CN202860977U - Drying machine capable of recycling residual heat - Google Patents
Drying machine capable of recycling residual heat Download PDFInfo
- Publication number
- CN202860977U CN202860977U CN 201220593263 CN201220593263U CN202860977U CN 202860977 U CN202860977 U CN 202860977U CN 201220593263 CN201220593263 CN 201220593263 CN 201220593263 U CN201220593263 U CN 201220593263U CN 202860977 U CN202860977 U CN 202860977U
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- CN
- China
- Prior art keywords
- residual heat
- air outlet
- shell
- air inlet
- housing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/18—Flow directing inserts
- C12M27/20—Baffles; Ribs; Ribbons; Auger vanes
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/26—Conditioning fluids entering or exiting the reaction vessel
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
- C12M41/20—Heat exchange systems, e.g. heat jackets or outer envelopes the heat transfer medium being a gas
Abstract
The utility model discloses a drying machine capable of recycling residual heat. The drying machine comprises a shell; the shell is driven by a gear box to be overturned; the shell is internally provided with an inclined blade for driving materials to be overturned; a blanking hopper is arranged above the right end of the shell; a high-temperature air inlet is arranged in the middle of the right end of the shell; a residual heat air outlet is arranged in the upper part of the left end of the shell; the residual heat air outlet is connected with a hot air diffusion device through an air inlet pipe; and the lower part of the left end of the shell is provided with an inclined downward discharging pipe. According to the drying machine disclosed by the utility model, the residual heat air outlet is connected with the hot air diffusion device through the air inlet pipe; and the hot air diffusion device can be arranged in a fermentation pot, and enables household garbage to be rapidly fermented and decomposed due to the self gravity of the garbage through a method of storing heavy pressure in the pot and heating by the hot air diffusion device. Therefore, the fermentation time is reduced, the fermentation period is shortened and the speed of treating the household garbage is increased. The residual heat of the drying machine is reutilized so that the energy source is saved and the environmental pollution is reduced.
Description
Technical field
The utility model relates to dryer.
Background technology
Traditional dryer, the waste heat wind that produces in the drying course is directly discharged, and has not only wasted the energy, and has polluted environment.
The present major part of house refuse in the city has realized that classification processes, rubbish after classification is processed, with organic solid waste by fermentation, be crushed into fertilizer.The quality of organic refuse fermentation directly has influence on the fertilizer efficiency for the treatment of effect and the fertilizer of rubbish, and a factor that affects organic refuse fermentation is exactly temperature.
How to utilize the waste heat of dryer to promote the fermentation of organic waste, become a problem that has prospect.
The utility model content
Technical problem to be solved in the utility model just provides a kind of residual heat recovery dryer that is applicable to the organic waste Rapid Fermentation, energy savings not only, and environmental contamination reduction, can impel simultaneously the house refuse Rapid Fermentation to decompose, thereby shorten fermentation time and cycle, accelerate the speed of domestic rubbish disposal, also improved accordingly the fertilizer efficiency of tunning fertilizer.
For solving the problems of the technologies described above, the utility model adopts following technical scheme: a kind of residual heat recovery dryer, it is characterized in that: comprise housing, the housing of described dryer drives upset by gear-box, there is dihedral vane to impel material turning in the housing, housing right-hand member top is provided with hopper, housing right-hand member middle part is provided with the high temperature air inlet, housing left end top is provided with the waste heat air outlet, described waste heat air outlet is connected with a hot blast device for dispensing by blast pipe, and described housing left end bottom is provided with a discharge duct under being tilted to.
As preferably, described hot blast device for dispensing comprises the loose solar or lunar halo of a horizontally disposed annular, and described loose solar or lunar halo is provided with the air outlet of an air inlet and several gondola water faucet shapes, and air inlet connects blast pipe.
As preferably, described air outlet is uniformly distributed in loose solar or lunar halo bottom.
As preferably, described air outlet tilts to loose solar or lunar halo outer circumferential sides below.
As preferably, described air inlet is located on the loose solar or lunar halo outer ring surface.
