Energy-efficient sulfonation reaction device and method for naphthalene water reducers
A naphthalene-based water-reducing agent and sulfonation reaction technology, applied in chemical instruments and methods, chemical/physical/physical-chemical stationary reactors, chemical/physical processes, etc., can solve the problem of low heat utilization efficiency and uneven heating , long reaction time of the synthesis process, etc., to achieve the effect of improving efficiency and reducing cost
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Embodiment 1
[0031] A high-efficiency and energy-saving naphthalene-based water reducer sulfonation reaction device, including a sulfonation reactor 1, the top of the sulfonation reactor 1 is provided with a waste gas outlet 2; the outer wall of the sulfonation reactor 1 is provided with a jacket 3 , the lower part of the jacket 3 is provided with a heat transfer oil inlet 4, and the top of the jacket 3 is provided with a heat transfer oil outlet 5, and the heat transfer oil inlet 4 and the heat transfer oil outlet 5 are respectively connected with the heat transfer oil heating cycle device The outlet is connected to the inlet; the jacket 3 is provided with a baffle 6 extending spirally from the heat transfer oil inlet 4 to the heat transfer oil outlet 5, and the baffle 6 separates the jacket 3 into a spiral flow road. The sulfonation reactor 1 is provided with a stirring device 7 . It also includes a naphthalene melting tank 8; the outer wall of the naphthalene melting tank 8 is provided...
Embodiment 2
[0033] (1) Put solid industrial naphthalene into the naphthalene melting kettle, and enter high-temperature steam (above 100° C.) from the steam inlet into the heating channel of the naphthalene melting kettle. When the temperature in the naphthalene melting kettle reaches 80° C., the industrial naphthalene starts Melting; when the industrial naphthalene is completely melted, it is transported from the material outlet to the sulfonation reactor through a gear pump.
[0034] (2) Import high-temperature heat-conducting oil with a temperature of 135°C into the jacket of the sulfonation reaction kettle from the heat-conduction oil inlet, heat the sulfonation reaction kettle, and simultaneously weigh it according to the weight ratio of industrial naphthalene:concentrated sulfuric acid of 1.0 For 98% concentrated sulfuric acid, heat up to 128°C, start stirring, and start to add concentrated sulfuric acid dropwise; the sulfuric acid is added dropwise for 0.9 hours, and then react at a...
Embodiment 3
[0037](1) Put solid industrial naphthalene into the naphthalene melting kettle, and enter high-temperature steam (above 100° C.) from the steam inlet into the heating channel of the naphthalene melting kettle. When the temperature in the naphthalene melting kettle reaches 80° C., the industrial naphthalene starts Melting; when the industrial naphthalene is completely melted, it is transported from the material outlet to the sulfonation reactor through a gear pump.
[0038] (2) Import high-temperature heat-conducting oil with a temperature of 140°C into the jacket of the sulfonation reaction kettle from the heat-conduction oil inlet, heat the sulfonation reaction kettle, and simultaneously weigh it according to the weight ratio of industrial naphthalene:concentrated sulfuric acid of 1.05 For 98% concentrated sulfuric acid, heat up to 135°C, start stirring, and start to add concentrated sulfuric acid dropwise; the sulfuric acid is added dropwise for 0.5h, and then the temperature...
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