CN106225425A - The using method of corn cob dehydrator - Google Patents
The using method of corn cob dehydrator Download PDFInfo
- Publication number
- CN106225425A CN106225425A CN201610588117.5A CN201610588117A CN106225425A CN 106225425 A CN106225425 A CN 106225425A CN 201610588117 A CN201610588117 A CN 201610588117A CN 106225425 A CN106225425 A CN 106225425A
- Authority
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- Prior art keywords
- dehydrator
- corn cob
- under
- corn
- air
- 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
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- 235000005824 corn Nutrition 0.000 title claims abstract description 37
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- 235000007466 Corylus avellana Nutrition 0.000 title claims abstract description 35
- 241000209149 Zea Species 0.000 title claims abstract description 32
- 238000001035 drying Methods 0.000 claims abstract description 13
- 210000000582 Semen Anatomy 0.000 claims abstract description 5
- 240000008042 Zea mays Species 0.000 claims abstract description 5
- 229920002456 HOTAIR Polymers 0.000 claims abstract description 4
- 239000004744 fabric Substances 0.000 claims abstract description 4
- 238000000926 separation method Methods 0.000 claims abstract description 4
- 238000007790 scraping Methods 0.000 claims abstract description 3
- 239000000463 material Substances 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 3
- 240000007594 Oryza sativa Species 0.000 claims 1
- 235000007164 Oryza sativa Nutrition 0.000 claims 1
- 239000010977 jade Substances 0.000 claims 1
- 235000009566 rice Nutrition 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 210000001519 tissues Anatomy 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/02—Biomass, e.g. waste vegetative matter, straw
Abstract
The using method of the open corn cob dehydrator of the present invention, it is characterized in that, comprise the following steps, first screen cloth is used to separate mixing corn cob, after wet corn core after separation enters dehydrator, under flight uniform in drying machine drum stirs, corn cob dispersed hot-air produced with supplying heat source in dehydrator is fully contacted, and accelerates drying heat and mass；Corn cob is with under the flight of gradient and the effect of thermal medium, and under scraping wings and xeothermic wind action, Semen Maydis carries out reciprocation type along the direction in opposite direction with fresh dry-heat air and moves；Discharge to another section of star discharge valve of dehydrator and dry finished product.
Description
Technical field
The invention belongs to agricultural technology field, particularly relate to the using method of corn cob dehydrator.
Background technology
During production estimation, corn cob is that cob after seed sloughed by Semen Maydis, typically constitutes from about the 20-30% of corncob,
China has substantial amounts of corn cob be dropped or burn as fuel every year, and this is the biggest waste in fact, and corn cob can be processed into
A kind of preferably Linesless charcoal succedaneum substituted plant carbon, it is smokeless, dustless, without waste residue, and consumption is the 4/5 of Linesless charcoal, and price is the most cheap
Many, but owing to it is difficult to preserve, need this is improved.
Summary of the invention
It is contemplated that overcome the defect of prior art, it is provided that the using method of a kind of corn cob dehydrator, there is drying
Mechanization degree is high, and production capacity is relatively big, the feature that can continuously run.
In order to solve above-mentioned technical problem, the present invention provides techniques below scheme:
The using method of corn cob dehydrator, comprises the following steps, and first uses screen cloth to separate mixing corn cob, wet after separation
Corn cob enters after dehydrator, under flight uniform in drying machine drum stirs, corn cob in dehydrator dispersed with
The hot-air that supplying heat source produces is fully contacted, and accelerates drying heat and mass；Corn cob is situated between in flight and the heat with gradient
Under the effect of matter, under scraping wings and xeothermic wind action, Semen Maydis is carried out along the direction in opposite direction with fresh dry-heat air
Reciprocation type moves；Discharge to another section of star discharge valve of dehydrator and dry finished product.
Further, the first step, the broken processing of corn cob corncob is made through strict screening again, has tissue equal
The advantages such as even, hardness is suitable, good toughness, water absorption are strong, anti-wear performance is good, the most broken.
Further, corn cob dehydrator include supplying heat source, charger, revolving cylinder, discharging machine, air-introduced machine, tiltedly material valve and
Power distribution cabinet is constituted.
Compared with prior art, the present invention has a following beneficial effect:
Benefit of the invention is, dries mechanization degree height, and production capacity is relatively big, can continuously run.2. the excellent letter of structure
Single material operates steadily easy to operate by cylinder resistance.3. the few maintenance cost low-power consumption of fault is low.4. product is dried
Uniformity good.5. corn cob drying production line have employed special dispersing device, it is ensured that the drying effect of dehydrator.
Detailed description of the invention
The most peering the preferred embodiments of the present invention illustrate, it will be appreciated that preferred embodiment described herein is only
For instruction and explanation of the present invention, it is not intended to limit the present invention.
