CN204768701U - Waste oil recovery system - Google Patents
Waste oil recovery system Download PDFInfo
- Publication number
- CN204768701U CN204768701U CN201520474085.7U CN201520474085U CN204768701U CN 204768701 U CN204768701 U CN 204768701U CN 201520474085 U CN201520474085 U CN 201520474085U CN 204768701 U CN204768701 U CN 204768701U
- Authority
- CN
- China
- Prior art keywords
- sulfonation
- cylinder
- capping
- neutralization
- grease
- 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.)
- Expired - Fee Related
Links
Abstract
The utility model discloses a waste oil recovery system, including waste oil collecting pit, grease sulphonation unit and the grease neutrodyne system who communicates in proper order, grease neutrodyne system includes a neutralization section of thick bamboo, closing cap and material circulating pipe, the both ends of material circulating pipe are connected with the top of closing cap in with the bottom of a neutralization section of thick bamboo respectively, and all the inner chamber with a neutralization section of thick bamboo communicates, in set up with the top of closing cap in and the motor, set up in the neutralization section of thick bamboo install in with stirring vane in and the pivot, in pass with the output shaft of motor in with the closing cap in with and the pivot be connected, in with the closing cap on still be provided with at least one intake pipe and at least one neutralization section of thick bamboo gas outlet, the one end of intake pipe is arranged in the outside with the closing cap, during passing, the other end of intake pipe stretches into to the material of a neutralization section of thick bamboo in with the closing cap, the intake pipe is arranged in and the one end in the closing cap outside is provided with the heating device who is used for heating intake pipe gas. The utility model discloses can make waste oil obtain fine recovery.
Description
Technical field
The utility model relates to chemical machinery field, particularly relates to a kind of waste grease recovery system.
Background technology
At present, under normal conditions, urban catering, unit dining room, particularly chafing dish restaurant be mingled with the waste grease of waste residue, mostly be discharged into sewer, in discharge process, very easily caking blocks sewer, easily causes pipe explosion accident, and any discharge of waste grease is also that one is wasted greatly to resource.Known biodiesel is a kind of fuel of Gong the diesel engine use taking animal and plant fat as raw material production.Present subject matter is that raw material sources are on the high side, with catering trade produce waste grease just can solve this difficult problem, only have and set up effective used edible oil recovery and processing system, be only realization address this problem basic.
Utility model content
The purpose of this utility model is to provide a kind of waste grease recovery system to solve above technical problem.
For reaching this object, the utility model by the following technical solutions:
A kind of waste grease recovery system, comprise be communicated with successively waste grease collecting pit, two can carry out to grease the grease xanthator of sulfonation process and one can carry out neutralisation treatment grease neutralising arrangement to the grease of sulfonation;
Described grease neutralising arrangement comprises the neutralization cylinder of open top, for seal described neutralization cylinder uncovered in and capping and Matter Transfer pipe, the two ends of described Matter Transfer pipe respectively with the bottom of described neutralization cylinder and described in and the top of capping be connected, and all with the inner space of described neutralization cylinder, for the material constantly circulated in described neutralization cylinder, the outer cover of described Matter Transfer pipe is provided with the cartridge heater for heating material in described Matter Transfer pipe, during in the described and top of capping is arranged and motor, to arrange in described neutralization cylinder in being provided with and in stirring vane and rotating shaft, in described with the output shaft of motor through in described and capping with described in be connected with rotating shaft, at least one neutralization cylinder charging aperture for adding materials in described neutralization cylinder is provided with in described and in capping, at least one is also provided with for passing into the air inlet pipe of gas in the material to described neutralization cylinder and at least one makes the neutralization cylinder gas outlet that in neutralization cylinder, gas is discharged in described and in capping, one end of described air inlet pipe is arranged in described and outside that is capping, the other end of described air inlet pipe stretches in the material of described neutralization cylinder with capping in described, the bottom of described neutralization cylinder is provided with neutralization cylinder discharge nozzle, described neutralization cylinder discharge nozzle is provided with the first control valve, described air inlet pipe is arranged in described and one end that is closure skirt and is provided with heater for heating described air inlet pipe gas.
As the preferred technical scheme of one, the quantity of described Matter Transfer pipe is at least two.