As preferably, described blast pipe is provided with the waste heat air-introduced machine at the waste heat air opening end.
The waste heat air outlet of the utility model dryer is connected with a hot blast device for dispensing by blast pipe, and this hot blast device for dispensing can be located in the fermentation tank, and this fermentation tank is a kind of fermentation tank without piling up the place, can carry out stereo stocking weight heating fermentation.Have the saving soil, non-environmental-pollution without the characteristics of atmosphere pollution, through the weight of rubbish self, stores the way that weight and hot blast device for dispensing are heated in tank, impel the house refuse Rapid Fermentation to decompose.Thereby reduced fermentation time, shortened fermentation period, accelerated the speed of domestic rubbish disposal.And the dryer waste heat has also obtained recycling, energy savings not only, and reduced environmental pollution.
Description of drawings
Below in conjunction with the drawings and specific embodiments the utility model is further described:
Fig. 1 is for using the structural representation of Zymolysis Equipment of the present utility model;
Fig. 2 is the structural representation of hot blast device for dispensing.
The specific embodiment
Specify embodiment of the present utility model below in conjunction with Fig. 1 and Fig. 2, this dryer 3 comprises housing 30, housing 30 drives upset by gear-box, there is dihedral vane to impel material turning in the housing, housing right-hand member top is provided with hopper 31, and housing right-hand member middle part is provided with high temperature air inlet 32, and housing left end top is provided with waste heat air outlet 34, described waste heat air outlet is connected by blast pipe 25 with the air inlet of hot blast device for dispensing, and described housing left end bottom is provided with a discharge duct 33 under being tilted to.
And the fermentation tank 1 of the organic waste 14 that is used for fermenting comprises tank body 13, and tank body 13 tops are provided with feeding port 10, and the tank body bottom is provided with feed opening 11, and hot blast device for dispensing 2 is located in the tank body 13, fills organic waste 14 in the tank body.
Hot blast device for dispensing 2 comprises the loose solar or lunar halo 20 of a horizontally disposed annular, and described loose solar or lunar halo is provided with the air outlet 21 of an air inlet 22 and several gondola water faucet shapes.Described air outlet is uniformly distributed in loose solar or lunar halo bottom.Described air outlet tilts to loose solar or lunar halo outer circumferential sides below.Described air inlet is located on the loose solar or lunar halo outer ring surface.Described air inlet connects blast pipe 25, and described blast pipe is provided with waste heat air-introduced machine 24, and described waste heat air-introduced machine connects waste heat air outlet 34.Gondola water faucet can prevent that down the air-out micropore of gondola water faucet is blocked.
As the improvement of above-described embodiment, can also increase a marsh gas stove, the high warm air that described biogas furnace combustion produces is introduced the high temperature air inlet 32 of dryer by warm-air pipe.The tank body top of described fermentation tank is provided with blast pipe 12 and connects marsh gas stove on feeding port 10 next doors.
As the distortion of above-described embodiment, described hot blast device for dispensing comprises a spiralling loose airduct, and described loose airduct is provided with several air outlets.
Perhaps described hot blast device for dispensing also can arrange like this, and this hot blast device for dispensing comprises a loose wind supervisor who vertically is located at the tank body center, is distributed with several loose wind branched pipes on the described loose wind supervisor, and loose wind branched pipe is provided with several air outlets.
The below specifies operation principle of the present utility model:
Its work mainly may further comprise the steps:
1, the high warm air that produces of the high temperature very hot oven in the methane cooker enters dryer 3 through air-introduced machine, and dryer is to the organic waste oven dry of overturning;
2, the waste heat of dryer 3 most ends is discharged through air-introduced machine 24;
3, enter air inlet 22 through blast pipe 25;
4, enter again heat radiation solar or lunar halo 20, through air outlet 21 waste heat is slowly scattered and evenly in rubbish, discharge, make in the whole tank body and heat up;
5, organic waste 14 enters fermentation tank 1 through feeding port 10, and tank body 13 is higher, stores manyly, and tank diameter is larger, stores more;
6, organic waste 14 enters after the fermentation tank 1, and all organic wastes evenly are deposited in the tank body 13;
7, the organic waste of piling up is piled higher and higher, and more heap is heavier, makes organic waste produce gravity pressure, and organic waste is pressed more closely knit and more closely knit, thereby organic waste produces the heat fermentation, impels the Humic Substances fermentation in the organic waste to decompose.
