CN205659427U - Distilling Recycle system of silicon chip cutting oil - Google Patents

Distilling Recycle system of silicon chip cutting oil Download PDF

Info

Publication number
CN205659427U
CN205659427U CN201620434435.1U CN201620434435U CN205659427U CN 205659427 U CN205659427 U CN 205659427U CN 201620434435 U CN201620434435 U CN 201620434435U CN 205659427 U CN205659427 U CN 205659427U
Authority
CN
China
Prior art keywords
distillation
outlet
oil
collecting box
silicon chip
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201620434435.1U
Other languages
Chinese (zh)
Inventor
田利中
张力峰
白青松
邹文龙
梁会宁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Suzhou Crystal Photoelectric Polytron Technologies Inc
Original Assignee
SUZHOU JINGYING PHOTOELECTRIC TECHNOLOGY CO LTD
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SUZHOU JINGYING PHOTOELECTRIC TECHNOLOGY CO LTD filed Critical SUZHOU JINGYING PHOTOELECTRIC TECHNOLOGY CO LTD
Priority to CN201620434435.1U priority Critical patent/CN205659427U/en
Application granted granted Critical
Publication of CN205659427U publication Critical patent/CN205659427U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The utility model discloses a distilling Recycle system of silicon chip cutting oil, including stills, last inlet, liquid outlet and the distillation mouth of being provided with of stills, the inlet is connected with the feed liquor pipeline, the liquid outlet is connected with liquid outlet pipe, the distillation mouth feeds through with the one end of distillation pipeline, and the distillation medium inlet of the other end heat exchanger of this distillation tube pipeline feeds through, the distillation medium export of heat exchanger and the entry intercommunication of water pump, the exit linkage collecting box of water pump, the top of this collecting box are provided with the gas outlet, the heat transferring medium entry and the heat exchange medium outlet of heat exchanger are connected with the heat transferring medium feeding mechanism. This distilling Recycle system can retrieve distilling cutting oil when the distillation of the cutting oil to retrieving, avoids the waste of cutting oil.