Two are at least by the quantity arranging Matter Transfer pipe, on the one hand, the circulation neutralizing material in cylinder can be accelerated, on the other hand, when one of them Matter Transfer pipe goes wrong and can not make Matter Transfer, other Matter Transfer pipe still can circulate to material in neutralization cylinder, achieves the sustainability of Matter Transfer.In the present embodiment, the quantity of Matter Transfer pipe is two.
As the preferred technical scheme of one, the first temperature gauge for measuring temperature of charge in described neutralization cylinder is detachably installed in described and in capping, described first temperature gauge is arranged in the instrument of one end setting for showing temperature of charge that be described and closure skirt, and described first temperature gauge stretches in the material of described neutralization cylinder with capping in described away from the temperature sense end of described instrument.
As the preferred technical scheme of one, described heater comprises cylindrical shell, is provided with heater strip in described cylindrical shell, and the two ends of described heater strip extend the outside of described cylindrical shell through the sidewall of described cylindrical shell.
Preferably, described heater strip coiled coil is close to the inwall of described cylindrical shell in described cylindrical shell.
Preferably, the quantity of described neutralization cylinder charging aperture is four, be respectively neutralization cylinder water inlet, neutralization cylinder alkali inlet, neutralization cylinder grease import and neutralization cylinder to mix machine oil import, be respectively used to provide in described neutralization cylinder the assorted machine oil that water, NaOH, the grease of sulfonation and motor produce.
As the preferred technical scheme of one, described grease xanthator comprise open top sulfonation cylinder and for sealing the uncovered sulfonation capping of described sulfonation cylinder, the top of described sulfonation capping arranges sulfonation motor, the sulfonation rotating shaft being provided with sulfonation stirring vane is set in described sulfonation cylinder, the output shaft of described sulfonation motor is connected with described sulfonation rotating shaft through described sulfonation capping, described sulfonation capping is provided with at least one for the sulfonation cylinder charging aperture to filling in described sulfonation cylinder, the bottom of described sulfonation cylinder is provided with sulfonation cylinder discharge nozzle, described sulfonation cylinder discharge nozzle is provided with the second control valve, there is in the sidewall of described sulfonation cylinder the cavity interlayer for heating or cool material, the lateral wall of described sulfonation cylinder is provided with the heating steam import all communicated with cavity interlayer, cooling water inlet, first delivery port and the second delivery port, described heating steam import and the first delivery port are arranged at top and the bottom of sulfonation cylinder respectively, for jointly forming heat tunnel with described cavity interlayer, described cooling water inlet and described second delivery port are arranged at bottom and the top of described sulfonation cylinder respectively, for jointly forming cooling duct with described cavity interlayer, described sulfonation capping is provided with the second temperature gauge, the temperature survey end of described second temperature gauge is positioned at material, the signal output part of described second temperature gauge is positioned at the outside of described sulfonation capping, described heating steam import and described first delivery port arrange the 3rd control valve, described cooling water inlet and described second delivery port arrange the 4th control valve, the signal output part of described second temperature gauge, two described 3rd control valves and two described 4th control valves are all electrically connected with control device.
In whipping process, the temperature of material in sulfonation cylinder is detected by the second temperature gauge, communicate the temperature to control device, compared by control device, if material current temperature value is in the threshold value that control device sets, then illustrate that the temperature of material is suitable temperature, if the threshold value that material Current Temperatures sets higher than control device, then illustrate that the temperature of material is too high, at this moment, control device drives two the 4th control valves to open, cooling water is made to enter into the cavity interlayer of sulfonation cylinder, material in sulfonation cylinder is lowered the temperature, under making the temperature of material in sulfonation cylinder get back to suitable stirring, if the threshold value that in sulfonation cylinder, material Current Temperatures sets lower than control device, then exponent material temperature is spent low, this timed unit controls two the 3rd control valves and opens, steam is made to enter into the cavity interlayer of sulfonation cylinder, material in sulfonation cylinder is heated, under making the temperature of material in sulfonation cylinder get back to suitable stirring.It can thus be appreciated that, the utility model can regulate the temperature of material in sulfonation cylinder according to reaction needed, make sulfonating reaction can keep carrying out at a certain temperature, thus the sulfonating reaction energy gentleness of grease is controllably carried out, reduce the generation of side reaction as far as possible, make sulfonating reaction more thorough.
As the preferred technical scheme of one, described grease xanthator also comprises the vapor can for storing steam, the gas outlet of described vapor can and described heating steam inlet communication.
