CN202226741U - Kitchen waste disposal system - Google Patents
Kitchen waste disposal system Download PDFInfo
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- CN202226741U CN202226741U CN2011203211504U CN201120321150U CN202226741U CN 202226741 U CN202226741 U CN 202226741U CN 2011203211504 U CN2011203211504 U CN 2011203211504U CN 201120321150 U CN201120321150 U CN 201120321150U CN 202226741 U CN202226741 U CN 202226741U
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Abstract
The utility model discloses a kitchen waste disposal system which comprises a storage device, a separating device and a collecting device that are sequentially connected, wherein the storage device is used for receiving and filtering kitchen waste so as to obtain filtered mixture and transmitting the filtered mixture into the separating device; the separating device is used for separating oil fat out from the filter mixture and transmitting the oil fat into the collecting device; and the collecting device (10) is used for collecting the oil fat coming from the separating device. After the technical scheme is adopted, the kitchen waste disposal system utilizes the independent separating device to disposal the kitchen waste so as to lead the oil fat separated out from the kitchen waste to be recovered and stored. The method is high in treatment efficiency, stable in work and suitable for large-scale kitchen waste disposal, and the oil fat obtained by the method is higher in quality.
Description
Technical field
The utility model relates to the changing food waste treatment system, particularly, relates to a kind of efficiently treatment system of processing utensil rubbishes.
Background technology
Changing food waste need be separated grease in innocent treatment procedure from changing food waste sewage, as the raw materials for production of biofuel or Chemicals.Adopting more treatment process at present is natural sedimentation top and bottom process and oil removal groove aeration, and these two kinds of methods device commonly used is respectively oil removal groove and air-flotation type grease trap.
Oil removal groove and air-flotation type grease trap are similar; All be different according to the proportion of oil, water and solid residue; Leave standstill or assist air supporting through waste water, make the layering in the pond of oil, water and solid residue, through oil scraping plate frizing or hydraulic pressure lift the oil slick on upper strata is taken away again; The water in middle layer flows away through pipeline, the artificial or removing automatically that the solid residue of bottom can be regular.
The oil removal groove is to utilize the proportion of oil, water and solid residue different; Oil-water mixture introduced in a series of oil removal grooves leave standstill; After for some time, oil, water and solid residue be the meeting layering in the pond, can the oil slick on upper strata be taken away through oil scraping plate like this; The water in middle layer flows away through pipeline, and the solid residue of bottom can artificially termly be removed.
The air-flotation type grease trap is through oil-water mixture being introduced the grease trap water tank; Produce a large amount of micro-bubbles through microbubble generator; Accelerate the velocity of separation of grease and water, sewage is in the bottom and flows away, and grease floats on the grease trap water tank upper and in hydraulic pressure lift is spilled over to fuel tank.
But above-mentioned conventional treatment method can't guarantee oil quality, and processing efficiency is lower, and job insecurity is difficult to adapt to the needs that large-scale changing food waste is handled.
The utility model content
The purpose of the utility model provides a kind of changing food waste treatment system, and this treatment system can be stablized and efficiently changing food waste handled.
To achieve these goals, the utility model provides a kind of changing food waste treatment system, and wherein, this treatment system comprises storing unit, tripping device and the collection device that connects successively, wherein,
Said storing unit is used to receive changing food waste and filters and obtains filtering mixt, and this filtering mixt is sent to said tripping device;
Said tripping device is used for isolating grease from filtering mixt, and this grease is sent to said collection device;
Said collection device is used to collect the grease that comes from said tripping device.
Preferably; Said storing unit comprises first storage pool and second storage pool; Said first storage pool is used to receive changing food waste and said changing food waste is filtered and obtains the primary filter mixture; And this primary filter mixture is pumped in said second storage pool, said second storage pool is used to receive said primary filter mixture and said primary filter mixture is filtered and obtains filtering mixt.
Preferably, said treatment system also comprises squeezing machine, and this squeezing machine is that second storage pool provides the primary filter mixture.
Preferably, be provided with stirrer in said first storage pool and/or said second storage pool.
Preferably, said tripping device comprises horizontal centrifuge and the disk centrifugal separator that connects successively, and this horizontal centrifuge is used for isolating oil-water mixture from said filtering mixt, and this disk centrifugal separator is used for isolating grease from said oil-water mixture.
