TW202234008A - A brazed plate heat exchanger - Google Patents
A brazed plate heat exchanger Download PDFInfo
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- TW202234008A TW202234008A TW111105889A TW111105889A TW202234008A TW 202234008 A TW202234008 A TW 202234008A TW 111105889 A TW111105889 A TW 111105889A TW 111105889 A TW111105889 A TW 111105889A TW 202234008 A TW202234008 A TW 202234008A
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- skirt
- port opening
- brazed
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0043—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
- F28D9/005—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0037—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the conduits for the other heat-exchange medium also being formed by paired plates touching each other
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/005—Arrangements for preventing direct contact between different heat-exchange media
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
- F28F3/042—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
- F28F3/046—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element the deformations being linear, e.g. corrugations
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/027—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
- F28F9/0273—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes with multiple holes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
- F25B39/022—Evaporators with plate-like or laminated elements
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2225/00—Reinforcing means
- F28F2225/08—Reinforcing means for header boxes
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
本發明是關於一種硬焊型板式熱交換器。更具體地,本發明是關於一種硬焊型板式熱交換器,該硬焊型板式熱交換器包含一疊多個熱交換器板,該多個熱交換器板具有一脊突和溝槽的圖案,以形成用於流體交換熱的多個板間隙,其中該多個熱交換器板設有多個端口開口及一裙部,該裙部至少部分地圍繞至少部分該板的一個端口開口延伸。此種板式熱交換器是用於為了各種目的在流體之間交換熱。舉例言之,此類型的熱交換器用於加熱或冷卻目的,例如在一熱泵或冷卻系統中。舉例言之,此類型的熱交換器用作一蒸發器或一冷凝器。The present invention relates to a brazed plate heat exchanger. More particularly, the present invention relates to a brazed plate heat exchanger comprising a stack of a plurality of heat exchanger plates having a ridge and groove. pattern to form a plurality of plate gaps for fluid exchange heat, wherein the plurality of heat exchanger plates are provided with a plurality of port openings and a skirt extending at least partially around at least a portion of a port opening of the plates . Such plate heat exchangers are used to exchange heat between fluids for various purposes. For example, heat exchangers of this type are used for heating or cooling purposes, such as in a heat pump or cooling system. For example, a heat exchanger of this type is used as an evaporator or a condenser.
多個板式熱交換器在先前技術中是已知的。此種已知的多個板式熱交換器包含用於流體交換熱的多個端口開口及多個板間隙。多個端口開口區域設置在多個端口開口周圍,從而實現所述多個端口開口與該多個板間隙之間的選擇性連通。此多個端口開口區域通常是平坦的且設置成彼此交替地接觸以提供與該多個板間隙的選擇性連通。該多個端口開口區域通常是環形的,圍繞該多個端口開口並設置成選擇性密封一相鄰熱交換器板的一端口開口區域,例如透過硬焊接合。Multiple plate heat exchangers are known in the prior art. Such known multiple plate heat exchangers include multiple port openings and multiple plate gaps for fluid exchange of heat. A plurality of port opening regions are disposed around the plurality of port openings to enable selective communication between the plurality of port openings and the plurality of plate gaps. The plurality of port opening areas are generally flat and arranged in alternating contact with each other to provide selective communication with the plurality of plate gaps. The plurality of port opening regions are generally annular, surrounding the plurality of port openings and arranged to selectively seal a port opening region of an adjacent heat exchanger plate, eg, by brazing.
已知圍繞多個端口開口設置多個裙部以為該流體之一者提供一入口通道。多個腔室在多個裙部與該多個板間隙之間形成。該入口通道透過該多個裙部中的多個孔洞和該多個板中的多個孔洞與該腔室和選定的多個板間隙連通。It is known to provide skirts around port openings to provide an inlet channel for one of the fluids. A plurality of cavities are formed between the plurality of skirts and the plurality of plate gaps. The inlet passage communicates with the chamber and selected plate gaps through holes in the skirts and holes in the plates.
對於部分應用,例如在使用一致冷劑作為該流體之一者的一熱泵應用中,該熱交換器必須能夠承受相對較高的壓力。如果承受高壓,硬焊型板式熱交換器的該多個端口開口區域往往會破裂。For some applications, such as in a heat pump application using a refrigerant as one of the fluids, the heat exchanger must be able to withstand relatively high pressures. The multiple port opening regions of the brazed plate heat exchanger tend to rupture if subjected to high pressure.
因此,先前技術之熱交換器的一個問題是它們很脆弱且不能承受高壓。Therefore, one problem with prior art heat exchangers is that they are fragile and cannot withstand high pressures.
先前技術之熱交換器的另一個問題是它們效率差。Another problem with prior art heat exchangers is that they are inefficient.
先前技術之熱交換器的另一個問題是它們的生產成本可能很高。Another problem with prior art heat exchangers is that they can be expensive to produce.
本發明的一個目的是減輕先前技術熱交換器的問題,以及提供一種具有良好的流體分佈的硬焊型板式熱交換器,這可以產生一種堅固且有效的硬焊型板式熱交換器。根據一些方面,該硬焊型板式熱交換器的生產相對容易且具有成本效益。根據本發明的另外一些方面,一種硬焊型板式熱交換器在各種條件下,例如在低流體流動條件下,具有良好的介質分佈。It is an object of the present invention to alleviate the problems of prior art heat exchangers and to provide a brazed plate heat exchanger with good fluid distribution, which results in a robust and efficient brazed plate heat exchanger. According to some aspects, the brazed plate heat exchanger is relatively easy and cost-effective to produce. According to further aspects of the present invention, a brazed plate heat exchanger has good media distribution under various conditions, such as low fluid flow conditions.
