CN108662876A - Sea-buckthorn pomace stirring and drying tank device and its stirring and drying method - Google Patents
Sea-buckthorn pomace stirring and drying tank device and its stirring and drying method Download PDFInfo
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- CN108662876A CN108662876A CN201810706641.7A CN201810706641A CN108662876A CN 108662876 A CN108662876 A CN 108662876A CN 201810706641 A CN201810706641 A CN 201810706641A CN 108662876 A CN108662876 A CN 108662876A
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- drying
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- sea
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- 238000001035 drying Methods 0.000 title claims abstract description 69
- 235000003145 Hippophae rhamnoides Nutrition 0.000 title claims abstract description 38
- 238000003756 stirring Methods 0.000 title claims abstract description 37
- 240000000950 Hippophae rhamnoides Species 0.000 title abstract 2
- 239000000463 material Substances 0.000 claims abstract description 83
- 241000229143 Hippophae Species 0.000 claims description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 36
- 239000002002 slurry Substances 0.000 claims description 21
- 238000007599 discharging Methods 0.000 claims description 20
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 230000036760 body temperature Effects 0.000 claims description 6
- 230000005540 biological transmission Effects 0.000 claims description 2
- 239000002245 particle Substances 0.000 abstract description 3
- 238000007602 hot air drying Methods 0.000 abstract description 2
- 238000012544 monitoring process Methods 0.000 abstract description 2
- 238000004321 preservation Methods 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 4
- 229940088594 vitamin Drugs 0.000 description 3
- 229930003231 vitamin Natural products 0.000 description 3
- 235000013343 vitamin Nutrition 0.000 description 3
- 239000011782 vitamin Substances 0.000 description 3
- 150000003722 vitamin derivatives Chemical class 0.000 description 3
- 235000003935 Hippophae Nutrition 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 2
- 206010009866 Cold sweat Diseases 0.000 description 1
- 206010013786 Dry skin Diseases 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B11/00—Machines or apparatus for drying solid materials or objects with movement which is non-progressive
- F26B11/12—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices
- F26B11/16—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices the stirring device moving in a vertical or steeply-inclined plane
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N12/00—Machines for cleaning, blanching, drying or roasting fruits or vegetables, e.g. coffee, cocoa, nuts
- A23N12/08—Machines for cleaning, blanching, drying or roasting fruits or vegetables, e.g. coffee, cocoa, nuts for drying or roasting
- A23N12/083—Machines for cleaning, blanching, drying or roasting fruits or vegetables, e.g. coffee, cocoa, nuts for drying or roasting with stirring, vibrating or grinding devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/10—Heating arrangements using tubes or passages containing heated fluids, e.g. acting as radiative elements; Closed-loop systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/04—Agitating, stirring, or scraping devices
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Combustion & Propulsion (AREA)
- Sustainable Development (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a kind of sea-buckthorn pomace stirring and drying tank device and its stirring and drying method, solve the problems, such as that existing equipment existing drying efficiency in the higher small particles material of baking density is low and exhaust structure is not scientific and reasonable.The present invention can be divided mainly into stirring and shed system, send hot air drying system, take out humid air system, temperature humidity monitoring system in discharge system and tank body Heat preservation system and tank；These systems can realize control by an industrial personal computer, temperature sensor and humidity sensor are installed in tank body, industrial personal computer is by acquiring the signals of these sensors, and pass through automatic control program, realization controls temperature in tank, and the signal transmitted by humidity sensor, carries out material and sheds and take out the job rotating between humid air, the high efficiency and low cost for improving drying, substantially increase the dries quantity of material.
Description
Technical field
The present invention relates to a kind of stirring and drying tank device, more particularly to a kind of sea-buckthorn pomace to after squeezing the juice is dried
When a kind of used drying tank arrangement and stirring and drying method.
