CN2687107Y - Gas-liquid mixed high-speed evaporating sea water desalting device - Google Patents
Gas-liquid mixed high-speed evaporating sea water desalting device Download PDFInfo
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- CN2687107Y CN2687107Y CNU032098286U CN03209828U CN2687107Y CN 2687107 Y CN2687107 Y CN 2687107Y CN U032098286 U CNU032098286 U CN U032098286U CN 03209828 U CN03209828 U CN 03209828U CN 2687107 Y CN2687107 Y CN 2687107Y
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- 239000007788 liquid Substances 0.000 title claims abstract description 28
- 239000013535 sea water Substances 0.000 title claims abstract description 27
- 238000001704 evaporation Methods 0.000 title claims abstract description 19
- 238000011033 desalting Methods 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 40
- 238000009834 vaporization Methods 0.000 claims abstract description 32
- 230000008016 vaporization Effects 0.000 claims abstract description 32
- 238000002156 mixing Methods 0.000 claims abstract description 21
- 238000010612 desalination reaction Methods 0.000 claims abstract description 18
- 230000008020 evaporation Effects 0.000 claims abstract description 17
- 239000013505 freshwater Substances 0.000 claims description 17
- 239000012267 brine Substances 0.000 claims description 16
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 16
- 238000002955 isolation Methods 0.000 claims description 9
- 239000012153 distilled water Substances 0.000 claims description 6
- 238000001802 infusion Methods 0.000 claims description 6
- 238000005192 partition Methods 0.000 claims description 5
- 239000000203 mixture Substances 0.000 abstract description 14
- 239000003595 mist Substances 0.000 abstract description 12
- 239000002245 particle Substances 0.000 abstract description 11
- 238000000889 atomisation Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 12
- 238000000926 separation method Methods 0.000 description 7
- 239000007921 spray Substances 0.000 description 6
- 230000005855 radiation Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 239000011229 interlayer Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000007701 flash-distillation Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000909 electrodialysis Methods 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- 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
- Y02A20/124—Water desalination
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- 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
- Y02A20/124—Water desalination
- Y02A20/138—Water desalination using renewable energy
- Y02A20/142—Solar thermal; Photovoltaics
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- 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
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
本实用新型公开了一种气液混合高速蒸发海水淡化装置,旨在提供一种结构简单、投资较少、成本较低、性能稳定、水质较优的海水淡化装置。其技术方案的要点是,设置的透明汽化大棚体内设置有飓风罩,飓风罩体内设置有鼓风机、压力水泵射流雾化喷嘴、混合室、扩散器,迫使高压高速海水小雾滴与高密度的空气气流充分混合后,形成微细悬浮雾滴小颗粒汽液混合物,并再次被设置的接力形式的鼓风机吹起,远行程漂移分离隔离,不断地被快速蒸发汽化。
The utility model discloses a gas-liquid mixing high-speed evaporation seawater desalination device, which aims to provide a seawater desalination device with simple structure, less investment, lower cost, stable performance and better water quality. The key point of the technical solution is that a hurricane hood is installed in the transparent vaporization greenhouse, and a blower, a pressure water pump jet atomization nozzle, a mixing chamber, and a diffuser are arranged in the hurricane hood to force high-pressure, high-speed seawater droplets and high-density air After the airflow is fully mixed, a mixture of fine suspended mist and small particles of vapor and liquid is formed, which is blown up again by the blower in the form of a relay, separated and isolated by long-distance drifting, and continuously vaporized by rapid evaporation.
