WO2024082419A1 - Air purifier - Google Patents

Air purifier Download PDF

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Publication number
WO2024082419A1
WO2024082419A1 PCT/CN2022/139859 CN2022139859W WO2024082419A1 WO 2024082419 A1 WO2024082419 A1 WO 2024082419A1 CN 2022139859 W CN2022139859 W CN 2022139859W WO 2024082419 A1 WO2024082419 A1 WO 2024082419A1
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Prior art keywords
liquid
film carrier
liquid film
air
purification
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PCT/CN2022/139859
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French (fr)
Chinese (zh)
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路建霞
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路建霞
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Publication of WO2024082419A1 publication Critical patent/WO2024082419A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/02Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/18Absorbing units; Liquid distributors therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/72Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Definitions

  • the present application relates to the field of air purification, and in particular to an air purifier.
  • Existing air purification technologies mainly include passive adsorption filtration purification technology and active air purification technology.
  • the principle of passive air purifiers is: using a fan to suck air into the purifier, and filtering the air through the built-in filter of the purifier, which can filter dust, odor, toxic gases and kill some bacteria.
  • the filter is mainly divided into a particle filter and an organic filter, and the particle filter is further divided into a coarse particle filter, a fine particle filter, etc.;
  • the difference between the principle of active air purifiers and the principle of passive air purification is that active air purifiers get rid of the restrictions on fans and filters, and actively release purification and sterilization factors into the air.
  • the technologies for purification and sterilization factors on the market mainly include silver ion technology, negative ion technology, low-temperature plasma technology, photocatalyst technology, and net ion group ion technology.
  • the pore size of the filter cannot be too small, otherwise the resistance will be very large and the flux will be greatly affected. There is almost no removal effect on fine particles, especially those with a size below the micron level. The finer the particles, the easier they are to reach deep into the lungs and cause harm to the human body. Therefore, the purification effect is poor.
  • the filter should be replaced frequently, otherwise the resistance of the fan will increase with the accumulation of particulate matter, greatly affecting the filtration efficiency. It is not only expensive, but also easy to cause secondary pollution because the fabric is generally chemical fiber.
  • the adsorption efficiency is low. Since the thickness of the adsorption layer is generally in the centimeter level, while the wind speed is in the meter level, the time for wind to pass through the adsorption layer is only in the millisecond level, and there is not enough time for diffusion. Therefore, the efficiency of one-time filtration and adsorption is very low. The adsorption rate can only be increased by circulating large air volume, which requires increasing the air volume.
  • Water foam/falling film purification technology is commonly used in the petrochemical field as an industrial tail gas treatment technology. It is suitable for washing and purification before high-concentration tail gas emissions.
  • the absorption liquid is dispersed on the membrane medium by spraying, such as ceramic, stainless steel, plastic ring, saddle, and tubular media.
  • the present application proposes an air purifier, which dissolves or disperses pollutants in an absorbing liquid by free diffusion and exchange with the absorbing liquid substance to improve the purification effect.
  • An air purifier comprises a box body, a laminar flow purification component, an air inlet driver and a controller, wherein opposite side walls of the box body are respectively provided with an air inlet and an air outlet, the air inlet driver is installed at the air inlet, the laminar flow purification component is installed in the box body, the controller is installed on the front side of the box body and is used to control the laminar flow purification component and the air inlet driver, the laminar flow purification component comprises a partition, a circulation pump and a liquid film carrier plate, the partition is horizontally fixed in the box body and divides the box body into an upper liquid storage chamber and a lower mounting chamber, the liquid film carrier plates are vertically spaced in the lower mounting chamber, a purification channel is formed between any two adjacent liquid film carrier plates, the surface of the liquid film carrier plates is coated with absorbent liquid, a groove is provided on the side of the lower mounting chamber close to the air outlet, a circulation pump is installed in the groove, the liquid outlet end of the circulation pump is connected with the
  • the width of the purification channel is between 2 mm and 20 mm.
  • the liquid film carrier is a thin sheet structure made of hydrophilic material.
  • the liquid-to-gas weight ratio in the box is between 0.1 and 2.
  • the liquid film carrier plate comprises a front liquid film carrier plate and a rear liquid film carrier plate, and an extension line of the front liquid film carrier plate is obliquely intersected with an extension line of the rear liquid film carrier plate.
  • the rear liquid film carrier plates are multiple groups arranged front to back, and the purification channels formed by the multiple groups of rear liquid film carrier plates are staggered front to back.
  • the solute of the absorption liquid is a liquid medium that is easily soluble in water, difficult to volatilize and has air purification effect.
  • the absorption liquid is an air purification absorption liquid
  • the air purification absorption liquid comprises water and a chemical solute
  • the chemical solute is selected from at least one of alcohols, ammonium salts, hydroxylamines, compounds containing primary/secondary amine functional groups and their salts.
  • the pollutants purified by the air purifier include VOCs, dust, smoke and aerosols.
  • the air purifier of the present invention adopts a hydrophilic liquid film carrier plate with a large specific surface area, which can construct a material and energy exchange area as large as possible in a smaller volume space, achieve efficient removal of pollutants, and have a higher efficiency ratio.
  • the air purifier of the present invention is suitable for air purification with low pollution concentration in closed or semi-closed spaces, such as indoors, in cars, in warehouses, in tunnels, on streets and other places. It can effectively absorb pollutants including dust, smoke and gas, and the smaller the particles, the better the effect. Specifically, by exchanging substances through free diffusion rather than filtering, a larger gas channel can be established to achieve a large flow rate and low resistance, so the air circulates faster, the noise is lower, and it will never be blocked.
  • the air purifier of the present invention uses a substance that is easily soluble in water and difficult to volatilize, which can effectively control the evaporation of the absorption liquid, thereby controlling the air humidity, and can maintain a comfortable humidity by replenishing water when humidification is required. It is particularly suitable for dry areas or winter.
  • the absorption liquid in the present invention contains a substance that reacts with formaldehyde condensation, which can effectively fix formaldehyde without causing secondary pollution.
  • the chemical solute is a biodegradable substance, which can be directly biodegraded through a septic tank or purified and recycled by a professional organization without generating difficult-to-degrade waste, thus truly realizing a green cycle.
  • FIG1 is a perspective schematic diagram of an air purifier according to an embodiment of the present application.
