WO2024045477A1 - 一种衣物处理装置 - Google Patents
一种衣物处理装置 Download PDFInfo
- Publication number
- WO2024045477A1 WO2024045477A1 PCT/CN2023/072564 CN2023072564W WO2024045477A1 WO 2024045477 A1 WO2024045477 A1 WO 2024045477A1 CN 2023072564 W CN2023072564 W CN 2023072564W WO 2024045477 A1 WO2024045477 A1 WO 2024045477A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- moisture absorption
- space
- drum
- moisture
- dehumidification
- Prior art date
Links
- 238000010521 absorption reaction Methods 0.000 claims abstract description 326
- 238000007791 dehumidification Methods 0.000 claims abstract description 159
- 238000011069 regeneration method Methods 0.000 claims abstract description 97
- 230000008929 regeneration Effects 0.000 claims abstract description 95
- 238000001035 drying Methods 0.000 claims abstract description 74
- 238000010438 heat treatment Methods 0.000 claims description 125
- 238000012545 processing Methods 0.000 claims description 21
- 238000005192 partition Methods 0.000 claims description 20
- 238000001514 detection method Methods 0.000 claims description 11
- 230000007423 decrease Effects 0.000 description 11
- 238000003795 desorption Methods 0.000 description 11
- 238000005259 measurement Methods 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 230000000694 effects Effects 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 238000005406 washing Methods 0.000 description 5
- 238000001816 cooling Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- -1 alkali metal aluminosilicate Chemical class 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F25/00—Washing machines with receptacles, e.g. perforated, having a rotary movement, e.g. oscillatory movement, the receptacle serving both for washing and for centrifugally separating water from the laundry and having further drying means, e.g. using hot air
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F58/00—Domestic laundry dryers
- D06F58/20—General details of domestic laundry dryers
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F58/00—Domestic laundry dryers
- D06F58/20—General details of domestic laundry dryers
- D06F58/24—Condensing arrangements
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F58/00—Domestic laundry dryers
- D06F58/20—General details of domestic laundry dryers
- D06F58/26—Heating arrangements, e.g. gas heating equipment
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B40/00—Technologies aiming at improving the efficiency of home appliances, e.g. induction cooking or efficient technologies for refrigerators, freezers or dish washers
Definitions
- the present application relates to the field of household appliances, and in particular, to a clothes processing device.
- the air flow treated by this method still contains a high proportion of moisture, and recycling also requires the air flow to be "heated, cooled, dehumidified, and re-used.” Warming up”, the dehumidification efficiency is low and the power consumption is large.
- the existing drying components can no longer meet the needs of consumers, and it is necessary to propose a new drying structure and improve the structure of the existing clothes processing device.
- the technical problem solved by this application is to provide a clothes processing device with shorter drying time and higher drying efficiency.
- the present application provides a clothes processing device, which is characterized in that it includes: a drum and a drying module; wherein,
- the drum has at least one drum air outlet and one drum air inlet;
- the drying module includes: a shell and a moisture absorption and dehumidification component
- the shell at least includes a first shell and a second shell, and the first shell and the second shell are sealingly matched to form at least a space for accommodating the moisture absorption and drainage member; the moisture absorption and drainage member is in the rotation in space;
- At least two partitions are arranged in the radial direction at corresponding positions of the first shell and the second shell, and the projection of the at least two partitions perpendicular to the rotation direction of the moisture absorption and discharge member On the plane, the space is divided into at least a hygroscopic space and a regeneration space;
- a first hygroscopic space and a second hygroscopic space are respectively formed on both sides of the hygroscopic and moisture-absorbing member;
- the temperature difference between at least part of the first moisture-absorbing space and at least part of the second moisture-absorbing space is between 70°C and 80°C.
- At least part of the surface temperature difference on both sides of the moisture absorption and moisture removal component is between 70-80°C.
- the temperature difference at substantially symmetrical positions of the moisture absorption first space and the moisture absorption second space is between 70-80°C, or the temperature difference between the moisture absorption and dehumidification
- the temperature difference at roughly symmetrical positions on both sides of the component is between 70-80°C.
- At least a first airflow inlet is formed on the first housing, and at least a first airflow outlet is formed on the second housing.
- the first airflow inlet and the first airflow outlet are respectively disposed adjacent to the at least two partitions.
- the moisture absorption and moisture removal component rotates through the regeneration space, the first air flow outlet and the first air flow inlet in sequence, and is in the moisture absorption space and located at the first air flow inlet during at least part of the dehumidification operation period.
- the temperature difference at the location between the air flow outlet and the first air flow inlet is between 70-80°C.
- the drying module includes a heating component, the heating component is disposed in the regeneration space; the heating component fluctuates or operates alternately between the first heating power and the second heating power.
- the first heating power is between 400-800W
- the second heating power is between 1200-1600W.
- the thickness to diameter ratio of the moisture absorption and moisture removal member ranges from 1/80 to 1/4.
- the thickness to diameter ratio of the moisture absorption and moisture removal member ranges from 1/20 to 1/10.
- this application also provides a clothes processing device, which is characterized in that it includes: a drum and a drying module; wherein,
- the drum has at least one drum air outlet and one drum air inlet;
- the drying module includes: a shell and a moisture absorption and dehumidification component
- the shell at least includes a first shell and a second shell, and the first shell and the second shell are sealingly matched to form at least a space for accommodating the moisture absorption and drainage member; the moisture absorption and drainage member is in the rotation in space;
- At least two partitions are arranged in the radial direction at corresponding positions of the first shell and the second shell, and the projection of the at least two partitions perpendicular to the rotation direction of the moisture absorption and discharge member On the plane, the space is divided into at least a hygroscopic space and a regeneration space;
- the first housing is formed with at least a first airflow inlet connected to the air outlet of the drum;
- the second housing is formed with at least a first airflow outlet connected to the air inlet of the drum;
- the air flow temperature at at least one position adjacent to the drum air inlet is a first temperature, and the first temperature is Between 70-80°C.
- the air flow temperature at at least one position of the drum close to the air outlet of the drum is a second air flow temperature, and the second air flow temperature is between 50-60°C.
- At least one air outlet pipe is provided between the first air flow inlet and the drum air outlet, and the air flow temperature at at least one position in the air outlet pipe close to the drum air outlet is the second air flow temperature, The second air flow temperature is between 50-60°C.
- the temperature difference between the first air flow temperature and the second air flow temperature is 25 ⁇ 5°C.
- a first temperature detection unit is provided at a position of the air inlet duct close to the drum air inlet. Yuan; On the drum or the air outlet pipe, a second temperature detection unit is provided close to the air outlet of the drum.
- the drying module includes a heating component, which is disposed in the regeneration space; the heating component fluctuates or operates alternately between the first heating power and the second heating power.
- the first heating power is between 400-800W
- the second heating power is between 1200-1600W.
- the thickness to diameter ratio of the moisture absorption and moisture removal member ranges from 1/80 to 1/4.
- the thickness to diameter ratio of the moisture absorption and moisture removal member ranges from 1/20 to 1/10.
- a circulation fan and a regeneration fan are respectively provided on the air flow path where the moisture absorption space is located and on the air flow path where the regeneration space is located.
- This application limits the working power of the heating component and the ratio of the thickness and diameter of the moisture absorption and dehumidification component within a certain range, so that during at least part of the dehumidification operation period, at least part of the first moisture absorption space and at least part of the second moisture absorption space
- the temperature difference between the two spaces is between 70-80°C.
- this application also limits the working power of the heating component and the ratio of the thickness and diameter of the moisture absorption and dehumidification member within a certain range, so that between the first air flow outlet and the drum air inlet, the distance between the first air flow outlet and the drum air inlet is close to the drum air inlet.
- the first air flow temperature at at least one location is between 70-80°C.
- Figure 1 is a structural diagram of an integrated drying machine according to an optional embodiment of the present application.
- FIG. 2 is a structural diagram of a drying module according to an optional embodiment of the present application.
- Figure 3 is an exploded view of a drying module according to an optional embodiment of the present application.
- Figure 4 is a schematic diagram of the circulation flow direction according to an optional embodiment of the present application.
- the present application provides a clothes treatment device, including a housing 10, a drying module 20 and a drum 30; as shown in Figures 2 and 3, the drying module 20 includes a moisture absorption and dehumidification component 203, Shell 206 and heating module 208; the shell 206 includes a first shell 2061 and a second shell 2062. The first shell 2061 and the second shell 2062 are sealed and matched to form a space for accommodating the moisture absorption and dehumidification component 203.
- the moisture dehumidification member 203 rotates in the space where the first shell 2061 and the second shell 2062 are sealed and matched to accommodate the moisture absorption and dehumidification member 203; at the corresponding positions of the first shell 2061 and the second shell 2062, along the At least two partitions 2063 are arranged approximately radially, and the at least two partitions 2063 separate the space into at least the moisture absorption space 201 and the regeneration space 202 on a projection plane perpendicular to the rotation direction of the moisture absorption and dehumidification member 203; the first shell
- the body 2061 is provided with a first airflow inlet 2011 near the partition
- the second housing 2062 is provided with a first airflow outlet 2012 near another partition.
- the first airflow inlet 2011 and the first airflow outlet 2012 are respectively adjacent to the There are at least two partitions, and both are located in the hygroscopic space 201.
- partitions referred to here refer to each individual partition component connected from the circumferential side wall of the first housing 2061 or the second housing 2062 to the middle position of the housing.
- the intermediate position is not necessarily the central position, so it can be understood that the partition is not necessarily arranged in the radial direction.
- the at least two partitions 2063 can be integrally formed, or can be manufactured and installed separately. This manufacturing method does not affect the definition of the partitions.
