Problems with pressure swing adsorption hydrogen production systems
Thread Content
I want to build a pressure swing adsorption hydrogen production system with a normal capacity of 400 standard cubic feet per hour, and a maximum capacity of 2000 standard cubic feet per hour. The difference between the normal amount and the maximum amount is too large; I don’t know what to do. Please give me some advice.
Build a 2000 model directly, using an inverter compressor.
Hello classmate, if you plan to build such a facility, you might consider cooperating with us. We will fund the construction for you, and all you need to do is use the gas; you can then pay a reasonable fee each month based on the amount measured by the meter and the corresponding price. To avoid any other concerns. What do you think? Contact me! 15832633424 Yu Qiang, Beijing Zhengtuo Gas Technology Co., Ltd.
First, determine the times of the wave peaks and troughs for using hydrogen, and then decide on the scale of hydrogen production!
We can help you build it on your behalf – no problem. EPC is a bit too limited, but that’s okay
For variable-frequency compressors, I think it would work to install a tank at the air intake and use a control valve to stabilize the air volume
The load range of pressure swing adsorption is wide, between 30% and 120%.