本發明是關於一種硬焊型板式熱交換器,包含一疊至少第一和第二熱交換器板,每個熱交換器板均有一包含脊突和溝槽的圖案,適於在相鄰的熱交換器板之間形成接觸點,使得該多個熱交換器板的多個板對形成交替的多個第一和第二板間隙,用於第一和第二流體在該多個熱交換器板上進行熱交換,其中該多個熱交換器板設有多個端口開口以形成用於該第一和第二流體的入口和出口通道,其中一板對中的該第一和第二熱交換器板之至少一者設有一裙部,該裙部至少部分地圍繞其第一端口開口延伸,以在該裙部和多個板間隙之間形成一腔室,且其中該腔室透過該板對的該第一和第二熱交換器板之一者中的一孔洞與該第一或第二板間隙連通,其特徵在於,該腔室透過該裙部的至少一個自由端部與一相鄰的熱交換器板之間的一間隙通向通道,且該間隙沿該通道的該周圍改變及/或該腔室的一橫截面沿該通道的該周圍改變。該自由端部或該裙部的該自由端與該相鄰的熱交換器板之間的該間隙變化及/或該腔室橫截面的變化導致良好的壓降和流體分佈以在該端口開口周圍分佈該壓力和該應力,並實現該流體從一入口通道均勻有效地流入該多個板間隙。控制該壓降和流體分佈進入該腔室及進一步進入該孔洞並因此進入該板間隙的可能性導致實現能夠承受高壓的一更強熱交換器的可能性。本發明提供了該入口通道中該流體更均勻的流動及改善的在其中的該流體的分佈,其中該熱交換器承受壓力的可能性隨著該裙部處該熱交換器板的壓力更大程度地分佈在其周圍而增加。該熱交換器可以包含在該裙部處的一徑向間隙及/或一軸向間隙,用於流體從該入口通道流到該腔室。該裙部以一偏離該熱交換器板之一平面的一角度延伸,例如通常垂直於該熱交換器板的平面,以形成該入口通道並且還形成該裙部與該多個板間隙之間的該腔室。The present invention relates to a brazed plate heat exchanger comprising a stack of at least first and second heat exchanger plates, each heat exchanger plate having a pattern of ridges and grooves suitable for use in adjacent Contact points are formed between the heat exchanger plates such that the plurality of plate pairs of the plurality of heat exchanger plates form an alternating plurality of first and second plate gaps for the first and second fluids to exchange heat between the plurality of heat exchanger plates heat exchange on heat exchanger plates, wherein the plurality of heat exchanger plates are provided with a plurality of port openings to form inlet and outlet passages for the first and second fluids, wherein the first and second fluids in a pair of plates At least one of the heat exchanger plates is provided with a skirt extending at least partially around its first port opening to form a chamber between the skirt and the plurality of plate gaps, and wherein the chamber passes through A hole in one of the first and second heat exchanger plates of the plate pair is in gap communication with the first or second plate, characterized in that the chamber communicates through at least one free end of the skirt with A gap between an adjacent heat exchanger plate leads to the channel, and the gap varies along the circumference of the channel and/or a cross-section of the chamber varies along the circumference of the channel. The change in the gap between the free end or the free end of the skirt and the adjacent heat exchanger plate and/or the change in the chamber cross-section results in good pressure drop and fluid distribution to the port opening The pressure and the stress are distributed around and uniform and efficient flow of the fluid from an inlet channel into the plurality of plate gaps is achieved. The possibility of controlling the pressure drop and fluid distribution into the chamber and further into the hole and thus into the plate gap leads to the possibility of realizing a stronger heat exchanger capable of withstanding high pressures. The present invention provides a more uniform flow of the fluid in the inlet channel and improved distribution of the fluid therein, wherein the likelihood of the heat exchanger being under pressure increases with the pressure of the heat exchanger plate at the skirt increase in degree distributed around it. The heat exchanger may include a radial gap and/or an axial gap at the skirt for fluid flow from the inlet channel to the chamber. The skirt extends at an angle offset from a plane of the heat exchanger plate, eg generally perpendicular to the plane of the heat exchanger plate, to form the inlet channel and also to form the gap between the skirt and the plurality of plate gaps of the chamber.
離該孔洞越近,該間隙越小,離該孔洞越遠,該間隙越大,使該流體分佈更良好。因此,該間隙的變化可以平衡該入口通道進入該腔室中的該流體分佈。舉例言之,該孔洞的前面沒有間隙。類似地,該腔室的橫截面可以在靠近該孔洞的一位置較小,而在圍繞該入口通道的一方向上遠離該孔洞的一位置較大,以平衡該流體到該腔室的分佈。因此,該腔室的體積圍繞該入口通道朝向該孔洞或包括多個孔洞的一截面減小,例如,使得該腔室的體積在該孔洞與最靠近該孔洞的該裙部部分之間最小。舉例言之,從該孔洞或孔洞的截面看,該腔室在穿過該入口通道的一部分較大。該腔室的橫截面是在該軸向方向的一截面,即,垂直於該板的平面。以下通常以一單孔洞為例。然而,可以使用包含多個孔洞的該熱交換器板的一截面。該孔洞可以是一限制孔洞。舉例言之,該孔洞的面積,或者如果使用多個孔洞,則該多個孔洞的總面積可以顯著小於該入口通道與該腔室之間的該開口的總面積,從而提供流量的限制。The closer to the hole, the smaller the gap, and the farther from the hole, the larger the gap, making the fluid distribution better. Thus, the change in the gap can balance the fluid distribution of the inlet channel into the chamber. For example, there is no gap in front of the hole. Similarly, the cross-section of the chamber may be smaller at a location close to the hole and larger at a location away from the hole in a direction around the inlet channel to balance the distribution of the fluid to the chamber. Thus, the volume of the chamber decreases around the inlet channel towards a cross-section comprising the hole or holes, eg such that the volume of the chamber is minimal between the hole and the skirt portion closest to the hole. For example, the chamber is larger in a portion passing through the inlet channel, viewed from the hole or the cross-section of the hole. The cross section of the chamber is a section in the axial direction, ie perpendicular to the plane of the plate. The following usually takes a single hole as an example. However, a section of the heat exchanger plate containing holes may be used. The hole may be a confinement hole. For example, the area of the hole, or if multiple holes are used, the total area of the plurality of holes can be significantly smaller than the total area of the opening between the inlet channel and the chamber, thereby providing flow restriction.
