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WO2018196351A1 - Novel device for photothermal evaporation of sea water by solar energy - Google Patents

Novel device for photothermal evaporation of sea water by solar energy Download PDF

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Publication number
WO2018196351A1
WO2018196351A1 PCT/CN2017/111850 CN2017111850W WO2018196351A1 WO 2018196351 A1 WO2018196351 A1 WO 2018196351A1 CN 2017111850 W CN2017111850 W CN 2017111850W WO 2018196351 A1 WO2018196351 A1 WO 2018196351A1
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photothermal conversion
fabric
hydrophilic
sides
fiber
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French (fr)
Chinese (zh)
Inventor
陈志钢
刘子潇
张丽莎
朱美芳
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Donghua University
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Donghua University
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    • 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
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/08Thin film evaporation
    • 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
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/14Treatment of water, waste water, or sewage by heating by distillation or evaporation using solar energy
    • 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
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20Controlling water pollution; Waste water treatment
    • Y02A20/208Off-grid powered water treatment
    • Y02A20/212Solar-powered wastewater sewage treatment, e.g. spray evaporation

Definitions

  • the utility model belongs to the technical field of seawater evaporation, in particular to a novel solar thermal seawater evaporation device.
  • Seawater accounts for more than 70% of the Earth's surface and is one of the most abundant resources on Earth. However, compared with abundant sea water resources, fresh water on the earth only accounts for 2.8% of all water resources, and 68.69% of fresh water is stored in permanent glaciers in the earth's poles, plateaus and snow-capped mountains. Freshwater shortage is recognized in the world. One of the most serious challenges. The most ideal way to overcome this problem is to use desalination of seawater to produce fresh water. To achieve this goal, various seawater desalination technologies have been developed, including seawater distillation, electrodialysis, and reverse osmosis filtration technologies. Most of these methods require direct or indirect consumption of large amounts of fossil energy, which increases costs and creates an environmental burden. The use of solar energy for seawater distillation can get rid of the consumption of fossil energy in the desalination process, attracting great attention.
  • the heat-generating layer of this method has a large area of contact with the surface of the seawater, and the generated heat is inevitably lost to the seawater, thereby reducing the utilization of solar energy; in addition, this method causes the salt in the seawater to be
  • the surface of the heat generating layer is deposited to cover the light receiving surface and block the void, thereby causing the photothermal conversion layer to fail.
  • the technical problem to be solved by the utility model is to provide a novel solar thermal seawater evaporation device, which utilizes solar energy resources to realize high-efficiency evaporation of seawater, reduce cost, improve seawater evaporation efficiency, and avoid salt conversion in seawater to reduce solar energy conversion efficiency.
  • the technical solution adopted by the utility model to solve the technical problem thereof is to provide a novel solar photothermal seawater evaporation device, which comprises a water tank on both sides, a hydrophilic photothermal conversion fabric and a concentrate collection box, and the hydrophilic photothermal conversion Fabric sides They are respectively laid on the water tanks on both sides, and the two ends of the hydrophilic photothermal conversion fabric are respectively placed in the water tanks on both sides and immersed below the sea surface, and the hydrophilic light-heat conversion fabric between the water tanks on both sides is under a concave arc shape, wherein the middle portion of the hydrophilic photothermal conversion fabric is a photothermal conversion region containing a photothermal conversion material, and the concentrate collection box is disposed below the lowest point of the central arc of the hydrophilic photothermal conversion fabric.
  • the height difference h 1 between the high point of the two ends of the hydrophilic photothermal conversion fabric and the intermediate low point is 0 ⁇ h 1 ⁇ 10 m.
  • the height difference of the sea surface in the water tanks on both sides is greater than or equal to 0 and less than or equal to 10 m.
  • the height difference h 2 between the sea surface and the high point of the hydrophilic photothermal conversion fabric is 0 ⁇ h 2 ⁇ 10 m.
  • the hydrophilic photothermal conversion fabric is composed of a hydrophilic fabric substrate and a photothermal conversion material.
  • the hydrophilic fabric substrate is a knitted fabric, a woven fabric or a non-woven fabric made of one or more of natural fibers, regenerated cellulose fibers, and chemical fibers.
  • the natural fiber is cotton, hemp, silk, wool or pulp
  • the regenerated cellulose fiber is Lyocell fiber, Modal fiber, bamboo fiber, chitin fiber or copper ammonia fiber
  • the chemical fiber is polyester, spandex, acrylic fiber, Nylon, vinylon or polypropylene.
  • the non-woven fabric is a nonwoven fabric.
  • the photothermal conversion material includes one or more of metal nanoparticles, carbon nano materials, organic photothermal materials, and semiconductor photothermal nano materials.
  • the metal nanoparticles are gold nanoparticles, palladium nanoparticles, platinum nanoparticles or aluminum nanoparticles
  • the carbon nano materials are carbon black, carbon powder, porous carbon, carbon nanotubes, graphene or fullerenes.
  • the organic photothermal material is polypyrrole, polythiophene, polyaniline, polydopamine, phthalocyanine green or Prussian blue
  • the semiconductor photothermal nano material is copper sulfide, copper selenide, barium sulfide, barium selenide, tungsten sulfide, Tungsten oxide, titanium dioxide, titanium trioxide, iron sulfide or molybdenum sulfide.
