JP3139784U - Honeycomb seawater desalination processor - Google Patents

Abstract

[PROBLEMS] To effectively improve the evaporation efficiency of seawater, reduce the thermal energy necessary for evaporation of seawater, and avoid the occurrence of salt.
The seawater desalination processor includes a hollow vacuum high pressure steam box 1, a seawater inlet pipe 11 and a water vapor discharge pipe 12 provided at the top of the hollow vacuum high pressure steam box 1, and a hollow vacuum high pressure steam box 1. A discharge port 13 provided at the bottom, and an evaporation device 4 that is installed in the hollow vacuum high pressure steam box 1 at one or more intervals at the same interval and includes a plurality of superconductor rods 40 and a fixed plate 41, are provided from the seawater inlet pipe 11. The seawater that has entered is heated and brought into contact with the superconductor rod 40 that has become high temperature to quickly evaporate.
[Selection] Figure 5

Description

  The present invention relates to a honeycomb type seawater desalination processor.

  The surface is full of water, but not all water is available. Currently, the development scale of water resources is gradually shrinking, and the situation of resource shortages is becoming more and more severe, and seawater desalination technology becomes increasingly important. There are five seawater desalination methods: distillation, coagulation, reverse osmosis, electrodeposition, and bioexchange. Among them, desalinated water by the distillation method and reverse osmosis method has a relatively good water quality. The apparatus of the distillation method is simple and robust, has a low production cost, a large amount of water for desalination, consumes energy, and is heavily contaminated.

This related technique is disclosed in Patent Document 1. This document 1 relates to “an apparatus in which combustion decontamination and combustion heat are used for seawater desalination”, and this apparatus is provided with an incinerator, a first chimney, and a desalination component. An incinerator has a combustion chamber, a furnace door and a burner, and a water storage chamber for receiving heat on it. The combustion chamber has a flue pipe facing outwards, the water containment chamber has a water intake pipe and a steam pipe for steam discharge, the flue pipe is connected to the first chimney, and the smoke exhausted via the steam pipe and the first chimney The tube is further connected to a desalination component. The first chimney is provided with a sprayer and a partition part. The desalination parts have a steam chamber and a seawater storage chamber above and below, respectively. A condenser is provided outside the steam chamber, and a collection tank is provided in the steam chamber for at least the outside. Steam pipes and flue gas pipes pass through the seawater storage chamber, and seawater is put in. In this way, through the water in the water storage chamber for receiving the heat of the incinerator, and the seawater storage chamber through which the steam pipe and the smoke exhaust pipe penetrate, the seawater is heated and evaporated, and the fresh water is distilled. ing.
Taiwan Patent Publication No. 5801093 Combustion decontamination and heat used for seawater desalination

However, the apparatus of Patent Document 1 has the following problems.
1. When distilling seawater, the water is heated and evaporated through the water in the water storage chamber to receive the heat of the incinerator and the seawater storage chamber through which the steam pipe and smoke pipe penetrate, and the fresh water is distilled. The heavy fuel oil required for incinerators causes great pollution to the environment after combustion, and an exhaust gas purification system must be installed to prevent harm to the environment.
2. In addition, a large amount of seawater is heated from room temperature to the boiling point so that the seawater accumulated in the seawater storage chamber is directly heated and steam is generated through the steam pipe and smoke exhaust pipe. .
3. And if the usage time becomes longer, salt will be generated in the pipeline for heating the seawater, which will seriously affect the distillation efficiency of the seawater, so that the pipeline should be regularly installed so as not to negatively affect the production rate. Must be cleaned.

  The present invention has been made in view of such conventional problems. In this type of seawater desalination processor, the seawater evaporation efficiency is effectively improved and the thermal energy required for seawater evaporation is reduced. In addition, the purpose is to avoid the occurrence of salt.

