CN209554820U - Dope belt evaporative crystallization drying machine - Google Patents
Dope belt evaporative crystallization drying machine Download PDFInfo
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- CN209554820U CN209554820U CN201820717598.XU CN201820717598U CN209554820U CN 209554820 U CN209554820 U CN 209554820U CN 201820717598 U CN201820717598 U CN 201820717598U CN 209554820 U CN209554820 U CN 209554820U
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- dope
- evaporative crystallization
- belt
- drying machine
- crystallization drying
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Abstract
The utility model discloses a kind of dope belt evaporative crystallization drying machine, including several dope evaporative crystallization drying units and at least one layer of crystalline carrier mesh belt is set in several dope evaporative crystallization drying units, setting carries out crystals dried carrier filler for carrying dope on the crystalline carrier mesh belt, several dope evaporative crystallization drying units include cabinet, configured with dehumidifying heat pump condensing heat-exchange unit in the cabinet.The utility model has the following advantages: sufficiently can be evaporated crystallization to the high-concentration waste liquid of various kinds of equipment discharge, 80% or more decrement can be carried out to dope, not volatile substance removal rate is up to 95% or more in the dope that gives up；The totally-enclosed drying process of low temperature inhibits escaping gas volatilization, can be safely operated；Emission-free discharge is not necessarily to additional stench processing system；Entire drying process can be carried out all under the conditions of closed environment, do not had gas and be discharged in external environment, not will cause secondary environmental pollution.
Description
[technical field]
The utility model relates to drying device field, specially a kind of dope belt evaporative crystallization drying machine.
[background technique]
There is the discharge of a large amount of dopes in industrial production, treatment of urban garbage etc., it is dirty not deal carefully with that there are serious environment
Dye problem.In the prior art, there are a large amount of residual dopes when reverse osmosis using nanofiltration, MVR evaporation technique carries out liquid waste processing
Deficiency.And dope is handled using the technologies such as spray drying (flash distillation) or burning.Because dope is complex in composition, corrosivity is strong
And the characteristics such as water content height, the defects of will lead to treatment facility secondary pollution serious, high failure rate, high operating cost, therefore
Above-mentioned processing technique can not wide popularization and application.
Waste liquid evaporative crystallization can partially overcome drawbacks described above, but because current waste liquid evaporative crystallization technique component of effluent is multiple
Miscellaneous, easy fouling, easy coking and the complex characteristics such as perishable there is also being difficult to crystallization treatment, and exist big in technical process
The deficiency of the dope exhaust emission of amount.
In summary and status in industry is combined, existing dope processing has deficiency to be overcome there are following:
(1) using spray drying or direct-injection incineration technology processing dope, there are energy consumption height, tail gas are difficult, stable
The deficiencies of property is poor, technology is difficult to promote；
(2) using the technical treatments dope such as spray drying or direct-injection burning it is all made of non-renewable energy when and directly burns and add
Heat, energy consumption is high, and every equivalent consumption quantity of steam of one ton of water of evaporation needs 2 tons or more, consumes electricity about 70kw.h；
(3) feature of environmental protection is poor, and can discharge a large amount of foul smell, need to build complicated exhaust treatment system and carry out aid in treatment.
[utility model content]
The purpose of this utility model is that providing a kind of energy saving, processing for deficiency existing for prior art described above
The dope belt evaporative crystallization drying machine that effect is good and operating condition is stable.
To achieve the above purpose, the technical solution of the present invention is: dope belt evaporative crystallization drying machine, dope belt
Evaporative crystallization drying machine, which is characterized in that evaporate and tie in several dopes including several dope evaporative crystallization drying units and setting
At least one layer of crystalline carrier mesh belt in brilliant drying unit is arranged on the crystalline carrier mesh belt and is crystallized for carrying dope
Dry carrier filler, several dope evaporative crystallization drying units include cabinet, configured with dehumidifying heat pump in the cabinet
Condensing heat-exchange unit.
The dope belt evaporative crystallization drying machine further includes having the hydrojet that dope is sprayed onto the crystalline carrier mesh belt
Device, the liquid-jet device are connect with feed liquor system.
