CN206656545U - A kind of drying plant - Google Patents
A kind of drying plant Download PDFInfo
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- CN206656545U CN206656545U CN201720301419.XU CN201720301419U CN206656545U CN 206656545 U CN206656545 U CN 206656545U CN 201720301419 U CN201720301419 U CN 201720301419U CN 206656545 U CN206656545 U CN 206656545U
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- 238000001035 drying Methods 0.000 title claims abstract description 174
- 239000000463 material Substances 0.000 claims abstract description 295
- 230000033001 locomotion Effects 0.000 claims abstract description 17
- 238000000926 separation method Methods 0.000 claims abstract description 13
- 238000007599 discharging Methods 0.000 claims abstract description 9
- 239000007789 gas Substances 0.000 claims description 12
- 239000012535 impurity Substances 0.000 claims description 12
- 239000000428 dust Substances 0.000 claims description 10
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 10
- 238000004880 explosion Methods 0.000 claims description 6
- 239000003345 natural gas Substances 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 4
- 241000196324 Embryophyta Species 0.000 abstract description 50
- 244000025254 Cannabis sativa Species 0.000 abstract description 31
- 239000004459 forage Substances 0.000 abstract description 29
- 239000010902 straw Substances 0.000 abstract description 27
- 239000004615 ingredient Substances 0.000 abstract description 5
- 235000016709 nutrition Nutrition 0.000 abstract description 5
- 230000002035 prolonged effect Effects 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 11
- 230000000694 effects Effects 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000000050 nutritive effect Effects 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 244000038280 herbivores Species 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 238000003306 harvesting Methods 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 210000001367 artery Anatomy 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000011089 mechanical engineering Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000001932 seasonal effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The utility model provides a kind of drying plant, and the drying plant includes：Hot-blast stove, air-flow pulser and first material separator, wherein, hot-blast stove is connected with the charging aperture of air-flow pulser, and the discharging opening of air-flow pulser is connected with the charging aperture of first material separator；Hot-blast stove, for providing hot air flow, hot air flow is carried material to be dried and enter air-flow pulser；Air-flow pulser, for making material to be dried suspended motion in hot air flow, drying and processing is carried out to treat material drying, forms material drying, and the material drying is transferred to by the first material separator by hot air flow；First material separator, for by material drying and hot blast flow separation.Due to not needing prolonged natural drying, the loss of forage grass and agricultural crop straw nutritional ingredient will not be caused, more will not moldy metamorphism.The quality for drying forage grass and agricultural crop straw is obtained therefore, it is possible to improve.
Description
Technical field
Mechanical engineering technical field is the utility model is related to, more particularly to a kind of drying plant.
Background technology
With the development of animal husbandry, a kind of important feed of forage grass and agricultural crop straw as Herbivore, the amount of asking is not
Disconnected increase.But because the growth of forage grass and crops has seasonality, and the higher forage grass of water content and agricultural crop straw
It is easily mouldy during accumulation, cause nutritive value to reduce.In order to meet Herbivore the Various Seasonal the needs of, it is necessary to forage grass
It is dried with agricultural crop straw, by storing dried forage grass and agricultural crop straw, to ensure forage grass and agricultural crop straw
Nutritive value.
At present, the drying mode of forage grass and agricultural crop straw is mainly natural drying, i.e., by manual type by forage grass and
Agricultural crop straw is spread out to be dried under the sun.
Because the temperature of natural drying is relatively low, it is often necessary to which longer time could dry forage grass and agricultural crop straw
Entirely, and natural drying is had a great influence by weather, such as rainy weather, on the one hand makes forage grass and agricultural crop straw moister,
The natural drying of longer time is caused, and the loss of forage grass and agricultural crop straw nutritional ingredient can be caused by drying overlong time, separately
On the one hand forage grass and agricultural crop straw moldy metamorphism can also be made.Therefore, forage grass and agricultural crop straw are dried by existing
Method, the drying forage grass obtained and the quality of agricultural crop straw are relatively low.
Utility model content
The utility model embodiment provides a kind of drying plant, it is possible to increase obtains and dries forage grass and agricultural crop straw
Quality.
