CN214003402U - Drying and quantitative conveying system for waste vinasse of sauce-flavor wine - Google Patents
Drying and quantitative conveying system for waste vinasse of sauce-flavor wine Download PDFInfo
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- CN214003402U CN214003402U CN202022818143.7U CN202022818143U CN214003402U CN 214003402 U CN214003402 U CN 214003402U CN 202022818143 U CN202022818143 U CN 202022818143U CN 214003402 U CN214003402 U CN 214003402U
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- drying chamber
- lees
- desiccator
- drying
- vinasse
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- 238000001035 drying Methods 0.000 title claims abstract description 94
- 239000002699 waste material Substances 0.000 title claims abstract description 28
- 239000000796 flavoring agent Substances 0.000 title claims abstract description 21
- 235000015067 sauces Nutrition 0.000 claims abstract description 7
- 238000010438 heat treatment Methods 0.000 claims abstract description 3
- 238000007599 discharging Methods 0.000 claims description 7
- 239000000446 fuel Substances 0.000 abstract description 10
- 239000002028 Biomass Substances 0.000 abstract description 9
- 238000011161 development Methods 0.000 abstract description 4
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000005192 partition Methods 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- 238000002156 mixing Methods 0.000 description 6
- 238000002360 preparation method Methods 0.000 description 5
- 238000007789 sealing Methods 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- 238000000855 fermentation Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 235000020068 maotai Nutrition 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- KDYFGRWQOYBRFD-UHFFFAOYSA-N succinic acid Chemical compound OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 2
- SWGJCIMEBVHMTA-UHFFFAOYSA-K trisodium;6-oxido-4-sulfo-5-[(4-sulfonatonaphthalen-1-yl)diazenyl]naphthalene-2-sulfonate Chemical compound [Na+].[Na+].[Na+].C1=CC=C2C(N=NC3=C4C(=CC(=CC4=CC=C3O)S([O-])(=O)=O)S([O-])(=O)=O)=CC=C(S([O-])(=O)=O)C2=C1 SWGJCIMEBVHMTA-UHFFFAOYSA-K 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000001384 succinic acid Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 235000021419 vinegar Nutrition 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
Images
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- Processing Of Solid Wastes (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The utility model provides a dried and quantitative conveying system of sauce fragrant wine abandonment lees, including lees desiccator and dry lees quantitative conveyor, the desiccator feed inlet, the room of airing exhaust, the observation room, first drying chamber and second drying chamber all are fixed in the desiccator frame in proper order along length direction, and the desiccator conveyer belt is drawn forth to the feed end of dry lees quantitative conveyor by the discharge end of second drying chamber, the room of airing exhaust, the observation room, first drying chamber and second drying chamber are sealed the intercommunication in proper order, the air exit has been seted up on the room of airing exhaust, the observation window has been seted up on the observation room, be provided with first drying chamber heater and second drying chamber heater in first drying chamber and the second drying chamber respectively and be the inside heating of drying chamber. The system can realize continuous drying and quantitative conveying operation of the waste lees of the Maotai-flavor liquor to finish pretreatment of the waste lees generated in the Maotai-flavor liquor brewing engineering, so that biomass granular fuel can be prepared subsequently, the problems of difficult treatment, environmental pollution and the like of waste cellar mud and lees of the Maotai-flavor liquor are solved, the resource utilization of the cellar mud and the lees is also realized, and the system belongs to the field of liquor making waste recycling and development.
Description
Technical Field
The utility model relates to a dry and quantitative conveying system of sauce fragrant wine abandonment lees belongs to and makes technical field.