As the preferred technical scheme of one, described xanthator also comprises the steam raising plant for water being converted into steam, the water inlet of described steam raising plant is communicated with described first delivery port, and the gas outlet of described steam raising plant is communicated with the air inlet of described vapor can.
By arranging steam raising plant, making steam can be heat vaporized to the liquid of the rear liquefaction formation of sulfonation cylinder heating, because the liquid of steam liquefied also has certain temperature, therefore the energy manufacturing the required consumption of steam can be reduced.
As the preferred technical scheme of one, described steam raising plant comprises the heating shell of square sealing, the top board that described heating shell comprises base plate, be oppositely arranged with described base plate and four are for being connected the side plate of described top board and described base plate, the inner side of described base plate is provided with the dry combustion method pipe of S shape, the two ends of described dry combustion method pipe are connected with the power supply of described heating shell outside through described heating shell, the water inlet of described steam raising plant is arranged on a described side plate of described heating shell, and the gas outlet of described steam raising plant is arranged on the top board of described heating shell.
Preferably, described sulfonation cylinder charging aperture is two, is respectively sulfonation cylinder oil-in and sulfonation cylinder acid inlet, is respectively used to the concentrated sulfuric acid adding waste grease He can carry out sulfonation to waste grease in described sulfonation cylinder.
As the preferred technical scheme of one, each described sulfonation stirring vane and each described in and stirring vane edge on be evenly provided with breach.
By each sulfonation stirring vane and each in and several breach of edge of 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, each described sulfonation stirring vane all offers axis direction and the tangent angling hole of described sulfonation rotating shaft, the axis being parallel of described angling hole is in described sulfonation capping.
By offering parallel with sulfonation capping and tangent with the sulfonation rotating shaft angling hole of axis direction on each sulfonation stirring vane, the resistance that sulfonation stirring vane is subject to when stirring material can be reduced, sulfonation stirring vane not only can be made not yielding, also can reduce the energy consumption of sulfonation motor.
Contrast prior art, the beneficial effects of the utility model are: the utility model by and capping is arranged 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, make the material neutralized in cylinder be neutralized the cyclone mixing that also can be formed by gas while rotating shaft is stirred, further enhance 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, make gas can also heated material while formation cyclone mixing material, it is more abundant that the neutralization reaction being conducive to sulfonation grease and NaOH is carried out; By arranging Matter Transfer pipe, making the abundant mixed flow of material neutralizing different depth aspect in cylinder, being conducive to material and being sufficiently agitated; By the sheathed cartridge heater for material in heated material circulation pipe outside on Matter Transfer pipe, on the inwall making the grease in material to condense to adhere to Matter Transfer pipe, to avoid the passage of the grease blocking material circulation pipe in material.
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 waste grease recovery system described in the utility model embodiment one.
Fig. 2 is the structural representation of the grease xanthator described in the utility model embodiment one.
Fig. 3 is the structural representation of the grease neutralising arrangement described in the utility model embodiment.
Fig. 4 is the structural representation of the grease xanthator described in the utility model embodiment two.
Fig. 5 is the top view of the sulfonation stirring vane described in the utility model embodiment two.
In figure:
1, waste grease collecting pit;
2, grease xanthator; 21, sulfonation cylinder; 211, cavity interlayer; 212, heating steam import; 213, the first delivery port; 214, cooling water inlet; 215, the second delivery port; 216, sulfonation cylinder discharge nozzle; 22, sulfonation capping; 221, sulfonation cylinder oil-in; 222, sulfonation cylinder acid inlet; 223, the second temperature gauge; 23, sulfonation motor; 24, sulfonation rotating shaft; 241, sulfonation stirring vane; 2411, angling hole; 25, the second control valve; 26, the 3rd control valve; 27, the 4th control valve; 28, vapor can; 29, steam raising plant;
3, grease neutralising arrangement; 31, cylinder is neutralized; 32, in and capping; 321, cylinder water inlet is neutralized; 322, neutralize cylinder to mix machine oil import; 233, cylinder alkali inlet is neutralized; 234, the import of cylinder grease is neutralized; 325, cylinder gas outlet is neutralized; 33, in and motor; 34, in and rotating shaft; 341, in and stirring vane; 35, air inlet pipe; 36, cylindrical shell; 361, heater strip; 37, Matter Transfer pipe; 371, mechanical pump; 372, cartridge heater; 38, cylinder discharge nozzle is neutralized; 381, the first control valve; 39, the first temperature gauge; 391, instrument.
