WO2003011765A1 - An ultra-efficient vaporizer for desalinating seawater instantaneously - Google Patents
An ultra-efficient vaporizer for desalinating seawater instantaneously Download PDFInfo
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- WO2003011765A1 WO2003011765A1 PCT/CN2002/000535 CN0200535W WO03011765A1 WO 2003011765 A1 WO2003011765 A1 WO 2003011765A1 CN 0200535 W CN0200535 W CN 0200535W WO 03011765 A1 WO03011765 A1 WO 03011765A1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/06—Flash evaporation
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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
Definitions
- the present invention relates to ultra-high-speed desalination of seawater and rapid salt-making of seawater and rapid waste water and sewage treatment, especially by high-pressure vessels, high-pressure gas, liquid conduits, nozzles, blasting discs, liquid-contact hood disks, blasting vaporization greenhouses, and high-temperature water vapor.
- Ultra-efficient seawater desalination instantaneous vaporization device consisting of discharge port, valve and so on.
- phase change 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
- flash distillation which accounts for about 70% of the total seawater desalination output in the world today.
- the flash distillation method uses the characteristic that the boiling point of water decreases as the pressure decreases. First, the seawater is heated in a pipe, and then introduced into an evaporation chamber with a lower pressure. The introduced high-temperature seawater will evaporate quickly.
- the fresh steam was caused by cold steam outside the pipeline containing cold seawater.
- Repeated multi-segment flash distillation is required. At present, it has reached the need to repeatedly repeat multiple flash-distillation operations for more than 30 knots / times. The equipment is huge and the efficiency is low). Its disadvantages are: high equipment investment, large seawater circulation, small water production, low concentration rate and high operating costs. (It requires a large amount of seawater production, only about 1 part of fresh water is produced, but about 9 parts of polluted thick seawater are produced). Summary of the Invention
- the purpose of the present invention is to provide an ultra-efficient instant seawater desalination vaporization device, which has a simple structure, very little investment, large batches of produced water, stable performance, small volume, small scale, convenient use, fast water production, high freshwater output, The water quality is good (produces about 90% of fresh water and only about 10% of concentrated brine).
- the solution of the present invention is to use the characteristic that salt molecules in seawater do not participate in the evaporation and vaporization process, and the high-pressure gas explosion vaporization method is used:
- the high-pressure gas compresses the high-temperature and high-pressure detonation water droplets, and the instantaneous decompression, rapid expansion, blasting and ultra-high-speed evaporation and vaporization mechanisms.
- the huge compressed gas shock waves formed by the gas stream have a strong and sharp impact. Segmentation, enveloping, high-speed blasting, omnidirectional three-dimensional ultra-high-speed evaporation and vaporization of seawater water liquid droplets.
- the mixed vapor-liquid of high-temperature, high-pressure, and ultra-high-density dissolved gas first causes strong high-pressure compression, and then the high-temperature and high-pressure detonated water liquid is instantly decompressed and rapidly expanded to burst and vaporize, so that the droplets of the ultra-high-density dissolved gas instantly have severe mechanical instability.
- Freshwater molecular water liquids form ultra-high-density fine-particle suspension droplet vapor-liquid mixtures with the smallest particles after ultra-high-speed evaporation and vaporization; salt molecular aqueous liquids are not easily vaporized by high-temperature and high-pressure evaporation to form concentrated brine with the largest particle droplets; After changing the operation mode, they are separated and isolated in an instant, so as to achieve the purpose of seawater desalination at the moment of ultra-high-speed vaporization.
- An ultra-efficient instant seawater desalination vaporization device a heater is installed or not installed in a high-pressure vessel injected with pretreated seawater, and a liquid pipe, an air pipe or no Place the air pipe, nozzle, and explosive plate; can put or not put the appropriate amount of environmentally friendly explosives, igniters, pressure-resistant box lids, high-pressure containers are provided with connecting fluid guide tubes, air pipes, nozzles, and connected to place explosive plates ;
- the high pressure vessel is provided with a Unicom water inlet valve or not without a water inlet valve, an air inlet valve connected to a Unicom low pressure gas storage tank, an medium pressure gas storage tank inlet valve, a high pressure gas storage tank inlet valve, or Set up a ceramic door for compressed gas inlet; set a single-layer or double-layer or multi-layer detonation vaporization greenhouse on the high-pressure vessel; connect a multilayer high-temperature filter in the detonation vaporization greenhouse; In the det
- the working process of the ultra-efficient seawater desalination instant vaporization device is:
- High-pressure compressed gas, high-temperature and high-pressure detonation of water droplets, instantaneous decompression and rapid expansion High-speed evaporation and vaporization: first place heaters, liquid tubes, air tubes or no air tubes and nozzles in the high-pressure container; appropriate environmental explosives, igniters, pressure-resistant box covers, and explosive plates can be used Open the water inlet valve to inject pre-treated seawater, and close the water inlet valve when the water inlet level in the high-pressure vessel reaches a certain level; then open and close each one separately: the inlet valve of the low-pressure gas storage tank, the medium-pressure gas storage tank Intake valve, inlet valve of high-pressure gas storage tank or an inlet valve provided with compressed gas; when the inlet pressure of the high-pressure container reaches the required working pressure, the inlet of the high-pressure gas storage tank can be closed.
- the air valve or the intake valve closing the compressed gas stops gas injection. Turn on the heater to heat or not install or install the heater. After the high-pressure ultra-high-density dissolved seawater water solution is heated to a certain high temperature, turn off the heater to stop heating.
- An environmentally friendly explosive can be detonated using a igniter to ignite a directional explosion in high-temperature and high-pressure seawater.
- the vapor and liquid of the high-pressure high-speed jet are ejected from the liquid pipe, the air pipe, and the nozzle, forming a secondary explosion at the same time.
- the fresh water molecules in the seawater that is, the huge energy released after the explosion and detonation, generate a large amount of high-temperature, high-pressure, and high-speed shock wave airflows. They were exploded by high-speed impact collisions in the space of the detonation and vaporization greenhouse, and were strongly decomposed into fog liquid. The state of the material changes, and the ultra-high-speed evaporation vaporizes into a vapor-liquid mixture.
- the multi-layer high-temperature filter can be turned on before the explosion of environmentally friendly explosives, or the multi-layer high-temperature filter is not installed.
- the fresh water outlet valve and the concentrated brine outlet valve and the distilled water outlet water can be opened. valve.
- the seawater vapor and liquid are ejected from the nozzles of the liquid pipe and the air pipe after being impacted by the high-temperature, high-pressure, and high-speed shock wave giant airflow, and they are atomized in a conical expansion jet with a continuous bifurcation structure.
- the fractal characteristics of the droplet size during the atomization process have a probability that the droplet splitting obeys a uniform distribution.
- the liquid droplets collide with the high-speed gas-liquid shock wave (shock wave) gas, the liquid droplets are deformed and the surface is peeled until they are completely broken.
- shock wave gas-liquid shock wave
- the salt molecular water liquid is not easy to be evaporated and vaporized by high temperature and pressure to form the largest particle droplets.
- the concentrated brine is washed into the multi-layer high-temperature filter. After being blocked by the plate wall of the liquid hood, the liquid flows down the surface of the plate and accumulates from the concentrated brine.
- Freshwater molecules in the seawater are vaporized by ultra-high-speed evaporation to form ultra-high-density fine-particle suspension droplets and liquid-liquid mixtures with the smallest particles, which are sharply ejected.
- the automatic pressure relief window can automatically and quickly discharge the excess gas under pressure or there is no automatic pressure relief window.
- Fresh water vapor is formed by rapid cooling and cold condensation in the degassing greenhouse, and then is formed into fresh water, which is output from the fresh water outlet pipe.
