JP5664852B2 - Solar water heating system - Google Patents
Solar water heating system Download PDFInfo
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- JP5664852B2 JP5664852B2 JP2010242708A JP2010242708A JP5664852B2 JP 5664852 B2 JP5664852 B2 JP 5664852B2 JP 2010242708 A JP2010242708 A JP 2010242708A JP 2010242708 A JP2010242708 A JP 2010242708A JP 5664852 B2 JP5664852 B2 JP 5664852B2
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 112
- 238000010438 heat treatment Methods 0.000 title claims description 32
- 229910001285 shape-memory alloy Inorganic materials 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 15
- 238000000926 separation method Methods 0.000 claims description 5
- 238000009835 boiling Methods 0.000 description 47
- 238000004891 communication Methods 0.000 description 12
- 238000005338 heat storage Methods 0.000 description 11
- 238000009825 accumulation Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 230000002093 peripheral effect Effects 0.000 description 6
- 238000005192 partition Methods 0.000 description 5
- 230000003111 delayed effect Effects 0.000 description 4
- 230000017525 heat dissipation Effects 0.000 description 4
- 238000013459 approach Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- 230000002528 anti-freeze Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
Landscapes
- Heat-Pump Type And Storage Water Heaters (AREA)
Description
本発明は、循環ポンプの作動により、貯湯タンク内の湯水を熱交換加熱するための熱交換器と、太陽熱の集熱パネルとの間で熱媒を強制循環させることで太陽熱の集熱を温水として貯湯タンク内に蓄熱し、この温水を給湯等に利用するために用いられる太陽熱温水システムに関し、特に集熱パネルで沸騰が開始するのを遅らせ、たとえ沸騰が発生したとしても沸騰蒸気に起因する水崩れの発生や集熱回路内における熱媒量不足の発生を抑制・防止し得るようにするための技術に係る。 According to the present invention, solar heat collection is performed by forcibly circulating a heat medium between a heat exchanger for heat exchange heating of hot water in a hot water storage tank and a solar heat collection panel by operating a circulation pump. As for the solar hot water system used to store heat in a hot water storage tank and to use this hot water for hot water supply, etc., in particular, it delays the start of boiling in the heat collection panel, even if boiling occurs due to boiling steam The present invention relates to a technique for enabling to suppress / prevent water collapse and heat medium shortage in a heat collecting circuit.
従来、強制循環手段である循環ポンプを用いない太陽熱利用温水器において、太陽熱を吸収するコレクタと貯湯槽とを連結するための温水取出管に機械作動式の流量調節弁を介装することが提案されている(例えば特許文献1参照)。このものでは、流量調節弁として、温水取出管の途中を仕切る隔壁に孔を貫通形成し、バイメタルにより付勢した弁体でその孔を閉止するようにしている。これにより、コレクタでの集熱により水温が上昇すればバイメタルが湾曲して弁体が開くというように、水温が高く上昇するほど大きく開口させて温水の流量を増大させることを意図している。 Conventionally, in solar water heaters that do not use a circulation pump, which is a forced circulation means, it has been proposed to install a mechanically operated flow control valve in the hot water outlet pipe for connecting the collector that absorbs solar heat and the hot water tank (For example, refer to Patent Document 1). In this device, a hole is formed through a partition wall that partitions the hot water discharge pipe as a flow control valve, and the hole is closed by a valve body biased by a bimetal. In this way, if the water temperature rises due to heat collection by the collector, the bimetal is bent and the valve body is opened, so that the flow rate of the hot water is increased by increasing the water temperature so as to increase.
又、複数の集熱パネル毎に一単位の集熱器群を構成し、複数の集熱器群を直列に配設したソーラシステムにおいて、複数の集熱器群毎に熱媒出口近傍に流量制御装置を設け、熱媒温度が高いほど流量を増加させるようにすることも提案されている(例えば特許文献2参照)。このものでは、流量制御装置の例として、形状記憶合金を用いて低温になれば流量を低減させ、高温になれば流量を増加させるように開閉させるものが提案されている。
さらに、太陽熱温水器において、集熱パネルの熱媒出口に設けた開閉弁として、形状記憶合金ワイヤにより開閉作動されるようにし、熱媒が高温になれば開となり、低温になれば復元して閉となるようにしたものが提案されている(例えば特許文献3参照)。
Moreover, in a solar system in which a single heat collector group is configured for each of the plurality of heat collector panels, and the plurality of heat collector groups are arranged in series, the flow rate near the heat medium outlet for each of the plurality of heat collector groups. It has also been proposed to provide a control device and increase the flow rate as the temperature of the heat medium increases (see, for example, Patent Document 2). In this device, as an example of the flow rate control device, a shape memory alloy is proposed that opens and closes so as to reduce the flow rate when the temperature is low and increase the flow rate when the temperature is high.
Furthermore, in a solar water heater, as an on-off valve provided at the heat medium outlet of the heat collecting panel, it is opened and closed by a shape memory alloy wire, opened when the heat medium becomes high temperature, restored when it becomes low temperature What has been closed has been proposed (see, for example, Patent Document 3).
ところで、家屋の屋根上等に設置される集熱パネルにおいては強力な太陽光に照らされて内部の熱媒(例えば不凍液)が沸騰するに至る場合がある。沸騰が発生すると、その結果、集熱パネル内に沸騰蒸気(気泡)が発生して充満し、これに伴い熱媒が集熱パネルから半密閉式の集熱循環回路内に下降してしまうという水崩れの原因になったり、それが気液分離部から溢れ出して以後の集熱運転時における熱媒不足の原因になったりする、という不都合発生のおそれがある。 By the way, in the heat collection panel installed on the roof of a house, etc., an internal heat medium (for example, antifreeze liquid) may boil by being illuminated with strong sunlight. When boiling occurs, as a result, boiling steam (bubbles) is generated and filled in the heat collecting panel, and as a result, the heat medium falls from the heat collecting panel into the semi-enclosed heat collecting circuit. There is a risk of inconveniences such as causing water collapse or overflowing from the gas-liquid separator and causing a shortage of heat medium during the subsequent heat collecting operation.
近年の太陽熱利用の普及に伴い、集熱パネルを従来よりもさらに高所(例えば3階建て家屋の屋根上等の高低差が10m以上の高所)に設置することが行われるようになりつつあり、集熱パネルと貯湯タンクとの高低差がより大きくなる傾向にある。これに伴い、前記の不都合発生のおそれはより高まることになると考えられる。 With the spread of solar heat use in recent years, it is becoming possible to install a heat collecting panel at a higher place than before (for example, a height difference of 10 m or more on the roof of a three-story house). There is a tendency that the height difference between the heat collecting panel and the hot water storage tank becomes larger. In connection with this, it is thought that the possibility of the occurrence of the inconvenience is further increased.
又、従来の技術としては、集熱により熱媒の温度が高くなれば、より多くの熱媒を循環させて貯湯に利用させることで、より大きな集熱量を得ようという手法が採られているものの、かかる手法は通常時の集熱運転に対するものであり、前記の如き沸騰発生に起因する不都合発生をより助長するおそれもある。 In addition, as a conventional technique, when the temperature of the heat medium increases due to heat collection, a technique for obtaining a larger amount of heat collection by circulating more heat medium and using it for hot water storage has been adopted. However, this method is for normal heat collecting operation, and there is a risk of further inconvenience due to the occurrence of boiling as described above.
