Continuous reforming supercharger problem
Thread Content
The continuous reforming workshop has a three-to-one centrifugal compressor and a 3C control system to control the hydrogen delivery volume and ensure system pressure. Since the beginning of this year, the inlet flow rate of one stage has continued to decline, the outlet pressure of one stage has also dropped, the outlet pressure of the second stage has dropped, the anti-surge valve of the second stage has closed, and the energy consumption of the unit has increased. I suspect that it may be caused by the clogging of the first or second stage inlet filter due to the crystallization of ammonia salts. I wonder if the seniors in the bar have experienced this or have other ideas? I hope you can give me some advice, thank you very much! Provide 3C system control points.
There is probably something wrong with the entrance to a section.
The problem of salt formation at the compressor inlet of the reforming unit is still a common problem. It can be solved from this aspect.
Inlet filter clogged file:///E:/相片/增压机/增压机二级入口过滤器.jpg