CN110319680A - A kind of dry cooling integrated machine of continuous scraper-type - Google Patents
A kind of dry cooling integrated machine of continuous scraper-type Download PDFInfo
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- CN110319680A CN110319680A CN201910687601.7A CN201910687601A CN110319680A CN 110319680 A CN110319680 A CN 110319680A CN 201910687601 A CN201910687601 A CN 201910687601A CN 110319680 A CN110319680 A CN 110319680A
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- 238000001816 cooling Methods 0.000 title claims abstract description 35
- 239000000463 material Substances 0.000 claims abstract description 33
- 230000007246 mechanism Effects 0.000 claims abstract description 11
- 238000007790 scraping Methods 0.000 claims abstract description 11
- 239000003507 refrigerant Substances 0.000 claims abstract description 9
- 229910000831 Steel Inorganic materials 0.000 claims description 48
- 239000010959 steel Substances 0.000 claims description 48
- 239000012530 fluid Substances 0.000 claims description 7
- 230000015572 biosynthetic process Effects 0.000 claims description 4
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 claims description 3
- 239000000428 dust Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 238000001035 drying Methods 0.000 description 16
- 238000000034 method Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 230000035515 penetration Effects 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 235000013305 food Nutrition 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000003889 chemical engineering Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 240000002791 Brassica napus Species 0.000 description 1
- 235000004977 Brassica sinapistrum Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B15/00—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form
- F26B15/10—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions
- F26B15/12—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a kind of dry cooling integrated machines of continuous scraper-type, it is mentioned including scraper-type drier, scraper-type cooler and bucket, have in the scraper-type drier, scraper-type cooler and has been sequentially distributed multiple plate-type heat-exchange plates up and down, it which is provided with the scraping mechanism for pushing material from the mobile discharge port of feed inlet, the material to fall from the discharge port of scraper-type cooler mentions the feed inlet being delivered on scraper-type drier through belt conveyor, bucket；In scraper-type drier with the plate-type heat-exchange plate pipeline mutual conduction in the scraper-type cooler, in refrigerant circulation flowing.Scraper-type drier is equivalent to a condenser, and scraper-type cooler is equivalent to an evaporator, and energy-saving effect is good, and dust emission is small, reaches the environmental requirement of energy-saving and emission-reduction.
Description
Technical field
The present invention relates to a kind of dry cooling integrated machines of continuous scraper-type, can be widely used in agricultural, chemical engineering industry, food
Field, pharmacy, bioengineering etc. are related to the dry cooling occasion of powder solid.
Background technique
It is well known that in agricultural, chemical engineering industry, field of food, pharmacy.The fields such as bioengineering need extensive utilization to dry
Dry, cooling technology, such as the drying and cooling of agriculture field rapeseed, corn, cereal, the drying and cooling of industrial chemicals, food
The various fields such as the drying and cooling of product additive and occasion all apply to the drying of powder solid material, cooling technique, traditional
Dry, cooling common equipment has fluidized bed, roller, but energy consumption is high, dust discharge amount is big for fluidized bed, roller, matches
Equipment it is more, installation maintenance difficulty is big.The requirement of environmental protection and energy saving is not met.
Summary of the invention
The purpose of the present invention is to provide a kind of dry cooling integrated machines of continuous scraper-type, mention for overcoming in background technique
To the problem of.
In order to reach the goals above, the technical solution adopted by the present invention is that: a kind of dry cooling integrated machine of continuous scraper-type,
It being mentioned including scraper-type drier, scraper-type cooler and bucket, the scraper-type drier, scraper-type cooler all have cabinet,
The cabinet upper end is equipped with feed inlet, the lower end of cabinet is equipped with discharge port；It has been sequentially distributed up and down in the cabinet multiple board-like
Heat exchanger plates, the scraping mechanism for pushing material mobile is provided on the plate-type heat-exchange plate, and the scraping mechanism is accepted up and down and will
The material that feed inlet enters is elapsed to discharge port and is discharged；
The material to fall from the discharge port of the scraper-type cooler is delivered to the entrance that bucket mentions, institute by belt conveyor
It states the outlet that bucket proposes and passes through guide pipe for the feed inlet on material diversion to the scraper-type drier；
Plate-type heat-exchange plate in the scraper-type drier and the plate-type heat-exchange plate pipeline phase in the scraper-type cooler
It is mutually connected, the plate-type heat-exchange plate in the scraper-type drier, the plate-type heat-exchange plate in scraper-type cooler have circulated system
Cryogen.
