CN205512014U - Drying -machine for grain - Google Patents
Drying -machine for grain Download PDFInfo
- Publication number
- CN205512014U CN205512014U CN201620108342.XU CN201620108342U CN205512014U CN 205512014 U CN205512014 U CN 205512014U CN 201620108342 U CN201620108342 U CN 201620108342U CN 205512014 U CN205512014 U CN 205512014U
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- CN
- China
- Prior art keywords
- urceolus
- inner core
- dehydrator
- baffle plate
- hot blast
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- 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
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Abstract
The utility model belongs to a drying -machine for grain, including raw materials warehouse and lifting machine, the end of lifting machine links to each other with two feeding feed bins at drying -machine top, the drying -machine includes inner tube and urceolus, the top of urceolus is equipped with feeding feed bin and dust remover, install the distributing device on the position that the urceolus is inside and feeding feed bin lower part is corresponding, the lower part of urceolus is equipped with hot -blast intake stack, and the bottom of urceolus is equipped with the discharge gate, and the air inlet of give vent to anger pipeline and the inner tube lower part of dust remover links to each other, and the top of inner tube is equipped with the waste gas exhaust pipe way, the inside of inner tube is equipped with the hot -blast circulation baffle in a plurality of layers, the lower part of distributing device is equipped with a plurality of layers of slope ring shape flitch down, have the occupation of land less, the small investment, the loss is little, power consumption is little, heat utilization rate is high, output is big, operation safety, fault rate low, broken low, the running cost is low, for dry is thorough, long service life and easy operation's advantage.
Description
Technical field
This utility model belongs to dehydrator technical field, relates to a kind of grain dehydrator.
Background technology
Tradition drying plant mainly has two kinds, is respectively as follows: tower drier and rotating drum type drying machine；Tower drier energy consumption is low, good drying effect, but also exist investment high and easily catch fire, the problem of easy putty, operationally there is the biggest potential safety hazard；Although rotating drum type drying machine is invested little, there is energy consumption high, rate of heat exchange is low, and drying effect is poor, and percentage of damage is high, the defect that equipment failure rate is high and maintainability is poor；Specific in foodstuff drying device, conveyer belt is often used to transmit in order to improve rate of heat exchange inside most vertical foodstuff drying device, when increase while energy resource consumption due to conveyer belt is at high temperature continuous firing easily break down and affect service life, inflammable additionally, due to grain, therefore generally entering the heat source temperature within dehydrator unsuitable too high, this results in grain needs long-time delay dehydrator and there is the defect of drying effect difference.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, and provides a kind of small investment, and thermal efficiency utilization rate is high, and drying materials is thorough, service life is long, runs safety and a kind of grain tower drier of maintenance cost reduction.
The purpose of this utility model is achieved in that this dehydrator includes raw material warehouse and elevator, the end of elevator is connected with two charging feed bins at dehydrator top, described dehydrator includes inner core and urceolus, the top of described urceolus is provided with charging feed bin and cleaner unit, on the position that described outer barrel is corresponding with charging feed bin bottom, distributing device is installed, the bottom of urceolus is provided with hot-air inlet pipe road, the bottom of urceolus is provided with discharging opening, the outlet pipe of cleaner unit is connected with the air inlet of inner core bottom, the top of inner core is provided with exhaust emission tube road, if the inside of described inner core is provided with dried layer hot air flow leads to baffle plate, if the bottom of described distributing device is provided with dried layer tilts annular blanking plate.
Preferably, if described dried layer tilts annular blanking plate and is arranged between inner core and urceolus, the middle part tilting annular blanking plate is higher than two ends, and the middle part that lower floor tilts annular blanking plate is corresponding with the bottom that upper strata tilts annular blanking plate end.
Preferably, if described dried layer hot air flow leads to baffle plate and includes the first hot blast circulation baffle plate and the second hot blast circulation baffle plate, first hot blast circulation baffle plate and the second hot blast circulation baffle plate are crisscross arranged in the inside of inner core, one end of first hot blast circulation baffle plate is connected with the inwall of inner core, and the other end of the second hot blast circulation baffle plate is connected with the inwall of inner core.
Preferably, described cleaner unit includes threeway dedusting wind pipe, the inner core being connected with threeway dedusting wind pipe the first end, the dedusting funnel being connected with threeway dedusting wind pipe the second end and the outlet pipe being connected with threeway dedusting wind pipe the 3rd end.
Preferably, if described dried layer tilts the cavity body structure that annular blanking plate is interior side opening, inner core offers the heat exchange elongated hole suitable with above-mentioned opening.
Preferably, if it is heat resisting steel goods that described dried layer tilts annular blanking plate.
