CN105972937A - Corn vinasse drying system - Google Patents
Corn vinasse drying system Download PDFInfo
- Publication number
- CN105972937A CN105972937A CN201610477282.3A CN201610477282A CN105972937A CN 105972937 A CN105972937 A CN 105972937A CN 201610477282 A CN201610477282 A CN 201610477282A CN 105972937 A CN105972937 A CN 105972937A
- Authority
- CN
- China
- Prior art keywords
- outlet
- spiral
- returning charge
- pipe bundle
- discharging
- 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.)
- Pending
Links
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B1/00—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids
- F26B1/005—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids by means of disintegrating, e.g. crushing, shredding, milling the materials to be dried
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/001—Handling, e.g. loading or unloading arrangements
- F26B25/002—Handling, e.g. loading or unloading arrangements for bulk goods
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/005—Treatment of dryer exhaust gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/005—Treatment of dryer exhaust gases
- F26B25/007—Dust filtering; Exhaust dust filters
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention discloses a corn vinasse drying system. The corn vinasse drying system mainly comprises a tube bundle drier, a material inlet and outlet system and an air exhausting system, wherein the material inlet and outlet system comprises a material inlet spiral, a material outlet spiral, a material returning spiral and a material mixer; and the air exhausting system comprises a cyclone separator, a moisture exhausting fan and a washing tower. The whole system has the advantages that the drying time is short; the working environment is clean; pollution is not caused; the whole machine volume and use amount of steam are both lower than those of other drying equipment; the corn vinasse drying system is an energy-saving product; the structure is simple; operation is convenient; the occupation area is small; and the investment is saved.
Description
Technical field
The present invention relates to distiller grains and be dried field, particularly relate to a kind of maize alcohol stillage drying system.
Background technology
Maize alcohol stillage be wine brewing after remaining residue, maize alcohol stillage through after drying can as forage feed animal,
Maize alcohol stillage is dried special distiller grains dehydrator, maize alcohol stillage dehydrator is mainly made up of thermal source, feeder, drying roller, actuating device, blanking machine, air-introduced machine and power distribution cabinet, maize alcohol stillage sends into drying roller, it is provided with in cylinder and multiple is arranged as spiral flight, by the flight that rotarily drives of cylinder, distiller grains are ceaselessly kicked up, the beating unit of barrel prevents materials from bonding barrel and flight, the material kicked up is fully contacted with by the thermal current that induced draught system is incoming, accelerate drying heat and mass, transpiring moisture, complete to be dried, discharging opening discharge.
Maize alcohol stillage dehydrator there is problems in that 1 in the course of the work, is left intact charging at present, is directly dried；2, unnecessary steam is not processed by dehydrator, causes the waste of heat；3, alcoholic steam is not recycled by dehydrator, and directly discharge can contaminated air；4, the distiller grains discharging discharging opening do not do returning charge and process: when some distiller grains is discharged and not up to dry standard, in addition it is also necessary to be again dried.
Summary of the invention
The present invention is directed to the deficiencies in the prior art, it is provided that a kind of feed rationally, steam saving, have vapour-recovery unit, discharging to have the maize alcohol stillage drying system of revert system.
The technical scheme following for realizing purpose of the present invention employing: a kind of maize alcohol stillage drying system, mainly include pipe bundle drier, discharging system and extract system, described discharging system is connected with charging aperture and the discharging opening of pipe bundle drier respectively, described extract system is connected with the bleeding point of pipe bundle drier, described discharging system includes feed auger, discharging spiral, returning charge spiral and batch mixer, described discharging spiral one end is connected with pipe bundle drier discharging opening, the other end is provided with product outlet and returning charge outlet, described returning charge outlet is connected with returning charge spiral, wet feed import and wet feed outlet it is additionally provided with on returning charge spiral, the outlet of described wet feed is connected with batch mixer import, batch mixer outlet is connected with feed auger import, feed auger outlet is connected with pipe bundle drier charging aperture；Described extract system includes cyclone separator, wet-emitting blower and scrubbing tower, described cyclone inlet is connected with pipe bundle drier bleeding point, being provided with Blowing stopper bottom described cyclone separator, Cyclone outlet is connected with wet-emitting blower, and the wet-emitting blower other end is connected with scrubbing tower.