  • Water vapor can be generated from the upper and lower surfaces of the photothermal conversion fabric, increasing the area generated by the steam and improving the steam generation efficiency;
  • the present invention can The heat produced by Yangneng concentrates on heating the seawater on the surface of the fabric, avoiding the longitudinal loss of heat to the interior of the seawater, and greatly improving the evaporation efficiency of seawater;
  • the utility model relates to a continuous solar water evaporation-concentration synergistic generating device, which can remove residual salt on the surface of the fabric while evaporating seawater, so that the surface of the photothermal conversion fabric does not precipitate a salt cover layer and affects the solar energy.
  • the utilization efficiency reduces the evaporation performance.
  • FIG. 1 is a schematic structural view of a conventional solar thermal seawater evaporation device.
  • Figure 2 is a schematic view of the structure of the present invention.
  • FIG 3 is a comparison diagram of accumulated steam generation amount of the utility model and the conventional solar thermal seawater evaporation device in the first embodiment.
  • Figure 4 is a graph showing the evaporation rate of seawater at different times in the present embodiment in Example 2.
  • Fig. 5 is a graph showing the cumulative steam generation amount of the present invention in the second embodiment.
  • a novel solar thermal seawater evaporation device as shown in FIG. 2 includes a water tank on both sides, a hydrophilic photothermal conversion fabric 2, and a concentrate collection tank 3.
  • the two sides of the hydrophilic photothermal conversion fabric 2 are respectively laid on the water tanks 1 on both sides, and the two ends of the hydrophilic photothermal conversion fabric 2 are respectively placed in the water tanks 1 on both sides and submerged below the sea surface, and the water tanks on both sides 1
  • the height difference between the sea surface and the height of both ends of the hydrophilic photothermal conversion fabric 2 is 0 ⁇ h 2 ⁇ 10 m.
  • the hydrophilic photothermal conversion fabric 2 between the water tanks 1 on both sides has a concave arc shape, and the height difference h 1 between the high point and the middle low point of the hydrophilic photothermal conversion fabric 2 is 0 ⁇ h 1 ⁇ 10m.
  • the hydrophilic photothermal conversion fabric 2 is composed of a hydrophilic fabric substrate and a photothermal conversion material.
  • the hydrophilic fabric substrate is a knitted fabric, a woven fabric or a non-woven fabric (such as a non-woven fabric) made of one or more of natural fibers, regenerated cellulose fibers and chemical fibers, and the natural fibers are cotton, hemp and silk. , hair or pulp, etc., regenerated cellulose fiber is Lyocell fiber, Modal fiber, bamboo fiber, chitin fiber or copper ammonia fiber, chemical fiber is polyester, spandex, acrylic, nylon, vinylon or polypropylene.
  • Photothermal conversion materials include metal nanoparticles, carbon nanomaterials, organic photothermal materials, and semiconductor light One or more of the thermal nanomaterials.
  • the metal nanoparticles are gold nanoparticles, palladium nanoparticles, platinum nanoparticles or aluminum nanoparticles
  • carbon nano materials are carbon black, carbon powder, porous carbon, carbon nanotubes, graphene or fullerenes
  • organic photothermal materials are poly Pyrrole, polythiophene, polyaniline, polydopamine, phthalocyanine green or Prussian blue
  • semiconductor photothermal nanomaterials are copper sulfide, copper selenide, antimony sulfide, antimony selenide, tungsten sulfide, tungsten oxide, titanium dioxide, trioxide Titanium, iron sulfide or molybdenum sulfide.
  • the middle portion of the hydrophilic photothermal conversion fabric 2 is a photothermal conversion region containing a photothermal conversion material, and the concentrate collection box 3 is disposed below the lowest point of the central arc of the hydrophilic photothermal conversion fabric 2.
  • the obtained photothermal conversion fabric is fixed on the ports of two square polyethylene plastic boxes by clips, and the edge portion of the fabric naturally hangs down and contacts the seawater in the water box, and the height difference between the center of the fabric and the plastic box port is 1 cm, plastic
  • the seawater level in the box is 2mm lower than the plastic box port.
  • An ethanol dispersion of 8 mg/mL of polyaniline was prepared as in Example 1. Take 600mL of dispersion, drop it repeatedly in the middle part of 80 ⁇ 240cm cotton cloth, control the dropping area to the 80 ⁇ 140cm part of the cotton cloth center, and blow it dry with hair dryer, fix the two ends of the cotton cloth with clips.
  • the device is placed under the sunlight to record the change in the quality of the water evaporation.
  • the sunlight intensity and the corresponding water evaporation rate at different times are shown in Figure 4.
  • the device is accumulated in one day.
  • the quality of the generated steam is shown in Figure 5.

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Photovoltaic Devices (AREA)

Abstract

A novel device for photothermal evaporation of sea water by solar energy, comprising water tanks (1) on two sides, a hydrophilic photothermal conversion fabric (2) and a concentrated solution collection tank (3). The two sides of the hydrophilic photothermal conversion fabric (2) are respectively laid on the water tanks (1) at the two sides, and the two ends of the hydrophilic photothermal conversion fabric (2) are respectively placed in the water tanks (1) on two sides and immersed below the sea water surface. The hydrophilic photothermal conversion fabric (2) between the water tanks (1) on two sides is in a concave arc shape; the middle part of the hydrophilic photothermal conversion fabric (2) is a photothermal conversion area containing photothermal conversion materials; and the concentrated solution collection tank (3) is correspondingly arranged below the lowest point of the arc in the middle of the hydrophilic photothermal conversion fabric (2). The present invention employs solar energy resources to efficiently evaporate sea water, which reduces costs, improves evaporation efficiency of seawater, and avoids salt precipitation in seawater.

