CN111238260B - U-shaped pipe positive displacement heat exchanger - Google Patents
U-shaped pipe positive displacement heat exchanger Download PDFInfo
- Publication number
- CN111238260B CN111238260B CN202010109396.9A CN202010109396A CN111238260B CN 111238260 B CN111238260 B CN 111238260B CN 202010109396 A CN202010109396 A CN 202010109396A CN 111238260 B CN111238260 B CN 111238260B
- Authority
- CN
- China
- Prior art keywords
- mixed flow
- cylinder
- pipe
- fixedly connected
- iii
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000006073 displacement reaction Methods 0.000 title abstract 2
- 230000007246 mechanism Effects 0.000 claims abstract description 140
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 50
- 238000006243 chemical reaction Methods 0.000 claims abstract description 18
- 230000026683 transduction Effects 0.000 claims description 56
- 238000010361 transduction Methods 0.000 claims description 56
- 238000004891 communication Methods 0.000 claims description 14
- 230000002463 transducing effect Effects 0.000 claims description 11
- 230000005540 biological transmission Effects 0.000 claims description 10
- 230000007423 decrease Effects 0.000 claims description 4
- 239000007788 liquid Substances 0.000 abstract description 3
- 230000001737 promoting effect Effects 0.000 abstract description 2
- 238000003756 stirring Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 9
- 239000000243 solution Substances 0.000 description 8
- 238000005457 optimization Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Images
Classifications
-
- 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
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/08—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
- F28D7/082—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
- F28D7/085—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration in the form of parallel conduits coupled by bent portions
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
- F28F13/12—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
- F28F13/125—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation by stirring
-
- 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
- F28F9/26—Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators
Landscapes
- 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
技术领域technical field
本发明涉及换热器,更具体的说是一种U型管容积式换热器。The invention relates to a heat exchanger, more specifically a U-tube volumetric heat exchanger.
背景技术Background technique
例如公开号CN205808184U一种高效U型管容积式换热器,包括一注水箱和一热媒模组,将注水箱用多块回程隔板隔开,形成多个回程混合腔室,这样,使热媒与冷水形成强烈的逆流和错流,从而形成传热学中的完美换热流动方式,强烈的逆流和错流提高了雷诺系数,加大了传热膜系数,促使热媒充分放热,冷水充分吸热,从而提高热效率和能源利用率;但是该实用新型的缺点是热效率底,不能进一步的提高热效率和能源利用率。For example, Publication No. CN205808184U is a high-efficiency U-tube volumetric heat exchanger, which includes a water injection tank and a heat medium module. The water injection tank is separated by multiple return partitions to form multiple return mixing chambers, so that the The heat medium and the cold water form strong countercurrent and cross-flow, thus forming a perfect heat exchange flow mode in heat transfer. , the cold water fully absorbs heat, thereby improving the thermal efficiency and energy utilization rate; but the disadvantage of the utility model is that the thermal efficiency is low, and the thermal efficiency and energy utilization rate cannot be further improved.
发明内容SUMMARY OF THE INVENTION
本发明的目的是提供一种U型管容积式换热器,可以提高热效率和能源利用率。The purpose of the present invention is to provide a U-tube volumetric heat exchanger, which can improve thermal efficiency and energy utilization rate.
本发明的目的通过以下技术方案来实现:The object of the present invention is achieved through the following technical solutions:
一种U型管容积式换热器,包括装置支架、换能支架、行星机构、混流机构Ⅰ、混流机构Ⅱ、混流机构Ⅲ和换能管道,所述装置支架上固定连接有换能支架,行星机构固定连接在装置支架上,换能支架内转动连接有混流机构Ⅰ,混流机构Ⅰ和行星机构连接,混流机构Ⅰ内转动连接有混流机构Ⅱ,混流机构Ⅱ和行星机构连接,混流机构Ⅱ内转动连接有和行星机构连接的混流机构Ⅲ,混流机构Ⅰ、混流机构Ⅱ和混流机构Ⅲ均同轴设置,混流机构Ⅰ、混流机构Ⅱ和混流机构Ⅲ的长度依次增长,换能管道固定连接在换能支架上,换能管道插入换能支架内,换能管道位于混流机构Ⅰ、混流机构Ⅱ和混流机构Ⅲ之间。A U-tube volumetric heat exchanger, comprising a device support, an energy conversion support, a planetary mechanism, a mixed flow mechanism I, a mixed flow mechanism II, a mixed flow mechanism III and an energy conversion pipeline, and the device support is fixedly connected with an energy conversion support, The planetary mechanism is fixedly connected to the device bracket, and a mixed flow mechanism I is rotatably connected in the transducer bracket. The mixed flow mechanism I is connected with the planetary mechanism. The mixed flow mechanism I is rotatably connected with a mixed flow mechanism II, and the mixed flow mechanism II is connected with the planetary mechanism. The mixed flow mechanism II There is a mixed-flow mechanism III connected to the planetary mechanism in the inner rotating connection. The mixed-flow mechanism I, the mixed-flow mechanism II and the mixed-flow mechanism III are all coaxially arranged. The lengths of the mixed-flow mechanism I, the mixed-flow mechanism II and the mixed-flow mechanism III increase in turn, and the transduction pipes are fixedly connected. On the transducer support, the transducer pipe is inserted into the transducer holder, and the transducer pipe is located between the mixed flow mechanism I, the mixed flow mechanism II and the mixed flow mechanism III.
