CN206232674U - A kind of waste heat recovery of lubricating oil processing steam and impurity treatment system - Google Patents
A kind of waste heat recovery of lubricating oil processing steam and impurity treatment system Download PDFInfo
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- CN206232674U CN206232674U CN201621175679.9U CN201621175679U CN206232674U CN 206232674 U CN206232674 U CN 206232674U CN 201621175679 U CN201621175679 U CN 201621175679U CN 206232674 U CN206232674 U CN 206232674U
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- pipe
- lubricating oil
- condenser pipe
- heat exchange
- steam
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Abstract
Waste heat recovery and impurity treatment system the utility model discloses a kind of lubricating oil processing steam, including kettle, motor, paddle, resistive heater, condenser pipe, heat exchange tank, air exhauster, vent gas treatment ware and gas discharge pipe, the kettle upper end right side is connected with blast pipe, blast pipe right-hand member is connected with condenser pipe, condenser pipe periphery is provided with heat exchange tank, condenser pipe lower end is provided with blow-off pipe through heat exchange tank lower end, condenser pipe right-hand member is connected with air exhauster, air exhauster lower section is provided with vent gas treatment ware, upper end right side is connected with gas discharge pipe.The utility model makes full use of lubricating oil to process the heat of steam using heat exchanger tube, simultaneously liquefaction lubricating oil is obtained using heat transferring medium cooling steam, production cost is reduced while increasing operation rate, while coordinating the impurity in activated carbon removal tail gas using alkaline solution, it is to avoid pollution environment.
Description
Technical field
The utility model is related to a kind of lubricating oil processing knot screen, and specifically a kind of waste heat of lubricating oil processing steam is returned
Receive and impurity treatment system.
Background technology
At present, the plant equipment that people use in life and work is more and more, and lubricating oil is used as protection machinery and processing
The fluid lubricant of part, demand increasingly increases.The element such as sulphur therein, nitrogen, phosphorus can be formed with lubricating oil in process of production
Harmful gas is discharged with tail gas, and these tail gas can carry parts of lubricating oil discharge in discharge, so both cause waste, and
Serious pollution can be caused to environment.
The general exhaust gas processing device for using too is complicated when lubricating oil is reclaimed in present production application, using compared with
Cost high could complete less work, and cost performance is relatively low, while treatment of these equipment after lubricating oil is reclaimed to tail gas
New pollution not enough can be caused again in place or while treatment, and these are all a lack of application；In existing production, high temperature
When being liquefied using condenser pipe, substantial amounts of heat is all wasted steam, lacks application.
Utility model content
The purpose of this utility model is waste heat recovery and the impurity treatment system for providing a kind of lubricating oil processing steam, with
Solve the problems, such as to be proposed in above-mentioned background technology.
To achieve the above object, the utility model provides following technical scheme：
A kind of waste heat recovery of lubricating oil processing steam and impurity treatment system, including kettle, motor, paddle, heating
Resistance wire, condenser pipe, heat exchange tank, air exhauster, vent gas treatment ware and gas discharge pipe, the kettle upper end are provided with motor, institute
State motor output end and be connected with agitating shaft, paddle is provided with the agitating shaft, the kettle upper end left side is provided with
Charging aperture, the inner wall of kettle winding is provided with resistive heater, and the kettle lower end is provided with discharge nozzle, on the discharge nozzle
With controlled valve, the kettle upper end right side is connected with blast pipe, and drain tap is provided with the blast pipe, described
Blast pipe right-hand member is connected with condenser pipe, and the condenser pipe periphery is provided with heat exchange tank, the heat exchange tank upper end be provided with into
Water pipe, the heat exchange tank lower end is connected with outlet pipe, and the condenser pipe lower end is provided with row through the heat exchange tank lower end
Dirt pipe, carries locking knob on the blow-off pipe, the condenser pipe right-hand member is connected with air exhauster, and the air exhauster lower section sets
Vent gas treatment ware is equipped with, the air exhauster outlet side is provided with grass tube, and the upper end right side is connected with gas discharge
Pipe.
As further program of the utility model：The motor and the kettle upper end are welded and fixed, and the motor is defeated
Go out end to be stretched into the kettle by the kettle upper end.
As further program of the utility model：The paddle is elliptic cylindrical shape strip, the paddle paddle
It is symmetrically arranged with multiple rows of.
As further program of the utility model：The resistive heater is carried out by thermocouple and temperature control equipment
Temperature adjustment is controlled.
