CN204079905U - Waste oil regeneration emulsion treater - Google Patents
Waste oil regeneration emulsion treater Download PDFInfo
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- CN204079905U CN204079905U CN201320894024.7U CN201320894024U CN204079905U CN 204079905 U CN204079905 U CN 204079905U CN 201320894024 U CN201320894024 U CN 201320894024U CN 204079905 U CN204079905 U CN 204079905U
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Abstract
The utility model discloses a kind of waste oil regeneration emulsion treater, comprise closed breakdown of emulsion room, be arranged on the spraying gun of the downward spraying in closed breakdown of emulsion room, resonance occurring source, air blowing device, bleeding point and liquid circulation mouth for upwards 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 described liquid circulation mouth is connected with the fluid inlet of recycle pump, 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.The utility model 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.
Description
Technical field
The utility model belongs to waste oil treatment technical field, is specifically related to a kind of waste oil regeneration emulsion treater.
Background technology
Along with the energy is day by day deficient and natural environment quality declines fast, countries in the world energy environment protection expert explores in effort, exploitation energy-saving and environmental protection product improves real Tough questions, market has occurred a series of equipment to useless waste oil regeneration process.
Popular at present useless, waste oil regeneration treatment technology major part adopt chemical method to carry out useless waste oil regeneration process, mainly there is following technical problem: (1) dehydration aspect adopts the monotechnics dehydrations such as coalescent conjunction or vacuum separation, cause breakdown of emulsion not thorough, easily emulsification again, and process index is lower, process fluid water content high (reaching 200ppm).(2) removal of impurities aspect all adopts mechanical filter, cannot remove comparatively small impurities, and easy accumulated plugging.(3) breaking water-in-oil technical elements at deemulsification all adopts oil in water emulsion doping method again to solve, and such oil can produce infringement, emulsification and contamination phenomenon can occur again again.(4) oil leakage phenomenon is serious at work.
Utility model content
The utility model, for solving the problems of the technologies described above, provides a kind of pure physics mode degree of depth breakdown of emulsion and the good waste oil regeneration emulsion treater of technique effect.
The technical scheme realizing the utility model object is: a kind of waste oil regeneration emulsion treater, comprises closed breakdown of emulsion room, is arranged on the spraying gun of the downward spraying in closed breakdown of emulsion room, resonance occurring source, air blowing device, bleeding point and liquid circulation mouth for upwards 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 described liquid circulation mouth is connected with the fluid inlet of recycle pump, 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 technique scheme, spraying gun comprises the fog nozzle of the Jet with downward flow direction being arranged on top, breakdown of emulsion room; Resonance occurring source is arranged on the middle part of breakdown of emulsion room; Air blowing device is arranged on the bottom of breakdown of emulsion room; Bleeding point is arranged on the top of breakdown of emulsion room, and liquid circulation mouth is arranged on the bottom of breakdown of emulsion room.
In technique scheme, between spraying gun and well heater, be provided with the liquid flow rate controller for controlling atomised jet amount; The vacuum sensor be connected with this liquid flow rate controller is provided with in described breakdown of emulsion room.
In technique 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 room is connected with this gas-flow rate controller.
In technique scheme, described resonance occurring source is ultrasonic generator.
The utility model 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 utility model.
The one application schematic diagram that Fig. 2 is emulsion treater shown in Fig. 1.
Embodiment
(embodiment 1, emulsion treater)
The present embodiment is a kind of waste oil regeneration emulsion treater, as shown in Figure 2, well heater 21, the emulsion treater 4 be connected with well heater, the recycle pump 22 being connected emulsion treater, the high pressure static electricity adsorber 23 connecting recycle pump and well heater, the bomb 24 that is connected with emulsion treater is comprised; Emulsion treater comprises closed breakdown of emulsion room 41, and is arranged on the spraying gun 42 of the downward spraying in closed breakdown of emulsion room, resonance occurring source 43, air blowing device 44, bleeding point 45 and liquid circulation mouth 46 for upwards 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 external vacuum air pump, and described liquid circulation mouth is connected with the fluid inlet of recycle pump, 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 occurring source is ultrasonic generator.
Spraying gun comprises the fog nozzle 421 of the Jet with downward flow direction being arranged on top, breakdown of emulsion room; Resonance occurring source is arranged on the middle part of breakdown of emulsion room; Air blowing device is arranged on the bottom of breakdown of emulsion room; Bleeding point is arranged on the top of breakdown of emulsion room, and liquid circulation mouth is arranged on the bottom of breakdown of emulsion room.
In the present embodiment, between spraying gun and well heater, be provided with the liquid flow rate controller for controlling atomised jet amount; The vacuum sensor be connected with this liquid flow rate controller is provided with in described breakdown of emulsion room.The gas-flow rate controller for controlling gas blow-out amount is provided with between air blowing device and bomb; Vacuum sensor in described breakdown of emulsion room is connected with this gas-flow rate controller.
The present embodiment 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.
