CN205449630U - Waste oil receives preceding processing apparatus of sample - Google Patents
Waste oil receives preceding processing apparatus of sample Download PDFInfo
- Publication number
- CN205449630U CN205449630U CN201620191487.0U CN201620191487U CN205449630U CN 205449630 U CN205449630 U CN 205449630U CN 201620191487 U CN201620191487 U CN 201620191487U CN 205449630 U CN205449630 U CN 205449630U
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- China
- Prior art keywords
- storehouse
- cell body
- waste grease
- flase floor
- shaftless
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- 239000002699 waste material Substances 0.000 title claims abstract description 55
- 238000005070 sampling Methods 0.000 claims abstract description 59
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 239000004519 grease Substances 0.000 claims description 52
- 238000002203 pretreatment Methods 0.000 claims description 20
- 229910001220 stainless steel Inorganic materials 0.000 claims description 11
- 239000010935 stainless steel Substances 0.000 claims description 11
- 239000012530 fluid Substances 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 7
- 239000007921 spray Substances 0.000 claims description 5
- 238000004332 deodorization Methods 0.000 claims description 4
- 230000000875 corresponding Effects 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 230000035943 smell Effects 0.000 claims description 3
- 241000216843 Ursus arctos horribilis Species 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 16
- 239000012535 impurity Substances 0.000 abstract description 12
- 238000000926 separation method Methods 0.000 abstract description 9
- 238000009434 installation Methods 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 16
- 235000019198 oils Nutrition 0.000 description 15
- 238000006297 dehydration reaction Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 239000000706 filtrate Substances 0.000 description 5
- 238000001914 filtration Methods 0.000 description 5
- 230000000903 blocking Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 239000007790 solid phase Substances 0.000 description 3
- 239000010775 animal oil Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 235000019476 oil-water mixture Nutrition 0.000 description 2
- 230000000717 retained Effects 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000196435 Prunus domestica subsp. insititia Species 0.000 description 1
- 241000220317 Rosa Species 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 235000014593 oils and fats Nutrition 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 230000001376 precipitating Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000003981 vehicle Substances 0.000 description 1
Abstract
The utility model relates to a waste oil receives preceding processing apparatus of sample, including sampling groove, pretreatment mechanism, row sediment screw mechanism and the connecting pipe of connection between sampling groove and pretreatment mechanism, the sampling groove includes cell body, grid board and agitator, and two -layer removable the installation on the upper portion of cell body of grid board that is equipped with the trompil has charge door and at least three thief hole on at least, and the agitator is installed on the supporting rack on cell body upper portion, pretreatment mechanism is including being equipped with the receipt storehouse and the multiunit steam pipe of top cap, and the steam pipe setting is in the well lower part of receiving the storehouse, and receives and be equipped with the collecting tank in the storehouse, receive the row's sediment screw mechanism who upwards puts to one side at the well rear portion in storehouse, and its shaftless row sediment spiral lower part is equipped with the collecting tank, the upper portion of collecting tank is equipped with at least a set of wash tub pipe. The utility model discloses compact structure is reasonable, not only can satisfy the function of supplied materials sample, and can increase solid -liquid separation's ability, can effectively reduce and cause follow -up equipment to block up the high problem of frequency of overhauing because of impurity exists.
Description
Technical field
This utility model relates to a kind of waste grease and receives sampling pretreating device, belongs to waste grease process field.
Background technology
Waste grease such as waste oil derives from the oil interceptor of municipal sewage system, and oil content is about 30～40%, and resourcebility degree is higher.The more impurity such as the greasy floating thing of canescence and food residues, fruit and vegerable putrefaction, plastics and house refuse is typically had above waste grease.