Above-mentioned scraping mechanism includes circumversion chain, and scraper plate is intervally distributed on the circumversion chain, and above structure can refer to
Patent CN200720153976.8 belongs to the known prior art.
Furthermore, it is understood that the first general pipeline, the second general pipeline are provided between the scraper-type drier and scraper-type cooler,
It is provided with compressor on first general pipeline, is provided with expansion valve on second general pipeline；One end of first general pipeline passes through
Branch pipe is connected with the arrival end of each plate-type heat-exchange plate in scraper-type drier, and the other end of first general pipeline passes through branch pipe
It is connected with the outlet end of each plate-type heat-exchange plate in scraper-type cooler；One end of second general pipeline passes through branch pipe and scraper plate
The outlet end of each plate-type heat-exchange plate in formula drier is connected, and one end of second general pipeline is cooling by branch pipe and scraper-type
The arrival end of each plate-type heat-exchange plate in device is connected.
Furthermore, it is understood that the plate-type heat-exchange plate in the scraper-type drier includes the first steel plate being distributed up and down, second
Steel plate, first steel plate, the second steel plate are welded together by laser penetration, and are led between the first steel plate and the second steel plate
High-pressure fluid is crossed the first inner passage of expansion formation, be provided on first steel plate or the second steel plate logical with the first inside
The arrival end of road conducting, outlet end.
It is preferably located at first be provided on the plate-type heat-exchange plate where on the outside of the first inner passage convenient for moisture discharge
Through-hole.
Furthermore, it is understood that the plate-type heat-exchange plate in the scraper-type cooler includes the third steel plate being distributed up and down, the 4th
Steel plate, the third steel plate, the 4th steel plate are welded together by laser penetration, and are led between third steel plate and the 4th steel plate
High-pressure fluid is crossed the second inner passage of expansion formation, be provided on the third steel plate or the 4th steel plate logical with the second inside
The arrival end of road conducting, outlet end.
Furthermore, it is understood that being provided with distribution up and down, the type chamber be connected in serpentine, the type chamber and cabinet in the cabinet
On feed inlet, discharge port conducting；There are multiple steps, the plate-type heat-exchange plate is arranged on the step on the type chamber.
Furthermore, it is understood that the upper end of the scraper-type drier is provided with first row port, the exhaust outlet be connected with type chamber,
The lower end of the scraper-type drier is provided with the air inlet be connected with type chamber, the air outlet phase of the air inlet and air blower
Even.The upper end of the scraper-type cooler is provided with the second exhaust port be connected with type chamber.
Working principle are as follows: the higher material of water capacity enters scraper-type drier, and material enters horizontal positioned board-like change
The refrigerant of high temperature and pressure exchanges heat in hot plate, with plate-type heat-exchange plate, and the higher temperature of charge of water capacity increases after heat exchange, water
Divide and be evaporated, the moisture evaporated is taken away by the wind that air blower band comes.The mistake that scraper plate advances with material in plate-type heat-exchange plate
Heat exchange drying is carried out in journey, heat drying is continued by the plate-type heat-exchange plate scraped to lower layer from the plate-type heat-exchange plate on upper layer, after dry
High-temperature material be discharged from scraper-type drier discharge port, be delivered to bucket through belt conveyor and mention, bucket is mentioned for material being delivered to and scraped
Panel cooler feed inlet.The high temperature and high pressure gaseous refrigerant simultaneously flowed through in scraper-type drier heat exchanger plates is condensed into liquid,
Expansion valve is flowed through to shut off into scraper-type cooler, into the plate-type heat-exchange plate in scraper-type cooler, liquid refrigerant
High-temperature material exchanges heat outside evaporation endothermic, with plate-type heat-exchange plate, and scraper plate is with material during plate-type heat-exchange plate advances
Heat exchange cooling is carried out, is continued to cool down by the plate-type heat-exchange plate scraped to lower layer from the plate-type heat-exchange plate on upper layer, thus by high-temperature material
It is down to target temperature, is discharged through discharge port, is delivered to lower segment process eventually by belt conveyor.
