CN2926193Y - Water treatment equipment - Google Patents
Water treatment equipment Download PDFInfo
- Publication number
- CN2926193Y CN2926193Y CNU200620118542XU CN200620118542U CN2926193Y CN 2926193 Y CN2926193 Y CN 2926193Y CN U200620118542X U CNU200620118542X U CN U200620118542XU CN 200620118542 U CN200620118542 U CN 200620118542U CN 2926193 Y CN2926193 Y CN 2926193Y
- Authority
- CN
- China
- Prior art keywords
- water
- refrigeration cycle
- cooling
- staving
- unit
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 139
- 238000001816 cooling Methods 0.000 claims abstract description 69
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims abstract 6
- 238000003860 storage Methods 0.000 claims description 17
- 239000000498 cooling water Substances 0.000 claims description 13
- 230000010355 oscillation Effects 0.000 claims description 5
- 238000005057 refrigeration Methods 0.000 claims 11
- 230000003750 conditioning effect Effects 0.000 claims 6
- 239000000463 material Substances 0.000 claims 1
- 239000008399 tap water Substances 0.000 claims 1
- 235000020679 tap water Nutrition 0.000 claims 1
- 238000004821 distillation Methods 0.000 abstract description 15
- 239000013535 sea water Substances 0.000 abstract description 15
- 238000010612 desalination reaction Methods 0.000 abstract description 12
- 239000003651 drinking water Substances 0.000 abstract description 8
- 238000010438 heat treatment Methods 0.000 abstract description 8
- 235000020188 drinking water Nutrition 0.000 abstract description 7
- 238000012423 maintenance Methods 0.000 abstract description 7
- 238000010276 construction Methods 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 150000003839 salts Chemical class 0.000 abstract description 4
- 239000012535 impurity Substances 0.000 abstract description 3
- 239000010865 sewage Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 15
- 239000012528 membrane Substances 0.000 description 11
- 239000012267 brine Substances 0.000 description 7
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical group O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000001556 precipitation Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 150000001450 anions Chemical class 0.000 description 4
- 239000013505 freshwater Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 231100000614 poison Toxicity 0.000 description 4
- 238000005381 potential energy Methods 0.000 description 4
- 238000001223 reverse osmosis Methods 0.000 description 4
- 239000003440 toxic substance Substances 0.000 description 4
- 150000001768 cations Chemical class 0.000 description 3
- 238000000909 electrodialysis Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000003204 osmotic effect Effects 0.000 description 2
- 238000006424 Flood reaction Methods 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000002384 drinking water standard Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000013468 resource allocation Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Images
Classifications
-
- 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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
Description
技术领域:Technical field:
本实用新型涉及一种可将海水进行淡化与过滤的饮用水处理技术,亦可为一种污水的过滤处理技术,具体涉及一种水质处理设备。The utility model relates to a drinking water treatment technology capable of desalinating and filtering sea water, and also a sewage filtering treatment technology, in particular to a water quality treatment equipment.
现有技术:current technology:
人类生活中不可或缺的水,可由其固态、液态或气态的三相进行变化。水在地球上形成一循环系统,在地球表面占总面积达四分之三的水域所蒸发的水汽,经凝结而降至地面上,即成为水资源的主要来源。而此等经水循环过程所提供的水资源,理论上应不匮乏。但由于水汽凝结而降水的过程,受限于气象条件的配合,并非人为可随时掌控,因此无法随时随地因应需要来控制降水,因此,一旦气候异常导致长期缺雨,即会造成旱灾;反之,豪雨不停则成水灾。同时在气候干燥地区,大气湿度偏低,降水不易,将使干旱愈加严重;而湿润地区则因大气水汽的补充容易,降雨频繁,常陷于水患的恶性循环。此等降水在空间分布的不平均,使得水资源的分配在世界各地有极大的差异。由此可知,水资源虽可经水循环的过程而不断生成,但因降水受时间与空间的影响,无法依实际的需要在世界各地获得满足,因此水绝非是取之不尽、用之不绝的再生资源。Water, which is indispensable in human life, can be changed by its three phases of solid, liquid or gas. Water forms a circulatory system on the earth. The water vapor evaporated from the water area covering three quarters of the earth's surface is condensed and falls to the ground, which becomes the main source of water resources. Theoretically, there should be no shortage of water resources provided by these water cycle processes. However, the process of precipitation due to water vapor condensation is limited by the cooperation of meteorological conditions and cannot be controlled by humans at any time, so it is impossible to control precipitation anytime and anywhere according to needs. Therefore, once the abnormal climate causes long-term lack of rain, it will cause drought; otherwise, If the heavy rain does not stop, it will cause floods. At the same time, in dry climate areas, the atmospheric humidity is low and precipitation is not easy, which will make the drought more serious; while in humid areas, due to the easy replenishment of atmospheric water vapor and frequent rainfall, they often fall into a vicious cycle of flooding. The uneven spatial distribution of such precipitation makes the allocation of water resources very different in different parts of the world. It can be seen from this that although water resources can be continuously generated through the process of water cycle, because precipitation is affected by time and space, it cannot be met in various parts of the world according to actual needs. Therefore, water is by no means inexhaustible and inexhaustible Absolutely renewable resources.
