CN103740402A - Waste oil regeneration machine - Google Patents
Waste oil regeneration machine Download PDFInfo
- Publication number
- CN103740402A CN103740402A CN201310755007.XA CN201310755007A CN103740402A CN 103740402 A CN103740402 A CN 103740402A CN 201310755007 A CN201310755007 A CN 201310755007A CN 103740402 A CN103740402 A CN 103740402A
- Authority
- CN
- China
- Prior art keywords
- breakdown
- emulsion
- waste oil
- adsorber
- blowing device
- 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.)
- Pending
Links
Images
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention discloses a waste oil regeneration machine. The waste oil regeneration machine comprises a vortex separator, an inclined-plate separator, a magnetic-filtration adsorber, a heater, a demulsifier, a circulating pump, a high-voltage electrostatic adsorber, a gas storage bottle, a vacuum pump, a condenser and clay fine-filtration absorption towers, wherein the demulsifier comprises a closed demulsifying chamber, an atomizer, a resonance generating source, a gas blowing device, an exhaust opening and a liquid circulation opening, wherein the atomizer is arranged in the closed demulsifying chamber and is used for atomizing downwards, and the gas blowing device is used for upwards jetting gas; an inlet of the atomizer is connected with an outlet of the heater; a gas inlet of the gas blowing device is connected with the gas storage bottle; the exhaust opening is connected with the vacuum pump, the liquid circulation opening is connected with a liquid inlet of a circulating pump, a liquid outlet of the circulating pump is connected with a liquid inlet of the high-voltage electrostatic adsorber, and a liquid outlet of the high-voltage electrostatic adsorber is connected with an inlet of the heater. According to the waste oil regeneration machine, pure physical manners are adopted for deeply demulsifying to remove water-in-oil, and the index of regenerated oil reaches over 95% of fresh oil, so that the technology is at the domestic leading level.
Description
Technical field
The invention belongs to waste oil treatment technical field, be specifically related to a kind of waste oil regeneration machine.
Background technology
Along with the energy is day by day deficient and natural environment quality fast-descending, countries in the world energy environment protection expert explores in effort, exploitation energy-saving and environmental protection product improves real Tough questions, has occurred a series of equipment to useless waste oil regeneration processing on market.
At present popular useless, waste oil regeneration treatment technology is most of adopts the chemical method waste oil regeneration processing of giving up, mainly there is following technical problem: (1) dehydration aspect adopts coalescent closing or the dehydration of the monotechnics such as vacuum separation, cause breakdown of emulsion not thorough, easily emulsification again, and it is lower to process index, process fluid water content high (reaching 200ppm).(2) removal of impurities aspect all adopts mechanical filter, cannot remove compared with small impurities, and easily pile up and stop up.(3) at the broken water-in-oil technical elements of deemulsification, all adopt oil in water emulsion doping method again to solve, oil can produce infringement like this, and emulsification and contamination phenomenon can occur again again.(4) oil leakage phenomenon is serious at work.
summary of the invention
The present invention, for solving the problems of the technologies described above, provides a kind for the treatment of effect good waste oil regeneration machine.
The technical scheme that realizes the object of the invention is: a kind of waste oil regeneration machine, comprises whirlpool separator, the tilted plate separator connected with whirlpool separator, the magnetic filter adsorber connected with tilted plate separator, the well heater connected with magnetic filter adsorber, the emulsion treater connected with well heater, the recycle pump connected with emulsion treater, is connected the high pressure static electricity adsorber of recycle pump and well heater, the bomb being connected with emulsion treater, the vacuum air pump being connected with emulsion treater, the condenser being connected with vacuum air pump, the carclazyte essence that is connected with condenser filter adsorption tower; Emulsion treater comprises closed breakdown of emulsion chamber, and be arranged on the spraying gun, resonance generation source of the downward spraying in closed breakdown of emulsion chamber, for upwards air blowing device, bleeding point and the liquid circulation mouth of jet-stream wind; The import of described spraying gun is connected with the outlet of well heater; The inlet mouth of described air blowing device is connected with bomb; Described bleeding point is connected with vacuum air pump, and the fluid inlet of described liquid circulation mouth and recycle pump is connected, and the liquid outlet of described recycle pump is connected with the fluid inlet of high pressure static electricity adsorber, and the liquid outlet of high pressure static electricity adsorber is connected with the import of well heater.