本発明は、このような事情に鑑みてなされたものであり、その目的とするところは、沸騰の開始をより遅らせて沸騰を生じ難くし、たとえ沸騰が発生したとしても沸騰に起因する不都合を生じ難くし得る太陽熱温水システムを提供することにある。 The present invention has been made in view of such circumstances, and its purpose is to delay the start of boiling to make it difficult for boiling to occur, and to prevent inconvenience caused by boiling even if boiling occurs. The object is to provide a solar water heating system that is less likely to occur.
上記目的を達成するために、本発明では、太陽熱を集熱して熱媒を加熱する集熱パネルと、貯湯タンクと、この貯湯タンク内の湯水を熱交換加熱するための熱交換器と、循環ポンプの作動により前記集熱パネルと前記熱交換器との間で熱媒を循環させることで前記貯湯タンク内の湯水を熱交換加熱して貯湯として蓄熱させる集熱循環回路を備えた太陽熱温水システムを対象にして次の特定事項を備えることとした。すなわち、集熱循環回路内に流通する熱媒の流通量を熱媒温度に応じて変更する流量調整手段を備え、前記流量調整手段として、前記熱媒の熱媒温度に反比例して熱媒の流通量を低減させる、又は、所定の熱媒温度以上になれば熱媒の流通量を低減変更させる構成とする。 In order to achieve the above object, in the present invention, a heat collecting panel for collecting solar heat and heating a heat medium, a hot water storage tank, a heat exchanger for heat exchange heating of hot water in the hot water storage tank, and a circulation A solar hot water system comprising a heat collection circuit that heats and heats hot water in the hot water storage tank to store heat as hot water by circulating a heat medium between the heat collecting panel and the heat exchanger by operating a pump. The following specific items are to be provided. That is, a flow rate adjusting means for changing the flow rate of the heat medium flowing in the heat collecting circuit according to the heat medium temperature is provided, and the flow rate adjusting means is in inverse proportion to the heat medium temperature of the heat medium. reducing the circulation amount, or, a configuration for reducing change the circulation amount of heat medium if more than a predetermined heating medium temperature.
この特定事項を備える場合、熱媒が高温側に昇温すると、熱媒の流通量が熱媒温度に反比例して徐々に低減される、又は、熱媒の流通量が低減変更されることになる。このため、集熱パネルで集熱された熱の搬送量もより小さく制限されることになって、集熱運転中であっても、循環流量が大きい場合に比べて、集熱パネル内や集熱パネルを出てからの集熱循環回路の流路内での熱媒の滞在時間がより長くなって放熱がより進むことになる。この結果、集熱パネルでの沸騰を起こり難くして沸騰の開始が遅れることになる。たとえ最終的に沸騰に至ったとしても、熱媒の流通量が低減されているため水崩れが抑制されるとともに、集熱パネルの側から下降しようとする沸騰蒸気(気泡)の下降も抑制されることになる。これにより、集熱パネルから貯湯タンク等に至る集熱循環回路の流路での熱媒や沸騰蒸気の滞在時間がより長くされ、その放熱が増大化される結果、沸騰に伴う水崩れ(落水)の進行が妨げられ、沸騰蒸気の下降が妨げられて熱媒不足の発生も回避し得るようになる。 When this specific matter is provided, when the heating medium is heated to the high temperature side, the circulation amount of the heating medium is gradually reduced in inverse proportion to the heating medium temperature, or the circulation amount of the heating medium is reduced and changed. Become. For this reason, the amount of heat collected by the heat collection panel is also limited to a smaller value, and even during the heat collection operation, the amount of heat collected in the heat collection panel and the collection is higher than when the circulation flow rate is large. The staying time of the heat medium in the flow path of the heat collecting circuit after leaving the heat panel becomes longer, and the heat radiation further proceeds. As a result, the boiling of the heat collecting panel is difficult to occur and the start of boiling is delayed. Even reached if ultimately boils, with Tei because water collapse circulation amount of heat medium is reduced is suppressed, is suppressed lowering of the boiling steam to be lowered from the side of the heat collection panel (bubbles) Will be. As a result, the residence time of the heat medium and boiling steam in the flow path of the heat collecting circuit from the heat collecting panel to the hot water storage tank, etc. is lengthened and the heat dissipation is increased. ) Is hindered, the boiling steam is prevented from descending, and the occurrence of a shortage of heat medium can be avoided.
加えて、本発明の太陽熱温水システムでは、前記熱交換器の下流側位置であってその熱交換器と循環ポンプとの間の集熱循環回路に気液分離部を介装し、前記流量調整手段を前記熱交換器の下流側位置であってその熱交換器と気液分離部との間の集熱循環回路に介装することとした(請求項1)。このようにすることにより、前記の流量調整手段には、熱交換器を通過した熱媒、つまり、通常の集熱運転においては熱交換器での熱交換加熱により低温となった熱媒が導入されることになる。このため、流量調整手段において熱媒の流通量を増大させることで集熱量を増大させることができ、集熱運転による貯湯タンクへの蓄熱に支障を与えることもない。その一方、沸騰前又は沸騰発生の段階の熱媒は高温となり、貯湯タンク内も蓄熱が十分されていると、熱交換器で熱を奪われることもないため、流量調整手段において熱媒の流通量を低減させることで、請求項1による沸騰開始の遅延化や、沸騰発生に伴う不都合発生の回避等の作用が効果的に得られることになる。 In addition, in the solar hot water system of the present invention, by interposing a gas-liquid separator to the heat collecting circulation circuit between a downstream position before Symbol heat exchanger and the heat exchanger and the circulation pump, the flow it was decided to interposed heat collection circulation circuit between the heat exchanger and the gas-liquid separator adjusting means a position downstream of the heat exchanger (claim 1). In this way, the heat medium that has passed through the heat exchanger, that is, the heat medium that has become low temperature by heat exchange heating in the heat exchanger is introduced into the flow rate adjusting means. Will be. For this reason, the amount of heat collection can be increased by increasing the flow rate of the heat medium in the flow rate adjusting means, and there is no hindrance to the heat storage in the hot water storage tank by the heat collection operation. On the other hand, the heat medium before boiling or at the stage of occurrence of boiling becomes high temperature, and heat storage in the hot water storage tank does not take heat away from the heat exchanger. By reducing the amount, actions such as delaying the start of boiling according to claim 1 and avoiding the occurrence of inconvenience associated with the occurrence of boiling can be obtained effectively.
