CN204369837U - Waste lubricating oil distillation and clay-filtered merging device - Google Patents
Waste lubricating oil distillation and clay-filtered merging device Download PDFInfo
- Publication number
- CN204369837U CN204369837U CN201520004837.3U CN201520004837U CN204369837U CN 204369837 U CN204369837 U CN 204369837U CN 201520004837 U CN201520004837 U CN 201520004837U CN 204369837 U CN204369837 U CN 204369837U
- Authority
- CN
- China
- Prior art keywords
- distillation
- carclazyte
- clay
- lubricating oil
- tower body
- 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
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses the distillation of a kind of waste lubricating oil and clay-filtered merging device, comprise distillation tower tower body, the top of described tower body is provided with air outlet, the sidewall bottom of described distillation tower is provided with feed inlet and outlet, described distillation tower is provided with inside and outside double wall, is provided with heating unit between described inside and outside double wall, and described distillation tower inside is provided with stir shaft, described stir shaft is provided with agitating vane, and described stir shaft is connected with the agitator motor transmission being arranged on described tower body exterior bottom; The inner tip of described tower body is provided with carclazyte room, and the top of described carclazyte room is provided with entrance, and top is provided with outlet, and described carclazyte chamber interior has been horizontally disposed with multilayer screen cloth, and on every layer of screen cloth, tiling has carclazyte particle; The utility model has the advantage of: distillation and clay-filtered step have been come by a device, reduced equipment investment, decrease production cost, structure is simple, easy to use.
Description
Technical field
The utility model relates to a kind of regenerator for waste lubricating oil, and specifically a kind of waste lubricating oil distillation and clay-filtered merging device, belong to regenerator for waste lubricating oil field.
Background technology
The machinery of most type all will use lubricating oil, and this is because lubricating oil can reduce frictional force between machinery or between parts, to protect the surface of machinery or parts, to reduce wear, and the work-ing life of prolonged mechanical.Lubricating oil is the doping of petroleum refining base oil and refines to obtain, and its output accounts for about 2% of petroleum products total amount.Because the environment for use of dissimilar machinery differs greatly, therefore lubricating oil easily goes bad because of generation physics or chemical transformation and becomes waste lubricating oil in various complex environment.
For the process of waste lubricating oil, at present mostly both at home and abroad to use after waste lubricant oil regeneration, its process is: waste lubricating oil is after sedimentation, purification, filtration, absorption remove most of impurity, its water content is reduced again through dehydration, then the waste lubricant oil by hydrogenation processed is refined to remove the materials such as oxide compound, sulfocompound, halogen compounds, nitride and the heavy metal compound in waste oil, obtain spendable rerefined oil finally by after blending.Wherein, purifying step needs to carry out in a distillation column usually, and clay-filtered step needs to use extra equipment again, because this increasing equipment investment, improves production cost.
Utility model content
In order to solve the problem, the utility model devises the distillation of a kind of waste lubricating oil and clay-filtered merging device, distillation and clay-filtered step has been come by a device, has reduced equipment investment, decrease production cost, and structure is simple, easy to use.
The technical solution of the utility model is:
Waste lubricating oil distillation and clay-filtered merging device, comprise distillation tower tower body, the top of described tower body is provided with air outlet, the sidewall bottom of described distillation tower is provided with feed inlet and outlet, described distillation tower is provided with inside and outside double wall, heating unit is provided with between described inside and outside double wall, described distillation tower inside is provided with stir shaft, described stir shaft is provided with agitating vane, described stir shaft is connected with the agitator motor transmission being arranged on described tower body exterior bottom, by agitating vane, material is stirred, material is heated more even, improves working efficiency; The inner tip of described tower body is provided with carclazyte room, the top of described carclazyte room is provided with entrance, top is provided with outlet, described carclazyte chamber interior has been horizontally disposed with multilayer screen cloth, on every layer of screen cloth, tiling has carclazyte particle, and described carclazyte granular size is 0.1-2 millimeter, is preferably 1 millimeter, thus carclazyte filtration treatment can be carried out to retort gas, complete clay-filtered step.