Description

一种新型太阳能光热海水蒸发装置Novel solar photothermal seawater evaporation device 技术领域Technical field

本实用新型属于海水蒸发的技术领域,特别是涉及一种新型太阳能光热海水蒸发装置。The utility model belongs to the technical field of seawater evaporation, in particular to a novel solar thermal seawater evaporation device.

背景技术Background technique

海水占据了地球表面70%以上的面积,是地球上最丰富的资源之一。然而,相比于丰富的海水资源,地球上淡水只占全部水资源的2.8%,其中还有68.69%的淡水被封存与地球两极、高原与雪山等地区的永久冰川中,淡水紧缺成为世界公认的最严峻的挑战之一。克服这一难题最理想的途径是利用海水脱盐生产淡水,为了达到这一目的,人们开发出了多种海水淡化技术,包括海水蒸馏、电渗析、反渗透过滤技术等。这些方法大多需要直接或间接消耗大量化石能源,提高成本并会造成环境负担。利用太阳能进行海水蒸馏能够摆脱海水淡化过程中化石能源的消耗,吸引了人们极大的关注。Seawater accounts for more than 70% of the Earth's surface and is one of the most abundant resources on Earth. However, compared with abundant sea water resources, fresh water on the earth only accounts for 2.8% of all water resources, and 68.69% of fresh water is stored in permanent glaciers in the earth's poles, plateaus and snow-capped mountains. Freshwater shortage is recognized in the world. One of the most serious challenges. The most ideal way to overcome this problem is to use desalination of seawater to produce fresh water. To achieve this goal, various seawater desalination technologies have been developed, including seawater distillation, electrodialysis, and reverse osmosis filtration technologies. Most of these methods require direct or indirect consumption of large amounts of fossil energy, which increases costs and creates an environmental burden. The use of solar energy for seawater distillation can get rid of the consumption of fossil energy in the desalination process, attracting great attention.

早在两千年之前,古人就利用太阳光直接照射海水制盐,利用这种方法,太阳光使海水升温加快蒸发速度,然而,在这种情况下太阳光将对一定厚度下的所有海水进行均匀加热,海水升温不明显,效果较差。为了提高太阳光的利用率、加快海水蒸发速度,人们利用光热纳米材料与基体材料相复合,制备成光热转换层,平铺到海水表面,其装置图如图1所示。这种方法能够将太阳光高效的转换为热量,并集中在海水的表面,相对集中的热量能够有效地提高光热转换层的表面温度,很大程度上增加海水蒸发速度。但是,这种方法的发热层与海水表面有较大面积的接触,所产生的热量难以避免的会向海水中散失,从而降低太阳能的利用率;另外,这种方法会使海水中的盐分在发热层的表面析出,覆盖受光面并堵塞空隙,造成光热转换层失效。As early as two thousand years ago, the ancients used direct sunlight to illuminate seawater to make salt. With this method, sunlight warms the seawater to accelerate the evaporation rate. However, in this case, the sunlight will uniformize all the seawater at a certain thickness. Heating, sea water temperature is not obvious, the effect is poor. In order to improve the utilization of sunlight and accelerate the evaporation rate of seawater, people use photothermal nanomaterials to combine with matrix materials to prepare a photothermal conversion layer, which is laid flat on the surface of seawater. The device diagram is shown in Figure 1. This method can efficiently convert sunlight into heat and concentrate on the surface of seawater. The relatively concentrated heat can effectively increase the surface temperature of the light-to-heat conversion layer and greatly increase the evaporation rate of seawater. However, the heat-generating layer of this method has a large area of contact with the surface of the seawater, and the generated heat is inevitably lost to the seawater, thereby reducing the utilization of solar energy; in addition, this method causes the salt in the seawater to be The surface of the heat generating layer is deposited to cover the light receiving surface and block the void, thereby causing the photothermal conversion layer to fail.

因此,有必要开发一种海水蒸发装置,避免热量向海水中散失,同时还能够带走海水中所析出的盐分。Therefore, it is necessary to develop a seawater evaporation device to prevent heat from being dissipated into the seawater, and at the same time, it is possible to take away the salt precipitated in the seawater.

发明内容Summary of the invention

本实用新型所要解决的技术问题是提供一种新型太阳能光热海水蒸发装置,利用太阳能资源实现海水的高效蒸发,降低成本,提高海水蒸发效率,避免海水中盐分析出降低太阳能的转化效率。The technical problem to be solved by the utility model is to provide a novel solar thermal seawater evaporation device, which utilizes solar energy resources to realize high-efficiency evaporation of seawater, reduce cost, improve seawater evaporation efficiency, and avoid salt conversion in seawater to reduce solar energy conversion efficiency.

