CN213090397U - Continuous microwave dryer for waste straw powder in sauce-flavor liquor starter propagation - Google Patents
Continuous microwave dryer for waste straw powder in sauce-flavor liquor starter propagation Download PDFInfo
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- CN213090397U CN213090397U CN202021521434.3U CN202021521434U CN213090397U CN 213090397 U CN213090397 U CN 213090397U CN 202021521434 U CN202021521434 U CN 202021521434U CN 213090397 U CN213090397 U CN 213090397U
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- drying chamber
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- 239000010902 straw Substances 0.000 title claims abstract description 75
- 239000002699 waste material Substances 0.000 title claims abstract description 13
- 239000000843 powder Substances 0.000 title claims abstract description 8
- 239000000796 flavoring agent Substances 0.000 title claims description 9
- 239000007858 starting material Substances 0.000 title claims description 5
- 238000001035 drying Methods 0.000 claims abstract description 60
- 235000015067 sauces Nutrition 0.000 claims abstract description 8
- 230000001954 sterilising effect Effects 0.000 claims abstract description 5
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims abstract description 4
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 claims abstract description 4
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 4
- 238000007599 discharging Methods 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 8
- 230000017525 heat dissipation Effects 0.000 claims description 5
- 235000019634 flavors Nutrition 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims 1
- 239000002245 particle Substances 0.000 description 16
- 238000000605 extraction Methods 0.000 description 11
- 239000008187 granular material Substances 0.000 description 10
- 230000005540 biological transmission Effects 0.000 description 9
- 238000005192 partition Methods 0.000 description 8
- 238000012856 packing Methods 0.000 description 6
- 230000009471 action Effects 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 230000007246 mechanism Effects 0.000 description 4
- 239000002028 Biomass Substances 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- 230000006835 compression Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000009958 sewing Methods 0.000 description 2
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000001256 steam distillation Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Abstract
The utility model discloses a continuous microwave dryer of sauce wine yeast waste straw powder, it includes the desiccator support, be provided with two drying chambers side by side on the desiccator support, a microwave drying and the sterilization for smashing the straw, be provided with desiccator electric control box in the drying chamber left side, at the drying chamber, be provided with the desiccator conveyer belt between desiccator electric control box and desiccator support top, this desiccator conveyer belt realizes smashing the straw and dry and carry in the drying chamber in succession, set up crushing straw feed inlet on the desiccator support on drying chamber right side, and smash the straw feed inlet and be located and smash the straw discharge gate under, the drying efficiency and the conveying speed of continuous microwave dryer are controlled by desiccator electric control box, this system simple structure simultaneously, high durability and convenient operation, therefore, the clothes hanger is strong in practicability.
Description
Technical Field
The utility model relates to a system wine accessory substance recycle technical field especially relates to the continuous microwave dryer of sauce flavor wine yeast waste straw powder.
Background
The national sauce-flavor wine production is mainly concentrated in the river basin of red water, and the amount of straw required for making koji every year reaches thousands of tons. At present, most of starter propagation waste straws of enterprises with more than scale are directly treated as garbage, and part of the straws are directly burnt in small workshops, so that the waste of resources is caused, and the environment is polluted. As all straws for koji making are in direct contact with the koji blocks, a plurality of koji making raw material wheat flour and microorganisms are adhered to the straws, so that the treatment and resource utilization of the waste straws for koji making are difficult.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a continuous microwave dryer of bent abandonment straw powder of sauce fragrant wine system, an important mode of the bent abandonment straw utilization of sauce fragrant wine system both can reduce the pollution to the environment and the waste of resource, and the biomass fuel granule that makes simultaneously can bring certain income as power plant's electricity generation raw materials or the fuel of the used steam of winery steam distillation.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the utility model provides a continuous microwave dryer of sauce wine yeast waste straw powder, it includes the desiccator support, be provided with two parallel drying chambers side by side on the desiccator support, be used for the microwave drying and the sterilization of crushing straw, be provided with the desiccator electric cabinet on the left of the drying chamber, be provided with the desiccator conveyer belt between drying chamber, desiccator electric cabinet and desiccator support top, this desiccator conveyer belt realizes that crushing straw is continuous dry and is carried in the drying chamber, set up crushing straw feed inlet on the desiccator support on drying chamber right side, and crushing straw feed inlet is located crushing straw discharge gate under, the drying efficiency and the transfer rate of continuous microwave dryer are controlled by the desiccator electric cabinet.
