Unlock instant, AI-driven research and patent intelligence for your innovation.

System and method for reducing energy consumption of organic silicon wastewater treatment by using waste heat

A wastewater treatment and organic silicon technology, which is applied in natural water treatment, chemical instruments and methods, water/sewage multi-stage treatment, etc., can solve the problems of limited efficiency of wastewater treatment, high energy consumption of wastewater treatment, high treatment cost, etc., to achieve Save labor costs and time costs, high recycling efficiency, and low operating costs

Pending Publication Date: 2022-07-12
内蒙古恒星化学有限公司
View PDF6 Cites 1 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The present invention provides a system and method for reducing the energy consumption of organic silicon wastewater treatment by using waste heat, which is used to solve the problems of high energy consumption, high treatment cost and limited wastewater treatment efficiency in the existing organic silicon wastewater treatment

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • System and method for reducing energy consumption of organic silicon wastewater treatment by using waste heat
  • System and method for reducing energy consumption of organic silicon wastewater treatment by using waste heat
  • System and method for reducing energy consumption of organic silicon wastewater treatment by using waste heat

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0079] A system for reducing energy consumption of organosilicon wastewater treatment by utilizing waste heat, the operation process of which is as follows:

[0080] 1) The deep-removal waste water, washing tower waste water, alkali washing waste water and hydrogen-containing silicone oil waste water etc. produced in the organic silicon production process are sent into the waste water collection tank 11, and after the waste water collection tank 11 is homogenized with the mixing device 1101 , temporary storage;

[0081] 2) The organic silicon waste water is sent into the waste heat utilization unit from the outlet of the waste water collecting tank 11, enters from the cooling medium inlet of the heat exchanger 21 of a plurality of methyl chloride synthesis sections, and enters from the heat exchanger 21 of a plurality of methyl chloride synthesis sections The cooling medium outlet is discharged;

[0082] 3) The heated organosilicon waste water enters the multi-effect evaporat...

Embodiment 2

[0085] A system for utilizing waste heat to reduce the energy consumption of organosilicon waste water treatment, the difference between its operation process and Example 1 is only:

[0086] 1) The deep-removal waste water, washing tower waste water, alkali washing waste water and hydrogen-containing silicone oil waste water etc. produced in the organic silicon production process are sent into the waste water collection tank 11, and after the waste water collection tank 11 is homogenized with the mixing device 1101 , discharge into the flocculation sedimentation tank 12 through the outlet of the waste water collecting tank 11, add flocculant to the silicone wastewater in the flocculation sedimentation tank 12 from the dosing port of the flocculation sedimentation tank 12 through the dosing device 13, and wait for the silicone wastewater to flocculate. After the sedimentation is completed, the supernatant liquid is sent to the waste heat utilization unit through the discharge po...

Embodiment 3

[0088] The working principle of the de-foaming device and the de-foaming device in the four-effect evaporation device is as follows:

[0089] (1) De-foaming: After the organic silicon wastewater enters the separator from the heater of the four-effect evaporation device 31, gas-liquid separation is carried out in the separator, and the secondary steam carries part of the liquid foam in the separator to move from bottom to upward, and runs to When the defoaming device 3101 is installed at the steam outlet of the separator, it enters the defoaming channel 3115 from the inlet section 1121 of the damping vane 3112, and then collides at the wave-shaped turning section 1123, and during the collision, the larger liquid foam is blocked by the damping vane. 3112 and the wave-shaped protrusions 1124 on it are broken, and then discharged from the outlet section 1122, and then enter the screen plate 3114, the smaller liquid foam is broken and blocked, and the steam smoothly passes through t...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention provides a system and method for reducing energy consumption of organic silicon wastewater treatment by using waste heat, and belongs to the technical field of wastewater treatment.The system comprises a wastewater pretreatment unit, a waste heat utilization unit, a multi-effect evaporation unit and a desalting unit; wherein the waste heat utilization unit comprises heat exchangers of a plurality of chloromethane synthesis sections, and the heat exchangers of the chloromethane synthesis sections are used for recovering and utilizing waste heat of the chloromethane synthesis sections by taking organic silicon wastewater as a cooling medium; and the heated organic silicon wastewater obtained by the waste heat utilization unit is fed into the multi-effect evaporation unit from the output end of the waste heat utilization unit through a pipeline. The system and the method provided by the invention are used for solving the problems of high wastewater treatment energy consumption, high treatment cost and limited wastewater treatment efficiency in the existing organic silicon wastewater treatment; according to the system and the method, waste heat in organic silicon production can be recovered and utilized, the use amount of steam is reduced, the multi-effect evaporation efficiency and the wastewater treatment efficiency are improved, and the energy consumption and the cost of organic silicon wastewater treatment are remarkably reduced.

Description

technical field [0001] The present invention relates to the technical field of wastewater treatment, in particular to a system and method for reducing energy consumption of organosilicon wastewater treatment by utilizing waste heat. Background technique [0002] Silicone, known as "industrial monosodium glutamate", is widely used in various fields. Organosilicon production usually adopts the direct method of synthesizing methyl chlorosilane, that is, using silicon powder and methyl chloride gas to react in the presence of a copper catalyst system to produce methyl chlorosilane mixed monomers, and the synthesized mixed methyl monomers pass through. Dimethyldichlorosilane and other various rectification monomers are obtained by rectification and separation. Dimethyldichlorosilane is hydrolyzed and cracked to obtain dimethylsiloxane oligomers (DMC, D4), which are used as basic raw materials for further processing into various organic silicon polymerization products. [0003] ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
IPC IPC(8): C02F9/10C02F11/122C02F103/36
CPCC02F9/00C02F11/122C02F2001/007C02F1/38C02F1/5236C02F1/56C02F1/5281C02F2103/36C02F1/04C02F1/20C02F2301/08C02F2303/10C02F2303/14Y02A20/124
Inventor 周文博渠国忠刘志强王旭普
Owner 内蒙古恒星化学有限公司