An energy-saving production system and method for monochloromethane
A monochloromethane and production method technology, applied in the field of monochloromethane energy-saving production systems, can solve the problems of unreasonable use of reaction heat and consumption of external cooling capacity, so as to save cooling capacity and production and operation costs, reduce recovery costs, The effect of reducing usage
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Embodiment 1
[0041] Such as figure 1 As shown, an energy-saving production system for monochloromethane includes a reactor 1, a methanol vaporizer 2, and a condenser. The methanol vaporizer 2 is used to heat raw methanol and is connected to the reactor 1 through a pipeline. The system condenser includes a first condenser 3 and a second condenser 4 connected in series for condensing unreacted raw materials in the separated product.
[0042] Such as figure 2 As shown, the top of the reactor 1 is provided with a gas phase outlet 21, the wall of the reactor is sequentially provided with a liquid phase inlet 22, a return port 23 and a gas phase inlet 24, and the bottom of the reactor is provided with a liquid phase outlet 25. A liquid phase distributor 11, a tray gas phase distributor 12 and a tray 13 are installed in the reactor 1, the installation position of the liquid phase distributor 11 corresponds to the liquid phase inlet 22, and the position of the gas phase distributor 12 correspond...
Embodiment 2
[0046] In this embodiment, on the basis of the above embodiments, the first temperature regulating valve 5 is installed on the first circulation line 74 , and the second temperature regulating valve 6 is installed on the return line 76 . The first temperature regulating valve 5 controls the output temperature of the methanol vaporizer 2 by adjusting the flow rate of the production liquid at the bottom of the reaction kettle 1 . The second temperature regulating valve 6 controls the reaction temperature in the reactor 1 by adjusting the reflux flow rate of the condensate in the first condenser 3 . The temperature automatic control valve can effectively guarantee the stability of the process parameters and the stable operation of the reaction.
Embodiment 3
[0048] In this implementation, on the basis of the above-mentioned embodiments, the number of the trays 13 is 1 to 10, which are designed and selected according to the reaction parameters. The form of the tray 13 may be any one of a sieve tray, a bubble cap tray or a valve tray. And the material of the tray 13 can be selected from 1Cr18Ni9Ti, 00Cr17Ni 14Mo2, 00Cr18Ni5Mo3Si2, Hastelloy, NI+Q345R, TA+Q345R and other anti-corrosion materials.
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