Background
In the production process of Maotai-flavor liquor represented by Guizhou Maotai liquor, an anaerobic fermentation process is cellar fermentation in the process, and fermented grains are required to be completely sealed in a cellar. The pit mud is clay for sealing the pit, namely, the fermented grains are sealed on the surface layer in the pit through anaerobic fermentation, the pit mud is purple red mud within several kilometers of a square circle in the Maotai town, and the purple red mud has the characteristics of strong adhesion, good sealing performance and the like. The production practice of the Maotai-flavor liquor shows that the pit sealing mud not only plays a role in sealing the pit, but also has a close relation with the quality of the fermented grains on the upper layer, and the microbial population quantity plays an important role in the quality of the fermented grains on the upper layer. The pit mud is used as a carrier of microorganisms, plays an important role, is called as brewing microbial gold, and is an indispensable thing in the process of brewing Maotai-flavor liquor. However, the used waste pit mud has the defects of more microorganisms, large odor, more impurities, difficulty in treatment, large waste amount and the like, most wineries simply dehydrate the waste pit mud and transport the dewatered waste pit mud to a landfill site for landfill treatment, and the environmental pollution is large. Therefore, research on reasonable harmless and recycling treatment of the waste pit mud is urgent.
The vinasse is solid waste generated in the process of producing the white spirit, 6-10 t of vinasse can be generated every time 1t of the white spirit is produced, and the vinasse is the largest byproduct of the white spirit manufacturing industry, wherein the Maotai-flavor white spirit accounts for more than 90% of Guizhou spirit products and is one of important post industries of Guizhou province, and nearly 100 million tons of Maotai-flavor white spirit vinasse in 2020 of the whole province are estimated. However, the vinasse has the defects of large yield, complex components, high water content, high acidity, easiness in mildewing, easiness in rotting, difficulty in storage and the like, so that the active resource utilization of the vinasse can reduce the problems of resource waste and environmental pollution caused by stacking the vinasse, change waste into valuable and have higher economic, environmental-friendly and social benefits. At present, the comprehensive utilization approaches of the vinasse comprise feed production, vinegar brewing, glycerol preparation, edible fungus cultivation, energy methane production, succinic acid preparation, fertilizer preparation, sugar activated carbon preparation and the like, but most of the approaches are limited in the experimental research stage and are not popularized and used in a large scale. Therefore, how to comprehensively utilize the vinasse more reasonably and suitable for popularization is still to be further researched.
SUMMERY OF THE UTILITY MODEL
To the above problem, the utility model provides a dry and quantitative conveying system of sauce flavor wine abandonment lees to make produced abandonment lees among the engineering with sauce flavor type white spirit and carry out the preliminary treatment, so that biomass pellet fuel is prepared into to the follow-up, solve the independent difficult fashioned problem of abandonment lees.
In order to solve the problems, the system for drying and quantitatively conveying the waste lees of the Maotai-flavor liquor comprises a lees dryer and a dried lees quantitative conveyor which are sequentially arranged, wherein the lees dryer comprises a dryer feed inlet, an exhaust chamber, an observation chamber, a first drying chamber, a second drying chamber and a dryer frame, the dryer feed inlet, the exhaust chamber, the observation chamber, the first drying chamber and the second drying chamber are sequentially fixed on the dryer frame along the length direction, a dryer conveying belt is sequentially arranged at the bottom of the dryer feed inlet, the exhaust chamber, the observation chamber, the first drying chamber and the second drying chamber, the dryer conveying belt is led out from the discharge end of the second drying chamber to the feed end of the dried lees quantitative conveyor, the exhaust chamber, the observation chamber, the first drying chamber and the second drying chamber are sequentially communicated in a sealing way, and an exhaust outlet is formed in the exhaust chamber, the observation window has been seted up on the observation room to whether the lees pile up on the observation desiccator conveyer belt, be provided with first drying chamber heater and second drying chamber heater respectively in first drying chamber and the second drying chamber for the inside heating of drying chamber, be provided with the exhaust fan in first drying chamber and the second drying chamber, and drive by first drying chamber motor and second drying chamber motor respectively.