专家预估,下半世纪地球将会增加30亿人口并且面临严重水资源短缺的问题,事实上目前已有许多国家缺乏足够的饮水,导致无法满足生活、卫生需求及粮食生产。依据全球水资源分配的调查,台湾列名全世界排名第18的缺水地区。另,预计到公元2050年,印度将会增加519(百万)人口和中国211(百万)人口。这些和其它面临水资源短缺的国家,其人口成长将迫使数百万计的人面临水枯竭的挑战。Experts predict that in the second half century, the earth will increase its population by 3 billion and face severe water shortages. In fact, many countries currently lack sufficient drinking water, resulting in the inability to meet the needs of life, sanitation and food production. According to the survey of global water resource allocation, Taiwan ranks the 18th most water-scarce region in the world. In addition, it is estimated that by 2050 AD, India will increase its population by 519 (million) and China by 211 (million). Population growth in these and other countries facing water scarcity will force millions of people to face the challenge of water depletion.
为解决部分地区水资源缺乏的困境,海水淡化的技术,近年来相当受到重视,其也是解决邻海国家缺水的不二方法。海水淡化(Desalination)技术,乃是利用能源将盐水(Saline Water)分离成两部分,一部分为含盐极低的淡水(Fresh Water),另一部分则为含高盐量的卤水(Brine),由此可达到海水淡化的目的。In order to solve the plight of lack of water resources in some areas, seawater desalination technology has received considerable attention in recent years, and it is also the only way to solve water shortage in countries adjacent to the sea. Desalination technology uses energy to separate saline water into two parts, one part is fresh water with very low salinity, and the other part is brine with high salinity. This can achieve the purpose of seawater desalination.
习知海水淡化方法之一的逆渗透法,自公元1970年代后期发展出第一座海水淡化厂以来,一直是最具竞争力的处理技术的一。逆渗透法的原理是利用半透膜中分子晶格空隙对水及盐类溶解度的差异而将其分离。在半透膜两侧分别为淡水及含盐类的溶液。依热力学定律,物质会向较低化学势能的方向移动,因盐水的化学势能较清水低,故由淡水一侧会产生渗透流,通过膜面,进入盐水溶液,直到膜两侧化学势能达到平衡为止。当两侧的压力差等于渗透压时,则达到平衡状。若在盐水一侧施以一大于渗透压的压力时,则盐水的化学势能会高于清水,而使盐水中的水份,通过膜面流向清水侧,此种现象即称为逆渗透。传统逆渗透的海水处理,虽广为应用,但其存在设备建置造价昂贵、耗材费用高、维修不易等缺点,特别是制水比率仅在1∶0.3而已,换言之有约70%的处理废水需排放回流,造成极大污染。再者,设备易被海水腐蚀,且处理后的水不符饮用水标准,是以,该种设备仍具缺失Reverse osmosis, one of the known seawater desalination methods, has been one of the most competitive treatment technologies since the first seawater desalination plant was developed in the late 1970s. The principle of reverse osmosis is to use the difference in the solubility of water and salts in the molecular lattice gaps in the semi-permeable membrane to separate them. On both sides of the semi-permeable membrane are fresh water and saline solution. According to the law of thermodynamics, substances will move to the direction of lower chemical potential energy. Because the chemical potential energy of salt water is lower than that of clear water, permeation flow will be generated from the fresh water side, pass through the membrane surface, and enter the brine solution until the chemical potential energy on both sides of the membrane reaches equilibrium. until. Equilibrium is reached when the pressure difference between the two sides is equal to the osmotic pressure. If a pressure greater than the osmotic pressure is applied to the brine side, the chemical potential energy of the brine will be higher than that of the clean water, so that the water in the brine will flow to the clean water side through the membrane surface. This phenomenon is called reverse osmosis. Although traditional reverse osmosis seawater treatment is widely used, it has disadvantages such as expensive equipment construction, high cost of consumables, and difficult maintenance. In particular, the water production ratio is only 1:0.3, in other words, about 70% of the treated wastewater It needs to be discharged back, causing great pollution. Furthermore, the equipment is easily corroded by seawater, and the treated water does not meet drinking water standards, so this equipment still has deficiencies.