Wherein, described heating unit is electromagnetic heating coil, the magnetic field of described electromagnetic heating coil is corresponding with the magnetic field of described stir shaft, thus can carry out Electromagnetic Heating by described electromagnetic heating coil to described stir shaft, then by stir shaft and agitating vane to heating material, adopt Electromagnetic Heating that heating material not only can be made even, without dead angle, avoid material local heating too high or too low for temperature, and energy consumption is low, non-exhaust emission, pollution free green environment protection.
Further, described tower body inside is provided with temperature sensor, described temperature sensor controls to be connected by controller and described electromagnetic heating coil, controlled the heating work of electromagnetic heating coil according to the temperature of temperature sensor by controller, the temperature of device interior is made to control, in rational scope, to improve reaction efficiency.Described controller is PLC or singlechip controller.
Further, described agitating vane is preferably downward-sloping setting, and angle of inclination is 5-15 ° of angle, thus makes to produce downward pressure in the process of stirring, further increases heated and stirred effect.
Further, described air outlet is also connected with described feed inlet and outlet by reflux line, and is provided with control valve; The outer wall coiling of described reflux line has condensing coil, can make material rapid condensation.
During use, first material is added distillation tower inside, open agitator motor and heating unit, regulate the rotating speed of agitator motor and the temperature of heating unit, the more abundant of mixing of materials is made by stirring, simultaneously because heating unit uses electromagnetic heating coil, temperature controls more accurate, effectively can reduce impurity contained in lubricating oil, thus alleviate follow-up work pressure, steam enters pipeline by air outlet, from air outlet, material out reenters distillation tower inside through reflux line and carries out second distillation, the interior contained impurity of the crude product lubricating oil extract can be reduced, Improving The Quality of Products.
The utility model has the advantage of: distillation and clay-filtered step have been come by a device, reduced equipment investment, decrease production cost, structure is simple, easy to use.
Below in conjunction with drawings and Examples, the utility model is described in further detail.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment.
Embodiment
Below preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein is only for instruction and explanation of the utility model, and be not used in restriction the utility model.
Embodiment 1
As shown in Figure 1, a kind of waste lubricating oil distillation and clay-filtered merging device, comprise distillation tower tower body 1, the top of described tower body 1 is provided with air outlet 2, the sidewall bottom of described distillation tower 1 is provided with feed inlet and outlet 3, described distillation tower 1 is provided with inside and outside double wall, heating unit 4 is provided with between described inside and outside double wall, described distillation tower 1 inside is provided with stir shaft 5, described stir shaft 5 is provided with agitating vane, described stir shaft 5 is connected with agitator motor 6 transmission being arranged on described tower body 1 exterior bottom, by agitating vane, material is stirred, material is heated more even, improve working efficiency.Described agitating vane is preferably downward-sloping setting, and angle of inclination is 5-15 ° of angle, thus makes to produce downward pressure in the process of stirring, further increases heated and stirred effect, described air outlet 2 is also connected with described feed inlet and outlet 3 by reflux line 7, and is provided with control valve, the outer wall coiling of described reflux line 7 has condensing coil 8, can make material rapid condensation, wherein, described heating unit 4 is electromagnetic heating coil, the magnetic field of described electromagnetic heating coil 7 is corresponding with the magnetic field of described stir shaft, thus Electromagnetic Heating can be carried out by described electromagnetic heating coil 7 to described stir shaft, again by stir shaft and agitating vane to heating material, adopt Electromagnetic Heating that heating material not only can be made even, without dead angle, avoid material local heating too high or too low for temperature, and energy consumption is low, non-exhaust emission, pollution free green environment protection, described tower body 1 inside is respectively equipped with temperature sensor 9, described temperature sensor 9 controls to be connected by controller and described electromagnetic heating coil, controlled the heating work of electromagnetic heating coil according to the temperature of temperature sensor by controller, the temperature of device interior is made to control in rational scope, improve reaction efficiency.Described controller is PLC or singlechip controller, is conventional structure;
The inner tip of described tower body 1 is provided with carclazyte room 10, the top of described carclazyte room 10 is provided with entrance 11, top is provided with outlet 12, described carclazyte room 10 inner horizontal is provided with multilayer screen cloth 13, on every layer of screen cloth 13, tiling has carclazyte particle, and described carclazyte granular size is 0.1-2 millimeter, is preferably 1 millimeter, thus carclazyte filtration treatment can be carried out to retort gas, complete clay-filtered step.
