CN201164845Y - Biochemical consecutive processing system for restaurant garbage - Google Patents
Biochemical consecutive processing system for restaurant garbage Download PDFInfo
- Publication number
- CN201164845Y CN201164845Y CNU2008200430940U CN200820043094U CN201164845Y CN 201164845 Y CN201164845 Y CN 201164845Y CN U2008200430940 U CNU2008200430940 U CN U2008200430940U CN 200820043094 U CN200820043094 U CN 200820043094U CN 201164845 Y CN201164845 Y CN 201164845Y
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- treating apparatus
- food waste
- treatment system
- changing food
- biochemical
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Abstract
The utility model relates to a culinary garbage biochemical continuous processing system and the method thereof, wherein, the system comprises a feeding device, a processing device connected with the feeding device, a discharging device connected with the processing device, an air inlet system connected with the processing device, as well as an air outlet system and a supporting and rotating device which are connected with the processing. The feeding device and the discharging device are arranged at two ends of the processing device; the air inlet system and the discharging device are arranged at the same end of the processing device; the air outlet system and the feeding device are arranged at the same end of the processing device.
Description
Technical field
The treatment system of the utility model design changing food waste particularly relates to a kind of changing food waste biochemical continuous treatment system.
Background technology
Changing food waste belongs to a kind of of house refuse, Chinese utility model patent (publication number: CN 1872437A) disclose rotary changing food waste biochemical treatment system of a kind of sphere and method thereof.This system comprises switch type hot-blast stove, garbage disposer, deodorizing deduster.Hot-blast stove inside is provided with hot-air exchange pipe, the inlet of this exchange pipe connects air filter, its outlet connects processor through warm-air pipe and air-heater, this processor is a spherical shell, which is provided with into, discharging opening, its inwall is provided with flight, and its two ends are symmetrically fixed with the hollow tile axle, the hollow tile of the end decelerator that is coupling wherein, this end connects sealing deodorizing deduster through blast pipe, air-introduced machine, flue gas leading.Said system is owing to there is following defective in structural reason: 1, batch production, and production capacity is limited; 2, production efficiency is lower; 3, production cost is higher relatively.Therefore, we press for a kind of can the overcome system of above-mentioned shortcoming and the production method that matches.
The utility model content
The utility model is the shortcoming according to prior art, and a kind of efficient, energy-saving and environmental protection and can quantity-produced changing food waste biochemical continuous treatment system are provided.
The utility model is achieved through the following technical solutions: a kind of changing food waste biochemical continuous treatment system, comprise feed arrangement, inlet duct, treating apparatus, drawing mechanism, exhaust apparatus and support whirligig,
Described feed arrangement comprises a spiral pusher machine;
Described treating apparatus comprises a biochemical reaction device, and described treating apparatus is connected with described feed arrangement;
Described drawing mechanism comprises at least one collision discharging opening that is distributed in described treating apparatus one end and the impact curve plate that is positioned at described treating apparatus same side below, described impact curve plate matches to realize continuous discharging with described collision discharging opening, and described feed arrangement and described drawing mechanism are positioned at the two ends of described treating apparatus;
Described inlet duct comprises the insulating tube that heat-resisting wind furnace that heat-exchange device is connected with described heat-exchange device is connected with described heat-resisting wind furnace, the insulating tube that is connected with described heat-resisting wind furnace, described inlet duct is connected with described treating apparatus, and described inlet duct and described drawing mechanism are positioned at the same side of described treating apparatus;
Described exhaust apparatus comprises the exhaust gas processing device that the tail gas export cylinder is connected with described tail gas export cylinder, and described exhaust apparatus is connected with described treating apparatus, and described exhaust apparatus and described feed arrangement are positioned at the same side of described treating apparatus.
Preferably, described heat-exchange device is an oxygen supply sterilization hot-blast stove.
Preferably, described treating apparatus comprises a preheating mixing arrangement, and described preheating mixing arrangement is between described feed arrangement and described biochemical reaction device.
Preferably, described treating apparatus comprises a drying and sterilizing device and cooling device, and described drying and sterilizing device is connected with described biochemical reaction device, and described cooling device is connected with described drying and sterilizing device.
