CN207313988U - A kind of dryer - Google Patents
A kind of dryer Download PDFInfo
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- CN207313988U CN207313988U CN201721193125.6U CN201721193125U CN207313988U CN 207313988 U CN207313988 U CN 207313988U CN 201721193125 U CN201721193125 U CN 201721193125U CN 207313988 U CN207313988 U CN 207313988U
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Abstract
The utility model discloses a kind of dryer, including body, the drying outer barrel being located in body, the drying roller being located in drying outer barrel and the power part being connected with drying roller, the heating part being located at the top of body, the condensation part for being located at the heat exchange department of organism bottom, being located at heat exchange department side, the air inlet pipe being located in body and the exhaust pipe being located in body are further included.Heating part includes heating chamber and is located at the indoor ceramic heating plate of heating；Heat exchange department includes heat-exchanging chamber, is located at the indoor plate heat exchanger of heat exchange；Condensation part includes condensation chamber and is distributed on the indoor condensation pin of condensation.By the energy regenerating to hot-air, the efficient utilization of heat can be realized, and be set by multiple heat exchanges, realize the lifting to condensation effect, can reduce the operating cost of dryer, improve drying effect.
Description
Technical field
It the utility model is related to household appliance technical field, and in particular to a kind of dryer.
Background technology
Dryer may be roughly divided into exhaust, condensing, heat-pump-type.Three kinds of prices are about 1：2：4 relation.
Exhaust：There are clothes hanger and a cylinder type, after principle is heating air, moisture is blown away with hot wind.High energy consumption, efficiency
Low, noise is big, and temperature is high, and clothing damage is big, it is necessary to exhaust pipe drains hot wind, generally in the more of rental house or transition.
The principle of condensing type clothes dryer is：1. air is heated to be hot wind after heater；2. hot wind becomes through clothing
Clammy air；3. clammy air separates out moisture by condenser system, become cold dry air；4. cold dry air is again by heater
Become hot wind and pass through clothing, so circulation constantly drains the moisture of clothing.Exhaust pipe is not required, there is a water storage case or draining
Pipe（Typically water storage case）.Condensing drying temperature is lower than exhaust, and smoothing wrinkle and care effect are good.
Heat-pump-type is known as the upgrade version of condensing, and one kind of condensing, heat pump system are fallen within from basic principle
System can dexterously recycle the heat produced in drying process, it is not necessary to which heating tube heats, so as to reduce energy dissipation.Because not yet
There is heating tube heating, so temperature will not produce high-temperature damage usually all at 60 degree or so.It is exactly efficiency height in simple terms, consumes
Electricity is low, and highest can be than condensing energy-saving 50%-70%.Since drying temperature can be lower than traditional condensing, care clothing effect
Fruit exceedes traditional condensing.
The dryer scope of application is wide, is not affected by the weather, and family has become standard configuration abroad.But in state
Interior market, is limited to intrinsic thinking and higher price, and dryer is all in a small number of families and uses, and reduces the price of dryer and makes
It is contributed to be easier to be acceptable to the market with cost.
Utility model content
The utility model, which aims to provide one kind, can improve drying effect, improve the dryer of heat utilization ratio.
The utility model adopts the following technical solution：
A kind of dryer, including body, be located in body drying outer barrel, be located at drying outer barrel in drying roller and with
The power part of drying roller connection, further includes the heating part being located at the top of body, is located at the heat exchange department of organism bottom, is located at heat
The condensation part of exchange part side, the air inlet pipe being located in body and the exhaust pipe being located in body；
The heating part includes heating chamber and is located at the indoor ceramic heating plate of heating；
The ceramic heating plate is evenly arranged along indoor airflow direction is heated；
The heat exchange department includes heat-exchanging chamber, is located at the indoor plate heat exchanger of heat exchange；
The condensation part includes condensation chamber and is distributed on the indoor condensation pin of condensation；
The input terminal of one end of the air inlet pipe and body through connection, the other end and heat-exchanging chamber connects；
The output terminal of the heat-exchanging chamber and the input terminal of heating chamber connect；
The output terminal of the heating chamber is connected with drying outer barrel；
The input terminal of the condensation chamber is connected with drying outer barrel；
The output terminal of the condensation chamber and one end of exhaust pipe connect；
The other end of the exhaust pipe and body through connection.
