CN201688672U - Dryer - Google Patents
Dryer Download PDFInfo
- Publication number
- CN201688672U CN201688672U CN2010201998243U CN201020199824U CN201688672U CN 201688672 U CN201688672 U CN 201688672U CN 2010201998243 U CN2010201998243 U CN 2010201998243U CN 201020199824 U CN201020199824 U CN 201020199824U CN 201688672 U CN201688672 U CN 201688672U
- Authority
- CN
- China
- Prior art keywords
- drying
- housing
- drying machine
- heater
- change
- 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 claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000011343 solid material Substances 0.000 abstract description 2
- 239000002440 industrial waste Substances 0.000 abstract 1
- 238000012216 screening Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 230000003115 biocidal effect Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000000855 fermentation Methods 0.000 description 5
- 230000004151 fermentation Effects 0.000 description 5
- 102000004169 proteins and genes Human genes 0.000 description 5
- 108090000623 proteins and genes Proteins 0.000 description 5
- 229930194936 Tylosin Natural products 0.000 description 4
- 239000004182 Tylosin Substances 0.000 description 4
- WBPYTXDJUQJLPQ-VMXQISHHSA-N tylosin Chemical compound O([C@@H]1[C@@H](C)O[C@H]([C@@H]([C@H]1N(C)C)O)O[C@@H]1[C@@H](C)[C@H](O)CC(=O)O[C@@H]([C@H](/C=C(\C)/C=C/C(=O)[C@H](C)C[C@@H]1CC=O)CO[C@H]1[C@@H]([C@H](OC)[C@H](O)[C@@H](C)O1)OC)CC)[C@H]1C[C@@](C)(O)[C@@H](O)[C@H](C)O1 WBPYTXDJUQJLPQ-VMXQISHHSA-N 0.000 description 4
- 229960004059 tylosin Drugs 0.000 description 4
- 235000019375 tylosin Nutrition 0.000 description 4
- 244000144972 livestock Species 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 240000008042 Zea mays Species 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- CGQCWMIAEPEHNQ-UHFFFAOYSA-N Vanillylmandelic acid Chemical compound COC1=CC(C(O)C(O)=O)=CC=C1O CGQCWMIAEPEHNQ-UHFFFAOYSA-N 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000003864 humus Substances 0.000 description 1
- 235000009973 maize Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- UURAUHCOJAIIRQ-QGLSALSOSA-N tiamulin Chemical compound CCN(CC)CCSCC(=O)O[C@@H]1C[C@@](C)(C=C)[C@@H](O)[C@H](C)[C@@]23CC[C@@H](C)[C@]1(C)[C@@H]2C(=O)CC3 UURAUHCOJAIIRQ-QGLSALSOSA-N 0.000 description 1
- 229960004885 tiamulin Drugs 0.000 description 1
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- Processing Of Solid Wastes (AREA)
Abstract
The utility model relates to drying equipment, in particular to a helical pitch-change temperature adjustment dryer used for drying fermented industrial waste and capable of adjusting drying heat within a certain range and achieving the drying of separated material and water. The helical pitch-change can vary the structural style of materials, extrude liquid with dilute concentration in a pitch-change manner, and achieve the drying of material at last. The temperature range is adjusted to protect the variation relationship between water and material, and to achieve better separation of solid material and liquid simultaneously.
Description
Technical field
The utility model relates to a kind of drying equipment, is specifically related to be used for the drying machine of fermentation industry waste material drying, particularly a kind of drying machine that is used for the fermented maize screenings drying of fermentation industry generation.
Background technology
Exist the great waste material of a large amount of water content in traditional fermentation industry, as preparing AVM, tylosin, Tiamulin and Cobastab
12The time, all there is such problem, with the preparation tylosin is example, its general corn fermentation that adopts is prepared, produce one ton of tylosin and will produce about 22 tons of screenings, and contain a large amount of moisture in these screenings, oil content, separation difficulty, and wherein contain amounts of protein, amino acid and the tylosin that is not extracted out, and general processing mode is that screenings directly is processed into feed, but owing to wherein contain the Qin Le rhzomorph that is not extracted out, at first reduced the nutrition of feed after joining in the feed as antibiotic, secondly can cause the edible back of the livestock interior antibiotic content of body high, so also can bring unnecessary threat the human health of edible livestock.
Traditional processing technology generally is to adopt the processing method of high temperature drying, though this method can reduce the content of antibiotic in feed to a certain extent, but also can cause a large amount of damages of protein simultaneously, reduce the efficient of feed, simultaneously under the condition of high temperature, screenings since chemical reaction particularly the coking of protein cause very big peculiar smell, for operating personnel's health and surrounding environment bigger influence is arranged, and the equipment that is adopted also exists the energy consumption height, the problem that treatment effeciency is low.
Summary of the invention
Many weak points at the prior art existence, many weak points of existing of drying equipment particularly, the utility model provides a kind of drying machine that is used for fermentation industry waste material drying. can carry out the adjusting of dry heat within the specific limits, can realize the disengaging drying of material and water again. variable-pitch propeller can change the version of material, the liquid of displacement extruding dilute concentration, and finally realize the dry of material and guarantee that the protein etc. in the screenings can not be consumed, finish better separating of solid material and liquid simultaneously.
The concrete technical scheme that the utility model adopted is: a kind of drying machine, comprise housing and power set, described hull outside is provided with heater, being provided with in the housing can be with the variable-pitch propeller propeller of power set rotation, described housing is provided with charging aperture and discharging opening, also be provided with at least one gas outlet and at least one the liquid outlet that runs through heater on the housing, described gas outlet is positioned at housing top, and described liquid outlet is positioned at lower housing portion.
