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

Inactive Publication Date: 2018-08-24
XUZHOU UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The carbon tetrachloride injector used in the treatment is prone to clogging
Clogging of these injectors has caused a lot of problems and in the past it was usually solved by doing an air purge which was a waste of time and handling fluids
At the same time, the processing of the existing equipment can not meet the design requirements. This kind of equipment is not easy to turn. When designing, a crowbar must be used to lift the balance roller in the middle and rely on manpower to turn it. It is laborious and time-consuming, and the efficiency is very low. Urgent improvement
In addition, the technology of the sediment control system has not yet matured, and the existing traditional processes and treatment methods still have the disadvantages of high treatment cost and low work efficiency.

Method used

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  • Ejector for tetrachloromethane treatment equipment
  • Ejector for tetrachloromethane treatment equipment
  • Ejector for tetrachloromethane treatment equipment

Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention discloses an ejctor for tetrachloromethane treatment equipment. The sprayerejector is characterized in that an impeller, a stator copper coil, bearings, a mixing chamber, a rotor roller,a stator magnet and a rotor are arranged in a casing of the impeller; one end of the casing is provided with a solution inlet, the other end of the casing is provided with an ejection port, and the solution inlet is communicated with the ejctor; the rotor roller is arranged at the middle axis of the interior of the casing, is provided with the impeller at the spraying portinjection orifice end, and is fixedly connected with the impeller; the bearings are respectively arranged at both ends of the rotor roller, the exterior of each bearing is fixedly connected with the casing, and the interiorof each bearing is rotationally connected with the rotor roller; the rotor is arranged in the middle of the rotor roller, the stator magnet and the stator copper coil are arranged around the rotor, and the stator copper coil is connected with an external conducting wire at the exterior of the casing; the mixing chamber is positioned at the solution inlet end of the interior of the casing; the solution is sent into the mixing chamber through the solution inlet. The ejector has the advantages that the structure is novel and reasonable, the treatment efficiency is high, and the application rangeis broad.

Description

technical field [0001] The invention belongs to the field of hydrology and water resources engineering equipment, in particular to an injector in carbon tetrachloride treatment equipment. Background technique [0002] In mixed liquor aftertreatment systems for carbon tetrachloride, so-called injectors are typically used to inject treatment fluid into the mixed liquor stream, although there are other situations when injectors are used to increase the mixed liquor temperature To increase the temperature of the mixed liquor flow, usually to filter the carbon tetrachloride in the mixed liquor post-treatment system. The carbon tetrachloride injectors used in the disposal are prone to clogging. Blockage of these injectors has caused many problems and in the past, blockages have typically been resolved by performing an air purge, which is a waste of time and disposal fluid. At the same time, the processing of the existing equipment can not meet the design requirements. This kind ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01F13/10B01F13/00B01F15/00B01F15/02C08L75/04C08K13/06C08K9/00C08K9/04C08K3/08C08K7/24
CPCC08L75/04C08K2003/085C08K2201/011C08K2201/003B01F33/5023B01F33/8305B01F33/86B01F35/7179C08L101/025C08K13/06C08K9/00C08K9/08C08K9/04C08K3/08C08K7/24
Inventor 张双圣刘喜坤周明方刘汉湖于向辉梁峙
Owner XUZHOU UNIV OF TECH
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