CN201300008Y - Oil filter system for reclaiming waste oil - Google Patents
Oil filter system for reclaiming waste oil Download PDFInfo
- Publication number
- CN201300008Y CN201300008Y CNU2008201004211U CN200820100421U CN201300008Y CN 201300008 Y CN201300008 Y CN 201300008Y CN U2008201004211 U CNU2008201004211 U CN U2008201004211U CN 200820100421 U CN200820100421 U CN 200820100421U CN 201300008 Y CN201300008 Y CN 201300008Y
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- oil
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- filter
- pipeline
- valve
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Abstract
Disclosed is an oil filter system for reclaiming waste oil, comprising a reactor, a filter press, and a heat transfer oil heating and circulating device; wherein an oil outlet at the bottom of the reactor is connected with the filter press and then is communicated with the upper part of the reactor to form an external circulating processing loop; the processed oil is output through the output end of the filter press; or the oil outlet pipe at the bottom of the reactor is connected with the filter press and then is connected with a vacuum separator to remove the water and gas contained in the oil, and the oil is processed to be base oil through the vacuum separator and a fine filter; an exhaust gas outlet arranged at the top of the reactor is connected with an exhaust gas purification and disposal device; and the reactor is provided with a vacuum heat insulation layer. The oil filter system removes the impurities, peculiar smell, moisture and gas in the waste oil, and the exhaust gas of the system is disposed without causing any harm. The oil filter system can produce oil products at various purities and can save energy and reduce the wastage of the relevant equipment and is high in work efficiency.
Description
Technical field
The utility model relates to oil filter, particularly a kind ofly waste oil disposal can be become highly purified base oil, have waste oil regeneration oil filter system energy-conservation, that can increase work efficiency and reduce the relevant device loss.
Background technology
The product oil purity that the oil filter of prior art extracts is low, can not be suitable for the demand in market fully, smell with irritating of reclaimed oil after treatment and quality are low, our experiments show that, water content 〉=100mg/L, air content 〉=0.1% in the reclaimed oil after prior art is handled, filtering accuracy is not high, when going back consumption energy consumption.Existing oil filter does not have special emission-control equipment, and institute's exhaust gas discharged works the mischief to environment.
Summary of the invention
The purpose of this utility model is in order to overcome the prior art above shortcomings, and providing a kind of can become high quality base oil with waste oil disposal, and can be energy-conservation, increase work efficiency and reduce the waste oil regeneration oil filter system of relevant device loss.
The utility model is achieved through the following technical solutions, it is a kind of waste oil regeneration oil filter system, the heat-conducting oil heating EGR that comprises reactor, filter press, constitutes by oil conservator and heater and heat(ing) coil thereof, wherein heat(ing) coil is arranged in reactor, the connecting oil conservator and heater respectively into and out of pipeline and constitute the circulation heating circuit of heat(ing) coil; The inflow pipeline of reactor connects the oil-feed control valve by oil pump, coarse filter; The flowline of reactor bottom is communicated with circular treatment loop in the formation by valve, oil pump, valve and pipeline with the top of reactor; Described reactor comprises retort and is arranged on the interior central stirring shaft of retort; It is characterized in that:
(1), the flowline of reactor bottom is connected with pressure filter by valve F1, oil pump, valve F2 and pipeline, is communicated with formation outer circulation treatment loop with reactor top by pipeline and valve F7 again, the oil product after the processing is exported product oil by the valve F4 that pressure filter goes out to hold;
Or the flowline of (2) reactor bottom is connected with pressure filter by F1, oil pump K3, valve F2 and pipeline, connect vacuum separator by valve F5 and pipeline again and slough aqueous vapor in the oil, oil product after the processing connects fine filter by the pipeline of vacuum separator bottom by oil pump, again by valve F6 output product oil;
(3) the waste gas delivery outlet of reactor bottom setting connects exhaust gas purification and treatment device by pipeline and blower fan.
In the said system, the oil outlet end of pressure filter connects the peculiar smell device that deoils by valve F4.
The advantage that the utility model has owing to said structure is conspicuous: each circulating oil path can one uses separately, also can be used in combination by different circulating oil paths, thereby just can extract the reclaimed oil of different purity; Be provided with the peculiar smell device that deoils in this structure, can remove the peculiar smell in the reclaimed oil, improved the quality of reclaimed oil; Owing to also be provided with vacuum separation unit and fine filter in the system, can further improve the purity of reclaimed oil; The emission-control equipment that is provided with in the system can be handled the waste gas that produces in the extractive process, and making the tail gas that drains in the atmosphere is innocuous gas.In a word, the utility model can extract various purity base oil, energy-conservation, increase work efficiency and reduce the relevant device loss.