Description

A kind of Distillation recovery system of silicon chip cutting oil
Technical field
This utility model relates to a kind of Distillation recovery system, particularly relates to the Distillation recovery system of a kind of silicon chip cutting oil.
Background technology
Silicon rod needs to use cutting fluid when cutting into silicon chip, and cutting fluid needs to change after a certain period of use time, and more The cutting fluid changed can be with recycling, and cutting fluid includes solid particle and cutting oil, by filter pressing centrifugal after by solid Granule and cutting oil are separately recovered, and cut oil and have extremely strong hydrophilic, can bring certain water into, therefore in removal process Needs distill, and during distilling, control water content accurately due to needs so that it is control at below %2, during distillation Evacuation, reduces boiling point, and the volatilization of right steam along with the volatilization of more cutting oil, and can cut oil through evacuation simultaneously Device is directly discharged in cooling tower after being evacuated in heat exchanger carry out heat exchange, can often supplement water again, thus cause in cooling tower The waste of cutting oil, it is impossible to reclaim.
Utility model content
Technical problem to be solved in the utility model is: provide the Distillation recovery system of a kind of silicon chip cutting oil, this steaming Evaporate recovery system can be reclaimed by the cutting oil of distillation when recovery is cut oil distillation, it is to avoid the waste of cutting oil.
For solving above-mentioned technical problem, the technical solution of the utility model is: the Distillation recovery system of a kind of silicon chip cutting oil System, including distillating still, described distillating still is provided with inlet, liquid outlet and distillation mouth, and described inlet connects feed tube Road, described liquid outlet connects has drain pipe road, described distillation mouth to connect with one end of distillation pipeline, another of this distillation tube pipeline The distillation medium inlet connection of end heat exchanger, the distillation media outlet of heat exchanger connects with the entrance of water pump, going out of described water pump Mouth connects collecting box, and the top of this collecting box is provided with gas outlet, and the heat transferring medium entrance of described heat exchanger and heat transferring medium go out Mouth is connected with heat transferring medium feeding mechanism.
As the preferred scheme of one, at the gas outlet of described collecting box, it is provided with gs-oil separator.
As the preferred scheme of one, described collecting box being additionally provided with liquid outlet, this liquid outlet connects drain pipe road, It is provided with electromagnetic valve on this liquid storage pipeline.
As the preferred scheme of one, in described collecting box, it is provided with liquid level sensor, described liquid level sensor and control Device connects, and this control device is connected with described electromagnetic valve.
As the preferred scheme of one, described heat transferring medium feeding mechanism includes that cooling tower, described cooling tower pass through feed flow Pipeline connects with the heat transferring medium entrance of heat exchanger, connects back to liquid pipeline between described cooling tower and heat transferring medium outlet.
As the preferred scheme of one, described water pump also cools down the cooling of entrance and coolant outlet, cooling tower and water pump Connect between entrance, coolant outlet and have cooling line circulation connection.
After have employed technique scheme, effect of the present utility model is: owing to stating one end of distillation mouth and distillation pipeline Connection, the distillation medium inlet connection of the other end heat exchanger of this distillation tube pipeline, the distillation media outlet of heat exchanger and water pump Entrance connection, described water delivery side of pump connect collecting box, the top of this collecting box is provided with gas outlet, changing of described heat exchanger Thermal medium entrance and heat transferring medium outlet are connected with heat transferring medium feeding mechanism, therefore, can take out in distillating still during starting mode of pump Vacuum, extracts out steam and the cutting oil of gasification from distillation mouth, the cutting oil of steam and gaseous state after heat exchanger heat exchange Becoming liquid and have water pump to deliver in collecting box, the top of collecting box is provided with gas outlet and facilitates oil water mixture to replace collecting box Interior gas, so, oil water mixture can focus on after collecting again, thus is avoided that the waste of cutting oil, saving when distillation Cost, decreases pollution.
Again owing to being provided with gs-oil separator at the gas outlet of described collecting box, utilize this gs-oil separator can avoid collecting Cutting oil volatilization in case and loss, in air, protect environment while reducing waste.
Again owing to being additionally provided with liquid outlet on described collecting box, this liquid outlet connects has drain pipe road, on this liquid storage pipeline It is provided with electromagnetic valve.Being provided with liquid level sensor in described collecting box, described liquid level sensor is connected with controlling device, this control Device is connected with described electromagnetic valve.This liquid level sensor can be real-time detection collecting box in liquid level, when reaching high level Show that the oil water mixture in collecting box is collected and reach maximum limitation, now can be opened by controlling device control electromagnetic valve, will receive The oil water mixture of header is released and is focused on, and the oil water mixture amount thus being avoided that in collecting box too much causes spilling.
