CN205279684U - Energy -conserving lees drying device of sorting formula - Google Patents
Energy -conserving lees drying device of sorting formula Download PDFInfo
- Publication number
- CN205279684U CN205279684U CN201520827472.4U CN201520827472U CN205279684U CN 205279684 U CN205279684 U CN 205279684U CN 201520827472 U CN201520827472 U CN 201520827472U CN 205279684 U CN205279684 U CN 205279684U
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- CN
- China
- Prior art keywords
- drying
- sorting
- machine
- energy
- heat tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000001035 drying Methods 0.000 title claims abstract description 87
- 239000002912 waste gas Substances 0.000 claims abstract description 9
- 239000012535 impurity Substances 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims description 15
- 239000000428 dust Substances 0.000 claims description 9
- 238000004134 energy conservation Methods 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 5
- 239000007789 gas Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 230000008676 import Effects 0.000 abstract 1
- 239000002918 waste heat Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 3
- 239000000446 fuel Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 206010013786 Dry skin Diseases 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000000643 oven drying Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model relates to an energy -conserving lees drying device of sorting formula, including selecting separately and once dry unit and secondary stoving unit, the sorting and the unit of once drying include the pneumatic drying tower, and there are feed inlet and hot -blast import in pneumatic drying tower lower part, pneumatic drying tower bottom is the impurity export, secondary stoving unit includes internal heat tube bank drying -machine, termination feeding conveyer, back termination ejection of compact conveyer before the internal heat tube bank drying -machine, select separately and discharge after the waste gas that reaches once dry unit and secondary stoving unit device rear end passes through bag collector. The beneficial effect of the utility model: this equipment has adopted the pneumatic drying tower to dry for the first time and internal heat tube bank drying -machine is dried for the second time, in the in -process of once drying can be simultaneously with lees the institute thoughtlessly some impurity get rid of, adopt the direct contact formula to dry and indirect stoving of internal heat tube bank drying -machine respectively, and internal heat tube bank drying -machine utilizes the waste heat, make the quality of the lees of producing obtain the improvement, the energy has been practiced thrift again to the while.
Description
Technical field
This utility model relates to a kind of equipment drying production process at distiller grains.
Background technology
In brewed spirit process, it is necessary to the distiller grains after wine brewing are processed, it is used for after the drying being processed into feedstuff or being used as the fuel of environment-protection boiler. In drying course, because distiller grains high humidity, viscosity are big, poor fluidity, and the inside is more or less possibly together with certain foreign material, such as pit mud, stone etc. One of traditional distiller grains drying is: adopt drying roller to be directly directly connected to hot air apparatus, distiller grains are first drying in cylinder, material can only progressively overturn under the drive of cylinder and contact with hot blast, and slowly move to cylinder tail end, ensure that material is all dried, its drying time is longer, completes drying course during close to drum outlet end. The shortcoming of this drying mode is that the impurity in material can not be removed, and after cylinder is directly connected with hot air apparatus, in its cylinder, temperature difficulty controls, understand in rear end will the material adustion of drying, both directly affect the quality of distiller grains. Another way is to adopt deep fat tube bank to dry, although the problem that material is burnt can be solved, but deep fat tube bank drying plant manufacture difficulty is big, under high temperature, the sealing of rotating part easily produces leakage, and hot oil furnace and the high temperature fuel delivery device of front end are also required to bigger input; Simultaneously because distiller grains high humidity, viscosity are big, poor fluidity, the efficiency of its deep fat tube bank indirect drying is low. And the impurity in above drying mode distiller grains can not remove.
Utility model content
The purpose of this utility model is to provide a kind of energy-conservation wine-tank drying apparatus of sorting type to make up the deficiency of prior art.
This utility model the technical scheme is that the energy-conservation wine-tank drying apparatus of sorting type for realizing purpose, it is characterized in that: includes sorting and first drying unit and secondary drying unit;
Sorting and first drying unit include airstream drying tower, and charging aperture and hot wind inlet are arranged at airstream drying tower bottom; Pneumatic conveying drying tower bottom is impurities outlet;
Secondary drying unit includes interior-heat tube bundle drying machine, and interior-heat tube bundle drying machine front end taps into material conveyer, rear end picks out material conveyer;
The waste gas of sorting and first drying unit and secondary drying cell arrangement rear end is by discharging after sack cleaner.