另一种海水淡化主要方法之一为电透析法,电透析法是将无数的阴/阳离子薄膜,交错的串联在一起,电解质溶液则在膜间流动,两侧施以直流电电压后,阳离子将移向阴极而阴离子将移向阳极。其中阴离子可顺利通过阴离子薄膜,但是再往前时却会被邻近的阳离子膜阻挡,反之,阳离子也仅能通过阳离子膜,而无法通过阴离子膜。最后乃得以分离出低电解质浓度的溶液(淡水)以及高电解质浓度的溶液(卤水)。以电透析法进行水处理,存在设备建置造价昂贵、耗材费用高、维修不易等重大缺点。One of the main methods of seawater desalination is electrodialysis. Electrodialysis is to connect countless anion/cation membranes in series, and the electrolyte solution flows between the membranes. After DC voltage is applied to both sides, the cations will move towards the cathode while the anions will move towards the anode. Among them, anions can pass through the anion membrane smoothly, but they will be blocked by the adjacent cationic membrane when they go forward. Conversely, cations can only pass through the cationic membrane, but cannot pass through the anionic membrane. Finally, a solution with low electrolyte concentration (fresh water) and a solution with high electrolyte concentration (brine) can be separated. Water treatment by electrodialysis has major disadvantages such as expensive equipment construction, high cost of consumables, and difficult maintenance.
至于其它的海水淡化方法,例如多级闪化法、蒸馏压缩法、多效蒸馏法、冷冻法、太阳能蒸馏法、水合物法、溶剂萃取法……等,普遍存在诸多不利于实施或应用的缺失。As for other seawater desalination methods, such as multi-stage flashing method, distillation compression method, multi-effect distillation method, freezing method, solar distillation method, hydrate method, solvent extraction method, etc., there are many disadvantages that are not conducive to implementation or application. missing.
实用新型内容:Utility model content:
本实用新型主要目的在于提供一种可付诸实现与应用的海水淡化处理设备。The main purpose of the utility model is to provide a seawater desalination treatment equipment that can be put into practice and application.
本实用新型的水质处理设备,包括有振荡蒸馏装置与冷却装置,其中:该振荡蒸馏装置,在一桶体设置有入水管,该桶体内部设置有加可以产生热能的热组件与磁石振荡组件;该磁石振荡组件,为取材自矿石且经人造加工过的磁石结构;该桶体顶部设置有蒸气排出口,且桶体底部设置有泄水管;该蒸气排出口,利用管路连接到冷却装置;该冷却装置,为一将蒸气冷却后变化成水并输出的桶体。The water quality treatment equipment of the present utility model includes an oscillating distillation device and a cooling device, wherein: the oscillating distillation device is provided with a water inlet pipe in a barrel body, and a heat component and a magnet oscillating component that can generate heat energy are arranged inside the barrel body The magnet oscillating component is a magnet structure obtained from ore and artificially processed; the top of the barrel is provided with a steam outlet, and the bottom of the barrel is provided with a drain pipe; the steam outlet is connected to the cooling device by a pipeline ; The cooling device is a barrel that cools the steam and changes it into water and outputs it.
其中,该冷却装置的桶体,顶部设置有喷雾器,该喷雾器顶部与管路连通。Wherein, the barrel body of the cooling device is provided with a sprayer on the top, and the top of the sprayer is communicated with the pipeline.
