Ejector for tetrachloromethane treatment equipment
A technology for processing equipment and carbon tetrachloride, which is applied in chemical instruments and methods, chemical/physical processes, mixers, etc., and can solve problems such as laborious, low efficiency, and difficult steering
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Embodiment 1
[0087] Prepare the impeller 4-7-2 of the present invention according to the following steps, and in parts by weight:
[0088] Step 1: In the stirred biomass thermal reactor, add 337.4 parts of demineralized pure water and 129.0 parts of 13-methylpentadecaepoxy-10-en-2-one, start the stirred biomass thermal reactor The stirrer, the set speed is 130rpm, start the steam extraction heating evaporator in the stirred biomass thermal energy reactor, make the temperature rise to 145.4 °C, add 2-[4-[[1-[[(2-methoxy -132.6 parts of 5-methyl-4-sulfonic acid phenyl)amino]carbonyl]-2-oxopropyl]azo]phenyl]-6-methyl-7-benzothiazolesulfonic acid disodium salt Stir evenly, react for 122.0 minutes, add 128.9 parts of 3-(methylthio) propionaldehyde, and the flow rate is 121.7m 3 Argon gas per min for 122.0 minutes; then add 131.8 parts of Jinguanghong into the stirred biomass thermal energy reactor, and start the steam extraction heating evaporator in the stirred biomass thermal energy reactor ...
Embodiment 2
[0095] Prepare the impeller 4-7-2 of the present invention according to the following steps, and in parts by weight:
[0096] Step 1: In the stirred biomass thermal reactor, add 562.3 parts of demineralized pure water and 171.9 parts of 13-methylpentadecaepoxy-10-en-2-one, start the stirred biomass thermal reactor The stirrer, the set speed is 176rpm, start the steam extraction heating evaporator in the stirred biomass thermal energy reactor, so that the temperature rises to 146.3 °C, add 2-[4-[[1-[[(2-methoxyl -241.5 parts of 5-methyl-4-sulfonic acid phenyl)amino]carbonyl]-2-oxopropyl]azo]phenyl]-6-methyl-7-benzothiazolesulfonic acid disodium salt Stir evenly, react for 133.9 minutes, add 145.4 parts of 3-(methylthio)propanal, and the flow rate is 162.4m 3 / min of argon for 133.9 minutes; then add 188.6 parts of Jinguanghong into the stirred biomass thermal energy reactor, and start the steam extraction heating evaporator in the stirred biomass thermal energy reactor again, ...
Embodiment 3
[0103] Prepare the impeller 4-7-2 of the present invention according to the following steps, and in parts by weight:
[0104] Step 1: In the stirred biomass thermal reactor, add 337.9 parts of demineralized pure water and 129.9 parts of 13-methylpentadecaepoxy-10-en-2-one, start the stirred biomass thermal reactor The stirrer, the set speed is 130rpm, start the steam extraction heating evaporator in the stirred biomass thermal energy reactor, make the temperature rise to 145.9 °C, add 2-[4-[[1-[[(2-methoxyl -132.9 parts of 5-methyl-4-sulfonic acid phenyl)amino]carbonyl]-2-oxopropyl]azo]phenyl]-6-methyl-7-benzothiazolesulfonic acid disodium salt Stir evenly, carry out the reaction for 122.9 minutes, add 128.9 parts of 3-(methylthio) propionaldehyde, and the flow rate is 121.9m 3 / min of argon for 122.9 minutes; then add 131.9 parts of Jinguanghong into the stirred biomass thermal energy reactor, and start the steam extraction heating evaporator in the stirred biomass thermal e...
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