本实用新型解决其技术问题所采用的技术方案是提供一种新型太阳能光热海水蒸发装置,包括两侧水箱、亲水性光热转换织物和浓缩液收集箱,所述亲水性光热转换织物两侧 分别铺设于两侧的水箱上,所述亲水性光热转换织物的两端分别置于两侧的水箱中且浸没于海水面以下,两侧水箱之间的亲水性光热转换织物呈下凹的弧形,所述亲水性光热转换织物中部为含有光热转换材料的光热转换区,所述浓缩液收集箱对应设置于亲水性光热转换织物中部弧形最低点的下方。The technical solution adopted by the utility model to solve the technical problem thereof is to provide a novel solar photothermal seawater evaporation device, which comprises a water tank on both sides, a hydrophilic photothermal conversion fabric and a concentrate collection box, and the hydrophilic photothermal conversion Fabric sides They are respectively laid on the water tanks on both sides, and the two ends of the hydrophilic photothermal conversion fabric are respectively placed in the water tanks on both sides and immersed below the sea surface, and the hydrophilic light-heat conversion fabric between the water tanks on both sides is under a concave arc shape, wherein the middle portion of the hydrophilic photothermal conversion fabric is a photothermal conversion region containing a photothermal conversion material, and the concentrate collection box is disposed below the lowest point of the central arc of the hydrophilic photothermal conversion fabric. .

所述亲水性光热转换织物的两端高点与中间低点的高度差h1为0<h1≤10m。The height difference h 1 between the high point of the two ends of the hydrophilic photothermal conversion fabric and the intermediate low point is 0 < h 110 m.

所述两侧水箱内的海水面高度差大于等于0且小于等于10m。The height difference of the sea surface in the water tanks on both sides is greater than or equal to 0 and less than or equal to 10 m.

所述海水面与亲水性光热转换织物两端高点的高度差h2为0<h2≤10m。The height difference h 2 between the sea surface and the high point of the hydrophilic photothermal conversion fabric is 0 < h 210 m.

所述亲水性光热转换织物由亲水性织物基底和光热转换材料组成。The hydrophilic photothermal conversion fabric is composed of a hydrophilic fabric substrate and a photothermal conversion material.

所述亲水性织物基底为天然纤维、再生纤维素纤维和化学纤维中的一种或者多种制成的针织织物、机织织物或非织物。The hydrophilic fabric substrate is a knitted fabric, a woven fabric or a non-woven fabric made of one or more of natural fibers, regenerated cellulose fibers, and chemical fibers.

所述天然纤维为棉、麻、丝、毛或者纸浆,所述再生纤维素纤维为Lyocell纤维、Modal纤维、竹纤维、甲壳素纤维或者铜氨纤维,所述化学纤维为涤纶、氨纶、腈纶、锦纶、维纶或者丙纶。The natural fiber is cotton, hemp, silk, wool or pulp, and the regenerated cellulose fiber is Lyocell fiber, Modal fiber, bamboo fiber, chitin fiber or copper ammonia fiber, and the chemical fiber is polyester, spandex, acrylic fiber, Nylon, vinylon or polypropylene.

所述非织物为无纺布。The non-woven fabric is a nonwoven fabric.

所述光热转换材料包括金属纳米颗粒、碳纳米材料、有机光热材料和半导体光热纳米材料中的一种或者多种。The photothermal conversion material includes one or more of metal nanoparticles, carbon nano materials, organic photothermal materials, and semiconductor photothermal nano materials.

所述金属纳米颗粒为金纳米颗粒、钯纳米颗粒、铂纳米颗粒或者铝纳米颗粒,所述碳纳米材料为碳黑、碳粉、多孔碳、碳纳米管、石墨烯或者富勒烯,所述有机光热材料为聚吡咯、聚噻吩、聚苯胺、聚多巴胺、吲哚菁绿或者普鲁士蓝,所述半导体光热纳米材料为硫化铜、硒化铜、硫化铋、硒化铋、硫化钨、氧化钨、二氧化钛、三氧化二钛、硫化铁或者硫化钼。The metal nanoparticles are gold nanoparticles, palladium nanoparticles, platinum nanoparticles or aluminum nanoparticles, and the carbon nano materials are carbon black, carbon powder, porous carbon, carbon nanotubes, graphene or fullerenes. The organic photothermal material is polypyrrole, polythiophene, polyaniline, polydopamine, phthalocyanine green or Prussian blue, and the semiconductor photothermal nano material is copper sulfide, copper selenide, barium sulfide, barium selenide, tungsten sulfide, Tungsten oxide, titanium dioxide, titanium trioxide, iron sulfide or molybdenum sulfide.

有益效果Beneficial effect

(1)使用太阳能对海水进行加热并促进海水蒸发,无需额外能源消耗,产生的水蒸气通过冷凝可得含盐量极低的蒸馏水,滴落的浓缩海水可以用于进一步的海水制盐工艺,有利于提高制盐效率、降低成本;(1) Using solar energy to heat seawater and promote seawater evaporation, no additional energy consumption is required, and the generated steam can be condensed to obtain distilled water with extremely low salt content, and the concentrated concentrated seawater can be used for further seawater salt making process. Conducive to improving salt production efficiency and reducing costs;

(2)水蒸气能够从光热转换织物的上下两个表面产生,增加了蒸汽产生的面积,提高蒸汽产生效率;(2) Water vapor can be generated from the upper and lower surfaces of the photothermal conversion fabric, increasing the area generated by the steam and improving the steam generation efficiency;

(3)相比于将光热转换织物直接铺到海水表面上用于海水蒸发,本实用新型能够将太 阳能所产热量集中加热织物表面的海水,避免了热量向海水内部的纵向流失,能够大大提高海水蒸发效率;(3) Compared with the direct transfer of the photothermal conversion fabric to the surface of the seawater for seawater evaporation, the present invention can The heat produced by Yangneng concentrates on heating the seawater on the surface of the fabric, avoiding the longitudinal loss of heat to the interior of the seawater, and greatly improving the evaporation efficiency of seawater;

(4)本实用新型为连续化太阳能海水蒸发-浓缩协同发生装置,该装置能够在蒸发海水的同时带走织物表面的残留盐分,使光热转换织物的表面不会析出盐分覆盖层而影响太阳能的利用效率,降低蒸发性能。(4) The utility model relates to a continuous solar water evaporation-concentration synergistic generating device, which can remove residual salt on the surface of the fabric while evaporating seawater, so that the surface of the photothermal conversion fabric does not precipitate a salt cover layer and affects the solar energy. The utilization efficiency reduces the evaporation performance.

