CN101077459A - Regeneration processing device for waste lubricant oil - Google Patents
Regeneration processing device for waste lubricant oil Download PDFInfo
- Publication number
- CN101077459A CN101077459A CN 200610082384 CN200610082384A CN101077459A CN 101077459 A CN101077459 A CN 101077459A CN 200610082384 CN200610082384 CN 200610082384 CN 200610082384 A CN200610082384 A CN 200610082384A CN 101077459 A CN101077459 A CN 101077459A
- Authority
- CN
- China
- Prior art keywords
- lubricating oil
- evaporimeter
- oil
- waste lubricating
- inner bag
- 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.)
- Granted
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 45
- 230000008929 regeneration Effects 0.000 title description 6
- 238000011069 regeneration method Methods 0.000 title description 6
- 239000000314 lubricant Substances 0.000 title description 3
- 239000010687 lubricating oil Substances 0.000 claims abstract description 47
- 238000010438 heat treatment Methods 0.000 claims abstract description 30
- 239000003921 oil Substances 0.000 claims abstract description 23
- 230000001172 regenerating effect Effects 0.000 claims abstract description 15
- 239000002893 slag Substances 0.000 claims abstract description 3
- 239000011229 interlayer Substances 0.000 claims description 15
- 239000000446 fuel Substances 0.000 claims description 8
- 239000003208 petroleum Substances 0.000 claims description 7
- 239000007789 gas Substances 0.000 claims description 5
- 238000002485 combustion reaction Methods 0.000 claims description 4
- 238000007789 sealing Methods 0.000 claims description 3
- 239000002737 fuel gas Substances 0.000 claims description 2
- 238000009413 insulation Methods 0.000 claims description 2
- 239000010410 layer Substances 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims 1
- 238000001704 evaporation Methods 0.000 abstract description 12
- 238000005336 cracking Methods 0.000 abstract description 6
- 230000008020 evaporation Effects 0.000 description 8
- 239000012535 impurity Substances 0.000 description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 238000004821 distillation Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000005461 lubrication Methods 0.000 description 2
- 239000010721 machine oil Substances 0.000 description 2
- 239000010705 motor oil Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000002199 base oil Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000013528 metallic particle Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Images
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The waste lubricating oil regenerating apparatus is one evaporator, which has one outer casing, one inner container with one combined rotating body, one distilling tower, one heating sandwich with oil inlet and oil outlet, one central rotation shaft with oil hole mounted through bearing on the bottom of the inner container, one oil pipe connected to the oil outlet in the bottom of the evaporator, one scraper mounted on the central shaft and fitting the inner wall of the inner container, one sprayer in the upper part of the scraper and communicated with the oil path of the central shaft, one heater in the lower part of the evaporator, one slag draining port in the bottom of the evaporator, and one motor to drive the central shaft. The present invention has constant temperature heating, great evaporating area, less cracking of the lubricating oil and high heat efficiency.
Description
Technical field
The invention belongs to the device for regenerating and processing that makes device for regenerating and processing waste lubrication oil, particularly waste lubricating oil that useless machine oil recycled.
Background technology
Owing to reasons such as lubricating oil oxidation in use, cracking and condensation cause the part component rotten, sneak into some impurity (as the metallic particles of dust, light oil, wearing and tearing etc.) simultaneously from the external world, and portions additive is destroyed.When rotten composition and impurities accumulation to a certain degree the time, lubricating oil just can not continue to use again, becomes waste lubricating oil.
What the process for regeneration of waste lubricating oil that adopts in the many waste oil regenerations manufacturer of China adopted all is acid/native method of reproduction, passes through sulfuric acid washing-clay-treated method and carries out waste lubricant oil regeneration.Because acid/local method causes the appearance of a large amount of acid sludges with the sulfuric acid scrubbing meeting, causes the pollution to environment.Waste lubricating oil distillation circular heating, making heat carrier and heat carrier circulating pump must be to possess the heat resistance of bearing temperature more than 450 ℃, the heating-up temperature height, disengagement area is little, and power consumption is high, easily cracking.