作为本技术方案的进一步优化,本发明一种U型管容积式换热器,所述装置支架包括侧支架、支撑环、转动环Ⅰ和转动环Ⅱ,侧支架设置有两个,两个侧支架的前端之间固定连接有支撑环,两个侧支架的后端之间固定连接有转动环Ⅰ,转动环Ⅰ内部同轴固定连接有转动环Ⅱ。As a further optimization of the technical solution, the present invention is a U-tube volumetric heat exchanger. The device bracket includes a side bracket, a support ring, a rotating ring I and a rotating ring II. There are two side brackets and two side brackets. A support ring is fixedly connected between the front ends of the brackets, a rotating ring I is fixedly connected between the rear ends of the two side brackets, and a rotating ring II is fixedly connected coaxially inside the rotating ring I.
作为本技术方案的进一步优化,本发明一种U型管容积式换热器,所述换能支架包括换能外筒Ⅰ、入水管道、换能外筒Ⅱ、换能外筒Ⅲ和连接盘Ⅰ,换能外筒Ⅰ的上端固定有入水管道,入水管道和换能外筒Ⅰ连通,换能外筒Ⅰ的前端固定连接有换能外筒Ⅱ,换能外筒Ⅱ的前端固定连接有换能外筒Ⅲ,换能外筒Ⅰ、换能外筒Ⅱ和换能外筒Ⅲ均同轴设置,换能外筒Ⅰ、换能外筒Ⅱ和换能外筒Ⅲ的直径逐渐减小,换能外筒Ⅲ的前端固定连接有连接盘Ⅰ。As a further optimization of the technical solution, the present invention is a U-tube volumetric heat exchanger, wherein the transduction support includes an outer transduction cylinder I, a water inlet pipe, an outer transduction cylinder II, an outer transduction cylinder III and a connecting plate Ⅰ, the upper end of the transduction outer cylinder I is fixed with a water inlet pipe, and the water inlet pipe is connected with the transduction outer cylinder I, the front end of the transduction outer cylinder I is fixedly connected with the transduction outer cylinder II, and the front end of the transduction outer cylinder II is fixedly connected with a Transduction outer cylinder III, transduction outer cylinder I, transduction outer cylinder II and transduction outer cylinder III are all coaxially arranged, and the diameters of transduction outer cylinder I, transduction outer cylinder II and transduction outer cylinder III gradually decrease , the front end of the transducing outer cylinder III is fixedly connected with the connecting plate I.
作为本技术方案的进一步优化,本发明一种U型管容积式换热器,所述行星机构包括电机、齿轮、行星齿轮Ⅰ、齿圈Ⅰ、连接柱Ⅰ、行星齿轮Ⅱ、齿圈Ⅱ和连接柱Ⅱ,电机固定连接在转动环Ⅰ上,电机的输出轴上固定连接有齿轮,齿轮的外侧啮合传动有行星齿轮Ⅰ,行星齿轮Ⅰ的外侧啮合传动有齿圈Ⅰ,齿圈Ⅰ上固定连接有连接柱Ⅰ,齿圈Ⅰ的外侧啮合传动有行星齿轮Ⅱ,行星齿轮Ⅱ的外侧啮合传动有齿圈Ⅱ,齿圈Ⅱ上固定连接有连接柱Ⅱ,齿圈Ⅱ转动连接在转动环Ⅰ上,行星齿轮Ⅰ和行星齿轮Ⅱ均转动连接在转动环Ⅰ上,齿圈Ⅰ转动连接在转动环Ⅱ上。As a further optimization of the technical solution, the present invention is a U-tube volumetric heat exchanger. The planetary mechanism includes a motor, a gear, a planetary gear I, a ring gear I, a connecting column I, a planetary gear II, a ring gear II and Connecting column II, the motor is fixedly connected to the rotating ring I, the output shaft of the motor is fixedly connected with a gear, the outer meshing transmission of the gear has a planetary gear I, the outer meshing transmission of the planetary gear I has a ring gear I, and the ring gear I is fixed on Connected with connecting column I, the outer meshing transmission of ring gear I has planetary gear II, the outer meshing transmission of planetary gear II has ring gear II, the ring gear II is fixedly connected with connecting column II, and the ring gear II is rotatably connected to the rotating ring I The planetary gear I and the planetary gear II are both rotatably connected to the rotating ring I, and the ring gear I is rotatably connected to the rotating ring II.