Description
技术领域Technical field
本实用新型涉及一种海水淡水装置,特别是涉及一种气液混合海水淡化装置和一种快速制盐装置及一种水处理装置,由压力进水阀门、蓄水箱、压力水泵、压力输液阀门、飓风罩、雾化喷嘴、远程涡轮鼓风机[或风扇]、气体进口端、混合室、扩散器、混合物出口端、接力形式的远程涡轮鼓风机[或接力形式的风扇]透明汽化大棚、区间隔离板、透明百叶窗隔层板、汽化室、自动泄压排气窗、太阳能涂黑吸热浓缩盐水池、太阳能涂黑吸热淡水池、管道阀门等组成的气液混合高速蒸发海水淡化装置。The utility model relates to a seawater desalination device, in particular to a gas-liquid mixed seawater desalination device, a rapid salt making device and a water treatment device, which are composed of a pressure water inlet valve, a water storage tank, a pressure water pump and a pressure infusion Valve, hurricane hood, atomizing nozzle, remote turbo blower [or fan], gas inlet port, mixing chamber, diffuser, mixture outlet port, remote turbo blower in relay form [or fan in relay form] transparent vaporization greenhouse, section isolation A gas-liquid mixed high-speed evaporation seawater desalination device consisting of panels, transparent louver partitions, vaporization chambers, automatic pressure relief and exhaust windows, solar blackened heat-absorbing concentrated brine pools, solar blackened heat-absorbing fresh water pools, and pipeline valves.
背景技术 Background technique
目前国内、外采用的海水淡化方法比较多,变相法:蒸发法、蒸馏法、冷却法;膜分离法:反渗透法、电渗析法;化学平衡法:离子交换法、水合法、溶剂萃取法等主要三大类型。目前技术领先的也是应用最多的是闪急蒸馏法,约占当今世界海水淡化总产量的70%。闪急蒸馏法就是利用水的沸点随压力降低而降低这一特性,首先使海水在管道中加热,然后引到一个压力较低的蒸发室中,被引入的高温海水就会在一刹那间迅速蒸发(短暂的蒸发饱和后即停止),产生的蒸气在装有冷海水的管道外得到冷凝而造成淡水。其缺点是:设备投资多,海水循环量大、制水量小,制水速度慢,浓缩率较低,操作费用较高。有关气液混合高速蒸发海水淡化的技术,文献中记载得较少。At present, there are many seawater desalination methods used at home and abroad, disguised phase method: evaporation method, distillation method, cooling method; membrane separation method: reverse osmosis method, electrodialysis method; chemical equilibrium method: ion exchange method, hydration method, solvent extraction method and other three main types. At present, the leading technology and the most widely used is flash distillation, which accounts for about 70% of the world's total desalination production. The flash distillation method is to use the characteristic that the boiling point of water decreases with the decrease of pressure. First, the seawater is heated in the pipeline, and then introduced into an evaporation chamber with a lower pressure. The introduced high-temperature seawater will evaporate rapidly in an instant. (It stops after a short period of evaporation saturation), and the generated steam is condensed outside the pipeline with cold sea water to form fresh water. Its disadvantages are: high investment in equipment, large seawater circulation, small water production, slow water production, low concentration rate, and high operating costs. There are few records in the literature about the technology of gas-liquid mixing and high-speed evaporation of seawater desalination.
发明内容Contents of the invention
本实用新型的目的是提供一种气液混合高速蒸发海水淡化装置。The purpose of the utility model is to provide a gas-liquid mixing high-speed evaporation seawater desalination device.
为了达到上述的目的,本实用新型的技术方案是:所述的飓风罩体外的出口端的前方下部设置有单个或多个接力形式的远程涡轮鼓风机[或接力形式的风扇]。若不设置飓风罩,在雾化喷嘴的喷射出口端的前方下部设置有单个或多个接力形式的远程涡轮鼓风机[或接力形式的风扇]。In order to achieve the above purpose, the technical solution of the utility model is: the lower part in front of the outlet end outside the hurricane housing is provided with single or multiple remote turbo blowers [or relay fans]. If the hurricane cover is not provided, a single or multiple remote turbo blowers [or fans in the form of relays] in the form of relays are arranged on the lower part in front of the spray outlet of the atomizing nozzle.
由于采用上述技术方案,本实用新型提供的气液混合高速蒸发海水淡化装置,具有这样的有益效果,即结构简单、投资较少、成本较低、性能稳定、水垢少、污染少、水质优、制造淡水产量高。Due to the adoption of the above technical scheme, the gas-liquid mixing high-speed evaporation seawater desalination device provided by the utility model has such beneficial effects as simple structure, less investment, lower cost, stable performance, less scale, less pollution, excellent water quality, Produces high yields of fresh water.
