CN203881085U - Dewatering and drying device for vinasse - Google Patents
Dewatering and drying device for vinasse Download PDFInfo
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- CN203881085U CN203881085U CN201420228257.8U CN201420228257U CN203881085U CN 203881085 U CN203881085 U CN 203881085U CN 201420228257 U CN201420228257 U CN 201420228257U CN 203881085 U CN203881085 U CN 203881085U
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- vinasse
- microwave heating
- dewatering
- microwave
- drying device
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Abstract
The utility model discloses a dewatering and drying device for vinasse and belongs to the technical field of drying devices. The dewatering and drying device comprises a spiral extruding dewatering device and a microwave heating device. The spiral extruding dewatering device comprises a feeding device, and an adjustable-speed motor transmits power to a drum shaft through a power transmission shaft. The drum shaft and spirals are matched with a screen to extrude raw materials of the vinasse to reduce the moisture content of the vinasse. Waste liquid is discharged through a clean liquid outlet groove. The microwave heating device, a driving wheel, a driven wheel and a conveying belt jointly form a continuous conveying device. The conveying belt forms a tunnel through the communicated interiors of four symmetric microwave heating boxes, microwave emitting elements are installed on the microwave heating boxes and are controlled by independent power supply circuits, and moisture is discharged through a moisture discharging pipeline. According to the dewatering and drying device for vinasse, energy is saved, efficiency is improved, clean production is achieved, and the drying machine which is economical and applicable is provided for vinasse processing enterprises.
Description
Technical field
The utility model relates to a kind of dewatering whole stillage drying device, belongs to drying equipment technical field.
Background technology
In China's food industry, the industry such as alcohol, starch sugar, monosodium glutamate, citric acid mainly be take grain as raw material, but the utilization rate of raw material is lower, has at least 30% ~ 40% raw material to become waste water and dregs.In schlempe waste liquid, dry matter content reaches 5% ~ 8%, and in 1 ton of alcohol distillation waste liquid, residual organic matter total amount is more than 500kg, and the waste liquid environmental pollution of production alcohol discharge is very serious.And vinasse are nutritious, contain multiple organic compound, B family vitamin and cellulose etc., it is a kind of good edible fungus culturing raw material, as long as add in right amount auxiliary material in vinasse, just can be applicable to the growth of multiple eating bacterium, both the production cost of edible mushroom can be reduced, problem of environmental pollution can be solved again.When vinasse are done to feed use, be the most successfully that dewatering whole stillage is made to mixed feed, the economical and effective method that increase benefit, it is digested and assimilated better.Dry vinasse are the basic links of turning waste into wealth, and increase economic benefit, and to curbing environmental pollution, alleviate the shortage of China's mixed feed, energy-saving and emission-reduction, development aquaculture, all important in inhibiting.The moisture content of vinasse is higher, and convection drying need to consume huge energy, and therefore first dehydration is dry again can reduce energy consumption significantly.Microwave drying has that speed is fast, efficiency is high, reduce energy consumption, improve the quality of products and the advantage such as safety and sanitation.Therefore, this research integrates dehydration and two kinds of functions of microwave drying, as a kind of novel dewatering drying device, the dry cost-saving synergistic of vinasse is had great importance.
Summary of the invention
The purpose of this utility model is to provide a kind of dewatering whole stillage drying device, can complete dewatering whole stillage and dry two links, adopts screw extrusion dehydration and microwave drying, can abridged edition, synergy, energy-conservation.
For achieving the above object, the utility model adopts following technical scheme: a kind of dewatering whole stillage drying device, comprises screw extrusion dewater unit and microwave heating equipment.Described dewatering whole stillage drying device first passes through screw extrusion dewater unit by dewatering whole stillage, reduces the moisture content of vinasse; Vinasse after dehydration enter microwave heating equipment and are dried.
Described screw extrusion dewater unit, comprises feeding device, and described feeding device is used for adding vinasse raw material.Described screw extrusion dewater unit be take buncher as power, regulates the rotating speed of this screw extrusion dewater unit; Described buncher by power transmission shaft by transmission of power to rotating drum shaft.Described rotating drum shaft increases gradually along feeding mouth to discharging opening diameter, is evenly distributed with spiral on rotating drum shaft, and described spiral is fed forward vinasse, and rotating drum shaft and screen cloth push vinasse raw material, makes the overflow in vinasse.By extruding, vinasse raw material moisture after vinasse dried feed I and vinasse dried feed II significantly reduces, and the liquid overflowing by extruding is discharged by purified liquor outlet groove.Vinasse after extruding enter dewatering whole stillage dirt-excluding groove after hindering by discharging opening baffle plate.Described screw extrusion dewater unit is by 4 seat supports.
