Structural layout of the absorber
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In the ammonia absorption refrigeration systems currently in use in the chemical industry, the absorber serves as the main heat exchange device, and its configuration can be vertical or horizontal. There are also two absorption methods: submersion and spraying. What are the advantages and disadvantages of each method? I hope fellow sailors will kindly share their insights; it would be great to have a general layout diagram for reference. Thank you!
I’m also quite interested in this area. Which companies in China are more active in it? We have indeed built isobaric recovery towers; is the amount of ammonia used very large?