Also having a kind of waste lubricant oil regeneration technology is moisture, gas and the mechanical admixture that utilizes in the vacuum oil-filter removal waste lubricating oil.But this vacuum oil-filter is applicable to the in-line purification of machine oil, but medium-to-high grade I. C. engine oil, engine oil and some impurity oil big to viscosity, impure complicated component then can't filter, and often cause vacuum filter plugged filter and Impurity removal not thorough.
Summary of the invention
The object of the present invention is to provide a kind of device for regenerating and processing of waste lubricating oil, can realize the waste lubricating oil heated at constant temperature, increase the disengagement area of lubricating oil, make the disposable evaporation of waste lubricating oil on the evaporating surface, avoided the hydronic drawback of waste lubricating oil, heat time heating time is short, energy savings, reduced the cracking of waste lubricating oil, and, improved the quality of reclaimed oil the Impurity removal in the waste lubricating oil.
The object of the present invention is achieved like this: a kind of device for regenerating and processing of waste lubricating oil, constitute evaporimeter by shell and inner bag with sealing heating interlayer, its inner bag is the closure casing that top has the combination revolution bodily form of connector, on the connector of inner bag, adorning rectifying column by flange, top and bottom at the evaporimeter heating interlayer are being provided with oil-in and oil-out respectively, by sealed bearing the central rotating shaft that the upper end has fuel feed hole is installed in evaporimeter inner bag bottom centre, the petroleum pipeline end that is provided with above in evaporimeter is installed with sealed bearing, match with sealed bearing in the upper end of central rotating shaft, the oil-out of base of evaporator is connecting petroleum pipeline, the bracket end that has pipeline by symmetry on central rotating shaft is installed with the scraper plate that matches with the inner bag inwall respectively, the oil circuit of central rotating shaft fuel feed hole is communicated with the injector that is installed in scraper plate top by the pipeline on the support, bottom at evaporimeter is installed with heater, at the bottom of the evaporimeter person's of setting slag-drip opening, motor drives central rotating shaft by decelerator and rotates.
It is such utilizing the course of work of processing unit (plant) regeneration processing waste lubricating oil of the present invention: the waste lubricating oil through the heating furnace heating is delivered to evaporimeter by pressure, heated waste lubricating oil enters the heating interlayer from the oil-in of evaporimeter, hot waste lubricating oil in the further heating fumigators heating interlayer of the heater of base of evaporator, make the hot lubricating oil in the heating interlayer keep comparatively constant heating-up temperature, with the inner bag of heating fumigators as heat carrier.The motor drives central rotating shaft rotates, support on the central rotating shaft drives scraper plate and does gyration along the circumferential wall of inner bag and the bottom surface of the bottom of a pan shape, and the oil-out of evaporimeter heating interlayer bottom is ejected into the hot lubricating oil in the evaporimeter heating interlayer on the inner bag face of evaporimeter by injector through the fuel feed hole of central rotating shaft, oil pipe on the support equably by petroleum pipeline.Central rotating shaft drives scraper plate and does gyration along the bottom surface of inner bag circumferential wall and the bottom of a pan shape, make injector be ejected into used heat lubricating oil on the inner bag face by scraper plate to spread to oil film at the uniform velocity equably, to satisfy the needs of disengagement area less than 0.5mm thickness.Because the hot waste lubricating oil in the evaporimeter heating interlayer, has guaranteed the inner bag of the waste lubricating oil of heating in the evaporimeter heating interlayer with the stationary temperature heating fumigators by the heater heat temperature raising of evaporimeter bottom.The utility model has been created evaporation conditions at a lower temperature, owing to guarantee uniform all the time the heated oil film less than 0.5mm thickness on the inner bag, makes the disengagement area maximization.Can make waste lubricating oil guarantee to distill under the temperature required prerequisite according to the test fuel film vaporization, required high-temperature temperature has reduced by 100 degrees centigrade than the required temperature of conventional distillation, and the hot oil outlet temperature that adds of heating furnace is to get final product about 400 ℃.The time of evaporation also became disposable evaporation by former circulation intensification-evaporation, the waste lubricating oil that serves as heat carrier in the evaporimeter heating interlayer need not to return the heating that circulates in the heating furnace, does not also need anti-high temperature heat-resistant carrier circulating pump more than 450 ℃ simultaneously.Significantly reduce the time of evaporation, reduced the cracking that causes waste lubricating oil because of long high temperature evaporation.After the waste lubricating oil composition is evaporated, carries out classification by the rectifying column of installing on the evaporimeter inner bag connector and reclaim, can obtain regenerate base oil and light oil.After the waste lubricating oil evaporation, the impurity of generation is discharged from the slag-drip opening that base of evaporator is provided with in the evaporimeter inner bag.Device for regenerating and processing waste lubrication oil of the present invention has been realized heated at constant temperature to waste lubricating oil, increased the disengagement area of lubricating oil, make the disposable evaporation of waste lubricating oil on the evaporating surface, avoided the hydronic drawback of waste lubricating oil, warm-up time is short, and energy savings has reduced the cracking of waste lubricating oil, and, improved the quality of reclaimed oil with the Impurity removal in the waste lubricating oil.The combustion gas that heater burnt is the flammable light gas that discharge at the rectifying column top, has therefore also just solved the gas emission problem.