- High pressure gas explosion vaporization method is: high pressure compressed gas explosion at high temperature and high pressure, the liquid droplets are decompressed quickly and rapidly expanded and exploded and ultra-high speed evaporation vaporizer 0535, after the seawater liquid is released by the explosion, it releases a huge amount of energy to generate a large amount of high temperature, high pressure, high-speed shock wave airflow, strong impact, segmentation, enclosing, blasting, and decomposition of seawater.
- a sudden ultra-high-speed evaporation and vaporization occurred within an instant to form an ultra-high density fine particle suspension droplet vapor-liquid mixture with the smallest particle point. The distance between the molecules increased dramatically by many times, and the volume rapidly increased by many times.
- FIG. 1 is a schematic diagram of the working principle of a detonation vaporization cooling system for the continuity of a super-efficient seawater desalination instantaneous vaporization device according to an embodiment of the present invention.
- Figure 2 is a schematic diagram of the working principle of the high-pressure compressed gas high-temperature and high-pressure detonation water droplets of the ultra-efficient seawater desalination instantaneous vaporization device according to the embodiment of the present invention.
- the ultra-efficient instant seawater desalination device of the present invention is mainly composed of two large components.
- High pressure vessel 3 On the high-pressure container 3 is connected to connect the communication catheter 8, the air pipe 9, the nozzle 10, and the connection is arranged to place the explosive disc 11;
- High pressure vessel 3 is equipped with a Unicom water inlet valve 12 or no water inlet valve 12 is installed outside the body, an air inlet valve 13 connected to a Unicom low pressure gas storage tank 13 is installed, a wide air inlet door 14 for a medium pressure gas storage tank, and a high pressure gas storage tank Inlet valve 15 or pressurized gas inlet valve 15 is provided;
- On the high-pressure vessel 3 On the high-pressure vessel 3, a single-layer or double-layer or multi-layer detonation vaporization greenhouse 2 is provided, and a multi-layer high-temperature filter is installed in the detonation vaporization greenhouse 2 16 or no multi-layer high-temperature filter 16 is not installed, the multi-layer high-temperature filter 16 is provided on the periphery of the connecting liquid-disc cover plate 17 and is connected to the concentrated brine outlet valve 21 or is
- the automatic pressure relief window 18 is not installed and connected with the Unicom freshwater outlet valve 22 or the freshwater outlet valve 22 is not provided.
- Single or multiple high-temperature water vapor outlets 19 are connected to the automatic pressure relief window 20 or are not provided without automatic pressure relief window 20 and connected to the connected distilled water outlet valve 23 or are not provided without steam Distilled water outlet valve 23.
- High-pressure compressed gas, high-temperature and high-pressure detonation of water, instantaneous decompression, rapid expansion, blasting, ultra-high-speed evaporation and vaporization Install heater 4 or no heater 4, fluid guide tube 8, air guide tube 9 or not Place the air guide tube 9, the nozzle 10, (the appropriate amount of environmentally friendly explosives 5, the igniter 6, and the pressure-resistant box cover 7 can be placed or not.) Place the explosive disc 11. Open the seawater inlet valve 12 or leave the water inlet valve 12 closed.
- the igniter 6 can be turned on to detonate the environmentally friendly explosive 5 in a high-temperature and high-pressure seawater to produce a high-pressure and high-pressure compressed gas explosion.
- the environmentally-friendly explosive 5 can be used to generate a large amount of high-pressure compressed gas to detonate the high-pressure container 3.
- Explosive detonation can also be used directly.
- the ultra-high-pressure compressed gas detonated the high-pressure vessel 3 and exploded.
- the water liquid was instantly decompressed and rapidly expanded and exploded.
- the upper mouth of the nozzle 10 ejects, forming a secondary explosion at the same time. Due to the huge explosive energy caused by the explosion of explosive 5, the high-temperature and high-density dissolved gas in the high-temperature and high-pressure mixed vapor-liquid liquid water and salt molecular water, that is, the huge energy released after the explosion detonation produced a large amount of energy.
- the high-temperature, high-pressure, and high-speed shock wave airflow is violently blasted by high-speed impact in the space of the detonation vaporization greenhouse 2 to form an ultra-high density mist.
- Freshwater molecular water liquid is strongly and sharply decomposed and suddenly changes its physical state. After ultra-high-speed evaporation and vaporization, it forms vapor-liquid, forming ultra-high-density fine particle suspension droplets with minimal particle size.
- the vapor-liquid mixture expands and diffuses at high speed; salt molecular water is not easy Evaporated and vaporized by high temperature and high pressure. After being impacted, the concentrated salt solution with the largest particle size will be subjected to the largest impact force and the fastest operating speed.
- salt molecules are not easy to be high High-temperature, high-pressure, evaporation and vaporization to form the largest particles of droplets of concentrated brine and sprayed into the multilayer high-temperature filter 16 at high speed or without the multilayer high-temperature filter 16 and then blocked by the wall of the liquid-shielding plate 17
- the wall surface flows down and is accumulated and discharged from the outlet pipe of the concentrated brine discharge valve 21; the fresh water molecular water in the high-temperature and high-pressure mixed vapor-liquid is strongly and rapidly expanded and exploded. After ultra-high-speed evaporation and vaporization, an ultra-high minimum particle is formed.
- the vapor-liquid mixture of fine particle suspension droplets After being ejected, the vapor-liquid mixture of fine particle suspension droplets swells rapidly and diffuses rapidly, and encounters a large amount of high-temperature gas generated in the multi-layer high-temperature filter screen 16. After being blocked by the high temperature, it further vaporizes and expands rapidly and diffuses rapidly around it. Ascent, that is, the detour continues to ascend from the periphery of the wetted disc 17.
- the high-temperature mixed vapor can turn around and go up because the high-temperature water vapor is lighter than air and has its own rising kinetic energy. After the high-temperature and high-pressure detonation, fresh water molecular droplets and salt molecular droplets in the high-temperature mixed vapor can be converted into Running in different directions of operation, achieve the purpose of instantaneous separation and isolation.) At this time, the automatic pressure relief window 18 or the automatic pressure relief window 18 is not installed will automatically and timely discharge excess pressurized gas.) After being rapidly cooled and condensed and accumulated by the detonation vaporization greenhouse 2, a fresh water liquid is formed and output from the fresh water outlet valve 22; in addition, most of the high-temperature water vapor rises from the single or multiple high-temperature water vapor discharge ports 19 and enters the upper layer of detonation.
- Vaporization greenhouse 2 the excess pressure gas is discharged from the automatic pressure relief window 20 or the automatic pressure relief window 20 is not installed, and the high-temperature water vapor is rapidly cooled and condensed to form a distilled water liquid after the upper detonation vaporization greenhouse 2
- the water outlet valve 23 is discharged from the pipeline.
- the single-disc or multi-disc rotary shaft seat 1 of the continuous detonation and vaporization cooling system of the high-pressure vessel 3 is a continuous detonation vaporization and cooling combined system.
- the high-efficiency working capacity of the detonation and vaporization cooling can continuously meet the continuous continuity of the high-pressure vessel 3. Explosion. So it goes on and on.
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Abstract
Description
超高效海水淡化瞬间汽化装置 技术领域 TECHNICAL FIELD
本发明涉及海水超高速淡化和海水快速制盐及快速废水污水处 理, 尤其是由高压容器、 高压气体、 导液管、 喷嘴、 放爆片、 接液罩 盘、 放爆汽化大棚、 高温水蒸气排放口、 阀门等组成的超高效海水淡 化瞬间汽化装置。 The present invention relates to ultra-high-speed desalination of seawater and rapid salt-making of seawater and rapid waste water and sewage treatment, especially by high-pressure vessels, high-pressure gas, liquid conduits, nozzles, blasting discs, liquid-contact hood disks, blasting vaporization greenhouses, and high-temperature water vapor. Ultra-efficient seawater desalination instantaneous vaporization device consisting of discharge port, valve and so on.