Description of drawings
The utility model said structure can further specify by the non-limiting example that accompanying drawing provides.
Fig. 1 is a structural representation of the present utility model.
Among the figure: A, reactor; B, coarse filter; C, filter press; D, exhaust gas purification and treatment device; E, the peculiar smell device deoils; F, vacuum separation unit; G, fine filter; H, heater; I, oil conservator; J, air exhauster; K1～K3, oil pump; L, oil-feed control valve; F1～F6, valve; 1, vavuum pump; 2, vacuum heat-insulating layer; 3, shaft; 4, remove the peculiar smell layer; 5, spray head; 6, vacuum separator; 7, semisphere valve; 8, water tank reactor; 9, water circulating pump; 10, activated carbon reactor; 11, active carbon adsorption layer; 12, outlet port; 13, three-dimensional separator.
The specific embodiment
The utility model is described in further detail below in conjunction with drawings and Examples:
Referring to accompanying drawing, waste oil regeneration oil filter system among the figure, waste oil regeneration oil filter system, the heat-conducting oil heating EGR that comprises reactor A, filter press C, constitutes by oil conservator I and heater H and heat(ing) coil thereof, wherein heat(ing) coil is arranged in reactor, the connecting oil conservator I and heater H respectively into and out of pipeline and constitute the circulation heating circuit of heat(ing) coil; The inflow pipeline of reactor connects oil-feed control valve L by oil pump K1, coarse filter B; The flowline of reactor bottom is communicated with circular treatment loop in the formation by valve F1, oil pump K3, valve F3 and pipeline with the top of reactor; Described reactor comprises retort and is arranged on the interior central stirring shaft 3 of retort; It is characterized in that:
(1), the flowline of reactor bottom is connected with pressure filter C by F1, oil pump K3, valve F2 and pipeline, be communicated with reactor top by pipeline and valve F7 again and constitute the outer circulation treatment loop, the valve F4 output product oil that the oil product after the processing goes out to hold by pressure filter;
Or the flowline of (2) reactor bottom is connected with pressure filter C by F1, oil pump K3, valve F2 and pipeline, connect vacuum separator F by valve F5 and pipeline again and slough aqueous vapor in the oil, oil product after the processing connects fine filter G by the pipeline of vacuum separator bottom by oil pump, again by delivery valve F6 output product oil;
(3) the waste gas delivery outlet of reactor bottom setting connects exhaust gas purification and treatment device D by pipeline and blower fan J.
G of fine filter described in the said system and pressure filter C all adopt fine filter and the pressure filter in the commercially available food oil processing.
The retort of described reactor has double-deck tank skin, and the inner chamber of double-deck tank skin connects vavuum pump 1 by pipeline, by constituting enclosed vacuum thermal insulation layer 2 after the vavuum pump suction.Owing to described structure, shortened the intensification heat time heating time of pending oil product, saved the energy and prolonged the service life of relevant device and improved operating efficiency.
Described exhaust gas purification and treatment device D comprises water tank reactor 8, is located at the waste gas tube connector that is connected with air exhauster J on the water tank reactor; The bottom of described water tank reactor 8 is connected with activated carbon reactor 10 by water circulating pump 9 and outlet conduit thereof; The tank body that described activated carbon reactor is communicated with the water tank reactor by the bottom and be arranged on active carbon adsorption layer 11 in the tank body and the blast pipe 12 at tank body top constitutes, the described water side of outlet conduit in activated carbon reactor that is connected with water circulating pump 9 be positioned at described activated carbon adsorption layer 11 below.The gas outlet of described waste gas tube connector is stretched under the liquid level of water tank reactor 8, and its outlet side has the mesh-type tube wall or is connected with the spray tube.The described water side of outlet conduit in activated carbon reactor 10 that is connected with water circulating pump 9 is provided with the spray tube.Since described structure, the innoxious after treatment discharging of waste gas that system is produced.
The oil outlet end of described pressure filter can also connect the peculiar smell device E that deoils by valve F4; The described peculiar smell device E that deoils is by the turnover oil-piping of tank body and bottom provided thereon and go peculiar smell adsorption layer 4, oil-in place to be provided with spray head 5 to constitute.This device can effectively be removed the peculiar smell in the oil, thereby improves the quality of oil product.
Described vacuum separation unit F comprises vacuum separator 6 and by connected another vavuum pump 1 of pipeline, is provided with oil inlet pipe at the top of vacuum separator that the oil-out end of described oil inlet pipe 3 is equipped with and makes oil produce vaporific shower nozzle 5.The bottom of vacuum separator connects fine filter G by pipeline and oil drain pump, and the end that goes out of fine filter connects valve 6 as the base oil oil-out.This device can effectively be removed aqueous vapor remaining in the oil, further improves the quality of oil product.