(application examples 1, waste oil regeneration treatment system and method)
The present embodiment is the application waste oil regeneration treatment system made of above-described embodiment 1 and method of work thereof: as shown in Figure 2, comprise the following steps:
1. pre-treatment: allow waste oil filter adsorber 13 by whirlpool separator 11, the tilted plate separator 12 be connected with whirlpool separator, the magnetic that is connected with tilted plate separator successively, oily water separation and coarse filtration process are carried out to waste oil; Sampling Detection is carried out to pretreated waste oil, when quality content be less than 1%, the mass content of oxide compound and carbide be less than 0.75% time, 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 mainly adsorbs for easy magnetized impurity such as the metals existed in processed waste oil, drastically increases filter core work-ing life and ensure that following operation is normally run by this device;
2. advanced treatment: allow waste oil be heated it by well heater 21, allows the waste oil after heating be entered the emulsion treater 4 with breakdown of emulsion room 41 by spraying gun; The top of breakdown of emulsion room used is provided with the spraying gun 42 and bleeding point 45 with fog nozzle 421, and middle part is provided with resonance occurring source 43, and bottom is provided with air blowing device 44 for upwards jet-stream wind and liquid circulation mouth 46; Air blowing device extracts nitrogen from bomb 24; Waste oil after heating from fog nozzle 421 Jet with downward flow direction formed mist of oil, mist of oil sinks under gravity, and air blowing device is jet-stream wind upwards, thus upwards stirs mist of oil, described mist of oil resonance occurring source effect under vibrate, thus 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 bottom breakdown of emulsion room 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 DEG C, and the Oil-temperature control of the present embodiment is at 63 ± 2 DEG C; Vacuum tightness in breakdown of emulsion room is preferably 500 mbar to 800mbar, and the present embodiment adopts 650 ± 50 mbar; The flow of the jet-stream wind of air blowing device blowout 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 occurring source is ultrasonic generator, vibrational frequency used preferably 30,000 hertz to 50,000 hertz, and the present embodiment vibrational frequency used is 40,000 hertz;
High pressure static electricity adsorber mainly realizes 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, with adsorption paper, micro dust particle is adsorbed, thorough purification fluid purity is thorough from micro dust particle in oil and water separation, another is by high pressure static electricity ionizing event, repairs certain molecular structure of petroleum products;
3. essence filter process: vacuum air pump 31 is extracted the gaseous mixture in breakdown of emulsion room out from bleeding point 45, sends into condenser 32 and carries out condensation process to it; Obtain liquid oil after condensation to send in carclazyte essence filter adsorption tower 33 and carry out essence filter process to it, after essence filter processes, the liquid oil that obtains 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, change color and luster and acid number, especially have better result of use to high-quality oil product.
The liquid flow rate controller for controlling atomised jet amount is provided with between spraying gun and well heater; The vacuum sensor be connected with this liquid flow rate controller is provided with in described breakdown of emulsion room.The gas-flow rate controller for controlling gas blow-out amount is provided with between air blowing device and bomb; Vacuum sensor in described breakdown of emulsion room is connected with this gas-flow rate controller.
Sampling Detection is carried out, moisture content :≤2PPM to the final processed oil obtained; Machinery acrobatics :≤2PPM; Dustiness (NAS1633) < NAS6-7; Relative to new oil viscosity rate rate < ± 5%, complete fitness for service standard.
The present embodiment 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.
Obviously, above-described embodiment of the present utility model is only for the utility model example is clearly described, and is not the restriction to embodiment of the present utility model.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here exhaustive without the need to also giving all embodiments.And these belong to connotation of the present utility model the apparent change of extending out or variation still belong to protection domain of the present utility model.
Claims (2)
1. a waste oil regeneration emulsion treater, comprise closed breakdown of emulsion room (41), it is characterized in that: also comprise the spraying gun (42) of the downward spraying be arranged in closed breakdown of emulsion room, resonance occurring source (43), air blowing device (44), bleeding point (45) and liquid circulation mouth (46) for upwards 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 described liquid circulation mouth is connected with the fluid inlet of recycle pump, 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 emulsion treater according to claim 1, is characterized in that: spraying gun comprises the fog nozzle (421) of the Jet with downward flow direction being arranged on top, breakdown of emulsion room; Resonance occurring source is arranged on the middle part of breakdown of emulsion room; Air blowing device is arranged on the bottom of breakdown of emulsion room; Bleeding point is arranged on the top of breakdown of emulsion room, and liquid circulation mouth is arranged on the bottom of breakdown of emulsion room; The liquid flow rate controller for controlling atomised jet amount is provided with between spraying gun and well heater; The vacuum sensor be connected with this liquid flow rate controller is provided with in described breakdown of emulsion room; The gas-flow rate controller for controlling gas blow-out amount is provided with between air blowing device and bomb; Vacuum sensor in described breakdown of emulsion room is connected with this gas-flow rate controller; Described resonance occurring source is ultrasonic generator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320894024.7U CN204079905U (en) | 2013-12-31 | 2013-12-31 | Waste oil regeneration emulsion treater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320894024.7U CN204079905U (en) | 2013-12-31 | 2013-12-31 | Waste oil regeneration emulsion treater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204079905U true CN204079905U (en) | 2015-01-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320894024.7U Expired - Fee Related CN204079905U (en) | 2013-12-31 | 2013-12-31 | Waste oil regeneration emulsion treater |
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| Country | Link |
|---|---|
| CN (1) | CN204079905U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103740401A (en) * | 2013-12-31 | 2014-04-23 | 宏秀电气有限公司 | Treatment method and demulsifier for waste oil regeneration |
-
2013
- 2013-12-31 CN CN201320894024.7U patent/CN204079905U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103740401A (en) * | 2013-12-31 | 2014-04-23 | 宏秀电气有限公司 | Treatment method and demulsifier for waste oil regeneration |
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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: 20150107 Termination date: 20151231 |
|
| EXPY | Termination of patent right or utility model |