在一板對中的該第一熱交換器板可以設有一第一裙部,該第一裙部至少部分地圍繞該第一熱交換器板的該第一端口開口,且同一板對中的該第二熱交換器板可以設有一第二裙部,該第二裙部至少部分地圍繞該第二熱交換器板的該第一端口開口。在該第二裙部與該第一裙部的該自由端之間可以設置一徑向間隙。該第一和第二裙部可以實質上沿相反方向延伸。因此,該第一裙部可以提供一流暢的入口通道,其中該第二裙部可以防止流體分佈不均,且該第一和第二裙部可以一起為該腔室提供進入該腔室的不同間隙及/或該腔室的不同橫截面。The first heat exchanger plate in a pair of plates may be provided with a first skirt that at least partially surrounds the first port opening of the first heat exchanger plate, and the The second heat exchanger plate may be provided with a second skirt at least partially surrounding the first port opening of the second heat exchanger plate. A radial gap may be provided between the second skirt and the free end of the first skirt. The first and second skirts may extend in substantially opposite directions. Thus, the first skirt can provide a smooth inlet passage, wherein the second skirt can prevent fluid maldistribution, and the first and second skirts together can provide the chamber with differential access to the chamber gaps and/or different cross-sections of the chamber.
該第一熱交換器板的該第一端口開口可以小於該第二熱交換器板的該第一端口開口。因此,當該第一熱交換器板包含該第一裙部時,將該第一熱交換器板徑向地設置在該第二熱交換器板的該第一端口開口內,以提供該流體一流暢入口及良好分佈。該第一和第二熱交換器板的該多個第一端口開口可以具有一中心軸線,該中心軸線例如可以與該入口通道的中心軸線對齊或者可以相對於該入口通道徑向地偏移(即,偏心)。該多個第二熱交換器板的該多個第一端口開口可以相對於該多個第一熱交換器板的該多個第一端口開口以偏心的方式設置(即,徑向地偏移),使得該多個第一熱交換器板的該多個第一端口開口與該多個第二熱交換器板的該多個第一端口開口在該軸向方向上不對齊。或者,該第一和第二端口開口具有相似的尺寸及/或彼此對齊。因此,可以以一有效的方式實現該不同間隙及/或該腔室的不同橫截面。The first port opening of the first heat exchanger plate may be smaller than the first port opening of the second heat exchanger plate. Thus, when the first heat exchanger plate includes the first skirt, the first heat exchanger plate is radially positioned within the first port opening of the second heat exchanger plate to provide the fluid A smooth entry and good distribution. The plurality of first port openings of the first and second heat exchanger plates may have a central axis, which may be aligned with a central axis of the inlet passage, for example, or may be radially offset relative to the inlet passage ( That is, eccentric). The plurality of first port openings of the plurality of second heat exchanger plates may be disposed eccentrically (ie, radially offset) relative to the plurality of first port openings of the plurality of first heat exchanger plates ) such that the plurality of first port openings of the plurality of first heat exchanger plates and the plurality of first port openings of the plurality of second heat exchanger plates are not aligned in the axial direction. Alternatively, the first and second port openings are of similar size and/or aligned with each other. Thus, the different gaps and/or the different cross-sections of the chambers can be achieved in an efficient manner.
該多個第一熱交換器板設有圍繞該第一端口開口徑向地延伸的第一端口開口區域,且該多個第二熱交換器板設有圍繞該第一端口開口並接觸一相鄰熱交換器板之該第一端口開口區域徑向地延伸的第二端口開口區域,其中該第二端口開口區域可以設有與該第一端口開口區域不同的一尺寸。因此,可以以一有效的方式實現該不同間隙及/或該腔室的不同橫截面。舉例言之,該第一端口開口面積大於該第二端口開口面積及/或該第一和第二端口開口區域相對於彼此以偏心的方式設置,即,相對於彼此徑向地位移且在該軸向方向上不對齊。The plurality of first heat exchanger plates are provided with a first port opening area extending radially around the first port opening, and the plurality of second heat exchanger plates are provided with a first port opening around the first port opening and contact a phase A second port opening area extending radially adjacent the first port opening area of the heat exchanger plate, wherein the second port opening area may have a different dimension than the first port opening area. Thus, the different gaps and/or the different cross-sections of the chambers can be achieved in an efficient manner. For example, the first port opening area is larger than the second port opening area and/or the first and second port opening areas are arranged eccentrically relative to each other, ie, radially displaced relative to each other and at the Misalignment in the axial direction.
該第一及/或第二裙部可以設置成具有不同的長度、角度及/或形狀,以提供該不同間隙及/或不同的腔室橫截面。The first and/or second skirts may be provided with different lengths, angles and/or shapes to provide the different gaps and/or different chamber cross-sections.
本發明的其他特徵和優勢將從以下實施態樣的說明、附圖和申請專利範圍中變得顯而易見。Other features and advantages of the present invention will become apparent from the following description of embodiments, drawings and claims.