The common processing mode of waste grease is to pour the swill of recovery into first class purification pond by recovery vehicle, it is heated to 80 °, residue is taken out, again by oil water mixture suction secondary purification pond, it is heated to 100 °, after precipitation certain time, enter three grades of clarifier-tanks, after repeatedly precipitating purification, i.e. produce industrial oils and fats.For improving treatment effeciency, disclosed recovery hogwash fat environmental protection equipment, it is in a casing, be provided with filter chamber, oil suction room and charge of oil room from top to bottom, by hogwash fat by arranging the Rose Box in filter chamber, oil suction is carried out indoor by the profit hole on filter box the profit pipe on upper spacer, through the indoor oil suction float of oil suction and gather oil pipe to enter back into the charge of oil of bottom indoor, and by being arranged on charge of oil indoor oil pump, fluid after process is discharged, discharge outside casing by drain pipe, to realize solid-liquid separation and oil-water separation by the water that oil suction is indoor simultaneously.But this processing means can not realize continuous prodution, it is impossible to meeting and process big requirement, production efficiency is low.The processing method carried out at first at present is to first pass through physics centrifuging to carry out solid-liquid separation, then carries out two-stage purification by " three-phase carries oil machine+disc-type and puies forward oil machine ", produces the crude oil that purity is about 97.5%.But before centrifugal solid-liquid separates, although can remove the impurity in waste grease by filtration treatment, but removal of impurity is low, easily by filter net jam during entrance centrifugation, because impurity exists the fault that results in blockage, there is repair rate increases and affects work efficiency.
Summary of the invention
The purpose of this utility model is to provide a kind of waste grease and receives sampling pretreating device, compact conformation is reasonable, not only can meet the function of supplied materials sampling, and the ability of solid-liquid separation can be increased, the impurity of more than 90% in removable waste grease, can effectively reduce the problem causing follow-up equipment blocking repair rate high because impurity exists.
This utility model is that the technical scheme reaching above-mentioned purpose is: a kind of waste grease receives sampling pretreating device, it is characterised in that: include sampling groove, pre-treatment mechanism, deslagging screw mechanism and for connecting the connecting tube between sampling groove and pre-treatment mechanism；Described sampling groove includes cell body, flase floor and agitator, at least two-layer is provided with the removable top being arranged on cell body of flase floor of perforate, perforate on each layer flase floor is staggered setting, and cell body has charge door and at least three thief hole, and agitator is arranged on the bearing support on cell body top；Described connecting tube one end is connected to the bottom of cell body, the other end is connected to the import department on the reception storehouse of pre-treatment mechanism, and connecting tube is provided with the gate valve that can automatically control；Described pre-treatment mechanism includes the reception storehouse being provided with top cover and organizes steam pipe more, and the steam pipe being provided with multiple pore is provided with collecting tank in being arranged on the middle and lower part in reception storehouse, and reception storehouse；The postmedian in described reception storehouse is provided with along the most tilting deslagging screw mechanism of feed direction, the porous filter pocket that described deslagging screw mechanism is U-shaped in including being arranged on reception storehouse, it is connected to receive the sleeve of storehouse outer closures and shaftless deslagging spiral and drive motor, motor is driven to be connected with shaftless deslagging spiral, shaftless deslagging spiral is arranged in porous filter pocket and sleeve, sleeve rear portion is provided with slag-drip opening, porous filter pocket is provided with multiple rows of sieve aperture, and the external diameter of shaftless deslagging spiral is along conveying direction the most from large to small, pitch is from large to small, shaftless deslagging spiral periphery is fixed with the stainless steel brush for clearing up filter opening, the collecting tank being positioned at shaftless deslagging spiral bottom is provided with leakage fluid dram, and the top of collecting tank is provided with the least one set corresponding with porous filter pocket and has the wash tub pipe of multiple high-pressure nozzle.