In such scheme, spraying gun comprises the fog nozzle of the Jet with downward flow direction that is arranged on top, breakdown of emulsion chamber; Resonance generation source is arranged on the middle part of breakdown of emulsion chamber; Air blowing device is arranged on the bottom of breakdown of emulsion chamber; Bleeding point is arranged on the top of breakdown of emulsion chamber, and liquid circulation mouth is arranged on the bottom of breakdown of emulsion chamber.
In such scheme, between spraying gun and well heater, be provided with the liquid flow rate controller for controlling atomised jet amount; In described breakdown of emulsion chamber, be provided with the vacuum sensor being connected with this liquid flow rate controller.
In such scheme, between air blowing device and bomb, be provided with the gas-flow rate controller for controlling gas blow-out amount; Vacuum sensor in described breakdown of emulsion chamber is connected with this gas-flow rate controller.
In such scheme, described resonance generation source is ultrasonic generator.
The present invention adopts pure physics mode degree of depth breakdown of emulsion, removes water-in-oil, and recovered oil device index reaches fresh oil more than 95%, the domestically leading level of its technical finesse.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of the present invention.
Embodiment
(embodiment 1)
The present embodiment is a kind of waste oil regeneration machine, as shown in Figure 1, comprise whirlpool separator 11, the tilted plate separator 12 connected with whirlpool separator, the magnetic filter adsorber 13 connected with tilted plate separator, the well heater 21 connected with magnetic filter adsorber, the emulsion treater 4 connected with well heater, the recycle pump 22 connected with emulsion treater, be connected the high pressure static electricity adsorber 23 of recycle pump and well heater, the bomb 24 being connected with emulsion treater, the vacuum air pump 31 being connected with emulsion treater, the condenser 32 being connected with vacuum air pump, the carclazyte essence that is connected with condenser filter adsorption tower 33; Emulsion treater comprises closed breakdown of emulsion chamber 41, and be arranged on the spraying gun 42, resonance generation source 43 of the downward spraying in closed breakdown of emulsion chamber, for upwards air blowing device 44, bleeding point 45 and the liquid circulation mouth 46 of jet-stream wind; The import of described spraying gun is connected with the outlet of well heater; The inlet mouth of described air blowing device is connected with bomb; Described bleeding point is connected with vacuum air pump, and the fluid inlet of described liquid circulation mouth and recycle pump is connected, and the liquid outlet of described recycle pump is connected with the fluid inlet of high pressure static electricity adsorber, and the liquid outlet of high pressure static electricity adsorber is connected with the import of well heater.Described resonance generation source is ultrasonic generator.
Spraying gun comprises the fog nozzle 421 of the Jet with downward flow direction that is arranged on top, breakdown of emulsion chamber; Resonance generation source is arranged on the middle part of breakdown of emulsion chamber; Air blowing device is arranged on the bottom of breakdown of emulsion chamber; Bleeding point is arranged on the top of breakdown of emulsion chamber, and liquid circulation mouth is arranged on the bottom of breakdown of emulsion chamber.
In the present embodiment, between spraying gun and well heater, be provided with the liquid flow rate controller for controlling atomised jet amount; In described breakdown of emulsion chamber, be provided with the vacuum sensor being connected with this liquid flow rate controller.Between air blowing device and bomb, be provided with the gas-flow rate controller for controlling gas blow-out amount; Vacuum sensor in described breakdown of emulsion chamber is connected with this gas-flow rate controller.