其中,该冷却装置,包括一冷却水入口,其分支有第一管体与第二管体,其中的第一管体,自桶体顶部进入,连接至顶端冷却循环单元,该顶端冷却循环单元呈绕圈方式设置于桶体顶部,依次连接至一输水管、一侧壁冷却循环单元、另一输水管及一排水管;该第二管体,连通至悬置冷却循环单元,其呈绕圈方式设置于桶体中间,该悬置冷却循环单元连接有导水管连通至贮水室,该贮水室位于悬置冷却循环单元下方,又贮水室设有溢流管,溢流管顶部的开口恰位于贮水室内,溢流管末端另与排水管连接;另于贮水室外围区隔有导水室,且连通有一饮用水排出口。Wherein, the cooling device includes a cooling water inlet, which is branched into a first pipe body and a second pipe body, wherein the first pipe body enters from the top of the barrel and is connected to the top cooling circulation unit, and the top cooling circulation unit It is arranged on the top of the barrel body in a coiled manner, and is connected to a water delivery pipe, a cooling circulation unit on the side wall, another water delivery pipe and a drainage pipe in turn; The ring is arranged in the middle of the barrel body. The suspended cooling circulation unit is connected with a water guide pipe to the water storage room. The opening of the water storage room is just located in the water storage room, and the end of the overflow pipe is connected with the drain pipe; in addition, a water guide room is separated from the water storage room, and is connected with a drinking water outlet.
其中,该磁石振荡组件,是将磁石包覆于一表面具有若干孔洞的壳体内。Wherein, the magnet oscillating component wraps the magnet in a casing with several holes on the surface.
其中,该冷却装置,包括有第一进水口、顶端冷却循环单元、导流组件、侧壁冷却循环单元及第一出水口组成的冷却水流通路线;另,该冷却装置中还包括有第二进水口、悬置冷却循环单元、导水管及第二排水口组成的水流循环;又该冷却装置还包括有第三进水口、底端冷却循环单元及第三排水口组成的水流循环。Wherein, the cooling device includes a cooling water circulation path composed of a first water inlet, a top cooling circulation unit, a flow guide assembly, a side wall cooling circulation unit and a first water outlet; in addition, the cooling device also includes a second A water flow cycle composed of a water inlet, a suspended cooling circulation unit, a water guide pipe and a second water outlet; and the cooling device also includes a water flow cycle composed of a third water inlet, a bottom cooling cycle unit and a third water outlet.
其中,该导流组件呈螺旋状设于侧壁冷却循环单元内。Wherein, the flow guide assembly is spirally arranged in the side wall cooling circulation unit.
采用以上方案的水质处理设备,振荡蒸馏装置中包括有加热组件与磁石振荡组件,利用加热与蒸馏方式配合特殊的磁石振荡过滤,可取得去除盐份与杂质的纯净水,续经冷却装置降温处理后,即可获得过滤淡化后的饮用水,借以达到海水淡化、解决水荒等主要目的。The water quality treatment equipment adopting the above scheme, the oscillating distillation device includes a heating component and a magnet oscillating component, and the heating and distillation method is combined with a special magnet oscillating filter to obtain pure water that removes salt and impurities, and continues to be cooled by the cooling device. After that, the filtered and desalinated drinking water can be obtained, so as to achieve the main purpose of seawater desalination and solve water shortage.
本实用新型具体存在的优点为:处理后的水质佳,且具有高制水比率(约为1∶0.93),且建置与维护成本低,保养容易,极具利用和实施价值。The specific advantages of the utility model are: good water quality after treatment, high water production ratio (about 1:0.93), low construction and maintenance costs, easy maintenance, and great utilization and implementation value.
附图说明:Description of drawings:
图1:为本实用新型的剖面示意图。Fig. 1: is the sectional schematic view of the utility model.
图2:为本实用新型中冷却装置的剖面结构示意图。Fig. 2: is the schematic cross-sectional structure diagram of the cooling device in the utility model.
图3:为本实用新型中冷却装置的立体剖面结构示意图。Fig. 3: is the three-dimensional cross-sectional structural schematic diagram of the cooling device in the utility model.