Description of drawings
The invention will be further described below in conjunction with accompanying drawing.
Accompanying drawing is a structural representation of the present invention.
The specific embodiment
A kind of device for regenerating and processing of waste lubricating oil, as shown in drawings, constitute evaporimeter by shell 1 and inner bag 2 with sealing heating interlayer, its inner bag 2 has the closure casing of the combination revolution bodily form of connector 5 for top, inner bag 2 be shaped as the closure casing that the bodily form is turned round in top cone with connector 5 and the combination that constitutes at the bottom of cylinder and the arc pot.On the connector 5 of inner bag 2, adorning rectifying column 6 by flange, top and bottom at evaporimeter heating interlayer shell 1 are being provided with oil-in 4 and oil-out 15 respectively, by sealed bearing the central rotating shaft 3 that the upper end has fuel feed hole is installed in evaporimeter inner bag bottom centre, petroleum pipeline 7 ends that are provided with above in evaporimeter are installed with sealed bearing, match with sealed bearing in the upper end of central rotating shaft 3, the oil-out 15 of base of evaporator links to each other with petroleum pipeline 7, support 8 by symmetry on central rotating shaft 3 is installed with upright scraper plate 10 respectively, match with the inwall of inner bag 2 in the outer end of scraper plate 10, match with the circumferential wall and the circular arc the bottom of a pan of inner bag 2 in the outer end that is scraper plate 10, pipeline 9 is installed on support 8, and the oil circuit of central rotating shaft 3 fuel feed holes is communicated with the injector 11 that is installed in scraper plate 10 tops by the pipeline on the support 89.Injector 11 is the atomizer of flat, uniform nozzle opening on atomizer.Bottom at evaporimeter is installed with heater, and heater is the concentric circles tubular combustion dish 13 that Gas Pipe connects, uniform fuel gas hole on the concentric pipe of tray for combustion 13.Heat-insulation layer 12 in the outer setting of evaporimeter,, improve the efficiency of heating surface to reduce scattering and disappearing of heating heat.In the bottom of evaporimeter slag-drip opening 16 is being set, slag-drip opening 16 is connecting slag ladle 17 by pipeline.Motor 14 drives central rotating shaft 3 by decelerator and rotates.Be subjected to backing 18 and fin 19 uniform respectively setting the on the outer wall of evaporator shell 1 and on the inwall,, achieve constant temperature and improve heat exchange efficiency for the waste lubricating oil that serves as heat carrier in the evaporimeter heating interlayer provides heat.