(application examples 1)
Should use-case be the method for the transformer insulated waste oil of manipulation of regeneration of application above-described embodiment 1, comprise the following steps:
1. pre-treatment: allow waste oil successively by whirlpool separator 11, the tilted plate separator 12 being connected with whirlpool separator, the magnetic filter adsorber 13 that is connected with tilted plate separator, waste oil is carried out to oily water separation and coarse filtration processing; Pretreated waste oil is carried out to sampling Detection, when quality content is less than 1%, the mass content of oxide compound and carbide is while being less than 0.75%, just as qualified pre-treatment;
Whirlpool separator used is mainly for separating of oil-water mixture, tilted plate separator is mainly used in removing the impurity such as oxide compound and carbide, magnetic filter adsorber is mainly to adsorb for easy magnetized impurity such as the metals existing in processed waste oil, has greatly improved filter core normally move with the following operation of assurance work-ing life by this device;
2. advanced treatment: allow waste oil by well heater 21, it be heated, allow the waste oil after heating enter the emulsion treater 4 with breakdown of emulsion chamber 41 by spraying gun; The top of breakdown of emulsion used chamber is provided with spraying gun 42 and the bleeding point 45 with fog nozzle 421, and middle part is provided with resonance generation source 43, and bottom is provided with for upwards air blowing device 44 and the liquid circulation mouth 46 of jet-stream wind;
Waste oil after heating from fog nozzle 421 Jet with downward flow directions form mist of oils, mist of oil sinks under action of gravity, air blowing device is jet-stream wind upwards, thereby upwards stirs mist of oil, described mist of oil resonance generation source effect under vibrate, thereby make oil and gas and water from; Recycle pump 22 enters in well heater 21 after the liquid suction high pressure static electricity adsorber 23 of bottom, breakdown of emulsion chamber is processed again;
The spray pressure of spraying gun is preferably 0.2 Mpa to 0.6Mpa, and the present embodiment adopts 0.4 Mpa, and mist flow is 26 liters/min; Oil temperature is preferably room temperature to 75 ℃, and the oil temperature of the present embodiment is controlled at 63 ± 2 ℃; Vacuum tightness in breakdown of emulsion chamber is preferably 500 mbar to 800mbar, and the present embodiment adopts 650 ± 50 mbar; The flow of the jet-stream wind that air blowing device blows out is preferably 10 liters/min to 30 liters/min, and the present embodiment adopts 20 liters/min; Whiff pressure is preferably 0.2 Mpa to 0.6Mpa, and the present embodiment adopts 0.4 Mpa;
Described resonance generation source is ultrasonic generator, preferably 30,000 hertz to 50,000 hertz of vibrational frequencies used, and the present embodiment vibrational frequency used is 40,000 hertz;
High pressure static electricity adsorber is mainly realized two technique effects: one be by under high pressure, negative polarity in fluid micro dust particle produce charging, by there is a natural attraction between the sexes principle of same-sex repulsion, micro dust particle is adsorbed with adsorption paper, thoroughly purify fluid purity and be thorough from micro dust particle in oil and water separation, another,, for by high pressure static electricity ionizing event, repairs certain molecular structure of petroleum products;
3. essence filter is processed: vacuum air pump 31 is extracted the gaseous mixture in breakdown of emulsion chamber out from bleeding point 45, sends into condenser 32 it is carried out to condensation process; After condensation, obtain liquid oil and send into and in carclazyte essence filter adsorption tower 33, it is carried out to essence filter and process, the liquid oil obtaining after essence filter processing is as processed oil;
Carclazyte essence filter adsorption tower is a pure physical adsorption tower, can adsorb impurity particle in a certain amount of waste oil, changes color and luster and acid number, especially high-quality oil product is had to better result of use.
Between spraying gun and well heater, be provided with the liquid flow rate controller for controlling atomised jet amount; In described breakdown of emulsion chamber, be provided with the vacuum sensor being connected with this liquid flow rate controller.Between air blowing device and bomb, be provided with the gas-flow rate controller for controlling gas blow-out amount; Vacuum sensor in described breakdown of emulsion chamber is connected with this gas-flow rate controller.
The processed oil of final acquisition is carried out to sampling Detection, moisture content :≤2PPM; Machinery acrobatics :≤2PPM; Dustiness (NAS1633) < NAS6-7; With respect to new oil viscosity rate rate < ± 5%, conform with use standard completely.
Obviously, the above embodiment of the present invention is only for example of the present invention is clearly described, and is not the restriction to embodiments of the present invention.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here without also giving exhaustive to all embodiments.And these belong to apparent variation or the variation that connotation of the present invention extends out and still belong to protection scope of the present invention.
Claims (5)
1. a waste oil regeneration machine, comprise whirlpool separator (11), the tilted plate separator (12) being connected with whirlpool separator, the magnetic filter adsorber (13) being connected with tilted plate separator, the well heater (21) being connected with magnetic filter adsorber, the emulsion treater (4) being connected with well heater, the recycle pump (22) being connected with emulsion treater, connect the high pressure static electricity adsorber (23) of recycle pump and well heater, the bomb (24) being connected with emulsion treater, the vacuum air pump (31) being connected with emulsion treater, the condenser (32) being connected with vacuum air pump, the carclazyte essence filter adsorption tower (33) being connected with condenser, it is characterized in that: emulsion treater comprises closed breakdown of emulsion chamber (41), and be arranged on the spraying gun (42), resonance generation source (43) of the downward spraying in closed breakdown of emulsion chamber, for the upwards air blowing device of jet-stream wind (44), bleeding point (45) and liquid circulation mouth (46), the import of described spraying gun is connected with the outlet of well heater, the inlet mouth of described air blowing device is connected with bomb, described bleeding point is connected with vacuum air pump, and the fluid inlet of described liquid circulation mouth and recycle pump is connected, and the liquid outlet of described recycle pump is connected with the fluid inlet of high pressure static electricity adsorber, and the liquid outlet of high pressure static electricity adsorber is connected with the import of well heater.
