating packed bed;
旋转填料床中臭氧化处理染料废水的试验
3.
Experimental study on capacity of gas hydrate in a rotating packed bed;
超重力旋转填料床中天然气水合物含气量研究
6) Rotating packed bed technology
旋转填料床技术
补充资料:XLB型旋转流化床制丸(粒)包衣机
[工作原理]
粉末或者母粒在旋转流化床内,受到环隙空气浮力、旋转离心力、自身重力作用,呈环周绳股状,粘合剂或包衣液喷入料层形成真球度极高的丸粒或连续均匀的衣膜。
[特 点]
转子速度连续可控。
粒丸在床内处于泛丸状态,使其表面致密,真球度极高。
适用于粉末微粒、微粒包衣、制丸、包衣。
[原理图]
[外形尺寸图]
[技术参数]
1.5 | 10 | 20 | 30 | 60 | 120 | |||
工作容积 | L | 5 | 30 | 60 | 105 | 180 | 420 | |
投料量 | kg/批 | 1.5 | 10 | 20 | 30 | 60 | 120 | |
旋转功率 | Kw | 0.55 | 1.5 | 4 | 5.5 | 7.5 | 11 | |
风机功率 | Kw | 4 | 5.5 | 7.5 | 15 | 18.5 | 22 | |
蒸汽耗量 | Kg/h | 35 | 42 | 84 | 166 | 250 | 332 | |
压缩空气量 | m3/min | 0.3 | 0.6 | 0.6 | 0.9 | 0.9 | 1.1 | |
安装尺寸参考 | A | mm | 2175 | 2250 | 2400 | 2550 | 2850 | 3300 |
B | mm | 905 | 1040 | 1240 | 1540 | 1960 | 2280 | |
C | mm | 1200 | 1350 | 1800 | 2050 | 2550 | 3200 | |
D | mm | 920 | 970 | 1130 | 1130 | 1180 | 1380 |
说明:补充资料仅用于学习参考,请勿用于其它任何用途。
参考词条