CN2697073Y - Sea water desalination device - Google Patents
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- CN2697073Y CN2697073Y CNU03280556XU CN03280556U CN2697073Y CN 2697073 Y CN2697073 Y CN 2697073Y CN U03280556X U CNU03280556X U CN U03280556XU CN 03280556 U CN03280556 U CN 03280556U CN 2697073 Y CN2697073 Y CN 2697073Y
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- 239000013535 sea water Substances 0.000 title claims abstract description 25
- 238000010612 desalination reaction Methods 0.000 title description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 51
- 230000008016 vaporization Effects 0.000 claims abstract description 39
- 238000009834 vaporization Methods 0.000 claims abstract description 36
- 238000011033 desalting Methods 0.000 claims abstract 6
- 239000012530 fluid Substances 0.000 claims abstract 3
- 239000013505 freshwater Substances 0.000 claims description 19
- 239000007788 liquid Substances 0.000 claims description 15
- 239000012153 distilled water Substances 0.000 claims description 6
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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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Abstract
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快速蒸发汽化海水淡化装置和一种快速制盐装置及一种水处理装置——新型海水淡化装置。The utility model relates to a seawater desalination device, in particular to a gas-liquid mixing fast evaporation vaporization seawater desalination device, a fast salt making device and a water treatment device - a new seawater desalination device.
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。有关气液混合高温高速飓风气流快速蒸发汽化的海水淡化的技术,文献中记载得较少,到目前为止,尚未见到市场上有此类技术产品推广应用。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 seawater desalination technology of gas-liquid mixing high-temperature and high-speed hurricane airflow rapid evaporation and vaporization. So far, no such technology products have been popularized and applied in the market.
发明内容Contents of invention
本实用新型的目的是提供一种新型海水淡化装置。The purpose of this utility model is to provide a novel seawater desalination device.
为了达到上述的目的,本实用新型的技术方案是:所述的透明汽化大棚体内设置有飓风筒,所述的飓风筒体内设置有接力形式的远程涡轮鼓风机所述的飓风筒体内的下部设置有接液盘。所述的透明汽化大棚体内设置有倾斜角度安装的分段式透明飓风筒所述的透明飓风筒的体内设置有巨大功力的单个或多个的接力形式的远程涡轮鼓风机。所述的透明飓风筒的壁体上设置有单个或多个的水质检测杯阀门;所述的透明飓风筒5体内的下部设置连接有接液盘与浓缩盐水出液阀门连接联通。在所述的汽化室的顶部出口处设置有加速汽化室内热蒸气流动的拔风筒;在拔风筒的上方设置有太阳能涡轮发电机。由于采用上述技术方案,本实用新型提供的新型海水淡化装置,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。In order to achieve the above-mentioned purpose, the technical solution of the present utility model is: a hurricane cylinder is arranged in the transparent vaporization greenhouse, and a remote turbo blower in the form of a relay is arranged in the described hurricane cylinder. Wet pan. The body of the transparent vaporization greenhouse is equipped with a segmented transparent hurricane tube installed at an oblique angle. The body of the transparent hurricane tube is equipped with a single or multiple relay-type remote turbo blowers with great power. The wall of the transparent hurricane cylinder is provided with single or multiple water quality detection cup valves; the lower part of the
附图说明Description of drawings
图1是本实用新型实施例新型海水淡化装置的透明汽化大棚和透明百叶窗隔层板及透明飓风筒剖面的工作原理的简介示意图。Fig. 1 is a brief schematic diagram of the working principle of the transparent vaporization greenhouse, the transparent louver interlayer board and the transparent hurricane cylinder section of the new seawater desalination device of the embodiment of the utility model.
图2是本实用新型实施例新型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 new seawater desalination device according to the embodiment of the present invention.
图3是本实用新型实施例新型海水淡化装置的透明汽化大棚顶端和透明飓风筒的工作原理的简介示意图。Fig. 3 is a brief schematic diagram of the working principle of the top of the transparent vaporization greenhouse and the transparent hurricane cylinder of the new seawater desalination device according to the embodiment of the utility model.
