CN206872758U - One kind production and processing bio-fuel production facility - Google Patents

One kind production and processing bio-fuel production facility Download PDF

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Publication number
CN206872758U
CN206872758U CN201720377321.2U CN201720377321U CN206872758U CN 206872758 U CN206872758 U CN 206872758U CN 201720377321 U CN201720377321 U CN 201720377321U CN 206872758 U CN206872758 U CN 206872758U
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CN
China
Prior art keywords
chamber
fuel
bio
conveyer belt
rotating shaft
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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
Application number
CN201720377321.2U
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Chinese (zh)
Inventor
李万青
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TIANJIN HENGSHENG XINGWANG BIOTECHNOLOGY Co Ltd
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TIANJIN HENGSHENG XINGWANG BIOTECHNOLOGY Co Ltd
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Priority to CN201720377321.2U priority Critical patent/CN206872758U/en
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Publication of CN206872758U publication Critical patent/CN206872758U/en
Expired - Fee Related legal-status Critical Current
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

The utility model discloses one kind to produce and process bio-fuel production facility, including pulverizer housing, the upper center of the pulverizer housing is provided with charging aperture, crushing wheel is provided with the middle part of the inner chamber of the pulverizer housing, it is plugged on respectively on pulverizer housing or so side by rotating shaft in the middle part of the left and right sides of the crushing wheel, on the left of the crushing wheel the first rotating disk is fixedly connected with rotating shaft, the inner chamber bottom of the pulverizer housing is provided with slide plate, the left upper part of pulping chamber is connected on the right side of the lower end of the pulverizer housing by pipeline, the upper center of the pulping chamber is provided with motor.The production and processing bio-fuel production facility, by the structure provided with pulping chamber, ensure that the mobility of slurries, the filtering of screen pack so that be not in slurries residual bulky grain bio-fuel enter balancing gate pit in;By the structure provided with drying chamber and conveyer belt, the bio-fuel for the sheet that can allow uniformly is toasted.

