TW201144705A - Thermal energy storage - Google Patents

Thermal energy storage Download PDF

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Publication number
TW201144705A
TW201144705A TW100103377A TW100103377A TW201144705A TW 201144705 A TW201144705 A TW 201144705A TW 100103377 A TW100103377 A TW 100103377A TW 100103377 A TW100103377 A TW 100103377A TW 201144705 A TW201144705 A TW 201144705A
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TW
Taiwan
Prior art keywords
heat transfer
heat
thermal energy
fluid
transfer fluid
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TW100103377A
Other languages
Chinese (zh)
Inventor
Andrey N Soukhojak
David H Bank
Kalyan K Sehanobish
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Dow Global Technologies Inc
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Publication of TW201144705A publication Critical patent/TW201144705A/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/02Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
    • F28D20/026Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat with different heat storage materials not coming into direct contact
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60HARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
    • B60H1/00Heating, cooling or ventilating [HVAC] devices
    • B60H1/00492Heating, cooling or ventilating [HVAC] devices comprising regenerative heating or cooling means, e.g. heat accumulators
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/02Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60KARRANGEMENT OR MOUNTING OF PROPULSION UNITS OR OF TRANSMISSIONS IN VEHICLES; ARRANGEMENT OR MOUNTING OF PLURAL DIVERSE PRIME-MOVERS IN VEHICLES; AUXILIARY DRIVES FOR VEHICLES; INSTRUMENTATION OR DASHBOARDS FOR VEHICLES; ARRANGEMENTS IN CONNECTION WITH COOLING, AIR INTAKE, GAS EXHAUST OR FUEL SUPPLY OF PROPULSION UNITS IN VEHICLES
    • B60K11/00Arrangement in connection with cooling of propulsion units
    • B60K11/02Arrangement in connection with cooling of propulsion units with liquid cooling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60KARRANGEMENT OR MOUNTING OF PROPULSION UNITS OR OF TRANSMISSIONS IN VEHICLES; ARRANGEMENT OR MOUNTING OF PLURAL DIVERSE PRIME-MOVERS IN VEHICLES; AUXILIARY DRIVES FOR VEHICLES; INSTRUMENTATION OR DASHBOARDS FOR VEHICLES; ARRANGEMENTS IN CONNECTION WITH COOLING, AIR INTAKE, GAS EXHAUST OR FUEL SUPPLY OF PROPULSION UNITS IN VEHICLES
    • B60K1/00Arrangement or mounting of electrical propulsion units
    • B60K2001/008Arrangement or mounting of electrical propulsion units with means for heating the electrical propulsion units
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D2020/0004Particular heat storage apparatus
    • F28D2020/0008Particular heat storage apparatus the heat storage material being enclosed in plate-like or laminated elements, e.g. in plates having internal compartments
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D2020/0004Particular heat storage apparatus
    • F28D2020/0021Particular heat storage apparatus the heat storage material being enclosed in loose or stacked elements
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage

Abstract

The invention is directed at articles and devices for thermal energy storage, and for process of storing energy using these articles and devices. The articles comprise a capsular structure 10 having one or more sealed spaces 14, wherein the sealed spaces encapsulate one or more thermal energy storage materials 26; wherein the capsular structure has one or more fluid passages 16 which are sufficiently large to allow a heat transfer fluid to flow through the one or more fluid passages; and when a heat transfer fluid contacts the capsular structure 10 the thermal energy storage material 26 is isolated from the heat transfer fluid. The devices include two or more articles arranged so that a fluid, such as a heat transfer fluid, may flow through the fluid passage 16 of an article before or after flowing through a space between two of the articles.

Description

201144705 六、發明說明: c發明戶斤屬之技術領域3 提申日之權利主張 本申請案係對於2010年1月29曰提申的美國臨時申請 案No. 61/299,565之提申日作權利主張,該案對於所有用途 被合併於本文中以供參考。 發明領域 本發明係有關於使用一熱能儲存材料之熱能儲存技 術,且有關於該熱能儲存材料的封裝技術以容許具有高效 率的熱量儲存及高效率的熱量轉移。 C先前技系好3 發明背景 產業一般已積極尋求一種新穎途徑以有效率地擷取及 儲存廢熱,故可在一較適宜時間予以利用。並且,在一密 實空間中達成能量儲存之欲望,係驅動著能夠在每單位重 量及單位體積中儲存高能量含量之新穎材料的研發。突破 性技術的潛在應用領域係包括運輸、太陽能、工業製造方 法暨公用及/或商用建築物暖氣技術。 對於運輸產業來說,已熟知内燃引擎的運作缺乏效 率。此缺乏效率的來源係包括從系統經由排氣、冷卻、輻 射熱及機械損失所喪失之熱量。被供應至一内燃引擎(内燃 引擎)之燃料能量估計係有高於30%經由引擎排氣喪失至環 境。 已熟知在一“冷啟動”期間,因為燃燒發生於一非最適 201144705 值溫度且内則擎由於冷潤滑_高黏度㈣要對 進行額外工作引擎如顯著較低的料操作 察 較多排放、或兩者皆然。對於内燃引擎間歇地操作藉= 長冷啟動狀況、及/或在操作载具的單—獅㈣造^冷启^ 動複數次發生之複合式電裁具,此問題益加重要。為 助解決此關,原純備製造商正尋求能夠高效率儲存及 釋放廢熱之解決方案。基本概念料在正常載具操作:間 收回及儲存廢熱’接著在1後時間㈣式釋放此熱量藉 以降低或盡量減少冷啟動狀況的時程及料並終將改良; 燃引擎效率、降低排放、或兩者皆然。 & 為了成為-實際的解決方案,熱能儲存系統具有極高 的能量密度及熱功率密度要求。中請人先前6經提申:二 名稱為“熱能儲存材料”且於2〇〇9年2月20日提申的美國專 利申請案N。. 12/389,416 ; 2)名稱為“熱量儲存裝置”且於 2〇09年2月2G日提中的美國專利中請案N。12/389,598 ;及 3 )名稱為“利用熱能儲#材料之熱量轉移系統,,且於2 〇 〇 9年 12月14日提巾的PCT巾請額。· pcT/測9/67823。這些先前 申凊案整體被合併於本文中以供參考。 先則技藝中具有已知的熱量儲存裝置及排氣熱量收回 裝置然而,為了提供一長期(譬如大於約6小時)熱量儲存 旎力,其一般佔用大型體積、需要泵送大量的熱量轉移流 體、需要一相對較大的泵來克服液壓阻抗、及類似作用。 因此’需要具有-可提供高能量密度、高功率密度、長熱 量留置時間、輕重量、對於熱量轉移流體之低液壓阻抗的 4 201144705 一前所未見組合、或其任何組合之熱量儲存系統。 c發明内容3 發明概要 本發明的一態樣係為一物件,其包含一具有一或多個 經密封空間之囊狀結構,其中經密封空間係包封一或多個 熱能儲存材料;其中囊狀結構具有一或多個充分夠大的流 體通道以容許一熱量轉移流體流過該一或多個流體通道; 且當一熱量轉移流體接觸囊狀結構時,熱能儲存材料係與 熱量轉移流體隔離。 本發明的另一態樣係為一裝置,其包括一容器及複數 個物件,其具有一流體通道且含有該熱能儲存材料,諸如 複數個此處所述的物件,其中該等複數個物件係堆積使得 流體通道軸向地對準。 本發明的一方法相關態樣係為一用於從一諸如此處所 述的裝置等熱量儲存裝置移除熱量之方法,其中該方法包 括一使一熱量轉移流體流過該裝置之步驟。較佳地,該方 法包括使一具有一初始溫度的熱量轉移流體流過裝置的一 入口;使熱量轉移流體流過一軸向流徑,故熱量轉移流體 可被分成複數個徑向流徑;使熱量轉移流體流過一徑向流 徑故其可從熱能儲存材料移除熱量,其中熱能儲存材料具 有大於熱量轉移流體的初始溫度之一溫度;使熱量轉移流 體流過一不同軸向流徑故複數個徑向流徑可重新合併;使 具有一出離溫度的熱量轉移流體流過裝置的一出口;其中 熱量轉移流體出離溫度大於熱量轉移流體的初始溫度。 201144705 本發明的另-方法相_樣係為1於製備或組裝_ 物件之方法’包括切割一基底片中的一開口浮 二使其具有:或多個槽’以一熱能儲存材料充填一或;個 槽,切割-覆蓋片中的-開口,及至少沿著—外周邊及— 開口周邊將覆蓋片密封性附接至基底片藉以形成—呈有— 或多個含有熱能儲存材料的經密封空間之物件。 本發明的又另-態樣係為一系統,其包括一諸如此處 所述的熱量儲存裝置等熱4儲存裝置,及—熱量轉移流 體’其中歸轉移越係熱料通於—經密触間(壁如, 熱量儲存裝置中之-物相—經密封空間)中的熱能 材料。 一本發明的物件、裝置、系統及方法係有利地能夠含有 高濃度的熱能儲存材料故可儲存大量的熱能(譬如具有高 能量密度)’㈣在熱量轉㈣體與含有熱⑽存材料的物 件之間具有-高的表面積故可使熱量被快速地轉移入及/ 或轉移出熱能儲存材料(譬如具有—高功率密度,較佳大於 約8kW/L),能夠具有類似或相等液壓阻抗之多重流徑故使 熱量被均勻地轉移至及/或轉移自不同區;具有一旋轉對稱 性使其可容易被配置;具有一強固且耐久的結構;具有一 高熱量儲存密度使其可被使用於需要密實設計、輕重量組 件或兩者之應用中;具有對於一熱量轉移流體流之較低 液壓阻抗(譬如,在約1 〇升/分鐘的熱量轉移流體泵送速率之 小於約1.5kPa的一壓降)藉以降低對於熱量轉移流體之泵送 要求,或其一組合。 6 201144705 圖式簡單說明 在下文詳細描述中藉由本發明實施例的非限制性範例 參照所註記的複數個圖式,進一步描述地詳細本發明,其 中類似的編號代表數個圖中類似的部份,其中: 第1A圖是一具有一或多個經密封隔室及一流體通道之 示範性物件的圖式; 第1B圖是一具有複數個分段之示範性物件的圖式,各 分段含有一或多個經密封隔室,分段係配置成使物件具有 一流體通道; 第2A圖是一具有一經密封隔室及一流體通道之示範性 物件的圖式; 第2B圖是可使用於該物件中之一具有一流體通道的示 範性覆蓋片之圖式; 第2C圖是一示範性物件、諸如第2A圖所示的物件之橫 剖面; 第2D圖是一可使用於一物件中之示範性經浮雕基底片 的橫剖面; 第3 A圖是可使用於一物件中之兩示範性相鄰分段的側 視圖,分段可具有一概括地對接之邊緣; 第3B圖是可使用於一物件中之兩示範性相鄰分段的側 視圖,分段可具有一概括地對接之邊緣; 第4圖是分段的一者被移位使得分段之相鄰分段底表 面位於不同平行平面上時,沿著其邊緣對接之相鄰分段的 側視圖; 7 201144705 第5A圖是可使用於一具有複數個含有熱能儲存材料的 經密封隔室之物件十之一具有複數個槽的示範性經浮雕基 底片之圖式; 第5B圖是第5圖的經浮雕片之一示範性部分的圖式; 第5C圖顯示具有對應的流體通道之物件的一示範性堆 積體; 第6A圖是一具有一或多個表面的示範性物件之圖式, 該一或多個表面含有複數個從開口延伸至外周邊之溝槽; 第6B圖是顯示一第一物件的一底表面及一第二物件的 頂表面一當兩表面各具有複數個彎曲狀溝槽時一之間的介 面之圖式; 第6C圖是一示範性物件之兩分段的圖式; 第6D圖是第6C圖的分段之一堆積體的側視圖; 第7圖是顯示一具有一頂表面之示範性物件的俯視 圖,該頂表面係為非圓形及/或具有一非圓形的開口; 第8圖顯示一示範性熱量儲存裝置之橫剖面,其包括一 容器中之物件的一堆積體; 第9圖是一示範性熱量儲存裝置之另一橫剖面,其包括 一容器中之物件的一堆積體; 第10圖是顯示一熱能儲存系統的示範性特徵構造之示 意圖。 I:實施方式3 本發明詳細描述 下文詳細描述中,連同其較佳實施例描述本發明的特 201144705 定實施例。然而’下幻_特定針對本技 施例或一特定使用技術’其 特疋貫 性實施例之簡明描述。為此,範用且僅提供示範 施例,而是;本發明包括落 =於下述的特定實 之所有替代物、修改物、及均=專__真實範圍内201144705 VI. Description of the invention: c Invented the technical field of the households. 3 Claims on the date of filing This application is for the filing date of US Provisional Application No. 61/299,565, which was filed on January 29, 2010. It is claimed that the case is incorporated herein by reference for all uses. FIELD OF THE INVENTION The present invention relates to thermal energy storage techniques using a thermal energy storage material, and packaging techniques for the thermal energy storage material to permit efficient heat storage and efficient heat transfer. BACKGROUND OF THE INVENTION The industry has generally actively sought a novel way to efficiently extract and store waste heat, so that it can be utilized at a suitable time. Moreover, the desire to achieve energy storage in a compact space drives the development of novel materials capable of storing high energy content per unit weight and unit volume. Potential applications for breakthrough technologies include transportation, solar energy, industrial manufacturing methods, and public and/or commercial building heating technologies. For the transportation industry, it is well known that the operation of internal combustion engines is inefficient. This source of inefficiency includes heat lost from the system via exhaust, cooling, radiant heat, and mechanical losses. The estimated fuel energy supplied to an internal combustion engine (internal combustion engine) is greater than 30% lost to the environment via engine exhaust. It is well known that during a "cold start" period, because combustion occurs at a non-optimal 201144705 temperature and within the engine, due to cold lubrication _ high viscosity (four), it is necessary to perform more work on an additional work engine such as significantly lower material operation, or Both are true. This problem is important for the internal electric combustion engine that intermittently operates the internal combustion engine intermittently, and/or in the operation of the single-lion (four) making of the vehicle. To help solve this problem, original pure-manufacturers are looking for solutions that efficiently store and release waste heat. The basic concept is to operate the normal vehicle: recover and store the waste heat. Then release the heat in the second time (4) to reduce or minimize the time and material of the cold start condition and improve the engine efficiency; reduce engine emissions, reduce emissions, Or both. & In order to be a practical solution, thermal energy storage systems have extremely high energy density and thermal power density requirements. The applicant has previously submitted 6 applications for the United States patent entitled “Thermal Energy Storage Materials” and submitted on February 20, 2009. 12/389,416 ; 2) In the US patent entitled "Thermal Storage Device" and filed on February 2nd, 2nd, 2009, please file N. 12/389,598; and 3) The name of the “Use of Thermal Energy Storage #materials for heat transfer system, and the amount of PCT towel for toweling on December 14, 2000. · pcT/test 9/67823. These previous The application is incorporated herein by reference in its entirety. The prior art has known heat storage devices and exhaust heat recovery devices. However, in order to provide a long-term (e.g., greater than about 6 hours) heat storage force, it is generally It takes up a large volume, needs to pump a large amount of heat transfer fluid, requires a relatively large pump to overcome the hydraulic impedance, and the like. Therefore, it needs to provide high energy density, high power density, long heat retention time, and light weight. Weight, low hydraulic impedance for heat transfer fluids 4 201144705 A heat storage system of a combination of no prior choices, or any combination thereof. c SUMMARY OF THE INVENTION An aspect of the invention is an object comprising one a one or more sealed space capsule structures, wherein the sealed space encloses one or more thermal energy storage materials; wherein the bladder structure has one or more sufficiently large fluids The passage allows a heat transfer fluid to flow through the one or more fluid passages; and when a heat transfer fluid contacts the bladder structure, the thermal energy storage material is isolated from the heat transfer fluid. Another aspect of the invention is a device A container and a plurality of articles having a fluid passageway and containing the thermal energy storage material, such as a plurality of articles described herein, wherein the plurality of articles are stacked such that the fluid passages are axially aligned. A method related to the invention is a method for removing heat from a heat storage device such as the device described herein, wherein the method includes the step of flowing a heat transfer fluid through the device. The method includes flowing a heat transfer fluid having an initial temperature through an inlet of the apparatus; causing the heat transfer fluid to flow through an axial flow path, so that the heat transfer fluid can be divided into a plurality of radial flow paths; The transfer fluid flows through a radial flow path such that it can remove heat from the thermal energy storage material, wherein the thermal energy storage material has an initial temperature greater than the heat transfer fluid a temperature; the heat transfer fluid flows through a different axial flow path so that the plurality of radial flow paths can be recombined; the heat transfer fluid having an exit temperature flows through an outlet of the device; wherein the heat transfer fluid exits the temperature An initial temperature greater than the heat transfer fluid. 201144705 A further method of the present invention is the method of preparing or assembling an article comprising cutting an open float in a substrate sheet to have: or a plurality of grooves. Filling a heat storage material with a groove, cutting-covering the opening in the cover sheet, and sealingly attaching the cover sheet to the base sheet at least along the outer periphery and the periphery of the opening to form - presenting - or more A sealed space object containing a thermal energy storage material. A further aspect of the invention is a system comprising a thermal storage device such as a heat storage device as described herein, and a heat transfer fluid The heat transfer material is transferred to the thermal energy material in the dense contact zone (the wall, such as the heat storage device - the phase - the sealed space). An object, apparatus, system and method of the present invention advantageously can contain a high concentration of thermal energy storage material so that a large amount of thermal energy can be stored (e.g., having a high energy density) '(4) in a heat transfer (four) body and an object containing heat (10) material. Having a high surface area between them allows heat to be rapidly transferred into and/or out of the thermal energy storage material (e.g., having a high power density, preferably greater than about 8 kW/L), capable of multiple or similar hydraulic impedances. The flow path allows the heat to be evenly transferred to and/or transferred from different zones; has a rotational symmetry that allows it to be easily configured; has a strong and durable structure; has a high heat storage density that allows it to be used Requires a dense design, lightweight components, or both applications; has a lower hydraulic impedance for a heat transfer fluid stream (eg, a heat transfer fluid pumping rate of less than about 1.5 kPa at about 1 liter/minute) Pressure drop) thereby reducing pumping requirements for heat transfer fluids, or a combination thereof. 6 201144705 BRIEF DESCRIPTION OF THE DRAWINGS In the following detailed description, the invention is further described in detail by reference to the accompanying drawings Wherein: Figure 1A is a diagram of an exemplary article having one or more sealed compartments and a fluid passage; Figure 1B is a diagram of an exemplary article having a plurality of segments, each segment Containing one or more sealed compartments, the segmentation system is configured to provide a fluid passage for the article; Figure 2A is a diagram of an exemplary article having a sealed compartment and a fluid passage; Figure 2B is usable A schematic view of an exemplary cover sheet having a fluid passageway in one of the articles; FIG. 2C is a cross-sectional view of an exemplary article, such as the object shown in FIG. 2A; and FIG. 2D is an object that can be used for an object A cross-section of an exemplary embossed base sheet; Figure 3A is a side view of two exemplary adjacent segments that can be used in an object, the segments can have a generally butted edge; Figure 3B is Can be used A side view of two exemplary adjacent segments of the article, the segments may have a generally butted edge; Figure 4 is the one of the segments being displaced such that the adjacent segmented bottom surfaces of the segments are in different parallel Side view of adjacent sections abutting along its edges in a plane; 7 201144705 Figure 5A is a diagram of a plurality of articles that can be used in a sealed compartment having a plurality of sealed compartments containing thermal energy storage materials. A schematic view of an exemplary embossed base sheet; Figure 5B is a diagram of an exemplary portion of the embossed sheet of Figure 5; Figure 5C shows an exemplary stack of articles having corresponding fluid passages; The figure is a diagram of an exemplary article having one or more surfaces, the one or more surfaces including a plurality of grooves extending from the opening to the outer periphery; and FIG. 6B is a bottom surface showing a first object and A top surface of a second object is a pattern of interfaces between the two surfaces when there are a plurality of curved grooves; FIG. 6C is a diagram of two segments of an exemplary object; FIG. 6D is a Side view of one of the segments of the 6C diagram; 7 is a top plan view showing an exemplary article having a top surface that is non-circular and/or has a non-circular opening; FIG. 8 shows a cross-section of an exemplary heat storage device. A stack comprising an object in a container; Figure 9 is another cross section of an exemplary heat storage device including a stack of articles in a container; Figure 10 is an illustration showing a thermal energy storage system Schematic diagram of the construction of sexual characteristics. I. Embodiment 3 Detailed Description of the Invention In the following detailed description, the specific embodiment of the present invention is described in conjunction with the preferred embodiments thereof. However, the following is a brief description of the specific embodiments of the present technology or a specific use technique. To this end, the exemplary embodiments are provided, and the present invention includes all of the alternatives, modifications, and