Background technology
Fructus hippophae is a kind of higher fruit of vitamin content, and remaining sea-buckthorn pomace also contains after squeezing the juice to it
Abundant vitamin, in order not to destroy its vitamin composition, dries to its deep processing, generally carry out drying and processing to it
Dry temperature cannot be too high, to control environment temperature at 70 degree Celsius or so, if temperature is too low to extend drying time, influences
, can be burned by sea-buckthorn pomace if temperature is too high to drying efficiency, influence subsequent deep processing；Existing drying equipment is general
Using drum-type rotary furnace drying tank, but that there are equipment volumes is big for drum-type rotary furnace drying tank, and power configuration demand is high, cost of investment
The high sea-buckthorn pomace of big defect, especially density is easy caking in roller, and the object of diverging will not be formed with the rotation of roller
Stream influences the efficiency of its drying；In the transmission process of material drying, the prior art is generally discharged using spiral conveying
Mode, it is this to send discharge method, for the higher sea-buckthorn pomace material of density, there is the uneven and material of stirring and conveying
The problem of being not easy to dry in the process；In addition, the humid air discharge structure in the drying tank of existing drying unit designs not science
Rationally, when humid air is discharged, it be easy to cause the loss for being oven-dried material being entrained in discharge gas.
Invention content
The present invention provides a kind of sea-buckthorn pomace stirring and drying tank device and its stirring and drying methods, solve existing set
The standby existing drying efficiency in the higher small particles material of baking density is low and the not scientific and reasonable technical problem of discharging structure.
The present invention is to solve the above technical problem by the following technical programs：
The present general inventive concept is：Three groups of stirring slurries are set on the central shaft of closed tank body, and every group of stirring slurry is by three pieces
Paddle forms, and every paddle is in ∏ shapes, and the shovel material that beanstalk shape of winnowing with a dustpan is arranged on the outer end floor beam of ∏ shape paddles sheds slot, centre axis
It moves three groups of stirring slurries to rotate in tank, the shovel material of the beanstalk shape of winnowing with a dustpan in every paddle sheds slot, and sea-buckthorn pomace material is scooped up, and throws
It is spread to tank middle and upper part, material is in suspended state, makes it that drying, the shovel material of the beanstalk shape of winnowing with a dustpan in each every paddle be accelerated to shed slot
It is to scoop up the material of material heap bottom, realizes the conversion in turn of the levels material of material heap, in tank middle and upper part material
It is moved to lower layer from the upper layer of material heap successively again after suspended state, landing, is scooped up and is shed again by lower layer, whole materials
The conversion for realizing dynamic spatial location accelerates dry materials speed.
A kind of sea-buckthorn pomace stirring and drying tank device, including cylindrical dry tank body, on a left side for cylindrical dry tank body
It is provided with tank body left end cap on port, tank body right end cap is provided in the right output port of cylindrical dry tank body, in tank body left end
The upper end of lid is provided with feed inlet, and the lower end of tank body left end cap is provided with hot air inlet, is arranged in the upper end of tank body right end cap
There is suction opening, whirlwind discharger is connected on suction opening, exhaust fan is connected in the upper port of whirlwind discharger, is unloaded in whirlwind
It is provided with material belt conveyor immediately below the whirlwind discharger discharge port of glassware, hot wind air inlet is connected on hot air inlet
Pipe, the other end and the Hot-blast Heating case of hot-air inlet pipe are connected together；It is provided in the left port of cylindrical dry tank body
Tank body left end horizontal girder is provided with tank body right end horizontal girder, in tank body left end in the right output port of cylindrical dry tank body
It is provided with left end bearing on horizontal girder, right end bearing is provided on tank body right end horizontal girder, in left end bearing and right end
It is provided with central shaft between bearing, left end cap bearing is provided at the center of tank body left end cap, the left end of central shaft passes through a left side
It links together with driving gear after bearing with end cover, driving gear is linked together by driving belt and stirring driving motor；
It is respectively arranged with left part square frame-shaped paddle group, middle part square frame-shaped paddle group and right part square frame-shaped paddle group on center shaft.