- the drum 30 has a drum air inlet and a drum air outlet.
- the first air flow outlet 2012 of the housing 206 and the drum air inlet are connected by the air inlet pipe 40 of the drum 30.
- the drum air outlet is connected to the first air flow outlet of the housing 206.
- the air inlets 2011 are connected by the air outlet pipe 50 of the drum 30 .
- the moisture absorption and dehumidification member 203 is disposed in the moisture absorption space 201 and the regeneration space 202 so that the circulating air flow and the moisture dehumidification air flow flow through the moisture absorption and dehumidification member 203 respectively; the moisture absorption and dehumidification member 203 is used to absorb moisture from the circulating air flow in the moisture absorption space 201 , and discharge the moisture through the dehumidification airflow of the regeneration space 202.
- a first moisture absorption space and a second moisture absorption space are respectively formed on both sides of the moisture absorption and dehumidification member 203.
- the first moisture absorption space is a space with the first airflow humidity flowing in from the drum air outlet
- the second moisture absorption space is After absorbing moisture through the moisture absorption and dehumidification member 203, the space has a second airflow humidity, and the first airflow humidity is greater than the second airflow humidity.
- the moisture absorption and drainage member 203 is rotatably placed in the space formed by the first shell 2061 and the second shell 2062, and at least part of the moisture absorption and drainage member 203 periodically passes through the moisture absorption space 201 and the regeneration space 202.
- a circulation fan 204 is provided on the gas passage where the moisture absorption space 201 is located, so that a circulating air flow is formed in the drum 30 and the moisture absorption space 201 .
- a regeneration fan 205 is provided on the gas passage where the regeneration space 202 is located, so that a dehumidification airflow is formed in the regeneration space 202 .
- a heating module 208 is also provided in the regeneration space 202.
- the heating module 208 includes a cover body 2081 and a heating component 2082 installed on the cover body 2081.
- the heating module 208 is set to Close to the regeneration space and adjacent to the moisture absorption and drainage component.
- a rotating part 207 is also provided, which is connected to the outer edge of the moisture absorption and dehumidification member 203 in a transmission manner.
- a motor is provided inside the rotating part 207, and the motor drives the rotating part 207 to rotate, thereby driving the moisture absorption device that is drivingly connected to the rotating part 207.
- the moisture discharge member 203 rotates relative to the housing 206 .
- the rotation speed is 2-10 revolutions per minute.
- the laundry treatment device may also include, but is not limited to, components such as a controller.
- the gas circulates in the drum 30 and the moisture absorption space 201, so that The clothes in the drum 30 continuously exchange heat with the circulating air flow to take away the remaining moisture in the clothes, thereby achieving the purpose of drying the clothes.
- the operation of the regeneration fan 205 causes an air pressure difference to be formed on both sides of the regeneration fan 205, forming a dehumidification airflow in the regeneration space 202, so that the air from the drum 30 enters the regeneration space 202, flows through the moisture absorption and dehumidification component 203, and The moisture on the moisture absorption and dehumidification member 203 is desorbed, thereby reducing the moisture in the moisture absorption and dehumidification member 203, so that the moisture absorption and dehumidification member 203 can have continuous and high water absorption capacity, and improve the dehumidification efficiency.
- the moisture absorption and moisture removal member 203 dynamically and periodically switches between the moisture absorption space 201 and the regeneration space 202 .
- the part of the moisture absorption and dehumidification component 203 located in the moisture absorption space 201 absorbs water vapor in the circulating air flow, and uses its own high temperature to heat the passing circulating air flow. Then this part rotates to the regeneration space 202, and the heating assembly 2082 heats this part, so that The moisture in this part can be quickly desorbed.
- the moisture absorption and discharge member 203 can continue to absorb moisture and heat the circulating airflow in the moisture absorption space 201, and can also continue to discharge the moisture absorbed by the moisture absorption and discharge member 203, so that The moisture absorption and discharge member 203 always has good water absorption capacity, thereby improving the efficiency of moisture absorption.
- the moisture absorption and dehumidification member 203 can be configured as a disc-shaped structure with a certain thickness, and the ratio of thickness to diameter is 1/80 to 1/4 to adapt to the overall structure of the clothes treatment device; in one embodiment , the thickness to diameter ratio of the moisture absorption and drainage member 203 is 1/20 to 1/10, so as to improve the performance of the moisture absorption and drainage member 203.
- the moisture absorption and dehumidification member 203 can be made of materials with strong water absorption capacity, such as zeolite, alkali metal aluminosilicate, lithium chloride, silica gel, modified silica gel, activated alumina, etc.
- the cover body 2081 is arranged on the regeneration space 202, and the heating component 2082 is installed on the cover body 2081.
- Elements with heating functions such as electric heating wires or PTC heaters can be used; affected by the performance of the moisture absorption and dehumidification component 203 itself, it must be
- the heating temperature of the heating component 2082 is controlled within a certain range, so that the regeneration performance of the moisture absorption and dehumidification component 203 is optimal, and when this part rotates to the moisture absorption space 201, it is also within the range of the optimal moisture absorption temperature; cover body 2081
- the edge of the casing 206 is fixedly connected, so during the rotation of the moisture absorption and dehumidification component 203, the cover 2081 and the heating component 2082 do not rotate accordingly.
- the cover 2081 is as close as possible to the moisture absorption and dehumidification component 203, thereby achieving The moisture absorption and dehumidification member 203 rotates to an area adjacent to the heating component 2082 for
- the heating component 2082 operates alternately between a first heating power and a second heating power, where the first heating power is between 400-800W and the second heating power is between 1200-1600W.
- the first heating power is set between 400 and 800W in order to obtain a higher temperature in the regeneration space 202 to heat the moisture absorption and desorption component 203 and improve the regeneration efficiency of moisture desorption on the moisture absorption and desorption component 203.
- the second heating power is set between 1200 and 1600W to prevent the moisture absorption and dehumidification component 203 from being too hot after passing through the regeneration space 202 and rotating to the moisture absorption space 201 to overheat the circulating air flow, causing the circulating air flow to enter the drum 30 Damaged clothing and excessive temperature of moisture absorption and dehumidification components affect their moisture absorption efficiency; set the working power of the heating component 2082 to run alternately between the first heating power and the second heating power, and adjust the first heating power and the second heating power.
- the range is limited, which can take into account higher regeneration efficiency and control the temperature of the circulating airflow entering the cylinder to prevent damage to the clothes.
- the heating component 2082 operates with fluctuations between the first heating power and the second heating power, such as square waves, sine/cosine waves and other periodic waveforms, wherein the first heating power is between 400-800W. time, the second heating power is between 1200-1600W.
- the startup phase refers to the phase in which the clothes treatment device starts the circulation fan 204, the regeneration fan 205, the motor that drives the moisture absorption and dehumidification component 203 to rotate, the heating component 2082 and other components according to user instructions;
- the dry command controls the circulation fan 204, the regeneration fan 205 and the motor to start running, the heating component 2082 starts to heat up, and the fan speed, heating power and other parameters are in a rapid increase state;
- the dehumidification operation stage means that the circulation fan 204, the regeneration fan 205 and the motor are running stably and heating
- the speed of the moisture absorption and dehumidification component 203 can be set to a fixed value, and the heating component 2082
- the working power alternates between the first heating power of 400-800W and the second heating power of 1200-1600W;
- the cooling stage refers to a stage in which the heating component 2082 stops working and the circulation fan 204, the regeneration fan 205 and the motor continue to operate until the clothes are cooled.
- the controller determines that the clothes have been dried and turns off the heating component. That is, the drying process ends and the cooling stage is entered.
- the circulation fan 204, the regeneration fan 205 and the motor continue to operate, and the drum Clothes within 30 seconds enter the cooling process, and various parameters such as fan speed gradually return to zero.
- the moisture absorption and dehumidification component 203 uses its own water absorption characteristics to absorb moisture in the circulating airflow, absorbing water vapor in the circulating airflow, and the humidity of the circulating airflow is therefore reduced. , at the same time, the latent heat of condensation in the water vapor is released, and the temperature of the circulating air flow increases; on the other hand, after the moisture absorption and dehumidification component 203 rotates from the regeneration space 202 to the moisture absorption space 201, it uses the high temperature it obtains to carry out treatment on the passing circulating air flow.
- Heating the temperature of the circulating air flow increases; in this way, the humidity of the circulating air flow decreases and the temperature increases after passing through the moisture absorption and dehumidification component 203, forming a temperature difference within a certain range between the first moisture absorption space and the second moisture absorption space. .
- the laundry treatment device further includes a controller, and there is an air inlet duct between the first air flow outlet and the drum air inlet, and a first temperature detection unit is provided in the air inlet duct close to the drum air inlet. ; A second temperature detection unit is provided on the drum or on the air outlet pipe close to the air outlet of the drum. Through the temperatures detected by the first temperature detection unit and the second temperature detection unit, the cycle can be controlled respectively by the controller. The power or rotation speed of the fan 204, the regeneration fan 205, and the heating component 2082.
- This application limits the ratio of the thickness to the diameter of the moisture absorption and dehumidification component, the rotation speed of the moisture absorption turntable, and the working power of the heating component within a certain range, thereby ensuring that during at least part of the dehumidification operation phase, the first airflow detected by the first temperature detection unit
- the temperature is approximately between 70-80°C
- the second airflow temperature detected by the second temperature detection unit is approximately between 50-60°C.
- the temperature difference between the first air flow temperature and the second air flow temperature is 25 ⁇ 5°C.
- the inventor found through research that during at least a partial dehumidification operation stage, when the temperature difference between the first moisture absorption space and the second moisture absorption space in the moisture absorption space 201 is stabilized in the range of 70-80°C for drying, the clothes treatment device It can achieve good drying effect, and the feel and dryness of the washed clothes at this temperature are satisfactory.
