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Oil tank solid-liquid separation device in carbon tetrachloride precipitation block end face grinding equipment

A carbon tetrachloride and solid-liquid separation technology, which is applied in the direction of sedimentation separation, grinding device, feeding/discharging device of settling tank, etc., can solve the problems of low efficiency and low safety

Inactive Publication Date: 2018-09-21
XUZHOU TENGRUI INTELLIGENT EQUIP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] In modern society, the development of the solid-liquid separation device in the end grinding machine has become more and more important. However, in the current grinding machine market, the traditional solid-liquid separation device, the manual control mode has low safety and low efficiency. problems, can not meet the needs of the market

Method used

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  • Oil tank solid-liquid separation device in carbon tetrachloride precipitation block end face grinding equipment
  • Oil tank solid-liquid separation device in carbon tetrachloride precipitation block end face grinding equipment
  • Oil tank solid-liquid separation device in carbon tetrachloride precipitation block end face grinding equipment

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0049] According to the following steps to prepare the disc 3-5-9 of the present invention, and in parts by weight:

[0050] Step 1: In the stirred vertical tower reactor, add 339.2 parts of purified lake water and N-methyl-1,1,2,2,3,3,4,4,5,5,5-undecafluoro - 131.5 parts of 1-pentanesulfonamide, start the stirrer in the stirring vertical tower reactor, set the speed at 132rpm, start the steam type oil heater in the stirring vertical tower reactor, raise the temperature to 147.2°C, add 134.2 parts of 1-(methoxymethyl)-4-methylbenzene were stirred evenly, and the reaction was carried out for 124.5 minutes. 3 / min of helium for 124.5 minutes; then add 133.1 parts of rutile to the stirred vertical tower reactor, start the steam oil heater in the stirred vertical tower reactor again, raise the temperature to 164.2°C, keep it warm for 124.4 minutes, add 136.9 parts of polymers of 4,4'-(1-methylethylene)bis[2-(2-propenyl)]phenol and (chloromethyl)oxirane, adjusted and stirred in a ...

Embodiment 2

[0057] According to the following steps to prepare the disc 3-5-9 of the present invention, and in parts by weight:

[0058] Step 1: In the stirred vertical tower reactor, add 564.8 parts of purified lake water and N-methyl-1,1,2,2,3,3,4,4,5,5,5-undecafluoro - 173.6 parts of 1-pentanesulfonamide, start the stirrer in the stirring vertical tower reactor, set the speed at 178rpm, start the steam type oil heater in the stirring vertical tower reactor, raise the temperature to 148.8°C, add 243.1 parts of 1-(methoxymethyl)-4-methylbenzene were stirred evenly, and the reaction was carried out for 135.6 minutes. 3 / min of helium for 135.6 minutes; then add 190.3 parts of rutile to the stirred vertical tower reactor, start the steam type oil heater in the stirred vertical tower reactor again, raise the temperature to 197.1°C, keep it warm for 135.4 minutes, add 197.5 parts of polymers of 4,4'-(1-methylethylene)bis[2-(2-propenyl)]phenol and (chloromethyl)oxirane, adjusted and stirred i...

Embodiment 3

[0065] According to the following steps to prepare the disc 3-5-9 of the present invention, and in parts by weight:

[0066] Step 1: In the stirred vertical tower reactor, add 339.9 parts of purified lake water and N-methyl-1,1,2,2,3,3,4,4,5,5,5-undecafluoro - 131.9 parts of 1-pentanesulfonamide, start the stirrer in the stirring vertical tower reactor, set the speed at 132rpm, start the steam type oil heater in the stirring vertical tower reactor, raise the temperature to 147.9°C, add 134.9 parts of 1-(methoxymethyl)-4-methylbenzene were stirred evenly, and the reaction was carried out for 124.9 minutes. 3 / min of helium for 124.9 minutes; then add 133.9 parts of rutile to the stirred vertical tower reactor, start the steam type oil heater in the stirred vertical tower reactor again, raise the temperature to 164.9°C, keep it warm for 124.9 minutes, add 136.9 parts of polymers of 4,4'-(1-methylethylene)bis[2-(2-propenyl)]phenol and (chloromethyl)oxirane, adjusted and stirred ...

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Abstract

The invention discloses an oil tank solid-liquid separation device in carbon tetrachloride precipitation block end face grinding equipment. The oil tank solid-liquid separation device is arranged inside an oil tank and comprises a precipitate discharge pipe, a detection pipe, an oil collecting groove, oil overflow ports, an oil return pipeline, dispersing ports, oil discharge dispersing head, an oil inlet vertical pipe, a flying-saucer-shaped plate and an oil inlet pipe and is characterized that one end of the oil inlet pipe located on one side is communicated with a hydraulic cylinder, the other end of the oil inlet pipe is communicated with the oil inlet vertical pipe, the other end of the oil inlet vertical pipe is communicated with the oil discharge dispersing head, the surface of theoil discharge dispersing head is provided with the dispersing ports, and the six dispersing ports are arranged in an equal-angle manner along the central axis of the oil inlet vertical pipe; the oil return channel is arranged between a shell and the oil discharge dispersing head and the oil inlet vertical pipe; the oil return pipeline is communicated with the flying-saucer-shaped hollow plate on the lower portion. The oil tank solid-liquid separation device is high in automation level, thorough in oil tank solid-liquid separation, high in stability, fast in separation and high in oil yield.

Description

technical field [0001] The invention belongs to the field of special material processing, and in particular relates to a solid-liquid separation device for an oil tank in end face grinding equipment for carbon tetrachloride sedimentation blocks. Background technique [0002] In modern society, the development of the solid-liquid separation device in the end grinding machine has become more and more important. However, in the current grinding machine market, the traditional solid-liquid separation device, the manual control mode has low safety and low efficiency. The problem is that it cannot meet the needs of the market. Contents of the invention [0003] In order to solve the above-mentioned technical problems, the present invention provides a solid-liquid separation device for a fuel tank in a carbon tetrachloride sediment block end face grinding device, comprising: a shock-absorbing foot pad 1, a fixed frame 2, a grinding mechanism 3, a workpiece fixture 4, and a suppor...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B24B37/005B24B37/013B24B37/10B24B37/30B24B37/34B01D21/24
CPCB01D21/2416B24B37/005B24B37/013B24B37/107B24B37/30B24B37/34
Inventor 梁峙梁骁马捷张猛
Owner XUZHOU TENGRUI INTELLIGENT EQUIP CO LTD