技术背景 technical background
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, 产生的蒸气在装有冷海水的管道外得到 冷疑而造成淡水。 (需要进行重复多节闪馏, 目前已达需要反反复复重 复闪馏操作三十多节 /次, 设备庞大效率较低)。 其缺点是: 设备投资 多, 海水循环量大、 制水量小、 浓缩率较低操作费用较高。 (需要大批 量的海水制作, 只得约 1份淡水, 却要产生约 9份有污染的浓海水)。 发明内容 At present, there are many domestic and foreign seawater desalination methods. Phase change 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 There are three main types. At present, the technology that is leading and also the most widely used is flash distillation, which accounts for about 70% of the total seawater desalination output in the world today. The flash distillation method uses the characteristic that the boiling point of water decreases as the pressure decreases. First, the seawater is heated in a pipe, and then introduced into an evaporation chamber with a lower pressure. The introduced high-temperature seawater will evaporate quickly. The fresh steam was caused by cold steam outside the pipeline containing cold seawater. (Repeated multi-segment flash distillation is required. At present, it has reached the need to repeatedly repeat multiple flash-distillation operations for more than 30 knots / times. The equipment is huge and the efficiency is low). Its disadvantages are: high equipment investment, large seawater circulation, small water production, low concentration rate and high operating costs. (It requires a large amount of seawater production, only about 1 part of fresh water is produced, but about 9 parts of polluted thick seawater are produced). Summary of the Invention
本发明的目的是提供一种超高效海水淡化瞬间汽化装置, 其结构 简单、 投资非常少、 产水批量大、 性能稳定、 体积小、 水垢少、 使用 方便、 制水特快、 出淡水产量高、 水质好 (可产生约 90%的淡水, 只 产生约 10%的浓盐水)。 The purpose of the present invention is to provide an ultra-efficient instant seawater desalination vaporization device, which has a simple structure, very little investment, large batches of produced water, stable performance, small volume, small scale, convenient use, fast water production, high freshwater output, The water quality is good (produces about 90% of fresh water and only about 10% of concentrated brine).
为了达到上述目的, 本发明的解决方案是: 利用海水中的盐类分 子均不参与蒸发汽化过程的这一特性, 采用高压气体爆碎汽化法即: 高压气体压缩高温高压放爆水液液滴瞬间减压快速膨胀爆碎超高速蒸 发汽化机理。 或采用环保炸药爆炸产生压缩气体引爆高压容器放爆, 使海水中的淡水分子水液在高温高压放爆后液滴强烈急剧爆碎超高速 蒸发汽化形成汽液混合体, 最大限度地扩大淡水分子与盐类分子之间 的间距离、 水液体积 (所有的淡水分子水液液滴的体积爆碎后扩大了 约数十倍至数百倍以上)、 密度差距和运行速度。 瞬间内分离出并隔离 出不同运行方式的汽与液, 经快速冷却冷凝形成淡水和浓盐水及蒸馏 水, 达到超高速汽化瞬间海水淡化的目的。 In order to achieve the above object, the solution of the present invention is to use the characteristic that salt molecules in seawater do not participate in the evaporation and vaporization process, and the high-pressure gas explosion vaporization method is used: The high-pressure gas compresses the high-temperature and high-pressure detonation water droplets, and the instantaneous decompression, rapid expansion, blasting and ultra-high-speed evaporation and vaporization mechanisms. Or the use of environmentally friendly explosives to produce compressed gas to detonate the high-pressure container to detonate, so that the freshwater molecules in the seawater are strongly and sharply blasted after the high-temperature and high-pressure detonation, and the ultra-high-speed evaporation is vaporized to form a vapor-liquid mixture, which maximizes the freshwater molecules. The distance to the salt molecules, the volume of the water liquid (the volume of all the fresh water molecules and the size of the liquid droplets expands by about tens to hundreds of times after explosion), the density gap and the running speed. Vapor and liquid in different operating modes are separated and isolated in an instant, and fresh water and concentrated brine and distilled water are formed by rapid cooling and condensation to achieve the purpose of ultra-high-speed instantaneous seawater desalination.
海水在高温中淡水分子水液容易挥发, 比重、 间距离变化较大; 盐类分子水液不易挥发, 比重、 间距离变化较小。 若采用环保炸药在 高温高压海水中定向爆炸放爆, (海水在高温沸腾中, 淡水分子水液容 易被高温蒸发汽化是由于含有较多的易挥发组分, 所以随着温度的升 高淡水分子水液的体积和比重变化非常大; 盐类分子水液不易被高温 蒸发汽化是由于含有较多的难挥发组分, 所以随着温度的升高盐类分 子水液的体积和比重变化非常小。)海水水液液滴在被高温高压爆炸放 爆后释放出巨大能量产生大量的高温、 高压、 高速冲击波 (激波) 气 流所形成的巨大的压缩气体冲击激波爆碎动能强烈急剧冲击、 分割、 包围、 高速爆碎、 全方位立体超高速蒸发汽化分解海水水液液滴。 让 高温高压超高密度溶气的混合汽液先引起强烈高压压缩, 然后高温高 压放爆水液瞬间减压快速膨胀爆碎汽化, 使超高密度溶气的液滴瞬间 内产生了严重力学不平衡, 液滴体积强烈急剧高速膨胀, 分子之间的 碰撞力急剧增加, 液滴变形、 表面剥离直至完全破碎, 高温、 高压、 高速冲击波 (激波)气流以超过外界大气压许多倍的压强压力冲破各 个淡水分子水液液滴之间的间隙及促使液滴内部气泡胀大破碎, 高温、 高压、 高速气流争先恐后地往外挤, 使微小颗粒的液滴在各个方向即 刻胀大爆碎超高速蒸发汽化。 体积膨胀许多倍, 比重减轻许多倍, 分 子之间的间距离拉大许多倍, 最大限度地扩大淡水分子与盐类分子之 间的密度差距和运行速度。 淡水分子水液在超高速蒸发汽化后形成质 点最小的超高密度微细颗粒悬浮液滴汽液混合体; 盐类分子水液不易 被高温高压蒸发汽化形成质点最大的颗粒液滴浓盐水; 在它们改变了 运行方式后, 使它们在瞬间内分离开并隔离开, 达到超高速汽化瞬间 海水淡化的目的。 At high temperature, freshwater molecular water is easily volatile, and the specific gravity and distance between salt molecules are not easy to change. Salt molecular water is not easily volatile, and the specific gravity and distance between them is small. If environmentally friendly explosives are used to explode in high temperature and high pressure seawater, (in seawater boiling at high temperature, fresh water molecules are easily vaporized at high temperature due to the inclusion of more volatile components, so as the temperature rises, freshwater molecules The change in volume and specific gravity of water is very large; the salt molecular water is not easily evaporated by high temperature because it contains more non-volatile components, so the change in volume and specific gravity of salt molecular water is very small as the temperature increases .) Seawater water droplets release huge energy after being detonated by high-temperature and high-pressure explosions, generating a large amount of high-temperature, high-pressure, and high-speed shock waves (shock waves). The huge compressed gas shock waves formed by the gas stream have a strong and sharp impact. Segmentation, enveloping, high-speed blasting, omnidirectional three-dimensional ultra-high-speed evaporation and vaporization of seawater water liquid droplets. The mixed vapor-liquid of high-temperature, high-pressure, and ultra-high-density dissolved gas first causes strong high-pressure compression, and then the high-temperature and high-pressure detonated water liquid is instantly decompressed and rapidly expanded to burst and vaporize, so that the droplets of the ultra-high-density dissolved gas instantly have severe mechanical instability. Equilibrium, the volume of liquid droplets expands rapidly and sharply, the collision force between molecules increases sharply, the liquid droplets deform, the surface peels until they are completely broken, and the high-temperature, high-pressure, and high-speed shock wave (shock) gas flow is broken by a pressure that is many times the outside atmospheric pressure The gaps between water droplets of various freshwater molecules and the bubbles inside the droplets are swelled and broken. High-temperature, high-pressure, and high-speed air streams rush out to rush out, so that droplets of tiny particles swell instantly in all directions. . Many times the volume expansion and many times the specific gravity reduction. The distance between the electrons is multiplied many times, which maximizes the density gap and operating speed between freshwater molecules and salt molecules. Freshwater molecular water liquids form ultra-high-density fine-particle suspension droplet vapor-liquid mixtures with the smallest particles after ultra-high-speed evaporation and vaporization; salt molecular aqueous liquids are not easily vaporized by high-temperature and high-pressure evaporation to form concentrated brine with the largest particle droplets; After changing the operation mode, they are separated and isolated in an instant, so as to achieve the purpose of seawater desalination at the moment of ultra-high-speed vaporization.