Preferably, described preheating mixing arrangement, described biochemical reaction device and described drying and sterilizing device are rolled by the double-level-metal thin plate and form, in the middle of described double-level-metal thin plate, be filled with heat-insulation layer, described cooling device comprise cooling chamber and match with described cooling chamber be positioned at cooling chamber top spray thrower, described cooling chamber is rolled by the single-layer metal thin plate and forms.
Preferably, described exhaust gas processing device comprises primary purification chamber, the secondary injection absorption chamber that is connected with described primary purification chamber, the water storing tank that is connected with described secondary injection absorption chamber, the circulation power pump that is connected with described secondary injection absorption chamber and described water storing tank.
Preferably, described preheating mixing arrangement, described biochemical reaction device, described drying and sterilizing device and described cooling chamber are built-in with material rotating plate.
Preferably, described insulating tube is positioned at described cooling chamber inside, and the hot blast ejiction opening of described insulating tube is positioned at the end of described cooling chamber near described drying and sterilizing device.
Implement the utility model, following beneficial effect is arranged: because the utility model is changed into continous way production with traditional batch production, therefore improved greatly to produce and renderd a service and disposal ability, can build up daily handling ability at 100～150 tons wall scroll production line, the production of units floor space is littler simultaneously, more saves production cost.Production can also bring the reduction of power source consumption and more easily control the quality of production and reduce labor strength continuously.
Description of drawings
Fig. 1 is the structural representation of a specific embodiment of the utility model changing food waste biochemical continuous treatment system;
Fig. 2 is the structural representation of feed arrangement and tail gas export cylinder among Fig. 1;
Fig. 3 is the cross-sectional figure of preheating mixing arrangement among Fig. 1;
Fig. 4 is the cross-sectional figure of Fig. 1 mesophytization reaction unit;
Fig. 5 is the cross-sectional figure of drying and sterilizing device among Fig. 1;
Fig. 6 is the cross-sectional figure of cooling chamber among Fig. 1;
Fig. 7 is the structural representation of drawing mechanism among Fig. 1;
Fig. 8 is that the A of drawing mechanism among Fig. 7 is to view;
Fig. 9 is the structural representation of oxygen supply sterilization hot-blast stove among Fig. 1;
Figure 10 is the structural representation of exhaust gas processing device among Fig. 1.
The specific embodiment
Below in conjunction with accompanying drawing the utility model changing food waste biochemical continuous treatment system further is described in detail.
Shown in Figure 1 is the structural representation of a utility model changing food waste biochemical continuous treatment system and a preferred embodiment of method thereof.The utility model changing food waste biochemical continuous treatment system mainly is made of inlet duct 3, exhaust apparatus 1, treating apparatus, drawing mechanism 4, feed arrangement 2 and support whirligig 6.Treating apparatus mainly comprises cooling device 5, drying and sterilizing device 9, biochemical reaction device 8, preheating mixing arrangement 7 again.Inlet duct 3 mainly comprises heat-exchange device, heat resisting exhauster 32 and insulating tube 33, and heat-exchange device is an oxygen supply sterilization hot-blast stove 31.Cooling device 5 mainly comprises cooling chamber 51 and spray thrower 52, spray thrower 52 is positioned at cooling chamber 51 tops, but spray thrower spraying cooling liquid, make the material temperature in the cooling chamber 51 reduce, support whirligig 6 and mainly comprise transmission mechanism seat 61 and holder liquid seat 62, holder liquid seat 62 is arranged at the below of preheating mixing arrangement 7 near feed arrangement 2 one ends, and holder liquid seat 63 is arranged at the below of cooling chamber 51 near drawing mechanism 4 one ends.Cooling chamber 51, drying and sterilizing device 9, biochemical reaction device 8 and preheating mixing arrangement 7 are connected and fixed by connecting flange, and the axial line of the entire process device after the installation becomes 5～8 degree angles (the high discharge end of feed end is low) with horizontal line.Provide rotary power by transmission mechanism seat drive support roller and roller.
As shown in Figure 2, changing food waste is introduced into feed arrangement 2 from the feeding mouth 21 of feed arrangement 2, and changing food waste can be introduced into continuously, also can intermittently be introduced into.Feed arrangement 2 mainly comprises feeding mouth 21, inner core 22 and spiral pusher machine 27.Described tail gas export cylinder includes gas inlet 24, gas inlet 24 is communicated with urceolus 23, and urceolus 23 is communicated with tail gas outlet 26, and urceolus 23 is enclosed within inner core 22 outsides, inner core 22 is built-in with helical stir plate 25, and helical stir plate 25 is the agitating device of spiral pusher machine 27.