  • FIG2 is a schematic diagram of the internal structure of FIG1 (front view);
  • FIG3 is a schematic diagram of the internal structure of FIG1 (top view);
  • the housing 10 The housing 10 , the air inlet 101 , the air outlet 102 , the groove 103 , the air inlet driver 11 , the controller 12 , the partition 21 , the penetration hole 211 , the circulation pump 22 , and the liquid film carrier plate 23 .
  • this embodiment discloses an air purifier, including a housing 10 , a laminar flow purification component, an air inlet driver 11 and a controller 12 .
  • the opposite side walls of the box body 10 are respectively provided with an air inlet 101 and an air outlet 102.
  • the box body 10 is preferably a rectangular structure.
  • the air inlet 101 and the air outlet 102 are respectively provided at the center of the left and right sides of the box body 10.
  • An air inlet drive 11 is installed at the air inlet 101.
  • the air inlet drive 11 is preferably a fan, which is used to introduce external air into the box body 10 for filtering.
  • the laminar flow purification component is installed in the box 10, and the controller 12 is installed on the front of the box 10 to control the laminar flow purification component and the air inlet driver 11.
  • the front of the box 10 is also provided with a display screen electrically connected to the controller, and the display screen is used to display filtering parameters.
  • the laminar flow purification component includes a partition 21, a circulation pump 22 and a liquid film carrier 23.
  • the partition 21 is horizontally fixed in the box body 10 and divides the box body 10 into an upper liquid storage chamber and a lower installation chamber.
  • the liquid film carrier 23 is vertically spaced in the lower installation chamber, and a purification channel is formed between any two adjacent liquid film carriers 23.
  • the surface of the liquid film carrier 23 is coated with absorption liquid.
  • a groove 103 is provided on one side of the lower installation chamber close to the air outlet 102.
  • the circulation pump 22 is installed in the groove 103.
  • the liquid outlet end of the circulation pump 22 is connected to the upper liquid storage chamber through an infusion pipeline.
  • the partition 21 is evenly provided with penetration holes 211 for penetrating the absorption liquid into the liquid film carrier.
  • the liquid film carrier 23 is coated with an absorption liquid, and the external air is input into the purification channel through the air inlet driver 11.
  • the molecular thermal motion of the gas and the Brownian motion of the pollutant particles are utilized to fully exchange substances with the liquid film carrier 23, so that the pollutants are dissolved or dispersed in the absorption liquid, thereby eliminating particulate matter and harmful gases in the air, and then the active or toxic pollutants, such as formaldehyde, react with the active ingredients in the liquid to generate non-volatile and low-toxic substances, thereby avoiding the pollution caused by the re-volatilization of harmful gases.
  • the absorption liquid on the liquid film carrier 23 flows slowly downward under the action of gravity, and then gathers in the groove 103, and is input into the upper liquid storage cavity again through the circulation pump 22, and is coated on the liquid film carrier 23 again through the penetration hole 211, so as to achieve the purpose of reuse.
  • the absorption liquid on the liquid film carrier 23 can be replaced after being used for a period of time.
  • the absorption liquid can be coated on the liquid film carrier 23 by gravity, infiltration/capillary action, centrifugal force alone or in combination, and the coated absorption liquid must fully cover the liquid film carrier 23.
  • the material of the liquid film carrier 23 is a single metal (such as iron) or an alloy (such as aluminum alloy), or it can be a material containing natural fibers such as bamboo, wood, plant leaves, and biomass of animal fur. It can also be an inorganic material, such as glass, cement, gypsum, quartz, limestone, granite, and synthetic fiber board.
  • the material selection of the liquid film carrier 23 is relatively wide.
  • the shape of the liquid film carrier 23 can be sheet, tube, column, preferably a thin sheet structure of hydrophilic material, and the thickness of the liquid film carrier 23 is not more than 10 mm, so that more liquid film carriers 23 can be arranged in a limited space, which helps to increase the coating amount of the absorption liquid.
  • the solute of the absorption liquid is a liquid medium that is easily soluble in water, difficult to volatilize, and has air purification effect, such as monohydric or polyhydric alcohol, ammonia, hydroxylamine, or organic substances with less than 15 carbon atoms in the molecular structure and containing primary amine and secondary amine functional groups and their salts.
  • the gap of the purification channel should be as small as possible, preferably not more than 50 mm.
  • the width of the purification channel is between 2 mm and 20 mm, which has a high cost performance.
  • the circulation amount of the absorption liquid is determined according to the concentration of air pollutants.
  • the liquid-to-gas weight ratio in the box 10 is between 0.1 and 2, wherein the greater the concentration of air pollutants, the greater the liquid-to-gas weight ratio, and the smaller the concentration of air pollutants, the smaller the liquid-to-gas weight ratio.
  • an absorption liquid cooling or heating device can be installed. Since the liquid film carrier plate 23 has a large heat exchange area and high heat exchange efficiency, it does not require a high temperature difference when directly exchanging heat with the air like an ordinary air conditioner. Therefore, the operating temperature of the cooling and heating device can be close to the target air temperature, thereby reducing the load of the air conditioning device and achieving the purpose of energy saving. Moreover, since the temperature difference with the target temperature is small, especially in summer, the temperature of the blown wind is close to the ambient temperature, and the human body feels more comfortable.
  • the liquid film carrier 23 includes a front liquid film carrier and a rear liquid film carrier, and the extension line of the front liquid film carrier is obliquely intersected with the extension line of the rear liquid film carrier.
  • the front liquid film carrier and the wind direction initially output by the air inlet driver 11 are at an acute angle, and the angle is preferably between 5°-10°, so as to facilitate uniform coating of the absorption liquid and ensure uniform clearance of the purification channel to ensure absorption effect.
  • the rear liquid film carrier is a plurality of groups arranged front and back, and the purification channels formed by the plurality of groups of rear liquid film carriers are staggered front and back. By staggering the purification channels front and back, the gas flow direction can be changed, so that the liquid film material exchange is more sufficient, which is conducive to the dissolution or dispersion of pollutants in the absorption liquid.
  • pollutants purified by the liquid film carrier 23 include VOCs, dust, smoke and aerosols.
  • the air purifier of this embodiment adopts a hydrophilic liquid film carrier plate 23 with a large specific surface area, which can construct the largest possible material and energy exchange area in a smaller volume space, achieve efficient removal of pollutants, and have a higher efficiency ratio.