As further program of the utility model：The condenser pipe is helical metal pipe, and the condenser pipe left end connects
It is connected with high pressure nitrogen.
As further program of the utility model：Be enclosed in the condenser pipe in the heat exchange tank by the heat exchange tank
Portion, the condenser pipe left end is connected through the heat exchange tank left wall top with the blast pipe, and the condenser pipe right-hand member is passed through
The heat exchange tank right wall bottom stretches out.
As further program of the utility model：Akaline liquid is housed in the vent gas treatment ware.
As further program of the utility model：The grass tube lower end extends to bottom in the vent gas treatment ware
Portion.
As further program of the utility model：Activated carbon is filled with the gas discharge pipe.
Compared with prior art, the beneficial effects of the utility model are：During work, drain tap and air exhauster are opened, made
The mixed gas such as lubrication oil vapour, foreign gas and air are suctioned out from kettle, when mixed gas are by condenser pipe, by entering
Water pipe injects in heat exchange tank heat transferring medium, and mixed gas are gradually lowered the temperature in the spirality channel of condenser pipe, is easier to liquefaction
Lubrication oil vapour etc. will cool down and be attached on the inwall of condenser pipe, at the same time temperature gradually rises heat transferring medium, opens
Outlet pipe can be discharged for production and living heat transferring medium, and such setting can effectively utilize the energy in high-temperature tail gas,
High-temperature tail gas are lowered the temperature using heat transferring medium also simultaneously, will wherein be easier to liquefied lubricating oil steam condensate, it is to avoid be dirty
Dye environment；Mixed gas are entered in vent gas treatment ware by passing through air exhauster and grass tube after condenser pipe, in vent gas treatment ware
Sulphur, phosphorus, nitrogen and other related impuritieses that middle reaction removal contains, are discharged by blast pipe gas discharge pipe afterwards, such to set
Putting can fully go the removal of impurity, it is to avoid the discharge of contaminative, improve the environmentally friendly coefficient of device；Mixing opens discharge nozzle after terminating
Material is discharged, drain tap is closed and to high pressure nitrogen is passed through in condenser pipe, blow-off pipe is now opened, high pressure nitrogen enters cold
In solidifying pipe, the air-flow of high speed can drive the lubricating oil in rinse condenser pipe inwall to be collected by blow-off pipe, at this mode
The device of reason lubrication oil vapour is simple to operation, and input also seldom, can play a part of energy-saving and emission-reduction, reduce the dirt of air
Dye, the lubricating oil of recovery can be reused by treatment.
Brief description of the drawings
Fig. 1 is waste heat recovery and the structural representation of impurity treatment system of a kind of lubricating oil processing steam.
Fig. 2 is waste heat recovery and the structural representation of condenser pipe in impurity treatment system of a kind of lubricating oil processing steam.
In figure：1- kettlies, 2- motors, 3- agitating shafts, 4- paddles, 5- charging apertures, 6- resistive heaters, 7- discharge nozzles,
8- blast pipes, 9- drain taps, 10- condenser pipes, 11- heat exchange tanks, 12- water inlet pipes, 13- outlet pipes, 14- blow-off pipes, 15- exhausting
Machine, 16- vent gas treatment wares, 17- grass tubes, 18- gas discharge pipes.
Specific embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment for being obtained, belongs to the scope of the utility model protection.