附图说明DRAWINGS

图1为传统太阳能光热海水蒸发装置的结构示意图。1 is a schematic structural view of a conventional solar thermal seawater evaporation device.

图2为本实用新型的结构示意图。Figure 2 is a schematic view of the structure of the present invention.

图3为实施例1中本实用新型与传统太阳能光热海水蒸发装置的累计蒸汽产生量对比图。3 is a comparison diagram of accumulated steam generation amount of the utility model and the conventional solar thermal seawater evaporation device in the first embodiment.

图4为实施例2中本实用新型不同时刻海水蒸发速率图。Figure 4 is a graph showing the evaporation rate of seawater at different times in the present embodiment in Example 2.

图5为实施例2中本实用新型的累计蒸汽产生量图。Fig. 5 is a graph showing the cumulative steam generation amount of the present invention in the second embodiment.

具体实施方式detailed description

下面结合具体实施例,进一步阐述本实用新型。应理解,这些实施例仅用于说明本实用新型而不用于限制本实用新型的范围。此外应理解,在阅读了本实用新型讲授的内容之后,本领域技术人员可以对本实用新型作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。The present invention is further illustrated below in conjunction with specific embodiments. It is to be understood that the examples are not intended to limit the scope of the invention. In addition, it should be understood that various modifications and changes may be made by those skilled in the art in the form of the present invention.

如图2所示的一种新型太阳能光热海水蒸发装置,包括两侧水箱1、亲水性光热转换织物2和浓缩液收集箱3。A novel solar thermal seawater evaporation device as shown in FIG. 2 includes a water tank on both sides, a hydrophilic photothermal conversion fabric 2, and a concentrate collection tank 3.

亲水性光热转换织物2两侧分别铺设于两侧的水箱1上,亲水性光热转换织物2的两端分别置于两侧的水箱1中且浸没于海水面以下,两侧水箱1内的海水面高度差大于等于0且小于等于10m,海水面与亲水性光热转换织物2两端高点的高度差h2为0<h2≤10m。两侧水箱1之间的亲水性光热转换织物2呈下凹的弧形,亲水性光热转换织物2的两端高点与中间低点的高度差h1为0<h1≤10m。The two sides of the hydrophilic photothermal conversion fabric 2 are respectively laid on the water tanks 1 on both sides, and the two ends of the hydrophilic photothermal conversion fabric 2 are respectively placed in the water tanks 1 on both sides and submerged below the sea surface, and the water tanks on both sides 1 The height difference between the sea surface and the height of both ends of the hydrophilic photothermal conversion fabric 2 is 0 < h 2 ≤ 10 m. The hydrophilic photothermal conversion fabric 2 between the water tanks 1 on both sides has a concave arc shape, and the height difference h 1 between the high point and the middle low point of the hydrophilic photothermal conversion fabric 2 is 0 < h 1 ≤ 10m.

亲水性光热转换织物2由亲水性织物基底和光热转换材料组成。亲水性织物基底为天然纤维、再生纤维素纤维和化学纤维中的一种或者多种制成的针织织物、机织织物或非织物(如无纺布),天然纤维为棉、麻、丝、毛或者纸浆等,再生纤维素纤维为Lyocell纤维、Modal纤维、竹纤维、甲壳素纤维或者铜氨纤维,化学纤维为涤纶、氨纶、腈纶、锦纶、维纶或者丙纶。光热转换材料包括金属纳米颗粒、碳纳米材料、有机光热材料和半导体光 热纳米材料中的一种或者多种。金属纳米颗粒为金纳米颗粒、钯纳米颗粒、铂纳米颗粒或者铝纳米颗粒,碳纳米材料为碳黑、碳粉、多孔碳、碳纳米管、石墨烯或者富勒烯,有机光热材料为聚吡咯、聚噻吩、聚苯胺、聚多巴胺、吲哚菁绿或者普鲁士蓝,半导体光热纳米材料为硫化铜、硒化铜、硫化铋、硒化铋、硫化钨、氧化钨、二氧化钛、三氧化二钛、硫化铁或者硫化钼。The hydrophilic photothermal conversion fabric 2 is composed of a hydrophilic fabric substrate and a photothermal conversion material. The hydrophilic fabric substrate is a knitted fabric, a woven fabric or a non-woven fabric (such as a non-woven fabric) made of one or more of natural fibers, regenerated cellulose fibers and chemical fibers, and the natural fibers are cotton, hemp and silk. , hair or pulp, etc., regenerated cellulose fiber is Lyocell fiber, Modal fiber, bamboo fiber, chitin fiber or copper ammonia fiber, chemical fiber is polyester, spandex, acrylic, nylon, vinylon or polypropylene. Photothermal conversion materials include metal nanoparticles, carbon nanomaterials, organic photothermal materials, and semiconductor light One or more of the thermal nanomaterials. The metal nanoparticles are gold nanoparticles, palladium nanoparticles, platinum nanoparticles or aluminum nanoparticles, carbon nano materials are carbon black, carbon powder, porous carbon, carbon nanotubes, graphene or fullerenes, and organic photothermal materials are poly Pyrrole, polythiophene, polyaniline, polydopamine, phthalocyanine green or Prussian blue, semiconductor photothermal nanomaterials are copper sulfide, copper selenide, antimony sulfide, antimony selenide, tungsten sulfide, tungsten oxide, titanium dioxide, trioxide Titanium, iron sulfide or molybdenum sulfide.