作为本技术方案的进一步优化,本发明一种U型管容积式换热器,所述混流机构Ⅰ包括混流筒Ⅰ、转动挡板Ⅰ、混流板Ⅰ和连通孔,混流筒Ⅰ上固定连接有转动挡板Ⅰ,换能外筒Ⅰ转动连接在转动挡板Ⅰ上,混流筒Ⅰ上固定连接有多个混流板Ⅰ,混流筒Ⅰ上设置有多个连通孔,连接柱Ⅱ固定连接在混流筒Ⅰ上。As a further optimization of the technical solution, the present invention is a U-tube volumetric heat exchanger. The mixed flow mechanism I includes a mixed flow cylinder I, a rotating baffle I, a mixed flow plate I and a communication hole. The mixed flow cylinder I is fixedly connected with a Rotating the baffle I, the transducing outer cylinder I is rotatably connected to the rotating baffle I, the mixed flow cylinder I is fixedly connected with a plurality of mixed flow plates I, the mixed flow cylinder I is provided with a plurality of communication holes, and the connecting column II is fixedly connected to the mixed flow. on the barrel I.
作为本技术方案的进一步优化,本发明一种U型管容积式换热器,所述混流机构Ⅱ包括混流筒Ⅱ、转动挡板Ⅱ和混流板Ⅱ,混流筒Ⅱ上固定连接有转动挡板Ⅱ,混流筒Ⅰ转动连接在转动挡板Ⅱ上,混流筒Ⅱ上固定连接有多个混流板Ⅱ,连接柱Ⅰ固定连接在混流筒Ⅱ上。As a further optimization of this technical solution, the present invention is a U-tube volumetric heat exchanger. The mixed flow mechanism II includes a mixed flow cylinder II, a rotating baffle II and a mixed flow plate II, and the mixed flow cylinder II is fixedly connected with a rotating baffle plate. II, the mixed flow cylinder I is rotatably connected to the rotating baffle II, a plurality of mixed flow plates II are fixedly connected to the mixed flow cylinder II, and the connecting column I is fixedly connected to the mixed flow cylinder II.
作为本技术方案的进一步优化,本发明一种U型管容积式换热器,所述混流机构Ⅲ包括混流筒Ⅲ、转动挡板Ⅲ、混流板Ⅲ、连通管道、出水筒、转动挡板Ⅳ和出水管道,混流筒Ⅲ上固定连接有转动挡板Ⅲ,混流筒Ⅱ转动连接在转动挡板Ⅲ上,混流筒Ⅲ上固定连接有多个混流板Ⅲ,混流筒Ⅲ的后端固定连接有连通管道,混流筒Ⅲ的后端转动连接有出水筒,出水筒上转动连接有转动挡板Ⅳ,连通管道穿过转动挡板Ⅳ和出水筒连通,出水筒上固定连接有出水管道,出水管道固定连接在转动环Ⅰ上,电机的输出轴固定连接在混流筒Ⅲ上。As a further optimization of the technical solution, the present invention is a U-tube volumetric heat exchanger. The mixed flow mechanism III includes a mixed flow cylinder III, a rotating baffle III, a mixed flow plate III, a communication pipe, a water outlet cylinder, and a rotating baffle IV. And the outlet pipe, the mixed flow cylinder III is fixedly connected with the rotating baffle III, the mixed flow cylinder II is rotatably connected to the rotating baffle III, the mixed flow cylinder III is fixedly connected with a plurality of mixed flow plates III, and the rear end of the mixed flow cylinder III is fixedly connected with a Connecting pipe, the rear end of the mixed-flow cylinder III is rotatably connected with a water outlet cylinder, and a rotating baffle IV is rotatably connected to the water outlet cylinder. It is fixedly connected to the rotating ring I, and the output shaft of the motor is fixedly connected to the mixed flow cylinder III.