參考圖1,示意性顯示根據本發明一個實施態樣的熱交換器10。熱交換器10包含第一和第二端板11a、11b及多個第一和第二熱交換器板12a、12b堆疊成疊層以形成熱交換器10。熱交換器10是一種硬焊型板式熱交換器。舉例言之,熱交換器10被配置為用作蒸發器或冷凝器,例如在熱泵或冷卻系統中。熱交換器10被配置為至少在第一流體與第二流體之間進行熱交換。舉例言之,其中一種流體是致冷劑,例如R32、R290或類似的致冷劑。Referring to Figure 1, a
熱交換器板12a、12b設有脊突R和溝槽G的圖案,使得當板堆疊時在熱交換器板12a、12b之間形成交替的第一和第二板間隙13a、13b用於流體交換熱。在形成用於流體交換熱的板間隙13a、13b的情況下,透過在相鄰的熱交換器板12a、12b的至少部分交叉脊突R與溝槽G之間提供接觸點來形成熱交換器10的疊層,下面將有更詳細的描述。根據所示實施態樣的圖案是人字形圖案。然而,圖案也可以是斜向延伸的直線或其他合適的圖案。脊突R和溝槽G的圖案是具有波紋深度的波紋圖案。該圖案是壓製圖案。該圖案適用於使板12a、12b彼此保持一定距離(但與接觸點除外),以在相鄰的熱交換器板12a、12b之間形成板間隙13a、13b,以供流體進行熱交換。舉例言之,熱交換器板12a、12b由金屬片(例如不銹鋼、銅或其他合適的金屬或合金)製成。舉例言之,熱交換器板12a、12b的壓入深度為1至3mm,例如1至2mm或1至1.7mm。The
在所示實施態樣中,為了沿熱交換器10的周圍提供密封,每個熱交換器板12a、12b被裙部S包圍,該裙部通常垂直於熱交換器板12a、12b的平面延伸且適於接觸相鄰熱交換器板12a、12b的裙部S。In the embodiment shown, in order to provide a seal around the perimeter of the
熱交換器板12a、12b設有端口開口O1、O2、O3和O4,形成用於流體的入口和出口通道,以將熱交換進出板間隙13a、13b。在所示實施態樣中,第一端板11a和熱交換器板12a、12b設有四個端口開口。或者,熱交換器板12a、12b設有其他數量的端口開口,例如六或八個或甚至更多。在各種所示實施態樣中,第一熱交換器板12a設有第一端口開口O1a,其中第二熱交換器板12b形成有第一端口開口O1b。第二熱交換器板12b的第一端口開口O1b與例如第一熱交換器板12a的第一端口開口O1a不同。在所示實施態樣中,第一熱交換器板12a的第一端口開口O1a小於第二熱交換器板12b的第一端口開口O1b,下面將有更詳細的描述。或者,第一和第二熱交換器板12a、12b的第一端口開口O1a、O1b在尺寸上相似。The
舉例言之,提供第二、第三和第四端口開口O2-O4。提供圍繞端口開口O1-O4的端口開口區域15。 提供端口開口區域15,以實現所述端口開口O1-O4與板間隙13a、13b之間的選擇性連通。舉例言之,端口開口區域15是平坦的且彼此交替接觸以提供選擇性連通。端口開口區域15設置成用於密封相鄰熱交換器板12a、12b的相應端口開口區域15。舉例言之,端口開口區域15實質上是平坦的且透過硬焊接合彼此連接。舉例言之,端口開口區域15在熱交換器板12a、12b的平面中延伸或與其平行延伸。舉例言之,端口開口區域15是環形的且具有圓形外周。或者,端口開口區域15具有橢圓形外周或以另一種合適的方式形成。For example, second, third and fourth port openings O2-O4 are provided.
在所示實施態樣中,熱交換器板12a、12b為圓角矩形,其中端口開口O1a、O1b、O2、O3、O4設置在彎角附近。或者,熱交換器板12a、12b是正方形,例如具有圓角。或者,熱交換器板12a、12b為圓形、橢圓形或以其他合適的形狀設置,其中端口開口以合適的方式分佈。在所示實施態樣中,熱交換器板12a、12b設有人字形圖案,其中第一熱交換器板12a的人字形圖案沿一個方向設置,第二熱交換器板的人字形圖案沿相反方向設置。In the embodiment shown, the
第一熱交換器板12a設有至少部分地圍繞第一熱交換器板12a的第一端口開口O1a。第一裙部16a是例如第一熱交換器板12a的折疊部分,該折疊部分完全或部分圍繞第一端口開口O1a。在所示實施態樣中,第二熱交換器板12b設有至少部分地圍繞第二熱交換器板12b的第一端口開口O1b的第二裙部16b。第二裙部16a可以是第二熱交換器板12b的折疊部分。舉例言之,第一及/或第二端口裙部16a、16b是環形。還參考圖2至7,第一和第二裙部16a、16b圍繞或至少部分地圍繞一對熱交換器板12a、12b的第一端口開口O1a、O1b形成腔室17。腔室17如圖5至7所示。由熱交換器板12a、12b形成的腔室17圍繞由第一端口開口O1a、O1b形成的入口通道14延伸。在所示實施態樣中,腔室17是環形且圍繞入口通道14。舉例言之,腔室17由裙部16a、16b及圍繞第一熱交換器板12a的第一端口開口O1a的端口開口區域15a和圍繞第二熱交換器板12b的第一端口開口O1b的端口開口區域15b形成。所述端口開口區域15a、15b交替地設置在較高和較低的水平面上且圍繞第一端口開口O1a、O1b彼此接合。端口開口區域15a、15b接合相鄰板對的熱交換器板12a、12b的相鄰端口開口區域15a、15b。每個腔室17透過第一和第二熱交換器板12a、12b之一中的孔洞18與第一或第二板間隙13a、13b連通。在圖5的實施態樣中,腔室17透過第一熱交換器板12a中的孔洞18與第二板間隙13b連通。在圖6所示的第二實施態樣中,腔室17透過第二熱交換器板12b中的孔洞18與第二板間隙13b連通。舉例言之,第一和第二熱交換器板12a、12b中的一個設有單個孔洞18。或者,第一和第二熱交換器板12a、12b中的一個在,例如相同區域或分佈在小於一半或小於三分之一的腔室周圍周圍,設有多個孔洞。根據一個實施態樣,孔洞具有至少0.5mm的直徑,例如0.5至2mm或0.5至1.5mm或0.5至1mm。The first
入口通道14至少部分地沿軸向方向延伸,如圖5中的中心軸線A所示。軸向方向垂直於熱交換器板的平面。第一裙部16a以偏離熱交換器板平面的角度延伸,因此至少部分地在軸向方向上延伸。第一裙部16a具有基部及至少一個自由端部。第一裙部16a以偏離熱交換器板平面的角度從基部朝向自由端延伸。第一裙部16a的基部與自由端之間的距離為其長度。舉例言之,第一裙部的整個長度以偏離熱交換器板平面的角度設置,例如垂直或實質上垂直。舉例言之,第一裙部16a在其整個長度上沿相同方向延伸。在所示實施態樣中,整個第一裙部16a具有自由端且不接觸任何其他裙部或板。第一裙部16a沿朝向其自由端的方向延伸。第一裙部16a實質上沿著入口通道14且平行於中心軸線A的方向上延伸,例如在沿著通過入口通道14軸向流入熱交換器10的流體的方向上,以圖5中的箭頭B示意性表示。在所示實施態樣中,軸向方向垂直於熱交換器板的平面。舉例言之,第一裙部16a在朝向其自由端的方向上實質上軸向延伸且朝向由第一端口開口O1a、O1b形成的通道14的中心軸線A徑向向內傾斜。軸向間隙19設置在相鄰板對中第一裙部16a的自由端與的下一個第一熱交換器板12a的第一裙部16a之間。或者,軸向間隙19在第一裙部16a的自由端與第二熱交換器板12b的端口開口區域15b之間沿軸向方向或實質上沿軸向方向延伸。舉例言之,軸向間隙19在第一裙部16a的自由端與下一個第一裙部16a的基部之間沿軸向方向或實質上沿軸向方向延伸,以圖7中的雙箭頭y示意性表示。因此,腔室17透過軸向間隙19通向入口通道14,使得流體可以從入口通道14通過軸向間隙19進入腔室17。第一裙部16a形成用於流體的流暢入口。The