This utility model uses sampling groove, pre-treatment mechanism, deslagging screw mechanism, owing to sampling groove top is provided with at least two-layer with flase floor, and the perforate dislocation on each layer flase floor is arranged, by flase floor, the waste grease entering sampling groove is carried out coarse filtration, the bulk materials in waste grease can be retained.The removable top being arranged on cell body of this utility model each layer flase floor, therefore flase floor is replaced and is very convenient to, and can keep the functional reliability of anterior coarse filtration.This utility model arranges agitator in sampling groove, after waste grease adds in sampling groove, and can be by waste grease mix homogeneously by agitator work, in order to the accuracy to waste grease sampling.This utility model is provided with at least three thief hole on the cell body of sampling groove, therefore after every batch materials adds, the thief hole of multiple diverse locations from cell body waste grease can be sampled, waste grease is analyzed, per car waste grease supplied materials to be sampled monitoring, the collection of energy specification restaurant waste grease, solves waste grease in recent years and more food safety accident has occurred.Gate valve between this utility model sampling groove and pre-treatment mechanism is Electronic control, after sampling terminates, starts gate valve, is entered in pre-treatment mechanism by the waste grease after sampling, can reduce operator's workload.This utility model is provided with deslagging screw mechanism in pre-treatment mechanism, deslagging screw mechanism is provided with a reducing varying pitch structure and with the shaftless deslagging spiral of pressing function and porous filter pocket, shaftless deslagging spiral on deslagging screw mechanism is along its diameter of conveying direction from large to small, pitch is from large to small, therefore in the operation process of shaftless deslagging spiral, solid phase residue is extruded dehydration, and the residue moisture content after its dehydration is about about 70%, the beneficially biochemical treatment of postorder.This utility model is arranged on the porous filter pocket received in storehouse and is arranged on shaftless deslagging spiral bottom, and multiple rows of sieve aperture is set on porous filter pocket, filtrate is made to be discharged to collecting tank by sieve aperture, porous filter pocket is scraped clearly effect by the stainless steel brush that shaftless deslagging spiral periphery is fixed, cleaning sieve aperture can be arrived in time, keeping the ability of stable solid-liquid separation, the leakage fluid dram making filtrate pass through collecting tank is discharged.This utility model is rational in infrastructure, not only can meet the function of supplied materials sampling, is processed by twice remove impurity, the impurity of more than 90% in removable waste grease, improve pre-treatment efficiency, can effectively reduce the problem causing because impurity exists follow-up equipment blocking repair rate high, improve production efficiency.
Accompanying drawing explanation
Below in conjunction with the accompanying drawings embodiment of the present utility model is described in further detail.
Fig. 1 is the structural representation that a kind of waste grease of this utility model receives sampling pretreating device.
Fig. 2 is the plan structure schematic diagram of Fig. 1.
Fig. 3 is the schematic cross-section of this utility model steam pipe.
Fig. 4 is the partial structurtes schematic diagram of this utility model flase floor.
Fig. 5 is this utility model porous filter pocket cross-sectional view.
Wherein: 1 sampling groove, 1-1 baffle plate, 1-2 agitator, 1-3 flase floor, 1-31 perforate, 1-4 bearing, 1-5 cell body, 1-6 thief hole, 1-7 bearing support, 2 pre-treatment mechanisms, 2-1 top cover, 2-2 receives storehouse, 2-3 deodorization collection port, 2-4 steam pipe, 2-5 dividing plate, 2-6 wash tub pipe, 2-7 collecting tank, 2-8 leakage fluid dram, 2-9 manhole, 2-10 radar levelmeter, 3 deslagging screw mechanisms, 3-1 porous filter pocket, 3-11 sieve aperture, 3-2 shaftless deslagging spiral, 3-3 sleeve, 3-4 slag-drip opening 3-5 drives motor, the stainless steel brush of 3-6, 4 connecting tubes, 4-1 gate valve.
Detailed description of the invention
As shown in Figure 1, this utility model one waste grease receives sampling pretreating device, including sampling groove 1, pre-treatment mechanism 2, deslagging screw mechanism 3 and for connecting the connecting tube 4 between sampling groove 1 and pre-treatment mechanism 2.Such as Fig. 1, shown in 2, sampling groove 1 of the present utility model includes cell body 1-5, flase floor 1-3 and agitator 1-2, and sampling groove 1 dischargeable capacity can be at 1.5m3Left and right, can arrange the most long-pending of sampling groove 1 according to production requirement.As shown in Figure 1, this utility model at least two-layer is provided with the removable top being arranged on cell body 1-5 of flase floor 1-3 of perforate 1-31, multiple bearing 1-4 can be provided with on cell body 1-5, it is used for each flase floor 1-3 is installed by bearing, flase floor 1-3 can be arranged on bearing 1-4 by securing member, or flase floor 1-3 is placed on bearing 1-4, or flase floor 1-3 is connected on bearing 1-4, and version does not limits.Flase floor 1-3 of the present utility model can be provided with multilamellar, such as three layers, and is provided with the distance of 5～10mm between each layer, and the perforate 1-31 on each layer flase floor 1-3 is staggered setting, i.e. convenient processes flase floor 1-3, and can play again coarse filtration effect.Perforate 1-31 on this utility model flase floor 1-3 is circular hole or polygonal hole and arranges in array, arrange in multiple rows of array, perforate 1-31 diameter is between 15～40mm, if the perforate 1-31 aperture on screen is between 25mm or 30mm, and the distance 50～100mm between adjacent apertures 1-31, it can be controlled between 60～90mm.Perforate on this utility model flase floor 1-3 is grizzly bar shape.As shown in Figure 4, each perforate 1-31 on this utility model flase floor 1-3 is staggered setting, by flase floor 1-3 by material bigger for the part in the waste grease entered in sampling groove 1, retained by flase floor 1-3 such as plastics etc., rest materials enters cell body 1-5, it is arranged on cell body 1-5 owing to each flase floor 1-3 is removable, very convenient replacement and replacing flase floor 1-3, to keep solid-liquid separation efficiency during waste grease entrance sampling groove 1.