さらに、本発明の太陽熱温水システムにおいて、前記流量調整手段として、前記集熱循環回路部の流路に対し開閉方向に移動可能に配設された弁体と、この弁体を熱媒温度に応じて作動させる形状記憶合金製のバネとを備えるものとし、前記形状記憶合金製のバネとして、その作動温度以上の熱媒からの熱を受けて前記弁体を前記集熱循環回路の流路を閉止する側に移動させる構成とすることができる(請求項2)。このようにすることで、熱媒温度の上昇に伴い熱媒の流通量を低減させるという本発明による流量調整手段の作動を、駆動エネルギーや制御のための電源投入を必要とすることなく、熱媒温度に応じて機械式に作動する構成により実現し得ることになる。これにより、集熱パネルでの熱媒の沸騰発生が、最初に設置された時点から起こる可能性があったり、集熱運転停止時等の電源が投入されていない状態で起こる可能性が高かったりしても、通電の有無に拘わらず本発明による作用を得ることができるようになる。 Further, in the solar hot water system of the present invention, as the flow rate adjusting means, a valve body disposed so as to be movable in the opening and closing direction with respect to the flow path of the heat collection circuit portion, and the valve body according to the heat medium temperature. And a spring made of a shape memory alloy to be operated, and the valve made of the shape memory alloy spring receives heat from a heat medium having a temperature equal to or higher than its operating temperature to flow through the heat collecting circuit. It can be set as the structure moved to the side to close (Claim 2 ). In this way, the operation of the flow rate adjusting means according to the present invention, which reduces the circulation amount of the heat medium as the heat medium temperature rises, can be performed without requiring driving energy or turning on the power for control. This can be realized by a configuration that operates mechanically according to the medium temperature. As a result, the boiling of the heat medium in the heat collection panel may occur from the time it is first installed, or it is highly likely that the heat collection operation will not occur when the heat collection operation is stopped. Even in this case, the effect of the present invention can be obtained regardless of the presence or absence of energization.
以上、説明したように、本発明の太陽熱温水システムによれば、熱媒が高温側に昇温すると、熱媒の流通量を熱媒温度に反比例して徐々に低減させることができ、又は、熱媒の流通量を低減変更させることができるため、集熱パネルで集熱された熱の搬送量をより小さく制限することができ、集熱運転中であっても、循環流量が大きい場合に比べて、集熱パネル内や集熱パネルを出てからの集熱循環回路の流路内での熱媒の滞在時間をより長くすることができ、放熱をより進行させることができる。この結果、集熱パネルでの沸騰を起こり難くして沸騰の開始を遅らせることができるようになる。そして、たとえ最終的に沸騰に至ったとしても、熱媒の流通量が低減されているため水崩れを抑制することができるとともに、集熱パネルの側から下降しようとする沸騰蒸気(気泡)の下降も抑制することができる。これにより、集熱パネルから貯湯タンク等に至る集熱循環回路の流路での熱媒や沸騰蒸気の滞在時間をより長くして、その放熱を増大化することができる結果、沸騰に伴う水崩れ(落水)の進行や、沸騰蒸気の下降を妨げて、熱媒不足の発生を回避することができるようになる。 As described above, according to the solar hot water system of the present invention, when the heating medium is heated to the high temperature side, the flow rate of the heating medium can be gradually reduced in inverse proportion to the heating medium temperature, or Since the flow rate of the heat medium can be reduced and changed, the amount of heat collected by the heat collection panel can be limited to a smaller amount, even when the circulation flow rate is large even during the heat collection operation. In comparison, the residence time of the heat medium in the heat collection circuit and in the flow path of the heat collection circuit after exiting the heat collection panel can be made longer, and heat dissipation can be further advanced. As a result, it becomes difficult to cause boiling in the heat collecting panel, and the start of boiling can be delayed. Then, even if reached eventually boils, it is possible to flow the amount of the heating medium is suppressed reduced Tei because water collapses, boiling vapor (bubbles) to be lowered from the side of the heat collection panel Lowering can also be suppressed. As a result, the residence time of the heat medium and the boiling steam in the flow path of the heat collection circuit extending from the heat collection panel to the hot water storage tank or the like can be increased, and the heat radiation can be increased. It is possible to prevent the occurrence of a shortage of the heat medium by preventing the collapse (falling water) and the boiling steam from descending.
特に、前記流量調整手段を前記熱交換器と、熱交換器の下流側に設置した気液分離部との間の集熱循環回路に介装するようにしているため、前記の流量調整手段による熱媒の流通量の低減に伴う沸騰開始の遅延化や、沸騰発生に伴う不都合発生の回避等の効果を得る上で、より最適化することができるようになる。 In particular, since the pre-Symbol flow regulating means have to be interposed heat collection circulation circuit between said heat exchanger, a gas-liquid separation unit installed downstream of the heat exchanger, the flow rate adjustment delaying or boiling starting with the reduction of the circulation amount of heat medium by means, on the Ru give effect of avoiding such disadvantages occur due to boiling occurs, it is possible to further optimize.
さらに、請求項2によれば、前記流量調整手段として、弁体と、形状記憶合金製のバネとを備えるものとし、前記形状記憶合金製のバネとして、その作動温度以上の熱媒からの熱を受けて前記弁体を前記集熱循環回路の流路を閉止する側に移動させる構成とすることで、熱媒温度の上昇に伴い熱媒の流通量を低減させるという本発明の流量調整手段を、駆動エネルギーや制御のための電源投入を必要とすることなく、熱媒温度に応じて機械式に作動する構成により実現させることができる。これにより、集熱パネルでの熱媒の沸騰発生が、最初に設置された時点から起こる可能性があったり、集熱運転停止時等の電源が投入されていない状態で起こる可能性が高かったりしても、通電の有無に拘わらず本発明による効果を得ることができるようになる。
Further, according to claim 2 , the flow rate adjusting means includes a valve body and a spring made of a shape memory alloy, and the shape memory alloy spring has a heat from a heat medium at or above its operating temperature. In response to this, the valve body is moved to the side where the flow path of the heat collecting circuit is closed, so that the flow rate of the heat medium is reduced as the heat medium temperature rises. Can be realized by a configuration that operates mechanically in accordance with the temperature of the heating medium without requiring driving energy or power-on for control. As a result, the boiling of the heat medium in the heat collection panel may occur from the time it is first installed, or it is highly likely that the heat collection operation will not occur when the heat collection operation is stopped. Even in this case, the effect of the present invention can be obtained regardless of the presence or absence of energization.
以下、本発明の実施形態を図面に基づいて説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.
図1は、本発明の実施形態に係る太陽熱温水システムを示す。同図中の符号1は例えば地上に設置されたシステム本体、2は内部を通る熱媒(例えば不凍液)に太陽熱を集熱させるための集熱パネル、3は貯湯タンク、4は集熱パネル2と貯湯タンク3内の熱交換器43との間に熱媒を循環させることにより熱媒の熱を貯湯タンク3内に貯湯として蓄熱する集熱循環回路、5は外部から水道水等を貯湯タンク3内に給水する給水路、6は貯湯タンク3内の貯湯を用いて給湯栓(図示省略)等に給湯するために出湯する出湯路、7はこの太陽熱温水システムの作動制御を行うコントローラである。 FIG. 1 shows a solar water heating system according to an embodiment of the present invention. In the figure, reference numeral 1 is, for example, a system main body installed on the ground, 2 is a heat collection panel for collecting solar heat by a heat medium (for example, antifreeze) passing through the inside, 3 is a hot water storage tank, 4 is a heat collection panel 2 And a heat collecting circuit that stores heat from the heat medium as hot water in the hot water storage tank 3 by circulating a heat medium between the heat exchanger 43 in the hot water storage tank 3 and a hot water storage tank for tap water and the like from the outside A water supply passage for supplying water into 3, 6 is a hot water supply passage for supplying hot water to the hot water tap (not shown) using hot water stored in the hot water storage tank 3, and 7 is a controller for controlling the operation of this solar hot water system. .