除了孔洞18或多個孔洞以外,腔室17透過圍繞腔室17的密封區域20與板間隙13a、13b封閉。在所示實施態樣中,密封區域20由板對中的第一和第二熱交換器板12a、12b的平坦區域相互接合而形成。舉例言之,密封區域20由第一熱交換器板12a中的凹陷及/或第二熱交換器板12b中的***形成。舉例言之,第一和第二熱交換器板12a、12b在密封區域20中透過,例如圍繞腔室17的硬焊接合彼此連接。舉例言之,密封區域20是環形。With the exception of the
在所示實施態樣中,第二熱交換器板12b設有第二裙部16b,第二裙部16b實質上沿與第一裙部16a相反的方向延伸。舉例言之,第二裙部16b沿逆著入口通道14中的預期軸向流體流動的方向延伸,如箭頭B所示。第二裙部16b具有基部和自由端,例如類似於第一裙16a。在所示實施態樣中,第二裙部16b的自由端未與第一裙部16a的自由端對齊。因此,第一裙部16a相對於第二裙部16b徑向位移,其中在第一裙部16a與第二裙部16b之間形成徑向間隙21。徑向間隙21在圖7中以雙箭頭x示意性表示。In the embodiment shown, the second
如圖5所示,第一和第二裙部16a、16b重疊,即,它們的總長度超過在同一板對中與裙部16a、16b相鄰的端口開口區域15a、15b之間的距離。因此,徑向間隙21實質上在第一裙部16a的自由端與第二裙部16b的自由端之間沿徑向方向延伸。第二裙部16b設置在第一裙部16a的徑向外側。因此,第一裙部16a至少在其自由端處設置成具有比第二裙部16b小的直徑。第二裙部16b形成流動防護以防止流體的分佈不均。舉例言之,第二裙部16b形成對氣泡的防護。As shown in Figure 5, the first and
根據本發明所示的實施態樣,徑向間隙21改變。因此,徑向間隙21在第一裙部16a和第二裙部16b的自由端之間圍繞入口通道14的周圍改變。因此,徑向間隙21在一或多個位置比在其他位置更小。舉例言之,徑向間隙21在較靠近孔洞18的位置處較小且在較遠離孔洞18的位置處較大。根據所示的實施態樣,徑向間隙21在與孔洞18相對的位置處最大,即,在從孔洞18穿過第一端口開口O1a的位置處,且在孔洞18附近進入腔室17中最小。因此,徑向間隙21朝向孔洞18逐漸變細。According to the embodiment of the invention shown, the
在所示實施態樣中,第一熱交換器板12a的第一端口開口O1a周圍的端口開口面積15a大於第二熱交換器板12b的第一端口開口O1b周圍的端口開口面積15b。舉例言之,第一熱交換器板12a的第一端口開口O1a周圍的端口開口面積15a在第一熱交換器板12a的第一端口開口O1a周圍的尺寸改變。在所示實施態樣中,第一熱交換器板12a的第一端口開口O1a以偏心的方式設置在端口開口區域15a中。因此,所述端口開口區域15a朝向孔洞18逐漸變細。In the embodiment shown, the
在圖5至7的實施例中,腔室17的橫截面在入口通道14周圍實質上恆定。或者,腔室17的橫截面改變,例如使得橫截面在與孔洞18相對的區域中較大,而在孔洞18附近的區域較小。舉例言之,腔室17的橫截面在朝向孔洞18的方向上逐漸變細。In the embodiment of FIGS. 5 to 7 , the cross-section of the
在所示實施態樣中,裙部16a、16b圍繞第一端口開口O1a、O1b以恆定長度設置。或者,第一裙部及/或第二裙部16b的長度圍繞第一端口開口O1a、O1b的周圍改變。舉例言之,第一裙部16a在靠近孔洞18處較長,其中其長度在遠離孔洞18的方向上減小。因此,軸向間隙19可以在朝向孔洞18的方向上逐漸變細。可以改變第二裙部16b的長度以提供遠離孔洞進入腔室17的較大流量並限制流體流入較靠近孔洞18的腔室。In the embodiment shown, the
在所示實施態樣中,第一端口開口O1a、O1b為圓形,直徑不同且相互偏心。或者,第一及/或第二第一端口開口O1a、O1b是橢圓形,其中徑向間隙21改變。In the embodiment shown, the first port openings O1a, O1b are circular, have different diameters and are eccentric to each other. Alternatively, the first and/or second first port openings O1a, O1b are elliptical, wherein the
在所示實施態樣中,第一和第二裙部16a、16b實質上在軸向方向上延伸且圍繞第一端口開口O1a、O1b的周圍以恆定的角度向內傾斜。或者,第一及/或第二裙部16a、16b以不同的傾角設置以提供不同的徑向間隙21。In the embodiment shown, the first and
參考圖8至10,示意性顯示本發明的第三實施態樣。第三實施態樣的熱交換器10包含交替設置的具有壓製圖案的第一和第二熱交換器板12a、12b、端口開口O1-O4、端口開口區域15a、15b及板間隙13a、13b,從而實現如上所述端口開口O1-O4與板間隙13a、13b之間的選擇性連通。8 to 10, a third embodiment of the present invention is schematically shown. The
在第三實施態樣中,第一熱交換器板12a設有裙部16,裙部16部分地圍繞第一熱交換器板12a的第一端口開口O1a延伸,而第二熱交換器板12b可以設置或不設置任何裙部。或者,裙部16圍繞第一端口開口O1a的整個周圍延伸。In the third embodiment, the first
特別參考圖9和10,裙部16在實質上沿著入口通道14的方向上延伸且選擇性地稍微向內傾斜。裙部16具有至少連接到第一熱交換器板12a的端口開口區域15a的自由端部和基部。在圖9和10中,裙部16具有沿其圍繞入口通道 14 的整個周圍延伸的自由端。軸向間隙19設置在裙部16的自由端與下一個熱交換器板之間。舉例言之,軸向間隙19在裙部16的自由端與第二熱交換器板12b的端口開口區域15b之間沿軸向方向或實質上沿軸向方向延伸,如圖10中的雙箭頭y所示。或者,間隙19可以在裙部16的自由端與下一個裙部16之間延伸,例如實質上在下一個裙部16的基部。With particular reference to Figures 9 and 10, the
在圖9和10的實施態樣中,裙部16形成部分圍繞入口通道14的腔室17。因此,裙部16僅沿入口通道14的部分周圍延伸以形成僅部分地圍繞入口通道14的腔室17。裙部16由第一熱交換器板12a的圍繞第一端口開口O1a的折疊部分形成。裙部16被設置成使孔洞18免受從入口通道14流入並進入板間隙13a、13b的流體的影響。因此,裙部16設置在入口通道14與孔洞18之間,其中腔室17設置在入口通道14與孔洞18之間。舉例言之,裙部16圍繞第一端口開口O1a的周圍的至少一半延伸,例如其大約30至90%、40至80%或50至80%。In the embodiment of FIGS. 9 and 10 , the
在第三實施態樣中,裙部16設置為不同長度,並沿遠離孔洞18的方向逐漸變細,從而使軸向間隙19相應地改變。因此,裙部16靠近孔洞18較大,遠離孔洞18長度減小,其中軸向間隙19靠近孔洞18最小,遠離孔洞18較大,使得裙部16的屏蔽效果在孔洞18前面最大。裙部16或第一裙部16a和第二裙部16b的組合可以在孔洞18前面的區域中形成屏蔽,該屏蔽可以在遠離孔洞18的方向上減小,以分配在通道14中流動的流體,並提供從所述通道14進入選定板間隙的更均勻和良好的流體流動。因此,根據替代實施態樣(未顯示),第二熱交換器板12b設有第二裙部16b,該第二裙部16b可以設置為具有恆定長度且長度可以不同,例如在遠離孔洞18的方向上逐漸變細。In the third embodiment, the