In the vinasse drying machine, the discharge end of the second drying chamber is of an open structure, the discharge end is provided with a lifting vinasse discharging adjusting door, the feed end of the exhaust chamber is also of an open structure, the feed end is provided with a lifting vinasse feeding adjusting door, the opening and closing sizes of the vinasse discharging adjusting door and the vinasse feeding adjusting door can be adjusted as required, and the vinasse discharging adjusting door and the vinasse feeding adjusting door can be flexibly used according to the drying yield;
in the system, the dried vinasse quantitative conveyor comprises a vinasse quantitative conveyor hopper, a vinasse quantitative conveyor partition conveyer belt, a vinasse quantitative conveyor motor and a vinasse quantitative conveyor rack, the vinasse quantitative conveyor hopper is supported and fixed on the lower side of the discharge end of the dryer conveyer belt through the vinasse quantitative conveyor rack, the lower feed end of the vinasse quantitative conveyor partition conveyer belt is arranged at the bottom in the vinasse quantitative conveyor hopper, the upper discharge end of the vinasse quantitative conveyor partition conveyer belt extends to the feed end of the mixing stirrer, and the vinasse quantitative conveyor partition conveyer belt is driven by the vinasse quantitative conveyor motor;
the development and utilization degree of renewable resources in China is very low. With the development of economy, energy consumption is on a continuous rising trend, high-quality energy is insufficient in supply, and the energy utilization efficiency is low. The waste pit mud and vinasse of the sauce fragrant wine contain microorganisms and organic matters, and the production of biomass energy by using the waste pit mud and the vinasse has good development prospect. The utility model discloses can dry the preliminary treatment to the abandonment lees that produces among the maotai-flavor type white spirit brewing engineering, make its moisture content 5% -10%, so that use maotai-flavor type white spirit abandonment cellar mud and the lees of preliminary treatment to mix and prepare the biomass fuel granule, simultaneously, lees ejection of compact regulating gate and lees feeding regulating gate's opening and shutting size can be adjusted as required, can use in a flexible way according to drying output, this lees desiccator has the advantage such as can realize continuous drying and transport, drying output and speed are controllable, this system cooperates granulation equipment etc. to use together, solve on the one hand abandonment cellar mud and lees and handle not difficult, the problem such as polluted environment is solved, can kill microorganism and bacterium in cellar mud and the lees with its mixed preparation biomass pellet fuel burning, reduce transportation and processing cost, the foul smell pollution etc., the biomass pellet fuel that makes can be used for steaming heat supply of wine or be used for power plant's electricity generation link, the ash after combustion can be used for manufacturing fertilizers or building materials and the like, and the waste vinasse and pit mud are really turned into wealth. On the other hand, the abandoned vinasse is not easy to form independently, the pit mud is easy to form but not easy to burn, the biomass fuel particles prepared by mixing the two materials solve the problem that the two materials are not easy to treat independently, and the prepared biomass fuel has the advantages of high compactness, high heat value and the like. Meanwhile, the waste vinasse and pit mud are wastes generated in the Maotai-flavor liquor brewing engineering, the waste time and the waste position are consistent, and the biomass fuel particles prepared by mixing the waste vinasse and the pit mud can be conveniently recycled.
Drawings
Fig. 1 is a schematic diagram of the system of the present invention;
FIG. 2 is a schematic view of the construction of a distiller's grains dryer;
FIG. 3 is a front view of the vinasse dryer;
FIG. 4 is a schematic view showing the construction of a quantitative conveyor for dried distiller's grains.
Detailed Description
To further clarify the objects, technical solutions and advantages of the present invention, a more particular description of the invention will be rendered by reference to the appended drawings, which are illustrated in the appended drawings.