- the temperature difference of at least part of the surfaces on both sides of the moisture absorption and dehumidification component 203 is between 70°C and 80°C.
- the temperature difference at the approximately symmetrical positions of the first moisture-absorbing space and the second moisture-absorbing space is between 70-80°C, or the temperature difference on both sides of the moisture-absorbing and moisture-absorbing member 203 is The temperature difference at roughly symmetrical positions is between 70-80°C.
- the moisture absorption and dehumidification component 203 rotates through the regeneration space 202, the first air flow outlet 2012 and the first air flow inlet 2011 in order, and is in the moisture absorption space 201 and located at the first air flow outlet 2012 during at least part of the dehumidification operation period.
- the temperature difference between the first air flow inlet 2011 and the first air flow inlet 2011 is between 70-80°C.
- the weight of the laundry is about 4Kg
- the ratio of the thickness to the diameter of the moisture absorption and drainage member 203 is roughly between 1/20 and 1/10
- the rotation speed of the moisture absorption and drainage member 203 is 2-10 rpm
- the heating component 2082 In the dehumidification operation stage, the first heating power is about 400-800W, and the second heating power is about 1200-1600W.
- the detection point of the temperature difference can be set at a substantially symmetrical position between the first moisture absorption space and the second moisture absorption space, or at a substantially symmetrical position on both sides of the moisture absorption and dehumidification member 203, or it can also be set at a position between the first airflow outlet 2012 and the first moisture absorption and desorption component 203.
- the regeneration performance and moisture absorption performance of the moisture absorption and drainage component 203 itself are affected by the heating temperature. If the temperature is higher or lower than the optimal regeneration temperature range, the regeneration performance of the moisture absorption and moisture removal component 203 will be reduced. At the same time, After this part of the moisture absorption and desorption component 203 rotates to the moisture absorption space 201, it will also be higher or lower than the optimal moisture absorption temperature range, causing the moisture absorption performance of the moisture absorption and desorption component 203 to also decrease, thereby affecting the final drying efficiency of the clothes.
- Experimental measurements show that during the dehumidification operation stage, the actual temperature difference between the first moisture absorption space and the second moisture absorption space roughly varies within the range of 72.7-77.9°C. At this time, the drying time is approximately 128 minutes.
- the rotation speed of the moisture absorption and dehumidification component 203 is slower than in the first embodiment, and the heating time when passing through the regeneration space 202 is longer, the temperature of the part of the moisture absorption and dehumidification component 203 that passes through the regeneration space 202 is still basically optimal.
- the moisture absorption efficiency of the moisture absorption and desorption member 203 will not be greatly affected.
- the actual temperature difference between the first moisture absorption space and the second moisture absorption space roughly varied within the range of 72.9-78.6°C. At this time, the drying time was approximately 130 minutes.
- the moisture absorption and desorption component 203 rotates faster. Due to the increase in rotation speed, the moisture cannot be fully desorbed in the regeneration space, causing a certain loss in moisture absorption efficiency after the moisture absorption and desorption component 203 rotates to the moisture absorption space 201.
- the heating time in the space 202 is shorter, and the heating efficiency of the circulating air flow is also lost after rotating to the moisture absorption space 201, but the above efficiency loss is still within the acceptable range.
- the actual temperature difference between the first moisture absorption space and the second moisture absorption space roughly varied within the range of 70.3-76.2°C. At this time, the drying time was approximately 133 minutes.
- the heating temperature of the moisture absorption and dehumidification component 203 is lower when passing through the regeneration space 202, but it is still within the optimal regeneration temperature range, and when the moisture absorption and dehumidification component 203 rotates to the moisture absorption space 201 to absorb moisture, it is still at the optimal moisture absorption temperature.
- the heating efficiency of the circulating air flow decreases due to the temperature drop of the moisture absorption and dehumidification component 203 after passing through the moisture absorption space 201, but the circulation The temperature of the air flow is still controlled within the preset range, which has an impact on the final drying efficiency. The sound is smaller.
- the heating temperature of the moisture absorption and dehumidification component 203 is higher when passing through the regeneration space 202, but it is still within the optimal regeneration temperature range.
- the moisture absorption and dehumidification component 203 rotates to the moisture absorption space 201 to absorb moisture, it is still at the optimal moisture absorption temperature.
- the size of the moisture absorption and dehumidification component 203 increases, but the heating power remains unchanged.
- the moisture absorption and dehumidification component 203 passes through the regeneration space 202, the temperature rise will be lower than that in the first embodiment, but it is still within the optimal regeneration temperature range.
- the moisture component 203 rotates to the moisture absorption space 201 to absorb moisture, it is still within the optimal moisture absorption temperature range.
- the moisture absorption efficiency is due to moisture absorption and dehumidification.
- the increase in the size of the component 203 substantially offsets the impact on the drying efficiency due to the reduction in the heating efficiency of the circulating air flow.
- the size of the moisture absorption and dehumidification component 203 is reduced, but the heating power remains unchanged.
- the moisture absorption and dehumidification component 203 passes through the regeneration space 202, the temperature rise will be higher than that in the first embodiment, but it is still within the optimal regeneration temperature range.
- the moisture component 203 rotates to the moisture absorption space 201 to absorb moisture, it is still within the optimal moisture absorption temperature range.
- the moisture absorption efficiency is due to moisture absorption and dehumidification.
- the size of the component 203 is reduced, which is related to the impact on the drying efficiency due to the increase in the heating efficiency of the circulating air flow. Basically offset.
- the comparative example of this application changes the thickness-to-diameter ratio, rotation speed, and heating efficiency of the heating component 2082 of the moisture absorption and desorption component 203 outside the selected range, so that the regeneration temperature of the moisture absorption and desorption component 203 in the regeneration space 202 increases or decreases. Beyond the optimal regeneration temperature range, the regeneration performance of the moisture absorption and dehumidification component 203 itself decreases. At the same time, after this part of the moisture absorption and dehumidification component 203 rotates into the moisture absorption space 201, the moisture absorption performance also decreases, thus affecting the final treatment. Clothes drying efficiency.
- the heating efficiency of the circulating air flow also changes greatly due to the temperature increase or decrease of the moisture absorption and dehumidification component 203 in the moisture absorption space 201, thus affecting the final drying effect of the clothes.
- the following comparative examples 1 to 6 all adjust relevant parameters outside the limited range, so as to have a greater impact on the regeneration efficiency, moisture absorption efficiency and heating efficiency of the circulating air flow of the moisture absorption and dehumidification component 203, thereby absorbing moisture during the dehumidification operation stage.
- the temperature difference between the first moisture-absorbing space and the second moisture-absorbing space in space 201 cannot be maintained within the range of 70-80°C. At this time, the drying time of the clothes is longer and the drying effect is not good. In some cases, it may cause damage. Clothing.
- the regeneration efficiency and moisture absorption efficiency of the moisture absorption and dehumidification component 203 itself are reduced.
- the heating efficiency of the moisture absorption and dehumidification component 203 for the passing circulating air flow is also affected by the moisture absorption space 201. As the temperature rises, the heated circulating airflow entering the drum 30 may damage the clothes due to excessive temperature. In this case, the dehumidification of the circulating airflow is insufficient and the heating is too sufficient.
- the first space for moisture absorption and the second space for moisture absorption are The temperature difference between the two spaces will be higher than 70-80°C, and the drying time will become longer; through experimental measurements, during the dehumidification operation stage, the actual temperature difference between the first moisture-absorbing space and the second moisture-absorbing space is approximately 83.5-90.9°C, and the drying time will be longer. About 162min.
- the heating efficiency of the moisture absorption and dehumidification component 203 for the passing circulating air flow is also reduced due to the temperature of the moisture absorption space 201 In this case, the dehumidification and heating of the circulating air flow are insufficient, the temperature difference between the first hygroscopic space and the second hygroscopic space will be lower than the range of 70-80°C, and the drying time will become longer; measured through experiments , during the dehumidification operation stage, the actual temperature difference between the first moisture absorption space and the second moisture absorption space is approximately 66.6-72.5°C, and the drying time is approximately 169 minutes.
- the heating temperature is low, causing the temperature of the moisture absorption and dehumidification component 203 in the regeneration space 202 to be lower than the optimal regeneration temperature range, and the moisture absorption and dehumidification component 203 rotates to the moisture absorption space 201.
- the moisture absorption and dehumidification component 203 does not fully dehumidify and heat the circulating air flow, the temperature difference between the first moisture absorption space and the second moisture absorption space will be lower than the range of 70-80°C, and the drying time will become longer; measured through experiments , during the dehumidification operation stage, the actual temperature difference between the first moisture absorption space and the second moisture absorption space is approximately 66.5-72.3°C, and the drying time is approximately 168 minutes.
- the heating temperature is relatively high, causing the temperature of the moisture absorption and dehumidification component 203 in the regeneration space 202 to be higher than the optimal regeneration temperature range, and the moisture absorption and dehumidification component 203 rotates to the part behind the moisture absorption space 201.
- the regeneration efficiency and moisture absorption efficiency of the moisture absorption and dehumidification component 203 itself are reduced.
- the heating efficiency of the circulating air flow is increased due to the increase in the temperature of the moisture absorption space 201.
- the temperature difference between the first moisture absorption space and the second moisture absorption space will be higher than 70-80°C, and the drying The drying time will become longer, and due to the higher operating power of the clothing treatment device, it will consume more power.
- the actual temperature difference between the first moisture absorption space and the second moisture absorption space is approximately 79.6-92.8°C. Drying time is about 171min.