所教導所見’本發明提供用於儲存餘及/或轉移 所儲存熱能至-流體之__件H 本發明之用於儲存熱能的物件及裝置係在儲存:能 上更具效率’可容許更㈣地轉移熱能,可料以_ 移流體的-較小壓降來轉移熱能,或其任何植人。…、 之物ΓΓ月1 各種不同態樣係、斷言位於-包括-囊狀結構 物件上’該囊狀結構具有-或多個經密封空間(亦即囊袋) 及破包封在囊狀結構的—或多個經密封空間中之—或多個 熱能儲存材料,故使熱能儲存材料無法流出囊狀結構外或 以另外方式從囊狀結構被移I囊狀結構具有—新賴幾何 結構,其包括-或多個充份夠大的流體通道使得囊狀结構 —容許-流體(譬如-熱量轉移流體)流過流體通道。轨能 儲存材料係被充分地包封於經密封空間的一或多者中故 t熱量轉移流體接觸囊狀結構時,熱能儲存材料係與流體 隔離本發明的其他树係包括包含複數個料物件之新 賴配置,包含該等物件的—或多者之新縣置用於製造 遠物件之新穎方法,及使用該等物件的-❹者之新穎方 法。利用該新穎物件,可以組裝能夠儲存大量熱能、能夠 將熱能快速轉移人或轉移出減儲存材料、能夠身為密實 201144705 狀、能夠具有輕重量、能夠具有一熱量轉移流體的低壓降、 或其任何組合之裝置。 囊狀結構 囊狀結構一般具有比其他方向的維度更小之位於一方 向中的一維度(亦即厚度)。囊狀結構具有一或多個開口(亦 即流體通道),較佳位於囊狀結構的較小方向中。 開口 /流體通道 囊狀結構具有一或多個流體通道。較佳地,囊狀結構 具有一流體通道。該一或多個流體通道可容許一流體、諸 如一熱量轉移流體流過物件而不接觸熱能儲存材料。流體 通道(譬如流體通道的橫剖面區域)較佳充份夠大使得熱量 轉移流體可以極小壓力損失流過流體通道。流體通道較佳 係接近或包括囊狀結構的幾何中心。如後文所述,一接近 或包括囊袋幾何中心之流體通道,係可容許物件被使用在 一特徵概括身為一揭歇曼系統(Tichelmann system)之裝置 中。 流體通道可具有利於流體通過囊狀結構之任何橫剖面 形狀。非限制性地,流體通道可具有一軸向方向,且流體 通道對於軸向方向的一法向平面之一橫剖面係可概呈圓 形,概呈多角形,或概呈卵形。較佳地,流體通道具有一 概呈圓柱形形狀。譬如,流體通道可具有一軸向方向,且 流體通道之對於軸向方向的一法向平面之橫剖面可概呈圓 形。 流體通道的長度可能是容許高效率熱量轉移之任何長 10 201144705 度且較佳身為囊狀結構的厚度。流體通道的尺寸係為流體 通道的直徑之—测量值(譬如,對於一具有概呈圓枉形形狀 之流體通道)’或從開口中心至囊狀結構的一表面之最短距 離的兩倍。流體通道的尺寸較佳大於約0.1mm,更佳大於 、、勺〇’5mm,甚至更佳大於約1mm,且最佳大於約2mm,故 一流體可流過開π。流體通道的尺寸可充份夠小使得流體 通道不佔用大體積的空間(譬如,其原本可被—熱能儲存材 料所佔用)。較佳地,流體通道具有小於約20mm的-尺寸。 S如"IL體通道可具有一包括較佳小於約10mm的半徑之概 呈圓形橫剖面。 將瞭解:—具有一或多個經密封空間及一流體通道之 囊狀結構可從具有一諸如編號16所示的流體通道之單—纽 件形成,諸如第1A圖所示的物件1〇中所顯示,或藉由組裝 及/或配置複數個一起提供概括相同形狀之分段2而成諸 如第1B圖所示的囊狀結構1〇,。因此,可藉由單一分段或藉 複數個分段2提供-層的囊袋,包括—或多個經密封空間。 <有利地藉由複數個分段提供—囊狀結構,故紐或降低 該結構中的應力(顺應力,或其他)^可有繼藉由複數個 分段提供一囊狀結構,因此一經密封空間若失效(譬如洩漏 或刺穿)時’將導致熱能储存材料的損失減少。若囊狀結構 由複數個分段形成,分段數可為二或更大,i或更大,約 四或更大,或約六或更大。分段數較佳為約1〇〇或更小,更 佳約30或更小,且最佳約1〇或更小。將瞭解當囊狀結構為 大贺(譬如在-或多個方向中大於約5〇〇_)時、或當囊狀結 201144705 構中的熱能儲存材料欲以隔室分成100或更多個經密封空 間時,可採用大於100個分段。一囊狀結構的一分段一諸如 第1B圖所示的一囊狀結構10之分段2—可具有一頂表面及 一底表面,其形成囊狀結構之頂表面4及底表面6的一部 分。一囊狀結構的一分段一諸如第1B圖所示的一囊狀結構 10之分段2—可具有一邊緣表面,其變成囊狀結構的外邊緣 表面8之一部分。一囊狀結構的一分段一諸如第1B圖所示的 一囊狀結構10之分段2—可具有一邊緣表面,其形成囊狀結 構的開口之一部分。一囊狀結構的一分段一諸如第1B圖所 示的一囊狀結構10之分段2—可具有一或多個邊緣(譬如兩 邊緣),其各對接於一相鄰分段的一邊緣。 一囊狀結構的二或更多個分段(譬如,共用一共同邊緣 之兩分段)、或甚至全部分段係可包括相同的熱能儲存材料 或可包括二或更多種不同的熱能儲存材料。較佳地,一囊 狀結構中之分段係包括複數個具有相同熱能儲存材料之分 段。更佳地,囊狀結構中的全部分段具有相同的熱能儲存 材料。 一對相鄰的分段可具有相同形狀、體積、或兩者,或 可具有不同形狀、體積、或兩者。較佳地,囊狀結構係包 括具有概括相同體積之相鄰分段。較佳地,囊狀結構包括 概括具有相同厚度之相鄰分段。更佳地,囊狀結構包括概 括具有相同形狀及尺寸之相鄰分段。最佳地,囊狀結構係 包括具有相同形狀、尺寸及體積之相鄰分段;實質由其組 成;或由其組成。 12 201144705 當一囊狀結構包括二或更多分段時,可能需將分段配 置成使相鄰分段的邊緣之間的流體流被降低、盡量減少、 或甚至消除。將瞭解若相鄰分段由一間隙所分離,一流體 (譬如一熱量轉移流體)可徑向地流動於開口與囊狀結構的 外部周邊之間並因此減少沿著囊狀結構的頂及底表面之熱 量轉移。本發明的不同實施例中,一囊狀結構中的相鄰分 段可被定形及/或配置有對接邊緣,故使相鄰分段之間的熱 量轉移流體流被降低、盡量減少、或消除。較佳地,相鄰 分段係具有概括地對接之邊緣。 囊狀結構及/或物件的形狀可由封裝空間所界定並可 被奇特地定形。物件可包括一具有一頂表面之覆蓋片(亦即 一覆蓋片)及一具有一底表面之概括相對的基底片。覆蓋片 (譬如覆蓋片的頂表面)、基底片(譬如基底片的底表面)、或 兩者係可具有一身為(或可可)概呈扁平(譬如具有一概呈平 面性表面)、概呈梹形、或其任何組合之部分。較佳地,基 底片及/或基底片的底表面係包括一概呈拱形部分或概呈 拱形,且物件的頂表面概呈平面性(譬如覆蓋片概呈扁平)。 覆蓋片及基底片皆包括一或多個開口。覆蓋片及基底 片配置成使覆蓋片的至少一開口重疊於基底片的至少一開 口。因此,覆蓋片及基底片具有一或多個對應的開口。覆 蓋片具有最遠離覆蓋片中心之區中的一外周邊。覆蓋片在 接近覆蓋片的一開口(較佳接近中心)之覆蓋片的區中具有 一或多個開口周邊。基底片在遠離基底片中心之區中具有 一外周邊,以及接近基底片的開口(較佳接近中心)之一開口 13 201144705 周邊。覆蓋片及基底片各者可沿著片的各別外周邊被密封 性附接至彼此或密封性附接至_或多個其他選用性次結構 (諸如-外環)’以在其間形成—或多個經密封空間。覆 及基底片各者可沿著片的各別開口周邊被密封性附接至彼 此或密封性附接至-或多個其他制性次結構(諸如一内 環),以在其間形成一或多個經密封空間。較佳地,覆蓋片 及基底片沿著其各別外周邊、沿著其各別對應開口周邊的 至少-者、或兩者被密封性附接至彼此。最佳地,覆蓋片 及基底片沿著其各別外周邊且沿著其各別對應開口周邊的 至^者被密封性附接至彼此。將瞭解覆蓋片及基底片亦 °著4多個額外的區(並非其周邊)被密封性附接至彼 此或密封性_至-❹個其他_祕次 複數個經密封空間。 〜成 囊狀結構可選用性地包括一或多個次結構,其當被密 =附接至—基底片及一覆蓋片時係形成一或多個經密封 Γ間二或多個次結構可用來形成-或多個壁,其使一或 二:二空間與一熱量轉移流體分離。譬如囊狀結構 其壁以沿著囊狀結構的—或多個側 r s㈣讀空間與-熱量轉移流體隔離。另- Ιϋ例t ’囊狀結構可包括 囊狀結構之流體通.曾心, 沿著經過 4通道的至少—部分__或多個經密封空 二一二的話’内環可具有能夠被密封性附接至基底片 何結周邊、覆蓋片的—開"周邊且較佳兩者之任何幾 〇 德地,内環的内橫剖面具有與覆蓋片、基底片、 14 201144705 或兩者的開口相似的一尺寸及形狀。若採用的話,外广 具有可被密封性附接至基底片的外周邊、覆蓋片的―:: 邊且較佳兩者之任何幾何結構。較佳地,該環的外周 具有與覆蓋片、基底片、或兩者的外周緣相似的面 形狀。-或多個次結構可用來形成—或多個壁,其及 或更多個經韻空間或提供兩或更多個經密封空間^兩 -流體隔離。譬如,-或多個次結構可包括—或多個概= 徑向壁’-或多個概呈圓柱形壁,及類似物。另—範例 -或多個次結構可包括-蜂巢或其他開放格室結構,語’ 2_年Η)月8日公開的班克(Bank)等人的美國專利申= 公告胤2_初〇189的_4段所描述,該案合併於本= 以供參考…或多個次結構(譬如,内環,外環, 至結構)的Μ度應充份夠厚以含有熱_存材料、 該結構、或兩者。一或多個次結構的壁厚度較佳大於撐 一’且更佳大於約。一或多個次結構(譬如 ^ 外環,或職格室結構)_厚度應充份夠薄錢物=’ 及/或重1的-大部分可為熱能儲存材料。—或多個a社積 的壁厚度較佳小於約5mm,更佳小於約lmm,且^構 約0.2mm。 小於 囊狀結構的厚度係由物件的頂表面(譬如,覆蓋 表面)與物件的底表面(譬如,基底片的底細k間的的頂 分離所界定。物件可具有_幾何結構使得熱量可L均 -流體被提供至熱能料材料及/或快速地從熱能^ 料被移除至-流體。譬如,物件可能相對較薄(譬如,與= 15 201144705 件的長度或直徑作比較)。較佳地,物件的厚度小於約 80mm,更佳小於約2〇_,甚至更佳小於約⑺腿且最佳小 於約5mm。物件的厚度較佳大於狐5_,更佳大於約 1mm 〇 物件的最長維度(譬如物件的長度或直徑)通常遠大於 料的厚度’使得物件可譬如具有—大體積(譬如用於含有 大體積的熱能儲存材料)、及一大表面積(譬如用於快速轉 移熱能)。物件的最長維度較佳大於約3〇,更佳大於約50mm 且最佳大於約lGGmm。最長維度由用途界定,並可身為滿 足特疋用途中對於熱量儲存、熱量轉移、或兩者的需求 之任何長度。物件的最長維度通常小於約(亦即 2000mm),然而亦可採用具有大於約2m最長維度之物件。 夕物件可具有-或多個側表面。譬如,物件可具有一或 夕個非平面性的側表面。物件可具有概呈拱形、概呈非平 。、概呈連續性、或其任何組合之單一側表面❶較佳地, 一或多個側表面係與物件的—中心概呈等距,故物件可被 放置在-具有—概呈圓柱形腔體之容器中,該概呈圓柱形 腔體具有只略微大於物件平均直徑之一腔體直徑。當腔體 於物件平均直徑具有低的比值時,大量_體被物As taught, the present invention provides for storing and/or transferring stored thermal energy to a fluid. The object and apparatus for storing thermal energy of the present invention are more efficient in storage: energy can be tolerated. (4) Transfer of thermal energy from the ground, it is possible to transfer heat energy with a small pressure drop of _ fluid, or any implanted person. ..., the object of the month 1 various aspects of the system, assertions located on - including - capsule structure object - the capsule structure has - or a plurality of sealed spaces (ie pockets) and broken envelopes in the capsule structure - or a plurality of heat-storage materials in the sealed space - so that the thermal energy storage material cannot flow out of the sac structure or otherwise be moved from the sac structure - the rib structure has a new structure, It includes - or a plurality of sufficiently large fluid passages such that the bladder-allowing-fluid (e.g., heat transfer fluid) flows through the fluid passage. The rail energy storage material is sufficiently encapsulated in one or more of the sealed spaces such that when the heat transfer fluid contacts the bladder structure, the thermal energy storage material is isolated from the fluid. Other tree systems of the present invention include a plurality of material objects. The new configuration, including the novel method of manufacturing the remote object, or the novel method of using the object. With the novel object, it is possible to assemble a low pressure drop capable of storing a large amount of heat energy, capable of transferring heat energy quickly or transferring out of a storage material, capable of being dense, capable of having a light weight, capable of having a heat transfer fluid, or any Combined device. Cystic Structure The capsular structure generally has a dimension (i.e., thickness) that is smaller in the lateral direction than the dimension in the other direction. The bladder structure has one or more openings (i.e., fluid passages), preferably located in a smaller orientation of the bladder structure. Opening/Fluid Channel The capsule structure has one or more fluid passages. Preferably, the bladder structure has a fluid passage. The one or more fluid passages allow a fluid, such as a heat transfer fluid, to flow through the article without contacting the thermal energy storage material. The fluid passage (e.g., the cross-sectional area of the fluid passage) is preferably sufficiently large that the heat transfer fluid can flow through the fluid passage with minimal pressure loss. The fluid passage preferably approximates or includes the geometric center of the bladder structure. As will be described hereinafter, a fluid passageway that is close to or includes the geometric center of the bladder allows the article to be used in a device that is characterized as a Tichelmann system. The fluid passageway can have any cross-sectional shape that facilitates fluid passage through the bladder structure. Without limitation, the fluid passageway may have an axial direction, and the fluid passageway may be substantially circular in shape to one of the normal planes of the axial direction, substantially polygonal, or substantially oval. Preferably, the fluid passage has a generally cylindrical shape. For example, the fluid passage may have an axial direction and the cross section of the fluid passage to a normal plane in the axial direction may be substantially circular. The length of the fluid passage may be any length that allows for a high efficiency heat transfer of 10 201144705 degrees and preferably a bladder structure. The fluid passage is sized to measure the diameter of the fluid passage (e.g., for a fluid passage having a generally circular shape) or twice the shortest distance from the center of the opening to a surface of the bladder. Preferably, the fluid passageway has a size greater than about 0.1 mm, more preferably greater than, less than 5 mm, even more preferably greater than about 1 mm, and most preferably greater than about 2 mm, so that a fluid can flow through the opening π. The size of the fluid passage can be sufficiently small that the fluid passage does not occupy a large volume of space (e.g., it can be occupied by the thermal energy storage material). Preferably, the fluid passage has a - dimension of less than about 20 mm. The <IL body channel can have a generally circular cross-section including a radius preferably less than about 10 mm. It will be appreciated that: a capsule structure having one or more sealed spaces and a fluid passageway may be formed from a single piece having a fluid passage such as number 16 as shown in Figure 1A. As shown, or by assembling and/or configuring a plurality of segments 2 that together provide the same shape, such as the capsule structure 1A shown in FIG. 1B. Thus, a layer of bags can be provided by a single segment or by a plurality of segments 2, including - or a plurality of sealed spaces. <Advantageously provided by a plurality of segments - a sac-like structure, so that the stress in the structure (reducing stress, or other) can be followed by providing a saclike structure by a plurality of segments, thus If the sealed space fails (such as leaking or piercing), it will result in a loss of thermal energy storage material. If the sac structure is formed by a plurality of segments, the number of segments may be two or more, i or greater, about four or greater, or about six or greater. The number of segments is preferably about 1 Torr or less, more preferably about 30 or less, and most preferably about 1 Torr or less. It will be understood that when the capsular structure is Dahe (such as greater than about 5 〇〇 in multiple directions), or when the thermal energy storage material in the saclike junction 201144705 is intended to be divided into 100 or more compartments by compartment When sealing the space, more than 100 segments can be used. A segment of a bladder structure, such as segment 2 of a bladder structure 10 as shown in FIG. 1B, may have a top surface and a bottom surface that form the top surface 4 and the bottom surface 6 of the bladder structure. portion. A segment of a bladder structure, such as segment 2 of a bladder structure 10 as shown in Fig. 1B, may have an edge surface that becomes part of the outer edge surface 8 of the bladder structure. A segment of a bladder structure, such as segment 2 of a bladder structure 10 as shown in Fig. 1B, can have an edge surface that forms part of the opening of the capsule structure. A segment of a capsule structure, such as segment 2 of a capsule structure 10 as shown in FIG. 1B, may have one or more edges (eg, two edges) that each abut one of an adjacent segment edge. Two or more segments of a capsule structure (for example, two segments sharing a common edge), or even all segments may comprise the same thermal energy storage material or may comprise two or more different thermal energy stores material. Preferably, the segmentation in a capsule structure comprises a plurality of segments having the same thermal energy storage material. More preferably, all segments in the bladder structure have the same thermal energy storage material. A pair of adjacent segments may have the same shape, volume, or both, or may have a different shape, volume, or both. Preferably, the bladder structure comprises adjacent segments having substantially the same volume. Preferably, the bladder structure includes adjacent segments that are of the same thickness. More preferably, the bladder structure includes adjacent segments that are of the same shape and size. Most preferably, the capsular structure comprises adjacent segments of the same shape, size and volume; consisting essentially of; or consisting of. 12 201144705 When a capsule structure comprises two or more segments, it may be necessary to configure the segments such that fluid flow between the edges of adjacent segments is reduced, minimized, or even eliminated. It will be appreciated that if adjacent segments are separated by a gap, a fluid (such as a heat transfer fluid) can flow radially between the opening and the outer periphery of the bladder structure and thereby reduce the top and bottom of the bladder structure. Heat transfer from the surface. In various embodiments of the present invention, adjacent segments in a bladder structure may be shaped and/or configured with butted edges such that heat transfer fluid flow between adjacent segments is reduced, minimized, or eliminated. . Preferably, adjacent segments have edges that are generally butted. The shape of the bladder structure and/or article may be defined by the package space and may be oddly shaped. The article can include a cover sheet having a top surface (i.e., a cover sheet) and a generally opposite base sheet having a bottom surface. The cover sheet (such as the top surface of the cover sheet), the base sheet (such as the bottom surface of the base sheet), or both may have a flat shape (e.g., having a planar surface), an outline 梹Shape, or part of any combination thereof. Preferably, the bottom surface of the base sheet and/or the base sheet comprises a generally arcuate portion or a generally arched shape, and the top surface of the article is substantially planar (e.g., the cover sheet is generally flat). Both the cover sheet and the base sheet include one or more openings. The cover sheet and the substrate sheet are configured such that at least one opening of the cover sheet overlaps at least one opening of the base sheet. Thus, the cover sheet and the substrate sheet have one or more corresponding openings. The cover sheet has an outer periphery that is furthest from the center of the cover sheet. The cover sheet has one or more open perimeters in the region of the cover sheet adjacent an opening (preferably near the center) of the cover sheet. The substrate sheet has an outer periphery in a region away from the center of the substrate sheet, and an opening 13 201144705 near the opening (preferably near the center) of the substrate sheet. Each of the cover sheet and the substrate sheet may be sealingly attached to each other along the respective outer periphery of the sheet or sealingly attached to _ or a plurality of other optional secondary structures (such as an outer ring) to form therebetween - Or multiple sealed spaces. Each of the covering substrate sheets may be sealingly attached to each other along the perimeter of the respective opening of the sheet or sealingly attached to - or a plurality of other sub-structures (such as an inner ring) to form an Multiple sealed spaces. Preferably, the cover sheet and the substrate sheet are hermetically attached to each other along at least their respective outer periphery, at least along the perimeter of their respective corresponding openings, or both. Most preferably, the cover sheet and the substrate sheet are hermetically attached to each other along their respective outer periphery and along their respective corresponding opening perimeters. It will be appreciated that the cover sheet and the substrate sheet are also sealed to each other by more than four additional zones (not the periphery thereof) or sealed to a plurality of sealed spaces. The sac-like structure optionally includes one or more sub-structures which, when densely attached to the substrate sheet and a cover sheet, form one or more sealed inter-secondary or multiple sub-structures available To form - or a plurality of walls that separate one or two: two spaces from a heat transfer fluid. For example, a saclike structure whose walls are isolated from the heat transfer fluid along the - or multiple side r s (four) read spaces of the sac structure. In addition - the case t 'capsule structure may include a fluid passage of the saclike structure. Zeng Xin, along at least - part __ or a plurality of sealed empty two or two through the 4 channels, the inner ring may have a seal Attached to the periphery of the substrate sheet, the cover sheet-opening " peripheral and preferably any of the two, the inner cross section of the inner ring has a cover sheet, a base sheet, 14 201144705 or both A similar size and shape of the opening. If used, the outer cover has any geometry that can be sealingly attached to the outer periphery of the substrate sheet, the ":: edge of the cover sheet, and preferably both. Preferably, the outer circumference of the ring has a face shape similar to the outer periphery of the cover sheet, the base sheet, or both. - or a plurality of secondary structures may be used to form - or a plurality of walls, and or more of the rhyme space or to provide two or more sealed spaces. For example, - or a plurality of secondary structures may include - or a plurality of substantially radial walls - or a plurality of substantially cylindrical walls, and the like. Alternatively - the example - or multiple substructures may include - a honeycomb or other open cell structure, the US patent application of Bank et al. published on the 8th of the month of the term '2_年Η', 8th Anniversary As described in paragraph _4 of 189, the case is incorporated in this = for reference... or multiple secondary structures (for example, inner ring, outer ring, to structure) should be sufficiently thick to contain heat_storage material, The structure, or both. The wall thickness of the one or more secondary structures is preferably greater than the support and more preferably greater than about. One or more secondary structures (such as ^ outer ring, or compartment structure) _ thickness should be sufficient for thin money = ' and / or weight 1 - most of which can be thermal energy storage materials. Preferably, the wall thickness of the plurality of a-composites is less than about 5 mm, more preferably less than about 1 mm, and the structure is about 0.2 mm. The thickness of the smaller than the capsular structure is defined by the top surface of the article (for example, the covering surface) and the bottom surface of the article (for example, the top separation between the bottom k of the substrate sheet. The object may have a geometry such that the heat can be L - the fluid is supplied to the thermal energy material and/or quickly removed from the thermal energy to the fluid. For example, the article may be relatively thin (e.g., compared to the length or diameter of the piece = 201144705). Preferably The thickness of the article is less than about 80 mm, more preferably less than about 2 〇, even more preferably less than about (7) legs and most preferably less than about 5 mm. The thickness of the article is preferably greater than the longest dimension of the fox 5_, more preferably greater than about 1 mm. For example, the length or diameter of the article is generally much larger than the thickness of the material so that the article can have, for example, a large volume (for example, for containing a large volume of thermal energy storage material), and a large surface area (such as for rapid transfer of thermal energy). The longest dimension is preferably greater than about 3 Torr, more preferably greater than about 50 mm, and most preferably greater than about 1 GG mm. The longest dimension is defined by the use and can be used for thermal storage, heat transfer, etc. Any length of demand for both. The longest dimension of the article is typically less than about (i.e., 2000 mm), although articles having a longest dimension greater than about 2 m may also be employed. The article may have - or multiple side surfaces. For example, the article may have One or a non-planar side surface. The article may have a generally arched, substantially non-flat, substantially continuous, or any combination thereof, preferably a single side surface, preferably one or more side surface systems The object is substantially equidistant from the center of the object, so that the object can be placed in a container having a generally cylindrical cavity having a cavity diameter that is only slightly larger than the average diameter of the object. When the cavity has a low ratio of the average diameter of the object, a large amount of body

件所佔用。譬如,腔體直徑對於物件平均直徑之比值可小 於約1 R •,較佳小於約1.2 ,更佳小於約u,且最佳小於約 l05。將瞭解腔體直徑對於物件平均直徑之比值一般至少 為約1〇(譬如至少約1.001)。 囊狀結構體積的一大部分係為經包封體積(亦即,一或 16 201144705 多個經密封空間的體積),故物件可含有—相對較大 =存材料。物件的-或多個經密封空間之總體積係佔物 仏體積之較佳至少約灣前分比,更佳至少物體積 百分比,甚至更佳至少約85體積百分比且最佳9〇體積百分 比。物件的-或多個經密封空間之總體積—般係佔物件:Occupied by the pieces. For example, the ratio of the diameter of the cavity to the average diameter of the article can be less than about 1 R •, preferably less than about 1.2, more preferably less than about u, and most preferably less than about 105. It will be appreciated that the ratio of the cavity diameter to the average diameter of the article is typically at least about 1 Torr (e.g., at least about 1.001). A large portion of the volume of the capsular structure is the enveloped volume (i.e., one or 16 201144705 volumes of multiple sealed spaces), so the article may contain - relatively large = stored material. Preferably, the total volume of the article- or plurality of sealed spaces is at least about the bay front ratio, more preferably at least the volume percent, even more preferably at least about 85 volume percent and most preferably 9 volume percent. The total volume of the object's - or multiple sealed spaces - is generally the object:

體積之小於約99.9體積百分比。未被熱能儲存材料佔用Z 剩餘體積係可包括囊狀結構、空隙空間(譬如含有—或多氣 體)、-或多個用於改良熱能儲存材料與囊狀結構之間2 量轉移之結構 '或其任何組合,或者實質完全由其組 用於改良熱能儲存材料與囊狀結構之間的熱量轉移之結構 係包括由—具有—相對較高熱傳導率(譬如相對於熱_ 存材料)藉以能夠增加從熱能儲存材料至—熱量轉移 的熱量流率之㈣卿成的任何結構。用於改良熱量流率 之適當的結構係包括H片,索線網目,進人經密封空: 之突件,及類似物》 二0 物件較佳易於與其他相同形狀的物件、或具有—概括 對接表面之其他物件作堆積。譬如,兩待堆積物件可具有 身為概括對接表面之相對的表面,故當堆積時,兩物;嵌 套,-起。將瞭解i於堆積物件使其易於嵌套在—起: 途也係選擇具有—高階旋轉對稱性之—形狀(譬如,—拱形 ,面的—形狀,經密封空間的—形狀,或兩旬。旋轉對稱 =可沿堆積方向中的-條減(譬如—條經過囊狀結構的 ^體通道之軸線)。旋轉對稱性的階數(〇,_般係描述被 堆積在—起的兩表面之間的不同旋轉數,其中將使之嵌套 17 201144705 在一起。物件、基底片(譬如基底片的拱形表面)、或兩者之 旋轉對稱性的階數係較佳為至少2,更佳至少3,甚至更佳 至少5,且最佳至少7。 本發明的一特佳實施例中,相鄰層(譬如相鄰的囊狀結 構)未嵌套在一起。譬如,一第一層的(譬如一第一囊狀結構 的)一頂表面可接觸於一第二層的(譬如一第二囊狀結構的) 一底表面。接觸中的頂表面、底表面、或兩者可具有一或 多個徑向溝槽或徑向通路(亦即,一具有一徑向組件(亦即, 溝槽或通路之至少一部分的定向包括徑向方向上的一突 部)、且較佳從中心開口延伸至囊狀結構的外周邊之溝槽或 通路),其容許一熱量轉移流體流動於兩表面之間。譬如, 第一層的覆蓋片及第二層的基底片可具有一從開口至外周 邊延伸於一直線中之直線狀溝槽或通路。除了具有一徑向 組件外,一溝槽或通路可具有一切線組件(亦即,溝槽或通 路之至少一部分的定向包括切線方向上的一突部)。譬如, 一溝槽或通路可具有一螺旋形狀,其包括一徑向組件及一 切線組件兩者。處於接觸的兩片可具有不同(譬如具有不同 方向及/或不同量值)或相同之切線組件。相鄰片的切線組件 可配置成使流動於相鄰片之間的流體至少部份地混合。有 利地,一片可具有包含順時針方向中的一切線組件之溝槽 或通路,而相鄰片可具有包含逆時針方向中的一切線組件 之溝槽或通路,故當溝槽相交時(譬如,當流動於兩相鄰囊 狀結構的溝槽中的流體之兩物流在小於其完整流徑處構成 直接接觸時),流動於兩層之間的流體係至少部份地混合。 18 201144705 第6A圖是一囊狀結構10的示意圖,其具有延伸於結構16的 開口與結構的外部周邊19之間的複數個徑向溝槽15。參照 第6A圖,溝槽15可具有下列特徵構造之一者或任何組合: 身為彎曲狀,溝槽可為彎曲狀使其具有一切線組件,溝槽 可為均勻分隔,相鄰溝槽可具有相同長度,溝槽可具有一 螺旋形狀,及相鄰溝槽可提供具有相同液壓阻抗之流徑。 第6B圖是顯示一第一囊狀結構之一基底片30的一部分及一 第二囊狀結構之一覆蓋片2 8的一部分之間的接觸之示意 圖。兩接觸表面可具有概括不同的形狀或相同的概括形 狀,諸如第6B圖所示。接觸表面的溝槽可具有一或多個交 會部。如第6B圖所示,第一接觸表面的溝槽可具有一切線 部分,而第二接觸表面的溝槽可相對於第一接觸表面具有 一位於一相反方向中之切線部分。若採用溝槽或通路以提 供一流徑,一或多個表面可具有任何數量的溝槽或通路。 較佳地,囊狀結構中之溝槽或通路數量係充份夠多且充分 分散,使得流動於兩層之間(譬如兩表面之間)的熱量轉移流 體可被分入複數個流徑中以有效率地移除熱量。相鄰流徑 可為相同或不同。較佳地,兩或更多個流徑(譬如全部的流 徑)具有概括相同的長度,概括相同的液壓阻抗,或兩者。 囊狀結構一諸如第6A圖所示的囊狀結構一可具有一開 口 16,較佳位於或接近於囊狀結構的幾何中心。囊狀結構 包括一或多個經密封空間。囊狀結構可包括單一經密封空 間,諸如第6A圖所示。囊狀結構可概呈薄型並包括一頂表 面18、一底表面20—接近於外部周邊19之表面22及一接近 19 201144705 於開口之邊緣表面24。囊狀結構可包括頂表面、底表面、 或兩者上之一或多個特徵構造,其提供一流徑以供一流體 流動於至少一徑向方向中(譬如,當複數個囊狀結構被堆積 時)。此一特徵構造較佳從囊狀結構的一開口周邊21延伸至 囊狀結構的一外周邊19。此一特徵構造可提供一概呈拱 形、概呈線性之流動方向,或具有線性的區及直線狀的區。 如第6 A圖所示,可藉由從中心周邊延伸至外周邊之一或多 個通路或溝槽提供流徑。囊狀結構的頂表面或底表面中之 溝槽或通路可分佈於表面上方,故各流徑(當複數個囊狀結 構被堆積時)具有概括相同的液壓阻抗。如第6A圖所示,溝 槽或通路可具有一曲率使得流徑除了徑向組件外具有一切 線組件。當相同的囊狀結構被堆積時,此曲率可有利地防 止相鄰的囊狀結構嵌套在一起。譬如,如第6 A圖所示,可 藉由將具有概括相同形狀且皆具有複數個彎曲狀溝槽之一 覆蓋片及一基底片接合在一起,藉以製備囊狀結構。當接 合時,頂表面及底表面中之彎曲狀溝槽係彎曲於反方向(從 頂表面觀視時)。如第6A圖所示,覆蓋片及基底片可沿著開 口周邊且沿著外周邊被密封,藉以形成一經密封空間。 第6C圖是顯示用於形成一囊狀結構的一部分之兩相鄰 分段2的示意圖。如第6C圖所示,各分段可包括沿著分段的 一周邊作密封性附接之兩片。附接的區位可位於一邊緣表 面9上。如第6C圖所示,各分段可包括一或多個經密封空 間。個別分段雖可能無開口,分段可被配置於邊緣,藉以 形成一包括一開口之囊狀結構。如第6D圖所示,當一分段 20 201144705 相對於相鄰分段平移達到厚度的一比例部分(譬如厚度的 一半)時,相鄰分段的邊緣9係可對接。 囊狀結構的頂表面可概呈圓形形狀,諸如第1A及6A圖 所示的頂表面。囊狀結構之頂表面可能具有其他形狀,且 可能甚至想要具有其他形狀。譬如,囊狀結構可使用在一 需配合於一緊密空間一諸如一載具的罩蓋底下或地板底 下一之熱量儲存裝置中。雖然圓柱形狀可能有利於降低表 面積,其他較為長形、或箱形的形狀可能有利於配合至一 可取得空間内。將瞭解根據此處的教導,囊狀結構的概呈 圓形表面可有利地以非圓形的形狀所取代。因此,囊狀結 構可具有概呈卵形、概呈矩形、概呈正方形、概呈不規則 形、或其任何組合之一頂表面及/或一底表面。譬如,囊狀 結構的頂表面及/或底表面可具有一包含圓角的概呈矩形 形狀。第7圖是顯示一囊狀結構的一表面之示範性特徵構造 的圖式。如第7圖所示,囊狀結構的頂表面及底表面之周邊 的輪廓可具有一長形形狀。譬如,頂表面及底表面之(外周 邊的)輪廓可具有一概呈矩形形狀,一概呈正方形形狀,或 一概呈卵形形狀)。將瞭解頂表面中之開口的輪廓可為任何 形狀。頂表面中之開口的輪廓及頂表面之外周邊.的輪廓可 具有類似(但不同尺寸)的形狀或可具有不同(諸如一概呈圓 形開口及一非圓形外周邊)的形狀。如第7圖所示,開口的 輪廓及外周邊的輪廓可具有相同形狀,諸如概呈卵形。 物件較佳具有一難以彎折的囊狀結構。譬如,囊狀結 構可不含有其中使一覆蓋片及一基底片在橫剖面的大部份 21 201144705 或甚至全部長度(諸如囊狀結構的一直徑)處於接觸之橫剖 面。具有各種不同途徑可用來確保囊狀結構難以彎折,其 中包括·選擇囊袋的一配置使得旋轉對稱性的階數不是偶 數,選擇囊袋的一配置藉以不具有旋轉對稱性,選擇囊袋 的一配置而其包括相對於彼此旋轉使每個徑向段包括至少 一經在、封空間之兩或更多環(諸如同心環)的囊袋,或其任何 組合。將瞭解可採用其他幾何結構及其他手段使得囊狀物 件可抗彎折。譬如,囊狀結構的材料可選擇成概括具有勁 性,結構可包括一或多個肋(譬如在一切線方向中),及類似 物。 物件的所有熱能儲存材料可位於單一經密封空間中。 較佳地’物件的熱能儲存材料分佈於複數個經密封空間之 間,所以若有一經密封空間被刺穿或有其他洩漏,則只會 移除。亥熱t儲存材料的一部分。因此,物件中之經密封空 間(譬如’含有熱能儲存材料之經密封空間)的數量較佳至少 為2 ’更佳至少3,且甚至更佳至少約5 ^經密封空間數的上 限係為實例且對於一特定應用而言則由該應用的需求決 疋。然而’物件中的經密封空間數一般小於丨〇〇〇。然而, 將瞭很大的物件可具有1〇〇〇或更多個經密封空間。基於相 同理由’在任何單一經密封隔室中所發現的熱能儲存材料 之體積比例部分係佔物件中的熱能儲存材料總體積之較佳 小於約55°/。,更佳小於約38%,甚至更佳小於約29%,且最 佳小於約21%。一般而言,一經密封空間係包括至少0.1體 積%之物件中的熱能儲存材料。然而,將瞭解物件可包括 22 201144705 實質 空間 不含或甚至完全不含熱能儲存材料之―或多個經密封 0 ⑽、封空間可選驗地配置於複數_叫中 =内環(譬如~最靠近開口周邊之環)及-最外環(孽如-最錢㈣邊之環)’其各含有-或多個經密封空間:一環 中之、以封工間可具有—概呈重覆的圖案。譬如,—環中 之各、W封空間或者各群組的2、3、4或更多個經密封空間 Z具有概括相同的形狀及尺寸。各環中之經密封空間數可 W相同或不同。較佳地’最外環比S最内環具有更多個經 =間、最外環的經密封空間之平均長度小於最内環的 左 間之平均長度(其中平均長度在從開Π至外周邊 向方向中作測篁)、或兩者,故最外環及最 封空間之間的體積變異係減低。 如後文討論’物件可放置在—具有一概呈圓柱形腔 體-諸如一只比物件最長維度具有略微更大維度的腔體— m中。譬如’容H的腔體之直徑可只略微大於物件的 囊狀結構之直徑。腔體的直徑應充份夠大使得物件可被插 入腔體内。當物件(或物件的_堆積體)放置在容器中時可 能想要使-越能夠流動於物件料周邊與容器的—内部 壁之間。可藉由設計容器的内部及物件形狀之關係以生成 並維持流體紐’如達纽作用。可使祕何用於生成 此等流體流徑之手段。S1此,物件可選雜地沿著其周邊 具有-或多個凹缺(譬如,覆蓋片及基底片可沿其各別外周 邊具有-或多個對應的凹缺),藉以形成—用於供—熱量轉 23 201144705 移"IL體流動之二間。以添加或取代方式,容器的腔體可具 有一包含一或多個溝槽之表面,以供一流體流動於物件的 外周邊與容器的表面之間。另一範例中,物件的直徑相對 於腔體内部的直徑可充份夠小使得一流體可沿著物件的完 整外周邊流動。譬如,對於經密封空間的最外環中之各經 在、封空間,物件可具有一或多個凹缺或容器可具有一戋多 個溝槽。一凹缺或一溝槽可具有任何形狀,諸如一多角形, —拱形,一楔形,及類似物,限制條件在於其具有一充分 尺寸以容許熱量轉移流體流動。若採用的話,凹缺及/或溝 槽的最小維度通常為至少約〇將瞭解可使用二或更 多個用於生成-流體流徑之手段的—組合。譬如物件可 沿其外周邊具有-或多個凹缺,且物件可具有—充份夠小 的直徑故當放置在—腔體中時流體可沿其完整外周邊流 動。 "丨 丞低月1選用性地具有 〜八ΙΊ·,5又頁物什异 -具有—概括對接於基底片的表面之物件作堆積時,I 件只部份地絲m多個突件可作為一分^ 分離概括對接的表面,故-流體(譬如_熱量轉移流體)· 動於對接的表面之間。物件及魏分隔料之堆積係: 文討論。若制的話,突件較佳只覆蓋住表面及基底 -小部分,故-❹减件絲料干制流體流。 擇突件的高度轉定兩概㈣接的細之間的流徑, (譬如平均高度)。覆蓋片難不含此等突件且具有一概; 平的外表面,故兩㈣我置歧㈣以概括在其: 24 201144705 頂表面上處於接觸。 熱能儲存材料 非哏制性地 m ㈣熱量儲存裝置之適當熱能儲存材料 2=能_•賴、潛熱、妹仙兩者展現-相對較高 度之㈣。熱_存㈣·_量料裝置的操 乍’皿度㈣相*。譬如’熱能儲存材料較佳在熱量儲存裝 置的較低操作溫度時係、為-固體,在熱量儲存裝置的最: 值操作溫度時至少部份地為—液體(譬如完全為_液體),在 裝置的最大值操作溫度時未顯著地劣化或分解或其任何 虹合。當被加熱至裝置㈣大值操作溫度為期約_小時 或更久、或甚至約1_0或更久時,減儲存㈣較佳未顯 著地劣化或分解。 熱能儲存材料可為一具有一固體至液體轉換溫度之相 變材料。熱能儲存材料的固體至液體轉換溫度可為一液相 線溫度’ -融化溫度、或一共晶溫度。固體至液體轉換溫 度應充份夠高,故當熱能儲存材料至少部份地或甚至實質 完全地處於液態時,儲存有足夠能量以將一或多個受加熱 物體加熱至一所想要溫度。固體至液體轉換溫度應充份夠 低’故不使熱量轉移流體、一或多個受加熱物體、或兩者 被加熱至可能令其劣化之溫度。因此’固體至液體轉換溫 度之所想要溫度可能依據受加熱物體及轉移熱量的方法而 定。譬如,一利用一種乙二醇/水熱量轉移流體將所儲存熱 量轉移至一引擎(譬如内燃引擎)之應用中,最大值固體至液 體轉換溫度可能是熱量轉移流體劣化之溫度。另—範例 25 201144705 中,所儲存熱量可利用-熱量轉移流體被轉移至一電池的 一電化學電池芯,其中熱量轉移流體具有一高劣化溫度, 且最大值固體至液體溫度可能取決於電化學電池芯劣化或 產生其他失效之溫度。固體至液體轉換溫度可大於約3〇 °c。’較佳大於約饥,更佳大於約机,甚至更佳大於約 衫C ’且最佳大於約坑。熱能儲存材料可具有小於約働 Μ圭】、於約350 c、更佳小於約29()£>(:、甚至更佳小於 勺250 C、且最佳小於約2〇(rc的1體至液體轉換溫度。 ’、解依據應用而疋,固體至液體轉換溫度可為從約贼 "彳< 約 5GCS^15()°c’ 從約 100°C 至約 200°C, % \〇C至約25〇C ’從約175°c至約400°C,從約200°C至 C從約225 C至約彻。(:,或從約2〇(rc至約3〇(Γ(:。 心十於。^刀應用,諸如運輸相關應用,可能想要使孰能 儲存材料有效率地U 存 二間中儲存能量。因此,熱能儲 表_: °具有-高溶合熱量密度(以百萬焦耳每升的單位 25V、’ I〔、由熔°熱4(以百萬#、耳每公斤表示)與密度(在約 存材公斤每升的單位表之乘積所界定。熱能儲 …〃有大於約〇.1Mj/升、較佳大於約〇 2mj/升、更佳 -妒勺°TMJ/升、且最佳大於約〇·_升的熔合熱量密度。 户。又而t ’熱能儲存材料具有小於約蕭升的熔合熱量密 料。;、而亦可採用具有較高炫合熱量密度之熱能儲存材 儲存=二應用,諸如運輸相關應用,可能想要使熱能 材枓具有輕重量。譬如,域儲存材料可具有小於約 26 201144705 5g/cm3、較佳小於約4g/cm3、更佳小於約3㈣咖3、且最佳 小於約3g/cm3的密度(在坑測量)β密度的下限係為實例。 熱能儲存材料可具有大於約〇 6g/cm3、較佳大於約 1.2g/cm3、且更佳大於約Ug/cm3的密度(在約25它測量)。 經密封空間可含有任何技藝習知的熱能儲存材料。熱 能儲存材料隔室中可採用之熱能儲存材料的範例係包括夏 馬(Atul Sharma)、塔吉(V.V. Tyagi)、陳(c.R. Chen)、布帝(D.The volume is less than about 99.9 volume percent. Not occupied by thermal energy storage material Z Residual volume may include a saclike structure, a void space (such as containing - or multiple gases), or a plurality of structures for improving the transfer between the thermal energy storage material and the sac structure - or Any combination thereof, or a structure substantially entirely used by the group to improve heat transfer between the thermal energy storage material and the capsular structure, can be increased by having - a relatively high thermal conductivity (e.g., relative to the heat storage material) Any structure from the thermal energy storage material to the heat transfer rate of heat transfer (4). Suitable structural means for improving the heat flow rate include H-pieces, cable nets, sealed air-filled: protruding members, and the like. The objects are preferably easy to be compared with other objects of the same shape, or have Other objects on the docking surface are stacked. For example, the two objects to be stacked may have opposite surfaces that are generally abutting surfaces, so when stacked, the two objects; nested, and raised. It will be understood that the i-stacked objects make it easy to nest in the same way: the way is to have a shape with high-order rotational symmetry (for example, arched, face-shaped, sealed space-shaped, or two-way Rotational symmetry = can be reduced along the - strip in the stacking direction (for example, the axis of the strip through the hull structure). The order of rotational symmetry (〇, _ like the two surfaces that are stacked on the surface Between the different rotation numbers, which will be nested 17 201144705 together. The order of the rotational symmetry of the object, the base sheet (such as the arched surface of the base sheet), or both is preferably at least 2, more Preferably at least 3, even more preferably at least 5, and most preferably at least 7. In a particularly preferred embodiment of the invention, adjacent layers, such as adjacent bladder structures, are not nested together. For example, a first layer a top surface (such as a first bladder structure) may be in contact with a bottom surface of a second layer (such as a second bladder structure). The top surface, the bottom surface, or both of the contacts may have One or more radial grooves or radial passages (ie, one having a diameter The assembly (ie, the orientation of at least a portion of the trench or via includes a protrusion in the radial direction) and preferably extends from the central opening to a groove or passage in the outer periphery of the bladder structure, which allows for a heat The transfer fluid flows between the two surfaces. For example, the cover sheet of the first layer and the base sheet of the second layer may have a linear groove or passage extending from the opening to the outer periphery in a straight line. In addition to having a radial component Additionally, a trench or via may have all of the line components (ie, the orientation of at least a portion of the trench or via includes a protrusion in the tangential direction). For example, a trench or via may have a spiral shape, including A radial component and all of the wire assemblies. The two pieces in contact may have different (eg, different directions and/or different magnitudes) or the same tangent assembly. The tangent assembly of the adjacent sheets may be configured to flow in phase The fluid between the adjacent sheets is at least partially mixed. Advantageously, one piece may have grooves or passages containing all of the line components in a clockwise direction, and adjacent sheets may have a counterclockwise side a groove or passage of any of the wire assemblies, such that when the grooves intersect (for example, when two streams of fluid flowing in the grooves of two adjacent bladder structures form a direct contact at less than their full flow path) The flow system flowing between the two layers is at least partially mixed. 18 201144705 Figure 6A is a schematic illustration of a capsule structure 10 having a plurality of paths extending between the opening of the structure 16 and the outer periphery 19 of the structure. To the groove 15. Referring to Figure 6A, the groove 15 can have one or any combination of the following features: as a curved shape, the groove can be curved to have a line assembly, the grooves can be evenly spaced, Adjacent trenches may have the same length, the trenches may have a spiral shape, and adjacent trenches may provide a flow path having the same hydraulic impedance. Figure 6B is a portion of a substrate sheet 30 showing a first bladder structure. And a schematic view of contact between a portion of the sheet 28 of a second bladder structure. The two contact surfaces can have a generally different shape or the same general shape, such as shown in Figure 6B. The grooves of the contact surface may have one or more intersections. As shown in Fig. 6B, the groove of the first contact surface may have a line portion, and the groove of the second contact surface may have a tangential portion in an opposite direction with respect to the first contact surface. If grooves or passages are used to provide a first diameter, one or more surfaces may have any number of grooves or passages. Preferably, the number of grooves or passages in the bladder structure is sufficiently sufficient and sufficiently dispersed that heat transfer fluid flowing between the two layers, such as between the two surfaces, can be split into a plurality of flow paths To remove heat efficiently. Adjacent flow paths can be the same or different. Preferably, two or more flow paths (e.g., all of the flow paths) have generally the same length, summarizing the same hydraulic impedance, or both. The sac-like structure, such as the capsular structure shown in Figure 6A, may have an opening 16, preferably located at or near the geometric center of the capsular structure. The bladder structure includes one or more sealed spaces. The sac structure may comprise a single sealed space, such as shown in Figure 6A. The bladder structure can be generally thin and includes a top surface 18, a bottom surface 20 - a surface 22 proximate the outer perimeter 19, and an edge surface 24 adjacent the opening of the 2011. The bladder structure can include one or more features on the top surface, the bottom surface, or both that provide a first-rate diameter for a fluid to flow in at least one radial direction (eg, when a plurality of bladder structures are stacked Time). This feature configuration preferably extends from an open perimeter 21 of the bladder structure to an outer perimeter 19 of the bladder structure. This feature configuration provides a generally arched, generally linear flow direction, or a linear region and a linear region. As shown in Fig. 6A, the flow path can be provided by extending one or more passages or grooves from the center periphery to the outer periphery. The grooves or passages in the top or bottom surface of the bladder structure may be distributed over the surface so that each flow path (when a plurality of capsule structures are stacked) has substantially the same hydraulic impedance. As shown in Fig. 6A, the grooves or passages may have a curvature such that the flow path has a line assembly in addition to the radial components. This curvature advantageously prevents adjacent bladder structures from nesting together when the same bladder structure is stacked. For example, as shown in Fig. 6A, a capsular structure can be prepared by joining together a cover sheet having a substantially identical shape and having a plurality of curved grooves and a base sheet. When joined, the curved grooves in the top and bottom surfaces are curved in the opposite direction (when viewed from the top surface). As shown in Fig. 6A, the cover sheet and the base sheet can be sealed along the periphery of the opening and along the outer periphery to form a sealed space. Figure 6C is a schematic diagram showing two adjacent segments 2 for forming a portion of a capsule structure. As shown in Figure 6C, each segment can include two sheets that are sealingly attached along a perimeter of the segment. The attached location can be located on an edge surface 9. As shown in Figure 6C, each segment may include one or more sealed spaces. Although the individual segments may have no openings, the segments may be disposed at the edges to form a capsular structure including an opening. As shown in Fig. 6D, when a segment 20 201144705 is translated relative to an adjacent segment to a proportional portion of the thickness (e.g., half the thickness), the edges 9 of adjacent segments can be docked. The top surface of the bladder structure can have a generally circular shape, such as the top surface shown in Figures 1A and 6A. The top surface of the sac structure may have other shapes and may even want to have other shapes. For example, the bladder structure can be used in a heat storage device that needs to fit under a tight space such as a cover of a carrier or under the floor. While the cylindrical shape may be advantageous for reducing the surface area, other relatively elongated, or box-shaped shapes may be advantageous for fit into an accessible space. It will be appreciated that the generally circular surface of the bladder structure can advantageously be replaced with a non-circular shape in accordance with the teachings herein. Thus, the capsular structure can have a top surface and/or a bottom surface that is generally oval, generally rectangular, generally square, generally irregular, or any combination thereof. For example, the top surface and/or the bottom surface of the bladder structure may have a generally rectangular shape including rounded corners. Figure 7 is a diagram showing an exemplary feature configuration of a surface of a capsule structure. As shown in Fig. 7, the contours of the top and bottom surfaces of the bladder structure may have an elongated shape. For example, the (outer peripheral) contour of the top and bottom surfaces may have a generally rectangular shape, a generally square shape, or an oval shape). It will be appreciated that the contour of the opening in the top surface can be any shape. The contour of the opening in the top surface and the contour of the outer perimeter of the top surface may have similar (but differently sized) shapes or may have different shapes such as a generally circular opening and a non-circular outer periphery. As shown in Fig. 7, the contour of the opening and the contour of the outer periphery may have the same shape, such as an oval shape. The article preferably has a bladder structure that is difficult to bend. For example, the capsular structure may be free of cross-sections in which a cover sheet and a substrate sheet are in contact with a major portion of the cross-section 21 201144705 or even the entire length (such as a diameter of the capsular structure). There are a variety of different ways to ensure that the capsule structure is difficult to bend, including a configuration in which the capsule is selected such that the order of rotational symmetry is not even, and a configuration of the pocket is selected so as not to have rotational symmetry, the pocket is selected A configuration comprising a pocket that rotates relative to each other such that each radial segment includes at least one, two or more rings, such as concentric rings, in the enclosed space, or any combination thereof. It will be appreciated that other geometries and other means may be employed to render the bladder member resistant to bending. For example, the material of the bladder structure can be selected to be generally stiff, and the structure can include one or more ribs (e.g., in all line directions), and the like. All of the thermal energy storage material of the article can be located in a single sealed space. Preferably, the thermal energy storage material of the article is distributed between the plurality of sealed spaces, so that if a sealed space is pierced or otherwise leaked, it is removed. Haihe t stores a part of the material. Therefore, the number of sealed spaces in the article (such as the sealed space containing the thermal energy storage material) is preferably at least 2' more preferably at least 3, and even more preferably at least about 5 ^ the upper limit of the number of sealed spaces is an example And for a particular application, it is determined by the needs of the application. However, the number of sealed spaces in an object is generally less than 丨〇〇〇. However, a large article can have 1 or more sealed spaces. The volumetric proportion of the thermal energy storage material found in any single sealed compartment for the same reason is preferably less than about 55°/ of the total volume of thermal energy storage material in the article. More preferably less than about 38%, even more preferably less than about 29%, and most preferably less than about 21%. Generally, a sealed space includes at least 0.1% by volume of the thermal energy storage material. However, it will be understood that the object may include 22 201144705 substantial space does not contain or even completely contains no thermal energy storage material - or a plurality of sealed 0 (10), sealed space optional inspection configuration in the complex number _ called = inner ring (such as ~ most Rings near the periphery of the opening) and - the outermost ring (such as the ring of the most money (four) side) - each containing - or a plurality of sealed spaces: one in the ring, the enclosed room can have - is repeated pattern. For example, each of the rings, the W-enclosed space, or the 2, 3, 4 or more sealed spaces Z of each group have generally the same shape and size. The number of sealed spaces in each ring may be the same or different. Preferably, the outermost ring has a larger average length of the sealed space of the innermost ring than the outermost ring of S, which is smaller than the average length of the left side of the innermost ring (wherein the average length is from the opening to the outer periphery) The volumetric variation between the outermost ring and the most enclosed space is reduced by measuring the direction in the direction, or both. As discussed later, the object can be placed in a cavity having a generally cylindrical cavity, such as a cavity having a slightly larger dimension than the longest dimension of the object. For example, the diameter of the cavity of the H can be only slightly larger than the diameter of the sac structure of the object. The diameter of the cavity should be sufficiently large that the object can be inserted into the cavity. When an object (or a stack of objects) is placed in the container, it may be desirable to have - a flow between the periphery of the article and the inner wall of the container. The relationship between the interior of the container and the shape of the object can be designed to create and maintain a fluid neon such as a Danni. The secret can be used as a means of generating such fluid flow paths. S1 Thus, the object may have a miscellaneous ground along its perimeter - or a plurality of recesses (for example, the cover sheet and the base sheet may have - or a plurality of corresponding recesses along their respective outer perimeters), thereby forming - for Supply - heat transfer 23 201144705 Move " IL body flow two. In addition or in place, the cavity of the container may have a surface comprising one or more grooves for a fluid to flow between the outer periphery of the article and the surface of the container. In another example, the diameter of the article may be sufficiently small relative to the diameter of the interior of the cavity such that a fluid can flow along the entire outer periphery of the article. For example, for each of the outer and outer spaces of the sealed space, the article may have one or more recesses or the container may have more than one groove. A recess or a groove can have any shape, such as a polygonal shape, an arch shape, a wedge shape, and the like, with the proviso that it has a sufficient size to allow heat transfer fluid to flow. If employed, the minimum dimension of the recess and/or groove is typically at least about a combination of two or more means for generating a fluid flow path. For example, the article may have - or more recesses along its outer periphery, and the article may have a sufficiently small diameter so that fluid can flow along its entire outer periphery when placed in the cavity. "丨丞低月1Optionally has ~ ΙΊ·············································································· It can be used as a separate point to separate the surfaces of the butt joints, so - fluids (such as heat transfer fluids) move between the butted surfaces. The accumulation of objects and Wei partitions: Discussion. If so, the projections preferably cover only the surface and the base-small portion, so that the filaments dry the fluid stream. The height of the selected protrusion is determined by the flow path between the two (four) joints (such as the average height). The cover sheet is difficult to contain without such protrusions and has a flat; flat outer surface, so two (four) I disambiguate (four) to summarize in its: 24 201144705 top surface is in contact. Thermal energy storage materials Non-mantle m(4) Appropriate thermal energy storage materials for thermal storage devices 2=Energy _• Lai, latent heat, and sister sensation - relatively high (4). Heat_存(四)·_The operation of the measuring device is the degree (4) phase*. For example, the 'thermal energy storage material is preferably a solid at the lower operating temperature of the heat storage device, and at least partially - liquid (eg, completely _ liquid) at the most operating temperature of the heat storage device, The maximum operating temperature of the device does not significantly degrade or decompose or any of its rainbows. The reduced storage (4) preferably does not significantly deteriorate or decompose when heated to a maximum operating temperature of the device (4) for about _hour or longer, or even about 1_0 or longer. The thermal energy storage material can be a phase change material having a solid to liquid transition temperature. The solid to liquid transition temperature of the thermal energy storage material can be a liquidus temperature'-melting temperature, or a eutectic temperature. The solid to liquid switching temperature should be sufficiently high so that when the thermal energy storage material is at least partially or even substantially completely in a liquid state, sufficient energy is stored to heat one or more heated objects to a desired temperature. The solid to liquid transition temperature should be sufficiently low that the heat transfer fluid, one or more heated objects, or both are not heated to a temperature that may degrade them. Therefore, the desired temperature of the solid to liquid transition temperature may depend on the heated object and the method of transferring heat. For example, in an application where an ethylene glycol/water heat transfer fluid transfers stored heat to an engine, such as an internal combustion engine, the maximum solids to liquid transition temperature may be the temperature at which the heat transfer fluid degrades. In addition, in Example 25, 201144705, the stored heat can be transferred to an electrochemical cell of a battery using a heat transfer fluid, wherein the heat transfer fluid has a high degradation temperature, and the maximum solid to liquid temperature may depend on the electrochemical The battery cell deteriorates or produces other failure temperatures. The solid to liquid transition temperature can be greater than about 3 Torr. Preferably, it is greater than about hunger, more preferably greater than about the machine, and even more preferably greater than about the shirt C' and preferably greater than about the pit. The thermal energy storage material can have a volume of less than about 】, about 350 c, more preferably less than about 29 () £ (:, even better than less than 250 C, and optimally less than about 2 〇 (1 of rc) To the liquid conversion temperature. ', the solution depends on the application, the solid to liquid conversion temperature can be from about thief " 彳 < about 5GCS ^ 15 () ° c ' from about 100 ° C to about 200 ° C, % \ 〇C to about 25 〇C 'from about 175 ° C to about 400 ° C, from about 200 ° C to C from about 225 C to about 100 ° (:, or from about 2 〇 (rc to about 3 〇 (Γ (:. The heart is ten. ^ Knife applications, such as transportation-related applications, may want to make the energy storage material efficiently store energy in the second room. Therefore, the thermal energy storage table _: ° has a high heat density (in millions of joules per liter of unit 25V, 'I [, expressed by melting heat 4 (in millions, ears per kilogram) and density (defined in the product of kilograms per liter of unit table). Thermal energy The storage enthalpy has a fusion heat density greater than about 〇1 Mj/liter, preferably greater than about 〇2 mj/liter, more preferably - 妒 TM TM J / liter, and preferably greater than about 〇·_ liter. 'Thermal energy storage material has less than about Xiaosheng's fusion heat-density material;; but also can use thermal energy storage material with higher heat density to store = two applications, such as transportation-related applications, may want to make the thermal energy material 轻 light weight. For example, domain storage materials can A lower limit of the density of β (density measured in pits) having a density of less than about 26 201144705 5 g/cm 3 , preferably less than about 4 g/cm 3 , more preferably less than about 3 (four) coffee 3, and preferably less than about 3 g/cm 3 is an example. The material may have a density greater than about 6 g/cm3, preferably greater than about 1.2 g/cm3, and more preferably greater than about Ug/cm3 (measured at about 25). The sealed space may contain any conventional thermal energy storage material. Examples of thermal energy storage materials that can be used in thermal energy storage material compartments include Atul Sharma, VV Tyagi, CR Chen, and D.