In order to solve the above problems, a first honeycomb seawater desalination processor of the present invention is characterized by having the following configuration.
(1) A hollow vacuum high pressure steam box 1 is provided.
(2) There is a discharge port 13 provided at the bottom of the vacuum high pressure steam box 1, and there is a gravity valve 131 provided in the discharge port 13 for discharging when the brine reaches a preset weight.
(3) There is a seawater inlet pipe 11 provided on the vacuum high pressure steam box 1 for guiding seawater into the vacuum high pressure steam box 1, the pipe end is connected to the shower head 2, and the shower head 2 is an evaporator. 4 and spaced.
(4) There is a water vapor discharge pipe 12 provided on the vacuum high pressure steam box 1 for discharging the water vapor in the vacuum high pressure steam box 1 to the outside, and the check function can be adjusted in the water vapor discharge pipe 12 There is a valve 121.
(5) and there is an evaporator 4 that is provided in the vacuum high pressure steam box 1 in one or more layers and spaced at the same interval, and the evaporator 4 is parallel to the plurality of superconductor rods 40 that are spaced at the same interval, and It consists of a fixing plate 41 for fixing and joining the superconductor rod 40.

Moreover, it is preferable that this processing machine is provided with the following structures in each part.
(6) The evaporator 4 and the temperature controller 3 for controlling the cold temperature switching of the evaporator 4 are electrically connected.
(7) The installation direction of the superconductor rod 40 of each evaporator 4 intersects the installation direction of the superconductor rod 40 of the evaporator 4 in the adjacent layer. In this case, the crossing angle is 90? Is the best.

Moreover, in order to solve the said subject, the 2nd honeycomb type seawater desalination processing machine of this invention is equipped with the following structures, It is characterized by the above-mentioned.
(1) A hollow vacuum high pressure steam box 1 is provided.
(2) There is a discharge port 13 provided at the bottom of the vacuum high pressure steam box 1, and there is a gravity valve 131 provided in the discharge port 13 for discharging when the brine reaches a preset weight.
(3) There is a seawater inlet pipe 11 provided at least above or in the center of the vacuum high pressure steam box 1 for guiding seawater into the vacuum high pressure steam box 1, the pipe end being connected to the shower head 2, and the shower head 2 is above the evaporator 4 and is spaced.
(4) There is a water vapor discharge pipe 12 provided on the vacuum high pressure steam box 1 for discharging the water vapor in the vacuum high pressure steam box 1 to the outside, and the check function can be adjusted in the water vapor discharge pipe 12 There is a valve 121.
(5) There is one evaporation device 4 that penetrates at least the vacuum high-pressure steam box 1 and is spaced at the same interval. The evaporation devices 4 are parallel, at the same interval, and at a tilt angle (θ). It consists of a rod 40 and a fixing plate 41 for fixing and joining the superconductor rod 40.
(6) At least one or more is provided at a high position in each evaporator 4, and there is a cooling device 43 that wraps one side of the superconductor rod 40 and lowers the temperature of the superconductor rod 40.
(7) At least one or more is provided in a low place of each evaporator 4, and there is a heating device 42 that wraps the other side of the superconductor rod 40 and raises the temperature of the superconductor rod 40.

Moreover, it is preferable that this processing machine is provided with the following structures in each part.
(8) The heating device 42 and the cooling device 43 are all electrically connected to the programmable controller 30 and controlled.
(9) The heating device 42 includes a plurality of heaters 422 provided at a low position of the superconductor rod 40, a fixing frame 421 for fixing the heaters 422, and a heater at a low position of the superconductor rod 40. 422 and a fixed housing 420 enclosing the fixed frame 421.
(10) The heater 422 is a quartz heating tube.
(11) The cooling device 43 is connected to the fixed casing 430 that encloses the high portion of the superconductor rod 40, the fixed casing 430, and a cooling water inlet pipe 431 for guiding the cooling water into the fixed casing 430, A cooling water discharge pipe 432 is connected to the fixed housing 430 to discharge water in the fixed housing 430 to the outside.
(12) The inclination angle (θ) is best from 5 ° to 45 °.