The using method of embodiment corn cob dehydrator, comprises the following steps, and is first divided by mixing corn cob employing screen cloth
From, after the wet corn core after separation enters dehydrator, under flight uniform in drying machine drum stirs, corn cob is at dehydrator
The hot-air that interior dispersed and supplying heat source produces is fully contacted, and accelerates drying heat and mass；The first step, corn cob is to use
The broken processing of corncob is made through strict screening again, has even tissue, hardness is suitable, good toughness, water absorption are strong, wearability
Advantage can be waited well, the most broken.Corn cob, with under the flight of gradient and the effect of thermal medium, is pushing away
Under flitch and xeothermic wind action, Semen Maydis carries out reciprocation type along the direction in opposite direction with fresh dry-heat air and moves；To drying
Another section of star discharge valve of dry machine is discharged and is dried finished product.Above-mentioned corn cob dehydrator include supplying heat source, charger, revolving cylinder,
Discharging machine, air-introduced machine, tiltedly material valve and power distribution cabinet are constituted.
In drying course, the technological parameter of production line and each equipment technical parameters and structure choose and design is at warp
Cross the earnest analytical study to material just to draw, and through the checking of actual corn cob baking test.
The foregoing is only explanation embodiments of the present invention, be not limited to the present invention, for the technology of this area
For personnel, all within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. made, should be included in
Within protection scope of the present invention.
Claims (3)
1. the using method of corn cob dehydrator, it is characterised in that comprise the following steps, first divides mixing corn cob employing screen cloth
From, after the wet corn core after separation enters dehydrator, under flight uniform in drying machine drum stirs, corn cob is at dehydrator
The hot-air that interior dispersed and supplying heat source produces is fully contacted, and accelerates drying heat and mass；Corn cob is with gradient
Flight and thermal medium effect under, under scraping wings and xeothermic wind action Semen Maydis along with fresh dry-heat air direction phase
Anti-direction carries out reciprocation type motion；Discharge to another section of star discharge valve of dehydrator and dry finished product.
The using method of corn cob dehydrator the most according to claim 1, it is characterised in that: the first step, corn cob is with jade
The broken processing of rice rod is made through strict screening again.
The using method of corn cob dehydrator the most according to claim 1, it is characterised in that: corn cob dehydrator includes supplying
Thermal source, charger, revolving cylinder, discharging machine, air-introduced machine, tiltedly material valve and power distribution cabinet are constituted.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610588117.5A CN106225425A (en) | 2016-07-25 | 2016-07-25 | The using method of corn cob dehydrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
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| US4549699A (en) * | 1983-09-26 | 1985-10-29 | Thompson Stanley P | Flighting for horizontal dryers |
| JP2001272169A (en) * | 2000-03-27 | 2001-10-05 | Kurimoto Ltd | Continuous type rotary drier |
| CN1640560A (en) * | 2004-01-02 | 2005-07-20 | 宝钢集团上海梅山有限公司 | Rollscale impurity-removing system and process |
| CN101167597A (en) * | 2007-12-05 | 2008-04-30 | 王建民 | Drum-type corn cob granule drying machine |
| CN201149411Y (en) * | 2007-12-27 | 2008-11-12 | 辽宁中田干燥设备制造有限公司 | Three back-travel barrel type dryer |
| CN201392086Y (en) * | 2009-04-22 | 2010-01-27 | 郑州市鼎力干燥设备有限公司 | Dehydration drying equipment of beer grains |
| CN101870548A (en) * | 2009-04-27 | 2010-10-27 | 上海环保工程成套有限公司 | Sludge stirring and granulating rotary drying device |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4549699A (en) * | 1983-09-26 | 1985-10-29 | Thompson Stanley P | Flighting for horizontal dryers |
| JP2001272169A (en) * | 2000-03-27 | 2001-10-05 | Kurimoto Ltd | Continuous type rotary drier |
| CN1640560A (en) * | 2004-01-02 | 2005-07-20 | 宝钢集团上海梅山有限公司 | Rollscale impurity-removing system and process |
| CN101167597A (en) * | 2007-12-05 | 2008-04-30 | 王建民 | Drum-type corn cob granule drying machine |
| CN201149411Y (en) * | 2007-12-27 | 2008-11-12 | 辽宁中田干燥设备制造有限公司 | Three back-travel barrel type dryer |
| CN201392086Y (en) * | 2009-04-22 | 2010-01-27 | 郑州市鼎力干燥设备有限公司 | Dehydration drying equipment of beer grains |
| CN101870548A (en) * | 2009-04-27 | 2010-10-27 | 上海环保工程成套有限公司 | Sludge stirring and granulating rotary drying device |
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