The structure of the structure of left part square frame-shaped paddle group, the structure and right part square frame-shaped paddle group of middle part square frame-shaped paddle group
It is identical, square frame-shaped paddle group is made of three square frame-shaped paddles, and every group of three square frame-shaped paddles are in
Radial arrangement centered on mandrel, the angle between two adjacent square frame-shaped paddles is 120 degree, and each square frame-shaped paddle is in
∏ shapes, each square frame-shaped paddle are by the company from central shaft outwardly directed two cantilever beams parallel to each other and two cantilever beam outer ends
Crossbeam composition is connect, being provided with shovel material on the connecting cross beam of the outer end of the square frame-shaped slurry of ∏ shapes sheds dovetail groove.
Square frame-shaped slurry and the corresponding ∏ shapes in the square frame-shaped paddle group of middle part of ∏ shapes in left part square frame-shaped paddle group
Angle between square frame-shaped slurry is 60 degree, square frame-shaped slurry and the right part square frame-shaped paddle group of the ∏ shapes in the square frame-shaped paddle group of middle part
In corresponding ∏ shapes square frame-shaped slurry between angle be 60 degree；The inside base angle that shovel material sheds dovetail groove is 120 degree；Tank is built-in
The ratio of the sea-buckthorn pomace volume of material and cylindrical dry tank volume that enter is 1：10.
Heat cycles water jacket is provided on the lateral wall of cylindrical dry tank body, heat cycles water jacket is followed with hot water heating
Ring case is connected together, and hot water circulating pump is connected on hot water heat cycles case；In the bottom of cylindrical dry tank body from a left side
It is disposed with left discharge port, middle discharge port and right discharge port to the right side, on left discharge port, on middle discharge port and on right discharge port
It is provided with completely identical in structure discharging returning face plate, air cylinder support is provided on the lateral wall of cylindrical dry tank body, in gas
Be provided with electronic control cylinder on jar support, the piston output shaft and discharging returning face plate of electronic control cylinder link together, left discharge port,
It is provided with material belt conveyor immediately below middle discharge port and right discharge port.
A kind of sea-buckthorn pomace stirring and drying method, includes the following steps：
The hot air inlet being arranged in the lower end of tank body left end cap is connected to by hot-air inlet pipe with Hot-blast Heating case by the first step
Together；The suction opening being arranged in the upper end of tank body right end cap is linked together with whirlwind discharger, in whirlwind discharger
Exhaust fan is connected in upper port, the whirlwind discharger discharge port of whirlwind discharger is arranged in the surface of material belt conveyor；It will
The driving gear of central shaft is linked together by driving belt and stirring driving motor；
Second step, by hot water heat cycles case water heat, start hot water circulating pump, make hot water in heat cycles water jacket into
Row cycle；Meanwhile starting Hot-blast Heating case, and exhaust fan is opened, the clammy air in cylindrical dry tank body is discharged, is supplemented in
Hot-air；
Third step, the feed inlet for opening top of the tank, bucket elevator work, will be added to tank body after sea-buckthorn pomace material lifting
In, at the same time, stirring driving motor starts, and three groups of square frame-shaped paddle groups in tank body start to rotate, by the fructus hippophae of addition
The feed inlet one end of slag material out of tank is pushed into the other end of tank body, and the substantially uniform beach of material in tank is made to open；After the completion of charging,
Charge door is automatically closed；The ratio of the sea-buckthorn pomace volume of material of addition and cylindrical dry tank volume is 1：10；
4th step carries out first stage drying：Tank body temperature is controlled, 65-75 degree Celsius is kept it in；Control heat cycles
The temperature of recirculated water in water jacket keeps it in 60 degree Celsius, and the speed of agitator of three groups of square frame-shaped paddle groups in tank body is
40-50 revs/min；High temperature drying phase duration is 1-2 hours；
5th step carries out second stage drying：Tank body temperature is controlled, 50-60 degree Celsius is kept it in；Control heat cycles
The temperature of recirculated water in water jacket keeps it in 50 degree Celsius；The speed of agitator of three groups of square frame-shaped paddle groups in tank body is
25-35 revs/min；The low temperature drying duration is 5-6 hours；
6th step closes exhaust fan, closes hot water circulating pump, starts electronic control cylinder, is beaten discharging returning face plate by electronic control cylinder
It opens, makes the sea-buckthorn pomace material after drying, pass through left discharge port, middle discharge port and right discharge port respectively, discharging to material conveys
On belt, during discharging, the speed of agitator of three groups of square frame-shaped paddle groups is 10-15 revs/min in tank body, plays auxiliary discharging
Effect.