Said structure is that work----is opened electrical control cabinet and the temperature required oil-feed control valve L that opens simultaneously is set on the temperature control instrument like this, pending oil enters to be sent into reactor A by oil pump K1 behind the coarse filter B and by shaft it is stirred, heater H adopts heat exchange pattern that oil product in the agitator is heated simultaneously, the conduction oil of heating by reactor A and oil conservator I and heater H by oil pipeline and be arranged on oil pump K2 on the pipeline and valve F2 and F3 constitute and add the deep fat circulating oil path and realize treating and handle the purpose that oil product heats, in this process, also in reactor A, be added with chemicals make chemical phase impurity and physics mutually impurity fully remove; In said process, oil product can also by reactor A and oil pipeline and be arranged on oil pump K2 on the pipeline and valve F1, F2 and F3 constitute in circulating oil path handle the removing repeatedly that reaches impurity, the oil of this moment is semi-finished product oil just; Semi-finished product oil is transported to filter press C by oil pipeline and be arranged on oil pump K2 on the pipeline and valve F4 constitutes the product oil circulating oil path and is treated to the product oil that is removed peculiar smell by described reactor A; Transport to the peculiar smell device E that deoils by reactor A again and remove peculiar smell in the oil; Filter press C and vacuum separation unit F and fine filter G are by oil pipeline and be arranged on oil pump on the pipeline and valve constitutes high-purity product oil circulating oil path product oil is further purified; Waste gas in the above process is connected with emission-control equipment D with the waste discharge feed channel by ventilating fan J handles the waste gas that is produced in the reactor A.
In sum, the utility model realized to various purity product oils refinement, energy-conservation, improved operating efficiency and reduced the loss of relevant device.
Claims (9)
1, a kind of waste oil regeneration oil filter system, the heat-conducting oil heating EGR that comprises reactor (A), filter press (C), constitutes by oil conservator (I) and heater (H) and heat(ing) coil thereof, wherein heat(ing) coil is arranged in reactor, the connecting oil conservator (I) and heater (H) respectively into and out of pipeline and constitute the circulation heating circuit of heat(ing) coil; The inflow pipeline of reactor connects oil-feed control valve (L) by oil pump (K1), coarse filter (B); The flowline of reactor bottom is communicated with circular treatment loop in the formation by valve (F1), oil pump (K3), valve (F3) and pipeline with the top of reactor; Described reactor comprises retort and is arranged on the interior central stirring shaft (3) of retort; It is characterized in that:
(1), the flowline of reactor bottom is connected with pressure filter (C) by (F1), oil pump (K3), valve (F2) and pipeline, be communicated with reactor top by pipeline and valve (F7) again and constitute the outer circulation treatment loop, valve (F4) the output product oil that the oil product after the processing goes out to hold by pressure filter;
Or the flowline of (2) reactor bottom is connected with pressure filter (C) by (F1), oil pump (K3), valve (F2) and pipeline, connect vacuum separator (F) by valve (F5) and pipeline again and slough aqueous vapor in the oil, oil product after the processing connects fine filter (G) by the pipeline of vacuum separator bottom by oil pump, again by delivery valve (F6) output product oil;
(3) the waste gas delivery outlet of reactor bottom setting connects exhaust gas purification and treatment device (D) by pipeline and blower fan (J).
2, waste oil regeneration oil filter according to claim 1 system, it is characterized in that: the retort of described reactor has double-deck tank skin, the inner chamber of double-deck tank skin connects vavuum pump (1) by pipeline, by constituting enclosed vacuum thermal insulation layer (2) after the vavuum pump suction.
3, waste oil regeneration oil filter according to claim 1 system, it is characterized in that: described exhaust gas purification and treatment device (D) comprises water tank reactor (8), is located at the waste gas tube connector that is connected with air exhauster (J) on the water tank reactor; The bottom of described water tank reactor (8) is connected with activated carbon reactor (10) by water circulating pump (9) and outlet conduit thereof; The tank body that described activated carbon reactor is communicated with the water tank reactor by the bottom and be arranged on active carbon adsorption layer (11) in the tank body and the blast pipe (12) at tank body top constitutes, the described water side of outlet conduit in activated carbon reactor that is connected with water circulating pump (9) is positioned at the below of described activated carbon adsorption layer (11).
