TW201238647A - Water treatment system and water treatment method - Google Patents

Abstract

This invention intends to enhance the energy efficiency and to conduct a stable temperature control in a water treatment system. The water treatment system includes a plurality of devices 1, 2, 3, 4; a plurality of pipe zones 11, 12 which connect a plurality of devices adjacent to each other, and within which flows the water, and a heat pump 21 that absorbs heat from heat absorption pipe zones comprising at least one pipe zone 11, and exhausts the heat absorbed from the pipe zone 11 into heat absorption pipe zones comprising at least another one pipe zone 12.

Description

201238647 VI. Description of the Invention [Technical Field of the Invention] [0001] The present invention relates to a water treatment system and a water treatment water treatment system. In particular, the prior art [0002] is a system in which various devices for performing water treatment are connected by U. In this installation, the 'reverse (4)) device, filter device, etc. Each device, etc.) is played to '(f limit, there is an optimum water temperature range. Another -: face, 100 inch is used at the point of use (like 6? 〇 1 plus), for example, 25 (:, 6 〇. The part of the enthalpy that is being circulated, because the pumping heat 寺 随着 , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , Secret _ various parts of the temperature machine. Thieves shirt ° factors [0003] to the super ifim; where the raw water tank will be treated by the bad or membrane device, and sent to the next step. Since the fresh design temperature of the reverse osmosis membrane is 25t, the temperature of the treated water at the π point of the membrane device is adjusted to the temperature in the vicinity, and a plurality of heat exchangers are provided between the raw water tank and the degassing tank. 0004] Patent Document 2 discloses that a heat pump is used in a water treatment system for heat exchange. The pump system is known as an energy efficient heat exchange system. The heat pump draws heat from an external heat source and extracts the heat. Heat is supplied to the heating target or from cooling [Patent Document 1] Japanese Patent Laid-Open Publication No. JP-A-2002-183800 (Patent Document 2) JP-A-2006-095479 SUMMARY OF INVENTION [Problem to be Solved by the Invention] [0005] 睹, from H, for the water to be treated in the water treatment system, the utilization efficiency of one sound w, or even the second oxygen; ^, The problem. & find the load surface, there are the following [0006] object parts: into; 1 force is used to separate heating or cooling, then create a cooler pair. Like the i position. The cooling tower is used to cool the heat of the county. In addition, the cold water in the 'cooling water' is heated and cooled from the entire energy required to cool the target part of the target area. [0007] The heat energy supplied to the target part is generally difficult to convert to the surface heat energy. The miscellaneous material can also use the heat to heat the object part for the τ age but the object part is the high temperature side. When the temperature difference is, the profit method = right Second, to the temperature side and the low temperature side In the case of water, the temperature of the object is high (five) gamma*/current temperature, there is not much temperature difference; and the cooling is set to establish the relationship between Chen and the low temperature side, and it is not : [0008] The effective use of the heat exchanger in the vehicle is limited. Source. ϊί is the surface of the hot __ high temperature hot part of the temperature and the external heat source of the hot pump, its performance will depend on the field, for example, In the case of low-temperature air absorption, the heat absorption is as follows: Ϊ The above-mentioned 'uses of external heat sources such as air heat are easy to smash and it is difficult to stabilize the water temperature in the water treatment system ί 'If the heat pump has a coffee capacity, Although it can alleviate the effects of changes in external temperature conditions, it has a huge impact on costs. Designed in response to a variety of topics, the purpose is to provide a water treatment system and a water treatment method that combine energy efficiency with temperature control. [Technical means to solve the problem] [0009], smear ΐ ϋ The water treatment system has: a plurality of devices; and a plurality of piping sections, between the plurality of devices adjacent to each other, and the water flows inside; and the heat pump, and the interval is the heat absorption f interval, and the heat absorption pipe interval The heat absorption and the section of the Wei pipe are the heat exhaust pipe section ', and the heat energy absorbed between the suction pipe & is discharged to the heat pipe section. ',,, [0010] The heat pump can be used in the heat absorption target portion Take heat energy and make it use heat in the core._县魏'热=卩mi 二--, and the part that needs heat (heating) (heating piping section) The heat transfer from the piping section to the exhaust heat piping section is such that the heat energy discarded by the second cooling is utilized for the heating of the other part, this month b,,, 'the south energy efficiency. ..., [0011] When the interval and the heat-dissipating piping section are temperature-adjusting parts, respectively, it is difficult for Ai Shi to absorb heat, and the performance of the heat pump is lowered. For use =

iSESSSHiS 201238647 ίΐίίΐ The environment is around and can maintain stable heat pump performance. In addition, when the temperature of the outside air drops to a nearby temperature, the gas will be a heat source. If the heat pump of the rib groundwater or seawater is used as a heat source, countermeasures will be required. On the other hand, the present invention does not cause such a problem. Other implementations of i-Ming's provide water treatment system using water treatment system. The door system has a plurality of devices, and a plurality of piping sections connecting the plurality of devices adjacent to each other and the water k passing through the inside. The method includes the following treatments: one of the dental hot sputum sputum is one of the heat-dissipating piping sections, and the heat is taken from the suction piping section J, and the other piping sections of at least i are the heat-discharging piping sections, The heat energy absorbed from the heat absorption piping section is discharged to the heat exhaust piping section. [Effects of the Invention] As described above, according to the present invention, it is possible to provide a water treatment system and a water treatment method which are energy efficient and can perform stable temperature control. [Embodiment] [First Embodiment] A first embodiment of a water treatment system according to the present invention will be described with reference to Figs. The equations are displayed from the various devices constituting the water treatment system, and only the portions related to the embodiment of the present invention are extracted. For practical examples of water treatment systems, please see below. Fig. 1 shows a first piping section (endothermic piping section) 11 of the first and second devices i and 2, and the connection 1 and the like which are adjacent to each other. In the apparatus 2 and the piping area/inter-n, the fluid (water to be treated) flows to the right in the figure from the first apparatus 1 to the second apparatus 2. Similarly, FIG. 1 also shows the third and fourth devices 3 and 4 adjacent to each other, and the second pipe section (heat-dissipating pipe section) i2 that connects them. In the devices 3, 4 and the piping section 12, there is also a fluid (water to be treated) which flows from the third device 3 to the fourth device 6 201238647 = to the right-flow device of the figure, and there is no such thing. harm. Main brother 1 brother 4 device 1~4 Why [0017] Heat rejection ^q. Representation), and the treatment of 7lcA刼4 Ganzi set 4 points requires that the water temperature be low, and the sample and water must be heated. For its example, the standard design temperature is 25 as above. (:, but the treated water of the transflective membrane is added before the R0 membrane device is added. 7 4/, for the low day r must be [0018] For this purpose, the water treatment system is equipped with a pump 21 (endothermic The piping section) absorbs heat and drains to the 2nd = the officer's section 11 heat pump 21 series and the 丨S_fs, u 2 heat piping section). In the embodiment, the helium pump 21 is thermally connected with a space of 12. The actual - over two", and the 1 smear with rolling compression type. Specifically, 埶 pump 21 sentences.