The liquid-jet device is arranged between the first layer crystalline carrier mesh belt and second layer crystalline carrier mesh belt.
The carrier filler can be with knit-mesh at cake shape or open circles pieshape, outer diameter 50-
150mm, internal diameter 12-14mm.
Setting feeding crystalline spaces, dry place and heat pump installation space in the cabinet, the feeding crystalline spaces and
Vent passages are set between dry place and heat pump installation space, installation dehumidifying heat pump condensing heat-exchange in the heat pump installation space
Unit；The crystalline carrier net is installed in the upper material space and dry place, the feeding crystalline spaces and dry place
Between water-accepting board is set, for preventing the liquid in feeding crystalline spaces from entering dry place.
The water-accepting board includes several grooves and several tongues, and the two sides of tongue side of dripping is located at adjacent two
The top of a groove is arranged the first slot between the adjacent grooves, is arranged second between the tongue and adjacent grooves
Third slot is arranged between the adjacent tongue for slot.
The side of the groove is that the opposite other side is arranged diagonally downward, and main collecting tank is arranged in the horizontal low level side of groove.
Filter space is set between the drying operation space above and heat pump installation space.
The drying operation space is additionally provided with threshing zone, and the threshing zone is set to crystalline carrier mesh-belt operation direction
One side.
The threshing zone is arranged sheller unit, the sheller unit be mounted on the crystalline carrier mesh belt inner surface and
The lower section of outer surface is patted respectively by inner surface to crystalline carrier mesh belt and outer surface and carries out threshing, Ke Yiyou
The material particles of effect removal crystalline carrier mesh belt.
Two sets of sheller units are that threshing zone is arranged on different height, and the sheller unit that lower part is arranged in is located at mesh belt
Outer side-lower, be arranged in top sheller unit be located at mesh belt inside lower section.
Receiving hopper is set under the sheller unit, for accepting the crystalline solid to fall off.
The sheller unit includes that main shaft, the mounting rack being fixed on main shaft and the activity being mounted on the mounting rack are de-
Grain component, is equipped with bearing block on the mounting rack.
The mounting rack is triangle mounting rack, and threshing unit is movable is mounted on the triangle mounting rack for the activity
In three angles.
The activity threshing unit can be movable hammer, and fulcrum of the activity hammer on mounting rack rotates freely,
In, the activity hammer can be fixed on litter, and the litter is movably arranged on the limit in three angles of the triangle mounting rack
In the pipe of position.
The triangle mounting rack is by the triangle fixed plate that is fixed on the main shaft and is fixed on the triangle fixed plate
On three fulcrums composition, the position-limiting tube is fixed on the fulcrum.
The main shaft is connect with geared motor output shaft, and the main shaft is mounted on the bearing block.
For the sheller unit after opening decelerating motor, decelerating motor drives main shaft, main shaft to drive fulcrum and activity hammer one
Rotation is played, centrifugal force is generated.The activity hammer is contacted with the belt surface under the influence of centrifugal force, by the crystallization on mesh belt
Beating is split away off.
Vent passages are set between the feeding crystalline spaces and the heat pump installation space.
The crystalline carrier mesh belt installation includes being arranged in the intracorporal transmission of case in the conveying device on a conveyor
Bracket and the transmission chain being mounted in the transmission bracket, the crystalline carrier net are mounted on the transmission chain.
Minimum of one decelerating motor, the decelerating motor and driving axis connection is arranged in the end of the transmission bracket, described
Transmission chain is mounted on the driving gear of the drive shaft.
The crystalline carrier net is continuously to be layered to turn back to be circularly set in the feeding crystalline spaces and dry place,
Evaporative crystallization efficiency, energy saving can be improved in this way.
The utility model dope belt evaporative crystallization drying machine (dope steams knot machine) is using continous way carrier adsorption evaporation knot
Brilliant dry technology can sufficiently solve the problems such as energy consumption, environment protection emission present in existing dope, waste liquid evaporation technique.With suitable
The advantages such as Ying Xingqiang, Awaiting Parts are few, long service life, drying temperature are low, will receive significant attention, have good market to apply
Prospect；Waste liquid, a kind of recent studies on direction of dope processing and processing selection will be become, energy saving, in terms of have
Very big advantage will be the dominant direction of dense liquid waste processing.