集熱パネル2は例えば家屋の屋根に設置され、集熱により最も昇温した状態の熱媒の熱媒温度Tsを検出するための熱媒温度センサ21が設けられている。 The heat collecting panel 2 is installed on the roof of a house, for example, and is provided with a heat medium temperature sensor 21 for detecting the heat medium temperature Ts of the heat medium that has been most heated by heat collection.
貯湯タンク3は、例えばステンレス鋼により密閉式に構成された密閉容器である。この貯湯タンク3には、貯湯タンク3内の底部付近の湯又は水(以下「湯水」という)の温度Ttを検出する貯湯タンク温度センサ31が設置されている。給水路5は、その上流端が外部の水道管等に接続され、下流端が図示省略の逆止弁等を介して貯湯タンク3の底部に接続されている。又、出湯路6は、その上流端が貯湯タンク3の頂部に接続され、下流端が図示省略の補助熱源機や給湯栓等に接続されている。 The hot water storage tank 3 is an airtight container configured in a hermetic manner by, for example, stainless steel. The hot water storage tank 3 is provided with a hot water storage tank temperature sensor 31 that detects the temperature Tt of hot water or water (hereinafter referred to as “hot water”) near the bottom of the hot water storage tank 3. The upstream end of the water supply channel 5 is connected to an external water pipe or the like, and the downstream end is connected to the bottom of the hot water storage tank 3 via a check valve (not shown). Further, the hot water outlet 6 has an upstream end connected to the top of the hot water storage tank 3 and a downstream end connected to an auxiliary heat source machine, a hot water tap, etc. (not shown).
集熱循環回路4は、循環ポンプ(例えば可変流量ポンプ)41の作動により熱媒を循環経路42を通して集熱パネル2と貯湯タンク3内の蓄熱用熱交換器(例えばコイル型熱交換器)43との間で循環させるように構成されたものである。循環経路42は、集熱パネル2において昇温した高温の熱媒をその頂部近傍から導出させて貯湯タンク3内の蓄熱用熱交換器43に導いた後に前記循環ポンプ41の吸入側まで導く戻り路42aと、蓄熱用熱交換器43で熱交換されて低温になった熱媒を循環ポンプ41の吐出側から吐出させて集熱パネル2の底部まで集熱のために供給する往き路42bとから構成されている。前記の循環ポンプ41は、貯湯タンク3内の前記湯水温度Ttと、集熱パネル2の前記熱媒温度Tsとの温度差が設定値以上になればコントローラ7により作動が開始され、集熱運転が開始されるようになっている。 The heat collection and circulation circuit 4 is a heat storage heat exchanger (for example, a coil-type heat exchanger) 43 in the heat collection panel 2 and the hot water storage tank 3 through a circulation path 42 by operating a circulation pump (for example, a variable flow pump) 41. It is comprised so that it may circulate between. The circulation path 42 returns the high-temperature heat medium heated in the heat collection panel 2 from the vicinity of the top thereof, led to the heat storage heat exchanger 43 in the hot water storage tank 3, and then led to the suction side of the circulation pump 41. A path 42a, and a forward path 42b for discharging heat from the discharge side of the circulation pump 41 to supply heat to the bottom of the heat collecting panel 2 for heat collection by heat exchange in the heat storage heat exchanger 43. It is composed of The circulation pump 41 is started by the controller 7 when the temperature difference between the hot water temperature Tt in the hot water storage tank 3 and the heat medium temperature Ts of the heat collecting panel 2 becomes a set value or more, and the heat collecting operation is performed. Is supposed to start.
システム本体1内に形成された戻り路42aには半密閉式のアキュームタンク44が介装され、このアキュームタンク44の頂部は連通管451を介してリザーブタンク45の底部と連通されている。この連通管451を通してアキュームタンク44内からあふれた熱媒及び/又は空気をリザーブタンク45内に逃がすようになっている。これらアキュームタンク44とリザーブタンク45との組み合わせにより気液分離部が構成されている。又、アキュームタンク44には底部側の所定液位以上に熱媒があることを検出する低液位センサ441が配設されており、この低液位センサ441からの検出情報に基づいてコントローラ7により循環ポンプ41の作動を許容することで、循環ポンプ41の空回り作動の発生を回避するようになっている。 A semi-sealed accumulation tank 44 is interposed in the return path 42 a formed in the system main body 1, and the top portion of the accumulation tank 44 communicates with the bottom portion of the reserve tank 45 through a communication pipe 451. The heat medium and / or air overflowing from the accumulation tank 44 is allowed to escape into the reserve tank 45 through the communication pipe 451. A gas-liquid separation unit is configured by a combination of the accumulation tank 44 and the reserve tank 45. The accumulation tank 44 is provided with a low liquid level sensor 441 for detecting the presence of a heat medium above a predetermined liquid level on the bottom side. Based on detection information from the low liquid level sensor 441, the controller 7. Thus, the operation of the circulation pump 41 is allowed to avoid the idling operation of the circulation pump 41.
コントローラ7は、MPUやメモリ等を備え、リモコン71からの入力設定信号・操作信号の出力、温度センサ21,31や低液位電極441等からの検出信号の出力に基づいて、予め搭載されたプログラムの実行や制御回路により集熱運転制御等の各種制御を行うようになっている。集熱運転制御について簡単に説明すると、貯湯タンク3の蓄熱量が不足していることを例えば貯湯タンク温度センサ31により検出される湯水温度Ttに基づいて確認し、かつ、集熱パネル温度センサ21により検出される熱媒温度Tsが前記の湯水温度Ttよりも所定の温度差α℃(例えば6℃)以上の高温であることを確認し、これらの開始条件の成立を確認した上で循環ポンプ41を作動させて集熱運転が開始される。 The controller 7 includes an MPU, a memory, and the like, and is installed in advance based on the output of input setting signals / operation signals from the remote controller 71 and the output of detection signals from the temperature sensors 21, 31 and the low liquid level electrode 441. Various controls such as heat collection operation control are performed by program execution and a control circuit. Briefly describing the heat collection operation control, for example, it is confirmed based on the hot water temperature Tt detected by the hot water tank temperature sensor 31 that the amount of heat stored in the hot water tank 3 is insufficient, and the heat collection panel temperature sensor 21. It is confirmed that the heat medium temperature Ts detected by the above is higher than a predetermined temperature difference α ° C. (for example, 6 ° C.) than the hot water temperature Tt, and after confirming that these start conditions are satisfied, the circulation pump 41 is operated to start the heat collecting operation.
