M298107 八、新型說明： 【新型所屬之技術領域】 本:ij作係為-種板式熱父換⑤之流體通道結構改良，尤指—種提供兩不同 -難线體’可依其越性質之碰，聰較合適不同錢容狀輕進行流 通’藉其有效提升兩不同特性流體其熱交換之效益，俾達具高熱傳之效能。 【先前技術】 • 按，—般板式熱交換器之流道分配結構（請參閱圖一所示），其中，係應用 組設於-板式熱交換器1之内部，主要係由複數片第一流向隔與第二流向隔 板12相對交錯疊設所構成，具複數個互不導通之一次流通道A及二次流通道B，又 該第-流_板11與第二流向隔板12上，係各別分佈有相等間距排列之凸部ιη 121及凹σριΐ2、122 ’使其—次流通道Α及二次流通道β間，分別形成有複數個 相同流量容積之流道Μ、B1，以供兩流體，相互於—次流通道級二次流通道b 之流道Al、B1間，進行熱交換之機制； .准’上述所揭露之結構，雖可提供兩流體於各職·、關，進行熱交換 之機制’然而於實際應用時，往往一次流通道A間之越與二次流通道B間之流 體’其所具之流體性質特性皆不相同’導致若於_流量容積之流道Μ,間流 動下勢必k成其熱父換之效显降低’進而需相對增力喊第—流向隔板η與第二 流向隔板12之數量’以提升整體熱交換之效益，致使整體所需成本亦相對的提升； 疋故’如何將上述缺失加以摒除’並提供—種可供流體依其流體性質之特 性’選擇較合妨同流量容積之通道進行麵，難有效提升熱錢之效益， 俾達具高熱傳之效能，進而降低整ϋ熱傳結構所需之成本，即為本賴作人所 欲解決之技術困難點之所在，因此研發創新此—種板式熱交換器之流體通道結 構改良。 M298107 【新型内容】 本創作主要目的麟了提供—種板式熱交換器之流體通道結構改良，豆主要 係由複數片第-流料板與第二流向導板相互疊設所構成，並於該等第一流向導 板與第二流向導板相互疊設間，交錯形成有具互不導通及不同流量容積之一次流 通道及二次流通道，如此，藉以提供兩不同特性之流體進行熱交換時，則可靜 流體性質之特性，選擇較合適之通道進行流通，使其有效提升兩不同特性流體其 熱交換之效益下，俾達具高熱傳之效能，以減少第一流向導板與第二流向導板之 >使用數量，進而降低整體結構所需之成本。 【實施方式】 為使貴審查員方便簡捷瞭解本創作之其他特徵内容與優點及其所達成之 功效能夠更為顯現，兹將本創作配合附圖，詳細說明如下·· (請參閱圖二麻）本_健供—難式熱交難之趙通觀構改良， 係細相對組設於-板式熱交換器2之内部，其主要亦係由複數片第一流向導板 21與第二流向導板22相互疊設所構成，具複數個互不導狀—次麵道級二次 流通道B，又該第-流向導板21與第二流向導板四上，係各別分佈排列有相等間 距之凸部2H、221及凹部212、222，俾使相對於一次流通道A及二次流通綱， 則分卿成有魏_同缝容狀流韻、m，以供兩㈣介f之流體，可相 互於-次流通道A及二次流通道B之流道W、扮間，進行熱交換之機制； 再者，本創作之主要技術特徵在於：該等第一流向導板21係以兩兩相接合之 方式’予以再分別與-第二流向導板22依序相互交錯疊設，使其該等一次流通道 △及二次流通道B於該板式熱交換器2之内部，交錯形成有具互不導通及柯流量 容積之機制；如此，藉以提供兩不曝性之流體(如··冷媒與水··等）進行熱交 M298107 換時，進可依該兩流體性質的特性，選擇較合適之通道進行流通（即冷媒流體係 可選擇流量容積較小之二次流通道B ;其次，水流體則可選擇流量容積較大之一 次流通道A)，使其有效提升熱錢之效益，俾賴板式熱錢齡具高熱傳之效 能下，藉以減少第-流向導板21與第二流向導板22之使用數量，進而 整體結構所需之成本； $ 一 此外’（請再參閱圖三所示）為本創作另一實施例示意圖，其中，本創作之主 要技術特徵在於：該等第一流向_21與第二流向導板22上，係各別分佈排列有 不相等間距之凸部2n、221及凹部212'222，並令該第一流向導础與第二流向 導減其凸簡卜221及凹職、222，係分別呈反向相對應，進達相對賊等 -人抓通道A及一次流通道⑽’分別形成有複數個不相同流量容積之流道μ、扮 ，即進一步達到該等-次流通道級二次流通道B於該板式熱交換器2之内部，交 錯形成有具互不導通及不同流量容積之機制；如此，藉以提供兩不同特性之流體 (如冷媒與水· •.等）進行熱錢時，料健兩越性_紐，選擇較合適 之通道進行流通（即冷驗難可選騎量容雜小之二魏通道H欠，水法 nr綠容積鼓之—讀猶A)，使财效提升錄錢之效益，俾^ ，藉以減少第-流_與第二流向導板 里柄可有效降低整體結構所需之成本； 相互主要_特徵，係於該等第—流向導板21與第二流向導紐 道Β，_以接供Ά成有具互不導通及不同流量容積之—次流通道级二次流通 擇較合、高之、雨、f兩不同4寺性之流體進行熱交換時，則可依其流體性質之特性，選 能，以減少ssr ’㈣細升㈣之w，输高熱傳之效 需之成本。 °功與第二流向導板22之使用數量，進而降低整體結構所 用性，茲與習用作一比較分析如下·· 為使本創作更力喝現㈣進步性與實 M298107 習用缺失： 1、 該一、二次流通道之流量容積均相等。 2、 無法因應不同特性之流體，其流體性質特性不同，而作通道之調配。 3、 需相對增加其第―、二流向隔板之數量，以提升整體熱交換之效益， 致使整體所需成本亦相對的提升。 本創作優點： 1、该一、二次流通道之流量容積具不相等之機制。 φ 2、可因應不同特性之流體，其流體性質特性不同，而作通道之調配。 3、可減少其第-、二流向導板之使職量，有效降健體結構所需之成本。 綜上所述，本創作在突魏前之技術結構下，確實已達到所欲增進之功效， 且也非熟悉該項技藝者所易於思及，再者，本創作申請前未曾公開，其所具之進 步性、實用性’顯已符合創作專利之申請要件，爰依法提出創作申請，懇請貴 局核准本件創作專利申請案，以勵創作，至感德便。 _ 惟上列詳細說明係針對本創作之—可行實施例之具體說明，該實施例並非 用以限制本創作之專利範圍，而凡未脫離本創作技藝精神所為之等效實施或變 更，均應包含於本案之專利範圍中。 【圖式簡單說明】 第圖係為一般板式熱交換器之流道分配結構意圖。 第二圖係為本創作板式熱交換器之流體通道結構第-實施例示意圖。 第三圖係為本創作板式熱交換器之流體通道結構第二實施例示意圖。 M298107 【主要元件符號說明】 1.. .板式熱交換器 12.. .第二流向隔板 112、122. ·.凹部 21.. .第一流向導板 211、221...凸部 A... —次流通道 Al、B1...流道 11.. .第一流向隔板 111、121···凸部 2.. .板式熱交換器 22.. .第二流向導板 212、222. ··凹部 B...二次流通道M298107 VIII. New description: [New technical field] This: ij is a kind of plate channel type hot father for 5 fluid channel structure improvement, especially the kind of providing two different - difficult line body can be based on its nature Touch, Cong is more suitable for different types of money to carry out the flow of circulation. 'By using it to effectively improve the heat exchange efficiency of two different characteristic fluids, the performance of high heat transfer. [Prior Art] • Press, the flow channel distribution structure of the plate heat exchanger (see Figure 1), where the application group is located inside the plate heat exchanger 1, mainly by the first piece The flow direction partition and the second flow direction partition plate 12 are arranged in a staggered manner, and have a plurality of primary flow passages A and secondary flow passages B which are not electrically connected to each other, and the first flow plate 11 and the second flow direction partition plate 12 , the convex portions ιη 121 and the concave σριΐ2, 122' respectively arranged at equal intervals are arranged such that a plurality of flow channels Μ, B1 of the same flow volume are formed between the secondary flow channel Α and the secondary flow channel β, respectively. For the two fluids, the mechanism of heat exchange between the flow passages A1 and B1 of the secondary flow passage b of the secondary flow passage stage is the same as that