CN116924607A - Hydrogen-rich water preparation equipment and hydrogen production process thereof - Google Patents

Hydrogen-rich water preparation equipment and hydrogen production process thereof Download PDF

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Publication number
CN116924607A
CN116924607A CN202310872632.6A CN202310872632A CN116924607A CN 116924607 A CN116924607 A CN 116924607A CN 202310872632 A CN202310872632 A CN 202310872632A CN 116924607 A CN116924607 A CN 116924607A
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hydrogen
water
rich
rich water
hydrogen production
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杨兴富
周仁伟
李连洪
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Chongqing Itln Electrical Appliance Co ltd
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Chongqing Itln Electrical Appliance Co ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
    • C01B3/02Production of hydrogen; Production of gaseous mixtures containing hydrogen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/68Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02Non-contaminated water, e.g. for industrial water supply
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

本说明书涉及一种富氢水制取设备及其制氢工艺。该设备包括:交换树脂过滤装置,包括壳体和滤芯;滤芯设于壳体内,用于通过离子交换树脂降低水体TDS值;壳体上开设有入水口和出水口;出水口设于壳体底部;制氢反应堆,包括制氢部和供电部;制氢部包括质子交换膜以及依次向外设置的催化剂层和扩散层,供电部用于向制氢部供电以将水体处理得到氢气和氧气;供水装置,供水装置用于将制氢反应堆生成的氢气与水体混合得到富氢水。

This specification relates to a hydrogen-rich water production equipment and its hydrogen production process. The equipment includes: an exchange resin filtration device, including a shell and a filter element; the filter element is located in the shell and is used to reduce the TDS value of water through ion exchange resin; the shell is provided with a water inlet and a water outlet; the water outlet is located at the bottom of the shell ; The hydrogen production reactor includes a hydrogen production part and a power supply part; the hydrogen production part includes a proton exchange membrane and a catalyst layer and a diffusion layer arranged outward in sequence, and the power supply part is used to supply power to the hydrogen production part to process water to obtain hydrogen and oxygen; The water supply device is used to mix the hydrogen generated by the hydrogen production reactor with the water body to obtain hydrogen-rich water.

Description

一种富氢水制取设备及其制氢工艺Hydrogen-rich water production equipment and hydrogen production process

技术领域Technical field

本发明涉及富氢水制取领域,具体而言,涉及一种富氢水制取设备及其制氢工艺。The present invention relates to the field of hydrogen-rich water production, and specifically to a hydrogen-rich water production equipment and a hydrogen production process.

背景技术Background technique

富氢水是指含有一定浓度的氢分子的水,由于氢分子在一定程度上可以抵抗自由基引起的氧化反应,因此富氢水逐渐受到欢迎。目前市面上富氢水主要通过电解水得到氢气并将其与水混合,得到富氢水。但电解水可能存在污染,会产生其他副产物,或者对设备使用寿命造成影响。Hydrogen-rich water refers to water containing a certain concentration of hydrogen molecules. Since hydrogen molecules can resist oxidation reactions caused by free radicals to a certain extent, hydrogen-rich water has gradually become popular. Currently, hydrogen-rich water on the market mainly obtains hydrogen gas through electrolysis of water and mixes it with water to obtain hydrogen-rich water. However, electrolyzed water may be contaminated, produce other by-products, or affect the service life of the equipment.

因此,需要提供一种氢气纯度高且能够保护设备使用寿命的富氢水制取设备及其制氢工艺。Therefore, there is a need to provide a hydrogen-rich water production equipment and a hydrogen production process that have high hydrogen purity and can protect the service life of the equipment.