The cross-sectional figure of preheating mixing arrangement 7 shown in Figure 3, preheating mixing arrangement 7 is by connecting flange 74 and 2 coaxial connections of feed arrangement, and preheating mixing arrangement 7 opposite sides have a connecting flange (not shown) to be connected with biochemical reaction device 8 equally.The shell 71 of preheating mixing arrangement 7 is a sheet metal, stainless sheet steel for example, and inner bag 72 is similarly the layer of metal thin plate, and stainless sheet steel for example, shell 71 and inner bag 72 are not required to be the sheet metal of commaterial.Filled one deck heat-insulation layer 73 between shell 71 and inner bag 72, heat-insulation layer 73 can be made for any stable in properties has the material of function of heat insulation.Evenly arranged upright material rotating plate 74 on the inwall of inner bag 72, make changing food waste, bacterial classification, auxiliary additive evenly stir inside, fully mix, and the temperature of charge behind the mixing brought up to the suitable temperature (heat energy is provided by the waste heat that provides behind the biochemical reaction) of biochemical reaction, tail gas after simultaneously biochemical reactor being handled is discharged, and handles for exhaust apparatus 1.
The cross-sectional figure of the biochemical reaction device 8 among Fig. 1 shown in Figure 4.Biochemical reaction device 8 is a diameter than big spheroid of drying and sterilizing device 9 and preheating mixing arrangement 7 or six to eight gengon, its diameter will compare drying and sterilizing device 9 and preheating mixing arrangement 7 is big by 1/5 to 2/5, and purpose is indoor always maintain relatively on a small quantity " expecting always " (waste heat after biochemical reaction heat energy is taken from dried material) of biochemical reaction when normal operation.Four groups of temp probe (not shown) evenly are housed on the biochemical reaction device inwall, transmit signals to programmable logic controller (PLC) (Programmable Logic Controller, PLC, not shown in the figures) control biochemical reaction temperature.Press direct current generator " electric brush type principle " during the rotation thermometric, only measure the temperature of bottom (material) and top (air-flow).The shell 81 and the inner bag 82 of the biochemical reaction device 8 among Fig. 4 are made for sheet metal, accompany heat-insulation layer 83 in the middle of shell 81 and the inner bag 82, and heat-insulation layer 83 can be made for any stable in properties has the material of function of heat insulation.The inwall of inner bag 82 is evenly distributed with 45 degree material rotating plates 85, makes that 45 degree material rotating plates 85 can stir material, and it is heated evenly when biochemical reaction device 8 rotations.
The cross-sectional figure of drying and sterilizing device shown in Figure 5, one end are provided with connecting flange 94 and are connected to a fixed with biochemical reaction device, and the other end has another connecting flange (not looking among the figure) and cooling device to be connected and fixed.The shell 91 and the inner bag 92 of drying and sterilizing device form for sheet metal rolls, and two sheet metals can be different materials and make, and also can use same material, for example all use stainless sheet steel.Accompany heat-insulation layer 93 in the middle of shell 91 and inner bag 92, heat-insulation layer 93 can be made for any stable in properties has the material of function of heat insulation.The inwall of inner bag 92 is evenly distributed with 45 degree material rotating plates 95 and 90 degree material rotating plates 96, make when drying and sterilizing device 9 rotations, 45 degree material rotating plates 95 and 90 degree material rotating plates 96 can stir material, it is heated evenly, thereby the material after biochemical reaction finished carries out drying and dehydrating, make the product water content be reduced to qualified requirement, utilize the xeothermic further kill harmful bacterium of high temperature simultaneously.
That shown in Figure 6 is the cross-sectional figure of cooling chamber 51.One end of cooling chamber 51 is provided with connecting flange 513 and is connected to a fixed with dry sterilization 9 devices.The inner bag 511 of cooling chamber 51 is rolled by the layer of metal thin plate and forms, for example the stainless steel metal thin plate.The inwall of inner bag 511 is evenly distributed with 45 degree material rotating plates 512, makes that 45 degree material rotating plates 512 can stir material, and it is heated evenly when cooling chamber 51 rotations.
