WO2017023012A1 - Washing machine having moisture absorption member - Google Patents

Washing machine having moisture absorption member Download PDF

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Publication number
WO2017023012A1
WO2017023012A1 PCT/KR2016/008241 KR2016008241W WO2017023012A1 WO 2017023012 A1 WO2017023012 A1 WO 2017023012A1 KR 2016008241 W KR2016008241 W KR 2016008241W WO 2017023012 A1 WO2017023012 A1 WO 2017023012A1
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WO
WIPO (PCT)
Prior art keywords
moisture absorption
porous aluminosilicate
washing machine
tub
moisture
Prior art date
Application number
PCT/KR2016/008241
Other languages
French (fr)
Korean (ko)
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WO2017023012A8 (en
Inventor
정상윤
최권일
전신희
이대기
오명환
Original Assignee
주식회사 엘지화학
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from KR1020160094947A external-priority patent/KR102053323B1/en
Application filed by 주식회사 엘지화학 filed Critical 주식회사 엘지화학
Priority to CN201680028524.9A priority Critical patent/CN107690491B/en
Priority to US15/567,488 priority patent/US10443175B2/en
Publication of WO2017023012A1 publication Critical patent/WO2017023012A1/en
Publication of WO2017023012A8 publication Critical patent/WO2017023012A8/en

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Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06FLAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
    • D06F25/00Washing 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 
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06FLAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
    • D06F37/00Details specific to washing machines covered by groups D06F21/00 - D06F25/00
    • D06F37/02Rotary receptacles, e.g. drums
    • D06F37/04Rotary receptacles, e.g. drums adapted for rotation or oscillation about a horizontal or inclined axis
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06FLAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
    • D06F58/00Domestic laundry dryers
    • D06F58/20General details of domestic laundry dryers 
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06FLAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
    • D06F58/00Domestic laundry dryers
    • D06F58/20General details of domestic laundry dryers 
    • D06F58/26Heating arrangements, e.g. gas heating equipment

Definitions

  • the present invention relates to a washing machine, and more particularly, to a dry combined drum washing machine provided with a moisture absorbing member.
  • Drum washing machine is a device for washing laundry by rotating the drum by the driving force of the motor in a state in which detergent, washing water and laundry in the drum.
  • Such a drum washing machine has advantages of less damage to laundry, less tangling of laundry, and less water usage.
  • a combined drum washing machine capable of drying laundry by blowing hot air into the drum through a drying duct.
  • Such a dry combined drum washing machine selectively or continuously performs a washing stroke, a rinse stroke, a dehydration stroke, a drying stroke, and the like.
  • FIG. 1 is a side cross-sectional view schematically showing the main configuration of a conventional combined drying drum washing machine.
  • a drum washing machine generally includes a cabinet 10 having a laundry inlet formed on a front surface thereof, a door 11 installed to be opened and closed at a laundry inlet of the cabinet 10, and washing water inside the cabinet 10.
  • a tub 20 installed to store the drum, a drum 22 rotatably installed in the tub 20, and a motor 50 installed in the tub 20 to transmit driving force to the drum 22. It is composed.
  • a drying duct 60 and a male duct 70 are installed.
  • a heater 63 and a blowing fan 67 are installed in the drying duct 60 to discharge hot air into the tub 20.
  • the drying duct 60 and the male duct 70 are installed to communicate with each other and at the same time communicate with the inside of the drum 22.
  • the tub 20 is formed with an intake port through which the hot air is drawn through the drying duct 60 and an exhaust port through which the air is discharged to the male duct 70.
  • the expansion duct 70 is provided with a water supply nozzle 75 for supplying water angle so as to expand the moisture in the air.
  • the user opens the door 11, puts laundry into the drum 22, and closes the door 11 to seal the drum 22.
  • the water supply device 15 waters the water.
  • the water supplied is heated by the heater 17 and mixed with the detergent of the cesegong 12 and then supplied to the inside of the tub 20, introduced into the drum 22 through the through hole, and wetted with laundry.
  • the motor 50 is driven to rotate the drum 22 for a set washing time, the contaminated water in the tub 20 is drained out of the washing machine through the drain hose 83 by the drain pump 80. .
  • the present invention is to provide a washing machine that enables the reduction of energy required in the washing and drying stroke.
  • the atomic ratio of Si / Al is 15 or less, and V meso and
  • the total pore volume defined as the sum of the total Vmicro specific volume V is equipped with a moisture absorption member which comprises a porous aluminosilicate is less than 0.3 cmVg washing machine is provided with:
  • V meso is a Barrett-Joiner-Hellenda (BJH) cumulative volume for mesoprocessing of 2 to 300 nm
  • the washing machine is a washing machine
  • a door 11 installed to be opened and closed at the laundry inlet
  • Tub 20 installed to store the wash water in the cabinet
  • a motor 50 installed in the tub and transmitting a driving force to the drum, and fixed to an outer circumferential surface of the upper side of the tub, with both ends of the tub
  • a drying duct (60) connected to an intake port and an exhaust port to circulate hot air into the drum;
  • a moisture absorbing member 65 including the porous aluminosilicate, a heater 63 attached to an outer circumferential surface of the moisture absorbing member and heating the moisture absorbing member and air, and a blowing fan for circulating air ( 67) is built in.
  • a washing machine according to an embodiment of the present invention will be described.
  • the meaning of "include” as used herein specifies a particular characteristic, region, integer, step, operation, element or component, excluding the addition of other specific characteristics, region, integer, step, operation, element, or component. It is not meant to be.
  • the atomic ratio of Si / Al is 15 or less
  • a washing machine is provided with a hygroscopic member comprising a porous aluminosilicate having a total specific volume V tot al of pores defined by the volume sum of V meso and Vmicro of at least 0.3 Cm 3 / g:
  • V meso is a Barrett-Joiner-Hellenda (BJH) cumulative volume for mesopores having a pore size of 2 to 300 nm,
  • BJH Barrett-Joiner-Hellenda
  • V meso of the porous aluminosilicate is 0.05 cmVg or more or 0.05 to 1.0 cmVg may be advantageous for the expression of various properties according to the present invention.
  • V meso is 0 ⁇ 5 cmVg or more, or At least 0.09 cmVg, or at least 0.1 cmVg, or at least 0.15 cm 3 / g, or at least 0.2 cmVg, or at least 0.25 cmVg, or at least 0.5 cm 3 / g; 1.0 cmV or less, black may be 0.6 cm 3 / g or less, black may be 0.55 cm 3 / g or less.
  • Vmi cr... Of the porous aluminosilicate may be more than 0 ⁇ 1 cmVg or 0.01 to 0.5 cm 3 / g, which may be advantageous for expression of various properties according to the present invention.
  • the Vndcro is 0.01 cmVg or more, or 0 ⁇ 3 cmVg or more, or 0.06 cmVg or more, or 0.09 cm 3 / g or more, 0.1 cm 3 / g or more, or 0.15 cm or more, or 0.2 cmVg or more, or 0.25 cm 3 / g or greater;
  • 0.5 cmVg or less, black may be 0.3 cm 3 / g or less, black may be 0.28 cmVg or less.
  • Vtotai may be 0.3 cm 3 / g or more, black is 0.32 cm 3 / g or more, or 0.34 cmVg or more; 0.8 cm 3 / g or less, or 0.7 cm 3 / g or less, black may be 0.65 cmVg or less.
  • the porous aluminosilicate may have an argon adsorption Brunner-Emmett-Teller (BET) surface area of 200 to 850 m 2 / g black or more than 200 rnVg.
  • BET Brunner-Emmett-Teller
  • the BET surface area may be 200 m 2 / g or more, black 250 mVg or more, or 300 m 2 / g or more, or 350 n / g or more, and black may be 370 mVg or more; 850 mVg or less, or 800 m 2 / g or less, black may be 750 n / g or less, or 730 mVg or less.
  • porous aluminosilicates exhibiting all the above-described characteristics, for example, pore volume characteristics, specific surface areas, and the like, are subjected to conditions in a drying duct of a washing machine. Under the conditions of normal temperature and high humidity, excellent moisture absorption characteristics can be exhibited and high moisture absorption can be exhibited. Therefore, the drying process of the laundry can be appropriately performed by using the hygroscopic member including such porous aluminosilicate.
  • the moisture absorption process of the porous aluminosilicate corresponds to the exothermic reaction, so that the heat of adsorption generated at this time may be used for heating the air for drying. Therefore, it is possible to greatly reduce the energy used or lost in the drying stroke, or to proceed with the drying stroke substantially without additional energy input.
  • the porous aluminosilicate is 25 ° C and under a relative humidity of 95%
  • the moisture absorption amount which is defined by the following formula 1, which is included in one embodiment the moisture absorption member (%; 25 ° C, 95% RH) 22
  • the moisture absorption amount may be excellent as much as% or more or 22 to 50%, and the heat of adsorption may also be generated according to the high moisture absorption amount. Therefore, the moisture absorbing member of this embodiment can be preferably used in the drying stroke of the washing machine to exhibit an energy saving effect:
  • Moisture absorption (%; 25 ° C., 95% RH) [W (g) / AS (g)] * 100
  • AS (g) represents the weight of the porous aluminosilicate
  • the stratified V meso range of 0.05 cmVg or more or 0.05 to 1.0 cm 3 / g. Accordingly, the rate of natural dehumidification can be further increased.
  • the porous aluminosilicate included in the moisture absorption member of one embodiment has a relative moisture absorption ratio of 1.2 or more, black is 1.22 to 5.0, black is 1.24 to 3.0, and the relative humidity is 95. By lowering from 50% to 50%, very high levels of spontaneous dehumidification (e.g., about 30% or more) can be achieved without extra energy input:
  • Moisture absorption ratio by relative humidity moisture absorption (%; 25 ° C, 95% RH) / moisture absorption (%; 25 ° C, 50% RH)
  • moisture absorption (%; 25 ° C, 95% RH ) Represents the moisture absorption defined by the above formula 1
  • the moisture absorption amount (%; 25 ° C, 50% RH) is lowered from 95% to 50% relative humidity when dehumidification from the porous aluminosilicate
  • Wl (g) represents the weight of the water absorbed maximum by the porous aluminosilicate of AS (g) after dehumidification proceeds. .
  • the moisture absorbing member of the embodiment can also reduce the amount of energy used to dehumidify moisture from the drying stroke once.
  • the porous aluminosilicate that does not satisfy the characteristics of the embodiment is applied, it is confirmed that energy consumption is inevitably increased due to relatively poor dehumidification.
  • the moisture absorbing member of the embodiment can achieve a large energy saving effect by reducing energy use or loss of the washing machine.
  • the porous aluminosilicate exhibiting the above-described characteristics has previously been Among the commercially available porous aluminosilicates, those showing gastric properties may be selected and used, or may be manufactured and used directly.
  • porous aluminosilicates in the form of zeolites in which cations of alkali metals, alkaline earth metals or transition metals such as Ca cations, Na cations, K cations or Fe cations are bonded to the anions of aluminosilicates.
  • zeolites in which cations of alkali metals, alkaline earth metals or transition metals such as Ca cations, Na cations, K cations or Fe cations are bonded to the anions of aluminosilicates.
  • porous aluminosilicate may be represented by Formula 1 below:
  • M represents an alkali metal, an alkaline earth metal or a transition metal
  • X and y each independently represent a positive number
  • a, b and c are A number of zero or more is represented (where a + b is a positive number).
  • M may be Ca, Na, K, or Fe
  • X, y, a, b, and c may be determined in consideration of the valence of each constituent element or ion.
  • the atomic ratio of Si / Al in the porous aluminosilicate is 15 or less, or more than 1 and 15 or less, it may be advantageous for the above-mentioned expression.
  • the atomic ratio of Si / Al may be 15 or less, black may be 13.5 or less, or 13 or less, and black may be 12.5 or less; Greater than 1.0, black may be 1.1 or greater, or 1.2 or greater.
  • examples of the commercially available porous aluminosilicate include BEA type or 13X type zeolite.