Described microwave heating equipment, comprises transmission belt, and the vinasse after extruding are transported on transmission belt by dewatering whole stillage dirt-excluding groove.Described transmission belt is driven by driving wheel, and driving shaft provides power for driving wheel, and driving wheel, driven pulley and transmission belt be common forms continuous transmitting device.Described microwave heating equipment comprises 4 symmetrical identical microwave heating box, and the formation tunnel, inside that all microwave heating box communicate passes through for transmission belt.Microwave transmitting original paper is all installed on described microwave heating box, and the microwave transmitting original paper on each microwave heating box is controlled by power supply circuits independently.Described in each, microwave heating box top is provided with dehumidifying pipelines, and all dehumidifying pipelines branch roads converge into main line and get rid of.Vinasse after microwave drying are collected by dry vinasse discharging opening.
In sum, owing to having adopted technique scheme, the beneficial effects of the utility model are:
Dewatering whole stillage drying device of the present utility model, integrates screw extrusion dewater unit and microwave heating equipment, can reduce to greatest extent moisture content and production cost;
Dewatering whole stillage drying device of the present utility model, adopts tunnel type micro wave heater, and heating using microwave original paper is independently controlled, and can select according to actual needs;
Dewatering whole stillage drying device of the present utility model, stable work in work, and energy efficiency, produce clean, for vinasse processing enterprise provides a economic and practical drying machinery.
Accompanying drawing explanation
Fig. 1 is the overall structure figure of a kind of dewatering whole stillage drying device of the utility model.
Mark in figure: 1-feeding device, 2-vinasse raw material, 3-spiral, 4-rotating drum shaft, 5-vinasse dried feed I, 6-purified liquor outlet groove, 7-screen cloth, 8-vinasse dried feed II, 9-bearing, 10-discharging opening baffle plate, 11-power transmission shaft, 12-dewatering whole stillage dirt-excluding groove, 13-buncher, 14-microwave heating box, 15-dehumidifying pipelines, the dry vinasse discharging opening of 16-, 17-driven pulley, 18-microwave transmitting original paper, 19-transmission belt, 20-driving wheel, 21-driving shaft.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is elaborated.
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that concrete case study on implementation described herein is only in order to explain the utility model, and be not used in restriction the utility model.
As shown in Figure 1, the utility model is a kind of dewatering whole stillage drying device, comprises screw extrusion dewater unit and microwave heating equipment.Described dewatering whole stillage drying device first passes through screw extrusion dewater unit by dewatering whole stillage, reduces the moisture content of vinasse; Vinasse after dehydration enter microwave heating equipment and are dried.
Described screw extrusion dewater unit, comprises feeding device 1, and described feeding device 1 is for adding vinasse raw material.Described screw extrusion dewater unit be take buncher 13 as power, regulates the rotating speed of this screw extrusion dewater unit; Described buncher 13 by power transmission shaft 11 by transmission of power to rotating drum shaft 4.Described rotating drum shaft 4 increases to discharging opening diameter gradually along feeding mouth, is evenly distributed with spiral 3 on rotating drum shaft 4, and described spiral 3 is fed forward vinasse, and rotating drum shaft 4 pushes with 7 pairs of vinasse raw materials of screen cloth, makes the overflow in vinasse.By extruding, vinasse raw material 2 moisture after vinasse dried feed I 5 and vinasse dried feed II 8 significantly reduces, and the liquid overflowing by extruding is discharged by purified liquor outlet groove 6.Vinasse after extruding enter dewatering whole stillage dirt-excluding groove 12 after hindering by discharging opening baffle plate 10.Described screw extrusion dewater unit is supported by 4 bearings 9.
