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Discussion on the safety design for sharing a chlorine drying system between diaphragm and ion exchange membranes

2008-01-01View Original

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This post was last edited by sunjl1981 on 2013-1-6 at 23:45. Our company has a caustic soda production project with an annual capacity of 160,000 tons; the first phase involves 60,000 tons per year of diaphragm caustic soda, while the second phase covers 100,000 tons per year of ion-exchange membrane caustic soda. The original design called for a single chlorine drying system to be used for both phases. Now, the construction of the ion-exchange membrane caustic soda facility in the second phase has entered the design stage. Since there is very little knowledge available regarding manufacturers that share the same chlorine drying system, I have some concerns about the design approach proposed by the design institute, which involves first using a pressure reducing valve to lower the chlorine pressure to zero, and then passing the chlorine through a water seal before it mixes with the chlorine from the chlorine scrubber tower and diaphragm system and is integrated into the system. I would appreciate any guidance from experienced experts. # , , &
Reply #22008-01-01
The chlorine gas produced by diaphragm caustic and ion-exchange membrane caustic can share the same chlorine drying system. Our company uses one chlorine treatment system for 4 WT/year of diaphragm caustic and 10 WT/year of ion-exchange membrane caustic; it has been in operation for over half a year with no problems so far.
Reply #32008-01-01
Is the method mentioned by the original poster being used? Could you explain in detail how the two systems are connected?
Reply #42008-01-04
You can ask Yibin Tianyuan and Shandong Jinling; they are both in the same place.
Reply #52008-01-06
The guys above didn’t specify the exact process; I hope everyone can continue to offer their guidance! Thank you!
Reply #62008-01-08
A titanium fan can be installed at the diaphragm chlorine outlet to increase its pressure, after which it can be combined with the ion-exchange membrane chlorine gas
Reply #72008-01-08
It can be considered, but I’m not sure if the plan proposed by the design institute will work
Reply #82008-01-08
There is a concern regarding the titanium fan installed at the diaphragm chlorine outlet: whether the pressure will remain stable and whether this could affect the level of the brine

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