  • suitable methods for producing porous aluminosilicates exhibiting the above-mentioned characteristics include a method of preparing by coupled reaction of the coupled alumino-mediated dissolution and precipitation of the porous aluminosilicate precursor in an aqueous medium.
  • silicon sources humide silica, silicate, aluminosilicate, clay, mineral, metakaolin, activated clay, fly ash, slag, pozzolane, etc.
  • aluminum sources alumina, aluminate, aluminum salt, clay, metakaolin, activated clay, fly ash, slag, pozzolane, and the like may be used.
  • a basic or alkaline solution e.g. sodium hydroxide solution
  • the above-described heat treatment is performed by heat treating a geopolymer resin satisfying a specific metal atomic ratio under atmospheric pressure and low temperature (for example, 60 to 80 ° C., preferably 65 to 75 ° C.). Porous aluminosilicates exhibiting properties can be obtained.
  • the porous aluminosilicate exhibiting the above-described characteristics can be used as a moisture absorbing member of one embodiment by itself, or by adding an appropriate additive or the like can be prepared and used the moisture absorbing member of one embodiment.
  • the kind of the additive which can be used is not particularly limited, and any additive known to be included in the hygroscopic member can be used.
  • a door 11 installed to be opened and closed at the laundry inlet
  • Tub 20 installed to store the wash water in the cabinet
  • a motor 50 installed in the tub and transmitting a driving force to the drum, and fixed to an outer circumferential surface of the upper side of the tub, and both ends of which are connected to an inlet and an exhaust port of the tub to circulate hot air into the drum And duct 60.
  • the fan 67 is built in.
  • the washing machine according to the embodiment of the present invention shown in FIG. 2 further includes a moisture absorbing member 65 provided in the drying duct 60, as compared with the conventional washing machine shown in FIG. 1, and includes a male duct 70 and a water supply nozzle. Does not include (75).
  • the expansion duct 70 is a means for lowering humidity by condensing low temperature and humid air discharged from the drum 22 when performing a drying stroke, and the water supply angle supplied through the water supply nozzle 75. Flow.
  • the washing machine according to the embodiment of the present invention is provided with a moisture absorbing member 65 including porous aluminosilicate that meets the above-described characteristics, and can exhibit excellent moisture absorption characteristics under high humidity conditions. It is possible to carry out the construction stroke without any means of estimating.
  • the moisture absorption process of the porous aluminosilicate included in the moisture absorption member 65 corresponds to the exothermic reaction, so that the heat of adsorption generated at this time can be used for heating the air for performing the drying stroke.
  • the energy used or lost in the drying stroke can be greatly reduced, or the drying stroke can be carried out substantially without extra energy input.
  • porous aluminosilicate that meets the above-described characteristics can be subjected to significant natural dehumidification only by lowering the relative humidity. Therefore, natural dehumidification can be made from the moisture absorption member 65 when the relative humidity becomes low after completion of a drying stroke. If necessary, the heater 63 and the blower fan 67 may be operated in the washing stroke so that dehumidification of the moisture absorbing member 65 may be performed.
  • the heat accumulation may occur in the dehumidification process of the porous aluminosilicate included in the moisture absorbing member 65, and the heat storage may also be used as energy for heating water in the washing stroke.
  • the moisture absorbing member 65 includes the above-mentioned porous aluminosilicate.
  • the porous aluminosilicate may be layered in any container.
  • the moisture absorbing member 65 may be mounted inside or on one sidewall of the drying duct 60.
  • the moisture absorbing member 65 may be provided inside the drying duct 60 in a state in which the moisture absorbing member 65 is coupled to the heater 63, in which a flow path of humid air circulated by the blowing fan 67 is absorbed. It may be provided at a position capable of penetrating or contacting the member 65.
  • the washing machine may selectively or continuously perform a washing stroke, a rinse stroke, a dewatering stroke, and a drying stroke in the following manner with reference to FIG. 2.
  • the user opens the door 11, puts laundry into the drum 22 and closes the door 11 to seal the drum 22.
  • the water supply device 15 waters the water.
  • the water supplied is heated by the heater 17, mixed with the detergent of the detergent container 12, and then supplied into the tub 20, and introduced into the drum 22 through the through hole and wetted with laundry.
  • the washing machine through the contaminated water drain hose (83) in the tub 20 by the then motor 50 is driven is set laundry 'time the drum 22 rotates to come over, the drain pump (80) outside Drained.
  • power may be applied to the heater 63 and the blowing fan 67 in the drying duct 60 to dehumidify the moisture absorbing member 65 as necessary.
  • the male heat generated in the dehumidification process of the moisture absorbing member 65 may be introduced into the drum 22 and used as energy for heating water.
  • clean water is supplied into the tub 20 through the water supply device 15, and the motor 50 is driven for the set rinse time.
  • the motor 50 is stopped, the drain pump 80 is pumped, and the water containing bubbles in the tub 20 is drained out of the washing machine through the drain hose 83.
  • the motor 50 is driven to set the drum 22 at high speed for the set dehydration time.
  • the laundry in the drum 22 is dehydrated by centrifugal force.
  • the drain pump 80 is pumped so that the water discharged from the laundry is drained to the outside of the washing machine through the drain hose 83.
  • the drying stroke is started, power is applied to the heater 63 and the blowing fan 67 of the drying duct 60, and the generated hot air is introduced into the drum 22 by the guide of the drying duct 60. .
  • the hot air in the drum 22 is converted into low temperature and humid air while the laundry is heated and dried, and the low temperature and humid air is discharged to the drying tuft 60 through the exhaust port of the tub 20.
  • the low temperature means a temperature (for example, room temperature) lower than the temperature of the air heated by the heater.
  • the low temperature and humid air supplied to the drying tuck 60 is circulated by the blowing fan 67 toward the moisture absorbing member 65, and loses moisture by moisture absorption at the moisture absorbing member 65 and is dried. This series of steps is repeated to dry the laundry.
  • the dehumidification process of the moisture absorbing member 65 by simultaneously operating the heater 17 for heating the water in the washing stroke during the driving of the washing machine and the heater 63 for the dehumidifying the moisture absorbing member 65.
  • the generated heat storage can be used additionally.
  • the heat of adsorption e.g., 0.17 kWh per unit weight (kg) of the porous aluminosilicate
  • separate expansion means e.g., the expansion duct
  • the washing machine according to the present invention enables saving of energy required for washing and drying strokes.
  • FIG. 1 is a side cross-sectional view schematically showing the internal structure of a general washing machine
  • FIG. 2 is a side cross-sectional view schematically showing the internal structure of a washing machine according to an embodiment of the present invention.
  • the geopolymer resin was heated in Aubon for one day under atmospheric pressure and 70 ° C. to obtain a geopolymer resin of pH 14 level. Distilled water was added to the heat-treated geopolymer resin in an amount of tertiary distilled water, and the resultant was centrifuged at 10000 rpm for 5 minutes to decantation the clear supernatant at pH 14. This washing, centrifugation and decantation steps were repeated until the supernatant was at pH 7 level. The neutralized geopolymer resin was dried overnight in a vacuum oven at 80 ° C. to obtain the final product, porous aluminosilicate.
  • Example 2
  • Zeolyst BEA type zeolite (trade name: CP814E) was prepared in Example 2.
  • Example 3 Zeolyst BEA type zeolite (trade name: CP814E) was prepared in Example 2.
  • Zeolyst ZSM-5 type zeolite (product name: CBV8014) was prepared in Comparative Example 1. Test Example 1
  • Si / Al atomic ratio was analyzed using ICP-OES Optima 7300DV. Specifically, samples were collected in a corning tube (50ml) for Si / Al atomic ratio analysis, and then static electricity was removed with an electrostatic gun. Hydrochloric acid and hydrofluoric acid were added to the sample to dissolve it, and the solution was diluted with ultrapure water. After taking 1 ml of this solution, supersaturated boric acid and scandium (Sc) were added as internal standards, and then diluted with ultrapure water. Standard solutions were prepared with Blank, 1 g / ml, 5 g / ml, 10 pg / ml. The Si / Al atomic ratio of the ultra diluted solution was analyzed by the ICP-OES Optima 7300DV.
  • BET Brunauer-Emmett-Teller
  • Vmeso (cin J / g): Barrett-Joiner-Halenda (BJH) cumulative volume for mesopores with a pore size of 2 to 300 nm
  • the water (washing water) used for washing was 7 L, and the washing was performed by raising the temperature from the initial temperature of 15 ° C to 40 ° C.
  • the amount of laundry was 3 kg.
  • 0.5 kg of water was dried and removed at the time of drying, and for this purpose, the temperature was raised from 30 ° C to 60 ° C.
  • Energy requirements were calculated during this washing and drying process.
  • the energy requirement in the washing and drying stroke (Comparative Example 2; ie, the same method as the conventional washing and drying stroke without using the hygroscopic member) under the same conditions, except that aluminosilicate was not applied, was calculated as follows. Table 2 summarizes them.
  • A. Energy for desiccant dehumidification ⁇ [Required energy under the assumption that there is no natural dehumidification (0.34 kWh / 2 kg absorbent)]-[Energy saving by natural dehumidification rate] ⁇ ;
  • Washing water heating (heating) energy energy for raising 7 kg of water from 15 ° C to 40 ° C;
  • Comparative Example 2 air heating required energy (30-> 60 ° C) + heat of vaporization (60 ° C) Referring to Table 2, in the case of Examples 1 to 3, compared to Comparative Examples 1 and 2, It was found that the energy saving effect of the width was shown.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Detail Structures Of Washing Machines And Dryers (AREA)
  • Main Body Construction Of Washing Machines And Laundry Dryers (AREA)
  • Drying Of Gases (AREA)

Abstract

The present invention relates to a washing machine which can reduce energy required for a washing stroke and a drying stroke. The washing machine has a moisture absorption member including porous aluminosilicate in which the ratio of Si/Al is equal to or lower than 15 and the total specific volume Vtotal of pores, which is defined as the volumetric sum of Vmeso and Vmicro, is equal to or larger than 0.3 cm3/g.

Description

【명세서】  【Specification】
【발명의 명칭】  [Name of invention]
흡습 부재가 구비된 세탁기  Washing machine with moisture absorption member
【기술분야】  Technical Field
본 발명은 세탁기에 관한 것으로, 보다 상세하게는 흡습 부재가 구비된 건조 겸용 드럼 세탁기에 관한 것이다.  The present invention relates to a washing machine, and more particularly, to a dry combined drum washing machine provided with a moisture absorbing member.
관련 출원과의 상호 인용  Cross Citation with Related Applications
본 출원은 2015년 7월 31일자 한국 특허 출원 제 10-2015-0109124호와 2016년 7월 26일자 한국 특허 출원 제 10-2016-0094947호에 기초한 우선권의 이익을 주장하며, 해당 한국 특허 출원들의 문헌에 개시된 모든 내용은 본 명세서의 일부로서 포함된다.  This application claims the benefit of priority based on Korean Patent Application No. 10-2015-0109124 dated July 31, 2015 and Korean Patent Application No. 10-2016-0094947 dated July 26, 2016. All content disclosed in the literature is included as part of this specification.
【발명의 배경이 되는 기술】 [Technique to become background of invention]
드럼 세탁기는 세제, 세탁수 및 세탁물을 드럼 내에 투입한 상태에서 모터의 구동력에 의해 드럼을 회전시켜 세탁물을 세탁하는 장치이다. 이러한 드럼 세탁기는 세탁물의 손상이 적고 세탁물이 잘 엉키지 않으며 물의 사용량이 적은 장점이 있다.  Drum washing machine is a device for washing laundry by rotating the drum by the driving force of the motor in a state in which detergent, washing water and laundry in the drum. Such a drum washing machine has advantages of less damage to laundry, less tangling of laundry, and less water usage.