作为本技术方案的进一步优化,本发明一种U型管容积式换热器,所述换能管道包括连接盘Ⅱ、U形管道、连接管道Ⅰ、连接管道Ⅱ、折叠管道Ⅰ和折叠管道Ⅱ,连接盘Ⅱ固定连接在连接盘Ⅰ上,U形管道固定连接在连接盘Ⅱ上,U形管道的上侧设置有两个连接管道Ⅰ,两个连接管道Ⅰ分别一前一后设置,U形管道的下侧设置有两个连接管道Ⅱ,连接管道Ⅱ分别一前一后设置,折叠管道Ⅰ的两端分别转动连接在两个连接管道Ⅰ上,折叠管道Ⅰ和连接管道Ⅰ之间设有扭簧Ⅰ,折叠管道Ⅰ和U形管道连通,折叠管道Ⅱ的两端分别转动连接在两个连接管道Ⅱ上,折叠管道Ⅱ和连接管道Ⅱ之间设有扭簧Ⅱ,折叠管道Ⅱ和U形管道连通,U形管道插入混流筒Ⅱ和混流筒Ⅲ内,折叠管道Ⅰ和折叠管道Ⅱ均插入混流筒Ⅰ内。As a further optimization of the technical solution, the present invention is a U-tube volumetric heat exchanger, and the energy conversion pipeline includes a connecting plate II, a U-shaped pipeline, a connecting pipeline I, a connecting pipeline II, a folding pipeline I and a folding pipeline II , the connecting plate II is fixedly connected to the connecting plate I, the U-shaped pipeline is fixedly connected to the connecting plate II, and two connecting pipelines I are arranged on the upper side of the U-shaped pipeline. Two connecting pipes II are arranged on the lower side of the shaped pipe, and the connecting pipes II are respectively arranged one after the other. There is a torsion spring I, the folding pipe I and the U-shaped pipe are connected, the two ends of the folding pipe II are respectively connected to the two connecting pipes II, and a torsion spring II is arranged between the folding pipe II and the connecting pipe II. The U-shaped pipe is connected, the U-shaped pipe is inserted into the mixed flow cylinder II and the mixed flow cylinder III, and the folded pipe I and the folded pipe II are both inserted into the mixed flow cylinder I.
本发明一种U型管容积式换热器的有益效果为:The beneficial effects of the U-tube volumetric heat exchanger of the present invention are:
本发明一种U型管容积式换热器,可以通过行星机构同时带动混流机构Ⅰ、混流机构Ⅱ和混流机构Ⅲ进行转动,混流机构Ⅰ、混流机构Ⅱ和混流机构Ⅲ转动时对换能支架内的液体进行搅拌,起到一定的混流作用,混流机构Ⅰ、混流机构Ⅱ和混流机构Ⅲ的长度依次增长,将换能支架内的水进行分层,形成多个混流层,换能管道位于混流机构Ⅰ、混流机构Ⅱ和混流机构Ⅲ之间,使热媒与冷水形成强烈的逆流和错流,从而形成传热学中的完美换热流动方式,促使热媒充分放热,冷水充分吸热。The present invention is a U-tube volume type heat exchanger, which can simultaneously drive the mixed flow mechanism I, the mixed flow mechanism II and the mixed flow mechanism III to rotate through the planetary mechanism. The liquid inside is stirred to play a certain mixed-flow effect. The lengths of the mixed-flow mechanism I, the mixed-flow mechanism II and the mixed-flow mechanism III increase in turn, and the water in the transducer bracket is stratified to form multiple mixed-flow layers. Between the mixed flow mechanism I, the mixed flow mechanism II and the mixed flow mechanism III, the heat medium and the cold water form a strong countercurrent and cross flow, thus forming a perfect heat exchange flow mode in heat transfer, which promotes the heat medium to fully release heat and the cold water to fully absorb. hot.
附图说明Description of drawings
下面结合附图和具体实施方法对本发明做进一步详细的说明。The present invention will be described in further detail below with reference to the accompanying drawings and specific implementation methods.
在本发明的描述中,需要说明的是,术语“中心”、“纵向”、“横向”、“上”、“下”、“前”、“后”、“左”、“右”、“顶”、“底”、“内”、“外”和“竖着”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。In the description of the present invention, it should be noted that the terms "center", "portrait", "horizontal", "top", "bottom", "front", "rear", "left", "right", " The orientation or positional relationship indicated by "top", "bottom", "inside", "outside" and "vertical" is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present invention and simplifying the description, and It is not indicated or implied that the indicated device or element must have a particular orientation, be constructed and operate in a particular orientation, and therefore should not be construed as limiting the invention.
在本发明的描述中,需要说明的是,除非另有明确规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接可以是直接连接,亦可以是通过中间媒介间接连接,可以是两个部件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本发明中的具体含义。In the description of the present invention, it should be noted that the terms "installed", "connected" and "connected" should be understood in a broad sense unless otherwise expressly specified and limited, for example, it may be a fixed connection or a detachable connection , or the integral connection can be a direct connection, an indirect connection through an intermediate medium, or an internal communication between two components. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood in specific situations.
