1)  drying process
干燥工序
1.
This paper takes content of moisture and total saponin as quality index,draws the control chart of drying process of American gensing,judges stability of the process by control chart analysis,realizes dynamic control in the process.
以水分含量和西洋参总皂苷含量为质量指标,绘制西洋参干燥工序的控制图。
2)  drying
干燥
1.
Recent drying developments in Japan;
日本干燥技术的最新进展
2.
Experimental study on microwave drying of maize grain;
微波干燥玉米籽粒的试验研究
3.
Experimental study on drying kinetics of nanometer magnesium hydroxide;
纳米氢氧化镁的干燥动力学试验研究
3)  dry
干燥
1.
Study on potato′s adsorption drying conditions and quality;
马铃薯吸附式干燥条件及品质研究
2.
Choice and use of microwave dryer to hi-pure nano strontium carbonate;
高纯纳米碳酸锶干燥设备的选型和使用
3.
Applications of Paddle Drying Technology in PVA Production;
桨叶干燥技术在聚乙烯醇生产中的应用
4)  dryness
干燥
1.
Study on the dryness of urushiol catalyzed by PrCl_3;
PrCl_3催化漆酚干燥成膜的研究
2.
Influence of Processes of Concentration,Refine and Dryness onSoluble Constituent of Extractive Solution of Compound Saliva Miltiorrhiza;
浓缩、精制及干燥对复方丹参提取液中水溶性成分的影响
3.
Based on the calculation of the energy required for the pyrolysis and dryness of biomass,the selection of a suitable biogas processing and supplying unit as an energy source for drying biomass and heating up heat carrier in the process of producing bio-oil is of great practical and economic value in reducing energy consumption and production cost in large-scale production of bio-oil.
根据生物质热解及其干燥所需能量计算,选择一种生物质燃气制气供气装置作为生物燃油生产过程中用于生物质干燥和热载体加热的能量来源,对降低生物燃油规模化生产能耗和生产成本具有重要的研究实践价值和经济意义。
5)  dehydration
干燥
1.
The time of dehydration is sharply shortened.
38m/s的干燥条件,干燥60min可以制得含水27。
2.
Electronic moisture analyzer is used to study the dehydration of alfalfa during drying temperature 80 -230℃ and analyze other factors which influence on drying velocity of stems, leaves and stems with leaves attached and the shrinkage of stems and leaves.
采用红外水分分析仪研究了干燥温度在80-230℃范围内紫花苜蓿的干燥过程,分析了不同干燥因素对其茎、叶和茎叶相连情况的干燥速率的影响以及干燥前后茎、叶的收缩率。
3.
Seed dehydration of seedusing watermelon CV.
在人工控制条件下研究了“甘农一号”籽瓜籽的干燥过程。
6)  desiccation
干燥
1.
Study on the change of chemical components and antibacterial activity of Houttuynia cordata Thunb during desiccation;
鱼腥草干燥过程中化学成分含量及抑菌效果变化的研究
2.
Discussion on Desiccation Technology Application in Generator of Small Hydropower Station;
农村小水电发电机干燥技术探讨
3.
Mechanism design of pulser in pulsation flow desiccation machine;
脉动流化干燥机中脉冲气流发生器的机构设计
参考词条
补充资料：活性污泥干燥工艺及成套干燥设备
一、.工艺特点 该干燥工艺是针对高水份污泥(大于65%,小于85%)的干燥特点而设计的,干燥时,物料容易粘结成 团,因而采用搅拌气流干 燥机进行作业,搅拌气流干燥机采用强力打击剪切,破碎,抛撒的方式,将粘结而成的团块 破碎成微粒,增大物料与空气进行湿热交换的面积,使干燥有效地进行,提高干燥效率. 本工艺要求处理量大,物料终水份要求不高,因而采用二级搅拌气流干燥机串联作业以满足 干燥要求.配以直火式热风炉的热源,该热风炉热效率达90%以上,热风温度达900`C, 有条件时还可将锅炉尾气引入进一步降低能耗.
　该成套设备可用于造纸厂,制革厂,食品厂等活性污泥的干燥;酿造厂,豆制品厂. 淀粉加工厂等 渣物料的干燥;养鸡厂,养猪厂等粪便物料的干燥.
 
二、工作原理
　　物料由加料机加入搅拌干燥机后,受到同速转向相向的打板的打击,剪切,抛散,成 雾状弥漫于整个干燥器内,与热风炉进来的热空气进行强烈的湿热交换,强化干燥.由于打板的打击. 剪切,使物料难以粘结成团形成外焦内湿的小球,并使物料的表面和表面积不断地变化 ,从而顺利地进行干燥.当物料干燥到一定程度后,物料被气流夹带进入二级搅拌气流 干燥机中进行进一步干燥,最后由旋风分离器分离.
三,主要技术经济指标
　　 处理量: 6.25t/h       　　 物料初水份: <85%     　　 终水份: <40%
　　 水份蒸发量: 4.48T/H   　　 装机功率: 85KW       　　 煤耗: 700KG/小时
　　 占地面积: 10*20(M)    　　 操作人数: 7人
四,主要设备
　　 1. 加料机 2台    　　 2. 直热式热风炉 2台   　　 3. 搅拌气流干燥机 2台
　　 4.旋风分离器 2台      5. 引风机 1台   
说明：补充资料仅用于学习参考，请勿用于其它任何用途。