Claims (7)
1, a kind of device for regenerating and processing of waste lubricating oil, it is characterized in that: constitute evaporimeter with sealing heating interlayer by shell (1) and inner bag (2), its inner bag (2) has the closure casing of the combination revolution bodily form of connector (5) for top, connector (5) in inner bag (2) is upward being adorned destilling tower (6) by flange, top and bottom at the evaporimeter heating interlayer are being provided with oil-in (4) and oil-out (15) respectively, by sealed bearing the central rotating shaft (3) that the upper end has fuel feed hole is installed in evaporimeter inner bag (2) bottom centre, petroleum pipeline (7) end that is provided with above in evaporimeter is installed with sealed bearing, match with sealed bearing in the upper end of central rotating shaft (3), the oil-out of base of evaporator (15) is connecting petroleum pipeline (7), the support that has pipeline (9) (8) end of going up by symmetry at central rotating shaft (3) is installed with the scraper plate (10) that matches with inner bag (2) inwall respectively, the oil circuit of central rotating shaft (3) fuel feed hole is communicated with the injector (11) that is installed in scraper plate (10) top by the pipeline (9) on the support (8), bottom at evaporimeter is installed with heater, slag-drip opening (16) is being set in the bottom of evaporimeter, and motor (14) drives central rotating shaft (3) by decelerator and rotates.
2, the device for regenerating and processing of waste lubricating oil according to claim 1 is characterized in that: the closure casing of the combination revolution bodily form that constitutes at the bottom of the cone that is shaped as top tool cloth connector (5) of inner bag (2) and cylinder and the arc pot.
3, the device for regenerating and processing of waste lubricating oil according to claim 1 is characterized in that: injector (11) is the atomizer of flat, uniform nozzle opening on atomizer.
4, the device for regenerating and processing of waste lubricating oil according to claim 1 is characterized in that: heater is the concentric circles tubular combustion dish (13) that Gas Pipe connects, uniform fuel gas hole on the concentric pipe of tray for combustion (13).
5, the device for regenerating and processing of waste lubricating oil according to claim 1 is characterized in that: heat-insulation layer (12) in the outer setting of evaporimeter.
6, the device for regenerating and processing of waste lubricating oil according to claim 1 is characterized in that: slag-drip opening (16) is connecting slag ladle (17) by pipeline.
7, the device for regenerating and processing of waste lubricating oil according to claim 1 is characterized in that: on the outer wall of evaporator shell (1) and inwall on uniform respectively the setting be subjected to backing (18) and fin (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100823841A CN100460039C (en) | 2006-05-25 | 2006-05-25 | Regeneration processing device for waste lubricant oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100823841A CN100460039C (en) | 2006-05-25 | 2006-05-25 | Regeneration processing device for waste lubricant oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101077459A true CN101077459A (en) | 2007-11-28 |
| CN100460039C CN100460039C (en) | 2009-02-11 |
Family
ID=38905222
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100823841A Active CN100460039C (en) | 2006-05-25 | 2006-05-25 | Regeneration processing device for waste lubricant oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100460039C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102166421A (en) * | 2011-02-22 | 2011-08-31 | 广州迪森热能技术股份有限公司 | Preparation system of biomass distillate |
| CN102179058A (en) * | 2011-02-22 | 2011-09-14 | 广州迪森热能技术股份有限公司 | Distillation reactor |
| CN103463824A (en) * | 2013-09-29 | 2013-12-25 | 王金林 | Efficient rotating spray evaporator |
| CN104941229A (en) * | 2015-05-14 | 2015-09-30 | 江苏双仪光学器材有限公司 | Anti-acidification degreasing agent distillation tank |
| CN105238541A (en) * | 2015-08-21 | 2016-01-13 | 山西八达镁业有限公司 | Simple recovery and regeneration method for waste vacuum oil for magnesium metal smelting |
| CN107596717A (en) * | 2017-10-17 | 2018-01-19 | 上海庐骁机电设备有限公司 | A kind of distillation equipment for Chemical Manufacture |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58223473A (en) * | 1982-06-18 | 1983-12-26 | Toyota Motor Corp | Treatment for regenerating waste liquid of aqueous lubricating and release agent |