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 to Figure 3, present embodiment discloses a kind of waste grease recovery system, it comprise be communicated with successively waste grease collecting pit 1, can the grease xanthator 2 of sulfonation process be carried out to grease and the grease neutralising arrangement 3 of neutralisation treatment can be carried out the grease of sulfonation.
Grease neutralising arrangement 3 comprises the neutralization cylinder 31 of open top, for seal neutralization cylinder 31 uncovered in and capping 32 and Matter Transfer pipe 37, the two ends of Matter Transfer pipe 37 respectively with the bottom of neutralization cylinder 31 and in and the top of capping 32 be connected, and all with neutralization cylinder 31 inner space, for the material constantly circulated in neutralization cylinder 31, the outer cover of Matter Transfer pipe 37 is provided with the cartridge heater 372 for material in heated material circulation pipe 37, in and the top of capping 32 arrange in and motor 33, to arrange in neutralization cylinder 31 in being provided with and in stirring vane 341 and rotating shaft 34, in pass with the output shaft of motor 33 in capping 32 with in and rotating shaft 34 be connected, in and capping 32 is provided with at least one for the neutralization cylinder charging aperture that adds materials in neutralization cylinder 31, in and capping 32 is also provided with at least one for passing into the air inlet pipe 35 of gas in the material to neutralization cylinder 31 and at least one makes the neutralization cylinder gas outlet 325 that in neutralization cylinder 31, gas is discharged, one end of air inlet pipe 35 is arranged in the outside with capping 32, during the other end of air inlet pipe 35 passes and capping 32 stretch in the material of neutralization cylinder 31, the bottom of neutralization cylinder 31 is provided with neutralization cylinder discharge nozzle 38, neutralization cylinder discharge nozzle 38 is provided with the first control valve 381, air inlet pipe 35 is arranged in and one end outside capping 32 is provided with heater for heating air inlet pipe 35 gas.
By in and capping 32 is arranged at least one for pass in material the air inlet pipe 35 of gas and at least one make in and gas in cylinder 31 discharge in and cylinder gas outlet 325, make the material neutralized in cylinder 31 be neutralized the cyclone mixing that also can be formed by gas while rotating shaft 34 is stirred, further enhance the mixing effect to material in neutralization cylinder 31; By the one end being positioned at closure skirt in air inlet pipe 35, the heater for heating air inlet pipe 35 gas is set, gas in air inlet pipe 35 is just heated in entering with before the material in cylinder 31, make gas can also heated material while formation cyclone mixing material, it is more abundant that the neutralization reaction being conducive to sulfonation grease and NaOH is carried out; By arranging Matter Transfer pipe 37, making the abundant mixed flow of material neutralizing different depth aspect in cylinder 31, being conducive to material and being sufficiently agitated; By the sheathed cartridge heater 372 for material in heated material circulation pipe 37 outside on Matter Transfer pipe 37, on the inwall making the grease in material to condense to adhere to Matter Transfer pipe 37, to avoid the passage of the grease blocking material circulation pipe 37 in material.
The quantity of Matter Transfer pipe 37 is at least two.Two are at least by the quantity arranging Matter Transfer pipe 37, on the one hand, the circulation neutralizing material in cylinder 31 can be accelerated, on the other hand, when one of them Matter Transfer pipe 37 goes wrong and can not make Matter Transfer, other Matter Transfer pipe 37 still can circulate to material in neutralization cylinder 31, achieves the sustainability of Matter Transfer.In the present embodiment, the quantity of Matter Transfer pipe 37 is two.
In and capping 32 is detachably provided with for measuring the first temperature gauge 39 of temperature of charge in neutralization cylinder 31, first temperature gauge 39 is arranged in and one end outside capping 32 arrange instrument 391, first temperature gauge 39 for showing temperature of charge pass away from the temperature sense end of instrument 391 in and capping 32 stretch in the material of neutralization cylinder 31.
Heater comprises cylindrical shell 36, is provided with heater strip 361 in cylindrical shell 36, and the two ends of heater strip 361 extend the outside of cylindrical shell through the sidewall of cylindrical shell 36.
Preferably, heater strip 361 coiled coil is close to the inwall of cylindrical shell 36 in cylindrical shell 36.