附图说明Description of drawings
图1是本实用新型实施例气液混合高速蒸发海水淡化装置的透明汽化大棚和透明百叶窗隔层板及区间隔离板的工作原理的简介示意图。Figure 1 is a brief schematic diagram of the working principle of the transparent vaporization greenhouse, transparent louver partition board and section partition board of the gas-liquid mixing high-speed evaporation seawater desalination device of the embodiment of the utility model.
图2是本实用新型实施例气液混合高速蒸发海水淡化装置的总体的工作原理的简介示意图。Fig. 2 is a brief schematic diagram of the overall working principle of the gas-liquid mixing high-speed evaporation seawater desalination device according to the embodiment of the utility model.
图3是本实用新型实施例气液混合高速蒸发海水淡化装置的空气气体进口端被设置安置在透明汽化大棚前端下部体内的工作原理的简介示意图。Fig. 3 is a brief schematic diagram of the working principle of the gas-liquid mixing high-speed evaporation seawater desalination device according to the embodiment of the utility model.
图4是本实用新型实施例气液混合高速蒸发海水淡化装置的无飓风罩的接力形式的远程鼓风机[或接力形式的风扇]的工作原理的简介示意图。Fig. 4 is a brief schematic diagram of the working principle of the remote blower in the relay form [or the fan in the relay form] without a hurricane cover in the gas-liquid mixing high-speed evaporation seawater desalination device of the embodiment of the utility model.
图中:压力进水阀门1、蓄水箱2、压力水泵3、压力输液阀门4、飓风罩5、雾化喷嘴6、远程涡轮鼓风机7[或风扇7]、混合室8、扩散器9、汽液混合物10、透明汽化大棚11、区间隔离板12、透明百叶窗隔层板13、汽化室14、自动泄压排气窗15、太阳能涂黑吸热浓缩盐水池16、太阳能涂黑吸热淡水池17、浓缩盐水出液阀门18、淡水排水阀门19、蒸馏水出水阀门20、气体进口端21、混合物出口端22、安置在体内23、安置在体外24、接力形式的远程涡轮鼓风机25[或接力形式的风扇25]。In the figure: pressure
具体实施方式 Detailed ways
下面结合附图对本实用新型作进一步的描述。Below in conjunction with accompanying drawing, the utility model is further described.
压力进水阀门1、蓄水箱2、压力水泵3(压力水泵3的工作压力应根据不同需要的成品水质的不同要求,工作压力的设定范围为高于正常大气压的2倍至5000倍)、压力输液阀门4、雾化喷嘴6相互间顺序连接密封并联通;透明汽化大棚11体内前端的下部稍倾斜角度设置安置超长管形的飓风罩5,飓风罩5体内中端的狭小的腰部设置有混合室8,飓风罩5体内的出口端设置有扩散器9是汽液混合物10的混合扩散空间及喷射通道;飓风罩5体内的进口端设置有远程涡轮鼓风机7[或风扇7]、雾化喷嘴6,飓风罩5体内的空气气体的进口端21设置安置在透明汽化大棚11前端下部可安置在体内23[或安置在体外24]。由雾化喷嘴6高压高速喷射出的微小雾滴和远程涡轮鼓风机7[或风扇7]喷射出的快速空气气流在经过混合室8时,混合室8内产生低压力,吸入流速稍慢的空气气流,高压高速微小雾滴与快速空气气流充分混合后一同进入扩散器9。