Sodium hydrosulfide production technology and apparatus
A sodium hydrosulfide and production process technology, which is applied in the field of acid gas purification, can solve the problems of inability to produce valuable fuming sulfuric acid, difficult operation of the device, and difficulty in popularization, etc.
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Embodiment 1
[0079] use as figure 1 The shown method and device use acid gas and NaOH solution as raw materials for reaction. CO in acid gas 2 The volume fraction is 7%, H 2 The volume fraction of S is 92%, and the volume fraction of hydrocarbons is 1%. The mass concentration of NaOH solution is 38%.
[0080] In this embodiment, the first processor 3 and the second processor 4 are Venturi reactors, and the third processor 6 and the fourth processor 8 are rotary bed processors.
[0081] In this embodiment, the volume flow ratio of the second reaction product liquid 22 from the first processor 3 circulating back to the first processor 3 and the total reaction product liquid of the first processor is 5:6. The volume flow ratio of the second reaction product liquid 20 from the second processor 3 and the total reaction product liquid of the second processor circulating back to the second processor is 2:6, and the secondary reaction product liquid entering the fourth processor and The volu...
Embodiment 2
[0085] use as figure 2 In the shown method and device, in Embodiment 2, the first processor 3 and the second processor 4 adopt image 3 In the shown Venturi reactor, the third processor 6 and the fourth processor 8 adopt rotating bed processors.
[0086] In this embodiment, the volume flow ratio of the reaction product liquid from the first processor 3 and the total reaction product liquid of the first processor 3 that is circulated back to the first processor 3 through the absorption liquid inlet of the first processor 3 is 5: 8. The volume flow ratio of the reaction product liquid from the first processor 3 that circulates back to the first processor 3 through the circulating liquid inlet 32 of the first processor 3 and the total reaction product liquid of the first processor 3 is 5:24.
[0087] The volume flow ratio of the reaction product liquid 21 from the second processor 4 circulating back to the second processor 4 through the absorption liquid inlet of the second p...
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