Method for converting methyl hydride into methyl hydride chloride
A methane chloride, methane technology, applied in chemical instruments and methods, organic chemistry, halogenated hydrocarbon preparation, etc., to achieve the effects of low operating cost, reasonable and simple process structure, and easy operation and use
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Embodiment 1
[0024] refer to figure 1 As shown in the process flow chart, the specific process flow is as follows: first replace the gas in the system with an inert gas to make the system pressure slightly higher than atmospheric pressure, then close the inert gas inlet valve 3, and open the methane feed gas inlet valve 1 and chlorine gas raw material gas inlet valve 2, so that methane and chlorine gas are introduced into the discharge plasma reactor 5 in a certain proportion, and power is supplied to the discharge plasma reactor. In the reactor, methane and chlorine gas generate free radicals under the action of the discharge plasma The reaction generates methane chloride, and then the reacted mixture is cooled to room temperature through the gas cooler 5, washed with water and absorbed, then added with dilute NaOH solution to absorb the secondary absorption dehydrochlorination tower 7 and calcium chloride dehydrator 9, and then passed through the gas pump 10 It is transported to the cond...
Embodiment 2
[0039] Concrete technological process is with embodiment 1, and condition parameter is as follows:
[0040] Gas composition: the inert gas is helium, and the inert gas accounts for 1% of the gas composition; raw material gas chlorine / methane=0.2, the temperature in the reactor is -34.5°C, the residence time of the reactor gas is 0.3s, and other conditions are the same as in Example 1 .
[0041] Product conversion rate is 3~5%, and each methane chloride composition (%) in the product:
[0042] Chloromethane 40~60;
[0043] Dichloromethane 20-40;
[0044] Chloroform 10-20;
[0045] Carbon tetrachloride 0-1.
Embodiment 3
[0047] Concrete technological process is with embodiment 1, and condition parameter is as follows:
[0048] Gas composition: the inert gas is neon, and the inert gas accounts for 95% of the gas component; the feed gas chlorine / methane=6, the temperature in the reactor is 80° C., the reactor gas residence time is 60 s, and other conditions are the same as in Example 1.
[0049] The product conversion rate is 85%, and each methane chloride composition (%) in the product:
[0050] Chloromethane 1~5;
[0051] Dichloromethane 5~15;
[0052] Chloroform 25-45;
[0053] Carbon tetrachloride 45~65.
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