This utility model have occupation of land less, small investment, loss is little, power consumption is little, heat utilization rate is high, yield is big, run safety, failure rate is low, crush low, operating cost is low, drying materials is thorough, service life length and advantage simple to operate.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
In order to be more clearly understood from technical characteristic of the present utility model, purpose and effect, now comparison accompanying drawing illustrates detailed description of the invention of the present utility model, and the most identical label represents identical parts.For making simplified form, only schematically show the part relevant to utility model in each figure, they do not represent its practical structures as product.
As shown in Figure 1, this utility model is a kind of grain dehydrator, this dehydrator includes raw material warehouse 1 and elevator 2, the end of elevator 2 is connected with two charging feed bins 3 at dehydrator top, described dehydrator includes inner core 4 and urceolus 5, the top of described urceolus 5 is provided with charging feed bin 3 and cleaner unit 6, described urceolus 5 is provided with distributing device 10 on the internal position corresponding with charging feed bin 3 bottom, the bottom of urceolus 5 is provided with hot-air inlet pipe road 7, the bottom of urceolus 5 is provided with discharging opening 8, the outlet pipe 15 of cleaner unit 6 is connected with the air inlet 14 of inner core 4 bottom, the top of inner core 4 is provided with exhaust emission tube road 16, if the inside of described inner core 4 is provided with dried layer hot air flow leads to baffle plate 12, if the bottom of described distributing device 10 is provided with dried layer tilts annular blanking plate 13.Being arranged between inner core 4 and urceolus 5 if described dried layer tilts annular blanking plate 13, the middle part tilting annular blanking plate 13 is higher than two ends, and the middle part that lower floor tilts annular blanking plate 13 is corresponding with the bottom that upper strata tilts annular blanking plate 13 end.If described dried layer hot air flow leads to baffle plate 12 and includes the first hot blast circulation baffle plate and the second hot blast circulation baffle plate, first hot blast circulation baffle plate and the second hot blast circulation baffle plate are crisscross arranged in the inside of inner core 4, one end of first hot blast circulation baffle plate is connected with the inwall of inner core 4, and the other end of the second hot blast circulation baffle plate is connected with the inwall of inner core 4.Described cleaner unit 6 includes threeway dedusting wind pipe 17, the inner core 4 being connected with threeway dedusting wind pipe 17 first end, the dedusting funnel 9 being connected with threeway dedusting wind pipe 17 second end and the outlet pipe 15 being connected with threeway dedusting wind pipe 17 the 3rd end.If described dried layer tilts the cavity body structure that annular blanking plate 13 is interior side opening, inner core 4 offers the heat exchange elongated hole 11 suitable with above-mentioned opening.If it is heat resisting steel goods that described dried layer tilts annular blanking plate 13.
When using this utility model, material enters in the charging feed bin 3 at dehydrator top by raw material warehouse 1 and elevator 2, enter in dehydrator urceolus 5 by the action of gravity of material, if entering dried layer by distributing device 10 to tilt in annular blanking plate 13, if tilting annular blanking plate 13 by dried layer under gravity to enter discharging opening 8；Hot-air inlet pipe road 7 is entered in urceolus 5 by the bottom of urceolus 5 and dries material, if when hot blast walks around the upper strata that dried layer inclination annular blanking plate 13 enters dehydrator urceolus 5, impurity and airborne dust in hot blast and material enter in cleaner unit 6 by threeway dedusting wind pipe 17, impurity and airborne dust in material enter in dedusting funnel 9, hot blast is entered the bottom of inner core 4 by threeway dedusting wind pipe 17 the 3rd end and outlet pipe 15, if hot blast walks around dried layer hot air flow leads to baffle plate 12, and pass through exhaust emission tube road 16 after carrying out heat exchange by the barrel of inner core 4 and heat exchange elongated hole 11 are internal with urceolus 5 and discharge；The temperature of the hot blast described in this utility model is at least 800 DEG C, owing to material is dried in urceolus 5 by hot blast, can reduce hence into temperature during inner core 4, hot blast in inner core 4 can carry out heat exchange with the hot blast of urceolus 5, farthest dries material under ensureing the incombustible premise of material.Hot blast in inner core 4 carries out heat exchange by inner tube wall and heat exchange elongated hole 11 to urceolus 5 is internal, the top of urceolus 5 be preheating zone, middle and lower part be constant temperature drying district, material can also be dried if dried layer tilts annular blanking plate 13 top, the inside of its urceolus 5 can keep long constant temperature, and do not change, thus reach lasting material is uniformly dried, reach to be lost little, power consumption is little, heat utilization rate is high, yield is big, run safety, failure rate is low, broken low, operating cost is low, drying materials purpose thoroughly；Owing to top of the present utility model is provided with cleaner unit 6, therefore on the premise of ensureing material cleaning, environment is the most contaminated, is effectively guaranteed the healthy of field personnel.Only elevator 2 and the cleaner unit 6 of power consumption in this utility model, material motion in dehydrator is realized by action of gravity.
