WO2021189779A1 - 一种湿空气静电凝水的方法和装置 - Google Patents

一种湿空气静电凝水的方法和装置 Download PDF

Info

Publication number
WO2021189779A1
WO2021189779A1 PCT/CN2020/114454 CN2020114454W WO2021189779A1 WO 2021189779 A1 WO2021189779 A1 WO 2021189779A1 CN 2020114454 W CN2020114454 W CN 2020114454W WO 2021189779 A1 WO2021189779 A1 WO 2021189779A1
Authority
WO
WIPO (PCT)
Prior art keywords
charge generator
positive
negative
power supply
high voltage
Prior art date
Application number
PCT/CN2020/114454
Other languages
English (en)
French (fr)
Inventor
郑钦臻
Original Assignee
双良节能系统股份有限公司
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
Application filed by 双良节能系统股份有限公司 filed Critical 双良节能系统股份有限公司
Priority to US17/777,875 priority Critical patent/US20230211356A1/en
Priority to KR1020227019626A priority patent/KR20220092627A/ko
Publication of WO2021189779A1 publication Critical patent/WO2021189779A1/zh

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/017—Combinations of electrostatic separation with other processes, not otherwise provided for
    • B03C3/0175—Amassing particles by electric fields, e.g. agglomeration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02—Plant or installations having external electricity supply
    • B03C3/04—Plant or installations having external electricity supply dry type
    • B03C3/12—Plant or installations having external electricity supply dry type characterised by separation of ionising and collecting stations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/38—Particle charging or ionising stations, e.g. using electric discharge, radioactive radiation or flames
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/40—Electrode constructions
    • B03C3/41—Ionising-electrodes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/40—Electrode constructions
    • B03C3/45—Collecting-electrodes
    • B03C3/47—Collecting-electrodes flat, e.g. plates, discs, gratings
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/66—Applications of electricity supply techniques
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C2201/00—Details of magnetic or electrostatic separation
    • B03C2201/04—Ionising electrode being a wire
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use