22, used to make ammonia, carbon dicarbonate, fluorocarbon, or R medium evaporation; and the refrigerant _ Μ ί, cold-cooled cold -24, and cold _ _ _ 25 吏 configuration On _ Road 26. Therefore, the refrigerant-surface is connected to the surface of the ^^= Γϋ Γϋ 以 to send, Wei, condense and swell _ ring. In detail, in the secret device 22, the first pipe section U is provided, and the refrigerant is transferred from the fluid flowing through the first pipe section to extract heat and heat. Thereafter, the evaporated refrigerant is turned into a 6-temperature (four) gas phase by the compressor. Next, the refrigerant is sent to the condenser 2 = condensing by discharging heat energy. Further, adjacent to the condenser 24, a first & room 12 is provided to supply the condensed heat discharged during condensation to the second pipe-Lu = fluid. Then, the condensed refrigerant passes through the expansion valve 25 and is cooled under reduced pressure. s j During the operation of one cycle of the heat pump 21, heat is exhausted from the second pipe section u to the second pipe section 12. , , , and 201238647 [0019] At least 'thermal energy that can be extracted from the first piping section 11. Therefore, it is not necessary to change the heat energy U that is moved, and the device (shopping, etc.) is generated to be supplied to the second piping section and to obtain (4) ί 杂 energy system _" heating or cooling power is Q, nearby, 4 power consumption is ^ Temple, defined as Q / L) - generally in 3 ~ 5 open to ί: ίί far less than the generated thermal energy. As described above, the present embodiment shifts to the middle because the thermal energy 12 ′ taken from the first piping section 11 is less likely to cause waste of thermal energy. Moreover, the heat pump 2 can thus achieve less energy consumption. - In the case of cooling and heating, these devices have a fuel storage facility and the like. Among them, it is necessary to provide its n, and the kind of 附, which is strong. Therefore, the heat transfer loss when adding warm water or steam is large, and if it is added, it is disadvantageous in terms of energy efficiency and cost. Moreover, the i pump 52; 罟; ^ also has the problem of requiring a large amount of energy and a large environmental load. The heat transfer loss is minimized by the vicinity of the intermediate portion 11 of the younger brother 1 and the second interval f of the second match f. [0021] = and 'the heat pump 21 can be related to the heat absorption side and the heat removal side of the temperature ί ° = L, r is the heat absorption water temperature and the heat removal side of the water temperature is about the same ^ shape of the water temperature compared to the heat absorption side of the water In the case where the temperature is high, it is also possible to carry out heat transfer = „to cold water, etc., to supply steam (4) when it is hot. This type of day, due to the use of heat pump 21, is not limited to = | between η and 2 The temperature of the piping section 12 can be carried out in the required amount. [8] The form of the source of the 201238647 source can be exemplified by the use of air or external water as heat to extract heat energy that can absorb heat from the air. The air is twisted. However, in the case of the if g interval 12, the second piping section 12 ^ can be performed. When the working gas becomes low temperature, the suction efficiency of the number pump is lowered, and the pumping capacity (performance coefficient) is lowered. Heat will have to increase the capacity of the heat pump first. When the operation is inflated under the hunger, the heat pump capacity (performance coefficient) decreases in the county. ^' The sample must first be cooled to the capacity of the heat pump n function air. . c is below, and = empty is = for defrost, 戎 裒 裒 裒 - 罢 罢 罢 罢 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 十 成本 成本 成本 成本 成本 成本When using [0023] or external water (sea water, ground water, sewage, etc.) as a heat source, it will also cause problems. In the case of external water, the temperature changes are not as large as air, and the temperature of = is relatively stable, but it is still affected by temperature changes. j吏 4 Water 2 ’ (4) Produces a large amount of drainage, so it may also require a large number of instruments or for processing. When it is discharged as sewage, its cost will also be required. ^, in the case of a large amount of external water, there will be restrictions on the location. Moreover, in the case of using sea water, scale measures, salt damage, and corrosion measures are required. Further, [0024] Moreover, the heat utilization mode in which one of the heat absorption or the heat removal is performed by using an external heat source is broadly different from a conventional boiler or cooling tower.埶 The efficiency of the pump itself is high. Therefore, compared with the boiler or the cooling tower, the cost of electricity and the like can be suppressed. On the other hand, in order to cope with the annual load change, there is a problem that the load of the crucible peak is too large, etc., in the water treatment system: "Stomach is practical. [0025] Relative to this In the embodiment, the heat transfer is performed inside the water system where the temperature of the heat source is stable. Therefore, it is difficult to be affected by the external environment. The temperature is limited, and the temperature variation is limited. Therefore, the external heat source is used. To adjust the excessive and insufficient heat. The _ of the flat heat source is only at the minimum, and as far as possible (four) 纟 = $ to make the external movement, because [〇 〇 = in the conventional technology, economic and stable temperature control can be carried out Fig. 2 also shows the same system as Fig. 2. The first intermediate circuit is provided between the present embodiment 11 and the heat pump 21. The heat absorption of the θ officer's section η is transmitted to the heat (4). In the second state, a second intermediate circuit 16 is provided between the second heat pump 21 for reaching the second pipe section 12. Thus, by setting the intermediate circuit b16 and the heat pump 21, the setting position is limited. That is, Yu Yu, Temple I tempered 11 or In the case of the second piping section 12, the g6 pipe piping area ϊίϊί finds many (4) devices with large losses, so it is extremely important to suppress the technology. In the example of Fig. 2, as long as the distance between the first and second piping sections is The p device! is connected to the second device 2, the third device 3, and the first blade 1, and the first and second pipe sections u and 12 are connected to each other, and the intermediate circuits 15 and 16 having small losses are connected, because (4); ; between the H, the pressure f / member ^ and 'the heat system 21 away from the first piping interval 卩 (2) 2 intermediate circuit 16 can also be set to only one of them, or according to the j circuit 15, 16 double, triple In addition, the use is not particularly limited, and it is not necessary to use a corrosive "shell. If the intermediate circuit 15, 16 is filled with 3; the scale flow efficiently carries heat. The charge C〇2' then she In the case of filling water, the embodiment can be described as follows: Fig. 3 201238647 2, the 5th and 6th devices 5, 6, the third pipe section heat connection section, etc., and the design 1 and the third piping section U, 13 suction 2 = the inter-bed environment loop 15. As shown in Fig. 4, the water treatment system includes the above configuration, g includes The following part is designed to circulate the fluid: the second intermediate portion of the seventh and fourth devices and the second and fourth portions of the device that are adjacent to each other. 12, 14 for heat removal. [0028] As shown in the figure, the piping section to be carried out is limited to the crucible or the heat-dissipating side, and a plurality of sections may be provided. That is, the heat-absorbing piping section and the heat-distributing section may also be singular to singular and singular pairs. Any combination of a complex number, a complex number, and a complex number, and a complex number. The position of the heat exhaust pipe is closed or (4) heat, etc., * The intermediate circuit and the plural heat pump are set in the water treatment system. [0029] Regarding the compression capacity of the heat pump 21, generally, the necessary compression capacity Cc of the heat absorption 1 (cooling) in the heat absorption piping section and the necessary compression capacity CH of the heat generation (heating) in response to the heat exhaust piping section are not Will be consistent, decided to match either. Specifically, the following four forms are mentioned. /, (Form i) cH > cc, and the heat-dissipating (heating) side is used to set the compression capacity to Ch. At this time, 'the endothermic (cooling) in the heat-absorbing piping section is excessive, so the heat-absorbing piping section is heated; or a part of the heat energy is taken from the heat-absorbing piping section, and the remaining heat energy is taken from outside the system (for example, heat energy is extracted from the surrounding air, The ambient air is cooled so that the endothermic (cooling) in the endothermic piping section is not excessive. In other words, this technique can also be said to discharge excess cooling energy out of the system. (Form 2) CH > Cc ' and the endothermic (cooling) side is used to set the compression capacity to Cc. At this time, since the heat removal (heating) in the heat exhaust pipe section is insufficient, the heat exhaust pipe section is additionally heated. (Form 3) CH < Cc ' and the heat-dissipating (heating) side is used to set the compression capacity to cH. At this time, since the endothermic (cooling) in the heat absorbing piping section is insufficient, the heat is removed from the π 201238647 endothermic piping section in an additional manner. At this time (formation between the tenth: # ^ between the heat (heating) is excessive, so the heating energy from the heat exhaust piping area is discharged to the outside of the system. Piping, = 2 pairs of heat pipe or heat exchange heat exchange Here, for the system of the $f water treatment system, the 外 ΛΧ ΛΧ ΛΧ 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 参照 排 排 排 排 排 排 排 排 排 排 排 排 排 排 排 排 排Excessive heat absorption (cooling) [0031] In the secret, in order to reduce the heat capacity from the heat system 21 to the first piping 12, the pump 21 is the same as the pump, and the heater is used. The heat system is used. The force is q 为 ϋ , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , ,言, 埶 quantity Qm phase ί ί ^ ^ 5 ΓΛ Γ * * * * * * * * * * q q I I q q q q q I I I I I I I I I I I I Q Q Q Q Q Q Q Q Q Q Q Q Q Q Q Q Q Q And water (4) 纤 撷 k ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; 003 003 003 003 003 003 003 003 003 003 003 003 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热Hot 1 QC1, Asian Heat 1 (3) The discharge is made to the second piping room 12. Among them, the amount of heat Qm from the end to the second piping 12 is the desired amount of heat = lb ^ weeks, and the air is subjected to the heat Qa and the first piping section. Take the heat Q2 which is the difference between the two, and supply it to the second pipe i2. In other words, the heat from the first pipe section 11 and the atmosphere 'requires' Ιίίί pump 27 ', therefore, from a cost point of view, Advantageous 2 [0033] The pump 21 can be of the thermoelectric type in addition to the vapor compression type. Fig. 7 shows an embodiment of the electronic heat system 21, which is the same as the xenon gas. The compression heat pump 21 is replaced by a thermoelectric heat pump, and the basin is therefore 21 years old. Please refer to the above description for the description of the heat exchanger. The heat pump is a heat pump with a principle of 7L (Peltier). The two-body 29 and the n-type semiconductor 3G-based transmission electrode 33 are connected to each other to form an endothermic phenomenon, and the junction-type thermal phenomenon occurs in the n-type semiconductor. The p-type semiconductor 29 and the n-type semiconductor 3 are associated with Mao Shengzheng 31. i piping section U side, and p-type turning n-turning two = second piping section 12 side. Figure 3 shows three ^ knives 32 ^ semiconductor 3 0, but more pi 3 can be arranged in a staggered manner. In addition, hot electrons [0034] In addition, although the illustration is omitted, chemical formulas and fruits can be used. For example, chemical formulas are filled with = The reaction chamber and the cold 13 connected to the reaction chamber through the communication tube are at the position adjacent to the reaction chamber, and the second chamber is at the position of the chamber. Anti-filled with calcium chloride _ water ",, ^ heat, money hydrated water traits into water and moved to the condensation chamber. The water vapor moving to the condensation chamber is detached, to the adjacent position The second piping section is 12. 7 and liquefied, and the heat is discharged [0035] Next, in order to apply the water of the heat pump 21 described above, the water treatment system of the water can be made of ultra-pure water, and various devices such as a drain recovery device ( The unit is configured to be in accordance with the required water quality of the pure water, the quality of the raw water or the water quality of the drainage, etc. The following examples are still in the same example. The same applies to the water treatment system of all the embodiments of the present invention. Also, Ding, 歹可和依[0036] ' 〇 Figure 8 shows the production of ultrapure water in the water treatment system. Although the temperature of the water will be set according to the set position or season ^ 5 C, when pure water is produced, The raw water is passed to the turbid film. After passing through the activated carbon tower 109, it is sent to the RO membrane device 110. The heating is performed for two reasons. The standard design temperature of the reverse osmosis membrane used is pit. _ _ Prevent the salt from the other C "quasi & count a temperature of + Hill, Yan 7 has sense to find the set point. In the RO membrane 奘 Π Π Π Π Π Π Π Π Π Π Π Π Π Π Π Π Π Π Π RO RO RO RO RO RO RO RO RO RO RO RO RO RO RO RO RO ; from the RO points, and stored to the primary pure water tank 112. In order to regenerate the fat, the ion exchange device u heats the test chemical liquid and supplies it to the neutral acid waste liquid. In the middle of the road, I know you * Q, I stupid π 〒 spear groove 113 to make it cool. ',, and according to the need to ride the ship in the towel and slot 113 [0037] 201238647 raw ion exchange unit super (= carry on the gamma. Record the unprocessed point of the continuous cycle operation. At this time, the purity of the cycle: the temperature It is required to raise the person of the pure 3 pump f and so on. Then, the cooling point 119 is provided according to the use point on the side of the mouth. The second is in the siphoning device H4 into the si8^c- ^ -- ultrapure water for u Second, the middle of the branch from the pure water tank out of the high temperature device 122, the cylinder type high purification force; 121 after the temperature rise, through the ultraviolet oxidation using the point 125 stone recognition 1 〇〇 device 123 and ultrafiltration membrane device 124, and then transported to the previous cooling Point temperature ultrapure water, in its return to the primary pure water tank 112 ion ΐ P ° 'Because of the cartridge high purifier device 123 and ultrafiltration, membrane device 曰 in the cartridge high purifier device 123 [0038ί Hot spot 121, in order to replace the heating point (2). Water at the Nazi. _ can be treated by the drain can be directly _5|Bu 4疋7 processing system outside the generator. Also, ultra-pure fine 8A gas: With the drainage treatment. The county is too (four) two observing neoplasms and aerobic microorganisms are 36 ~ 耽 (medium temperature range Another-side dish because 'can also be set to 30~35 °C must have the appropriate temperature for the pit to be around, so the line shows that only the 'drain heating to the best temperature of the aerobic treatment is 201238647 degrees' 20~3〇.(: Left and right. [0040] There is a heating point. In addition, the ammonia money is installed on the side of the lion population by 20~35. (: Left and right. The more the P is, the better the efficiency, and the optimal temperature is [0041] After the anaerobic treatment described above, after the temperature adjustment, the temperature of the water is not required to be adjusted. 地 θ 理 理 理 t t 四 四 四 四 四 四 四 四 四 四 四 四 四 四 ° ° ° ° ° ° ° ° ° ° ° ° ° ° ° ° ° ° The search for the heat energy absorbed by the heat pump [0042] can make the system f. The pure water such as pure water, the water used for the wafer cleaning is transferred to the ultraviolet oxidation device 10 After the hydrogen peroxide, the row (T〇C, t〇tal 〇_e | is used to cool the total organic carbon in the water, and then the organic water is removed in the activated carbon column 103 to be exchanged at the cold portion/point 102 to the exchange device 1G4. When UV oxidizes the component, it is transported to the ion, and the temperature rises sharply. Therefore, ^ 'sometimes The water retention amount is small, and the cooling point 102 is provided. The discharge port side of the material external oxidation device 1〇1 [0043] Fig. 9 shows the pure water explained from the device device described above and the drainage treatment device described in Fig. 8A. An example of manufacturing. With regard to each of these requirements, the second "冓 becomes a water treatment system 100 [0044]. The month, the above description. Figure ·, the surface of the water repair station (four) unified hot water sterilization 16 201238647 The process of the shape, which shows the following system, ion or magnesium ion, and subjected to activated carbon treatment ===== after 'filtering treatment and ultraviolet oxidation. Fig. 10A is an example of the raw m ΐϊ 水 water, which is connected to the hot water source isolated from the pipeline to connect the rr brain; the circuit shown in =====^ ΐ 供给 is supplied with hot water from the hot water source to end the treatment of the cerebral palsy Cool the hot water and drain it. Due to the inflow of the main cooling heat exchanger [0045] In Fig. 8A 1B, the heat exhaust piping section and the heat absorbing piping section 2 are shown in bold lines. However, as explained above, when the water treatment system is in normal operation, there are various discharge pipe sections and sands regardless of whether or not maintenance is performed. [0046] The water treatment system according to the first embodiment described above will be further described in detail by way of examples. 11A to 11C are schematic views showing a portion A of Fig. 9 cut and shown. Fig. 11A shows a case where the heat-dissipating pipe section and the heat-absorbing pipe section are added to the portion by the respective devices (e.g., the hot parent converter) according to the prior art. In the description towel of the town, the flow of the fluid in the heat pipe section is set to 1〇〇t/h (mouth/hour), the water temperature before heating is set to 288k, and the heating degree after heating is set to 298K; The flow rate of the fluid in the piping section was set to 1 〇〇t/h (collar/hour). The water temperature before cooling was set to 3 〇 3 K, and the temperature after cooling was set to 298 k. Further, the specific heat of water was set to 4.2 J/g.K. [0047] If the necessary energy is calculated under the above conditions, the necessary energy in the heat-dissipating piping section is about 1.17xl 〇 3kW, and the necessary energy in the heat-absorbing piping section is about 5 8xl 〇 2kW, 17 201238647 totaling about 1.8 gt; <103 kW of energy. [0048] FIGS. 11B and 11C show the use of a heat pump from a suction pump, 5:6 〇 according to the embodiment;