Preferably, the quantity of neutralization cylinder charging aperture is four, be respectively neutralization cylinder water inlet 321, neutralization cylinder alkali inlet 233, neutralization cylinder grease import 234 and neutralization cylinder to mix machine oil import 322, be respectively used to provide in neutralization cylinder 31 the assorted machine oil that water, NaOH, the grease of sulfonation and motor produce.
Grease xanthator 2 comprise open top sulfonation cylinder 21 and for sealing the uncovered sulfonation capping 22 of sulfonation cylinder 21, the top of sulfonation capping 22 arranges sulfonation motor 23, the sulfonation rotating shaft 24 being provided with sulfonation stirring vane 241 is set in sulfonation cylinder 21, the output shaft of sulfonation motor 23 is connected with sulfonation rotating shaft 24 through sulfonation capping 22, sulfonation capping 22 is provided with at least one for the sulfonation cylinder charging aperture to filling in sulfonation cylinder 21, the bottom of sulfonation cylinder 21 is provided with sulfonation cylinder discharge nozzle 216, sulfonation cylinder discharge nozzle 216 is provided with the second control valve 25, there is in the sidewall of sulfonation cylinder 21 cavity interlayer 211 for heating or cool material, the lateral wall of sulfonation cylinder 21 is provided with the heating steam import 212 all communicated with cavity interlayer 211, cooling water inlet 214, first delivery port 213 and the second delivery port 215, heating steam import 212 and the first delivery port 213 are arranged at top and the bottom of sulfonation cylinder 21 respectively, for jointly forming heat tunnel with cavity interlayer 211, cooling water inlet 214 and the second delivery port 215 are arranged at bottom and the top of sulfonation cylinder 21 respectively, for jointly forming cooling duct with cavity interlayer 211, sulfonation capping 22 is provided with the second temperature gauge 223, the temperature survey end of the second temperature gauge 223 is positioned at material, the signal output part of the second temperature gauge 223 is positioned at the outside of sulfonation capping 22, heating steam import 212 and the first delivery port 213 arrange the 3rd control valve 26, cooling water inlet 214 and the second delivery port 215 arrange the 4th control valve 27, the signal output part of the second temperature gauge 223, two the 3rd control valves 26 and two the 4th control valves 27 are all electrically connected with control device.
In whipping process, the temperature of material in sulfonation cylinder 21 is detected by the second temperature gauge 223, communicate the temperature to control device, compared by control device, if material current temperature value is in the threshold value that control device sets, then illustrate that the temperature of material is suitable temperature, if the threshold value that material Current Temperatures sets higher than control device, then illustrate that the temperature of material is too high, at this moment, control device drives two the 4th control valves 27 to open, cooling water is made to enter into the cavity interlayer 211 of sulfonation cylinder 21, material in sulfonation cylinder 21 is lowered the temperature, under making the temperature of material in sulfonation cylinder 21 get back to suitable stirring, if the threshold value that in sulfonation cylinder 21, material Current Temperatures sets lower than control device, then exponent material temperature is spent low, this timed unit controls two the 3rd control valves 26 and opens, steam is made to enter into the cavity interlayer 211 of sulfonation cylinder 21, material in sulfonation cylinder 21 is heated, under making the temperature of material in sulfonation cylinder 21 get back to suitable stirring.It can thus be appreciated that, the utility model according to the temperature regulating material in sulfonation cylinder 21, can make sulfonating reaction can keep carrying out at a certain temperature, thus the sulfonating reaction energy gentleness of grease is controllably carried out, reduce the generation of side reaction as far as possible, make sulfonating reaction more thorough.
Grease xanthator 2 also comprises the vapor can 28 for storing steam, and the gas outlet of vapor can 28 is communicated with heating steam import 212.
Xanthator also comprises the steam raising plant 29 for water being converted into steam, and the water inlet of steam raising plant 29 is communicated with the first delivery port 213, and the gas outlet of steam raising plant 29 is communicated with the air inlet of vapor can 28.
By arranging steam raising plant 29, making steam after heating sulfonation cylinder 21, liquefy the liquid formed can be heat vaporized, because the liquid of steam liquefied also has certain temperature, therefore can reduce the energy manufacturing the required consumption of steam.