Compared with prior art, the utility model has the following advantages: the high-concentration waste liquid that can sufficiently discharge to various kinds of equipment
It is evaporated crystallization, 80% or more decrement can be carried out to dope, not volatile substance removal rate is up to 95% in the dope that gives up
More than, discharge liquid is evaporation and condensation water, and processing cost is low, and processing technique is simple；It is evaporated using low temperature (80 DEG C or less)
Crystallization is evaporated crystallization one ton of water consume electricity 220kw.h of every evaporation using dehumidifying heat pump；Crystallization is evaporated using waste heat source
One ton of water consume electricity 70kw.h of every evaporation；Low temperature (48-80 DEG C) totally-enclosed drying process inhibits escaping gas volatilization, can pacify
Row for the national games；Emission-free discharge is not necessarily to additional stench processing system；Entire drying process can be carried out all under the conditions of closed environment,
Gas is not had to be discharged in external environment, not will cause secondary environmental pollution.
[Detailed description of the invention]
Fig. 1 is the internal structure instance graph in the main view direction of the utility model dope belt evaporative crystallization drying machine；
Fig. 2 is the internal structure instance graph in the left view direction of the utility model dope belt evaporative crystallization drying machine；
Fig. 3 is the construction in the crystalline carrier mesh belt main view direction in the utility model dope belt evaporative crystallization drying machine
Instance graph；
Fig. 4 is that the construction in the crystalline carrier net left view direction in the utility model dope belt evaporative crystallization drying machine is real
Example diagram；
Fig. 5 is the threshing discharging device left view instance graph in the utility model dope belt evaporative crystallization drying machine.
Fig. 6 is the construction example in the main view direction of water-accepting board in the utility model dope belt evaporative crystallization drying machine
Figure；
Fig. 7 is the portion water-accepting board A-A section working principle diagram in the utility model dope belt evaporative crystallization drying machine；
Fig. 8 is the organigram of threshing zone in the utility model dope belt evaporative crystallization drying machine；
Fig. 9 is the local structure schematic diagram in the utility model dope belt evaporative crystallization drying machine inside threshing zone；
Figure 10 is the construction example in sheller unit main view direction in the utility model dope belt evaporative crystallization drying machine
Figure；
Figure 11 is the construction that sheller unit constructs left view direction in the utility model dope belt evaporative crystallization drying machine
Instance graph.
[specific embodiment]
The utility model is described in detail below in conjunction with the drawings and specific embodiments.Attached drawing shows practical
The specific structure of novel preferred embodiment.The wherein design feature of each element, and if there is be described to direction (it is upper and lower, left,
It is right, before and after) when, it is with structure shown in FIG. 1 for reference to description, but the actual use direction of the utility model is not limited to
This.
Dope belt evaporative crystallization drying machine, as shown in Figs 1-4, including cabinet 1 and setting at least one layer of knot in cabinet 1
Brilliant carrier web band 8, the installation of crystalline carrier mesh belt 8 is on a conveyor.Spray is provided with above the crystalline carrier mesh belt 8
Liquid device 5, the liquid-jet device 5 are connect by inlet tube 6 with feed liquor system, and the feed liquor system includes liquid feeding pump 15 and dope
Dense waste liquid in dope bucket 14 is transported to hydrojet dress through inlet tube 6 by liquid feeding pump 15 by bucket 14 and filter, valve etc. pipe fittings
It sets in 5, dope is uniformly sprayed on the crystalline carrier mesh belt 8 by liquid-jet device 5.It may include feeding knot in the cabinet 1
Brilliant space 21, dry place 22 and heat pump installation space 23, the interior installation dehumidifying heat pump condensing heat-exchange of the heat pump installation space 23
The air port of unit 4, the dehumidifying heat pump condensing heat-exchange unit 4 passes through vent passages and the feeding crystalline spaces 21 and drying
Space 22 is connected to；The crystalline carrier net 8 is mounted in the upper material space 21 and dry place 22, in feeding crystalline spaces 21
Water-accepting board 24 is set between dry place 22.Blower 10 is set in the dry place 22, strengthens convection current, improves drying
Efficiency.