1 ^ is as follows: H t ' is determined by the necessary heat removal on the heat absorption side, and 2 heat pump 27 (indicated as a gift in 0) distributes heat 1 which is insufficient on the heat removal side. Here, regarding the heat pumps 21 and 27, the u Μ σ 丨 energy coefficient is set to 5 when heated, and the property in the cooling C 〜 25 C _ _ [0049] 5 8xlt2 ^ I2i Example 1} ' is used to obtain the heat absorbing side The necessary compression capacity (about 5^8x10 kW) is about 146><1〇2 Na_=,· spoon will get about 7.3xl〇2kW in the heat removal side. The difference between this force 'exhaust heat (about U (four)): ^ The necessary compression capacity of the heat pump is about 2 ,, 合; to 2.3 = 7 electric energy. This is the comparative example shown in Fig. 11A (the conventional 'discharge, the case of Fig. 3UC (Example 2)' is used to obtain the necessary ability of the drainage side, and the heat absorption side must be kw. If this compression is left The amount is used for atmospheric cooling. Because the heat removal on f is the same, it is also about 2.3xl 〇 2kW. ▲The situation is as follows: [0051] Cooling pump: J dimorphism 'heating with heat pump' The necessary compression capacity of the amount and the necessary heating for cooling _ ^ 増 3 is about 2.3 χ 1 〇 2] ^ = heat ^. Since the heat pumping force on the heating side is about 1.5 x 1 〇 2 kW, then the heat of the JI cold part f The necessary compression energy of the system is advantageous, but compared with the example, the result is still more energy consumption of the above-mentioned 18 201238647. Here, the above description is summarized and shown in Table 1 [0052] Operation necessary heat丨kWl Energy consumption [kW] Comparative example Heating machine water heating 1167 1167 Cooling machine water cooling 583 583 Total 1750 Operation necessary heat [kWl cop Compressibility [kW] Reference example Heat pump water heating 1167 ' 5 233 2 Heat pump water cooling 583 4 146 Total 379 Example 1 Heat pump Heating 729 5 Water cooling 583 4 146 2nd heat pump water heating 438 5 88 Total 233 Example 2 Heat pump water heating 1167 —α α 1 5 Water cooling 583 233 (Wall ~ External cooling L-___ .....-丨一. 350 The heat cycle of hot fruit is generally designed to be a high temperature state (during condensation) and the temperature difference between low temperature = m and m. The reason is that the water is heated. The boiler of the heat pump is designed to discharge high-temperature water in the same manner as the boiler. Generally speaking, in the water treatment line, the rs that will flow through the internal water are extremely high or low. If it is heated [0054] :i into: paying isr, increasing the compression work of the compressor, the heat loss is also increased. Therefore, the temperature difference of the refrigerant = ί55 [ 第55] The second embodiment is fragrant to provide energy efficiency. High and can be used to carry out the water treatment, water treatment and water treatment methods of the 2012 2012 647 stable gif system. The state system shows: 乍 is the heat pump 2, the implementation of the heat pipe section) in the heat pump === word f2 piping section _ also. The actual ^f is controlled in the above temperature range. The second type of piping 'ΐ/: the factory is designed When the outlet temperature of the pump (the outlet of -131 is operated by the heat exchange part, the energy efficiency will increase _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ The above thermal cycle of condensation and expansion. And the body =, in the ^ 77 medium to send the article, compress, cold the high temperature of the fluid for heat & 奂 ("added refrigerant: and TM^de: V ^ The coefficient of performance when heating from the external fluid =}°, : b is such as /w, upper = qc/w. Therefore, the smaller the w, the higher the coefficient of performance, and the energy efficiency ib [0058] The helium ring ABCD corresponds to the condensation temperature and the base, and the second corresponds to the previous higher condensing temperature, the temperature phase is fixed to the cycle w 2Qh , /W,, therefore, when the condensing temperature production "the ancient B Shi as f J, no, because Qh / Similarly, due to Qc / W > 〇円 performance coefficient decreased. Saki QC / W ^ Qg / W, Therefore, the coefficient of performance of the #condensing temperature 20 201238647 is decreased. [0059] The monthly high degree of the degree 'as much as possible to make the condensation temperature and the evaporation temperature fit six + two have / effect. In addition, in the water treatment system In the middle, the temperature of the water fluctuates, and only the temperature difference between the temperature and the ambient temperature is several tens of degrees. Thus, the difference between the condensation temperature and the evaporation temperature of the refrigerant can be suppressed by setting the target water temperature of the water to be controlled by the temperature. for