4, oil filter emission-control equipment according to claim 3 is characterized in that: the gas outlet of described waste gas tube connector is stretched under the liquid level of water tank reactor (8), and its outlet side has the mesh-type tube wall or is connected with the spray tube.
5, oil filter emission-control equipment according to claim 3 is characterized in that: the described water side of outlet conduit in activated carbon reactor (10) that is connected with water circulating pump (9) is provided with the spray tube.
6, waste oil regeneration oil filter according to claim 1 system is characterized in that: the oil outlet end of pressure filter connects the peculiar smell device (E) that deoils by valve (F4); The described peculiar smell device (E) that deoils is by the turnover oil-piping of tank body and bottom provided thereon and go peculiar smell adsorption layer (4) to constitute, and the oil-in place is provided with spray head (5).
7, waste oil regeneration oil filter according to claim 1 system is characterized in that: described vacuum separation unit (F)
Comprise vacuum separator (6) and, be provided with oil inlet pipe that the oil-out end of described oil inlet pipe (3) is equipped with and makes oil produce vaporific shower nozzle (5) at the top of vacuum separator by connected another vavuum pump of pipeline (1).
8, oil filter vacuum purification device according to claim 7 is characterized in that: shower nozzle (5) below be provided with the three-dimensional separator (13) of space network, described three-dimensional separator and vacuum separator are fixed or are swum on the pasta.
9, oil filter vacuum purification device according to claim 7 is characterized in that: the bottom of vacuum separator connects fine filter (G) by pipeline and oil drain pump, and the end that goes out of fine filter connects valve (F6) as the product oil oil-out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201004211U CN201300008Y (en) | 2008-10-31 | 2008-10-31 | Oil filter system for reclaiming waste oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201004211U CN201300008Y (en) | 2008-10-31 | 2008-10-31 | Oil filter system for reclaiming waste oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201300008Y true CN201300008Y (en) | 2009-09-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201004211U Expired - Fee Related CN201300008Y (en) | 2008-10-31 | 2008-10-31 | Oil filter system for reclaiming waste oil |
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| CN (1) | CN201300008Y (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101884854A (en) * | 2010-07-13 | 2010-11-17 | 易治吉 | Novel oil filtering system |
| CN101940249A (en) * | 2010-07-23 | 2011-01-12 | 彭南生 | Collection method and collection device of edible waste oil and pork waste grease |
| CN102585989A (en) * | 2011-12-28 | 2012-07-18 | 重庆渝能滤油机制造有限公司 | Waste oil regeneration system |
| CN106098318A (en) * | 2016-07-27 | 2016-11-09 | 国网山东省电力公司茌平县供电公司 | A kind of oil-filled transformer oiling device |
| TWI561627B (en) * | 2014-04-09 | 2016-12-11 | Guntou Sangyo Co Ltd | |
| CN111085040A (en) * | 2020-01-03 | 2020-05-01 | 宝应县恒泰电器设备厂 | Oil purification system and method |
| CN111978979A (en) * | 2020-09-01 | 2020-11-24 | 山东工业职业学院 | Ultrasonic vacuum oscillation deodorizing composite oil liquid purifying process and device |
-
2008
- 2008-10-31 CN CNU2008201004211U patent/CN201300008Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101884854A (en) * | 2010-07-13 | 2010-11-17 | 易治吉 | Novel oil filtering system |
| CN101940249A (en) * | 2010-07-23 | 2011-01-12 | 彭南生 | Collection method and collection device of edible waste oil and pork waste grease |
| CN102585989A (en) * | 2011-12-28 | 2012-07-18 | 重庆渝能滤油机制造有限公司 | Waste oil regeneration system |
| CN102585989B (en) * | 2011-12-28 | 2013-08-07 | 重庆渝能滤油机制造有限公司 | Waste oil regeneration system |
| TWI561627B (en) * | 2014-04-09 | 2016-12-11 | Guntou Sangyo Co Ltd | |
| CN106098318A (en) * | 2016-07-27 | 2016-11-09 | 国网山东省电力公司茌平县供电公司 | A kind of oil-filled transformer oiling device |
| CN111085040A (en) * | 2020-01-03 | 2020-05-01 | 宝应县恒泰电器设备厂 | Oil purification system and method |
| CN111085040B (en) * | 2020-01-03 | 2022-05-27 | 宝应县恒泰电器设备厂 | Oil purification method utilizing oil purification system |
| CN111978979A (en) * | 2020-09-01 | 2020-11-24 | 山东工业职业学院 | Ultrasonic vacuum oscillation deodorizing composite oil liquid purifying process and device |
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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: 20090902 Termination date: 20151031 |
|
| EXPY | Termination of patent right or utility model |