1) porous adsorbent bed
多孔吸附床
2) Porous adsorbents
多孔吸附剂
1.
A series of poly(styrene-co-divinylbenzene) (St-DVB) porous adsorbents were prepared according to the suspension polymerization in the presence of toluene and n-heptane as mixed porogen with various Fm (the volume fraction in the organic mixture), composition of porgen (the volume ratio of toluene and n-heptane) and DVB% (the degree of crosslinking, i.
以甲苯和正庚烷为混合致孔剂,在不同的致孔剂组分、单体百分含量和交联度的条件下,通过悬浮聚合法制备了一系列聚苯乙烯-二乙烯苯(St-DVB)多孔吸附剂。
3) porous starch absorption
多孔淀粉吸附
1.
Different control-released materials of essential oil were prepared by microencapsulation and porous starch absorption.
用微胶囊化及多孔淀粉吸附法,制备一系列具有不同缓释性能的精油缓释制剂。
4) adsorbent bed
吸附床
1.
The structural designs & researches ofthe new solid adsorbent bed;
新型固体吸附制冷吸附床的结构比较研究
2.
Analysis of the heat and mass transfer process and design of the structure of adsorbent bed in adsorption refrigeration system;
吸附制冷系统中吸附床的传热传质分析及结构设计
3.
To shorten the refrigeration cycle of the solar solid adsorption refrigeration system, a system of solar solid adsorb refrigeration was put forward and a model of single tube was founded aiming at the concrete adsorbent bed in this paper.
针对具体的吸附床,建立了吸附床内单元管传热传质的数学模型,并运用多孔介质传热传质的理论分析了吸附床内单元管的传热传质的计算方法,列出了控制方程组和初始、边界条件。
5) Adsorption bed
吸附床
1.
Numerical simulation and heat transfer analysis of temperature field for adsorption bed of solar energy adsorption refrigeration air conditioner;
太阳能吸附制冷空调吸附床温度场数值模拟与传热分析
2.
Experimental study of heat transfer in natural gas adsorption bed during a desorption process;
天然气吸附床脱附过程的传热实验研究
3.
An experiment for heat transfer in a natural gas adsorption bed under adiabatic condition is made.
对天然气吸附床在绝热条件下进行了传热试验,试验测量了吸附床在吸附过程中的温度分布与变化,试验结果表明,吸附床的温度随充气量的增加不断升高,数值达75℃左右,而且温度分布极不均匀,相差达30℃。
6) Single adsorbent bed
单吸附床
补充资料：固定床吸附塔
分子式：
CAS号：
性质： 即用于固定床树脂清液吸附的离子交换装置。用于铀矿浸出液离子交换过程的固定床吸附塔的塔体一般用普通碳钢衬耐蚀材料制成，内部管路和分布器多用塑料或不锈钢制作。塔高一般为3.65m，塔径为2.13m，树脂充填体积为5.7m3。塔内树脂床上部的自由空间体积一般与原型树脂床的体积相等。
CAS号：
性质： 即用于固定床树脂清液吸附的离子交换装置。用于铀矿浸出液离子交换过程的固定床吸附塔的塔体一般用普通碳钢衬耐蚀材料制成，内部管路和分布器多用塑料或不锈钢制作。塔高一般为3.65m，塔径为2.13m，树脂充填体积为5.7m3。塔内树脂床上部的自由空间体积一般与原型树脂床的体积相等。
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