发明内容Contents of the invention

本发明的一些实施例提供了一种富氢水制取设备,其包括:交换树脂过滤装置,包括壳体和滤芯;所述滤芯设于所述壳体内,用于通过离子交换树脂降低水体TDS值;所述壳体上开设有入水口和出水口;所述出水口设于所述壳体底部;制氢反应堆,包括制氢部和供电部;所述制氢部包括质子交换膜以及依次向外设置的催化剂层和扩散层,供电部用于向制氢部供电以将所述水体处理得到氢气和氧气;供水装置,所述供水装置用于将所述制氢反应堆生成的所述氢气与所述水体混合得到富氢水。Some embodiments of the present invention provide a hydrogen-rich water production equipment, which includes: an exchange resin filtration device, including a housing and a filter element; the filter element is provided in the housing and is used to reduce the TDS of water through ion exchange resin value; the housing is provided with a water inlet and a water outlet; the water outlet is located at the bottom of the housing; the hydrogen production reactor includes a hydrogen production part and a power supply part; the hydrogen production part includes a proton exchange membrane and a A catalyst layer and a diffusion layer are provided outward. The power supply part is used to supply power to the hydrogen production part to process the water body to obtain hydrogen and oxygen; the water supply device is used to process the hydrogen generated by the hydrogen production reactor. Mixed with the water body to obtain hydrogen-rich water.

在本发明的一种实施例中:In an embodiment of the invention:

所述交换树脂过滤装置还包括排氧通道,所述排氧通道一端连通所述制氢反应堆生成的所述氧气,另一端设于所述壳体顶部。The exchange resin filter device also includes an oxygen exhaust channel, one end of the oxygen exhaust channel is connected to the oxygen generated by the hydrogen production reactor, and the other end is located on the top of the housing.

在本发明的一种实施例中:In an embodiment of the invention:

若所述水体不满足饮用水条件,则至少通过反渗透净水装置对所述水体进行过滤。If the water body does not meet drinking water conditions, then at least the water body is filtered through a reverse osmosis water purification device.

在本发明的一种实施例中:In an embodiment of the invention:

所述供水装置还包括喷头;所述喷头被配置成使经过所述水体扩散至所述氢气中。The water supply device further includes a nozzle; the nozzle is configured to diffuse into the hydrogen gas through the body of water.

在本发明的一种实施例中:In an embodiment of the invention:

还包括增压泵,用于至少对进入所述供水装置的所述水体进行增压。It also includes a booster pump for boosting at least the water entering the water supply device.

在本发明的一种实施例中:In an embodiment of the invention:

所述喷头的喷口直径不大于1.3mm。The nozzle diameter of the nozzle is no more than 1.3mm.

在本发明的一种实施例中:In an embodiment of the invention:

还包括氢气分离膜,用于将所述制氢反应堆生成的所述氢气进行过滤后输入至供水装置。It also includes a hydrogen separation membrane for filtering the hydrogen generated by the hydrogen production reactor and then inputting it to the water supply device.

在本发明的一种实施例中:In an embodiment of the invention:

供水装置还包括加热胆,所述加热胆用于将所述富氢水加热至不超过55摄氏度。The water supply device also includes a heating tank, which is used to heat the hydrogen-rich water to no more than 55 degrees Celsius.

本发明的一些实施例还提供一种富氢水制取设备的制氢工艺,其包括:至少通过交换树脂过滤装置将水体TDS值降低至不大于5;通过质子交换膜制氢技术处理过滤后的所述水体,得到氢气;通过氢气分离膜将所述氢气提纯至不小于99.5%的浓度,以用于制备富氢水。Some embodiments of the present invention also provide a hydrogen production process of hydrogen-rich water production equipment, which includes: reducing the TDS value of the water body to no more than 5 through at least an exchange resin filtration device; processing the filtered product through proton exchange membrane hydrogen production technology of the water body to obtain hydrogen; and purify the hydrogen to a concentration of not less than 99.5% through a hydrogen separation membrane for preparing hydrogen-rich water.

在本发明的一种实施例中:In an embodiment of the invention:

将水体利用喷口直径不大于1.3mm的喷头喷洒扩散至所述氢气中,得到所述富氢水。The water body is sprayed and diffused into the hydrogen gas using a nozzle with a nozzle diameter of no more than 1.3 mm to obtain the hydrogen-rich water.

附图说明Description of the drawings

为了更清楚地说明本发明实施例的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,应当理解,以下附图仅示出了本发明的某些实施例,因此不应被看作是对范围的限定,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他相关的附图。In order to explain the technical solutions of the embodiments of the present invention more clearly, the drawings required to be used in the embodiments will be briefly introduced below. It should be understood that the following drawings only show some embodiments of the present invention and therefore do not It should be regarded as a limitation of the scope. For those of ordinary skill in the art, other relevant drawings can be obtained based on these drawings without exerting creative efforts.