  • the air purifier of this embodiment is suitable for air purification with low pollution concentration in closed or semi-closed spaces, such as indoors, in cars, in warehouses, in tunnels, on streets and other places. It can effectively absorb pollutants including dust, smoke and gas, and the smaller the particles, the better the effect. Specifically, by exchanging substances through free diffusion rather than filtering, a larger gas channel can be established to achieve a large flow rate and low resistance, so the air circulates faster, the noise is lower, and it will never be blocked.
  • the air purifier of this embodiment uses a substance that is easily soluble in water and difficult to volatilize, which can effectively control the evaporation of the absorption liquid, thereby controlling the air humidity, and can maintain a comfortable humidity by adding water when humidification is needed. It is particularly suitable for dry areas or winter.
  • the absorption liquid is an air purification absorption liquid
  • the air purification absorption liquid includes water and a chemical solute; the chemical solute is selected from at least one of alcohol, ammonium salt, hydroxylamine and compounds containing primary amine/secondary amine functional groups and their salts.
  • the pH value of the air purification absorption liquid is 2-5; the percentage of chemical solutes in the air purification absorption liquid is 10%-90%; the number of carbon atoms of the alcohol is not more than 15; the alcohol is 1,2-propylene glycol, 1,3-propylene glycol or glycerol; the number of carbon atoms of the compound containing primary/secondary amine functional groups and its salts is not more than 15; the compound containing primary/secondary amine functional groups and its salts are selected from at least one of ethylamine, propylamine, butylamine, diethylamine, dipropylamine and dibutylamine.
  • the absorption liquid in this embodiment contains a substance that reacts with formaldehyde condensation, which can effectively fix formaldehyde without causing secondary pollution.
  • the chemical solute is a biodegradable substance and can be directly biodegraded through a septic tank or purified and recycled by a professional organization without generating difficult-to-degrade waste, thus truly realizing a green cycle.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
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Abstract

An air purifier, comprising a box (10), a laminar flow purification assembly, an air intake driver (11), and a controller (12). Opposite side walls of the box (10) are respectively provided with an air inlet (101) and an air outlet (102), the air intake driver (11) being mounted at the air inlet (101); the laminar flow purification assembly is mounted in the box (10), and the laminar flow purification assembly comprises a partition plate (21), a circulating pump (22), and liquid film carrier plates (23); the partition plate (21) is horizontally fixed in the box (10) and divides the interior of the box (10) into an upper liquid storage cavity and a lower mounting cavity; the liquid film carrier plates (23) are vertically arranged in the lower mounting cavity at intervals, a purification channel being formed between any two adjacent liquid film carrier plates (23), and absorption liquid being coated on the surfaces of the liquid film carrier plates (23); a recess (103) is provided on the side of the lower mounting cavity close to the air outlet (102), the circulating pump (22) is mounted in the recess (103), a liquid discharge end of the circulating pump (22) is in communication with the upper liquid storage cavity by means of a liquid transport pipeline, and permeation holes (211) are uniformly distributed on the partition plate (21) for penetration of the absorption liquid into the liquid film carrier plates (23).

Description

一种空气净化器An air purifier 技术领域Technical Field
本申请涉及空气净化领域,具体涉及一种空气净化器。The present application relates to the field of air purification, and in particular to an air purifier.
背景技术Background technique
现有空气净化技术主要包括被动吸附过滤式净化技术和主动式空气净化技术。其中,被动式空气净化器的原理是:使用风机将空气吸入净化器,通过净化器内置的滤网过滤空气,能够起到过滤粉尘、异味、有毒气体和杀灭部分细菌的作用,而滤网主要分为颗粒物滤网和有机物滤网,颗粒物滤网又分为粗颗粒物滤网、细颗粒物滤网等等;主动式空气净化器的原理与被动式空气净化原理的区别在于,主动式空气净化器摆脱了对风机与滤网的限制,主动向空气中释放净化灭菌因子,通过空气扩散的特性,到达室内的各个角落对空气进行无死角净化。市场上净化灭菌因子的技术主要有银离子技术、负离子技术、低温等离子技术、光触媒技术和净离子群离子技术等。Existing air purification technologies mainly include passive adsorption filtration purification technology and active air purification technology. Among them, the principle of passive air purifiers is: using a fan to suck air into the purifier, and filtering the air through the built-in filter of the purifier, which can filter dust, odor, toxic gases and kill some bacteria. The filter is mainly divided into a particle filter and an organic filter, and the particle filter is further divided into a coarse particle filter, a fine particle filter, etc.; the difference between the principle of active air purifiers and the principle of passive air purification is that active air purifiers get rid of the restrictions on fans and filters, and actively release purification and sterilization factors into the air. Through the characteristics of air diffusion, it reaches every corner of the room to purify the air without dead ends. The technologies for purification and sterilization factors on the market mainly include silver ion technology, negative ion technology, low-temperature plasma technology, photocatalyst technology, and net ion group ion technology.
对于被动式空气净化器而言,存在如下不足:For passive air purifiers, there are the following shortcomings:
1、以过滤颗粒物而言,由于滤网的孔径不能太小,否则阻力很大,通量会受很大影响,细微的颗粒物特别是粒径在微米级以下的几乎无去除效果,而恰恰是越细微的越容易到达肺的深处且为人体带来危害,因此,净化效果欠佳。1. As for filtering particulate matter, the pore size of the filter cannot be too small, otherwise the resistance will be very large and the flux will be greatly affected. There is almost no removal effect on fine particles, especially those with a size below the micron level. The finer the particles, the easier they are to reach deep into the lungs and cause harm to the human body. Therefore, the purification effect is poor.
2、为提高过滤效率,但不能增大滤网孔径,不得不提高风机的风压以克服阻力从而确保风量,无疑增加了功耗和噪声污染。2. In order to improve the filtering efficiency, but the filter mesh aperture cannot be increased, the wind pressure of the fan has to be increased to overcome the resistance and ensure the air volume, which undoubtedly increases power consumption and noise pollution.
3.过滤网要经常更换,否则风机的阻力会随着颗粒物的累积而增大,大大影响过滤效率,不但昂贵,而且由于织物一般为化学纤维,易造成二次污染。3. The filter should be replaced frequently, otherwise the resistance of the fan will increase with the accumulation of particulate matter, greatly affecting the filtration efficiency. It is not only expensive, but also easy to cause secondary pollution because the fabric is generally chemical fiber.