Definitions

  • the invention relates to a method and a device for electrostatic condensation of wet air, and belongs to the field of electrostatic technology application.
  • the ambient air humidity has an important impact on people's life and production.
  • a humid environment is prone to breed bacteria and viruses, which poses a serious threat to human health, and long-term living in a humid environment can induce skin, joints and many other diseases; in production activities and industrial fields, the humid environment seriously interferes
  • various production tools such as machines, instruments, equipment, such as scientific research, industry, medical and health, instrumentation, commodity storage, underground engineering, and computer rooms, archives, warehouses and other high-humidity places, resulting in meters, computers, telecommunications equipment , Drugs, materials, etc., caused by damp, rust, and mildew, causing serious economic and property losses.
  • the commonly used dehumidification methods mainly include heat exchange dehumidification, compression dehumidification, rotary disc dehumidification, liquid absorption dehumidification, solid adsorption dehumidification, etc.
  • these dehumidification methods are difficult to recycle water vapor in humid air.
  • the rotary disc dehumidification method converts the water vapor in the humid air from one environment to another environment, and the dehumidification effect is poor; the liquid absorption method and the solid absorption method are difficult to separate the water vapor from the absorbent or adsorbent, and the dehumidification cost Larger; although the heat exchange method and the compression method have better dehumidification effects, it is difficult to recover water vapor, such as the white mist at the outlet of an industrial cooling tower. Although the heat exchange method can effectively eliminate whiteness, it does not save water The effect of. Therefore, a humid air dehumidification technology that can recycle water vapor is very necessary.
  • the microscopic performance of gaseous water liquefaction is the shortening of the distance between gaseous water molecules, and the electric dust removal technology is a process in which particles are charged and then the charged particles are captured under the action of an electrostatic field. Therefore, the principle of electric dust removal can be used to make the The water vapor in the humid air is liquefied.
  • the Chinese patent with publication number CN2589860Y uses the principle of electrostatic dust removal to disclose an electrostatic condensation type dehumidifier. Moist air molecules are collected and condensed into water by the net-shaped water collecting plate under the action of high-voltage static electricity. The patent regards water molecules as particles, and expects that the high-voltage electrostatic field has a trapping effect on water molecules and condenses water. However, in practical applications, it is found that it only has a certain trapping effect on the droplets that already exist in the humid air, and has little effect on the effect of water vapor.
  • the purpose of the present invention is to solve the above-mentioned background problems and provide a method and device for electrostatic condensation of humid air. High, low cost, safe and reliable operation.
  • a method for electrostatic condensation of wet air including the following steps:
  • Step 1 Through positive and negative corona discharge, a large number of positive and negative charges are generated in the two areas respectively;
  • Step 2 Moist air enters the independent positive and negative corona zones to make the water molecules carry positive and negative charges respectively;
  • Step 3 After mixing, water molecules with positive and negative charges are attracted to each other and condense under the action of an electrostatic field.
  • the positive polarity corona discharge in the first step is driven by a positive polarity high voltage direct current power supply, and the negative polarity corona discharge is driven by a negative polarity high voltage direct current power supply.
  • corona area refers to the area of corona discharge, in which gas ionizes and generates a large amount of ion charge, which provides a source of charge for water molecules to be charged.
  • a device for electrostatic condensation of wet air comprising an inlet bell mouth, an air flow evenly distributed plate, a positive charge generator, a negative charge generator, a condenser and an outlet bell mouth, forming an integral shell and grounding;
  • the inlet bell mouth and the outlet bell mouth are arranged on both sides of the shell;
  • the air flow evenly distributed plate is arranged at the inlet end of the inlet bell mouth;
  • the positive charge generator and the negative charge generator are arranged in parallel and are arranged at the rear end of the airflow uniformly distributed plate along the airflow direction. They are not only a device for generating positive and negative charges, but also a channel for saturated humid air, which belongs to the original water molecule.
  • the bit-charged device does not require additional charge source injection, simplifies the structure layout, and effectively reduces the volume of the device.
  • the condenser is arranged at the rear end of the positive charge generator and the negative charge generator along the airflow direction.
  • the positive charge generator is driven by a positive polarity high-voltage direct current power supply
  • the negative charge generator is driven by a negative high voltage direct current power supply.
  • the positive polarity high-voltage direct current power supply drives a plurality of anode wires
  • the negative polarity high voltage direct current power source drives a plurality of cathode wires.
  • the positive charge generator is a rectangular parallelepiped, and includes a positive charge generator housing, a plate electrode, an anode wire, and a positive polarity high-voltage direct current power supply;
  • the positive charge generator housing is connected to the low voltage end of the positive polarity high voltage direct current power supply and is grounded;
  • the anode wire is arranged in the center of the positive charge generator along the airflow direction, and is connected to the high voltage end of the positive polarity high voltage direct current power supply;
  • the negative charge generator is a rectangular parallelepiped, which includes a negative charge generator housing, a cathode wire and a negative polarity high-voltage direct current power supply, and shares a plate electrode with the positive charge generator;
  • the plate electrode is connected to the positive charge generator housing and the negative charge generator housing;
  • the housing of the negative charge generator is connected to the low voltage end of the negative polarity high voltage direct current power supply and is grounded;
  • the cathode wire is placed in the center of the negative charge generator along the airflow direction, and is connected to the high voltage end of the negative polarity high voltage direct current power supply;
  • the positive charge generator housing and the negative charge generator housing are in direct contact.
  • the condenser includes a first layer of condensing net and a second layer of condensing net arranged in the housing;
  • the central axis of the first layer of condensation net coincides with the plate electrode in the horizontal direction, and the length in the vertical direction is equal to the distance between the anode wire and the cathode wire;
  • the area of the second layer of condensate net is equal to the cross-sectional area of the whole shell
  • the two layers of condensate nets are directly connected to the positive charge generator shell and the negative charge generator shell and are grounded.
  • the wet air electrostatic condensing device of the present invention works, the wet air evenly flows through the positive and negative charge generators, which ionize the air molecules in the wet air, and generate a large number of positive and negative charges respectively. Captured by water molecules, the water molecules carrying different kinds of charges are fully mixed in the mixer to condense water. At the same time, the grounded condensing network further promotes the condensation of the charged water molecules, and the condensed water is discharged from the inlet bell mouth under the action of gravity. Condensation and recovery of water vapor in humid air.
  • the method and device for electrostatic condensation of humid air according to the present invention has the following advantages:
  • the dry air in the moist air can be used as the source of charge of water vapor to form condensed water, without the need for external injection of charge sources;
  • the condensation effect is more than 10 times higher than that of electrostatic condensation with only the same charge, and the condensation efficiency is high;
  • Fig. 1 is a schematic top view of a device for electrostatic condensation of humid air according to the present invention.
  • Figure 2 is a schematic elevation view of a device for electrostatic condensation of humid air according to the present invention.
  • Fig. 3 is a schematic side view of a positive charge generator and a negative charge generator of a device for electrostatic condensation of wet air according to the present invention.
  • Fig. 4 is a schematic side view of the condensation net of a device for electrostatic condensation of humid air according to the present invention.
  • Fig. 5 is a schematic side view of a positive charge generator and a negative charge generator in another embodiment of a device for electrostatic condensation of humid air according to the present invention.
  • a device for electrostatic condensation of wet air including an inlet bell mouth 1, an air flow evenly distributed plate 2, a positive charge generator 3, a negative charge generator 4, a condenser 5 and an outlet bell mouth 6. Form an integral shell and ground;
  • the inlet bell mouth 1 and the outlet bell mouth 6 are arranged on both sides of the housing;
  • the air flow evenly distributed plate 2 is arranged at the inlet end of the inlet bell mouth 1;
  • the positive charge generator 3 and the negative charge generator 4 are arranged in parallel, and are arranged at the rear end of the airflow uniformly distributed plate 2 along the airflow direction;