これにより、集熱パネル2から高温の熱媒が戻り路42aを通して蓄熱用熱交換器43に供給され、蓄熱用熱交換器43において貯湯タンク3内の湯水を熱交換加熱することにより低温になった熱媒が流量調整手段8、アキュームタンク44、循環ポンプ41及び往き路42bを通して集熱パネル2に供給される。集熱パネル2に供給された熱媒は集熱パネル2内を頂部に進行する間に再加熱され、再び高温になった熱媒が戻り路42aを通して蓄熱用熱交換器43に供給されるというように循環される。そして、貯湯タンク3内の湯水が熱交換加熱されることにより、熱媒に担持された集熱熱量が貯湯タンク3内の湯水に移動し、貯湯として貯湯タンク3内に蓄熱されることになる。 As a result, a high-temperature heat medium is supplied from the heat collection panel 2 to the heat storage heat exchanger 43 through the return path 42a, and the hot water in the hot water storage tank 3 is heat-exchanged and heated in the heat storage heat exchanger 43. The heated heat medium is supplied to the heat collecting panel 2 through the flow rate adjusting means 8, the accumulation tank 44, the circulation pump 41, and the outgoing path 42b. The heat medium supplied to the heat collection panel 2 is reheated while proceeding to the top in the heat collection panel 2, and the heat medium that has become high temperature is supplied to the heat storage heat exchanger 43 through the return path 42a. So that it is circulated. Then, the hot water in the hot water storage tank 3 is heat-exchanged and heated, so that the amount of heat collected by the heat transfer medium moves to the hot water in the hot water storage tank 3 and is stored in the hot water storage tank 3 as hot water storage. .
以上の構成を備えた太陽熱温水システムを前提にして、本実施形態の特徴的な構成要素である流量調整手段8が、蓄熱用熱交換器43の出側と気液分離部であるアキュームタンク44との間の戻り路42aに介装されている。この流量調整手段8は戻り路42a内の熱媒温度が通常の集熱運転時の範囲であれば戻り路42aの流通開口を最大開口量にする一方、熱媒温度が前記の通常集熱運転時の範囲を超えて高温側に上昇すれば流通開口を徐々に最小開口量の側(閉側)に絞るように作動するようになっている。つまり、熱媒温度の上昇に反比例して熱媒の流通量(流量)を低減させるようになっている。前記の集熱運転時の熱媒温度範囲とは、集熱パネル2で集熱して昇温された熱媒が蓄熱用熱交換器43で貯湯タンク3内の湯水を熱交換加熱することで熱を奪われて蓄熱用熱交換器43から導出された低温状態の熱媒温度範囲のことである。この熱媒温度が、夏場等において集熱による熱媒の昇温度合が著しく、又、熱交換加熱対象の貯湯タンク3内の湯水温度(給水温度を含む)が元々高めである状況下では、集熱運転中で熱交換加熱した後であっても前記の通常集熱運転時の熱媒温度範囲を超えて高温側に上昇すると、流通開口量を徐々に絞るように作動することになる。そして、熱媒の沸騰温度(例えば50℃)まで高温側に上昇すると、前記の流量調整手段8はその流通開口を最小開口量まで絞り、極僅かな最小開口量での連通状態にされるようになっている。つまり、熱媒温度が高温側になると、熱媒の流通開口を絞って流路抵抗をより大きく変化させるようになっている。 On the premise of the solar hot water system having the above-described configuration, the flow rate adjusting means 8 which is a characteristic component of the present embodiment is an accumulator tank 44 which is an outlet side of the heat storage heat exchanger 43 and a gas-liquid separation unit. Is interposed in a return path 42a. The flow rate adjusting means 8 sets the flow opening of the return path 42a to the maximum opening amount when the temperature of the heat medium in the return path 42a is within the range of the normal heat collecting operation, while the heat medium temperature is the normal heat collecting operation. If the temperature rises beyond the time range and rises to the high temperature side, the flow opening is gradually reduced to the minimum opening amount side (closed side). That is, the flow rate (flow rate) of the heat medium is reduced in inverse proportion to the increase in the heat medium temperature. The heat medium temperature range at the time of the heat collecting operation means that the heat medium heated by collecting heat by the heat collecting panel 2 heats and heats hot water in the hot water storage tank 3 by the heat storage heat exchanger 43. Is a low temperature heat medium temperature range derived from the heat storage heat exchanger 43. In the situation where the temperature of the heat medium is remarkably increased due to heat collection in summer, etc., and the hot water temperature (including the feed water temperature) in the hot water storage tank 3 subject to heat exchange heating is originally high, Even after the heat exchange heating in the heat collecting operation, when the temperature rises beyond the heat medium temperature range in the normal heat collecting operation to the high temperature side, the flow opening amount is gradually reduced. When the temperature rises to the high temperature side to the boiling temperature of the heat medium (for example, 50 ° C.), the flow rate adjusting means 8 restricts the flow opening to the minimum opening amount so as to be in a communication state with a very small minimum opening amount. It has become. That is, when the temperature of the heat medium becomes higher, the flow path resistance is changed more greatly by narrowing the flow opening of the heat medium.
以下、前記の流量調整手段8として、熱媒温度に応じて機械式に作動するように構成した第1〜第3の形態に係る流量調整手段8a,8b,8cについて説明する。なお、流量調整手段8としては、通常の流量制御弁と、これを熱媒温度の検出値に応じて作動制御する制御部とを用いて、熱媒温度が所定の設定温度を超えれば、弁開口を徐々に絞るように作動制御し、熱媒の沸騰温度(例えば50℃)あるいは僅かに低めの温度まで到達すれば最小開口量で維持させるように作動制御するという構成を採用することもできる。これに対し、前記の流量調整手段8a,8b,8cの如く熱媒温度に応じて機械式に作動する構成とすることで、駆動エネルギーや制御のための電源投入を必要とすることなく、後述の作用効果を得ることができるようになる。集熱パネル2での熱媒の沸騰発生は、最初に設置された時点から起こる可能性があるし、集熱運転停止時等の電源が投入されていない状態で起こる可能性が高く、通電の有無に拘わらず流量調整(通路抵抗の増減調整)が可能である点で、前記の流量調整手段8a,8b,8cは有用なものとなる。 Hereinafter, the flow rate adjusting units 8a, 8b, and 8c according to the first to third embodiments configured to operate mechanically according to the heat medium temperature will be described as the flow rate adjusting unit 8. The flow rate adjusting means 8 uses a normal flow rate control valve and a control unit that controls the operation according to the detected value of the heat medium temperature, and if the heat medium temperature exceeds a predetermined set temperature, the valve It is also possible to adopt a configuration in which the operation is controlled so that the opening is gradually reduced, and the operation is controlled so that the opening is maintained at the minimum opening amount when reaching the boiling temperature of the heat medium (for example, 50 ° C.) or a slightly lower temperature. . On the other hand, by adopting a configuration that mechanically operates according to the heat medium temperature, such as the flow rate adjusting means 8a, 8b, and 8c, the drive energy and the power supply for control are not required, which will be described later. It becomes possible to obtain the operational effects. The boiling of the heat medium in the heat collecting panel 2 may occur from the time when it is first installed, and is likely to occur when the power is not turned on such as when the heat collecting operation is stopped. The flow rate adjusting means 8a, 8b, 8c are useful in that flow rate adjustment (increase / decrease adjustment of passage resistance) is possible regardless of the presence or absence.
<第1の実施形態>
第1の実施形態に係る流量調整手段8aは、図2に示すように、戻り路42aを仕切る隔壁81に連通孔82を貫通させ、この連通孔82に対し近接・離反するように移動案内されて熱媒が流通する開口量を増減させる弁体83を配設したものである。そして、弁体83を作動させるために、弁体83の一側に通常のバネ(例えばコイルスプリング)84を配設し、他側に形状記憶合金製のバネ(例えばコイルスプリング)85を配設している。
<First Embodiment>
As shown in FIG. 2, the flow rate adjusting means 8 a according to the first embodiment is guided to move so that the communication hole 82 penetrates the partition wall 81 that partitions the return path 42 a, and approaches and separates from the communication hole 82. Thus, a valve body 83 for increasing or decreasing the amount of opening through which the heat medium flows is provided. In order to operate the valve body 83, a normal spring (for example, a coil spring) 84 is disposed on one side of the valve body 83, and a spring (for example, a coil spring) 85 made of a shape memory alloy is disposed on the other side. doing.