Present invention accomplishes the drying requirements that drying temperature requires harsher big density small particles material, closed
The dynamic environment for recycling and shedding material in tank has been built in drying tank body, is kept drying more full and uniform, is improved drying
Quality and speed；Periodically humid air is extracted out, and in pumping process, by the material of entrainment by eddy flow discharger into
Row is collected, and the loss of material is avoided.
Description of the drawings
Fig. 1 is the structural schematic diagram of the present invention；
Fig. 2 is the structural schematic diagram of the rabbling mechanism of the present invention；
Fig. 3 is the sectional view along A-A in Fig. 2；
Fig. 4 is the schematic diagram when material of the present invention is shed；
Fig. 5 is the structural schematic diagram of the discharge port of the present invention.
Specific implementation mode
The present invention is described in detail below in conjunction with the accompanying drawings：
A kind of sea-buckthorn pomace stirring and drying tank device, including cylindrical dry tank body 1, in the left end of cylindrical dry tank body 1
It is provided with tank body left end cap 2 on mouthful, tank body right end cap 3 is provided in the right output port of cylindrical dry tank body 1, in tank body left end
The upper end of lid 2 is provided with feed inlet 16, and the lower end of tank body left end cap 2 is provided with hot air inlet 17, in the upper of tank body right end cap 3
End is provided with suction opening 25, and whirlwind discharger 26 is connected on suction opening 25, is connected in the upper port of whirlwind discharger 26
Exhaust fan 28 is provided with material belt conveyor, in hot wind in the underface of the whirlwind discharger discharge port 27 of whirlwind discharger 26
Hot-air inlet pipe 18 is connected on air inlet 17, the other end and the Hot-blast Heating case 21 of hot-air inlet pipe 18 are connected together；
It is provided with tank body left end horizontal girder 4 in the left port of cylinder drying tank body 1, in the right output port of cylindrical dry tank body 1
It is provided with tank body right end horizontal girder 5, left end bearing 6 is provided on tank body left end horizontal girder 4, it is vertical in tank body right end level
It is provided with right end bearing 7 on beam 5, central shaft 8 is provided between left end bearing 6 and right end bearing 7, in tank body left end cap 2
Left end cap bearing 9 is provided at center, the left end of central shaft 8 links together after left end cap bearing 9 with driving gear 10,
Driving gear 10 is linked together by driving belt 19 and stirring driving motor 20；It is respectively arranged with left part on central shaft 8
Square frame-shaped paddle group 11, middle part square frame-shaped paddle group 12 and right part square frame-shaped paddle group 13；The present invention can be divided mainly into stirring and throw
System is spread, hot air drying system is sent, takes out humid air system, temperature humidity in discharge system and tank body Heat preservation system and tank
Monitoring system；These systems can realize control by an industrial personal computer, and temperature sensor is equipped in tank body and humidity passes
Sensor, for industrial personal computer by acquiring the signals of these sensors, and by automatic control program, realization controls temperature in tank, and
The signal transmitted by humidity sensor carries out material and sheds and take out the job rotating between humid air, improves drying
High efficiency and low cost substantially increase the dries quantity of material.