Buddhi)的“相變材料的熱能儲存及應用評論”,再生及永續 能源評論13(2009) 318-345中,以及撒巴(Belen Zaiba)、馬 潤(Jose Ma Marin)、卡貝薩(Luisa F. Cabeza)、梅林(Harald Mehling)的“相變的熱能儲存:材料、熱量轉移分析及應用 之評論”,應用熱工程23 (2003) 251-283中所描述的材料, 兩文件整體合併於本文中以供參考。熱量轉移裝置中可採 用之適當熱能儲存材料的其他範例係包括在名稱為“熱能 儲存材料”且於2009年2月20曰提申的美國專利申請案No 12/389,416 ;及名稱為“熱量儲存裝置”且於2〇〇9年2月2〇日 提申的美國專利申請案No. 12/389,598中所描述之熱能儲 存材料。 熱能儲存材料可包括一有機材料,一無機材料或一有 機與一無機材料的一混合物,其展現前述的固體至液體轉 換溫度、熔合熱量密度、或兩者。可採用的有機化合物係 包括石蠟及非石蠟性有機材料,諸如脂肪酸。可採用的無 機材料係包括鹽水合物及金屬物質。熱能儲存材料可為一 概括在單一溫度具有一固體至液體轉換之混合物(譬如共 27 201144705 晶混合物)或一化合物。熱能儲存材料可為具有位於一溫度 範圍(譬如,大於約3°C、或大於約5°C的一範圍)的一固體至 液體轉換之一化合物或一混合物。 非限制性地,作為熱能儲存材料之適當的非石蠟性有 機材料係包括酸,醇,醛,醯胺,有機鹽,其混合物及其 組合。範例中,可單獨使用或作為一混合物之非石蠟性有 機材料係包括聚乙二醇,癸酸,反油酸,月桂酸,十五烷 酸,三硬脂酸甘油酯,肉豆蔻酸,軟脂酸,硬脂酸,乙醯 胺,富馬酸二曱酯,甲酸,辛酸,甘油,D-乳酸,棕櫚酸 曱酯,莰尼酮,溴二十二烷,十五烷酮,酚,十七烷酮, 1-環己基十八烷,4-十七烷酮,對-曱苯胺,氰胺,花生酸 曱醋,3-十七烧酮,2-十七烧酮,氫桂皮,録堪醇,萘胺, 莰烯,鄰-硝基苯胺,9-十七烷酮,麝香草酚,山蝓酸甲酯·, 二苯胺,對二氣苯,草酸鹽,連二磷苯,鄰二氯二甲苯, 氣乙酸,硝基萘,三肉豆蔻酸甘油S旨,十七酸,蜂堪,甘 醇酸,乙醇酸,對溴酚,偶氮苯,丙烯酸,二硝基甲苯, 苯乙酸,烯丙基硫脲,溴代樟腦,四曱苯,苯甲胺,溴苯 甲酸曱酯,α-萘酚,戊二酸,對二氣二甲苯,鄰苯二酚, 苯醌,乙醯苯胺,琥珀酸酐,苯甲酸,葸,苯曱醯胺,或 其任何組合。 非限制性地,熱能儲存材料可包括選自下列各物組成 的群組之一或多個無機鹽:硝酸鹽,亞硝酸鹽,溴化物, 氣化物,其他_化物,硫酸鹽,亞硫酸鹽,磷酸鹽,亞磷 酸鹽,氫氧化物,羰基化合物,溴酸鹽,其混合物,及其 28 201144705 組合。範例中,熱能儲存材料可包括下列物質或實質由其 組成:Κ2ΗΡ04·6Η20,FeBr3.6H20,Μη(Ν03)2·6Η20, FeBr3 6H20,CaCl212H20,LiN03.2H20,LiN03.3H20, Na2CO310H2O,Na2SO410H2〇,KFe(S03)2.12H20, CaBr2.6H20,LiBr2.2H20,Zn(N03)2.6H20,FeCl3.6H20, Mn(N03)2.4H20,Na2HP04.12H20,CoS04.7H20,KF.2H20, MgI2.8H20,CaI2.6H20,Κ2ΗΡ04·7Η20,Ζη(Ν03)2·4Η20, Mg(N03).4H20 ,Ca(N03).4H20 ,Fe(N03)2.9H20 , Na2Si03-4H20,Κ2ΗΡ04·3Η20,Na2S203.5H20,MgS04.7H20, Ca(N03).3H20,Ζη(Ν03)2·2Η20,FeCl3.2H20,Ni(N03)2.6H20, MnCl2_4H20,MgCl2.4H20,CH3C00Na.3H20,Fe(N03)2.6H20, NaAl(SO4).10H2O ,NaOHH20 ,Na3P0412H20 , LiCH3C00-2H20,Α1(Ν03)2·9Η20 , Ba(0H)2-8H20, Mg(N03)2,6H20,KAl(S〇4)2.12H20,MgCl2.6H20,或其任何組 合。將瞭解可使用具有較高或較低濃度的水之無機鹽。 熱能儲存材料可包括下列物質(或可甚至實質由其組 成或由其組成):至少一第一金屬包含材料,及更佳至少一 第一金屬包含材料及至少一第二金屬包含材料的一組合。 第一金屬包含材料、第二金屬包含材料、或兩者係可為一 實質純金屬,一合金、諸如包括一實質純金屬及一或多個 額外合金化成份(譬如,一或多個其他金屬)之合金,一金屬 間物質,一金屬化合物(譬如,一鹽,一氧化物或其他),或 其任何組合。一較佳途徑係採用一或多個金屬包含材料作 為一金屬化合物的部份;一更佳途徑係採用至少二金屬化 29 201144705 合物的-混合物。範例中,—適當金屬化合物可選自:氧 化物,氫氧化物,包括氮及氧的化合物(譬如,硝酸鹽,亞 石肖酸鹽或兩者),i化物,或其任何組合。可能亦可採用三 (ternary),四(quat⑽ry)或其他多重組份材料系統。此處的 熱能儲存材料可能是二或更多種展現—共晶之材料的混合 物。 物件的一或多個經密封空間中之熱能儲存材料的體積 係充份夠高以使物件可儲存大量熱能^物件中所含的熱能 儲存材料體積對於-或多個經密封空_總體積之比值、 熱能儲存材料的體積對於物件總體積之比值、或兩者(在約 饥溫度、或在熱_存㈣㈣賴之溫度賴量的體 積)較佳大於約0.5,更佳大於約〇·7,且最佳大於約〇 9。物 件中所含的熱能儲存材料體積對於—或多個經密封空間的 總體積之_、熱能儲存材料的體積對於物件總體積之比 0.995。 值或兩者(在約25。(:溫度、或在熱能鍺存材料身為液體之 溫度所測量的體積)一般係小於約i 〇,且更一般小於約 經密封空間可包括一含有一諸如空氣、N2等氣體或諸 如He、Αι*及類似物等惰性氣體之體積,故使熱能儲存材料 可在受熱時擴張。譬如,經密封空間可具有-在約25°c溫 度不含熱_存材料之區,故將熱能料材料加熱至其液 相線溫度以上時’熱能儲存材料可擴張而不在覆蓋片或基 底片中形成孔或造成—或多個片脫層。處於饥之一不含 熱能儲存材料的經密封空間的體積(譬如,含有—氣體之經 30 201144705 密封空間的體積)係可能佔經密封空間的總内部體積之至 少約0.5%,較佳至少約1%,且最佳至少約1.5%。 第2A圖是顯示一物件10的特徵構造之圖式,其包括一 具有單一經密封空間(亦即單一囊袋)之囊狀結構。囊狀結構 包括一具有一開口29之覆蓋片28及一具有一開口31之基底 片30。覆蓋片的開口29及基底片的開口31係彼此重疊(譬如 完全地重疊)並因此身為對應之開口。覆蓋片28及基底片係 密封性附接至一外環32。如圖所示,覆蓋片28的外周邊、 基底片的外周邊、或較佳兩者係可密封性附接至外環32。 覆蓋片係具有一頂表面18,其身為物件10的一外部表面, 及一相對的表面,其概括位於物件10的内部上。基底片係 具有一底表面20,其概括是物件10的一外部表面,及一相 對的表面,其概括位於物件的内部上。囊狀結構亦可具有 一内環34,其係密封性附接至覆蓋片28的一開口周邊、基 底片3 0的一開口周邊或較佳附接至兩者。如圖所示,外環 32可具有一概呈圓柱形外表面及一概呈圓柱形内表面,内 環34可具有一概呈圓柱形外表面及一概呈圓柱形内表面, 覆蓋片28(譬如覆蓋片的頂表面18)可具有一概呈圓形形 狀,基底片30(譬如,基底片的底表面)可具有一概呈圓形周 緣,或其任何組合。下列開口的任何組合之一者係可具有 一概呈圓柱形形狀:物件16的流體通道,覆蓋片29的開口, 基底片31的開口。將瞭解一開口的一橫剖面可具有一不同 形狀,諸如一多角形,或一不同的拱形形狀(譬如一卵形)。 如第2A圖所示,物件10可具有概呈拱形、概呈非平面 31 201144705 性、及概呈連續性之單一側表面22。此側表面可與物件中 心概呈等距,故物件可被放置在一具有一概呈圓柱形腔體 之容器中,該概呈圓柱形腔體具有只略微大於物件平均直 徑之一腔體直徑。 第2B圖中顯示使用於物件中之一具有一開口29的示範 性覆蓋片28。將瞭解可在覆蓋片附接(譬如密封性附接)至一 或多個其他片或者一或多個其他次結構之前 '同時、或之 後,形成覆蓋片中的開口。覆蓋片可具有一概呈圓形的外 周邊19,一概呈圓形的内或或開口周邊21,或兩者。覆蓋 片28可具有一概呈扁平的底表面38及一概呈扁平之相對的 頂表面18。覆蓋片28可由-或多個包封劑材料12形成。如 第2B圖所不’覆蓋片28的外周邊19可包括覆蓋片28的底表 面38上之一區23,接近於覆蓋片的外周界。參照第2八及26 圖,基底片28可沿著底表面38上的外周邊19之區23被密封 眭附接。用於頂表面18之包封劑材料較佳係為當接觸於熱 里轉移流體時可抵抗腐蝕之材料。用於底表面38之包封劑 材料較佳係為當接觸於熱能儲存材料時可抵抗腐蝕之材 料。用於頂表面18及底表面38之包封劑材料可為相同材料 或不同材料。開口 29除外之頂表面18可具有一概呈圓形形 狀。利用覆蓋片的頂表面18與底表面38之間距離所測量之 覆蓋片28的厚度係可概呈均勻狀。覆蓋片28厚度的標準差 係較佳小於覆蓋片平均厚度之約15%,更佳小於約1〇%,且 最佳小於約3%。 第2C圖顯示垂直於覆蓋片28的頂表面18所取之第2八 32 201144705 圖的物件10之—橫剖面。如第2C圖所示,物件可具有一或 夕個包括熱能儲存材料26之經密封空間14。經密封空間可 包括-未充填_27 ’亦即_體積含有—氣體4充填容 積27可谷許熱能儲存材料在其受熱時—諸如當熱能儲存材 料溫度增高時、當熱能儲存材料經歷-H相至液相轉換 時、或兩者時〜擴張。覆蓋片、基底片、外環、内環、或 二任何組合較佳係、包括:—或多個當接觸於熱能儲存材料 (譬如在-内部表面上)時可抵抗腐蚀之包封劑材料,一或多 個當被-熱量轉移流體(#如在—外部表面上)所接觸時可 抵抗腐li之包封劑材料,或兩者。覆蓋片、基底片、外環、 内%或其任何㈤合最佳係包括相同的_或多個包封劑材 料,或實為π整由其組成。覆蓋片28及基底片3〇皆沿其外 周邊19及㈣α周邊2丨被密封性附接以職固經 封空間14。 ' 杜叩珉的片4〇,其可作為供物件用之一 基底片。細彡成的卩可被雜或另外軸使其概呈拱形及/ 或-有複數個壁。經形成的片具有—能夠固持或圍堵 體之槽區43。經形成的片亦具有-開口 46,故-流體可流 過經形成的。_成的驗佳亦具有可獅接至—概^ 扁平覆蓋片(諸如第2B圖所描述的-覆蓋片)之-或多個概 呈扁平區’諸如—或多個唇區44。一或多個唇 共面性。經报屮u " 1主马 H成的片40並非概£扁平㈣。譬如 的片40可具有—庇 厶形成 _蓳,其包括一頂表面41及一概呈相 底表面42。經形士认μ 對的 /成的片可具有一從底壁延伸之侧壁。側辟 33 201144705 可包括一概括拱形的側表面49。經形成的片40可具有一從 底壁的一内部周邊延伸之開口壁。開口壁可具有一概呈拱 形且部份或完全地界定經過物件的流體通道之開口表面 48。經形成的片具有一外周邊45及一開口周邊47。外周邊 45、開口周邊47、或較佳兩者係為唇區44。將瞭解經形成 的片可包括一連接底壁及側壁之轉換區,或者底壁及側壁 可合併成一拱形壁。將瞭解經形成的片可包括一連接底壁 及開口壁之轉折區,或者底壁及開口壁可合併成一拱形壁。 如前述,囊狀結構可包括複數個分段,其配置為形成 具有一或多個經密封空間及一或多個流體通道之囊狀結 構。第3A、3B、4圖是囊狀結構的相鄰分段之示範性側視 圖。如第3A、3B、4圖所示,相鄰分段可具有對接邊緣9(亦 即,概括對接之邊緣表面)。諸如第3A及3B圖的分段2’、2” 所示,其中兩分段的表面4’及6’概呈共面,當相鄰分段配置 於一共面定向中時,分段可對接。當兩相鄰分段被移位時 相鄰分段的邊緣可對接,故其頂及底表面4’及6’未共面。譬 如,一分段可移位達分段2’”厚度的一半,如第4圖所示。 因此,一第一分段的對接邊緣9可對接於皆與第一分段相鄰 之兩經堆積分段之邊緣的部分。如第4圖所示,分段的一堆 積體可包括一或多個(譬如二個)比例性分段3,諸如一具有 其他分段2 ’ ” 一半高度之比例性分段。 將瞭解經成形的片40’之部分或全部的槽可部份地或 實質完全地充填有一熱能儲存材料,且一概呈扁平的覆蓋 片(諸如第2B圖所述)可被放置在槽上方使得覆蓋片概括地 34 201144705 接觸唇區。覆蓋片可在部分或甚至全部唇區中被密封性附 接至經形成的片,以形成複數個含有熱能儲存材料之經密 封空間。如第5A及5B圖所示,經形成的片4〇,可具有槽.的— 圖案,使得一第一經形成的片40,之底表面41,概括是一相同 第二經形成的片40’的一底表面41,之—對接表面。因此,利 用經形成的片40,製成之兩物件係能夠以其底表面4ι,彼此 相對而被堆積,故使兩物件將至少部份地嵌套。 第5B圖是-具有複數個經密封空間的物件中所可採 之-經形成的片40’之-部分(譬如_基底片)的示意圖二 形成的片係在接近片中心處具有—開〇46,其可能是 呈圓形開口。第5B圖只顯示經形成的片之1/4,且因此概 示開口。第5B圖顯示經形成的片4〇,之底表二 形成的片具有複數個槽區43,及複數個唇區料,。槽區4鉍 配置於槽50的複數個環中。如圖所示,經形成的=3,可 ^),的-最内環及槽5G”的—最外環。經形成的^ 有槽50”,的-或多個額外環,位於槽5〇,、5 了具 環之間。如第测所示,—環中之部分或全部糾= :嶋、或甚至實質為全等。將瞭解槽的:::中:: 可大於丨於或等於槽的最外環中之槽數 形成的片价之最内環中的槽數係小於最外環中的槽數if 第5B圖所示。部分、或較佳全部的槽區43,ι有 ° 周圍之魯區44,。因此,一槽區43,可藉由—辱區4= 他槽區分離。經形成的片4〇 . 1亡ύ,m '、其 片具有-外周邊45,。如第5B圖 35 201144705 所示,經形成的片可在接近外周邊45’處具有一或多個凹缺 51。一或多個凹缺可使用於沿著外周邊之流通路或流徑。 較佳地,經形成的片之底表面的外周界具有一概呈圓形形 狀(選用的一或多個凹缺係排除在外)。如第5B圖所示,外 周邊、内周邊、及較佳兩者係可為唇區44 ’。 第5A圖顯示一囊狀結構10’(譬如,一囊狀結構的一經 形成的片40’)及一容器68之間的一示範性關係。容器68可具 有一内壁60,一外壁62,一絕緣層64,或其任何組合。參 照第5A圖,容器68可具有一介於兩壁60、62之間的絕緣層 64。容器的内壁60具有比經形成的片直徑更大之一直徑使 得經形成的片可配合於容器内。片的周邊與容器的内側壁 之間的一流徑係可包括:經形成的片40’中之一或多個凹缺 51,由經形成的片40’及容器的腔體之尺寸(譬如直徑)差異 所形成的一間隙52,容器的一内側壁60中之一或多個溝槽 5 3,或其任何組合。 含有熱能儲存材料之物件較佳能夠與其他相同的物件 或與一具有一概括對接表面(諸如一概括對接基底片)之第 二物件作堆積。物件係堆積於軸向層中而在相鄰軸向層之 間具有一空間,使得一熱量轉移流體可流動於軸向層之 間。一軸向層將概括含有一、二或更多個物件。一軸向層(譬 如,各軸向層)較佳含有一或二個物件。譬如,一軸向層可 具有兩個物件,該等兩物件係在諸如一基底表面或一覆蓋 表面等一表面上處於接觸,故一流體概括無法流動於兩物 件之間)。因此,部分物件(譬如,位於一堆積體一端的物件 36 201144705 除外之各物件)可具有一第一表面(譬如,一基底表面),其 概括完全地接觸於一第一相鄰物件的一表面使得一流體無 法沿著第一表面流動,及一第二表面,其與一第二相鄰物 件分離(譬如,具有一概括身為與第二表面的一對接表面之 相對表面)使得一流體可沿著第二表面的部分、大部份或甚 至全部流動。兩相鄰軸向層之間的分離可藉由任何技藝習 知的分隔部件予以達成。範例中,適當的分隔部件係包括 位於物件至少一者的一表面上之一或多個突件,兩層之間 的一分隔件材料,兩層之間的一毛細管結構,或其任何組 合。較佳地,物件的第二表面具有一概呈拱形形狀,且物 件部份地嵌套於第二相鄰物件。部份地嵌套的兩物件之間 的分隔較佳係概呈恆定(造成相鄰物件被分離之突件或其 他分隔件除外)。將瞭解,物件的堆積係可包括一旋轉一軸 向層(譬如旋轉一物件)、或另外將其配置成使軸向層至少部 份地嵌套於一相鄰軸向層之步驟。兩相鄰軸向層的兩相對 表面之間的一流體的流動將概括位於一徑向方向中並可被 描述成一概呈徑向流。被分開之各對的軸向層將具有一徑 向流徑。物件的堆積體一般將具有複數個徑向流徑(譬如, 2、3或更多個)。二或更多個(譬如各徑向流徑可具有相同流 長度,相同厚度,相同橫剖面形狀,或其任何組合。譬如, 二或更多個(譬如全部的)徑向流徑可為全等。將瞭解,若開 口(亦即流體通道)位於物件中心,則徑向流徑可概括對稱, 而與流方向無關。 當被堆積(亦即位於一含有3、4或更多個物件之堆積體 37 201144705 中)時,物件較佳各具有至少-開口,其對應於來自各其他 物件(位於堆積體一端之一物件可能除外)的一開口故一流 體的-部分可藉由流過介於第-與最後物件之間物件的各 對應開口且不流動於相鄰物件之間(亦即不具有概呈徑向 流)而從堆積體中的-第-物件流至堆積體中的—最後物 件。經過開口之流係概括位於_軸向方向並可被描述成一 概呈轴向流。 如上述’物件的堆積體可界定一中央軸向流徑(譬如, 經過物件的開口所形成之中央軸線)及—或多個概括垂直 於中央軸向流徑之徑向流徑。 物件的堆積體將概括被緊密地裝填(譬如,徑向流徑除 外),故使物件的堆積體密實且含有大量熱能儲存材料。因 此’徑向流徑具有-概括短小的高度(在相鄰物件之間的方 向中)’譬如一平均高度。徑向流經的高度較佳小於約 15mm ’更佳小於約5_ ’甚至更佳小於約2_,甚至更佳 小於約^,且最佳小於約〇.5_。徑向流徑的高度係夠 大使得流體可流過該流徑。一般而言,徑向流徑的高度(譬 如平均高度)大於約0.001mm(譬如,大於約〇 〇1_)。= 第5 C圖顯示包括複數個物件! 〇,之本發明的一態樣,各 物件10’具有-或多個於容納_熱能儲存材料之經密封 空間14 ’物件10’可包括一具有一概呈棋形表面41”之經形 成的片4〇”。一物件的表面41 ”可概括對接於一第二物件的 表面。物件可配置成使相鄰物件部份地嵌套在一起。第5c 圖所示的物件具有8階的旋轉對稱性並因此可在8個不同位 38 201144705 置中:轉使其料份地絲。將瞭解可採隸有較高或較 氏=稱性之物件。如第所示,物件可具有—概呈圓 形松剖面。各物件的外周邊可具有複數侧大容許—流體 抓之凹缺51⑯件lQ,可具有配置於經密封空間的—或多個 同衣中之匕密封空間14。各物件1〇,可具有一概括接近於 物件中。之體通道46,,故當物件被堆積(譬如堆積於—轴 向方向中)時將形成車由向流徑84,。軸向流徑料,較佳包括各 物件10’的一流體通道46,。 熱量儲存裝置 此處所描述的物件(譬如物件的一堆積體)可被使用於 一熱量儲存裝置中。該熱量儲存裝置係可包括一容器或其 他殼體,其具有一或多個供一熱量轉移流體流入容器中之 孔口及一或多個供—熱量轉移流體流出容器外之孔口。熱 量儲存裝置具有一或多個熱量轉移流體隔室。較佳地,熱 量儲存裝置包括單一熱量轉移流體隔室。一熱量轉移流體 隔室係可包括入口與出口之間的容器中之一鄰接空間或實 質由其組成,其中可供熱量轉移流體流動。容器較佳至少 部份地絕緣,故可降低或盡量減少從容器至環室之熱量損 失。 熱量儲存裝置可設計成使其含有大濃度的熱能儲存材 料,使其可快速及/或均勻地轉移熱能於一熱量轉移流體與 熱能儲存材料之間,使其概呈密實,使其可長期儲存熱量, 或其任何組合。 熱量儲存裝置的容器之内側可具有任何能夠固持物件 39 201144705 的一堆積體之形狀1佳地 件的堆積體佔用容器的 内側之形狀係使得物 的經密封空間中所含之熱能錯存 容 25t測量)對於容评材科的總體積(譬如在約 值二 /l . λ.A 吏佳大於約〇·6 ’其$争 佳大於約0.7’且最佳大於約〇 8。容器 H^ μ BP ^ * ° …此儲存材料的 體積之上限係為:-接觸於物件的熱量轉移流體對於*門 之 之需求’以供轉移熱能。容器中物件的經密封空間中所含 熱此儲存材料的總體積(譬如在約25 °c測量)對於& 總内部體積(譬如在約2 5 °C測量)之比值可小於約〇 9 9谷益的 小於約0.95 » •,較佳 熱量轉移流體隔室/流徑 熱量儲存裝置具有一用於使一流動之熱量轉移流體3 室’其能夠在一熱量轉移流體流通經過裝置時; ▽ 丁从圍堵。 熱量轉移流體隔室較佳連接至一或多個用於使一熱量轉 流入熱量轉移流體隔室中之孔口(譬如,一或多個 )。 量轉移流體隔室較佳連接至一或多個用於使—叙息 *''' 里詞L移、’古 出熱量轉移流體隔室外之孔口(譬如,一或多個 抓 码D )。熱詈 轉移流體隔室可為至少部份地由一或多個熱量轉 “、' T今夕丨L體隔 至壁所界定之一空間,至少部份地由—或多個物件 之一空間’至少部份地由熱量儲存裝置的—砷 疋 — 趙或容器所 界定之一空間,或其任何組合。 熱量轉移流體隔室係界定經過熱量儲存裝置之〜 轉移流體的流徑。熱量轉移流體隔室係包括—熱里 成過物件的 40 201144705 堆積體的開口之概呈軸向流徑。熱量轉移流體隔室係包括 一位於兩相鄰物件之間的概呈徑向流徑。將瞭解徑向流可 為從一外周邊至一物件的開口之一往内流,或從一開口至 一物件的外周邊之一往外流。熱量轉移流體隔室包括一流 徑,其具有物件的一外周邊及容器的一壁之間的一概呈軸 向組件(及選用性地,一切線組件)。較佳地,經合併徑向流 徑具有一相對較高的液壓阻抗。譬如,經合併的徑向流徑 具有大於(更佳地,更大至少兩倍)中央轴向流徑、外軸向流 徑、或兩者的液壓阻抗之一液壓阻抗。 熱量轉移流體隔室較佳充分地熱性導通於含有熱能儲 存材料之經密封空間,故其可自熱能儲存材料移除熱量或 提供熱量至熱能儲存材料。熱量轉移流體隔室較佳直接地 熱性導通於一或多個(或更佳全部)經密封空間。一直接熱性 導通係可為一經密封空間與熱量轉移流體隔室的一部分之 間的最短距離之任何路徑,其不含具有低熱傳導率的材 料。低熱傳導率材料係包括具有小於約100W/(nvK)、較佳 小於約10W/(m_K)、且更佳小於約3 W/(nrK)的熱傳導率之材 料。譬如,熱量轉移流體或熱量轉移流體隔室係可接觸經 密封的一或多者(或較佳為全部)之一壁,或者藉由具有高熱 傳導率(譬如大於約5W/(m_K)、大於約12W/(nvK)、或大於 約110W/(nvK)的材料而實質或完全地與經密封空間分離。 熱量轉移流體隔室較佳直接熱性導通於熱量儲存裝置 中之經密封空間的一或多者(或更佳為全部)。一直接熱性導 通可為一熱能儲存隔室及熱量轉移流體隔室的一部分之間 41 201144705 的最短距離之任何路徑,其不含具有低熱傳導率之材料。 譬如,熱4_流體或熱量轉移㈣隔㈣可接觸經密封 工間(諸如基底片或-覆蓋片)的—或多者(或較佳為全部) 之一壁,或藉由具有高熱傳導率(譬如大於約5W/(m.K)、大 於約12W/(m.K)、或大於約i i〇w/(m.K)的材料而實質地或完 全地與經密封空間分離。將瞭解_具有低熱傳導率的材料 之-很薄層(譬如小於約0 lmm,較佳小於約〇 〇1臟,且更 佳小於約G.GGlmm)可位於熱量轉移流體隔室與—熱能储存 材料隔室之間而並未可察覺地影響熱量轉移。 可選擇經密封空間及/或物件的尺寸及形狀以盡量加 大前往及來自囊袋中所含的相變材料之熱量轉移。物件的 平均厚度可能相對較短使得熱量可快速地從經密封空間中 心逃逸。物件、經密封空間、或兩者的平均厚度可小於約 100mm,較佳小於約30mm,更佳小於約1〇mm,甚至更佳 小於約5mm,且最佳小於約3mm。物件、經密封空間、或 兩者的平均厚度可大於約〇.lmm,較佳大於約〇.5mm,更佳 大於約0.8mm ’且最佳大於i.Omm。 物件較佳具有一相對較高的表面積對於體積比值,故 與熱量轉移流體具有相對較高的接觸面積。譬如,物件可 具有一與一熱量轉移流體隔室盡量加大接觸之表面,物件 可具有一盡量加大囊袋與熱量轉移流體隔室之間的熱量轉 移之幾何結構,或兩者。熱量轉移流體隔室及熱量儲存裝 置中的物件之間的介面總表面積對於熱量儲存裝置中之熱 能儲存材料的總體積之比值係可大於約〇〇2111111-1,較佳大 42 201144705 於約0.05mm_1,更佳大於約0.1mm_1,甚至更佳大於約 0.2mm-1,且最佳大於約0.3mm·1。 容器/殼體 熱量儲存裝置具有一用於包含物件的堆積體之容器。 物件的堆積體可被包含在容器的一或多個腔體中。適當容 器具有一或多個用於使一熱量轉移流體流入容器的腔體中 之孔口(譬如一或多個入口)以及一或多個用於使一熱量轉 移流體流出容器的腔體外之孔口(譬如一或多個出口)。入口 及出口可位於熱量儲存裝置的相同側上或不同側(譬如相 對側)上。除了孔口外,容器較佳被密封或建構成使得一流 過容器的流體不會漏出容器外,故一流過容器之流體可具 有大於環室壓力之一壓力,或兩者皆然。 容器可具有任何形狀。較佳地,容器具有一可在中(譬 如在物件的堆積體之經密封空間中)充填有大量熱能儲存 材料之形狀,使得熱量儲存裝置可儲存大量熱量。非限制 性地,容器及/或容器的腔體可具有一概呈圓形、概呈卵 形、概呈矩形、概呈正方形的橫剖面(譬如,垂直於堆積方 向),或具有一不同的概呈多角形形狀。一特佳實施例中, 容器具有一概呈圓柱形形狀,容器的腔體具有一概呈圓柱 形形狀,或兩者。譬如,熱量儲存裝置的容器可具有一概 呈圓柱形内表面,一概呈圓柱形外表面,或兩者。一圓柱 形腔體可容許腔體中具有一概呈圓柱形橫剖面的物件之高 效率裝填。範例中,一概呈圓柱形物件具有一概呈圓形橫 剖面。一圓柱形物件、一圓柱形腔體、或兩者係可容許熱 43 201144705 量儲存裝置之高效率絕緣。一般而言,容器的特徵可能係 在於物件堆積方向(亦即軸向方向)中之一高度以及垂直於 堆積方向的方向中之一平均長度(譬如一直徑)。譬如,一圓 柱形容器的特徵可能係在於一高度及一直徑。容器的高度 對於長度(譬如直徑)比值可小於約20,較佳小於約5,更佳 小於約3,且最佳小於約2。容器的高度對於長度比值(譬如 高度對於直徑比值)可能大於約〇·〇5,較佳大於約〇 2,更佳 大於約0.33,甚至更佳大於約〇.5,且最佳大於約容器 的腔體之特徵可能係在於物件的堆積方向中之一高度及垂 直於堆積方向之方向中的一平均長度(譬如一直徑)。最佳 地,容器的内部具有一概呈圓柱形腔體,其特徵在於一腔 體直,-腔體高度,及一軸向中心。容器的内部可具有 一平行於腔體的軸向方向之概呈拱形壁(具有一棋形表 如前文討論’拱形表面較佳具有—概呈圓形橫剖面。 容器可用來容置物件的-堆積體。物件的堆積體較佳配置 成在容器的腔體之轴向中心或附近具有—中央轴向流徑 (譬如,經過複數個腔體的流體通道物件的外周邊可包括 一或多個凹缺,容器的内部壁 於-軸W…一 I、有一或多個溝槽(較佳位 具有—軸向組件的方向中),物件可JL 故使於^長度或直役之-長度或直徑、或其任何組合, 邊在一軸向方向中流動於物件的外周 ί:内部軸向表面之間。此流可被描述成—外軸向 積體較佳配置於容器中,使得物件的外周邊 “的棋形内部表面之間的距離對於一物件的不同區並 44 201144705 ;不同物j牛概呈均勻狀(物件中的任何凹#《容器壁中 的溝槽除外)。 ^量儲存裝置可使用在需要長時間儲存熱量、在—概 括(譬如"'具有小於約〇°c、或甚至小於約_3(rc溫度 的衣中儲存熱量、或兩者皆然之應用卜較佳地,儲存 於,量儲存I置中之熱量係緩慢地喪失至環境。因此,本 較佳使用某形式的絕緣。系統的絕緣愈好,則儲 時間愈長。 可心用使熱量儲存裝置的熱損失速率減緩之任何習知 $式的絕緣。譬如,可採用如整體被合併於本文中以供參 考之美國專利案N。. 6,889,751中所揭露的任何絕緣。熱量 储存袈置較麵為經(熱性)_的容器,使其在—或多個表 面上呈絕緣。較佳地,曝露於環室或外部之部分或全部表 將’、有-鄰接絕緣體。絕緣材料可藉由降低對流熱量損 人A降低||射熱置損失、降低傳導熱量損失、或其任何組 來運作。較佳地,絕緣可透過利用一較佳具有相對較低 熱傳導之絕緣體材料或結構。可利用相對分隔的壁之間的 間隙來獲得絕緣。間隙可被—氣體媒體 、諸如一空氣空 門所佔用’或可能甚至可身為—排空空間(譬如利用一杜瓦 奋器(Oewar vessel))、一具有低熱傳導率之材料或結構、一 -有低熱發射率之材料或結構、一具有低對流的材料或結 構或其任何組合。非限制性地,絕緣可含有陶瓷絕緣(諸 如石英或玻璃絕緣)’聚合性絕緣,或其任何組合。絕緣可 為-纖維性形式…泡綿形式,—密化層,一塗覆物或其 45 201144705 任何組合。絕緣可為一織造材料、一針織材料、一非織造 材料、或其一組合的形式。熱量轉移裝置可利用一杜瓦容 器(Dewar vessel)、且更特別是—包括概呈相對壁之容器被 絕緣,其組構為界定有一内部儲存腔體、及相對壁之間的 —壁腔體,壁腔體被排空至大氣壓力以下。壁可進—步利 用一反射性表面塗覆物(譬如—面鏡表面)來盡量減小輻射 熱量損失。 較佳地,提供熱量儲存裝置及或熱量儲存系統周圍之 一真空絕緣。更佳地,提供如同整體合併於本文中以供參 考的美國專利案No. 6,889,751所揭露之一真空絕緣。 密實化部件 熱量儲存裝置可選用性地包括對於物件的一堆積體之 -或多個密實化部件,藉以概括地維持層之間的分隔。密 實化部件可為任何能舰加—魏力至物件的堆積體之部 件。壓縮力應充份夠高錢兩物件不相對於彼此旋轉,不Buddhi) “Review of Thermal Energy Storage and Application of Phase Change Materials”, Renewable and Sustainable Energy Review 13 (2009) 318-345, and Belen Zaiba, Jose Ma Marin, Kabesa ( Luisa F.  Cabeza), Harald Mehling, “Responsive Thermal Energy Storage: Review of Materials, Heat Transfer Analysis and Applications”, Applied Materials described in Thermal Engineering 23 (2003) 251-283, the two documents are collectively incorporated herein. for reference. Other examples of suitable thermal energy storage materials that can be employed in a heat transfer device are disclosed in U.S. Patent Application Serial No. 12/389,416, entitled "Heat Energy Storage Material", filed on February 20, 2009; U.S. Patent Application No. filed on February 2, 2009.  Thermal energy storage material as described in 12/389,598. The thermal energy storage material may comprise an organic material, an inorganic material or a mixture of an organic and an inorganic material that exhibits the aforementioned solid to liquid conversion temperature, fused heat density, or both. Organic compounds which may be employed include paraffin waxes and non-paraffinic organic materials such as fatty acids. The inorganic materials that can be used include salt hydrates and metallic materials. The thermal energy storage material can be a mixture having a solid to liquid conversion (e.g., a total of 27 201144705 crystal mixture) or a compound at a single temperature. The thermal energy storage material can be a solid to liquid conversion compound or a mixture having a temperature range (e.g., a range greater than about 3 ° C, or greater than about 5 ° C). Suitable non-paraffinic organic materials for use as thermal energy storage materials include, but are not limited to, acids, alcohols, aldehydes, guanamines, organic salts, mixtures thereof, and combinations thereof. In the examples, non-paraffinic organic materials which may be used alone or as a mixture include polyethylene glycol, citric acid, oleic acid, lauric acid, pentadecanoic acid, glyceryl tristearate, myristic acid, soft Fatty acid, stearic acid, acetaminophen, dinonyl fumarate, formic acid, caprylic acid, glycerin, D-lactic acid, decyl palmitate, monidone, bromotetradecane, pentadecanone, phenol, Heptadecanone, 1-cyclohexyloctadecane, 4-heptadecanone, p-anisidine, cyanamide, arganic acid vinegar, 3-heptadecane, 2-heptadecane, hydrogen cinnamon, Record alcohol, naphthylamine, terpene, o-nitroaniline, 9-heptadecanone, thymol, methyl behenate, diphenylamine, p-benzene, oxalate, diphosphorane , o-dichloroxylene, gaseous acetic acid, nitronaphthalene, trimyristate glycerin S, heptadecanoic acid, beeswax, glycolic acid, glycolic acid, p-bromophenol, azobenzene, acrylic acid, dinitrotoluene , phenylacetic acid, allyl thiourea, brominated camphor, tetraphenylbenzene, benzylamine, decyl bromobenzoate, α-naphthol, glutaric acid, p-dioxylene, catechol, benzoquinone , 醯Amine, succinic anhydride, benzoic, anthracene, benzene Yue Amides, or any combination thereof. Without limitation, the thermal energy storage material may comprise one or more inorganic salts selected from the group consisting of nitrates, nitrites, bromides, vapors, other compounds, sulfates, sulfites. , phosphate, phosphite, hydroxide, carbonyl compound, bromate, mixtures thereof, and their 28 201144705 combination. In an example, the thermal energy storage material may comprise or consist essentially of: Κ2ΗΡ04·6Η20, FeBr3. 6H20, Μη(Ν03)2·6Η20, FeBr3 6H20, CaCl212H20, LiN03. 2H20, LiN03. 3H20, Na2CO310H2O, Na2SO410H2〇, KFe(S03)2. 12H20, CaBr2. 6H20, LiBr2. 2H20, Zn(N03)2. 6H20, FeCl3. 6H20, Mn(N03)2. 4H20, Na2HP04. 12H20, CoS04. 7H20, KF. 2H20, MgI2. 8H20, CaI2. 6H20, Κ2ΗΡ04·7Η20, Ζη(Ν03)2·4Η20, Mg(N03). 4H20, Ca(N03). 4H20, Fe(N03)2. 9H20, Na2Si03-4H20, Κ2ΗΡ04·3Η20, Na2S203. 5H20, MgS04. 7H20, Ca(N03). 3H20, Ζη(Ν03)2·2Η20, FeCl3. 2H20, Ni(N03)2. 6H20, MnCl2_4H20, MgCl2. 4H20, CH3C00Na. 3H20, Fe(N03)2. 6H20, NaAl(SO4). 10H2O, NaOHH20, Na3P0412H20, LiCH3C00-2H20, Α1(Ν03)2·9Η20, Ba(0H)2-8H20, Mg(N03)2,6H20, KAl(S〇4)2. 12H20, MgCl2. 6H20, or any combination thereof. It will be appreciated that inorganic salts having a higher or lower concentration of water can be used. The thermal energy storage material may comprise (or may even consist essentially of or consist of) at least one first metal containing material, and more preferably a combination of at least one first metal containing material and at least one second metal containing material . The first metal-containing material, the second metal-containing material, or both may be a substantially pure metal, an alloy, such as comprising a substantially pure metal and one or more additional alloying components (eg, one or more other metals) An alloy, an intermetallic substance, a metal compound (e.g., a salt, a monooxide or the like), or any combination thereof. A preferred approach employs one or more metal-containing materials as part of a metal compound; a preferred route is to use a mixture of at least two metallizations 29 201144705. In the examples, the appropriate metal compound may be selected from the group consisting of oxides, hydroxides, compounds including nitrogen and oxygen (e.g., nitrates, sulfites or both), imides, or any combination thereof. It is also possible to use ternary, quat (10) ry or other multi-reconstituted material systems. The thermal energy storage material herein may be a mixture of two or more materials exhibiting eutectic. The volume of the thermal energy storage material in the one or more sealed spaces of the article is sufficiently high to allow the article to store a large amount of thermal energy. The volume of thermal energy storage material contained in the article is for - or a plurality of sealed voids - total volume The ratio, the ratio of the volume of the thermal energy storage material to the total volume of the object, or both (at a temperature of about hunger, or a volume depending on the temperature of the heat (4) (four)) is preferably greater than about 0. 5, more preferably greater than about 〇·7, and optimally greater than about 〇 9. The volume of thermal energy storage material contained in the object is - or the ratio of the volume of the thermal energy storage material to the total volume of the object. 995. A value or both (at a temperature of about 25. (or temperature, or a volume measured by the temperature at which the thermal energy storage material is liquid) is generally less than about 〇, and more generally less than about the sealed space may include one containing one such as The volume of inert gas such as air, N2 or the like, or an inert gas such as He, Αι* and the like, so that the thermal energy storage material can be expanded when heated. For example, the sealed space can have a temperature at about 25 ° C without heat The area of the material, so when the thermal energy material is heated above its liquidus temperature, the 'thermal energy storage material can expand without forming holes or causing delamination in the cover sheet or the substrate sheet. The volume of the sealed space of the thermal energy storage material (for example, the volume containing the gas 30 201144705 sealed space) may account for at least about 0 of the total internal volume of the sealed space. 5%, preferably at least about 1%, and most preferably at least about 1. 5%. Fig. 2A is a diagram showing the characteristic construction of an article 10 including a capsule structure having a single sealed space (i.e., a single pocket). The bladder structure includes a cover sheet 28 having an opening 29 and a base sheet 30 having an opening 31. The opening 29 of the cover sheet and the opening 31 of the base sheet overlap each other (e.g., completely overlap) and thus serve as corresponding openings. The cover sheet 28 and the base sheet are hermetically attached to an outer ring 32. As shown, the outer perimeter of the cover sheet 28, the outer perimeter of the substrate sheet, or preferably both are sealably attached to the outer ring 32. The cover sheet has a top surface 18 that is an outer surface of the article 10 and an opposing surface that is generally located on the interior of the article 10. The base sheet has a bottom surface 20 which is generally an outer surface of the article 10 and a facing surface which is generally located on the interior of the article. The bladder structure can also have an inner ring 34 that is sealingly attached to an open perimeter of the cover sheet 28, an open perimeter of the backsheet 30 or preferably attached to both. As shown, the outer ring 32 can have a generally cylindrical outer surface and a generally cylindrical inner surface. The inner ring 34 can have a generally cylindrical outer surface and a generally cylindrical inner surface, a cover sheet 28 (such as a cover sheet). The top surface 18) can have a generally circular shape, and the base sheet 30 (e.g., the bottom surface of the base sheet) can have a generally circular perimeter, or any combination thereof. One of the combinations of any of the following openings may have a generally cylindrical shape: a fluid passage of the article 16, an opening of the cover sheet 29, and an opening of the base sheet 31. It will be appreciated that a cross section of an opening can have a different shape, such as a polygonal shape, or a different arcuate shape (e.g., an oval shape). As shown in FIG. 2A, the article 10 can have a single side surface 22 that is generally arched, generally non-planar, and has a continuous continuity. The side surface can be substantially equidistant from the center of the article so that the article can be placed in a container having a generally cylindrical cavity having a cavity diameter that is only slightly greater than the average diameter of the article. An exemplary cover sheet 28 for use in one of the articles having an opening 29 is shown in Figure 2B. It will be appreciated that the opening in the cover sheet can be formed simultaneously or after the cover sheet attachment (e.g., hermetic attachment) to one or more other sheets or one or more other substructures. The cover sheet can have a generally circular outer periphery 19, a generally circular inner or open perimeter 21, or both. The cover sheet 28 can have a generally flat bottom surface 38 and a generally flat opposite top surface 18. The cover sheet 28 may be formed from - or a plurality of encapsulant materials 12. The outer periphery 19 of the cover sheet 28, as shown in Fig. 2B, may include a region 23 on the bottom surface 38 of the cover sheet 28, adjacent to the outer perimeter of the cover sheet. Referring to Figures 2 and 26, the substrate sheet 28 can be sealed and attached along the region 23 of the outer periphery 19 on the bottom surface 38. The encapsulant material for the top surface 18 is preferably a material that resists corrosion when exposed to a heat transfer fluid. The encapsulant material for the bottom surface 38 is preferably a material that resists corrosion when contacted with a thermal energy storage material. The encapsulant materials for top surface 18 and bottom surface 38 may be the same material or different materials. The top surface 18 except the opening 29 can have a generally circular shape. The thickness of the cover sheet 28 as measured by the distance between the top surface 18 and the bottom surface 38 of the cover sheet can be substantially uniform. The standard deviation of the thickness of the cover sheet 28 is preferably less than about 15%, more preferably less than about 1%, and most preferably less than about 3% of the average thickness of the cover sheet. Figure 2C shows a cross-section of the object 10 perpendicular to the top surface 18 of the cover sheet 28 taken from the second eight 32 201144705. As shown in Figure 2C, the article may have a sealed space 14 including a thermal energy storage material 26 at one or the other. The sealed space may include - not filled - 27 'that is, the volume contains - the gas 4 filling volume 27 may be used when the thermal energy storage material is heated - such as when the temperature of the thermal energy storage material increases, when the thermal energy storage material undergoes -H phase When the liquid phase is switched, or both, it is expanded. A cover sheet, a substrate sheet, an outer ring, an inner ring, or any combination of two, preferably comprising: or a plurality of encapsulant materials that resist corrosion when contacted with a thermal energy storage material, such as on an interior surface, One or more encapsulant materials that are resistant to rot when contacted by a heat transfer fluid (# as on the outer surface), or both. The cover sheet, the base sheet, the outer ring, the inner % or any of the (f) optimum lines comprise the same _ or a plurality of encapsulant materials, or are actually composed of π. Both the cover sheet 28 and the base sheet 3 are hermetically attached along their outer periphery 19 and (4) a periphery 2 to seal the space 14. 