As further solution：The ceramic heating plate includes supporting rack and uniformly distributed ceramics on supporting rack add
Backing；The section of the ceramic heating flake is waveform.
As further solution：Heat exchanger plates in the plate heat exchanger are tablet.
As further solution：The condensation pin is cone；The condensation pin is equal on the bottom surface of condensation chamber
Even arrangement.
As further solution：The top surface of the condensation chamber is equipped with air compartment；The air compartment it is defeated
Enter end to be connected with air inlet pipe, the input terminal connection of output terminal and heat-exchanging chamber.
As further solution：Partition plate is equipped with the air compartment；The partition plate is arc panel；The partition plate
It is recessed to close to the direction of condensation chamber.
As further solution：One end of the air inlet pipe and body through connection is equipped with filter screen.
As further solution：Velveteen collector is equipped with the body；The velveteen collector includes collecting
Case and the trapezoidal air passage being located on collecting box.
As further solution：The upper top surface in the trapezoidal air passage and drying outer barrel through connection.
As further solution：The velveteen collector further includes the negative tube being connected with collecting box and the company of being located at
Connect the strainer at place；The other end of the negative tube and the input terminal of heat-exchanging chamber connect.
The good effect that the utility model produces is as follows：
The utility model optimizes the mode of heat transfer, adds heat exchange section, can realize the abundant profit to heat
With.Air enters heat exchange department by air inlet pipe, in heat exchange department, cold air and the hot-air progress heat by drying roller
Amount exchanges, and the temperature rise of cold air, hot air temperature reduces.Because can not be by by the heat in the hot-air of drying roller
Make full use of, so exclusion temperature is higher, therefore this partial heat is recycled by heat exchange department.On the one hand can
The utilization rate of energy is improved, reduces the consumption of electricity, and then reduces the operating cost of the utility model, on the other hand by drying
After the hot air temperature of roller reduces, its moisture can also decline therewith, be more conducive to follow-up condensation, that is, to water
The recycling operation divided.
The efficiency of heating surface higher of the utility model.Heating part is set using multigroup ceramic heating plate order, and heated length is more
Long, the air themperature after heating is also higher, and drying efficiency can also improve therewith.And ceramic heating flake employs wave
Shape designs, and the area that air contacts also increases therewith, can further improve heating effect.
The condensation effect of the utility model is more preferable.Matrix form condensation pin design is employed in condensation part, wet air is connecing
When contacting the tip of condensation pin, hydrone is easier to condense.The meeting during gliding along condensation wire surface of the water droplet of condensation
Droplet in path is taken away in the lump, the surface of condensation pin is exposed rapidly, contact area is vacateed to subsequent condensation.Condense pin
The rate of set at tip is significantly larger than the rate of set on its surface, can accelerate to condense the circulation rate of wire surface, improve condensation
Efficiency.
Air compartment is added above condensation chamber at the same time.Gas by the air compartment of air compartment is divided by partition plate
For two parts, partition plate is recessed to close to the direction of condensation chamber, can accelerate the air velocity of the part.Air is in flowing
During, the temperature of condensation chamber top surface can be reduced, further improves condensation effect.
The utility model can effectively collect the velveteen produced in drying course.Collecting box is located at the lower section of drying outer barrel,
It is connected by trapezoidal air passage with drying outer barrel.After velveteen drops into collecting box, because trapezoidal air passage and the connection of drying outer barrel
Locate it is narrow, it is wide with the junction of collecting box, can effectively prevent the escape of velveteen.And collecting box passes through negative tube and heat-exchanging chamber
Connection, under the pressure of heat-exchanging chamber moving air, forms negative pressure in junction, the air in negative tube is extracted out.It is so logical
A negative pressure state can be formed in collecting box by crossing negative tube, further prevent the escape of velveteen.