Examples
Referring to fig. 1 to 4, the present embodiment provides a method for preparing a pellet fuel by mixing the waste pit mud of the maotai-flavor liquor and the distiller's grains, which specifically comprises the following steps:
1) drying the waste vinasse (with the water content of 80-100%) of the sauce-flavor wine to ensure that the water content of the waste vinasse is 5-10%;
2) crushing the waste pit mud (blocky and with the water content of about 20-30%) of the sauce-flavor wine;
3) mixing the dried vinasse and the crushed pit mud, wherein the weight percentage of the vinasse to the pit mud is as follows: 50-60% of vinasse and 40-50% of pit mud;
4) molding the mixed vinasse and pit mud by a pressure molding machine;
5) and cooling and bagging the formed granular fuel.
And wherein 1) used sauce fragrant wine abandonment lees drying and quantitative conveying system, including lees desiccator 1 and dry lees quantitative conveyor 2 that set gradually, lees desiccator 1 includes desiccator feed inlet 101, exhaust chamber 102, observation chamber 103, first drying chamber 104, second drying chamber 105 and desiccator frame 107, desiccator feed inlet 101, exhaust chamber 102, observation chamber 103, first drying chamber 104 and second drying chamber 105 all are fixed in proper order on desiccator frame 107 along length direction, desiccator feed inlet 101, exhaust chamber 102, observation chamber 103, the bottom in first drying chamber 104 and the second drying chamber 105 sets gradually desiccator conveyer belt 106, and desiccator conveyer belt 106 is drawn forth to the feed end of dry lees quantitative conveyor 2 by the discharge end of second drying chamber 105, exhaust chamber 102, observation chamber 103, first drying chamber 104 and second drying chamber 105 seal in proper order and communicate, an air outlet 113 is arranged on the air exhaust chamber 102, an observation window is arranged on the observation chamber 103 so as to observe whether the vinasse on the drying machine conveyer belt 106 is accumulated or not, a first drying chamber heater 112 and a second drying chamber heater 110 are respectively arranged in the first drying chamber 104 and the second drying chamber 105 so as to heat the interior of the drying chambers, the discharge end of the second drying chamber 105 is of an open structure, a lifting vinasse discharging adjusting door 108 is arranged at the discharge end, the feed end of the air exhaust chamber 102 is also of an open structure, the lifting vinasse feeding adjusting door 114 is arranged at the feed end, the opening and closing sizes of the vinasse discharging adjusting door 108 and the vinasse feeding adjusting door 114 can be adjusted according to requirements, the vinasse drying machine 1 can be flexibly used according to the drying yield, the continuous drying transportation can be realized, and the drying yield and the drying rate can be controlled (the rotating speed of the drying machine conveyer belt 106 and the height of the vinasse feeding adjusting door 114 are adjusted, The height of the vinasse discharging adjusting door 108 can control the drying yield; adjusting the power of the first drying chamber heater 112 and the second drying chamber heater 110 to adjust the drying rate), and the like, wherein exhaust fans are arranged in the first drying chamber 104 and the second drying chamber 105 and are respectively driven by the first drying chamber motor 111 and the second drying chamber motor 109;
the dried vinasse quantitative conveyor 2 comprises a vinasse quantitative conveyor hopper 201, a vinasse quantitative conveyor partition plate conveyor belt 202, a vinasse quantitative conveyor motor 203 and a vinasse quantitative conveyor rack 204, the vinasse quantitative conveyor hopper 201 is supported and fixed on the lower side of the discharge end of the dryer conveyor belt 106 through the vinasse quantitative conveyor rack 204, the lower feed end of the vinasse quantitative conveyor partition plate conveyor belt 202 is arranged at the bottom in the vinasse quantitative conveyor hopper 201, the upper discharge end of the vinasse quantitative conveyor partition plate conveyor belt 202 extends to the feed end of the mixing stirrer 5, and the vinasse quantitative conveyor partition plate conveyor belt 202 is driven by the vinasse quantitative conveyor motor 203;
when the distiller's grains mixer works, dried distiller's grains are conveyed into a hopper 201 of a quantitative distiller's grains conveyor by a distiller's grain dryer 1, and the dried distiller's grains are conveyed into the mixer-stirrer by a clapboard conveyer belt 202 of the quantitative distiller's grains conveyor.