The conveying device include the transmission bracket 3 being arranged in cabinet 1 and be mounted on it is described transmission bracket 3 in transmission
Chain 2, the crystalline carrier mesh belt 8 are mounted on the transmission chain 2.It is arranged minimum one in end in the transmission bracket 3
A motor 7, the motor 7 are mounted on the driving gear of the drive shaft with driving axis connection, the transmission chain 2.It is described
Crystalline carrier mesh belt 8 is mounted in the upper material space 21 and dry place 22, and the crystalline carrier mesh belt 8 is in the dry work
It is continuous layering Zigzag type closed circulation setting in industry space, can be improved extend evaporative crystallization mesh belt running length in this way,
Energy saving.Motor 7, the motor 7 and driving axis connection is respectively set in one end of every layer of crystalline carrier mesh belt 8, described
Transmission chain 2 is mounted on the driving gear of the drive shaft, and the motor 7 drives transmission chain to drive crystallization by drive shaft
The movement of carrier mesh belt transmission.
As shown in Figure 3-Figure 5, setting is filled out for accepting the crystals dried carrier of dope progress on the crystalline carrier mesh belt 8
Material.The carrier filler can be the cake shape that the corrosion-resistant plastics such as PP material (polypropylene material) or metal twine are woven into
Or open circles pieshape, outer diameter 90-120mm, internal diameter 12-13mm, it is furthermore preferred that outer diameter is 100mm, internal diameter is
12mm.The carrier filler, which is worn, to be connect on the mesh belt fulcrum of the crystalline carrier mesh belt 8, is fixed by mesh belt fulcrum break-through.In
On the crystalline carrier mesh belt 8, the carrier filler be can be set two layers or more.Certainly, the carrier filler can also use
Net belt type, carrier filler and chain syn-chro-step operate.
As shown in Fig. 2, Fig. 4, Fig. 6 and Fig. 7, water-accepting board is set between the feeding crystalline spaces 21 and dry place 22
24, for preventing the liquid in feeding crystalline spaces 21 from entering dry place.The water-accepting board 24 is by groove 243 and tongue 246
It staggeredly forms, the cross section of the tongue 246 can be inverted " v " shape.The two sides of the tongue 246 side of dripping is located at phase
The top of two adjacent grooves 243, is arranged the first slot 2445 between the adjacent grooves 243, the tongue 246 with
Second slot 2454 is set between adjacent grooves 243, third slot 247 is set between the adjacent tongue 243.Dry place
Hot wind enters feeding crystalline spaces by the first slot 245, the second slot 244 and third slot 247；It is more in feeding crystalline spaces
Remaining dense waste liquid drops on tongue 246 and groove 243；The hot wind of dry place can pass through the first slot 245, the second slot
244 and third slot 247 enter feeding crystalline spaces, extra dense waste liquid cannot enter dry sky in feeding crystalline spaces
Between, to realize separating between feeding crystalline spaces and dry place.Preferably, the groove 243 is with respect to the horizontal plane
Side is down-set with respect to other side horizontal tilt, and main collecting tank 25 is arranged in the horizontal low level side of groove 243, each groove 243
For liquid after main collecting tank 25 confluence, extra dense waste liquid flows back into feed liquid bucket, whole zero-emission through return pipe 242.It is described convex
The two sides of slot 246 are to drip side, and liquid is dropped onto and fallen into groove 243 after tongue 246 along two sides side of dripping.
As illustrated in figs. 8-11, threshing zone is arranged in the cabinet 1, and the threshing zone can be located at feeding crystalline spaces 21 and do
Dry 22 1 side of space.Sheller unit for making crystallization fall off is set in the threshing zone.The sheller unit 11 is mounted on
The inner surface of the crystalline carrier mesh belt 8 and/or the lower section of outer surface, pass through the inner surface to crystalline carrier mesh belt 8
It is patted with outer surface and carries out threshing, the material particles on crystalline carrier mesh belt 8 can be effectively removed.Preferably, described in two sets
Sheller unit 11 is arranged on different height, and the sheller unit 11 that lower part is arranged in is located at the outer surface of crystalline carrier mesh belt 8
Lower section, be arranged in top sheller unit 11 be located at crystalline carrier mesh belt 8 inner surface lower section, can be to crystalline carrier net
With the material ratio more thoroughly threshing on 8.Two sets of sheller units 11 in the threshing zone of cabinet by being arranged above and below, in this way can be with
Space is saved, and can use dried material own wt and fall off.The sheller unit 11 is lower to be arranged receiving hopper 16, for accepting
The materials such as the crystalline solid to fall off.The receiving hopper 16 with converge hopper 12 and connect, material particles, which are converged, to be transferred out after hopper 12.
