CN204768702U - A neutrodyne system for oil recovery - Google Patents
A neutrodyne system for oil recovery Download PDFInfo
- Publication number
- CN204768702U CN204768702U CN201520474098.4U CN201520474098U CN204768702U CN 204768702 U CN204768702 U CN 204768702U CN 201520474098 U CN201520474098 U CN 201520474098U CN 204768702 U CN204768702 U CN 204768702U
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- China
- Prior art keywords
- air inlet
- inlet pipe
- oil recovery
- neutralization
- capping
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- 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.)
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Abstract
The utility model discloses a neutrodyne system for oil recovery, it includes a neutralization section of thick bamboo and closing cap, the top of closing cap sets up the motor, set up the pivot of installing stirring vane in the neutralization section of thick bamboo, the output shaft and the pivot of motor are connected, set up at least one feed inlet on the closing cap, it is arranged in letting in gaseous intake pipe and at least one gas outlet to the material still to set up at least one on the closing cap, the one end of intake pipe is located the outside of closing cap, the other end of intake pipe passes the closing cap and stretches into to the material of a neutralization section of thick bamboo in, the bottom of a neutralization section of thick bamboo sets up the discharging pipe, the one end setting that the intake pipe lies in the closing cap outside is used for the heating device with the hot gas. The utility model discloses make the interior material of a neutralization section of thick bamboo still can be stirred by gas formation's whirl in by the pivot stirring, further strengthened the stirring effect to material in the neutralization section of thick bamboo, in addition through set up heating device in the intake pipe for gas can also improve the temperature of material when forming whirl stirring material, can promote the neutralization reaction of grease.
Description
Technical field
The utility model relates to chemical machinery field, particularly relates to a kind of neutralising arrangement for oil recovery.
Background technology
Waste biomass grease refers to the animal and plant fat that can not eat again that food production or marketing unit produces in production management process, comprise: the grease that can not eat again that the vegetable and animals oils that can not eat again, catering trade waste grease and the oil-containing waste water that produce after grease uses produce after oil water separator or oil interceptor are separated, these waste greases not only have a strong impact on city appearance environment and civil plantation, but also can cause large-area water pollution.In addition, if the vegetable oil excessively used is not processed, continuing to use as edible oil, bringing great harm by giving the healthy of people.
Exist a kind of for reclaiming waste biomass grease system in prior art, this system comprises two are carried out sulfonation successively xanthator and a neutralising arrangement neutralized by the waste biomass grease through oversulfonate to waste biomass grease, wherein, neutralising arrangement comprises neutralization cylinder, existing neutralization cylinder is generally stirred the material in it by a rotating shaft with rectangular stirring vane, do not have other ancillary method, mixing effect is poor, easily causes in the material in cylinder with insufficient.
Utility model content
The purpose of this utility model is to provide a kind of neutralising arrangement for oil recovery to solve above technical problem.
For reaching this object, the utility model by the following technical solutions:
A kind of neutralising arrangement for oil recovery, comprise the neutralization cylinder of open top and the uncovered capping for sealing described neutralization cylinder, the top of described capping arranges motor, the rotating shaft being provided with stirring vane is set in described neutralization cylinder, the output shaft of described motor is connected with described rotating shaft through described capping, described capping is provided with at least one charging aperture, described capping is also provided with at least one for passing into the air inlet pipe of gas in the material to neutralization cylinder and at least one makes the gas outlet that in neutralization cylinder, gas is discharged, one end of described air inlet pipe is positioned at the outside of described capping, the other end of described air inlet pipe stretches in the material of described neutralization cylinder through described capping, the bottom of described neutralization cylinder is provided with discharge nozzle, described discharge nozzle is provided with control valve, one end that described air inlet pipe is positioned at described closure skirt is provided with the heater for heating described air inlet pipe gas.
As the preferred technical scheme of one, described heater comprises cartridge heater, is provided with heater strip in described cartridge heater, and the two ends of described heater strip extend the outside of described cartridge heater through the sidewall of described cartridge heater.
As the preferred technical scheme of one, described heater strip coiled coil is in described cartridge heater and be close to the inwall of described cartridge heater.
As the preferred technical scheme of one, one end that described air inlet pipe stretches into material in described neutralization cylinder arranges tapered pipe of dehiscing, described in the dehisce small end of pipe be connected with described air inlet pipe.
In stretching in air inlet pipe, tapered pipe of dehiscing is set with one end of material in cylinder, the contact area of gas and material can be made to increase further, thus more material in neutralization cylinder is heated, carry out neutralization reaction more fully to make the bronsted lowry acids and bases bronsted lowry in material.
As the preferred technical scheme of one, described in the dehisce small end of pipe be threaded with described air inlet pipe.Be threaded with air inlet pipe by the small end arranging pipe of dehiscing, be convenient to staff changes corresponding size pipe of dehiscing according to the actual stirring state of material.
As the preferred technical scheme of one, the marginal position of each described stirring vane offers several breach.
By several breach of edge at each stirring vane, stirring vane well can be cut becoming in material the grease of block, being stirred to accelerate material.