此外,在本发明的描述中,除非另有说明,“多个”、“多组”、“多根”的含义是两个或两个以上。In addition, in the description of the present invention, unless otherwise specified, "plurality", "multiple groups" and "plurality" mean two or more.
图1是本发明的U型管容积式换热器整体结构示意图;1 is a schematic diagram of the overall structure of a U-tube volumetric heat exchanger of the present invention;
图2是本发明的U型管容积式换热器剖视图结构示意图;2 is a schematic structural view of a cross-sectional view of a U-tube volumetric heat exchanger of the present invention;
图3是本发明的装置支架结构示意图;Fig. 3 is the schematic diagram of the device support structure of the present invention;
图4是本发明的换能支架结构示意图;Fig. 4 is the structure schematic diagram of the transducer support of the present invention;
图5是本发明的行星机构结构示意图;5 is a schematic structural diagram of a planetary mechanism of the present invention;
图6是本发明的混流机构Ⅰ结构示意图;6 is a schematic structural diagram of the mixed flow mechanism I of the present invention;
图7是本发明的混流机构Ⅱ结构示意图;7 is a schematic structural diagram of the mixed flow mechanism II of the present invention;
图8是本发明的混流机构Ⅲ结构示意图;8 is a schematic structural diagram of the mixed flow mechanism III of the present invention;
图9是本发明的混流机构Ⅲ剖视图结构示意图;9 is a schematic structural diagram of a cross-sectional view of the mixed flow mechanism III of the present invention;
图10是本发明的出换能管道结构示意图。FIG. 10 is a schematic structural diagram of the energy-transducing pipeline of the present invention.
图中:装置支架1;侧支架101;支撑环102;转动环Ⅰ103;转动环Ⅱ104;换能支架2;换能外筒Ⅰ201;入水管道202;换能外筒Ⅱ203;换能外筒Ⅲ204;连接盘Ⅰ205;行星机构3;电机301;齿轮302;行星齿轮Ⅰ303;齿圈Ⅰ304;连接柱Ⅰ305;行星齿轮Ⅱ306;齿圈Ⅱ307;连接柱Ⅱ308;混流机构Ⅰ4;混流筒Ⅰ401;转动挡板Ⅰ402;混流板Ⅰ403;连通孔404;混流机构Ⅱ5;混流筒Ⅱ501;转动挡板Ⅱ502;混流板Ⅱ503;混流机构Ⅲ6;混流筒Ⅲ601;转动挡板Ⅲ602;混流板Ⅲ603;连通管道604;出水筒605;转动挡板Ⅳ606;出水管道607;换能管道7;连接盘Ⅱ701;U形管道702;连接管道Ⅰ703;连接管道Ⅱ704;折叠管道Ⅰ705;折叠管道Ⅱ706。In the figure:
具体实施方式Detailed ways
下面结合附图对本发明作进一步详细说明。The present invention will be further described in detail below in conjunction with the accompanying drawings.
具体实施方式一:Specific implementation one:
下面结合图1-10说明本实施方式,一种U型管容积式换热器,包括装置支架1、换能支架2、行星机构3、混流机构Ⅰ4、混流机构Ⅱ5、混流机构Ⅲ6和换能管道7,所述装置支架1上固定连接有换能支架2,行星机构3固定连接在装置支架1上,换能支架2内转动连接有混流机构Ⅰ4,混流机构Ⅰ4和行星机构3连接,混流机构Ⅰ4内转动连接有混流机构Ⅱ5,混流机构Ⅱ5和行星机构3连接,混流机构Ⅱ5内转动连接有和行星机构3连接的混流机构Ⅲ6,混流机构Ⅰ4、混流机构Ⅱ5和混流机构Ⅲ6均同轴设置,混流机构Ⅰ4、混流机构Ⅱ5和混流机构Ⅲ6的长度依次增长,换能管道7固定连接在换能支架2上,换能管道7插入换能支架2内,换能管道7位于混流机构Ⅰ4、混流机构Ⅱ5和混流机构Ⅲ6之间;可以通过行星机构3同时带动混流机构Ⅰ4、混流机构Ⅱ5和混流机构Ⅲ6进行转动,混流机构Ⅰ4、混流机构Ⅱ5和混流机构Ⅲ6转动时对换能支架2内的液体进行搅拌,起到一定的混流作用,混流机构Ⅰ4、混流机构Ⅱ5和混流机构Ⅲ6的长度依次增长,将换能支架2内的水进行分层,形成多个混流层,换能管道7位于混流机构Ⅰ4、混流机构Ⅱ5和混流机构Ⅲ6之间,使热媒与冷水形成强烈的逆流和错流,从而形成传热学中的完美换热流动方式,促使热媒充分放热,冷水充分吸热。The present embodiment will be described below with reference to FIGS. 1-10 , a U-tube volumetric heat exchanger, including a
