Method for continuously preparing 2,6-dinonyl naphthalene sulfonic acid
A technology of dinonylnaphthalenesulfonic acid and nonylnaphthalenesulfonate, which is applied in the fields of sulfonic acid preparation and organic chemistry, can solve the problems of low product purity, difficult reaction control, difficult separation of products, etc., and achieve high product purity , fast gas-liquid separation, low equipment maintenance and operation costs
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Embodiment 1
[0032] Heat the stripping tower to bring the 20% oleum storage tank to 150±2°C, dilute the sulfur trioxide with dried air to an average gas concentration of 4.82wt%, press 2,6-dinonylnaphthalene: sulfur trioxide =1:1 (mol:mol) ratio, 2,6-dinonylnaphthalene is introduced into the upper end of the falling film sulfonation reactor, after 2,6-dinonylnaphthalene is metered, it passes through the uniform distributor along the sulfonation reaction The inner wall of the reactor is membrane-like flow down, and the SO sprayed from the central nozzle of the sulfonation reactor 3 , Dry air mixture occurs membrane sulfonation reaction on the inner wall of sulfonation reaction, the reaction extends downward, and local overheating is avoided. The external cooling water jacket of the reactor, the temperature of the upper jacket is about 22°C, the temperature of the lower jacket is about 31°C, and the inside of the reactor is maintained at 50°C. The product mixture from the falling film sulfo...
Embodiment 2
[0034] Heat the stripping tower to bring the 20% oleum storage tank to 153±2°C, dilute the sulfur trioxide with dried air to an average gas concentration of 5.0wt%, press 2,6-dinonylnaphthalene: sulfur trioxide =1:1.2 (mol:mol) ratio, 2,6-dinonylnaphthalene is introduced into the upper end of the falling film sulfonation reactor, after 2,6-dinonylnaphthalene is metered, it passes through the uniform distributor along the sulfonation reaction The inner wall of the reactor is membrane-like flow down, and the SO sprayed from the central nozzle of the sulfonation reactor 3, Dry air mixture occurs membrane sulfonation reaction on the inner wall of sulfonation reaction, the reaction extends downward, and local overheating is avoided. The external cooling water jacket of the reactor, the temperature of the upper jacket is about 24°C, the temperature of the lower jacket is about 33°C, and the inside of the reactor is maintained at 52°C. The product mixture from the falling film sulfo...
Embodiment 3
[0036] Heat the stripping tower to bring the 20% oleum storage tank to 148±2°C, dilute the sulfur trioxide with dried air to an average gas concentration of 4.5wt%, press 2,6-dinonylnaphthalene: sulfur trioxide =1:1.1 (mol:mol) ratio, 2,6-dinonylnaphthalene is introduced into the upper end of the falling film sulfonation reactor, after 2,6-dinonylnaphthalene is metered, it passes through the uniform distributor along the sulfonation reaction The inner wall of the reactor is membrane-like flow down, and the SO sprayed from the central nozzle of the sulfonation reactor 3 , Dry air mixture occurs membrane sulfonation reaction on the inner wall of sulfonation reaction, the reaction extends downward, and local overheating is avoided. The external cooling water jacket of the reactor, the temperature of the upper jacket is about 24°C, the temperature of the lower jacket is about 32°C, and the inside of the reactor is maintained at 48°C. The product mixture from the falling film sulf...
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