Compared with prior art, present invention has the advantage that
1, scraper-type drier is equivalent to a condenser, and scraper-type cooler is equivalent to an evaporator.It is mentioned using bucket
It is connected with belt conveyor and realizes dry cooling integration, device energy conservation effect is good, and dust emission is small, reaches the ring of energy-saving and emission-reduction
Guaranteed request；
2, the drying cooling integrated machine combined using scraper-type drier and scraper-type cooler, compared to traditional fluidisation
Bed, roller drying, cooling equipment, the integrated machine equipment space utilization rate is high, and occupation area of equipment is small, especially suitable for factory's skill
Art transformation；
3, by a series of plate-type heat-exchange plates (using pillow-type plate-type heat-exchange plate, abbreviation heat exchanger plates A) inside scraper-type drier
It is horizontally disposed by certain spacing, (pillow-type plate-type heat-exchange plate, letter are used by a series of plate-type heat-exchange plates inside scraper-type cooler
Claim heat exchanger plates B) it is horizontally disposed at a certain distance.Heat exchanger plates A and heat exchanger plates B is superimposed by two stainless steel plates, is led to
It crosses laser penetration to weld together, then expand forming inner passage by high-pressure fluid between plate, bearing capacity
Height, it is highly reliable.
4, a series of through-holes are disposed on the board-like heat exchanger plates of scraper-type drier, fled between plate conducive to moisture, convenient for wet
The discharge of gas.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the embodiment of the present invention.
Fig. 2 is condensation cycle schematic diagram in the embodiment of the present invention.
Fig. 3 is the schematic diagram of heat exchanger plates A in the embodiment of the present invention.
Fig. 4 is the schematic diagram of heat exchanger plates B in the embodiment of the present invention.
Specific embodiment
The preferred embodiments of the present invention will be described in detail with reference to the accompanying drawing, so that advantages and features of the invention energy
It is easier to be readily appreciated by one skilled in the art, so as to make a clearer definition of the protection scope of the present invention.
Embodiment
Referring to shown in attached drawing 1, Fig. 2, the continuous scraper-type of one of the present embodiment dries cooling integrated machine, including scraper-type
Drier 1, scraper-type cooler 2, bucket mention 3.
The scraper-type drier 1 includes drying box 11, and the upper end of drying box 11 is equipped with feed inlet 12, drying box
11 lower end is equipped with discharge port 13, has been sequentially distributed multiple plate-type heat-exchange plates 4, the plate-type heat-exchange plate up and down in drying box 11
The scraping mechanism for pushing material mobile is provided on 4, the scraping mechanism is accepted up and down and pushes away the material that feed inlet 12 enters
Move to the discharge of discharge port 13.Wherein plate-type heat-exchange plate 4 uses pillow-type plate-type heat-exchange plate, abbreviation heat exchanger plates A.
The scraper-type cooler 2 includes cooling box 21, and the upper end of the cooling box 21 is equipped with feed inlet 22, cooling
The lower end of cabinet 21 is equipped with discharge port 23, has been sequentially distributed multiple plate-type heat-exchange plates 5 in cooling box 21 up and down, described board-like to change
The scraping mechanism for pushing material mobile, the object that the scraping mechanism is accepted up and down and enters feed inlet 22 are provided on hot plate 5
Material passage to discharge port 23 is discharged.Wherein plate-type heat-exchange plate 5 uses pillow-type plate-type heat-exchange plate, abbreviation heat exchanger plates B.
Wherein scraper-type cooler 2, the scraping mechanism structure in scraper-type drier 1 are identical, including circumversion chain, described
Scraper plate is intervally distributed on circumversion chain, above structure can refer to patent CN200720153976.8, belong to known existing skill
Art.