Ϊΐίίΐ (such as the R0 membrane device), as usual, control its temperature in the work and dry circumference. Therefore, if the water temperature at a specific portion is adjusted to a difference between the condensation temperature and the evaporation temperature of 20 to 35 ° C, the energy efficiency can be performed. [0060] The compression plus 2 charge is as follows. In the general water heating or hot water supply steam, the human ... pump, the factory, the source is roughly divided into water and air. When the heat source is water, it is mainly ^ ^, and when the heat source is air, the outside air is the object. The situation of water is self-evident, and: the situation of being more suffocating is also in the water. . The end of the neighborhood. Therefore, the cold=degree will be higher than 〇c so that the line cannot be actually moved downward along the longitudinal axis. The position of the line CD(C, D,) depends on the compression work of the compressor. 12 The water temperature at the outlet side of the vapor compression heat pump is set from: ^ The condensing temperature can be lowered. 'The wire can reduce the compressor, and the performance coefficient of the heat pump is increased to improve the operating efficiency. ρ Λ Λ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ The difference in evaporation temperature may be small, and the energy efficiency may be further improved. ^ ^ [0062] The above-described "any embodiment shown in Figs. 1 to 6 is controlled by the second piping area = (or 14). When the pipe is to be piped, it is only necessary to set the heat in the second pipe section 14) to the vapor compression heat pump 31 = 201238647 to be 20 to 35 ° C. [0063] = that is, the intermediate circuit is provided. The medium temperature of the intermediate circuit has a large heat loss in the intermediate circuit. However, in the present embodiment, the temperature on the π side of the heat pump is 2 G to the low temperature of the hunger, so that the JDL of the medium can be suppressed. Lower, it is possible to suppress heat loss. [0064] ...,, and a bucket, _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ For l, 5kw in the helium pump 'heats the water flowing through the second piping section 12 to ίίίΐΐ The temperature is 2G to 35° C. In the present embodiment, the following is: 2'. “And the heat source of the heat pump. The water on the inlet side of the heat pump for heating the object water is 23t ° by changing the heating object. The water consumption energy and coefficient of performance (COP) of water are as follows. t The outlet side water temperature in each machine, 4 [0065] [Table 2]

Xi =: Medium 2 sets the water temperature on the side of the Μ to be higher. On the other hand, when the water of the adhering object is lowered, the COP is remarkably improved. If the water temperature on the exit side of the ^ cooked f is set to a particularly high COP. Therefore, it can be considered that the difference between the degree of the dish and the evaporation temperature is obtained in the temperature range of =5 ° C. 201238647 [Third embodiment] Since the circulation of the water treatment system When the water to be treated enters the production, the equipment such as a cooling tower or a boiler is generally installed. For example, when heating is performed using a boiler, warm water or steam which is higher in temperature than the portion to be heated is produced by the heat of the boiler to be supplied. 'The heat energy of the heat medium, i.e., warm water or steam, is supplied to the heating target portion. When cooling is performed using a cooling tower, the cooling water which is cooled and cooled is extracted from the cooling target portion. — [0067] In the case of a water treatment system, most of the parts are controlled to a temperature close to normal temperature, for example, the temperature of the warm water or steam produced by the boiler is much higher than the water in the water treatment system. Therefore, when piping water is supplied with warm water or steam, heat loss of the amount of heat may be generated. ’ ' [0068] The heat pump is different from the boiler and so on. It does not need to heat the heat medium to excessively high temperature. Therefore, it is effective as a temperature adjustment mechanism for the water treatment system. Moreover, compared with the boiler guide, the I efficiency of the heat pump is south, and it is easy to suppress power consumption. However, the temperature of the water in the water treatment system may vary due to various reasons such as temperature changes during the day and night. At this point, it is necessary to construct various devices in the water treatment system to operate within the optimum water temperature range, and use a heat pump to appropriately respond to changes in temperature conditions. As for the temperature range required for the point of use, it is also strictly managed according to the intended use. If the heat pump has an excess capacity (compression capacity), the influence due to temperature fluctuations can be alleviated, but the cost is greatly affected. [0069] In the third to sixth embodiments, a water treatment system that easily suppresses an increase in heat pump capacity and a water treatment method using the system are provided. [_] Dream Figure 14A, water system, system 201a has: a first officer section 2〇2 (endothermic piping section) connected to a plurality of adjacent nodes D1 and D2, and a piping area 23 201238647 202 - part of the heat pump 2 〇 3, the first! Thermal storage mechanism, and 1 shunt tube 205. The i-pipe connection 2〇2 is required for cooling in the water treatment system. The first piping section 202 is generally designed to allow water to flow therebetween, but is designed to contain any fluid flowing between the basins other than water or gas. The eighth water treatment system 201a further includes a second piping section 222 (heat exhaust piping section) and a second heat storage mechanism - a second bypass pipe 225 which are disposed adjacent to each other. The second piping section 222 is also designed to allow water to flow therebetween. 203 is connected to the first pipe section 2〇2 in the connection portion 206 of the first pipe section 202, and can exchange heat with the water flowing through the first pipe section 202; and the heat pump 203 is also A part of the piping section 222 is thermally connected to the connecting portion 226, and heat can be transferred between the water flowing through the second piping section 222. Therefore, the heat transfer from the first pipe section 202 and the second pipe section 222 can be transmitted through the heat pump 203'. In one embodiment, the heat pump 203 is of a vapor compression type. Fig. 14B is a partial detailed view of the heat pump 203 shown in Fig. 14B. The heat pump 203 includes: an evaporator 2〇3a for evaporating a refrigerant such as ammonia carbon dicarbonate, a fluorocarbon, or a fluorolong substitute such as R410A; and a compressor 2〇3b for compressing the refrigerant, and a refrigerant Condensation condensation benefit 203c, and expansion valve 2〇3d for expanding the refrigerant. These elements are placed in this order on circuit 203e. The refrigerant circulates in the closed circuit 2〇3e, and receives a thermal cycle of evaporation, compression, condensation, and expansion. In detail, the evaporator is thermally connected to the first pipe section 202 at the connection portion 206, and the heat of heat QC is extracted from the water flowing through the first pipe section 202 by the heat of vaporization at the time of evaporation of the refrigerant. Further, the evaporated refrigerant is compressed by the compressor 203b to become a high-temperature high-pressure gas phase. Next, the refrigerant is sent to the condenser 203c. The condenser 203c is thermally connected to the second piping area = 222 at the connecting portion 226 to supply the condensation heat QH discharged during the condensation to the water flowing through the second dispensing section 222. Further, the condensed refrigerant is cooled by the expansion valve 2 under reduced pressure. In the operation of one cycle of the heat pump 203, the cooling of the second piping section 202 and the heating of the second piping section 222 are performed. 24 201238647 • 【0073】 In addition to the vapor compression type, it is also possible to use a 敎 electronic type, a 4 adsorption type or an absorption type heat pump.叩:, ', package 10, chemical formula, [0074], and chestnut section 202 are compared with the downstream side of the heat storage mechanism 204, and the first flow rate 2 ϋτ211 is provided, and the flow rate adjustment can be used. The first tube 205 is adjusted from the first tying door 2 (7) to the upstream side of the connecting portion, and the two-way valve 208 ' can be adjusted for the flow ratio of the water to the squid 1 . In addition, the person who is in the piping section 202 with the brother 1 has a weeping sputum - 乜 在 第 第 第 第 第 第 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 205 007 007 007 007 In the piping section 202, the first point and the lower side of the L person ▲ are provided, and the first is provided! The temperature sensor 20f: the junction of the first blade 205 is [0077] The phase control unit 210 adjusts the opening degree of the two valves according to the water 测定 2 measured by the first temperature sensor 209, and Flow into the first / degree Τ 2, = ' and adjust the second! Flow adjustment machine "two; = the flow of water flowing out of the mechanism 204 to control. Saki Yuki first heat storage [0078] i J 2 storage mechanism 224 is set at 2 in the piping section 222, the filament-part portion. The second heat storage mechanism 224 and at least the storage tank of the first water. In the second heat storage: the structure 7(3). As the second flow rate adjusting machine, the second 25 201238647 The second branch pipe 225 branches from the second pipe section 222 on the upstream side of the connection portion 226, and merges with the second pipe section 222 on the downstream side of the second heat storage mechanism 224. The three-way valve 228 is provided to adjust the flow rate ratio of the water flowing to the second pipe section 222 and the second branch pipe 225. Alternatively, the three-way pipe 225 and the second pipe section 222 may be provided in a three-way flow. The valve replaces the second flow rate renewal mechanism 231. ^ [0080] The comparison between the second piping section 222 and the second The merging portion of the flow tube 225 is on the downstream side, and the second temperature sensor 229 is provided. [0081] The second control unit 23 depends on the temperature T2' of the water measured by the second temperature sensor 229, and flows in. The flow rate of the water in the second shunt tube 225 and the flow rate of the water flowing out from the second heat & configuration = 24 are controlled. Further, the second control unit 23A can be configured as a control unit common to the first control unit 210. [0082] f, the operation of the water treatment system 2〇1& described above is explained. In the simple example of t, the following is the case: the water of the temperature τι is in the fixed flow interval 222, in the three-way valve 228 branches into a second piping section 222 3 225 'and then merges to supply warm water as temperature T2.