The structure of left part square frame-shaped paddle group 11, the structure of middle part square frame-shaped paddle group 12 and right part square frame-shaped paddle group 13
Structure be identical, square frame-shaped paddle group is made of three square frame-shaped paddles, every group of three square frame-shaped paddles
It is the radial arrangement centered on central shaft 8, the angle between two adjacent square frame-shaped paddles is 120 degree, each box
Shape paddle is in ∏ shapes, and each square frame-shaped paddle is by being hanged from outwardly directed two cantilever beams 14 parallel to each other of central shaft 8 with two
The connecting cross beam composition of 14 outer end of arm beam, it is provided with to shovel on the connecting cross beam of the outer end of the square frame-shaped slurry of ∏ shapes and expects to shed ladder
Shape slot 15；The problem of being arranged so, overcoming material windrow in tank makes material in tank farthest be in suspended state, makes
The heating surface area of material is maximum.
Square frame-shaped slurry and the corresponding ∏ in middle part square frame-shaped paddle group 12 of ∏ shapes in left part square frame-shaped paddle group 11
Angle between the square frame-shaped slurry of shape is 60 degree, square frame-shaped slurry and the right part square frame-shaped of the ∏ shapes in middle part square frame-shaped paddle group 12
Angle in paddle group 13 between the square frame-shaped slurry of corresponding ∏ shapes is 60 degree；The inside base angle that shovel material sheds dovetail groove 15 is
120 degree；The ratio for 1 volume of 32 volume of sea-buckthorn pomace material and cylindrical dry tank body being packed into tank is 1：10；In half square shape
Shovel material can be set on the upper and lower two sides of the outer end floor beam of stirring slurry 14 and shed dovetail groove 15, it can be achieved that 8 positive and negative rotation of central shaft
When, material is shed with capable of realizing maximum area, since tank body is closed tank body, and when shedding, compartment of terrain carries out just
Shedding on anti-two direction is more advantageous to adequately being stirred for material.
It is provided with heat cycles water jacket 24, heat cycles water jacket 24 and hot water on the lateral wall of cylindrical dry tank body 1
Heat cycles case 22 is connected together, and hot water circulating pump 23 is connected on hot water heat cycles case 22；In cylindrical drying chamber
The bottom of body 1 has been set gradually from left to right left discharge port 29, middle discharge port 30 and right discharge port 31, on left discharge port 29,
On middle discharge port 30 and it is provided with completely identical in structure discharging returning face plate 36 on right discharge port 31, in cylinder drying tank body 1
Lateral wall on be provided with air cylinder support 34, electronic control cylinder 35 is provided on air cylinder support 34, the piston of electronic control cylinder 35 is defeated
Shaft links together with discharging returning face plate 36, is arranged in the underface of left discharge port 29, middle discharge port 30 and right discharge port 31
There is material belt conveyor.
