Questions about hydrogen chloride compressors
Thread Content
I would like to ask the experts: what should be the hydrogen chloride pressure required for synthesizing trichlorosilane, and what type of compressor should be used? Thank you all first
Each process package is different, right? Generally, a diaphragm pump is used in conditions with low flow rates and high compression ratios
Diaphragm compressor, pressure of 2.5 kg gauge pressure
Diaphragm pumps are generally used; imported 3K models are the better choice
It’s related to the process; we use diaphragm compressors here, with a capacity of 9 kilograms
It is generally determined by the size of the fluidized bed used for synthesizing trichlorosilane and the amount of silicon powder in the bed. We use diaphragm compressors with a bed size of 1400, and an outlet pressure of 2 kilograms is sufficient
The diaphragm compressors produced by Beijing Jingcheng Environmental Protection have an input capacity of around 1 kilogram and an output capacity of around 4 kilograms.
The volumetric flow rate of the compressor here is 60 cubic liters; it seems that its capacity isn’t sufficient
:hug::):o:lol
What is the size of your synthesis furnace? What is the production capacity? Here, the capacity is 20,000 tons per year; the compressor flow rate used is 1,200 M3/h, and the outlet pressure is determined based on your process requirements