CN204022764U - Waste oil regeneration treatment system - Google Patents
Waste oil regeneration treatment system Download PDFInfo
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- CN204022764U CN204022764U CN201420254517.9U CN201420254517U CN204022764U CN 204022764 U CN204022764 U CN 204022764U CN 201420254517 U CN201420254517 U CN 201420254517U CN 204022764 U CN204022764 U CN 204022764U
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- oil
- stirring tank
- treatment system
- waste oil
- regeneration treatment
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Abstract
The utility model discloses a kind of waste oil regeneration treatment system, comprise closed stirring tank, the powder filling apparatus be connected with stirring tank, the strainer be connected with stirring tank, also comprise the well heater for heating to stirring tank, described stirring tank top is provided with vacuum suction apparatus for bleeding and emission-control equipment, the utility model waste oil regeneration treatment system is by being provided with well heater, for the vacuum suction apparatus of bleeding and emission-control equipment, fine pumping device is added in oil regeneration process, to Light ends in oil, moisture and obnoxious flavour carry out fast eliminating, improve regeneration oil flash, remove the oxidizing gas that free acid in oil and high temperature produce, while improving quality of reclaimed and quality, centralized collection process is carried out to the gas produced in process oil product, the gas of discharge is made to reach the requirement of environment protection emission.
Description
Technical field
The utility model belongs to the lubricant of processing, to reclaim the technical field of useful products, specifically relates to a kind of waste oil regeneration treatment system.
Background technology
Technical oils (as oil engine wet goods) after long-term use, because of the existence of the undesirable substances such as carbon granule, mechanical impurity, deep oxidation thing, colloid, pitch, makes oily emulsification, blackout, needs to make oil reach requirement by regeneration.
Technology of waste oil regenerating mainly contains several both at home and abroad at present:
1, sulfuric acid carclazyte method: distillation pickling is exactly the oil refining of so-called local method, and indigenous oil refining plant is simple and crude, backward in technique, yield and composite merchandise rate low, poor product quality, seriously polluted, waste resource, dislike oil degenerating area public security, potential safety hazard exists at any time.
2, hydrofinishing method: be the important process process in Natural lubricating oils processing, be used widely in waste oil regeneration.It is the refining means widely adopted in pollution-free reclaiming process flow process, but its application in waste oil regeneration also has certain limitation.If near there is no the source of hydrogen, then also need the device for producing hydrogen of self-built costliness, this just needs bigger device, drops into greatly, therefore, only has and can collect a large amount of oil salvage factory and just can take hydrogenation technique.
3, chemical flocculation, filters: Waste oil regeneration machine is the specific equipment of technical oils regeneration, has been widely used in waste oil regeneration field.Existing Waste oil regeneration machine mainly comprises stirring tank, powder filling apparatus, vacuum pump, residual sea water pump, hot oil pump, strainer, oil inlet pipe, oil outlet pipe, escape pipe and valve etc., is connected therebetween by process pipeline.Pending waste oil in stirring tank after being heated to certain temperature, application powder filling apparatus adds powder additive and flocculates to waste oil, adsorbs, thus remove the undesirable substance such as carbon granule, mechanical impurity, deep oxidation thing, colloid, pitch be dispersed in oil, again by the press filtration of strainer, make the color restoration clear of oil, the property indices of the waste oil such as reduction oil engine, become qualified absolute oil, the absolute oil after regeneration is got rid of by oil outlet pipe.
Summary of the invention
In view of this, the purpose of this utility model is to provide a kind of waste oil regeneration treatment system, this waste oil regeneration treatment system is by being provided with well heater, for the vacuum suction apparatus of bleeding and emission-control equipment, fine pumping device is added in oil regeneration process, to Light ends in oil, moisture and obnoxious flavour carry out fast eliminating, improve regeneration oil flash, remove the oxidizing gas that free acid in oil and high temperature produce, while improving quality of reclaimed and quality, centralized collection process is carried out to the gas produced in process oil product, the gas of discharge is made to reach the requirement of environment protection emission.
In order to achieve the above object, a kind of waste oil regeneration of the utility model treatment system comprises closed stirring tank, the powder filling apparatus be connected with stirring tank, the strainer that is connected with stirring tank, also comprise the well heater for heating to stirring tank, described stirring tank top is provided with vacuum suction apparatus for bleeding and emission-control equipment.
Further, the oil outlet of described strainer is connected with molecule refining plant, storage tank and Mixer pot in turn.
Further, described vacuum suction apparatus is set to vacuum pump.