The honeycomb type seawater desalination processor of the present invention has the following operational effects by the above-described configurations.
(1) This processor combines the instantaneous heating function of the superconductor rod 40 with the fact that the boiling point of seawater is lowered by the vacuum environment in the vacuum high-pressure steam box 1, and the shower head 2 connected to the seawater inlet pipe 11. After being sprayed from the seawater, the volume of the seawater is reduced to rain, and when it comes into contact with the high-temperature superconductor rod 40, it quickly evaporates, which is faster than the conventional distillation type seawater desiccator. Since energy is reduced, there is an energy saving effect.
(2) The superconductor rod 40 is cooled from a high temperature by the control of the temperature controller 3, and in such an instantaneous temperature lowering action, the salt formed on the rod body of the superconductor rod 40 by the evaporation of seawater is rainy seawater. Is sprayed and washed away, the salt is immediately removed and falls onto the superconductor rod 10 and again instantly evaporates. As a result, the seawater is heated indirectly or heated through a steam pipe in a conventional distillation type seawater desiccator, and then the clogging of the pipeline or equipment is solved and the operation of the apparatus is performed successfully. Therefore, the occurrence of a failure can be avoided.
(3) The above-mentioned evaporated water vapor is discharged and collected from the water vapor discharge pipe 12, and the salt, the seawater after flowing and the seawater after evaporation and concentration flow to the bottom of the vacuum high-pressure steam box 1. Thus, when the gravity valve 131 at the bottom senses that the preset reference weight has been reached, they are discharged from the outlet 13 and collected.
(4) The shower head 2 at the end of the seawater inlet pipe 11 generates seawater after introduction in the form of rain and distributes it in an umbrella shape in the evaporator 4 to reduce the volume of the seawater so that it can be easily evaporated. The spray area is enlarged so that the evaporator 4 can be completely contacted.
(5) The evaporator 4 is installed in a multi-layer structure, and the superconductor rods 40 between the layers are arranged at an intersecting angle and are provided like a three-dimensional honeycomb, with seawater in the form of rain, Spraying the superconductor rod 40 of each layer like a shower to evaporate all the seawater, greatly improving the evaporation efficiency, removing the superconductor rod 40 and at the same time, Flow superconductor rod 40 cleanly.
(6) The superconductor rod 40 of the evaporation device 4 is electric power, and the present invention does not cause environmental pollution problems. If it is a conventional distillation type desalinator, there is contamination caused by fuel combustion. From the viewpoint, the effect of the present invention is further improved.
(7) The superconductor rod 40 of the evaporation device 4 is indirectly heated or cooled by the cooling device 43 and the heating device 42, and there is no problem of environmental pollution, and the risk of electrical leakage is avoided, Safety is improved. In addition, the control by the programmable controller 30 can be accurately controlled, there is no wasteful energy consumption, and the efficiency is further improved as compared with the conventional distillation type desalinator.

  Hereinafter, embodiments of the present invention will be described with reference to the drawings. 1 to 5 show a first embodiment of the present invention. As shown in FIGS. 1 and 2, the honeycomb seawater desalination processor includes a hollow vacuum high pressure steam box 1. The vacuum high pressure steam box 1 is provided with a seawater inlet pipe 11 for guiding seawater into the vacuum high pressure steam box 1 and a water vapor discharge pipe 12 for discharging water vapor in the vacuum high pressure steam box 1 to the outside. A discharge port 13 is provided at the bottom. Further, one or more evaporators 4 are installed at the same interval in the vacuum high pressure steam box 1. The evaporator 4 includes a plurality of superconductor rods 40 arranged in parallel at the same interval, and a fixing plate 41 for fixing and joining these superconductor rods 40. In this way, the instantaneous heating function of the superconductor rod 40 is combined with the boiling point of the seawater being lowered by the vacuum environment in the vacuum high-pressure steam box 1, and the seawater entering from the seawater inlet pipe 11 is heated and becomes hot. It contacts the superconductor rod 40 and evaporates quickly.

  Further, this processor employs the following configuration for each part.

  The top of the vacuum high-pressure steam box 1 has a solid semicircular curve shape or a solid quadrangular pyramid shape, so that water vapor is concentrated so as to be discharged upward, so that water molecules condense into water droplets and fall by gravity. Become.