在经过扩散器9时,混合流体的压力又逐渐上升,在微小雾滴与空气气流混合得更为均匀后形成汽液混合物10,然后排出扩散器9从混合物出口端22处高速向空中喷射被快速蒸发汽化。在透明汽化大棚11体内前端的下部设置有飓风罩5,在飓风罩5的出口端22的前方下部设置有单个或多个接力形式的远程涡轮鼓风机25[或接力形式的风扇25],若不设置飓风罩5,在雾化喷嘴6的喷射出口端22的前方下部设置有单个或多个接力形式的远程涡轮鼓风机25[或接力形式的风扇25]。透明汽化大棚11为巨型的透明的太阳能辐射热收集罩;透明汽化大棚11的体内中上部设置有由单个或2个或2个以上的全封隔离透明百叶窗隔层板13可隔离出单个或2个或2个以上的汽化室14,汽化室14被设置在透明汽化大棚11的体内上部,汽化室14的下部设置有蒸馏水出水阀门20,透明百叶窗隔层板13可迫使向上流动的水汽只能单方向进入汽化室14内。巨型的透明的太阳能透明汽化大棚11容积的大与小,应以能够满足巨大量的汽液混合物10连续不断地雾化汽化时,所必须吸收周围大量的热量——汽化热而设定其容积的大与小(为汽体与浓缩盐水小液滴的分离提供充足的大量的空间,因此,该巨大的空间罩体大棚可以借用其巨大的透明的罩体的独厚的有利条件进行太阳能辐射热的收集)。其透明汽化大棚11体内的容积,应根据所需的不同成品水质的不同需要,不同的工作气流量的需要,不同的水流量、不同的水液流速及不同的工作压力的需要,其容积的设定范围为压力输液阀门4每分钟流量体积的100倍至10万倍。透明汽化大棚11体内下部设置有区间隔离板12,区间隔离板12为大面积平面体,该区间隔离板12垂直于透明汽化大棚11体内底部上;透明汽化大棚11的体内或体外下部设置有自动泄压排气窗15可根据透明汽化大棚11体内的气压压差变化自动开启泄压排气及自动关闭停止泄压排气。透明汽化大棚11体内底部设置有太阳能涂黑吸热浓缩盐水池16、太阳能涂黑吸热淡水池17、浓缩盐水出液阀门18、淡水排水阀门19;浓缩盐水出液阀门18与浓缩盐水池16连接,淡水排水阀门19与淡水池17连接;太阳能涂黑吸热浓缩盐水池16、太阳能涂黑吸热淡水池17为太阳能辐射热能量收集池。Pressure
本实用新型气液混合高速蒸发海水淡化装置的工作流程为:首先开启压力进水阀门1通过压力进水管管道向蓄水箱2体内不断地高速注入注射已经过预处理后的冷海水,开启压力水泵3的电源开关,在压力水泵3的工作压力达到了一定的所需要的不同成品水质的不同要求的高压时,开启远程涡轮鼓风机7[或风扇7]的电源开关,然后开启压力输液阀门4通过雾化喷嘴6向飓风罩5体内高压高速喷射微小雾滴,巨量的高密度的空气气流从飓风罩5的气体进口端21进入后与高压高速海水微粒雾滴喷射束混合,当高压海水微粒喷射流体以高压高速喷射出雾化喷嘴6时,混合室8内产生低压力,吸入流速稍慢的空气气流体,使与微粒雾滴相混合,一同进入扩散器9,在经过扩散器9时,混合流体的压力又逐渐上升,在微小雾滴与空气气流混合得更为均匀在相互间进行双向溶解后,形成汽液混合物10,然后高速喷出扩散器9外,从混合物出口端22向空中高速喷射,在相互间再进一步进行双向溶解的同时,被快速蒸发汽化。The working process of the gas-liquid mixing high-speed evaporation seawater desalination device of the utility model is as follows: firstly, the pressure
汽液混合物10喷射出后在形成悬浮小颗粒的同时快速吸收周围的大量的热量,快速膨胀几十倍,数百倍。由于淡水水液容易膨胀,小雾滴在膨胀后形成雾云。较容易挥发的组分易蒸发汽化的淡水小雾滴的颗粒较小质点较小、容积较大,比重较小,在被高速气流喷射输送后漂移的行程较长,长时间地长距离地悬浮漂移下降缓慢,形成微细悬浮雾云颗粒,在透明汽化大棚11体内的太阳能辐射热高温下被快速蒸发汽化;不容易挥发的组分不易蒸发汽化的浓缩盐水小液滴的颗粒较大质点较大、容积较小,比重较大,在被高速气流喷射输送后飘移的行程较短,悬浮漂移的时间较短下降较快,形成细小液滴在透明汽化大棚11体内的太阳能辐射热高温下,蒸发汽化较慢下落较快。海水水液小雾滴在被压力水泵3的高压高速射流束和远程涡轮鼓风机7[或风扇7]的巨大的喷射空气气流量的快速气流高密度气体不断地长时间地搅拌长距离地输送,长时间的长距离的悬浮飘移,形成微细悬浮小雾滴不断地被巨量的空气气流同化,不断地运行上升,不断地被透明汽化大棚11体内的太阳能辐射热高温快速蒸发汽化。After the vapor-