The material to fall from the discharge port 13 of the scraper-type drier 1, which by belt conveyor 6 is delivered to bucket and mentions 3, to be entered
Mouthful, the outlet that the bucket mentions 3 passes through guide pipe 31 for the feed inlet on material diversion to scraper-type cooler 2, and material is in scraper plate
It is expelled on belt conveyor 7 after cooling from discharge port 23 in formula cooler 2, is delivered to lower segment process.
Heat exchanger plates A and heat exchanger plates B pipeline mutual conduction, and have circulated refrigerant therebetween.Specific side
Formula is as follows:
The first general pipeline 81, the second general pipeline 82 are provided between the scraper-type drier 1 and scraper-type cooler 2, it is described
It is provided with compressor 83 on first general pipeline 81, is provided with expansion valve 84 on second general pipeline 82；The one of first general pipeline 81
End is connected by branch pipe with the arrival end of each heat exchanger plates A in scraper-type drier 1, and the other end of first general pipeline 81 is logical
Branch pipe is crossed to be connected with the outlet end of each heat exchanger plates B in scraper-type cooler 2；One end of second general pipeline 82 passes through branch pipe
It is connected with the outlet end of each heat exchanger plates A in scraper-type drier 1, one end of second general pipeline 82 passes through branch pipe and scraper plate
The arrival end of each heat exchanger plates B in formula cooler 2 is connected.
As shown in figure 3, in the present embodiment, heat exchanger plates A includes the first steel plate 41 being distributed up and down, the second steel plate 42, institute
State the first steel plate 41, the second steel plate 42 is welded together by laser penetration, and between the first steel plate 41 and the second steel plate 42
Expansion is carried out by high-pressure fluid and forms the first inner passage 43, is provided on first steel plate 41 or the second steel plate 42 and the
The arrival end of one inner passage 43 conducting, outlet end are arranged on the plate-type heat-exchange plate 4 where 43 outside of the first inner passage
There is first through hole 44, is discharged convenient for moisture between plate.
As shown in figure 4, heat exchanger plates B includes the third steel plate 51 being distributed up and down, the 4th steel plate 52, the third steel plate 51,
4th steel plate 52 is welded together by laser penetration, and between third steel plate 51 and the 4th steel plate 52 by high-pressure fluid into
Row expansion forms the second inner passage 53, is provided on the third steel plate 51 or the 4th steel plate 52 and leads with the second inner passage 53
Logical arrival end, outlet end.
11 internal structure of drying box is identical as 21 internal structure of cooling box, therefore by drying box 11, cooling box 21
Uniform Name is cabinet.Distribution up and down, the type chamber be connected in serpentine, the charging on the type chamber and cabinet are all had in cabinet
Mouth, discharge port conducting；There are multiple steps, corresponding heat exchanger plates A, heat exchanger plates B are arranged on the step on the type chamber.Together
When the upper end of scraper-type drier 1 is provided with the first row port 14 be connected with type chamber, exhaust outlet 15, the scraper-type is dry
The lower end of device 1 is provided with the air inlet be connected with type chamber, and the air inlet is connected with the air outlet of air blower 16.The scraper-type
The upper end of cooler 2 is provided with the second exhaust port 24 be connected with type chamber.
Working principle are as follows: the higher material of water capacity enters scraper-type drier, and material enters horizontal positioned board-like change
The refrigerant of high temperature and pressure exchanges heat in hot plate, with plate-type heat-exchange plate, and the higher temperature of charge of water capacity increases after heat exchange, water
Divide and be evaporated, the moisture evaporated is taken away by the wind that air blower band comes.The mistake that scraper plate advances with material in plate-type heat-exchange plate
Heat exchange drying is carried out in journey, heat drying is continued by the plate-type heat-exchange plate scraped to lower layer from the plate-type heat-exchange plate on upper layer, after dry
High-temperature material be discharged from scraper-type drier discharge port, be delivered to bucket through belt conveyor and mention, bucket is mentioned for material being delivered to and scraped
Panel cooler feed inlet.The high temperature and high pressure gaseous refrigerant simultaneously flowed through in scraper-type drier heat exchanger plates is condensed into liquid,
Expansion valve is flowed through to shut off into scraper-type cooler, into the plate-type heat-exchange plate in scraper-type cooler, liquid refrigerant
High-temperature material exchanges heat outside evaporation endothermic, with plate-type heat-exchange plate, and scraper plate is with material during plate-type heat-exchange plate advances
Heat exchange cooling is carried out, is continued to cool down by the plate-type heat-exchange plate scraped to lower layer from the plate-type heat-exchange plate on upper layer, thus by high-temperature material
It is down to target temperature, is discharged through discharge port, is delivered to lower segment process eventually by belt conveyor.