具体实施方式二:Specific implementation two:
下面结合图1-10说明本实施方式,本实施方式对实施方式一作进一步说明,所述装置支架1包括侧支架101、支撑环102、转动环Ⅰ103和转动环Ⅱ104,侧支架101设置有两个,两个侧支架101的前端之间固定连接有支撑环102,两个侧支架101的后端之间固定连接有转动环Ⅰ103,转动环Ⅰ103内部同轴固定连接有转动环Ⅱ104。This embodiment will be described below with reference to FIGS. 1-10 . This embodiment will further describe
具体实施方式三:Specific implementation three:
下面结合图1-10说明本实施方式,本实施方式对实施方式二作进一步说明,所述换能支架2包括换能外筒Ⅰ201、入水管道202、换能外筒Ⅱ203、换能外筒Ⅲ204和连接盘Ⅰ205,换能外筒Ⅰ201的上端固定有入水管道202,入水管道202和换能外筒Ⅰ201连通,换能外筒Ⅰ201的前端固定连接有换能外筒Ⅱ203,换能外筒Ⅱ203的前端固定连接有换能外筒Ⅲ204,换能外筒Ⅰ201、换能外筒Ⅱ203和换能外筒Ⅲ204均同轴设置,换能外筒Ⅰ201、换能外筒Ⅱ203和换能外筒Ⅲ204的直径逐渐减小,换能外筒Ⅲ204的前端固定连接有连接盘Ⅰ205。The present embodiment will be described below with reference to FIGS. 1-10. This embodiment will further describe the second embodiment. The
具体实施方式四:Specific implementation four:
下面结合图1-10说明本实施方式,本实施方式对实施方式三作进一步说明,所述行星机构3包括电机301、齿轮302、行星齿轮Ⅰ303、齿圈Ⅰ304、连接柱Ⅰ305、行星齿轮Ⅱ306、齿圈Ⅱ307和连接柱Ⅱ308,电机301固定连接在转动环Ⅰ103上,电机301的输出轴上固定连接有齿轮302,齿轮302的外侧啮合传动有行星齿轮Ⅰ303,行星齿轮Ⅰ303的外侧啮合传动有齿圈Ⅰ304,齿圈Ⅰ304上固定连接有连接柱Ⅰ305,齿圈Ⅰ304的外侧啮合传动有行星齿轮Ⅱ306,行星齿轮Ⅱ306的外侧啮合传动有齿圈Ⅱ307,齿圈Ⅱ307上固定连接有连接柱Ⅱ308,齿圈Ⅱ307转动连接在转动环Ⅰ103上,行星齿轮Ⅰ303和行星齿轮Ⅱ306均转动连接在转动环Ⅰ103上,齿圈Ⅰ304转动连接在转动环Ⅱ104上。The present embodiment will be described below with reference to FIGS. 1-10 , and the third embodiment will be further described in this embodiment. The
具体实施方式五:Specific implementation five:
下面结合图1-10说明本实施方式,本实施方式对实施方式四作进一步说明,所述混流机构Ⅰ4包括混流筒Ⅰ401、转动挡板Ⅰ402、混流板Ⅰ403和连通孔404,混流筒Ⅰ401上固定连接有转动挡板Ⅰ402,换能外筒Ⅰ201转动连接在转动挡板Ⅰ402上,混流筒Ⅰ401上固定连接有多个混流板Ⅰ403,混流筒Ⅰ401上设置有多个连通孔404,连接柱Ⅱ308固定连接在混流筒Ⅰ401上。The present embodiment will be described below with reference to FIGS. 1-10. This embodiment will further describe the fourth embodiment. The mixed flow mechanism I4 includes a mixed flow cylinder I401, a rotating baffle I402, a mixed flow plate I403 and a
具体实施方式六:Specific implementation six:
下面结合图1-10说明本实施方式,本实施方式对实施方式五作进一步说明,所述混流机构Ⅱ5包括混流筒Ⅱ501、转动挡板Ⅱ502和混流板Ⅱ503,混流筒Ⅱ501上固定连接有转动挡板Ⅱ502,混流筒Ⅰ401转动连接在转动挡板Ⅱ502上,混流筒Ⅱ501上固定连接有多个混流板Ⅱ503,连接柱Ⅰ305固定连接在混流筒Ⅱ501上。The present embodiment will be described below with reference to Figs. 1-10. This embodiment will further describe the fifth embodiment. The mixed flow mechanism II5 includes a mixed flow cylinder II501, a rotating baffle II502 and a mixed flow plate II503. The mixed flow cylinder II501 is fixedly connected with a rotating block. Plate II502, the mixed flow cylinder I401 is rotatably connected to the rotating baffle II502, a plurality of mixed flow plates II503 are fixedly connected to the mixed flow cylinder II501, and the connecting column I305 is fixedly connected to the mixed flow cylinder II501.