本发明的技术方案如下: 一种超高效海水淡化瞬间汽化装置, 在 注入预处理海水的高压容器体内先安置加热器或不设置不安置加热 器、 和设置导液管、 导气管或不设置不安置导气管、 喷嘴、 放爆片; 可置放或不置放适量的环保炸药、 点火器、 耐压盒盖, 高压容器上设 置连接联通导液管、 导气管、 喷嘴和设置连接安置放爆片; 高压容器 体外设置连接联通进水阀门或不设置不安置进水阀门、 设置连接联通 低压储气罐的进气阀门、 中压储气罐的进气阀门、 高压储气罐的进气 阀门或设置安置压缩气体进气陶门; 在高压容器上设置连接单层或双 层或多层放爆汽化大棚, 放爆汽化大棚体内设置连接多层高温过滤网 或不设置不安置多层高温过滤网, 在放爆汽化大棚内设置连接接液罩 盘并与浓盐水出液阀门连接联通或不设置不安置浓盐水出液阀门; 放 爆汽化大棚体外设置连接自动泄压窗或不设置不安置自动泄压窗和设 置连接联通淡水出水阀门或不设置不安置淡水出水阀门; 放爆汽化大 棚上层的体内设置单个或多个高温水蒸气排放口和体外设置自动泄压 小窗或不设置不安置自动泄压小窗及设置连接联通蒸馏水出水阀门或 不设置不安置蒸馏水出水阀门; 高压容器的连续性放爆汽化组合系统: 单盘或多盘旋转轴座辐射的支杆分别与放爆汽化大棚连接固定; 高压 容器与放爆汽化大棚可快速连接。 The technical solution of the present invention is as follows: An ultra-efficient instant seawater desalination vaporization device, a heater is installed or not installed in a high-pressure vessel injected with pretreated seawater, and a liquid pipe, an air pipe or no Place the air pipe, nozzle, and explosive plate; can put or not put the appropriate amount of environmentally friendly explosives, igniters, pressure-resistant box lids, high-pressure containers are provided with connecting fluid guide tubes, air pipes, nozzles, and connected to place explosive plates ; The high pressure vessel is provided with a Unicom water inlet valve or not without a water inlet valve, an air inlet valve connected to a Unicom low pressure gas storage tank, an medium pressure gas storage tank inlet valve, a high pressure gas storage tank inlet valve, or Set up a ceramic door for compressed gas inlet; set a single-layer or double-layer or multi-layer detonation vaporization greenhouse on the high-pressure vessel; connect a multilayer high-temperature filter in the detonation vaporization greenhouse; In the detonation and vaporization greenhouse, a connection liquid receiving hood plate is provided and connected with the concentrated saline outlet valve, or there is no concentrated saline outlet valve. Doors; automatic pressure relief windows are installed outside the detonation vaporization greenhouse, or automatic pressure relief windows are not installed and not connected, or freshwater outlet valves are connected or not installed; single or multiple bodies are set in the upper body of the explosion vaporization greenhouse The high-temperature water vapor discharge port and the external body are equipped with automatic pressure relief windows or are not provided without automatic pressure relief windows and are connected with the connected distilled water outlet valve or are not provided without the distilled water outlet valve; the continuous detonation and vaporization combined system of the high-pressure vessel: The support rods radiated by the single-disk or multi-disk rotating shaft seat are respectively connected and fixed to the detonation vaporization greenhouse; the high-pressure vessel and the detonation vaporization greenhouse can be quickly connected.
超高效海水淡化瞬间汽化装置的工作流程为: The working process of the ultra-efficient seawater desalination instant vaporization device is:
1、 高压压缩气体高温高压放爆水液液滴瞬间减压快速膨胀爆碎超 高速蒸发汽化: 在高压容器体内先安置加热器、 导液管、 导气管或不 设置不安置导气管、 喷嘴; 可采用置放适量的环保炸药、 点火器、 耐 压盒盖和安置放爆片; 开启进水阀门注入预处理海水, 当高压容器体 内的进水水位达到一定的水位时关闭进水阀门; 然后逐个分别开启及 关闭: 低压储气罐的进气阀门、 中压储气罐的进气阀门、 高压储气罐 的进气阀门或设置安置压縮气体的进气阀门; 在高压容器体内的进气 压力达到了所需的工作要求压力时, 即可关闭高压储气罐的进气阀门 或关闭压缩气体的进气阀门停止注气。 开启加热器加热或不设置不安 置加热器, 在高压超高密度溶气的海水水液加热至一定的高温后关闭 加热器停止加热。 可采用幵启点火器引爆环保炸药在高温高压的海水 中定向爆炸。 [可置放或不置放适量的环保炸药、 点火器; 若不采用炸 药爆炸产生大量气体放爆; 可直接采用超高压增气放爆, 将海水水液 继续加热使气液超极限膨胀引爆高压容器爆炸放爆; 或直接采用特制 (能产生巨大量气体) 炸药爆炸产生巨大量的超高压压缩气体引爆高 压容器爆炸放爆。 ]一旦高压压缩气体高温高压放爆水液液滴瞬间减压 快速膨胀爆碎汽化, 爆炸放爆后释放出巨大的能量产生大量的高温高 压巨力冲击波气流聚力瞬间撕碎放爆片, 高温高压高速射流的汽与液 即从导液管、 导气管、 喷嘴内喷出, 形成同时二次爆炸放爆。 海水中 的淡水分子水液即被爆炸放爆后释放出的巨大能量产生大量的高温、 高压、 高速冲击波气流, 在放爆汽化大棚的空间内被高速冲击碰撞爆 碎成雾液强烈急剧分解突跃物态变化, 超高速蒸发汽化成汽液混合体, (淡水分子与盐类分子之间一旦脱离了水体母液, 相互间就不再产生 大的作用力) 形成质点最小的超高密度微细颗粒悬浮液滴汽液混合体 高速膨胀扩散上升。 盐类分子水液由于不易被高温、 高压、 高速气流 蒸发汽化受冲击后, 形成质点最大的颗粒液滴浓盐水, 所承受的冲击 作用力最大运行速度最快, 被冲击喷射至接液罩盘的壁板面上逐渐聚 积。 1, high-pressure compressed gas, high-temperature and high-pressure detonation of water droplets, instantaneous decompression and rapid expansion High-speed evaporation and vaporization: first place heaters, liquid tubes, air tubes or no air tubes and nozzles in the high-pressure container; appropriate environmental explosives, igniters, pressure-resistant box covers, and explosive plates can be used Open the water inlet valve to inject pre-treated seawater, and close the water inlet valve when the water inlet level in the high-pressure vessel reaches a certain level; then open and close each one separately: the inlet valve of the low-pressure gas storage tank, the medium-pressure gas storage tank Intake valve, inlet valve of high-pressure gas storage tank or an inlet valve provided with compressed gas; when the inlet pressure of the high-pressure container reaches the required working pressure, the inlet of the high-pressure gas storage tank can be closed. The air valve or the intake valve closing the compressed gas stops gas injection. Turn on the heater to heat or not install or install the heater. After the high-pressure ultra-high-density dissolved seawater water solution is heated to a certain high temperature, turn off the heater to stop heating. An environmentally friendly explosive can be detonated using a igniter to ignite a directional explosion in high-temperature and high-pressure seawater. [Can put or not put the right amount of environmentally friendly explosives and igniters; if a large amount of gas is not used to explode with explosives; ultra-high pressure gas can be used to explode directly, and the seawater water liquid will continue to be heated to cause the gas-liquid to exceed the limit expansion and detonate high pressure The container explodes and explodes; or directly uses a special product (which can generate a