  One or more shower heads 2 are connected to the end of the seawater inlet pipe 11. The shower head 2 is provided in the vacuum high pressure steam box 1 and is installed on the uppermost evaporator 4 at a predetermined interval. The shower head 2 generates seawater after introduction in the form of rain, distributes it in an umbrella shape, and sprays it on the evaporation device 4, thereby reducing the volume of the seawater and facilitating evaporation. . And since the shower head 2 is installed on the evaporator 4 at a predetermined interval, the spray area is enlarged, seawater is completely in contact with the evaporator 4, and energy can be used effectively without waste. . When the sprayed seawater comes into contact with the superconductor rod 40 of the evaporator 4, it absorbs the heat released from the superconductor rod 40 and further absorbs the heat released from the water vapor 6, and the seawater evaporates quickly, saving energy.

  The water vapor discharge pipe 12 is provided with an adjustable valve 121 having a check function. When a lot of water vapor is accumulated inside the vacuum high-pressure steam box 1 and the pressure reaches a preset value, the water vapor is discharged by the adjustable valve 121, so that the water vapor can be accumulated therein again, and the reverse flow of the water vapor is prevented. There is no damage to the device.

  A gravity valve 131 is provided at the discharge port 13 to discharge brine generated in the desalination process after reaching a preset weight value. The brine 7 made of the washed salt, the washed seawater and the evaporated and concentrated seawater is automatically discharged by the gravity valve 131 when the weight reaches the preset weight value, and the heat loss is reduced. As a result, energy is saved and efficiency is improved.

  Although the evaporators 4 in each layer are installed at the same interval, these evaporators 4 are divided into several groups, and different activation temperatures and activation operation times are set for each group to completely evaporate the seawater. It is supposed to fulfill its function. Taking these evaporators 4 as an example, the first set of superconductor rods 40 is set to a starting temperature of 80 ° C. to 100 ° C., and the second set of superconductor rods 40 is a first set of superconductor rods 40. It starts after 3 to 5 minutes after starting the superconductor rod 40, and the starting temperature is set to 80 ° C. The third set of superconductor rods 40 is activated 3 to 5 minutes after activation of the second set of superconductor rods 40, and the activation temperature is set to 60 ° C. The fourth set of superconductor rods 40 is started 3 to 5 minutes after the start of the third set of superconductor rods 40, and the startup temperature is set to 60 ° C. By setting the above grouping and the start temperature and start time of each group, the rainwater seawater 5 is easily evaporated. In this case, since the superconductor rods 40 are arranged in parallel at the same interval, the seawater guided to the seawater inlet pipe 11 passes through the intervals of the superconductor rods 40 in the evaporators 4 of each layer, and the evaporators of each layer. 4 can act with the atomized seawater, so that there is no waste of energy and the seawater is effectively distilled.

  The evaporator 4 of each layer is electrically connected to the temperature controller 3. The temperature controller 42 controls the positive and negative changes of the control power supply of the superconductor rod 40 to quickly heat or lower the temperature of the superconductor rod 40 so that the evaporator 4 evaporates the seawater or the cryogenic seawater. To remove the salt.

  As shown in FIG. 3, the evaporator 4 of each layer intersects the direction of the superconductor rod 40 of the evaporator 4 of adjacent layers as shown in FIG. When the surface of the superconductor rod 40 is increased, and the superconductor rod 40 is removed, the seawater used for the instant of cooling can completely wash all the superconductor rods 40. . In this case, the crossing angle is preferably 90 °. The superconductor rods 40 crossed at 90 ° are most effectively brought into contact with the seawater, and the seawater passes through a sufficient space to perform the functions of distillation and scraping.