'Du Fu's sheet 4 〇, which can be used as a substrate for one of the objects. The finely divided ridges may be arched and/or have a plurality of walls by the miscellaneous or additional axes. The formed sheet has a groove portion 43 capable of holding or enclosing the body. The formed sheet also has an opening 46 so that fluid can flow through it. The accompaniment also has a lion-to-finished flat cover sheet (such as the cover sheet described in Fig. 2B) - or a plurality of generally flat regions 'such as - or a plurality of lip regions 44. One or more lips coplanarity. It is reported that the film 40 of the main horse H Cheng is not flat (four). A sheet 40, for example, may have a top surface 41 and a substantially bottom surface 42. The shaped sheet may have a side wall extending from the bottom wall. Side slabs 33 201144705 may include a generally arched side surface 49. The formed sheet 40 can have an open wall extending from an inner periphery of the bottom wall. The opening wall can have an open surface 48 that is generally arched and partially or completely defines a fluid passageway through the article. The formed sheet has an outer perimeter 45 and an open perimeter 47. The outer perimeter 45, the open perimeter 47, or preferably both are lip regions 44. It will be appreciated that the formed sheet may comprise a transition zone joining the bottom wall and the side walls, or the bottom and side walls may be combined into an arched wall. It will be appreciated that the formed sheet may comprise a transition region connecting the bottom wall and the opening wall, or the bottom wall and the opening wall may be combined into an arched wall. As previously mentioned, the bladder structure can include a plurality of segments configured to form a bladder structure having one or more sealed spaces and one or more fluid passages. Figures 3A, 3B, and 4 are exemplary side views of adjacent segments of the capsular structure. As shown in Figures 3A, 3B, and 4, adjacent segments may have abutting edges 9 (i.e., generally abutting edge surfaces). Such as the segments 2', 2" of Figures 3A and 3B, wherein the surfaces 4' and 6' of the two segments are substantially coplanar, and when the adjacent segments are arranged in a coplanar orientation, the segments can be docked When the two adjacent segments are displaced, the edges of the adjacent segments can be docked, so that the top and bottom surfaces 4' and 6' are not coplanar. For example, a segment can be displaced up to the segment 2'" thickness Half of it, as shown in Figure 4. Thus, the butt edge 9 of a first segment can be docked to the portion of the edge of the two stacked segments that are both adjacent to the first segment. As shown in Fig. 4, a stack of segments may include one or more (e.g., two) proportional segments 3, such as a proportional segment having half heights of other segments 2'". A portion or all of the grooves of the formed sheet 40' may be partially or substantially completely filled with a thermal energy storage material, and a substantially flat cover sheet (such as described in FIG. 2B) may be placed over the grooves such that the cover sheets are summarized.地 34 201144705 Contact lip area. The cover sheet may be sealingly attached to the formed sheet in some or even all of the lip area to form a plurality of sealed spaces containing the thermal energy storage material, as shown in Figures 5A and 5B. The formed sheet 4〇 may have a groove. The pattern, such that the bottom surface 41 of a first formed sheet 40, is generally a bottom surface 41 of the same second formed sheet 40', the abutting surface. Thus, with the formed sheet 40, the two articles can be formed with their bottom surfaces 4i opposed to each other so that the two articles are at least partially nested. Figure 5B is a plan view of a portion of the formed sheet 40' that is plucked in a plurality of sealed spaces (e.g., a base sheet) having a pattern that has a pattern near the center of the sheet. 46, which may be a circular opening. Fig. 5B shows only 1/4 of the formed sheet, and thus the opening is outlined. Figure 5B shows the formed sheet 4, the sheet formed by the bottom sheet 2 having a plurality of grooves 43 and a plurality of lip materials. The groove area 4 is disposed in a plurality of rings of the groove 50. As shown, the formed outermost ring and the innermost ring of the groove 5G" are formed as =3, and the grooved 50", or more than one additional ring, is located in the groove 5. 〇,, 5 Between the rings. As shown in the first test, some or all of the rings are corrected: 嶋, or even substantially congruent. It will be understood that the groove:::in:: may be larger than or equal to the number of slots in the outermost ring of the slot, the number of slots in the innermost ring is smaller than the number of slots in the outermost ring if 5B Shown. A portion, or preferably all, of the grooved area 43, ι has a surrounding area 44. Therefore, a trough area 43 can be separated by the smear area 4 = his trough area. The formed piece 4〇.  1 dead, m ', its piece has - outer periphery 45,. As shown in Fig. 5B, 35, 201144705, the formed sheet may have one or more recesses 51 near the outer periphery 45'. One or more recesses can be used for flow paths or flow paths along the outer perimeter. Preferably, the outer perimeter of the bottom surface of the formed sheet has a generally circular shape (one or more recesses selected are excluded). As shown in Fig. 5B, the outer periphery, the inner periphery, and preferably both may be lip regions 44'. Fig. 5A shows an exemplary relationship between a capsule structure 10' (e.g., a formed sheet 40' of a capsule structure) and a container 68. The container 68 can have an inner wall 60, an outer wall 62, an insulating layer 64, or any combination thereof. Referring to Figure 5A, the container 68 can have an insulating layer 64 between the two walls 60,62. The inner wall 60 of the container has a diameter that is larger than the diameter of the formed sheet so that the formed sheet fits within the container. The preferred diameter between the perimeter of the sheet and the inner sidewall of the container may include one or more recesses 51 in the formed sheet 40', the size of the formed sheet 40' and the cavity of the container (e.g., diameter) A gap 52 formed by the difference, one or more of the grooves 5 in one of the inner side walls 60 of the container, or any combination thereof. The article containing the thermal energy storage material is preferably capable of being stacked with other identical articles or with a second article having a generalized abutment surface, such as a generally abutted substrate. The articles are stacked in the axial layer with a space between adjacent axial layers such that a heat transfer fluid can flow between the axial layers. An axial layer will generally contain one, two or more articles. An axial layer (e.g., each axial layer) preferably contains one or two articles. For example, an axial layer can have two articles that are in contact on a surface such as a substrate surface or a cover surface so that a fluid summary cannot flow between the two objects). Thus, a portion of the article (eg, an article other than the object 36 201144705 at one end of a stack) may have a first surface (eg, a substrate surface) that is generally in full contact with a surface of a first adjacent article Causing a fluid to flow along the first surface, and a second surface separated from a second adjacent article (eg, having an opposing surface that is generally associated with the mating surface of the second surface) such that a fluid is Flowing along part, most or even all of the second surface. The separation between two adjacent axial layers can be achieved by any of the art-receiving partition members. In an example, a suitable partition member includes one or more projections on one surface of at least one of the articles, a spacer material between the two layers, a capillary structure between the two layers, or any combination thereof. Preferably, the second surface of the article has a generally arcuate shape and the article is partially nested within the second adjacent article. The separation between the partially nested two items is preferably constant (except for the protrusions or other partitions that cause adjacent objects to be separated). It will be appreciated that the stack of articles can include a rotating axial layer (e.g., rotating an object), or otherwise configured to nest the axial layer at least partially within an adjacent axial layer. The flow of a fluid between the opposing surfaces of two adjacent axial layers will generally lie in a radial direction and may be described as a substantially radial flow. The axial layers of the separated pairs will have a radial flow path. The stack of articles will generally have a plurality of radial flow paths (e.g., 2, 3 or more). Two or more (for example, each radial flow path may have the same flow length, the same thickness, the same cross-sectional shape, or any combination thereof. For example, two or more (eg, all) radial flow paths may be full It will be appreciated that if the opening (i.e., fluid passage) is located at the center of the object, the radial flow path can be generally symmetrical regardless of the flow direction. When stacked (ie, located in a containing 3, 4 or more objects) In the case of the stacking body 37 201144705, the objects preferably have at least an opening corresponding to an opening from each of the other objects (possibly except for one of the ends of the stacking body), so that the fluid-portion can be passed through Between the first and last objects, the respective openings of the object and not flowing between adjacent objects (ie, without a substantially radial flow) from the -th object in the stack to the stack - The last object. The flow through the opening is generally located in the _ axial direction and can be described as a substantially axial flow. As described above, the stack of objects can define a central axial flow path (for example, through the opening of the object). Central axis) and A plurality of radial flow paths that are generally perpendicular to the central axial flow path. The stack of objects will be generally tightly packed (e.g., except for the radial flow path), thereby making the accumulation of objects dense and containing a large amount of thermal energy storage material. Thus the 'radial flow path has - generally short height (in the direction between adjacent objects) 'such as an average height. The height of the radial flow is preferably less than about 15 mm 'better than about 5_' or even better. Less than about 2_, even more preferably less than about ^, and optimally less than about 〇. 5_. The height of the radial flow path is large enough for fluid to flow through the flow path. In general, the height of the radial flow path (e.g., the average height) is greater than about zero. 001mm (for example, greater than about 〇 〇1_). = Figure 5 C shows that multiple objects are included! In one aspect of the invention, each article 10' has - or a plurality of sealed spaces 14 accommodating the thermal energy storage material. The article 10' can comprise a formed sheet having a generally chevable surface 41". 4〇”. The surface 41" of an object can be generally docked to the surface of a second object. The object can be configured to partially nest adjacent objects together. The object shown in Figure 5c has 8th order rotational symmetry and thus In 8 different positions 38 201144705 centered: turn to make the ground wire. It will be known that the object can be higher or better than the nominal. As shown, the object can have - a roughly circular cross section The outer periphery of each object may have a plurality of sides permitting - fluid grasping recesses 5116 pieces lQ, and may have a sealed space 14 disposed in the sealed space - or a plurality of the same clothes. Each object may have A body passage 46 is generally approximated in the object, so that when the object is stacked (such as in the axial direction), a vehicle-to-flow path 84 is formed. The axial flow diameter material preferably includes each object. A fluid passage 46 of 10'. Thermal storage device The articles described herein (such as a stack of articles) can be used in a thermal storage device. The thermal storage device can include a container or other housing. Having one or more heat transfer fluid streams The orifice in the vessel and one or more heat transfer fluids exit the orifice outside the vessel. The heat storage device has one or more heat transfer fluid compartments. Preferably, the heat storage device comprises a single heat transfer fluid compartment A heat transfer fluid compartment may comprise or consist essentially of one of the containers between the inlet and the outlet, wherein the heat transfer fluid is available for flow. The container is preferably at least partially insulated so that it may be reduced or Reducing heat loss from the container to the ring chamber. The heat storage device can be designed to contain a large concentration of thermal energy storage material that allows rapid and/or even transfer of thermal energy between a heat transfer fluid and the thermal energy storage material. It is compacted so that it can store heat for a long period of time, or any combination thereof. The inside of the container of the heat storage device can have any shape that can hold the object 39 201144705. The stack of good parts occupies the inside of the container. The shape system makes the thermal energy contained in the sealed space of the object 25t measured) for the total volume of the material (for example, Two value / l.  λ. A 吏佳 is greater than about 〇·6 ’ its $ vy is better than about 0. 7' and optimally greater than about 〇 8. Container H^ μ BP ^ * ° ... The upper limit of the volume of the stored material is: - the need to contact the heat transfer fluid of the article for the * door for transferring thermal energy. The total volume of the stored material (as measured at about 25 ° C) in the sealed space of the article in the container may be less than about 〇 9 9 for a ratio of & total internal volume (as measured at about 25 ° C). Gu Yi is less than about 0. 95 » •, preferably Heat Transfer Fluid Compartment/Flow Path The heat storage device has a heat transfer fluid 3 chamber that is capable of transferring a heat transfer fluid through the device; The heat transfer fluid compartment is preferably coupled to one or more orifices (e.g., one or more) for transferring a heat into the heat transfer fluid compartment. The volume transfer fluid compartment is preferably connected to one or more orifices for shifting the word L in the narrative *''', and the orifice of the ancient heat transfer fluid compartment (for example, one or more capture codes D) . The enthalpy transfer fluid compartment may be at least partially separated by one or more heats, 'T', and the space defined by the wall, at least in part by - or one of the plurality of objects' At least in part, a space defined by the arsenic arsenic or container of the heat storage device, or any combination thereof. The heat transfer fluid compartment defines a flow path through the heat storage device to the transfer fluid. The chamber system includes an axial flow path of the opening of the 40 201144705 deposit. The heat transfer fluid compartment includes a generally radial flow path between two adjacent objects. The flow may flow inwardly from one outer periphery to one of the openings of an object, or from one opening to one of the outer periphery of an object. The heat transfer fluid compartment includes a first-class diameter having an outer periphery of the object And an axial component (and optionally, a line assembly) between a wall of the container. Preferably, the combined radial flow path has a relatively high hydraulic impedance. For example, a combined radial Flow path has a large (more preferably, at least twice greater) one of the central axial flow path, the outer axial flow path, or one of the hydraulic impedances of the hydraulic impedance. The heat transfer fluid compartment is preferably sufficiently thermally conductive to the thermal energy storage material. The sealed space allows it to remove heat from the thermal energy storage material or provide heat to the thermal energy storage material. The heat transfer fluid compartment is preferably thermally coupled directly to one or more (or better all) sealed spaces. The direct thermal conduction system can be any path of the shortest distance between the sealed space and a portion of the heat transfer fluid compartment, which is free of materials having a low thermal conductivity. The low thermal conductivity material includes less than about 100 W/(nvK). a material having a thermal conductivity of less than about 10 W/(m_K), and more preferably less than about 3 W/(nrK). For example, the heat transfer fluid or heat transfer fluid compartment may contact one or more of the sealed ( Or preferably all of one of the walls, or substantially or completely by a material having a high thermal conductivity (e.g., greater than about 5 W/(m_K), greater than about 12 W/(nvK), or greater than about 110 W/(nvK) Sealed The heat transfer fluid compartment is preferably directly thermally conductive to one or more (or more preferably all) of the sealed space in the heat storage device. A direct thermal conduction can be a thermal energy storage compartment and a heat transfer fluid Any path between the part of the compartment 41 short distance of 201144705, which does not contain materials with low thermal conductivity. For example, thermal 4_ fluid or heat transfer (four) septum (four) can be contacted through the sealed chamber (such as substrate or cover) One or more (or preferably all) of one of the walls, or by having a high thermal conductivity (eg, greater than about 5 W/(m. K), greater than about 12W/(m. K), or greater than about i i〇w/(m. The material of K) is substantially or completely separated from the sealed space. It will be appreciated that a very thin layer of material having a low thermal conductivity (e.g., less than about 0 lmm, preferably less than about 〇 1 dirty, and more preferably less than about G. GGlmm) may be located between the heat transfer fluid compartment and the thermal energy storage material compartment without appreciably affecting heat transfer. The size and shape of the sealed space and/or article may be selected to maximize heat transfer to and from the phase change material contained in the bladder. The average thickness of the object may be relatively short so that heat can quickly escape from the sealed space center. The article, sealed space, or both may have an average thickness of less than about 100 mm, preferably less than about 30 mm, more preferably less than about 1 mm, even more preferably less than about 5 mm, and most preferably less than about 3 mm. The average thickness of the object, sealed space, or both may be greater than about 〇. Lmm, preferably greater than about 〇. 5mm, more preferably greater than about 0. 8mm ' and optimally greater than i. Omm. The article preferably has a relatively high surface area to volume ratio and therefore has a relatively high contact area with the heat transfer fluid. For example, the article may have a surface that is in intensive contact with a heat transfer fluid compartment, and the article may have a geometry that maximizes heat transfer between the bladder and the heat transfer fluid compartment, or both. The ratio of the total surface area of the interface between the heat transfer fluid compartment and the article in the heat storage device to the total volume of the thermal energy storage material in the heat storage device may be greater than about 〇〇2111111-1, preferably greater than 42 201144705 at about 0. . 05mm_1, more preferably greater than about 0. 1mm_1, even better than about 0. 2mm-1, and optimally greater than about 0. 3mm·1. Container/Shell The heat storage device has a container for the inclusion body containing the article. The stack of articles can be contained in one or more cavities of the container. Suitable containers have one or more orifices (such as one or more inlets) for allowing a heat transfer fluid to flow into the chamber of the vessel and one or more orifices for allowing a heat transfer fluid to flow out of the chamber of the vessel Oral (such as one or more exits). The inlet and outlet may be located on the same side of the heat storage device or on different sides (e.g., opposite sides). In addition to the orifice, the container is preferably sealed or constructed such that the fluid passing through the vessel does not leak out of the vessel, so that the fluid passing through the vessel can have a pressure greater than one of the pressures of the annulus, or both. The container can have any shape. Preferably, the container has a shape in which a large amount of thermal energy storage material is filled in the middle (e.g., in the sealed space of the accumulation of articles) so that the heat storage device can store a large amount of heat. Without limitation, the cavity of the container and/or container may have a generally circular, generally oval, generally rectangular, generally square cross section (eg, perpendicular to the stacking direction), or have a different general It has a polygonal shape. In a particularly preferred embodiment, the container has a generally cylindrical shape, the cavity of the container has a generally cylindrical shape, or both. For example, the container of the thermal storage device can have a generally cylindrical inner surface, a generally cylindrical outer surface, or both. A cylindrical cavity allows for efficient loading of articles having a generally cylindrical cross section in the cavity. In the example, a cylindrical object has a generally circular cross section. A cylindrical article, a cylindrical cavity, or both can tolerate high efficiency insulation of the heat storage device. In general, the characteristics of the container may be one of the heights of the object stacking direction (i.e., the axial direction) and one of the directions perpendicular to the stacking direction (e.g., a diameter). For example, a cylindrical container may be characterized by a height and a diameter. The height of the container may have a ratio of length (e.g., diameter) of less than about 20, preferably less than about 5, more preferably less than about 3, and most preferably less than about 2. The height of the container may be greater than about 〇·〇5, preferably greater than about 〇 2, more preferably greater than about 0, for length ratios (e.g., height to diameter ratio). 33, even better than about 〇. 5, and preferably the cavity of the container is characterized by a height in one of the stacking directions of the object and an average length (e.g., a diameter) in a direction perpendicular to the stacking direction. Most preferably, the interior of the container has a generally cylindrical cavity characterized by a cavity, a cavity height, and an axial center. The interior of the container may have a generally arcuate wall parallel to the axial direction of the cavity (having a checkerboard as previously discussed). The arched surface preferably has a generally circular cross section. The container can be used to accommodate objects. The accumulation body of the article is preferably configured to have a central axial flow path at or near the axial center of the cavity of the container (for example, the outer periphery of the fluid passage object passing through the plurality of cavities may include one or a plurality of recesses, the inner wall of the container is on the -axis W...I, one or more grooves (preferably in the direction of the axial assembly), and the object can be JL so that the length or the direct operation - The length or diameter, or any combination thereof, flows in an axial direction between the outer circumference of the article: between the inner axial surfaces. This flow can be described as - the outer axial assembly is preferably disposed in the container such that The distance between the chess-shaped inner surfaces of the outer periphery of the object is different for an object and 44 201144705; the different things are uniformly uniform (any recess in the object #" except for the groove in the container wall). Volume storage device can be used when it takes a long time to store heat , in general, (for example, "" having less than about 〇°c, or even less than about _3 (the heat stored in the clothes of the rc temperature, or both) is preferably stored, stored, and stored. The heat in the system is slowly lost to the environment. Therefore, it is better to use some form of insulation. The better the insulation of the system, the longer the storage time. Any conventional use that can slow down the heat loss rate of the heat storage device. Insulation of the type, for example, U.S. Patent No. N, which is incorporated herein by reference in its entirety.  Any insulation disclosed in 6,889,751. The heat storage device is a (hot) container that is insulated from the surface or surfaces. Preferably, some or all of the surface exposed to the ring chamber or the exterior will have an adjacent insulator. The insulating material can be operated by reducing the convective heat loss, the heat loss, the conduction heat loss, or any combination thereof. Preferably, the insulation is permeable to an insulator material or structure that preferably has relatively low thermal conductivity. The gap between the opposing walls can be utilized to obtain insulation. The gap may be occupied by a gas medium, such as an air empty door, or may even be an empty space (for example, using an Oewar vessel), a material or structure having a low thermal conductivity, A material or structure having a low thermal emissivity, a material or structure having a low convection, or any combination thereof. Without limitation, the insulation may comprise ceramic insulation (such as quartz or glass insulation) 'polymeric insulation, or any combination thereof. The insulation can be in the form of -fibrous form...foam form, - densified layer, a coating or any combination thereof 45 201144705. The insulation can be in the form of a woven material, a knitted material, a nonwoven material, or a combination thereof. The heat transfer device can be insulated with a Dewar vessel, and more particularly a container including an opposing wall, configured to define an internal storage cavity and a wall cavity between the opposing walls The wall cavity is evacuated below atmospheric pressure. Walls can be stepped in. Use a reflective surface coating (such as a mirror surface) to minimize radiative heat loss. Preferably, a vacuum insulation around the heat storage device and or the heat storage system is provided. More preferably, the U.S. Patent No. is incorporated herein by reference in its entirety for reference.  One of the vacuum insulations disclosed in 6,889,751. Densified Components The heat storage device optionally includes - or a plurality of densified components for a stack of articles to thereby generally maintain separation between the layers. The compacting component can be any component that can add to the stack of objects. The compressive force should be sufficiently high enough that the two objects do not rotate relative to each other,