huge amount of gas). Explosive explosion generates a huge amount of ultra-high pressure compressed gas to detonate the high-pressure container. ] Once the high-pressure compressed gas is released at high temperature and pressure, the liquid droplets are instantly decompressed and rapidly expanded and blasted and vaporized. After the explosion and blasting, huge energy is released to generate a large amount of high-temperature and high-pressure shock waves. The vapor and liquid of the high-pressure high-speed jet are ejected from the liquid pipe, the air pipe, and the nozzle, forming a secondary explosion at the same time. The fresh water molecules in the seawater, that is, the huge energy released after the explosion and detonation, generate a large amount of high-temperature, high-pressure, and high-speed shock wave airflows. They were exploded by high-speed impact collisions in the space of the detonation and vaporization greenhouse, and were strongly decomposed into fog liquid. The state of the material changes, and the ultra-high-speed evaporation vaporizes into a vapor-liquid mixture. (Once the fresh water molecules and the salt molecules are separated from the mother liquid of the water body, there is no longer a large force between them.) Ultra-high-density fine particles with the smallest particles are formed. Suspension droplet vapor-liquid mixture expands and diffuses at high speed. The salt molecular water liquid is not easy to be impacted by vaporization and vaporization of high temperature, high pressure, and high-speed airflow, and forms concentrated droplets of concentrated saltwater with the largest particle point. The maximum impact force is the fastest, and it is sprayed to the liquid-contact hood disk. Gradually accumulate on the siding surface Product.
2、 超速汽化冷却制取淡水: 可在环保炸药爆炸前先开启多层高温 过滤网热源加热或不设置不安置多层高温过滤网, 开启淡水出水阀门 和开启浓盐水出液阀门及开启蒸馏水出水阀门。 爆炸放爆后海水汽液 在被高温、 高压、 高速冲击波巨力气流冲击后从导液管、 导气管的喷 嘴内喷出, 呈圆锥状膨胀射流雾化, 具有连续性分叉结构。 雾化过程 中的液滴粒度分形特征, 有一个液滴分裂服从均匀分布的概率。 液滴 与高速气液冲击波 (激波)气体不断地碰撞撞击后, 液滴变形、 表面 剥离直至完全破碎。 在放爆汽化大棚的空间内急剧向上喷射剧烈膨胀 扩散。 盐类分子水液由于不易被高温高压蒸发汽化形成质点最大的颗 粒液滴浓盐水冲进多层高温过滤网内, 遭接液罩盘板壁受阻拦后顺板 壁面下液, 聚积后从浓盐水出液管道内排出。 海水中的淡水分子水液 被超高速蒸发汽化后形成质点最小的超高密度微细颗粒悬浮液滴汽液 混合体急剧向上喷射, 在遇到多层高温过滤网内产生的大量的高温时, 受高温阻拦后再次进一步汽化, 剧烈膨胀成水汽体急剧向四周扩散上 升。 此时的自动泄压窗能够自动迅速将有压的多余气体排出体外或不 设置不安置自动泄压窗。 淡水汽体水汽在放爆汽化大棚的快速冷却冷 凝聚积后形成淡水, 从淡水出水管道内输出。 另外, 大部分高温水蒸 气在上升后从单个或多个高温水蒸气排放口进入上层的放爆汽化大棚 内, 多余的有压气体即从自动泄压小窗口排出或不设置不安置自动泄 压小窗口。 高温水蒸气经上层的放爆汽化大棚快速冷却冷凝后形成蒸 馏水水液从蒸馏水出水阀门管道内排出。 最后关闭多层高温过滤网的 加热源, 关闭淡水出水阔门和关闭浓盐水出液阀门及关闭蒸馏水出水 阀门。 如此不断地反复循环不息。 2. Preparation of fresh water by ultra-high-speed vaporization cooling: The multi-layer high-temperature filter can be turned on before the explosion of environmentally friendly explosives, or the multi-layer high-temperature filter is not installed. The fresh water outlet valve and the concentrated brine outlet valve and the distilled water outlet water can be opened. valve. After the explosion and detonation, the seawater vapor and liquid are ejected from the nozzles of the liquid pipe and the air pipe after being impacted by the high-temperature, high-pressure, and high-speed shock wave giant airflow, and they are atomized in a conical expansion jet with a continuous bifurcation structure. The fractal characteristics of the droplet size during the atomization process have a probability that the droplet splitting obeys a uniform distribution. After the liquid droplets collide with the high-speed gas-liquid shock wave (shock wave) gas, the liquid droplets are deformed and the surface is peeled until they are completely broken. In the space where the vaporization greenhouse is detonated, it is ejected sharply upwards and violently expands and diffuses. The salt molecular water liquid is not easy to be evaporated and vaporized by high temperature and pressure to form the largest particle droplets. The concentrated brine is washed into the multi-layer high-temperature filter. After being blocked by the plate wall of the liquid hood, the liquid flows down the surface of the plate and accumulates from the concentrated brine. Discharge in the outlet pipe. Freshwater molecules in the seawater are vaporized by ultra-high-speed evaporation to form ultra-high-density fine-particle suspension droplets and liquid-liquid mixtures with the smallest particles, which are sharply ejected. When encountering a large amount of high temperature generated in a multilayer high-temperature filter, After being blocked by high temperature, it vaporizes again, and expands violently into water vapor, which diffuses and rises to the surroundings. At this time, the automatic pressure relief window can automatically and quickly discharge the excess gas under pressure or there is no automatic pressure relief window. Fresh water vapor is formed by rapid cooling and cold condensation in the degassing greenhouse, and then is formed into fresh water, which is output from the fresh water outlet pipe. In addition, most of the high-temperature water vapor rises from the single or multiple high-temperature water vapor discharge ports into the upper explosion degassing greenhouse after the rise, and the excess pressurized gas is discharged from the automatic pressure relief small window or is not provided without automatic pressure relief. Small window. The high-temperature water vapor is rapidly cooled and condensed in the upper detonation vaporization greenhouse to form distilled water. The liquid is discharged from the pipe of the distilled water outlet valve. Finally, close the heating source of the multilayer high-temperature filter, close the wide water outlet door, close the concentrated brine outlet valve, and close the distilled water outlet valve. So it goes on and on.