As the preferred technical scheme of one, some described breach are uniformly distributed along the edge of described stirring vane.
As the preferred technical scheme of one, the quantity of described charging aperture is three, is respectively water inlet, alkali inlet and oil-in, and be respectively used to provides water, NaOH and grease in described neutralization cylinder.
As the preferred technical scheme of one, in described discharge nozzle, be provided with screen pack.
By arranging screen pack in discharge nozzle, can make in neutralization cylinder, the foreign material that recovery waste biomass grease band is come in be filtered.
Contrast prior art, the beneficial effects of the utility model are: the utility model by arrange in capping at least one for pass in material the air inlet pipe of gas and at least one make in and gas in the cylinder gas outlet of discharging, the cyclone mixing that material in neutralization cylinder also can be formed by gas while being stirred by rotating shaft, further enhances the mixing effect to material in neutralization cylinder; By the one end being positioned at closure skirt in air inlet pipe, the heater for heating air inlet pipe gas is set, the thermal current formed is also heating material in cylinder while promotion dispersed with stirring, and it is more abundant that the neutralization reaction being conducive to sulfonation grease and NaOH is carried out.
Accompanying drawing explanation
According to drawings and embodiments the utility model is described in further detail below.
Fig. 1 is the structural representation of a kind of neutralising arrangement for oil recovery described in the utility model embodiment.
In figure:
1, cylinder is neutralized; 2, capping; 21, water inlet; 22, oil-in; 23, alkali inlet; 24, gas outlet; 3, motor; 4, rotating shaft; 41, stirring vane; 5, air inlet pipe; 6, cartridge heater; 61, heater strip; 7, dehisce to manage; 8, discharge nozzle; 81, screen pack; 82, control valve.
Detailed description of the invention
The technical solution of the utility model is further illustrated by detailed description of the invention below in conjunction with accompanying drawing.
Embodiment one:
As shown in Figure 1, the utility model discloses a kind of neutralising arrangement for oil recovery, comprise the neutralization cylinder 1 of open top and the uncovered capping 2 for sealing neutralization cylinder 1, the top of capping 2 arranges motor 3, in neutralization cylinder 1, the rotating shaft 4 being provided with stirring vane 41 is set, the output shaft of motor 3 is connected with rotating shaft 4 through capping 2, capping 2 is provided with at least one charging aperture, capping 2 is also provided with at least one for passing into the air inlet pipe 5 of gas in the material to neutralization cylinder 1 and at least one makes the gas outlet 24 that in neutralization cylinder 1, gas is discharged, one end of air inlet pipe 5 is positioned at the outside of capping 2, the other end of air inlet pipe 5 stretches to through capping 2 in the material of neutralization cylinder 1, the bottom of neutralization cylinder 1 is provided with discharge nozzle 8, discharge nozzle 8 is provided with control valve 82, air inlet pipe 5 one end be positioned at outside capping 2 is provided with the heater for heating air inlet pipe 5 gas.
Concrete, rotating shaft 4 with stirring vane 41 in and material in cylinder 1 carry out stirring simultaneously, in the material in neutralization cylinder 1, gas is passed into by air inlet pipe 5, the liquid material inside that gas orders about in neutralization cylinder 1 forms eddy flow, it can thus be appreciated that, by arrange in capping 2 at least one for pass in material the air inlet pipe 5 of gas and at least one make in and gas in cylinder 1 gas outlet 24 of discharging, make the cyclone mixing that the material in neutralization cylinder 1 also can be formed by gas while being stirred by rotating shaft 4, further enhance the mixing effect to material in neutralization cylinder 1, by the one end be positioned in air inlet pipe 5 outside capping 2, the heater for heating air inlet pipe 5 gas is set, the thermal current formed is also heating material in cylinder while promotion dispersed with stirring, and it is more abundant that the neutralization reaction being conducive to sulfonation grease and NaOH is carried out.
It will be appreciated by persons skilled in the art that the device of this programme not only may be used for the recovery of waste grease, other liquid reclaimed is applicable to the utility model too, such as assorted machine oil.
Heater comprises cartridge heater 6, is provided with heater strip 61 in cartridge heater 6, and the two ends of heater strip 61 extend the outside of cartridge heater 6 through the sidewall of cartridge heater 6.
In the present embodiment, heater strip 61 coiled coil is close to the inwall of cartridge heater 6 in cartridge heater 6.
One end that air inlet pipe 5 stretches into material in neutralization cylinder 1 arranges tapered pipe 7 of dehiscing, and the small end of pipe 7 of dehiscing is connected with air inlet pipe 5.
In stretching in air inlet pipe 5, tapered pipe 7 of dehiscing is set with one end of material in cylinder 1, the contact area of gas and material can be made to increase further, thus more material in neutralization cylinder 1 is heated, carry out neutralization reaction more fully to make the bronsted lowry acids and bases bronsted lowry in material.
The dehisce small end of pipe 7 is threaded with air inlet pipe 5.Be threaded with air inlet pipe 5 by the small end arranging pipe 7 of dehiscing, be convenient to staff changes corresponding size pipe 7 of dehiscing according to the actual stirring state of material.
