Suitable grain size proportion of coke fines for sintering fuel cells

Removal of catalyst fines from FCC slurry

催化裂化油浆催化剂粉末的脱除技术

The slurry oil withdrawn from heavy oil catalytic cracking contains catalyst fines which should be separated.

重油催化裂化油浆中含有催化剂粉末，需加以分离。

Study on grinding of cracking catalyst fines

裂化催化剂细粉研磨的研究

Utilization of the cracking catalyst fines recovered by the third stage cyclone

催化裂化装置三级旋风分离器回收的催化剂的利用

Pilot plant test of removing catalyst fines from FCC slurry with sintered stainless steel filter core

不锈钢粉末烧结滤芯脱除FCC油浆中催化剂粉末中试研究

Micro stress for nano Co catalyst fines by high energy ball milling

高能球磨纳米Co系催化剂粉末的微观应力

The speed and degree of water-rock reaction will increase with temperature, and mineral fines produced by chemical reaction contribute mainly to pore block when temperatures reach 200~ 300 ℃.

当温度升高时，水-岩反应的速度和程度提高；当温度上升到200~300℃时，由化学反应所产生的微粒将成为孔隙堵塞的主要原因。

A Study on Mineral Fines as Strengthening Agent to the Products of Silicone Rubber

矿物粉体作硅橡胶制品增强剂的研究

Functional groups on mineral fines surfaces and their effects in materials

矿物粉体表面官能团及其在材料中作用

In sintering process, for melted mineral fines bind unmelted core ores when cooled, the self-intensity of binding phase in iron ores is one of the basic indexes to estimate sintered binding status.

在铁矿粉烧结过程中，熔化的矿粉在冷却过程中起着粘结周围未熔矿粉的作用，因此这一粘结相的自身强度是衡量烧结矿固结状况的重要指标之一。

By means of IR spectrophotometer, the authors study the modifying action of silane coupling agent on the surface of clay mineral fines including kaolin and illite.

本文应用红外分光光度计，研究硅烷偶联剂对高岭土、伊利石等粘土矿粉的表面改性作用。

Experimental Study on Sintering of Iron Ore Fines With Medium Crystal Water Content

含中等程度结晶水的铁矿粉烧结试验研究

A preliminary numerical simulation study on iron ore fines fluidized bed

铁矿粉冷态流化床数值模拟的基础研究

Application Technology of Chromite Ore Fines for Producing Stainless Steel Master Alloy

生产不锈钢母液的铬矿粉利用技术

Study on High Properties Pellets Produced by Manganese Ore Fines Containing High Combined Water

高结晶水锰矿粉制备高性能球团研究

The desilting rate for coarse grain which diameter more than 0 5 mm is 100 percent, and for fines which grain diameter less than 0 5 mm is 90 percent, the water consumption is only 2-3 percent of channel diversion.

对0.5mm以上的粗颗粒泥沙的截沙率为100%，对0.5mm以下细颗粒泥沙的截沙率为90%，排沙耗水量仅占渠道引水量的2%～5%。

Using CeO_2 as Fining Agent

采用CeO2做为澄清剂

Specific carrageenan as a beer fining agent

卡拉胶作为啤酒澄清剂的功能特性

Chitosan as Fining Agent For Clarification of Apple Juice

壳聚糖澄清果汁作用的研究

Discussion on some issues of sulfate as fining agent in glass melting

硫酸盐在玻璃澄清中的若干问题探讨