Optimize: between sorting and first drying unit and secondary drying unit, have cyclone dust extractor.
Optimize: between sorting and first drying unit and secondary drying unit, have intermediate separator.
Optimize: being provided with air heat exchanger and waste gas realizes heat exchange, the hot air outlet of air heat exchanger connects the inner chamber of interior-heat tube bundle drying machine, and the gas outlet of inner chamber connects sack cleaner; The waste gas outlet of cyclone dust extractor connects the tube bank in interior-heat tube bundle drying machine, and the waste gas outlet of tube bank connects sack cleaner, provides by blower fan with the power in upper pipeline.
The beneficial effects of the utility model: in distiller grains drying course, by using the equipment of this programme, dry and the second time drying of interior-heat tube bundle drying machine owing to have employed airstream drying tower first time, in first drying process can simultaneously by distiller grains in the Impurity removal that is mixed with, when first time dries, distiller grains high humidity, adopt direct contact type to dry, ensure that distiller grains can quickly remove most of moisture in this process, and distiller grains are not by adustion. When second time adopts interior-heat tube bundle drying machine indirect drying, slow in the moisture removal in distiller grains further, be not as high owing to drying temperature, so can ensure that the dries quantity of distiller grains. And interior-heat tube bundle drying machine is to utilize the hot blast after cyclone dust extractor, the energy is made to be utilized effectively. Therefore, by the application of this utility model, make the quality of the product distiller grains produced be improved, the energy can be made again to be fully used simultaneously, save the energy.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of interior-heat tube bundle drying machine.
Detailed description of the invention
In the drawings: 1 is time delay conveyer, and 2 is belt conveyor, and 3 is feed auger, 4 is airstream drying tower, and 6 is conveying worm, and 7 is cyclone dust extractor, 8 is interior-heat tube bundle drying machine, and 9 is air-introduced machine, and 10 is sack cleaner, 11 is air-introduced machine, and 12 is sack cleaner, and 13 is air-introduced machine, 14 is air heat exchanger, and 15 is chimney, and 17 is discharging spiral conveyor, 18 is foreign material output spirals, and 19 is tube bank, and 20 is inner chamber.
Distiller grains to be dried are stored in time delay conveyer 1, uniformly exported by the conveyer belt of time delay conveyer 1, in guarantor unit's time, the material of output is consistent, can control the output of material by adjusting the speed of conveyer belt, to adapt to different yield simultaneously.
Distiller grains enter airstream drying tower 4 through belt conveyor 2 and feed auger 3.
Under the effect of air-introduced machine 9, the hot blast of 300 DEG C is inhaled into from A mouth bottom airstream drying tower 4, makes distiller grains be under suspended state in tower and contact with hot blast dry for the first time, and is entrained in intermediate separator 19 and cyclone dust extractor 7 and is easily separated.
The foreign material that in distiller grains, proportion is bigger are separated fall within bottom airstream drying tower 4 because of heavier can not taking away, foreign material export spiral 18 and export.
The first distiller grains dried being easily separated through intermediate separator 19 and cyclone dust extractor 7 are sent into the inner chamber 20 of interior-heat tube bundle drying machine 8 by conveying worm 6, carry out second time oven drying at low temperature and tube bank 19 heating indirect dryings in interior-heat tube bundle drying machine 8. In tube bank 19, used hot-air (about 100 DEG C) is introduced from cyclone dust extractor 7 by air-introduced machine 9, and the hot-air (about 50 DEG C) in inner chamber 20 is the air heated by air heat exchanger 14.
Distiller grains after drying enter conveying worm 17 and are transported to storage room after discharging from interior-heat tube bundle drying machine 8.