Fig. 1~2 are referred to, in the utility model embodiment, at a kind of waste heat recovery of lubricating oil processing steam and impurity
At reason system, including kettle 1, motor 2, paddle 4, resistive heater 6, condenser pipe 10, heat exchange tank 11, air exhauster 15, tail gas
Reason ware 16 and gas discharge pipe 18, the upper end of the kettle 1 are provided with motor 2, and the motor 2 and the welding of the upper end of the kettle 1 are solid
Fixed, the output end of the motor 2 is stretched into the kettle 1 by the upper end of the kettle 1, and the output end of the motor 2 is connected with
Agitating shaft 3, the motor 2 drives the agitating shaft 3 to rotate, and paddle 4 is provided with the agitating shaft 3, and the paddle 4 is
Elliptic cylindrical shape strip, the paddle paddle 4 is symmetrically arranged with multiple rows of, and the paddle 4 can rapidly and uniformly mix molten
Liquid, the upper end of the kettle 1 left side is provided with charging aperture 5, and the winding of the inwall of the kettle 1 is provided with resistive heater 6, the heating
Resistance wire 6 carries out temperature adjustment control by thermocouple and temperature control equipment, and the resistive heater 6 can heat the kettle
Oil body in body 1, the lower end of the kettle 1 is provided with discharge nozzle 7, has controlled valve on the discharge nozzle 7, and oil body is reconciling
Discharged by the discharge nozzle 7 into rear, the upper end of the kettle 1 right side is connected with blast pipe 8, and oil body enters in the kettle 1
Row reconciles when heating, and has a large amount of gases and produces, gas discharge from the kettle 1 by the blast pipe 8, it is to avoid the kettle
Pressure is excessive in body 1, and drain tap 9 is provided with the blast pipe 8, and the opening and closing of the drain tap 9 can be controlled
The flowing of gas in the blast pipe 8, the right-hand member of the blast pipe 8 is connected with condenser pipe 10, and solution is carried out in the kettle 1
During stirring, lubrication oil vapour, foreign gas, air etc. are entered in the condenser pipe 10 by the blast pipe 8, the condenser pipe
10 is helical metal pipe, and when gas passes through the condenser pipe 10, more long makes liquid by length and larger contact area
Changing the relatively low lubricating fluid of temperature requirement can obtain more sufficiently liquefaction, and the left end of the condenser pipe 10 is communicated with high pressure nitrogen,
After completion of the mixing, the drain tap 9 is closed, and now opens high pressure nitrogen, and now high pressure nitrogen passes through the condenser pipe 10,
Out of the circulating line can be taken such as wherein liquefied lubricating oil and a small amount of impurity, the periphery of the condenser pipe 10 is provided with heat exchange tank
11, be enclosed in the condenser pipe 10 inside the heat exchange tank 11 by the heat exchange tank 11, and the left end of the condenser pipe 10 is described in
The left wall top of heat exchange tank 11 is connected with the blast pipe 8, and the right-hand member of the condenser pipe 10 passes through the right wall bottom of the heat exchange tank 11
Stretch out, the upper end of the heat exchange tank 11 is provided with water inlet pipe 12, heat transferring medium injects the heat exchange by the water inlet pipe 12
In tank 11, the heat of high-temperature gas in the condenser pipe 10 can either be so obtained, water vapour and profit in gas can be accelerated again
The liquefaction of lubricating oil steam, the lower end of the heat exchange tank 11 is connected with outlet pipe 13, by described after the completion of heat transferring medium heat exchange
Outlet pipe 13 is discharged, and the lower end of the condenser pipe 10 is provided with blow-off pipe 14, the blow-off pipe 14 through the lower end of the heat exchange tank 11
It is upper to carry locking knob, after water vapour in the condenser pipe 10 and lubrication oil vapour are condensed, the blow-off pipe 14 can be opened
Liquid is discharged, so can also recycling, saved the impurity that cost also can be effectively gone in removing exhaust gas, it is to avoid pollution
Air, the right-hand member of the condenser pipe 10 is connected with air exhauster 15, and the air exhauster 15 can be by gas from the kettle after starting
Extracted out in body 1, promote the motion of gas, the lower section of the air exhauster 15 is provided with vent gas treatment ware 16, the vent gas treatment ware
Akaline liquid is housed in 16, generally contains sulphur, phosphorus, nitrogen and other related impuritieses in lubricating oil and mediation additive therefor, anti-
The compound that should be generated afterwards can be filtered effectively by akaline liquid, and the outlet side of the air exhauster 15 is provided with glass and leads
Pipe 17, the lower end of the grass tube 17 extends to the inner bottom part of vent gas treatment ware 16, and the upper end right side is connected with gas
Body delivery pipe 18, is filled with activated carbon in the gas discharge pipe 18, filling component is prevented from the gas discharge pipe 18
Gas takes akaline liquid pollution environment out of when discharging.