4.对于甲醛等有机气体是通过吸附去除的,但吸附具有可逆性,即吸附的同时也会脱附游离出来,所以吸附介质需经常更换,否则易造成吸附效率下降。4. Organic gases such as formaldehyde are removed by adsorption, but adsorption is reversible, that is, it will also desorb and become free during adsorption, so the adsorption medium needs to be replaced frequently, otherwise it will easily cause a decrease in adsorption efficiency.
5.吸附效率低,由于吸附层厚一般为厘米级,而风速为米级,风通过吸附层的时间仅在毫秒级,没有充分的时间进行扩散,所以一次过滤吸附的效率是很低的,只能通过大风量循环提高吸附率,又需要增加风量。5. The adsorption efficiency is low. Since the thickness of the adsorption layer is generally in the centimeter level, while the wind speed is in the meter level, the time for wind to pass through the adsorption layer is only in the millisecond level, and there is not enough time for diffusion. Therefore, the efficiency of one-time filtration and adsorption is very low. The adsorption rate can only be increased by circulating large air volume, which requires increasing the air volume.
水沫/降膜净化技术常用在石油化工领域作为工业尾气处理技术中,适用于高浓度尾气排放前的洗涤净化,一般是通过喷雾将吸收液分散于膜介质上,如陶瓷、不锈钢、塑料环状、马鞍状、管状介质,优点是处理量大,空气停留时间较长,阻力系数较小,效率较高;但存在如下问题:Water foam/falling film purification technology is commonly used in the petrochemical field as an industrial tail gas treatment technology. It is suitable for washing and purification before high-concentration tail gas emissions. Generally, the absorption liquid is dispersed on the membrane medium by spraying, such as ceramic, stainless steel, plastic ring, saddle, and tubular media. The advantages are large processing capacity, long air residence time, small resistance coefficient, and high efficiency; but there are the following problems:
1、由于此技术需要将吸收液均匀分布,所以需要较高的喷射速度,将吸收液分散为细小的液滴,尽可能均匀地使每一个部位都润湿,所以喷淋过程中会产生大量的雾状液体,再通过除沫装置如折流板、旋风分离器等装置将大部分雾状液拦截下来,但仍有部分雾状液会跑掉,下游往往还要设置活性炭吸附箱等再次拦截,还是会有少量雾状或气溶胶状液体会跑掉,不但造成吸收液损耗,还会造成环境污染;所以往往采用较高的净化塔和多级净化,因此不适用于室内使用;1. Since this technology requires the absorption liquid to be evenly distributed, a higher spraying speed is required to disperse the absorption liquid into fine droplets and wet every part as evenly as possible. Therefore, a large amount of mist liquid will be generated during the spraying process, and most of the mist liquid will be intercepted by defoaming devices such as baffles and cyclone separators, but some of the mist liquid will still escape. Activated carbon adsorption boxes are often set up downstream to intercept again, and a small amount of mist or aerosol liquid will still escape, which will not only cause absorption liquid loss, but also cause environmental pollution; therefore, higher purification towers and multi-stage purification are often used, so it is not suitable for indoor use;
2、因设备庞大,所以系统风阻会达到1kPa以上,需要大功率风机, 噪声大,能耗高;2. Due to the huge size of the equipment, the system wind resistance will reach more than 1kPa, requiring a high-power fan, which will generate high noise and high energy consumption;
3、均匀分布是一种理想化状态,实际上由于喷淋不可能均匀,液体从上往下流动时往往发生偏流,造成局部出现无吸收液,而无吸收液的部位阻力反而小,造成气流短路,影响吸收效果。3. Uniform distribution is an idealized state. In fact, since spraying cannot be uniform, liquid often deviates when flowing from top to bottom, resulting in local areas without absorption liquid. The resistance of the area without absorption liquid is small, causing air flow short circuit and affecting the absorption effect.
有鉴于此,特提出本发明。In view of this, the present invention is proposed.
发明内容Summary of the invention
有鉴于此,本申请提出一种空气净化器,通过自由扩散并与吸收液物质交换的方式将污染物溶解或分散于吸收液中,以提高净化效果。In view of this, the present application proposes an air purifier, which dissolves or disperses pollutants in an absorbing liquid by free diffusion and exchange with the absorbing liquid substance to improve the purification effect.
为了实现本发明的上述目的,采用以下技术方案:In order to achieve the above-mentioned purpose of the present invention, the following technical scheme is adopted:
一种空气净化器,包括箱体、层流净化组件、进风驱动器和控制器,所述箱体相对的侧壁分别开设有进风口和出风口,所述进风口处装设有进风驱动器,所述层流净化组件装设于箱体内,所述控制器装设于箱体的正面,并用于控制层流净化组件和进风驱动器,所述层流净化组件包括隔板、循环泵和液膜载板,所述隔板水平固设于箱体内,并将箱体内分隔成上储液腔和下安装腔,所述下安装腔内竖向间隔设有液膜载板,任意相邻两块液膜载板之间形成净化通道,所述液膜载板表面涂布有吸收液,所述下安装腔靠近出风口的一侧设有凹槽,所述凹槽内装设有循环泵,所述循环泵的出液端通过输液管路与上储液腔连通,所述隔板上均匀开设有用于向液膜载板渗透吸收液的渗透孔。An air purifier comprises a box body, a laminar flow purification component, an air inlet driver and a controller, wherein opposite side walls of the box body are respectively provided with an air inlet and an air outlet, the air inlet driver is installed at the air inlet, the laminar flow purification component is installed in the box body, the controller is installed on the front side of the box body and is used to control the laminar flow purification component and the air inlet driver, the laminar flow purification component comprises a partition, a circulation pump and a liquid film carrier plate, the partition is horizontally fixed in the box body and divides the box body into an upper liquid storage chamber and a lower mounting chamber, the liquid film carrier plates are vertically spaced in the lower mounting chamber, a purification channel is formed between any two adjacent liquid film carrier plates, the surface of the liquid film carrier plates is coated with absorbent liquid, a groove is provided on the side of the lower mounting chamber close to the air outlet, a circulation pump is installed in the groove, the liquid outlet end of the circulation pump is connected with the upper liquid storage chamber through an infusion pipeline, and penetration holes for penetrating the absorbent liquid into the liquid film carrier plates are evenly provided on the partition plate.
优选地,所述净化通道的宽度介于2mm~20mm之间。Preferably, the width of the purification channel is between 2 mm and 20 mm.