具体实施方式七:Specific implementation seven:
下面结合图1-10说明本实施方式,本实施方式对实施方式六作进一步说明,所述混流机构Ⅲ6包括混流筒Ⅲ601、转动挡板Ⅲ602、混流板Ⅲ603、连通管道604、出水筒605、转动挡板Ⅳ606和出水管道607,混流筒Ⅲ601上固定连接有转动挡板Ⅲ602,混流筒Ⅱ501转动连接在转动挡板Ⅲ602上,混流筒Ⅲ601上固定连接有多个混流板Ⅲ603,混流筒Ⅲ601的后端固定连接有连通管道604,混流筒Ⅲ601的后端转动连接有出水筒605,出水筒605上转动连接有转动挡板Ⅳ606,连通管道604穿过转动挡板Ⅳ606和出水筒605连通,出水筒605上固定连接有出水管道607,出水管道607固定连接在转动环Ⅰ103上,电机301的输出轴固定连接在混流筒Ⅲ601上。The present embodiment will be described below with reference to Figs. 1-10. This embodiment will further describe the sixth embodiment. The mixed flow mechanism III6 includes a mixed flow cylinder III601, a rotating baffle III602, a mixed flow plate III603, a
具体实施方式八:Eighth specific implementation:
下面结合图1-10说明本实施方式,本实施方式对实施方式七作进一步说明,所述换能管道7包括连接盘Ⅱ701、U形管道702、连接管道Ⅰ703、连接管道Ⅱ704、折叠管道Ⅰ705和折叠管道Ⅱ706,连接盘Ⅱ701固定连接在连接盘Ⅰ205上,U形管道702固定连接在连接盘Ⅱ701上,U形管道702的上侧设置有两个连接管道Ⅰ703,两个连接管道Ⅰ703分别一前一后设置,U形管道702的下侧设置有两个连接管道Ⅱ704,连接管道Ⅱ704分别一前一后设置,折叠管道Ⅰ705的两端分别转动连接在两个连接管道Ⅰ703上,折叠管道Ⅰ705和连接管道Ⅰ703之间设有扭簧Ⅰ,折叠管道Ⅰ705和U形管道702连通,折叠管道Ⅱ706的两端分别转动连接在两个连接管道Ⅱ704上,折叠管道Ⅱ706和连接管道Ⅱ704之间设有扭簧Ⅱ,折叠管道Ⅱ706和U形管道702连通,U形管道702插入混流筒Ⅱ501和混流筒Ⅲ601内,折叠管道Ⅰ705和折叠管道Ⅱ706均插入混流筒Ⅰ401内。The present embodiment will be described below with reference to FIGS. 1-10 , and the seventh embodiment will be further described in this embodiment. The
本发明的一种U型管容积式换热器,其工作原理为:The working principle of a U-tube volumetric heat exchanger of the present invention is as follows:
使用时将U形管道702插入换能外筒Ⅰ201、换能外筒Ⅱ203和换能外筒Ⅲ204内,如图2所示,换能外筒Ⅰ201、换能外筒Ⅱ203和换能外筒Ⅲ204的直径逐渐减小,U形管道702的前端可以插入到混流筒Ⅲ601和混流筒Ⅱ501内,并且在在U形管道702插入换能支架2内时,由于折叠管道Ⅰ705和连接管道Ⅰ703之间设有扭簧Ⅰ,折叠管道Ⅱ706和连接管道Ⅱ704之间设有扭簧Ⅱ,折叠管道Ⅰ705和U形管道702连通,折叠管道Ⅱ706和U形管道702连通,使得折叠管道Ⅰ705和折叠管道Ⅱ706同样可以插入换能支架2内,并且在扭簧Ⅰ和扭簧Ⅱ的作用下,使得折叠管道Ⅰ705和折叠管道Ⅱ706拥有一定的复位能力,在折叠管道Ⅰ705和折叠管道Ⅱ706插入到换能支架2内时,扭簧Ⅰ和扭簧Ⅱ使得折叠管道Ⅰ705和折叠管道Ⅱ706复位插入混流筒Ⅰ401内,两个连接管道Ⅰ703分别一前一后设置,连接管道Ⅱ704分别一前一后设置,使得折叠管道Ⅰ705内的水流可以从一端流入从另一端流出,连接管道Ⅱ704内的水流可以从一端流入从另一端流出,如图2所示,两个连接管道Ⅰ703之间的距离可以根据使用情况具体设置,两个连接管道Ⅱ704之间的距离可以根据使用情况具体设置,将冷水从U形管道702的上端通入,从U形管道702的下端流出,冷水可以流入折叠管道Ⅰ705和折叠管道Ⅱ706内;将热水通入入水管道202内,同时启动电机301,电机301的输出轴开始转动,电机301的输出轴带动齿轮302进行转动,齿轮302带动行星齿轮Ⅰ303进行转动,行星齿轮Ⅰ303带动齿圈Ⅰ304进行转动,齿圈Ⅰ304带动行星齿轮Ⅱ306进行转动,行星齿轮Ⅱ306带动齿圈Ⅱ307进行转动,电机301的输出轴带动混流筒Ⅲ601进行转动,齿圈Ⅰ304带动混流筒Ⅱ501进行转动,齿圈Ⅱ307带动混流筒Ⅲ601进行转动,混流筒Ⅰ401、混流筒Ⅱ501和混流筒Ⅲ601将热水进行分割,混流筒Ⅰ401、混流筒Ⅱ501和混流筒Ⅲ601将换能支架2内的水进行分层,形成多个混流层,换能管道7位于混流机构Ⅰ4、混流机构Ⅱ5和混流机构Ⅲ6之间,混流机构Ⅰ4、混流机构Ⅱ5和混流机构Ⅲ6的转动速度和转动方向均不相同,使热媒与冷水形成强烈的逆流和错流,从而形成传热学中的完美换热流动方式,促使热媒充分放热,冷水充分吸热;由于折叠管道Ⅰ705和折叠管道Ⅱ706的存在使得换能管道7不但可以和换能支架2完成快速的安装更换,并且由于折叠管道Ⅰ705和折叠管道Ⅱ706位于混流筒Ⅰ401内,进一步增加了冷热交换。When in use, insert the