The utility model embodiment provides a kind of drying plant, and the drying plant includes：Hot-blast stove, air-flow pulser and
First material separator, wherein,
The hot-blast stove is connected with the charging aperture of the air-flow pulser, the discharging opening of the air-flow pulser and described the
The charging aperture of one material separator is connected；
The hot-blast stove, for providing hot air flow, the hot air flow is carried material to be dried and enter the air-flow pulse
Device；
The air-flow pulser, for making the material to be dried suspended motion in the hot air flow, to be treated to described
Material drying carries out drying and processing, forms material drying, and the material drying is transferred into described the by the hot air flow
One material separator；
The first material separator, for by the material drying and the hot blast flow separation.
Preferably, the drying plant further comprises：Pulverizer and second material separator, wherein,
The discharging opening of the pulverizer is connected with the charging aperture of the second material separator, the second material separator
Discharging opening be connected between the hot-blast stove and the air-flow pulser；
The pulverizer, silk is rubbed for carrying out crushing to the material to be dried, and after being crushed by air-flow and rubbing silk
The material transferring to be dried gives the second material separator；
The second material separator, for separating the material to be dried crushed after rubbing silk and the air-flow,
And by the material transferring to be dried isolated between the hot-blast stove and the air-flow pulser, so that described to be dried
Material enters the air-flow pulser in the presence of the hot-blast stove.
Preferably, the drying plant further comprises：At least one desander, wherein,
The desander is connected between the hot-blast stove and the first material separator；
The desander, for the impurity for separating the material to be dried He being entrained in the material to be dried, and increase
Add the contact area of the material to be dried and the hot air flow.
Preferably, the drying plant further comprises：Baling press, wherein,
The baling press is connected with the first material separator；
The baling press, for receiving the material drying of first material separator separation, and by the drying
Packed after material compacting.
Preferably, the drying plant further comprises：Dehumidifier, wherein,
The dehumidifier is connected between the air-flow pulser and the first material separator；
The dehumidifier, the material drying is transferred to the hot air flow of the first material separator for reducing
Humidity, and reduce the temperature of the material drying.
Preferably, the drying plant further comprises：At least one explosion-proof valve, wherein,
The explosion-proof valve is connected between the hot-blast stove and the first material separator；
The explosion-proof valve, for when dust explosion, blast pressure is by the explosion-proof valve as caused by the powder explosion
Valve plate wash open, make one or more of the hot-blast stove, the air-flow pulser and described first material separator internal
Pressure leak.
Preferably, the drying plant further comprises：Sack cleaner, wherein,
The sack cleaner is connected with the first material separator；
The sack cleaner, the dust in the hot air flow isolated for trapping the first material separator.
Preferably, the drying plant further comprises：Bearing chassis and at least two wheels；
At least two wheel is connected with the bearing chassis；
The bearing chassis, for being carried out to the hot-blast stove, the air-flow pulser and the first material separator
Carrying, so that the band of the hot-blast stove, the air-flow pulser and the first material separator at least two wheel
Dynamic lower movement.
Preferably, the drying plant further comprises：Generator, wherein,
The generator, for in the hot-blast stove, the air-flow pulser and the first material separator appoint
Meaning one or more is powered.
Preferably, the drying plant further comprises：Gas bomb and steam turbine, wherein,
The gas bomb is connected with the steam turbine；
The gas bomb, for natural gas-storing；
The steam turbine, for providing the energy using the natural gas in the gas bomb for the generator.
The utility model embodiment provides a kind of drying plant, and the drying plant provides hot air flow by hot-blast stove, and
And material to be dried is blown into air-flow pulser, material to be dried suspended motion in air-flow pulser, make material to be dried
Being accumulated with the junction of hot-air increases, and with hot-air relative motion, so that material rapid draing to be dried.It is dried
Material drying separates hot air flow and material drying by first material separator, so as to obtain material drying.Due to not needing
Prolonged natural drying, the loss of forage grass and agricultural crop straw nutritional ingredient will not be caused, more will not moldy metamorphism.Therefore,
The quality for obtaining and drying forage grass and agricultural crop straw can be improved.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, drawings in the following description are these
Some embodiments of utility model, for those of ordinary skill in the art, on the premise of not paying creative work, also
Other accompanying drawings can be obtained according to these accompanying drawings.