优选地,所述液膜载板为亲水材质的薄片状结构。Preferably, the liquid film carrier is a thin sheet structure made of hydrophilic material.
优选地,所述箱体内液气重量比介于0.1~2之间。Preferably, the liquid-to-gas weight ratio in the box is between 0.1 and 2.
优选地,所述液膜载板包括前液膜载板和后液膜载板,所述前液膜 载板的延伸线与后液膜载板的延伸线斜交。Preferably, the liquid film carrier plate comprises a front liquid film carrier plate and a rear liquid film carrier plate, and an extension line of the front liquid film carrier plate is obliquely intersected with an extension line of the rear liquid film carrier plate.
优选地,所述后液膜载板为前后排布的多组,多组后液膜载板形成的净化通道前后错位设置。Preferably, the rear liquid film carrier plates are multiple groups arranged front to back, and the purification channels formed by the multiple groups of rear liquid film carrier plates are staggered front to back.
优选地,所述吸收液的溶质为易溶于水、难挥发且具有空气净化功效的液态介质。Preferably, the solute of the absorption liquid is a liquid medium that is easily soluble in water, difficult to volatilize and has air purification effect.
优选地,所述吸收液为空气净化吸收液,所述空气净化吸收液包括水和化学溶质;所述化学溶质选自醇、铵盐、羟胺和含有伯胺/仲胺官能团的化合物及其盐类中的至少一种。Preferably, the absorption liquid is an air purification absorption liquid, and the air purification absorption liquid comprises water and a chemical solute; the chemical solute is selected from at least one of alcohols, ammonium salts, hydroxylamines, compounds containing primary/secondary amine functional groups and their salts.
优选地,所述空气净化器净化的污染物包括VOCs、粉尘、烟雾和气溶胶。Preferably, the pollutants purified by the air purifier include VOCs, dust, smoke and aerosols.
本申请的有益效果:Beneficial effects of this application:
本发明的空气净化器,采用亲水性的大比表面积的液膜载板,可以实现在较小的体积空间构造尽可能大的物质和能量交换面积,实现污染物的高效清除,有更高的效能比。The air purifier of the present invention adopts a hydrophilic liquid film carrier plate with a large specific surface area, which can construct a material and energy exchange area as large as possible in a smaller volume space, achieve efficient removal of pollutants, and have a higher efficiency ratio.
本发明的空气净化器,适用于封闭或半封闭空间的低污染浓度的空气净化,如室内、车厢内、仓内、隧道、街道等场所,可以有效吸收包括粉尘、烟雾、气体的污染物,颗粒越小效果越好;具体通过自由扩散进行物质交换而不是过滤,可以建立较大的气体通道,实现大流量,低阻力,所以空气循环更快,噪声更低,永不堵塞。The air purifier of the present invention is suitable for air purification with low pollution concentration in closed or semi-closed spaces, such as indoors, in cars, in warehouses, in tunnels, on streets and other places. It can effectively absorb pollutants including dust, smoke and gas, and the smaller the particles, the better the effect. Specifically, by exchanging substances through free diffusion rather than filtering, a larger gas channel can be established to achieve a large flow rate and low resistance, so the air circulates faster, the noise is lower, and it will never be blocked.
本发明的空气净化器,采用易溶于水且难挥发的物质,可有效控制吸收液的蒸发,从而控制空气湿度,并且在需加湿时可通过补充水分保持舒适湿度,尤其适用于干燥地区或冬季。The air purifier of the present invention uses a substance that is easily soluble in water and difficult to volatilize, which can effectively control the evaporation of the absorption liquid, thereby controlling the air humidity, and can maintain a comfortable humidity by replenishing water when humidification is required. It is particularly suitable for dry areas or winter.
本发明中的吸收液包含与甲醛缩合反应的物质,可有效固定甲醛而不会造成二次污染而且化学溶质为易生物降解物质,可直接通过化粪池 进行生物降解,或通过专业机构净化再生使用,不会产生难以降解的废物,真正实现绿色循环。The absorption liquid in the present invention contains a substance that reacts with formaldehyde condensation, which can effectively fix formaldehyde without causing secondary pollution. Moreover, the chemical solute is a biodegradable substance, which can be directly biodegraded through a septic tank or purified and recycled by a professional organization without generating difficult-to-degrade waste, thus truly realizing a green cycle.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1是本申请实施例一种空气净化器的立体示意图;FIG1 is a perspective schematic diagram of an air purifier according to an embodiment of the present application;
图2是图1的内部结构示意图(正视);FIG2 is a schematic diagram of the internal structure of FIG1 (front view);
图3是图1的内部结构示意图(俯视);FIG3 is a schematic diagram of the internal structure of FIG1 (top view);
箱体10、进风口101、出风口102、凹槽103、进风驱动器11、控制器12、隔板21、渗透孔211、循环泵22、液膜载板23。The housing 10 , the air inlet 101 , the air outlet 102 , the groove 103 , the air inlet driver 11 , the controller 12 , the partition 21 , the penetration hole 211 , the circulation pump 22 , and the liquid film carrier plate 23 .
具体实施方式Detailed ways
以下结合附图以及具体实施例,对本申请的技术方案进行详细描述。其中相同的零部件用相同的附图标记表示。The technical solution of the present application is described in detail below in conjunction with the accompanying drawings and specific embodiments, wherein the same components are represented by the same reference numerals.
请参阅图1至图3,本实施例公开一种空气净化器,包括箱体10、层流净化组件、进风驱动器11和控制器12。Please refer to FIG. 1 to FIG. 3 , this embodiment discloses an air purifier, including a housing 10 , a laminar flow purification component, an air inlet driver 11 and a controller 12 .
其中,箱体10相对的侧壁分别开设有进风口101和出风口102,箱体10优选长方体结构,进风口101和出风口102分别开设在箱体10的左右侧的中心,进风口101处装设有进风驱动器11,进风驱动器11优选风机,利用风机将外部的空气引入箱体10内进行过滤。Among them, the opposite side walls of the box body 10 are respectively provided with an air inlet 101 and an air outlet 102. The box body 10 is preferably a rectangular structure. The air inlet 101 and the air outlet 102 are respectively provided at the center of the left and right sides of the box body 10. An air inlet drive 11 is installed at the air inlet 101. The air inlet drive 11 is preferably a fan, which is used to introduce external air into the box body 10 for filtering.