Further, described emission-control equipment comprise be connected with vacuum suction apparatus successively condensing works, adsorb tank body and chemical hydrolysis device.
Further, described chemical hydrolysis device is connected with air cooling equipment and secondary absorption tank body in turn, the outlet of described secondary absorption tank body is connected with the entrance of described chemical hydrolysis device.
Further, swirling flow mixer is provided with in described stirring tank.
The beneficial effects of the utility model are:
The utility model waste oil regeneration treatment system is by being provided with well heater, for the vacuum suction apparatus of bleeding and emission-control equipment, fine pumping device is added in oil regeneration process, fast eliminating is carried out to Light ends, moisture and obnoxious flavour in oil, improve regeneration oil flash, remove the oxidizing gas that free acid in oil and high temperature produce, while improving quality of reclaimed and quality, centralized collection process is carried out to the gas produced in process oil product, make the gas of discharge reach the requirement of environment protection emission.
Accompanying drawing explanation
Fig. 1 is the structural plan of the utility model waste oil regeneration treatment system;
Fig. 2 is the structural plan of vacuum system in Fig. 1.
Reference numeral: 1-fuel tank; 2-oil pump; 3-well heater; 4-stirring tank; 5-vacuum suction apparatus; 6-emission-control equipment; 7-powder filling apparatus; 8-strainer; 9-molecule refining plant; 10-storage tank; 11-Mixer pot; 12-vacuum pump; 13-condensing works; 14-adsorbs tank body; 15-chemical hydrolysis device; 16-air cooling equipment; 17-secondary absorption tank body.
Embodiment
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described in detail.
Be illustrated in figure 1 the structural plan of the utility model waste oil regeneration treatment system, a kind of waste oil regeneration of the utility model treatment system comprises closed stirring tank 4, the powder filling apparatus 7 be connected with stirring tank 4, the strainer 8 be connected with stirring tank 4, also comprise the well heater 3 for heating to stirring tank 4, described stirring tank 4 top is provided with vacuum suction apparatus 5 for bleeding and emission-control equipment 6, waste oil in the present embodiment fuel tank 1 passes through in oil inlet pipe suction stirring tank 4 through oil pump 2, and add appropriate flocculation agent and discoloring agent by powder filling apparatus 7, stirring tank 4 pairs of waste oil stir, well heater 3 carries out heating to waste oil makes its temperature be raised to 120 °, in flocculation process, organifying group concentrates faster, molecular weight is more firm, when temperature rises to 120 °, its flocculated impurities forms solid particulate, vacuum suction device 5 is to Light ends in oil, moisture and obnoxious flavour carry out fast eliminating, improve regeneration oil flash, Light ends in the oil that emission-control equipment 6 pairs of vacuum suction devices 5 are collected, moisture and obnoxious flavour process, recovered oil is subsequently by high-precision filter 8, base oil can be drawn after elimination impurity, the present embodiment is by being provided with well heater 3, for the vacuum suction apparatus 5 of bleeding and emission-control equipment 6, fine pumping device 5 is added in oil regeneration process, to Light ends in oil, moisture and obnoxious flavour carry out fast eliminating, improve regeneration oil flash, remove the oxidizing gas that free acid in oil and high temperature produce, while improving quality of reclaimed and quality, centralized collection process is carried out to the gas produced in process oil product, the gas of discharge is made to reach the requirement of environment protection emission.
Further, the oil outlet of preferred described strainer 8 is connected with molecule refining plant 9, storage tank 10 and Mixer pot 11 in turn, and this structure is conducive to improving quality of reclaimed and quality further.
Further, preferred described vacuum suction apparatus 5 is set to vacuum pump 12, and the vacuum absolute pressure of described vacuum pump 12 is set to 20 ~ 30kpa, and this structure makes oil product separation carry out dewatering and obnoxious flavour faster.
Further, preferred described emission-control equipment 6 comprises the condensing works 13 be connected with vacuum suction apparatus 5 successively, absorption tank body 14 and chemical hydrolysis device 15, described chemical hydrolysis device 15 is connected with air cooling equipment 16 and secondary absorption tank body 17 in turn, the outlet of described secondary absorption tank body 17 is connected with the entrance of described chemical hydrolysis device 15, have employed low temperature gathers cold, the two poles of the earth are adsorbed, the obnoxious flavour of chemical hydrolysis mode process volatilization and light hydrocarbon, obnoxious flavour and light hydrocarbon are by being reduced into the gas that water and part are not reduced into during condensing works 13, enter absorption tank body 14 again by during sorbent material in tank body heavy metal adsorption in the endoporus of sorbent material, but because of the excessive velocities of negative pressure ventilation and portion gas process incomplete, so my company adds secondary wind cool and secondary absorption tank body 17 in the design process, when obnoxious flavour untreated complete time again enter chemical hydrolysis mode, in water, add certain chemical reagent exactly carry out objectionable constituent in decomposition gas, thus reach the requirement of environment protection emission.