| CN87204808U (en) * | 1987-03-20 | 1988-06-08 | 刘楚兴 | Device for treating waste oil and purifying waste gas |
| NO170429C (en) * | 1991-03-05 | 1992-10-14 | Bgb V Snorre Bentsen Is | PROCEDURE FOR REFINING USED LUBRICATING OILS AND APPLIANCES FOR USING THE PROCEDURE |
| CN2584263Y (en) * | 2002-10-30 | 2003-11-05 | 吴进家 | Distillation recovery treatment device |
| CN2612434Y (en) * | 2003-04-10 | 2004-04-21 | 上海森松制药设备有限公司 | Agitating and vaporising device |
| CN100419053C (en) * | 2004-11-04 | 2008-09-17 | 田松庆 | Technology of waste oil regenerating and its used apparatus |
-
2006
- 2006-05-25 CN CNB2006100823841A patent/CN100460039C/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102166421A (en) * | 2011-02-22 | 2011-08-31 | 广州迪森热能技术股份有限公司 | Preparation system of biomass distillate |
| CN102179058A (en) * | 2011-02-22 | 2011-09-14 | 广州迪森热能技术股份有限公司 | Distillation reactor |
| CN103463824A (en) * | 2013-09-29 | 2013-12-25 | 王金林 | Efficient rotating spray evaporator |
| CN104941229A (en) * | 2015-05-14 | 2015-09-30 | 江苏双仪光学器材有限公司 | Anti-acidification degreasing agent distillation tank |
| CN105238541A (en) * | 2015-08-21 | 2016-01-13 | 山西八达镁业有限公司 | Simple recovery and regeneration method for waste vacuum oil for magnesium metal smelting |
| CN107596717A (en) * | 2017-10-17 | 2018-01-19 | 上海庐骁机电设备有限公司 | A kind of distillation equipment for Chemical Manufacture |
| CN107596717B (en) * | 2017-10-17 | 2021-06-01 | 山东聚恒能源设备有限公司 | Distillation equipment for chemical production |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100460039C (en) | 2009-02-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100460039C (en) | Regeneration processing device for waste lubricant oil | |
| CN204702642U (en) | A kind of continous way Thermal decomposition device for sludge | |
| CN111686571A (en) | Self-cleaning heat energy recovery energy-saving combustion waste gas treatment device | |
| CN104986934A (en) | Continuous thermal decomposition method and apparatus for sludge | |
| CN105737167B (en) | Heat accumulating type rotating bed segmentation utilizes the method and system of carbonaceous organic material thermal decomposition product | |
| CN103913049B (en) | The continuous drying system of slurry or powder | |
| CN101955178B (en) | Method and device for cooling high-temperature calcined coke of carbon rotary kiln | |
| CN203582815U (en) | Device for producing diesel by using waste lubricating oil | |
| CN103614152B (en) | Lignite upgrading device | |
| CN105481037B (en) | Substance thermally decomposes sub-argument device | |
| CN205974420U (en) | Smokeless carbonization system of straw | |
| CN205640923U (en) | System for segmentation of heat accumulation formula revolving bed utilizes carbonaceous organic material thermal decomposition product | |
| CN207031347U (en) | A kind of high-temperature retorting system | |
| CN115554804A (en) | Air conditioning system of pipeline production workshop | |
| CN101982529A (en) | High-temperature cracking system for tar in biomass fuel gas | |
| CN108048200B (en) | Waste oil distillation cracking catalytic system and production process | |
| CN205634946U (en) | Material thermolysis divides reason device | |
| CN101096603A (en) | Method for producing biodiesel by employing molecular distillation technology and manufacturing equipment | |
| CN208684864U (en) | Continuous cracking distillation system for waste oil regeneration | |
| CN2349212Y (en) | Vaporized cracking furnace for refining gasoline and diesel from waste plastics and rubber | |
| CN201695000U (en) | Sludge treatment system | |
| CN112457878A (en) | Device and process for preparing second-generation biodiesel based on hydrodeoxygenation of waste oil | |
| CN206882385U (en) | The system for handling house refuse | |
| JPH0931468A (en) | Carbonizing device | |
| CN207944074U (en) | A kind of device using producing base oil by regenerating waste lubricating oil |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: XINJIANG FUKE OIL CO., LTD. Free format text: FORMER OWNER: TU JING Effective date: 20091023 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20091023 Address after: 18, Urumqi economic and Technological Development Zone, the Xinjiang Uygur Autonomous Region fork building Patentee after: Xinjiang Fly C' Oil Co., Ltd. Address before: 18, Urumqi economic and Technological Development Zone, the Xinjiang Uygur Autonomous Region fork building Patentee before: Tu Jing |