由于上述解决方案中采用了: 高压气体爆碎汽化法即: 高压压縮 气体高温高压放爆水液液滴瞬间减压快速膨胀爆碎超高速蒸发汽化机 0535 理, 使海水水液在被爆炸放爆后释放出巨大能量产生大量的高温、 高 压、 高速冲击波气流巨力冲击、 分割、 包围、 爆碎、 分解海水后, 海 水中的淡水分子水液在瞬间内发生急剧的超高速蒸发汽化形成质点最 小的超高密度微细颗粒悬浮液滴汽液混合体, 分子之间的间距离急剧 成许多倍的加大, 体积迅速成许多倍的增长, 比重迅速成许多倍的减 轻; 海水中的盐类分子水液由于不易被高温高压蒸发汽化形成质点最 大的颗粒液滴浓盐水; 使淡水分子与盐类分子之间产生最大的汽与液 的比重差距和运行速度, 在它们改变了运行方式后, 达到了超高速分 离的目的并将它们迅速地隔离开。 其结构简单、 投资非常少, 性能稳 定、 体积小、 制水特快、 水垢少 (并便于清除) 高水质、 出淡水产量 高 (特别适合浓海水脱盐) 能够节省大量的能源和时间。 Because the above solution is used: High pressure gas explosion vaporization method is: high pressure compressed gas explosion at high temperature and high pressure, the liquid droplets are decompressed quickly and rapidly expanded and exploded and ultra-high speed evaporation vaporizer 0535, after the seawater liquid is released by the explosion, it releases a huge amount of energy to generate a large amount of high temperature, high pressure, high-speed shock wave airflow, strong impact, segmentation, enclosing, blasting, and decomposition of seawater. A sudden ultra-high-speed evaporation and vaporization occurred within an instant to form an ultra-high density fine particle suspension droplet vapor-liquid mixture with the smallest particle point. The distance between the molecules increased dramatically by many times, and the volume rapidly increased by many times. Reduced by many times; salt molecules in the seawater are not easily evaporated by high temperature and high pressure to form the largest droplets of concentrated saltwater; the largest gap between the specific gravity of vapor and liquid between freshwater molecules and salt molecules and The running speed, after changing the running mode, achieves the purpose of ultra-high speed separation and quickly isolates them. Its simple structure, very low investment, stable performance, small size, fast water production, low scale (and easy removal), high water quality, and high output of fresh water (especially suitable for thick seawater desalination) can save a lot of energy and time.
附图说明 BRIEF DESCRIPTION OF THE DRAWINGS
下面结合附图 1、 附图 2与实施例对本发明作进一步描述。 The present invention is further described below with reference to the accompanying drawings 1, 2 and embodiments.
附图 1 是本发明实施例的超高效海水淡化瞬间汽化装置的连续性 放爆汽化冷却系统的工作原理的简介示意图。 FIG. 1 is a schematic diagram of the working principle of a detonation vaporization cooling system for the continuity of a super-efficient seawater desalination instantaneous vaporization device according to an embodiment of the present invention.
附图 2 是本发明实施例的超高效海水淡化瞬间汽化装置的高压压 縮气体高温高压放爆水液液滴瞬间减压快速膨胀爆碎超高速蒸发汽化 冷却制水的工作原理的简介示意图。 Figure 2 is a schematic diagram of the working principle of the high-pressure compressed gas high-temperature and high-pressure detonation water droplets of the ultra-efficient seawater desalination instantaneous vaporization device according to the embodiment of the present invention.
具体实施方式 detailed description
本发明超高效海水淡化瞬间汽化装置如附图 1、 附图 2所示, 主 要由二大部件组合成。 一、 高压压缩气体高温高压放爆水液液滴瞬间 减压快速膨胀爆碎超高速蒸发汽化冷却制水: 在注入预处理海水的高 压容器 3体内先安置加热器 4或不设置不安置加热器 4和设置导液管 8、 导气管 9或不设置不安置导气管 9、 喷嘴 10、 放爆片 11 (或置放 或不置放适量的环保炸药 5、 点火器 6、 耐压盒盖 7。); 高压容器 3上 设置连接联通导液管 8、导气管 9、 喷嘴 10和设置连接安置放爆片 11 ; 高压容器 3 体外设置连接联通进水阀门 12或不设置不安置进水阀门 12、 设置连接联通低压储气罐的进气阀门 13、 中压储气罐的进气阔门 14、 高压储气罐的进气阀门 15或设置安置压缩气体的进气阀门 15 ; 在高压容器 3上设置连接单层或双层或多层放爆汽化大棚 2, 放爆汽 化大棚 2体内设置连接多层高温过滤网 16或不设置不安置多层高温过 滤网 16, 在多层高温过滤网 16外围设置连接接液罩盘 17并与浓盐水 出液阀门 21 连接联通或不设置不安置浓盐水出液阀门 21 ; 放爆汽化 大棚 2体外设置连接自动泄压窗 18或不设置不安置自动泄压窗 18和 设置连接联通淡水出水阀门 22或不设置不安置淡水出水阀门 22; 放 爆汽化大棚 2上层的体内设置单个或多个高温水蒸气排放口 19和体外 设置连接自动泄压小窗 20或不设置不安置自动泄压小窗 20及设置连 接联通蒸馏水出水阀门 23或不设置不安置蒸馏水出水阀门 23。 As shown in FIG. 1 and FIG. 2, the ultra-efficient instant seawater desalination device of the present invention is mainly composed of two large components. I. High-pressure compressed gas, high-temperature, high-pressure detonation, water droplets, instantaneous decompression, rapid expansion, blasting, ultra-high-speed evaporation, vaporization, and cooling of water: firstly install a heater 4 in the high-pressure container 3 injected with pre-treated seawater or not install a heater 4 and with or without liquid guide tube 8, air guide tube 9, or without air guide tube 9, nozzle 10, blasting disc 11 (or with or without a proper amount of environmentally friendly explosive 5, igniter 6, pressure-resistant box cover 7. ); On the high-pressure container 3 is connected to connect the communication catheter 8, the air pipe 9, the nozzle 10, and the connection is arranged to place the explosive disc 11; High pressure vessel 3 is equipped with a Unicom water inlet valve 12 or no water inlet valve 12 is installed outside the body, an air inlet valve 13 connected to a Unicom low pressure gas storage tank 13 is installed, a wide air inlet door 14 for a medium pressure gas storage tank, and a high pressure gas storage tank Inlet valve 15 or pressurized gas inlet valve 15 is provided; On the high-pressure vessel 3, a single-layer or double-layer or multi-layer detonation vaporization greenhouse 2 is provided, and a multi-layer high-temperature filter is installed in the detonation vaporization greenhouse 2 16 or no multi-layer high-temperature filter 16 is not installed, the multi-layer high-temperature filter 16 is provided on the periphery of the connecting liquid-disc cover plate 17 and is connected to the concentrated brine outlet valve 21 or is not provided without the concentrated brine outlet valve 21; The explosion-proof vaporization greenhouse 2 is provided with an automatic pressure relief window 18 outside the body or is not provided. The automatic pressure relief window 18 is not installed and connected with the Unicom freshwater outlet valve 22 or the freshwater outlet valve 22 is not provided. Single or multiple high-temperature water vapor outlets 19 are connected to the automatic pressure relief window 20 or are not provided without automatic pressure relief window 20 and connected to the connected distilled water outlet valve 23 or are not provided without steam Distilled water outlet valve 23.
二、 连续性放爆汽化冷却组合系统: 单盘或多盘旋转轴座 1 辐射 式的支杆分别与放爆汽化大棚 1连接固定; 高压容器 3与放爆汽化大 棚 2可快速连接。 2. Continuous detonation and vaporization cooling combined system: Single or multi-disc rotary shaft seat 1 Radiation type poles are connected and fixed to the detonation and vaporization greenhouse 1, respectively; The high-pressure vessel 3 and the detonation and vaporization greenhouse 2 can be quickly connected.