图1a为本发明实施例提供的一种富氢水制取设备的示意图;Figure 1a is a schematic diagram of a hydrogen-rich water production equipment provided by an embodiment of the present invention;

图1b为本发明实施例提供的另一种富氢水制取设备的示意图;Figure 1b is a schematic diagram of another hydrogen-rich water production equipment provided by an embodiment of the present invention;

图2为本发明实施例提供的一种交换树脂过滤装置的示意图;Figure 2 is a schematic diagram of an exchange resin filtering device provided by an embodiment of the present invention;

图3为本发明实施例提供的一种制氢反应堆的示意图;Figure 3 is a schematic diagram of a hydrogen production reactor provided by an embodiment of the present invention;

图4为本发明实施例提供的一种喷头的剖面示意图;Figure 4 is a schematic cross-sectional view of a nozzle provided by an embodiment of the present invention;

图5为本发明实施例提供的制氢工艺的示例流程图。Figure 5 is an example flow chart of a hydrogen production process provided by an embodiment of the present invention.

具体实施方式Detailed ways

为使本发明实施例的目的、技术方案和优点更加清楚,下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。通常在此处附图中描述和示出的本发明实施例的组件可以以各种不同的配置来布置和设计。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments These are some embodiments of the present invention, rather than all embodiments. The components of the embodiments of the invention generally described and illustrated in the figures herein may be arranged and designed in a variety of different configurations.

因此,以下对在附图中提供的本发明的实施例的详细描述并非旨在限制要求保护的本发明的范围,而是仅仅表示本发明的选定实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。Therefore, the following detailed description of the embodiments of the invention provided in the appended drawings is not intended to limit the scope of the claimed invention, but rather to represent selected embodiments of the invention. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without making creative efforts fall within the scope of protection of the present invention.

应注意到:相似的标号和字母在下面的附图中表示类似项,因此,一旦某一项在一个附图中被定义,则在随后的附图中不需要对其进行进一步定义和解释。It should be noted that similar reference numerals and letters represent similar items in the following figures, therefore, once an item is defined in one figure, it does not need further definition and explanation in subsequent figures.

在本发明实施方式的描述中,需要说明的是,术语“内”、“外”、“上”等指示的方位或位置关系为基于附图所示的方位或位置关系,或者是该发明产品使用时惯常摆放的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。In the description of the embodiments of the present invention, it should be noted that the orientation or positional relationship indicated by the terms "inner", "outer", "upper", etc. is based on the orientation or positional relationship shown in the drawings, or the product of the invention Orientations or positional relationships that are customarily placed during use are only for the convenience of describing the present invention and simplifying the description. They do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood. are limitations of the present invention.

实施例Example

如图1a所示,本说明书的一些实施例提供了一种富氢水制取设备100,包括:交换树脂过滤装置110、制氢反应堆120和供水装置130,图1b示出了富氢水制取设备100的常规变形。在一些实施例中,还可以包括如水泵、反渗透净水装置140、加热胆132和出水阀等装置。As shown in Figure 1a, some embodiments of this specification provide a hydrogen-rich water production equipment 100, including: an exchange resin filter device 110, a hydrogen production reactor 120 and a water supply device 130. Figure 1b shows a hydrogen-rich water production equipment. Take the conventional variant of device 100. In some embodiments, devices such as a water pump, a reverse osmosis water purification device 140, a heating tank 132, and a water outlet valve may also be included.

同时参考图2,图中示出了一种交换树脂过滤装置110,其包括壳体112和滤芯114;壳体112可以用于固定于如墙面等位置。所述滤芯114设于所述壳体112内,用于通过离子交换树脂降低水体TDS值(如不大于5);离子交换树脂工作原理属于常规技术,不再赘述。Referring to Figure 2 at the same time, the figure shows an exchange resin filtering device 110, which includes a housing 112 and a filter element 114; the housing 112 can be used to be fixed on a wall or other location. The filter element 114 is provided in the housing 112 and is used to reduce the TDS value of the water body (for example, not greater than 5) through ion exchange resin; the working principle of the ion exchange resin belongs to conventional technology and will not be described again.