图4:为本实用新型中冷却装置的顶视结构示意图。Fig. 4: It is a top view structural diagram of the cooling device in the utility model.
图5:为本实用新型的使用状态示意图。Fig. 5: It is a schematic diagram of the use state of the utility model.
图6:为本实用新型中磁石振荡组件的立体外观图。Fig. 6: It is the three-dimensional appearance diagram of the magnet oscillating assembly in the utility model.
图7:为本实用新型中磁石振荡组件的剖面结构图。Fig. 7: It is the cross-sectional structure diagram of the magnet oscillation assembly in the utility model.
图8:为本实用新型中冷却装置另一实施例的立体剖面图。Fig. 8: is a three-dimensional cross-sectional view of another embodiment of the cooling device in the present invention.
图9:为本实用新型中冷却装置另一实施例的剖面图。Fig. 9: is a sectional view of another embodiment of the cooling device in the present invention.
图中主要组件符号说明:Explanation of main component symbols in the figure:
1----振荡蒸馏装置,10---桶体,11---入水管,12---加热组件,13---磁石振荡组件,131--磁石,132--孔洞,133--壳体,14---蒸气排出口,15---泄水管,21---管路,3----冷却装置,30---桶体,31---喷雾器,38---导水室,39---饮用水排出口,4----冷却水入口,41---排水管,51---第一管体,52---顶端冷却循环单元,53---输水管,54---侧壁冷却循环单元,55---输水管,61---第二管体,62---悬置冷却循环单元,63---导水管,64---贮水室,65---溢流管,7----冷却装置,71---第一进水口,72---顶端冷却循环单元,73---导流组件,74---侧壁冷却循环单元,75---第一出水口,76---第二进水口,77---悬置冷却循环单元,78---导水管,79---第二排水口,81---第三进水口,82---底端冷却循环单元,83---第三排水口。1----oscillating distillation device, 10---barrel body, 11---water inlet pipe, 12---heating component, 13---magnet oscillating component, 131-magnet, 132-hole, 133- -Housing, 14---steam outlet, 15---drain pipe, 21---pipeline, 3---cooling device, 30---barrel, 31---sprayer, 38- -Water guide chamber, 39---drinking water outlet, 4---cooling water inlet, 41---drainage pipe, 51---first pipe body, 52---top cooling circulation unit, 53- --Water delivery pipe, 54---Side wall cooling circulation unit, 55---Water delivery pipe, 61---Second pipe body, 62---Suspension cooling circulation unit, 63---Water guide pipe, 64- --Water storage chamber, 65---overflow pipe, 7----cooling device, 71---first water inlet, 72---top cooling circulation unit, 73---flow guide assembly, 74- --Side wall cooling circulation unit, 75---first water outlet, 76---second water inlet, 77---suspension cooling circulation unit, 78---water guide pipe, 79---second drainage Port, 81---the third water inlet, 82---the bottom cooling circulation unit, 83---the third drain.
具体实施方式:Detailed ways:
兹谨就本实用新型水质处理设备的详细内容,及其所产生的功效,配合附图,举一较佳实施例说明如下。Hereby, with regard to the detailed content of the water quality treatment equipment of the present invention, and the effects thereof, together with the accompanying drawings, a preferred embodiment is described as follows.