최근에는 건조 덕트를 통해 드럼에 열풍을 불어 넣어줌으로써 세탁물을 건조시킬 수 있는 건조 겸용 드럼 세탁기가 많이 사용되고 있다. 이러한 건조 겸용 드럼 세탁기는 세탁 행정, 행굼 행정, 탈수 행정, 및 건조 행정 등을 선택적으로 또는 연속적으로 수행한다.  Recently, a combined drum washing machine capable of drying laundry by blowing hot air into the drum through a drying duct has been used. Such a dry combined drum washing machine selectively or continuously performs a washing stroke, a rinse stroke, a dehydration stroke, a drying stroke, and the like.
도 1은 종래 건조 겸용 드럼 세탁기의 주요 구성을 개략적으로 나타낸 측단면도이다.  1 is a side cross-sectional view schematically showing the main configuration of a conventional combined drying drum washing machine.
도 1을 참조하면, 일반적으로 드럼 세탁기는 전면에 세탁물 투입구가 형성된 캐비닛 (10), 상기 캐비닛 (10)의 세탁물 투입구에 개폐 가능하게 설치된 도어 (11), 상기 캐비닛 (10)의 내부에 세탁수를 저장하도록 설치된 터브 (20), 상기 터브 (20) 내에 회전 가능하게 설치된 드럼 (22), 및 상기 터브 (20)에 설치되어 상기 드럼 (22)에 구동력을 전달하는 모터 (50)를 포함하여 구성된다.  Referring to FIG. 1, a drum washing machine generally includes a cabinet 10 having a laundry inlet formed on a front surface thereof, a door 11 installed to be opened and closed at a laundry inlet of the cabinet 10, and washing water inside the cabinet 10. A tub 20 installed to store the drum, a drum 22 rotatably installed in the tub 20, and a motor 50 installed in the tub 20 to transmit driving force to the drum 22. It is composed.
그리고, 상기 드럼 세탁기에는 건조 행정을 위해 공기를 순환시키는 건조 덕트 (60)와 웅축 덕트 (70)가 설치된다. 상기 건조 덕트 (60)의 내부에는 상기 터브 (20) 내측으로 열풍을 토출할 수 있도록 히터 (63)와 송풍팬 (67)이 설치된다. 상기 건조 덕트 (60)와 웅축 덕트 (70)는 상호 연통됨과 동시에 드럼 (22)의 내부와 연통되도록 설치된다. 상기 터브 (20)에는 상기 건조 덕트 (60)를 통한 더운 공기가 흡입되는 흡기구와 상기 웅축 덕트 (70)로 공기가 배출되는 배기구가 형성된다. 상기 웅축 덕트 (70)에는 공기 중의 습기를 웅축시킬 수 있도록 넁각수를 공급하는 급수 노즐 (75)이 설치된다. 상기와 같이 구성된 드럼 세탁기는, 일반적으로 아래와 같은 방식에 따라 세탁 행정과 건조 행정이 수행된다. And, the drum washing machine to circulate the air for the drying stroke A drying duct 60 and a male duct 70 are installed. A heater 63 and a blowing fan 67 are installed in the drying duct 60 to discharge hot air into the tub 20. The drying duct 60 and the male duct 70 are installed to communicate with each other and at the same time communicate with the inside of the drum 22. The tub 20 is formed with an intake port through which the hot air is drawn through the drying duct 60 and an exhaust port through which the air is discharged to the male duct 70. The expansion duct 70 is provided with a water supply nozzle 75 for supplying water angle so as to expand the moisture in the air. In the drum washing machine configured as described above, a washing stroke and a drying stroke are generally performed in the following manner.
사용자는 도어 (11)를 열고 드럼 (22) 안으로 세탁물을 투입한 후 도어 (11)를 닫아 드럼 (22)을 밀폐한다. 세탁 행정이 시작되면 급수 장치 (15)는 물을 급수한다. 급수된 물은 히터 (17)에 의해 가열되어 세쎄통 (12)의 세제와 흔합된 후 터브 (20)의 내부로 공급되고, 통공을 통해 드럼 (22)의 내부로 유입되어 세탁물에 적셔진다. 이어서, 모터 (50)가 구동되어 설정된 세탁 시간 동안 드럼 (22)을 회전시킨 후, 배수 펌프 (80)에 의해 터브 (20) 내의 오염된 물이 배수 호스 (83)를 통해 세탁기 외부로 배수된다.  The user opens the door 11, puts laundry into the drum 22, and closes the door 11 to seal the drum 22. When the washing stroke starts, the water supply device 15 waters the water. The water supplied is heated by the heater 17 and mixed with the detergent of the cesegong 12 and then supplied to the inside of the tub 20, introduced into the drum 22 through the through hole, and wetted with laundry. Subsequently, after the motor 50 is driven to rotate the drum 22 for a set washing time, the contaminated water in the tub 20 is drained out of the washing machine through the drain hose 83 by the drain pump 80. .
그리고, 건조 행정이 시작되면 건조 덕트 (60)의 히터 (63)와 송풍팬 (67)에 전원이 인가되고, 발생된 열풍은 건조 덕트 (60)의 안내에 의해 드럼 (22)의 내부로 유입된다. 드럼 (22) 내의 열풍은 세탁물을 가열하여 건조시키면서 저온 다습한 공기로 바뀌고, 상기 저온 다습한 공기는 터브 (20)의 배기구를 통해 응축 덕트 (70)로 배출된다. 웅축 덕트 (70)에 공급된 상기 저온 다습한 공기는 급수 노즐 (75)을 통해 공급된 냉각수에 의해 웅축되어 수분을 잃는다. 이렇게 건조된 공기는 송풍팬 (67)에 의해 다시 건조 덕트 (60)로 유입되고, 이러한 일련의 과정이 반복적으로 수행되어 세탁물이 건조된다.  When the drying stroke is started, power is applied to the heater 63 and the blowing fan 67 of the drying duct 60, and the generated hot air flows into the drum 22 by the guide of the drying duct 60. do. The hot air in the drum 22 is changed to low temperature and humid air while heating and drying the laundry, and the low temperature and humid air is discharged to the condensation duct 70 through the exhaust port of the tub 20. The low temperature and humid air supplied to the expansion duct 70 is compressed by the cooling water supplied through the water supply nozzle 75 to lose moisture. The air thus dried is introduced into the drying duct 60 again by the blowing fan 67, and this series of processes is repeatedly performed to dry the laundry.
그런데, 이러한 세척 및 건조 행정에서, 물의 가열을 위한 에너지 사용, 공기의 가열을 위한 에너지 사용 및 응축열의 손실 등에 의한 에너지 손실 등이 발생하며, 이로 인해 다량의 열적 에너지 사용 및 손실이 불가피하게 발생한다. 드럼 세탁기는 상대적으로 세탁 시간이 길고 소비 전력이 크기 때문에, 가열 장치나 웅축 장치의 에너지 효율을 높여 세탁 및 건조 행정에서의 에너지 사용 및 손실을 줄이고자 하는 시도가 다각적으로 이루어져 왔다. 하지만, 이러한 장치의 효율화를 통한 에너지 절감은 한계에 부딪히고 있다. However, in such washing and drying strokes, energy loss due to energy use for heating water, energy use for heating air, and loss of condensation heat, etc. occurs, which inevitably causes a large amount of thermal energy use and loss. . Due to the relatively long washing time and the high power consumption of the drum washing machine, various attempts have been made to reduce energy use and loss in the washing and drying strokes by increasing the energy efficiency of the heating device or the shafting device. However, energy savings through efficiency of these devices are facing limitations.
특히, 최근 들어 세탁기의 규모가 대형화되고 환경 친화적인 제품의 중요성이 강조됨에 따라, 에너지 절감의 필요성이 더욱더 높아지고 있다.  In particular, as the size of washing machines has increased in recent years and the importance of environmentally friendly products is emphasized, the necessity of energy saving is increasing.
【발명의 내용】 [Content of invention]
【해결하고자 하는 과제】  Problem to be solved
본 발명은 세탁 및 건조 행정에서 소요되는 에너지의 절감을 가능케 하는 세탁기를 제공하기 위한 것이다.  The present invention is to provide a washing machine that enables the reduction of energy required in the washing and drying stroke.
【과제의 해결 수단】 [Measures of problem]
본 발명에 따르면, Si/Al의 원자비가 15 이하이고, 하기 VmesoAccording to the present invention, the atomic ratio of Si / Al is 15 or less, and V meso and
Vmicro의 체적 합으로 정의되는 기공의 총 비체적 Vtotal이 0.3 cmVg 이상인 다공성 알루미노실리케이트를 포함하는 흡습 부재가 구비된 세탁기가 제공된다: The total pore volume defined as the sum of the total Vmicro specific volume V is equipped with a moisture absorption member which comprises a porous aluminosilicate is less than 0.3 cmVg washing machine is provided with:
상기 Vmeso는 2 내지 300 nm의 기공 크기의 메소가공에 대한 바렛-조이너-할렌다 (BJH) 누적 체적이고, V meso is a Barrett-Joiner-Hellenda (BJH) cumulative volume for mesoprocessing of 2 to 300 nm,
상기 \ ^。는 아르곤 흡착 브루너-에메트 -텔러 (BET) 표면적으로부터 t-플롯법에 의해 계산된 2 nm 미만의 기공 크기를 갖는 미세기공의 체적이다.  Is the volume of micropores having a pore size of less than 2 nm calculated by the t-plot method from the argon adsorption Brunner-Emeth-Teller (BET) surface area.
본 발명에 따르면, 상기 세탁기는  According to the invention, the washing machine is
세탁물 투입구가 형성된 캐비닛 (10),  A cabinet 10 having a laundry inlet,
상기 세탁물 투입구에 개폐 가능하게 설치된 도어 (11),  A door 11 installed to be opened and closed at the laundry inlet;
상기 캐비닛 내부에 세탁수를 저장하도록 설치된 터브 (20),  Tub 20 installed to store the wash water in the cabinet,
상기 터브 내에 회전 가능하게 설치된 드럼 (22),  A drum 22 rotatably installed in the tub,
상기 터브에 설치되어 상기 드럼에 구동력을 전달하는 모터 (50), 및 상기 터브의 상부측 외주면에 고정되고 양 끝단부가 상기 터브의 흡기구 및 배기구에 연결되어 상기 드럼 내부로 열풍을 순환시키는 건조 덕트 (60)를 포함하고; A motor 50 installed in the tub and transmitting a driving force to the drum, and fixed to an outer circumferential surface of the upper side of the tub, with both ends of the tub A drying duct (60) connected to an intake port and an exhaust port to circulate hot air into the drum;
상기 건조 덕트 (60) 내에는 상기 다공성 알루미노실리케이트를 포함하는 흡습 부재 (65), 상기 흡습 부재의 외주면에 부착되어 흡습 부재와 공기를 가열하는 히터 (63), 및 공기를 순환시키는 송풍팬 (67)이 내장되어 있다. 이하, 발명의 구현 예에 따른 세탁기에 대하여 설명하기로 한다.  In the drying duct 60, a moisture absorbing member 65 including the porous aluminosilicate, a heater 63 attached to an outer circumferential surface of the moisture absorbing member and heating the moisture absorbing member and air, and a blowing fan for circulating air ( 67) is built in. Hereinafter, a washing machine according to an embodiment of the present invention will be described.
그에 앞서, 본 명세서 전체에서 명시적인 언급이 없는 한, 전문용어는 단지 특정 구현예를 언급하기 위한 것이며, 본 발명을 한정하는 것을 의도하지 않는다.  Prior to this, the terminology is for the purpose of describing particular embodiments only and is not intended to limit the invention, unless expressly stated throughout this specification.
그리고, 여기서 사용되는 단수 형태들은 문구들이 이와 명백히 반대의 의미를 나타내지 않는 한 복수 형태들도 포함한다.  As used herein, the singular forms “a,” “an” and “the” include plural forms as well, unless the phrases clearly indicate the opposite.