8, air outlet 21 hot blast of discharging enters among the organic waste of fermentation tank lower end equably, however heat move on slowly, the organic waste in the whole fermentation tank is heated up, impel the organic waste Rapid Fermentation;
9, produce biogas in the tank body by fermentation, discharge by blast pipe 12, enter the methane cooker internal combustion, the high warm air that the very hot oven through burning produces enters in the dryer again heats, so iterative cycles utilization.
In a word, technique scheme is that rubbish produces the gravity pressure intensification and external waste heat aerating heats up, i.e. the process of fermentation is accelerated in dual intensification.
Dryer and fermentation tank and marsh gas stove in the technique scheme have formed fermentation tank---cyclic utilization system of marsh gas stove---dryer---fermentation tank, and thus iterative cycles comprehensive utilization, its beneficial effect is:
1) utilize the waste heat in the oven dry that intensification in the fermentation tank body is provided, fermentation is decomposed;
2) utilize the rubbish intensification fermentation in the fermentation tank to produce biogas, biogas furnace combustion is provided, can save fire coal, save coal resources, protection of the environment;
3) very hot oven behind the biogas furnace combustion provides the dryer heat supply, with the fertilizer oven dry, carries out next procedure processing again.
Claims (6)
1. residual heat recovery dryer, it is characterized in that: comprise housing (30), the housing of described dryer (30) drives upset by gear-box, there is dihedral vane to impel material turning in the housing, housing right-hand member top is provided with hopper (31), housing right-hand member middle part is provided with high temperature air inlet (32), housing left end top is provided with waste heat air outlet (34), described waste heat air outlet is connected with a hot blast device for dispensing by blast pipe (25), and described housing left end bottom is provided with a discharge duct (33) under being tilted to.
2. residual heat recovery dryer according to claim 1, it is characterized in that: described hot blast device for dispensing comprises the loose solar or lunar halo (20) of a horizontally disposed annular, described loose solar or lunar halo is provided with the air outlet (21) of an air inlet (22) and several gondola water faucet shapes, and air inlet connects blast pipe (25).
3. residual heat recovery dryer according to claim 2 is characterized in that: described air outlet is uniformly distributed in loose solar or lunar halo bottom.
4. residual heat recovery dryer according to claim 3 is characterized in that: described air outlet tilts to loose solar or lunar halo outer circumferential sides below.
5. residual heat recovery dryer according to claim 4 is characterized in that: described air inlet is located on the loose solar or lunar halo outer ring surface.
6. residual heat recovery dryer according to claim 5 is characterized in that: described blast pipe (25) is provided with waste heat air-introduced machine (24) at waste heat air outlet (34) end.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220593263 CN202860977U (en) | 2012-11-12 | 2012-11-12 | Drying machine capable of recycling residual heat |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220593263 CN202860977U (en) | 2012-11-12 | 2012-11-12 | Drying machine capable of recycling residual heat |
Publications (1)
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CN202860977U true CN202860977U (en) | 2013-04-10 |
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CN 201220593263 Expired - Fee Related CN202860977U (en) | 2012-11-12 | 2012-11-12 | Drying machine capable of recycling residual heat |
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CN (1) | CN202860977U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103100547A (en) * | 2012-11-12 | 2013-05-15 | 黄陈超 | Dryer with waste heat reused |
-
2012
- 2012-11-12 CN CN 201220593263 patent/CN202860977U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103100547A (en) * | 2012-11-12 | 2013-05-15 | 黄陈超 | Dryer with waste heat reused |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130410 Termination date: 20131112 |