匕範例中,一或兩推實化部件可包括物件的堆積體上方In the 匕 example, one or two of the actualized components may include an object above the stack of objects

如固體至液體轉換)或兩者時在兩相鄰物件之間的一徑 減小當熱能儲存材料受到加熱、 諸如彈簧等密實化部件來降 受到加熱、經歷一相轉換(諸 46 201144705 向流徑之厚度變化。 熱®儲存裝置可具有複數個用於使一熱量轉移流體流 過裝置之流徑。各流徑較佳包括兩相鄰物件之間的至少一 心向/;IL。較佳地,經過熱量儲存裝置之流徑的兩或更多者 (§如各者)係具有一類似的總長度,一類似的總液壓阻抗, 或兩者。4如,流徑的兩或更多者(譬如各者)之特徵可概括 在於惕歇曼系統(Tichelmann system)。熱量儲存裝置的一 孔口可藉由一管或其他部件被連接至物件的堆積體之開 ,使付熱量轉移流體必須流過物件的堆積體之開口所形 成的軸向路徑。—般而言,—用於使—孔口連接至物件開 口所形成的軸向流徑之管储延伸至物件的-堆積體中之 第-(譬如第-)物件或是物件的—堆積體中 後)物件-者之任-者。該裝置可包括-或多個密封;= (譬如,位於物件的堆積體之頂部及/或底部),故從一入口 流至-出口之_熱量轉移流體必須流過_徑向流徑。一密 封件可包括1於容許-管將―孔口連接至物件堆積體的 開口之開口。可使用-密封件以沿著物件堆積體的開口阻 絕-軸向流徑-端之流體流,以沿著物件堆積體的_周邊 阻絕一軸向流徑—端之一流體流,或兩者。 用於製造囊狀結構之方法 可利用任何對於熱能儲存材料提供包封之; 含有熱能儲存材_物件及囊狀結構。非限制性’= 法可採用下者或純組合: ’该方 —孔)經過—覆蓋片,切割或衝壓壓—開口(譬如 Ί 如一孔)經過一 47 201144705 基—諸如Μ薄片),形成(譬如熱成形,模锻, 汗雕或其他變形卜基底片以在 、 5 _ nn T界疋圖案而其包 荦而乙Γ或槽區’形成—基底片以在該片中界定-圖 其底片、ΙΓ❹憾區及—或多個槽區,_或衝壓- 十Ρ外周邊(譬如—概呈圓形外蘭,切割或衝壓 形成之-槽),以-覆蓋片 充填的槽),密封性附接-覆蓋片(響如 一基底片)藉以形成一或多個含有熱能儲存材料之經密 封空二,沿著-外周邊密封性附接—基底片,沿著一開口 周邊在封n附接—基底片,沿著―開口周邊密封性附接— 覆蓋片(譬如至-基底片)’或沿著—外周邊密封性附接—覆 盍W譬如至-基底片)。用於形成物件之方法較佳係包括— 模取浮雕、或熱成形―基底#之步驟。用於形成物件之 方法可知用2GG9年2月2G日提巾且名稱為“熱量儲存裝置” 的美國專利中請案N。· 12/389,598所描述之一或多個用於 產生一囊袋的方法步驟。該用於形成物件之方法可選用性 包括下列的一者或任何組合:將一基底片密封性附接至一 或多個諸如一内環、一外環、或兩者等次結構;將一覆蓋 片密封性附接至一或多個諸如一内環、一外環、或兩者等 次結構;或沿著一基底片及/或一覆蓋片的外周邊切割、模 鍛或衝壓一或多個凹缺。 根據此處的教導,囊狀結構(或囊狀結構的一分段)可藉 由一包括將兩片沿其周邊密封性附接之方法所形成。較佳 201144705 地’ S玄等片的至少一者係被浮雕、模锻、或以其他方式形 成使其能夠容納一液體。更佳地,兩片皆被浮雕、模鍛或 以其他方式形成。譬如,囊狀結構、或其—分段係可藉由 包括下列步驟的一或多者之方法形成:只將一第一片的 一外周邊之一部分部份地接合至一第二片,故可以一熱能 儲存材料來充填兩片之間的一空間;以—熱能儲存材料充 填兩片之間的空間之至少 > 部分;及接合該等片的其餘部 分,藉以形成一包括熱能儲存材料之經密封空間。可重覆 —或多個這些步驟以提供一包括複數個經密封空間之結 構。 〇列恐此贿仔苻料之過富的片係包括耐久、抗腐 $、或兩者皆備之薄金屬片(譬如金屬络),使該等片能夠包 含熱能儲存材料,而較佳並無茂漏。金屬片可能能夠以大 於1年且較佳大於5年的一重覆熱循環在—載且環境中運 作。金屬片可另行具有-實質惰性的外表面,其在操作中 接觸於熱能儲存材料。接觸於熱能儲存材料之金屬片的外 =應包括當接騎熱_存材㈣未與麵著起反應、 非ft二或Μ皆然之—或多個材料或實質由其組成。 Γ 可採用的示範性金屬片係、包括具有至少-層 汽銅、銅、紹、錄-鐵合金、青銅 金屬K 不銹輞或類似物之 屬片。„亥片可為—概括的貴金 及考其可為包括一含 乳化物層(言如一原生氧化物層或 上之氧化物層)之金屬的片。一示 ::成於-表面 芦缸十屬片係為一包含一 或一 3紹合金(譬如-含有大㈣重量百分比的紹、較 49 201144705 佳大於90重量百分比_之銘合金)之料。另—示範性金 屬片係為不鎮鋼。適當的不錄鋼片係包括沃斯田鐵不錢 鋼,肥粒料賴或細散财㈣。雜制性地,不錄 鋼可包括大於約1〇重量百分比 '較佳大於約13重量百分 比、更佳大於約15重量百分比、且最佳大於約Π重量百分 比濃度的鉻。不錄鋼可包含小於約㈣重量百分比、較佳 小於約0.15重量百分比、更佳小於約Q l2重量百分比、且最 佳小於約0.10重量百分比濃度的碳。譬如,含有19重量百 /刀比的鉻及約0·08重量百分比的碳之不銹鋼3〇4(SAE代 號)。適當的不銹鋼亦包括含鉬不銹鋼諸如316(SAE代號)。 金屬片可具有可消除或降低金屬片腐姓之任何技藝 習知的 塗覆物。 金屬片具有-夠高厚度藉U當形成片日夺、當以熱能儲 存材料充填囊袋時、囊袋使用期間' 或其任何組合之時不 會形成孔或裂痕。對於諸如運輸等應用,金屬片較佳相對 較溥,使得熱量儲存裝置重量不因金屬片而大增。金屬片 的適§厚度可大於約ΙΟμπι,較佳大於約2(^m,且更佳大於 、勺50μηι。金屬鑌可具有小於約3mm、較佳小於約lmm、且 更佳小於0.5mm(譬如小於約〇.25mm)的一厚度。 第8圖顯示一具有複數個物件1〇,,及1〇”,之示範性熱量 儲存裝置80的一橫剖面,複數個物件1〇,,及1〇”,各具有被包 封在複數個經密封空間14中的熱能儲存材料26 。物件配置 於可具有一概呈圓柱形形狀的經絕緣容器82中。該裝置 包括一具有一第一相鄰物件l〇,,’(a)及一第二相鄰物件 50 201144705 Η),》之物件⑽。物件1〇,,及其第—相鄰物件i(),” 置成使其各⑽平覆蓋片_表面(亦即外部表面)概呈接 觸。物件10”及第二相鄰物_,,,(b)可具有概括對接的表面 (譬如,其各別基底片的外部表面可為概括對接的表面)並可 配置成使其部份地嵌套在一起。可使用一分隔件(未圖示) 維持物件10”及其第二相鄰物件l〇,,,(b)之間的一距離,故— 熱量轉移流體可在兩物件10”及l〇,,’(b)之間於—概呈徑向 方向中流過一徑向流徑83。物件10,,及第二相鄰物件丨〇,,,(b) 之間的空間係為熱量轉移流體隔室的部份。如第8圖所示, 各物件可具有一接觸於熱量轉移流體隔室之表面(譬如,基 底片的一表面)’故熱量轉移流體可直接接觸於各物件且較 佳直接接觸於各經密封空間。如第8圖所示,各徑向流徑μ 可具有相同長度,相同橫剖面’或甚至可為全等。各物件 具有一接近其中心之開口。開口亦為熱量轉移流體隔室的 部份。物件10”及10,,,配置成使其開口形成一中央軸向流徑 84。物件10”及10”,的外周邊及容器85的内部表面之間的空 間亦為熱量轉移流體隔室的部份並形成一外軸向流徑86。 熱量儲存裝置具有一流體連接於中央軸向流徑84之第一孔 口 。熱量儲存裝置可具有一第一密封件或板88,其使第 —孔口 87與外軸向流徑86分離。容器82具有一第二孔口 89 ’其可位於與第一孔口 87相同之容器的側上,或容器的 —不同側上,如第8圖所示。熱量儲存裝置可具有一第二密 封件90 ’其使第二孔口 89與中央軸向流徑分離。第一密封 件、第二密封件、或兩者可防止一流體流動於兩轴向流徑 51 201144705 84及86之間,而不流過一徑向流徑83。參照第8圖,一流動 於第一孔口 87及第二孔口 89之間的流體必須流過中央軸向 流徑84的一部分,且流過外軸向流徑86的一部分。熱量轉 移流體亦必須在流過兩軸向流徑84、86之間流過徑向流徑 83的一者。較佳選擇兩軸向流徑的尺寸使得流體的流力阻 抗(hydrodynamic resistance)概呈恆定,而與流體的一部分 採用何者徑向流徑無關。因此,經過熱量儲存裝置的熱量 轉移流體流較佳係為一惕歇曼系統(Tichelmann system)。容 器82較佳被絕緣。譬如,容器可具有一内壁91及一外壁92, 且兩壁之間的空間93可被排空。該裝置亦可具有一或多個 彈簧,諸如一或多個壓縮彈簧94,其施加一壓縮力於物件 的堆積體上。 第9圖顯示一在容器一側上具有兩孔口 87’及89’之熱量 儲存裝置80’。此裝置可採用一被連接至第一孔口 87,之管 95,用以使流體流動於第一孔口以及最遠離第一孔口之中 央軸向流徑84,的一區96之間。參照第9圖,第一密封件88’ 及第二密封件9 〇,可用來防止一流體未先流過一徑向流徑 83即從第一孔口 87,流至第二孔口 89,。並再度藉由對於兩軸 向流徑86及84’選擇尺寸,可使第9圖的熱量儲存裝置80,之 特徵在於一惕歇曼系統(Tichelmann system)。 熱量儲存系統 該熱量儲存裝置可使用在一採用一或多個熱量轉移流 體以將熱量轉移入熱量儲存裝置内、將熱量轉移出熱量儲 存裝置外之熱量儲存系統中。 52 201144705 熱量轉移流體/工作流體 用來將熱量轉移入及/或轉移出熱能儲存 轉移流體可能是任何液體或氣體,使得該流體流過心 以及_時所流通經過 < “如-熱讀供組件、一或多個連接管或線路 旦 移除组件、或其任何組合)。熱量轉移流體可為能夠核Γ 儲存裝置巾·用溫㈣移歸之任何技_ 量= 移流體或冷㈣。熱量轉移讀可為—液體或氣體:= ㈣轉移流體能夠在使用期間所可能曝露的最低操作 溫度(譬如,最低的預期環室溫度)作流動。譬如,埶 流體在約1大氣壓的壓力及約坑、較佳約、更佳 且最佳約,。(:溫度下可身為—液體或氣體。非限制性地, 用於加熱及/或冷卻一或多個電化學電池芯之—較佳的熱 量轉移流體係在約4〇艺身為液體。 熱量轉移流體應能夠運送通常身為顯熱之大量熱能。 適當的熱量轉移流體可具有至少約1J/g.K、#交佳至^約 2J/g.K、甚至更佳至少約25J/g.K、且最佳至少約撕&的 一比熱(譬如在約25t測量)。較佳地,熱量轉移流體係為一 液體。譬如,可採用任何技藝習知的引擎冷卻劑作為熱量 轉移流體。系統較佳採用用於將熱量轉移人熱量儲存裝置 中的熱能儲存材料内並從熱量儲存裝置中的熱能儲存材料 移除熱量之單—熱量轉移流體。或者,^統可採用一用於 將熱量轉移至熱能儲存㈣之第—熱量轉移流體及一用於 從熱能儲存材料移除熱量之第二熱量轉移流體。—包括一 53 201144705 第一熱量轉移流體及一第二熱量轉移流體之系統中,第一 熱量轉移流體係流過一第一熱量轉移流體隔室且第二熱量 轉移流體流過一第二熱量轉移流體隔室,其中熱量轉移流 體隔室概括由一相對較低熱傳導率材料、諸如熱能儲存材 料所分離。譬如,第一熱量轉移流體隔室之至少20%、至 少50%、或至少約80%的表面積可接觸於或身為含有熱能儲 存材料之物件的表面。這係與一其中兩熱量轉移流體處於 相對較好的熱性導通之熱交換器構成對比。 非限制性地,可單獨使用或以混合物使用之熱量轉移 流體係包括熟習該技術者習知的熱量轉移流體並較佳包括 含有水、一或多個烯烴二醇(alkylene glycol)、一或多個聚 稀烴二醇、一或多個油、一或多個致冷劑、一或多個醇、 一或多個甜菜鹼、或其任何組合之流體。熱量轉移流體可 (譬如對於上述流體以添加或取代方式)包括一諸如下述者 等工作流體、或實質由其組成。可採用之適當的油係包括 天然油、合成油、或其組合。譬如,熱量轉移流體可含有 下列項目或實質由其組成(譬如,至少80重量百分比,至少 90重量百分比,或至少95重量百分比):礦油,蓖麻油,石夕 氧油,氟碳油,或其任何組合。 一特佳的熱量轉移流體係包括一或多個烯烴二醇、或 實質由其組成。非限制性地,較佳的烯烴二醇包括從約1至 約8個稀烴氧基(alkylene oxy)基團。譬如,烯烴二醇可包括 含有從約1至約6個碳原子之烯烴氧基基團。一烯烴二醇分 子中的烯烴氧基基團係可能相同或可能不同。選用性地, 54 201144705 烯烴二醇可包括各含有不同浠 煙氧基基團之不同烯烴二團或不同比值的稀 基團係包括環氧乙尸,以丙r 較佳的烯烴氧基 ㈣u 及環氧丁院。選用性地, 可被替代。譬如’稀煙二醇可以-或二個烧基基 或ΐ個含有約1至約6個碳原子的烧基基團被替 馳二㈣包括-或多個烯烴二醇單院基趟、 ^戈夕個馳二醇二烧基醚、或其組合,或實f由其組成。 ㈣可包括—賴烴二醇1佳的馳二醇係包括 乙-酵’二乙二醇’丙二醇,及丁二醇。任何上述乙二醇 皆可早獨使用或以-混合物使用。譬如,乙二醇可用來作 為與水的混合物。㈣雜量轉移流_包括實質地(譬 如,佔熱量轉移流體總重量的至少8〇重量百分比至少9〇 重量百分比或至少96重量百分比)或完全地由乙二醇與水 的-混合物所組成之混合物。遇合物中的水濃度較佳佔熱 量轉移流體總重量的大於約5重量百分比,更佳大於約忉重 量百分比,甚至更佳大於約15重量百分比,且最佳大於約 20重量百分比。混合物中水的濃度較佳小於約“重量百分 比,更佳小於約90重量百分比’甚至更佳小於約以重量百 分比,且最佳小於約80重量百分比。混合物中乙二醇的濃 度佔熱量轉移流體總重量的較佳大於約5重量百分比,更佳 大於約10重量百分比’甚至更佳大於約15重量百分比,且 最佳大於約20百分比。混合物中的乙二醇濃度較佳小於約 95重量百分比,更佳小於約90重量百分比,甚至更佳小於 約85重量百分比,且最佳小於約80重量百分比。 55 201144705 選用性地,執县 全地由复料Γ 可咏-玉作錄或實質完 成 s如,系統可包括一工作流體,ι#、、Αι9Λ 流過熱量儲存:Μ乍流體 個使工件流體凝被加熱马發織前往一或多 熱量儲存裝置可:件(譬如—將被加熱的組件)。因此, 加熱的_可作用於工作流體之蒸發器,而一將被 作流體,提供至凝二於工:流體之凝結器。若採用-工 埶旦。/ " 、、'0器之熱里較佳係包括工作流體的汽化 =、里糸統可包括一用於使工作流體返回熱量儲存裝置之 、、&帛於從熱量儲存裝置移除工作流體之熱量線 路、、線路及熱量線路較佳能夠當工作流體流過一迴路時 予以圍堵而無姑。當熱量儲存裝置(譬如熱量儲存裝置中 的熱能儲存材料)處於足以造成卫作流體之所有組件的合 併蒸氣壓超過約1大氣壓之一溫度且-閥被打開容許工作 流體流動時,卫作流體可能a)被-毛細管結構収送;b) 被至少部份地汽化;。)被至少部份地運送至凝結器;及… 至少部份地凝結於凝結器中;藉以從熱量儲存裝置移除執 量。因此,系統可選用性地包括-毛細管菜送式迴路。、 工作流體 工作流體可歧可當減儲細料位於或高於其液相 線溫度時在熱㈣存裝置巾部份0全喊發(從液體轉 換至氣態)之任何流體。適當的工作流體(譬如用於毛細管系 送式迴路)係包括具有下列特徵的—者或任何組合之純物 質及混合物:處於最大值熱_衫統溫度之良好化學穩 定度,低黏度(譬如小於約l〇〇mPa.s),毛細管結構之良^ 56 201144705 濕潤(譬如,良好芯吸濕潤),與毛細管泵送式迴路的材料(諸 如容器材料,用來包封熱能儲存材料之材料,蒸氣及液體 線路的材料,及類似物)之化學相容性(譬如,工作流體造成 其低腐蝕),有益於蒸發器及凝結器溫度之溫度因變性蒸氣 壓,汽化的高容積性潛熱(譬如,以百萬焦耳每升為單位之 熔合潛熱及處於約25°C的工作流體的密度之乘積可大於約 4MJ/升),小於或等於凝結器的熱量轉移流體冷凍點之冷凍 點(譬如,小於或等於抗凍劑冷凍點之冷凍點),或小於或等 於約-40°C的冷凍點。譬如,工作流體的均衡狀態可在-40 °(:的溫度及1大氣壓的壓力下身為至少90百分比液體。 非限制性地,示範性工作流體可包括一或多個醇、一 或多個酮、一或多個碳氫化合物、一氟碳、一氫氟碳(譬如 一技藝習知的氫氟碳致冷劑,諸如一技藝習知的氫氟碳汽 車致冷劑)、水、銨、或其任何組合;或實質地由其組成。 工作流體應在蒸發器中具有夠高蒸氣壓藉以產生一足 以泵送工作流體之蒸氣物流。較佳地,工作流體的蒸氣壓 應在蒸發器中夠高,藉以產生一足將以瓦特測量的理想熱 功率從蒸發器攜載至凝結器之蒸氣物流。蒸發器中之工作 流體的蒸氣壓較佳充分夠低使得毛細管泵送式迴路不會洩 漏且不斷裂。 工作流體濕潤至毛細管結構之特徵係可在於毛細管結 構的材料上之一接觸角度。較佳地,接觸角度係小於約 80°,更佳小於約70°,甚至更佳小於約60°,且最佳小於約 55。。 57 201144705 工作流體較佳在低於約㈣溫度凝結於適度墨力。舉 如’工m體可在約9g°c凝結於小於約观以 、較佳小於約 0.8MPa、更佳小於約G 3MPa、甚至更佳小於削卿&、且 最佳小於約O.IMPa的一壓力。 工作流體較佳可在很低題錢。譬如,卫作流體可 曝露於很低的環室溫度且較佳能夠在約、較佳約、1〇 C、更佳約-25X:、甚至更佳約_贼、且最佳約俄的溫 度從凝結ϋ絲熱量儲存裝置。卫作㈣減#位於經= 全充載的熱量儲存裝置的_溫度時係處於氣態。譬如,工 作流體可在1大氣壓時具有小於熱量儲存裝置中敎能儲存 材料的相轉換溫度之-彿點,較佳比熱能儲存材料的相轉 換溫度更小至少2G°C、且更佳比熱能儲存材料的相轉換溫 度更小至少赋。本發明的不同態樣中,可能欲使工作流 體在1大氣壓具有下列沸點(或者,使卫作流體的所有組件 合併蒸氣壓特1大氣壓之溫度係可為)大於約贼、較佳 大於約35t、更佳大於約耽、甚至更佳大於觸、且 最佳大於約7 0 °C (譬如使工作流體在環室條件下為一液 體)。本發明的不同態樣中,工作流體在i大氣壓之沸點可 為(或者,使工作流體的所有組件合併蒸氣壓等於丨大氣壓 之溫度係可為)小於約18(TC,較佳小於約15(rc,更佳小於 約l2〇°C,且最佳小於約95。(:。 -特佳的工作越係包括水及録,或實f由其組成。 譬如,工作流體中之水及_合併濃度可佔工作流體總重 量的至少約80重量百分比,更佳至少約9〇重量百分比且 58 201144705 最佳至少約95重量百分比)水及録。銨可具有充分濃度以使 工作流體沸點保持低於水的沸點(譬如,水沸點以下至少10 C)。銨的濃度可佔工作流體總重量的大於約2重量百分 比,較佳大於約1 〇重量百分比,更佳大於約丨5重量百分比 且最佳大於約18重量百分比。銨的濃度可佔工作流體總重 畺的小於約80重量百分比,較佳小於約6〇重量百分比,更 佳小於約40重量百分比且最佳小於約30重量百分比。工作 流體中水的濃度可佔工作流體總重量的大於約2〇重量百分 比,較佳大於約40重量百分比,更佳大於約6〇重量百分比 且最佳大於約70重量百分比。工作流體中水的濃度可佔工 作流體總重量的小於約98重量百分比,較佳小於約95重量 百分比,更佳小於約90重量百分比,甚至更佳小於約85重 量百分比,且最佳小於約82重量百分比。譬如,約21重量 百分比的銨及約79重量百分比的水之一溶液係具有約-40 c的一液相線點以及小於約10(rc之處於丨大氣壓的一沸騰 範圍之上限。此溶液可在室溫(以一液體)儲存於一未加壓的 容器中。 較佳地,工作流體在從約〇它至約25〇它的一溫度具有 等於1大氣壓之其所有組件的一合併蒸氣壓。 工作流體能夠從熱量儲存裝置有效率地轉移熱能,以 使從熱量儲存裝置移除-熱量數量所需要的工作流體量相 對較小(譬如,相較於H不是卫作流體的熱量轉移流 體來移除熱量之裝置)。較佳地,卫作流體所轉移的熱量有 -大部分以汽化熱的形式被轉移。相較於—採用—不是工 59 201144705 作抓體的熱里轉移流體且具有相同初始功率之系統,工作 抓體的體積、工作流體的流率、或兩者可在熱能儲存中相 對較低。熱量儲存裝置的容器每升之工作流體(亦即,流入 熱量儲存裝置巾之處於㈣的卫作流體)的流率係可小於 勺升/刀4里車交佳小於約2升/分鐘,更佳小於約味纷鐘, 甚至更佳小於·5升/分鐘,且最佳小於·w分鐘。系 統中的工作流體體積對於熱量儲存裝置的容器中總體積、 或對於熱量儲存裝置中減儲存㈣體積之比值應充分夠 低’使得系統的總重量不受卫作流體重量過度地衝擊。系 統中(譬如’毛細管泵送式迴路中)之卫作流龍積對於熱量 儲存裝置的容器總體積(亦即’容器内側的體積)之比值(或 甚至系統巾卫作流體體積對於熱㈣存裝置巾熱能儲存材 料體積之比值)可小於約20 ;較佳小於約1〇, 1佳小於約4, 甚至更佳小於約2,且最佳小於約1。 如上述,工作流體可以汽化熱的熱量形式轉移部分熱 能。工作流體較佳具有高汽化熱,故可轉移高量值的熱量。 用於熱量儲存裝置之適當工作流體可具有大於約 200kJ/mole、較佳大於約500kJ/ mole、更佳大於約75〇kJ/ mole、甚至更佳大於約1000kJ/ mole且最佳大於約12〇〇kJ/ mole的汽化熱。 在工作流體溫度可小於〇 C之應用中,工作流體較佳不 是水(譬如’不使工作流體冷凍,造成斷裂,或兩者)。 將可瞭解:接觸於工作流體之材料可抵抗來自工作流 體的腐蚀。4如’可能接觸於工作流體之熱量儲存裝置或 60 201144705 ,、,、直儲存糸統的任-或全部表面(譬如卫作㈣Μ “ 的内部’工作流體液體線路的内部,熱量儲錢置之熱量 轉移流體隔室的表面,一或多個閥的内部表面,凝結器; 之一工作流體隔室的表面,一工作流體貯器的内部表面, 及類似物)可由不銹鋼製成。 將瞭解此處所述的熱能儲存裝置中所採用之任何工作 流體或熱量轉移流體可包括—添加裝體。此等添加劑 包裝體係為熟習該技術者所熟知並適可配合其中可運 發明的裝置之系統。譬如,添加劑包裝體可包括—穩定劑, 一腐触抑制劑’―潤滑劑,-極端壓力添加劑,或其任何 組合。 選用性加熱器 时=儲存系統可選用性地包括—或多個加熱器。加熱 量儲存裝置中的熱能儲存材料溫度增高 能修:能:二:::加熱器。加熱_是將 ⑽即_之、:7或其任何組合)轉換成熱 個電加熱器。-或多ϋΓ多個加熱_是一或多 一… 個加熱益可用來加熱熱量儲存裝置中 導:二二4熱能儲存。較佳地’系統包括-或多個熱性 導通於一熱$儲存梦w #如,㈣可包括位於 ’’’、里:子、的絕緣物内之_或多個加埶 器可採用來自―或多 ‘,,、 電… 或兩者之電力。馨如來自一外部供源、 物體之出口時,執量;/被插接八-連接至-靜態 睹存裝置可彻來自_外部供源的電 201144705 力而被維持在熱量儲存裝置中的熱能儲存材料液相線溫度 以上之一溫度。當載具未被插接入一連接至一靜態物體之 出口時,熱量儲存裝置可利用來自一電化學電池芯產生的 電力而被維持在熱量儲存裝置中的熱能儲存材料液相線溫 度以上之一溫度。 熱量儲存裝置可使用在一用於加熱一或多個組件之方 法中。該方法可包括使一熱量轉移流體流過熱量轉移裝 置。使一熱量轉移流體流過熱量儲存裝置之步驟可包括: 使一具有一初始溫度的熱量轉移流體流過該裝置的一入 口;使熱量轉移流體流過一軸向流徑,故熱量轉移流體可 被分入複數個徑向流徑中;使熱量轉移流體流過一徑向流 徑,故其可從熱能儲存材料移除熱量,其中熱能儲存材料 具有大於熱量轉移流體的初始溫度之一溫度;使熱量轉移 流體流過一不同的軸向流徑,故複數個徑向流徑可重新合 併;使具有一出離溫度的熱量轉移流體流過該裝置的一出 口;或其任何組合。較佳地,熱量轉移流體出離溫度溫度 係大於熱量轉移流體的初始溫度。用於加熱一或多個組件 之方法可採用一經過熱量儲存裝置之流徑,其包括徑向流 徑的一選擇之一者及兩軸向流徑,該流徑具有一總流長 度,其中總流長度對於不同徑向流徑概呈恆定。 熱量儲存裝置及/或熱量儲存系統之特徵可在於具有 一相對較高的功率(譬如,如初始30或60秒加熱期間所測 量),故其可快速地加熱一組件,諸如一内燃引擎。熱量儲 存裝置及/或熱量儲存系統之特徵可在於大於約5瓦特、較 62 201144705 佳大於約10瓦特、更佳大於約15瓦特、且最佳大於約20瓦 特的一平均功率。 熱1儲存裝置及/或熱量儲存系統之特徵可在於具有 一相對較高的功率密度’故其可在一相對較小的隔室中容 納大量熱能。譬如,熱量儲存裝置及/或熱量儲存系統之特 徵可在於具有大於約4kW/L、較佳大於約8kW/L、更佳大於 約10kW/L、且最佳大於約i2kW/L的功率密度。 熱量儲存裝置及/或熱量儲存系統之特徵可在於具有 熱量轉移流體的一相對較低壓降(在約10L/分鐘的熱量轉移 流體流率作測量)。譬如,熱量儲存裝置及/或熱量儲存系統 之特徵可能在於具有小於約2.0kPa、較佳小於約1.5kPa、更 佳小於約1.2kPa、且最佳小於約i.okpa的熱量轉移流體壓 降。 範例中,熱能儲存系統可使用在一運輸載具(譬如—汽 車載具)中以儲存來自一引擎排氣的能量。當引擎產生排氣 時,一旁通閥將氣體流導引經過熱量儲存裝置,使得熱量 儲存裝置被充載,或經過一旁通線路以防止熱量儲存裝置 過熱。當引擎停止時,譬如當載具停車的一段時期中,储 存在熱量儲存裝置中之一顯著部分的熱量可被留置一段長 時間(譬如由於圍繞熱量儲存裝置之真空絕緣所致)。較佳 地,載具在約-40°C的環室溫度停車16小時之後,熱量儲存 裝置中之熱能儲存材料的至少50%仍處於液態。若載具停 車一段夠長時間(譬如’至少二或三小時)使引擎實質地冷下 來(譬如使引擎與環室之間的溫差小於約2〇°C),可藉由一熱 63 201144705 量轉移流體(諸如引擎冷卻劑)流過包括用於工 、1下流體的凝 結器之熱交換器而使儲存在熱量儲存裝置中θ J热夏被間接 地排放入冷引擎或其他熱量受體中。利用复由 州,、中可供工作流 體汽化之熱量儲存裝置内側的毛細管結構,使卫 土 , 工作流體流 通於-毛細管栗送式迴路中。來自工作流體的熱量係 移至熱交換器中之引擎冷卻劑。利用熱量儲左 吻1子衮置,可掏 取原本在一先前行程期間被浪費的熱量,以、、#Α 从减輕冷啟動及/ 或提供立即性座搶加熱作用。 -用於儲存熱量、諸如來自載具排氣的熱量之熱㈣ 存系統係可包括第10圖所示的部分或全部特徵構▲ 儲存系統100係包括熱量儲存裝置101。熱能儲存=統 括一熱交換器或凝結器102,其具有一用於—结 '弟—熱量轉移 流體而之第-人口117及1於第—熱量轉移流體之第一 出口 117。熱能儲存系_〇可具有—管(譬如_線路)⑴, 管113將熱父換器1〇2的第一熱量轉移流體入口 Hi連接至 熱量儲存裝置101的第一熱量轉移流體出口。熱能儲存系统 100可具有一管⑽,管灣熱交換請的第-熱量轉移 流體出口 ^連接至熱量儲存裝置ωι的第—熱量轉移流體 入口。第-熱量轉移流體107流過熱量儲存裝置ι〇ι的一第 一熱量轉移流體隔室。[熱量轉移流體可流過熱交換器 102的-第-熱量轉移越隔n熱量轉移流體可為一 工作抓體雜量儲存裝置101至熱交換II1G2的線路係可 為-蒸氣線路,熱交換器⑽可為1於工作流體之凝結 器而第熱里轉移流體隔室可為工作流體隔室。因此, 64 201144705 熱能儲存系統100可含有一毛細管泵送式迴路,其包括熱量 儲存裝置中之工作流體隔室,凝結器中之一工作流體隔 室,工作流體蒸氣管109,及工作流體液體管113。熱能儲 存系統亦包括一或多個熱量轉移流體或工作流體貯器 110。使用於一毛細管泵送式迴路中時,貯器110較佳具有 一充填位準,其水平高度係高於熱量儲存裝置101的工作流 體入口且低於凝結器的工作流體出口 117,凝結器的工作流 體入口 111,或兩者。熱能儲存系統100可包括一閥118,以 調節用於連接熱量儲存裝置101及熱交換器102之管113中 的第一熱量轉移流體流。譬如,可利用閥118以當熱量儲存 裝置正在充載時及熱量儲存裝置正在儲存熱量時防止熱量 轉移流體之流通。當需要從熱量儲存裝置排放熱量時,閥 118可被打開。再度參照第10圖,熱能儲存系統可包括一熱 量轉移流體入口線路108及一熱量轉移流體出口線路106, 以供一第二熱量轉移流體流入及流出熱量儲存裝置101。熱 能儲存系統亦可具有一熱量轉移流體旁通線路10 5及一轉 向閥(譬如一旁通閥)104以使部分或全部的第二熱量轉移 流體轉向至旁通線路1〇5(譬如,當熱量儲存裝置被完全地 充載時,或當第二熱量轉移流體溫度低於熱量儲存裝置101 中之熱能儲存材料的一溫度時)。熱能儲存系統亦可包括一 用於提供另一熱量轉移流體至熱交換器中之冷線路116,及 一用於從熱交換器102移除經加熱的熱量轉移流體之熱量 線路115。冷線路116及熱量線路115係為一熱量轉移流體迴 路114的部份。熱量轉移流體迴路114可含有一引擎冷卻 65 201144705 劑。熱量轉移流體迴路114可被連接至一内燃引擎103。因 此,熱能儲存系統100可利用儲存在熱量儲存裝置101中的 能量來加熱一内燃引擎103。 可藉由開啟工作流體閥(亦即排放閥)來開始利用工作 流體之熱量轉移。經由一額外液體線路被連接至迴路之經 密封的工作流體貯器係可用來容納迴路内側之工作流體液 體體積的變化而無實質的壓力變化。一旦從熱量儲存裝置 轉移了充分或全部的有效熱量,排放閥可關閉。熱量儲存 裝置中之剩餘工作流體係可蒸發(譬如從熱量儲存裝置中 留存的熱量或當熱量儲存裝置開始充載時)且然後凝結於 凝結器中。當熱量儲存裝置變成已排空工作流體,工作流 體位準的液體位準可能改變(譬如升高)。 熱量儲存裝置可選用性身為一交叉流熱交換器(亦 即,具有一用於工作流體的流方向及一用於排氣流的垂直 流方向)。譬如,操作期間,熱量儲存裝置可包括由下列項 目佔用的三個腔室:1)排氣;2)停滯的相變材料(譬如,囊 袋内側,諸如一泡罩包體);及3)工作流體。所有三個腔室 藉由一適當材料、較佳為不銹鋼製成之薄壁保持分離。排 氣可流動於泡罩内側的相變材料之囊袋的表面(譬如彎曲 狀表面)之間,且工作流體可在一概括垂直於排氣流方向的 方向中流動於泡罩内側的相變材料之囊袋的不同表面(譬 如扁平表面)之間。進入其腔室之液體工作流體較佳係濕潤 一毛細管結構(譬如一金屬芯吸件)且藉由作用在毛細管内 側所形成之工作流體液體彎液面上的毛細力對抗重力及蒸 66 201144705 氣壓的合併力量被往上運送。利用從泡罩内側的相變材料 所抽取之熱量,藉由液體的連續蒸發來維繫此流。工作流 體的蒸氣係離開毛細管結構,並經由可能交錯於泡罩内側 之相變材料的囊袋表面(譬如扁平表面)之間所擠壓之毛細 管結構柱件之間的蒸氣通路逃逸至裝置的頂部。工作流體 的蒸氣係流入凝結器中,其在該處將其汽化熱及顯熱轉移 至冷的冷卻劑並再度變成液體以返回至熱量儲存裝置並繼 續其在迴路中的流通,只藉由存在於被液體工作流體所部 份地浸潰之毛細管結構(譬如金屬芯吸件)内側的毛細力予 以泵送。毛細管結構的全部柱件可連接至一共同的多孔基 底。可利用此多孔基底將從裝置底部進入的液體工作流體 分配至不同柱件。 尚且,本發明可與額外的元件/組件/步驟合併使用。譬 如,可對於冷的冷卻劑以添加或取代方式使用用於空調之 吸收或吸附循環冷凍系統作為熱量受體(譬如,凝結器亦可 用來作為一蒸發器,以供致冷劑流通於一空調器的流體迴 路内側)。另一應用中,可建構一使用一諸如朗肯循環 (Rankine cycle)等熱引擎之穩態廢熱收回系統,使其利用相 同或不同的毛細管泵送式迴路工作流體並將一機械功率產 生渦輪添加至熱量儲存裝置與凝結器之間的蒸氣線路,(譬 如,用以克服來自渦輪上游的高蒸氣壓),及/或將一液體泵 添加至凝結器與熱量儲存裝置之間的液體線路。上述渦輪 可將從排氣廢熱所擷取的一部份轉換成有效的機械或電功 率,並藉此改良載具的整體燃料效率。 67 201144705 雖然本發明可具有各種不同修改及替代形式,已藉由 範例顯示上文討論的示範性實施例。然而,應再度瞭解本 發明無意侷限於此處所揭露的特定實施例。事實上,本發 明的技術係涵蓋落在由申請專利範圍所界定之本發明的精 神與範圍内之所有修改、均等物、及替代物。 c圖式簡單說明3 第1A圖是一具有一或多個經密封隔室及一流體通道之 示範性物件的圖式; 第1B圖是一具有複數個分段之示範性物件的圖式,各 分段含有一或多個經密封隔室,分段係配置成使物件具有 一流體通道; 第2A圖是一具有一經密封隔室及一流體通道之示範性 物件的圖式; 第2B圖是可使用於該物件中之一具有一流體通道的示 範性覆蓋片之圖式; 第2C圖是一示範性物件、諸如第2A圖所示的物件之橫 剖面; 第2D圖是一可使用於一物件中之示範性經浮雕基底片 的橫剖面; 第3A圖是可使用於一物件中之兩示範性相鄰分段的側 視圖,分段可具有一概括地對接之邊緣; 第3B圖是可使用於一物件中之兩示範性相鄰分段的側 視圖,分段可具有一概括地對接之邊緣; 第4圖是分段的一者被移位使得分段之相鄰分段底表 68 201144705 面位於不同平行平面上時,沿著其邊緣對接之相鄰分段的 側視圖; 第5A圖是可使用於一具有複數個含有熱能儲存材料的 經密封隔室之物件中之一具有複數個槽的示範性經浮雕基 底片之圖式; 第5B圖是第5圖的經浮雕片之一示範性部分的圖式; 第5C圖顯示具有對應的流體通道之物件的一示範性堆 積體; 第6A圖是一具有一或多個表面的示範性物件之圖式, 該一或多個表面含有複數個從開口延伸至外周邊之溝槽; 第6B圖是顯示一第一物件的一底表面及一第二物件的 頂表面一當兩表面各具有複數個彎曲狀溝槽時一之間的介 面之圖式; 第6C圖是一示範性物件之兩分段的圖式; 第6D圖是第6C圖的分段之一堆積體的側視圖; 第7圖是顯示一具有一頂表面之示範性物件的俯視 圖,該頂表面係為非圓形及/或具有一非圓形的開口; 第8圖顯示一示範性熱量儲存裝置之橫剖面,其包括一 容器中之物件的一堆積體; 第9圖是一示範性熱量儲存裝置之另一橫剖面,其包括 一容器中之物件的一堆積體; 第10圖是顯示一熱能儲存系統的示範性特徵構造之示 意圖。 69 201144705 【主要元件符號說明】 2’,2”,2’”···分段 3···比例性分段 4..·囊狀結構之頂表面 4’,6’…分段的表面 6···囊狀結構之底表面 8···囊狀結構的外邊緣表面 9···第一分段的對接邊緣 10,10’…囊狀結構,物件 10”,10’”…物件 12…包封劑材料 14…經密封空間 15…徑向溝槽 16…物件,流體通道,開口 18,41…頂表面 19…外部周邊 20…底表面 21,47…開口周邊 22…側表面 23···底表面38上的外周邊19之區 24…邊緣表面 26…熱能儲存材料 27…未充填體積 28…覆蓋片 29,31,46…開口 30…基底片 32…外環 38…覆蓋片28的底表面 40,40’,40”…經形成的片 41’···經形成的片40’之底表面 41”···概呈拱形表面 42…底表面 43,43’···槽區 44,44’…唇區 45,45’…外周邊 46’···流體通道 48…開口表面 49…概括拱形的側表面 50,50’,50”,50’”...槽 51···凹缺 52…間隙 53…溝槽 60,91···内壁 62,92…外壁 64…絕緣層 68,85…容器 80…示範性熱量儲存裝置 70 201144705 80’,101…熱量儲存裝置 82···經絕緣容器 83…徑向流徑 84,84’…中央軸向流徑 86…外軸向流徑 88…第一密封件,第一密封件 87,87’…第一孔口 89,89’…第二孔口 90,90’…第二密封件 93…兩壁之間的空間 94…壓縮彈簀 95,109…管 96…區 100···熱能儲存系統 102···熱交換器或凝結器 103…内燃引擎 104."轉向閥 105···熱量轉移流體旁通線路 106···熱量轉移流體出口線路 107···第一熱量轉移流體 108···熱量轉移流體入口線路 109…工作流體蒸氣管 110···熱量轉移流體或工作流 體貯器 111···第一熱量轉移流體入口 113···工作流體液體管 114…熱量轉移流體迴路 115···熱量線路 116···冷線路 117···第一出口 118.··閥 71A reduction in diameter between two adjacent objects, such as solid to liquid conversion, or both, when the thermal energy storage material is heated, degraded by a dense component such as a spring, undergoes a phase transition (46 201144705) The thickness of the diameter varies. The thermal® storage device can have a plurality of flow paths for flowing a heat transfer fluid through the device. Each flow path preferably includes at least one core direction between the two adjacent objects, IL. Two or more of the flow paths through the heat storage device (§ as each) have a similar total length, a similar total hydraulic impedance, or both. 4 For example, two or more of the flow paths The characteristics of (for example, each) can be summarized in the Tichelmann system. An orifice of the heat storage device can be connected to the stack of the object by a tube or other component, so that the heat transfer fluid must be The axial path formed by the opening of the stack of objects flowing through the object. In general, the tube for connecting the orifice to the axial flow path formed by the opening of the object extends into the stack of the object. The first - (such as the -) object or Object - the accumulation of body after) the object - of any person - who. The apparatus may include - or a plurality of seals; = (e.g., at the top and/or bottom of the stack of articles) such that the heat transfer fluid from one inlet to the outlet must flow through the radial flow path. A seal may include an opening that allows the tube to connect the orifice to the opening of the article stack. A seal can be used to block the axial flow-end fluid flow along the opening of the object stack to block an axial flow path along the _periphery of the object stack - one of the fluid flows, or both . The method for making the bladder structure can utilize any encapsulation for the thermal energy storage material; it contains the thermal energy storage material_object and the capsule structure. The non-restrictive '= method may be either the following or a pure combination: 'the square-hole' is formed through a cover sheet, cut or stamped-opening (such as a hole) through a 47 201144705 base—such as a crucible sheet. For example, thermoforming, die forging, sweating or other deformation of the base sheet to the 5 _ nn T boundary pattern and its wrapping and the enamel or groove region 'formed — the base sheet to define in the sheet - the film , regret area and - or a plurality of trough areas, _ or stamping - the outer periphery of the Shiyan (such as - generally circular outer blue, cut or stamped to form a trough), to cover the filling of the sheet), sealing Attaching a cover sheet (such as a substrate sheet) to form one or more sealed voids containing thermal energy storage material, sealingly attached to the substrate along the outer periphery, attached to the periphery of an opening - a substrate sheet that is hermetically attached along the "opening perimeter" - a cover sheet (such as to a substrate sheet) or a seal-attachment along the outer periphery - such as to - a substrate sheet. Preferably, the method for forming the article comprises the steps of - embossing, or thermoforming - substrate #. The method for forming an article is known as N in the U.S. Patent No. 2, GG, February 2G, which is entitled "Thermal Storage Device". • One or more of the method steps described in 12/389,598 for creating a pouch. The method of selecting for forming an article includes one or any combination of the following: sealingly attaching a substrate sheet to one or more secondary structures such as an inner ring, an outer ring, or both; The cover sheet is sealingly attached to one or more secondary structures such as an inner ring, an outer ring, or both; or cut, stamped, or stamped along the outer perimeter of a substrate sheet and/or a cover sheet Multiple recesses. In accordance with the teachings herein, a bladder structure (or a segment of a bladder structure) can be formed by a method that includes sealingly attaching two sheets along their perimeter. Preferably, at least one of the 201144705 grounds is embossed, swaged, or otherwise formed to accommodate a liquid. More preferably, both pieces are embossed, stamped or otherwise formed. For example, the capsule structure, or a segment thereof, can be formed by one or more of the following steps: only one portion of an outer periphery of a first sheet is partially joined to a second sheet, A thermal energy storage material can be used to fill a space between the two sheets; at least a portion of the space between the two sheets is filled with the thermal energy storage material; and the remaining portions of the sheets are joined to form a thermal energy storage material. Sealed space. The steps may be repeated - or a plurality of these steps to provide a structure comprising a plurality of sealed spaces. The film that is too rich for the sake of bribery, including durable, anti-corrosion $, or both thin metal sheets (such as metal), so that the sheets can contain thermal energy storage materials, and preferably No leaks. The metal sheet may be capable of operating in a load-and-energy environment with a multiple thermal cycle of greater than one year and preferably greater than five years. The metal sheet may additionally have a substantially inert outer surface that is in operation in contact with the thermal energy storage material. The outer part of the metal sheet that is in contact with the thermal energy storage material should include when the riding heat _ storage material (4) is not reacted with the surface, not ft or Μ — - or a plurality of materials or substantially composed of it.示范 Exemplary metal sheet systems that can be used include those having at least a layer of vapor, copper, copper, iron-alloy, bronze metal K stainless steel or the like. „海片 can be—the general precious gold and the test piece can be a piece of metal including an emulsion layer (such as a layer of native oxide or an oxide layer thereon). The ten-slice film is a material containing one or one of the three alloys (for example, containing a large (four) weight percentage of Shao, and 49 201144705 is better than 90 weight percent of the alloy). The other - exemplary metal sheet is not town Steel. Appropriate non-recorded steel sheeting consists of Worthian iron, no grain steel, fat or fine material (4). Miscellaneous, non-recorded steel may include more than about 1% by weight 'better than about 13 More than about 15 weight percent, and more preferably greater than about 5% by weight concentration of chromium. The unrecorded steel may comprise less than about (four) weight percent, preferably less than about 0.15 weight percent, more preferably less than about Q 12 weight percent. And preferably less than about 0.10 weight percent carbon. For example, a stainless steel 3〇4 (SAE code) containing 19 weight percent/knife ratio chromium and about 0.08 weight percent carbon. Suitable stainless steel also includes molybdenum. Stainless steel such as 316 (SAE code). There may be any conventionally known coating that eliminates or reduces the stagnation of the metal sheet. The metal sheet has a high enough thickness to form a sheet, when the pouch is filled with a thermal energy storage material, and during use of the pouch. Or any combination thereof will not form holes or cracks. For applications such as transportation, the metal sheet is preferably relatively sturdy, so that the weight of the heat storage device is not greatly increased by the metal sheet. The thickness of the metal sheet can be greater than about ΙΟμπι Preferably, it is greater than about 2 (^m, and more preferably greater than, scoop 50 μηι. The metal tantalum may have a thickness of less than about 3 mm, preferably less than about 1 mm, and more preferably less than 0.5 mm (e.g., less than about 〇25 mm). Figure 8 shows a cross-section of an exemplary thermal storage device 80 having a plurality of articles 1 〇, and 1 〇", a plurality of articles 1 〇, and 1 〇", each having an envelope of a plurality of The heat energy storage material 26 in the sealed space 14. The object is disposed in the insulated container 82 which may have a substantially cylindrical shape. The apparatus includes a first adjacent object, '(a) and a first Two adjacent objects 50 201144705 Η),》 Its object ⑽ first object 1〇 ,, - adjacent item i (), "is set so that it covers each of the flat sheet ⑽ _ surface (i.e. outer surface) takes the form of contact. The object 10" and the second adjacent material _,, (b) may have surfaces that are generally butted (for example, the outer surface of each of the respective base sheets may be a surface that is generally butted) and may be configured to partially embed Sleeve together. A spacer (not shown) can be used to maintain a distance between the object 10" and its second adjacent object 10, (b), so that the heat transfer fluid can be in the two objects 10" And l〇,, between (b) in a radial direction, a radial flow path 83. The object 10, and the space between the second adjacent object 丨〇,, (b) Transferring the portion of the fluid compartment for heat. As shown in Figure 8, each item may have a surface that contacts the heat transfer fluid compartment (e.g., a surface of the substrate sheet) so that the heat transfer fluid can be in direct contact with each The article is preferably in direct contact with each sealed space. As shown in Fig. 8, each radial flow path μ may have the same length, the same cross section 'or even may be congruent. Each object has an opening close to its center. The opening is also part of the heat transfer fluid compartment. The objects 10" and 10, are configured such that Forming a central axial opening flow path 84. The space between the outer periphery of the articles 10" and 10" and the inner surface of the container 85 is also part of the heat transfer fluid compartment and forms an outer axial flow path 86. The heat storage device has a first orifice fluidly coupled to the central axial flow path 84. The heat storage device can have a first seal or plate 88 that separates the first orifice 87 from the outer axial flow path 86. The container 82 has a second aperture 89' which may be located on the side of the same container as the first aperture 87, or on a different side of the container, as shown in FIG. The heat storage device can have a second seal 90' that separates the second orifice 89 from the central axial flow path. The first seal, the second seal, or both prevent a fluid from flowing between the two axial flow paths 51 201144705 84 and 86 without flowing through a radial flow path 83. Referring to Fig. 8, a fluid flowing between the first orifice 87 and the second orifice 89 must flow through a portion of the central axial flow path 84 and through a portion of the outer axial flow path 86. The heat transfer fluid must also flow through one of the radial flow paths 83 between the two axial flow paths 84,86. Preferably, the size of the two axial flow paths is such that the hydrodynamic resistance of the fluid is substantially constant regardless of which radial flow path is used for a portion of the fluid. Therefore, the heat transfer fluid flow through the heat storage device is preferably a Tichelmann system. The container 82 is preferably insulated. For example, the container can have an inner wall 91 and an outer wall 92, and the space 93 between the two walls can be emptied. The device may also have one or more springs, such as one or more compression springs 94, that apply a compressive force to the stack of objects. Figure 9 shows a heat storage device 80' having two apertures 87' and 89' on one side of the container. The apparatus can employ a tube 95 coupled to the first orifice 87 for flowing fluid between the first orifice and a zone 96 furthest from the central axial flow path 84 of the first orifice. Referring to Fig. 9, the first sealing member 88' and the second sealing member 〇 can be used to prevent a fluid from flowing through a radial flow path 83, i.e., from the first orifice 87 to the second orifice 89. . Again, by selecting the dimensions for the two axial flow paths 86 and 84', the heat storage device 80 of Figure 9 can be characterized by a Tichelmann system. Thermal Storage System The thermal storage device can be used in a thermal storage system that uses one or more heat transfer fluids to transfer heat into the thermal storage device to transfer heat out of the thermal storage device. 52 201144705 Heat transfer fluid / working fluid Used to transfer heat into and/or out of heat storage. The transfer fluid may be any liquid or gas that causes the fluid to flow through the heart and flow through it. < "For example - a thermal read supply assembly, one or more connection tubes or a line removal assembly, or any combination thereof." The heat transfer fluid may be any technology capable of nuclear storage device wipes with temperature (four). Volume = fluid or cold (4). The heat transfer read can be - liquid or gas: = (iv) The transfer fluid can flow at the lowest operating temperature (eg, the lowest expected ring chamber temperature) that may be exposed during use. For example, helium fluid At a pressure of about 1 atm and about pit, preferably about, better and most preferably. (: at a temperature, it can be a liquid or a gas. Without limitation, for heating and/or cooling one or more The preferred heat transfer fluid system of the electrochemical cell is about 4 liters. The heat transfer fluid should be capable of transporting a large amount of thermal energy that is typically sensible heat. Suitable heat transfer fluids can have at least about 1 J/gK, #交佳至约约2J/gK, even more preferably at least about 25J/gK, and preferably at least about a specific heat of tearing & (e.g., measured at about 25t). Preferably, the heat transfer stream system is a liquid. For example, any art cooling can be used. As a heat transfer fluid, the system preferably employs a single heat transfer fluid for transferring heat into the thermal energy storage material in the human heat storage device and removing heat from the thermal energy storage material in the heat storage device. a second heat transfer fluid for transferring heat to the thermal energy storage (4) - a heat transfer fluid and a second heat transfer fluid for removing heat from the thermal energy storage material - including a 53 201144705 first heat transfer fluid and a second heat transfer In a fluid system, a first heat transfer fluid system flows through a first heat transfer fluid compartment and a second heat transfer fluid flows through a second heat transfer fluid compartment, wherein the heat transfer fluid compartment is summarized by a relatively low Thermal conductivity material, such as thermal energy storage material, is separated. For example, at least 20%, at least 50%, or at least about 80% of the surface area of the first heat transfer fluid compartment may be in contact with or be the surface of the article containing the thermal energy storage material. This is in contrast to a heat exchanger in which the two heat transfer fluids are in relatively good thermal conduction. The heat transfer fluid system, which may be used alone or in a mixture, includes heat transfer fluids well known to those skilled in the art and preferably includes water, one or more alkylene glycols, one or more polyhydrocarbons. a fluid of a diol, one or more oils, one or more refrigerants, one or more alcohols, one or more betaines, or any combination thereof. The heat transfer fluid can be added or replaced, for example, for the fluids described above. Means) comprises, or consists essentially of, a working fluid such as the following. Suitable oil systems which may be employed include natural oils, synthetic oils, or combinations thereof. For example, the heat transfer fluid may contain or consist essentially of the following items (e.g., at least 80 weight percent, at least 90 weight percent, or at least 95 weight percent): mineral oil, castor oil, alumite oil, fluorocarbon oil, or any combination thereof. A particularly preferred heat transfer stream system comprises, or consists essentially of, one or more olefinic diols. Non-limiting, preferred olefinic diols include from about 1 to about 8 alkylene oxy groups. For example, the olefin diol can include an olefinoxy group containing from about 1 to about 6 carbon atoms. The olefinoxy groups in the monoolefin diol molecules may be the same or may be different. Alternatively, 54 201144705 an olefin diol may comprise a divalent group of different olefins having different fluorenyloxy groups or different ratios including an epoxy group, a preferred olefin oxy group (IV) and Epoxy Institute. Alternatively, it can be replaced. For example, a 'smoke diol can be - or two alkyl groups or one alkyl group containing from about 1 to about 6 carbon atoms is substituted by a thiol (IV) including - or a plurality of olefin diols. Gexi diol diol dialkyl ether, or a combination thereof, or a solid f. (4) A preferred diol group which may include a lysine diol includes B-leano'diethylene glycol propylene glycol, and butylene glycol. Any of the above ethylene glycols may be used alone or in a mixture. For example, ethylene glycol can be used as a mixture with water. (d) a bulk transfer stream - comprising substantially (for example, at least 8% by weight or at least 96% by weight based on the total weight of the heat transfer fluid) or entirely composed of a mixture of ethylene glycol and water mixture. Preferably, the concentration of water in the conjugate is greater than about 5 weight percent, more preferably greater than about 5% by weight, even more preferably greater than about 15 weight percent, and most preferably greater than about 20 weight percent, based on the total weight of the heat transfer fluid. The concentration of water in the mixture is preferably less than about "weight percent, more preferably less than about 90 weight percent", even more preferably less than about weight percent, and most preferably less than about 80 weight percent. The concentration of ethylene glycol in the mixture is greater than the heat transfer fluid. Preferably, the total weight is greater than about 5 weight percent, more preferably greater than about 10 weight percent ' even more preferably greater than about 15 weight percent, and most preferably greater than about 20 percent. The ethylene glycol concentration in the mixture is preferably less than about 95 weight percent. More preferably, it is less than about 90% by weight, even more preferably less than about 85% by weight, and most preferably less than about 80% by weight. 