I was wondering if I could ask a colleague to help write out the startup and shutdown procedures for ion-exchange membrane caustic soda. Is that possible?
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This post was last edited by sunjl1981 on 2013-1-6 at 19:52. Our company is about to install an ion exchange membrane system, and we were wondering if any colleagues could help us draft the startup and shutdown procedures for ion exchange membrane caustic soda production. Would that be possible? This post was last edited by yzhms on 2009-4-7 12:48 ] # ， ， &
I would like to ask the moderators how to find in the forum the information I’m looking for, namely the start-up and shutdown procedures for ion-exchange membrane caustic soda production Thank you!
What is your specific process? Please explain it. If you want to commission the development of start-up and shutdown procedures that are perfectly suited to your needs, this may incur costs; it would be better if you arrange for your own staff to develop them.
I just want to refer to it. The existing ones are usually fine. But in more detail. Thank you
The materials needed by the poster, as there is a lot of content, have been uploaded to the resource sharing area; please download them from the following address. http://bbs.hcbbs.com/viewthread. ... ge=1&extra=page%3D1 Last edited by sgh1966 on 2009-4-9 22:51]
I’m from the control room; I’ve been on site in the workshop. There are many plans for reducing emissions during operation. First, run the secondary brine system once, increasing the current from 0 to 3 KA. For the chlorination process, adjust the chlorine level using the air intake valve and the chlorine compressor; as for the nitrogen compressor, just keep it running without worrying about the current level. At 5 KA, start the liquefaction unit, and then proceed to start the furnace unit. It’s not convenient to provide detailed instructions on how to carry out these operations. By the way, which factory do you work for?