Preferably; Said treatment system also comprises apparatus for temporary storage; This apparatus for temporary storage links to each other with the inlet of said disk centrifugal separator with first outlet of said horizontal centrifuge; This apparatus for temporary storage is used to store the isolated said oil-water mixture of said horizontal centrifuge, and said oil-water mixture is pumped in the said disk centrifugal separator.
Preferably; Said treatment system also comprises first heating tank that is used for to said filtering mixt heating; This first heating tank comprises first fluid inlet, first liquid outlet and first heating unit; Said first fluid inlet links to each other with said storing unit, and said first liquid outlet links to each other with the inlet of said horizontal centrifuge, and said first heating unit is used for to said filtering mixt heating.
Preferably, said first heating unit is a steam coils.
Preferably; Said first heating tank also comprises first liquid spill-way and the first discharge unit; This first discharge unit detects the liquid level of the said filtering mixt in said first heating tank; After this liquid level reached preset value, said first discharge unit control stopped the said filtering mixt of pumping in said first heating tank, and unnecessary said filtering mixt is transmitted back in the said storing unit.
Preferably; Said treatment system also comprises second heating tank that is used for to said oil-water mixture heating; This second heating tank comprises second fluid inlet, second liquid outlet and second heating unit; Said second fluid inlet links to each other with first outlet of said horizontal centrifuge, and said second liquid outlet links to each other with the inlet of said disk centrifugal separator, and said second heating unit is used for to said oil-water mixture heating.
Preferably; Said treatment system also comprises second heating tank that is used for to said oil-water mixture heating; This second heating tank comprises second fluid inlet, second liquid outlet and second heating unit; Said second fluid inlet links to each other with said apparatus for temporary storage, and said second liquid outlet links to each other with the inlet of said disk centrifugal separator, and said second heating unit is used for to said oil-water mixture heating.
Preferably, said second heating unit is a steam coils.
Preferably; Said second heating tank also comprises second liquid spill-way and the second discharge unit; This second discharge unit detects the liquid level of the said oil-water mixture in said second heating tank; After this liquid level reached preset value, said second discharge unit control stopped the said oil-water mixture of pumping in said second heating tank, and unnecessary said oil-water mixture is transmitted back in the said apparatus for temporary storage.
Preferably, said treatment system also comprises the control water tank that accommodates control water, and this control water tank links to each other with the control water inlet of said disk centrifugal separator, and this control water tank is used for regularly to said disk centrifugal separator input control water.
Preferably, said control water is the tap water after said control water tank filters.
Preferably; Said treatment system also comprises the cleaning water tank that accommodates rinse water; This cleaning water tank links to each other with the inlet of said horizontal centrifuge and/or the inlet of said disk centrifugal separator, and this cleaning water tank is used for to said horizontal centrifuge and/or said disk centrifugal separator input rinse water.
Preferably, said cleaning water tank has vapor inlet port, and this vapor inlet port is used in said cleaning water tank, importing steam.
Preferably, said rinse water is a tap water.
Through technique scheme, the independent tripping device of changing food waste treatment system utilization of the utility model is handled changing food waste, isolates grease from changing food waste and is used for reclaiming and stores thereby make.The processing efficiency of aforesaid method is high, and working stability is applicable to large-scale changing food waste processing, and higher through the oil quality of aforesaid method acquisition.
Other feature and advantage of the utility model will partly specify in embodiment subsequently.
Description of drawings
Accompanying drawing is the further understanding that is used to provide the utility model, and constitutes the part of specification sheets, is used to explain the utility model with following embodiment, but does not constitute the restriction to the utility model.In the accompanying drawings:
Fig. 1 is the synoptic diagram of preferred implementation of the changing food waste treatment system of the utility model.