The technical concepts and features of embodiment of above only to illustrate the invention, its object is to allow be familiar with technique
People understands the contents of the present invention and is implemented, and it is not intended to limit the scope of the present invention, all spiritual according to the present invention
The equivalent change or modification that essence is done, should be covered by the scope of protection of the present invention.
Claims (8)
1. a kind of dry cooling integrated machine of continuous scraper-type, which is characterized in that including scraper-type drier, scraper-type cooler and
Bucket mentions, and the scraper-type drier, scraper-type cooler all have cabinet, and the cabinet upper end is equipped under feed inlet, cabinet
End is equipped with discharge port；Multiple plate-type heat-exchange plates have been sequentially distributed up and down in the cabinet, has been provided with and pushes away on the plate-type heat-exchange plate
The mobile scraping mechanism of animal material, the scraping mechanism are accepted up and down and elapse the material that feed inlet enters to discharge port and arrange
Out；
The material to fall from the discharge port of the scraper-type drier is delivered to the entrance that bucket mentions, the bucket by belt conveyor
The outlet mentioned passes through guide pipe for the feed inlet on material diversion to the scraper-type cooler；
Plate-type heat-exchange plate in the scraper-type drier and the plate-type heat-exchange plate pipeline phase mutual conductance in the scraper-type cooler
Logical, the plate-type heat-exchange plate in plate-type heat-exchange plate, scraper-type cooler in the scraper-type drier has circulated refrigerant.
2. the dry cooling integrated machine of a kind of continuous scraper-type according to claim 1, it is characterised in that: the scraper-type is dry
It is provided with the first general pipeline, the second general pipeline between dry device and scraper-type cooler, is provided with compressor on first general pipeline, it is described
Expansion valve is provided on second general pipeline；
One end of first general pipeline is connected by branch pipe with the arrival end of each plate-type heat-exchange plate in scraper-type drier, institute
The other end for stating the first general pipeline is connected by branch pipe with the outlet end of each plate-type heat-exchange plate in scraper-type cooler；
One end of second general pipeline is connected by branch pipe with the outlet end of each plate-type heat-exchange plate in scraper-type drier, institute
The one end for stating the second general pipeline is connected by branch pipe with the arrival end of each plate-type heat-exchange plate in scraper-type cooler.
3. the dry cooling integrated machine of a kind of continuous scraper-type according to claim 1, it is characterised in that: the scraper-type is dry
Plate-type heat-exchange plate in dry device includes the first steel plate being distributed up and down, the second steel plate, and first steel plate, the second steel plate are by swashing
Light, which penetrates, to be welded together, and lead to inside expansion formation first by high-pressure fluid between the first steel plate and the second steel plate
Road is provided with the arrival end be connected with the first inner passage, outlet end on first steel plate or the second steel plate.
4. the dry cooling integrated machine of a kind of continuous scraper-type according to claim 3, it is characterised in that: be located inside first
The first through hole convenient for moisture discharge is provided on plate-type heat-exchange plate where on the outside of channel.
5. the dry cooling integrated machine of a kind of continuous scraper-type according to claim 1, it is characterised in that: the scraper-type is cold
But the plate-type heat-exchange plate in device includes the third steel plate being distributed up and down, the 4th steel plate, and the third steel plate, the 4th steel plate are by swashing
Light, which penetrates, to be welded together, and lead to inside expansion formation second by high-pressure fluid between third steel plate and the 4th steel plate
Road is provided with the arrival end be connected with the second inner passage, outlet end on the third steel plate or the 4th steel plate.