2. waste oil regeneration machine according to claim 1, is characterized in that: spraying gun comprises the fog nozzle (421) of the Jet with downward flow direction that is arranged on top, breakdown of emulsion chamber; Resonance generation source is arranged on the middle part of breakdown of emulsion chamber; Air blowing device is arranged on the bottom of breakdown of emulsion chamber; Bleeding point is arranged on the top of breakdown of emulsion chamber, and liquid circulation mouth is arranged on the bottom of breakdown of emulsion chamber.
3. waste oil regeneration machine according to claim 1, is characterized in that: between spraying gun and well heater, be provided with the liquid flow rate controller for controlling atomised jet amount; In described breakdown of emulsion chamber, be provided with the vacuum sensor being connected with this liquid flow rate controller.
4. waste oil regeneration machine according to claim 3, is characterized in that: between air blowing device and bomb, be provided with the gas-flow rate controller for controlling gas blow-out amount; Vacuum sensor in described breakdown of emulsion chamber is connected with this gas-flow rate controller.
5. waste oil regeneration machine according to claim 1, is characterized in that: described resonance generation source is ultrasonic generator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310755007.XA CN103740402A (en) | 2013-12-31 | 2013-12-31 | Waste oil regeneration machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310755007.XA CN103740402A (en) | 2013-12-31 | 2013-12-31 | Waste oil regeneration machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103740402A true CN103740402A (en) | 2014-04-23 |
Family
ID=50497471
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310755007.XA Pending CN103740402A (en) | 2013-12-31 | 2013-12-31 | Waste oil regeneration machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103740402A (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204058376U (en) * | 2013-12-31 | 2014-12-31 | 宏秀电气有限公司 | Waste oil regeneration machine |
-
2013
- 2013-12-31 CN CN201310755007.XA patent/CN103740402A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204058376U (en) * | 2013-12-31 | 2014-12-31 | 宏秀电气有限公司 | Waste oil regeneration machine |
Non-Patent Citations (1)
| Title |
|---|
| 胡贤郎: ""净化破乳脱水技术在导热油再生中的应用"", 《热载体加热技术》 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105080311B (en) | A kind of fire coal boiler fume ultra-clean discharge integrated tower and handling process | |
| CN202724862U (en) | Oil purification device | |
| CN102872671B (en) | Asphalt waste gas purifying method and device | |
| CN202876599U (en) | Purifying device of asphalt waste gas | |
| CN204026787U (en) | A kind of automatically cleaning without the extreme low-altitude discharge lampblack purifying system of oil fire prevention | |
| WO2015169125A1 (en) | Method for removing dust in gas fumes | |
| CN103740401A (en) | Treatment method and demulsifier for waste oil regeneration | |
| CN201643930U (en) | Waste gas purification apparatus | |
| CN203756279U (en) | Tail gas treatment device of diesel generator | |
| CN203342607U (en) | Wet-type water film constant-flow high-voltage industrial waste gas purifier | |
| CN204058376U (en) | Waste oil regeneration machine | |
| CN110548359A (en) | Wet dust removal demisting device and wet dust removal demisting method thereof | |
| CN204079905U (en) | Waste oil regeneration emulsion treater | |
| CN107245348A (en) | The electric dehydration handling process and device of crude oil Produced Liquid containing complicated emulsion | |
| CN111870983B (en) | Automatic defoaming multifunctional rectifying tower device and rectifying process thereof | |
| CN103740402A (en) | Waste oil regeneration machine | |
| CN102389679B (en) | Lampblack smell-removing method and lampblack smell-removing device using method | |
| CN203447927U (en) | Industrial waste gas purification equipment | |
| CN211726167U (en) | Coal tar hydrogenation tar sediment cooling VOCs gas cleaning device | |
| CN204583485U (en) | Domestic cooking fume remover high efficiency electrostatic degreasing unit | |
| CN2505177Y (en) | Electrostatic cooking fume purifier with water electrode | |
| AU2021273567B2 (en) | Fluid treatment systems and methods | |
| CN204767622U (en) | Concentrator with ultrasonic wave defoaming | |
| CA3090319A1 (en) | Improvements in wastewater evaporation systems | |
| CN205055736U (en) | Device of pollutant washing and heat dissipation matter in gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20140423 |