Described microwave heating equipment, comprises transmission belt 19, and the vinasse after extruding are transported on transmission belt 19 by dewatering whole stillage dirt-excluding groove 12.Described transmission belt 19 is driven by driving wheel 20, and driving shaft 21 provides power for driving wheel 20, and driving wheel 20, driven pulley 17 and transmission belt 19 be common forms continuous transmitting device.Described microwave heating equipment comprises 4 symmetrical identical microwave heating box 14, and the formation tunnel, inside that all microwave heating box 14 communicate passes through for transmission belt 19.Microwave transmitting original paper 18 is all installed on described microwave heating box 14, and the microwave transmitting original paper 18 on each microwave heating box 14 is controlled by power supply circuits independently.Described in each, microwave heating box 14 tops are provided with dehumidifying pipelines 15, and all dehumidifying pipelines 15 branch roads converge into main line and get rid of.Vinasse after microwave drying are collected after being dried vinasse discharging opening 16.
The operation principle of described dewatering whole stillage drying device is: by feeding device 1, add vinasse raw material 2, buncher 13 rotational powers pass to rotating drum shaft 4, and rotating drum shaft 4 rotates with spiral 3 simultaneously.Described spiral 3 is fed forward vinasse, and because described rotating drum shaft 4 increases to discharging opening diameter gradually along feeding mouth, rotating drum shaft 4 pushes with 7 pairs of vinasse raw materials of screen cloth, makes the overflow in vinasse, by dewatering whole stillage dirt-excluding groove 12, waste liquid is got rid of.By constantly pushing, vinasse raw material 2 moisture after vinasse dried feed I 5 and vinasse dried feed II 8 significantly reduces.Vinasse after extruding are transported on transmission belt 19 by discharging opening baffle plate 10, dewatering whole stillage dirt-excluding groove 12.Driving wheel 20 drives transmission belt 19 to transmit by driven pulley 17, by the formation tunnel, inside of 4 microwave heating box 14, further dry to the vinasse by tunnel for transmission belt 19.The number of the speed of transmission belt 19 and microwave heating box 14 heating can independently be controlled, and the moisture after heating is discharged by dehumidifying pipelines 15.Dried vinasse collect after being dried vinasse discharging opening 16.Its working procedure is:---extruding---is carried---being dried---blowing in charging.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all any modifications of doing within spirit of the present utility model and principle, be equal to and replace and improvement etc., within all should being included in protection domain of the present utility model.
Claims (3)
1. a dewatering whole stillage drying device, comprises screw extrusion dewater unit and microwave heating equipment, and described dewatering whole stillage drying device first dewaters vinasse raw material (2) by screw extrusion dewater unit, reduces the moisture content of vinasse; It is further dry that vinasse after dehydration enter microwave heating equipment.
2. a kind of dewatering whole stillage drying device as claimed in claim 1, is characterized in that described screw extrusion dewater unit: comprise feeding device (1), described feeding device (1) is for adding vinasse raw material (2); The buncher (13) of take is power, described buncher (13) by power transmission shaft (11) by transmission of power to rotating drum shaft (4); Described rotating drum shaft (4) increases gradually along feeding mouth to discharging opening diameter, on rotating drum shaft (4), be evenly distributed with spiral (3), rotating drum shaft (4) and spiral (3) coordinate vinasse raw material are pushed and is fed forward with screen cloth (7), and the liquid overflowing by extruding is discharged by purified liquor outlet groove (6); Vinasse after extruding enter dewatering whole stillage dirt-excluding groove (12) by discharging opening baffle plate (10); Described screw extrusion dewater unit is supported by 4 bearings (9).
