Heat exchange process in production of polyvinyl chloride
A heat exchange and polyvinyl chloride technology, which is applied in the field of heat exchange technology for polyvinyl chloride production, can solve problems such as cooling loss, and achieve the effects of easy molding, good overall strength and low price.
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Embodiment 1
[0034] The equipment used in this process is two tube-and-tube graphite heat exchangers. The shell side of the primary heat exchanger is mixed gas, and the tube side is vinyl chloride gas; the shell side of the secondary heat exchanger is mixed gas, and the tube side is acetylene gas; the heat transfer coefficient K of the graphite heat exchanger is 20kcal / (m 2h°C). The heat exchange area of the required primary and secondary graphite heat exchangers is selected as 380m 2 , the circulation area is 0.36m 2 . Shell D=1.7m, the outer diameter of the tubes is 32mm, the inner diameter is 22mm, arranged in an equilateral triangle, the spacing between the tubes is 1.25 times the outer diameter of the tubes, a total of 950 pieces, the length of the tubes is 4 meters, and a circular baffle is used. The gaps are arranged up and down, the distance between the baffles is h=0.9m, and the shell is treated with PO lining for anticorrosion.
[0035] The inlet temperature of the mixed ga...
Embodiment 2
[0037] The equipment used in this process is two tube-and-tube graphite heat exchangers. The shell side of the primary heat exchanger is mixed gas, and the tube side is vinyl chloride gas; the shell side of the secondary heat exchanger is mixed gas, and the tube side is acetylene gas; the heat transfer coefficient K of the graphite heat exchanger is 20kcal / (m 2 h°C). The heat exchange area of the required primary and secondary graphite heat exchangers is selected as 370m 2 , the circulation area is 0.34m 2 . Shell D=1.9m, the outer diameter of the tubes is 30mm, the inner diameter is 21mm, arranged in an equilateral triangle, the spacing between the tubes is 1.35 times the outer diameter of the tubes, a total of 900 pieces, the tube length is 4 meters, and a circular baffle is used. The gaps are arranged up and down, the distance between the baffles is h=0.9m, and the shell is treated with PO lining for anticorrosion.
[0038] The inlet temperature of the mixed gas prima...
Embodiment 3
[0040] The equipment used in this process is two tube-and-tube graphite heat exchangers. The shell side of the primary heat exchanger is mixed gas, and the tube side is vinyl chloride gas; the shell side of the secondary heat exchanger is mixed gas, and the tube side is acetylene gas; the heat transfer coefficient K of the graphite heat exchanger is 21kcal / (m 2 h°C). The heat exchange area of the required primary and secondary graphite heat exchangers is selected as 360m 2 , the circulation area is 0.38m 2 . Shell D=1.8m, the outer diameter of the tubes is 34mm, the inner diameter is 23mm, arranged in an equilateral triangle, the spacing between the tubes is 1.40 times the outer diameter of the tubes, a total of 900 pieces, the length of the tubes is 4 meters, and a circular baffle is used. The gaps are arranged up and down, the distance between the baffles is h=0.8m, and the shell is treated with PO lining for anticorrosion.
[0041] The inlet temperature of the mixed g...
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Abstract
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