Description of reference numerals
1 first storage pool, 2 second storage pools
The inlet of 3 horizontal centrifuges, 31 horizontal centrifuges
First outlet, 4 first heating tanks of 32 horizontal centrifuges
41 first fluid inlets, 42 first liquid outlets
43 first liquid spill-ways, 5 apparatus for temporary storage
6 second heating tanks, 61 second fluid inlets
62 second liquid outlets, 63 second liquid spill-ways
The inlet of 7 disk centrifugal separators, 71 disk centrifugal separators
The control water inlet of first outlet, 73 disk centrifugal separators of 72 disk centrifugal separators
8 control water tanks 9 clean water tank
10 collection devices, 11 squeezing machines
Embodiment
Be elaborated below in conjunction with the embodiment of accompanying drawing to the utility model.Should be understood that embodiment described herein only is used for explanation and explains the utility model, is not limited to the utility model.
In the utility model, do not doing under the situation of specified otherwise, " changing food waste " refers to the mixture of oil, water and small amount of solid residue in the changing food waste; " filtering mixt " fingering row is crossed the material of filtration treatment; " primary filter mixture " refers to that degree of filtration is lower than the material of filtering mixt.
The utility model provides a kind of changing food waste treatment system, and wherein, this treatment system comprises storing unit, tripping device and the collection device that connects successively, wherein,
Said storing unit is used to receive changing food waste and filters and obtains filtering mixt, and this filtering mixt is sent to said tripping device;
Said tripping device is used for isolating grease from filtering mixt, and this grease is sent to said collection device;
Said collection device 10 is used to collect the grease that comes from said tripping device.
The changing food waste treatment system utilization of the utility model is separated from each other and the storing unit, tripping device and the collection device that connect are separated the grease in the changing food waste.。Wherein, storing unit can carry out preliminary filtration to changing food waste through modes such as depositions, and tripping device comes out the solid residue in the changing food waste and water sepn and abandons, and grease is recovered in the collection device 10.The separating effect of aforesaid method will obviously be superior to passing through in the prior art deoiling method of air-flotation type grease trap or oil removal groove, and separating effect is better, and isolated oil quality is higher, is applicable to large-scale changing food waste processing.
Preferably; Said storing unit comprises first storage pool 1 and second storage pool 2; Said first storage pool 1 is used to receive changing food waste and said changing food waste is filtered and obtains the primary filter mixture, and this primary filter mixture is pumped in said second storage pool 2, and said second storage pool 2 is used to receive said primary filter mixture and said primary filter mixture filtered and obtains filtering mixt.
Storing unit comprises first storage pool 1 and second storage pool 2, and normally, this first storage pool 1 and the changing food waste storehouse that feeds intake links to each other, and changing food waste directly is stored in first storage pool 1 and tentatively filters.Changing food waste generally includes grease, water and small amount of solid residue, and through the preliminary filtration of first storage pool 1, a large amount of solid residues in the changing food waste are filtered, and the grease that filters out, water and small amount of solid residue are pumped in second storage pool 2.Second storage pool 2 also can have and filters and/or sedimentary function, obtains filtering mixt after like this primary filter mixture being filtered once more, and this filtering mixt is sent in the said tripping device goes.
Preferably, said treatment system also comprises squeezing machine 11, and this squeezing machine 11 is that second storage pool 2 provides the primary filter mixture.
Above-mentioned first storage pool 1 is used for receiving the feed intake changing food waste in storehouse of changing food waste; As indicated above; This changing food waste generally includes grease, water and small amount of solid residue, and solid residue is more in this changing food waste, therefore needs first storage pool 1 to carry out preliminary filtration and/or deposition.And squeezing machine 11 is to be used for thereby above-mentioned changing food waste is squeezed a large amount of solid residues of removing in this changing food waste; And obtain the primary filter mixture be made up of grease, water and small amount of solid residue, and squeezing machine 11 is sent to this primary filter mixture in second storage pool 2.
Preferably, be provided with stirrer in said first storage pool 1 and/or said second storage pool 2.
Handle in order can the product pump in the storing unit to be delivered in the next stage device of system; In first storage pool 1 and/or second storage pool 2, be provided with stirrer usually; This stirrer is used to make the mixture of changing food waste more even; Prevent that solid residue from too much precipitating at the bottom of the pond, thereby make the material pumping in first storage pool 1 and/or second storage pool 2 get more thorough.
Preferably, said tripping device comprises the horizontal centrifuge 3 and disk centrifugal separator 7 that connects successively, and this horizontal centrifuge 3 is used for isolating oil-water mixture from said filtering mixt, and this disk centrifugal separator 7 is used for isolating grease from said oil-water mixture.