The quantity of charging aperture is three, is respectively water inlet 21, alkali inlet 23 and oil-in 22, and be respectively used to provides water, NaOH and grease in neutralization cylinder 1.
Screen pack 81 is provided with in discharge nozzle 8.By arranging screen pack 81 in discharge nozzle 8, can make in neutralization cylinder 1, the foreign material that recovery waste biomass grease band is come in be filtered.
Embodiment two:
The difference of the present embodiment and embodiment one is: the marginal position of each stirring vane 41 offers several breach.By several breach of edge at each stirring vane 41, stirring vane 41 well can be cut becoming in material the grease of block, being stirred to accelerate material.
Some breach are uniformly distributed along the edge of stirring vane 41.
Below know-why of the present utility model is described in conjunction with specific embodiments.These describe just in order to explain principle of the present utility model, and can not be interpreted as the restriction to the utility model protection domain by any way.Based on explanation herein, those skilled in the art does not need to pay performing creative labour can associate other detailed description of the invention of the present utility model, and these modes all will fall within protection domain of the present utility model.
Claims (9)
1. the neutralising arrangement for oil recovery, it is characterized in that, comprise the neutralization cylinder of open top and the uncovered capping for sealing described neutralization cylinder, the top of described capping arranges motor, the rotating shaft being provided with stirring vane is set in described neutralization cylinder, the output shaft of described motor is connected with described rotating shaft through described capping, described capping is provided with at least one charging aperture, described capping is also provided with at least one for passing into the air inlet pipe of gas in the material to neutralization cylinder and at least one makes the gas outlet that in neutralization cylinder, gas is discharged, one end of described air inlet pipe is positioned at the outside of described capping, the other end of described air inlet pipe stretches in the material of described neutralization cylinder through described capping, the bottom of described neutralization cylinder is provided with discharge nozzle, described discharge nozzle is provided with control valve, one end that described air inlet pipe is positioned at described closure skirt is provided with the heater for heating described air inlet pipe gas.
2. a kind of neutralising arrangement for oil recovery according to claim 1, it is characterized in that, described heater comprises cartridge heater, is provided with heater strip in described cartridge heater, and the two ends of described heater strip extend the outside of described cartridge heater through the sidewall of described cartridge heater.
3. a kind of neutralising arrangement for oil recovery according to claim 2, is characterized in that, described heater strip coiled coil is in described cartridge heater and be close to the inwall of described cartridge heater.
4. a kind of neutralising arrangement for oil recovery according to claim 1, is characterized in that, one end that described air inlet pipe stretches into material in described neutralization cylinder arranges tapered pipe of dehiscing, described in the dehisce small end of pipe be connected with described air inlet pipe.
5. a kind of neutralising arrangement for oil recovery according to claim 4, it is characterized in that, the small end of described pipe of dehiscing is threaded with described air inlet pipe, be threaded with air inlet pipe by the small end arranging pipe of dehiscing, be convenient to staff changes corresponding size pipe of dehiscing according to the actual stirring state of material.
6. a kind of neutralising arrangement for oil recovery according to claim 5, is characterized in that, the marginal position of each described stirring vane offers several breach.
7. a kind of neutralising arrangement for oil recovery according to claim 6, is characterized in that, some described breach are uniformly distributed along the edge of described stirring vane.
8. a kind of neutralising arrangement for oil recovery according to claim 4, is characterized in that, the quantity of described charging aperture is three, is respectively water inlet, alkali inlet and oil-in, and be respectively used to provides water, NaOH and grease in described neutralization cylinder.
9. a kind of neutralising arrangement for oil recovery according to claim 1, is characterized in that, be provided with screen pack in described discharge nozzle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520474098.4U CN204768702U (en) | 2015-07-02 | 2015-07-02 | A neutrodyne system for oil recovery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520474098.4U CN204768702U (en) | 2015-07-02 | 2015-07-02 | A neutrodyne system for oil recovery |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204768702U true CN204768702U (en) | 2015-11-18 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520474098.4U Expired - Fee Related CN204768702U (en) | 2015-07-02 | 2015-07-02 | A neutrodyne system for oil recovery |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204768702U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106497672A (en) * | 2016-11-10 | 2017-03-15 | 贵州省湄潭县永隆粮油有限责任公司 | Rapeseed oil extraction technique |
| CN112159704A (en) * | 2020-09-27 | 2021-01-01 | 安徽凯奥新能源股份有限公司 | Regeneration preparation method of waste transformer oil |
-
2015
- 2015-07-02 CN CN201520474098.4U patent/CN204768702U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106497672A (en) * | 2016-11-10 | 2017-03-15 | 贵州省湄潭县永隆粮油有限责任公司 | Rapeseed oil extraction technique |
| CN112159704A (en) * | 2020-09-27 | 2021-01-01 | 安徽凯奥新能源股份有限公司 | Regeneration preparation method of waste transformer oil |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151118 Termination date: 20180702 |