图中:压力进水阀门1、蓄水池2、压力水泵3、压力输液阀门4、分段式透明飓风筒5、雾化喷嘴6、远程涡轮鼓风机7、拔风筒8、太阳能涡轮发电机9、汽液混合物10、透明汽化大棚11、高速气流状12、透明百叶窗隔层板13、汽化室14、水质检测杯阀门15、接力形式的远程涡轮鼓风机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、接液盘21。In the figure: pressure water inlet valve 1, reservoir 2, pressure water pump 3, pressure infusion valve 4, segmented
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、蓄水池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体内前端的下部倾斜角度安装设置安置分段式超长管形的透明飓风筒5,透明飓风罩5体内的空气气体的进口端设置有远程涡轮鼓风机7、雾化喷嘴6,透明飓风罩5体内的空气气体的进口端设置安置在透明汽化大棚11前端下部。由雾化喷嘴6高压高速喷射出的微小雾滴被远程涡轮鼓风机7喷射出的高速空气气流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倾斜角度安装的透明飓风筒5,透明飓风筒5的体内设置有单个或多个的接力形式的远程涡轮鼓风机16,远程涡轮鼓风机16开启后的高速气流即形成高速气流状12。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的上方设置有加速汽化室14内蒸气流动的拔风筒8,在拔风筒8的上方设置有太阳能涡轮发电机9。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可致使向上流动的水汽只能单方向进入汽化室14体内。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在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。在透明飓风筒5的体壁上设置有单个或多个的水质检测杯阀门15,在透明飓风筒5的体内下部设置有接液盘21。透明汽化大棚11体内底部设置有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;透明飓风筒5的下部接液盘21与浓缩盐水出液阀门18连接,淡水排水阀门19与吸热淡水池17连接;吸热淡水池17的池底涂有高效吸热材料,太阳能涂黑吸热淡水池17为太阳能辐射热能量收集池。Pressure water inlet valve 1, reservoir 2, pressure water pump 3 (the working pressure of the pressure water pump 3 should be based on the different requirements of the finished product water quality according to different needs, and the setting range of the working pressure is 2 times to 5000 times higher than the normal atmospheric pressure) , pressure infusion valve 4, and atomizing nozzle 6 are sequentially connected and sealed and communicated with each other; the inclination angle of the lower part of the front end of the
本实用新型新型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池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的电源开关,然后开启压力输液阀门4通过雾化喷嘴6向分段式透明飓风筒5体内高压高速喷射微小雾滴,同时巨量的高密度的热风空气气流从飓风筒5的气体进口端进入与高压高速海水微粒雾滴喷射束混合。此时开启单个或多个的接力形式的远程涡轮鼓风机16的电源开关,单个或多个的接力形式的远程涡轮鼓风机16产生的巨量的高温高速空气气流形成高速气流状12,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鼓、吹起送向空中快速远行程运行漂移不断地搅拌,使微小雾滴与高速热风空气气流混合得更为均匀,在相互间进行双向溶解同化后,形成汽液混合物10,在透明飓风筒5的体内体外,在促进相互间再进一步地不断地进行双向溶解的同化同时,被快速蒸发汽化。小雾滴在形成悬浮小颗粒的同时快速吸收周围的大量的热量,快速膨胀汽化几十倍,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,在被高速热风气流喷射输送后漂移的行程较长,长时间地长距离地悬浮下降缓慢,形成微细悬浮雾云颗粒,在透明飓风筒5体内的高温热风高速气流搅拌下,微细悬浮雾云颗粒逐渐跃出透明飓风筒5内壁筒体的最高端,并在透明汽化大棚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,在被高速热风气流喷射后的行程较短,悬浮的时间较短下降较快,形成细小液滴在透明飓风筒5体内的太阳能辐射热高温热风高速气流搅拌下下,蒸发汽化较慢下落较快,较容易汇集于透明飓风筒5的内壁上,流至透明飓风筒5体内的下部接液盘21聚集,并与浓缩盐水出液阀门18汇合。The working process of the new seawater desalination device of the utility model is as follows: firstly, the pressure water inlet valve 1 is opened, and the pretreated cold seawater is continuously injected into the body of the reservoir 2 through the pressure water inlet pipe at high speed, and the power supply of the pressure water pump 3 is turned on Switch, when the working pressure of the pressure water pump 3 reaches a certain high pressure required by the different water quality requirements of different finished products, turn on the power switch of the remote turbo blower 7, and then turn on the pressure infusion valve 4 through the atomizing nozzle 6 to segmented The