Accompanying drawing explanation
With embodiment, this utility model is further illustrated below in conjunction with the accompanying drawings.
Fig. 1 is the system connection figure of this utility model embodiment;
In accompanying drawing: 1. distillating still;2. inlet;3. liquid outlet;4. add heat pipe;5. distillation mouth;6. distillation pipeline;7. heat exchange Device;8. distillation media outlet;9. heat transferring medium entrance;10. heat transferring medium outlet;11. water pumps 11;12. outlets;13. cool down into Mouthful;14. entrances;15. coolant outlets;16. cooling towers 16;17. collecting boxs;18. gs-oil separators;19. liquid level sensors;20. Drain pipe road;21. electromagnetic valves;22. distillation medium inlets.
Detailed description of the invention
Below by specific embodiment, this utility model is described in further detail.
As it is shown in figure 1, the Distillation recovery system of a kind of silicon chip cutting oil, including distillating still 1, described distillating still 1 is arranged Having inlet 2, liquid outlet 3 and distillation mouth 5, this distillating still 1 includes a kettle and is in the chuck outside kettle, in this chuck Being provided with and add heat pipe 4, this adds heat pipe 4 and is arranged on bottom and the side of kettle, makes heating the most uniform.
Described inlet 2 connects water influent pipeline, and this water influent pipeline can connect with cutting fluid recovery system, at front road Reason cutting fluid by solid particle and cutting separating of oil after, cutting oil deliver in distillating still 1, described liquid outlet 3 connect have liquid Pipeline 20, cutting oil up to standard for water content after distillation is directly sent the cutting fluid that configuration makes new advances by this drain pipe road 20.Described steaming Evaporating mouth 5 to connect with one end of distillation pipeline 6, the distillation medium inlet 22 of the other end heat exchanger 7 of this distillation tube pipeline connects, and changes The distillation media outlet 8 of hot device 7 connects with the entrance 14 of water pump 11, and the outlet 12 of described water pump 11 connects collecting box 17, these receipts The top of header 17 is provided with gas outlet, the heat transferring medium entrance 9 of described heat exchanger 7 and heat transferring medium outlet 10 and heat transferring medium Feeding mechanism connects.The operation of this water pump 11 can reduce the pressure in distillating still 1 to evacuation in distillating still 1, make moisture content more Easily distillation, detaches water vapour and the gaseous state cutting oil of distillation simultaneously.
Being provided with gs-oil separator 18 at the gas outlet of described collecting box 17, this gs-oil separator 18 can be avoided cutting oil ease Dissipate.
Being additionally provided with liquid outlet 3 on described collecting box 17, this liquid outlet 3 connects has drain pipe road 20, on this liquid storage pipeline It is provided with electromagnetic valve 21.Being provided with liquid level sensor 19 in described collecting box 17, described liquid level sensor 19 connects with controlling device Connecing, this control device is connected with described electromagnetic valve 21, and described liquid level sensor 19 can use the liquid level sensor 19 of float-ball type, May be used without other liquid level sensors 19, and control device and can use single-chip microcomputer or PLC.
Described heat transferring medium feeding mechanism includes cooling tower 16, and described cooling tower 16 is by liquid feeding pipeline and heat exchanger 7 Heat transferring medium entrance 9 connects, and connects back to liquid pipeline between described cooling tower 16 and heat transferring medium outlet 10.It addition, water pump 11 exists Can generate heat during long-term use, the most described water pump 11 also cools down entrance 13 and coolant outlet 15, cooling tower 16 and water pump 11 Cooling entrance 13, connect between coolant outlet 15 and have cooling line circulation connection, so, utilize the water of cooling tower 16 to water pump 11 cool down, it is ensured that water pump 11 uses in the environment of stable.
Operation principle of the present utility model is: the aqueous cutting oil exceeded standard delivers to add in distillating still 1 thermal distillation, and water pump 11 is transported Row is to evacuation in distillating still 1, and the cutting oil of moisture and a part becomes gaseous state and is pumped down in heat exchanger 7 cooling, becomes liquid Oil water mixture and be sent in collecting box 17, when in collecting box 17 receive expired cutting oil after, control device open electromagnetic valve 21 collect unified for cutting oil and again process, and thus avoid the waste of cutting oil.
Embodiment described above is only the description to the preferred embodiment of the present invention, not as the limit to the scope of the invention Fixed, on the basis of designing spirit without departing from the present invention, the various deformation that technical solution of the present invention is made and transformation, all should fall Enter in the protection domain that claims of the present invention determines.