Fig. 1 is a kind of structural representation for drying plant that the utility model one embodiment provides；
Fig. 2 is a kind of structural representation for drying plant including pulverizer that the utility model one embodiment provides；
Fig. 3 is a kind of structural representation for drying plant including desander that the utility model one embodiment provides；
Fig. 4 is a kind of structural representation for drying plant including baling press that the utility model one embodiment provides；
Fig. 5 is a kind of structural representation for drying plant including dehumidifier that the utility model one embodiment provides；
Fig. 6 is a kind of structural representation for drying plant including explosion-proof valve that the utility model one embodiment provides；
Fig. 7 is a kind of structural representation for drying plant including bearing chassis that the utility model one embodiment provides
Figure；
Fig. 8 is a kind of structural representation for drying plant including generator that the utility model one embodiment provides；
Fig. 9 is the structural representation for another drying plant that the utility model one embodiment provides；
Figure 10 is a kind of flow chart for furnace drying method that the utility model one embodiment provides；
Figure 11 is the flow chart for another furnace drying method that the utility model one embodiment provides.
Embodiment
It is new below in conjunction with this practicality to make the purpose, technical scheme and advantage of the utility model embodiment clearer
Accompanying drawing in type embodiment, the technical scheme in the embodiment of the utility model is clearly and completely described, it is clear that is retouched
The embodiment stated is the utility model part of the embodiment, rather than whole embodiments, based on the implementation in the utility model
Example, the every other embodiment that those of ordinary skill in the art are obtained on the premise of creative work is not made, all belongs to
In the scope of the utility model protection.
As shown in figure 1, the utility model embodiment provides a kind of drying plant, the drying plant can include：Hot blast
Stove 101, air-flow pulser 102 and first material separator 103, wherein,
The hot-blast stove 101 is connected with the charging aperture of the air-flow pulser 102, the discharging of the air-flow pulser 102
Mouth is connected with the charging aperture of the first material separator 103；
The hot-blast stove 101, for providing hot air flow, the hot air flow is carried material to be dried and enter the air-flow arteries and veins
Rush device 102；
The air-flow pulser 102, for making the material to be dried suspended motion in the hot air flow, with to described
Material to be dried carries out drying and processing, forms material drying, and by the hot air flow is transferred to the material drying described
First material separator 103；
The first material separator 103, for by the material drying and the hot blast flow separation.
In the above-described embodiments, hot air flow is provided by hot-blast stove, and material to be dried is blown into air-flow pulser,
Material to be dried suspended motion in air-flow pulser, the junction of material and hot-air to be dried is set to accumulate increase, and with heat
Air relative motion, so that material rapid draing to be dried.Dried material drying passes through first material separator by heat
It is distinguished and admirable to be separated with material drying, so as to obtain material drying.Due to not needing prolonged natural drying, will not cause forage grass and
The loss of agricultural crop straw nutritional ingredient, more will not moldy metamorphism.Forage grass and crops straw are dried therefore, it is possible to improve to obtain
The quality of stalk.
Fully dried in order to treat material drying, as shown in Fig. 2 in the utility model one embodiment, the baking
Dry equipment may further include：Pulverizer 201 and second material separator 202, wherein,
The discharging opening of the pulverizer 201 is connected with the charging aperture of the second material separator 202, the second material
The discharging opening of separator 202 is connected between the hot-blast stove 101 and the air-flow pulser 102；
The pulverizer 201, silk is rubbed for carrying out crushing to the material to be dried, and after crushing is rubbed into silk by air-flow
The material transferring to be dried give the second material separator 202；
The second material separator 202, for separating the material to be dried crushed after rubbing silk and the gas
Stream, and by the material transferring to be dried isolated between the hot-blast stove and the air-flow pulser, so that described treat
Material drying enters the air-flow pulser in the presence of the hot-blast stove 101.
In this embodiment, because the volume of material to be dried is excessive, movement in a device, Er Qiehui can not only be influenceed
Influence drying effect.Pulverizer can make the length crushing of material to be dried rub silk and be less than 1cm for length.In order to ensure by powder
The broken material to be dried rubbed after silk can smoothly enter second material separator, can pulverizer and second material separator it
Between connect a blower fan.The material to be dried crushed after rubbing silk is blown into second material separator by blower fan, simultaneously because blower fan
The movement velocity of air-flow is accelerated in effect so that separating effect is more preferably.
In the utility model one embodiment, the drying plant may further include：：At least one desander, its
In,
The desander is connected between the hot-blast stove and the first material separator；
The desander, for the impurity for separating the material to be dried He being entrained in the material to be dried, and increase
Add the contact area of the material to be dried and the hot air flow.