Shown in Figure 7 is the structural representation of drawing mechanism 4 among Fig. 1, and Fig. 8 is that the A of drawing mechanism 4 among Fig. 7 is to view.With reference to figure 7, Fig. 8, the collision discharging opening 42 that drawing mechanism 4 mainly comprises impact curve plate 41 and matches with it.Switchboard 43 is installed on the collision discharging opening 42, and collision ball 44 is welded on switchboard 43 1 ends, and tension spring 45 is fixed between switchboard 43 and cooling chamber 51 outer walls.As shown in Figure 1, insulating tube 33 is built in the cooling chamber 51.The hot-wind inlet 46 of insulating tube 33 is positioned at cooling chamber 51 outsides, is connected by pipeline with heat resisting exhauster 32, and hot blast ejiction opening 47 is positioned at cooling chamber 51 inner ends near drying and sterilizing devices 9.When cooling chamber 51 rotations, be fixed on the constantly impact curve plate 41 of process cooling chamber 51 belows of the outer equally distributed collision discharging opening of cooling chamber 51 shells 42, switchboard 43 on the collision discharging opening 42 can tightly cover collision discharging opening 42 because of the tension force of tension spring 45 when not touching impact curve plate 41, when in case it touches impact curve plate 41, fixing impact curve plate 41 can contact with 43 collisions of collision ball, make tension spring 45 be compressed, at this moment, switchboard 43 on the collision discharging opening 42 can tilt and be close to collision discharging opening 42 no longer fully, like this, material is just poured out from the discharging opening of the hopper will 42 of below.By the mode of such rotation batch turning, material can continuously be poured out.
Fig. 9 is the structural representation of oxygen supply sterilization hot-blast stove 31 among Fig. 1.Oxygen supply sterilization hot-blast stove 31 inside are provided with heat exchange component 314, after the heat (air-flow) of utilizing burner to produce enters oxygen supply sterilization hot-blast stove 31 from port 311, cold air after filtering with air cleaner 318 is respectively at the inside and outside wall antikinesis of heat exchange component 314, hot-air after the heating is exported to heat resisting exhauster 32 from hot-blast outlet 312, and then offers biochemical reaction device 8 uses by follow up device.Heat exchange component 314 is divided into many groups, can build 3 to 5 layers as required for every group, separates by partition wall 315 between group and the group.For making full use of the waste heat of oxygen supply sterilization hot-blast stove 31, the rear section design of hot blast output in stove has an internal heat type hot oil 313, the heating of employing internal heat type, in internal heat type hot oil 313 chambeies, filled the deep fat (not shown), circulation provides heat energy more than 300 ℃ for preceding operation, to replace steam boiler operation heat supply forward.
Figure 10 is the structural representation of exhaust gas processing device among Fig. 1, and exhaust gas processing device comprises primary purification chamber 11, secondary injection absorption chamber 12, water storing tank 13 and circulation power pump 14.Because changing food waste is made of multiple organic food, will produce a kind of irritating smell (but the product after the high temperature sterilization drying gives out the delicate fragrance of protein) after the mixing.In the biochemical treatment process,, immediately tail gas is discharged again and the recovery dust, course of reaction is hedged off from the outer world for smell is not leaked.This just need extract tail gas out under the prerequisite of sealing.This work is born by tail gas unit.Wherein gas inlet 17 is connected with the tail gas outlet 26 of tail gas export cylinder, thereby tail gas is imported primary purification chamber 11, and primary purification chamber 11 completely cuts off with water storing tank 13, and there is slag-drip opening 112 11 lower ends, primary purification chamber, can supply deslagging; There is peep hole 111 11 upper ends, primary purification chamber, can supply to observe the liquid level situation.Secondary injection absorption chamber 12 is communicated with water storing tank 13.There are peep hole 121 and overflow pipe 122 in secondary injection absorption chamber 12 lower ends, and there is exhaust outlet 16 upper end to be used for discharging the gas after the processing.Primary purification chamber 11 is associated with an overflow pipe 18 with secondary injection chamber 12, once condensing in primary purification chamber 11, the water vapour that biochemical reaction device 8 is brought into can enter water storing tank 13 by secondary injection chamber 12 when too much, overflow pipe 18 water inlets must be installed on 11 bottoms, primary purification chamber, water side and the primary purification chamber 11 work waters surface are level mutually, otherwise the influence operation.There is hand-hole 19 water storing tank 13 upper ends, and there is slag-drip opening 131 lower end.