在圖8至10中,如上所述,第二熱交換器板12b在端口開口區域15b與密封區域20之間設有孔洞18,但孔洞18可以替代地設置在第一熱交換器板12a中。In Figures 8 to 10, as described above, the second
參考圖11和12,示意性顯示本發明的第四實施態樣。第四實施態樣類似於第三實施態樣,不同之處在於裙部16的一部分接合相鄰的熱交換器板及/或下一個第一熱交換器板12a的裙部16。舉例言之,裙部16在孔洞18前面與相鄰的熱交換器板及/或下一個裙部16接觸,使得孔洞18在入口通道14與孔洞18之間的徑向方向上被完全屏蔽。腔室17設置在入口通道14與孔洞18之間。11 and 12, a fourth embodiment of the present invention is schematically shown. The fourth embodiment is similar to the third embodiment, except that a portion of the
在圖11和12的實施態樣中,裙部16具有至少一個自由端部及一個非自由端部。舉例言之,裙部16在與相鄰板或裙部接觸的端部兩側具有自由端部。如上所述,間隙19設置在自由端部與相鄰板或裙部之間。舉例言之,間隙19是軸向間隙或至少部分地沿軸向方向延伸。間隙19在圖12中以雙箭頭y表示。因此,流體必須從入口通道14流入腔室17,圍繞裙部16在孔洞18前面的部分。流體可以例如通過間隙19流入腔室17。同樣在圖11和12的實施態樣中,裙部16被設置為具有不同長度且在遠離孔洞18的方向上逐漸變細,從而使軸向間隙19相應地改變。因此,裙部16靠近孔洞18較大,遠離孔洞18長度減小,其中孔洞18前面沒有軸向間隙,距離孔洞18越遠間隙19越大。In the embodiment of Figures 11 and 12, the
裙部16、或第一裙部16a和第二裙部16b的組合,可以在孔洞18前面的區域中形成屏蔽,以分配在通道14中流動的流體,並提供從所述通道14到選定板間隙的更均勻和更良好的流體流動。根據一個實施態樣(未顯示),第一和第二裙部16a、16b在孔洞18的前面相互接合,其中距離孔洞18越遠,它們之間的差距越大。The
參考圖13至15,示意性顯示本發明的第五實施態樣。根據第五實施態樣,第一和第二裙部16a、16b圍繞第一和第二板12a、12b的第一端口開口O1a、O1b設置且彼此相對,以在第一和第二裙部16a、16b的自由端之間形成軸向間隙19,用於流體從入口通道14流入腔室17。第一和第二裙部16a、16b以從板12a、12b的平面和從端口開口區域15a、15b的平面偏移的角度延伸,例如從端口開口區域15a、15b成90至120度。舉例言之,第一和第二裙部16a、16b實質上沿相反的軸向方向延伸,例如朝向入口通道14的中心稍微向內傾斜。舉例言之,第一和第二裙部16a、16b以類似的長度設置,該長度圍繞整個端口開口是恆定的。舉例言之,第一和第二裙部16a、16b彼此互為鏡像以提供通過入口通道14在兩個方向上的類似流動。在第五實施態樣中,第一裙部16a的自由端實質上面向第二裙部16b的自由端,且它們之間的間隙19圍繞入口通道14的整個周圍是恆定的。舉例言之,第一和第二裙部16a、16b圍繞端口開口O1a、O1b和入口通道14的整個周圍延伸並形成為環形閉合迴路。13 to 15, a fifth embodiment of the present invention is schematically shown. According to the fifth embodiment, the first and
在第五實施態樣中,第一和第二板12a、12b的端口開口區域15a、15b類似,彼此對齊且靠近孔洞18形成為具有較小的寬度。端口開口區域15a、15b是平坦的且在徑向方向上延伸,例如在板12a、12b的平面中或與其平行。第一和第二板12a、12b的第一端口開口O1a、O1b彼此對齊且以偏心的方式設置在端口開口區域15a、15b中,使得腔室17朝向孔洞18逐漸變細,進入第一和第二板間隙13a、13b中的一個。除孔洞18以外,腔室17透過如上所述的密封區域20與第一和第二板間隙13a、13b中的另一個封閉。腔室17在靠近孔洞18處具有較小的橫截面,而在遠離孔洞18處具有較大的橫截面。舉例言之,第一端口開口O1a、O1b以偏心的方式設置在端口開口區域15a、15b中,使得腔室17在朝向孔洞18的方向上逐漸變細。舉例言之,板12a、12b的端口開口區域15a、15b為圓形或橢圓形,其中第一端口開口O1a、O1b為圓形或橢圓形且以偏心的方式設置在端口開口區域15a、15b中。In the fifth embodiment, the
參考圖16至22,示意性顯示本發明的第六實施態樣。根據第六實施態樣,第一和第二板12a、12b的第一端口開口O1a、O1b是非圓形的且相對於彼此形成徑向延伸的凸部22a、22b和凹部23a、23b。第一和第二裙部16a、16b對應地形成為實質上遵循第一端口開口O1a、O1b的形狀。因此,第一端口開口O1a和第一裙部16a形成有凸部22a和凹部23a,其中第二端口開口O1b和第二裙部16b形成有凸部22b和凹部23b。如上所述,裙部16a、16b實質上沿相反方向軸向延伸且可以向內傾斜。凸部22a、22b和凹部23a、23b圍繞入口通道14的周圍交替設置。凸部22a、22b和凹部23a、23b是彎曲的且可以是多邊形的波浪形,其中多邊形的每個角對應於凹部23a、23b,每個凹部23a、23b之間具有凸部22a、22b。舉例言之,這種類似多邊形的形狀可以,例如具有四個到十個角(例如具有六個凸部22a、22b和六個凹部23a、23b的所示六邊形形狀)。舉例言之,凸部22a、22b和凹部23a、23b圍繞端口開口O1a、O1b和裙部16a、16b的周圍均勻分佈。因此,第一和第二裙部16a、16b設置為周圍波浪形管部分。16 to 22, a sixth embodiment of the present invention is schematically shown. According to the sixth embodiment, the first port openings O1a, O1b of the first and
第一板12a的凸部22a位於第二板12b的凹部23b處,反之亦然。因此,凸部22a、22b和凹部23a、23b也在軸向方向上交替。第一板12a的凸部22a在軸向方向上彼此對齊,其中第一板12a的凹部23a彼此對齊。類似地,第二板12b的凸部22b在軸向方向上彼此對齊,其中其凹部23b彼此對齊。舉例言之,對於第一板和第二板12a、12b,凸部22a、22b和凹部23a、23b的頻率相似,但相對於彼此圍繞周圍位移。因此,凸部22a、22b和凹部23a、23b的圖案透過入口通道14圍繞軸線A相對於彼此位移,使得第一板12a的凸部22a沿軸向方向設置在第二板12b的凹部23b的兩側。類似地,第二板12b的凸部22b沿軸向方向設置在第一板12a的凹部23a的兩側。因此,凸部22a、22b徑向突出到入口通道14中以引導流體流進入腔室17。舉例言之,凸部和凹部沿裙部均勻分佈,例如沿其整個周圍分佈。The
舉例言之,在第六實施態樣中,由於相鄰板12a、12b的凸部22a、22b和凹部23a、23b交替重疊,入口通道14與腔室17之間的徑向間隙21圍繞入口通道14的周圍改變。裙部16a、16b的自由端之間的距離可以在軸向方向上是恆定的且在徑向方向上改變,其中徑向間隙21交替改變,從相對的裙部16a、16b的自由端彼此更近的地方變小到它們彼此遠離的地方變大。徑向間隙21交替地從裙部16a、16b的自由端彼此面對的位置處的零變化到凸部22a、22b的中心點與相鄰板12a、12b的凹部23a、23b的中心點對齊的最大尺寸。舉例言之,軸向間隙19是恆定的且可以非常小。For example, in the sixth embodiment, since the