또한, 명세서에서 사용되는 '포함 '의 의미는 특정 특성, 영역, 정수, 단계, 동작, 요소 또는 성분을 구체화하며, 다른 특정 특성, 영역, 정수, 단계, 동작, 요소, 또는 성분의 부가를 제외시키는 것은 아니다. 발명의 일 구현 예에 따르면, Si/Al의 원자비가 15 이하이고, 하기 In addition, the meaning of "include" as used herein specifies a particular characteristic, region, integer, step, operation, element or component, excluding the addition of other specific characteristics, region, integer, step, operation, element, or component. It is not meant to be. According to one embodiment of the invention, the atomic ratio of Si / Al is 15 or less,
Vmeso및 Vmicro의 체적 합으로 정의되는 기공의 총 비체적 Vtotal이 0.3 Cm3/g 이상인 다공성 알루미노실리케이트를 포함하는 흡습 부재가 구비된 세탁기가 제공된다: A washing machine is provided with a hygroscopic member comprising a porous aluminosilicate having a total specific volume V tot al of pores defined by the volume sum of V meso and Vmicro of at least 0.3 Cm 3 / g:
상기 Vmeso는 2 내지 300 nm의 기공 크기의 메소기공에 대한 바렛-조이너-할렌다 (BJH) 누적 체적이고, V meso is a Barrett-Joiner-Hellenda (BJH) cumulative volume for mesopores having a pore size of 2 to 300 nm,
상기 ν„αο는 아르곤 흡착 브루너-에메트 -텔러 (BET) 표면적으로부터 t-플롯법에 의해 계산된 2 nm 미만의 기공 크기를 갖는 미세기공의 체적이다. 바람직하게는, 상기 다공성 알루미노실리케이트가 갖는 Vmeso는 0.05 cmVg 이상 혹은 0.05 내지 1.0 cmVg인 것이 본 발명에 따른 제반 특성의 발현에 유리할 수 있다. 구체적으로, 상기 Vmeso는 0Ό5 cmVg 이상, 혹은 0.09 cmVg 이상, 혹은 0.1 cmVg 이상, 혹은 0.15 cm3/g 이상, 혹은 0.2 cmVg 이상, 혹은 0.25 cmVg 이상, 혹은 0.5 cm3/g 이상일 수 있고; 1.0 cmV 이하, 흑은 0.6 cm3/g 이하, 흑은 0.55 cm3/g 이하일 수 있다. The ν "αο argon adsorption Bruner-a Teller (BET) the volume of fine pores having a pore size of less than a 2 nm calculated from the specific surface area method from the plot t--Emmett. Preferably, V meso of the porous aluminosilicate is 0.05 cmVg or more or 0.05 to 1.0 cmVg may be advantageous for the expression of various properties according to the present invention. Specifically, V meso is 0Ό5 cmVg or more, or At least 0.09 cmVg, or at least 0.1 cmVg, or at least 0.15 cm 3 / g, or at least 0.2 cmVg, or at least 0.25 cmVg, or at least 0.5 cm 3 / g; 1.0 cmV or less, black may be 0.6 cm 3 / g or less, black may be 0.55 cm 3 / g or less.
그리고, 상기 다공성 알루미노실리케이트가 갖는 Vmicr。는 0Ό1 cmVg 이상 혹은 0.01 내지 0.5 cm3/g인 것이 본 발명에 따른 제반 특성의 발현에 유리할 수 있다. 구체적으로, 상기 Vndcro는 0.01 cmVg 이상, 혹은 0Ό3 cmVg 이상, 혹은 0.06 cmVg 이상, 혹은 0.09 cm3/g 이상, 혹은 0.1 cm3/g 이상, 혹은 0.15 cm 이상, 혹은 0.2 cmVg 이상, 혹은 0.25 cm3/g 이상일 수 있고; 0.5 cmVg 이하, 흑은 0.3 cm3/g 이하, 흑은 0.28 cmVg 이하일 수 있다. In addition, Vmi cr... Of the porous aluminosilicate may be more than 0Ό1 cmVg or 0.01 to 0.5 cm 3 / g, which may be advantageous for expression of various properties according to the present invention. Specifically, the Vndcro is 0.01 cmVg or more, or 0Ό3 cmVg or more, or 0.06 cmVg or more, or 0.09 cm 3 / g or more, 0.1 cm 3 / g or more, or 0.15 cm or more, or 0.2 cmVg or more, or 0.25 cm 3 / g or greater; 0.5 cmVg or less, black may be 0.3 cm 3 / g or less, black may be 0.28 cmVg or less.
그리고, 상기 다공성 알루미노실리케이트가 갖는 Vmeso 및 V^icr。의 체적 합으로 정의되는 기공의 총 비체적 Vtotal은 0.3 cmVg 이상 흑은 으3 내지 0.8 cmVg인 것이 본 발명에 따른 제반 특성의 발현에 보다 유리할 수 있다. 구체적으로, 상기 Vtotai은 0.3 cm3/ g 이상, 흑은 0.32 cm3/ g 이상, 혹은 0.34 cmVg 이상일 수 있고; 0.8 cm3/g 이하, 혹은 0.7 cm3/g 이하, 흑은 0.65 cmVg 이하일 수 있다. And, the expression of Vmeso and V ^ icr. Total specific volume of pores that are defined as the volume V total is overall characteristics according to the invention that the at least 0.3 cmVg black is coming from 3 to 0.8 cmVg of having the porous aluminosilicate May be more advantageous. Specifically, the Vtotai may be 0.3 cm 3 / g or more, black is 0.32 cm 3 / g or more, or 0.34 cmVg or more; 0.8 cm 3 / g or less, or 0.7 cm 3 / g or less, black may be 0.65 cmVg or less.
또한, 바람직하게는, 상기 다공성 알루미노실리케이트는 200 rnVg 이상 흑은 200 내지 850 m2/g의 아르곤 흡착 브루너-에메트 -텔러 (BET) 표면적을 가질 수 있다. 구체적으로 상기 BET 표면적은 200 m2/g 이상, 흑은 250 mVg 이상, 혹은 300 m2/g 이상, 혹은 350 n /g 이상, 흑은 370 mVg 이상일 수 있고; 850 mVg 이하, 혹은 800 m2/g 이하, 흑은 750 n /g 이하, 혹은 730 mVg 이하일 수 있다. 본 발명자들의 실험 결과, 상술한 기공 체적 특성 및 Si/Al의 원자비 등을 충족하는 다공성 알루미노실리케이트를 포함하는 흡습 부재를 세탁기에 적용할 경우 세탁 및 건조 행정에 소요되는 에너지의 절감이 가능한 것으로 확인되었다. 이는 다음과 같은 원리에 기인한 것이다. 먼저, 상술한 제반 특성, 예를 들어, 기공 체적 특성 및 비표면적 등을 나타내는 다공성 알루미노실리케이트는 세탁기의 건조 덕트 내의 조건에 대응하는 상온, 고습의 조건 하에서 우수한 흡습 특성을 나타낼 수 있고, 높은 흡습량을 나타낼 수 있다. 따라서, 이러한 다공성 알루미노실리케이트를 포함하는 흡습 부재를 사용하여 세탁물의 건조 행정을 적절히 수행할 수 있다. Further, preferably, the porous aluminosilicate may have an argon adsorption Brunner-Emmett-Teller (BET) surface area of 200 to 850 m 2 / g black or more than 200 rnVg. Specifically, the BET surface area may be 200 m 2 / g or more, black 250 mVg or more, or 300 m 2 / g or more, or 350 n / g or more, and black may be 370 mVg or more; 850 mVg or less, or 800 m 2 / g or less, black may be 750 n / g or less, or 730 mVg or less. As a result of the experiments of the present inventors, when a moisture absorbing member including a porous aluminosilicate meeting the pore volume characteristics and the atomic ratio of Si / Al is applied to a washing machine, it is possible to reduce energy required for washing and drying strokes. Confirmed. This is due to the following principle. First, porous aluminosilicates exhibiting all the above-described characteristics, for example, pore volume characteristics, specific surface areas, and the like, are subjected to conditions in a drying duct of a washing machine. Under the conditions of normal temperature and high humidity, excellent moisture absorption characteristics can be exhibited and high moisture absorption can be exhibited. Therefore, the drying process of the laundry can be appropriately performed by using the hygroscopic member including such porous aluminosilicate.
또한, 이러한 다공성 알루미노실리케이트의 흡습 과정은 발열 반웅에 해당하므로, 이때 발생하는 흡착열을 건조를 위한 공기의 가열에 사용할 수 있다. 따라서, 상기 건조 행정에서 사용 또는 손실되는 에너지를 크게 줄이거나, 실질적으로 별도의 에너지 투입 없이 건조 행정을 진행할 수 있게 된다.  In addition, the moisture absorption process of the porous aluminosilicate corresponds to the exothermic reaction, so that the heat of adsorption generated at this time may be used for heating the air for drying. Therefore, it is possible to greatly reduce the energy used or lost in the drying stroke, or to proceed with the drying stroke substantially without additional energy input.
예를 들어, 일 구현예의 흡습 부재에 포함되는 상기 다공성 알루미노실리케이트는 25 °C 및 95%의 상대 습도 하에, 하기 식 1로 정의되는 흡습량 (%; 25 °C, 95% RH)이 22% 이상 혹은 22 내지 50%에 이를 정도로 우수한 흡습량을 나타낼 수 있고, 이러한 높은 흡습량에 따라 흡착열 역시 높게 발생시킬 수 있다. 따라서, 이러한 일 구현예의 흡습 부재는 세탁기의 건조 행정에 바람직하게 사용되어 에너지 절감 효과를 나타낼 수 있다: For example, the porous aluminosilicate is 25 ° C and under a relative humidity of 95%, the moisture absorption amount, which is defined by the following formula 1, which is included in one embodiment the moisture absorption member (%; 25 ° C, 95% RH) 22 The moisture absorption amount may be excellent as much as% or more or 22 to 50%, and the heat of adsorption may also be generated according to the high moisture absorption amount. Therefore, the moisture absorbing member of this embodiment can be preferably used in the drying stroke of the washing machine to exhibit an energy saving effect:
[식 1]  [Equation 1]
흡습량 (%; 25 °C, 95% RH) = [W (g) / AS (g)]*100 식 1에서, AS (g)는 다공성 알루미노실리케이트의 중량을 나타내고, WMoisture absorption (%; 25 ° C., 95% RH) = [W (g) / AS (g)] * 100 In formula 1, AS (g) represents the weight of the porous aluminosilicate, W
(g)는 25 °C 및 95%의 상대 습도 하에서 상기 AS (g)의 다공성 알루미노실리케이트를 사용하여 흡습을 진행하였을 때, 다공성 알루미노실리케이트가 최대로 흡수한 물의 중량을 나타낸다. 한편, 상기 흡습 부재를 사용하여 건조 행정을 진행한 후에는, 이러한 흡습재로부터 흡수된 수분을 탈습시키는 과정을 거칠 필요가 있다. 그런데, 일 구현예의 흡습 부재, 특히, 상술한 Si/Al의 원자비 범위 및 기공 체적 특성 등을 충족하는 다공성 알루미노실리케이트는 상대 습도를 낮추는 것만으로 상당한 자연 탈습이 이루어질 수 있는 것으로 확인되었다. 특히, 상기 0.05 cmVg 이상 혹은 0.05 내지 1.0 cm3/g의 Vmeso 범위를 층족함에 따라, 자연 탈습되는 비율을 보다 높일 수 있다. 예를 들어, 일 구현예의 흡습 부재에 포함되는 다공성 알루미노실리케이트는 하기 식 2로 정의되는 상대습도별 흡습량 비가 1.2 이상, 흑은 1.22 내지 5.0, 흑은 1.24 내지 3.0으로 되어, 상대 습도를 95%에서 50%로 낮추는 것만으로 별도의 에너지 투입 없이 매우 높은 수준의 자연 탈습 (예를 들어, 약 30% 이상)이 이루어질 수 있다: (g) shows the weight of the water absorbed to the maximum by the porous aluminosilicate when the moisture absorption was carried out using the porous aluminosilicate of AS (g) at 25 ° C and a relative humidity of 9 5 %. On the other hand, after carrying out a drying process using the said moisture absorption member, it is necessary to go through the process of dehumidifying the moisture absorbed from such a moisture absorption material. By the way, it was confirmed that the moisture absorbing member of one embodiment, in particular, the porous aluminosilicate satisfying the above-described atomic ratio range and pore volume characteristic of Si / Al, can achieve a significant natural dehumidification simply by lowering the relative humidity. In particular, the stratified V meso range of 0.05 cmVg or more or 0.05 to 1.0 cm 3 / g. Accordingly, the rate of natural dehumidification can be further increased. For example, the porous aluminosilicate included in the moisture absorption member of one embodiment has a relative moisture absorption ratio of 1.2 or more, black is 1.22 to 5.0, black is 1.24 to 3.0, and the relative humidity is 95. By lowering from 50% to 50%, very high levels of spontaneous dehumidification (e.g., about 30% or more) can be achieved without extra energy input:
[식 2]  [Equation 2]
상대습도별 흡습량 비 = 흡습량 (%; 25 °C, 95% RH)/ 흡습량 (%; 25 °C, 50% RH) 식 2에서, 흡습량 (%; 25 °C, 95% RH)은 상술한 식 1로 정의되는 흡습량을 나타내고, 흡습량 (%; 25°C, 50% RH)은 상대 습도를 95%에서 50%로 낮추어 상기 다공성 알루미노실리케이트로부터 탈습을 진행하였을 때, [Wl (g) I AS (g)]*100의 식에 따라 산출된 흡습량을 나타내며, Wl (g)은 탈습 진행된 후에 AS (g)의 다공성 알루미노실리케이트가 최대로 흡수한 물의 중량을 나타낸다. 이에 따라, 일 구현예의 흡습 부재는 일단 건조 행정의 진행 후 이로부터 수분을 탈습하기 위해 소요되는 에너지 사용량 역시 줄일 수 있다. 이와 반대로, 일 구현예의 특성을 층족하지 못하는 다공성 알루미노실리케이트를 적용할 경우, 상대적으로 자연 탈습이 잘 이루어지지 않아 에너지 사용량이 증가될 수밖에 없음이 확인되었다. Moisture absorption ratio by relative humidity = moisture absorption (%; 25 ° C, 95% RH) / moisture absorption (%; 25 ° C, 50% RH) In equation 2, moisture absorption (%; 25 ° C, 95% RH ) Represents the moisture absorption defined by the above formula 1, the moisture absorption amount (%; 25 ° C, 50% RH) is lowered from 95% to 50% relative humidity when dehumidification from the porous aluminosilicate, The moisture absorption calculated according to the formula [Wl (g) I AS (g)] * 100, Wl (g) represents the weight of the water absorbed maximum by the porous aluminosilicate of AS (g) after dehumidification proceeds. . Accordingly, the moisture absorbing member of the embodiment can also reduce the amount of energy used to dehumidify moisture from the drying stroke once. On the contrary, when the porous aluminosilicate that does not satisfy the characteristics of the embodiment is applied, it is confirmed that energy consumption is inevitably increased due to relatively poor dehumidification.