In the present embodiment, steam raising plant 29 comprises the heating shell of square sealing, the top board that heating shell comprises base plate, be oppositely arranged with base plate and four are for being connected the side plate of top board and base plate, the inner side of base plate is provided with the dry combustion method pipe of S shape, the two ends of dry combustion method pipe are connected with the power supply of heating shell outside through heating shell, the water inlet of steam raising plant 29 is arranged on a side plate of heating shell, and the gas outlet of steam raising plant 29 is arranged on the top board of heating shell.
Preferably, sulfonation cylinder charging aperture is two, is respectively sulfonation cylinder oil-in 221 and sulfonation cylinder acid inlet 222, is respectively used to the concentrated sulfuric acid adding waste grease He can carry out sulfonation to waste grease in sulfonation cylinder 21.
Waste grease recovery system of the present utility model comprises following procedure of processing:
1, waste grease is recovered in waste grease collecting pit 1;
2, waste grease in waste grease collecting pit 1 is fed through in first sulfonation cylinder 21, and in first sulfonation cylinder 21, add the concentrated sulfuric acid simultaneously, after adding material, start sulfonation motor 23, sulfonation motor 23 drives sulfonation rotating shaft 24 to rotate with sulfonation stirring vane 241, to stir the material in sulfonation bucket, in whipping process, if the threshold value that material Current Temperatures sets higher than control device, then illustrate that the temperature of material is too high, at this moment, control device drives two the 4th control valves 27 to open, cooling water is made to enter into the cavity interlayer 211 of sulfonation cylinder 21, material in sulfonation cylinder 21 is lowered the temperature, under making the temperature of material in sulfonation cylinder 21 get back to suitable stirring, if the threshold value that in sulfonation cylinder 21, material Current Temperatures sets lower than control device, then exponent material temperature is spent low, this timed unit controls two the 3rd control valves 26 and opens, steam is made to enter into the cavity interlayer 211 of sulfonation cylinder 21, material in sulfonation cylinder 21 is heated, under making the temperature of material in sulfonation cylinder 21 get back to suitable stirring.
3, when waste grease is in sulfonation cylinder 21 after sulfonation, the waste grease of sulfonation is fed through in neutralization cylinder 31 by the sulfonation cylinder discharge nozzle 216 of sulfonation cylinder 21, in neutralization cylinder 31, add NaOH simultaneously, the assorted machine oil that power and water machine produces, and be drawn into emulsifying kettle gradually, after adding material, with motor 33 in startup, in and motor 33 drive in and rotating shaft 34 with in and stirring vane 341 rotate, to stir the material in neutralization cylinder 31, and make emulsifying materials form oil emulsion, start mechanical pump 371 simultaneously, and in material, pass into gas by air inlet pipe 25, mechanical pump 371 makes the material neutralized in cylinder 31 be transported to the top of sulfonation cylinder 21 from the bottom of sulfonation cylinder 21, to realize the abundant mixed flow of material neutralizing different depth aspect in cylinder 31, the gas passed in material then orders about material and forms eddy flow, and then the material stirring effect in sulfonation cylinder 21 is strengthened further.
4, after neutralizing the complete emulsification of material in cylinder 31, the oil emulsion in neutralization cylinder 31 is taken out, and packs.
Embodiment two:
As shown in Figure 4 and Figure 5, the difference of the present embodiment and embodiment one is: each sulfonation stirring vane 241 and each in and stirring vane 341 edge on be evenly provided with breach.
By each sulfonation stirring vane 241 and each in and several breach of edge of stirring vane 341, stirring vane 341 well can be cut becoming in material the grease of block, being stirred to accelerate material.
Each sulfonation stirring vane 241 all offers axis direction and the tangent angling hole 2411 of sulfonation rotating shaft 24, the axis being parallel of angling hole 2411 is in sulfonation capping 22.
By offering parallel with sulfonation capping 22 and tangent with sulfonation rotating shaft 24 angling hole 2411 of axis direction on each sulfonation stirring vane 241, the resistance that sulfonation stirring vane 241 is subject to when stirring material can be reduced, sulfonation stirring vane 241 not only can be made not yielding, also can reduce the energy consumption of sulfonation motor 23.