After adopting this design, can send in the housing from charging aperture by the screenings that water content is bigger, under the drive of power set, spiral propeller begins to rotate, in pressing materials, it is advanced, because this spiral propeller is a variable-pitch propeller, therefore screenings can constantly be squeezed in the process that advances, thereby liquid component is wherein fast pushed out, under the effect of heater, volatile material such as moisture can be evaporated to gaseous state, thereby is discharged by the gas outlet on the housing simultaneously, same for the liquid that still can not vaporize after the heating, as oily matter etc., then can discharge, in order to reach better effect by the liquid outlet of lower housing portion, but heater is the temperature adjustment design, can adjust the temperature of heating like this according to the charging situation at any time, and, the material loosening device can be set on spiral propeller in order to be more preferably gaseous volatilization, carry out after making things convenient for material to be extruded to a certain degree loose, thereby gas-liquid wherein better is isolated and excluded.
In order to improve the effect of heating, the heater that the utility model adopts is to be attached to the outer heating jacket of whole housing, adopts in the described heating jacket to add deep fat or other heat-conducting mediums as thermal source, or directly adopts the electrical heating cover to heat.
For the reasonable utilization of implementation space, housing described in the utility model can be arranged on the support, and power set are arranged on the support bottom, can save a large amount of spaces like this, for enterprise saves cost.
After adopting this equipment, owing in the whole process heating arrangements effect is arranged all, the frictional heat of material in addition, formed a stable baking temperature, the mode that can change high-temperature process in the past like this is for protein and amino acid whose destruction, reduced the temperature when dry simultaneously, reduced energy consumption, because processing procedure is the long time treatment process in drying machine, and temperature constant, antibiotic is lost activity finally become humus, reduced antibiotic content when material is made feed after with drying and realized that harmless treatment has improved the active constituent content of feed, also reduce the edible feed of livestock and the unsafe factor that brings.
Description of drawings
Fig. 1 is the structure cut-away view of drying machine described in the utility model;
Fig. 2 is the cutaway view Amplified image of A-A among Fig. 1;
1 is support among the figure, and 2 are rotating shaft, and 3 is charging aperture, and 4 is the variable-pitch propeller propeller, and 5 is the gas outlet, and 6 is discharging opening, and 7 is liquid outlet, and 8 is housing, and 9 is heater.
The specific embodiment
A kind of drying machine, comprise housing 8 and power set, described housing 8 outer setting have heater 9, being provided with in the housing 8 can be with the variable-pitch propeller propeller 4 of power set rotation, described housing 8 is provided with charging aperture 3 and discharging opening 6, also be provided with two gas outlets 5 and three liquid outlets 7 of running through heater 9 on the housing 8, described gas outlet 5 is positioned at case top, and described liquid outlet 7 is positioned at housing bottom.
The heater 9 that is adopted is for being arranged on the thermal conductive cavity of hull outside continuously, and thermal conductive cavity inside is conduction oil;
Described housing 8 is arranged on the support 1.
Claims (4)
1. drying machine, comprise housing (8) and power set, described housing (8) is provided with charging aperture (3) and discharging opening (6), it is characterized in that: being provided with in the described housing (8) can be with the variable-pitch propeller propeller (4) of power set rotation, also be provided with at least one gas outlet (5) and the liquid outlet of at least one (7) that runs through heater on the housing (8), described gas outlet (5) is positioned at case top, and described liquid outlet (7) is positioned at housing bottom.
2. drying machine according to claim 1 is characterized in that: described housing (8) outer setting has heater (9).
3. drying machine according to claim 2 is characterized in that: described heater (9) is the thermal conductive cavity of electrical heating cover or built-in heat-conducting medium.
4. drying machine according to claim 1 is characterized in that: described housing (8) is arranged on the support (1).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010201998243U CN201688672U (en) | 2010-05-24 | 2010-05-24 | Dryer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010201998243U CN201688672U (en) | 2010-05-24 | 2010-05-24 | Dryer |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201688672U true CN201688672U (en) | 2010-12-29 |
Family
ID=43376952
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2010201998243U Expired - Fee Related CN201688672U (en) | 2010-05-24 | 2010-05-24 | Dryer |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201688672U (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102352432A (en) * | 2011-08-30 | 2012-02-15 | 杨佳定 | Concentrate drying and roasting device and method for directly drying and roasting concentrate by using same |
CN103438680A (en) * | 2013-08-20 | 2013-12-11 | 顾丽霞 | Fodder spiral transportation and drying equipment |
CN105556230A (en) * | 2013-09-18 | 2016-05-04 | 阿里-杰克控股私人有限公司 | Process and apparatus for treating sludge |
CN106804702A (en) * | 2015-11-30 | 2017-06-09 | 湖南角山米业有限责任公司 | A kind of rice drying unit |
CN110887370A (en) * | 2019-11-07 | 2020-03-17 | 湖南工业大学 | Blending type wood powder drying device and process thereof |
-
2010
- 2010-05-24 CN CN2010201998243U patent/CN201688672U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102352432A (en) * | 2011-08-30 | 2012-02-15 | 杨佳定 | Concentrate drying and roasting device and method for directly drying and roasting concentrate by using same |
CN103438680A (en) * | 2013-08-20 | 2013-12-11 | 顾丽霞 | Fodder spiral transportation and drying equipment |
CN105556230A (en) * | 2013-09-18 | 2016-05-04 | 阿里-杰克控股私人有限公司 | Process and apparatus for treating sludge |
CN106804702A (en) * | 2015-11-30 | 2017-06-09 | 湖南角山米业有限责任公司 | A kind of rice drying unit |
CN110887370A (en) * | 2019-11-07 | 2020-03-17 | 湖南工业大学 | Blending type wood powder drying device and process thereof |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101229 Termination date: 20130524 |