10:硬焊型板式熱交換器
11a:第一端板
11b:第二端板
12a:第一熱交換器板
12b:第二熱交換器板
13a:第一板間隙
13b:第二板間隙
15:端口開口區域
15a:第一端口開口區域
15b:第二端口開口區域
16a:第一裙部
16b:第二裙部
17:腔室
18:孔洞
19:軸向間隙
20:密封區域
21:徑向間隙
22a、22b:凸部
23a、23b:凹部
A:中心軸線
S:裙部
G:溝槽
R:脊突
O1-O4:端口開口
O1a、O1b:第一端口開口
10: Brazed
在下文中,將參照附圖描述本發明,其中: 圖1是本發明第一實施態樣的熱交換器的分解示意圖; 圖2是根據圖1熱交換器的第一熱交換器板的示意前視圖; 圖3是圖2第一熱交換器板的線A-A處的示意剖面圖,顯示根據一個實施態樣的第一熱交換器板的第一端口開口的端口開口區域及裙部; 圖4是根據圖1熱交換器的示意前視圖; 圖5是圖4熱交換器在線A-A處的示意和簡化剖面圖,顯示由根據第一實施態樣的第一和第二熱交換器板的第一端口開口處的端口開口區域及裙部形成的腔室; 圖6是根據第二實施態樣的熱交換器的示意和簡化剖面圖,顯示根據第二實施態樣,與板間隙連通的腔室; 圖7是圖5一部分的示意圖,顯示根據第一實施態樣,流體從入口通道流向腔室的軸向間隙及徑向間隙; 圖8是根據本發明第三實施態樣的熱交換器的分解示意圖; 圖9是圖8熱交換器的示意和簡化剖面圖,顯示由根據第三實施態樣的第一熱交換器板的第一端口開口處的端口開口區域及裙部形成的腔室; 圖10是圖9一部分的示意圖,顯示根據第三實施態樣,從入口通道到腔室的不同間隙; 圖11是根據第四實施態樣的熱交換器的示意和簡化剖面圖,顯示由根據第四實施態樣的第一熱交換器板的第一端口開口處的端口開口區域及裙部形成的腔室; 圖12是圖11一部分的示意圖,顯示根據第四實施態樣,從入口通道到腔室的裙部及不同間隙; 圖13是根據本發明第五實施態樣的熱交換器的分解示意圖; 圖14是根據第五實施態樣的熱交換器的示意和簡化剖面圖,顯示根據第五實施態樣的具有形成與板間隙連通的腔室的裙部的熱交換器板; 圖15是圖14一部分的示意圖,顯示根據第五實施態樣,相鄰熱交換器板的裙部之間的軸向間隙用於流體從入口通道流到腔室; 圖16是根據本發明第六實施態樣的熱交換器的分解示意圖; 圖17是根據第六實施態樣的熱交換器的示意剖面圖,顯示根據第五實施態樣的具有形成與板間隙連通的腔室的裙部的熱交換器板; 圖18是圖17一部分的示意圖,顯示根據第六實施態樣,用於流體從入口通道流到腔室的相鄰熱交換器板的裙部之間的間隙; 圖19是根據第六實施態樣的熱交換器板堆疊的示意透視圖; 圖20是圖19一部分的視圖,顯示根據第六實施態樣的第一和第二熱交換器板的裙部構造, 圖21是根據第六實施態樣的熱交換器板堆疊的示意前視圖; 圖22是圖21一部分的視圖,顯示根據第六實施態樣的第一和第二熱交換器板的裙部構造。 In the following, the present invention will be described with reference to the accompanying drawings, in which: Fig. 1 is the exploded schematic diagram of the heat exchanger of the first embodiment of the present invention; Figure 2 is a schematic front view of a first heat exchanger plate of the heat exchanger according to Figure 1; 3 is a schematic cross-sectional view at line A-A of the first heat exchanger plate of FIG. 2 showing the port opening area and skirt of the first port opening of the first heat exchanger plate according to one embodiment; Figure 4 is a schematic front view of the heat exchanger according to Figure 1; 5 is a schematic and simplified cross-sectional view of the heat exchanger of FIG. 4 at line A-A, shown formed by the port opening regions and skirts at the first port openings of the first and second heat exchanger plates according to the first embodiment. the chamber; 6 is a schematic and simplified cross-sectional view of a heat exchanger according to a second embodiment, showing a chamber in communication with a plate gap, according to the second embodiment; 7 is a schematic view of a portion of FIG. 5 showing the axial and radial gaps for fluid flow from the inlet passage to the chamber according to the first embodiment; 8 is an exploded schematic view of a heat exchanger according to a third embodiment of the present invention; 9 is a schematic and simplified cross-sectional view of the heat exchanger of FIG. 8 showing the chamber formed by the port opening area and skirt at the first port opening of the first heat exchanger plate according to a third embodiment; Fig. 10 is a schematic view of a portion of Fig. 9 showing different clearances from the inlet channel to the chamber according to a third embodiment; 11 is a schematic and simplified cross-sectional view of a heat exchanger according to a fourth embodiment, showing the formation of the skirt formed by the port opening area and the skirt at the first port opening of the first heat exchanger