Claims (6)

1. silicon chip cutting oil a Distillation recovery system, including distillating still, it is characterised in that: be provided with on described distillating still into Liquid mouth, liquid outlet and distillation mouth, described inlet connects water influent pipeline, and described liquid outlet connects drain pipe road, described steaming Evaporate mouth to connect with one end of distillation pipeline, the distillation medium inlet connection of the other end heat exchanger of this distillation tube pipeline, heat exchanger Distillation media outlet connect with the entrance of water pump, described water delivery side of pump connection collecting box, the top of this collecting box is provided with Gas outlet, the heat transferring medium entrance of described heat exchanger and heat transferring medium outlet are connected with heat transferring medium feeding mechanism.
The Distillation recovery system of a kind of silicon chip cutting the most as claimed in claim 1 oil, it is characterised in that: going out of described collecting box Gs-oil separator it is provided with at QI KOU.
The Distillation recovery system of a kind of silicon chip cutting the most as claimed in claim 2 oil, it is characterised in that: on described collecting box also Being provided with liquid outlet, this liquid outlet connects drain pipe road, and this drain pipe road is provided with electromagnetic valve.
The Distillation recovery system of a kind of silicon chip cutting the most as claimed in claim 3 oil, it is characterised in that: set in described collecting box Being equipped with liquid level sensor, described liquid level sensor is connected with controlling device, and this control device is connected with described electromagnetic valve.
The Distillation recovery system of a kind of silicon chip cutting the most as claimed in claim 4 oil, it is characterised in that: described heat transferring medium supplies Answering device to include cooling tower, described cooling tower is connected with the heat transferring medium entrance of heat exchanger by liquid feeding pipeline, described cooling tower And connect back to liquid pipeline between heat transferring medium outlet.
The Distillation recovery system of a kind of silicon chip cutting the most as claimed in claim 5 oil, it is characterised in that: the coldest on described water pump But entrance and coolant outlet, is connected between the cooling entrance of cooling tower and water pump, coolant outlet and has cooling line circulation connection.
CN201620434435.1U 2016-05-13 2016-05-13 Distilling Recycle system of silicon chip cutting oil Expired - Fee Related CN205659427U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620434435.1U CN205659427U (en) 2016-05-13 2016-05-13 Distilling Recycle system of silicon chip cutting oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620434435.1U CN205659427U (en) 2016-05-13 2016-05-13 Distilling Recycle system of silicon chip cutting oil

Publications (1)

Publication Number Publication Date
CN205659427U true CN205659427U (en) 2016-10-26

Family

ID=57160476

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620434435.1U Expired - Fee Related CN205659427U (en) 2016-05-13 2016-05-13 Distilling Recycle system of silicon chip cutting oil

Country Status (1)

Country Link
CN (1) CN205659427U (en)

Similar Documents

Publication Publication Date Title
CN104759108B (en) Three grades of continuous falling liquid film circulating and evaporating concentration systems with function of mechanical steam recompression
CN104922974B (en) A kind of concentration device for material liquid
CN203836931U (en) Centralized-packing closed type high temperature steam condensate water recovery system
CN105174219B (en) The system that a kind of use vacuum type Membrane Materials system concentrates watery hydrochloric acid
JP2017507024A (en) Evaporator
CN104922921B (en) A kind of self-loopa MVR thermo-compression evaporation systems
CN103007572B (en) Medicine extraction device and technique thereof
CN102748963B (en) Closed water cooling system with double-evaporative cooling pressure
CN205659427U (en) Distilling Recycle system of silicon chip cutting oil
CN205759788U (en) Energy-saving single-action concentrates rectifier unit
CN206372543U (en) A kind of low-temperature negative-pressure purifying plant
CN206232630U (en) A kind of multifunctional alcohol retracting device
CN104524806B (en) A kind of hexamethylenamine complete continuous crystallisation production technology and equipments
CN214781719U (en) Reflux extraction device of star anise oil
CN108815869A (en) Liquid-purifying device
CN205549612U (en) Liquid treatment device
CN211885428U (en) Falling film evaporator
JP4583583B2 (en) Steam heating device
CN206642389U (en) Alcohol recycle rectifying device
CN206027120U (en) Glycerine evaporation plant
CN209270868U (en) A kind of recovered liquid preprocessing system
CN206375694U (en) The double mode solar energy sea water desalination apparatus of auto-manual
CN105582685B (en) Liquid treatment equipment
CN205087954U (en) System for adopt concentrated watery hydrochloric acid of vacuum type membrane distillation system
CN221220963U (en) Vapor-liquid separation mechanism of vapor injection vacuumizing system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 215600, Suzhou, Jiangsu, Zhangjiagang province Shuanglong town of Phoenix Village, Suzhou crystal photoelectric Polytron Technologies Inc Sakura

Patentee after: Suzhou crystal photoelectric Polytron Technologies Inc

Address before: 215614, Jiangsu City, Suzhou province Zhangjiagang phoenix town Shuanglong Village Suzhou Crystal Photoelectric Technology Co., Ltd.

Patentee before: Suzhou Jingying Photoelectric Technology Co.,Ltd.

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20161026

Termination date: 20210513