- the rotation speed of the moisture absorption and moisture removal member 203 is set to 5 rpm
- the working power of the heating component 2082 is the minimum power of 600W and the maximum power of 1400W
- the size of the moisture absorption and dehumidification component 203 increases while the heating power remains unchanged.
- the temperature of the moisture absorption and dehumidification component 203 increases less when passing through the regeneration space 202, causing the temperature of the moisture absorption and dehumidification component 203 in the regeneration space 202 to be lower than the optimal regeneration temperature range.
- the moisture absorption and dehumidification component 203 rotates to the moisture absorption space 201 to absorb moisture, it will also be lower than the optimal moisture absorption temperature range, and the regeneration efficiency and moisture absorption efficiency of the moisture absorption and dehumidification component 203 itself are reduced.
- the heating efficiency of the circulating air flow Because the temperature of the moisture absorption space 201 decreases, in this case, the moisture absorption and dehumidification component 203 does not fully dehumidify and heat the circulating air flow, and the temperature difference between the first moisture absorption space and the second moisture absorption space will be lower than the range of 70-80°C. , the drying time will become longer; through experimental measurement, during the dehumidification operation stage, the actual temperature difference between the first moisture absorption space and the second moisture absorption space is roughly 75.1-82.9°C, drying time is about 155min.
- the rotation speed of the moisture absorption and moisture removal member 203 is set to 5 rpm
- the working power of the heating component 2082 is the minimum power of 600W and the maximum power of 1400W
- the size of the moisture absorption and dehumidification component 203 is reduced, but the heating power remains unchanged.
- the moisture absorption and dehumidification component 203 heats up more when passing through the regeneration space 202, causing the temperature of the moisture absorption and dehumidification component 203 in the regeneration space 202 to be higher than the optimal regeneration temperature range.
- the moisture absorption and discharge member 203 rotates to the moisture absorption space 201 to absorb moisture, it is still higher than the optimal moisture absorption temperature range.
- the regeneration efficiency and moisture absorption efficiency of the moisture absorption and discharge member 203 itself are reduced, and the moisture absorption efficiency is due to the moisture absorption and discharge member 203.
- the size is further reduced due to the reduction in size.
- the heating efficiency of the circulating air flow is improved due to the increase in the temperature of the moisture absorption space 201.
- the clothes are easily damaged due to excessive temperature; in this case, , the dehumidification of the circulating air flow is insufficient and the heating is too sufficient, the temperature difference between the first moisture absorption space and the second moisture absorption space will be higher than 70-80°C, and the drying time will become longer; through experimental measurements, during the main dehumidification operation stage, the moisture absorption
- the actual temperature difference between the first space and the second hygroscopic space is approximately 77.1-89.6°C, and the drying time is approximately 159 minutes.
- optimal regeneration temperature and optimal moisture absorption temperature described in the above embodiments are only the highest moisture absorption and regeneration efficiency at this temperature, and do not mean that regeneration and moisture absorption are impossible outside this temperature range.
- the present application provides a clothes processing device, which ensures that at least part of the moisture absorption first space and at least part of the first space are separated by limiting the structural parameters of the moisture absorption and dehumidification component in the drying module and the effective working power of the heating component.
- the temperature difference in the second hygroscopic space is between 70-80°C.
- the temperature of the first air flow at at least one position adjacent to the air inlet of the drum is approximately between 70 and 80°C.