Brief description of the drawings
Fig. 1 is the front view of the utility model；
Fig. 2 is the left view of the utility model；
Fig. 3 is the structure diagram of velveteen collecting box；
Wherein：Wherein：1 body, 11 drying outer barrels, 12 drying rollers, power part 13,2 air inlet pipe, 3 exhaust pipes, 41 heating
It is room, 42 ceramic heating plates, 421 supporting racks, 422 ceramic heating flakes, 51 heat-exchanging chambers, 52 plate heat exchangers, 61 condensation chambers, 62 cold
Solidifying pin, 7 air compartments, 71 partition plates, 8 filter screens, 91 collecting boxs, 92 trapezoidal air passages, 93 negative tubes, 94 strainers.
Embodiment
The utility model is further described with reference to Fig. 1-3.
The utility model adopts the following technical solution：
A kind of dryer, including body 1, be located in body 1 drying outer barrel 11, be located at drying outer barrel 11 in drying rolling
Cylinder 12 and the power part 13 being connected with drying roller 12, further include and are located at the heating part at the top of body 1, are located at 1 bottom of body
Heat exchange department, the condensation part for being located at heat exchange department side, the air inlet pipe 2 being located in body 1 and the exhaust pipe 3 being located in body 1；
The heating part includes heating chamber 41 and the ceramic heating plate 42 being located in heating chamber 41；
The ceramic heating plate 42 is evenly arranged along the airflow direction in heating chamber 41；
The heat exchange department includes heat-exchanging chamber 51, the plate heat exchanger 52 being located in heat-exchanging chamber 51；
The condensation part includes condensation chamber 61 and the condensation pin 62 being distributed in condensation chamber 61；
One end of the air inlet pipe 2 and 1 through connection of body, the other end are connected with the input terminal of heat-exchanging chamber 51；
The output terminal of the heat-exchanging chamber 51 is connected with the input terminal of heating chamber 41；
The output terminal of the heating chamber 41 is connected with drying outer barrel 11；
The input terminal of the condensation chamber 61 is connected with drying outer barrel 11；
The output terminal of the condensation chamber 61 is connected with one end of exhaust pipe 3；
The other end of the exhaust pipe 3 and 1 through connection of body.
As further solution：The ceramic heating plate 42 includes supporting rack 421 and is evenly distributed with supporting rack 421
Ceramic heating flake 422；The section of the ceramic heating flake 422 is waveform.
As further solution：Heat exchanger plates in the plate heat exchanger 52 are tablet.
As further solution：The condensation pin 62 is cone；The condensation pin 62 is at the bottom of condensation chamber 61
It is evenly arranged on face.
As further solution：The top surface of the condensation chamber 61 is equipped with air compartment 7；The air compartment 7
Input terminal be connected with air inlet pipe 2, output terminal is connected with the input terminal of heat-exchanging chamber 51.
As further solution：Partition plate 71 is equipped with the air compartment 7；The partition plate 71 is arc panel；Institute
Partition plate 71 is stated to close to the direction of condensation chamber 61 to be recessed.
As further solution：One end of the air inlet pipe 2 and 1 through connection of body is equipped with filter screen 8.
As further solution：Velveteen collector is equipped with the body 1；The velveteen collector includes collecting
Case 91 and the trapezoidal air passage 92 being located on collecting box 91.
As further solution：The upper top surface in the trapezoidal air passage 92 and drying 11 through connection of outer barrel.
As further solution：The velveteen collector further includes the negative tube 93 being connected with collecting box 91 and sets
Strainer 94 in junction；The other end of the negative tube 93 is connected with the input terminal of heat-exchanging chamber 51.