A kind of sea-buckthorn pomace stirring and drying method, includes the following steps：
The hot air inlet 17 being arranged in the lower end of tank body left end cap 2 is passed through hot-air inlet pipe 18 and Hot-blast Heating by the first step
Case 21 is connected together；The suction opening 25 being arranged in the upper end of tank body right end cap 3 is linked together with whirlwind discharger 26,
Exhaust fan 28 is connected in the upper port of whirlwind discharger 26, the whirlwind discharger discharge port 27 of whirlwind discharger 26 is arranged in material
The surface of belt conveyor；The driving gear 10 of central shaft 8 is connected to one by driving belt 19 and stirring driving motor 20
It rises；
Sea-buckthorn pomace material 32 is placed into cylindrical drying by second step, the feed inlet 16 being arranged by 2 upper end of tank body left end cap
In tank body 1, in placement process, driving motor 20 is stirred by control, makes left part square frame-shaped paddle group 11, middle part square frame-shaped slurry
Leaf group 12 and right part square frame-shaped paddle group 13 are in rotary work state, and the volume for the sea-buckthorn pomace material 32 being put into is cylinder
/ 10th of 1 volume of dry tank body；
Third step, the feed inlet 16 for opening top of the tank, bucket elevator work, are added to after sea-buckthorn pomace material 32 is promoted
In tank body, at the same time, stirring driving motor 20 starts, and three groups of square frame-shaped paddle groups in tank body start to rotate, by addition
The feed inlet one end of sea-buckthorn pomace material 32 out of tank is pushed into the other end of tank body, and the substantially uniform beach of material in tank is made to open；Add
After the completion of material, charge door 16 is automatically closed；32 volume of sea-buckthorn pomace material of addition and the ratio of cylinder 1 volume of dry tank body are
1：10；
4th step carries out first stage drying：Tank body temperature is controlled, 65-75 degree Celsius is kept it in；Control heat cycles
The temperature of recirculated water in water jacket 24 keeps it in 60 degree Celsius, the speed of agitator of three groups of square frame-shaped paddle groups in tank body
It is 40-50 revs/min；High temperature drying phase duration is 1-2 hours；
5th step carries out second stage drying：Tank body temperature is controlled, 50-60 degree Celsius is kept it in；Control heat cycles
The temperature of recirculated water in water jacket 24 keeps it in 50 degree Celsius；The speed of agitator of three groups of square frame-shaped paddle groups in tank body
It is 25-35 revs/min；The low temperature drying duration is 5-6 hours；
6th step repeats the 4th step to the 5th step, until sea-buckthorn pomace material 32 reaches design requirement；Drying stage is divided into two
Section, early period are high temperature dryings, and the low temperature drying in later stage, high temperature drying is mainly comparatively fast to evaporate the moisture of surface of material side by side
Go out, the low temperature drying stage is mainly evaporated and is discharged to the moisture of material internal layer, this drying time in stage is long；It is high
Warm drying stage：Suction opening flow is changed according to the humidity data detected, if humidity is high, can increase exhausting amount, such as
Fruit humidity is low, can reduce exhausting amount.It is by the automatic regulating valve control at tank body suction opening to take out air volume control
's；This high temperature drying time is controlled, prevents temperature is too high from hardening surface of material, influences the row of material internal moisture
Go out；During the low temperature drying stage, a part of lighter in weight, having reached the material of dry standard can be taken out of by air draft pipeline,
Be collected into discharger lower curtate by whirlwind discharger, automatic discharging valve is installed in discharger bottom, can time opening, discharge collection
Material；Discharging belt conveyer is opened simultaneously when unlatching, and material is sent to storage container；
7th step closes exhaust fan 28, closes hot water circulating pump 23, starts electronic control cylinder 35, will be discharged by electronic control cylinder 35
Returning face plate 36 is opened, and is made the sea-buckthorn pomace material 32 after drying, is passed through left discharge port 29, middle discharge port 30 and right discharge port respectively
31, it discharges onto material belt conveyor, during discharging, the speed of agitator of three groups of square frame-shaped paddle groups is 10-15 in tank body
Rev/min, play the role of auxiliary discharging；This discharging method overcomes traditional spiral discharging method, improves discharging efficiency,
Protect the quality of material.