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 (10)
1. a waste grease recovery system, is characterized in that, comprise be communicated with successively waste grease collecting pit, can the grease xanthator of sulfonation process be carried out to grease and the grease neutralising arrangement of neutralisation treatment can be carried out the grease of sulfonation;
Described grease neutralising arrangement comprises the neutralization cylinder of open top, for seal described neutralization cylinder uncovered in and capping and Matter Transfer pipe, the two ends of described Matter Transfer pipe respectively with the bottom of described neutralization cylinder and described in and the top of capping be connected, and all with the inner space of described neutralization cylinder, for the material constantly circulated in described neutralization cylinder, the outer cover of described Matter Transfer pipe is provided with the cartridge heater for heating material in described Matter Transfer pipe, during in the described and top of capping is arranged and motor, to arrange in described neutralization cylinder in being provided with and in stirring vane and rotating shaft, in described with the output shaft of motor through in described and capping with described in be connected with rotating shaft, at least one neutralization cylinder charging aperture for adding materials in described neutralization cylinder is provided with in described and in capping, at least one is also provided with for passing into the air inlet pipe of gas in the material to described neutralization cylinder and at least one makes the neutralization cylinder gas outlet that in neutralization cylinder, gas is discharged in described and in capping, one end of described air inlet pipe is arranged in described and outside that is capping, the other end of described air inlet pipe stretches in the material of described neutralization cylinder with capping in described, the bottom of described neutralization cylinder is provided with neutralization cylinder discharge nozzle, described neutralization cylinder discharge nozzle is provided with the first control valve, described air inlet pipe is arranged in described and one end that is closure skirt and is provided with heater for heating described air inlet pipe gas.
2. a kind of waste grease recovery system according to claim 1, is characterized in that, the quantity of described Matter Transfer pipe is at least two.
3. a kind of waste grease recovery system according to claim 1, it is characterized in that, the first temperature gauge for measuring temperature of charge in described neutralization cylinder is detachably installed in described and in capping, described first temperature gauge is arranged in the instrument of one end setting for showing temperature of charge that be described and closure skirt, and described first temperature gauge stretches in the material of described neutralization cylinder with capping in described away from the temperature sense end of described instrument.
4. a kind of waste grease recovery system according to claim 1, it is characterized in that, described heater comprises cylindrical shell, is provided with heater strip in described cylindrical shell, and the two ends of described heater strip extend the outside of described cylindrical shell through the sidewall of described cylindrical shell.
5. a kind of waste grease recovery system according to claim 1, it is characterized in that, described grease xanthator comprise open top sulfonation cylinder and for sealing the uncovered sulfonation capping of described sulfonation cylinder, the top of described sulfonation capping arranges sulfonation motor, the sulfonation rotating shaft being provided with sulfonation stirring vane is set in described sulfonation cylinder, the output shaft of described sulfonation motor is connected with described sulfonation rotating shaft through described sulfonation capping, described sulfonation capping is provided with at least one for the sulfonation cylinder charging aperture to filling in described sulfonation cylinder, the bottom of described sulfonation cylinder is provided with sulfonation cylinder discharge nozzle, described sulfonation cylinder discharge nozzle is provided with the second control valve, there is in the sidewall of described sulfonation cylinder the cavity interlayer for heating or cool material, the lateral wall of described sulfonation cylinder is provided with the heating steam import all communicated with cavity interlayer, cooling water inlet, first delivery port and the second delivery port, described heating steam import and the first delivery port are arranged at top and the bottom of sulfonation cylinder respectively, for jointly forming heat tunnel with described cavity interlayer, described cooling water inlet and described second delivery port are arranged at bottom and the top of described sulfonation cylinder respectively, for jointly forming cooling duct with described cavity interlayer, described sulfonation capping is provided with the second temperature gauge, the temperature survey end of described second temperature gauge is positioned at material, the signal output part of described second temperature gauge is positioned at the outside of described sulfonation capping, described heating steam import and described first delivery port arrange the 3rd control valve, described cooling water inlet and described second delivery port arrange the 4th control valve, the signal output part of described second temperature gauge, two described 3rd control valves and two described 4th control valves are all electrically connected with control device.
6. a kind of waste grease recovery system according to claim 5, is characterized in that, described grease xanthator also comprises the vapor can for storing steam, the gas outlet of described vapor can and described heating steam inlet communication.
7. a kind of waste grease recovery system according to claim 6, it is characterized in that, described xanthator also comprises the steam raising plant for water being converted into steam, the water inlet of described steam raising plant is communicated with described first delivery port, and the gas outlet of described steam raising plant is communicated with the air inlet of described vapor can.