亲水性光热转换织物2中部为含有光热转换材料的光热转换区,浓缩液收集箱3对应设置于亲水性光热转换织物2中部弧形最低点的下方。The middle portion of the hydrophilic photothermal conversion fabric 2 is a photothermal conversion region containing a photothermal conversion material, and the concentrate collection box 3 is disposed below the lowest point of the central arc of the hydrophilic photothermal conversion fabric 2.

实施例1Example 1

在烧杯中加入45mL水、5mL浓盐酸(HCl质量百分比:~36%)和1.141g过硫酸铵,在磁力搅拌下,向其中加入1mL苯胺和乙醇的混合溶液(体积比1:1),搅拌30s,放入6℃冰箱中静置24h,之后使用砂芯漏斗和0.45μm聚偏氟乙烯滤膜对反应溶液进行减压抽滤和洗涤,并将产物聚苯胺重新分散到乙醇中,配成8mg/mL的乙醇分散液。Add 45 mL of water, 5 mL of concentrated hydrochloric acid (HCl mass percentage: ~36%) and 1.141 g of ammonium persulfate in a beaker, and add 1 mL of a mixed solution of aniline and ethanol (volume ratio 1:1) under magnetic stirring, and stir. After 30 s, it was placed in a refrigerator at 6 ° C for 24 h, then the reaction solution was filtered under reduced pressure and washed with a sand core funnel and a 0.45 μm polyvinylidene fluoride filter, and the product polyaniline was redispersed into ethanol to prepare 8 mg/mL ethanol dispersion.

取尺寸为10×20cm棉布,在棉布上分多次、均匀地滴加5mL聚苯胺的乙醇分散液,控制滴加区域为棉布中心的10×10cm部分,并在60℃的烘箱中烘干,得到聚苯胺/棉光热转换织物。Take 10×20cm cotton cloth, add 5mL polyaniline ethanol dispersion to the cotton cloth multiple times, and control the dropping area to the 10×10cm part of the cotton cloth center, and dry it in an oven at 60°C. A polyaniline/cotton photothermal conversion fabric was obtained.

将所得的光热转换织物用夹子固定在两个方形聚乙烯塑料盒的端口上,织物边缘部分自然下垂并与水盒内海水接触,控制织物中心部位与塑料盒端口的高度差为1cm,塑料盒内海水液面比塑料盒端口低2mm,待海水完全浸润光热转换织物后,使用平均光强为0.16W/cm2、圆形光斑直径约10cm的氙灯模拟器照射织物,其水蒸气累计产生情况如图3所示。The obtained photothermal conversion fabric is fixed on the ports of two square polyethylene plastic boxes by clips, and the edge portion of the fabric naturally hangs down and contacts the seawater in the water box, and the height difference between the center of the fabric and the plastic box port is 1 cm, plastic The seawater level in the box is 2mm lower than the plastic box port. After the seawater is completely wetted by the light-heat conversion fabric, the fabric is irradiated with a xenon lamp simulator with an average light intensity of 0.16 W/cm 2 and a circular spot diameter of about 10 cm. The situation is shown in Figure 3.

海水蒸发后,并无明显的矿物质盐颗粒在光热转换织物表面析出。为进行对比,将相同的光热转换布放于10×10cm的海水面上,在相同的氙灯模拟器照射下,水蒸气累计产生情况如图3所示,由图可见本装置的蒸汽产生速度约为传统方式的3倍。After the seawater evaporates, no significant mineral salt particles are precipitated on the surface of the photothermal conversion fabric. For comparison, the same photothermal conversion cloth was placed on a sea surface of 10×10 cm. Under the same xenon lamp simulator, the cumulative generation of water vapor is shown in Fig. 3. The steam generation speed of the device can be seen from the figure. About three times the traditional way.

实施例2Example 2

按照实施例1中的方法制备8mg/mL的聚苯胺的乙醇分散液。取600mL分散液,多次、均匀地滴在80×240cm棉布的中间部分,控制滴加区域为棉布中心的80×140cm部分,并用电吹风吹干,将该棉布的两端用夹子固定在两个方形聚乙烯水槽(水槽开口尺寸:80×15cm)端口,控制织物中心部位与水槽端口的高度差为10cm、水槽内的水面比塑料盒端口低1cm,待水完全浸润光热转换织物后,将该装置放于太阳光下,记录水蒸发的质量变化,不同时刻太阳光光强和对应的水蒸发速率如图4所示,该装置在一天内累计 产生蒸汽的质量如图5所示。 An ethanol dispersion of 8 mg/mL of polyaniline was prepared as in Example 1. Take 600mL of dispersion, drop it repeatedly in the middle part of 80×240cm cotton cloth, control the dropping area to the 80×140cm part of the cotton cloth center, and blow it dry with hair dryer, fix the two ends of the cotton cloth with clips. Two square polyethylene sinks (sink opening size: 80×15cm) port, the height difference between the center of the fabric and the sink port is 10cm, and the water surface in the water tank is 1cm lower than the plastic box port. After the water is completely wetted by the light heat conversion fabric The device is placed under the sunlight to record the change in the quality of the water evaporation. The sunlight intensity and the corresponding water evaporation rate at different times are shown in Figure 4. The device is accumulated in one day. The quality of the generated steam is shown in Figure 5.