In this embodiment, due to that can have nonessential impurity in material to be dried, it is therefore desirable to remove.Such as：Wait to dry
Dry material is forage grass or agricultural crop straw, and to adulterate soil or stone etc. when harvesting miscellaneous for forage grass or agricultural crop straw
Matter, but these impurity cannot function as feed, so there is necessity of removing.In figure 3, desander 301 can be located at hot-blast stove
Between 101 and air-flow pulser 102,3-1 refer to；Desander 301 can also be located at air-flow pulser 102 and first material point
From between device 103,3-2 refer to；Desander 301 can also simultaneously between hot-blast stove 101 and air-flow pulser 102 and
Between air-flow pulser 102 and first material separator 103,3-3 refer to.
As shown in figure 4, in the utility model one embodiment, the drying plant may further include：Baling press
401, wherein,
The baling press 401 is connected with the first material separator 103；
The baling press 401, the material drying separated for receiving the first material separator 103, and by institute
Packed after stating material drying compacting.
In this embodiment it is possible to the material drying separated by conveyer reception first material separator, and it is defeated
It is sent to baling press.Material drying bundling stores, and is not only convenient for preserving and can reduce nutritive loss, can further prevent from raising
Careless moldy metamorphism.
As shown in figure 5, in the utility model one embodiment, the drying plant may further include：Dehumidifier
501, wherein,
The dehumidifier 501 is connected between the air-flow pulser 102 and the first material separator 103；
The dehumidifier 501, the material drying is transferred to described in the first material separator 103 for reducing
The humidity of hot air flow, and reduce the temperature of the material drying.
In this embodiment, after drying material to be dried due to hot air flow, the moisture in material to be dried inherently distributes
Into thermal current so that the humidity increase of thermal current.And thermal current humidity it is excessive if after material drying is touched so that dry
Dry material absorbs moisture, influences drying effect.
As shown in fig. 6, in the utility model one embodiment, the drying plant may further include：It is at least one
Explosion-proof valve 601, wherein,
The explosion-proof valve 601 is connected between the hot-blast stove 101 and the first material separator 103；
The explosion-proof valve 601, for when dust explosion, blast pressure will be described explosion-proof as caused by the powder explosion
The valve plate of valve 601 is washed open, is made in the hot-blast stove 101, the air-flow pulser 102 and the first material separator 103
Pressure inside one or more leaks.
In this embodiment, using explosion-proof valve, pressure is excessive in hot-blast stove, air-flow pulser and first material separator
When, internal pressure can wash valve plate open, internal pressure is leaked, and can effectively prevent because internal pressure is excessive to hot blast
One or more of stove, air-flow pulser and first material separator cause deformation or even damaged.Because explosion-proof valve is typically pacified
Loaded on cylinder or cylinder top, therefore explosion-proof valve needs to be connected with air-flow pulser.
In order to reduce the pollution to air, in the utility model one embodiment, the drying plant can be wrapped further
Include：Sack cleaner, wherein,
The sack cleaner is connected with the first material separator；
The sack cleaner, the dust in the hot air flow isolated for trapping the first material separator.
In this embodiment, when material to be dried is forage grass or agricultural crop straw, must be wrapped in forage grass or agricultural crop straw
Containing substantial amounts of dust, and these dust can be isolated with first material separator it is distinguished and admirable be drained into air, so as to draw
Play atmosphere pollution.Therefore being used cooperatively sack cleaner and first material separator being capable of effective air conservation.
As shown in fig. 7, in the utility model one embodiment, the drying plant may further include：Bearing chassis
701 and at least two wheels 702；
At least two wheel 702 is connected with the bearing chassis 701；
The bearing chassis 701, for the hot-blast stove 101, the air-flow pulser 102 and the first material point
Carried from device 103, so that the hot-blast stove 101, the air-flow pulser 102 and the first material separator 103 exist
Moved under the drive of at least two wheel 702.
In this embodiment, by bearing chassis and wheel make hot-blast stove, air-flow pulser and first material separator with
Meaning movement, is used under different environment and place, adds flexibility.Such as：By hot-blast stove, air-flow pulser and first
Material separator is positioned in flat car, can be moved whenever and wherever possible, is entered so as to treat material drying whenever and wherever possible
Row drying.
As shown in figure 8, in the utility model one embodiment, the drying plant may further include：Generator
801, wherein,
The generator 801, for being separated for the hot-blast stove 101, the air-flow pulser 102 and the first material
Any one or more in device 103 are powered.