The sheller unit exports the master of axis connection including decelerating motor 13, decelerating motor 13 as shown in Figure 10 and Figure 11
Axis 112, the mounting rack being fixed on main shaft 112 and the movable threshing unit being mounted on the mounting rack.Wherein, the installation
Frame is triangle mounting rack, and threshing unit is movable is mounted in three angles of the triangle mounting rack for the activity.Preferably,
The triangle mounting rack is equilateral triangle mounting rack.The activity threshing unit can be activity hammer 115, the activity hammer
Fulcrum 117 on mounting rack rotates freely or the activity hammer 115 is fixed on litter, and the litter is movably arranged on
In position-limiting tube 116 in three angles of the triangle mounting rack.The fulcrum 117 is fixed on the triangle of the triangle mounting rack
In fixed plate 114.Wherein, the activity hammer 115 is made of the light material material such as PP (polypropylene), it is possible to reduce weight with rub
It wipes.The triangle mounting rack is by the triangle fixed plate 114 that is fixed on the main shaft 112 and is fixed on the triangle fixed plate
Three fulcrums 117 composition on 114, the position-limiting tube 116 are fixed by screws on the fulcrum 117.The fulcrum 117 with
The triangle fixed plate 114 is fixed by screw 118.The main shaft 112 be mounted on described on bearing block 113.The bearing
Seat 113 can be tyre spherical bearing block.
For the sheller unit after opening decelerating motor, decelerating motor drives main shaft, main shaft to drive fulcrum and activity hammer one
Rotation is played, centrifugal force is generated.The activity hammer is contacted with the belt surface under the influence of centrifugal force, by the crystallization on mesh belt
Bat is split away off.The revolving speed of decelerating motor 13 can be adjusted by frequency converter, thus the size of centrifugal force needed for controlling.
The crystalline carrier mesh belt 8 is arranged two layers or more in closed feeding crystalline spaces 21 and dry place 22, excellent
Choosing can be set four or six layers, and the liquid-jet device 5 is arranged between one layer of mesh belt of the crystalline carrier and two layers of mesh belt.
8 both sides of crystalline carrier mesh belt should install retaining device additional, and width is 0.8-2.0 meters.
Homogenating plate is set on each layer crystalline carrier mesh belt 8, and the homogenating plate via area is not less than 25%.In cabinet
Condensate draining pipe 17 is arranged in 1 bottom, for condensed water to be discharged.
Preferably, dope belt evaporative crystallization drying machine may include several dope evaporative crystallization drying units；If described
Dry dope evaporative crystallization drying unit includes cabinet 1, and drying operation space (21 He of feeding crystalline spaces is arranged in the cabinet 1
Dry place 22) and heat pump installation space 23, vent passages are set between the drying operation space and heat pump installation space 23,
Installation dehumidifying heat pump condensing heat-exchange unit 4 in the heat pump installation space 23；Adjacent dope evaporative crystallization drying unit splicing
Together, the close drying working space that the drying operation space of each dope evaporative crystallization drying unit is communicated as one, In
At least one layer of crystalline carrier mesh belt 8 is arranged in the close drying working space, and the crystalline carrier net 9, which takes, to be arranged for holding
It carries dope and carries out crystals dried carrier filler.
It is as follows that the utility model dope crystallizes process: the dope in dense liquid box material 14 is defeated through inlet tube 6 by liquid feeding pump 15
It is sent to liquid-jet device 5, is then sprayed on crystalline carrier mesh belt 8, crystalline carrier mesh belt 8 is through second layer mesh belt, third layer net
Crystalline solid is fallen in receiving hopper through sheller unit after the multilayers crystallizing and dryings such as band, four-layer network band, five layers of mesh belt, six layers of mesh belt
Then feed bin is being transported to by discharging machine, wherein first layer mesh belt undertakes demisting effect.