1、 高压压缩气体高温高压放爆水液瞬间减压快速膨胀爆碎超高速 蒸发汽化: 在高压容器 3体内先安置加热器 4或不安置加热器 4、 导 液管 8、 导气管 9或不安置导气管 9、 喷嘴 10、 (可置放或不置放适量 的环保炸药 5、 点火器 6、 耐压盒盖 7。) 安置放爆片 11。 开启海水进 水阀门 12或不安置进水阀门 12当水泵压注入的进水的水位达到高压 容器 3体内一定的水位时, 可关闭海水进水阀门 12; 然后逐个分别开 启及关闭: 低压储气罐的进气阀门 13、 中压储气罐的进气阀门 14、 高 压储气罐的进气阀门 15 或设置安置压缩气体的进气阀门 15 ; 在高压 容器 3 体内的进气压力达到了所需的工作要求压力时, 即可关闭高压 储气罐的进气阀门 15或关闭压缩气体的进气阀门 15仃止注气。 开启 加热器 4高温加热, 在超高密度溶气的海水水液加热至一定的高温后 02 00535 关闭加热器 4停止加热。 可采用开启点火器 6引爆环保炸药 5在高温 高压的海水中定向爆炸, 产生大量的高压压缩气体高温高压放爆(可 采用环保炸药 5爆炸产生大量的高压压縮气体引爆高压容器 3放爆, 或不采用炸药爆炸直接超高压增气放爆, 将海水水液继续加热使气液 超极限膨胀引爆高压容器 3 爆炸放爆; 也可直接采用特制 (能够产生 巨大量气体) 炸药爆炸产生巨大量的超高压压缩气体引爆高压容器 3 爆炸放爆。)水液瞬间减压快速膨胀爆碎超高速蒸发汽化。 炸药 5爆炸 放爆后释放出巨大的能量产生大量的高温高压巨力冲击波气流聚力瞬 间撕碎放爆片 11, 高压容器 3体内的高温、 高压汽与液即从导液管 8、 导气管 9、 喷嘴 10上口喷出, 形成同时二次爆炸放爆。 由于炸药 5爆 炸引发放爆的能量巨大, 高压超高密度溶气的高温高压混合汽液中的 淡水分子水液和盐类分子水液, 即被爆炸放爆后释放出的巨大能量产 生大量的高温、 高压、 高速冲击波气流, 在放爆汽化大棚 2的空间内, 被高速冲击剧烈爆碎形成超高密度的雾液。 淡水分子水液在被强烈急 剧分解突跃物态变化超高速蒸发汽化后成汽液, 形成质点最小的超高 密度微细颗粒悬浮液滴汽液混合体高速膨胀扩散上升; 盐类分子水液 不易被高温高压蒸发汽化, 受冲击后形成质点最大的颗粒液滴浓盐水 承受的冲击作用力最大, 运行速度最快。 1. High-pressure compressed gas, high-temperature and high-pressure detonation of water, instantaneous decompression, rapid expansion, blasting, ultra-high-speed evaporation and vaporization: Install heater 4 or no heater 4, fluid guide tube 8, air guide tube 9 or not Place the air guide tube 9, the nozzle 10, (the appropriate amount of environmentally friendly explosives 5, the igniter 6, and the pressure-resistant box cover 7 can be placed or not.) Place the explosive disc 11. Open the seawater inlet valve 12 or leave the water inlet valve 12 closed. When the water level of the inlet water pump pressure reaches a certain water level in the high pressure vessel 3, you can close the seawater inlet valve 12; then open and close each one separately: Low-pressure gas storage Inlet valve 13 of the tank, Inlet valve 14 of the medium pressure storage tank, Inlet valve 15 of the high pressure storage tank or an inlet valve 15 for setting compressed gas; the pressure of the inlet air in the high pressure vessel 3 has reached When the required work requires pressure, the inlet valve 15 of the high-pressure gas storage tank or the inlet valve 15 of the compressed gas can be closed to stop the gas injection. Turn on the heater 4 to heat at a high temperature. After the ultra-high density dissolved seawater water is heated to a certain high temperature 02 00535 Turn off heater 4 to stop heating. The igniter 6 can be turned on to detonate the environmentally friendly explosive 5 in a high-temperature and high-pressure seawater to produce a high-pressure and high-pressure compressed gas explosion. (The environmentally-friendly explosive 5 can be used to generate a large amount of high-pressure compressed gas to detonate the high-pressure container 3. Or directly use ultra-high-pressure gas-increasing detonation without explosive explosion, and continue heating the seawater liquid to cause the gas-liquid ultra-expansion expansion to detonate the high-pressure container. 3 Explosive detonation can also be used directly. The ultra-high-pressure compressed gas detonated the high-pressure vessel 3 and exploded.) The water liquid was instantly decompressed and rapidly expanded and exploded. The ultra-high-speed evaporation vaporized. Explosive 5 releases huge energy after explosion and explosion, generates a large amount of high-temperature and high-pressure shock wave airflow, and instantly tears the explosive disc 11, the high-temperature, high-pressure steam and liquid in the high-pressure container 3 are from the liquid guide tube 8, the air tube 9. The upper mouth of the nozzle 10 ejects, forming a secondary explosion at the same time. Due to the huge explosive energy caused by the explosion of explosive 5, the high-temperature and high-density dissolved gas in the high-temperature and high-pressure mixed vapor-liquid liquid water and salt molecular water, that is, the huge energy released after the explosion detonation produced a large amount of energy. The high-temperature, high-pressure, and high-speed shock wave airflow is violently blasted by high-speed impact in the space of the detonation vaporization greenhouse 2 to form an ultra-high density mist. Freshwater molecular water liquid is strongly and sharply decomposed and suddenly changes its physical state. After ultra-high-speed evaporation and vaporization, it forms vapor-liquid, forming ultra-high-density fine particle suspension droplets with minimal particle size. The vapor-liquid mixture expands and diffuses at high speed; salt molecular water is not easy Evaporated and vaporized by high temperature and high pressure. After being impacted, the concentrated salt solution with the largest particle size will be subjected to the largest impact force and the fastest operating speed.
