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1)  bottom blowing CaCO_3
底吹CaCO_3
2)  CaCO3
CaCO_3
1.
Influence of Hyperbranched DHBC with Carboxyl Terminal Groups on the Crystallization of CaCO3;
超支化双亲水性嵌段共聚物对CaCO_3结晶影响的研究
2.
By compounding nano-CaCO3 with polyoxymethylene (POM) , the influence of nano-CaCO3 content, diameter on the mechanical properties, dispersion morphology of POM/nano-CaCO3 composties was investigated.
用纳米CaCO_3填充改性聚甲醛(POM),研究了纳米CaCO_3的含量、粒径对POM/纳米CaCO_3复合体系力学性能、分散形态等的影响。
3.
Polypropylene(PP) and CaCO3 blends were extruded in self-made dynamic capillary rheometer, and the effects of vibrating parameters on the dispersion of CaCO3 in melted PP were studied.
使用自制的毛细管动态流变仪挤出聚丙烯(PP)与CaCO_3混合料,研究了振动参数对CaCO_3在PP中分散效果的影响。
3)  calcium carbonate
CaCO_3
1.
Relationship of calcium carbonate content and water regime to bicarbonate content in the growth medium;
生长介质中CaCO_3质量分数及水分状况与HCO_3~-的关系
4)  bottom-blowing
底吹
1.
The flow field in liquid Wood's metal with centric gas bottom-blowing was predicted by a mathematical model.
本文用数学模型法预报了中心底吹气体搅拌的液态伍德合金流场。
2.
The critical value of liquid steel drawing slag is calculated out according to the relation between the bottom-blowing gas quantity of ladle and flowing speed on interface between molten steel and slag.
根据钢包底吹气量与钢渣界面流速的关系计算出钢水卷渣的临界值,按照相似原理用混合油模拟渣层、水模拟钢水进行水模试验,考察了吹气量、单双孔底吹透气砖对钢水卷渣行为的影响,单孔吹气量小于450L/min、双孔吹气量小于400L/min可避免卷渣。
5)  bottom blowing
底吹
1.
Realization of control programs of bottom blowing for No.1 converter in Baogang;
包钢1#转炉底吹控制程序的实现
2.
Reform of computer controlling system of converter bottom blowing;
转炉底吹计算机控制系统的改造
3.
The design and application of an automatic control system for the bottom blowing of a combined top-bottom blown converter;
基于PLC和IPC的长寿复吹转炉底吹自动控制系统设计与应用
6)  bottom stirring
底吹
1.
In the present study,a water model of slag ladle was used with a photographic technique to determine the effect of viscosity and bottom stirring gas flow rate on surface spout characteristics of the solution.
通过摄像法测定了粘度、气体流量对底吹渣罐水模型表面突起高度和宽度的影响。
2.
Over all and free surface gas liquid volumetric mass transfer coefficient in water model which is 1∶7 scale of 30 t bottom stirring EAF is determined from the relations of pH value and CO 2 content.
根据溶液的pH值与CO2溶解量间的关系,测定了30t底吹电弧炉1∶7水模型中溶液的气液总综合传质系数(kLA)与液体表面的气液综合传质系数(kLA)S,由此计算了气泡区综合传质系数(kLA)B。
补充资料:顶底复吹转炉的炉底(正在倾炉出钢)(宝钢)


顶底复吹转炉的炉底(正在倾炉出钢)(宝钢)


顶底复吹转炉的炉底(正在倾炉出钢)(宝钢)
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