The drying vinasse quantitative conveyor 2 adopts a clapboard conveying belt which is suitable for conveying and lifting the drying vinasse, the conveying is uniform, and the conveying amount is controllable (by adjusting the rotating speed of a vinasse quantitative conveyor motor 203).
The above description is only exemplary of the present invention and should not be taken as limiting the scope of the present invention, as any modifications, equivalents, improvements and the like made within the spirit and principles of the present invention are intended to be included within the scope of the present invention.
Claims (3)
1. The utility model provides a sauce fragrant wine abandonment lees is dry and quantitative conveying system which characterized in that: including lees desiccator (1) and dry lees quantitative conveyor (2) that set gradually, lees desiccator (1) includes desiccator feed inlet (101), exhaust chamber (102), observation room (103), first drying chamber (104), second drying chamber (105) and desiccator frame (107), desiccator feed inlet (101), exhaust chamber (102), observation room (103), first drying chamber (104) and second drying chamber (105) all are fixed in proper order on desiccator frame (107) along length direction, desiccator feed inlet (101), exhaust chamber (102), observation room (103), first drying chamber (104) and the bottom in the second drying chamber (105) set gradually desiccator conveyer belt (106), and desiccator conveyer belt (106) are drawn forth to the feed end of dry lees quantitative conveyor (2) by the discharge end of second drying chamber (105), exhaust chamber (102), observation room (103), first drying chamber (104) and second drying chamber (105) are sealed the intercommunication in proper order, have seted up air exit (113) on exhaust chamber (102), have seted up the observation window on observation chamber (103), are provided with first drying chamber heater (112) and second drying chamber heater (110) respectively in first drying chamber (104) and second drying chamber (105) and are for the inside heating of drying chamber, be provided with the exhaust fan in first drying chamber (104) and second drying chamber (105) to drive by first drying chamber motor (111) and second drying chamber motor (109) respectively.
2. The system for drying and quantitatively conveying the waste vinasse of sauce-flavor wine according to claim 1, wherein the system comprises: the discharge end of the second drying chamber (105) is of an open structure, the discharge end is provided with a lifting vinasse discharging adjusting door (108), the feed end of the exhaust chamber (102) is also of an open structure, and the feed end is provided with a lifting vinasse feeding adjusting door (114).
3. The system for drying and quantitatively conveying the waste vinasse of sauce-flavor wine according to claim 1, wherein the system comprises: drying lees quantitative conveyor (2) are including lees quantitative conveyor hopper (201), lees quantitative conveyor baffle conveyer belt (202), lees quantitative conveyor motor (203) and lees quantitative conveyor frame (204), lees quantitative conveyor hopper (201) are fixed in the downside of drier conveyer belt (106) discharge end through lees quantitative conveyor frame (204) support, the lower part feed end of lees quantitative conveyor baffle conveyer belt (202) sets up the bottom in lees quantitative conveyor hopper (201), lees quantitative conveyor baffle conveyer belt (202) are through lees quantitative conveyor motor (203) drive.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022818143.7U CN214003402U (en) | 2020-11-30 | 2020-11-30 | Drying and quantitative conveying system for waste vinasse of sauce-flavor wine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022818143.7U CN214003402U (en) | 2020-11-30 | 2020-11-30 | Drying and quantitative conveying system for waste vinasse of sauce-flavor wine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214003402U true CN214003402U (en) | 2021-08-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022818143.7U Expired - Fee Related CN214003402U (en) | 2020-11-30 | 2020-11-30 | Drying and quantitative conveying system for waste vinasse of sauce-flavor wine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214003402U (en) |
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2020
- 2020-11-30 CN CN202022818143.7U patent/CN214003402U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20210820 |