부가하여, 상기 일 구현예의 흡습 부재를 탈습하는 과정에서 일정 수준의 웅축열이 발생할 수 있고, 이러한 웅축열은 세척 행정에서 물을 가열하기 위한 에너지로도 적용될 수 있다. 따라서, 이러한 면에서도 일 구현예의 흡습 부재는 세탁기의 에너지 사용이나 손실을 줄여 큰 에너지 절감 효과를 거둘 수 있다. 한편, 상술한 특성을 나타내는 다공성 알루미노실리케이트로는 이전에 상업적으로 입수 가능한 다공성 알루미노실리케이트 중에서 위 물성을 나타내는 것을 선택 및 사용하거나, 직접 제조하여 사용할 수 있다. 예를 들어, 이러한 다공성 알루미노실리케이트로서, Ca 양이온, Na 양이온, K 양이온 또는 Fe 양이온과 같은 알칼리 금속, 알칼리토금속 또는 전이금속의 양이온이 알루미노실리케이트의 음이온에 결합된 제올라이트 형태의 다공성 알루미노실리케이트를 사용할 수 있다. In addition, a certain level of heat storage may occur in the process of dehumidifying the moisture absorbing member of the embodiment, and the heat storage may be applied as energy for heating water in the washing stroke. Therefore, in this respect, the moisture absorbing member of the embodiment can achieve a large energy saving effect by reducing energy use or loss of the washing machine. On the other hand, the porous aluminosilicate exhibiting the above-described characteristics has previously been Among the commercially available porous aluminosilicates, those showing gastric properties may be selected and used, or may be manufactured and used directly. For example, as such porous aluminosilicates, porous aluminosilicates in the form of zeolites in which cations of alkali metals, alkaline earth metals or transition metals such as Ca cations, Na cations, K cations or Fe cations are bonded to the anions of aluminosilicates. Can be used.
구체적으로, 상기 다공성 알루미노실리케이트는 하기 화학식 1로 표시되는 것으로 될 수 있다:  Specifically, the porous aluminosilicate may be represented by Formula 1 below:
[화학식 1]  [Formula 1]
MxSiAlyOa(OH)b(H20)c 상기 화학식 1에서, M은 알칼리 금속, 알칼리 토금속 또는 전이금속을 나타내고, X 및 y는 각각 독립적으로 양수를 나타내고, a, b 및 c는 0 이상의 수를 나타낸다 (단, a+b는 양수이다 .). M x SiAl y Oa (OH) b (H 2 0) c In Chemical Formula 1, M represents an alkali metal, an alkaline earth metal or a transition metal, X and y each independently represent a positive number, and a, b and c are A number of zero or more is represented (where a + b is a positive number).
이러한 화학식 1에서, 상기 M은ᅳ Ca, Na, K 또는 Fe로 될 수 있고, 상기 X, y, a, b 및 c는 각 구성 원소나 이온의 원자가를 고려하여 결정될 수 있다.  In Formula 1, M may be Ca, Na, K, or Fe, and X, y, a, b, and c may be determined in consideration of the valence of each constituent element or ion.
바람직하게는, 상기 다공성 알루미노실리케이트가 갖는 Si/Al의 원자비는 15 이하, 혹은 1 초과 15 이하인 것이 상술한 제반 특성의 발현에 유리할 수 있다. 구체적으로, 상기 Si/Al의 원자비는 15 이하, 흑은 13.5 이하, 혹은 13 이하, 흑은 12.5 이하일 수 있고; 1.0 초과, 흑은 1.1 이상, 혹은 1.2 이상일 수 있다. 구체적인 일 예에서, 상업적으로 입수 가능한 상기 다공성 알루미노실리케이트의 예로는 BEA형 또는 13X형 제올라이트 등을 들 수 있다.  Preferably, the atomic ratio of Si / Al in the porous aluminosilicate is 15 or less, or more than 1 and 15 or less, it may be advantageous for the above-mentioned expression. Specifically, the atomic ratio of Si / Al may be 15 or less, black may be 13.5 or less, or 13 or less, and black may be 12.5 or less; Greater than 1.0, black may be 1.1 or greater, or 1.2 or greater. In a specific example, examples of the commercially available porous aluminosilicate include BEA type or 13X type zeolite.
또한, 상술한 특성을 나타내는 다공성 알루미노실리케이트를 제조할 수 있는 적절한 방법으로는, 커플드 알칼리 -매개 용해 및 수성 매질 내에서 다공성 알루미노실리케이트 전구체의 침전 반웅에 의해 제조하는 방법을 들 수 있다. 이때, 규소 원 (silicon sources)으로는 훔드 실리카, 실리케이트, 알루미노실리케이트, 점토, 미네랄, 메타카올린, 활성 점토, 플라이 애쉬, 슬래그, 포졸란 등이 사용될 수 있다. 그리고, 알루미늄 원 (aluminium sources)으로는 알루미나, 알루미네이트, 알루미늄 염, 점토, 메타카올린, 활성 점토, 플라이 애쉬, 슬래그, 포졸란 등이 사용될 수 있다. In addition, suitable methods for producing porous aluminosilicates exhibiting the above-mentioned characteristics include a method of preparing by coupled reaction of the coupled alumino-mediated dissolution and precipitation of the porous aluminosilicate precursor in an aqueous medium. At this time, as silicon sources (humide silica, silicate, aluminosilicate, clay, mineral, metakaolin, activated clay, fly ash, slag, pozzolane, etc. may be used. As aluminum sources, alumina, aluminate, aluminum salt, clay, metakaolin, activated clay, fly ash, slag, pozzolane, and the like may be used.
비제한적인 예로, 발명의 구현 예에 따르면, 상기 다공성 알루미노실리케이트는 i) 염기성 또는 알칼리 용액 (예를 들어 수산화 나트륨 용액)에 규소 원, 알루미늄 원 및 물을 첨가하고 교반하여 특정 금속 원자 비 (예를 들어 Na:Al:Si=3:l:2)를 만족하는 지오폴리머 수지 (geopolymer resin)을 형성시키는 단계; ii) 상기 지오폴리머 수지를 상압 하에서 저온 (예를 들어 60 내지 80 °C) 열처리하는 단계; 및 iii) 열처리된 지오폴리머 수지를 세척하여 중화시키는 단계를 포함하는 방법을 통해 제조될 수 있다. 특히, 발명의 구현 예에 따르면, 특정 금속 원자비를 만족하는 지오폴리머 수지를 상압 및 저은 (예를 들어 60 내지 80 °C, 바람직하게는 65 내지 75 °C)조건 하에서 열처리함으로써, 상술한 제반 특성을 나타내는 다공성 알루미노실리케이트가 얻어질 수 있다. As a non-limiting example, according to an embodiment of the invention, the porous aluminosilicate is i) added to a basic or alkaline solution (e.g. sodium hydroxide solution) and stirred with the addition of a silicon source, an aluminum source and water to a specific metal atom ratio ( Forming a geopolymer resin that satisfies, for example, Na: Al: Si = 3: l: 2); ii) heat treating the geopolymer resin at low temperature (eg, 60 to 80 ° C.) under atmospheric pressure; And iii) washing and neutralizing the heat treated geopolymer resin. In particular, according to an embodiment of the present invention, the above-described heat treatment is performed by heat treating a geopolymer resin satisfying a specific metal atomic ratio under atmospheric pressure and low temperature (for example, 60 to 80 ° C., preferably 65 to 75 ° C.). Porous aluminosilicates exhibiting properties can be obtained.
한편, 상술한 제반 특성을 나타내는 다공성 알루미노실리케이트를 그 자체로 일 구현예의 흡습 부재로 사용하거나, 이에 적절한 첨가제 등을 부가하여 일 구현예의 흡습 부재를 제조 및 사용할 수 있다. 이때 사용 가능한 첨가제의 종류는 특히 제한되지 않고, 이전부터 흡습 부재에 포함 가능한 것으로 알려진 임의의 첨가제를 사용할 수 있다. 한편, 도 2를 참고하면, 발명의 구현 예에 따른 세탁기는  On the other hand, the porous aluminosilicate exhibiting the above-described characteristics can be used as a moisture absorbing member of one embodiment by itself, or by adding an appropriate additive or the like can be prepared and used the moisture absorbing member of one embodiment. At this time, the kind of the additive which can be used is not particularly limited, and any additive known to be included in the hygroscopic member can be used. On the other hand, referring to Figure 2, a washing machine according to an embodiment of the invention
세탁물 투입구가 형성된 캐비닛 (10),  A cabinet 10 having a laundry inlet,
상기 세탁물 투입구에 개폐 가능하게 설치된 도어 (11),  A door 11 installed to be opened and closed at the laundry inlet;
상기 캐비닛 내부에 세탁수를 저장하도록 설치된 터브 (20),  Tub 20 installed to store the wash water in the cabinet,
상기 터브 내에 회전 가능하게 설치된 드럼 (22),  A drum 22 rotatably installed in the tub,
상기 터브에 설치되어 상기 드럼에 구동력을 전달하는 모터 (50), 및 상기 터브의 상부측 외주면에 고정되고 양 끝단부가 상기 터브의 흡기구 및 배기구에 연결되어 상기 드럼 내부로 열풍을 순환시키는 건조 덕트 (60)를 포함한다. A motor 50 installed in the tub and transmitting a driving force to the drum, and fixed to an outer circumferential surface of the upper side of the tub, and both ends of which are connected to an inlet and an exhaust port of the tub to circulate hot air into the drum And duct 60.