As preferably, in described batch mixer, it is provided with stirring rod.
As preferably, at described pipe bundle drier condensation-water drain, it is provided with steam trap.
As preferably, between described discharging spiral and returning charge spiral, it is additionally provided with returning charge actuator.
Beneficial effects of the present invention: charging is stirred breaing up by discharging system of the present invention, is more beneficial for being dried, and discharging is carried out returning charge regulation, discharging the most up to standard is carried out returning charge and is dried；Bleeding point connects extract system, and the distiller grains contained in steam can effectively be removed by the scrubbing tower in extract system；Pipe bundle drier condensation-water drain is provided with steam trap simultaneously, it is possible to effective steam saving.
Accompanying drawing explanation
Fig. 1 is present configuration schematic diagram.
In figure: 1 is pipe bundle drier, 1.1 is charging aperture, 1.2 is discharging opening, 1.3 is bleeding point, 2 is feed auger, 2.1 is feed auger import, 2.2 is feed auger outlet, 3 is discharging spiral, 3.1 is product outlet, 3.2 is returning charge outlet, 4 is returning charge spiral, 4.1 is wet feed import, 4.2 is wet feed outlet, 5 is batch mixer, 5.1 is batch mixer import, 5.2 is batch mixer outlet, 6 is cyclone separator, 7 is wet-emitting blower, 8 is scrubbing tower, 9 is Blowing stopper, 10 is stirring rod, 11 is steam trap, 12 is returning charge actuator.
Detailed description of the invention
nullA kind of maize alcohol stillage drying system，Mainly include pipe bundle drier 1、Discharging system and extract system，Described discharging system is connected with charging aperture 1.1 and the discharging opening 1.2 of pipe bundle drier respectively，Described extract system is connected with the bleeding point 1.3 of pipe bundle drier，Described discharging system includes feed auger 2、Discharging spiral 3、Returning charge spiral 4 and batch mixer 5，Described discharging spiral 3 one end is connected with pipe bundle drier discharging opening 1.1，The other end is provided with product outlet 3.1 and returning charge outlet 3.2、Described returning charge outlet 3.2 is connected with returning charge spiral 4，Wet feed import 4.1 and wet feed outlet 4.2 it is additionally provided with on returning charge spiral 4，Described wet feed outlet 4.2 is connected with batch mixer import 5.1，Batch mixer outlet 5.2 is connected with feed auger import 2.1，Feed auger outlet 2.2 is connected with pipe bundle drier charging aperture 1.1；Described extract system includes cyclone separator 6, wet-emitting blower 7 and scrubbing tower 8, the import of described cyclone separator 6 is connected with pipe bundle drier bleeding point 1.3, it is provided with Blowing stopper 9 bottom described cyclone separator 6, cyclone separator 6 outlet is connected with wet-emitting blower 7, and wet-emitting blower 7 other end is connected with scrubbing tower 8；It is provided with stirring rod 10 in described batch mixer 5；It is provided with steam trap 11 at described pipe bundle drier 1 condensation-water drain；It is additionally provided with returning charge actuator 12 between described discharging spiral 3 and returning charge spiral 4.
The invention is not limited in the maize alcohol stillage drying system involved by above-mentioned detailed description of the invention, those skilled in the art also can make multiple change accordingly, but any is equal to the present invention or similar change all should be contained within the scope of the claims.