  • the condenser 5 is arranged at the rear end of the positive charge generator 3 and the negative charge generator 4 along the airflow direction.
  • the inlet bell mouth 1 is an air inlet for moist air
  • the change ratio of the circulation area of the shrinking opening and the flaring opening is ⁇ 1:4
  • the slope of the inlet bell mouth is ⁇ 45
  • the stainless steel metal material is used;
  • the air flow uniform distribution plate 2 is placed at the flared end of the inlet bell mouth 1.
  • the resistance of the air flow uniform distribution plate 2 is less than or equal to 20 Pa. It is made of polytetrafluoroethylene, which is hydrophobic and does not easily cause condensation to accumulate.
  • the positive charge generator 3 and the negative charge generator 4 are arranged side by side, and placed at the rear end of the air flow evenly distributed plate 2. They are both a positive and negative charge generating device and a flow of saturated humid air. Through the channel, it belongs to the in-situ charging device of water molecules, which does not require additional charge source injection, simplifies the structure layout, and effectively reduces the volume of the device;
  • the positive charge generator 3 is driven by a positive polarity high voltage direct current power supply 3.3;
  • the negative charge generator 4 is driven by a negative polarity high voltage direct current power supply 4.3.
  • the positive polarity high-voltage direct current power supply 3.3 drives a plurality of anode wires 3.1;
  • the negative polarity high-voltage direct current power supply 4.3 drives a plurality of cathode wires 4.1.
  • the positive charge generator 3 is a rectangular parallelepiped, and includes a positive charge generator housing 3.2, a plate electrode 3.4, an anode wire 3.1 and a positive polarity high-voltage direct current power supply 3.3;
  • the positive charge generator housing 3.2 is connected to the low voltage end of the positive polarity high voltage direct current power supply 3.3 and is grounded;
  • the anode wire 3.1 is arranged in the center of the positive charge generator 3 along the airflow direction, and is connected to the high voltage end of the positive polarity high voltage direct current power supply 3.3;
  • the negative charge generator 4 is a rectangular parallelepiped, which includes a negative charge generator housing 4.2, a cathode wire 4.1 and a negative polarity high-voltage direct current power supply 4.3, and shares a plate electrode 3.4 with the positive charge generator 3;
  • the plate electrode 3.4 is connected to the positive charge generator housing 3.2 and the negative charge generator housing 4.2;
  • the negative charge generator housing 4.2 is connected to the low voltage end of the negative high voltage DC power supply 4.3 and is grounded;
  • the cathode wire 4.1 is placed in the center of the negative charge generator 4 along the airflow direction, and is connected to the high voltage end of the negative polarity high voltage direct current power supply 4.3;
  • the positive charge generator housing 3.2 and the negative charge generator housing 4.2 are in direct contact.
  • the positive charge generator housing 3.2 can be composed of 4 rectangular stainless steel plates with a size of a ⁇ b to form a rectangular air flow channel with a size of a ⁇ a ⁇ b through a metal wire and a positive high-voltage DC power supply. 3.3 is connected to the ground terminal, the cuboid air flow channel is easy to install, and it is easy to seamlessly connect with the inlet bell mouth 1 and the outlet bell mouth 6;
  • the anode wire 3.1 is a stainless steel wire with a diameter of ⁇ 1mm, placed in the center of the rectangular parallelepiped airflow channel along the airflow direction, and is connected to the high-voltage end of the positive polarity high-voltage DC power supply 3.3 through a metal wire;
  • the negative charge generator housing 4.2 can be composed of 4 rectangular stainless steel plates with a size of a ⁇ b, forming a rectangular parallelepiped air flow channel with a size of a ⁇ a ⁇ b.
  • the ground terminal of the DC power supply 4.3 is connected, the rectangular parallelepiped air flow channel is easy to install, and it is easy to seamlessly connect with the inlet bell mouth and the outlet bell mouth;
  • the cathode wire 4.1 is a stainless steel wire with a diameter of ⁇ 1 mm, and is placed along the direction of the air flow. At the center of the rectangular parallelepiped air flow channel, it is connected to the high voltage end of the negative polarity high voltage DC power supply 4.3 through a metal wire;
  • the positive polarity high-voltage direct current power supply 3.3 Output voltage ⁇ 10kV, output current ⁇ 2mA, output frequency 50Hz ⁇ 300Hz; output voltage ⁇ 15kV, output current ⁇ 2mA, output frequency 50Hz ⁇ 300Hz of the negative polarity high-voltage DC power supply 4.3, keep low output current operation
  • the required output voltage is reduced accordingly, which saves power consumption, and the use safety is high, the insulation requirement is reduced, the safety distance is reduced, and the space utilization rate is high;
  • the plate electrode 3.4 shared by the positive charge generator 3 and the negative charge generator 4 is a rectangular stainless steel plate with a size of a ⁇ b; the size of the rectangular stainless steel plate is 50mm ⁇ a ⁇ 100mm;
  • the size of the rectangular stainless steel plate is 2a ⁇ b ⁇ 4a; b ⁇ 2a is to ensure that the gas is fully ionized so that the water molecules are fully charged, and b ⁇ 4a is to prevent the charged water molecules from being trapped by the plate electrode and the charge is lost. , It also saves equipment costs.
  • the condenser 5 includes a first layer of condensing net 5.1 and a second layer of condensing net 5.2 arranged in the housing;
  • the central axis of the first layer of condensation net 5.1 coincides with the plate electrode 3.4 in the horizontal direction, and the vertical length is equal to the distance between the anode wire 3.1 and the cathode wire 4.1;
  • the area of the second layer of condensate net 5.2 is equal to the cross-sectional area of the whole shell
  • the two layers of condensate nets are directly connected to the positive charge generator housing 3.2 and the negative charge generator housing 4.2 and grounded.
  • the first layer of condensing net 5.1 and the second layer of condensing net 5.2 are both stainless steel metal nets, which are connected to the shell, and the meshes are 300 meshes, arranged along the airflow direction.
  • the temperature of the humid air is ⁇ 95°C; for the use of a set of positive and negative charge generators, the humid air Total flow ⁇ 3.6ab ⁇ 10-3m3/h;
  • the present invention can use n groups of positive and negative charge generators simultaneously.
  • the combined use of multiple groups can enhance the turbulence intensity of charged water molecules in the mixer and promote condensation.
  • the amount of condensed water S used by the negative charge generator is much larger than n ⁇ a, and the above a refers to the amount of condensed water used by a group of positive and negative charge generators.
  • a method for electrostatic condensation of wet air including the following steps:
  • Step 1 Through positive and negative corona discharge, a large number of positive and negative charges are generated in the two areas respectively;
  • Step 2 Moist air enters the independent positive and negative corona zones to make the water molecules carry positive and negative charges respectively;
  • Step 3 After mixing, water molecules with positive and negative charges are attracted to each other and condense under the action of an electrostatic field.
  • corona area refers to the area of corona discharge, in which gas ionizes and generates a large amount of ion charge, which provides a source of charge for water molecules to be charged;
  • the above-mentioned positive polarity corona discharge is driven by a positive polarity high voltage DC power supply, and the negative polarity corona discharge is driven by a negative polarity high voltage DC power supply;
  • the airflow organization should be optimized before the moist air enters the positive polarity corona zone and the negative polarity corona zone respectively.
  • the angle between the airflow direction and the horizontal plane is ⁇ 75°.
  • a wet air electrostatic condensation method of the present invention is to start the above device, connect the positive polarity high voltage direct current power supply 3.3 and the negative polarity high voltage direct current power supply 4.3, the positive charge generator 3 and the negative charge generator 4 A large number of positive and negative charges are generated respectively.
  • the moist air enters the positive charge generator 3 and the negative charge generator 4 uniformly from the inlet bell mouth 1 through the airflow uniformly distributed plate 2, and the water molecules in the moist air are charged with positive and negative charges respectively.
  • the negative charge then enters the condenser 5.
  • the saturated humid air with a volume flow of 5L/min and a dry bulb temperature of 85°C enters the wet air according to the present invention.
  • Air electrostatic condensing device after 1h, 300ml of condensed water will be obtained by natural condensation; start positive charge generator 3 and negative charge generator 4, positive polarity high voltage DC power supply 3.3 with output voltage 10kV, output current 2mA, output frequency 50Hz parameters Run, the negative polarity high-voltage DC power supply 4.2 runs with output voltage of 15kV, output current of 2mA, and output frequency of 50Hz. After 1h, 1100ml of condensed water is obtained, and the condensate yield per unit energy consumption is 16ml/W.
  • this embodiment is different from Embodiment 1.
  • the positive charge generator 3 and the negative charge generator 4 respectively use N anode wires 3.1 and cathode wires 4.1;
  • N anode wires 3.1 are connected in parallel with the high voltage end of the positive polarity high voltage DC power supply 3.3;
  • the N cathode wires 4.1 are connected to the high voltage end of the negative polarity high voltage direct current power supply 4.3 in parallel.
  • the advantage of this embodiment is that the positive charge generator 3 and the negative charge generator 4 operate at a higher power to increase the processing flow rate of humid air and increase the condensate yield per unit energy consumption.