특히, 상기 건조 덕트 (60) 내에는 상기 다공성 알루미노실리케이트를 포함하는 흡습 부재 (65), 상기 흡습 부재의 외주면에 부착되어 흡습 부재와 공기를 가열하는 히터 (63), 및 공기를 순환시키는 송풍팬 (67)이 내장되어 있다.  In particular, in the drying duct 60, a moisture absorbing member 65 including the porous aluminosilicate, a heater 63 attached to an outer circumferential surface of the moisture absorbing member to heat the moisture absorbing member and air, and a blower for circulating air. The fan 67 is built in.
도 2에 나타낸 발명의 구현 예에 따른 세탁기는, 도 1에 나타낸 종래의 세탁기와 비교하여, 건조 덕트 (60) 내에 구비된 흡습 부재 (65)를 더 포함하고, 웅축 덕트 (70)와 급수 노즐 (75)을 포함하지 않는다.  The washing machine according to the embodiment of the present invention shown in FIG. 2 further includes a moisture absorbing member 65 provided in the drying duct 60, as compared with the conventional washing machine shown in FIG. 1, and includes a male duct 70 and a water supply nozzle. Does not include (75).
도 1의 일반적인 세탁기에서, 웅축 덕트 (70)는 건조 행정의 수행시 드럼 (22)으로부터 배출된 저온 다습한 공기를 응축시켜 습도를 낮추기 위한 수단으로서, 급수 노즐 (75)을 통해 공급된 넁각수가 흐른다.  In the general washing machine of FIG. 1, the expansion duct 70 is a means for lowering humidity by condensing low temperature and humid air discharged from the drum 22 when performing a drying stroke, and the water supply angle supplied through the water supply nozzle 75. Flow.
그런데, 발명의 구현 예에 따른 세탁기에는 상술한 제반 특성을 충족하는 다공성 알루미노실리케이트를 포함하는 흡습 부재 (65)가 구비됨에 따라, 고습의 조건 하에서 우수한 흡습 특성을 나타낼 수 있어, 상기 웅축 덕트에 대웅하는 수단 없이도 건조 행정의 수행이 가능하다.  By the way, the washing machine according to the embodiment of the present invention is provided with a moisture absorbing member 65 including porous aluminosilicate that meets the above-described characteristics, and can exhibit excellent moisture absorption characteristics under high humidity conditions. It is possible to carry out the construction stroke without any means of estimating.
특히, 상기 흡습 부재 (65)에 포함된 다공성 알루미노실리케이트의 흡습 과정은 발열 반웅에 해당하므로, 이때 발생하는 흡착열을 건조 행정의 수행을 위한 공기의 가열에 사용할 수 있다. 따라서, 건조 행정에서 사용 또는 손실되는 에너지를 크게 줄이거나, 실질적으로 별도의 에너지 투입 없이 건조 행정이 수행될 수 있다.  In particular, the moisture absorption process of the porous aluminosilicate included in the moisture absorption member 65 corresponds to the exothermic reaction, so that the heat of adsorption generated at this time can be used for heating the air for performing the drying stroke. Thus, the energy used or lost in the drying stroke can be greatly reduced, or the drying stroke can be carried out substantially without extra energy input.
그리고, 상술한 제반 특성을 충족하는 다공성 알루미노실리케이트는 상대 습도를 낮추는 것만으로 상당한 자연 탈습이 이루어질 수 있다. 따라서, 건조 행정의 종료 후 상대 습도가 낮아지면 흡습 부재 (65)로부터 자연 탈습이 이루어질 수 있다. 필요에 따라, 세척 행정에서 히터 (63)와 송풍팬 (67)을 가동하여 흡습 부재 (65)에 대한 탈습이 이루어지도록 할 수 있다.  In addition, the porous aluminosilicate that meets the above-described characteristics can be subjected to significant natural dehumidification only by lowering the relative humidity. Therefore, natural dehumidification can be made from the moisture absorption member 65 when the relative humidity becomes low after completion of a drying stroke. If necessary, the heater 63 and the blower fan 67 may be operated in the washing stroke so that dehumidification of the moisture absorbing member 65 may be performed.
부가하여, 상기 흡습 부재 (65)에 포함된 다공성 알루미노실리케이트의 탈습 과정에서 웅축열이 발생할 수 있고, 이러한 웅축열은 세척 행정에서 물을 가열하기 위한 에너지로도 사용될 수 있다.  In addition, the heat accumulation may occur in the dehumidification process of the porous aluminosilicate included in the moisture absorbing member 65, and the heat storage may also be used as energy for heating water in the washing stroke.
상기 흡습 부재 (65)는 상술한 다공성 알루미노실리케이트를 포함하는 것으로서, 예를 들어, 임의의 컨테이터 내에 상기 다공성 알루미노실리케이트가 층진된 것일 수 있다. The moisture absorbing member 65 includes the above-mentioned porous aluminosilicate. As, for example, the porous aluminosilicate may be layered in any container.
그리고, 상기 흡습 부재 (65)는 건조 덕트 (60)의 내부 또는 일 측벽에 장착될 수 있다. 예를 들어, 상기 흡습 부재 (65)는 히터 (63)와 결합된 상태로 건조 덕트 (60)의 내부에 구비될 수 있는데, 이때 송풍팬 (67)에 의해 순환되는 다습한 공기의 유로가 흡습 부재 (65)를 관통 또는 접촉할 수 있는 위치에 구비될 수 있다. 발명의 구현 예에 따르면, 상기 세탁기는 도 2를 참조로 아래와 같은 방식에 따라 세탁 행정, 행굼 행정, 탈수 행정, 및 건조 행정이 선택적으로 또는 연속적으로 수행될 수 있다.  In addition, the moisture absorbing member 65 may be mounted inside or on one sidewall of the drying duct 60. For example, the moisture absorbing member 65 may be provided inside the drying duct 60 in a state in which the moisture absorbing member 65 is coupled to the heater 63, in which a flow path of humid air circulated by the blowing fan 67 is absorbed. It may be provided at a position capable of penetrating or contacting the member 65. According to an embodiment of the present invention, the washing machine may selectively or continuously perform a washing stroke, a rinse stroke, a dewatering stroke, and a drying stroke in the following manner with reference to FIG. 2.
먼저, 사용자는 도어 (11)를 열고 드럼 (22) 안으로 세탁물을 투입한 후 도어 (11)를 닫아 드럼 (22)을 밀폐한다. 세탁 행정이 시작되면 급수 장치 (15)는 물을 급수한다. 급수된 물은 히터 (17)에 의해 가열되어 세제통 (12)의 세제와 흔합된 후 터브 (20)의 내부로 공급되고, 통공을 통해 드럼 (22)의 내부로 유입되어 세탁물에 적셔진다. 이어서, 모터 (50)가 구동되어 설정된 세탁'시간 동안 드럼 (22)올 회전시킨 후, 배수 펌프 (80)에 의해 터브 (20) 내의 오염된 물이 배수 호스 (83)를 통해 세탁기의 외부로 배수된다. 이러한 세탁 행정이 이루어지는 동안 필요에 따라 건조 덕트 (60) 내의 히터 (63)와 송풍팬 (67)에 전원을 인가하여 흡습 부재 (65)에 대한 탈습이 이루어지도록 할 수 있다. 흡습 부재 (65)의 탈습 과정에서 발생한 웅축열은 드럼 (22)의 내부로 유입되어 물을 가열하기 위한 에너지로 사용될 수 있다. 행굼 행정이 시작되면, 급수 장치 (15)를 통해 깨끗한 물이 터브 (20) 내부로 공급되고, 설정된 행굼 시간 동안 모터 (50)가 구동된다. 행굼 설정 시간이 경과하면 모터 (50)가 정지되고, 배수펌프 (80)가 펌핑되어, 터브 (20) 내의 거품이 포함된 물이 배수 호스 (83)를 통해 세탁기의 외부로 배수된다. 탈수 행정이 시작되면, 설정된 탈수 시간 동안 모터 (50)가 구동되어 드럼 (22)을 고속으로 회전시킨다. 드럼 (22) 내의 세탁물은 원심력에 의해 탈수된다. 이때 배수 펌프 (80)가 펌핑되어, 상기 세탁물에서 빠져나은 물이 배수 호스 (83)를 통해 세탁기의 외부로 배수된다. 건조 행정이 시작되면, 건조 덕트 (60)의 히터 (63)와 송풍팬 (67)에 전원이 인가되고, 발생된 열풍은 건조 덕트 (60)의 안내에 의해 드럼 (22)의 내부로 유입된다. 드럼 (22) 내의 열풍은 세탁물을 가열하여 건조시키면서 저온 다습한 공기로 바뀌고, 상기 저온 다습한 공기는 터브 (20)의 배기구를 통해 건조 턱트 (60)로 배출된다. 여기서, 상기 저온은 히터에 의해 가열된 공기의 온도보다 낮은 온도 (예를 들어 상온)를 의미한다. 건조 턱트 (60)에 공급된 상기 저온 다습한 공기는 송풍팬 (67)에 의해 흡습 부재 (65)를 향해 순환되고, 흡습 부재 (65)에서의 흡습에 의해 수분을 잃고 건조된다. 이러한 일련의 과정이 반복적으로 수행되어 세탁물이 건조된다. First, the user opens the door 11, puts laundry into the drum 22 and closes the door 11 to seal the drum 22. When the washing stroke starts, the water supply device 15 waters the water. The water supplied is heated by the heater 17, mixed with the detergent of the detergent container 12, and then supplied into the tub 20, and introduced into the drum 22 through the through hole and wetted with laundry. Then, in the washing machine through the contaminated water drain hose (83) in the tub 20 by the then motor 50 is driven is set laundry 'time the drum 22 rotates to come over, the drain pump (80) outside Drained. During this washing process, power may be applied to the heater 63 and the blowing fan 67 in the drying duct 60 to dehumidify the moisture absorbing member 65 as necessary. The male heat generated in the dehumidification process of the moisture absorbing member 65 may be introduced into the drum 22 and used as energy for heating water. When the rinse stroke starts, clean water is supplied into the tub 20 through the water supply device 15, and the motor 50 is driven for the set rinse time. When the rinse setting time has elapsed, the motor 50 is stopped, the drain pump 80 is pumped, and the water containing bubbles in the tub 20 is drained out of the washing machine through the drain hose 83. When the dehydration stroke is started, the motor 50 is driven to set the drum 22 at high speed for the set dehydration time. The laundry in the drum 22 is dehydrated by centrifugal force. At this time, the drain pump 80 is pumped so that the water discharged from the laundry is drained to the outside of the washing machine through the drain hose 83. When the drying stroke is started, power is applied to the heater 63 and the blowing fan 67 of the drying duct 60, and the generated hot air is introduced into the drum 22 by the guide of the drying duct 60. . The hot air in the drum 22 is converted into low temperature and humid air while the laundry is heated and dried, and the low temperature and humid air is discharged to the drying tuft 60 through the exhaust port of the tub 20. Here, the low temperature means a temperature (for example, room temperature) lower than the temperature of the air heated by the heater. The low temperature and humid air supplied to the drying tuck 60 is circulated by the blowing fan 67 toward the moisture absorbing member 65, and loses moisture by moisture absorption at the moisture absorbing member 65 and is dried. This series of steps is repeated to dry the laundry.