首请参阅图1、图2、图3与图4所示,本实用新型水质处理设备,主要包括有振荡蒸馏装置1与冷却装置3,其中:Please refer to Fig. 1, Fig. 2, Fig. 3 and Fig. 4. The water quality treatment equipment of the present utility model mainly includes an oscillating distillation device 1 and a
该振荡蒸馏装置1,包括一可容置液体的桶体10,适当处设置有入水管11,该桶体10内部设置有加热组件12与磁石振荡组件13,该加热组件12可以产生热能,当桶体10内存在水时,可就水进行升温加热的作用;至于该磁石振荡组件13(如图6与图7),是为一取材自矿石且经人造加工过的磁石结构,其具有将水中的金属分子与有毒物质吸附过滤的作用。该磁石131可以是被包覆于一表面具有若干孔洞132的壳体133内,该孔洞132可提供水的出、入,且磁石131本身具有细小的毛细孔,亦可提供水分子流通,同时并拦阻水中的金属分子与有毒物质;前述桶体10顶部设置有蒸气排出口14,且桶体10底部设置有泄水管15,具体来说,泄水管15可用以排出卤水。The oscillating distillation device 1 includes a
前述蒸气排出口14,利用一管路21连接到冷却装置3,该冷却装置3,包括一桶体30,顶部设置有喷雾器31,该喷雾器31顶部与管路21连通,为使冷却装置3获致良好的冷却效果,该桶体30采循环式水冷方式进行冷却。包括一冷却水入口4,其分支有第一管体51与第二管体61,其中的第一管体51,自桶体30顶部进入,连接至顶端冷却循环单元52,该顶端冷却循环单元52呈绕圈方式设置于桶体30顶部,而后连接至输水管53,再连接至侧壁冷却循环单元54,而后经输水管55最后由排水管41输出;至于第二管体61,连通至悬置冷却循环单元62,其呈绕圈方式设置于桶体30中间适当处,特别是喷雾器31下方,该悬置冷却循环单元62连接有导水管63,可连通至贮水室64,该贮水室64位于悬置冷却循环单元62下方,又贮水室64适当处设有溢流管65,溢流管65顶部的开口恰位于贮水室64内,溢流管65末端另与排水管41连接;另于贮水室64外围区隔有导水室38,且连通有一饮用水排出口39。前述冷却水入口4内,可流通有冷却用的水、气态氮气或液态氮。
本实用新型实施时,如图5,将海水自入水管11导入桶体10内,令加热组件12启动产生热能并就海水进行蒸馏,海水于桶体10内因温度变化不断翻搅,往复流通于磁石振荡组件13间,利用磁石振荡组件13可将水分子分解至最小,并破坏分解过滤出有毒物质与重金属并留存于磁石振荡组件13处,至于被加热达到沸点的水转变形成蒸气并上升,经通过蒸气排出口14、管路21来到冷却装置3,经由喷雾器31向桶体30内喷出蒸气,该蒸气可附着于桶体30内各处壁面,经环围的冷却降温后,蒸气转变成液态水,引流至导水室38并由饮用水排出口39送出,此时的排出水,已完成处理而可直接饮用。When the utility model is implemented, as shown in Figure 5, the seawater is introduced into the
前述冷却水,当由冷却水入口4进入第一管体51后,经顶端冷却循环单元52、输水管53、侧壁冷却循环单元54、输水管55而由排水管41输出;另一回路的冷却水,由第二管体61、悬置冷却循环单元62、导水管63流至贮水室64,当贮水室64内的冷却水水位高过溢流管65,方由溢流管65流出至排水管41。显见,本实用新型的冷却系统,三百六十度环设于整个桶体30内,具有绝佳的冷却效果与效率。The aforementioned cooling water, after entering the
由于本实用新型的磁石振荡组件13可将水分子分解至最小,并将分解过滤出的有毒物质与重金属留存于磁石振荡组件13间,因此,维护时只需将磁石振荡组件13取出,以高周波或其它方式进行去除杂质的程序即可,相当方便、容易且低成本。Since the
本实用新型除可应用于海水的淡化外,污水等各式水质的处理皆属本实用新型可应用与保护的范围。In addition to being applicable to the desalination of sea water, the utility model can also be used for the treatment of various water quality such as sewage, etc., all belong to the scope of application and protection of the utility model.