In this embodiment, by setting generator to realize field work of the drying plant in the no peripheral hardware energy
Possibility.Steam turbine and air accumulator can also be configured simultaneously, the energy is used as using natural gas.Not only cost is low for natural gas, and relatively
Less pollution in other energy gas such as gasoline, coal to environment.
As shown in figure 9, the utility model embodiment provides a kind of drying plant, the drying plant includes：Hot-blast stove
101st, air-flow pulser 102, first material separator 103, pulverizer 201, the first blower fan 901, second material separator 202,
First desander 3011, the second desander 3012, the second blower fan 902, dehumidifier 501, transporter 903, baling press 401 and generating
Machine 801.
Material to be dried is positioned over to the charging aperture of pulverizer 201, pulverizer 201, which treats material drying and carries out crushing, to be rubbed
Silk, and it is common in air-flow caused by the cold airflow as caused by the first blower fan 901 and pulverizer 201 caused by push away airflow function under,
The material transferring to be dried after rubbing silk will be crushed to second material separator 202.
Second material separator 202 separates the material to be dried crushed after rubbing silk with pushing away air-flow, and is treated what is isolated
Material drying is transmitted in the Drying being connected to hot-blast stove 101 with the first desander 3011, so that material to be dried is in hot-blast stove
Enter the first desander 3011 in the presence of 101.
Material to be dried is separated with the impurity being entrained in material to be dried in the first desander 3011, and increases and treats
The contact area of material drying and hot air flow, the material to be dried after being separated in the presence of hot air flow enter air-flow pulser
102。
Material to be dried enter air-flow pulser 102 after in hot air flow suspended motion, on the one hand increase material to be dried
With the contact area of hot air flow, on the other hand changing the flowing velocity of thermal current makes speed that lighter material to be dried moves more
It hurry up, at the same time, material to be dried is sent into the second desander 3012 by hot air flow.
Clean impurity is not separated again by material to be dried and in the first desander 3011 in the second desander 3012
It is secondary to be separated, while increase the contact area of material and hot air flow to be dried again, then it will wait to dry using the second blower fan 902
Dry material pumps to dehumidifier 501, and one side dehumidifier 501 takes the moisture in thermal current away, on the other hand reduces to be dried
The temperature of material, then material to be dried be finally fed to first material separator 103, by hot air flow and the second blower fan 902
Caused cold wind stream and feed separation to be dried, so as to obtain material drying.
Material drying enters conveyer 903 after being isolated from first material separator 103, transmits to baling press 401, bundling
Dress bag, whole process are completed.
Because temperature and pressure is of a relatively high in the first desander 3011 and air-flow pulser 102, in order to prevent due to
Internal pressure is excessive to be caused deformation to the drying plant or even damages, and is set on the first desander 3011 and air-flow pulser 102
Put explosion-proof valve 601.In order to ensure in the environment of no external power supply the drying plant can normal use, in the drying plant
Middle configuration generator 801.On the premise of reduce environmental pollution as far as possible, the drying plant can also include steam turbine and air accumulator,
The energy is used as using natural gas.
In this embodiment, the drying plant also includes flat car (not shown), by above-mentioned hot-blast stove 101, air-flow
Pulser 102, first material separator 103, pulverizer 201, the first blower fan 901, second material separator 202, the first desanding
Device 3011, the second desander 3012, the second blower fan 902, dehumidifier 501, transporter 903, baling press 401 are fixed on the flat car
On, material drying can be treated whenever and wherever possible dried.
What deserves to be explained is the first separator and the second separator can configure sack cleaner, to prevent dust from entering
Air.Fig. 1 to Fig. 9 is only the structural representation of drying plant, only for showing the annexation of each several part, is not represented real
Thing.
As shown in Figure 10, the utility model embodiment is provided one kind and dried using any of the above-described drying plant
The furnace drying method of material to be dried, the furnace drying method may comprise steps of：
Step 1001：Hot air flow is provided by hot-blast stove, the hot air flow is carried material to be dried and enters air-flow pulse
Device.
Step 1002：The material to be dried suspended motion in the hot air flow is made by the air-flow pulser, with
Drying and processing is carried out to the material to be dried, forms material drying, and transmit the material drying by the hot air flow
Give first material separator.
Step 1003：By first material separator by the material drying and the hot blast flow separation.