Such as Fig. 1, shown in 2, there is on this utility model cell body 1-5 charge door and at least three thief hole 1-6, agitator 1-2 is arranged on the bearing support 1-7 on cell body 1-5 top, by agitator 1-2 to waste grease mix homogeneously, to obtain the more uniform waste grease sample of composition.Agitator 1-2 of the present utility model can use frequency conversion agitator, and the stirring paddle of agitator 1-2 is welded on shaft, and this stirring paddle is the above stirring paddle of two-layer, makes the waste grease in sampling groove 1 can be sufficiently mixed uniformly by the stirring paddle of multilamellar.This utility model cell body 1-5 top can be provided with groove lid, and groove lid is provided with charge door.nullThis utility model is also shown in Fig. 1、Shown in 2，Cell body 1-5 top is open type，And bearing support 1-7 includes the framework being fixed on cell body 1-5 inwall and the backbar being connected in framework，This backbar includes longeron or crossbeam，Can also is that the longitudinal and cross beam that backbar is connected，The intensity of sampling groove 1 can not only be increased，And agitator 1-2 and flase floor 1-3 can be conveniently installed again，Make this utility model backbar and framework that cell body 1-5 upper part is divided at least two cavity for installing flase floor 1-3，Backbar is or/and framework is provided with at least two-layer in order to install the bearing 1-4 of each layer flase floor 1-3 along short transverse，Utility model framework or backbar are provided with at least three thief hole 1-6，Or the periphery of each flase floor 1-3 is provided with at least two thief hole 1-6，Within every batch of waste grease adds sampling groove 1，Can be by the thief hole 1-6 of the multiple diverse locations on sampling groove 1，Every batch of waste grease supplied materials is sampled detection，Can be using the meansigma methods of desirable waste grease composition as the actual physicochemical character of this batch materials，The collection of energy effective specification restaurant waste grease，And retrain restaurant with the unexpected infringement such as sell.Spilling when this utility model can prevent waste grease discharging and during stirring, as shown in Figure 1, the top of cell body 1-5 is placed with baffle plate 1-1, baffle plate 1-1 height and is being arranged on 20mm～100mm, and this baffle plate 1-1 could be secured on cell body 1-5
As shown in Figure 1, this utility model connecting tube 4 one end is connected to the bottom of cell body 1-5, the other end is connected to the import department on the reception storehouse 2-2 of pre-treatment mechanism 2, connecting tube 4 is provided with the gate valve 4-1 that can automatically control, this gate valve 4-1 can use electric gate valve or Pneumatic gate valve, after sampling terminates, waste grease after making coarse filtration by control gate valve 4-1 enters in pre-treatment mechanism 2, also can effectively reduce the working strength of operator by automatically controlling gate valve 4-1.
Such as Fig. 1, shown in 2, this utility model pre-treatment mechanism 2 includes reception storehouse 2-2 and the steam pipe 2-4 being provided with top cover 2-1, the many groups steam pipe 2-4 being provided with multiple pore is arranged on the middle and lower part receiving storehouse 2-2, when outdoor temperature is relatively low, open the intake valve on the air supply pipe in vapour system, by steam by waste grease being heated in steam pipe 2-4, to melt the animal oil of solidification in waste grease.As shown in Fig. 1～3, this utility model steam pipe 2-4 uses stainless steel tube, this steam pipe 2-4 arranges along the bottom receiving storehouse 2-2 and is connected with air supply pipe, this air supply pipe is also adopted by stainless steel tube, the most multiple rows of setting of spray orifice on steam pipe 2-4, and adjacent two row's spray orifices radially between folder degree α 45～90 ° of settings that are staggered, these adjacent two row's spray orifices radially between folder degree α can be staggered setting 40 °, 45 ° or 60 °, in all directions, the waste grease in reception storehouse 2-2 quickly can be heated.As shown in Figure 1, this utility model is provided with collecting tank 2-7 in receiving storehouse 2-2, it is provided with in the 2-2 of this reception storehouse and porous filter pocket 3-1 front end connecting partition 2-5, collecting tank 2-7 can be formed in porous filter pocket 3-1 bottom, make filtrate be discharged to collecting tank 2-7 by porous filter pocket 3-1 sieve aperture 3-11, discharge finally by being arranged on the leakage fluid dram 2-8 of minimum point in collecting tank 2-7.