大量的悬浮小雾滴在远程涡轮鼓风机7的巨大的高温高速的喷射气流的长时间地长行程地喷射悬浮下,在不断地缓慢下降时,单个或多个的接力形式的远程涡轮鼓风机16产生的巨量的高温高速空气气流形成高速气流状12,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鼓、吹起送向空中快速远行程运行漂移不断地搅拌,迫使微细悬浮小雾滴全部在透明飓风筒5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在与大量的高温高速空气气体不断地长时间地反复地充分地搅拌混合后,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。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,较容易汇集在透明飓风筒5的内壁上,流至飓风筒5的下部接液盘21聚集;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,悬浮微颗粒一旦超越出透明飓风筒5的内壁筒体的最高端,即逐渐汇集至太阳能涂黑吸热的淡水池17中。通常的情况下:淡化水水质的优劣可根据检测分段式透明飓风筒5体壁最高端的水质检测杯15的杯中的水质,从水质检测杯阀门15中取水化验,检测淡化水是否达到所需要的水质要求,如果发生检测的淡化水未能达到所需的水质要求时,可采取的措施是:1、大幅度地提高水泵的工作压力;2、将远程涡轮鼓风机7的转速提高,加大鼓风机的风力;3、将接力形式的远程涡轮鼓风机16的转速提高,加大鼓风机的风力或增加接力形式的远程涡轮鼓风机16的接力段段数;4、增加分段式透明飓风筒5的筒体,加长透明飓风筒5筒体的长度;直到淡化水的水质达到所需要的水质要求为止。太阳能涂黑吸热淡水池17一般为在早晨将淡水排光,再将白天汇集的热水蓄热过夜,使其热水热能在夜间逐渐释放热量。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,巨量的快速流动的热风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,其中的部分热蒸气继续上升至拔风筒8,高速推动太阳能涡轮发电机9旋转发电。在太阳能涡轮发电机9高速旋转发电的同时可不断地促进汽化室14内的热蒸气流速,提高淡化效率,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。如此不断地反复循环运行不息。可达到低耗能、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,并进行长距离隔离的新型海水淡化的目的。A large number of suspended small mist droplets are sprayed and suspended by the huge high-temperature and high-speed jet airflow of the remote turbo blower 7 for a long time and a long distance. The huge amount of high-temperature and high-speed air flow forms a high-speed
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CN103693700A (en) * | 2013-12-25 | 2014-04-02 | 中国地质大学(武汉) | A seawater desalination device |
CN110467234A (en) * | 2019-09-18 | 2019-11-19 | 内蒙古工业大学 | Portable photovoltaic direct distillation desalinates water installations |
WO2024148444A1 (en) * | 2023-01-10 | 2024-07-18 | 吕建华 | Refrigerating appliance for high-speed vaporization of water working medium and design and manufacturing method therefor |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN103693700A (en) * | 2013-12-25 | 2014-04-02 | 中国地质大学(武汉) | A seawater desalination device |
CN103693700B (en) * | 2013-12-25 | 2015-09-16 | 中国地质大学(武汉) | A kind of sea water desalinating plant |
CN110467234A (en) * | 2019-09-18 | 2019-11-19 | 内蒙古工业大学 | Portable photovoltaic direct distillation desalinates water installations |
CN110467234B (en) * | 2019-09-18 | 2024-01-26 | 内蒙古尖锋科技有限公司 | Portable photovoltaic direct distillation method water desalination device |
WO2024148444A1 (en) * | 2023-01-10 | 2024-07-18 | 吕建华 | Refrigerating appliance for high-speed vaporization of water working medium and design and manufacturing method therefor |
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