Select horizontal centrifuge 3 and disk centrifugal separator 7 to be used as the preferred implementation of tripping device in the preferred implementation of the utility model.The selection of these two kinds of whizzer kinds and use-pattern are that horizontal centrifuge 3 can separate solid-state and liquid material better by the decision of the performance of whizzer, and disk centrifugal separator 7 then is applied to the separation of fluent meterial more more.
Said horizontal centrifuge 3 is solid-state slag charge with basic for liquid oil-water mixture basically through accessing after the spinning; Here said " basic for liquid " and " basically for solid-state " are that " basically " refers to great majority because tripping device can not be separated solid matter and fluent meterial fully.Wherein, the slag charge that horizontal centrifuge 3 is separated can be delivered to pulping engine and pulverize, because contain large amount of organic matter in the slag charge, therefore can reclaim purposes such as being used to produce biogas, has greatly improved the utilization ratio of material.Perhaps, thereby selectively the spinning product of horizontal centrifuge 3 is divided into oil-water mixture, sewage and slag charge through the setting and the type selecting of horizontal centrifuge 3, oil-water mixture is wherein sent apparatus for temporary storage 5 back to.
Disk centrifugal separator 7 is separated grease through after the spinning, and remainder water is directly sent into the sewage preparing pool with a small amount of residue and preserved, and the sewage in this sewage preparing pool can be imported the pulverizing that is used for slag charge in the pulping engine.
Preferably; Said treatment system also comprises apparatus for temporary storage 5; First outlet 32 of this apparatus for temporary storage 5 and said horizontal centrifuge links to each other with the inlet 71 of said disk centrifugal separator; This apparatus for temporary storage 5 is used to store said horizontal centrifuge 3 isolated said oil-water mixtures, and said oil-water mixture is pumped in the said disk centrifugal separator 7.
Because therefore the finite capacity of horizontal centrifuge 3 and disk centrifugal separator 7 is provided with above-mentioned apparatus for temporary storage 5, plays the function of temporary transient oil in reserve water mixture between horizontal centrifuge 3 and disk centrifugal separator 7.The oil-water mixture of separating from horizontal centrifuge 3 temporarily is stored in the apparatus for temporary storage 5, and more preferably, this apparatus for temporary storage also has filtration and/or sedimentary function, therefore can help from oil-water mixture, to remove more up hill and dale solid residue.
Preferably; Said treatment system also comprises first heating tank 4 that is used for to said filtering mixt heating; This first heating tank 4 comprises first fluid inlet 41, first liquid outlet 42 and first heating unit; Said first fluid inlet 41 links to each other with said storing unit, and said first liquid outlet 42 links to each other with the inlet 31 of said horizontal centrifuge, and said first heating unit is used for to said filtering mixt heating.
Filtering mixt is being sent into before tripping device separates; Just send into before the horizontal centrifuge 3; The utility model preferably adopts 4 pairs of these filtering mixts of first heating tank to heat; Thereby it is separated in horizontal centrifuge 3 more to help filtering mixt, this mainly be because grease on the blade that is not easy under the higher temperature attached to whizzer.In addition, grease can solidify and becomes solid-stately when temperature was low, so not only was unfavorable for centrifugally operated, and when carrying out spinning, will it be together abandoned with solid residue as solid-state, thereby cause waste.Usually this filtering mixt is heated to about 85 ℃ in this first heating tank 4, and then feeds in the horizontal centrifuge 3.
Preferably, said first heating unit is a steam coils.
First heating unit mentioned above can adopt various ways, for example electrically heated etc., and the utility model preferably adopts steam-heated method, utilizes steam coils that the filtering mixt in first heating tank 4 is heated.Steam coils is made up of the pipe of coiling; Feed the water vapour of heat from an end of this pipe; Carry out heat exchange through this steam coils and the external world, and then be condensed into water, the other end of this pipe is connected with condensate pipe; Can the water of this vapor condensation be reclaimed once more and utilize, thereby practice thrift the energy and avoided pollution.This steam coils can be arranged on suitable position arbitrarily, for example can be arranged on the inside of first heating tank 4, and the outer tube wall of steam coils directly contacts with filtering mixt, also can be arranged on this tank body setting of outer surrounding of first heating tank 4.