See Fig. 1, shown in 2, this utility model receives the postmedian of storehouse 2-2 and is provided with along the most tilting deslagging screw mechanism 3 of feed direction, the porous filter pocket 3-1 that this deslagging screw mechanism 3 is U-shaped in including being arranged on reception storehouse 2-2, it is connected to receive the sleeve 3-3 and shaftless deslagging spiral 3-2 of storehouse 2-2 outer closures and drive motor 3-5, motor 3-5 is driven to be connected with shaftless deslagging spiral 3-2, shaftless deslagging spiral 3-2 is arranged in porous filter pocket 3-1 and sleeve 3-3, and sleeve 3-3 rear portion is provided with slag-drip opening 3-4, motor 3-5 is driven to drive shaftless deslagging spiral 3-2 to rotate, material slag after dehydration is discharged from slag-drip opening 3-4.As shown in Fig. 1,4,5, this utility model porous filter pocket 3-1 is provided with multiple rows of sieve aperture 3-11, the sieve aperture 3-11 of this porous filter pocket 3-1 can be up-small and down-big tubaeform, and sieve aperture 3-11 end diameter is 6～25mm, this end diameter is 8～20mm, make sieve aperture 3-11 both be difficult to stifled slag, can facilitate again and the sieve aperture 3-11 on porous filter pocket 3-1 is rushed Xian.The external diameter of this utility model shaftless deslagging spiral 3-2 along conveying direction the most from large to small, pitch from large to small, it is provided with leakage fluid dram 2-8 at the collecting tank 2-7 of shaftless deslagging spiral 3-2 bottom, this utility model shaftless deslagging spiral 3-2 is a shaftless reducing varying pitch structure, in the rotary course of shaftless deslagging spiral 3-2, solid phase residue is extruded dehydration, residue moisture content after its dehydration is about about 70%, and final residue is discharged from the slag-drip opening 3-4 of collecting tank 2-7 lowest part.This utility model shaftless deslagging spiral 3-2 periphery is fixed with the stainless steel brush 3-6 for clearing up filter opening, continuously or discontinuously can arrange in shaftless deslagging spiral 3-2 periphery, make stainless steel brush 3-6 can produce certain amount of deflection when shaftless deslagging spiral 3-2 operates, make to produce certain effect of scraping clearly between stainless steel brush 3-6 energy and porous filter pocket 3-1, thus play the effect of cleaning sieve aperture 3-11, in running, keep the ability of solid-liquid separation, make filtrate be discharged to collecting tank 2-7 by sieve aperture 3-11 and discharge from leakage fluid dram 2-8.
Such as Fig. 1, shown in 2, the top of this utility model collecting tank 2-7 is provided with the least one set corresponding with porous filter pocket 3-1 and has the wash tub pipe 2-6 of high-pressure nozzle, by high-pressure nozzle on many group wash tub pipe 2-6, the sieve aperture 3-11 of porous filter pocket 3-1 can be carried out backwash, sieve aperture 3-11 cleaning is conducive to prevent blocking, the ability of solid-liquid separation can be increased further, keep the disposal ability of equipment.
Such as Fig. 1, shown in 2, this utility model receives the top cover 2-1 of storehouse 2-2 and is provided with to monitor and receives the radar levelmeter 2-10 of liquid level in the 2-2 of storehouse and for collecting deodorization collection port 2-3 of foul smell, by radar levelmeter 2-10 on Central Control Room and equipment control box can real-time monitored to liquid level in warehouse, and foul smell is collected in processing procedure and focused on by deodorization collection port 2-3 on top cover 2-1, secondary pollution will not be produced to external world.This utility model is safeguarded for ease of giving, and the top cover 2-1 receiving storehouse 2-2 and the rear portion receiving storehouse 2-2 are provided with the manhole 2-9 of quick opening structure.