상술한 바와 같이, 상기 세탁기의 구동시 세탁 행정에서 물을 가열하기 위한 히터 (17)와 흡습 부재 (65)의 탈습을 위한 히터 (63)를 동시에 가동시킴으로써, 흡습 부재 (65)의 탈습 과정에서 발생한 웅축열을 추가적으로 사용할 수 있게 된다. 특히, 건조 행정에서 흡습 부재 (65)에서 흡습에 의한 흡착열 (예를 들어 상기 다공성 알루미노실리케이트 단위 중량 (kg) 당 0.17 kWh)이 발생함에 따라, 별도의 웅축 수단 (예를 들어, 웅축 덕트) 없이도 건조 행정의 수행이 가능하다.  As described above, in the dehumidification process of the moisture absorbing member 65 by simultaneously operating the heater 17 for heating the water in the washing stroke during the driving of the washing machine and the heater 63 for the dehumidifying the moisture absorbing member 65. The generated heat storage can be used additionally. In particular, as the heat of adsorption (e.g., 0.17 kWh per unit weight (kg) of the porous aluminosilicate) is generated by the moisture absorption in the moisture absorption member 65 in the drying stroke, separate expansion means (e.g., the expansion duct) The drying stroke can be carried out without.
【발명의 효과】 【Effects of the Invention】
본 발명에 따른 세탁기는 세탁 및 건조 행정에 소요되는 에너지의 절감을 가능케 한다.  The washing machine according to the present invention enables saving of energy required for washing and drying strokes.
【도면의 간단한 설명】 [Brief Description of Drawings]
도 1은 일반적인 세탁기의 내부 구조를 개략적으로 나타낸 측단면도이고,  1 is a side cross-sectional view schematically showing the internal structure of a general washing machine,
도 2는 본 발명의 일 구현 예에 따른 세탁기의 내부 구조를 개략적으로 나타낸 측단면도이다.  2 is a side cross-sectional view schematically showing the internal structure of a washing machine according to an embodiment of the present invention.
【발명을 실시하기 위한 구체적인 내용】 [Specific contents to carry out invention]
이하, 본 발명의 이해를 돕기 위하여 바람직한 실시예들을 제시한다. 그러나 하기의 실시예들은 본 발명을 예시하기 위한 것일 뿐, 본 발명을 이들만으로 한정하는 것은 아니다. 실시예 1 Hereinafter, preferred embodiments will be presented to aid in understanding the present invention. However, the following examples are only for illustrating the present invention, the present invention It is not limited only to these. Example 1
3.02g의 NaOH를 반응기에 투입한 후 3차 증류수 5.43g을 넣고 잘 섞는다. 이 용액에 그 76g의 소듐 실리케이트 (~1으 6% Na20, -26.5% Si02)를 넣고, 상온 하에서 800 rpm으로 교반하여 완전히 용해시킨다. 이렇게 준비한 용액에 메타카올린 3.8g을 투입하고 상온 하에서 800 rpm으로 40분 동안 교반하여 약 3:1:2의 Na:Al:Si 원자비를 갖는 지오폴리머 수지를 얻었다. 3.02 g of NaOH was added to the reactor, and 5.43 g of tertiary distilled water was added and mixed well. 76 g of sodium silicate (~ 1 6% Na 2 0, -26.5% Si0 2 ) was added to the solution, and the mixture was stirred at 800 rpm at room temperature to completely dissolve it. 3.8 g of metakaolin was added to the solution thus prepared, and stirred at 800 rpm for 40 minutes at room temperature to obtain a geopolymer resin having an atomic ratio Na: Al: Si of about 3: 1: 2.
상기 지오폴리머 수지를 오본 내에서 상압 및 70 °C의 조건 하에 하루 동안 가열하여 pH 14 수준의 지오폴리머 수지를 수득하였다. 열처리된 지오폴리머 수지에 층분한 양의 3차 증류수를 가하여 세척하고 10000 rpm에서 5분간 원심분리한 후 pH 14 수준의 맑은 상등액을 decantation 시켰다. 이러한 세척, 원심분리 및 decantation 단계는 상등액이 pH 7수준이 될 때까지 반복하였다ᅳ 중화된 지오폴리머 수지를 80°C의 진공 오본에서 밤새 건조하여 최종 생성물인 다공성 알루미노실리케이트를 얻었다. 실시예 2 The geopolymer resin was heated in Aubon for one day under atmospheric pressure and 70 ° C. to obtain a geopolymer resin of pH 14 level. Distilled water was added to the heat-treated geopolymer resin in an amount of tertiary distilled water, and the resultant was centrifuged at 10000 rpm for 5 minutes to decantation the clear supernatant at pH 14. This washing, centrifugation and decantation steps were repeated until the supernatant was at pH 7 level. The neutralized geopolymer resin was dried overnight in a vacuum oven at 80 ° C. to obtain the final product, porous aluminosilicate. Example 2
Zeolyst 사의 BEA 타입 제을라이트 (제품명: CP814E)를 실시예 2로 준비하였다. 실시예 3  Zeolyst BEA type zeolite (trade name: CP814E) was prepared in Example 2. Example 3
Cosmo Fine Chemicals 사의 zeolite 13X 타입 제을라이트 (제품명: CX)LITE-MS80)를 실시예 3으로 준비하였다. 비교예 1  Zeolite 13X type zeolite (product name: CX) LITE-MS80) from Cosmo Fine Chemicals was prepared in Example 3. Comparative Example 1
Zeolyst사의 ZSM-5 타입 제을라이트 (제품명: CBV8014)를 비교예 1로 준비하였다. 시험예 1  Zeolyst ZSM-5 type zeolite (product name: CBV8014) was prepared in Comparative Example 1. Test Example 1
상기 실시예 비교예의 알루미노실리케이트에 대한 제반 측정하여 하기 표 1에 나타내었다. General Examples of Aluminosilicates of Comparative Examples The measurement is shown in Table 1 below.
Si/Al 원자비는 ICP-OES Optima 7300DV를 이용하여 분석하였다. 구체적으로, Si/Al 원자비 분석을 위해 시료를 corning tube (50ml)에 분취한 후 정전기 gun으로 정전기를 제거하였다. 상기 시료에 염산 및 불산을 가하여 녹인 후, 이 용액을 초순수로 희석하였다. 이 용액에서 1 ml를 취한 후 과포화붕산수, 내부표준물질로서 스칸듐 (Sc)을 첨가한 후, 초순수로 다시 희석하였다. 표준 용액은 Blank, 1 g/ml, 5 g/ml, 10 pg/ml을 조제하였다. 초순수로 희석한 용액의 Si/Al 원자비를 상기 ICP-OES Optima 7300DV로 분석하였다.  Si / Al atomic ratio was analyzed using ICP-OES Optima 7300DV. Specifically, samples were collected in a corning tube (50ml) for Si / Al atomic ratio analysis, and then static electricity was removed with an electrostatic gun. Hydrochloric acid and hydrofluoric acid were added to the sample to dissolve it, and the solution was diluted with ultrapure water. After taking 1 ml of this solution, supersaturated boric acid and scandium (Sc) were added as internal standards, and then diluted with ultrapure water. Standard solutions were prepared with Blank, 1 g / ml, 5 g / ml, 10 pg / ml. The Si / Al atomic ratio of the ultra diluted solution was analyzed by the ICP-OES Optima 7300DV.
【표 11 Table 11
Figure imgf000016_0002
Figure imgf000016_0002
- BET (in2/ g): the Brunauer-Emmett-Teller(BET) surface area BET (in 2 / g): the Brunauer-Emmett-Teller (BET) surface area
- Vmeso (cinJ/g): 2 내지 300 nm의 기공 크기의 메소기공에 대한 바렛-조이너-할렌다 (BJH) 누적 체적 Vmeso (cin J / g): Barrett-Joiner-Halenda (BJH) cumulative volume for mesopores with a pore size of 2 to 300 nm
-
Figure imgf000016_0001
(Clrf/g): 아르곤 흡착 브루너-에메트 -텔러 (BET) 표면적으로부터 t-플롯법에 의해 계산된 2 nm 미만의 기공 크기를 갖는 미세기공의 체적 - Vtotai (cin3/g): Total pore volume 시험예 2
-
Figure imgf000016_0001
(Clrf / g): volume of micropores with pore size less than 2 nm calculated by t-plot method from argon adsorption Brunner-Emmett-Teller (BET) surface area -Vtotai (cin 3 / g): Total pore volume Test Example 2
(세탁기에 적용시 에너지 소요량 산출)  (Calculate energy requirement when applied to washing machine)
상기 실시예 및 비교예에 따른 각각의 알루미노실리케이트 2 kg을 도 Figure 2 kg of each aluminosilicate according to the Examples and Comparative Examples
2의 세탁기에 흡습 부재 (65)로서 적용하여 세탁 및 건조 행정을 진행하였다. 세탁시 사용된 물 (세척수)은 7 L 였고, 초기 온도 15°C에서 40°C로 승온하여 세탁을 진행하였다. 세탁물의 양은 3 kg 이었다. 그리고, 건조시에는 0.5 kg의 물을 건조 및 제거하였고, 이를 위해 30°C에서 60°C로 승온하였다. 이러한 세탁 및 건조 과정에서 에너지 소요량을 산출하였다. 또한, 알루미노실리케이트를 적용하지 않은 것을 제외하고, 동일 조건 하의 세탁 및 건조 행정 (비교예 2; 즉, 흡습 부재를 사용하지 않는 기존의 세탁 및 건조 행정과 동일한 방법)에서의 에너지 소요량을 산출하여 하기 표 2에 정리하여 나타내었다. It applied to the washing machine of 2 as the moisture absorption member 65, and advanced washing and drying process. The water (washing water) used for washing was 7 L, and the washing was performed by raising the temperature from the initial temperature of 15 ° C to 40 ° C. The amount of laundry was 3 kg. And, 0.5 kg of water was dried and removed at the time of drying, and for this purpose, the temperature was raised from 30 ° C to 60 ° C. Energy requirements were calculated during this washing and drying process. In addition, the energy requirement in the washing and drying stroke (Comparative Example 2; ie, the same method as the conventional washing and drying stroke without using the hygroscopic member) under the same conditions, except that aluminosilicate was not applied, was calculated as follows. Table 2 summarizes them.