Landscapes

  • Electrostatic Separation (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)

Abstract

一种湿空气静电凝水的方法，通过正极性和负极性电晕放电，使两个区域内分别产生大量的正、负电荷；湿空气分别进入独立的正极性电晕区和负极性电晕区使水分子分别携带正、负电荷；混合后携带正、负电荷的水分子在库仑力的作用下相互吸引而凝结；一种湿空气静电凝水的装置，包括进口喇叭口(1)、气流均布板(2)、正电荷发生器(3)、负电荷发生器(4)、凝水器(5)和出口喇叭口(6)；凝水器(5)沿气流方向设置在正电荷发生器(3)和负电荷发生器(4)的后端；湿空气静电凝水的方法和装置在除湿的同时可对水蒸气进行回收利用，装置体积小、结构简单，易于安装，制造和运行成本低，使用安全性高。

Description

一种湿空气静电凝水的方法和装置
本申请要求于2020年3月24日提交中国专利局、申请号为202010210287.6、发明名称为“一种湿空气静电凝水的方法和装置”的中国专利申请的优先权，其全部内容通过引用结合在本申请中。
技术领域
本发明涉及一种湿空气静电凝水的方法和装置，属于静电技术应用领域。
背景技术
现有技术下，环境空气湿度无论是对人们的生活还是生产，均有重要的影响。潮湿的环境容易滋生细菌、病毒，对人的健康带来严重威胁，而且长期生活在潮湿的环境中会诱发皮肤、关节及其他众多疾病；在生产活动和工业领域中，潮湿的环境严重干扰了机器、仪器、设备等各种生产工具的运行，如在科研、工业、医疗卫生、仪器仪表，商品储藏、地下工程以及电脑室、档案室、仓库等高湿度场所，导致仪表、电脑、电讯器材、药品、资料等受潮、锈蚀、霉烂而造成严重经济财产损失。
目前常用的除湿方法主要有换热除湿法、压缩除湿法、转盘除湿法、液体吸收式除湿法、固体吸附式除湿法等，但是这些除湿方法难以对湿空气中的水蒸气进行回收利用。如转盘除湿法是将湿空气中的水蒸气由一个环境中转换到另一个环境中，而且除湿效果差；液体吸收法和固体吸附法难以将水蒸气与吸收剂或吸附剂分开，而且除湿成本较大；换热法和压缩法虽然具有较优的除湿效果，但是难以对水蒸气进行回收，比如工业冷却塔出口的白雾，虽然采用换热法可有效的消白，但是并没有节水的功效。因此，一种能够对水蒸气进行回收利用的湿空气除湿技术是十分有必要的。
气态水液化微观表现为气态水分子间距的缩短，而电除尘技术是通过微粒荷电然后在静电场作用下使荷电微粒被捕集的过程，所以可利用电除尘原理，通过高压静电场使湿空气中的水蒸气液化。公开号CN2589860Y的中国专利利用静电除尘的原理公开了一种静电凝结式除湿机，技术核心 为高压静电发生器，具体为电晕线和网状集水板，这两者之间施加高电压，潮湿空气分子在高压静电作用下由网状集水板收集凝结成水。该专利将水分子看作微粒，期望高压静电场对水分子具有捕集作用而凝水。但是在实际应用中发现只是对湿空气中已存在的雾滴具有一定捕集效果，对水蒸气作用影响不大。
发明内容
本发明的目的是为了解决上述背景问题中提出的问题，提供一种湿空气静电凝水的方法和装置，它可适用于大风量、高湿度的湿空气条件，可以长时间持续运行，且效率高、成本低、运行安全可靠。
本发明的目的是这样实现的：一种湿空气静电凝水的方法，包括以下步骤：
步骤一：通过正极性和负极性电晕放电，使两个区域内分别产生大量的正、负电荷；
步骤二：湿空气分别进入独立的正极性电晕区和负极性电晕区使水分子分别携带正、负电荷；
步骤三：混合后携带正、负电荷的水分子在静电场作用下相互吸引而凝结。
所述步骤一中的正极性电晕放电采用正极性高压直流电源驱动，负极性电晕放电采用负极性高压直流电源驱动。
上述电晕区是指电晕放电的区域，在该区域中气体发生电离并产生大量的离子电荷，为水分子荷电提供了电荷来源。
一种湿空气静电凝水的装置，包括进口喇叭口、气流均布板、正电荷发生器、负电荷发生器、凝水器和出口喇叭口，形成整体外壳并接地；
所述进口喇叭口和出口喇叭口设置在外壳两侧；
所述气流均布板设置在进口喇叭口的进口端；
所述正电荷发生器和负电荷发生器并行排列，并沿气流方向设置在气流均布板后端，既是正电荷和负电荷的发生装置，也是饱和湿空气的流经通道，属于水分子原位荷电装置，不需要额外的电荷源注入，简化了结构 布置，有效的缩减了装置的体积。
所述凝水器沿气流方向设置在正电荷发生器和负电荷发生器的后端。
所述正电荷发生器由正极性高压直流电源驱动；
所述负电荷发生器由负极性高压直流电源驱动。
所述正极性高压直流电源驱动多根阳极线；
所述负极性高压直流电源驱动多根阴极线。
所述正电荷发生器为长方体，包括正电荷发生器壳体、板电极、阳极线和正极性高压直流电源；
所述正电荷发生器壳体与正极性高压直流电源的低压端相连并接地；
所述阳极线顺着气流方向布置于正电荷发生器的中心，与正极性高压直流电源的高压端相连；
所述负电荷发生器为长方体，包括负电荷发生器壳体、阴极线和负极性高压直流电源，并与正电荷发生器共用板电极；
所述板电极与正电荷发生器壳体和负电荷发生器壳体相连；