Further, swirling flow mixer is provided with in described stirring tank 4, the present embodiment adds cyclone mixing by tank interior, so just can make oil product dehydration be separated during obnoxious flavour faster, after adding chemical, oil product contacts lower with air when sealing, and chemistry organifying group in flocculation process concentrates faster, molecular weight is more firm, and when temperature rises to 120 °, its flocculated impurities forms solid particulate.
Adopt before and after the utility model waste oil regeneration treatment system process recovered oil and contrast:
Useless garage waste oil detection case is as follows:
After process, recovered oil detection case is as follows:
According to the high-quality oil product that recovered oil detected result is qualified.
What finally illustrate is, above preferred embodiment is only in order to illustrate the technical solution of the utility model and unrestricted, although be described in detail the utility model by above preferred embodiment, but those skilled in the art are to be understood that, various change can be made to it in the form and details, and not depart from the utility model claims limited range.
Claims (6)
1. a waste oil regeneration treatment system, comprise closed stirring tank, the powder filling apparatus be connected with stirring tank, the strainer that is connected with stirring tank, it is characterized in that: also comprise the well heater for heating to stirring tank, described stirring tank top is provided with vacuum suction apparatus for bleeding and emission-control equipment.
2. waste oil regeneration treatment system as claimed in claim 1, is characterized in that: the oil outlet of described strainer is connected with molecule refining plant, storage tank and Mixer pot in turn.
3. waste oil regeneration treatment system as claimed in claim 1, is characterized in that: described vacuum suction apparatus is set to vacuum pump.
4. waste oil regeneration treatment system as claimed in claim 1, is characterized in that: described emission-control equipment comprise be connected with vacuum suction apparatus successively condensing works, adsorb tank body and chemical hydrolysis device.
5. waste oil regeneration treatment system as claimed in claim 4, it is characterized in that: described chemical hydrolysis device is connected with air cooling equipment and secondary absorption tank body in turn, the outlet of described secondary absorption tank body is connected with the entrance of described chemical hydrolysis device.
6. waste oil regeneration treatment system as claimed in claim 1, is characterized in that: be provided with swirling flow mixer in described stirring tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420254517.9U CN204022764U (en) | 2014-05-19 | 2014-05-19 | Waste oil regeneration treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420254517.9U CN204022764U (en) | 2014-05-19 | 2014-05-19 | Waste oil regeneration treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204022764U true CN204022764U (en) | 2014-12-17 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420254517.9U Expired - Fee Related CN204022764U (en) | 2014-05-19 | 2014-05-19 | Waste oil regeneration treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204022764U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105080379A (en) * | 2015-08-04 | 2015-11-25 | 周荣国 | Device for blending fuel oil for ship and processing technology thereof |
| CN111229773A (en) * | 2019-05-05 | 2020-06-05 | 云南新昊环保科技有限公司 | Oil contamination disposal system and process |
| CN112980559A (en) * | 2021-04-12 | 2021-06-18 | 朝阳金达钛业股份有限公司 | Vacuum pump oil treatment and recycling device for titanium sponge production and recycling method thereof |
-
2014
- 2014-05-19 CN CN201420254517.9U patent/CN204022764U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105080379A (en) * | 2015-08-04 | 2015-11-25 | 周荣国 | Device for blending fuel oil for ship and processing technology thereof |
| CN111229773A (en) * | 2019-05-05 | 2020-06-05 | 云南新昊环保科技有限公司 | Oil contamination disposal system and process |
| CN112980559A (en) * | 2021-04-12 | 2021-06-18 | 朝阳金达钛业股份有限公司 | Vacuum pump oil treatment and recycling device for titanium sponge production and recycling method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP02 | Change in the address of a patent holder |
Address after: 400039 Chongqing Xie culture seven village 23 Patentee after: CHONGQING DINGNENG OIL PURIFIER MANUFACTURE CO., LTD. Address before: 400039 Chongqing Jiulongpo Chen Ping Tian Cun in No. 218 Patentee before: CHONGQING DINGNENG OIL PURIFIER MANUFACTURE CO., LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141217 Termination date: 20190519 |