层流净化组件装设于箱体10内,控制器12装设于箱体10的正面,并控制层流净化组件和进风驱动器11,箱体10的正面还设有与控制器电连接的显示屏,显示屏用于显示过滤参数。The laminar flow purification component is installed in the box 10, and the controller 12 is installed on the front of the box 10 to control the laminar flow purification component and the air inlet driver 11. The front of the box 10 is also provided with a display screen electrically connected to the controller, and the display screen is used to display filtering parameters.
如图2所示,层流净化组件包括隔板21、循环泵22和液膜载板23,隔板21水平固设于箱体10内,并将箱体10内分隔成上储液腔和下安装 腔,下安装腔内竖向间隔设有液膜载板23,任意相邻两块液膜载板23之间形成净化通道,液膜载板23表面涂布有吸收液,下安装腔靠近出风口102的一侧设有凹槽103,凹槽103内装设有循环泵22,循环泵22的出液端通过输液管路与上储液腔连通,隔板21上均匀开设有用于向液膜载板渗透吸收液的渗透孔211。As shown in Figure 2, the laminar flow purification component includes a partition 21, a circulation pump 22 and a liquid film carrier 23. The partition 21 is horizontally fixed in the box body 10 and divides the box body 10 into an upper liquid storage chamber and a lower installation chamber. The liquid film carrier 23 is vertically spaced in the lower installation chamber, and a purification channel is formed between any two adjacent liquid film carriers 23. The surface of the liquid film carrier 23 is coated with absorption liquid. A groove 103 is provided on one side of the lower installation chamber close to the air outlet 102. The circulation pump 22 is installed in the groove 103. The liquid outlet end of the circulation pump 22 is connected to the upper liquid storage chamber through an infusion pipeline. The partition 21 is evenly provided with penetration holes 211 for penetrating the absorption liquid into the liquid film carrier.
基于上述空气净化器,液膜载板23涂布有吸收液,经进风驱动器11将外界的空气输入净化通道,利用空气通过液膜载板23时气体的分子热运动,污染物微粒的布朗运动,与液膜载板23进行充分的物质交换,使污染物溶解或分散于吸收液中,以此消除空气中的颗粒物和有害气体,再将有活性或毒性的污染物,如甲醛与液体中的活性成分反应生成难挥发低毒的物质,从而避免有害气体的再挥发产生的污染,液膜载板23上的吸收液受重力作用缓慢向下流动,之后在凹槽103内汇集,并经循环泵22再次输入上储液腔内,经渗透孔211向液膜载板23再次涂布,达到重复使用的目的,液膜载板23上的吸收液使用一段时间后,可进行更换。Based on the above-mentioned air purifier, the liquid film carrier 23 is coated with an absorption liquid, and the external air is input into the purification channel through the air inlet driver 11. When the air passes through the liquid film carrier 23, the molecular thermal motion of the gas and the Brownian motion of the pollutant particles are utilized to fully exchange substances with the liquid film carrier 23, so that the pollutants are dissolved or dispersed in the absorption liquid, thereby eliminating particulate matter and harmful gases in the air, and then the active or toxic pollutants, such as formaldehyde, react with the active ingredients in the liquid to generate non-volatile and low-toxic substances, thereby avoiding the pollution caused by the re-volatilization of harmful gases. The absorption liquid on the liquid film carrier 23 flows slowly downward under the action of gravity, and then gathers in the groove 103, and is input into the upper liquid storage cavity again through the circulation pump 22, and is coated on the liquid film carrier 23 again through the penetration hole 211, so as to achieve the purpose of reuse. The absorption liquid on the liquid film carrier 23 can be replaced after being used for a period of time.
在本申请的一个可选的实施例中,吸收液可通过重力、浸润/毛细作用、离心力单独或组合的方式涂布在液膜载板23上,涂布的吸收液必须全覆盖液膜载板23。In an optional embodiment of the present application, the absorption liquid can be coated on the liquid film carrier 23 by gravity, infiltration/capillary action, centrifugal force alone or in combination, and the coated absorption liquid must fully cover the liquid film carrier 23.
具体的,液膜载板23的材质为单一金属(如铁)或合金(如铝合金),也可以为含天然纤维的材料如竹、木、植物叶子、动物皮毛的生物质,还可以为无机物,例如玻璃、水泥、石膏、石英、石灰石、花岗岩石、合成纤维板,液膜载板23的选材较广。Specifically, the material of the liquid film carrier 23 is a single metal (such as iron) or an alloy (such as aluminum alloy), or it can be a material containing natural fibers such as bamboo, wood, plant leaves, and biomass of animal fur. It can also be an inorganic material, such as glass, cement, gypsum, quartz, limestone, granite, and synthetic fiber board. The material selection of the liquid film carrier 23 is relatively wide.
具体的,液膜载板23的形状可采用片状、管状、柱状,优选亲水材质的薄片状结构,液膜载板23的厚度不大于10mm,以使有限的空间排 布更多的液膜载板23,进而有助于增加吸收液的涂布量。Specifically, the shape of the liquid film carrier 23 can be sheet, tube, column, preferably a thin sheet structure of hydrophilic material, and the thickness of the liquid film carrier 23 is not more than 10 mm, so that more liquid film carriers 23 can be arranged in a limited space, which helps to increase the coating amount of the absorption liquid.
在本申请的一个可选的实施例中,吸收液的溶质为易溶于水、难挥发且具有空气净化功效的液态介质。如一元或多元醇,氨、羟胺或分子结构中含碳15个以下的并包含伯胺、仲胺官能团的有机物及其盐类。In an optional embodiment of the present application, the solute of the absorption liquid is a liquid medium that is easily soluble in water, difficult to volatilize, and has air purification effect, such as monohydric or polyhydric alcohol, ammonia, hydroxylamine, or organic substances with less than 15 carbon atoms in the molecular structure and containing primary amine and secondary amine functional groups and their salts.
为了确保吸收效果和降低空气阻力,净化通道的间隙越小越好,宜不大于50mm,优选地,净化通道的宽度介于2mm~20mm之间,其性价比较高。In order to ensure the absorption effect and reduce air resistance, the gap of the purification channel should be as small as possible, preferably not more than 50 mm. Preferably, the width of the purification channel is between 2 mm and 20 mm, which has a high cost performance.