Preferably, heating pipes are uniformly arranged in the drying chamber, gaps are formed between the heating pipes and a conveyor belt of the drying machine, drying chamber exhaust fans are respectively arranged on the side surfaces of the drying chamber, and a drying chamber exhaust fan is arranged on one side of each drying chamber exhaust fan; the top of the drying chamber is provided with a heat extraction chamber which is communicated with each other, the inside of the heat extraction chamber is provided with a heat extraction chamber exhaust fan, one side of the heat extraction chamber exhaust fan is provided with a heat dissipation exhaust fan, and a heat extraction pipe is arranged above the heat extraction chamber to jointly complete heat extraction and humidity elimination of the continuous microwave dryer; and a drying chamber observation window is arranged on the front surface of the drying chamber to realize real-time observation of the drying state.
The utility model has the advantages that:
the utility model discloses the straw after will smashing enters into in the continuous microwave dryer by smashing straw discharge gate and smashing the straw feed inlet and carries out continuous drying and transport, wherein be provided with the heating pipe in two drying chambers side by side and play the dry sterilization to smashing the straw, can drop to 10-15% that is suitable for the pelletization with smashing straw moisture content by initial 50-60%, the heat extraction room, the heat extraction pipe, the heat dissipation exhaust fan, heat extraction room exhaust fan, the drying chamber exhaust fan plays the effect that the heat extraction hydrofuge, this system simple structure simultaneously, high durability and convenient operation, therefore, the clothes hanger is strong in practicability.
Drawings
FIG. 1 is a partial cross-sectional view of the present invention;
FIG. 2 is an internal structural view of the present invention;
FIG. 3 is a schematic diagram of the system according to the present invention;
FIG. 4 is a schematic diagram of a second embodiment of the present invention;
FIG. 5 is a schematic view of the straw pulverizer of the present system;
FIG. 6 is a front view of the shredder rotor of the present system;
FIG. 7 is a view showing the structure of an exhaust fan in the system;
FIG. 8 is a view showing the structure of an exhaust fan in the present system;
FIG. 9 is a view showing the construction of a baffle conveyor for comminuted straw in the present system;
FIG. 10 is a view showing the internal structure of the granulation machine in the present system;
fig. 11 is a perspective view of the pelletizer in accordance with the present invention;
FIG. 12 is a drawing of the structure of the middle press roll and the flat mold of the present invention;
FIG. 13 is a drawing of a transmission gear box of the middle granulating machine of the present invention;
FIG. 14 is a block diagram of a particle baffle conveyor of the present system;
fig. 15 is a schematic view of the pellet packer arrangement of the present system.
Detailed Description
The technical solution of the present patent will be described in further detail with reference to the following embodiments.
Reference will now be made in detail to embodiments of the present patent, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the drawings are exemplary only for the purpose of explaining the present patent and are not to be construed as limiting the present patent.
In the description of this patent, it is to be understood that the terms "center," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," and the like are used in the orientations and positional relationships indicated in the drawings for the convenience of describing the patent and for the simplicity of description, and are not intended to indicate or imply that the referenced devices or elements must have a particular orientation, be constructed and operated in a particular orientation, and are not to be considered limiting of the patent.
In the description of this patent, it is noted that unless otherwise specifically stated or limited, the terms "mounted," "connected," and "disposed" are to be construed broadly and can include, for example, fixedly connected, disposed, detachably connected, disposed, or integrally connected and disposed. The specific meaning of the above terms in this patent may be understood by those of ordinary skill in the art as appropriate.