- the present application also provides a clothes processing device, which uses the structure of the moisture absorption and dehumidification component in the drying module.
- the parameters and the effective working power of the heating component are defined so that the second airflow temperature at at least one position of the drum close to the air outlet of the drum is approximately between 50-60°C, and the temperature difference between the first airflow temperature and the second airflow temperature is is 25 ⁇ 5°C.
Abstract
一种衣物处理装置，包括：滚筒（30）以及烘干模组（20）；其中，滚筒至少具有一滚筒出气口和一滚筒进气口；烘干模组包括：壳体（206）、吸湿排湿构件（203）；壳体至少包括第一壳体（2061）和第二壳体（2062），吸湿排湿构件在第一壳体和第二壳体密封配合形成的空间内旋转；空间分隔为至少吸湿空间（201）和再生空间（202）；在吸湿空间的吸湿排湿构件的两侧分别形成吸湿第一空间和吸湿第二空间，至少部分除湿运行时间段，至少部分吸湿第一空间与至少部分吸湿第二空间的温差在70-80℃之间。该衣物处理装置满足了更高效和更便捷地处理衣物的需求，且不会损伤衣物。
Description
相关申请的交叉引用
本申请要求于2022年08月31日提交的中国专利申请202211060628.1和202211057592.1的优先权，其全部内容通过引用整体结合在本申请中。
本申请涉及家用电器领域，尤其涉及一种衣物处理装置。
随着人们生活水平的提高，更高效和更便捷地处理衣物成为越来越多消费者的需求。洗烘一体全自动洗衣机可在洗涤结束后直接对衣物烘干处理，而无需将衣物进行长时间的晾晒，这一功能尤其适用于潮湿、阴雨天气，因此越来越受到消费者的青睐。
现有的衣物处理装置的烘干系统大多数都是利用蒸发器对洗烘机内筒的潮湿空气进行加热吸湿，得到高温空气之后，再重新进入洗烘机内筒，从而使衣物中的水分得以蒸发。但是，蒸发器的整体温度一致，在潮湿空气蒸发的过程中，蒸发器对潮湿空气的吸湿能力下降，导致吸湿效率低、烘干时间长，功耗高。此外，也有部分采用冷凝水喷淋或冷凝器直接对湿气流除湿的方式，但该方式处理过的气流仍然含有很高比例的水分，且循环利用还需要对气流进行“升温-降温除湿-再升温”，除湿效率较低，功耗较大。
因此，现有的烘干组件已经不能满足消费者的需求，有必要提出新的烘干结构，并对现有衣物处理装置的结构加以改进。
发明内容
本申请解决的技术问题是提供一种烘干时间更短、烘干效率更高的衣物处理装置。
在发明内容部分中引入了一系列简化形式的概念，这将在具体实施方式部分中进一步详细说明。本申请的发明内容部分并不意味着要试图限定出所要求保护的技术方案的关键特征和必要技术特征，更不意味着试图确
定所要求保护的技术方案的保护范围。
为解决上述技术问题，本申请提供一种衣物处理装置，其特征在于，包括：滚筒以及烘干模组；其中，
所述滚筒至少具有一滚筒出气口和一滚筒进气口；
所述烘干模组包括：壳体、吸湿排湿构件；
所述壳体至少包括第一壳体和第二壳体，所述第一壳体和第二壳体密封配合至少形成容纳所述吸湿排湿构件的空间；所述吸湿排湿构件在所述空间内旋转；
在所述第一壳体和所述第二壳体的对应位置处分别沿径向设置有至少两个分隔件，所述至少两个分隔件在垂直于所述吸湿排湿构件旋转方向的投影平面上，将所述空间分隔为至少吸湿空间和再生空间；
在所述吸湿空间，所述吸湿排湿构件的两侧分别形成吸湿第一空间和吸湿第二空间；
在至少部分除湿运行时间段，至少部分所述吸湿第一空间与至少部分所述吸湿第二空间的温差在70-80℃之间。
在一个实施例中，在至少部分除湿运行时间段，在所述吸湿空间，所述吸湿排湿构件的两侧至少部分表面温差在70-80℃之间。
在一个实施例中，在至少部分除湿运行时间段，在所述吸湿第一空间与所述吸湿第二空间的大致对称位置处的温差在70-80℃之间，或在所述吸湿排湿构件两侧表面的大致对称位置处的温差在70-80℃之间。
在一个实施例中，所述第一壳体上至少形成有第一气流入口，所述第二壳体上至少形成有第一气流出口，所述第一气流入口和所述第一气流出口分别临近所述至少两个分隔件设置。
在一个实施例中，所述吸湿排湿构件旋转依次经过再生空间、所述第一气流出口以及所述第一气流入口，在至少部分除湿运行时间段，在所述吸湿空间且在位于第一气流出口和第一气流入口之间的位置处的温差在70-80℃之间。
在一个实施例中，所述烘干模组包括加热组件，所述加热组件设置于所述再生空间；所述加热组件在第一加热功率和第二加热功率之间波动运行或交替运行。
在一个实施例中，所述第一加热功率在400-800W之间，所述第二加热功率在1200-1600W之间。
在一个实施例中，所述吸湿排湿构件的厚度与直径比的范围在1/80～1/4之间。
在一个实施例中，所述吸湿排湿构件的厚度与直径比的范围在1/20～1/10之间。
此外，本申请还提供一种衣物处理装置，其特征在于，包括：滚筒以及烘干模组；其中，
所述滚筒至少具有一滚筒出气口和一滚筒进气口；
所述烘干模组包括：壳体、吸湿排湿构件；
所述壳体至少包括第一壳体和第二壳体，所述第一壳体和第二壳体密封配合至少形成容纳所述吸湿排湿构件的空间；所述吸湿排湿构件在所述空间内旋转；
在所述第一壳体和所述第二壳体的对应位置处分别沿径向设置有至少两个分隔件，所述至少两个分隔件在垂直于所述吸湿排湿构件旋转方向的投影平面上，将所述空间分隔为至少吸湿空间和再生空间；
所述第一壳体上至少形成有与所述滚筒出气口连通的第一气流入口；所述第二壳体上至少形成有与所述滚筒进气口连通的第一气流出口；
在至少部分除湿运行时间段，在所述第一气流出口和所述滚筒进气口之间，临近所述滚筒进气口的至少一个位置的气流温度为第一温度，所述第一温度在70-80℃之间。
在一个实施例中，在滚筒靠近所述滚筒出气口处的至少一个位置的气流温度为第二气流温度，所述第二气流温度在50-60℃之间。
在一个实施例中，在所述第一气流入口与滚筒出气口之间至少设置有一出气管道，所述出气管道内靠近所述滚筒出气口处的至少一个位置的气流温度为第二气流温度，所述第二气流温度在50-60℃之间。
在一个实施例中，所述第一气流温度和所述第二气流温度的温差为25±5℃。
在一个实施例中，在所述第一气流出口和所述滚筒进气口之间有进气管道，在所述进气管道靠近所述滚筒进气口的位置设置有第一温度检测单
元；在所述滚筒上或所述出气管道上，靠近所述滚筒出气口的位置设置有第二温度检测单元。
在一个实施例中，所述烘干模组包括加热组件，所述加热组件设置于所述再生空间；所述加热组件在第一加热功率和第二加热功率之间波动运行或交替运行。
在一个实施例中，所述第一加热功率在400-800W之间，所述第二加热功率在1200-1600W之间。
在一个实施例中，所述吸湿排湿构件的厚度与直径比的范围在1/80～1/4之间。
在一个实施例中，所述吸湿排湿构件的厚度与直径比的范围在1/20～1/10之间。
在一个实施例中，所述吸湿空间所在的气流通路上以及所述再生空间所在的气流通路上分别设置有循环风机以及再生风机。
本申请通过将加热组件的工作功率以及吸湿排湿构件的厚度与直径比限定在一定范围之内，使得在至少部分除湿运行时间段，至少部分所述吸湿第一空间与至少部分所述吸湿第二空间的温差在70-80℃之间。通过将两个空间的温差限定在一定温度范围内，衣物处理装置的烘干时间将有效缩短，烘干效率提高，且不会损伤衣物，满足了更高效和更便捷地处理衣物的需求。
此外，本申请还通过将加热组件的工作功率以及吸湿排湿构件的厚度与直径比限定在一定范围之内，使得在第一气流出口和滚筒进气口之间，临近所述滚筒进气口的至少一个位置的第一气流温度在70-80℃之间。通过将第一气流温度限定在一定温度范围内，既能够节约功耗，又能实现更好的烘干效果，且在该温度下洗涤好的衣物手感以及干燥程度均令人满意。
根据在下文中所描述的实施例，本公开的这些和其它方面将是清楚明白的，并且将参考在下文中所描述的实施例而被阐明。
本申请的下列附图在此作为本申请实施例的一部分用于理解本申请。附图中示出了本申请的实施例及其描述，用来解释本申请的原理。
附图中：
图1为根据本申请的一个可选实施例的烘干一体机结构图；
图2为根据本申请的一个可选实施例的烘干模组的结构图；
图3为根据本申请的一个可选实施例的烘干模组的爆炸图；
图4为根据本申请的一个可选实施例的循环气流流向的示意图；
附图标记说明：
10-外壳，20-烘干模组，201-吸湿空间，2011-第一气流入口，2012-第一气流出口，202-再生空间，203-吸湿排湿构件，204-循环风机，205-再生风机，206-壳体，2061-第一壳体，2062-第二壳体，2063-分隔件，207-转动部，208-加热模组，2081-罩体，2082-加热组件，30-滚筒，40-出气管道，50-进气管道。
在下文的描述中，给出了大量具体的细节以便提供对本申请更为彻底的理解。然而，对于本领域技术人员而言显而易见的是，本申请可以无需一个或多个这些细节而得以实施。在其他的例子中，为了避免与本申请发生混淆，对于本领域公知的一些技术特征未进行描述。
应予以注意的是，这里所使用的术语仅是为了描述具体实施例，而非意图限制根据本申请的示例性实施例。如在这里所使用的，除非上下文另外明确指出，否则单数形式也意图包括复数形式。此外，还应当理解的是，当在本说明书中使用术语“包含”和/或“包括”时，其指明存在特征、整体、步骤、操作、元件和/或组件，但不排除存在或附加一个或多个其他特征、整体、步骤、操作、元件、组件和/或它们的组合。
现在，将参照附图更详细地描述根据本申请的示例性实施例。然而，这些示例性实施例可以多种不同的形式来实施，并且不应当被解释为只限于这里所阐述的实施例。应当理解的是，提供这些实施例是为了使得本申请的公开彻底且完整，并且将这些示例性实施例的构思充分传达给本领域普通技术人员。
如图1所示，本申请提供了一种衣物处理装置，包括外壳10、烘干模组20和滚筒30；如图2和图3所示，烘干模组20包括吸湿排湿构件203、壳体206、加热模组208；壳体206包括第一壳体2061和第二壳体2062，第一壳体2061和第二壳体2062密封配合形成容置吸湿排湿构件203的空间。吸