Such as Fig. 1, shown in 2, when waste grease discharging is to sampling groove 1, by flase floor 1-3, bigger material such as plastics etc. are trapped, rest materials enters in cell body 1-5, open agitator 1-2 in sampling groove 1, under the effect of low speed hydraulic mixing, oil water mixture uniformly mixes, and is sampled homogeneous material by the thief hole 1-6 on cell body 1-5, is analyzed.After sampling terminates, start gate valve 4-1, the material after sampling is made to be drained in the reception storehouse 2-2 of pre-treatment mechanism 2 by connecting tube 4, it is monitored by radar levelmeter 2-10, when receiving the certain liquid level of liquid arrival in the 2-2 of storehouse, open and drive motor 3-5 to drive shaftless deslagging spiral 3-2 to rotate, in the operation process of shaftless deslagging spiral 3-2, on the one hand solid phase residue is extruded dehydration in the porous filter pocket 3-1 of shaftless deslagging spiral 3-2 bottom, residue moisture content after the right side makes dehydration is about about 70%, and discharged by slag-drip opening 3-4, and filtrate is by porous filter pocket 3-1 drip to collecting tank 2-7, discharged by leakage fluid dram 2-8, the most stainless steel brush 3-6 constantly clears up with the sieve aperture 3-11 of porous filter pocket 3-1.When outdoor temperature is relatively low, opens steam feed valve, waste grease is heated, to melt the animal oil of solidification in waste grease.Periodically flase floor 1-3 it is replaced and clears up, periodically porous filter pocket 3-1 being carried out backwash simultaneously.This utility model not only can meet the function of supplied materials sampling, the impurity of more than 90% in the most removable waste grease, can effectively reduce the problem causing follow-up equipment blocking repair rate high because impurity exists.
Claims (10)
1. a waste grease receives sampling pretreating device, it is characterized in that: include sampling groove (1), pre-treatment mechanism (2), deslagging screw mechanism (3) and be used for the connecting tube (4) connecting between sampling groove (1) and pre-treatment mechanism (2), described sampling groove (1) includes cell body (1-5), flase floor (1-3) and agitator (1-2), at least two-layer is provided with the removable top being arranged on cell body (1-5) of flase floor (1-3) of perforate (1-31), perforate (1-31) on each layer flase floor (1-3) is staggered setting, there is on cell body (1-5) charge door and at least three thief hole (1-6), agitator (1-2) is arranged on the bearing support (1-7) on cell body (1-5) top；Described connecting tube (4) one end is connected to the bottom of cell body (1-5), the other end is connected to the import department on the reception storehouse (2-2) of pre-treatment mechanism (2), and connecting tube (4) is provided with the gate valve (4-1) that can automatically control；Described pre-treatment mechanism (2) includes the reception storehouse (2-2) being provided with top cover (2-1) and organizes steam pipe (2-4) more, the steam pipe (2-4) being provided with multiple pore is arranged on the middle and lower part of reception storehouse (2-2), and is provided with collecting tank (2-7) in reception storehouse (2-2)；nullThe postmedian of described reception storehouse (2-2) is provided with along the most tilting deslagging screw mechanism (3) of feed direction，The porous filter pocket (3-1) that described deslagging screw mechanism (3) is U-shaped in including being arranged on reception storehouse (2-2)、It is connected to receive the sleeve (3-3) of storehouse (2-2) outer closures and shaftless deslagging spiral (3-2) and drive motor (3-5)，Motor (3-5) is driven to be connected with shaftless deslagging spiral (3-2)，Shaftless deslagging spiral (3-2) is arranged in porous filter pocket (3-1) and sleeve (3-3)，Sleeve (3-3) rear portion is provided with slag-drip opening (3-4)，Porous filter pocket (3-1) is provided with multiple rows of sieve aperture (3-11)，And the external diameter of shaftless deslagging spiral (3-2) is along conveying direction the most from large to small、Pitch is from large to small，Shaftless deslagging spiral (3-2) periphery is fixed with the stainless steel brush (3-6) for clearing up filter opening，The collecting tank (2-7) being positioned at shaftless deslagging spiral (3-2) bottom is provided with leakage fluid dram (2-8)，And the top of collecting tank (2-7) is provided with the least one set corresponding with porous filter pocket (3-1) and has the wash tub pipe (2-6) of multiple high-pressure nozzle.