Claims (4)
1. a maize alcohol stillage drying system, mainly include pipe bundle drier, discharging system and extract system, described discharging system is connected with charging aperture and the discharging opening of pipe bundle drier respectively, described extract system is connected with the bleeding point of pipe bundle drier, it is characterized in that: described discharging system includes feed auger, discharging spiral, returning charge spiral and batch mixer, described discharging spiral one end is connected with pipe bundle drier discharging opening, the other end is provided with product outlet and returning charge outlet, described returning charge outlet is connected with returning charge spiral, wet feed import and wet feed outlet it is additionally provided with on returning charge spiral, the outlet of described wet feed is connected with batch mixer import, batch mixer outlet is connected with feed auger import, feed auger outlet is connected with pipe bundle drier charging aperture；Described extract system includes cyclone separator, wet-emitting blower and scrubbing tower, described cyclone inlet is connected with pipe bundle drier bleeding point, being provided with Blowing stopper bottom described cyclone separator, Cyclone outlet is connected with wet-emitting blower, and the wet-emitting blower other end is connected with scrubbing tower.
A kind of maize alcohol stillage drying system the most according to claim 1, it is characterised in that: it is provided with stirring rod in described batch mixer.
A kind of maize alcohol stillage drying system the most according to claim 1, it is characterised in that: it is provided with steam trap at described pipe bundle drier condensation-water drain.
A kind of maize alcohol stillage drying system the most according to claim 1, it is characterised in that: it is additionally provided with returning charge actuator between described discharging spiral and returning charge spiral.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610477282.3A CN105972937A (en) | 2016-06-27 | 2016-06-27 | Corn vinasse drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610477282.3A CN105972937A (en) | 2016-06-27 | 2016-06-27 | Corn vinasse drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105972937A true CN105972937A (en) | 2016-09-28 |
Family
ID=57020689
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610477282.3A Pending CN105972937A (en) | 2016-06-27 | 2016-06-27 | Corn vinasse drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105972937A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109007320A (en) * | 2018-06-13 | 2018-12-18 | 马鞍山中粮生物化学有限公司 | A kind of maize alcohol stillage feed and preparation method thereof |
| CN114950060A (en) * | 2022-05-23 | 2022-08-30 | 江苏益元泰生物技术有限公司 | Integrated treatment method for distillers' grains drying tail gas |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201795667U (en) * | 2010-04-29 | 2011-04-13 | 陕西科技大学 | Novel energy-saving pomace drying device |
| CN103344095A (en) * | 2013-07-25 | 2013-10-09 | 湖北泰盛化工有限公司 | Recovery method for sending glyphosate original chemical back automatically |
| CN203454664U (en) * | 2013-08-15 | 2014-02-26 | 山东星光生物科技有限公司 | Corn protein powder drying system |
| CN203629203U (en) * | 2013-12-25 | 2014-06-04 | 山东奥诺能源科技有限公司 | Superheat steam drying device |
| CN205897703U (en) * | 2016-06-27 | 2017-01-18 | 宜兴市格兰特干燥浓缩设备有限公司 | Maize lees drying system |
-
2016
- 2016-06-27 CN CN201610477282.3A patent/CN105972937A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201795667U (en) * | 2010-04-29 | 2011-04-13 | 陕西科技大学 | Novel energy-saving pomace drying device |
| CN103344095A (en) * | 2013-07-25 | 2013-10-09 | 湖北泰盛化工有限公司 | Recovery method for sending glyphosate original chemical back automatically |
| CN203454664U (en) * | 2013-08-15 | 2014-02-26 | 山东星光生物科技有限公司 | Corn protein powder drying system |
| CN203629203U (en) * | 2013-12-25 | 2014-06-04 | 山东奥诺能源科技有限公司 | Superheat steam drying device |
| CN205897703U (en) * | 2016-06-27 | 2017-01-18 | 宜兴市格兰特干燥浓缩设备有限公司 | Maize lees drying system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109007320A (en) * | 2018-06-13 | 2018-12-18 | 马鞍山中粮生物化学有限公司 | A kind of maize alcohol stillage feed and preparation method thereof |
| CN114950060A (en) * | 2022-05-23 | 2022-08-30 | 江苏益元泰生物技术有限公司 | Integrated treatment method for distillers' grains drying tail gas |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160928 |