Taking the time and degree of the time, in contrast, the temperature T1 is assumed to be ^jtm ^, and the heat supply QH ^ 224 201a ^ [0083] received by the heat pump 203 is used. 'The two squares 228 are first adjusted to flow into the second distribution, and the ratio of H, L is assumed to be a predetermined value. Here, the second shunt tube 225 is simplified for the purpose of 224. Further, the second heat storage machine cleaning mechanism 231 is first set to a state in which the flow rate adjustment is not performed, and 26 201238647 'that is, the total amount of water directly passes through the shape of the second heat storage mechanism 224. After the autumn, the pump 203 is started, and the continuous measurement is carried out at a temperature T1, a water supply, and a temperature T2 of the water on the outlet side. Using the brother 2 / dish to measure 229 pairs [0084] At the temperature T2, exceed the target temperature, the following fall. The first two square valves = 28, so that the - part of the water flow flows into the second shunt tube 225. However, it is recorded that only the water flowing through the second piping section 222 has a flow rate of _ _ temperature T2, so the temperament: with the second ',, the second flow reduction of the outlet side of the storage mechanism 224 The water in the flow rate of the second heat storage mechanism 224 on the outlet side and the water flowing through the second branch pipe 225 have the same effect as the total heat loss to the combined water, and can be low. And the temperature T2' is controlled to the target temperature. The junction that performs the above operation = the second heat storage mechanism 224 stores warm water, that is, heat. ', ' ° ; [0085] ‘,,, and 3 ^ ^ temperature Τ 2, from the situation where the target temperature drops. In this case, 2'_the heat required at the target temperature is not enough, so the control unit f 231 ' is such that when the aborted 流出 flowing out of the second heat storage mechanism 224 is returned to the target temperature, the state is maintained; In the case of Ϊ, , the upper heat storage mechanism is further created by the second heat storage mechanism: this means that the second heat storage lining 224 夂 fills up the insufficient heat. In this way, the white amount of μ 2Q or more can be supplied to the water flow, and the temperature T2 can be controlled to be the same as that shown in the figure. 15 eight ιΤηΐ^ϊΖ^ 5 ® 15Β 2 The relationship between the fox water storage I. At a temperature of 71, the higher the amount of warm water stored in the second heat storage mechanism 224 is increased (in the heat of storage). In other words, the second heat storage mechanism 224 can heat one of the heat exchangeable between the heat pump 203 and the second portion of the heat exchanger 203. The heat exchange can be performed according to the temperature T1. And the situation. When the temperature enthalpy becomes low, the amount of warm water in the storage mechanism 224 is temporarily reduced (i.e., heat consumption) due to insufficient heating amount. When the temperature T2 of the first piping section 202 is lower than the temperature T2 of the first piping section 202, the temperature is lowered by cooling. The low temperature water stored in 2〇4 is used to cool the water to the desired level, and the mechanism 204 can temporarily heat the heat pump 203 and at least a part of the storage capacity of the i-th pipe g (ie, part or all). 1 is a cold water. The cold water can flow from the first piping section. The first thermal storage shaft 4 can be stored as i: [_] as in the present embodiment, it will be in the water treatment system. It is possible to greatly improve the energy efficiency by heating and cooling the other piping sections from one of the heat exchangers. In this regard, referring to Figs. 16A to 16F, the left side shows the piping to be heated.