Claims (10)

一种新型太阳能光热海水蒸发装置,包括两侧水箱(1)、亲水性光热转换织物(2)和浓缩液收集箱(3),其特征在于:所述亲水性光热转换织物(2)两侧分别铺设于两侧的水箱(1)上,所述亲水性光热转换织物(2)的两端分别置于两侧的水箱(1)中且浸没于海水面以下,两侧水箱(1)之间的亲水性光热转换织物(2)呈下凹的弧形,所述亲水性光热转换织物(2)中部为含有光热转换材料的光热转换区,所述浓缩液收集箱(3)对应设置于亲水性光热转换织物(2)中部弧形最低点的下方。A novel solar photothermal seawater evaporation device comprises a water tank on both sides (1), a hydrophilic photothermal conversion fabric (2) and a concentrate collection tank (3), characterized in that: the hydrophilic photothermal conversion fabric (2) The two sides are respectively laid on the water tanks (1) on both sides, and the two ends of the hydrophilic photothermal conversion fabric (2) are respectively placed in the water tanks (1) on both sides and submerged below the sea surface, two The hydrophilic photothermal conversion fabric (2) between the side water tanks (1) has a concave curved shape, and the middle portion of the hydrophilic photothermal conversion fabric (2) is a photothermal conversion region containing a photothermal conversion material. The concentrate collection tank (3) is disposed below the lowest point of the arc shape in the middle of the hydrophilic photothermal conversion fabric (2). 根据权利要求1所述的一种新型太阳能光热海水蒸发装置,其特征在于:所述亲水性光热转换织物(2)的两端高点与中间低点的高度差h1为0<h1≤10m。A novel solar thermal seawater evaporation device according to claim 1, wherein a height difference h 1 between the high point of the two ends of the hydrophilic photothermal conversion fabric (2) and the intermediate low point is 0 < h 1 ≤ 10m. 根据权利要求1所述的一种新型太阳能光热海水蒸发装置,其特征在于:所述两侧水箱(1)内的海水面高度差大于等于0且小于等于10m。A novel solar thermal seawater evaporation device according to claim 1, characterized in that the difference in sea surface height between the two sides of the water tank (1) is greater than or equal to 0 and less than or equal to 10 m. 根据权利要求1所述的一种新型太阳能光热海水蒸发装置,其特征在于:所述海水面与亲水性光热转换织物(2)两端高点的高度差h2为0<h2≤10m。A novel solar thermal seawater evaporation device according to claim 1, wherein the height difference h 2 between the sea surface and the high point of the hydrophilic photothermal conversion fabric (2) is 0 < h 2 ≤10m. 根据权利要求1所述的一种新型太阳能光热海水蒸发装置,其特征在于:所述亲水性光热转换织物(2)由亲水性织物基底和光热转换材料组成。A novel solar thermal seawater evaporation apparatus according to claim 1, wherein said hydrophilic photothermal conversion fabric (2) is composed of a hydrophilic fabric substrate and a photothermal conversion material. 根据权利要求5所述的一种新型太阳能光热海水蒸发装置,其特征在于:所述亲水性织物基底为天然纤维、再生纤维素纤维和化学纤维中的一种或者多种制成的针织织物、机织织物或非织物。A novel solar thermal seawater evaporation device according to claim 5, wherein the hydrophilic fabric substrate is knitted by one or more of natural fibers, regenerated cellulose fibers and chemical fibers. Fabric, woven or non-woven. 根据权利要求6所述的一种新型太阳能光热海水蒸发装置,其特征在于:所述天然纤维为棉、麻、丝、毛或者纸浆,所述再生纤维素纤维为Lyocell纤维、Modal纤维、竹纤维、甲壳素纤维或者铜氨纤维,所述化学纤维为涤纶、氨纶、腈纶、锦纶、维纶或者丙纶。A novel solar thermal seawater evaporation device according to claim 6, wherein the natural fiber is cotton, hemp, silk, wool or pulp, and the regenerated cellulose fiber is Lyocell fiber, Modal fiber, bamboo. Fiber, chitin fiber or copper ammonia fiber, the chemical fiber is polyester, spandex, acrylic, nylon, vinylon or polypropylene. 根据权利要求6所述的一种新型太阳能光热海水蒸发装置,其特征在于:所述非织物为无纺布。A novel solar thermal seawater evaporation device according to claim 6, wherein the non-woven fabric is a nonwoven fabric. 根据权利要求1或7所述的一种新型太阳能光热海水蒸发装置,其特征在于:所述光热转换材料包括金属纳米颗粒、碳纳米材料、有机光热材料和半导体光热纳米材料中的一种或者多种。A novel solar thermal seawater evaporation device according to claim 1 or 7, wherein the photothermal conversion material comprises metal nanoparticles, carbon nano materials, organic photothermal materials and semiconductor photothermal nano materials. One or more. 根据权利要求9所述的一种新型太阳能光热海水蒸发装置,其特征在于:所述金属纳米颗粒为金纳米颗粒、钯纳米颗粒、铂纳米颗粒或者铝纳米颗粒,所述碳纳米材料为碳黑、碳粉、多孔碳、碳纳米管、石墨烯或者富勒烯,所述有机光热材料为聚吡咯、聚噻吩、聚苯胺、聚多巴胺、吲哚菁绿或者普鲁士蓝,所述半导体光热纳米材料为硫 化铜、硒化铜、硫化铋、硒化铋、硫化钨、氧化钨、二氧化钛、三氧化二钛、硫化铁或者硫化钼。 A novel solar thermal seawater evaporation device according to claim 9, wherein the metal nanoparticles are gold nanoparticles, palladium nanoparticles, platinum nanoparticles or aluminum nanoparticles, and the carbon nano materials are carbon Black, carbon powder, porous carbon, carbon nanotubes, graphene or fullerene, the organic photothermal material is polypyrrole, polythiophene, polyaniline, polydopamine, phthalocyanine green or Prussian blue, the semiconductor light Thermal nanomaterial is sulfur Copper, copper selenide, barium sulfide, barium selenide, tungsten sulfide, tungsten oxide, titanium dioxide, titanium oxide, iron sulfide or molybdenum sulfide.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115448403A (en) * 2022-10-13 2022-12-09 西安交通大学 Multistage solar water evaporation and collection device and method for photo-thermal/evaporation interface separation