The utility model circulated air process is as follows: the hot wind come out from dehumidifying heat pump condensing heat-exchange unit 4 adds through main air blower
After pressure, in dry place 22 and in upper material space 21 from bottom to up after each layer crystalline carrier mesh belt 8, a part of wind by into
Wind filter screen enters dehumidifying heat pump condensing heat-exchange unit 4, enters dry place 22 after dehumidifying heating；A part of wind is through circulated air
It is directly entered in material space 21, converges with the hot wind brought from dry place 22, the bottom of by after machine and heater pressurized, heated
Upwards through each layer crystalline carrier mesh belt 8.
It is as follows that the utility model also sets up cooling water flow path: cooling tower enters dehumidifying heat pump by cooling water circulating pump and condenses
Heat-exchange unit heat exchanger, subsequently into cooling tower.Cooling water circulation use, water consumption is small, save the cost.
The cabinet is not less than 25mm, compound inner cord using the composite insulation boards for having thermal insulation property, insulation layer thickness
Plate should have the good hot-dip galvanizing sheet steel of Corrosion Protection, aluminium sheet or stainless steel plate.Bracket should be using structural section, sheet metal processing or aluminium
Alloy profile production.
As described above, the only preferred embodiment of the utility model is real when that cannot limit the utility model with this
The range applied, i.e., generally according to simple equivalence changes made by present utility model application the scope of the patents and utility model description
With modification, all still belong in the range of the utility model patent covers.
Claims (23)
1. dope belt evaporative crystallization drying machine, which is characterized in that exist including several dope evaporative crystallization drying units and setting
At least one layer of crystalline carrier mesh belt in several dope evaporative crystallization drying units is arranged for holding on the crystalline carrier mesh belt
It carries dope and carries out crystals dried carrier filler, several dope evaporative crystallization drying units include cabinet, in the cabinet
Configured with dehumidifying heat pump condensing heat-exchange unit.
2. dope belt evaporative crystallization drying machine according to claim 1, which is characterized in that further include having to spray dope
To the liquid-jet device of the crystalline carrier mesh belt, the liquid-jet device is connect with feed liquor system.
3. dope belt evaporative crystallization drying machine according to claim 2, which is characterized in that the liquid-jet device setting exists
Between the first layer crystalline carrier mesh belt and second layer crystalline carrier mesh belt.
4. dope belt evaporative crystallization drying machine according to claim 1, which is characterized in that the carrier filler is to use net
The cake shape or open circles pieshape that silk is woven into.
5. dope belt evaporative crystallization drying machine according to claim 4, which is characterized in that open circles pieshape carrier is filled out
The outer diameter of material is 50-150mm, internal diameter 12-14mm.
6. dope belt evaporative crystallization drying machine according to claim 1, which is characterized in that feeding is arranged in the cabinet
Vent passages, institute is arranged in crystalline spaces, dry place and heat pump installation space between the dry place and heat pump installation space
State installation dehumidifying heat pump condensing heat-exchange unit in heat pump installation space；The crystalline carrier net is installed on the feeding crystalline spaces
In dry place.
7. dope belt evaporative crystallization drying machine according to claim 6, which is characterized in that the feeding crystalline spaces and
Water-accepting board is set between dry place.
8. dope belt evaporative crystallization drying machine according to claim 7, which is characterized in that the water-accepting board includes several
Groove and several tongues, the two sides of tongue side of dripping is located at the tops of two adjacent grooves, described adjacent
First slot is set between groove, the second slot is set between the tongue and adjacent grooves, is arranged between the adjacent tongue
Third slot.
9. dope belt evaporative crystallization drying machine according to claim 8, which is characterized in that the side of the groove is phase
The other side is arranged diagonally downward, main collecting tank is set in the horizontal low level side of groove.
10. dope belt evaporative crystallization drying machine according to claim 6, which is characterized in that above the dry place
Filter space is set between heat pump installation space.