湿排湿构件203在第一壳体2061和第二壳体2062密封配合形成容置吸湿排湿构件203的空间内旋转；在第一壳体2061和第二壳体2062的对应位置处分别沿大致径向设置有至少两个分隔件2063，该至少两个分隔件2063在垂直于吸湿排湿构件203旋转方向的投影平面上，将空间分隔为至少吸湿空间201和再生空间202；第一壳体2061在靠近分隔件处设置有第一气流入口2011，第二壳体2062在靠近另一个分隔件处设置有第一气流出口2012，第一气流入口2011和第一气流出口2012分别临近所述至少两个分隔件，且均位于吸湿空间空间201内。
需要说明的是，这里所指的分隔件是指从第一壳体2061或第二壳体2062环周侧壁向壳体中间位置之间连接设置的每个单独分隔组件，需要说明的是该中间位置并非一定是中心位置，因此可以理解的是：该分隔件并不一定是沿径向方向设置的。该至少两个分隔件2063两者可以一体成型，也可以分别制造安装，该制造方式不影响分隔件的定义。
滚筒30具有滚筒进气口和滚筒出气口，在壳体206的第一气流出口2012与滚筒进气口之间由滚筒30的进气管道40连通，在滚筒出气口与壳体206的第一气流入口2011之间由滚筒30的出气管道50连通。
吸湿排湿构件203设置在吸湿空间201及再生空间202内，以使循环气流及排湿气流分别流经吸湿排湿构件203；吸湿排湿构件203用于吸收吸湿空间201内的循环气流的水分，以及将水分通过再生空间202的排湿气流排出。在吸湿空间201，吸湿排湿构件203的两侧分别形成吸湿第一空间和吸湿第二空间，其中吸湿第一空间为从滚筒出气口流入的具有第一气流湿度的空间，吸湿第二空间为经吸湿排湿构件203吸湿后具有第二气流湿度的空间，该第一气流湿度大于第二气流湿度。吸湿排湿构件203可旋转地置于第一壳体2061和第二壳体2062所形成的空间，吸湿排湿构件203上的至少部分区域周期性地经过吸湿空间201和再生空间202。
在一个实施例中，吸湿空间201所在的气体通路上设有循环风机204，以使滚筒30与吸湿空间201内形成循环气流。再生空间202所在的气体通路上设有再生风机205，以使再生空间202内形成排湿气流。
在一个实施例中，在再生空间202还设置有加热模组208，加热模组208包括罩体2081以及罩体2081上安装的加热组件2082。加热模组208设置为
靠近所述再生空间，且临近所述吸湿排湿构件。
除此以外，还设置有转动部207，与吸湿排湿构件203的外侧边缘以传动方式连接，转动部207内部设有电机，电机驱动转动部207旋转，进而带动与转动部207传动连接的吸湿排湿构件203相对于壳体206转动。一个实施例中，该转速为每分钟2-10转。在具体应用中，衣物处理装置还可以包括但不限于控制器等部件。
如图4中的箭头所示，在循环风机204运转的过程中，循环风机204的两侧形成气压差，在滚筒30与吸湿空间201之间形成循环气流，使滚筒30内的潮湿空气经过出气管道50由吸湿空间201的第一气流入口2011进入到吸湿空间201内，通过吸湿排湿构件203时，循环气流的水蒸气被吸收，转盘自身的高温对循环气流进行加热，循环气流湿度降低，温度升高，然后将处理后的高温干燥空气由吸湿空间201的第一气流出口2012经过进气管道40排放至滚筒30内，如此一来，气体在滚筒30与吸湿空间201内循环流动，使滚筒30内的衣物与循环气流不断地进行热交换，以带走衣物中残留的水分，从而达到了烘干衣物的目的。与此同时，再生风机205的运转使再生风机205两侧形成气压差，在再生空间202内形成排湿气流，使得来自滚筒30的空气进入到再生空间202内，流经吸湿排湿构件203并脱附吸湿排湿构件203上的水分，从而降低吸湿排湿构件203的水分，使吸湿排湿构件203能够具有持续的、较高的吸水能力，提高除湿效率。
在烘干过程中，由于吸湿排湿构件203持续旋转，吸湿排湿构件203的至少部分在吸湿空间201与再生空间202之间动态、周期性切换。吸湿排湿构件203位于吸湿空间201的部分吸收循环气流中的水蒸气，并利用自身高温对通过的循环气流进行加热，然后该部分旋转至再生空间202，加热组件2082对该部分进行加热，使该部分的水分能够快速脱附。由此在吸湿排湿构件203转动的过程中，吸湿排湿构件203能够持续对吸湿空间201内的循环气流进行吸湿和加热，并且也能持续将吸湿排湿构件203吸收的水分排出，而使吸湿排湿构件203一直具有良好的吸水能力，从而提高了吸湿的效率。
在本实施例中，吸湿排湿构件203可设置为具有一定厚度的圆盘状结构，厚度与直径比为1/80～1/4，以适应衣物处理装置的整机结构；一个实施例中，吸湿排湿构件203的厚度与直径比为1/20～1/10，以提高吸湿排湿构件203的
吸湿效率。吸湿排湿构件203可采用具有较强吸水能力的材料，可为沸石、碱金属硅铝酸盐、氯化锂、硅胶、改性硅胶和活性氧化铝等。
具体地，罩体2081设置在再生空间202上，加热组件2082安装在罩体2081上，可采用电热丝或者PTC加热器等具有加热功能的元件；受到吸湿排湿构件203本身性能的影响，须控制加热组件2082的加热温度在一定范围之内，使得吸湿排湿构件203的再生性能最佳，且当该部分旋转至吸湿空间201时，也处于最佳吸湿温度的范围之内；罩体2081的边缘与壳体206固定连接，因此在吸湿排湿构件203转动的过程中，罩体2081及加热组件2082并不随之旋转，同时罩体2081尽可能地靠近吸湿排湿构件203，从而实现对吸湿排湿构件203旋转至加热组件2082临近的区域进行加热。
一个实施例中，加热组件2082在第一加热功率和第二加热功率之间交替运行，其中，第一加热功率在400-800W之间，第二加热功率在1200-1600W之间。一方面，设置第一加热功率在400-800W之间，是为了在再生空间202内获得较高的温度对吸湿排湿构件203加热，提高吸湿排湿构件203上水分脱附的再生效率，另一方面，设置第二加热功率在1200-1600W之间，是为了防止吸湿排湿构件203经过再生空间202后的温度过高，旋转至吸湿空间201对循环气流加热过度，使得循环气流进入滚筒30后损伤衣物以及吸湿排湿构件温度过高影响其吸湿效率；设置加热组件2082的工作功率在第一加热功率和第二加热功率之间交替运行，并对第一加热功率和第二加热功率的范围进行限定，能够兼顾更高的再生效率和控制循环气流进筒时的温度，防止损伤衣物。在另一个实施例中，该加热组件2082在第一加热功率和第二加热功率之间波动运行，例如方波、正弦/余弦波等周期性波形，其中，第一加热功率在400-800W之间，第二加热功率在1200-1600W之间。
在本申请中，将整个烘干过程分为启动阶段、除湿运行阶段以及冷却阶段三个阶段。启动阶段是指衣物处理装置根据用户指令启动循环风机204、再生风机205、驱动吸湿排湿构件203转动的电机、加热组件2082等各项部件的阶段；在启动阶段，控制器根据用户输入的烘干指令，控制循环风机204、再生风机205及电机开始运转，加热组件2082开始加热升温，风机转速、加热功率等各项参数处于快速上升状态；
除湿运行阶段是指循环风机204、再生风机205及电机运转稳定且加热
组件2082在有效功率范围内工作的阶段；进入除湿运行阶段后，风机转速、加热功率等各项参数的变化趋于稳定，吸湿排湿构件203的转速可以设定为一固定值，加热组件2082的工作功率在400-800W的第一加热功率和1200-1600W的第二加热功率之间交替变化；
冷却阶段是指加热组件2082停止工作，循环风机204、再生风机205以及电机继续运行至衣物冷却的阶段。当检测到出筒温度的变化出现拐点时，控制器据此判断衣物已完成烘干，关闭加热组件，即烘干过程结束、进入冷却阶段，循环风机204、再生风机205及电机继续运转，滚筒30内的衣物进入降温过程，风机转速等各项参数逐渐归零。
在除湿运行阶段，循环气流在通过吸湿排湿构件203时，一方面，吸湿排湿构件203利用自身的吸水特性对循环气流进行吸湿处理，吸收循环气流中的水蒸气，循环气流的湿度因此降低，同时水蒸气中的冷凝潜热被释放，循环气流的温度因此升高；另一方面，吸湿排湿构件203从再生空间202旋转至吸湿空间201后，利用自身获得的高温对通过的循环气流进行加热，循环气流的温度因此升高；如此一来，循环气流在通过吸湿排湿构件203后湿度降低、温度升高，在吸湿第一空间和吸湿第二空间之间形成一定范围内的温度差。
在一个实施例中，衣物处理装置还包括控制器，并在第一气流出口和滚筒进气口之间有进气管道，在进气管道靠近滚筒进气口的位置设置有第一温度检测单元；在滚筒上、或出气管道上，靠近滚筒出气口的位置设置有第二温度检测单元，通过该第一温度检测单元以及第二温度检测单元所检测的温度，能够通过控制器分别控制该循环风机204、再生风机205、加热组件2082的功率或转速。
本申请通过将吸湿排湿构件的厚度与直径比、吸湿转盘的转速以及加热组件的工作功率限制在一定范围之内，保证了在至少部分除湿运行阶段，第一温度检测单元检测的第一气流温度大致在70-80℃之间，第二温度检测单元检测的第二气流温度大致在50-60℃之间。一个实施例中，第一气流温度和所述第二气流温度的温差为25±5℃。通过将该第一气流温度以及第二气流温度设定为该温度范围内，既能够节约功耗，并能实现更好的烘干效果，且在该温度下洗涤好的衣物手感以及干燥程度均令人满意。
此外，发明人经过研究发现，在至少部分除湿运行阶段，当吸湿空间201内的吸湿第一空间和吸湿第二空间的温差稳定在70-80℃的范围内进行烘干时，该衣物处理装置能够实现良好的烘干效果，且在该温度下洗涤好的衣物手感以及干燥程度均令人满意。
在一个实施例中，在至少部分除湿运行时间段，在吸湿空间201，吸湿排湿构件203的两侧至少部分表面温差在70-80℃之间。
在一个实施例中，在至少部分除湿运行时间段，在吸湿第一空间与吸湿第二空间的大致对称位置处的温差在70-80℃之间，或在吸湿排湿构件203两侧表面的大致对称位置处的温差在70-80℃之间。
在一个实施例中，吸湿排湿构件203旋转依次经过再生空间202、第一气流出口2012以及第一气流入口2011，在至少部分除湿运行时间段，在吸湿空间201且在位于第一气流出口2012和第一气流入口2011之间的位置处的温差在70-80℃之间。
通过以上方式，能够实现更佳的烘干效果，且在该温度下洗涤好的衣物手感以及干燥程度均令人满意。