所述壳体112上开设有入水口116和出水口118;入水口116用于通入水体(如桶装水(图1b所示)或经过过滤后的水(图1a所示)),具体的,所述水体为饮用水;在一些实施例中,若所述水体不满足饮用水条件,则至少通过如图1a所示的反渗透净水装置140对所述水体进行过滤,以使输入至交换树脂过滤装置110的水体的TDS值较低(如不大于20),保证交换树脂过滤装置110的过滤效果以及使用寿命。在一些实施例中,交换树脂过滤装置110的出水口118设于所述壳体112底部;入水口116高于出水口118设置,使得进水过程中不会残留空气,避免后续制氢过程中干烧,造成设备损坏或影响寿命。The housing 112 is provided with a water inlet 116 and a water outlet 118; the water inlet 116 is used to pass into a water body (such as bottled water (shown in Figure 1b) or filtered water (shown in Figure 1a)). Specifically, , the water body is drinking water; in some embodiments, if the water body does not meet the drinking water conditions, the water body is at least filtered through the reverse osmosis water purification device 140 as shown in Figure 1a, so that the input The TDS value of the water flowing to the exchange resin filter device 110 is low (for example, not greater than 20), ensuring the filtering effect and service life of the exchange resin filter device 110 . In some embodiments, the water outlet 118 of the exchange resin filter device 110 is located at the bottom of the housing 112; the water inlet 116 is located higher than the water outlet 118, so that air will not remain during the water inlet process and avoid subsequent hydrogen production processes. Dry burning may damage the equipment or affect its service life.

同时参考图1a和图3,图中示出了一种制氢反应堆120,包括制氢部122和供电部124;所述制氢部122包括质子交换膜以及依次向外设置的催化剂层和扩散层,供电部124用于向制氢部122供电以将所述水体处理得到氢气和氧气;制氢反应堆120利用质子交换膜制氢技术,得到纯度高且无环境污染的氢气。Referring to FIG. 1a and FIG. 3 simultaneously, the figure shows a hydrogen production reactor 120, including a hydrogen production part 122 and a power supply part 124; the hydrogen production part 122 includes a proton exchange membrane and a catalyst layer and a diffusion layer arranged outward in sequence. layer, the power supply unit 124 is used to supply power to the hydrogen production unit 122 to process the water body to obtain hydrogen and oxygen; the hydrogen production reactor 120 uses proton exchange membrane hydrogen production technology to obtain hydrogen with high purity and no environmental pollution.

再次参考图2,所述交换树脂过滤装置110还包括排氧通道119,所述排氧通道119一端连通所述制氢反应堆120生成的所述氧气,另一端设于所述壳体112顶部。将氧气远离制氢反应堆120排放,保证设备安全运行。Referring again to FIG. 2 , the exchange resin filter device 110 further includes an oxygen exhaust channel 119 . One end of the oxygen exhaust channel 119 is connected to the oxygen generated by the hydrogen production reactor 120 , and the other end is located on the top of the housing 112 . Keep oxygen away from the hydrogen production reactor 120 to ensure safe operation of the equipment.

供水装置130,所述供水装置130用于将所述制氢反应堆120生成的所述氢气与所述水体混合得到富氢水。在一些实施例中,供水装置130可以包括三通头结构。Water supply device 130. The water supply device 130 is used to mix the hydrogen generated by the hydrogen production reactor 120 with the water body to obtain hydrogen-rich water. In some embodiments, the water supply device 130 may include a tee structure.

在一些实施例中,所述供水装置130还包括如图4所示的喷头;所述喷头160被配置成使经过所述水体扩散至所述氢气中,以增加氢气的溶解,同时还可以解决氢气在水体中的存留时间,使其留存时间可以达到8小时以上。In some embodiments, the water supply device 130 also includes a nozzle as shown in Figure 4; the nozzle 160 is configured to diffuse into the hydrogen gas through the water body to increase the dissolution of hydrogen gas, while also solving the problem of The retention time of hydrogen in water can reach more than 8 hours.

如图1a所示,在一些实施例中,为了保证水体的扩散效果,富氢水制取设备100还可以包括增压泵150,用于至少对进入所述供水装置130的所述水体进行增压。As shown in Figure 1a, in some embodiments, in order to ensure the diffusion effect of the water body, the hydrogen-rich water production equipment 100 may also include a booster pump 150 for at least increasing the water body entering the water supply device 130. pressure.