Under the effect of air-introduced machine 13, the air outlet slit in tube bank 19 is discharged from chimney 15 after connecing sack cleaner 12. Because this temperature discharging gas also has about 80 DEG C, for this partial heat that is used, connecing air heat exchanger 14 on pipeline before chimney 15, make expellant gas inside air heat exchanger 14, the new air sucked be heated, heated new air enters inner chamber 20.
Under the effect of air-introduced machine 11, the air outlet slit in inner chamber 20 is discharged from chimney 15 after connecing sack cleaner 10.
Claims (4)
1. the energy-conservation wine-tank drying apparatus of sorting type, is characterized in that: include sorting and first drying unit and secondary drying unit;
Sorting and first drying unit include airstream drying tower, and charging aperture and hot wind inlet are arranged at airstream drying tower bottom; Pneumatic conveying drying tower bottom is impurities outlet;
Secondary drying unit includes interior-heat tube bundle drying machine, and interior-heat tube bundle drying machine front end taps into material conveyer, rear end picks out material conveyer;
The waste gas of sorting and first drying unit and secondary drying cell arrangement rear end is by discharging after sack cleaner.
2. the energy-conservation wine-tank drying apparatus of sorting type according to claim 1, is characterized in that: have cyclone dust extractor between sorting and first drying unit and secondary drying unit.
3. the energy-conservation wine-tank drying apparatus of sorting type according to claim 1 and 2, is characterized in that: have intermediate separator between sorting and first drying unit and secondary drying unit.
4. the energy-conservation wine-tank drying apparatus of sorting type according to claim 2, it is characterized in that: be provided with air heat exchanger and waste gas realizes heat exchange, the hot air outlet of air heat exchanger connects the inner chamber of interior-heat tube bundle drying machine, and the gas outlet of inner chamber connects sack cleaner; The waste gas outlet of cyclone dust extractor connects the tube bank in interior-heat tube bundle drying machine, and the waste gas outlet of tube bank connects sack cleaner, provides by blower fan with the power in upper pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520827472.4U CN205279684U (en) | 2015-10-23 | 2015-10-23 | Energy -conserving lees drying device of sorting formula |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520827472.4U CN205279684U (en) | 2015-10-23 | 2015-10-23 | Energy -conserving lees drying device of sorting formula |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205279684U true CN205279684U (en) | 2016-06-01 |
Family
ID=56064252
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520827472.4U Expired - Fee Related CN205279684U (en) | 2015-10-23 | 2015-10-23 | Energy -conserving lees drying device of sorting formula |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205279684U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106268109A (en) * | 2016-08-31 | 2017-01-04 | 宜宾市南溪区国科中农生物科技有限公司 | A kind of processing technique of environment-friendly type distiller grains |
| CN108458566A (en) * | 2018-05-02 | 2018-08-28 | 朱增伟 | A kind of vinasse dryer |
| CN108534530A (en) * | 2018-05-02 | 2018-09-14 | 朱增伟 | A kind of wine-tank drying apparatus |
| CN108548409A (en) * | 2018-05-02 | 2018-09-18 | 朱增伟 | Wine-tank drying apparatus |
| CN108731457A (en) * | 2018-05-02 | 2018-11-02 | 朱增伟 | A kind of vinasse airflow dryer |
-
2015
- 2015-10-23 CN CN201520827472.4U patent/CN205279684U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106268109A (en) * | 2016-08-31 | 2017-01-04 | 宜宾市南溪区国科中农生物科技有限公司 | A kind of processing technique of environment-friendly type distiller grains |
| CN108458566A (en) * | 2018-05-02 | 2018-08-28 | 朱增伟 | A kind of vinasse dryer |
| CN108534530A (en) * | 2018-05-02 | 2018-09-14 | 朱增伟 | A kind of wine-tank drying apparatus |
| CN108548409A (en) * | 2018-05-02 | 2018-09-18 | 朱增伟 | Wine-tank drying apparatus |
| CN108731457A (en) * | 2018-05-02 | 2018-11-02 | 朱增伟 | A kind of vinasse airflow dryer |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160601 |