In the utility model one embodiment, when the drying plant includes pulverizer and second material separator,
Before the placement preliminary drying dry using Drying, further comprise：
Crushing is carried out to the material to be dried by the pulverizer and rubs silk, and the institute after rubbing silk will be crushed by air-flow
Material transferring to be dried is stated to the second material separator；
The material to be dried crushed after rubbing silk and the air-flow are separated by the second material separator, and
By the material transferring to be dried isolated between the hot-blast stove and the air-flow pulser, so that the thing to be dried
Material enters the air-flow pulser in the presence of the hot-blast stove.
In the utility model one embodiment, when the drying plant includes baling press,
It is described by first material separator by the material drying and the hot blast flow separation after, further bag
Include：
The material drying that the first material separator separates is received by the baling press, and by the drying object
Packed after material compacting.
In order to better illustrate the furnace drying method of drying plant, the utility model embodiment is set to the drying shown in Figure 10
Example, expansion explanation furnace drying method, as shown in figure 11, the furnace drying method may comprise steps of：
Step 1101：Material drying is treated by pulverizer carry out crushing and rub silk.
In this step, material to be dried is crushed and rubs silk, obtain a certain size material to be dried of user,
And the more uniform of drying materials to be dried can be made by smashing material to be dried.
Step 1102：Airflow function is pushed away by what air-flow caused by the cold airflow as caused by the first blower fan and pulverizer merged
Under, give the material transferring to be dried crushed after rubbing silk to second material separator.
In this step, although pulverizer can produce it is distinguished and admirable, it is distinguished and admirable caused by pulverizer to have pushed away smaller, waiting to dry
When dry material water content is of a relatively high, caused by pulverizer it is distinguished and admirable can not by material transferring to be dried to second material separator,
So the first blower fan is set herein, so that air-flow common transport caused by cold airflow caused by the first blower fan and pulverizer is waited to dry
Dry material.
Step 1103：Material to be dried after rubbing silk is crushed by the separation of second material separator and pushes away air-flow, and will be divided
In the Drying that the material transferring to be dried separated out is connected to hot-blast stove with the first desander.
In this step, second material separator can be equipped with sack cleaner, prevent dust from entering external air.
Step 1104：By hot air flow caused by hot-blast stove by material transferring to be dried to the first desander.
In this step, hot air flow caused by hot-blast stove can not only promote material transferring to be dried to the first desander,
And in transmitting procedure, material drying can be treated and heated, make the water content of material to be dried reduce.
Step 1105：Material to be dried is separated with the impurity being entrained in material to be dried by the first desander, and
Air-flow pulser is streamed to by hot blast.
In this step, forage grass or agricultural crop straw can adulterate the impurity such as soil or stone when harvesting, but this
A little impurity cannot function as feed, so there is necessity of removing.And material to be dried and heat can be increased in the first desander
Distinguished and admirable contact area, advantageously in the drying for treating material drying.
Step 1106：Material to be dried suspended motion in hot air flow is made by air-flow pulser, and spread by hot blast
Transport to the second desander.
In this step, on the one hand increase the contact area of material and hot air flow to be dried, on the other hand change thermal current
The flowing velocity speed that moves lighter material to be dried it is faster, that is, make the of a relatively high material to be dried of water content
Drying time is grown relative to the water content relatively low dry materials time to be dried.
Step 1107：Increase the contact area of material and hot air flow to be dried by the second desander.
In this step, the second desander main purpose is that the contact area for increasing material and hot air flow to be dried makes to wait to dry
Dry materials more fully, secondly can not also separate clean impurity again by material to be dried and in the first desander
Separated.
Step 1108：Material to be dried is pumped to by dehumidifier by the second blower fan.
In this step, because hot air flow have passed through longer distance, the motive force of hot air flow may be not enough to promotion and treat
Material drying continues to transmit, therefore the second blower fan can be set to treat material drying and pumped.
Step 1109：The moisture in thermal current is taken away by dehumidifier, and by material transferring to be dried to first material
Separator.
In this step, because thermal current treats the drying of material drying so that the moisture of material to be dried enters hot gas
Stream, if the moisture in thermal current not taken away, will treat material drying and has an impact.Material to be dried can be reduced simultaneously
Temperature.
Step 1110：Material to be dried is separated with distinguished and admirable by first material separator, material drying is obtained and will divide
The material drying separated out is transmitted to conveyer.
In this step, the air-flow of the second blower fan and the distinguished and admirable of thermal current are separated with material to be dried.
Step 1111：Material drying is transmitted to baling press by conveyer.