6. the dry cooling integrated machine of a kind of continuous scraper-type according to claim 1, it is characterised in that: set in the cabinet
It is equipped with distribution up and down, the type chamber be connected in serpentine, the type chamber is connected with feed inlet, the discharge port on cabinet；On the type chamber
With multiple steps, the plate-type heat-exchange plate is arranged on the step.
7. the dry cooling integrated machine of a kind of continuous scraper-type according to claim 6, it is characterised in that: the scraper-type is dry
The upper end of dry device is provided with first row port, the exhaust outlet be connected with type chamber, the lower end of the scraper-type drier be provided with
The air inlet of type chamber conducting, the air inlet are connected with the air outlet of air blower.
8. the dry cooling integrated machine of a kind of continuous scraper-type according to claim 6, it is characterised in that: the scraper-type is cold
But the upper end of device is provided with the second exhaust port be connected with type chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910687601.7A CN110319680A (en) | 2019-07-29 | 2019-07-29 | A kind of dry cooling integrated machine of continuous scraper-type |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910687601.7A CN110319680A (en) | 2019-07-29 | 2019-07-29 | A kind of dry cooling integrated machine of continuous scraper-type |
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| CN110319680A true CN110319680A (en) | 2019-10-11 |
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| CN201910687601.7A Pending CN110319680A (en) | 2019-07-29 | 2019-07-29 | A kind of dry cooling integrated machine of continuous scraper-type |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113332739A (en) * | 2021-05-27 | 2021-09-03 | 商南天和泥浆有限公司 | Polyacrylonitrile ammonium salt low temperature evaporation drying system hydrolysises |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201053809Y (en) * | 2007-05-22 | 2008-04-30 | 曹晓伟 | Scrap plate type boiling, drying and cooling machine |
| CN103851838A (en) * | 2012-11-30 | 2014-06-11 | 苏州必信空调有限公司 | Plate type integrated refrigerant heat recovery circulation system |
| CN104132525A (en) * | 2014-08-13 | 2014-11-05 | 北京广厦环能科技有限公司 | Powder material drying and cooling integrated device |
| CN106931763A (en) * | 2017-04-03 | 2017-07-07 | 东莞市皓奇企业管理服务有限公司 | Intelligent air energy shrimp shell dryer |
| CN108131932A (en) * | 2017-12-15 | 2018-06-08 | 苏州协宏泰节能科技有限公司 | A kind of pincushion screen plate is uniformly into the powder flow heat exchanger of outlet |
| KR101967180B1 (en) * | 2018-06-22 | 2019-04-09 | 김성웅 | Material drying and cooling apparatus |
| CN210321032U (en) * | 2019-07-29 | 2020-04-14 | 瀚能(苏州)节能科技有限公司 | Continuous scraper type drying and cooling integrated machine |
-
2019
- 2019-07-29 CN CN201910687601.7A patent/CN110319680A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201053809Y (en) * | 2007-05-22 | 2008-04-30 | 曹晓伟 | Scrap plate type boiling, drying and cooling machine |
| CN103851838A (en) * | 2012-11-30 | 2014-06-11 | 苏州必信空调有限公司 | Plate type integrated refrigerant heat recovery circulation system |
| CN104132525A (en) * | 2014-08-13 | 2014-11-05 | 北京广厦环能科技有限公司 | Powder material drying and cooling integrated device |
| CN106931763A (en) * | 2017-04-03 | 2017-07-07 | 东莞市皓奇企业管理服务有限公司 | Intelligent air energy shrimp shell dryer |
| CN108131932A (en) * | 2017-12-15 | 2018-06-08 | 苏州协宏泰节能科技有限公司 | A kind of pincushion screen plate is uniformly into the powder flow heat exchanger of outlet |
| KR101967180B1 (en) * | 2018-06-22 | 2019-04-09 | 김성웅 | Material drying and cooling apparatus |
| CN210321032U (en) * | 2019-07-29 | 2020-04-14 | 瀚能(苏州)节能科技有限公司 | Continuous scraper type drying and cooling integrated machine |
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| CN113332739A (en) * | 2021-05-27 | 2021-09-03 | 商南天和泥浆有限公司 | Polyacrylonitrile ammonium salt low temperature evaporation drying system hydrolysises |
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