nullA kind of waste grease the most according to claim 1 receives sampling pretreating device，It is characterized in that: described cell body (1-5) top is open type，Described bearing support (1-7) includes the framework being fixed on cell body (1-5) inwall and the backbar being connected in framework，Described backbar includes longeron or crossbeam，Or backbar includes the longitudinal and cross beam that is connected，Make backbar and framework that cell body (1-5) upper part is divided at least two cavity for installing flase floor (1-3)，Backbar is or/and framework is provided with at least two bearing (1-4) for grafting each layer flase floor (1-3) along short transverse，And framework or backbar are provided with at least three thief hole (1-6)，Or the periphery of each flase floor (1-3) is provided with at least two thief hole (1-6).
A kind of waste grease the most according to claim 1 and 2 receives sampling pretreating device, it is characterized in that: the top of described cell body (1-5) is provided peripherally with baffle plate (1-1), and baffle plate (1-1) height is being arranged on 20mm～100mm.
A kind of waste grease the most according to claim 1 and 2 receives sampling pretreating device, it is characterised in that: the stirring paddle on described agitator (1-2) is welded on shaft, and stirring paddle is more than two-layer.
A kind of waste grease the most according to claim 1 receives sampling pretreating device, it is characterized in that: the top cover (2-1) of described reception storehouse (2-2) is provided with to monitor and receives the radar levelmeter (2-10) of storehouse (2-2) interior liquid level and for collecting the deodorization collection port (2-3) of foul smell, and the top cover (2-1) receiving storehouse (2-2) and the rear portion receiving storehouse (2-2) are provided with the manhole (2-9) of quick opening structure.
A kind of waste grease the most according to claim 1 receives sampling pretreating device, it is characterized in that: be provided with the dividing plate (2-5) being connected with porous filter pocket (3-1) front end in described reception storehouse (2-2), and form collecting tank (2-7) in porous filter pocket (3-1) bottom.
A kind of waste grease the most according to claim 1 receives sampling pretreating device, it is characterized in that: the sieve aperture (3-11) of described porous filter pocket (3-1) is up-small and down-big tubaeform, and the end diameter of sieve aperture (3-11) is 6～25mm.
A kind of waste grease the most according to claim 1 receives sampling pretreating device, it is characterized in that: described steam pipe (2-4) uses stainless steel tube, folder degree α between the most multiple rows of setting of spray orifice on steam pipe (2-4), and adjacent two row's spray orifices radial directions is 45～90 ° of settings that are staggered.
A kind of waste grease the most according to claim 1 receives sampling pretreating device, it is characterized in that: the described perforate (1-31) on flase floor (1-3) is circular hole or polygonal hole and arranges in array, and the aperture of perforate (1-31) is between 15～40mm, and distance H between adjacent apertures (1-31) is between 50～100mm.
A kind of waste grease the most according to claim 1 receives sampling pretreating device, it is characterised in that: the described perforate (1-31) on flase floor (1-3) is grizzly bar shape.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620191487.0U CN205449630U (en) | 2016-03-11 | 2016-03-11 | Waste oil receives preceding processing apparatus of sample |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620191487.0U CN205449630U (en) | 2016-03-11 | 2016-03-11 | Waste oil receives preceding processing apparatus of sample |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205449630U true CN205449630U (en) | 2016-08-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620191487.0U Withdrawn - After Issue CN205449630U (en) | 2016-03-11 | 2016-03-11 | Waste oil receives preceding processing apparatus of sample |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205449630U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105606431A (en) * | 2016-03-11 | 2016-05-25 | 江苏维尔利环保科技股份有限公司 | Waste grease receiving, sampling and pretreating device |
-
2016
- 2016-03-11 CN CN201620191487.0U patent/CN205449630U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105606431A (en) * | 2016-03-11 | 2016-05-25 | 江苏维尔利环保科技股份有限公司 | Waste grease receiving, sampling and pretreating device |
| CN105606431B (en) * | 2016-03-11 | 2018-05-25 | 江苏维尔利环保科技股份有限公司 | Waste grease receives sampling pretreating device |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160810 Effective date of abandoning: 20180525 |
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| AV01 | Patent right actively abandoned |