Step 1112：Material drying bundling is filled by baling press and wrapped.
What deserves to be explained is flat car is to realize that treating material drying whenever and wherever possible is dried, generator be for
Ensure that the drying of material to be dried can be normally carried out in the environment of no external power supply.
To sum up, each embodiment of the present utility model, at least has the advantages that：
1st, in embodiment of the present utility model, hot air flow is provided by hot-blast stove, and material to be dried is blown into gas
Flow in pulser, material to be dried suspended motion in air-flow pulser, the junction of material and hot-air to be dried is accumulated increase,
And with hot-air relative motion, so that material rapid draing to be dried.Dried material drying passes through first material
Separator separates hot air flow and material drying, so as to obtain material drying., will not due to not needing prolonged natural drying
The loss of forage grass and agricultural crop straw nutritional ingredient is caused, more will not moldy metamorphism.Forage grass is dried therefore, it is possible to improve to obtain
With the quality of agricultural crop straw.
2nd, in embodiment of the present utility model, by setting pulverizer and second material separator, one side pulverizer
Crushing material to be dried is rubbed into silk, material to be dried can be made fully to dry；Another aspect second material separator will be to be dried
Material and cold air flow separation, avoid influenceing the work of hot-blast stove.
3rd,, on the one hand can be by material to be dried and doping by setting desander in embodiment of the present utility model
Impurity separation in material to be dried, the material drying quality having increased access to；On the other hand can increase material to be dried with
The contact area of hot air flow, increase rate of drying and drying effect.
4th, in embodiment of the present utility model, by setting baling press, material drying bundling is stored, is on the one hand easy to
Preserve material drying and the nutritive loss of material drying can be reduced；On the other hand the mouldy change of material drying can be prevented
Matter.
5th, in embodiment of the present utility model, by setting explosion-proof valve, can effectively prevent due to internal pressure mistake
Deformation is caused to one or more of hot-blast stove, air-flow pulser, first material separator and desander greatly or even is damaged
6th, can be that drying is set by setting bearing chassis and at least two wheels in embodiment of the present utility model
It is standby to be used under different environment and place, flexibility is added, is realized and is treated material drying whenever and wherever possible and done
It is dry.
7th, in embodiment of the present utility model, by setting generator, drying plant can be realized in no peripheral hardware energy
The possibility of the field work in source.
8th, in embodiment of the present utility model, the feeding cost of fodder grass is reduced, improves existing fodder grass and farmland
The forage grassization utilization rate of stalk resource, the culture benefit of Herbivore is improved, promote building Socialist New, be structure
Build the rational industrial structure, there is provided new opportunity to develop.
9th, in embodiment of the present utility model, on the one hand, the utilization of Feeds of vegetarian resource is greatly improved
And transformation efficiency, be on the other hand advantageous to develop potential feed resource, increase the supply source of fodder grass, alleviate grain
Supply pressure.
It should be noted that herein, such as first and second etc relational terms are used merely to an entity
Or operation makes a distinction with another entity or operation, and not necessarily require or imply and exist between these entities or operation
Any this actual relation or order.Moreover, term " comprising ", "comprising" or its any other variant be intended to it is non-
It is exclusive to include, so that process, method, article or equipment including a series of elements not only include those key elements,
But also the other element including being not expressly set out, or also include solid by this process, method, article or equipment
Some key elements.In the absence of more restrictions, the key element limited by sentence " including one ", is not arranged
Except other identical factor in the process including the key element, method, article or equipment being also present.
One of ordinary skill in the art will appreciate that：Realizing all or part of step of above method embodiment can pass through
Programmed instruction related hardware is completed, and foregoing program can be stored in computer-readable storage medium, the program
Upon execution, the step of execution includes above method embodiment；And foregoing storage medium includes：ROM, RAM, magnetic disc or light
Disk etc. is various can be with the medium of store program codes.
It is last it should be noted that：Preferred embodiment of the present utility model is the foregoing is only, is merely to illustrate this practicality
New technical scheme, is not intended to limit the scope of protection of the utility model.It is all the spirit and principles of the utility model it
Interior done any modification, equivalent substitution and improvements etc., are all contained in the scope of protection of the utility model.