2、 连续性放爆超速汽化冷却制取淡水: 在环保炸药 5爆炸放爆前 先开启多层高温过滤网 16 热源加热或不设置不安置多层高温过滤网 16, 开启浓盐水出液阀门 21或不安置浓盐水出液阀门 21和开启淡水 出水阔门 22或不安置淡水出水阀门 22及开启蒸馏水出水阀门 23或不 安置蒸馏水出水阀门 23, 在炸药 5爆炸放爆后, 高温高压海水水液混 合汽与液被高温、 高压、 高速冲击波巨力气流冲击后从导液管 8、 导 气管 9或不安置导气管 9、 喷嘴 10上口喷出, 在放爆汽化大棚 2的空 间内急剧向上喷射, 剧烈膨胀爆碎扩散。 盐类分子水液由于不易被高 温、 高压、 蒸发汽化形成质点最大的颗粒液滴浓盐水喷出后高速冲进 多层高温过滤网 16内或不安置多层高温过滤网 16, 遭接液罩盘 17板 壁阻拦后即顺板壁面下流, 聚积后从浓盐水出液阀门 21的出液管道内 排出; 高温、 高压的混合汽液中的淡水分子水液被强烈急剧膨胀爆碎 超高速蒸发汽化后, 形成质点最小的超高密度微细颗粒悬浮液滴汽液 混合体喷出后剧烈膨胀高速扩散上升, 遇到多层高温过滤网 16内所产 生的大量的高温气体, 受高温阻拦后再次进一步汽化剧烈膨胀急剧高 速向四周扩散上升, 即转弯绕道从接液罩盘 17的周边外围继续上升。 2. Continuous detonation and over-speed vaporization cooling to obtain fresh water: Before the environmental protection explosive 5 detonates, open the multi-layer high-temperature filter 16 before heating or without setting the multi-layer high-temperature filter 16 and open the concentrated brine outlet valve 21 Or do not install concentrated brine outlet valve 21 and open fresh water outlet gate 22 or do not install fresh water outlet valve 22 and open distilled water outlet valve 23 or do not install distilled water outlet valve 23. After explosive 5 detonates, high temperature and high pressure seawater water liquid The mixed vapor and liquid are ejected from the upper end of the liquid guide tube 8, the air guide tube 9, or the air guide tube 9, and the nozzle 10 after being impacted by the high-temperature, high-pressure, high-speed shock wave giant airflow, and rises sharply in the space of the vaporization greenhouse 2 Jet, violent expansion bursts and spreads. Because salt molecules are not easy to be high High-temperature, high-pressure, evaporation and vaporization to form the largest particles of droplets of concentrated brine and sprayed into the multilayer high-temperature filter 16 at high speed or without the multilayer high-temperature filter 16 and then blocked by the wall of the liquid-shielding plate 17 The wall surface flows down and is accumulated and discharged from the outlet pipe of the concentrated brine discharge valve 21; the fresh water molecular water in the high-temperature and high-pressure mixed vapor-liquid is strongly and rapidly expanded and exploded. After ultra-high-speed evaporation and vaporization, an ultra-high minimum particle is formed. After being ejected, the vapor-liquid mixture of fine particle suspension droplets swells rapidly and diffuses rapidly, and encounters a large amount of high-temperature gas generated in the multi-layer high-temperature filter screen 16. After being blocked by the high temperature, it further vaporizes and expands rapidly and diffuses rapidly around it. Ascent, that is, the detour continues to ascend from the periphery of the wetted disc 17.
(高温混合汽体能够转弯绕道上升, 是因为高温水蒸气比空气轻, 自 身具有上升的动能。 在高温高压放爆后, 高温混合汽液中的淡水分子 液滴和盐类分子液滴能够以各自不同的运行方向运行, 达到了瞬间分 离和隔离的目的。)此时自动泄压窗 18或不安置自动泄压窗 18即自动 及时地排放出多余的有压气体) 高温淡水分子水蒸气在被放爆汽化大 棚 2的快速冷却冷凝聚积后形成淡水水液, 从淡水出水阀门 22管道内 输出; 另外大部分高温水蒸汽上升后从单个或多个高温水蒸气排放口 19进入上层的放爆汽化大棚 2, 多余有压气体即从自动泄压小窗 20口 排出或不安置自动泄压小窗 20, 高温水蒸气经上层的放爆汽化大棚 2 快速冷却冷凝后形成蒸馏水水液, 从蒸馏水出水阀门 23管道内排出。 最后关闭多层高温过滤网 16的加热源关闭浓盐水出液阀门 21和关闭 淡水出水阀门 22及关闭蒸馏水出水阀门 23。 高压容器 3的连续性放 爆汽化冷却系统单盘或多盘旋转轴座 1 为连续性放爆汽化冷却组合系 统其放爆汽化冷却的高效工作能力, 能够不断地满足高压容器 3 所连 续性的不断的放爆。 如此不断地反复循环不息。 (The high-temperature mixed vapor can turn around and go up because the high-temperature water vapor is lighter than air and has its own rising kinetic energy. After the high-temperature and high-pressure detonation, fresh water molecular droplets and salt molecular droplets in the high-temperature mixed vapor can be converted into Running in different directions of operation, achieve the purpose of instantaneous separation and isolation.) At this time, the automatic pressure relief window 18 or the automatic pressure relief window 18 is not installed will automatically and timely discharge excess pressurized gas.) After being rapidly cooled and condensed and accumulated by the detonation vaporization greenhouse 2, a fresh water liquid is formed and output from the fresh water outlet valve 22; in addition, most of the high-temperature water vapor rises from the single or multiple high-temperature water vapor discharge ports 19 and enters the upper layer of detonation. Vaporization greenhouse 2, the excess pressure gas is discharged from the automatic pressure relief window 20 or the automatic pressure relief window 20 is not installed, and the high-temperature water vapor is rapidly cooled and condensed to form a distilled water liquid after the upper detonation vaporization greenhouse 2 The water outlet valve 23 is discharged from the pipeline. Finally, close the heating source of the multi-layer high-temperature filter 16 to close the concentrated brine outlet valve 21 and close the fresh water outlet valve 22 and close the distilled water outlet valve 23. The single-disc or multi-disc rotary shaft seat 1 of the continuous detonation and vaporization cooling system of the high-pressure vessel 3 is a continuous detonation vaporization and cooling combined system. The high-efficiency working capacity of the detonation and vaporization cooling can continuously meet the continuous continuity of the high-pressure vessel 3. Explosion. So it goes on and on.
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN01126403.9 | 2001-08-03 | ||
| CN01126403A CN1334244A (en) | 2001-08-03 | 2001-08-03 | Instantaneous evaporator for super-efficient seawater disalination |
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| Publication Number | Publication Date |
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| WO2003011765A1 true WO2003011765A1 (en) | 2003-02-13 |
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| Application Number | Title | Priority Date | Filing Date |
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| PCT/CN2002/000535 Ceased WO2003011765A1 (en) | 2001-08-03 | 2002-08-05 | An ultra-efficient vaporizer for desalinating seawater instantaneously |
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| WO (1) | WO2003011765A1 (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2059299A5 (en) * | 1970-08-25 | 1971-05-28 | Rizza Louis | Desalination process for sea-water |
| US4017421A (en) * | 1975-12-16 | 1977-04-12 | Othmer Donald F | Wet combustion process |
| DE3613871A1 (en) * | 1986-04-24 | 1987-10-29 | Sep Tech Studien | Method for operating a system for using wind energy |
| US4735722A (en) * | 1987-06-15 | 1988-04-05 | Krepak John C | Desalination of seawater or brackish water |
| CN1228714A (en) * | 1996-06-27 | 1999-09-15 | 罗伯特·R·霍尔库姆 | Water treatment equipment and methods |
| RU2142912C1 (en) * | 1999-04-27 | 1999-12-20 | Моторин Виктор Николаевич | Method of desalination of sea water and device for realization on this method |
-
2001
- 2001-08-03 CN CN01126403A patent/CN1334244A/en active Pending
-
2002
- 2002-08-05 WO PCT/CN2002/000535 patent/WO2003011765A1/en not_active Ceased
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2059299A5 (en) * | 1970-08-25 | 1971-05-28 | Rizza Louis | Desalination process for sea-water |
| US4017421A (en) * | 1975-12-16 | 1977-04-12 | Othmer Donald F | Wet combustion process |
| DE3613871A1 (en) * | 1986-04-24 | 1987-10-29 | Sep Tech Studien | Method for operating a system for using wind energy |
| US4735722A (en) * | 1987-06-15 | 1988-04-05 | Krepak John C | Desalination of seawater or brackish water |
| CN1228714A (en) * | 1996-06-27 | 1999-09-15 | 罗伯特·R·霍尔库姆 | Water treatment equipment and methods |
| RU2142912C1 (en) * | 1999-04-27 | 1999-12-20 | Моторин Виктор Николаевич | Method of desalination of sea water and device for realization on this method |
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| CN1334244A (en) | 2002-02-06 |
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