前述设备中,冷却装置3可相对于振荡蒸馏装置1适当形成有一负压,使致该冷却装置3可相对于振荡蒸馏装置1具有吸取的作用。In the aforementioned equipment, the
再请参阅图8与图9,为本实用新型冷却装置7的另一实施例,该结构中包括有第一进水口71、顶端冷却循环单元72、导流组件73、侧壁冷却循环单元74及第一出水口75,其可形成一冷却水的流通路线,其中,该侧壁冷却循环单元74中的螺旋状导流组件73,可导引水流环绕冷却装置7并朝向第一出水口75流通;另,该冷却装置7中还包括有第二进水口76、悬置冷却循环单元77、导水管78及第二排水口79,其间可形成水流循环;又该冷却装置7还包括有第三进水口81、底端冷却循环单元82及第三排水口83,其间可形成水流循环;藉此,该冷却装置7四周完全遍设有冷却水流通,本实施例相较于前一实施例,具有更完善的冷却效用。Please refer to Fig. 8 and Fig. 9 again, it is another embodiment of the cooling device 7 of the present invention, the structure includes a first water inlet 71, a top cooling circulation unit 72, a guide assembly 73, and a side wall cooling circulation unit 74 And the first water outlet 75, which can form a cooling water flow path, wherein, the spiral guide assembly 73 in the side wall cooling circulation unit 74 can guide the water flow around the cooling device 7 and toward the first water outlet 75 In addition, the cooling device 7 also includes a second water inlet 76, a suspension cooling circulation unit 77, a water conduit 78 and a second drain 79, and water circulation can be formed therebetween; and the cooling device 7 also includes a second Three water inlets 81, a bottom cooling circulation unit 82 and a third water outlet 83 can form water circulation among them; thereby, the cooling device 7 is completely provided with cooling water circulation all around. Compared with the previous embodiment, this embodiment , with a more complete cooling effect.
综上所述,本实用新型水质处理设备,虽通过前述实施例来描述,但仍可变化其形态与细节,在不脱离本实用新型的精神下达成。前述较佳实施例,仅是本实用新型可以具体实施的方式之一,但并不以此为限制。To sum up, although the water quality treatment equipment of the present utility model is described by the foregoing embodiments, its shape and details can still be changed without departing from the spirit of the present utility model. The foregoing preferred embodiment is only one of the ways in which the utility model can be specifically implemented, but it is not limited thereto.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200620118542XU CN2926193Y (en) | 2006-06-06 | 2006-06-06 | Water treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200620118542XU CN2926193Y (en) | 2006-06-06 | 2006-06-06 | Water treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2926193Y true CN2926193Y (en) | 2007-07-25 |
Family
ID=38280433
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU200620118542XU Expired - Fee Related CN2926193Y (en) | 2006-06-06 | 2006-06-06 | Water treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2926193Y (en) |
-
2006
- 2006-06-06 CN CNU200620118542XU patent/CN2926193Y/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103304088B (en) | Recycling method of high brine waste water based on forward osmosis | |
| CN100591628C (en) | Seawater desalination and inferior water purification device and method | |
| KR20150099590A (en) | Seawater desalting apparatus and method using solar energy for continuously supplying heat | |
| US8273156B2 (en) | Method and apparatus for water distillation and recovery | |
| CN103253722B (en) | Plate type low-temperature multieffect seawater desalting device and method | |
| CN108328831A (en) | A kind of method for concentration and equipment of reverse osmosis concentrated brine | |
| CN103663589B (en) | Seawater desalinization method and seawater desalinization device | |
| CN113443788B (en) | Solar energy coupling heat pump contain salt effluent disposal system | |
| Belessiotis | Delyannis | |
| Chandwankar et al. | Thermal processes for seawater desalination: Multi-effect distillation, thermal vapor compression, mechanical vapor compression, and multistage flash | |
| CN104445761A (en) | Energy-saving seawater purification equipment | |
| CN2926193Y (en) | Water treatment equipment | |
| CN207608448U (en) | Utilize the seawater desalination system of power station thermal energy production and living water | |
| CN104843922A (en) | Low-temperature evaporative type high-salt wastewater treatment device using wastewater waste heat | |
| CN204644039U (en) | Utilize the low-temperature evaporation formula high slat-containing wastewater treatment unit of waste water residual heat | |
| JP2003126841A (en) | Desalination plant with solar thermal energy utilization | |
| CN203582533U (en) | Sea water desalting device | |
| CN101205086A (en) | Seawater Desalination Concentrated Brine Vacuum Membrane Distillation Process | |
| WO2008049280A1 (en) | A water quality treating equipment | |
| CN205873941U (en) | Wave power oscillating type solar -powered seawater desalination device | |
| CN204849897U (en) | Superconductive strong effect water extraction from air machine | |
| US20080011598A1 (en) | Freshwater Recycling System | |
| Tyagi et al. | Model-based zero liquid discharge desalination for land-locked arid/semi-arid regions in India | |
| RU2553880C2 (en) | Sea water desalination unit and process | |
| WO2013134901A1 (en) | Sea water desalination processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070725 |