所述负电荷发生器壳体与负极性高压直流电源的低压端相连并接地；
所述阴极线顺着气流方向置于负电荷发生器的中心，并与负极性高压直流电源的高压端相连；
所述正电荷发生器壳体和负电荷发生器壳体直接接触。
所述凝水器包括设置在壳体内的第一层凝水网和第二层凝水网；
所述第一层凝水网的中心轴线在水平方向上与板电极重合，且竖直方向长度与阳极线和阴极线之间的距离相等；
所述第二层凝水网的面积与整体外壳的横截面面积相等；
两层凝水网均直接与正电荷发生器壳体和负电荷发生器壳体相连并接地。
当本发明的一种湿空气静电凝水的装置工作后，湿空气均匀地分别流经正、负电荷发生器，会对湿空气中的空气分子进行电离，分别产生大量的正、负电荷而被水分子捕获，携带异种电荷的水分子在混合器中充分混合而凝水，同时接地的凝水网进一步促进荷电水分子的凝结，凝水在重力作用下从入口喇叭口排出，实现了对湿空气中水蒸气的凝水以及回收。
相比于现有技术，本发明一种湿空气静电凝水的方法和装置具有以下优点：
1、体积小、占地小、便于建造和安装，建造和运行成本低、效率高；
2、能够利用湿空气中干空气作为水蒸气的电荷来源形成凝水，不需要外界注入电荷来源；
3、凝水效果高于只有同种电荷的静电凝水效果高10倍以上，凝水效率高；
4、能够长时间持续运行，放电输出电压低，运行安全稳定；
5、对湿空气温度、湿度的适用范围大；
6、易于多组正、负电荷发生器并用，其建造成本、运行成本远低于目前大型的空气除湿机。
附图说明
图1为本发明一种湿空气静电凝水的装置俯视示意图。
图2为本发明一种湿空气静电凝水的装置立面示意图。
图3为本发明一种湿空气静电凝水的装置的正电荷发生器和负电荷发生器的侧面示意图。
图4为本发明一种湿空气静电凝水的装置的凝水网的侧面示意图。
图5为本发明一种湿空气静电凝水的装置的另一种实施方式下正电荷发生器和负电荷发生器的侧面示意图。
其中：
1、进口喇叭口；2、气流均布板；3、正电荷发生器；3.1、阳极线；3.2、正电荷发生器壳体；3.3、正极性高压直流电源；3.4、板电极；4、负电荷发生器；4.1、阴极线；4.2、负电荷发生器壳体；4.3、负极性高压直流电源；5、凝水器；5.1、第一层凝水网；5.2、第二层凝水网；6、出口喇叭口。
具体实施方式
下面结合附图和具体实施例对本发明加以说明：
如图1～4所示，一种湿空气静电凝水的装置，包括进口喇叭口1、气流均布板2、正电荷发生器3、负电荷发生器4、凝水器5和出口喇叭口6，形成整体外壳并接地；
所述进口喇叭口1和出口喇叭口6设置在外壳两侧；
所述气流均布板2设置在进口喇叭口1的进口端；
所述正电荷发生器3和负电荷发生器4并行排列，并沿气流方向设置在气流均布板2后端；
所述凝水器5沿气流方向设置在正电荷发生器3和负电荷发生器4的后端。
在本实施例中，所述的进口喇叭口1为湿空气的进气口，缩口与扩口的流通面积变化比≤1:4，入口喇叭口的坡度≤45，采用不锈钢金属材质；
所述的气流均布板2置于进口喇叭口1的扩口端，气流均布板2的阻力≤20Pa，采用聚四氟乙烯材质，为疏水性，不易造成凝水积累。
在本实施例中，所述的正电荷发生器3和负电荷发生器4并列布置，且置于气流均布板2后端，既是正电荷和负电荷的发生装置，也是饱和湿空气的流经通道，属于水分子原位荷电装置，不需要额外的电荷源注入，简化了结构布置，有效的缩减了装置的体积；
所述正电荷发生器3由正极性高压直流电源3.3驱动；
所述负电荷发生器4由负极性高压直流电源4.3驱动。
所述正极性高压直流电源3.3驱动多根阳极线3.1；
所述负极性高压直流电源4.3驱动多根阴极线4.1。
所述正电荷发生器3为长方体，包括正电荷发生器壳体3.2、板电极3.4、阳极线3.1和正极性高压直流电源3.3；
所述正电荷发生器壳体3.2与正极性高压直流电源3.3的低压端相连并接地；
所述阳极线3.1顺着气流方向布置于正电荷发生器3的中心，与正极性高压直流电源3.3的高压端相连；
所述负电荷发生器4为长方体，包括负电荷发生器壳体4.2、阴极线4.1和负极性高压直流电源4.3，并与正电荷发生器3共用板电极3.4；
所述板电极3.4与正电荷发生器壳体3.2和负电荷发生器壳体4.2相连；
所述负电荷发生器壳体4.2与负极性高压直流电源4.3的低压端相连并接地；
所述阴极线4.1顺着气流方向置于负电荷发生器4的中心，并与负极性高压直流电源4.3的高压端相连；
所述正电荷发生器壳体3.2和负电荷发生器壳体4.2直接接触。
在本实施例中，所述正电荷发生器壳体3.2可以由4块尺寸为a×b的长方形不锈钢平板构成尺寸为a×a×b的长方体气流通道，通过金属导线与正极性高压直流电源3.3的接地端相连，长方体气流通道易于安装，而且易于与所述的进口喇叭口1和出口喇叭口6无缝连接；
所述阳极线3.1为不锈钢金属丝，直径≤1mm，沿着气流方向置于长方体气流通道的中心，通过金属导线与所述的正极性高压直流电源3.3的高压端相连；