11. dope belt evaporative crystallization drying machine according to claim 6, which is characterized in that the dry place is also set
It is equipped with threshing zone, the threshing zone is set to a side in crystalline carrier mesh-belt operation direction.
12. dope belt evaporative crystallization drying machine according to claim 11, which is characterized in that the threshing zone setting is de-
Grain device, the sheller unit are mounted on the inner surface of the crystalline carrier mesh belt and/or the lower section of outer surface.
13. dope belt evaporative crystallization drying machine according to claim 12, which is characterized in that two sets of sheller units
It is that threshing zone is arranged on different height, the sheller unit that lower part is arranged in is located at the outer side-lower of mesh belt, and top is arranged in
Sheller unit is located at the lower section of the inside of mesh belt.
14. dope belt evaporative crystallization drying machine according to claim 12, which is characterized in that the sheller unit is divided into
Set receiving hopper.
15. dope belt evaporative crystallization drying machine described in 2,13 or 14 according to claim 1, which is characterized in that described de-
Grain device includes main shaft, the mounting rack being fixed on main shaft and the movable threshing unit being mounted on the mounting rack, the peace
It shelves and bearing block is installed.
16. dope belt evaporative crystallization drying machine according to claim 15, which is characterized in that the mounting rack is triangle
Shape mounting rack, threshing unit is movable is mounted in three angles of the triangle mounting rack for the activity.
17. dope belt evaporative crystallization drying machine according to claim 16, which is characterized in that the activity threshing unit
It is movable hammer, the activity hammer is fixed on litter, and the litter is movably arranged in three angles of the triangle mounting rack
In position-limiting tube.
18. dope belt evaporative crystallization drying machine according to claim 17, which is characterized in that the triangle mounting rack
It is made of the triangle fixed plate being fixed on the main shaft and three fulcrums being fixed on the triangle fixed plate, the limit
Pipe is fixed on the fulcrum.
19. dope belt evaporative crystallization drying machine according to claim 15, which is characterized in that the main shaft and the electricity that slows down
Machine exports axis connection, and the main shaft is mounted on the bearing block.
20. dope belt evaporative crystallization drying machine according to claim 6, which is characterized in that the feeding crystalline spaces
Vent passages are set between the heat pump installation space.
21. dope belt evaporative crystallization drying machine according to claim 1, which is characterized in that the crystalline carrier mesh belt
Installation on a conveyor, includes setting in the intracorporal transmission bracket of case in the conveying device and is mounted on the transmission bracket
Interior transmission chain, the crystalline carrier net are mounted on the transmission chain.
22. dope belt evaporative crystallization drying machine according to claim 21, which is characterized in that the end of the transmission bracket
Minimum of one motor is arranged in portion, and the motor and driving axis connection, the transmission chain are mounted on the sliding tooth of the drive shaft
On wheel.
23. dope belt evaporative crystallization drying machine according to claim 6, which is characterized in that the crystalline carrier net exists
It turns back and is circularly set for continuous layering in the feeding crystalline spaces and dry place.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820717598.XU CN209554820U (en) | 2018-05-14 | 2018-05-14 | Dope belt evaporative crystallization drying machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820717598.XU CN209554820U (en) | 2018-05-14 | 2018-05-14 | Dope belt evaporative crystallization drying machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209554820U true CN209554820U (en) | 2019-10-29 |
Family
ID=68298159
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820717598.XU Active CN209554820U (en) | 2018-05-14 | 2018-05-14 | Dope belt evaporative crystallization drying machine |
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| Country | Link |
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| CN (1) | CN209554820U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108862430A (en) * | 2018-05-14 | 2018-11-23 | 广州晟启能源设备有限公司 | Dope belt evaporative crystallization drying machine |
-
2018
- 2018-05-14 CN CN201820717598.XU patent/CN209554820U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108862430A (en) * | 2018-05-14 | 2018-11-23 | 广州晟启能源设备有限公司 | Dope belt evaporative crystallization drying machine |
| CN108862430B (en) * | 2018-05-14 | 2024-03-15 | 广州晟启能源设备有限公司 | Concentrated liquid belt type evaporation crystallization dryer |
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