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CN116395775A (en) * 2023-03-03 2023-07-07 深圳中拓天达环境工程有限公司 Solar evaporator and preparation method thereof
CN116268661A (en) * 2023-03-17 2023-06-23 青岛大学 A comfortable mask for quickly discharging exhaled moisture

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2063515U (en) * 1990-03-30 1990-10-10 国家海洋局天津海水淡化与综合利用研究所 Full-plastic solar and electric energy dual-purpose fresh water producer
CN2152790Y (en) * 1993-03-16 1994-01-12 中国人民解放军59174部队 Domestic solar desalination device
DE10222316A1 (en) * 2002-05-18 2003-12-11 Georg Gallon Apparatus and method for solar desalination of seawater and current generation involves use of a solar heated sea water boiler provided with a membrane letting through steam but not salt
CN1583584A (en) * 2004-05-25 2005-02-23 周梦然 Marine solar energy capillary evaporating seawater desalting apparatus
CN1583583A (en) * 2004-05-25 2005-02-23 周梦然 Landing solar energy capillary evaporating seawater desalting apparatus
US20050115819A1 (en) * 2003-12-01 2005-06-02 Ching-Piau Lai System for desalinating and purifying seawater and devices for the system (II type)
CN201068408Y (en) * 2007-07-23 2008-06-04 陈坚胜 Device for using solar energy to desalt water by direct method
CN102583609A (en) * 2012-03-20 2012-07-18 浙江大学 Multi-effect vertical plate falling film solar desalination unit and method thereof
CN103253722A (en) * 2013-06-07 2013-08-21 浙江大学 Plate type low-temperature multieffect seawater desalting device and method
US20160368785A1 (en) * 2015-06-16 2016-12-22 Ilan ZAMIR Methods and systems to reduce air pollution combined with water desalination of power station's marine waste water
CN106396224A (en) * 2016-06-17 2017-02-15 北京理工大学 Micro-cavity type solar seawater desalination unit based on condensation

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2063515U (en) * 1990-03-30 1990-10-10 国家海洋局天津海水淡化与综合利用研究所 Full-plastic solar and electric energy dual-purpose fresh water producer
CN2152790Y (en) * 1993-03-16 1994-01-12 中国人民解放军59174部队 Domestic solar desalination device
DE10222316A1 (en) * 2002-05-18 2003-12-11 Georg Gallon Apparatus and method for solar desalination of seawater and current generation involves use of a solar heated sea water boiler provided with a membrane letting through steam but not salt
US20050115819A1 (en) * 2003-12-01 2005-06-02 Ching-Piau Lai System for desalinating and purifying seawater and devices for the system (II type)
CN1583584A (en) * 2004-05-25 2005-02-23 周梦然 Marine solar energy capillary evaporating seawater desalting apparatus
CN1583583A (en) * 2004-05-25 2005-02-23 周梦然 Landing solar energy capillary evaporating seawater desalting apparatus
CN201068408Y (en) * 2007-07-23 2008-06-04 陈坚胜 Device for using solar energy to desalt water by direct method
CN102583609A (en) * 2012-03-20 2012-07-18 浙江大学 Multi-effect vertical plate falling film solar desalination unit and method thereof
CN103253722A (en) * 2013-06-07 2013-08-21 浙江大学 Plate type low-temperature multieffect seawater desalting device and method
US20160368785A1 (en) * 2015-06-16 2016-12-22 Ilan ZAMIR Methods and systems to reduce air pollution combined with water desalination of power station's marine waste water
CN106396224A (en) * 2016-06-17 2017-02-15 北京理工大学 Micro-cavity type solar seawater desalination unit based on condensation

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115448403A (en) * 2022-10-13 2022-12-09 西安交通大学 Multistage solar water evaporation and collection device and method for photo-thermal/evaporation interface separation
CN115448403B (en) * 2022-10-13 2023-08-15 西安交通大学 Multi-stage solar water evaporation and collection device and method with photo-thermal/evaporation interface separation

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