During use, first material is added distillation tower 1 inner, open agitator motor and heating unit, regulate the rotating speed of agitator motor and the temperature of heating unit, the more abundant of mixing of materials is made by stirring, simultaneously because heating unit uses electromagnetic heating coil, temperature controls more accurate, effectively can reduce impurity contained in lubricating oil, thus alleviate follow-up work pressure, steam enters pipeline by air outlet, from air outlet, material out reenters distillation tower inside through reflux line and carries out second distillation, the interior contained impurity of the crude product lubricating oil extract can be reduced, Improving The Quality of Products.
In addition, aforesaid device is except the modified node method pointed by the utility model, and all the other structures all belong to prior art, therefore seldom state.The junction circuit of aforesaid device is conventional circuit design, one of ordinary skill in the art can obtain according to the ordinary skill in this field, much more no longer as long as can realize linkage function of the present utility model, concrete structure can be selected according to actual needs, therefore to state.
Claims (4)
1. waste lubricating oil distillation and clay-filtered merging device, it is characterized in that: comprise distillation tower tower body, the top of described tower body is provided with air outlet, the sidewall bottom of described distillation tower is provided with feed inlet and outlet, described distillation tower is provided with inside and outside double wall, is provided with heating unit between described inside and outside double wall, and described distillation tower inside is provided with stir shaft, described stir shaft is provided with agitating vane, and described stir shaft is connected with the agitator motor transmission being arranged on described tower body exterior bottom; The inner tip of described tower body is provided with carclazyte room, and the top of described carclazyte room is provided with entrance, and top is provided with outlet, and described carclazyte chamber interior has been horizontally disposed with multilayer screen cloth, and on every layer of screen cloth, tiling has carclazyte particle.
2. waste lubricating oil distillation according to claim 1 and clay-filtered merging device, it is characterized in that: described heating unit is electromagnetic heating coil, the magnetic field of described electromagnetic heating coil is corresponding with the magnetic field of described stir shaft; Described tower body inside is provided with temperature sensor, and described temperature sensor controls to be connected by controller and described electromagnetic heating coil, is controlled the heating work of electromagnetic heating coil by controller according to the temperature of temperature sensor.
3. waste lubricating oil distillation according to claim 1 and clay-filtered merging device, it is characterized in that: the downward-sloping setting of described agitating vane, angle of inclination is 5-15 ° of angle.