在本实施例中，所述负电荷发生器壳体4.2可以由4块尺寸为a×b的长方形不锈钢平板，构成了尺寸为a×a×b的长方体气流通道，通过金属导线与负极性高压直流电源4.3的接地端相连，长方体气流通道易于安装，而且易于与所述的入口喇叭口和出口喇叭口无缝连接；所述阴极线4.1为不锈钢金属丝，直径≤1mm，沿着气流方向置于长方体气流通道的中心，通过金属导线与负极性高压直流电源4.3的高压端相连；
在本实施例中，由于电晕放电发生后离子个数远大于湿空气中水分子个数，足以使水分子荷电，为了提高电能利用率，优选的，所述的正极性高压直流电源3.3的输出电压≥10kV，输出电流≥2mA，输出频率50Hz～300Hz；所述负极性高压直流电源4.3的输出电压≥15kV，输出电流≥2mA，输出频率50Hz～300Hz，保持较低输出电流运行的情况下，所需输出电压随之降低，节约电耗，而且使用安全性高，绝缘要求降低，缩小了安全距离，空间利用率高；
在本实施例中，所述的正电荷发生器3和负电荷发生器4共用的板电极3.4是尺寸为a×b的长方形不锈钢平板；上述长方形不锈钢平板尺寸50mm≤a≤100mm；
当a＜50mm极易容易导致板电极和线电极之间发生火花放电而运行不稳定；
当a＞100mm增大了板电极和线电极之间的距离和放电难度，需要额外增加输出电压方可实施，提高了电耗，而且增加了运行的不稳定性；
所述长方形不锈钢平板尺寸2a≤b≤4a；b≥2a为了保证气体的充分电离使水分子充分荷电，而b≤4a是防止荷电的水分子被所述的板电极捕集而流逝电荷，同时也节约了设备成本。
所述凝水器5包括设置在壳体内的第一层凝水网5.1和第二层凝水网5.2；
所述第一层凝水网5.1的中心轴线在水平方向上与板电极3.4重合，且竖直方向长度与阳极线3.1和阴极线4.1之间的距离相等；
所述第二层凝水网5.2的面积与整体外壳的横截面面积相等；
两层凝水网均直接与正电荷发生器壳体3.2和负电荷发生器壳体4.2相连并接地。
在本实施例中，所述的第一层凝水网5.1和第二层凝水网5.2均为不锈钢金属网，与壳体相连，且目数采用300目，沿气流方向布置。
在本实施例中，为了保证电晕放电的顺利进行及所述的电荷发生器产生足够的离子电荷，湿空气的温度≤95℃；对于一组正、负电荷发生器的使用，湿空气的总流量≤3.6ab×10-3m3/h；
为了提高湿空气处理流量，本发明可进行n组所述的正、负电荷发生器同时并用，多组并用可以增强荷电水分子在混合器的湍流强度，促进凝水作用，n组正、负电荷发生器并用的凝水量S将远大于n×a，上述a指的是一组正、负电荷发生器使用的凝水量。
一种湿空气静电凝水的方法，包括以下步骤：
步骤一：通过正极性和负极性电晕放电，使两个区域内分别产生大量的正、负电荷；
步骤二：湿空气分别进入独立的正极性电晕区和负极性电晕区使水分子分别携带正、负电荷；
步骤三：混合后携带正、负电荷的水分子在静电场作用下相互吸引而 凝结。
上述电晕区是指电晕放电的区域，在该区域中气体发生电离并产生大量的离子电荷，为水分子荷电提供了电荷来源；
上述正极性电晕放电采用正极性高压直流电源驱动，负极性电晕放电采用负极性高压直流电源驱动；
在本实施例中，为了使进入正极性电晕区和负极性电晕区的水分子含量相同，湿空气分别进入正极性电晕区和负极性电晕区前应进行气流组织优化，两个电晕区进口断面上的气流速度均方根δ≤0.15；
为了防止凝水的积累造成爬电、电源短路等不稳定现象，以及实现凝水的回收，气流走向与水平面的角度≥75°。
在本实施例中，本发明的一种湿空气静电凝水方法是启动上述装置，接通正极性高压直流电源3.3和负极性高压直流电源4.3后，正电荷发生器3和负电荷发生器4分别产生大量的正电荷和负电荷，湿空气由进口喇叭口1通过气流均布板2均匀地进入正电荷发生器3和负电荷发生器4，湿空气中的水分子分别荷上正电荷和负电荷，然后进入凝水器5，由于第一层凝水网5.1和第二层凝水网5.2接地为零电势，与阳极线3.1和阴极线4.1之间形成静电场，驱使荷电的水分子聚集在凝水网上，在凝水网表面正、负电荷的水分子相互吸引而凝结成水，从而实现湿空气的静电凝水。
在本实施例中，在正电荷发生器3和负电荷发生器4在关闭的条件下，体积流量为5L/min、干球温度为85℃的饱和湿空气进入本发明所述的一种湿空气静电凝水装置，1h后通过自然冷凝得到300ml的冷凝水；启动正电荷发生器3和负电荷发生器4，正极性高压直流电源3.3以输出电压10kV、输出电流2mA、输出频率50Hz的参数运行，负极性高压直流电源4.2以输出电压15kV、输出电流2mA、输出频率50Hz的参数运行，1h后得到冷凝水1100ml，单位能耗的凝水产率为16ml/W。
实施例2：
如图5所示，本实施例区别于实施例1，正电荷发生器3和负电荷发生器4分别采用N根阳极线3.1和阴极线4.1；
N根阳极线3.1以并联的方式与正极性高压直流电源3.3的高压端相 连；
N根阴极线4.1以并联的方式与负极性高压直流电源4.3的高压端相连。
本实施例的优势在于正电荷发生器3和负电荷发生器4运行更高的功率，以提高湿空气的处理流量，以及提高单位能耗的凝水产率。
实施例2的其他技术特征以及技术方法均与实施例1相同。
以上仅是本发明的具体应用范例，对本发明的保护范围不构成任何限制，凡采用等同变换或者等效替换而形成的技术方案，均落在本发明权利保护范围之内。