Preferably; Said first heating tank 4 also comprises first liquid spill-way 43 and the first discharge unit; This first discharge unit detects the liquid level of the said filtering mixt in said first heating tank 4; After this liquid level reached preset value, said first discharge unit control stopped the said filtering mixt of pumping in said first heating tank 4, and unnecessary said filtering mixt is transmitted back in the said storing unit.
Because the restriction of the capacity of first heating tank 4 and horizontal centrifuge 3, therefore first heating tank 4 can also have first liquid spill-way 43.Like this; When storing unit when the filtering mixt of first heating tank, 4 pumpings is excessive; The filtering mixt that the said first discharge unit can detect in first heating tank 4 surpasses specified liquid level, controls first fluid inlet 41 then and closes, and stops to continue pumping filtering mixt in first heating tank 4; And first liquid spill-way 43 opened; Flow out and flow back to said storing unit through this first liquid spill-way 43, comprise the preferred implementation of first storage pool 1 and second storage pool 2 according to storing unit mentioned above, filtering mixt is got back to said second storage pool 2 after 43 outflows of said first liquid spill-way.
This first discharge unit can comprise the detection module that is used for detecting first heating tank, 4 liquid levels, is used for the processing module and the control module that is used for controlling according to comparative result the switching of first fluid inlet 41 and first liquid spill-way 43 of more detected liquid level and specified liquid level.Usually, above-mentioned detection module adopts float(ing)valve, between the direct control linkage storing unit of above-mentioned control module and first fluid inlet 41, and the pump between first liquid spill-way 43 and the storing unit.
Preferably; Said treatment system also comprises second heating tank 6 that is used for to said oil-water mixture heating; This second heating tank 6 comprises second fluid inlet 61, second liquid outlet 62 and second heating unit; Said second fluid inlet 61 links to each other with first outlet 32 of said horizontal centrifuge, and said second liquid outlet 62 links to each other with the inlet 71 of said disk centrifugal separator, and said second heating unit is used for to said oil-water mixture heating.
Preferably; Said treatment system also comprises second heating tank 6 that is used for to said oil-water mixture heating; This second heating tank 6 comprises second fluid inlet 61, second liquid outlet 62 and second heating unit; Said second fluid inlet 61 links to each other with said apparatus for temporary storage 5, and said second liquid outlet 62 links to each other with the inlet 71 of said disk centrifugal separator, and said second heating unit is used for to said oil-water mixture heating.
Before oil-water mixture is sent into disk centrifugal separator 3; The utility model preferably adopts 6 pairs of these oil-water mixtures of second heating tank to heat; Separated in disk centrifugal separator 7 more to help oil-water mixture, this mainly be because grease on the blade that is not easy under the higher temperature attached to whizzer.In addition, grease can solidify and becomes solid-stately when temperature was low, so not only was unfavorable for centrifugally operated, and when carrying out spinning, will it be together abandoned with solid residue as solid-state, thereby cause waste.Usually this oil-water mixture is heated to 90 ℃-95 ℃ in this second heating tank 6, and then feeds in the disk centrifugal separator 7.Therefore, no matter whether comprise apparatus for temporary storage in the preferred implementation of the changing food waste treatment system of the utility model, before oil-water mixture gets into disk centrifugal separator 7, all want first through second heating tank 6.
Preferably, said second heating unit is a steam coils.
Second heating unit mentioned above can adopt various ways, for example electrically heated etc., and the utility model preferably adopts steam-heated method, utilizes steam coils that the oil-water mixture in second heating tank 6 is heated.Steam coils is made up of the pipe of coiling; Feed the water vapour of heat from an end of this pipe; Carry out heat exchange through this steam coils and the external world, and then be condensed into water, the other end of this pipe is connected with condensate pipe; Can the water of this vapor condensation be reclaimed once more and utilize, thereby practice thrift the energy and avoided pollution.This steam coils can be arranged on suitable position arbitrarily, for example can be arranged on the inside of second heating tank 6, and the outer tube wall of steam coils directly contacts with filtering mixt, also can be arranged on this tank body setting of outer surrounding of second heating tank 6.