When carrying out drying operation using the utility model, clothing to be dried is placed into drying roller 12, Ran Houjie
Energization source.Power part 13 obtains exporting power after supply of electric power, drives drying roller 12 to rotate, clothing during rotation with
The contact of hot-air is more abundant, can accelerate drying efficiency, and be less prone to fold, additionally it is possible to produces fluffy effect.
Power part 13 is exactly the combination of motor and gear reducer, this is most ripe type of drive, is not repeated herein.
While drying roller 12 rotates, remainder also begins to work.Extraneous cold air enters after filter screen 8
Air inlet pipe 2, filter screen 8 can effectively filter dust in cool ambient air etc., on the one hand prevent it from forming secondary dirt to clothing
Dye, on the other hand can prevent it from falling on ceramic heating flake and either causing accumulated heat or blocking inside plate heat exchanger.Then edge
Air inlet pipe 2 and enter heat-exchanging chamber 51, with carrying out heat by the hot-air of 12 roller of drying roller in plate heat exchanger 52
Exchange.On the one hand the temperature of cold air is improved, reduces heating time and electric quantity consumption, on the other hand reduces the temperature of hot-air,
Prepare for follow-up condensation.
After the completion of heat exchange, air enters heating chamber 41, after several ceramic heating plates 42, its temperature is gradual successively
Rise.The ceramic heating flake 422 of ceramic heating plate 42 uses undulated design, can increase contact surface in a certain distance
Product, improves the efficiency of heating surface.After the completion of heating, hot-air enters drying outer barrel 11.Drying roller 12 is located inside drying outer barrel 11,
Be evenly distributed with aperture on its surface, hot-air passes through aperture and contact with clothing, clothing during being rotated with drying roller 12,
It can be come into full contact with hot-air, its moisture enters in hot-air and discharges therewith.
Hot-air enters heat-exchanging chamber 51 after drying outer barrel 11 is left, conscientious with cool ambient air in heat-exchanging chamber 51
Heat exchange, the part are not being repeated already described above herein.
After the completion of heat exchange, enter in condensation chamber 61, the hydrone in air condenses on condensation pin 62.By condensation
Discharged behind room 61 by exhaust pipe 3.
In the flow process of air, air compartment 7 can be passed through, can be right after the completion of course of work description above
The part is described.Extraneous cold air can initially enter air compartment 7 after air inlet pipe 2, after, by partition plate 71
It is divided into two parts.Partition plate 71 is an arc panel, towards condensation chamber 61 direction be recessed, when cold air respectively from partition plate above with
When lower section is flowed through, by Bernoulli equation it is recognised that the air velocity of the lower section of partition plate 71 can be higher than the top of partition plate 71
Air velocity,, can be indirect because 7 bottom surface of air compartment is contacted with condensation chamber 61 when cold air blows over air 7 bottom surface of compartment
The heat in condensation chamber 61 is taken away, declines its temperature, further improves condensation effect.
Clothing can produce velveteen in drying course, can be in mobile process when velveteen is transferred in drying outer barrel 11
In fallen into by trapezoidal air passage 92 in collecting box 91.Trapezoidal air passage 92 and the junction for drying outer barrel 11 are narrow, with collecting box 91
Junction is wide, can effectively prevent the escape of velveteen.And collecting box 91 is connected by negative tube 93 with heat-exchanging chamber 51, in heat
In switch room 51 under the pressure of moving air, negative pressure can be formed in the junction of the two, the air in negative tube 93 is extracted out,
Negative pressure state is presented in negative tube 93.A negative pressure state so can be formed in collecting box 91 by negative tube 93, into one
Step prevents the escape of velveteen.Strainer 94 can prevent velveteen from entering in negative tube 93.
Finally it should be noted that the above embodiments are merely illustrative of the technical solutions of the present invention, rather than its limitations, although
The present invention is described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that, it still may be used
To modify to the technical solution described in previous embodiment, or equivalent substitution is carried out to which part technical characteristic, and
These modifications are replaced, and the essence of appropriate technical solution is departed from the spirit and model of technical solution of the embodiment of the present invention
Enclose.