Tail gas after the biochemical reaction imports below 11 liquid levels of primary purification chamber, enters 11 sky, primary purification chamber and is involved in secondary injection chamber 12 by extradition pipe 15 by air-distribution net (not shown) and carry out secondary absorption washing.The negative pressure (power) that whole process produces is provided by supercharging circulating pump 14 and injector.The dust that is mingled with in the air-flow absorbs 12 bottoms, jet chamber by primary purification chamber 11 and secondary and regularly discharges the utilization of recovery back.
The biochemical continous treatment process of changing food waste
Changing food waste from feeding mouth 21 feed arrangement 2 of packing into, is added protease thalline and wheat bran or rice bran or chaff etc. simultaneously, and spiral pusher machine 27 promotes materials and transports forward, also constantly mixes material simultaneously.After material is admitted to preheating mixing arrangement 7, because preheating mixing arrangement 7, biochemical reaction device 8, drying and sterilizing device 9 and cooling chamber 51 are coaxial fixing by connecting flange, and the preheating mixing arrangement is higher, cooling chamber is lower, coaxial axis and ground are 5 and spend to the angle of 8 degree, so material can be sent to discharge end from feed end.Supporting 6 pairs of preheating mixing arrangements 7 of whirligig, biochemical reaction device 8, drying and sterilizing device 9 and cooling chamber 51 is rotated, so material can both be by the continuous stirring mixing of material rotating plate quilt of its inwall in preheating mixing arrangement 7, biochemical reaction device 8, drying and sterilizing device 9 and cooling chamber 51, can guarantee that like this material component mixes, it is also comparatively even to be heated.Material at first carries out the preheating mixing in preheating mixing arrangement 7 makes its temperature can reach the suitable temperature of biochemical reaction.Be admitted to then and carry out biochemical reaction in the biochemical reaction device 8, be sent at last in the dry sterilization device 9 it is carried out drying and dehydrating, make material moisture can be reduced to qualified requirement, utilize the xeothermic further kill harmful bacterium of high temperature simultaneously.Material is admitted to cooling chamber 51 and cools then, at last from 42 dischargings of collision discharging opening.Since in the processing procedure, the device good airproof performance, and material is not subjected to the erosion of extraneous assorted bacterium, has guaranteed the quality of end product.
Constantly enter in the discharge end discharging from feed end at material, hot blast also enters system from heat-exchange device 3 and provides heat for system, hot blast at first is admitted to heat resisting exhauster 3 from heat-exchange device 31, after be blown into insulating tube 33 again, contrary then material direction of advance continue to flow drying sterilizing unit 9, biochemical reaction device 8 and preheating mixing arrangement 7, after become tail gas and enter exhaust apparatus 2 from gas inlet 24, be introduced into exhaust gas processing device after the urceolus 23 of flowing through again, the tail gas outlet 26.Tail gas imports below 11 liquid levels of primary purification chamber, enters 11 sky, primary purification chamber and is involved in secondary injection absorption chamber 12 by extradition pipe 15 by the air-distribution net and carry out secondary absorption washing.The negative pressure (power) that whole process produces is provided by supercharging circulating pump 14 and injector.The dust that is mingled with in the air-flow is regularly discharged the recovery back by primary purification chamber 11 and secondary injection absorption chamber 12 bottoms and is utilized.
Above disclosed only is the preferred embodiment of the utility model changing food waste biochemical continuous treatment system, certainly can not limit the interest field of the utility model with this, therefore the equivalent variations of being done according to the utility model claim still belongs to the scope that the utility model is contained.
Claims (10)
1, a kind of changing food waste biochemical continuous treatment system comprises feed arrangement, inlet duct, treating apparatus, drawing mechanism, exhaust apparatus and support whirligig, it is characterized in that:
Described feed arrangement comprises a spiral pusher machine;
Described treating apparatus comprises a biochemical reaction device, and described treating apparatus is connected with described feed arrangement;
Described drawing mechanism comprises at least one collision discharging opening that is distributed in described treating apparatus one end and the impact curve plate that is positioned at described treating apparatus same side below, described impact curve plate matches to realize continuous discharging with described collision discharging opening, and described feed arrangement and described drawing mechanism are positioned at the two ends of described treating apparatus;
Described inlet duct comprises the insulating tube that heat-resisting wind furnace that heat-exchange device is connected with described heat-exchange device is connected with described heat-resisting wind furnace, described inlet duct is connected with described treating apparatus, and described inlet duct and described drawing mechanism are positioned at the same side of described treating apparatus;
Described exhaust apparatus comprises the exhaust gas processing device that the tail gas export cylinder is connected with described tail gas export cylinder, and described exhaust apparatus is connected with described treating apparatus, and described exhaust apparatus and described feed arrangement are positioned at the same side of described treating apparatus.