of the above-mentioned disclosed structure. Off, the mechanism of heat exchange' However, in practical applications, the flow between the primary flow channel A and the secondary flow channel B is often different from the fluid properties of the fluid flow. The flow path is sloppy, and the flow between the two will become a decrease in the efficiency of the hot father. In turn, it is necessary to increase the number of the flow-through partitions η and the second flow-through partitions 12 to enhance the overall heat exchange efficiency, so that the overall cost is relatively increased; therefore, 'how to eliminate the above-mentioned defects' And provide a kind of fluid for the characteristics of the fluid properties of the 'selecting the channel that is more suitable for the flow volume, it is difficult to effectively improve the benefits of hot money, and the high heat transfer efficiency, thereby reducing the heat transfer structure required The cost is the technical difficulty point for the person to solve, so the research and development of this type of plate heat exchanger fluid channel structure improvement. M298107 [New content] The main purpose of this creation is to provide a fluid channel structure improvement for a plate-type heat exchanger. The bean is mainly composed of a plurality of first-flow plates and second flow guide plates stacked on each other. When the first flow guiding plate and the second flow guiding plate are overlapped with each other, the primary flow channel and the secondary flow channel having mutually non-conducting and different flow volumes are alternately formed, so as to provide heat exchange between two different characteristics of the fluid. , the characteristics of the static fluid properties, the selection of a suitable channel for circulation, so as to effectively improve the heat exchange efficiency of the two different characteristics of the fluid, the high heat transfer performance of the 俾 to reduce the first flow guide and the second flow direction The number of guides used reduces the cost of the overall structure. [Embodiment] In order to make it easier for your examiner to understand the other features and advantages of this creation and the effects achieved, you can use this drawing with the drawings to explain in detail... (See Figure 2 The _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ 22 is formed by stacking one another, having a plurality of mutually non-conductive-secondary-stage secondary flow passages B, and the first-flow guide plate 21 and the second flow guide plate four are arranged at equal intervals respectively. The convex portions 2H, 221 and the concave portions 212, 222 are arranged to have a fluid flow of the Wei_the same slit-like rhyme, m, for the flow of the two (four) mediums with respect to the primary flow passage A and the secondary flow passage. The mechanism of heat exchange between the flow channels W and the flow paths of the secondary flow channel A and the secondary flow channel B; further, the main technical feature of the present invention is that the first flow guide plates 21 are two The two-phase joining method is further alternately arranged with the second flow guiding plate 22 in sequence. The primary flow channel Δ and the secondary flow channel B are internally formed in the plate heat exchanger 2, and a mechanism for mutually non-conducting and a volume of the flow volume is formed in a staggered manner; thereby providing two non-exposure fluids (eg, ·Refrigerant and water··etc.) When the heat exchange M298107 is changed, the inlet can be circulated according to the characteristics of the two fluid properties (ie, the refrigerant flow system can select the secondary flow channel B with a smaller flow volume; Secondly, the water fluid can select the primary flow channel A) with a larger flow volume, so that the utility of the hot money can be effectively improved, and the first flow guide plate 21 and the second flow direction can be reduced by the high heat transfer performance of the plate type hot money. The number of guides 22 used, and the cost required for the overall structure; $1' (please refer to FIG. 3 again) is a schematic diagram of another embodiment of the present creation, wherein the