  FIG. 4 shows a flow of seawater desalination by this processor, and FIG. 5 shows an image of seawater desalination by this processor. 4 and 5, after introducing seawater into the seawater inlet pipe 11 (8a), the showerhead 2 sprays seawater (8b). Seawater becomes rainy seawater 5, the volume of seawater is reduced, and the evaporation rate is improved. The rainy seawater 5 is heated and evaporated through the multilayer superconductor rod 40 of the evaporator 4 (8c). The boiling point of seawater is lowered in the vacuum environment in the vacuum high-pressure steam box 1, and the volume of seawater is reduced by the rainy seawater 5 sprayed from the showerhead 2 connected to the seawater inlet pipe 11. The amount of water vapor generated increases and the time it takes is shortened. For example, when the superconductor rod 40 is set to 30 ° C., when the rainy seawater 5 falls on the superconductor rod 40, water vapor is generated, but when the superconductor rod 40 is set to 40 ° C. to 50 ° C., the rain When the seawater 5 falls on the superconductor rod 40, water vapor is instantly generated. By the combination as described above, the heated seawater comes into contact with the superconductor rod 40 and quickly evaporates. When the water vapor temperature in the vacuum high pressure steam box 1 becomes 100 ° C. or higher, the superconductor rod 40 is instantaneously cooled (8d). Under the control of the temperature controller 3, the superconductor rod 40 is condensed and the temperature is lowered to 18 ° C. to 0 ° C., and salt is generated from boiling and evaporation of water in the rod body of the superconductor rod 40. Rainy seawater pours the salt on the superconductor rod 40 (8e), and when the superconductor rod 40 is instantaneously heated again, the seawater quickly evaporates (8f). At this time, in order to remove salt, the water vapor 6 generated in the previous stage of heating the seawater with the superconductor rod 40 contains the heat released at that time, and the superconductor rod 40 condenses in about 5 seconds to 10 seconds. Is mainly for removing the salt attached to the rod body of the superconductor rod 40. Since there is very little heat loss during the cold / hot intersection, the heat energy is saved during heating, and the superconductor rod 40 is used for rainwater. When 5 is heated and evaporated, energy consumption is reduced and energy is saved. By repeating the above steps, when the vacuum high pressure steam box 1 is filled with water vapor, the water vapor is discharged (8 g). In this case, the water vapor is discharged under the control of the adjustable valve 121 provided on the water vapor discharge pipe 12 and led to the condenser or the reservoir, where it is condensed and the seawater is desalinated. The washed saltwater, the washed rainy sea water 5, the seawater after evaporation and concentration fall to the bottom of the vacuum high pressure steam box 1 by gravity, and the brine 7 formed there flows to the discharge port (8h), When a certain weight is reached, for example 5 kg or 10 kg, the brine is discharged beyond the preset weight of the gravity valve (8i). The discharged brine 7 is used for coolers, automotive refrigerant dyeing finishing factories and semiconductors after predetermined treatment, avoiding environmental pollution problems, generating water resources from seawater desalination, and by-products There is an advantage in reducing the cost of energy consumption in the manufacturing process.

  6 to 8 show a second embodiment of the present invention. As shown in FIGS. 6 and 7, the honeycomb seawater desalination processor includes a hollow vacuum high pressure steam box 1. The vacuum high-pressure steam box 1 is provided with a seawater inlet pipe 11 for introducing seawater into the vacuum high-pressure steam box 1 at least at the upper part and / or the center, and further the water vapor in the vacuum high-pressure steam box 1 at the upper part. A water vapor discharge pipe 12 for discharging to the outside is provided, and a discharge port 13 is provided at the bottom. The vacuum high pressure steam box 1 is also provided with at least one evaporator 4 penetrating the vacuum high pressure steam box 1 at the same interval. The evaporator 4 includes a plurality of superconductor rods 40 arranged in parallel at the same inclination angle (θ) and at the same interval, and a fixing plate 41 for fixing and joining these superconductor rods 40. At least one cooling device 43 for covering one side of the superconductor rod 40 and lowering the temperature of the superconductor rod 40 is provided at a high position of each evaporator 4. At least one heating device 42 is provided at a lower portion of each evaporator 4 to wrap one side of the superconductor rod 40 and raise the temperature of the superconductor rod 40. In this way, a plurality of superconductor rods 40 are arranged in parallel at the same interval, and the seawater guided to the seawater inlet pipe 11 passes through the intervals between the superconductor rods 40 of the respective evaporators 4, and all the evaporators 4 are fogged. It becomes possible to act on the seawater, and by attaching an inclination angle (θ) to a plurality of superconductor rods 40, salt and water droplets can be quickly dropped by gravity, so there is no wasted energy consumption, Heat loss is minimized and the energy used to distill seawater is used effectively. In addition, the superconductor rod 40 is indirectly heated or cooled by the cooling device 43 and the heating device 42, so that there is no environmental pollution problem, and the occurrence of electrical leakage and work accidents can be avoided, improving safety. .