Claims (7)

  1. 一种湿空气静电凝水的方法，其特征在于：包括以下步骤：
    步骤一：通过正极性和负极性电晕放电，使两个区域内分别产生大量的正、负电荷；
    步骤二：湿空气分别进入独立的正极性电晕区和负极性电晕区使水分子分别携带正、负电荷；
    步骤三：混合后携带正、负电荷的水分子在静电场作用下相互吸引而凝结。
  2. 根据权利要求1所述的一种湿空气静电凝水的方法，其特征在于：所述步骤一中的正极性电晕放电采用正极性高压直流电源驱动，负极性电晕放电采用负极性高压直流电源驱动。
  3. 一种湿空气静电凝水的装置，其特征在于：包括进口喇叭口(1)、气流均布板(2)、正电荷发生器(3)、负电荷发生器(4)、凝水器(5)和出口喇叭口(6)，形成整体外壳并接地；
    所述进口喇叭口(1)和出口喇叭口(6)设置在外壳两侧；
    所述气流均布板(2)设置在进口喇叭口(1)的进口端；
    所述正电荷发生器(3)和负电荷发生器(4)并行排列，并沿气流方向设置在气流均布板(2)后端；
    所述凝水器(5)沿气流方向设置在正电荷发生器(3)和负电荷发生器(4)的后端。
  4. 根据权利要求3所述的一种湿空气静电凝水的装置，其特征在于：所述正电荷发生器(3)由正极性高压直流电源(3.3)驱动；
    所述负电荷发生器(4)由负极性高压直流电源(4.3)驱动。
  5. 根据权利要求4所述的一种湿空气静电凝水的装置，其特征在于：所述正极性高压直流电源(3.3)驱动多根阳极线(3.1)；
    所述负极性高压直流电源(4.3)驱动多根阴极线(4.1)。
  6. 根据权利要求3所述的一种湿空气静电凝水的装置，其特征在于：所述正电荷发生器(3)为长方体，包括正电荷发生器壳体(3.2)、板电极(3.4)、阳极线(3.1)和正极性高压直流电源(3.3)；
    所述正电荷发生器壳体(3.2)与正极性高压直流电源(3.3)的低压端相连并接地；
    所述阳极线(3.1)顺着气流方向布置于正电荷发生器(3)的中心，与正极性高压直流电源(3.3)的高压端相连；
    所述负电荷发生器(4)为长方体，包括负电荷发生器壳体(4.2)、阴极线(4.1)和负极性高压直流电源(4.3)，并与正电荷发生器(3)共用板电极(3.4)；
    所述板电极(3.4)与正电荷发生器壳体(3.2)和负电荷发生器壳体(4.2)相连；
    所述负电荷发生器壳体(4.2)与负极性高压直流电源(4.3)的低压端相连并接地；
    所述阴极线(4.1)顺着气流方向置于负电荷发生器(4)的中心，并与负极性高压直流电源(4.3)的高压端相连；
    所述正电荷发生器壳体(3.2)和负电荷发生器壳体(4.2)直接接触。
  7. 根据权利要求3所述的一种湿空气静电凝水的装置，其特征在于：所述凝水器(5)包括设置在壳体内的第一层凝水网(5.1)和第二层凝水网(5.2)；
    所述第一层凝水网(5.1)的中心轴线在水平方向上与板电极(3.4)重合，且竖直方向长度与阳极线(3.1)和阴极线(4.1)之间的距离相等；
    所述第二层凝水网(5.2)的面积与整体外壳的横截面面积相等；
    两层凝水网均直接与正电荷发生器壳体(3.2)和负电荷发生器壳体(4.2)相连并接地。
PCT/CN2020/114454 2020-03-24 2020-09-10 一种湿空气静电凝水的方法和装置 WO2021189779A1 (zh)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US17/777,875 US20230211356A1 (en) 2020-03-24 2020-09-10 Method and apparatus for electrostatic water condensation of wet air
KR1020227019626A KR20220092627A (ko) 2020-03-24 2020-09-10 습윤 공기를 정전식으로 물로 응축하는 방법 및 장치