Claims (5)
1. a kind of sea-buckthorn pomace stirring and drying tank device, including cylindrical dry tank body（1）, in the dry tank body of cylinder（1）
Left port on be provided with tank body left end cap（2）, in the dry tank body of cylinder（1）Right output port on be provided with tank body right end cap
（3）, which is characterized in that in tank body left end cap（2）Upper end be provided with feed inlet（16）, tank body left end cap（2）Lower end setting
There is hot air inlet（17）, in tank body right end cap（3）Upper end be provided with suction opening（25）, in suction opening（25）On be connected with rotation
Wind discharger（26）, whirlwind discharger（26）Upper port on be connected with exhaust fan（28）, in whirlwind discharger（26）Whirlwind
Discharger discharge port（27）Underface be provided with material belt conveyor, in hot air inlet（17）On be connected with hot-air inlet pipe
（18）, hot-air inlet pipe（18）The other end and Hot-blast Heating case（21）It is connected together；In the dry tank body of cylinder（1）A left side
Tank body left end horizontal girder is provided in port（4）, in the dry tank body of cylinder（1）Right output port in be provided with tank body right end water
Flat longeron（5）, in tank body left end horizontal girder（4）On be provided with left end bearing（6）, in tank body right end horizontal girder（5）On set
It is equipped with right end bearing（7）, in left end bearing（6）With right end bearing（7）Between be provided with central shaft（8）, in tank body left end cap（2）
Center at be provided with left end cap bearing（9）, central shaft（8）Left end pass through left end cap bearing（9）Afterwards with driving gear（10）
It links together, drives gear（10）Pass through driving belt（19）With stirring driving motor（20）It links together；In central shaft
（8）On be respectively arranged with left part square frame-shaped paddle group（11）, middle part square frame-shaped paddle group（12）With right part square frame-shaped paddle group
（13）.
2. a kind of sea-buckthorn pomace stirring and drying tank device according to claim 1, which is characterized in that left part square frame-shaped is starched
Leaf group（11）Structure, middle part square frame-shaped paddle group（12）Structure and right part square frame-shaped paddle group（13）Structure be complete phase
With, square frame-shaped paddle group is made of three square frame-shaped paddles, and every group of three square frame-shaped paddles are with central shaft（8）For
The radial arrangement in center, the angle between two adjacent square frame-shaped paddles is 120 degree, and each square frame-shaped paddle is in ∏ shapes,
Each square frame-shaped paddle is by from central shaft（8）Outwardly directed two cantilever beams parallel to each other（14）With two cantilever beams（14）Outside
The connecting cross beam composition at end, it is provided with to shovel on the connecting cross beam of the outer end of the square frame-shaped slurry of ∏ shapes and expects to shed dovetail groove
（15）.
3. a kind of sea-buckthorn pomace stirring and drying tank device according to claim 2, which is characterized in that left part square frame-shaped is starched
Leaf group（11）In ∏ shapes square frame-shaped slurry with middle part square frame-shaped paddle group（12）In corresponding ∏ shapes square frame-shaped slurry between
Angle be 60 degree, middle part square frame-shaped paddle group（12）In ∏ shapes square frame-shaped slurry with right part square frame-shaped paddle group（13）In it is right
Angle between the square frame-shaped slurry for the ∏ shapes answered is 60 degree；Shovel material sheds dovetail groove（15）Inside base angle be 120 degree；Tank is built-in
The sea-buckthorn pomace material entered（32）Volume and cylindrical dry tank body（1）The ratio of volume is 1：10.
4. a kind of sea-buckthorn pomace stirring and drying tank device according to claim 3, which is characterized in that dry in cylinder
Tank body（1）Lateral wall on be provided with heat cycles water jacket（24）, heat cycles water jacket（24）With hot water heat cycles case（22）
It is connected together, in hot water heat cycles case（22）On be connected with hot water circulating pump（23）；In the dry tank body of cylinder（1）Bottom
Portion has been set gradually from left to right left discharge port（29）, middle discharge port（30）With right discharge port（31）, in left discharge port（29）Upper,
Middle discharge port（30）Upper and right discharge port（31）On be provided with completely identical in structure discharging returning face plate（36）, dry in cylinder
Tank body（1）Lateral wall on be provided with air cylinder support（34）, in air cylinder support（34）On be provided with electronic control cylinder（35）, automatically controlled gas
Cylinder（35）Piston output shaft with discharging returning face plate（36）It links together, in left discharge port（29）, middle discharge port（30）The right side and
Discharge port（31）Underface be provided with material belt conveyor.