下面进一步提供具体实施例对其进行说明，在各实施例中，基于以上描述的衣物处理装置的基本结构设置，在不同参数条件下的实验来测定吸湿第一空间和吸湿第二空间的温差以及烘干时长。实验条件包括：洗涤衣物重量为4Kg左右，并限定吸湿排湿构件203的厚度与直径比大致在1/20～1/10之间、吸湿排湿构件203的转速为2-10rpm、加热组件2082在除湿运行阶段的的第一加热功率约为400-800W、第二加热功率约为1200-1600W。温差的检测点可设置在吸湿第一空间与吸湿第二空间的大致对称位置，或设置在吸湿排湿构件203两侧表面的大致对称位置，也可设置在位于第一气流出口2012和第一气流入口2011处的位置。需要说明的是，该洗涤衣物的重量仅仅是示意性的，其并不是烘干效果的影响参数。
需要说明的是，吸湿排湿构件203本身的再生性能和吸湿性能受加热温度的影响，如果温度高于或者低于最佳再生温度范围，将导致吸湿排湿构件203的再生性能下降，同时，该部分吸湿排湿构件203旋转至吸湿空间201后，也将高于或者低于最佳吸湿温度范围，导致吸湿排湿构件203吸湿性能也下降，从而影响到最终对衣物的烘干效率。
在实施例一中，设置吸湿排湿构件203的厚度与直径比为25mm/320mm＝0.0780，吸湿排湿构件203的转速为5rpm，加热组件2082的工作功率为最低功率600W、最高功率1400W，通过实验测量得到，在除湿运行阶段，吸湿第一空间和吸湿第二空间之间的实际温差大致在72.7-77.9℃的范围内变化，此时烘干时间约为128min。
在实施例二中，保持吸湿排湿构件203的厚度与直径比为25mm/320mm＝0.0780，加热组件2082的工作功率为最低功率600W、最高功率1400W不变，吸湿排湿构件203的转速降低为3rpm，此时吸湿排湿构件203虽转速较实施例一变慢，通过再生空间202时的加热时间较长，但此时吸湿排湿构件203通过再生空间202的部分的温度基本仍在最佳再生温度范围内，且该转速下也并不会对吸湿排湿构件203的吸湿效率产生大的影响。通过实验测量得到，在除湿运行阶段，吸湿第一空间和吸湿第二空间之间的实际温差大致在72.9-78.6℃的范围内变化，此时烘干时间约为130min。
在实施例三中，保持吸湿排湿构件203的厚度与直径比为25mm/320mm＝0.0780，加热组件2082的工作功率为最低功率600W、最高功率1400W不变，吸湿排湿构件203的转速增加为8rpm，此时吸湿排湿构件203转速较快，由于转速增加造成在再生空间中无法充分脱附水分，使得吸湿排湿构件203旋转至吸湿空间201后的吸湿效率有一定损失，同时由于通过再生空间202时的加热时间较短，旋转至吸湿空间201后对循环气流的加热效率也有损失，但以上效率的损失仍在可接受的范围之内。通过实验测量得到，在除湿运行阶段，吸湿第一空间和吸湿第二空间之间的实际温差大致在70.3-76.2℃的范围内变化，此时烘干时间约为133min。
在实施例四中，保持吸湿排湿构件203的厚度与直径比为25mm/320mm＝0.0780，吸湿排湿构件203的转速为5rpm不变，加热组件2082的工作功率为最低功率400W、最高功率1200W，此时吸湿排湿构件203经过再生空间202时加热温度较低，但是仍在最佳再生温度范围内，且吸湿排湿构件203旋转至吸湿空间201吸附水分时，也仍处于最佳吸湿温度的范围内，因此对吸湿排湿构件203本身的再生效率和吸湿效率影响均较小，对循环气流的加热效率因吸湿排湿构件203经过吸湿空间201后的温度降低而有所下降，但循环气流的温度仍然控制在预设范围之内，对最终烘干效率的影
响较小。通过实验测量得到，在除湿运行阶段,吸湿第一空间和吸湿第二空间的实际温差大致在70.2-75.6℃的范围内变化，烘干时间约为136min。
在实施例五中，保持吸湿排湿构件203的厚度与直径比为25mm/320mm＝0.0780，吸湿排湿构件203的转速为5rpm不变，加热组件2082的工作功率为最低功率600W、最高功率1600W，此时吸湿排湿构件203经过再生空间202时加热温度较高，但是仍在最佳再生温度范围内，吸湿排湿构件203旋转至吸湿空间201进行吸附水分时，也仍处于最佳吸湿温度的范围内，因此对吸湿排湿构件203本身的再生效率和吸湿效率影响均较小，对循环气流的加热效率因吸湿空间201内温度升高而有所提高，但循环气流的温度仍然控制在预设范围之内，不会造成对衣物的损伤。通过实验测量得到，在除湿运行阶段,吸湿第一空间和吸湿第二空间的实际温差大致在73.7-79.5℃的范围内变化，烘干时间约为130min。
在实施例六中，保持吸湿排湿构件203的转速为5rpm，加热组件2082的工作功率为最低功率600W、最高功率1400W不变，吸湿排湿构件203的厚度与直径比改变为23mm/350mm＝0.0657，此时吸湿排湿构件203的尺寸增大，而加热功率不变，吸湿排湿构件203经过再生空间202时升温会较实施例一低，但是仍在最佳再生温度范围内，吸湿排湿构件203旋转至吸湿空间201吸附水分时，也仍处于最佳吸湿温度的范围内，因此对吸湿排湿构件203本身的再生效率、吸湿效率影响均较小，而吸湿效率又由于吸湿排湿构件203的尺寸增加而有所提高，这与因循环气流加热效率的降低对烘干效率的影响基本抵消。通过实验测量得到，在除湿运行阶段,吸湿第一空间和吸湿第二空间的实际温差大致在70.4-75.5℃的范围内变化，烘干时间约为132min。
在实施例七中，保持吸湿排湿构件203的转速为5rpm，加热组件208的工作功率为最低功率600W、最高功率1400W不变，吸湿排湿构件203的厚度与直径比改变为27mm/300mm＝0.0900，此时吸湿排湿构件203的尺寸减小，而加热功率不变，吸湿排湿构件203经过再生空间202时升温会较实施例一高，但是仍在最佳再生温度范围内，吸湿排湿构件203旋转至吸湿空间201吸附水分时，也仍处于最佳吸湿温度的范围内，因此对吸湿排湿构件203本身的再生效率、吸湿效率影响均较小，而吸湿效率又由于吸湿排湿构件203的尺寸减小而有所降低，这与因循环气流加热效率的提高对烘干效率的影响
基本抵消。通过实验测量得到，在除湿运行阶段,吸湿第一空间和吸湿第二空间的实际温差大致在74.5-79.2℃的范围内变化，烘干时间约为133min。
上述实施例一到实施例七的整体数据参见下表1。
表1各实施例数据对比表
本申请比较例通过在所选择范围之外改变吸湿排湿构件203的厚径比、转速以及加热组件2082的加热效率，使得吸湿排湿构件203在再生空间202内的再生温度升高或降低，超出最佳再生温度范围之外，吸湿排湿构件203本身的再生性能因此下降，同时，该部分吸湿排湿构件203旋转至吸湿空间201内后，吸湿性能也随之下降，从而影响到最终对衣物的烘干效率。同时，对循环气流的加热效率也因吸湿空间201内的吸湿排湿构件203温度升高或降低有较大变化，从而影响到最终对衣物的烘干效果。以下的比较例一至六均是在限定范围之外对相关参数进行调整，以使得对于吸湿排湿构件203的再生效率、吸湿效率及对循环气流的加热效率影响较大，从而在除湿运行阶段吸湿空间201内的吸湿第一空间和吸湿第二空间的温差无法维持在70-80℃的范围内，此时对衣物的烘干时间较长且烘干效果不好，某些情况下还会损伤衣物。
在比较例一中，设置吸湿排湿构件203的厚度与直径比为25mm/320mm＝0.0780，加热组件2082的工作功率为最低功率600W、最高功率1400W，设置吸湿排湿构件203的转速为1rpm；此时因转速过慢导致再生空间202内的加热时间较长，吸湿排湿构件203在再生空间202的温度高于最佳再生温度的范围，进而吸湿排湿构件203旋转至吸湿空间201后的部分时段内处于最佳吸湿温度的范围之外，使得吸湿排湿构件203本身的再生效率和吸湿效率均降低，此外，吸湿排湿构件203对通过的循环气流的加热效率也因吸湿空间201的温度升高而提高，经过加热后的循环气流进入滚筒30后因温度过高有可能会损伤衣物，此种情形下，对循环气流的除湿不充分而加热过于充分，吸湿第一空间和吸湿第二空间的温差将高于70-80℃，烘干时间将变长；通过实验测量，在除湿运行阶段，吸湿第一空间和吸湿第二空间的实际温差大致为83.5-90.9℃，烘干时间约为162min。
在比较例二中，设置吸湿排湿构件203的厚度与直径比为25mm/320mm＝0.0780，加热组件2082的加热功率为最低功率600W、最高功率1400W，设置吸湿排湿构件203的转速为12rpm；此时因转速过快导致再生空间202的加热时间过短，吸湿排湿构件203在再生空间202的温度小于最佳再生温度的范围，进而吸湿排湿构件203旋转至吸湿空间201后的部分时段内处于最佳吸湿温度的范围之外，使得吸湿排湿构件203本身的再生效率和吸湿效率均降低，此外，吸湿排湿构件203对通过的循环气流的加热效率也因吸湿空间201的温度降低而降低，此种情形下，对循环气流的除湿和加热均不充分，吸湿第一空间和吸湿第二空间的温差将低于70-80℃的范围，烘干时间将变长；通过实验测量，在除湿运行阶段，吸湿第一空间和吸湿第二空间的实际温差大致为66.6-72.5℃，烘干时间约为169min。
在比较例三中，设置吸湿排湿构件203的厚度与直径比为25mm/320mm＝0.0780，吸湿排湿构件203的转速5rpm，设置加热组件2082的工作功率为最低功率200W、最高功率1400W，此时吸湿排湿构件203经过再生空间202时加热温度较低，导致吸湿排湿构件203在再生空间202的温度低于最佳再生温度范围，而吸湿排湿构件203旋转至吸湿空间201
后的部分时段内处于最佳吸湿温度的范围之外，吸湿排湿构件203本身的再生效率和吸湿效率均降低，此外，对循环气流的加热效率因吸湿空间201的温度降低而下降，此种情形下，吸湿排湿构件203对循环气流的除湿和加热均不充分，吸湿第一空间和吸湿第二空间的温差将低于70-80℃的范围，烘干时间将变长；通过实验测量，在除湿运行阶段，吸湿第一空间和吸湿第二空间的实际温差大致为66.5-72.3℃，烘干时间约为168min。
在比较例四中，设置吸湿排湿构件203的厚度与直径比为25mm/320mm＝0.0780，吸湿排湿构件203的转速5rpm，设置加热组件2082的工作功率为最低功率600W、最高功率2200W，此时吸湿排湿构件203经过再生空间202时加热温度较高，导致吸湿排湿构件203在再生空间202的温度高于最佳再生温度范围，而吸湿排湿构件203旋转至吸湿空间201后的部分时段内处于最佳吸湿温度的范围之外，吸湿排湿构件203本身的再生效率和吸湿效率均降低，此外，对循环气流的加热效率因吸湿空间201温度升高而提高，经过加热后的循环气流进入滚筒30后因温度过高易损伤衣物；此种情形下，对循环气流的除湿不充分而加热过于充分，吸湿第一空间和吸湿第二空间的温差将高于70-80℃，烘干时间将变长，且由于衣物处理装置的运行功率较高，更加耗电；通过实验测量，在除湿运行阶段，吸湿第一空间和吸湿第二空间的实际温差大致为79.6-92.8℃，烘干时间约为171min。