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202010210287.6 2020-03-24
CN202010210287.6A CN111250264A (zh) 2020-03-24 2020-03-24 一种湿空气静电凝水的方法和装置

Publications (1)

Publication Number Publication Date
WO2021189779A1 true WO2021189779A1 (zh) 2021-09-30

Family

ID=70955168

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2020/114454 WO2021189779A1 (zh) 2020-03-24 2020-09-10 一种湿空气静电凝水的方法和装置

Country Status (4)

Country Link
US (1) US20230211356A1 (zh)
KR (1) KR20220092627A (zh)
CN (1) CN111250264A (zh)
WO (1) WO2021189779A1 (zh)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111250264A (zh) * 2020-03-24 2020-06-09 双良节能系统股份有限公司 一种湿空气静电凝水的方法和装置
CN112797513B (zh) * 2021-01-14 2022-03-01 常州大学 一种非平衡态等离子体电荷诱导凝结除湿装置及除湿方法
CN114618272B (zh) * 2022-02-25 2023-06-16 华南理工大学 高压静电场真空干燥捕水器

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6287261A (ja) * 1985-10-09 1987-04-21 Isao Miyahara 除湿装置
CN2589860Y (zh) * 2002-12-13 2003-12-03 庞昭进 静电凝结式除湿机
CN104525372A (zh) * 2014-12-02 2015-04-22 中国重型机械研究院股份公司 一种微细颗粒物电凝并装置
CN107234004A (zh) * 2017-05-16 2017-10-10 江苏大学 一种静电除湿装置
CN108325750A (zh) * 2018-02-26 2018-07-27 中国科学院过程工程研究所 一种电除尘器
CN108339665A (zh) * 2018-02-01 2018-07-31 北京航空航天大学 室外新风和室内空气细颗粒电凝并方法与装置
CN111250264A (zh) * 2020-03-24 2020-06-09 双良节能系统股份有限公司 一种湿空气静电凝水的方法和装置
CN211964588U (zh) * 2020-03-24 2020-11-20 双良节能系统股份有限公司 一种湿空气静电凝水的装置

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6287261A (ja) * 1985-10-09 1987-04-21 Isao Miyahara 除湿装置
CN2589860Y (zh) * 2002-12-13 2003-12-03 庞昭进 静电凝结式除湿机
CN104525372A (zh) * 2014-12-02 2015-04-22 中国重型机械研究院股份公司 一种微细颗粒物电凝并装置
CN107234004A (zh) * 2017-05-16 2017-10-10 江苏大学 一种静电除湿装置
CN108339665A (zh) * 2018-02-01 2018-07-31 北京航空航天大学 室外新风和室内空气细颗粒电凝并方法与装置
CN108325750A (zh) * 2018-02-26 2018-07-27 中国科学院过程工程研究所 一种电除尘器
CN111250264A (zh) * 2020-03-24 2020-06-09 双良节能系统股份有限公司 一种湿空气静电凝水的方法和装置
CN211964588U (zh) * 2020-03-24 2020-11-20 双良节能系统股份有限公司 一种湿空气静电凝水的装置

Also Published As

Publication number Publication date
CN111250264A (zh) 2020-06-09
KR20220092627A (ko) 2022-07-01
US20230211356A1 (en) 2023-07-06

Similar Documents

Publication Publication Date Title
WO2021189779A1 (zh) 一种湿空气静电凝水的方法和装置
KR102306248B1 (ko) 공기 정화용 바이폴라 이오나이저 및 바이폴라 이오나이저를 이용한 디퓨저
US10843206B2 (en) Cylindrical IFD filter
CN206483573U (zh) 一种静电式空气净化装置及空气净化器
CN104971823B (zh) 一种便于清洗的空气集尘设备及具有该设备的空气净化器
JP2022508873A (ja) 空気除塵システム及び方法
CN102188871B (zh) 板式静电过滤器
CN201706963U (zh) 冷却塔回收水装置
CN211964588U (zh) 一种湿空气静电凝水的装置
CN108339667B (zh) 一种带有太阳能电池板的静电除尘装置
TWI601919B (zh) 電漿淨化模組
CN114543220B (zh) 一种空气净化器
CN217235981U (zh) 空气消杀装置
CN207153959U (zh) 筒式棒型电离结构静电集尘装置
CN205987516U (zh) 一种低温等离子体发生器
CN211060273U (zh) 一种微积电传导式换热净化模块
CN202460832U (zh) 一种静电过滤器
CN104741278A (zh) 高压静电水雾发生装置
CN210385390U (zh) 家用油烟净化设备
CN213161319U (zh) 一种空气清新机
CN103817004A (zh) Pm2.5深度治理高气速高效湿式电滤装备
CN210568909U (zh) 一种空气净化组件
WO2021012064A1 (zh) 一种空气净化器
CN205253374U (zh) 静电空气净化器
CN111672629A (zh) 一种去除电晕封闭的湿式电除尘器

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 20926523

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 20227019626

Country of ref document: KR

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 20926523

Country of ref document: EP

Kind code of ref document: A1