Preferably; Said second heating tank 6 also comprises second liquid spill-way 63 and the second discharge unit; This second discharge unit detects the liquid level of the said oil-water mixture in said second heating tank 6; After this liquid level reached preset value, said second discharge unit control stopped the said oil-water mixture of pumping in said second heating tank 6, and unnecessary said oil-water mixture is transmitted back in the said storing unit.
Because the restriction of the capacity of second heating tank 6 and disk centrifugal separator 7, therefore second heating tank 6 can also have second liquid spill-way 63.Like this; When apparatus for temporary storage when the oil-water mixture of second heating tank, 6 pumpings is excessive; The oil-water mixture that the said second discharge unit can detect in second heating tank 6 surpasses specified liquid level, controls second fluid inlet 61 then and closes, and stops to continue pump oil water mixture in second heating tank 6; And second liquid spill-way 63 opened, flow out and flow back in the said apparatus for temporary storage through this second liquid spill-way 63.
This second discharge unit can comprise the detection module that is used for detecting second heating tank, 6 liquid levels, is used for the processing module and the control module that is used for controlling according to comparative result the switching of first fluid inlet 41 and first liquid spill-way 43 of more detected liquid level and specified liquid level.Usually, above-mentioned detection module adopts float(ing)valve, between the direct control linkage apparatus for temporary storage of above-mentioned control module and second fluid inlet 61, and the pump between second liquid spill-way 63 and the apparatus for temporary storage 5.
Preferably, said treatment system also comprises the control water tank 8 that accommodates control water, and this control water tank links to each other with the control water inlet 73 of said disk centrifugal separator 7, and this control water tank is used for regularly to said disk centrifugal separator 7 input control water.
On period at disk centrifugal separator 7; The control water tank constantly regularly injects control water to guarantee its works better in disk centrifugal separator 7; Owing to also be mixed with solid residue inevitably in the oil-water mixture; Therefore this control water is mainly used in the inner deslagging of disk centrifugal separator, thereby prevents the inner obstruction of movement.The water of this cleaning water tank output is normal-temperature water.
Preferably, said control water is for filtering the tap water that has through said control water tank 8.Because this control water is used for the deslagging of disk centrifugal separator 7 inside, therefore, control the function that water tank 8 has filtered water usually for controlling having relatively high expectations of water, this control water is process control water tank 8 filtering clean tap water.
Preferably; Said treatment system also comprises the cleaning water tank 9 that accommodates rinse water; This cleaning water tank links to each other with the inlet 31 of said horizontal centrifuge 3 and/or the inlet 71 of said disk centrifugal separator, and this cleaning water tank is used for to said horizontal centrifuge 3 and/or said disk centrifugal separator 7 input rinse water.
This rinse water is used to clean horizontal centrifuge 3 and/or disk centrifugal separator 7, therefore uses cleaning water tank 9 after the treatment system end-of-job, to clean horizontal centrifuge 3 and/or disk centrifugal separator 7.When utilizing cleaning 9 pairs of horizontal centrifuges 3 of water tank and/or disk centrifugal separator 7 to wash; The treatment system of the utility model is not worked; Start horizontal centrifuge 3 and disk centrifugal separator 7; This moment is injecting material in two whizzers not, and cleaning water tank 9 washes to said horizontal centrifuge 3 and/or disk centrifugal separator 7 injection rinse water through inlet separately.
Preferably, said cleaning water tank 9 has vapor inlet port 91, and this vapor inlet port 91 is used for input steam in said cleaning water tank 9.
This steam is directly imported and is cleaned water tank inside, directly contacts with rinse water and carries out heat exchange, and steam can be condensed into water and can not produce pollution.Usually, the temperature in this cleaning water tank 9 remains on about 90 ℃, so rinse water is also greatly about 90 ℃.
Preferably, said rinse water is a tap water.Need to prove here, will be lower than tap water as control water as the clean-up performance of the tap water of cleaning water.
Usually; Because oil-water mixture was heated by second heating tank 6 before getting into disk centrifugal separator 7; So having usually, grease is about 60 ℃-70 ℃ temperature when disk centrifugal separator 7 gets into said collection device 10; Even under cold snap, the temperature of collection device 10 at least also will remain on more than 20 degree, and this is not only to be not easy to flow because prevent that grease from solidifying under the lower situation of temperature for the temperature of collection device.