In description of the present utility model, it will be appreciated that, orientation or the position relationship of term " bottom ", " bottom ", " top " etc. instruction are based on orientation shown in the drawings or position relationship, it is for only for ease of description this utility model and simplifies description, rather than instruction or the device of hint indication or element must have specific orientation, with specific azimuth configuration and operation, therefore it is not intended that to restriction of the present utility model.In description of the present utility model, it should be noted that unless otherwise clearly defined and limited, term " is provided with ", " installation ", " connection ", " being connected " etc. should be interpreted broadly, and connects for example, it may be fixing, it is integrally connected, it is also possible to be to removably connect；It can also be the connection of two element internals；Can be to be joined directly together, it is also possible to be indirectly connected to by intermediary, for the ordinary skill in the art, above-mentioned term concrete meaning in this utility model can be understood as the case may be.Foregoing detailed description is only for illustrating of feasibility embodiment of the present utility model; they are also not used to limit protection domain of the present utility model, all made without departing from this utility model skill spirit equivalent implementations, change and within transformation should be included in protection domain of the present utility model.
Claims (6)
- null1. a grain dehydrator，This dehydrator includes raw material warehouse (1) and elevator (2)，It is characterized in that: the end of elevator (2) is connected with two chargings feed bin (3) at dehydrator top，Described dehydrator includes inner core (4) and urceolus (5)，The top of described urceolus (5) is provided with charging feed bin (3) and cleaner unit (6)，Described urceolus (5) is provided with distributing device (10) on the internal position corresponding with charging feed bin (3) bottom，The bottom of urceolus (5) is provided with hot-air inlet pipe road (7)，The bottom of urceolus (5) is provided with discharging opening (8)，The outlet pipe (15) of cleaner unit (6) is connected with the air inlet (14) of inner core (4) bottom，The top of inner core (4) is provided with exhaust emission tube road (16)，Described inner core (4) if inside be provided with dried layer hot air flow and lead to baffle plate (12)，Described distributing device (10) if bottom be provided with dried layer tilt annular blanking plate (13).
- A kind of grain dehydrator, it is characterized in that: if described dried layer tilts annular blanking plate (13) and is arranged between inner core (4) and urceolus (5), the middle part tilting annular blanking plate (13) is higher than two ends, and the middle part that lower floor tilts annular blanking plate (13) is corresponding with the bottom that upper strata tilts annular blanking plate (13) end.
- A kind of grain dehydrator, it is characterized in that: if described dried layer hot air flow leads to baffle plate (12) and includes the first hot blast circulation baffle plate and the second hot blast circulation baffle plate, first hot blast circulation baffle plate and the second hot blast circulation baffle plate are crisscross arranged in the inside of inner core (4), one end of first hot blast circulation baffle plate is connected with the inwall of inner core (4), and the other end of the second hot blast circulation baffle plate is connected with the inwall of inner core (4).
- A kind of grain dehydrator, it is characterised in that: described cleaner unit (6) includes the dedusting funnel (9) that the inner core (4) that threeway dedusting wind pipe (17) is connected is connected with threeway dedusting wind pipe (17) second end and the outlet pipe (15) being connected with threeway dedusting wind pipe (17) the 3rd end with threeway dedusting wind pipe (17) first end.
- A kind of grain dehydrator, it is characterized in that: if described dried layer tilts the cavity body structure that annular blanking plate (13) is interior side opening, inner core (4) offers heat exchange elongated hole (11) suitable with above-mentioned opening.
- A kind of grain dehydrator, it is characterised in that: if it is heat resisting steel goods that described dried layer tilts annular blanking plate (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620108342.XU CN205512014U (en) | 2016-02-03 | 2016-02-03 | Drying -machine for grain |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620108342.XU CN205512014U (en) | 2016-02-03 | 2016-02-03 | Drying -machine for grain |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205512014U true CN205512014U (en) | 2016-08-31 |
Family
ID=56776451
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620108342.XU Expired - Fee Related CN205512014U (en) | 2016-02-03 | 2016-02-03 | Drying -machine for grain |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205512014U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115574586A (en) * | 2022-10-17 | 2023-01-06 | 河南省中农嘉吉化工有限公司 | Dryer for microbial organic fertilizer and using method thereof |
-
2016
- 2016-02-03 CN CN201620108342.XU patent/CN205512014U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115574586A (en) * | 2022-10-17 | 2023-01-06 | 河南省中农嘉吉化工有限公司 | Dryer for microbial organic fertilizer and using method thereof |
| CN115574586B (en) * | 2022-10-17 | 2024-01-26 | 河南省中农嘉吉化工有限公司 | Dryer for microbial organic fertilizer and application method thereof |
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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 |
Granted publication date: 20160831 Termination date: 20220203 |
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| CF01 | Termination of patent right due to non-payment of annual fee |