Description

One kind production and processing bio-fuel production facility
Technical field
Industrial technical field is the utility model is related to, is specially a kind of production and processing bio-fuel production facility.
Background technology
Bio-fuel refers to the solid for being made up of or converting organism, liquid or gaseous fuel.It is that regenerative resource is opened The important directions utilized are sent out, there are good storing properties and rodability, it is possible to provide the liquid fuel of alternative oil.Narrow sense Bio-fuel only refer to liquid biofuel, mainly including alcohol fuel, biodiesel and aviation bio-fuel etc., bio-fuel Refer to using big gas and water, soil etc. by photosynthesis and caused various organisms, i.e., all lived can grow Organic substance.It includes, animal and microorganism.Different from traditional fuels such as oil, coal, nuclear energy, this emerging fuel is can Generative fuel, but common bio-fuel can cause bio-fuel that bulk is made in production and processing, be unfavorable for bio-fuel Burning, and drying of the common drying plant to bio-fuel be not thorough, therefore we have proposed one kind production and processing biology Fuel production facility.
Utility model content
The purpose of this utility model is to provide a kind of production and processing bio-fuel production facility, to solve above-mentioned background skill The problem of being proposed in art.
To achieve the above object, the utility model provides following technical scheme:One kind production and processing bio-fuel film-making is set Standby, including pulverizer housing, the upper center of the pulverizer housing is provided with charging aperture, in the middle part of the inner chamber of the pulverizer housing Provided with crushing wheel, it is plugged on respectively on pulverizer housing or so side by rotating shaft in the middle part of the left and right sides of the crushing wheel, institute State and be fixedly connected with the first rotating disk in rotating shaft on the left of crushing wheel, the inner chamber bottom of the pulverizer housing is provided with slide plate, the crushing The left upper part of pulping chamber is connected on the right side of the lower end of machine casing by pipeline, the upper center of the pulping chamber is provided with motor, Feed tube is provided with the right side of the upper end of the pulping chamber, blade, the lower end of the motor are provided with the middle part of the inner chamber of the pulping chamber Rotating blade is connected by rotating shaft, the inner chamber bottom of the pulping chamber is provided with screen pack, and the right-hand member bottom of the pulping chamber passes through Pipeline connects the left upper part of balancing gate pit, and the pipeline between the pulping chamber and balancing gate pit is provided with water pump, the balancing gate pit Upper end connects admission line, and the admission line is provided with air pressure-adjusting valve, shower nozzle, institute are connected in the middle part of the lower end of the balancing gate pit The lower section for stating shower nozzle is provided with conveyer belt, and the upper end of the conveyer belt is provided with flitch processed, and the left side of the conveyer belt, which is provided with, dries Dry chamber, the inner chamber top of the drying chamber are provided with heater strip, and the inwall upper end of the drying chamber is provided with PID temperature controller, institute State PID temperature controller to be electrical connected with heater strip, temperature sensor, the drying chamber are provided with the upside of the inwall of the drying chamber Lower end on the right side of be provided with hot blast air inlet pipe.
Preferably, the flitch processed by framework, rotating shaft, lamina affixad and frame net ring group into the lamina affixad passes through rotating shaft Framework is connected to, the lamina affixad can surround axis of rotation, and the frame surrounding of the lamina affixad is fixed with frame net ring.
Preferably, the conveyer belt is plugged in the middle part of drying chamber, the middle part of one section in drying chamber of the conveyer belt For hollow form, the conveyor width is more than the width of framework, and the width of the hollow form is more than the width of lamina affixad.
Preferably, the rotating blade and blade are arranged in a crossed manner.
Preferably, there is the angle of 20 to 30 degree with horizontal plane in the slide plate, and the surface of the slide plate is smooth.
Compared with prior art, the beneficial effects of the utility model are:The production and processing bio-fuel production facility, passes through Structure provided with pulping chamber, the material after crushing is entered in pulping chamber by slide plate carries out mixed pulp, is driven by motor Rotating blade rotates and slurries is stirred with blade, accelerates the mixing of slurries, while rotating blade can be to not with blade Pulverized bio-fuel is crushed again, ensure that the mobility of slurries, the filtering of screen pack so that will not be deposited in slurries Enter in the bulky grain bio-fuel of residual in balancing gate pit, by the structure provided with drying chamber and conveyer belt, adding in drying chamber Heated filament and hot blast air inlet pipe are dried to bio-fuel, due to being hollow in the middle part of the conveyer belt in drying chamber, along with heat The effect of wind air inlet pipe, rotates lamina affixad, and the bio-fuel for the sheet that can allow uniformly is toasted, will not be because of same One position is toasted for a long time there is burned black and cracking phenomenon;By the structure provided with shower nozzle, enable to slurries uniform It is sprayed on flitch processed, ensure that the film-making of bio-fuel is more uniform.
Brief description of the drawings
Fig. 1 is the utility model structure entirety schematic cross-sectional view;
Fig. 2 is the utility model flitch overlooking the structure diagram;
Fig. 3 is the utility model conveyer structure schematic diagram.
In figure:1 pulverizer housing, 2 charging apertures, 3 crushing wheels, 4 first rotating disks, 5 slide plates, 6 pulping chambers, 7 motor, 8 are entered Liquid pipe, 9 rotating blades, 10 blades, 11 screen packs, 12 water pumps, 13 air pressure-adjusting valves, 14 balancing gate pits, 15 admission lines, 16 sprays Head, 17 conveyer belts, 171 hollow forms, 18 drying chambers, 19 PID temperature controllers, 20 heater strips, 21 temperature sensors, 22 system material Plate, 221 rotating shafts, 222 lamina affixads, 223 frameworks, 224 frame net rings, 23 air inlet pipe.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made The every other embodiment obtained, belong to the scope of the utility model protection.