55 201144705 Selectively, the entire area of the county is made up of 复 咏 玉 玉 玉 玉 玉 玉 或 或For example, the system may include a working fluid, ι#, Αι9Λ flowing through the heat storage: the enthalpy fluid causes the workpiece fluid to be condensed and heated to the one or more heat storage devices: a component (eg, will be heated) Component). Therefore, the heated _ can act on the evaporator of the working fluid, and the one that will be used as the fluid, is supplied to the condensate: the condenser of the fluid.埶 。 / / / / / / / / / / / / / / / 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 工作 工作 工作 工作 工作The heat circuit, the line and the heat circuit for removing the working fluid are preferably capable of being enclosed when the working fluid flows through the primary circuit. When the heat storage device (such as the heat energy storage material in the heat storage device) is sufficient to cause When the combined vapor pressure of all components of the fluid exceeds one of the temperatures of about 1 atmosphere and the valve is opened to allow the working fluid to flow, the operating fluid may a) be delivered by the capillary structure; b) be at least partially vaporized; Being at least partially transported to the condenser; and ... at least partially condensing in the condenser; thereby removing the load from the heat storage device. Thus, the system optionally includes a capillary feed circuit. The fluid working fluid may be any fluid that can be shouted (converted from liquid to gaseous) in the hot (four) storage device portion when the fines are at or above their liquidus temperature. Appropriate workflow (for example, for capillary delivery circuits) is a pure substance and mixture that has the following characteristics - or any combination: good chemical stability at a maximum temperature, low viscosity (eg less than about 1 〇〇) mPa.s), good capillary structure ^ 56 201144705 Wetting (for example, good wicking and wetting), materials with capillary pumping circuits (such as container materials, materials used to encapsulate thermal energy storage materials, vapor and liquid lines) The chemical compatibility of materials, and the like (for example, the working fluid causes low corrosion), is beneficial to the temperature of the evaporator and condenser temperature due to the denatured vapor pressure, vaporized high volume latent heat (for example, in millions of joules) The product of the latent heat of fusion per unit of liter and the density of the working fluid at about 25 ° C may be greater than about 4 MJ / liter), less than or equal to the freezing point of the freezing point of the heat transfer fluid of the condenser (for example, less than or equal to frost resistance) The freezing point of the freezing point of the agent, or a freezing point of less than or equal to about -40 °C. For example, the equilibrium state of the working fluid can be at least 90 percent liquid at a temperature of -40 ° (: and 1 atmosphere). Without limitation, an exemplary working fluid can include one or more alcohols, one or more ketones. One or more hydrocarbons, monofluorocarbons, monofluorocarbons (such as a conventional hydrofluorocarbon refrigerant, such as a conventional hydrofluorocarbon automotive refrigerant), water, ammonium, Or substantially any combination thereof. The working fluid should have a high vapor pressure in the evaporator to produce a vapor stream sufficient to pump the working fluid. Preferably, the vapor pressure of the working fluid is in the evaporator. High enough to generate a vapor stream that carries the ideal thermal power measured in watts from the evaporator to the condenser. The vapor pressure of the working fluid in the evaporator is preferably sufficiently low that the capillary pumping circuit does not leak and The working fluid is wetted to the capillary structure and may be characterized by a contact angle on the material of the capillary structure. Preferably, the contact angle is less than about 80°, more preferably less than about 70°, even better. Less than about 60°, and optimally less than about 55. 57 201144705 The working fluid preferably condenses at a moderate ink force below about (iv). For example, the working body can condense at less than about 9g °c. Preferably, it is less than about 0.8 MPa, more preferably less than about G 3 MPa, even more preferably less than a pressure of sharpening & and preferably less than about 0.1 MPa. The working fluid is preferably at a low cost. For example, Wei Zuo The fluid can be exposed to a very low ring chamber temperature and preferably can be condensed from a coagulated filament at a temperature of about, preferably about 1, 1 C, more preferably about -25 X:, even better, about _ thief, and optimally about Russian. The heat storage device. Wei Zuo (4) minus # is in a gaseous state at the temperature of the fully charged thermal storage device. For example, the working fluid can have a phase transition temperature lower than that of the energy storage device in the heat storage device at 1 atmosphere. Preferably, the Buddha point preferably has a phase transition temperature of at least 2 G ° C less than the thermal energy storage material, and is preferably at least less than the phase transition temperature of the thermal energy storage material. In various aspects of the invention, it may be desirable to The fluid has the following boiling point at 1 atm (or, to make the fluid The temperature at which the component is combined with the vapor pressure of 1 atmosphere may be greater than about thief, preferably greater than about 35t, more preferably greater than about 耽, even more preferably greater than about, and preferably greater than about 70 °C (eg, working fluid) In the different conditions of the present invention, the boiling point of the working fluid at i atmosphere may be (or the temperature of all components of the working fluid combined with the vapor pressure equal to the atmospheric pressure may be less than about 18 (TC, preferably less than about 15 (rc, more preferably less than about 12 ° C, and most preferably less than about 95. (-: - The better work includes water and recording, or real f consists of it. For example, the water in the working fluid and the combined concentration may comprise at least about 80 weight percent of the total weight of the working fluid, more preferably at least about 9 weight percent and 58 201144705 is preferably at least about 95 weight percent water and recorded. The ammonium may have a sufficient concentration to maintain the boiling point of the working fluid below the boiling point of water (e.g., at least 10 C below the boiling point of water). The concentration of ammonium can be greater than about 2 weight percent, preferably greater than about 1 weight percent, more preferably greater than about 5% by weight, and most preferably greater than about 18 weight percent, based on the total weight of the working fluid. The concentration of ammonium can be less than about 80 weight percent, preferably less than about 6 weight percent, more preferably less than about 40 weight percent, and most preferably less than about 30 weight percent, based on the total weight of the working fluid. The concentration of water in the working fluid may be greater than about 2 weight percent, preferably greater than about 40 weight percent, more preferably greater than about 6 weight percent, and most preferably greater than about 70 weight percent, based on the total weight of the working fluid. The concentration of water in the working fluid may be less than about 98 weight percent, preferably less than about 95 weight percent, more preferably less than about 90 weight percent, even more preferably less than about 85 weight percent, and most preferably less than about 82 weight percent of the total weight of the working fluid. Weight percentage. For example, a solution of about 21 weight percent ammonium and about 79 weight percent water has a liquidus point of about -40 c and an upper limit of less than about 10 (the boiling range of rc at atmospheric pressure. Stored in an unpressurized vessel at room temperature (in a liquid). Preferably, the working fluid has a combined vapor pressure of all of its components equal to 1 atmosphere at a temperature from about 〇 to about 25 Torr. The working fluid is capable of efficiently transferring thermal energy from the heat storage device to remove a small amount of working fluid from the heat storage device - the amount of working fluid is relatively small (for example, compared to H, which is not a heat transfer fluid of the working fluid) Preferably, the heat transferred by the turbine fluid is - mostly transferred in the form of heat of vaporization. Compared to - employed - is not a working heat transfer fluid of the working body of 2011. For systems of the same initial power, the volume of the working body, the flow rate of the working fluid, or both may be relatively low in thermal energy storage. The container of the heat storage device per liter of working fluid (ie, inflow) The flow rate of the storage device in the (four) servant fluid can be less than the scoop liter/knife 4 and the car traverse is less than about 2 liters/min, more preferably less than about aliquots, and even more preferably less than 5 liters/ Minutes, and optimally less than · w minutes. The volume of working fluid in the system should be sufficiently low for the total volume in the container of the heat storage device, or for the volume of the reduced storage (four) in the heat storage device, so that the total weight of the system is not The weight of the fluid is excessively impacted. The ratio of the total volume of the container in the system (for example, in the capillary pumping circuit) to the total volume of the container of the heat storage device (ie, the volume inside the container) (or even the system towel) The ratio of the volume of the fluid to the volume of the thermal energy storage material of the thermal device may be less than about 20; preferably less than about 1 Torr, preferably less than about 4, even more preferably less than about 2, and most preferably less than about 1. In the above, the working fluid can transfer part of the heat energy by vaporizing the heat of the heat. The working fluid preferably has a high heat of vaporization, so that a high amount of heat can be transferred. The appropriate working fluid for the heat storage device can have more than about 20 0kJ/mole, preferably greater than about 500kJ/ mole, more preferably greater than about 75〇kJ/ mole, even more preferably greater than about 1000kJ/ mole and most preferably greater than about 12〇〇kJ/ mole of heat of vaporization. In applications less than 〇C, the working fluid is preferably not water (such as 'not freezing the working fluid, causing fracture, or both.) It will be appreciated that the material in contact with the working fluid is resistant to corrosion from the working fluid. 'There may be contact with the working fluid's heat storage device or 60 201144705 , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , The surface of the fluid compartment, the inner surface of one or more valves, the condenser; the surface of one of the working fluid compartments, the inner surface of a working fluid reservoir, and the like) may be made of stainless steel. It will be appreciated that any working fluid or heat transfer fluid employed in the thermal energy storage devices described herein can include an add-on package. Such additive packaging systems are systems well known to those skilled in the art and suitable for use with the devices in which they may be invented. For example, the additive package can include a stabilizer, a corrosion inhibitor, a lubricant, an extreme pressure additive, or any combination thereof. Optional Heaters = The storage system optionally includes - or multiple heaters. The temperature of the thermal energy storage material in the heating storage device is increased. The energy can be repaired: 2::: heater. Heating _ is the conversion of (10) _, : 7 or any combination thereof into a hot electric heater. - or more than one heating _ is one or more... A heating benefit can be used to heat the heat storage device. Guide: 22 or 4 thermal energy storage. Preferably, the system includes - or a plurality of thermal conduction to a heat $ storage dream w #如, (4) may include in the ''', 里:子, the insulation _ or a plurality of twisters may be from ― Or more ',,, electric... or both. Xin is from an external source, the exit of the object, the capacity; / plugged eight-connected to - static storage device can be from the external source of electricity 201144705 force is maintained in the heat storage device thermal energy Stores one of the temperatures above the liquidus temperature of the material. When the carrier is not inserted into an outlet connected to a static object, the heat storage device can be maintained above the liquidus temperature of the thermal energy storage material in the thermal storage device by using electricity generated from an electrochemical cell. a temperature. The heat storage device can be used in a method for heating one or more components. The method can include flowing a heat transfer fluid through the heat transfer device. The step of flowing a heat transfer fluid through the heat storage device may include: flowing a heat transfer fluid having an initial temperature through an inlet of the device; causing the heat transfer fluid to flow through an axial flow path, so that the heat transfer fluid may Divided into a plurality of radial flow paths; the heat transfer fluid is passed through a radial flow path so that it can remove heat from the thermal energy storage material, wherein the thermal energy storage material has a temperature greater than one of the initial temperatures of the heat transfer fluid; The heat transfer fluid is caused to flow through a different axial flow path so that the plurality of radial flow paths can be recombined; the heat transfer fluid having an exit temperature is passed through an outlet of the apparatus; or any combination thereof. Preferably, the heat transfer fluid exits the temperature temperature greater than the initial temperature of the heat transfer fluid. The method for heating one or more components can employ a flow path through the heat storage device that includes one of a selection of radial flow paths and a biaxial flow path having a total flow length, wherein The total flow length is constant for different radial flow paths. The heat storage device and/or the heat storage system can be characterized by having a relatively high power (e.g., as measured during the initial 30 or 60 seconds of heating) so that it can rapidly heat a component, such as an internal combustion engine. The thermal storage device and/or the thermal storage system can be characterized by an average power greater than about 5 watts, preferably greater than about 10 watts, more preferably greater than about 15 watts, and most preferably greater than about 20 watts. The thermal 1 storage device and/or the thermal storage system can be characterized by having a relatively high power density so that it can accommodate a significant amount of thermal energy in a relatively small compartment. For example, the heat storage device and/or the heat storage system can be characterized by having a power density greater than about 4 kW/L, preferably greater than about 8 kW/L, more preferably greater than about 10 kW/L, and most preferably greater than about i2 kW/L. The heat storage device and/or the heat storage system can be characterized by a relatively low pressure drop of the heat transfer fluid (measured at a heat transfer fluid flow rate of about 10 L/min). For example, the heat storage device and/or the heat storage system may be characterized by a heat transfer fluid pressure drop of less than about 2.0 kPa, preferably less than about 1.5 kPa, more preferably less than about 1.2 kPa, and most preferably less than about 1.0 kPa. In an example, the thermal energy storage system can be used in a transport vehicle (e.g., a vehicle) to store energy from an engine exhaust. When the engine produces exhaust, a bypass valve directs the flow of gas through the heat storage device, causing the thermal storage device to be loaded or passed through a bypass line to prevent overheating of the thermal storage device. When the engine is stopped, for example, during a period of time when the vehicle is parked, a significant portion of the heat stored in the heat storage device can be retained for a long period of time (e.g., due to vacuum insulation surrounding the heat storage device). Preferably, at least 50% of the thermal energy storage material in the thermal storage device is still in a liquid state after the carrier has been parked for 16 hours at a ring chamber temperature of about -40 °C. If the vehicle is parked for a long period of time (such as 'at least two or three hours') to cool the engine substantially (for example, to make the temperature difference between the engine and the ring chamber less than about 2 ° C), a heat of 63 201144705 can be used. A transfer fluid (such as an engine coolant) flows through a heat exchanger including a condenser for the work fluid, such that the heat stored in the heat storage device is indirectly discharged into the cold engine or other heat receiver. . The utility model utilizes a capillary structure inside the heat storage device for vaporizing the working fluid in the state, and the working fluid and the working fluid flow into the capillary pumping circuit. Heat from the working fluid is transferred to the engine coolant in the heat exchanger. Using the heat storage left kiss 1 device, you can extract the heat that was originally wasted during a previous trip, and #Α from mitigating the cold start and/or providing immediate seat heating. - heat for storing heat, such as heat from the exhaust of the vehicle. (4) The storage system may include some or all of the features shown in Fig. 10. The storage system 100 includes a heat storage device 101. Thermal energy storage = a heat exchanger or condenser 102 having a first population 117 and a first outlet 117 for the first heat transfer fluid for the heat transfer fluid. The thermal energy storage system may have a tube (e.g., _ line) (1), and the tube 113 connects the first heat transfer fluid inlet Hi of the hot parent converter 1〇2 to the first heat transfer fluid outlet of the heat storage device 101. The thermal energy storage system 100 can have a tube (10) to which the first heat transfer fluid outlet of the bay heat exchange is connected to the first heat transfer fluid inlet of the heat storage device ωι. The first heat transfer fluid 107 flows through a first heat transfer fluid compartment of the heat storage device ι〇ι. [The heat transfer fluid can flow through the heat exchanger 102 - the first heat transfer is separated by the n heat transfer fluid can be a working grab mass storage device 101 to the heat exchange II1G2 line system can be - steam line, heat exchanger (10) The first thermal transfer fluid compartment may be a working fluid compartment. Thus, 64 201144705 thermal energy storage system 100 can include a capillary pumping circuit including a working fluid compartment in a heat storage device, a working fluid compartment in a condenser, a working fluid vapor tube 109, and a working fluid liquid tube 113. The thermal energy storage system also includes one or more heat transfer fluids or working fluid reservoirs 110. When used in a capillary pumping circuit, the reservoir 110 preferably has a filling level that is higher than the working fluid inlet of the heat storage device 101 and lower than the working fluid outlet 117 of the condenser, the condenser Working fluid inlet 111, or both. Thermal energy storage system 100 can include a valve 118 to regulate a first heat transfer fluid stream in tube 113 for connecting heat storage device 101 and heat exchanger 102. For example, valve 118 can be utilized to prevent the transfer of heat transfer fluid when the heat storage device is being loaded and while the heat storage device is storing heat. Valve 118 can be opened when it is desired to dissipate heat from the heat storage device. Referring again to Fig. 10, the thermal energy storage system can include a heat transfer fluid inlet line 108 and a heat transfer fluid outlet line 106 for a second heat transfer fluid to flow into and out of the heat storage device 101. The thermal energy storage system can also have a heat transfer fluid bypass line 105 and a steering valve (such as a bypass valve) 104 to divert some or all of the second heat transfer fluid to the bypass line 1〇5 (eg, when heat When the storage device is fully loaded, or when the temperature of the second heat transfer fluid is lower than a temperature of the thermal energy storage material in the heat storage device 101). The thermal energy storage system can also include a cold line 116 for providing another heat transfer fluid to the heat exchanger, and a heat line 115 for removing the heated heat transfer fluid from the heat exchanger 102. Cold line 116 and heat line 115 are part of a heat transfer fluid circuit 114. The heat transfer fluid circuit 114 can contain an engine cooling 65 201144705 agent. The heat transfer fluid circuit 114 can be coupled to an internal combustion engine 103. Thus, thermal energy storage system 100 can utilize an energy stored in thermal storage device 101 to heat an internal combustion engine 103. The transfer of heat from the working fluid can be initiated by opening the working fluid valve (i.e., the discharge valve). A sealed working fluid reservoir connected to the circuit via an additional liquid line can be used to accommodate changes in the volume of working fluid liquid inside the circuit without substantial pressure changes. The discharge valve can be closed once sufficient or all of the effective heat has been transferred from the heat storage device. The remaining working fluid system in the heat storage device can evaporate (e.g., from the heat retained in the heat storage device or when the heat storage device begins to charge) and then condense in the condenser. When the heat storage device becomes emptied of the working fluid, the level of the liquid at the working fluid level may change (e.g., rise). The heat storage device can optionally be a cross-flow heat exchanger (i.e., having a flow direction for the working fluid and a vertical flow direction for the exhaust flow). For example, during operation, the heat storage device can include three chambers occupied by: 1) exhaust; 2) stagnant phase change material (eg, inside the pocket, such as a blister pack); and 3) Working fluid. All three chambers are separated by a thin wall of a suitable material, preferably stainless steel. The exhaust gas may flow between the surface of the pocket of the phase change material inside the blister (such as a curved surface), and the working fluid may flow in a direction perpendicular to the direction of the exhaust flow to the inside of the blister. Between different surfaces of the bag of material (such as a flat surface). The liquid working fluid entering the chamber preferably wets a capillary structure (such as a metal wicking member) and acts against the gravity and steaming by the capillary force acting on the meniscus of the working fluid liquid formed on the inside of the capillary tube. The combined power is carried up. This flow is maintained by continuous evaporation of the liquid using the heat extracted from the phase change material inside the blister. The vapor of the working fluid exits the capillary structure and escapes to the top of the device via a vapor path between the capillary structure columns that are squeezed between the surface of the bladder (such as a flat surface) that may be interlaced with the phase change material on the inside of the blister. . The vapor of the working fluid flows into the condenser where it transfers its heat of vaporization and sensible heat to the cold coolant and again becomes liquid to return to the heat storage device and continue its circulation in the circuit, only by being present Capillary forces on the inside of a capillary structure (such as a metal wicking) that is partially impregnated by a liquid working fluid are pumped. All of the columns of the capillary structure can be joined to a common porous substrate. This porous substrate can be utilized to distribute the liquid working fluid entering from the bottom of the unit to different columns. Still further, the invention may be combined with additional components/components/steps. For example, an absorption or adsorption cycle refrigeration system for an air conditioner may be used as a heat receptor for the addition or replacement of a cold coolant (for example, a condenser may also be used as an evaporator for the refrigerant to circulate to an air conditioner. Inside the fluid circuit of the device). In another application, a steady-state waste heat recovery system using a thermal engine such as a Rankine cycle can be constructed to utilize the same or different capillary pumped circuit working fluids and add a mechanical power generating turbine. A vapor line to the heat storage device and the condenser (for example, to overcome high vapor pressure from upstream of the turbine), and/or a liquid pump is added to the liquid line between the condenser and the heat storage device. The turbine can convert a portion of the exhaust heat from the exhaust into effective mechanical or electrical power and thereby improve the overall fuel efficiency of the vehicle. 67 201144705 While the invention may be susceptible to various modifications and alternatives, the exemplary embodiments discussed above are shown by way of example. However, it should be understood that the invention is not intended to be limited to the particular embodiments disclosed herein. In fact, the technology of the present invention covers all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined by the appended claims. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1A is a diagram of an exemplary article having one or more sealed compartments and a fluid passage; FIG. 1B is a diagram of an exemplary article having a plurality of segments, Each segment contains one or more sealed compartments configured to provide a fluid passage for the article; Figure 2A is a diagram of an exemplary article having a sealed compartment and a fluid passage; Figure 2B Is a pattern that can be used for an exemplary cover sheet having one of the fluid passages in the article; FIG. 2C is a cross-sectional view of an exemplary article, such as the object shown in FIG. 2A; FIG. 2D is a usable A cross-section of an exemplary embossed base sheet in an article; Figure 3A is a side view of two exemplary adjacent segments that can be used in an article, the segments can have a generally butted edge; The figure is a side view that can be used for two exemplary adjacent segments in an object, the segments can have a generally butt edge; Figure 4 is a segment of one of which is shifted such that the segments are adjacent End table 68 201144705 When the faces are on different parallel planes, along the edge Side view of adjacent sections of the edge butt joint; Figure 5A is a diagram of an exemplary embossed base sheet that can be used in a plurality of articles having a plurality of sealed compartments containing thermal energy storage material having a plurality of grooves Figure 5B is a diagram of an exemplary portion of the embossed sheet of Figure 5; Figure 5C shows an exemplary stack of articles having corresponding fluid passages; Figure 6A is one with one or more A pattern of an exemplary object of the surface, the one or more surfaces comprising a plurality of grooves extending from the opening to the outer periphery; and FIG. 6B is a bottom surface of the first object and a top surface of the second object A pattern of interfaces between a plurality of surfaces having a plurality of curved grooves; Figure 6C is a diagram of two segments of an exemplary object; and Figure 6D is a stack of segments of Figure 6C. Side view of the body; Figure 7 is a top plan view showing an exemplary article having a top surface that is non-circular and/or has a non-circular opening; Figure 8 shows an exemplary heat storage a cross section of the device comprising a container A stacked body; FIG. 9 is a cross section of another exemplary apparatus of the heat storage, which includes a stacked body of a container object; FIG. 10 is a graph showing an exemplary schematic of a thermal energy storage system configuration of features. 69 201144705 [Description of main component symbols] 2', 2", 2'"··· Section 3···Proportional segmentation 4..·Top surface of the capsule structure 4', 6'... segmented surface 6··· The bottom surface of the capsule structure 8··· The outer edge surface of the capsule structure 9···The abutting edge of the first segment 10,10′...the capsule structure, the object 10”,10′”...object 12... encapsulant material 14... sealed space 15... radial groove 16... object, fluid passage, opening 18, 41... top surface 19... outer perimeter 20... bottom surface 21, 47... opening perimeter 22... side surface 23 Area 24 of the outer periphery 19 on the bottom surface 38... edge surface 26... thermal energy storage material 27... unfilled volume 28... cover sheet 29, 31, 46... opening 30... base sheet 32... outer ring 38... cover sheet The bottom surface 40, 40', 40" of the bottom surface of the sheet 40' is formed. The bottom surface 41 of the formed sheet 40' is formed on the bottom surface 43, 43'·· Slot area 44, 44'... lip area 45, 45'... outer periphery 46'... fluid passage 48... opening surface 49... generalized arched side surfaces 50, 50', 50", 50'"... Slot 51···concave Defect 52... gap 53...groove 60,91···inner wall 62,92...outer wall 64...insulation layer 68,85...container 80...exemplary heat storage device 70 201144705 80',101...heat storage device 82··· Through the insulating container 83... radial flow diameter 84, 84'... central axial flow path 86... outer axial flow path 88... first seal, first seal 87, 87'... first orifice 89, 89' ...the second orifice 90,90'...the second seal 93...the space 94 between the two walls...compressed magazine 95,109...tube 96...zone 100···thermal energy storage system 102···heat exchanger or condenser 103...internal combustion engine 104."steering valve 105···heat transfer fluid bypass line 106···heat transfer fluid outlet line 107···first heat transfer fluid 108···heat transfer fluid inlet line 109...work Fluid vapor tube 110···heat transfer fluid or working fluid reservoir 111···first heat transfer fluid inlet 113··· working fluid liquid tube 114...heat transfer fluid circuit 115···heat line 116···cold Line 117···First exit 118.·· Valve 71