Hi ft requires the necessary heat absorption heat of the piping section to be cooled.求 Simplify, single, change with time, the necessary heat absorption is set to be fixed ... can ^ =; Λ. The reason for the fluctuation of the necessary heating heat in the pure processing is to increase the temperature of the raw water at night and the like. [0090] (4) The figure shows that the two pairs of iti! 7 objects constituting the heat pump 203, which are the most suitable for the heat of the necessary heat, are taken up by the heat pump, and are transferred by the heat pump, and i詈it;: iqh' is therefore compared with the individual Cooling and heating, month b •...A. However, in this example, since the endothermic heat QC is smaller than the necessary endothermic heat 28 201238647, it is necessary to use the same amount of suction heat as the other type of cooling mechanism, as shown in Fig. 16C. Others [0091] Fig. 16D shows that the average of the necessary heating heat is combined to constitute the hot fruit 2〇3. In this case, since the heat transferred by the wire 203 is increased, the energy efficiency is further improved as compared with the figure-column. However, in this example, since the heat absorption is still relatively small, the heat absorption heat is required to be small. Therefore, as shown in Fig. 16E, the two mechanisms must make up the amount of heat absorption heat QC. Similarly, an insufficient amount of heating mechanism is used to make up. Moreover, the excess addition must be discarded and become the cause of the decline in energy efficiency. The _^@ example of the example of the deposit diagram should be discarded. This example shows the excess heating heat QH," plus the shortage I The secret agent assumes that the two are not-induced, and that the (four) f-structure can also be used; However, even if the amount of heating is insufficient, the amount is high. In addition to the water treatment vehicle form of the embodiment of FIG. 17 and the embodiment of the water treatment vehicle of the embodiment 4 of FIG. 17 , the heat absorption heat amount QC ′′ is required to be the first embodiment. 3Implement 2〇4 backflow to: The cooling capacity of the upstream storage mechanism ΐΓϊϊ, ί^:^ 1 204 29 201238647 at the connection section. [0094] Π, 224, can also be provided with the same return pipe. The second pipe section 22^m return pipe 235 is used to make the water flow back to: the branching portion of the 225 is the lower side, so the upstream side of the spoon connecting portion 226, and the warm water t2 stored by the second shunt tube The second heat storage mechanism 224 uses the heat pump 203 to heat exchange and the temperature is lowered. Therefore, the temperature of the water can be reduced by the water of the JJ^9 Aj, 々丨L tube 235. σ热, IS] The remaining portion of the wire stored in the storage mechanism 224 is lower than the inflow portion η of the Δ start a 2 brother 2 interval 226. #1, The uppermost inflow portion Η is preferably disposed on the upper side of the second heat storage mechanism 224, and the warm water heated by the heat pump is stored in 224 households. Since the second heat storage mechanism 224 is in a short-lived condition, the second heat storage mechanism 224 is in a state of being layered by both the right water and the low water in the second heat storage mechanism, so that the low temperature can be efficiently (2) The heat storage mechanism 224 is supplied to the heat (4) 3 to improve the heating efficiency. [0096] (Fifth Embodiment) The door %2 is the same as the third and fourth embodiments, and is applied to the case where heating is performed from another piping in one piping area. The mosquito is provided with the intermediate m in the same embodiment. * As shown in Fig. 18, the water treatment system 2 has a first piping section, /, ..., pump 203 which is designed to allow water to flow therebetween. In this embodiment The water treatment system 2〇lc also has a = road 212. The first intermediate circuit 212 is partially connected to the i-th pipe section 2〇2^ and the heat pump 203 is connected to the connection parts 206 and 216, respectively. The intermediate circuit 212 is set to 201238647. = Between: There is no special restriction on the flow through the first piping area, and it is not necessary to use the ^. Also, if the first heat medium can be in the first middle _ road 2 = / = Zhao, silk (four) scale-forming fluid Efficiently carry heat energy. Filling 2' is better than filling water. '0097 218 from the middle of the second intermediate system / intermediate circuit shunt tube 214 'the three-way valve ^ f 11 M212 ^ and the heat pump 203 side of the connection adjacent / σ brother 1 heat medium flow direction, and on the downstream side of the first pipe from The first intermediate circuit 212 branches and 212 merges: the upstream side of the connecting portion 206 of the first °°·| φρν/' and the first intermediate circuit are used to flow through the i-th heat storage mechanism 213, and the first side is swam. [0098] The first temperature sense is set in the connection side of the second intermediate pipe 212 to the second intermediate pipe 212. ' 2 The first control unit 210 depends on the i-th temperature sensor 2 〇 = for the inflow! The flow rate of the first heat medium flowing out of the intermediate circuit shunt pipe 214 is controlled by the flow rate of the first heat medium flowing out of the third pipe. The water treatment system 2〇lc has the second pipe = the intermediate circuit 232, the fourth The heat storage mechanism 233 and the second middle eight, the second intermediate circuit 232 are connected to the second pipe section, and the second officer 234 is thermally connected to the connecting portions 226 and 236. The second intermediate knife = the 203 / knife medium is in the middle of the flow, and the second medium is used for the interval between the heat and the heat between the second and the second heat and the hot chest 2〇3. 2 and the second piping section 222 between the heat "accepted 31 201238647. Use: u heat medium, can be prepared with the first heat fine sample. · Specific and ancient, the second ^ knife branch, sub- downstream and the second The intermediate circuit 232 merges, and the branching word 234 branches along the flow direction of the second heat medium, and branches from the second intermediate circuit 232 on the downstream side of the second pipe, and merges 232. In the second, pv, the connection, The upstream side of the 226 and the second intermediate circuit are used to flow through the second intermediate mechanism 233. The fourth flow rate adjusting mechanism 23 is provided on the temporary side of the fourth intermediate storage unit ▲. = the second heat, the lower flow direction of the I shell [0102] The joint portion of the tube|=:= The flow rate of the second heat medium flowing out of the mechanism 233 is performed, [0105] The structure of the intermediate circuit of the first form is known. The pump tank circuit 212 and the second intermediate circuit 232 can sometimes be moderated. In the water treatment system, the heat pump 203 is used. The general 2 is too large, and the pressure is ί Ϊ Ϊ Ϊ = 2. 2 The connection can be made with the shortest pipe length. Therefore, the pressure loss of the water treatment system can be suppressed. Moreover, 32 201238647 203 is away from the first piping section 202 and the like, and this advantage shows that the middle intermediate circuit 212 can also be used as needed. In addition, the second intermediate circuit 232 is the same as the second intermediate circuit 232. - Heavy and double circuit. [0106] Further, although not shown, at least one of the first intermediate circuit 212 and the cymbal may be combined with a plurality of pipes. The interval 埶2, the road 32 is the second intermediate circuit 232' and the gamma tube tube 222 that needs to be heated is heated. Since the middle circuit is ^=2 = _ 岐 卩, '[0107] For the water treatment system 2 described above, the water is solid = 222, and is supplied as the warm water of the temperature T2, wherein the j ^ gate reaches the target temperature, and the temperature T1 is False == The heat QH received by the heat pump 203 is set to ί二Γ The heat is given to the second 2^^^^==233; The second heat medium of the intermediate circuit 232 is the heat i2G3 222 water exchanges heat ~ Ya Ya [0108] First, in terms of initial state, first three parties The r in 2 becomes a predetermined value. Here, (10) + ί the intermediate circuit branch pipe 234. Further, after the fourth bank is stored, the second flow rate adjusting mechanism 231 is set to the off state. 3 Τ 1 1 feed water flow ' and use the second temperature to sense the temperature τ 2 of the water loss, continuous measurement. Three parties = 3 ί, Ϊ first super = target situation, the following operations. First, adjust the first; a part of the mussel inflow The second intermediate circuit shunt tube 234. 33 201238647 By this, the flow rate of the second heat medium circulating in the second intermediate circuit 232 is reduced, and the amount of heat supplied to the water per unit time is lowered. As a result, the temperature T2 can be lowered, and the temperature T2 can be controlled to the target temperature. As a result of the above operation, the fourth heat storage means 233 stores the heat amount of the second heat medium which has been heated. [0110] ' Next, the temperature T2' is lowered from the target temperature. In this case, since the amount of enthalpy required to maintain the temperature Τ2' at the target temperature is insufficient, the second flow rate adjusting mechanism 231 is suppressed, so that the first heat storage medium stored in the fourth heat storage mechanism ′ is at a predetermined flow rate. emission. The flow rate of the discharge depends on the amount of heat that is insufficient, which can be determined by the measurement results. Thus, the heat stored in the fourth heat storage means 233 can be observed, so that the temperature τ2 can be controlled to be the same as the section 202 of the target [0111]. When the first pipe section 202 is lower than the inlet side, the temperature is lowered and the temperature is lowered: 'when the temperature T1 is high, the first touch is made; 1 heat medium to cool the water to a desired temperature [0112] (Sixth embodiment) Referring to Fig. 19, the water treatment system 2〇ld has a calculated first pipe section 2〇2 and a rail pump path 217, It is provided with the water-disc property of the first piping section 202, and is used to flow at least a portion of the first heat of the 'and the third heat storage mechanism 213. The third intermediate circuit 2 is used to divide the heat medium into the first heat storage mechanism 213 of the first circulation circuit 217a7, and the tear circulation circuit of the coffee design is cycled through the third heat storage mechanism 213. The first heat storage device is connected to the first heat storage device, and the medium includes a supply pipe 219a for supplying the first heat medium to 34 201238647 via the third and second ship circuit 2nb. In the same manner, the water treatment system 201d further includes a metering and second piping section 222 and a heat pump 2〇3 path 237 which are provided between the water passing through the second piping section 222 and the heat pump 2〇3, and are used. The fourth heat storage mechanism 233 is used to temporarily double at least a portion of the second heat. The fourth intermediate circuit 237 is divided into a third circulation circuit 237a and a fourth cycle J storage mechanism 233 via the second heat medium, and is calculated as a second ==3 cycle in the connection portion. The connecting portion 236 is circulated with the heat pump period heat storage mechanism 233. Further, the second and second heat mediums are supplied to the supply pipe 239a of the second heat medium via the fourth. The clothing k-way 237b includes a second soil heat-f for the second rising of the J on the inlet side of the piping section 222. The heating is performed and the temperature is «233 2 [0115] on the inlet side of the first piping section 202. , θ + 213 [0116] Preferably, the flow-out portion L flowing to the fourth circulation loop is lower than the flow portion H of the flow f of the fourth circulation loop. In particular, the flow out of the fourth portion of the fourth heat storage unit 233 is preferably located at the lower portion of the fourth heat storage take-up 201238647 233. The reason and the fifth embodiment are described in the following descriptions of the third to sixth embodiments. The heat phase threatening pipe 203 ==; the remaining heat is stored, and it is needed when needed; there is no need to operate the heat in order to cope with the load fluctuation. On the other hand, there is no need to heat the fruit. [0118] (Example) w At 1匕', use the system with the intermediate circuit shown in Figure 20 to carry out the following machine? Use a storage tank with a capacity of 5m3, and use a compression for the wire.