大量的悬浮小雾滴在远程涡轮鼓风机7[或风扇7]的巨大的快速的喷射气流的长时间地长距离地喷射输送下,大量的悬浮小雾滴在远程涡轮鼓风机7[或风扇7]的巨大的快速的喷射气流的长时间地长行程地喷射输送下,不断地缓慢下降时,此时开启接力形式的单个或多个接力形式的远程涡轮鼓风机25[或接力形式的风扇25],单个或多个接力形式的远程涡轮鼓风机25[或接力形式的风扇25]产生的巨量的快速空气气流将大量的正在缓慢漂移逐渐下降的悬浮小雾滴微细颗粒再次吹起送向空中快速远行程运行漂移,不断地搅拌分离隔离,迫使微细悬浮小雾滴全部在透明汽化大棚11体内的空中长时间的悬浮漂移搅拌,形成悬浮汽液混合物10在与大量的空气气体不断地长时间地反复充分地搅拌混合后,悬浮汽液混合物10很容易被空气同化,使其不断地被高温快速蒸发汽化。此时,自动排气窗15在透明汽化大棚11体内的大量的多余的气体聚集后,在根据气压的不断地变化中,不断地被自动快速输送出去。由于浓缩盐水小液滴在空中停留的时间较短,悬浮漂移的行程较短,下降较快,在区间隔离板12的分隔下,汇集至太阳能涂黑吸热的浓缩盐水池16中;由于淡水微细小雾滴在空中悬浮滞留的时间较长、悬浮漂移的行程较长;下降较慢,在区间隔离板12的分隔下,汇集至太阳能涂黑吸热的淡水池17中。透明汽化大棚11在高效太阳能的辅助加热作用下,将空中滞游徘徊的微细悬浮汽液混合物10进行快速蒸发汽化,巨量的快速流动的水气流携带着大量的悬浮小雾滴同时运行上升,其中的部分微细颗粒被蒸发汽化上升后,部分的上升水汽流从单向入口的透明百叶窗隔层板13的百叶窗孔进入至上层的汽化室14内,再经蒸发汽,化汇集后形成蒸馏水。最后,开启浓缩盐水出液阀门18,将浓缩盐水水液不断地排出;开启淡水排水阀门19,将淡水水液不断地排出;开启蒸馏水出水阀门20,将蒸馏水水液不断地排出;达到低耗能、体积悬殊差、比重悬殊差、悬浮飘移行程悬殊差、悬浮滞留时间悬殊差,长时间地进行长距离分离进行长距离隔离的气液混合高速蒸发海水淡化的目的。A large number of suspended small mist droplets are sprayed and transported for a long time and long distance by the huge and fast jet airflow of the remote turbo blower 7 [or fan 7]. When the huge and fast jet airflow is sprayed and transported for a long time and long stroke, when it is continuously and slowly descending, the single or multiple remote turbo blowers 25 [or the fan 25] of the relay form are turned on at this time, The huge amount of fast air flow produced by the remote turbo blower 25 [or the
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CN109292864A (en) * | 2018-11-09 | 2019-02-01 | 武汉纺织大学 | A kind of low-concentration salt-containing wastewater evaporation and concentration device and treatment method |
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CN109292864A (en) * | 2018-11-09 | 2019-02-01 | 武汉纺织大学 | A kind of low-concentration salt-containing wastewater evaporation and concentration device and treatment method |
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