2, changing food waste biochemical continuous treatment system as claimed in claim 1 is characterized in that: described heat-exchange device is an oxygen supply sterilization hot-blast stove.
3, changing food waste biochemical continuous treatment system as claimed in claim 1 is characterized in that: described treating apparatus comprises a preheating mixing arrangement, and described preheating mixing arrangement is between described feed arrangement and described biochemical reaction device.
4, changing food waste biochemical continuous treatment system as claimed in claim 1, it is characterized in that: described treating apparatus comprises a drying and sterilizing device and cooling device, described drying and sterilizing device is connected with described biochemical reaction device, and described cooling device is connected with described drying and sterilizing device.
5, as claim 1 or claim 3 or the described changing food waste biochemical continuous treatment system of claim 4, it is characterized in that: described preheating mixing arrangement, described biochemical reaction device and described drying and sterilizing device are rolled by the double-level-metal thin plate and form, in the middle of described double-level-metal thin plate, be filled with heat-insulation layer, described cooling device comprise cooling chamber and match with described cooling chamber be positioned at cooling chamber top spray thrower, described cooling chamber is rolled by the single-layer metal thin plate and forms.
6, changing food waste biochemical continuous treatment system as claimed in claim 1 is characterized in that: described exhaust gas processing device comprises primary purification chamber, the secondary injection absorption chamber that is connected with described primary purification chamber, the water storing tank that is connected with described secondary injection absorption chamber, the circulation power pump that is connected with described secondary injection absorption chamber and described water storing tank.
7, changing food waste biochemical continuous treatment system as claimed in claim 5 is characterized in that: described preheating mixing arrangement, described biochemical reaction device, described drying and sterilizing device and described cooling chamber are built-in with material rotating plate.
8, changing food waste biochemical continuous treatment system as claimed in claim 5 is characterized in that: described insulating tube is positioned at described cooling chamber inside, and the hot blast ejiction opening of described insulating tube is positioned at the end of described cooling chamber near described drying and sterilizing device.
9, changing food waste biochemical continuous treatment system as claimed in claim 7 is characterized in that: described biochemical reaction device and the built-in material rotating plate of described cooling chamber are 45 degree material rotating plates.
10, changing food waste biochemical continuous treatment system as claimed in claim 7 is characterized in that: the built-in material rotating plate of described drying and sterilizing device is 45 degree material rotating plates and 90 degree material rotating plates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200430940U CN201164845Y (en) | 2008-01-21 | 2008-01-21 | Biochemical consecutive processing system for restaurant garbage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200430940U CN201164845Y (en) | 2008-01-21 | 2008-01-21 | Biochemical consecutive processing system for restaurant garbage |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201164845Y true CN201164845Y (en) | 2008-12-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200430940U Expired - Lifetime CN201164845Y (en) | 2008-01-21 | 2008-01-21 | Biochemical consecutive processing system for restaurant garbage |
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| CN (1) | CN201164845Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109458855A (en) * | 2018-12-25 | 2019-03-12 | 菏泽市牡丹区盛鑫源食品有限公司 | Feed high temperature sterilization cooling system |
| CN111136090A (en) * | 2020-02-05 | 2020-05-12 | 孟召阳 | High-temperature environment-friendly treatment device for garbage biomass |
-
2008
- 2008-01-21 CN CNU2008200430940U patent/CN201164845Y/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109458855A (en) * | 2018-12-25 | 2019-03-12 | 菏泽市牡丹区盛鑫源食品有限公司 | Feed high temperature sterilization cooling system |
| CN109458855B (en) * | 2018-12-25 | 2024-05-28 | 菏泽市牡丹区盛鑫源食品有限公司 | Fodder high temperature sterilization cooling system |
| CN111136090A (en) * | 2020-02-05 | 2020-05-12 | 孟召阳 | High-temperature environment-friendly treatment device for garbage biomass |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20081217 Effective date of abandoning: 20080121 |