Claims (1)

201144705 七 '申請專利範圍: 一種物件,包含: 一囊狀結構’具有—或多個經密封空間,其中該等 經密封空間係包封—或多個熱能儲存材料; 其中該囊狀結構具有一或多個充分夠大的流體通 道以容許—熱4轉移流體流職—❹财體通道,及 當一熱量轉移流體接觸該囊狀結構時,該熱能儲存 材料係與該熱量轉移流體隔離。 2·如申請專利第1項之物件,其中該囊狀結構包括二 個成夠包封該熱能儲存材料之片,該等片具有—外周邊 且各片沿著該外周邊被密封性附接至彼此及/或至-或 多個額外的次結構且在其間形成該一或多個含有該等 熱能儲存材料之經密封空間。 3. ΐ申請專利範圍第2項之物件,其中該等片沿著該外周 邊且沿著其開口的邊密封性_至彼此。 4. 如申請專利範圍第1項之物件,其中該囊狀結構具有一 頂表面及一外周邊; 其中顧表面包括二或更多個溝槽,其各從該流體 伸至4外周邊且各提供該通道與該外周邊之間 的流體連接。 如申清專利範圍第1項之物件,其中 6亥囊狀結構具有ϋ表面及-第二外表面,該 囊狀結構具有由該第一外表面及該第二外表面之間的 平均分離所界定之一厚度; 72 5. 201144705 其中該囊狀結構充份夠薄以使熱量可被快速地轉 移出該一或多個經密封空間外; 該熱能儲存材料係為一具有大於約3 0 °C且小於約 350°C的一固體至液體轉換溫度之相變材料;及 該一或多個經密封空間在約2 5 °C的一溫度具有一 總内部體積,且該等經密封空間在約25°C的一溫度含有 熱能儲存材料的一總體積,其中該熱能儲存材料的總體 積對於該總内部體積之比值係為至少約0.50 ; 故該物件可儲存一大量的熱能。 6. 如申請專利範圍第5項之物件,其中該流體通道係接近 該第一外表面的幾何中心。 7. 如申請專利範圍第1至6項中任一項之物件,其中該物件 包括3或更多個經密封空間。 8. 如申請專利範圍第1至6項中任一項之物件,其中 該物件的外周邊包括一或多個凹缺,故當該等物件 的一堆積體被放置在一中空圓柱體中時,一熱量轉移流 體可流過由該等凹缺形成之空間; 該物件的厚度小於約1 cm,該物件具有大於約5cm 的一維度;及 該物件的一表面包括一或多個突件,故當複數個該 等物件被堆積時該等物件之間將具有一空間以供一熱 量轉移流體之流動。 9. 一種裝置,包括一容器及複數個如申請專利範圍第1至6 項中任一項之物件,其中該等複數個物件被堆積使得該 73 201144705 等物件的流體通道軸向地對準。 10. 如申請專利範圍第9項之裝置,其中 i)兩物件係對準於鄰接的該等兩物件之概呈扁平表 面,使得該等兩物件形成經密封空間的一軸向 層;或 Π)單一物件形成經密封囊袋的一軸向層;及 其中該裝置包括一熱量轉移流體流徑,其包括一經 過物件的該堆積體的流體通道之轴向流徑,一包括經密 封空間的相鄰軸向層之間的一空間之徑向流徑,及一包 括超過該等物件的外周邊之該容器内側的一空間之不 同的軸向流徑;及 經過該等物件的流體通道之該軸向流徑及包括超 過該等物件的外周邊之一空間之該軸向流徑係由該徑 向流徑所分離。 11. 一種用於從如申請專利範圍第9或10項之一熱量儲存裝 置移除熱量之方法,包括一使一熱量轉移流體流過該裝 置之步驟; 其中該使一熱量轉移流體流過裝置之步驟係包括: a. 使一具有一初始溫度的熱量轉移流體流過該裝置 的一入口; b. 使該熱量轉移流體流過一軸向流徑,故該熱量轉 移流體可被分入複數個徑向流徑中; c. 使該熱量轉移流體流過一徑向流徑故其可從該熱 能儲存材料移除熱量,其中該熱能儲存材料具有 74 201144705 大於該熱量轉移流體的初始溫度之一溫度; d. 使該熱量轉移流體流過一不同的軸向流徑,故複 數個徑向流徑可重新合併; e. 使具有一出離溫度的該熱量轉移流體流過該裝置 的一出口; 其中該熱量轉移流體出離溫度大於該熱量轉移的 初始溫度。 12. —種用於形成如申請專利範圍第1至6項中任一項之一 物件的方法,其中該方法係包括切割一基底片中的一開 口;浮雕一基底片使其具有一或多個槽;以一熱能儲存 材料充填一或多個槽;切割一覆蓋片中的一開口;及至 少沿著一外周邊及一開口周邊密封性附接該覆蓋片至 該基底片,藉以形成一具有一開口且包含一或多個含有 該熱能儲存材料的經密封空間之物件。 13. —種系統,包括一如申請專利範圍第9或10項之熱量儲 存裝置及一熱量轉移流體,其中該熱量轉移流體係熱性 導通於該一或多個經密封空間中的該熱能儲存材料。 75201144705 Seven' patent application scope: An object comprising: a capsule structure having - or a plurality of sealed spaces, wherein the sealed spaces are encapsulated - or a plurality of thermal energy storage materials; wherein the capsule structure has a Or a plurality of sufficiently large fluid passages to allow the heat transfer fluid to flow into the cargo passage, and when a heat transfer fluid contacts the bladder structure, the thermal energy storage material is isolated from the heat transfer fluid. 2. The article of claim 1, wherein the capsule structure comprises two sheets enclosing the thermal energy storage material, the sheets having an outer periphery and the sheets being sealingly attached along the outer periphery To each other and/or to - or a plurality of additional substructures and forming the one or more sealed spaces containing the thermal energy storage materials therebetween. 3. The article of claim 2, wherein the sheets are sealed to each other along the outer circumference and along the sides of the opening thereof. 4. The article of claim 1, wherein the capsule structure has a top surface and an outer perimeter; wherein the surface comprises two or more grooves each extending from the fluid to the outer periphery of each of the four A fluid connection is provided between the channel and the outer perimeter. The object of claim 1, wherein the hexagonal structure has a meandering surface and a second outer surface, and the capsule structure has an average separation between the first outer surface and the second outer surface. Defining one of the thicknesses; 72 5. 201144705 wherein the bladder structure is sufficiently thin to allow heat to be quickly transferred out of the one or more sealed spaces; the thermal energy storage material is one having greater than about 30 ° And a phase change material having a solid to liquid transition temperature of less than about 350 ° C; and the one or more sealed spaces having a total internal volume at a temperature of about 25 ° C, and the sealed spaces are A temperature of about 25 ° C contains a total volume of thermal energy storage material, wherein the ratio of the total volume of the thermal energy storage material to the total internal volume is at least about 0.50; thus the article can store a substantial amount of thermal energy. 6. The article of claim 5, wherein the fluid passageway is near a geometric center of the first outer surface. 7. The article of any one of claims 1 to 6, wherein the article comprises 3 or more sealed spaces. 8. The article of any one of claims 1 to 6, wherein the outer periphery of the article comprises one or more recesses, such that when a stack of the objects is placed in a hollow cylinder a heat transfer fluid can flow through the space formed by the recesses; the article has a thickness of less than about 1 cm, the article has a dimension greater than about 5 cm; and a surface of the article includes one or more protrusions, Therefore, when a plurality of such objects are stacked, there will be a space between the objects for the flow of a heat transfer fluid. A device comprising a container and a plurality of articles according to any one of claims 1 to 6, wherein the plurality of articles are stacked such that fluid passages of the articles such as 73 201144705 are axially aligned. 10. The device of claim 9 wherein i) the two articles are aligned with the generally planar surface of the adjacent two articles such that the two articles form an axial layer of the sealed space; or a single article forming an axial layer of the sealed bladder; and wherein the apparatus includes a heat transfer fluid flow path including an axial flow path through the fluid passage of the deposit of the article, one including the sealed space a radial flow path of a space between adjacent axial layers, and a different axial flow path including a space inside the container beyond the outer periphery of the articles; and a fluid passage through the objects The axial flow path and the axial flow path including a space beyond the outer periphery of the articles are separated by the radial flow path. 11. A method for removing heat from a heat storage device according to claim 9 or 10, comprising the step of flowing a heat transfer fluid through the device; wherein the heat transfer fluid flows through the device The steps include: a. flowing a heat transfer fluid having an initial temperature through an inlet of the apparatus; b. causing the heat transfer fluid to flow through an axial flow path, so the heat transfer fluid can be divided into plural a radial flow path; c. causing the heat transfer fluid to flow through a radial flow path such that it can remove heat from the thermal energy storage material, wherein the thermal energy storage material has 74 201144705 greater than an initial temperature of the heat transfer fluid a temperature; d. causing the heat transfer fluid to flow through a different axial flow path, so that the plurality of radial flow paths can be recombined; e. causing the heat transfer fluid having an exit temperature to flow through the device An outlet; wherein the heat transfer fluid exit temperature is greater than an initial temperature of the heat transfer. 12. A method for forming an article according to any one of claims 1 to 6, wherein the method comprises cutting an opening in a substrate sheet; embossing a substrate sheet to have one or more a slot; filling one or more slots with a thermal energy storage material; cutting an opening in a cover sheet; and sealingly attaching the cover sheet to the base sheet at least along an outer periphery and an open perimeter to form a An article having an opening and containing one or more sealed spaces containing the thermal energy storage material. 13. A system comprising a heat storage device according to claim 9 or 10 and a heat transfer fluid, wherein the heat transfer flow system thermally conducts the heat energy storage material in the one or more sealed spaces . 75
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KR20120139704A (en) 2012-12-27
WO2011094371A3 (en) 2012-08-09
BR112012017117A2 (en) 2017-10-03
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EP2529173A2 (en) 2012-12-05
US20120279679A1 (en) 2012-11-08

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