Fig. 1-3 are referred to, the utility model provides a kind of technical scheme:One kind production and processing bio-fuel production facility, Including pulverizer housing 1, pulverizer housing 1 is the framework of pulverizer, and the upper center of the pulverizer housing 1 is provided with charging aperture 2, charging aperture 2 is the material inlet for needing to crush, and is provided with crushing wheel 3 in the middle part of the inner chamber of the pulverizer housing 1, crushing wheel 3 is Crushing wheel is crushed, pulverizer housing 1 or so is plugged on respectively by rotating shaft in the middle part of the left and right sides of the crushing wheel 3 On side, the first rotating disk 4 is fixedly connected with the left side rotating shaft of crushing wheel 3, the first rotating disk 4 in order to connect external impetus equipment, Crushing wheel 3 is driven to rotate, the inner chamber bottom of the pulverizer housing 1 is provided with slide plate 5, and slide plate 5 is in order that the material crushed is concentrated To discharge outlet, there is the angle of 20 to 30 degree with horizontal plane in the slide plate 5, the surface of the slide plate 5 is smooth.The pulverizer Connect the left upper part of pulping chamber 6 on the right side of the lower end of casing 1 by pipeline, pulping chamber 6 is in order to make slurry, the pulping chamber 6 Upper center be provided with motor 7, for motor 7 in order to give rotating blade 9 to provide rotational power, the upper end of the pulping chamber 6 is right Side is provided with feed tube 8, is provided with blade 10 in the middle part of the inner chamber of the pulping chamber 6, rotating blade 9 can be to not being crushed with blade 10 Bio-fuel crushed again, ensure that the mobility of slurries, the rotating blade 9 and blade 10 are arranged in a crossed manner.It is described The lower end of motor 7 connects rotating blade 9 by rotating shaft, and the inner chamber bottom of the pulping chamber 6 is provided with screen pack 11, the slurry of formation The filtering that liquid passes through screen pack 11 so that be not in the bulky grain bio-fuel of residual in slurries, the right-hand member of the pulping chamber 6 Bottom connects the left upper part of balancing gate pit 14 by pipeline, and the pipeline between the pulping chamber 6 and balancing gate pit 14 is provided with water pump 12, pulping chamber 6 is sent into slurries in slurry room 14 by water pump 12, the upper end connection admission line 15 of the balancing gate pit 14, institute State admission line 15 and be provided with air pressure-adjusting valve 13, air pressure-adjusting valve 13 can adjust the input size of air, so as to control pressure Pressure size in power room 14, connection shower nozzle 16 in the middle part of the lower end of the balancing gate pit 14, the slurries in balancing gate pit 14 are in air Under compression so that slurries spray from shower nozzle 16 so that slurries are uniformly sprayed on flitch 22 processed, the lower section of the shower nozzle 16 Provided with conveyer belt 17, the conveyer belt 17 is plugged on the middle part of drying chamber 18, one in drying chamber 18 of the conveyer belt 17 Section middle part is hollow form 171, and the width of conveyer belt 17 is more than the width of framework 223, and the width of the hollow form 171 is more than attached The width of plate 222.The upper end of the conveyer belt 17 is provided with flitch 22 processed, and the flitch 22 processed is by framework 223, rotating shaft 221, attached Plate 222 and frame net ring 224 forms, the lamina affixad 222 is connected to framework 223, the lamina affixad 222 by rotating shaft 221 It can be rotated around rotating shaft 221, the frame surrounding of the lamina affixad 222 is fixed with frame net ring 224.The conveyer belt 17 left side is provided with drying chamber 18, and the inner chamber top of the drying chamber 18 is provided with heater strip 20, the heater strip 20 in drying chamber 18 Bio-fuel is dried with hot blast air inlet pipe 23, because the middle part of conveyer belt 17 of drying chamber 18 is hollow, along with heat The effect of wind air inlet pipe 23, rotate lamina affixad 222, the bio-fuel for the sheet that can allow uniformly is toasted, will not Because same position toasts for a long time burned black and cracking phenomenon occurs, the inwall upper end of the drying chamber 18 is provided with PID temperature Controller 19 is spent, the PID temperature controller 19 is electrical connected with heater strip 20, and PID temperature controller 15 uses JM TEMP2000PID model, PID temperature controller 19 adjust the temperature of heater strip 20 in drying chamber 18.The drying chamber 18 Temperature sensor 21 is provided with the upside of inwall, hot blast air inlet pipe 23 is provided with the right side of the lower end of the drying chamber 18.
Operation principle:When producing and processing bio-fuel, raw material is put into charging aperture 2, by the crushing of crushing wheel 3, Material after crushing is entered in pulping chamber 6 by slide plate 5, and enter liquid by feed tube 8 is mixed with the bio-fuel crushed Slurrying is closed, drives rotating blade 9 to rotate by motor 7, slurries is stirred with blade 10, while rotating blade 9 and knife Piece 10 can be crushed again to not pulverized bio-fuel, ensure that the mobility of slurries, the slurries of formation passed through The filtering of filter screen 11 so that be not in the bulky grain bio-fuel of residual in slurries, pulping chamber 6 send slurries by water pump 12 Enter in slurry room 14, by the structure of admission line 15, air is pressed into balancing gate pit 14, air pressure-adjusting valve 13 can adjust sky The input size of gas, so as to the pressure size in control pressure room 14, the slurries in balancing gate pit 14 are under the compression of air so that Slurries spray from shower nozzle 16 so that slurries are uniformly sprayed on flitch 22 processed, flitch 22 processed with the motion of conveyer belt 17, So that flitch 22 processed enters in drying chamber 18, flitch 22 processed is reached in drying chamber 18, heater strip 20 and hot blast in drying chamber 18 Air inlet pipe 23 is dried to bio-fuel, because the middle part of conveyer belt 17 of drying chamber 18 is hollow, along with hot blast air inlet The effect of pipe 23, rotate lamina affixad 222, the bio-fuel for the sheet that can allow uniformly is toasted, will not be because of same One position is toasted for a long time there is burned black and cracking phenomenon, while can adjust drying chamber by PID temperature controller 19 The temperature of heater strip 20 in 18.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art, It is appreciated that these embodiments can be carried out with a variety of changes in the case where not departing from principle of the present utility model and spirit, repaiied Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.

