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The design task is the preliminary design of the hydrogen treatment process 60,000 tons diaphragm legal caustic. The main significance of this design is the main equipment, process design, process calculation as well as auxiliary equipment selection and calculation, to identify the most effective method of handling hydrogen, increase the yield of caustic soda, in order to maximize the use of hydrogen synthesis other products or used as an energy source.
In this design, the first hydrogen material balance and heat balance, and selected a certain basis of calculation in order to facilitate the calculation of hydrogen from the electrolyzer, contains saturated water vapor at the same time with the salt and the entrainment of the alkali in the production process, cooling and washing, and cooling of hydrogen by the hydrogen compressor compressed to a certain pressure, the hydrogen dispensing stations sent to the hydrogen cabinet and hydrogen sector. The design applied to a heat exchanger and cooling tower. Its selection, respectively, with reference to the heat exchanger design "and" tower equipment.
Key words: hydrogen treatment process design process to calculate the selection of equipment

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The purpose of this  work is   to design  the hydrogen treatment process 60,000 tons diaphragm legal caustic preliminarily.

The main significance of this design lies  in  that  through  examinig  the equipment selection and calculation of the main equipment, process design, process calculation as well as auxiliary , and to identify the most effective method of handling hydrogen  and increase the yield of caustic soda. By  this way ,the purpose of maximize the use of hydrogen into other products or used as energy has been achieved.





Therein ,we  firstly   made a  hydrogen material balance and heat balance, and selected a certain basis of calculation in order to facilitate the calculation of hydrogen from the electrolyzer, contains saturated water vapor at the same time with the salt and the entrainment of the alkali in the production process, cooling and washing, and cooling of hydrogen by the hydrogen compressor compressed to a certain pressure, the hydrogen dispensing stations sent to the hydrogen cabinet and hydrogen sector.  thus the design applied the  heating exchanger and cooling tower.
we  made  the  option-type with reference to the heat exchanger design "and" tower equipment,respectively.


Key words: hydrogen  processing   technological design         and  calculation, equipment selection


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