Energy-saving device and process for vaporizing methyl chloride as organic silicon monomer raw material
A methyl chloride and organosilicon technology, which is applied in the field of organosilicon monomer production equipment, can solve the problems of energy waste, heat dissipation of steam condensed water, large energy consumption, etc., and achieves the effects of reducing production costs, reducing consumption, and smoothing hydrophobicity.
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Embodiment 1
[0019] An energy-saving device for the vaporization of organic silicon monomer raw material chloromethane, the top of the thermally coupled heat exchanger 1 is connected to the bottom of the steam condensed water preheater 2, the top of the steam condensed water preheater 2 is connected to the bottom of the reactor 3, and the reactor 3 The top is connected with the rectification tower 4, and the bottom of the rectification tower 4 is connected with the rectification tower reboiler 5 and then connected with the lower part of the rectification tower 4 to form a circulation loop.
[0020] The rectification column reboiler 5 is connected to the upper part of the steam condensate water preheater 2 .
[0021] The top of the rectification tower 4 is connected to the upper part of the thermal coupling heat exchanger 1 .
[0022] The bottom of the thermal coupling heat exchanger 1 is provided with a liquid methyl chloride inlet pipe; the lower part is provided with a rectification towe...
specific Embodiment approach
[0025] Liquid chloromethane first enters the thermally coupled heat exchanger (1) for primary preheating, and the heat medium used for preheating is the high-temperature gas at 50~60°C extracted from the top of the rectification tower (4); then enters the steam condensate water preheating Heater (2) performs two-stage preheating. The heat medium used for preheating is 1.0MPa steam condensed water. The 1.0MPa steam condensed water comes from the rectification tower reboiler (5). The heated gaseous methyl chloride has a temperature of 50~60°C and a pressure of 0.3~0.8MPa, and enters the reactor (3) for synthesis reaction of organosilicon monomer, and the reacted gas phase mixture enters the rectification tower (4) for purification and rectification The high-temperature gas extracted from the top of the tower (4) enters the thermally coupled heat exchanger (1) as a heat medium to cool, and then enters the condenser to condense, and can be extracted as a product.
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