A method for producing trichloroisocyanuric acid in a supergravity field
A technology for producing trichloroisocyanide and hypergravity field, which is applied in the direction of organic chemistry, etc., can solve the problems of low comprehensive value of recyclability, high consumption of kettle type reactor, high process labor intensity, etc., and achieves the advantages of recycling operation, The product yield is safe and environmentally friendly, and the effect of easy promotion and application
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Embodiment 1
[0024] The steps of producing trichloroisocyanuric acid are as follows:
[0025] (1) Hypochlorous acid mist production: Excess chlorine gas and metal oxides are reacted in the hypergravity field formed by the first hypergravity reactor, and hypochlorous acid mist is separated upwards, and chlorine is separated downwards. Salt solution, recovery and extraction of chloride salt in the chloride salt solution, the remaining chlorine gas is discharged from the tail gas outlet of the first high gravity reactor and then returned to the first high gravity field to prepare hypochlorous acid mist;
[0026] (2) Desalting: use a salt catcher to desalt the hypochlorous acid mist produced in step (1);
[0027] (3) Preparation of trichloroisocyanuric acid: the hypochlorous acid mist and cyanuric acid slurry treated in step (2) undergo a gas-liquid-solid three-phase reaction in the hypergravity field formed by the second hypergravity reactor to obtain Trichloroisocyanuric acid. The cyanuric...
Embodiment 2
[0031] The differences between this embodiment and Embodiment 1 are:
[0032] In step (1), chlorine gas and metal hydroxide react in the hypergravity field formed by the first hypergravity reactor, and the metal hydroxide can specifically be sodium hydroxide, calcium hydroxide or / and magnesium hydroxide, etc., as long as It only needs to be able to consume the hydrochloric acid produced in the reaction, and its specific substance is not specifically limited;
[0033] In step (3), the preparation of trichloroisocyanuric acid: the concentration of the cyanuric acid slurry used is 35%, and the molar ratio of chlorine gas to cyanuric acid is 6:1.
[0034] The prepared trichloroisocyanuric acid has been tested and its available chlorine is above 91.5%. All the other are the same as embodiment one.
Embodiment 3
[0036] The differences between this embodiment and Embodiment 1 are:
[0037] In step (1), chlorine gas and carbonate react in the hypergravity field formed by the first hypergravity reactor. Specifically, the carbonate can be sodium carbonate, calcium carbonate or / and magnesium carbonate, as long as it can consume the Hydrochloric acid can be used, and its specific substance is not specifically limited;
[0038] In step (3), the preparation of trichloroisocyanuric acid: the concentration of the cyanuric acid slurry used is 50%, and the molar ratio of chlorine gas to cyanuric acid is 10:1. All the other are the same as embodiment one.
[0039] The prepared trichloroisocyanuric acid has been tested and its available chlorine is above 91.4%. All the other are the same as embodiment one.
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