The Lfi energy efficiency coefficient is 4 (when heating). The heat supply was not adjusted according to the load, and the supply heat was fixed at 30 kw (= 75 kW x coefficient of performance 4), and the outlet temperature (outlet water temperature) T4 of the,,,,,,, was set to 65 〇c. The inlet temperature T1 of the heating target water in the heat exhaust piping section is set to vary with the time of day, and the outlet ί is controlled to 25 °c. Further, the discharge flow of the heat medium from the heat storage means is controlled in accordance with the measurement result of the temperature sensor. [0119] The inlet temperature T1 and the outlet temperature T2 of water were set as shown in Table 3. [0120] Table 3. Time (hours) 8:10:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:20 22 22 23 22 22 21 20 20 19 20 20 Water temperature T2fc) 25 25 25 25 25 25 25 25 25 25 25. 25 25

w »-3=. ^ ^ W’J is shown in Table 4. In this table, "flow rate (L/h)" is the supply flow rate of water, and δ history is a fixed value of 6500 L/h. "Required heat (kv/)" means the amount of heat required to warm the water to 25 ° C, which varies with time (ie, inlet temperature τι). "Over and underheating heat (kW)" is the difference between the amount of heat supplied by the heat pump and the amount of heat required, and the case where the amount of heat is sufficient is positive, and the case where the amount of heat is insufficient is negative. "Storage of heat (kwh)" is the heat stored in the thermal storage 36 201238647 sub-organization. When there is a remaining amount of heat pump 30 kW, the addition is stored in the heat storage mechanism, so when the remaining state continues, the stored heat is increased, and FIG. 21A is a diachronic change of the excess and the insufficient heat in the embodiment. Shown on the chart. [0121] 6:00 8:20 21 25 25 6500 6500 35 30 -5 0 5 0 [Table 4]

Table 5 shows the changes in various parameters in the intermediate circuit. The temperature is set equal to the outlet temperature Τ2 of the water. "The amount of water stored in the heat medium storage unit (L/h)" means the amount of heat medium stored in the heat storage mechanism per hour. The "heat medium discharge capacity (L/h)" is not discharged from the heat storage mechanism every hour. The amount of heat medium. On the other hand, the "heat storage (kWh)" in Table 4 is the cumulative value of the heat that has accumulated in the heat storage mechanism before that. [0122] Time (hour) 8:10:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00 T2 (eC) 25 25 25 25 25 25 25 25 25 25 25 25 T4(°C) 65 65 65 65 65 65 65 65 65 65 65 65 effluent warm water 650 650 650 650 650 650 650 650 650 650 650 Heat medium storage mechanism drain 0 0 0 0 0 0 108 217 325 *217 108 heat Media storage mechanism water storage 0 108 217 325 217 • 108 0 0 0 0 0 0

' 'Knife' is a stupid 1* & & 益 益 益 益 益 益 益 益 益 I I I I I I I I I I I I Therefore, there is no need to use other heat sources to reduce the amount of power. In addition, all the necessary heating heat is 72 〇 kWh, and the actual monthly consumption of the package 5 is 18 〇 kWh when converted to the power of the compressor. The supply of 30 kW from the heat pump is the amount of heat that can be exchanged between the heat pump and the heat-dissipating piping section. Between 8:00 and 20:00, only a portion of the heat that can be exchanged for heat is used for heat exchange, and the remaining heat is temporarily stored between _, and the heat of the heat stored temporarily by the heat storage mechanism is used. The shortage is filled. i I. As for the time from 22 o'clock to 8 o'clock, the heat pipe distribution section [0123] (Comparative example 1): the heat supply (kw) of the heat source of the heat storage system is set as the heating factor when the heat is insufficient. "From other hot heat, and negative in the negative situation. The first half ^; = 冓 (pin furnace, etc.) make up the necessary heat 'so do not need to come from other heat sources" Fully all need to go from ~ this, by setting [0124] [Table 6]

Change to the heat of the boiler, etc. 7 ° Figure 21C is the charter. In this case, the necessary energy is also here. The same measurement has been carried out using the configuration in which the heat pump is replaced in the apparatus configuration of the embodiment, and the results are shown in the table. The diachronicity of the excess heat and the excess heat in Comparative Example 2 is shown. The variation is shown in the same form as the embodiment, with all necessary heat being 720 kWh, but 38 201238647 is 720 kWh', which requires 4 times more energy than the embodiment. [0125] [Table 7] Time (hour) 8:10:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00:00 pm ———— inlet water temperature (°c) 21 22 22 23 22 22 21 20 20 19 20 __20^ 25 21 ——— Outlet water temperature (°c) 25 25 25 25 25 25 25 25 25 25 25 Flow t(L) 6500 6500 6500 6500 6500 6500 6500 6500 6500 ] 6500 a 45 6500 6500 35 25 _65〇〇^ *3Λ Necessary heat 〇c\V) 30 25 20 15 20 25 30 [Simplified illustration] [0014] Fig. 1 shows the second and second embodiments of the water treatment system of the present invention. Departure picture. The water treatment system shown in the section is provided with a plurality of money heat pipe area. The pipe water treatment system is provided with a plurality of heat absorption and heat removal modes. The water treatment system shown in Fig. 1 is provided with an auxiliary heating mechanism. In the water treatment system shown in Fig. 1, the water treatment system shown in Fig. 1 is a schematic diagram showing an example of a configuration of a real S water system in which hot metal type hot fruit is used. Figure ΐ shows an overview of other examples of ^. Schematic diagram. Line configuration at the time of hot water sterilization of the water treatment system Fig. 11A is a schematic view showing the configuration of a reference example. 39 201238647 Fig. 1 IB and 11C show schematic views of the configuration of the embodiment. Figure 12 is a line drawing). A line drawing showing the effect of the second embodiment of the present invention (Mollier diagram 13 is a conceptual diagram showing an embodiment of the water treatment system of the present invention. Figs. 14A and 14B are diagrams showing the water treatment of the present invention. Fig. 15B is a schematic view showing the function of the water treatment system shown in Figs. 14A and 14B. Fig. 16A to Fig. 16F show the water treatment system shown in Figs. 14A and 14B. Fig. 17 is a conceptual diagram showing a fourth embodiment of the water treatment system of the present invention. Fig. 18 is a view showing the concept of the fifth embodiment of the water treatment system of the present invention. Fig. 19 is a conceptual view showing a sixth embodiment of the water treatment system of the present invention. Fig. 20 is a schematic view showing the configuration of the water treatment system of the embodiment. Fig. 21A shows the excessive and insufficient heat in the embodiment. Fig. 21B is a graph showing the diachronic change of the excess heat and the insufficient heat in the comparative example. Fig. 21C is a graph showing the diachronic change of the necessary heat in the comparative example. [Description of main component symbols] [0126 ] 1 ～8～第1～8 device 11, 13~3rd pipe section (heat absorption piping section) 12, 14~2nd, 4th piping section (heating piping section) 15, 16~1st, 2nd middle Circuit 21 '21', 27 to heat pump 21a to water heat exchange unit 11b1 to air heat exchange unit 22 to evaporator 201238647 23 to compressor 24 to condenser 25 to expansion valve 26 to closed circuit 29 to p type semiconductor 30 to η Type semiconductor 31 to n-type turn p-type joint portion 32 to p-type to n-type joint portion 33 to electrode 34, 35 to substrate 101 to ultraviolet oxidizer 102 to cooling point 103 to activated carbon column 104 to ion exchange device 105~ Heating point 108 to turbid film 109 to activated carbon column 100 to water treatment system 110 to reverse osmosis membrane device 111 to ion exchange device 112 to primary pure water tank 113 to neutralization tank 114 to ultraviolet oxidizing device 115 to cylindrical high purifier device 116~Ultrafiltration membrane device 117~Use point 118~Circulation circuit 119~Cooling point 120~High temperature ultrapure water supply line 121,12Γ~Heating point 41 201238647 - 122~UV oxidation device 123~Tube type high purifier device 124~ Ultrafiltration membrane device 125 The points 201a, 201b, 201c, and 201d to the water exchange system 202 to the first piping section (the heat absorption piping section) 203 to the heat pump using the points 126 and 128 to the cooling point 127 to the heating points 131 and 132 to the piping section. 203a to evaporator 203b to compressor 203c to condenser 203d to expansion valve 203e to closed circuit 204 to first heat storage mechanism 205 to first branch pipe 206 to connecting portion 208 to three-way valve 209 to first temperature sensor 210 The first control unit 211 to the first flow rate adjustment unit 212 to the first intermediate circuit 213 to the third heat storage unit 214 to the first intermediate circuit branch pipe 215 to the first return flow pipe 216 to the connection portion 217 to the third intermediate circuit 217a to 1st loop circuit 217b to second loop circuit 42 201238647 '218 to tripartite valve 219a to supply pipe 222 to second pipe section (heat exhaust pipe section) 224 to 2nd heat storage mechanism 225 to 2nd branch pipe 226 From the connection portion 228 to the three-way valve 229 to the second temperature sensor 230 to the second control unit 231 to the second flow rate adjustment mechanism 232 to the second intermediate circuit 233 to the fourth heat storage mechanism 234 to the second intermediate circuit branch pipe 235 ~2nd return pipe 236~connection part 237 The fourth intermediate circuit 237a to the third circulation circuit '237b to the fourth circulation circuit 238 to the three-way valve 239a to the supply pipes D1 to D4 to the device Η to the inflow portion L to the outflow portion Q to the heat amount Q2 to the difference heat Qc, QC , Qci ~ endothermic heat 5 QC ', QC" ~ insufficient heat absorption heat Qh, Qh', QH, Qhi ~ heating (heat removal) heat QH', QH" ~ insufficient heating heat r QH'" ~ excess heating heat 43 201238647 ΤΙ , ΤΓ ~ inlet temperature Τ 2, Τ 2' ~ outlet temperature Τ 3 ~ temperature Τ 4 ~ water temperature W, W' ~ compression work