  Further, this processor employs the following configuration for each part.

  The inclination angle (θ) of each superconductor rod 40 is 5 ° to 45 °, which is the angle range where the effect is the best, the efficiency is improved, and the time for removing the dirt is reduced.

  The cooling device 43 includes a fixed housing 430 that encloses one side of the superconductor rod 40, a cooling water inlet pipe 431 that is connected to the fixed housing 430 and guides cooling water into the fixed housing 430, and the fixed housing. It is connected to 430 and consists of a cooling water outlet pipe 432 for discharging the water in the fixed housing 430 to the outside. It is the most basic cooling installation, optimally and quickly controlled in the most efficient state. It is easy and provides a cooling effect and at the same time does not waste energy.

  The heating device 42 includes a plurality of fixed housings 420 that wrap the other side of the superconductor rod 40, a heater 422 provided on the other side of the evaporation device 4 (superconductor rod 40), and one fixing for fixing the heater 422. It consists of a frame 421, the most basic heating structure, the most efficient state, optimal, quick, easy to control, failure free, long lasting, providing a heating effect and long-term energy The consumption of is stable. In this case, the heater 422 is a quartz heating tube, is a heating device with good heating effect, low heat loss and zero contamination, which is a well-known know-how and will not be described further.

  The heating device 42 and the cooling device 43 are electrically connected to and controlled by a programmable controller 30 (Programmable Logic Controller, PLC), whereby the operations of the heating device 42 and the cooling device 43 are accurately controlled, and the superconductor The rod 40 quickly heats or lowers the temperature, the evaporation device 4 evaporates the seawater, and the salt of the rod of the superconductor rod 40 can flow with low-temperature seawater that is easy to flow, so there is no wasted energy consumption, Overall efficiency increases.

  FIG. 8 shows an image of seawater desalination by this processor. In FIG. 8, when the water vapor temperature in the vacuum high pressure steam box 1 reaches 150 ° C., the superconductor rod 40 is cooled by the cooling device 43 under the control of the programmable controller 30 (Programmable Logic Controller, PLC), and the temperature is lowered. Salt is generated in the rod 40 of the superconductor rod 40 due to boiling and evaporation of water, and the rainy seawater 5 causes the salt in the superconductor rod 40 to flow, and depending on the inclination angle (θ) of the superconductor rod 40, Condensed water droplets fall at an accelerated rate due to gravity, and the removal of dirt is performed quickly, so that the consumption of heat energy is suppressed. Thereafter, the superconductor rod 40 is heated again by the heating device 42 so that the seawater evaporates, and the evaporation proceeds quickly and the consumption of heat energy is minimized due to the cold / hot intersection of the superconductor rod 40. At times, the saving of thermal energy will cause the seawater to evaporate again quickly, which will be more effective than the conventional distillation seawater desiccator.

The perspective view which shows the whole structure of the honeycomb type seawater desalination processing machine in the 1st Embodiment of this invention. Partially broken perspective view showing the entire configuration of the processing machine Top view of the evaporator of the processor Flow chart showing the flow of seawater desalination by the processor Sectional view showing the image of seawater desalination by the processor The perspective view which shows the whole structure of the honeycomb type seawater desalination processing machine in the 2nd Embodiment of this invention. Cross-sectional perspective view showing the internal configuration of the processor Sectional view showing the image of seawater desalination by the processor

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Vacuum high pressure steam box 11 Seawater inlet pipe 12 Water vapor discharge pipe 121 Adjustable valve 13 Outlet 131 Gravity valve 2 Shower head 3 Temperature controller 30 Programmable controller 4 Evaporator 40 Superconductor rod 41 Fixed plate 42 Heating device 420 Fixed housing 421 Fixed Frame 422 Heater 43 Cooling device 430 Fixed housing 431 Cooling water inlet pipe 432 Cooling water outlet pipe 5 Rainy seawater 6 Water vapor 7 Brine

Claims (10)