8. a kind of waste grease recovery system according to claim 7, it is characterized in that, described steam raising plant comprises the heating shell of square sealing, described heating shell comprises base plate, the top board be oppositely arranged with described base plate and four are for being connected the side plate of described top board and described base plate, the inner side of described base plate is provided with the dry combustion method pipe of S shape, the two ends of described dry combustion method pipe are connected with the power supply of described heating shell outside through described heating shell, the water inlet of described steam raising plant is arranged on a described side plate of described heating shell, the gas outlet of described steam raising plant is arranged on the top board of described heating shell.
9. a kind of waste grease recovery system according to claim 5, is characterized in that, each described sulfonation stirring vane and each described in and stirring vane edge on be evenly provided with breach.
10. a kind of waste grease recovery system according to claim 5, is characterized in that, each described sulfonation stirring vane all offers axis direction and the tangent angling hole of described sulfonation rotating shaft, the axis being parallel of described angling hole is in described sulfonation capping.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520474085.7U CN204768701U (en) | 2015-07-02 | 2015-07-02 | Waste oil recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520474085.7U CN204768701U (en) | 2015-07-02 | 2015-07-02 | Waste oil recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204768701U true CN204768701U (en) | 2015-11-18 |
Family
ID=54508832
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520474085.7U Expired - Fee Related CN204768701U (en) | 2015-07-02 | 2015-07-02 | Waste oil recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204768701U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107619717A (en) * | 2017-10-16 | 2018-01-23 | 罗志江 | A kind of waste grease equipment |
| CN107828516A (en) * | 2017-11-06 | 2018-03-23 | 叶丛杰 | A kind of waste grease device |
| CN107474965B (en) * | 2017-10-11 | 2018-10-16 | 竺裕东 | A kind of waste grease collecting device |
| CN109569403A (en) * | 2018-12-07 | 2019-04-05 | 皇氏集团湖南优氏乳业有限公司 | A kind of closed milk mixing tank of constant temperature |
-
2015
- 2015-07-02 CN CN201520474085.7U patent/CN204768701U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107474965B (en) * | 2017-10-11 | 2018-10-16 | 竺裕东 | A kind of waste grease collecting device |
| CN107619717A (en) * | 2017-10-16 | 2018-01-23 | 罗志江 | A kind of waste grease equipment |
| CN107828516A (en) * | 2017-11-06 | 2018-03-23 | 叶丛杰 | A kind of waste grease device |
| CN109569403A (en) * | 2018-12-07 | 2019-04-05 | 皇氏集团湖南优氏乳业有限公司 | A kind of closed milk mixing tank of constant temperature |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204768701U (en) | Waste oil recovery system | |
| CN103464452B (en) | For the fermentation dried device of kitchen castoff process | |
| CN204554904U (en) | A kind of combustion gas digester with water tank | |
| CN205838958U (en) | A kind of soap leftover pieces secondary operations equipment | |
| CN108201830B (en) | Reation kettle is used in lubricating oil production convenient to it is clean | |
| CN202813413U (en) | Stirring-type ultrasonic emulsification on-line combustion device | |
| CN102310072A (en) | Garbage treatment device | |
| CN205361349U (en) | Alkali fusion cauldron with steam heating device | |
| CN205470827U (en) | Add fever type soybean phospholipil oil storage device | |
| CN204768702U (en) | A neutrodyne system for oil recovery | |
| CN204768699U (en) | A sulphonation unit for oil recovery | |
| CN106417038A (en) | Double-screw cheese stretching machine | |
| CN206309453U (en) | Exhaust heat distribution utilizes system | |
| CN107117614B (en) | Leak-proof environment-friendly vulcanizing device in carbon disulfide production | |
| CN106393365B (en) | A kind of bamboo wood intelligence boiling melded system | |
| CN204908067U (en) | PVC gloves isolating agent groove and cooling system | |
| CN211274624U (en) | Soapstock oil foot pretreatment system | |
| CN202180076U (en) | Garbage disposal device | |
| CN203403078U (en) | Automatic scraping plate type animal grease refining machine | |
| CN204768700U (en) | A neutrodyne system for oil recovery | |
| CN202773939U (en) | Integrated type rosin hollowware with constant temperature | |
| CN209098592U (en) | A kind of biofuel oil deodorization device | |
| CN206101508U (en) | Soybean soaking jar | |
| CN206452949U (en) | A kind of double helix cheese stretching-machine | |
| CN202410657U (en) | Reaction kettle for preparing vanadium liquid and heating and cooling structure of reaction kettle |
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 |