具体的には、戻り路42aに弁室86を介装させ、この弁室内86に前記の隔壁81及び連通孔82を形成し、この連通孔82の上下流側の一側に弁体83を配置したものである。そして、通常のバネ84を弁体83の一側部と、これに相対向する弁室86の内壁面861との間に介装し、形状記憶合金製のバネ85を弁体83の他側部と、これに相対向する弁室86の内壁面862との間に介装している。 Specifically, the valve chamber 86 is interposed in the return path 42 a, the partition wall 81 and the communication hole 82 are formed in the valve chamber 86, and the valve body 83 is provided on one side of the upstream and downstream sides of the communication hole 82. It is arranged. Then, a normal spring 84 is interposed between one side of the valve body 83 and the inner wall surface 861 of the valve chamber 86 opposite to the valve body 83, and the shape memory alloy spring 85 is disposed on the other side of the valve body 83. And an inner wall surface 862 of the valve chamber 86 facing each other.
形状記憶合金製のバネ85は、戻り路42a内の熱媒が前記の通常集熱運転時の熱媒温度範囲にあれば縮んだ状態をほぼ維持する一方、通常のバネ84は弾性力が開放状態とされ、これにより、弁体83と連通孔82との間隔が開いて流路開口を最大開口量に維持することになる(図2(a)に示す状態を参照)。そして、戻り路42a内の熱媒が通常集熱運転時の熱媒温度範囲を超えてより高温になると、つまり熱媒温度が形状記憶合金製のバネ85の作動温度以上になると、熱媒温度の昇温度合に比例して形状記憶合金製のバネ85が伸びていく一方、通常のバネ84はそれに押されて縮んでいき、これにより、弁体83が連通孔82に対し徐々に近づいていき、これに伴い前記の流路開口は徐々に狭くなる。つまり、熱媒温度の昇温度合に反比例して熱媒の流通量が低減されるようになっている。熱媒温度が熱媒の沸騰温度になれば、あるいは、沸騰温度に近づくと、形状記憶合金製のバネ85に押された弁体83がストッパ87に行き当たって停止することで、弁体83と連通孔82との間の流通開口は最小開口量に維持されることになる(図2(b)に示す状態を参照)。 The spring 85 made of a shape memory alloy substantially maintains a contracted state if the heat medium in the return path 42a is in the heat medium temperature range during the normal heat collecting operation, while the normal spring 84 has an elastic force released. Thus, the distance between the valve body 83 and the communication hole 82 is increased, and the flow path opening is maintained at the maximum opening amount (see the state shown in FIG. 2A). When the heat medium in the return path 42a exceeds the heat medium temperature range during normal heat collecting operation and becomes higher, that is, when the heat medium temperature becomes equal to or higher than the operating temperature of the spring 85 made of shape memory alloy, While the shape memory alloy-made spring 85 expands in proportion to the temperature rise, the normal spring 84 is pushed and contracted, so that the valve body 83 gradually approaches the communication hole 82. Along with this, the passage opening is gradually narrowed. That is, the flow rate of the heat medium is reduced in inverse proportion to the increase in the heat medium temperature. When the temperature of the heating medium reaches the boiling temperature of the heating medium, or when the temperature of the heating medium approaches the boiling temperature, the valve body 83 pressed by the shape memory alloy spring 85 comes into contact with the stopper 87 and stops. And the communication opening 82 are maintained at the minimum opening amount (see the state shown in FIG. 2B).
このような流量調整手段8aを戻り路42aに介装することで、次のような作用効果を得ることができるようになる。すなわち、熱媒が通常集熱運転時の熱媒温度範囲であれば、流通開口は最大開口量に維持されるため、流路抵抗も極小となって熱媒の循環がスムーズに行われて集熱運転を良好に行わせることができる。その一方、前記の熱媒温度範囲を超えて熱媒が高温側に昇温すると、流通開口が徐々に絞られていって流路抵抗が大きくなり循環流量がより小さく制限されることになるため、その分、集熱パネル2で集熱された熱の搬送量もより小さく制限されることになる。これにより、集熱運転中であっても、循環流量が大きい場合に比べて、集熱パネル2内や集熱パネル2を出てからの戻り路42a内での熱媒の滞在時間がより長くなって放熱がより進むことになる。この結果、集熱パネル2での沸騰を起こり難くして沸騰の開始を遅らせることができるようになる。 By interposing such a flow rate adjusting means 8a in the return path 42a, the following operational effects can be obtained. That is, if the heat medium is in the heat medium temperature range during normal heat collection operation, the flow opening is maintained at the maximum opening amount, so that the flow resistance is minimized and the heat medium is smoothly circulated and collected. Thermal operation can be performed satisfactorily. On the other hand, when the temperature of the heating medium exceeds the above-mentioned temperature range of the heating medium, and the temperature of the heating medium is increased, the flow opening is gradually narrowed, the flow resistance is increased, and the circulation flow rate is restricted to be smaller. Accordingly, the amount of heat transported by the heat collecting panel 2 is also limited to be smaller. Thereby, even during the heat collection operation, the residence time of the heat medium in the return path 42a after exiting the heat collection panel 2 and the heat collection panel 2 is longer than when the circulation flow rate is large. It will become more heat dissipation. As a result, the boiling of the heat collecting panel 2 hardly occurs and the start of boiling can be delayed.
そして、たとえ最終的には沸騰に至ったとしても、流通開口が最小開口量に絞られて流路抵抗が最大になるため、内部の熱媒の流動も制限されて水崩れを抑制するとともに、集熱パネル2の側から下降しようとする沸騰蒸気(気泡)にも抵抗してその下降を抑制することができるようになる。そして、集熱パネル2から貯湯タンク3等に至る戻り路42aでの熱媒や沸騰蒸気の滞在時間をより長くして、その放熱を増大化させることができる結果、放熱促進により一部の沸騰蒸気を液体に戻すことができ、集熱パネル2から貯湯タンク3等のシステム本体1の側への下降圧力を減少させることができるようになる。この結果、沸騰に伴う水崩れ(落水)の進行を妨げ、沸騰蒸気がシステム本体1の側に連続的に下降してくることを妨げることができ、アキュームタンク44からの溢れ出しによる熱媒不足の発生を防止することができるようになる。 And even if it finally reaches boiling, the flow opening is restricted to the minimum opening amount and the flow path resistance is maximized, so that the flow of the internal heating medium is also restricted and water collapse is suppressed, Resisting the boiling steam (bubbles) about to descend from the heat collecting panel 2 side, it is possible to suppress the descending. As a result, the heat medium and boiling steam stay in the return path 42a from the heat collecting panel 2 to the hot water storage tank 3 and the like can be made longer to increase the heat dissipation. The steam can be returned to the liquid, and the descending pressure from the heat collecting panel 2 toward the system main body 1 such as the hot water storage tank 3 can be reduced. As a result, it is possible to prevent water from collapsing (falling water) due to boiling, to prevent boiling steam from continuously descending toward the system body 1, and insufficient heat medium due to overflow from the accumulator tank 44. Can be prevented.