Claims (10)
1. a kind of dryer, including body（1）, be located at body（1）Interior drying outer barrel（11）, be located at drying outer barrel（11）Interior
Drying roller（12）With with drying roller（12）The power part of connection（13）, it is characterised in that：Further include and be located at body（1）Top
Heating part, be located at body（1）The heat exchange department of bottom, the condensation part for being located at heat exchange department side, be located at body（1）It is interior into
Tracheae（2）Be located at body（1）Interior exhaust pipe（3）；
The heating part includes heating chamber（41）Be located at heating chamber（41）Interior ceramic heating plate（42）；
The ceramic heating plate（42）Along heating chamber（41）Interior airflow direction is evenly arranged；
The heat exchange department includes heat-exchanging chamber（51）, be located at heat-exchanging chamber（51）Interior plate heat exchanger（52）；
The condensation part includes condensation chamber（61）Be distributed on condensation chamber（61）Interior condensation pin（62）；
The air inlet pipe（2）One end and body（1）Through connection, the other end and heat-exchanging chamber（51）Input terminal connection；
The heat-exchanging chamber（51）Output terminal and heating chamber（41）Input terminal connection；
The heating chamber（41）Output terminal with drying outer barrel（11）Connection；
The condensation chamber（61）Input terminal with drying outer barrel（11）Connection；
The condensation chamber（61）Output terminal and exhaust pipe（3）One end connection；
The exhaust pipe（3）The other end and body（1）Through connection.
A kind of 2. dryer according to claim 1, it is characterised in that：The ceramic heating plate（42）Including supporting rack
（421）With in supporting rack（421）Upper uniformly distributed ceramic heating flake（422）；The ceramic heating flake（422）Section be wave
Shape.
A kind of 3. dryer according to claim 1, it is characterised in that：The plate heat exchanger（52）Interior heat exchanger plates are
Tablet.
A kind of 4. dryer according to claim 1, it is characterised in that：The condensation pin（62）For cone；It is described cold
Solidifying pin（62）In condensation chamber（61）Bottom surface on be evenly arranged.
A kind of 5. dryer according to claim 1, it is characterised in that：The condensation chamber（61）Top surface be equipped with air
Compartment（7）；The air compartment（7）Input terminal and air inlet pipe（2）Connection, output terminal and heat-exchanging chamber（51）Input terminal connect
Connect.
A kind of 6. dryer according to claim 5, it is characterised in that：The air compartment（7）It is interior to be equipped with partition plate（71）；
The partition plate（71）For arc panel；The partition plate（71）To close to condensation chamber（61）Direction depression.
A kind of 7. dryer according to claim 1, it is characterised in that：The air inlet pipe（2）With body（1）Through connection
One end be equipped with filter screen（8）.
A kind of 8. dryer according to claim 1, it is characterised in that：The body（1）It is interior to be equipped with velveteen collector；Institute
Stating velveteen collector includes collecting box（91）Be located at collecting box（91）On trapezoidal air passage（92）.
A kind of 9. dryer according to claim 8, it is characterised in that：The trapezoidal air passage（92）Upper top surface with drying
Outer barrel（11）Through connection.
A kind of 10. dryer according to claim 9, it is characterised in that：The velveteen collector further includes and collecting box
（91）The negative tube of connection（93）With the strainer for being located at junction（94）；The negative tube（93）The other end and heat-exchanging chamber
（51）Input terminal connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721193125.6U CN207313988U (en) | 2017-09-18 | 2017-09-18 | A kind of dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721193125.6U CN207313988U (en) | 2017-09-18 | 2017-09-18 | A kind of dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207313988U true CN207313988U (en) | 2018-05-04 |
Family
ID=62382933
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721193125.6U Expired - Fee Related CN207313988U (en) | 2017-09-18 | 2017-09-18 | A kind of dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207313988U (en) |
-
2017
- 2017-09-18 CN CN201721193125.6U patent/CN207313988U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180504 Termination date: 20210918 |