Need to prove, in the description of preceding text, feed first heating tank 4, second heating tank 6 and the steam that cleans in the water tank 9 all is preferably 0.6MPa the preferred implementation of the utility model.In addition; Because the changing food waste treatment system main processing of the utility model is the fluidised form mixture that oil, water and small amount of solid residue are formed; Therefore fluid transmission between each device in system can transmit through pump; Also can utilize the gravity of fluid self; Concern and make fluid under action of gravity, flow into another device from a device promptly that for example filtering mixt can rely on gravity to get into horizontal centrifuges 3 from first heating tank 4 through each height of devices is set, oil-water mixture can rely on gravity to get into disk centrifugal separators 7 from second heating tank 6.Therefore; Each embodiment of above-mentioned the utility model has only provided the annexation between the device; And do not provide actual deployment scenarios; That is to say in the scope of the utility model; The TP setting of each device in the treatment system can be arbitrarily, and for example first heating unit, second heating unit and the cleaning steam that water tank was connected can come from same pipeline, and the other end of the water of condensation of the output steam of first heating unit and second heating unit also can be merged into same pipeline.
More than combine accompanying drawing to describe the preferred implementation of the utility model in detail; But; The utility model is not limited to the detail in the above-mentioned embodiment; In the technical conceive scope of the utility model, can carry out multiple simple variant to the technical scheme of the utility model, these simple variant all belong to the protection domain of the utility model.
Need to prove in addition; Each concrete technical characterictic described in above-mentioned embodiment under reconcilable situation, can make up through any suitable manner; For fear of unnecessary repetition, the utility model is to the explanation no longer separately of various possible array modes.
In addition, also can carry out arbitrary combination between the various embodiment of the utility model, as long as its thought without prejudice to the utility model, it should be regarded as content disclosed in the utility model equally.
Claims (18)
1. a changing food waste treatment system is characterized in that, this treatment system comprises storing unit, tripping device and the collection device that connects successively, wherein,
Said storing unit is used to receive changing food waste and filters and obtains filtering mixt, and this filtering mixt is sent to said tripping device;
Said tripping device is used for isolating grease from filtering mixt, and this grease is sent to said collection device;
Said collection device (10) is used to collect the grease that comes from said tripping device.
2. changing food waste treatment system according to claim 1; It is characterized in that; Said storing unit comprises first storage pool (1) and second storage pool (2); Said first storage pool (1) is used to receive changing food waste and said changing food waste is filtered and obtains the primary filter mixture; And this primary filter mixture is pumped in said second storage pool (2), said second storage pool (2) is used to receive said primary filter mixture and said primary filter mixture is filtered and obtains filtering mixt.
3. changing food waste treatment system according to claim 1 is characterized in that, said treatment system also comprises squeezing machine (11), and this squeezing machine (11) is that second storage pool (2) provides the primary filter mixture.
4. changing food waste treatment system according to claim 2 is characterized in that, is provided with stirrer in said first storage pool (1) and/or said second storage pool (2).
5. changing food waste treatment system according to claim 1; It is characterized in that; Said tripping device comprises horizontal centrifuge (3) and the disk centrifugal separator (7) that connects successively; This horizontal centrifuge (3) is used for isolating oil-water mixture from said filtering mixt, and this disk centrifugal separator (7) is used for isolating grease from said oil-water mixture.
6. changing food waste treatment system according to claim 5; It is characterized in that; Said treatment system also comprises apparatus for temporary storage (5); This apparatus for temporary storage (5) links to each other with first outlet (32) of said horizontal centrifuge (3) and the inlet (71) of said disk centrifugal separator (7), and this apparatus for temporary storage (5) is used to store the isolated said oil-water mixture of said horizontal centrifuge (3), and said oil-water mixture is pumped in the said disk centrifugal separator (7).
7. changing food waste treatment system according to claim 5; It is characterized in that; Said treatment system also comprises first heating tank (4) that is used for to said filtering mixt heating; This first heating tank (4) comprises first fluid inlet (41), first liquid outlet (42) and first heating unit; Said first fluid inlet (41) links to each other with said storing unit, and said first liquid outlet (42) links to each other with the inlet (31) of said horizontal centrifuge (3), and said first heating unit is used for to said filtering mixt heating.