Hollow vacuum high pressure steam box 1,
Provided in the upper part of the hollow vacuum high pressure steam box 1, connected to the seawater inlet pipe 11 for guiding seawater into the hollow vacuum high pressure steam box 1 and the end of the pipe, and installed in the hollow vacuum high pressure steam box 1 A shower head 2 installed at a predetermined interval on the evaporator to be
Provided in the upper part of the hollow vacuum high pressure steam box 1, provided in the water vapor discharge pipe 12 for discharging the water vapor in the hollow vacuum high pressure steam box 1 to the outside, and in the water vapor discharge pipe 12, and has a non-return function. An adjustable valve 121 having
A discharge port 13 provided at the bottom of the hollow vacuum high-pressure steam box 1 and a gravity valve 131 provided in the discharge port 13 for discharging brine by reaching a preset weight;
Evaporation apparatus having a plurality of superconductor rods 40 arranged at the same interval in the hollow vacuum high pressure steam box 1 in parallel and arranged at the same interval, and a fixing plate 41 for fixing and coupling the superconductor rods 40. 4 and
A honeycomb-type seawater desalination processor.   The honeycomb type seawater desalination processor according to claim 1, wherein the evaporator 4 is electrically connected to a temperature controller 3 for controlling a cooling temperature switching of the evaporator 4.   The honeycomb type seawater desalination processor according to claim 1, wherein the evaporator 4 has a superconductor rod 40 installed in a direction intersecting with the superconductor rod 40 installed in the evaporator 4 adjacent to each other.   The honeycomb seawater desalination processor according to claim 3, wherein the crossing angle is 90 °. Hollow vacuum high pressure steam box 1,
The hollow vacuum high pressure steam box 1 is provided at least in the upper part or the center of the hollow vacuum high pressure steam box 1 and is connected to a seawater inlet pipe 11 for guiding seawater into the hollow vacuum high pressure steam box 1 and the pipe end. A shower head 2 installed at a predetermined interval on an evaporator installed inside;
Provided in the upper part of the hollow vacuum high pressure steam box 1, provided in the water vapor discharge pipe 12 for discharging the water vapor in the hollow vacuum high pressure steam box 1 to the outside, and in the water vapor discharge pipe 12, and has a non-return function. An adjustable valve 121 having
A discharge port 13 provided at the bottom of the hollow vacuum high-pressure steam box 1 and a gravity valve 131 provided in the discharge port 13 for discharging brine by reaching a preset weight;
A plurality of superconductor rods 40 penetrating through the hollow vacuum high pressure steam box 1, arranged at the same interval, arranged in parallel at the inclination angle (θ) and at the same interval, and the superconductor rods 40 are fixed and coupled. An evaporator 4 having a fixing plate 41 for
At least one cooling device 43 provided at a high position of the evaporator 4 and enclosing one side of the superconductor rod 40 to lower the temperature of the superconductor rod 40;
At least one heating device 42 provided at a low position of the evaporator 4, enclosing one side of the superconductor rod 40 and raising the temperature of the superconductor rod 40;
A honeycomb-type seawater desalination processor.   The honeycomb seawater desalination apparatus according to claim 5, wherein the inclination angle (θ) of the superconductor rod 40 is set to 5 ° to 45 °.   The cooling device 43 includes a fixed housing 430 that encloses the high portion of the superconductor rod 40, a cooling water inlet pipe 431 that is connected to the fixed housing 430 and guides cooling water into the fixed housing 430, and the fixed The honeycomb seawater desalination processor according to claim 5, further comprising a cooling water outlet pipe 432 connected to the casing 430 and configured to discharge water in the fixed casing 430 to the outside.   The heating device 42 includes a plurality of heaters 422 provided at a low position of the superconductor rod 40, a fixed frame 421 for fixing the heaters 422, and a fixed housing that wraps the heaters 422 and the fixed frame 421. The honeycomb type seawater desalination processor according to claim 5, comprising 420.   The honeycomb seawater desalination processor according to claim 8, wherein the heater 422 is a quartz heating tube.   The honeycomb type seawater desalination processor according to claim 5, wherein the heating device and the cooling device 43 are electrically connected to and controlled by the programmable controller 30.

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