在本实施例中,吸收液循环量视空气污染物的浓度确定,优选地,箱体10内液气重量比介于0.1~2之间,其中,空气污染物的浓度越大,液气重量比越大,空气污染物的浓度越小,液气重量比越小。In this embodiment, the circulation amount of the absorption liquid is determined according to the concentration of air pollutants. Preferably, the liquid-to-gas weight ratio in the box 10 is between 0.1 and 2, wherein the greater the concentration of air pollutants, the greater the liquid-to-gas weight ratio, and the smaller the concentration of air pollutants, the smaller the liquid-to-gas weight ratio.
在本申请的一个可选的实施例中,可选装吸收液制冷或制热装置,由于液膜载板23换热面积大,换热效率高,不需要像普通空调直接与空气热交换时需要较高的温差,所以对于制冷和制热装置的工作温度可以接近空气目标温度,从而降低空调装置的负荷,实现节能的目的,且由于与目标温度温差小,尤其是夏季,吹出的风温度与环境温度接近,人体感受更为舒适。In an optional embodiment of the present application, an absorption liquid cooling or heating device can be installed. Since the liquid film carrier plate 23 has a large heat exchange area and high heat exchange efficiency, it does not require a high temperature difference when directly exchanging heat with the air like an ordinary air conditioner. Therefore, the operating temperature of the cooling and heating device can be close to the target air temperature, thereby reducing the load of the air conditioning device and achieving the purpose of energy saving. Moreover, since the temperature difference with the target temperature is small, especially in summer, the temperature of the blown wind is close to the ambient temperature, and the human body feels more comfortable.
在本申请的一个可选的实施例中,液膜载板23包括前液膜载板和后液膜载板,前液膜载板的延伸线与后液膜载板的延伸线斜交,优选地,前液膜载板与进风驱动器11初次输出的风向呈锐角的夹角,优选该角度介于5°-10°之间,以方便吸收液涂布均匀,并确保净化通道间隙均匀,保证吸收效果。后液膜载板为前后排布的多组,多组后液膜载板形成的净化通道前后错位设置,通过将净化通道前后错位设置,可改变气体流动方向,使液膜物质交换更充分,有利于污染物溶解或分散于吸收液中。In an optional embodiment of the present application, the liquid film carrier 23 includes a front liquid film carrier and a rear liquid film carrier, and the extension line of the front liquid film carrier is obliquely intersected with the extension line of the rear liquid film carrier. Preferably, the front liquid film carrier and the wind direction initially output by the air inlet driver 11 are at an acute angle, and the angle is preferably between 5°-10°, so as to facilitate uniform coating of the absorption liquid and ensure uniform clearance of the purification channel to ensure absorption effect. The rear liquid film carrier is a plurality of groups arranged front and back, and the purification channels formed by the plurality of groups of rear liquid film carriers are staggered front and back. By staggering the purification channels front and back, the gas flow direction can be changed, so that the liquid film material exchange is more sufficient, which is conducive to the dissolution or dispersion of pollutants in the absorption liquid.
在本申请的一个可选的实施例中,液膜载板23净化的污染物包括 VOCs、粉尘、烟雾和气溶胶。In an optional embodiment of the present application, pollutants purified by the liquid film carrier 23 include VOCs, dust, smoke and aerosols.
本实施例的空气净化器,采用亲水性的大比表面积的液膜载板23,可以实现在较小的体积空间构造尽可能大的物质和能量交换面积,实现污染物的高效清除,有更高的效能比。The air purifier of this embodiment adopts a hydrophilic liquid film carrier plate 23 with a large specific surface area, which can construct the largest possible material and energy exchange area in a smaller volume space, achieve efficient removal of pollutants, and have a higher efficiency ratio.
本实施例的空气净化器,适用于封闭或半封闭空间的低污染浓度的空气净化,如室内、车厢内、仓内、隧道、街道等场所,可以有效吸收包括粉尘、烟雾、气体的污染物,颗粒越小效果越好;具体通过自由扩散进行物质交换而不是过滤,可以建立较大的气体通道,实现大流量,低阻力,所以空气循环更快,噪声更低,永不堵塞。The air purifier of this embodiment is suitable for air purification with low pollution concentration in closed or semi-closed spaces, such as indoors, in cars, in warehouses, in tunnels, on streets and other places. It can effectively absorb pollutants including dust, smoke and gas, and the smaller the particles, the better the effect. Specifically, by exchanging substances through free diffusion rather than filtering, a larger gas channel can be established to achieve a large flow rate and low resistance, so the air circulates faster, the noise is lower, and it will never be blocked.
本实施例的空气净化器,采用易溶于水且难挥发的物质,可有效控制吸收液的蒸发,从而控制空气湿度,并且在需加湿时可通过补充水分保持舒适湿度,尤其适用于干燥地区或冬季。The air purifier of this embodiment uses a substance that is easily soluble in water and difficult to volatilize, which can effectively control the evaporation of the absorption liquid, thereby controlling the air humidity, and can maintain a comfortable humidity by adding water when humidification is needed. It is particularly suitable for dry areas or winter.
实施例2Example 2
本实施例与实施例1相比,其不同点在于:吸收液为空气净化吸收液,空气净化吸收液包括水和化学溶质;化学溶质选自醇、铵盐、羟胺和含有伯胺/仲胺官能团的化合物及其盐类中的至少一种。Compared with Example 1, this embodiment is different in that the absorption liquid is an air purification absorption liquid, and the air purification absorption liquid includes water and a chemical solute; the chemical solute is selected from at least one of alcohol, ammonium salt, hydroxylamine and compounds containing primary amine/secondary amine functional groups and their salts.
具体的,空气净化吸收液的pH值为2~5;空气净化吸收液中化学溶质的百分含量为10%~90%;醇的碳原子个数不大于15;醇为1,2-丙二醇,1,3-丙二醇或丙三醇;含有伯胺/仲胺官能团的化合物及其盐类的碳原子个数不大于15;含有伯胺/仲胺官能团的化合物及其盐类选自乙胺、丙胺、丁胺、二乙胺、二丙胺和二丁胺中的至少一种。Specifically, the pH value of the air purification absorption liquid is 2-5; the percentage of chemical solutes in the air purification absorption liquid is 10%-90%; the number of carbon atoms of the alcohol is not more than 15; the alcohol is 1,2-propylene glycol, 1,3-propylene glycol or glycerol; the number of carbon atoms of the compound containing primary/secondary amine functional groups and its salts is not more than 15; the compound containing primary/secondary amine functional groups and its salts are selected from at least one of ethylamine, propylamine, butylamine, diethylamine, dipropylamine and dibutylamine.