在一些实施例中,为了进一步提高水体扩散效果,提高氢气溶解以及在水体的留存时间,所述喷头160的喷口162直径不大于1.3mm,例如,喷口162直径为1.2mm,更进一步的,该喷头160的入水口116直径与喷口162直径比不小于3:1。In some embodiments, in order to further improve the water diffusion effect, improve hydrogen dissolution and retention time in the water, the diameter of the nozzle 162 of the nozzle 160 is not greater than 1.3 mm. For example, the diameter of the nozzle 162 is 1.2 mm. Further, the diameter of the nozzle 162 is 1.2 mm. The diameter ratio of the water inlet 116 of the nozzle 160 to the diameter of the nozzle 162 is not less than 3:1.

在一些实施例中,为保证溶于饮用水中的氢气的纯度,富氢水制取设备100还可以包括氢气分离膜(图中未示出),用于将所述制氢反应堆120生成的所述氢气进行过滤(如将所述氢气提纯至不小于99.5%的浓度)后输入至供水装置130。示例性的,氢气分离膜可以设于制氢反应堆120与喷口162之间。由于制氢反应堆120使用的是经过交换树脂过滤装置110二次净化的水体,因此,生成的氢气纯度已经很高,此时,氢气分离膜仅对高纯度氢气进行过滤,使其使用损耗大大降低,可以提高氢气浓度同时,降低维护次数和维护成本。In some embodiments, in order to ensure the purity of hydrogen dissolved in drinking water, the hydrogen-rich water production equipment 100 may also include a hydrogen separation membrane (not shown in the figure) for converting the hydrogen produced by the hydrogen production reactor 120 The hydrogen gas is filtered (eg, the hydrogen gas is purified to a concentration of no less than 99.5%) and then input to the water supply device 130 . For example, a hydrogen separation membrane may be provided between the hydrogen production reactor 120 and the nozzle 162 . Since the hydrogen production reactor 120 uses water that has been purified twice by the exchange resin filtration device 110, the purity of the generated hydrogen is already very high. At this time, the hydrogen separation membrane only filters the high-purity hydrogen, greatly reducing its use loss. , which can increase the hydrogen concentration while reducing the number of maintenance times and maintenance costs.

在一些实施例中,供水装置130还包括加热胆132,所述加热胆132用于将所述富氢水加热至不超过55摄氏度。控制水温不超过55摄氏度能够避免水体中氢含量在加热后降低的问题,也可以使得所生成的富氢水在能够尽快饮用的温度区间。In some embodiments, the water supply device 130 further includes a heating tank 132, which is used to heat the hydrogen-rich water to no more than 55 degrees Celsius. Controlling the water temperature to not exceed 55 degrees Celsius can avoid the problem of the hydrogen content in the water decreasing after heating, and can also keep the generated hydrogen-rich water in a temperature range that can be drunk as soon as possible.

本说明书提供的富氢水制取设备100,其制得到氢气纯度高且富氢水中含氢更多、留存时间长,同时其各个部件使用寿命相较于现有设备大大延长。The hydrogen-rich water production equipment 100 provided in this manual can produce hydrogen with high purity, more hydrogen in the hydrogen-rich water, and a long retention time. At the same time, the service life of each component is greatly extended compared to existing equipment.

参考图5,说明书还提供了一种富氢水制取设备100(如图1a和图1b所示的富氢水制取设备100)的制氢工艺,其包括:Referring to Figure 5, the description also provides a hydrogen production process of a hydrogen-rich water production equipment 100 (the hydrogen-rich water production equipment 100 shown in Figures 1a and 1b), which includes:

S01,至少通过交换树脂过滤装置将水体TDS值降低至不大于5。S01, at least reduce the TDS value of the water body to no more than 5 through an exchange resin filter device.

S02,通过质子交换膜制氢技术处理过滤后的所述水体,得到氢气。S02, process the filtered water through proton exchange membrane hydrogen production technology to obtain hydrogen.