8. changing food waste treatment system according to claim 7 is characterized in that, said first heating unit is a steam coils.
9. changing food waste treatment system according to claim 7; It is characterized in that; Said first heating tank (4) also comprises first liquid spill-way (43) and the first discharge unit; This first discharge unit detects the liquid level of the said filtering mixt in said first heating tank (4); After this liquid level reached preset value, said first discharge unit control stopped the said filtering mixt of pumping in said first heating tank (4), and unnecessary said filtering mixt is transmitted back in the said storing unit.
10. the changing food waste treatment system of stating according to claim 5; It is characterized in that; Said treatment system also comprises second heating tank (6) that is used for to said oil-water mixture heating; This second heating tank (6) comprises second fluid inlet (61), second liquid outlet (62) and second heating unit; Said second fluid inlet (61) links to each other with first outlet (32) of said horizontal centrifuge (3), and said second liquid outlet (62) links to each other with the inlet (71) of said disk centrifugal separator (7), and said second heating unit is used for to said oil-water mixture heating.
11. changing food waste treatment system according to claim 6; It is characterized in that; Said treatment system also comprises second heating tank (6) that is used for to said oil-water mixture heating; This second heating tank (6) comprises second fluid inlet (61), second liquid outlet (62) and second heating unit; Said second fluid inlet (61) links to each other with said apparatus for temporary storage (5), and said second liquid outlet (62) links to each other with the inlet (71) of said disk centrifugal separator (7), and said second heating unit is used for to said oil-water mixture heating.
12., it is characterized in that said second heating unit is a steam coils according to claim 10 or 11 described changing food waste treatment systems.
13. changing food waste treatment system according to claim 11; It is characterized in that; Said second heating tank (6) also comprises second liquid spill-way (63) and the second discharge unit; This second discharge unit detects the liquid level of the said oil-water mixture in said second heating tank (6); After this liquid level reached preset value, said second discharge unit control stopped the said oil-water mixture of pumping in said second heating tank (6), and unnecessary said oil-water mixture is transmitted back in the said apparatus for temporary storage (5).
14. changing food waste treatment system according to claim 5; It is characterized in that; Said treatment system also comprises the control water tank (8) that accommodates control water; This control water tank links to each other with the control water inlet (73) of said disk centrifugal separator (7), and this control water tank is used for regularly to said disk centrifugal separator (7) input control water.
15. changing food waste treatment system according to claim 14 is characterized in that, said control water is the tap water after filtering through said control water tank (8).
16. changing food waste treatment system according to claim 5; It is characterized in that; Said treatment system also comprises the cleaning water tank (9) that accommodates rinse water; This cleaning water tank links to each other with the inlet (31) of said horizontal centrifuge (3) and/or the inlet (71) of said disk centrifugal separator (7), and this cleaning water tank is used for to said horizontal centrifuge (3) and/or said disk centrifugal separator (7) input rinse water.
17. changing food waste treatment system according to claim 16 is characterized in that, said cleaning water tank (9) has vapor inlet port (91), and this vapor inlet port (91) is used for input steam in said cleaning water tank (9).
18. changing food waste treatment system according to claim 16 is characterized in that, said rinse water is a tap water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203211504U CN202226741U (en) | 2011-08-30 | 2011-08-30 | Kitchen waste disposal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203211504U CN202226741U (en) | 2011-08-30 | 2011-08-30 | Kitchen waste disposal system |
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| Publication Number | Publication Date |
|---|---|
| CN202226741U true CN202226741U (en) | 2012-05-23 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203211504U Expired - Fee Related CN202226741U (en) | 2011-08-30 | 2011-08-30 | Kitchen waste disposal system |
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| CN (1) | CN202226741U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114343042A (en) * | 2022-01-20 | 2022-04-15 | 福建海丽天食品有限公司 | Comprehensive recycling process method of leftovers and sugar immersion liquid based on preserved fruit processing |
-
2011
- 2011-08-30 CN CN2011203211504U patent/CN202226741U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114343042A (en) * | 2022-01-20 | 2022-04-15 | 福建海丽天食品有限公司 | Comprehensive recycling process method of leftovers and sugar immersion liquid based on preserved fruit processing |
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