In this embodiment: as shown in attached figures 1-15, the method comprises a method for preparing biomass fuel particles by using waste straws of sauce-flavor liquor koji-making, which comprises the steps of feeding the waste straws of sauce-flavor liquor koji-making into a straw crusher 1 from a straw feeding hole 102, crushing the straws into 3-5mm in length under the action of a fixed knife 10502 and a movable knife 10503 which rotate at a high speed, and supplying power to a crusher motor 103; crushed straws enter the continuous microwave dryer 2 from the crushed straw outlet 104 and the crushed straw inlet 201 for continuous drying and conveying, wherein heating pipes 203 are arranged in two drying chambers 204 which are arranged side by side to dry and sterilize the crushed straws, the moisture content of the crushed straws can be reduced from 50-60% to 10-15% which is suitable for granulation, and the heat exhausting chamber 205, the heat exhausting pipe 206, the heat radiating exhaust fan 210, the heat exhausting chamber exhaust fan 211, the drying chamber exhaust fan 212 and the drying chamber exhaust fan 213 play roles of heat exhausting and moisture exhausting. The dryer conveyor belt 209 functions as a continuous conveyor; the tail end of a conveyor belt 209 of the crushed and dried straw dryer after drying enters a crushed straw clapboard conveyor 3 through a feed inlet 301 of the crushed straw clapboard conveyor, the crushed straw clapboard conveyor is arranged to be of an inclined structure, the conveyor belt is a clapboard type conveyor belt which is suitable for continuous and uniform conveying of crushed and dried straws and plays a role in lifting the height, and the power of the conveyor belt is provided by a motor 302 of the crushed straw clapboard conveyor; then, the crushed straws enter a feed inlet 401 of the granulator from the tail end of a crushed straw partition conveyor 3, and uniformly fall into a granulating chamber under the action of a feeding scraper 407, the crushed straws are pressed into granules under the action of a compression roller 408 and a flat die 409, a granulator motor 403 is connected with the input end of a granulator transmission gear box 411 through a coupler, and the output end of the granulator transmission gear box 411 is connected with a granulator spindle 406 and finally drives the compression roller 408 to work; the prepared granules enter the granule separator conveyor 5 through a granule separator conveyor feed inlet 501 through a granulator discharge outlet 402, the granule separator conveyor is arranged in an inclined structure, the conveyor belt is a separator type conveyor belt, is suitable for continuous and uniform conveying of the granules, plays a role in lifting the height, and is powered by a granule separator conveyor motor 502; finally, the particles enter a feeding hole 601 of the particle packing machine from the tail end of the particle partition plate conveyor 5, the bagging of the particles is completed by the bagging mechanism 602, after the bagging is completed, the conveyor belt is controlled by the electric cabinet 603 of the packing machine to move, and the bagged particle bags are conveyed to the sewing mechanism 604 to complete bag sealing.
The system for preparing the biomass fuel particles by the waste straws of the sauce flavor wine starter is mainly composed of a straw crusher 1, a continuous microwave dryer 2, a crushed straw clapboard conveyor 3, a flat die granulator 4, a particle clapboard conveyor 5 and a particle packer 6; the straw pulverizer 1 mainly comprises a pulverizer frame 101, a straw feeding port 102, a pulverizer motor 103, a pulverized straw discharging port 104 and a pulverizer rotor 105. The crusher rotor 105 consists of a cutter head 10501, a movable cutter 10502, a fixed cutter 10503 and a supporting shaft 10504; the continuous microwave dryer 2 consists of a crushed straw feeding hole 201, a drying chamber observation window 202, a heating pipe 203, a drying chamber 204, a heat exhaust chamber 205, a heat exhaust pipe 206, a dryer electric control box 207, a dryer bracket 208, a dryer conveying belt 209, a heat dissipation exhaust fan 210, a heat exhaust chamber exhaust fan 211, a drying chamber exhaust fan 212 and a drying chamber exhaust fan 213; the crushed straw clapboard conveyor 3 mainly comprises a crushed straw clapboard conveyor feed inlet 301, a crushed straw clapboard conveyor motor 302, a crushed straw clapboard conveyor rack 303 and a crushed straw clapboard conveyor clapboard 304; the flat-die granulator 4 mainly comprises a granulator feeding hole 401, a granulator discharging hole 402, a granulator motor 403, a granulator electric cabinet 404, a granulator base 405, a granulator main shaft 406, a feeding scraper 407, a press roller 408, a flat die 409, a discharging tray 410, a granulator transmission gear box 411, a granulator outer shell 412 and the like; the particle partition conveyor 5 mainly comprises a particle partition conveyor feed inlet 501, a particle partition conveyor motor 502, a particle partition conveyor frame 503 and a particle partition conveyor partition 504; the particle packing machine 6 mainly comprises a packing machine feeding port 601, a bagging mechanism 602, a packing machine electric cabinet 603, a sewing mechanism 604, a packing machine conveying belt and the like.
The straw feeding port 102, the pulverizer motor 103, the pulverized straw discharging port 104 and the pulverizer rotor 105 are mounted on the pulverizer frame 101. Pulverizer frame 101 sets up four universal wheels, conveniently removes and the adjustment position. The crusher rotor 105 is provided with a cutter head 10501, eight movable cutters 10403 and two fixed cutters 10402, the eight movable cutters 10402 are saw-tooth-shaped cutting edges, and the two fixed cutters 10403 are curved cutting edges, so that the crushed grain size of the straws is more uniform.