Claims (10)
- A kind of 1. drying plant, it is characterised in that including：Hot-blast stove, air-flow pulser and first material separator, wherein,The hot-blast stove is connected with the charging aperture of the air-flow pulser, the discharging opening of the air-flow pulser and first thing The charging aperture of material separator is connected；The hot-blast stove, for providing hot air flow, the hot air flow is carried material to be dried and enter the air-flow pulser；The air-flow pulser, for making the material to be dried suspended motion in the hot air flow, with to described to be dried Material carries out drying and processing, forms material drying, and the material drying is transferred into first thing by the hot air flow Expect separator；The first material separator, for by the material drying and the hot blast flow separation.
- 2. drying plant according to claim 1, it is characterised in that further comprise：Pulverizer and second material separation Device, wherein,The discharging opening of the pulverizer is connected with the charging aperture of the second material separator, and the second material separator goes out Material mouth is connected between the hot-blast stove and the air-flow pulser；The pulverizer, silk is rubbed for carrying out crushing to the material to be dried, and will be crushed and rubbed described in after silk by air-flow Material transferring to be dried gives the second material separator；The second material separator, for separating the material to be dried crushed after rubbing silk and the air-flow, and will The material transferring to be dried isolated is between the hot-blast stove and the air-flow pulser, so that the material to be dried Enter the air-flow pulser in the presence of the hot-blast stove.
- 3. drying plant according to claim 1, it is characterised in that further comprise：At least one desander, wherein,The desander is connected between the hot-blast stove and the first material separator；The desander, for the impurity for separating the material to be dried He being entrained in the material to be dried, and increase institute State the contact area of material to be dried and the hot air flow.
- 4. drying plant according to claim 1, it is characterised in that further comprise：Baling press, wherein,The baling press is connected with the first material separator；The baling press, for receiving the material drying of first material separator separation, and by the material drying Packed after compacting.
- 5. drying plant according to claim 1, it is characterised in that further comprise：Dehumidifier, wherein,The dehumidifier is connected between the air-flow pulser and the first material separator；The dehumidifier, for reduce by the material drying be transferred to the first material separator the hot air flow it is wet Degree, and reduce the temperature of the material drying.
- 6. drying plant according to claim 1, it is characterised in that further comprise：At least one explosion-proof valve, wherein,The explosion-proof valve is connected between the hot-blast stove and the first material separator；The explosion-proof valve, for when dust explosion, blast pressure is by the valve of the explosion-proof valve as caused by the powder explosion Plate is washed open, makes the internal pressure of one or more of the hot-blast stove, the air-flow pulser and described first material separator Power leaks.
- 7. drying plant according to claim 1, it is characterised in that further comprise：Sack cleaner, wherein,The sack cleaner is connected with the first material separator；The sack cleaner, the dust in the hot air flow isolated for trapping the first material separator.
- 8. drying plant according to any one of claims 1 to 7, it is characterised in that further comprise：Bearing chassis and at least Two wheels；At least two wheel is connected with the bearing chassis；The bearing chassis, for being carried to the hot-blast stove, the air-flow pulser and the first material separator, So that the hot-blast stove, the air-flow pulser and the first material separator move down in the drive of at least two wheel It is dynamic.
- 9. drying plant according to claim 8, it is characterised in that further comprise：Generator, wherein,The generator, for be any one in the hot-blast stove, the air-flow pulser and the first material separator It is individual or multiple be powered.
- 10. drying plant according to claim 9, it is characterised in that further comprise：Gas bomb and steam turbine, wherein,The gas bomb is connected with the steam turbine；The gas bomb, for natural gas-storing；The steam turbine, for providing the energy using the natural gas in the gas bomb for the generator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720301419.XU CN206656545U (en) | 2017-03-27 | 2017-03-27 | A kind of drying plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720301419.XU CN206656545U (en) | 2017-03-27 | 2017-03-27 | A kind of drying plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206656545U true CN206656545U (en) | 2017-11-21 |
Family
ID=60316215
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720301419.XU Expired - Fee Related CN206656545U (en) | 2017-03-27 | 2017-03-27 | A kind of drying plant |
Country Status (1)
| Country | Link |
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| CN (1) | CN206656545U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106885461A (en) * | 2017-03-27 | 2017-06-23 | 内蒙古凯程农牧业科技有限公司 | A kind of drying plant and furnace drying method |
-
2017
- 2017-03-27 CN CN201720301419.XU patent/CN206656545U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106885461A (en) * | 2017-03-27 | 2017-06-23 | 内蒙古凯程农牧业科技有限公司 | A kind of drying plant and furnace drying method |
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Granted publication date: 20171121 |