plate according to the fourth embodiment Chamber; Figure 12 is a schematic view of a portion of Figure 11 showing the skirt and various gaps from the inlet channel to the chamber according to a fourth embodiment; 13 is an exploded schematic view of a heat exchanger according to a fifth embodiment of the present invention; 14 is a schematic and simplified cross-sectional view of a heat exchanger according to a fifth embodiment, showing a heat exchanger plate according to the fifth embodiment having a skirt forming a chamber communicating with the plate gap; Figure 15 is a schematic view of a portion of Figure 14 showing an axial gap between skirts of adjacent heat exchanger plates for fluid flow from the inlet channel to the chamber according to a fifth embodiment; 16 is an exploded schematic view of a heat exchanger according to a sixth embodiment of the present invention; 17 is a schematic cross-sectional view of a heat exchanger according to a sixth embodiment, showing a heat exchanger plate according to the fifth embodiment having a skirt forming a chamber communicating with the plate gap; Fig. 18 is a schematic view of a portion of Fig. 17 showing a gap between skirts of adjacent heat exchanger plates for fluid flow from an inlet channel to a chamber according to a sixth aspect; Figure 19 is a schematic perspective view of a stack of heat exchanger plates according to a sixth aspect; Figure 20 is a view of a portion of Figure 19 showing the skirt configuration of the first and second heat exchanger plates according to the sixth embodiment, Figure 21 is a schematic front view of a stack of heat exchanger plates according to a sixth aspect; Fig. 22 is a view of a portion of Fig. 21 showing the skirt configuration of the first and second heat exchanger plates according to the sixth embodiment.
10:硬焊型板式熱交換器 10: Brazed plate heat exchanger
11a:第一端板 11a: First end plate
11b:第二端板 11b: Second end plate
12a:第一熱交換器板 12a: First heat exchanger plate
12b:第二熱交換器板 12b: Second heat exchanger plate
13a:第一板間隙 13a: First board clearance
13b:第二板間隙 13b: Second plate clearance
15:端口開口區域 15: Port opening area
16a:第一裙部 16a: First skirt
16b:第二裙部 16b: Second skirt
S:裙部 S: skirt
G:溝槽 G: Groove
R:脊突 R: Spinal process
O1-O4:端口開口 O1-O4: Port openings
O1a、O1b:第一端口開口 O1a, O1b: first port opening
Claims (24)
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SE2150186A SE2150186A1 (en) | 2021-02-22 | 2021-02-22 | A brazed plate heat exchanger |
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SE (1) | SE2150186A1 (en) |
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JP5940970B2 (en) * | 2012-02-10 | 2016-06-29 | 株式会社ティラド | Laminate heat exchanger |
SE541284C2 (en) * | 2016-05-30 | 2019-06-11 | Alfa Laval Corp Ab | A plate heat exchanger |
JP7247717B2 (en) * | 2019-04-01 | 2023-03-29 | 株式会社デンソー | Heat exchanger |
-
2021
- 2021-02-22 SE SE2150186A patent/SE2150186A1/en unknown
-
2022
- 2022-02-14 WO PCT/SE2022/050156 patent/WO2022177494A1/en active Application Filing
- 2022-02-17 TW TW111105889A patent/TW202234008A/en unknown
- 2022-02-21 FR FR2201529A patent/FR3120119B3/en active Active
Also Published As
Publication number | Publication date |
---|---|
SE2150186A1 (en) | 2022-08-23 |
WO2022177494A1 (en) | 2022-08-25 |
FR3120119B3 (en) | 2023-02-17 |
FR3120119A3 (en) | 2022-08-26 |
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