Operation principle of the present utility model is：During work, material is entered in kettle 1 by charging aperture 5, starts resistive heater
Start motor 2 after 6 heating drives paddle 4 to be stirred by agitating shaft 3, opens drain tap 9 and air exhauster 15, makes lubrication
The mixed gas such as oil vapour, foreign gas and air are suctioned out from kettle 1, when mixed gas are by condenser pipe 10, by entering
Water pipe 12 injects in heat exchange tank 11 heat transferring medium, and mixed gas are gradually lowered the temperature in the spirality channel of condenser pipe 10, relatively holds
Liquescent lubrication oil vapour etc. will be cooled down and is attached on the inwall of condenser pipe 10, and at the same time temperature gradually rises heat transferring medium
Height, opening outlet pipe 13 can discharge for production and living heat transferring medium, and such setting can effectively utilize high-temperature tail gas
In energy, while also using heat transferring medium to high-temperature tail gas lower the temperature, will wherein be easier to liquefied lubricating oil steam condensate
Change, it is to avoid pollution environment；Mixed gas enter vent gas treatment ware by after condenser pipe 10 by air exhauster 15 and grass tube 17
In 16, sulphur, phosphorus, nitrogen and other related impuritieses that removal contains are reacted in vent gas treatment ware 16, afterwards by blast pipe gas
Delivery pipe 18 is discharged, and such setting can fully go the removal of impurity, it is to avoid the discharge of contaminative, improves the environmental protection system of device
Number；Mixing is opened discharge nozzle 7 and discharges material after terminating, and closes drain tap 9 and to being passed through high pressure nitrogen in condenser pipe 10, this
When open blow-off pipe 14, high pressure nitrogen enter condenser pipe 10 in, the air-flow of high speed can drive the lubrication on the inwall of condenser pipe 10
Oil is collected by blow-off pipe 14, and the device that this mode processes lubrication oil vapour is simple to operation, and input is also little, energy
Enough play a part of energy-saving and emission-reduction, reduce the pollution of air, the lubricating oil of recovery can be reused by treatment.
It is obvious to a person skilled in the art that the utility model is not limited to the details of above-mentioned one exemplary embodiment, and
And in the case of without departing substantially from spirit or essential attributes of the present utility model, can in other specific forms realize that this practicality is new
Type.Therefore, no matter from the point of view of which point, embodiment all should be regarded as exemplary, and is nonrestrictive, this practicality is new
The scope of type limits by appended claims rather than described above, it is intended that the equivalency fallen in claim is contained
All changes in justice and scope are included in the utility model.Any reference in claim should not be considered as limitation
Involved claim.
Moreover, it will be appreciated that although the present specification is described in terms of embodiments, not each implementation method is only wrapped
Containing an independent technical scheme, this narrating mode of specification is only that for clarity, those skilled in the art should
Specification an as entirety, the technical scheme in each embodiment can also be formed into those skilled in the art through appropriately combined
May be appreciated other embodiment.
Claims (9)
1. a kind of waste heat recovery of lubricating oil processing steam and impurity treatment system, including kettle, motor, paddle, heating electricity
Resistance silk, condenser pipe, heat exchange tank, air exhauster, vent gas treatment ware and gas discharge pipe, it is characterised in that the kettle upper end is set
There is motor, the motor output end is connected with agitating shaft, paddle is provided with the agitating shaft, the kettle upper end is left
Side is provided with charging aperture, and the inner wall of kettle winding is provided with resistive heater, and the kettle lower end is provided with discharge nozzle, described
There is controlled valve, the kettle upper end right side is connected with blast pipe, exhaust is provided with the blast pipe on discharge nozzle
Valve, the blast pipe right-hand member is connected with condenser pipe, and the condenser pipe periphery is provided with heat exchange tank, the heat exchange tank upper end
Water inlet pipe is provided with, the heat exchange tank lower end is connected with outlet pipe, and the heat exchange tank lower end is run through in the condenser pipe lower end
Blow-off pipe is provided with, locking knob is carried on the blow-off pipe, the condenser pipe right-hand member is connected with air exhauster, the exhausting
Machine lower section is provided with vent gas treatment ware, and the air exhauster outlet side is provided with grass tube, and the upper end right side is connected with
Gas discharge pipe.
2. a kind of lubricating oil according to claim 1 processes waste heat recovery and the impurity treatment system of steam, and its feature exists
In the motor and the kettle upper end are welded and fixed, and the motor output end stretches into the kettle by the kettle upper end
It is interior.
3. a kind of lubricating oil according to claim 1 processes waste heat recovery and the impurity treatment system of steam, and its feature exists
In the paddle is elliptic cylindrical shape strip, and the paddle paddle is symmetrically arranged with multiple rows of.
4. a kind of lubricating oil according to claim 1 processes waste heat recovery and the impurity treatment system of steam, and its feature exists
In the resistive heater carries out temperature adjustment control by thermocouple and temperature control equipment.