Claims (5)

1. one kind production and processing bio-fuel production facility, including pulverizer housing (1), it is characterised in that:The pulverizer machine The upper center of shell (1) is provided with charging aperture (2), and crushing wheel (3), the powder are provided with the middle part of the inner chamber of the pulverizer housing (1) It is plugged on respectively by rotating shaft on pulverizer housing (1) left and right side in the middle part of the left and right sides of broken wheel (3), the crushing wheel (3) The first rotating disk (4) is fixedly connected with the rotating shaft of left side, the inner chamber bottom of the pulverizer housing (1) is provided with slide plate (5), the crushing The left upper part of pulping chamber (6) is connected on the right side of the lower end of machine casing (1) by pipeline, the upper center of the pulping chamber (6) is set There is motor (7), feed tube (8) is provided with the right side of the upper end of the pulping chamber (6), is provided with the middle part of the inner chamber of the pulping chamber (6) Blade (10), the lower end of the motor (7) connect rotating blade (9) by rotating shaft, and the inner chamber bottom of the pulping chamber (6) is set There is screen pack (11), the right-hand member bottom of the pulping chamber (6) connects the left upper part of balancing gate pit (14), the slurrying by pipeline Pipeline between room (6) and balancing gate pit (14) is provided with water pump (12), the upper end connection admission line of the balancing gate pit (14) (15), the admission line (15) is provided with air pressure-adjusting valve (13), and shower nozzle is connected in the middle part of the lower end of the balancing gate pit (14) (16), the lower section of the shower nozzle (16) is provided with conveyer belt (17), and the upper end of the conveyer belt (17) is provided with flitch processed (22), described The left side of the conveyer belt (17) is provided with drying chamber (18), and the inner chamber top of the drying chamber (18) is provided with heater strip (20), institute The inwall upper end for stating drying chamber (18) is provided with PID temperature controller (19), the PID temperature controller (19) and heater strip (20) It is electrical connected, temperature sensor (21), the lower end right side of the drying chamber (18) is provided with the upside of the inwall of the drying chamber (18) Provided with hot blast air inlet pipe (23).
A kind of 2. production and processing bio-fuel production facility according to claim 1, it is characterised in that:The flitch processed (22) it is made up of framework (223), rotating shaft (221), lamina affixad (222) and frame net ring (224), the lamina affixad (222) passes through Rotating shaft (221) is connected to framework (223), and the lamina affixad (222) can surround rotating shaft (221) and rotate, the lamina affixad (222) Frame surrounding be fixed with frame net ring (224).
A kind of 3. production and processing bio-fuel production facility according to claim 1, it is characterised in that:The conveyer belt (17) it is plugged in the middle part of drying chamber (18), the middle part of one section in drying chamber (18) of the conveyer belt (17) is hollow form (171), conveyer belt (17) width is more than the width of framework (223), and the width of the hollow form (171) is more than lamina affixad (222) width.
A kind of 4. production and processing bio-fuel production facility according to claim 1, it is characterised in that:The rotating blade (9) and blade (10) is arranged in a crossed manner.
A kind of 5. production and processing bio-fuel production facility according to claim 1, it is characterised in that:The slide plate (5) The angle of 20 to 30 degree with horizontal plane be present, the surface of the slide plate (5) is smooth.
CN201720377321.2U 2017-04-12 2017-04-12 One kind production and processing bio-fuel production facility Expired - Fee Related CN206872758U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720377321.2U CN206872758U (en) 2017-04-12 2017-04-12 One kind production and processing bio-fuel production facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720377321.2U CN206872758U (en) 2017-04-12 2017-04-12 One kind production and processing bio-fuel production facility

Publications (1)

Publication Number Publication Date
CN206872758U true CN206872758U (en) 2018-01-12

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110487036A (en) * 2019-10-12 2019-11-22 河南多赛畜牧设备有限公司 A kind of semi-enclosed chicken manure Pressure chamber

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110487036A (en) * 2019-10-12 2019-11-22 河南多赛畜牧设备有限公司 A kind of semi-enclosed chicken manure Pressure chamber

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CF01 Termination of patent right due to non-payment of annual fee
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Granted publication date: 20180112

Termination date: 20180412