CONTROL OF PHYSICAL STRUCTURE OF SILICA-ALUMINA CATALYST
CONTROL OF PHYSICAL STRUCTURE OF SILICA-ALUMINA CATALYST
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DOI:
10.1021/ie50516a029
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发表时间:
1952-01-01
影响因子:
--
通讯作者:
INNES, WB
中科院分区:
文献类型:
--
作者:
ASHLEY, KD;INNES, WB
This presented the problem of developing a process suitable for the handling of over 160 tons per day of gelatinous silica. The old method, based on the concept that the silica gel had to be partly dried with low temperature air and then washed free of sodium before applying the aluminum, appeared impractical for such a large scale operation.It was soon established that washing the hydrogel with the large volume of water required to free it of sodium would require a reslurrying operation because of cracking of the filter cake. The most economical way of carrying out such an operation is to wash on a series of vacuum drum-type rotary filters with repulping of the cake between each stage of filtration. Attempts to do this soon demonstrated that the gel slurry prepared by mixing acid and sodium silicate with moderate agitation had too broad a range of particle size. The semicolloidalmaterial quickly blinded a filter cloth so that the gel could not be washed on a rotary filter. The problem was first solved by one of the authors (3) by use of a screen-shrouded impeller-agitator during the mixing of acid and silicate, followed byaddition of a flocculating agent (4)—ie, glue or aluminum hydroxide. This gave a gel slurry of optimum particle size for rotary filtration and washing. Theflocculating effect of aluminum hydroxide made it seem that addition of an aluminum salt and ammonia before filtering, washing, or drying the hydrogel would solve the washing problem and greatly sim-plify operations. Therefore, this procedure was tried while vary-ing temperature, concentra-