<第2の実施形態>
図3(a)は、熱媒が通常集熱運転時の熱媒温度範囲にあるときに、戻り路42aの流通開口が第2の実施形態に係る流量調整手段8bにより最大開口量に維持された状態を示す。この流量調整手段8bは熱媒温度が高温(例えば沸騰温度)に昇温した場合の最小開口量の流通開口を、第1の実施形態の流量調整手段8aにおけるストッパ87による最小開口量の確保の代わりに、常時連通状態のバイパス路88により確保して、弁体83自体は形状記憶合金製のバネ85によって連通孔82を全閉状態に押し付けられるようにしたものである(図3(b)参照)。
<Second Embodiment>
FIG. 3A shows that when the heat medium is in the heat medium temperature range during normal heat collection operation, the flow opening of the return path 42a is maintained at the maximum opening amount by the flow rate adjusting means 8b according to the second embodiment. Indicates the state. This flow rate adjusting means 8b ensures the minimum opening amount by the stopper 87 in the flow rate adjusting means 8a of the first embodiment when the heating medium temperature is raised to a high temperature (for example, the boiling temperature). Instead, the valve body 83 is secured by a bypass 85 that is always in communication, and the communication hole 82 can be pressed to a fully closed state by a spring 85 made of a shape memory alloy (FIG. 3B). reference).
この点以外の構成は第1の実施形態の流量調整手段8aとほぼ同様であるため、第1実施形態と同じ符号を付して詳細な説明を省略する。 Since the configuration other than this point is almost the same as that of the flow rate adjusting means 8a of the first embodiment, the same reference numerals as those of the first embodiment are used and detailed description thereof is omitted.
そして、この第2実施形態の流量調整手段8bによっても、第1実施形態の流量調整手段8aと同様の作用効果を得ることができる。 The same effect as that of the flow rate adjusting unit 8a of the first embodiment can be obtained also by the flow rate adjusting unit 8b of the second embodiment.
<第3の実施形態>
図4は第3の実施形態に係る流量調整手段8cを示す。この流量調整手段8cは第1又は第2の実施形態よりも具体化させたものであり、戻り路42aに介装された本体ハウジング91と、本体ハウジング91内に内嵌された弁ガイド92及び弁座93と、弁ガイド92により前後進可能に保持された弁体94と、弁ガイド92及び弁体94の両者間に介装された形状記憶合金製のバネ(例えばコイルスプリング)95とを備えて構成されたものである。
<Third Embodiment>
FIG. 4 shows the flow rate adjusting means 8c according to the third embodiment. The flow rate adjusting means 8c is more specific than the first or second embodiment, and includes a main body housing 91 interposed in the return path 42a, a valve guide 92 fitted in the main body housing 91, and A valve seat 93, a valve body 94 held by the valve guide 92 so as to be movable forward and backward, and a spring (for example, a coil spring) 95 made of a shape memory alloy interposed between the valve guide 92 and the valve body 94. It is prepared.
弁ガイド92は本体ハウジング91の内周面に内嵌される外筒部921と、この外筒部921から放射方向に延びる複数のリブ922,922,…によって一体化された内筒部923とからなり、この内筒部923内に弁体94の弁軸部941が前後方向(図4の上下方向)に摺動可能に保持されるようになっている。 The valve guide 92 includes an outer cylindrical portion 921 fitted into the inner peripheral surface of the main body housing 91, and an inner cylindrical portion 923 integrated by a plurality of ribs 922, 922,... Extending radially from the outer cylindrical portion 921. The valve shaft portion 941 of the valve body 94 is slidably held in the inner cylinder portion 923 in the front-rear direction (vertical direction in FIG. 4).
弁座93は、本体ハウジング91の内周面に内嵌されて弁ガイド92と共に固定される筒部931と、一側に内周側に膨出して弁体94の後述の弁部942の周縁部と当接する弁座部932とを備えて構成されている。 The valve seat 93 is fitted into the inner peripheral surface of the main body housing 91 and fixed together with the valve guide 92. The valve seat 93 bulges to the inner peripheral side on one side and the peripheral edge of a later-described valve portion 942 of the valve body 94. And a valve seat portion 932 that contacts the portion.
弁体94は、図5に詳細を示すように、弁部942と、弁部942の中心位置から中心軸Xに沿って一側に延びる弁軸部941とを備えたものである。弁部942には、外縁部に対し放射方向に延びて中心軸X方向に貫通する複数(図例で4つ)のスリット開口部943,943,…が形成されている。このスリット開口部943,943,…は後述の如く最小開口量を確保するためのものである。 As shown in detail in FIG. 5, the valve body 94 includes a valve portion 942 and a valve shaft portion 941 extending from the center position of the valve portion 942 to the one side along the central axis X. The valve portion 942 is formed with a plurality of (four in the illustrated example) slit openings 943, 943,... Extending radially from the outer edge portion and penetrating in the central axis X direction. The slit openings 943, 943,... Are for securing a minimum opening amount as will be described later.
そして、形状記憶合金製のバネ95は、一端が弁ガイド92のリブ922,922,…の内周側に支持され、他端が弁体94の弁部942の一側面の内周側に支持されている。この形状記憶合金製のバネ95は、戻り路42a内の熱媒が前記の通常集熱運転時の熱媒温度範囲であれば縮んだ状態を維持し、これにより、弁体94は図4(a)に示すように弁部942が弁座93の弁座部932から最も離れた位置に維持され、本体ハウジング91内の流通開口も最大開口量に維持されることになる。一方、戻り路42a内の熱媒が前記の熱媒温度範囲よりも高温になると、形状記憶合金製のバネ95はその温度上昇に比例して伸びていき、弁部942を弁座部932に対しより近付けることになり、熱媒が沸騰温度近傍の所定温度まで昇温すると、図4(b)に示すように形状記憶合金製のバネ95は最大伸長状態になって弁部942が弁座部932に押し付けられた状態になる。これにより、流通開口はスリット開口部943,943,…により構成される最小開口量に制限され、流路抵抗も最大となる。 The one end of the spring 95 made of shape memory alloy is supported on the inner peripheral side of the ribs 922, 922,... Of the valve guide 92, and the other end is supported on the inner peripheral side of one side surface of the valve portion 942 of the valve body 94. Has been. This shape memory alloy spring 95 maintains a contracted state if the heat medium in the return path 42a is within the temperature range of the heat medium during the normal heat collecting operation. As shown in a), the valve portion 942 is maintained at the position farthest from the valve seat portion 932 of the valve seat 93, and the flow opening in the main body housing 91 is also maintained at the maximum opening amount. On the other hand, when the heat medium in the return path 42a becomes higher than the temperature range of the heat medium, the shape memory alloy spring 95 extends in proportion to the temperature rise, and the valve portion 942 is moved to the valve seat portion 932. When the heating medium is heated to a predetermined temperature near the boiling temperature, the spring 95 made of a shape memory alloy is in the maximum extension state as shown in FIG. 4B, and the valve portion 942 is moved to the valve seat. It will be in the state pressed against the part 932. Accordingly, the flow opening is limited to the minimum opening amount constituted by the slit openings 943, 943,..., And the flow path resistance is maximized.