在比较例五中，设置吸湿排湿构件203的转速5rpm，加热组件2082的工作功率为最低功率600W、最高功率1400W，吸湿排湿构件203的厚度与直径比为18mm/400mm＝0.0450，此时吸湿排湿构件203的尺寸增大，而加热功率不变，吸湿排湿构件203经过再生空间202时升温较少，导致吸湿排湿构件203在再生空间202的温度低于最佳再生温度的范围，而吸湿排湿构件203旋转至吸湿空间201吸附水分时，也将低于最佳吸湿温度的范围，吸湿排湿构件203本身的再生效率和吸湿效率均降低，此外，对循环气流的加热效率因吸湿空间201温度降低而下降，此种情形下，吸湿排湿构件203对循环气流的除湿和加热均不充分，吸湿第一空间和吸湿第二空间的温差将低于70-80℃的范围，烘干时间将变长；通过实验测量，在除湿运行阶段，吸湿第一空间和吸湿第二空间的实际温差大致为
75.1-82.9℃，烘干时间约为155min。
在比较例六中，设置吸湿排湿构件203的转速5rpm，加热组件2082的工作功率为最低功率600W、最高功率1400W，吸湿排湿构件203的厚度与直径比为30mm/250mm＝0.1200，此时吸湿排湿构件203的尺寸减小，而加热功率不变，吸湿排湿构件203经过再生空间202时升温较多，导致吸湿排湿构件203在再生空间202的温度高于最佳再生温度范围，吸湿排湿构件203旋转至吸湿空间201吸附水分时，也仍高于最佳吸湿温度的范围，吸湿排湿构件203本身的再生效率和吸湿效率均降低，而吸湿效率又由于吸湿排湿构件203的尺寸减小而进一步降低，此外，对循环气流的加热效率因吸湿空间201温度升高而有所提高，经过加热后的循环气流进入滚筒30后因温度过高易损伤衣物；此种情形下，对循环气流的除湿不充分而加热过于充分，吸湿第一空间和吸湿第二空间的温差将高于70-80℃，烘干时间将变长；通过实验测量，在主要除湿运行阶段，吸湿第一空间和吸湿第二空间的实际温差大致为77.1-89.6℃，烘干时间约为159min。
需要说明的是，上述实施例中所述的最佳再生温度、最佳吸湿温度仅仅是在此温度下吸湿和再生效率最高，并不表示在该温度范围之外无法再生和吸湿。
上述比较例一到比较例六的整体数据参见下表2。
表2各比较例数据对比表
综上所述，本申请提供一种衣物处理装置，其通过将烘干模组中的吸湿排湿构件的结构参数以及加热构件的有效工作功率进行限定，保证至少部分吸湿第一空间与至少部分吸湿第二空间的温差在70-80℃之间。此外，临近滚筒进气口的至少一个位置的第一气流温度大致在70-80℃之间，本申请还提供一种衣物处理装置，其通过将烘干模组中的吸湿排湿构件的结构参数以及加热构件的有效工作功率进行限定，使得在滚筒靠近滚筒出气口处的至少一个位置的第二气流温度大致在50-60℃之间，第一气流温度和所述第二气流温度的温差为25±5℃。通过衣物处理装置，能够兼顾较好的烘干效率以及烘干效果。
以上所述实施例的各技术特征可以进行任意的组合，为使描述简洁，未对上述实施例中的各个技术特征所有可能的组合都进行描述，然而，只要这些技术特征的组合不存在矛盾，都应当认为是本说明书记载的范围。换句话说，上述实施例中不冲突的部分可以相互替代或补充，形成新的实施例。
本申请已经通过上述实施例进行了说明，但应当理解的是，上述实施例只是用于举例和说明的目的，而非意在将本申请限制于所描述的实施例范围内。此外本领域技术人员可以理解的是，本申请并不局限于上述实施例，根据本申请的教导还可以做出更多种的变型和修改，这些变型和修改均落在本申请所要求保护的范围以内。本申请的保护范围由附属的权利要求书及其等效范围所界定。
Claims (19)
- 一种衣物处理装置，其特征在于，包括：滚筒以及烘干模组；其中，所述滚筒至少具有一滚筒出气口和一滚筒进气口；所述烘干模组包括：壳体、吸湿排湿构件；所述壳体至少包括第一壳体和第二壳体，所述第一壳体和第二壳体密封配合至少形成容纳所述吸湿排湿构件的空间；所述吸湿排湿构件在所述空间内旋转；在所述第一壳体和所述第二壳体的对应位置处分别从所述第一壳体和所述第二壳体的侧壁向中心区域的方向设置有至少两个分隔件，所述至少两个分隔件在垂直于所述吸湿排湿构件旋转方向的投影平面上，将所述空间分隔为至少吸湿空间和再生空间；在所述吸湿空间，所述吸湿排湿构件的两侧分别形成吸湿第一空间和吸湿第二空间，其中所述吸湿第一空间为从所述滚筒出气口流入的具有第一气流湿度的空间，所述吸湿第二空间为经所述吸湿排湿构件吸湿后具有第二气流湿度的空间，该第一气流湿度大于第二气流湿度；在至少部分除湿运行时间段，至少部分所述吸湿第一空间与至少部分所述吸湿第二空间的温差在70-80℃之间。
- 根据权利要求1所述的衣物处理装置，其特征在于，在至少部分除湿运行时间段，在所述吸湿空间，所述吸湿排湿构件的两侧至少部分表面温差在70-80℃之间。
- 根据权利要求1或2所述的衣物处理装置，其特征在于，在至少部分除湿运行时间段，在所述吸湿第一空间与所述吸湿第二空间的大致对称位置处的温差在70-80℃之间，或在所述吸湿排湿构件两侧表面的大致对称位置处的温差在70-80℃之间。
- 根据权利要求3所述的衣物处理装置，其特征在于，所述第一壳体上至少形成有第一气流入口，所述第二壳体上至少形成有第一气流出口，所述第一气流入口和所述第一气流出口分别临近所述至少两个分隔件设置。
- 根据权利要求4所述的衣物处理装置，其特征在于，所述吸湿排湿构件旋转依次经过再生空间、所述第一气流出口以及所述第一气流入口， 在至少部分除湿运行时间段，在所述吸湿空间且在位于第一气流出口和第一气流入口之间的位置处的温差在70-80℃之间。
- 根据权利要求1所述的衣物处理装置，其特征在于，所述烘干模组包括加热组件，所述加热组件设置于所述再生空间；所述加热组件在第一加热功率和第二加热功率之间波动运行或交替运行。
- 根据权利要求6所述的衣物处理装置，其特征在于，所述第一加热功率为400-800W之间，所述第二加热功率为1200-1600W之间。
- 根据权利要求1所述的衣物处理装置，其特征在于，所述吸湿排湿构件的厚度与直径比的范围在1/80～1/4之间。
- 根据权利要求8所述的衣物处理装置，其特征在于，所述吸湿排湿构件的厚度与直径比的范围在1/20～1/10之间。
- 一种衣物处理装置，其特征在于，包括：滚筒以及烘干模组；其中，所述滚筒至少具有一滚筒出气口和一滚筒进气口；所述烘干模组包括：壳体、吸湿排湿构件；所述壳体至少包括第一壳体和第二壳体，所述第一壳体和第二壳体密封配合至少形成容纳所述吸湿排湿构件的空间；所述吸湿排湿构件在所述空间内旋转；在所述第一壳体和所述第二壳体的对应位置处分别从所述第一壳体和所述第二壳体的侧壁向中心区域的方向设置有至少两个分隔件，所述至少两个分隔件在垂直于所述吸湿排湿构件旋转方向的投影平面上，将所述空间分隔为至少吸湿空间和再生空间；所述第一壳体上至少形成有与所述滚筒出气口连通的第一气流入口；所述第二壳体上至少形成有与所述滚筒进气口连通的第一气流出口；在至少部分除湿运行时间段，在所述第一气流出口和所述滚筒进气口之间，临近所述滚筒进气口的至少一个位置的气流温度为第一温度，所述第一温度在70-80℃之间。
- 根据权利要求10所述的衣物处理装置，其特征在于，在滚筒靠近所述滚筒出气口处的至少一个位置的气流温度为第二气流温度，所述第二气流温度在50-60℃之间。
- 根据权利要求10所述的衣物处理装置，其特征在于，在所述第一气流入口与滚筒出气口之间至少设置有一出气管道，所述出气管道内靠近所述滚筒出气口处的至少一个位置的气流温度为第二气流温度，所述第二气流温度在50-60℃之间。
- 根据权利要求11或权利要求12所述的衣物处理装置，其特征在于，所述第一气流温度和所述第二气流温度的温差为25±5℃。
- 根据权利要求13所述的衣物处理装置，其特征在于，在所述第一气流出口和所述滚筒进气口之间有进气管道，在所述进气管道靠近所述滚筒进气口的位置设置有第一温度检测单元；在所述滚筒上或所述出气管道上，靠近所述滚筒出气口的位置设置有第二温度检测单元。
- 根据权利要求10所述的衣物处理装置，其特征在于，所述烘干模组包括加热组件，所述加热组件设置于所述再生空间；所述加热组件在第一加热功率和第二加热功率之间波动运行或交替运行。
- 根据权利要求15所述的衣物处理装置，其特征在于，所述第一加热功率在400-800W之间，所述第二加热功率在1200-1600W之间。
- 根据权利要求10所述的衣物处理装置，其特征在于，所述吸湿排湿构件的厚度与直径比的范围在1/80～1/4之间。
- 根据权利要求16所述的衣物处理装置，其特征在于，所述吸湿排湿构件的厚度与直径比的范围在1/20～1/10之间。
- 根据权利要求10所述的衣物处理装置，其特征在于，所述吸湿空间所在的气流通路上以及所述再生空间所在的气流通路上分别设置有循环风机以及再生风机。
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| WO2023030394A1 (zh) * | 2021-09-01 | 2023-03-09 | 深圳洛克创新科技有限公司 | 衣物处理设备 |
| WO2024046325A1 (zh) * | 2022-08-31 | 2024-03-07 | 深圳洛克创新科技有限公司 | 一种餐具处理装置 |
| WO2024046211A1 (zh) * | 2022-08-31 | 2024-03-07 | 深圳洛克创新科技有限公司 | 烘干模组以及洗烘一体机 |
| WO2024045512A1 (zh) * | 2022-08-31 | 2024-03-07 | 深圳洛克创新科技有限公司 | 一种烘干模组及洗烘一体机 |
| CN218621460U (zh) * | 2022-08-31 | 2023-03-14 | 深圳洛克创新科技有限公司 | 洗烘一体机 |
| WO2024046358A1 (zh) * | 2022-08-31 | 2024-03-07 | 深圳洛克创新科技有限公司 | 一种烘干模组及洗烘一体机 |
| WO2024045711A1 (zh) * | 2022-08-31 | 2024-03-07 | 深圳洛克创新科技有限公司 | 衣物处理设备的控制方法、衣物处理设备和可读存储介质 |
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