S03,通过氢气分离膜将所述氢气提纯至不小于99.5%的浓度,以用于制备富氢水。S03, purify the hydrogen gas to a concentration of not less than 99.5% through a hydrogen separation membrane for preparing hydrogen-rich water.

在一些实施例中,步骤S03后还可以包括:In some embodiments, step S03 may also include:

S04,将水体利用喷口直径不大于1.3mm的喷头160喷洒扩散至所述氢气中,得到所述富氢水。S04: Spray water into the hydrogen gas using a nozzle 160 with a nozzle diameter of no more than 1.3 mm to obtain the hydrogen-rich water.

制氢工艺的具体说明书可以参见前文中富氢水制取设备100的描述,此处不在赘述,该制氢工艺可以得到适用于制造饮用级别的富氢水所需的氢气。For specific instructions on the hydrogen production process, please refer to the previous description of the hydrogen-rich water production equipment 100 and will not be repeated here. This hydrogen production process can obtain hydrogen suitable for producing drinking-grade hydrogen-rich water.

以上所述仅为本发明的优选实施例而已,并不用于限制本发明,对于本领域的技术人员来说,本发明可以有各种更改和变化。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention and are not intended to limit the present invention. For those skilled in the art, the present invention may have various modifications and changes. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present invention shall be included in the protection scope of the present invention.

Claims (10)

1. A hydrogen-rich water producing apparatus, comprising:
the exchange resin filtering device comprises a shell and a filter element; the filter element is arranged in the shell and is used for reducing the TDS value of the water body through ion exchange resin; the shell is provided with a water inlet and a water outlet; the water outlet is arranged at the bottom of the shell;
the hydrogen production reactor comprises a hydrogen production part and a power supply part; the hydrogen production part comprises a proton exchange membrane, a catalyst layer and a diffusion layer which are sequentially arranged outwards, and the power supply part is used for supplying power to the hydrogen production part so as to treat the water body to obtain hydrogen and oxygen;
and the water supply device is used for mixing the hydrogen generated by the hydrogen production reactor with the water body to obtain hydrogen-rich water.
2. A hydrogen-rich water producing apparatus according to claim 1, wherein:
the exchange resin filtering device further comprises an oxygen discharging channel, one end of the oxygen discharging channel is communicated with the oxygen generated by the hydrogen production reactor, and the other end of the oxygen discharging channel is arranged at the top of the shell.
3. A hydrogen-rich water producing apparatus according to claim 1, wherein: the water body is drinking water;
and if the water body does not meet the drinking water condition, filtering the water body at least through a reverse osmosis water purifying device.
4. A hydrogen-rich water producing apparatus according to claim 1, wherein:
the water supply device also comprises a spray head; the showerhead is configured to diffuse through the body of water into the hydrogen gas.
5. The hydrogen-rich water producing apparatus according to claim 4, further comprising:
and the booster pump is used for boosting at least the water body entering the water supply device.
6. A hydrogen-rich water producing apparatus according to claim 4, wherein:
the diameter of the nozzle of the spray head is not more than 1.3mm.
7. The hydrogen-rich water producing apparatus according to claim 4, further comprising:
and the hydrogen separation membrane is used for filtering the hydrogen generated by the hydrogen production reactor and inputting the filtered hydrogen into the water supply device.
8. A hydrogen-rich water producing apparatus according to claim 1, further comprising:
the water supply device further comprises a heating liner for heating the hydrogen-rich water to a temperature of not more than 55 ℃.
9. A process for producing hydrogen in a hydrogen-rich water production facility, comprising:
reducing the TDS value of the body of water to not more than 5 at least by means of an exchange resin filtration device;
treating the filtered water body by a proton exchange membrane hydrogen production technology to obtain hydrogen;
the hydrogen gas is purified to a concentration of not less than 99.5% by a hydrogen separation membrane for use in preparing hydrogen-rich water.
10. The hydrogen production process of claim 9, wherein the means for producing hydrogen-enriched water comprises:
and spraying and diffusing the water body into the hydrogen by using a spray head with the diameter of the spray nozzle not larger than 1.3mm to obtain the hydrogen-rich water.
CN202310872632.6A 2023-07-17 2023-07-17 Hydrogen-rich water preparation equipment and hydrogen production process thereof Pending CN116924607A (en)

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Application publication date: 20231024