4. waste lubricating oil distillation according to claim 1 and clay-filtered merging device, is characterized in that: described air outlet is also connected with described feed inlet and outlet by reflux line, and is provided with control valve; The outer wall coiling of described reflux line has condensing coil, can make material rapid condensation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520004837.3U CN204369837U (en) | 2015-01-06 | 2015-01-06 | Waste lubricating oil distillation and clay-filtered merging device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520004837.3U CN204369837U (en) | 2015-01-06 | 2015-01-06 | Waste lubricating oil distillation and clay-filtered merging device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204369837U true CN204369837U (en) | 2015-06-03 |
Family
ID=53326073
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520004837.3U Expired - Fee Related CN204369837U (en) | 2015-01-06 | 2015-01-06 | Waste lubricating oil distillation and clay-filtered merging device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204369837U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105964000A (en) * | 2016-06-23 | 2016-09-28 | 望江县大唐资源再生有限公司 | Waste engine oil recycling treatment device |
| CN105963998A (en) * | 2016-06-23 | 2016-09-28 | 望江县大唐资源再生有限公司 | Waste oil recovery treatment device |
| CN108201704A (en) * | 2016-12-19 | 2018-06-26 | 泰奥星（天津）有限公司 | A kind of distilling apparatus of OIL IN LUBRICATING OIL PRODUCTION equipment |
| CN111748404A (en) * | 2019-03-27 | 2020-10-09 | 江苏察克润滑科技有限公司 | Lubricating oil production equipment |
-
2015
- 2015-01-06 CN CN201520004837.3U patent/CN204369837U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105964000A (en) * | 2016-06-23 | 2016-09-28 | 望江县大唐资源再生有限公司 | Waste engine oil recycling treatment device |
| CN105963998A (en) * | 2016-06-23 | 2016-09-28 | 望江县大唐资源再生有限公司 | Waste oil recovery treatment device |
| CN108201704A (en) * | 2016-12-19 | 2018-06-26 | 泰奥星（天津）有限公司 | A kind of distilling apparatus of OIL IN LUBRICATING OIL PRODUCTION equipment |
| CN111748404A (en) * | 2019-03-27 | 2020-10-09 | 江苏察克润滑科技有限公司 | Lubricating oil production equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204369837U (en) | Waste lubricating oil distillation and clay-filtered merging device | |
| CN205550266U (en) | Portable chemical industry reation kettle of heatable cooling material | |
| CN104030482B (en) | A kind of working method of biogas residue liquid | |
| CN101571344B (en) | Multifunctional vacuum conical mixing-drying unit | |
| CN204298219U (en) | Sludge hot hydrolysis reaction device | |
| CN101818086B (en) | Production process and production equipment of sludge and garbage carbonized slurry fuel | |
| CN204369816U (en) | Waste lubricating oil produces the system of diesel oil | |
| CN107502441A (en) | A kind of lubricating oil mechanical delamination constant temperature dewaxing device | |
| CN107353996A (en) | Waste lubricant oil regeneration utilization process and its process units | |
| CN204237844U (en) | One effectively utilizes the remaining temperature of steam to improve sintering mixing dosage hot water adding set | |
| CN201476475U (en) | Vacuum conical mixing drying machine set | |
| CN105854859A (en) | Efficient bifunctional catalyst as well as preparation and application thereof | |
| CN105329945B (en) | Device and method for preparing high-purity and high-dissolvability molybdenum trioxide with industrial molybdic acid | |
| CN206731123U (en) | A kind of white glue with vinyl production reactor of heat energy recycling | |
| CN100497319C (en) | Rectifying method for methyl benzotrizole | |
| CN206463856U (en) | A kind of pipeline production variable ratio frequency changer formula raw material heating device | |
| CN206622102U (en) | A kind of process units of isolonglifolene | |
| CN108314527A (en) | A kind of microbial organic fertilizer production technology | |
| CN204417451U (en) | The full-automatic regeneration treatment system of energy-saving waste lubricating oil | |
| CN202785701U (en) | Reactor for preparing ferric oxide through adopting circulation type precipitation method | |
| CN210496408U (en) | 2-chlorine-5-chloromethyl pyridine apparatus for producing | |
| CN105732368B (en) | Method for synthesizing polyol fatty acid ester by adopting wiped film evaporator | |
| CN103626329A (en) | Resource treatment method and system for garbage and/or sludge pressing water | |
| CN102838171B (en) | Reactor and process for preparing iron oxide by utilizing circulation type precipitation method | |
| CN203307290U (en) | Lubricating oil production device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150603 Termination date: 20170106 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |