200923285 九、發明說明： 【發明所屬之技術領域】 本發明係關於一種建築物熱能管理系統，特別是指—種經 由熱管將地熱之熱能或經由熱管將冰水之溫度帶引至建築物内 的调溫裝置0 【先前技術】 近年來’人類對於地球環境的破壞，有如氣候高溫化、酸 雨、臭氧層破壞以及異常氣候等現象，再加上人類過去不當的 都市建築政f，使居住環境急速惡化，地球環保受到極大的漠 視。 現在都市的人口過度集中、人造環境不透水化、建築物通 風不良，往往是造成能源浪費與都市氣候高溫化；& 了應付日 益炎熱的都市氣候，家_家；玲^ 豕豕戶戶更大篁使用冷氣空調、進而加速 熱空氣的排放，更造成都市炎熱化的循環。 Ο 為了、‘友和上述都市建築環境惡化的問題，在政府所推動的 「綠建築推動方案」，中逮筮Α ”甲建杀。ρ刀盯疋了環境評估七大指摞糸 統’包括：綠化、基地保水、欠 巴侏求水貝源、日常節能、二氧化破減 里、/于水垃圾改善等綠化建筚物之古私 泛杀物之方針，而如何減低建築物二 氧化碳的排放量，乃熹太安代Dn 乃疋本案發明人極欲改良之處。 【發明内容】 本發明之目的即在於 種建桌物熱能管理系統，其弟 一散熱組内部設置有高埶導 ，、、'、羊比舁同傳熱溫差效果的熱管，圩 200923285 提供快速將地熱之熱空氣導引至建築物内，適用於冬天時調高 室内溫度。 本毛月之人目的係在於提供一種建築物熱能管理系統， 其第二散熱組内之熱管可吸取容器内冰水之溫度，以藉由戶外 之外部空氣以及吸水性材料上之水分，來降低建築物室内之溢 度。 的货'在於提供一種建築物熱能管理系 Γ 〇 二散熱組其㈣設置有熱量通量大的熱管，當熱管與地熱或对 水接觸後，可有效調整建築物内之調溫裝置。 可達成上述發明目的之建築物熱能管理系統，包括有： 第—散熱組，係提供導引地熱及外部空氣進人，亦由複數 散熱片、複數熱管以及至少一尾 ^ ㉟扇所構成，且該散熱組徑向排 列設有熱管，且該孰管盆_ ^ Μ別構a發段與冷凝段，該蒸 發段係深,肖转 ?| Λ1 畎熟片連接，而該風扇則導 邛空氣進入後間接與散熱片接觸； 送風扇，係提供導引外部空氣進入· 第二散熱組’係以一通道與第 焚蚁热組連接，亦以一進溃 吕相送風扇連接，該第H㈣ ” —風扇、一a 旻数政熱片、禝數熱管、 奋益以及一吸水性材料所槿成 列却_右刼& 成’且該散熱組徑向排 列汉有熱官，該風扇係設置於散熱 门排 係設置散埶片之g 側，而該吸水性材料 月文…、片之另一側，且該熱管I _ 而刀別構成蒸發段與冷 200923285 ' 忒瘵發段與該吸水性材料係置入容器，該冷凝段係與散 熱片連接，卷姑 田^風扇導引通道或進氣管道内之空氣進入後，該 二虱則兵政熱片和吸水性材料接觸，以供調節建築物内之溫度； 中。亥熱官内之工作介質的汽化溫度將設計成人體和環境 ' X，因此當熱管其蒸發段吸收地熱（或水）熱量的溫度 會大於工作介哲+ ，，、> 貝之 >气化溫度’工作介質吸熱並汽化，汽化的工 (作"貝矛夕動到冷凝段，冷凝段經由散熱片調溫’亦再經由風扇 :卩二氣和政熱片的溫度帶引至建築物内，以調整建築物内 之溫度。 【實施方式】 »月芩閱圖一至圖五，本發明所提供之建築物熱能管理系 、”先主要包括有：一第一散熱組（1)、一送風扇（？）' —第二散 熱組（3)所構成。 ν 第一散熱組（1)，係提供導引地熱（Η)及外部空氣進入，亦 由複數排列之散熱片（丨1)、複數熱管（12)以及至少一風扇（丨3) 所構成，且該散熱組徑向排列設有熱管（12)，且該熱管具 有一密封空間，該密封空間具有毛細結構（121)以及密封於内之 工作介質（124)，其二端分別構成蒸發段（122)與冷凝段（123)， 该蒸發段（122)係深入地表下，該冷凝段（123)係與散熱片（11) 連接，而該風扇（13)則導引外部空氣進入後間接與散熱片（丨〇 接觸；層 200923285 送風扇（2),係提供導引外部空氣進入； 第二散熱組（3) ’係以一通道（14)與第—散熱組（1)連接， 亦以—進氣管道與送風扇（2)連接，該第二散熱組（3)係由複數 散熱片（31)、複數熱管（32)、一風扇（33)、一容器（34)以及一 吸水丨生材料（35)所構成，且該散熱組徑向排列設有熱管（μ)， 該風扇（33)係設置於散熱片（31)之一側，而該吸水性材料（35) 係叹置散熱片（31)之另-側，且該熱管（32)其二端分別構成蒸 發段（322)與冷凝段（323)，該蒸發段（322)與該吸水性材料（35) 係置入容器（34)，該冷疑段（323)係與散熱片（31)連接，當該風 扇（33)導引通道⑽或進氣管道内之空氣進入後，該空氣則與 散熱片（31)和吸水性材料（35)接觸，以供調節建築物（A)内之溫 度； 請參閱圖二與圖三，其密封於熱管（12)内之工作介質 (124) 4工作介質（124)係充滿於多孔毛細結構（丨21)用以傳遞 熱量，是在熱力學中指實現熱能與機械能或其他能量的轉換或 傳遞過程中所用的工作介質（124)。本發明之工作介質（124)除 了是流體外，也可以是氣體（如理想氣體、實際氣體、混合氣體） 或水蒸汽，因為氣態物質有良好的流動性和壓縮性，便於吸收、 輪運、釋放或轉換能量。該載熱之工作介質（124)按工作要求選 用，可從深冷液化氣（如：水、曱醇、丙酮）直到液態金屬（如： 鈉、汞、氟里昂、鈉、銀）；水和水蒸汽容易獲得，其成本低廉， 200923285 並具有無腐蝕性、比熱容和汽化潛熱較大等優良性能，所以是 最常用的工作介質（124)。 該第一散熱組（1)内之熱管（i 2)係利用工作介質（丨2 4)的汽 化溫度（彿點）取決於相應的壓力的特性，而根據理論分析和實 驗測定可得知。透過調整熱t(12)管内壓力來控制工作介質 (124)的汽化溫度，該工作介質⑽)的汽化溫度將設計成人體 體溫和環境的中間溫度。 因此當第-散熱組⑴之熱管（12)經由蒸發段〇22)置入土 地表面，並與地表附近可供利㈣地熱（h)能時，熱管（⑵其菜 發段⑽)吸收地熱(H)能的溫度大於工作介質⑽的汽化溫 又因此工作"貝（124)吸熱並汽化；汽化的工作介質⑽）移 動到冷凝段⑽），回到環境溫度，凝結成液態；該工作介質⑽) 由於重力作用，再沿著毛細結構（121)重新流回蒸發段⑽）。 〃平衡定律係“述非均勻復相系處於平衡時的性質；—個復 相系在完全平衡時的自由度數F等於其獨立組元數C減去相數p 再加2。數學表達式為： P+2 一 可〜為是代表溫度和壓力兩個變量的數目。對於岸 70單相系，例如水，自由 _ 目由度數為2 ’故溫度7和壓力户可在合超 的範圍内獨立地改蠻。 人 文對於皁元二相系，例如水和水蒸氣的渴 s體’自由度數，表 表月度和壓力兩個變量中只有一個可以 200923285 獨立地改變，故此時平衡態可在（溫度7，壓力户)相圖用一條曲 線來表示。對於單元三相系，例如冰、水、水蒸氣的混合體， 自由度數為0 ’表明溫度7和壓力戶都有固定值而不能改變，此 時平衡態在（溫度7’壓力户)相圖上就用一個點（通常稱為三相 點）來表示。 熱力學理論可以證明，一定量的某種氣體，當容積保持不 變時’溫度71與壓力户成正比。液體的飽和蒸氣壓等於液面上 ’大氣壓之溫度，此時液體各點均呈劇烈汽化現象，且液氣相可 八存若液面上為1大氣壓（1 atm(76 mmHg))時，則該沸點稱為 「正常沸點」，如工作介質（124)為水，則水的正常沸點為1〇{rc。 田本發明之工作介質（124)欲填入熱管（12)内部時，須預設 工作介質（124)之汽化溫度（如27t)，因熱管（12)吸收地熱（H) 能的溫度（約30。〇會大於工作介質（124)之汽化溫度；如圖四所 〇示為水的三相圖，〇為三相點，0K為汽化曲線，0L為融化曲線’ "在單組分系統的相平衡中，沒有組成變量，只須考慮溫度和壓 力兩個變量，因此，所有可能的相平衡關係均可用壓力-溫度圖 表示’如S以工作；I吳（124)其汽化溫度和壓力的平撰t關係落在 汽化曲線上，則曲、線的斜率d/ydM可用克拉㈣方程表示：200923285 IX. Description of the invention: [Technical field of the invention] The present invention relates to a building thermal energy management system, in particular to a type of thermal energy that transmits geothermal heat through a heat pipe or a temperature of ice water into a building via a heat pipe. Temperature control device 0 [Prior technology] In recent years, human beings have caused damage to the global environment, such as high temperature, acid rain, destruction of the ozone layer, and abnormal weather, coupled with the improper urban construction policy of the past, which has caused the living environment to deteriorate rapidly. The earth's environmental protection has been greatly ignored. Nowadays, the urban population is over-concentrated, the man-made environment is impervious, and the buildings are poorly ventilated, which often causes energy waste and urban climate hyperthermia; & to cope with the increasingly hot urban climate, home _ home; Ling ^ 豕豕 更Daxie uses air-conditioning to accelerate the discharge of hot air, which causes a cycle of urban heat. Ο In order to solve the problem of the deterioration of the urban construction environment and the above-mentioned urban green building promotion plan, the “Green Building Promotion Plan” promoted by the government has been arrested. “A Jiansui. The slashing of the environmental assessment seven major commanders” includes: How to reduce the carbon dioxide emissions of buildings, such as greening, base water conservation, owing water to the source of water, daily energy conservation, dioxide depletion, / improvement of water and garbage, etc.乃熹太安代 Dn 疋 疋 疋 发明 发明 发明 发明 发明 。 。 。 。 。 。 。 。 。 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 。 【 。 。 。 。 。 。 。 。 。 。 。 。 。 。 The heat pipe with the heat transfer temperature difference effect of the sheep, 圩200923285 provides the rapid introduction of geothermal hot air into the building, which is suitable for raising the indoor temperature in winter. The purpose of this month is to provide a building thermal management. In the system, the heat pipe in the second heat dissipation group can absorb the temperature of the ice water in the container to reduce the overflow in the building room by the outdoor air outside and the moisture on the water absorbent material. The goods 'is to provide a building thermal management system 〇 散热 2 heat dissipation group (4) is equipped with a heat pipe with a large heat flux, when the heat pipe is in contact with geothermal or water, it can effectively adjust the temperature control device in the building. The building thermal energy management system of the above object includes: a first heat dissipation group, which provides a guide for geothermal heat and external air entering, and is also composed of a plurality of heat sinks, a plurality of heat pipes, and at least one tail 35 fan, and the heat dissipation The group is arranged in a radial arrangement with a heat pipe, and the 孰 tube basin _ Μ 构 a a a 与 与 与 与 与 , , , , , , , 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发 蒸发Indirect contact with the heat sink; the fan is provided to guide the outside air to enter. The second heat dissipation group is connected to the first incineration ant heat group by a channel, and is also connected by a fan connected to the Lv phase, the H (four) ” — The fan, a 旻 政 政 政 , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , The heat-dissipation door arrangement is set to g Side, and the water-absorbing material is on the other side of the sheet, the other side of the sheet, and the heat pipe I _ and the knife constitutes the evaporation section and the cold 200923285 ' burst section and the water-absorbing material are placed in the container, the condensation section Connected with the heat sink, after the air in the guide channel or the intake duct of the coiled Gutian ^ fan enters, the second squadron is in contact with the water-absorbing material to adjust the temperature inside the building; The vaporization temperature of the working medium in the Haige official will design the adult body and the environment 'X, so when the heat pipe absorbs the geothermal (or water) heat in the evaporation section, the temperature will be greater than that of the working Jiezhe+,,, > The temperature of the working medium absorbs heat and vaporizes, and the vaporization work (for the "Bai spear to the condensation section, the condensation section is tempered by the heat sink" is also led to the building by the temperature of the fan: the second gas and the political heat sheet In the object, the temperature in the building is adjusted. [Embodiment] » The monthly heat management system provided by the present invention includes: a first heat dissipation group (1), A fan (?)' - a second heat dissipation group (3) is formed. ν The first heat dissipation group (1) is provided with a guide heat (Η) and external air entering, and is also arranged by a plurality of heat sinks (丨1) a plurality of heat pipes (12) and at least one fan (丨3), wherein the heat dissipation group is radially arranged with a heat pipe (12), and the heat pipe has a sealed space having a capillary structure (121) and a working medium (124) sealed inside, the two ends of which are respectively An evaporation section (122) and a condensation section (123), the evaporation section (122) is deep down, the condensation section (123) is connected to the heat sink (11), and the fan (13) guides the outside air. After entering, indirectly contact with the heat sink (丨〇 contact; layer 200923285 fan (2), providing guidance for external air to enter; second heat dissipation group (3) 'with one channel (14) and the first - heat dissipation group (1) The connection is also connected to the air supply fan (2), and the second heat dissipation group (3) is composed of a plurality of heat sinks (31), a plurality of heat pipes (32), a fan (33), and a container (34). And a heat absorbing material (35), wherein the heat dissipation group is arranged radially with a heat pipe (μ), the fan (33) is disposed on one side of the heat sink (31), and the water absorbing material (35) The sigh is disposed on the other side of the heat sink (31), and the heat pipe (32) has two ends forming an evaporation section (322) and a condensation section (323), respectively, the evaporation section (322) and the water absorbing material (35) Is placed in the container (34), the cold suspect section (323) is connected to the heat sink (31), when the fan (33) guides the passage (10) or the air in the intake duct enters The air is in contact with the heat sink (31) and the water absorbing material (35) for adjusting the temperature in the building (A); see Fig. 2 and Fig. 3, the working medium sealed in the heat pipe (12) ( 124) 4 The working medium (124) is filled with a porous capillary structure (丨21) for transferring heat, and is a working medium (124) used in thermodynamics to realize the conversion or transfer of thermal energy and mechanical energy or other energy. The working medium (124) of the invention may be a gas (such as an ideal gas, an actual gas, a mixed gas) or water vapor, because the gaseous substance has good fluidity and compressibility, and is convenient for absorption, rotation, and release. Or convert energy. The heat-carrying working medium (124) is selected according to the working requirements, from cryogenic liquefied gas (such as water, sterol, acetone) to liquid metal (such as: sodium, mercury, freon, sodium, silver); water and Water vapor is easy to obtain, its cost is low, and 200923285 has excellent properties such as non-corrosiveness, specific heat capacity and latent heat of vaporization, so it is the most commonly used working medium (124). The heat pipe (i 2) in the first heat dissipation group (1) utilizes the vaporization temperature (fool point) of the working medium (丨 24) depending on the characteristics of the corresponding pressure, and can be known from theoretical analysis and experimental measurements. The vaporization temperature of the working medium (124) is controlled by adjusting the pressure inside the hot t(12) tube, and the vaporization temperature of the working medium (10)) is designed to be an intermediate temperature between the body temperature of the adult body and the environment. Therefore, when the heat pipe (12) of the first heat dissipation group (1) is placed on the surface of the land via the evaporation section 〇22) and is available for the (4) geothermal (h) energy near the surface, the heat pipe ((2) its vegetable hair segment (10)) absorbs the geothermal heat ( H) the temperature of the energy is greater than the vaporization temperature of the working medium (10) and therefore works "Bei (124) absorbs heat and vaporizes; the vaporized working medium (10)) moves to the condensation section (10)), returns to ambient temperature, and condenses into a liquid state; (10)) Re-flow back to the evaporation section (10) along the capillary structure (121) due to gravity. The law of equilibrium is “the nature of the non-uniform complex phase when it is in equilibrium; the degree of freedom F of a complex phase in complete equilibrium is equal to the number of independent components C minus the number of phases p plus 2. The mathematical expression is : P+2 can be ~ is the number of two variables representing temperature and pressure. For the shore 70 single phase system, such as water, the free _ mesh is 2 ', so the temperature 7 and the pressure can be within the range of the super Independently change the human body. For the two-phase system of soap, such as water and water vapor, only one of the two variables of the monthly and the pressure can be independently changed by 200923285, so the equilibrium state can be The phase diagram of temperature 7, pressure household) is represented by a curve. For a unit three-phase system, such as a mixture of ice, water and water vapor, the degree of freedom is 0 ', indicating that temperature 7 and the pressure household have fixed values and cannot be changed. At this point the equilibrium state is represented by a point (commonly referred to as a triple point) on the (temperature 7' pressure household) phase diagram. Thermodynamic theory can prove that a certain amount of a certain gas, when the volume remains the same, 'temperature 71 is proportional to the pressure household The saturated vapor pressure of the liquid is equal to the temperature of the 'atmospheric pressure on the liquid surface. At this time, the liquid is vaporized at various points, and the liquid gas phase can be stored at 1 atmosphere (1 atm (76 mmHg)). The boiling point is called "normal boiling point". If the working medium (124) is water, the normal boiling point of water is 1 〇 {rc. When the working medium (124) of the invention is to be filled into the heat pipe (12), the vaporization temperature (such as 27t) of the working medium (124) must be preset, and the temperature of the geothermal (H) energy is absorbed by the heat pipe (12). 30. 〇 will be greater than the vaporization temperature of the working medium (124); as shown in Figure 4, it is a three-phase diagram of water, 〇 is a three-phase point, 0K is a vaporization curve, and 0L is a melting curve ' " in a one-component system In the phase equilibrium, there is no compositional variable, only two variables of temperature and pressure have to be considered. Therefore, all possible phase equilibrium relationships can be expressed by a pressure-temperature diagram 'such as S; I Wu (124) its vaporization temperature and pressure The flattened t relationship falls on the vaporization curve, and the slope d/ydM of the curve and line can be expressed by the carat (four) equation:
άρ — LH η (2) 公式（2)說明單組分系統兩相平衡時溫度τ與壓力户的關 係為-定量的該物質從„個相轉變為與之平衡共存的 10 200923285 另一個相時的熱效應和體積變化。 本發明其工作介質（124)填入熱管（12)之操作壓力會落在 况化曲線〇K ’當工作介質（124)為水時，水在lOOt：和一個標準 大氣壓情況下’水的汽化熱為539卡/克，如水要在27〇c汽化， 則可對應汽化曲線0K計算出填充熱管（12)之操作壓力值。 本發明之熱管（12)為使用真空封裝的金屬管將熱自蒸發段 (122)傳導至冷凝段（123)，在熱管（12)内有工作介質（124)，其 f、 、 中約有90%的水分’水則是為增加熱傳的添加物。 當建築物（A)欲增高其室内溫度時’則第一散熱組（1)之風 扇（13)轉動後，可將熱管（12)所吸收之地熱（H)引導至散熱片 (11 )，因熱管（12)内的壓力極低，所以工作介質（124)在約攝氏 27〜30度時即可蒸發，當地表處之蒸發段（122)的工作介質（124) 吸第熱蒸發變成蒸氣而流向冷凝段（123),並在冷凝段（123)凝 結，釋放出氣化潛熱，並於冷凝段（123)傳出熱管（12)外；在冷 "凝段（123)凝結下來的液體工作介質（124)，因管芯内的毛細壓 差重新流回蒸發段（122)，如此繼續循環帶熱，並將散熱片（u) 的熱量由風扇（13)將熱空氣流引導至第二散熱組（3)後送至建 築物（A)内’或再可再啟動第二散熱組（3)之風扇將熱空氣 加速流動至建築物（A )内’如此則可增加建築物（A )内之熱空氣。 其中’當建築物（A)欲降低其室内溫度時，則送風扇（2)啟 動以直接將室外之外部空氣藉由進氣管道導引至第二散熱組 200923285 内，同時亦可於容器（34)内置入5°C〜1(TC的水或冰水，亦將熱 管（32)内的壓力設計成工作介質（124)在約攝氏以上即可致 發，故當熱管（32)吸收容器（34)内之水後則直接降低散熱片（31) 之溫度，當風扇（33)啟動後，戶外之空氣則進入散熱片（3丨）並 通過吸水性材料（35)，該吸水性材料（35)利用表面張力作用產 生虹吸原理，使容器（34)内之水擴散在吸水性材料（35)，當外 。卩二氣經風扇（33)吹向吸水性材料（35)時，·亦將吸水性材料（35) 的水分帶引至建築物（A)内，以達調降溫之功效。 本發明之熱管U2)(32)係利用蒸發—凝結之過程傳遞熱 量，兩端溫差报小，在熱管（12)(32)兩端（蒸發段（122)與冷凝 段（123))的平均溫度差可以達到攝氏8度，所以熱管⑽⑽ 具有非常高的有效熱導’它的傳熱能力相當於同等截面銅棒的 數百倍。 統，與其他習用技術相 本發明所提供之建築物熱能管理系 互比較時，更具有下列之優點： 1.熱管的特點是當量熱導率高和等溫性好。 作介質的氣化潛熱通常报大，所以有很高的熱導率 作介質的汽化溫度取決於相應的壓力。 的溫度也相差 ，並能較習用 4·熱管内屢力沿軸線的變化不大，管内各點 不夕因而熱管具有良好的等溫性。 綜上所述，本案不但在空間型態上確屬創新 12 200923285 物品增進上❹項功效，應已充分符合新穎性及進步性之法定 發明專利要件’爰依法提出巾請，料t局核准本件發明^ 利申請案，以勵發明，至感德便。 【圖式簡單說明】 圖一為本發明建築物熱能管理系統之示音圖. 圖二為該熱管之立體剖示圖； 圖三為圖四之局部放大視意圖本發明散熱組之上視圖； 圖四為水的三相圖；以及 圖五為第二散熱組之放大示意圖。 【主要元件符號說明】 1第一散熱組 11散熱片 12熱管 121 毛細結構 122蒸發段 123 冷凝段 124 工作介質 13 風扇 14 通道 2 送風扇 3第二散熱組 13 200923285 31 散熱片 32 熱管 322蒸發段 323 冷錢段 33 風扇 34 容器 35 吸水性材料 36 進氣管道 A 建築物 Η 地熱 0 三相點 0Κ 汽化曲線 0L 融化曲線Άρ — LH η (2) Equation (2) shows that the relationship between the temperature τ and the pressure household in the two-phase equilibrium of a one-component system is - the quantitative conversion of the substance from „ phase to the equilibrium with it 10 200923285 another phase Thermal effect and volume change. The operating pressure of the working medium (124) of the present invention filled into the heat pipe (12) will fall on the conditional curve 〇K 'When the working medium (124) is water, the water is at 100 t: and a standard atmospheric pressure In the case of 'the heat of vaporization of water is 539 cal/g, if the water is to be vaporized at 27〇c, the operating pressure value of the filling heat pipe (12) can be calculated corresponding to the vaporization curve 0K. The heat pipe (12) of the present invention is vacuum-packed. The metal tube conducts heat from the evaporation section (122) to the condensation section (123), and there is a working medium (124) in the heat pipe (12), wherein about 90% of the water in the f, and the water is for increasing heat Additions. When the building (A) wants to increase its indoor temperature, the fan (13) of the first heat dissipation group (1) can be rotated to guide the heat (H) absorbed by the heat pipe (12) to the heat dissipation. Piece (11), because the pressure inside the heat pipe (12) is extremely low, the working medium (124) is about Celsius It can be evaporated at 27~30 degrees. The working medium (124) of the evaporation section (122) in the local table is evaporated to the vapor and flows to the condensation section (123), and is condensed in the condensation section (123) to release the gasification. Latent heat, and outside the heat pipe (12) in the condensation section (123); the liquid working medium (124) condensed in the cold "condensing section (123), re-flows back to the evaporation section due to the capillary pressure difference in the die ( 122), so continue to cycle with heat, and the heat of the heat sink (u) is guided by the fan (13) to the second heat dissipation group (3) and then sent to the building (A)' or again The fan that activates the second heat dissipation group (3) accelerates the flow of hot air into the building (A). This increases the hot air in the building (A). Where 'When the building (A) wants to lower its indoor temperature When the fan (2) is activated, the outdoor air outside is directly guided to the second heat dissipation group 200923285 through the intake pipe, and the water of the container (34) can also be built into the 5°C~1 (TC water). Or ice water, the pressure in the heat pipe (32) is also designed as the working medium (124) can be emitted above about the Celsius, so when the heat (32) After absorbing the water in the container (34), the temperature of the heat sink (31) is directly lowered. When the fan (33) is activated, the outdoor air enters the heat sink (3丨) and passes through the water absorbing material (35). The water absorbing material (35) utilizes the surface tension to generate a siphon principle, so that the water in the container (34) is diffused in the water absorbing material (35), and the second gas is blown toward the water absorbing material through the fan (33) ( 35), the water of the water-absorbing material (35) is also brought into the building (A) to achieve the effect of cooling. The heat pipe U2) (32) of the present invention transfers heat by means of an evaporation-condensation process, and the temperature difference between the two ends is small, and the average of the two ends of the heat pipe (12) (32) (evaporation section (122) and condensation section (123)) The temperature difference can reach 8 degrees Celsius, so the heat pipe (10) (10) has a very high effective thermal conductivity 'its heat transfer capacity is equivalent to hundreds of times the equivalent cross-section copper rod. Compared with other conventional technologies, the building thermal management system provided by the present invention has the following advantages: 1. The heat pipe is characterized by high equivalent thermal conductivity and good isothermality. The latent heat of vaporization of the medium is usually reported, so there is a high thermal conductivity. The vaporization temperature of the medium depends on the corresponding pressure. The temperature is also different, and can be used more. 4. The change of the force in the heat pipe along the axis is not large, and the heat pipes have good isothermality. To sum up, this case is not only in the space type, but also in the innovation of the 12 200923285 article to improve the effectiveness of the project. It should be fully in line with the novelty and progressiveness of the statutory invention patent requirements. Invented the ^ application, in order to invent invention, to the sense of virtue. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic view of a heat management system of a building according to the present invention. FIG. 2 is a perspective view of the heat pipe; FIG. 3 is a partial enlarged view of FIG. Figure 4 is a three-phase diagram of water; and Figure 5 is an enlarged schematic view of the second heat dissipation group. [Main component symbol description] 1 first heat dissipation group 11 heat sink 12 heat pipe 121 capillary structure 122 evaporation section 123 condensation section 124 working medium 13 fan 14 channel 2 delivery fan 3 second heat dissipation group 13 200923285 31 heat sink 32 heat pipe 322 evaporation section 323 Cold money section 33 Fan 34 Container 35 Absorbent material 36 Intake duct A Building 地 Geothermal 0 Triple point 0Κ Vaporization curve 0L Melting curve