【표 2] [Table 2]
실시예 실시예 실시예 비교예 비교예 Examples Examples Examples Comparative Examples Comparative Examples
1 2 3 1 21 2 3 1 2
(kWh) (kWh) (kWh) (kWh) (kWh) 세척 흡습재 탈습을 0.22 0.13 0.27 0.28 0 행정 위한 에너지 A (kWh) (kWh) (kWh) (kWh) (kWh) Washing Absorbent Dehumidification 0.22 0.13 0.27 0.28 0 Energy A for Stroke
세척수 가열 (승온) 0.20 0.20 0.20 0.20 0.20 소요 에너지흐  Washing water heating (heating) 0.20 0.20 0.20 0.20 0.20 Energy required
흡습재 웅축열 -0.08 -0.09 -0.07 -0.03 0 활용에 의한 절감  Hygroscopic material heat storage -0.08 -0.09 -0.07 -0.03 0 Saving by application
에너지  energy
건조 공기 가열 (승온 및 0.34 0.34 0.34 0.34 0.35 행정 건조) 소요 Dry air takes heating (temperature rise and 0.34 0.34 0.34 0.34 0.35 stroke drying)
에너지 £  Energy £
흡습재 흡착열 -0.34 -0.34 -0.34 -0.34 0 활용에 의한 절감  Absorbent heat of absorbent -0.34 -0.34 -0.34 -0.34 0 Saving by application
에너지 세탁기 운전 및 유지용 0.03 0.03 0.03 0.03 0.03 기본 소요 에너지 energy 0.03 0.03 0.03 0.03 0.03 Basic energy required for operating and maintaining the washing machine
총 에너지 소요량 0.37 0.27 0.43 0.48 0.58  Total energy requirement 0.37 0.27 0.43 0.48 0.58
A. 흡습재 탈습을 위한 에너지 = { [자연 탈습이 없다는 가정 하에 필요한 소요 에너지 (0.34 kWh/ 2kg 흡습재)] - [자연 탈습 비율에 의한 에너지 절감량] }; A. Energy for desiccant dehumidification = {[Required energy under the assumption that there is no natural dehumidification (0.34 kWh / 2 kg absorbent)]-[Energy saving by natural dehumidification rate]};
*' '자연 탈습 비율에 의한 에너지 절감량":  * '' Energy savings from natural dehumidification rates ":
(1) 실시예 1: 0.34kWh흡습재 * 35% = 0.12 kWh  (1) Example 1: 0.34 kWh absorbent * 35% = 0.12 kWh
(2) 실시예 2: 0.34kWh흡습재 * 63% = 0.21 kWh (2) Example 2 : 0.34 kWh absorbent * 63% = 0.21 kWh
(3) 실시예 3:0.34kWh흡습재 *20% = 0.07kWh (3) Example 3: 0.3 4 kWh absorbent * 20% = 0.07 kWh
(4) 비교예 l:0.34kWh 흡습재 *19% = 0.06kWh  (4) Comparative Example l: 0.34 kWh Absorbent * 19% = 0.06 kWh
B. 세척수 가열 (승온) 에너지 = 물 7 kg을 15°C에서 40°C로 승온하기 위한 에너지; B. Washing water heating (heating) energy = energy for raising 7 kg of water from 15 ° C to 40 ° C;
C. 흡습재 웅축열 활용에 의한 절감 에너지 = [(흡습량 (%; 25°C, 95%RH))- (흡습량 (%;25°C,0%RH))]* 기화열 (40°C)*(1 - 자연 탈습 비율) C. Energy savings due to the use of humectant heat storage = [(moisture absorption (%; 25 ° C, 95% RH))-(moisture absorption (%; 25 ° C, 0% RH))] * heat of vaporization (40 °) C) * (1-natural dehumidification rate)
D. 공기 가열 (건조) 소요 에너지: D. Air heating (drying) energy requirements:
(1) 실시예 1,2,3 및 비교예 1= 기화열 (30°C) (1) Examples 1,2,3 and Comparative Example 1 = heat of vaporization (30 ° C)
(2) 비교예 2= 공기 승온 소요 에너지 (30->60°C) + 기화열 (60°C) 상기 표 2를 참고하면, 실시예 1 내지 3의 경우, 비교예 1 및 2에 비해, 큰 폭의 에너지 절감 효과가 나타남이 확인되었다. (2) Comparative Example 2 = air heating required energy (30-> 60 ° C) + heat of vaporization (60 ° C) Referring to Table 2, in the case of Examples 1 to 3, compared to Comparative Examples 1 and 2, It was found that the energy saving effect of the width was shown.
【부호의 설명】 [Explanation of code]
10: 캐비닛  10: cabinet
11: 도어  11: door
12: 세제통 15: 급수 장치12: detergent container 15: watering device
17: 물 히터17: water heater
20: 터브20: Tub
22: ― ᄆ22:-
50: 모터50: motor
60: 건조 덕트60: drying duct
63: 공기 히터63: air heater
65: ᄇ ᄇ 丁세65: ᄇ 丁 丁 세
67: 67:
70: 은촌 더ᄐ 70: Eunchon The Dungeon
75: 급수 노즐75: water supply nozzle
80: 배수 펌프80: drain pump
83: 배수 호스 83: drain hose

Claims

【청구범위】 [Claim]
【청구항 11 [Claim 11
Si/Al의 원자비가 15 이하이고, 하기 V meso 및 Vmicro의 체적 합으로 정의되는 기공의 총 비체적 ¼otai이 0.3 cmVg 이상인 다공성 알루미노실리케이트를 포함하는 흡습 부재가 구비된 세탁기: Washing machine equipped with a hygroscopic member comprising a porous aluminosilicate having an atomic ratio of Si / Al of 15 or less and a total specific volume ¼ ota i of pores defined by the volume sum of V meso and Vmicro of 0.3 cmVg or more:
상기 Vmeso는 2 내지 300 nm의 기공 크기의 메소기공에 대한 바렛-조이너-할렌다 (BJH) 누적 체적이고, V meso is a Barrett-Joiner-Hellenda (BJH) cumulative volume for mesopores having a pore size of 2 to 300 nm,
상기 V^cro는 아르곤 흡착 브루너-에메트 -텔러 (BET) 표면적으로부터 t-플롯법에 의해 계산된 2 nm 미만의 기공 크기를 갖는 미세기공의 체적이다.  V ^ cro is the volume of micropores having a pore size of less than 2 nm calculated by t-plot method from argon adsorption Brunner-Emmett-Teller (BET) surface area.
【청구항 21 [Claim 21]
제 1 항에 있어서,  The method of claim 1,
세탁물 투입구가 형성된 캐비닛 (10),  A cabinet 10 having a laundry inlet,
상기 세탁물 투입구에 개폐 가능하게 설치된 도어 (11),  A door 11 installed to be opened and closed at the laundry inlet;
상기 캐비닛 내부에 세탁수를 저장하도록 설치된 터브 (20),  Tub 20 installed to store the wash water in the cabinet,
상기 터브 내에 회전 가능하게 설치된 드럼 (22),  A drum 22 rotatably installed in the tub,
상기 터브에 설치되어 상기 드럼에 구동력을 전달하는 모터 (50), 및 상기 터브의 상부측 외주면에 고정되고 양 끝단부가 상기 터브의 흡기구 및 배기구에 연결되어 상기 드럼 내부로 열풍을 순환시키는 건조 덕트 (60)를 포함하고;  A motor 50 installed in the tub and transmitting a driving force to the drum, and a drying duct fixed to an upper circumferential surface of the tub and having both ends connected to an inlet and an exhaust port of the tub to circulate hot air into the drum ( 60);
상기 건조 덕트 (60) 내에는 상기 다공성 알루미노실리케이트를 포함하는 흡습 부재 (65), 상기 흡습 부재의 외주면에 부착되어 흡습 부재와 공기를 가열하는 히터 (63), 및 공기를 순환시키는 송풍팬 (67)이 내장되어 있는, 세탁기.  In the drying duct 60, a moisture absorbing member 65 including the porous aluminosilicate, a heater 63 attached to an outer circumferential surface of the moisture absorbing member and heating the moisture absorbing member and air, and a blowing fan for circulating air ( 67) built-in washing machine.
【청구항 3] [Claim 3]
제 1 항에 있어서,  The method of claim 1,
상기 다공성 알루미노실리케이트의 Vmeso는 0.05 cmVg 이상인, 세탁기. V meso of the porous aluminosilicate is 0.05 cmVg or more, washer.
【청구항 4】 [Claim 4]
제 1 항에 있어서,  The method of claim 1,
상기 다공성 알루미노실리케이트는 25°C 및 95%의 상대 습도 하에, 하기 식 1로 정의되는 흡습량 (%; 25°C, 95% RH)이 22% 이상이고, 하기 식 2로 정의되는 상대습도별 흡습량 비가 1.2 이상인, 세탁기: The porous aluminosilicate has a moisture absorption amount (%; 25 ° C., 95% RH) defined by the following Equation 1 at 25 ° C. and 95% relative humidity of 22% or more, and a relative humidity defined by Equation 2 below. Washing machine with star moisture absorption ratio of 1.2 or more:
[식 ]  [Expression]
흡습량 (%; 25 °C, 95% RH) = [W (g) / AS (g)]*100 Moisture Absorption (%; 25 ° C, 95% RH) = [W (g) / AS (g)] * 100
[식 2]  [Equation 2]
상대습도별 흡습량 비 = 흡습량 (%; 25 °C, 95% RH)/ 흡습량 (%; 25 °C, 50% RH) Relative humidity by the moisture absorption amount ratio of moisture-absorbing amount (%; C 25 °, 95% RH) / absorption capacity (%; C 25 °, 50% RH)
식 1에서, AS (g)은 다공성 알루미노실리케이트의 중량을 나타내고, W (g)는 25°C 및 95%의 상대 습도 하에서 상기 AS (g)의 다공성 알루미노실리케이트를 사용하여 흡습을 진행하였을 때, 다공성 알루미노실리케이트가 최대로 흡수한 물의 중량을 나타내고, In Equation 1, AS (g) represents the weight of the porous aluminosilicate, W (g) was subjected to moisture absorption using the porous aluminosilicate of AS (g) at 25 ° C and 95% relative humidity When the porous aluminosilicate shows the weight of the water absorbed to the maximum,
식 2에서, 흡습량 (%; 25°C, 95% RH)은 식 1로 정의되는 흡습량을 나타내고, 흡습량 (%; 25 °C, 50% RH)은 상대 습도를 95%에서 50%로 낮추어 상기 다공성 알루미노실리케이트로부터 탈습을 진행하였을 때, [Wl (g) I AS (g)]*100의 식에 따라 산출된 흡습량을 나타내며, Wl (g)은 탈습 진행된 후에 AS (g)의 다공성 알루미노실리케이트가 최대로 흡수한 물의 중량을 나타낸다. In Equation 2, the moisture absorption amount (%; 25 ° C, 95% RH) represents the moisture absorption amount defined by Equation 1, and the moisture absorption amount (%; 25 ° C, 50% RH) represents a relative humidity of 95% to 50%. When dehumidifying from the porous aluminosilicate and lowering to, Wl (g) I AS (g)] represents the moisture absorption calculated according to the formula of [100], Wl (g) represents AS (g) The porous aluminosilicate of shows the weight of the water which the maximum absorbed.
【청구항 5】 [Claim 5]
제 1 항에 있어서,  The method of claim 1,
상기 다공성 알루미노실리케이트는 200 rnVg 이상의 아르곤 흡착 브루너-에메트 -텔러 (BET) 표면적을 갖는, 세탁기.  Wherein said porous aluminosilicate has an argon adsorption Brunner-Emmett-Teller (BET) surface area of at least 200 rnVg.
【청구항 6】 [Claim 6]
제 1 항에 있어서, 상기 다공성 알루미노실리케이트는 하기 화학식 1로 표시되는 화합물인, 세탁기: The method of claim 1, The porous aluminosilicate is a compound represented by the following Formula 1, washing machine:
[화학식 1]  [Formula 1]
MxSiAlyOa(OH)b(H20)c M x SiAl y Oa (OH) b (H 2 0) c
상기 화학식 1에서, M은 알칼리 금속, 알칼리 토금속 또는 전이금속을 나타내고, X 및 y는 각각 독립적으로 양수를 나타내고, a, b 및 c는 0 이상의 수를 나타낸다 (단, a+b는 양수이다 .).  In Formula 1, M represents an alkali metal, an alkaline earth metal or a transition metal, X and y each independently represent a positive number, and a, b and c each represent a number of 0 or more (where a + b is positive). ).
PCT/KR2016/008241 2015-07-31 2016-07-27 Washing machine having moisture absorption member WO2017023012A1 (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100724298B1 (en) * 2000-05-25 2007-06-04 니찌아스 카부시키카이샤 Humidity adsorbent element
KR20080104643A (en) * 2007-05-28 2008-12-03 엘지전자 주식회사 Dehumidifying apparatus for washing machine and dehumidifying method of the same
KR20090036253A (en) * 2007-10-09 2009-04-14 (주)호성화학 Desiccant containing indicator for hygroscopic level and preparing method thereof
WO2012174374A2 (en) * 2011-06-17 2012-12-20 Emerson Climate Technologies, Inc. Compressor dehydration via sorbent technology
KR20130023234A (en) * 2010-04-01 2013-03-07 상뜨로 나쇼날 드 라 러쉐르쉐 샹띠피크 Microreactor comprising a porous ceramic material

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100724298B1 (en) * 2000-05-25 2007-06-04 니찌아스 카부시키카이샤 Humidity adsorbent element
KR20080104643A (en) * 2007-05-28 2008-12-03 엘지전자 주식회사 Dehumidifying apparatus for washing machine and dehumidifying method of the same
KR20090036253A (en) * 2007-10-09 2009-04-14 (주)호성화학 Desiccant containing indicator for hygroscopic level and preparing method thereof
KR20130023234A (en) * 2010-04-01 2013-03-07 상뜨로 나쇼날 드 라 러쉐르쉐 샹띠피크 Microreactor comprising a porous ceramic material
WO2012174374A2 (en) * 2011-06-17 2012-12-20 Emerson Climate Technologies, Inc. Compressor dehydration via sorbent technology

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