5. a kind of lubricating oil according to claim 1 processes waste heat recovery and the impurity treatment system of steam, and its feature exists
In the condenser pipe is helical metal pipe, and the condenser pipe left end is communicated with high pressure nitrogen.
6. a kind of lubricating oil according to claim 1 processes waste heat recovery and the impurity treatment system of steam, and its feature exists
In be enclosed in the condenser pipe inside the heat exchange tank by the heat exchange tank, and the condenser pipe left end is left through the heat exchange tank
Wall top is connected with the blast pipe, and the condenser pipe right-hand member stretches out through the heat exchange tank right wall bottom.
7. a kind of lubricating oil according to claim 1 processes waste heat recovery and the impurity treatment system of steam, and its feature exists
In equipped with akaline liquid in the vent gas treatment ware.
8. a kind of lubricating oil according to claim 1 processes waste heat recovery and the impurity treatment system of steam, and its feature exists
In the grass tube lower end extends to the vent gas treatment ware inner bottom part.
9. a kind of lubricating oil according to claim 1 processes waste heat recovery and the impurity treatment system of steam, and its feature exists
In filled with activated carbon in the gas discharge pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621175679.9U CN206232674U (en) | 2016-11-02 | 2016-11-02 | A kind of waste heat recovery of lubricating oil processing steam and impurity treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621175679.9U CN206232674U (en) | 2016-11-02 | 2016-11-02 | A kind of waste heat recovery of lubricating oil processing steam and impurity treatment system |
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| Publication Number | Publication Date |
|---|---|
| CN206232674U true CN206232674U (en) | 2017-06-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621175679.9U Expired - Fee Related CN206232674U (en) | 2016-11-02 | 2016-11-02 | A kind of waste heat recovery of lubricating oil processing steam and impurity treatment system |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107828441A (en) * | 2017-12-14 | 2018-03-23 | 无锡市飞天油脂有限公司 | A kind of device of efficiently fractionation lubricating oil |
| CN107941038A (en) * | 2018-01-17 | 2018-04-20 | 张家港洁利环保科技有限公司 | A kind of industrial waste acid process tank heat-energy recovering apparatus |
| CN108775286A (en) * | 2018-08-03 | 2018-11-09 | 深圳市石金科技股份有限公司 | A kind of cleaning device of dry vacuum pump |
| CN108939879A (en) * | 2018-05-24 | 2018-12-07 | 夏文斌 | A kind of industrial steam recovery and processing system |
| CN109270226A (en) * | 2018-11-29 | 2019-01-25 | 江苏省环境科学研究院 | A kind of the organic liquid volatilization and processing unit of controlled condition |
| CN110242738A (en) * | 2019-06-05 | 2019-09-17 | 吉林工程技术师范学院 | A kind of automobile gearbox oil filter device |
| CN115671946A (en) * | 2023-01-04 | 2023-02-03 | 江苏新迪环保设备有限公司 | Waste desulfurization device |
-
2016
- 2016-11-02 CN CN201621175679.9U patent/CN206232674U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107828441A (en) * | 2017-12-14 | 2018-03-23 | 无锡市飞天油脂有限公司 | A kind of device of efficiently fractionation lubricating oil |
| CN107941038A (en) * | 2018-01-17 | 2018-04-20 | 张家港洁利环保科技有限公司 | A kind of industrial waste acid process tank heat-energy recovering apparatus |
| CN108939879A (en) * | 2018-05-24 | 2018-12-07 | 夏文斌 | A kind of industrial steam recovery and processing system |
| CN108775286A (en) * | 2018-08-03 | 2018-11-09 | 深圳市石金科技股份有限公司 | A kind of cleaning device of dry vacuum pump |
| CN109270226A (en) * | 2018-11-29 | 2019-01-25 | 江苏省环境科学研究院 | A kind of the organic liquid volatilization and processing unit of controlled condition |
| CN109270226B (en) * | 2018-11-29 | 2024-04-19 | 江苏省环境科学研究院 | Organic liquid volatilizing and treating device with controllable conditions |
| CN110242738A (en) * | 2019-06-05 | 2019-09-17 | 吉林工程技术师范学院 | A kind of automobile gearbox oil filter device |
| CN115671946A (en) * | 2023-01-04 | 2023-02-03 | 江苏新迪环保设备有限公司 | Waste desulfurization device |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| 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: 20170609 Termination date: 20191102 |