Claims (1)

201238647 VII. Scope of application for patents: 1. A water treatment system having a plurality of devices; and the water is circulated between the plurality of devices that are connected to each other, the piping is::, and from the endothermic Heat-dissipating pipe of heat-absorbing pipe __ '2. If the water treatment room or heat-dissipating pipe area of the first application of the patent scope _t heats or removes heat: , ·· == 1 i heat or to Insufficient heat dissipation or excessive heat pumping of the heat-dissipating _ 2 such as the water treatment system of the patent scope g 2, wherein the mechanism is the fourth. The water treatment system of the j-th aspect of the patent application and at least - The i-th intermediate circuit is provided in the heat-absorbing pipe section = by the heat absorption from the heat-absorbing pipe section to the heat pump; and the second middle road 'han is between the_heat|& official (four) and the Lai pump Use heat to convey the contact area of the Na. The row of the wood suction pump. 5. If the application of the patent item 1 is in the water system, the suction is matched with the setting, and the middle is provided between the plural suction interval and the heat pump. a circuit for squeezing the hot fruit from the wicking section of the Wei endothermic piping section. 45 1 For example, in the water treatment system of the application scope of the patent scope, in the Shen section, there is Wei's and the heat pump is conveyed from the hot fruit in the multiple tube section and the miscellaneous pump. To the multiple heat exhaust piping section. 7. For example, the water surface type, absorption type, adsorption type, thermoelectric type or chemical type of the water in the application scope of the patent scope is the steaming structure, and the system has at least the heat exchanged by the heat storage machine. f hot yarn can be heated between the heat-dissipating pipe sections. t = the connection part of the water treatment system m of the eighth item of the patent range is configured and disposed in the heat-absorbing pipe section, and the heat pump is less than the heat pump. The upstream side of the connecting portion merges with the heat absorbing pipe area door october to the downstream side of the storage mechanism and the heat absorbing pipe section. The s knife, as in the water treatment system of the eighth aspect of the patent application, has: and the stem 2 = s, branches from the endothermic piping section on the upstream side of the connecting portion, and the downstream side of the storage mechanism and the endothermic The piping section merges; and the connecting portion is configured to return water from the first heat storage mechanism to: the suction application area in the hot piping area and the downstream side of the first partial flow f The water treatment system of the eighth aspect has: a connection portion structure and a heat pipe which is disposed in the heat storage pipe section, and the row side from the upstream side of the connection portion in the heat exhaust pipe section, ,, S. . The branch branches and merges with the heat exhaust pipe 46 201238647 in the downstream side of the second heat storage means. 12. The water treatment system according to claim 8 of the patent scope, having: _ ί ΐΓ 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该The heat pipe is arranged such that water flows back from the second heat storage means to the heat exhaust pipe section located on the downstream side. j 2 fine divergence 13. If the water treatment system of the patent scope 帛8 is applied, the second shunt of the basin is smashed between the heat-dissipating sections, and on the downstream side of the second heat storage mechanism, Li In the second part, the part is the heat-discharging section on the downstream side; and in the second heat storage means, the flow of the second total flow from the heat-discharging section is τ in the second heat storage means square. *5 U Department 'is located in the intermediate circuit of the water treatment system of the 8th item of the patent scope, designed to be connected to the suction and distribution, and used to flow through the heat absorption pipe area. The first heat medium to be exchanged is in between; 〃δΛ,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, The upstream a of the connection portion of the pipe section is provided to the first heat medium of the first intermediate circuit of the second and second heat storage means via the third heat storage means for temporarily storing the flow knife. 1 No. 5·3=Please request a water treatment system with a scope of 苐8, send I right. The third intermediate circuit is designed to be connected with the heat absorption. Yes, the friends come through the heat-absorbing pipe. The first heat medium flows therebetween; and 笊/, heat is transferred between the heat pumps, wherein the third heat storage mechanism 'is temporarily stored at least a portion of the ith heat medium; the third intermediate circuit includes ··j Thermally connected, the first heat medium is designed to be circulated with the pumping mechanism via the λ heat absorbing pipe 'and the second circulation circuit', and the material is circulated through the third heat storage mechanism: And the flow of the first medium of the i-th heat medium is performed on the upstream side of the connection portion with the heat-dissipating pipe section, and the second heat storage mechanism is provided in the second towel. At least a portion of the second heat medium that flows back between the second intermediate circuits is temporarily as wide as the water treatment system of the application of the eighth aspect of the invention, wherein: the miscellaneous 'designed to be separate from the heat-dissipating pipe section and the heat pump Sexually ίί, the water and the heat passing through the heat pipe section The fourth heat storage mechanism is used to temporarily store at least a portion of the second heat medium; 48 201238647 wherein the fourth intermediate circuit includes: Interval thermal connection, and the first technical circuit is designed to be connected with the heat exhaust pipe; and the fourth circulation circuit is designed to circulate the fourth heat storage mechanism and circulate the material through the fourth heat storage mechanism. And the second heat medium 18. The fourth intermediate circuit of the eighth aspect of the patent application is designed as a * 兮 $ system, which has: =, and is used to flow through the heat distribution; the heat pump respectively The second heat medium is thermally distributed; and a heat is exchanged between the pumps, wherein the fourth heat storage mechanism temporarily stores at least a portion of the second age; the fourth intermediate circuit includes: a third cycle < Thermally connected, and the second heat medium is circulated through the heat-discharging pipe of the I, and is designed to circulate the material through the fourth heat storage mechanism through the fourth heat storage mechanism. The fourth cycle flows from the inflow portion of the fourth circulation circuit Below. , ~, machine (5) 邛 is located in the water treatment system of the scope of the patent application, the gas compression type heat pump, and in the heat pipe section and the hot chestnut, Ί ', ', is the outlet side of the steaming part The water temperature is 2 〇 ~ 35 ° C. ^ S line..., the father's taste of 2〇·If you apply for the water treatment system of the 19th item of the patent scope, the section of the population of the second part of the section of the Ming Dynasty is changed to '' ^ ^ Institution 21. If the scope of patent application is 19 In the water treatment system of the item, the water treatment system of the heat treatment pipe section or the heat absorption pipe section is added to or otherwise;; 201224647 - 22. The water treatment system of claim 19 The intermediate circuit is provided between: the heat-dissipating pipe section and the heat pump, or at least one of the heat-absorbing pipe section and the vapor compression heat pump, for the heat-dissipating pipe section or the heat absorbing section The piping section exchanges heat with the heat pump. 23. The water treatment system of claim 19, wherein the heat pump heats the water flowing through the inlet side piping section of the reverse osmosis membrane device to a water temperature of 23 to 25 〇C. [24] The water treatment system of claim 19, wherein the heat pump heats the water flowing through the inlet side piping section of the ultraviolet oxidizing apparatus to a water temperature of 20 to 30 °C. Soil The water treatment system of claim 19, wherein the heat pump heats the water flowing through the inlet side piping section of the ammonia stripping device to a water temperature of 2 〇 35 Torr. _26. For example, the water treatment system of claim 19, wherein the heat pump heats the water in the inlet side piping section of the aerobic treatment device to a water temperature of 2 〇 to 30 P. 〇 Λ 7. The water treatment method adopts a water treatment system which has a plurality of piping sections of a plurality of packages, which are connected between the plurality of devices adjacent to each other, and have water circulation therein; and the 孰 ΐ ΐ ΐ 湘 湘 heat pump 'At least one thin tube section is sucked:,, and the heat is absorbed from the endothermic piping section, and is absorbed from the endothermic piping section by at least the bean 2::^: 28. A method for treating water, comprising: a water passing step of passing water to a heat-discharging pipe 50 connected to a vapor-compressed heat pumping stage; 201238647 section and an endothermic piping section; and a shrinking-type operation to make the noodle type hot In the above-mentioned steaming, the condensing step of the refrigerant is carried out, and the heat transfer piping section is carried out in the heat-absorbing piping section. The control is performed to make the heat-discharging piping section 20 to 35. = (10) type heating process age _ part 1 _ water temperature is 51