3. a kind of dewatering whole stillage drying device as claimed in claim 1, it is characterized in that described microwave heating equipment: comprise transmission belt (19), described transmission belt (19) is driven by driving wheel (20), driving shaft (21) provides power for driving wheel (20), and driving wheel (20), driven pulley (17) and transmission belt (19) form continuous transmitting device jointly; Described microwave heating equipment comprises 4 symmetrical microwave heating box (14), and the formation tunnel, inside that all microwave heating box (14) communicate passes through for transmission belt (19); Microwave transmitting original paper (18) is all installed on described microwave heating box (14), and the microwave transmitting original paper (18) on each microwave heating box (14) is controlled by power supply circuits independently; Microwave heating box described in each (14) top is provided with dehumidifying pipelines (15), and the vinasse after microwave drying are collected after being dried vinasse discharging opening (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420228257.8U CN203881085U (en) | 2014-05-07 | 2014-05-07 | Dewatering and drying device for vinasse |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420228257.8U CN203881085U (en) | 2014-05-07 | 2014-05-07 | Dewatering and drying device for vinasse |
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| Publication Number | Publication Date |
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| CN203881085U true CN203881085U (en) | 2014-10-15 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420228257.8U Expired - Fee Related CN203881085U (en) | 2014-05-07 | 2014-05-07 | Dewatering and drying device for vinasse |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105036511A (en) * | 2015-07-23 | 2015-11-11 | 柳州市德缘科技开发有限责任公司 | Sugar refinery filter mud microwave dewatering and drying treatment process and dewatering and drying device |
| CN106017047A (en) * | 2016-07-07 | 2016-10-12 | 山东端信堂大禹药业有限公司 | Rapid drying treatment device of Chinese herb waste residue |
| CN106403562A (en) * | 2016-08-31 | 2017-02-15 | 盐城工学院 | Microwave drying system |
| CN106556228A (en) * | 2015-09-25 | 2017-04-05 | 哈尔滨华藻生物科技开发有限公司 | A kind of dewatered drying equipment |
| RU2618779C1 (en) * | 2016-01-26 | 2017-05-11 | федеральное государственное бюджетное образовательное учреждение высшего образования "Волгоградский государтвенный аграрный университет" (ФГБОУ ВО Волгоградский ГАУ) | Method and device for transportation and processing of bulk materials |
| CN107940911A (en) * | 2017-12-25 | 2018-04-20 | 安徽赛月环境科技有限公司 | Full-automatic wheat grain dewaterer |
| CN107976055A (en) * | 2017-11-17 | 2018-05-01 | 芜湖县宏大机械设备制造有限公司 | A kind of helical feed drying device |
| CN109228482A (en) * | 2018-10-20 | 2019-01-18 | 浙江华业塑料机械有限公司 | A kind of vinasse processing unit of pollution-free environmental protection |
| CN115449446A (en) * | 2022-09-02 | 2022-12-09 | 安徽省金裕皖酒业有限公司 | Health-preserving white spirit brewing slag material recycling system and method |
-
2014
- 2014-05-07 CN CN201420228257.8U patent/CN203881085U/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105036511A (en) * | 2015-07-23 | 2015-11-11 | 柳州市德缘科技开发有限责任公司 | Sugar refinery filter mud microwave dewatering and drying treatment process and dewatering and drying device |
| CN105036511B (en) * | 2015-07-23 | 2017-02-01 | 柳州市德缘科技开发有限责任公司 | Sugar refinery filter mud microwave dewatering and drying treatment process and dewatering and drying device |
| CN106556228A (en) * | 2015-09-25 | 2017-04-05 | 哈尔滨华藻生物科技开发有限公司 | A kind of dewatered drying equipment |
| RU2618779C1 (en) * | 2016-01-26 | 2017-05-11 | федеральное государственное бюджетное образовательное учреждение высшего образования "Волгоградский государтвенный аграрный университет" (ФГБОУ ВО Волгоградский ГАУ) | Method and device for transportation and processing of bulk materials |
| CN106017047A (en) * | 2016-07-07 | 2016-10-12 | 山东端信堂大禹药业有限公司 | Rapid drying treatment device of Chinese herb waste residue |
| CN106017047B (en) * | 2016-07-07 | 2018-08-14 | 山东端信堂大禹药业有限公司 | Waste residue of Chinese herbs rapid draing processing unit |
| CN106403562A (en) * | 2016-08-31 | 2017-02-15 | 盐城工学院 | Microwave drying system |
| CN107976055A (en) * | 2017-11-17 | 2018-05-01 | 芜湖县宏大机械设备制造有限公司 | A kind of helical feed drying device |
| CN107940911A (en) * | 2017-12-25 | 2018-04-20 | 安徽赛月环境科技有限公司 | Full-automatic wheat grain dewaterer |
| CN109228482A (en) * | 2018-10-20 | 2019-01-18 | 浙江华业塑料机械有限公司 | A kind of vinasse processing unit of pollution-free environmental protection |
| CN115449446A (en) * | 2022-09-02 | 2022-12-09 | 安徽省金裕皖酒业有限公司 | Health-preserving white spirit brewing slag material recycling system and method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141015 Termination date: 20150507 |
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| EXPY | Termination of patent right or utility model |