以上の第3の実施形態の流量調整手段8cによっても、第1実施形態の流量調整手段8aの場合と同様の作用効果を得ることができる。すなわち、集熱運転中であっても、循環流量が大きい場合に比べて、集熱パネル2内や集熱パネル2を出てからの戻り路42a内での熱媒の滞在時間がより長くなって放熱がより進むことになる結果、集熱パネル2での沸騰を起こり難くして沸騰の開始を遅らせることができるようになる。そして、たとえ最終的には沸騰に至ったとしても、流通開口が最小開口量に絞られて流路抵抗が最大になるため、沸騰に伴う水崩れ(落水)の進行を妨げ、沸騰蒸気がシステム本体1の側に連続的に下降してくることを妨げることができ、アキュームタンク44からの溢れ出しによる熱媒不足の発生を防止することができるようになる。 Also by the flow rate adjusting means 8c of the third embodiment described above, it is possible to obtain the same effects as the flow rate adjusting means 8a of the first embodiment. That is, even during the heat collection operation, the residence time of the heat medium in the heat collection panel 2 and the return path 42a after exiting the heat collection panel 2 is longer than when the circulation flow rate is large. As a result, the heat radiation is further advanced. As a result, the boiling of the heat collecting panel 2 hardly occurs and the start of the boiling can be delayed. And even if it eventually reaches the boiling point, the flow opening is restricted to the minimum opening amount and the flow path resistance is maximized, which prevents the progress of water collapse (falling water) accompanying boiling, and the boiling steam is generated in the system. It is possible to prevent continuous lowering to the main body 1 side, and it is possible to prevent a shortage of the heat medium due to overflow from the accumulation tank 44.
<他の実施形態>
なお、本発明は以上の各実施形態に限定されるものではなく、その他種々の実施形態を包含するものである。すなわち、前記各実施形態では、形状記憶合金製のバネ85,95を用いた流通開口量の変更特性として、熱媒温度の上昇に反比例して流通開口を制限して熱媒の流通量(流量)が低減されるものを説明したが、これに限らず、ある設定温度以上になれば流通開口量がそれまでよりも小さくなって熱媒の流通量が段階的に低減するようにしてもよい。
<Other embodiments>
Note that the present invention is not limited to the above embodiments, and includes other various embodiments. That is, in each of the above embodiments, as a change characteristic of the flow opening amount using the springs 85 and 95 made of the shape memory alloy, the flow opening is limited in inverse proportion to the increase in the heat medium temperature, and the flow amount of the heat medium (flow rate). However, the present invention is not limited to this, and the flow opening amount may be smaller than before and the flow rate of the heat medium may be reduced step by step when the temperature exceeds a certain set temperature. .
さらに、前記実施形態では熱交換器43が貯湯タンク3内に設置された例を示したが、これに限らず、熱交換器が貯湯タンク3の外部に設置され、この熱交換器に対し集熱循環回路の熱媒を熱源側に循環供給する一方、貯湯タンク3内の湯水を他の循環ポンプにより被加熱側に循環供給することで、貯湯タンク内の湯水が熱媒により熱交換加熱されるように構成された太陽熱温水システムも本発明に含まれる。 Furthermore, although the heat exchanger 43 was installed in the hot water storage tank 3 in the above embodiment, the present invention is not limited to this, and the heat exchanger is installed outside the hot water storage tank 3 and collects the heat exchanger. While the heat medium of the heat circulation circuit is circulated and supplied to the heat source side, the hot water in the hot water storage tank 3 is circulated and supplied to the heated side by another circulation pump, so that the hot water in the hot water storage tank is heat-exchanged and heated by the heat medium. A solar water heating system configured as described above is also included in the present invention.
2 集熱パネル
3 貯湯タンク
4 集熱循環回路
8,8a,8b,8c 流量調整手段
41 循環ポンプ
42 戻り路
44 アキュームタンク(気液分離部)
85,95 形状記憶合金製のバネ
2 Heat collection panel 3 Hot water storage tank 4 Heat collection circulation circuit 8, 8a, 8b, 8c Flow rate adjusting means 41 Circulation pump 42 Return path 44 Accumulation tank (gas-liquid separation part)
85,95 Shape memory alloy spring
Claims (2)
集熱循環回路内に流通する熱媒の流通量を熱媒温度に応じて変更する流量調整手段を備え、
前記流量調整手段は、前記熱媒の熱媒温度に反比例して熱媒の流通量を低減させる、又は、所定の熱媒温度以上になれば熱媒の流通量を低減変更させるように構成され、
前記熱交換器の下流側位置であってその熱交換器と循環ポンプとの間の集熱循環回路部には気液分離部が介装され、
前記流量調整手段は前記熱交換器の下流側位置であってその熱交換器と気液分離部との間の集熱循環回路に介装されている、
ことを特徴とする太陽熱温水システム。 A heat collecting panel for collecting solar heat to heat the heat medium, a hot water storage tank, a heat exchanger for heat exchange heating of the hot water in the hot water storage tank, and the heat collecting panel and the heat exchange by operating a circulation pump A solar water heating system comprising a heat collection and circulation circuit that heat-exchanges and heats hot water in the hot water storage tank to store heat as hot water storage by circulating a heat medium between the tank and
A flow rate adjusting means for changing the flow rate of the heat medium flowing in the heat collection circuit according to the heat medium temperature;
The flow rate adjusting means is configured to reduce the flow rate of the heat medium in inverse proportion to the heat medium temperature of the heat medium, or to reduce and change the flow rate of the heat medium when the temperature exceeds a predetermined heat medium temperature. ,
A gas-liquid separation unit is interposed in the heat collection and circulation circuit unit between the heat exchanger and the circulation pump at a downstream position of the heat exchanger,
The flow rate adjusting means that is interposed in the heat collecting circulation circuit between the heat exchanger and the gas-liquid separator a position downstream of the heat exchanger,
Solar heat hot water system characterized in that.
前記流量調整手段は、前記集熱循環回路部の流路に対し開閉方向に移動可能に配設された弁体と、この弁体を熱媒温度に応じて作動させる形状記憶合金製のバネとを備え、
前記形状記憶合金製のバネは、その作動温度以上の熱媒からの熱を受けて前記弁体を前記集熱循環回路の流路を閉止する側に移動させるように構成されている、
太陽熱温水システム。 The solar hot water system according to claim 1 ,
The flow rate adjusting means includes a valve body disposed so as to be movable in the open / close direction with respect to the flow path of the heat collection circuit portion, and a spring made of a shape memory alloy that operates the valve body in accordance with the heat medium temperature. With
The shape memory alloy spring is configured to receive heat from a heat medium at or above its operating temperature and move the valve body to the side that closes the flow path of the heat collection circuit,
Solar water heating system.
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| JP2586832B2 (en) * | 1994-09-22 | 1997-03-05 | 株式会社ノーリツ | Bathing equipment for bathtub |
| JP4261524B2 (en) * | 2005-08-11 | 2009-04-30 | リンナイ株式会社 | Hot water storage device |
| JP2008138898A (en) * | 2006-11-30 | 2008-06-19 | Matsushita Electric Ind Co Ltd | Heating device |
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