本实施例中的吸收液包含与甲醛缩合反应的物质,可有效固定甲醛而不会造成二次污染而且化学溶质为易生物降解物质,可直接通过化粪池进行生物降解,或通过专业机构净化再生使用,不会产生难以降解的 废物,真正实现绿色循环。The absorption liquid in this embodiment contains a substance that reacts with formaldehyde condensation, which can effectively fix formaldehyde without causing secondary pollution. In addition, the chemical solute is a biodegradable substance and can be directly biodegraded through a septic tank or purified and recycled by a professional organization without generating difficult-to-degrade waste, thus truly realizing a green cycle.
以上,结合具体实施例对本申请的技术方案进行了详细介绍,所描述的具体实施例用于帮助理解本申请的思想。本领域技术人员在本申请具体实施例的基础上做出的推导和变型也属于本申请保护范围之内。The technical solution of the present application is described in detail above in combination with specific embodiments, and the described specific embodiments are used to help understand the concept of the present application. Derivations and modifications made by those skilled in the art based on the specific embodiments of the present application also fall within the scope of protection of the present application.

Claims (9)

  1. 一种空气净化器,包括箱体(10)、层流净化组件、进风驱动器(11)和控制器(12),所述箱体(10)相对的侧壁分别开设有进风口(101)和出风口(102),所述进风口(101)处装设有进风驱动器(11),所述层流净化组件装设于箱体(10)内,所述控制器(12)装设于箱体(10)的正面,并用于控制层流净化组件和进风驱动器(11),其特征在于:An air purifier comprises a housing (10), a laminar flow purification component, an air inlet driver (11) and a controller (12), wherein opposite side walls of the housing (10) are respectively provided with an air inlet (101) and an air outlet (102), the air inlet driver (11) is installed at the air inlet (101), the laminar flow purification component is installed in the housing (10), the controller (12) is installed on the front side of the housing (10) and is used to control the laminar flow purification component and the air inlet driver (11), and is characterized in that:
    所述层流净化组件包括隔板(21)、循环泵(22)和液膜载板(23),所述隔板(21)水平固设于箱体(10)内,并将箱体(10)内分隔成上储液腔和下安装腔,所述下安装腔内竖向间隔设有液膜载板(23),任意相邻两块液膜载板(23)之间形成净化通道,所述液膜载板(23)表面涂布有吸收液,所述下安装腔靠近出风口(102)的一侧设有凹槽(103),所述凹槽(103)内装设有循环泵(22),所述循环泵(22)的出液端通过输液管路与上储液腔连通,所述隔板(21)上均匀开设有用于向液膜载板(23)渗透吸收液的渗透孔(211)。The laminar flow purification component comprises a partition (21), a circulation pump (22) and a liquid film carrier (23); the partition (21) is horizontally fixed in a box body (10) and divides the box body (10) into an upper liquid storage chamber and a lower installation chamber; the liquid film carrier (23) is vertically spaced in the lower installation chamber, and a purification channel is formed between any two adjacent liquid film carriers (23); the surface of the liquid film carrier (23) is coated with an absorption liquid; a groove (103) is provided on one side of the lower installation chamber close to the air outlet (102); a circulation pump (22) is installed in the groove (103); the liquid outlet end of the circulation pump (22) is connected to the upper liquid storage chamber through a liquid infusion pipeline; and penetration holes (211) are evenly provided on the partition (21) for penetrating the absorption liquid into the liquid film carrier (23).
  2. 根据权利要求1所述的一种空气净化器,其特征在于,所述净化通道的宽度介于2mm~20mm之间。An air purifier according to claim 1, characterized in that the width of the purification channel is between 2 mm and 20 mm.
  3. 根据权利要求2所述的一种空气净化器,其特征在于,所述液膜载板为亲水材质的薄片状结构。An air purifier according to claim 2, characterized in that the liquid film carrier is a thin sheet structure made of hydrophilic material.
  4. 根据权利要求1所述的一种空气净化器,其特征在于,所述箱体(10)内液气重量比介于0.1~2之间。An air purifier according to claim 1, characterized in that the liquid-to-gas weight ratio in the box (10) is between 0.1 and 2.
  5. 根据权利要求4所述的一种空气净化器,其特征在于,所述液膜载板(23)包括前液膜载板和后液膜载板,所述前液膜载板的延伸线与后液膜载板的延伸线斜交。An air purifier according to claim 4, characterized in that the liquid film carrier plate (23) comprises a front liquid film carrier plate and a rear liquid film carrier plate, and the extension line of the front liquid film carrier plate is obliquely intersected with the extension line of the rear liquid film carrier plate.
  6. 根据权利要求5所述的一种空气净化器,其特征在于,所述后液 膜载板为前后排布的多组,多组后液膜载板形成的净化通道前后错位设置。An air purifier according to claim 5, characterized in that the rear liquid film carrier plates are multiple groups arranged front to back, and the purification channels formed by the multiple groups of rear liquid film carrier plates are staggered front to back.
  7. 根据权利要求1所述的一种空气净化器,其特征在于,所述吸收液的溶质为易溶于水、难挥发且具有空气净化功效的液态介质。An air purifier according to claim 1, characterized in that the solute of the absorption liquid is a liquid medium that is easily soluble in water, difficult to volatilize and has air purification effect.
  8. 根据权利要求7所述的一种空气净化器,其特征在于,所述吸收液为空气净化吸收液,所述空气净化吸收液包括水和化学溶质;所述化学溶质选自醇、铵盐、羟胺和含有伯胺/仲胺官能团的化合物及其盐类中的至少一种。An air purifier according to claim 7, characterized in that the absorption liquid is an air purification absorption liquid, and the air purification absorption liquid comprises water and a chemical solute; the chemical solute is selected from at least one of alcohols, ammonium salts, hydroxylamines, and compounds containing primary amine/secondary amine functional groups and their salts.
  9. 根据权利要求8所述的一种空气净化器,其特征在于,所述空气净化器净化的污染物包括VOCs、粉尘、烟雾和气溶胶。An air purifier according to claim 8, characterized in that the pollutants purified by the air purifier include VOCs, dust, smoke and aerosols.
PCT/CN2022/139859 2022-10-17 2022-12-19 Air purifier WO2024082419A1 (en)

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