5. a kind of sea-buckthorn pomace stirring and drying method, includes the following steps：
The first step, will be in tank body left end cap（2）Lower end setting hot air inlet（17）Pass through hot-air inlet pipe（18）With heat
Wind heater box（21）It is connected together；It will be in tank body right end cap（3）Upper end setting suction opening（25）With whirlwind discharger
（26）It links together, in whirlwind discharger（26）Upper port on connect exhaust fan（28）, whirlwind discharger（26）Whirlwind
Discharger discharge port（27）It is arranged in the surface of material belt conveyor；By central shaft（8）Driving gear（10）Pass through transmission
Belt（19）With stirring driving motor（20）It links together；
Sea-buckthorn pomace material 32 is placed into cylindrical drying by second step, the feed inlet 16 being arranged by 2 upper end of tank body left end cap
In tank body 1, in placement process, driving motor 20 is stirred by control, makes left part square frame-shaped paddle group 11, middle part square frame-shaped slurry
Leaf group 12 and right part square frame-shaped paddle group 13 are in rotary work state, and the volume for the sea-buckthorn pomace material 32 being put into is cylinder
/ 10th of 1 volume of dry tank body；
Third step, the feed inlet for opening top of the tank（16）, bucket elevator work, by sea-buckthorn pomace material（32）Add after promotion
Enter into tank body, at the same time, stirs driving motor（20）Start, three groups of square frame-shaped paddle groups in tank body start to rotate, will
The sea-buckthorn pomace material of addition（32）Feed inlet one end out of tank is pushed into the other end of tank body, keeps material in tank substantially uniform
It opens on beach；After the completion of charging, charge door（16）It is automatically closed；The sea-buckthorn pomace material of addition（32）Volume and cylindrical dry tank body
（1）The ratio of volume is 1：10；
4th step carries out first stage drying：Tank body temperature is controlled, 65-75 degree Celsius is kept it in；Control heat cycles
Water jacket（24）In recirculated water temperature, keep it in 60 degree Celsius, the stirrings of three groups of square frame-shaped paddle groups in tank body turns
Speed is 40-50 revs/min；High temperature drying phase duration is 1-2 hours；
5th step carries out second stage drying：Tank body temperature is controlled, 50-60 degree Celsius is kept it in；Control heat cycles
Water jacket（24）In recirculated water temperature, keep it in 50 degree Celsius；The stirring of three groups of square frame-shaped paddle groups in tank body turns
Speed is 25-35 revs/min；The low temperature drying duration is 5-6 hours；
6th step closes exhaust fan（28）, close hot water circulating pump（23）, start electronic control cylinder（35）, pass through electronic control cylinder
（35）To discharge returning face plate（36）It opens, makes the sea-buckthorn pomace material after drying（32）, pass through left discharge port respectively（29）, in go out
Material mouth（30）With right discharge port（31）, it discharges onto material belt conveyor, during discharging, three groups of square frame-shaped paddles in tank body
The speed of agitator of group is 10-15 revs/min, plays the role of auxiliary discharging.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810706641.7A CN108662876A (en) | 2018-07-02 | 2018-07-02 | Sea-buckthorn pomace stirring and drying tank device and its stirring and drying method |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810706641.7A CN108662876A (en) | 2018-07-02 | 2018-07-02 | Sea-buckthorn pomace stirring and drying tank device and its stirring and drying method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108662876A true CN108662876A (en) | 2018-10-16 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810706641.7A Pending CN108662876A (en) | 2018-07-02 | 2018-07-02 | Sea-buckthorn pomace stirring and drying tank device and its stirring and drying method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111773752A (en) * | 2020-06-11 | 2020-10-16 | 广东轻工职业技术学院 | Resource utilization device and method for kumquat pulp |
| CN115435569A (en) * | 2022-11-09 | 2022-12-06 | 山东佳士博食品有限公司 | Drying device for food processing |
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Application publication date: 20181016 |