The continuous microwave dryer 2 consists of a crushed straw feeding hole 201, a drying chamber observation window 202, a heating pipe 203, a drying chamber 204, a heat exhaust chamber 205, a heat exhaust pipe 206, a dryer electric control box 207, a dryer bracket 208, a dryer conveying belt 209, a heat dissipation exhaust fan 210, a heat exhaust chamber exhaust fan 211, a drying chamber exhaust fan 212 and a drying chamber exhaust fan 213;
the flat die granulator 4 is provided with a granulator feeding hole 401, a feeding scraper 407 is arranged below the granulator feeding hole 401, crushed straws can uniformly enter a granulating chamber, a press roller 408 and a flat die 409 are arranged below the feeding scraper 407, a granulating hole is formed in the flat die 409, and loose crushed straws are extruded into the granulating hole in the flat die 409 by utilizing the mutual extrusion pressure between the press roller 408 and the flat die 409 to be prepared into granules. A discharging tray 410 is arranged below the flat die 409, a granulator discharging port 402 is arranged at the edge of the discharging tray 410, and the prepared granules fall onto the discharging tray 410 through granulating holes of the flat die 409 and slide down to the granulator discharging port 402 under the action of gravity. The compression roller 408 is driven by the granulator spindle 406 to rotate, the granulator spindle 406 is connected with the output end of the granulator transmission gear box 411, the input end of the granulator transmission gear box 411 is connected with the granulator motor 403 through a coupler, the granulator transmission gear box 411 is in bevel gear transmission and has the functions of reducing the rotating speed and changing the transmission direction, and the working rotating speed and the working efficiency of the flat-die granulator 4 are controlled by the granulator electric cabinet 404.
The above, only be the concrete implementation of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the utility model, the concept of which is equivalent to replace or change, should be covered within the protection scope of the present invention.
Claims (2)
1. The utility model provides a continuous microwave dryer of sauce flavor wine yeast preparation abandonment straw powder which characterized in that: the straw drying and sterilizing device comprises a dryer support (208), two drying chambers (204) which are arranged side by side are arranged on the dryer support (208) and are used for microwave drying and sterilization of the crushed straws, a dryer electric control box (207) is arranged on the left side of the drying chamber (204), a dryer conveying belt (209) is arranged between the drying chamber (204), the dryer electric control box (207) and the top of the dryer support (208), the dryer conveying belt (209) is used for realizing continuous drying and conveying of the crushed straws in the drying chamber (204), a crushed straw feeding hole (201) is arranged on the dryer support (208) on the right side of the drying chamber (204), the crushed straw feeding hole (201) is located under a crushed straw discharging hole (104), and the drying efficiency and the conveying speed of the continuous microwave dryer (2) are controlled by the dryer electric control box (207).
2. The continuous microwave dryer for the waste straw powder of the sauce flavor liquor starter propagation according to claim 1, characterized in that: heating pipes (203) are uniformly arranged in the drying chamber (204), a gap is formed between each heating pipe (203) and the corresponding drying machine conveying belt (209), drying chamber exhaust fans (212) are respectively arranged on the side surfaces of the drying chamber (204), and a drying chamber exhaust fan (213) is arranged on one side of each drying chamber exhaust fan (212); the top of the drying chamber (204) is provided with a heat exhaust chamber (205) which is communicated with each other, an exhaust fan (211) of the heat exhaust chamber is arranged in the heat exhaust chamber (205), a heat dissipation exhaust fan (210) is arranged beside the exhaust fan (211) of the heat exhaust chamber, and a heat exhaust pipe (206) is arranged above the heat exhaust chamber (205) to jointly complete heat exhaust and moisture exhaust of the continuous microwave drying machine (2); a drying chamber observation window (202) is arranged on the front surface of the drying chamber (204) to realize real-time observation of the drying state.
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CN202021521434.3U CN213090397U (en) | 2020-07-28 | 2020-07-28 | Continuous microwave dryer for waste straw powder in sauce-flavor liquor starter propagation |
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CN202021521434.3U CN213090397U (en) | 2020-07-28 | 2020-07-28 | Continuous microwave dryer for waste straw powder in sauce-flavor liquor starter propagation |
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CN202021521434.3U Expired - Fee Related CN213090397U (en) | 2020-07-28 | 2020-07-28 | Continuous microwave dryer for waste straw powder in sauce-flavor liquor starter propagation |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111998651A (en) * | 2020-07-28 | 2020-11-27 | 茅台学院 | Continuous microwave dryer for waste straw powder in sauce-flavor liquor starter propagation |
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2020
- 2020-07-28 CN CN202021521434.3U patent/CN213090397U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111998651A (en) * | 2020-07-28 | 2020-11-27 | 茅台学院 | Continuous microwave dryer for waste straw powder in sauce-flavor liquor starter propagation |
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GR01 | Patent grant | ||
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CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20210430 |
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CF01 | Termination of patent right due to non-payment of annual fee |