main technical features of the creation are: The first-stage _21 and the second-flow guide 22 are arranged with unequal-spaced protrusions 2n, 221 and recesses 212'222, and the first flow guide and the second flow guide are reduced. Bu 221 and a job, 222 The systems are respectively in opposite directions, and the corresponding thieves, etc. - the person grasping the channel A and the primary flow channel (10) respectively form a plurality of flow channels μ and different flow volumes, that is, further reaching the secondary flow channel level two The secondary flow channel B is internally formed in the plate heat exchanger 2, and has a mechanism of mutually non-conducting and different flow volume; thus, to provide two different characteristics of fluid (such as refrigerant and water, etc.) for hot money , material health two _ _ New Zealand, choose the appropriate channel for circulation (ie cold test difficult to ride the amount of small two Wei channel H owed, water law nr green volume drum - read still A), make money Effectively improve the efficiency of recording money, 俾^, in order to reduce the cost of the first-flow _ and the second flow guide sill can effectively reduce the overall structure; mutual main _ characteristics, tied to the first-flow guide board 21 The second flow guide 纽 Β , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , In the case of heat exchange, energy can be selected according to the characteristics of its fluid properties to reduce ssr (Iv) (iv) of fine L w, high thermal output for an effect of cost. The number of work and the second flow guide 22 are used to reduce the overall structure. The comparison between the work and the use of the second structure is as follows: · To make the creation more powerful. (4) Progressive and real M298107 Lack of use: 1. First, the flow volume of the secondary flow channel is equal. 2, can not respond to different characteristics of the fluid, its fluid properties are different, and the channel is deployed. 3. The number of the first and second flow barriers is relatively increased to enhance the overall heat exchange efficiency, resulting in a corresponding increase in overall cost. The advantages of this creation: 1. The flow volume of the first and second flow channels has an unequal mechanism. φ 2, according to different characteristics of the fluid, its fluid properties are different, and the channel is matched. 3. It can reduce the workload of the first and second flow guide boards and effectively reduce the cost of the body structure. In summary, this creation has indeed achieved the desired effect under the technical structure before the Wei Dynasty, and it is not easy for people who are familiar with the art to think about it. Moreover, this creation has not been disclosed before the application. The progressive and practical 'has been in line with the application requirements for the creation of patents, and the application for creation is submitted in accordance with the law. You are requested to approve the application for the creation of this patent to encourage creation. The detailed description above is a detailed description of the possible embodiments of the present invention, and is not intended to limit the scope of the patents of the present invention, and all equivalent implementations or changes that are not departing from the spirit of the present invention should be It is included in the patent scope of this case. [Simple description of the drawings] The figure is intended to be a flow channel distribution structure of a general plate heat exchanger. The second figure is a schematic view of the first embodiment of the fluid passage structure of the inventive plate heat exchanger. The third figure is a schematic view of a second embodiment of the fluid passage structure of the inventive plate heat exchanger. M298107 [Description of main component symbols] 1.. Plate heat exchanger 12... Second flow direction partition 112, 122. · Concave part 21.. First flow guide plate 211, 221... convex part A.. - Secondary flow passages A1, B1... Flow passages 11.. First flow direction partitions 111, 121 · · · convex parts 2. Plate heat exchanger 22.. Second flow guide plates 212, 222 ·· recess B... secondary flow channel