当然,上述说明并非对本发明的限制,本发明也不仅限于上述举例,本技术领域的普通技术人员在本发明的实质范围内所做出的变化、改型、添加或替换,也属于本发明的保护范围。Of course, the above description does not limit the present invention, and the present invention is not limited to the above examples. Changes, modifications, additions or substitutions made by those of ordinary skill in the art within the essential scope of the present invention also belong to the present invention. protected range.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010109396.9A CN111238260B (en) | 2020-02-22 | 2020-02-22 | U-shaped pipe positive displacement heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010109396.9A CN111238260B (en) | 2020-02-22 | 2020-02-22 | U-shaped pipe positive displacement heat exchanger |
Publications (2)
Publication Number | Publication Date |
---|---|
CN111238260A CN111238260A (en) | 2020-06-05 |
CN111238260B true CN111238260B (en) | 2020-09-22 |
Family
ID=70864261
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010109396.9A Active CN111238260B (en) | 2020-02-22 | 2020-02-22 | U-shaped pipe positive displacement heat exchanger |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111238260B (en) |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5734553A (en) * | 1980-08-12 | 1982-02-24 | Yamashiyou Denki Sangyo Kk | Processor for photosensitive film or the like |
EP2987522B1 (en) * | 2010-05-18 | 2018-10-24 | Ivax Pharmaceuticals Ireland | Dose counters for inhalers |
CN205808184U (en) * | 2016-06-13 | 2016-12-14 | 东莞市恒丰换热器有限公司 | High-efficiency U-tube volumetric heat exchanger |
CN206716416U (en) * | 2017-04-06 | 2017-12-08 | 衢州圣荣电子科技有限公司 | A kind of multi-stage rotary architectural engineering filter |
CN206739930U (en) * | 2017-04-27 | 2017-12-12 | 绍兴金泰容器制造有限公司 | A kind of vertical flow guiding type positive displacement water water- to-water heat exchanger |
JP6973009B2 (en) * | 2017-12-13 | 2021-11-24 | トヨタ自動車株式会社 | Stirring mechanism and manufacturing method of stirring mechanism |
CN207730060U (en) * | 2017-12-29 | 2018-08-14 | 绍兴金泰容器制造有限公司 | A kind of U heat exchange can front and back reciprocally swinging volumetric heat exchanger |
CN110252724B (en) * | 2019-07-29 | 2020-10-13 | 林美丽 | Aquatic product cleaning and screening device |
-
2020
- 2020-02-22 CN CN202010109396.9A patent/CN111238260B/en active Active
Also Published As
Publication number | Publication date |
---|---|
CN111238260A (en) | 2020-06-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202013125U (en) | Novel fluid impact rotary-type heat exchanger | |
CN201242373Y (en) | Composite casing tube double helix heat exchanger | |
CN207635933U (en) | A kind of reinforced heat exchanger of built-in rotating fan blades formula | |
CN111238260B (en) | U-shaped pipe positive displacement heat exchanger | |
CN209279723U (en) | A kind of spherical heat exchanger with Dual heat exchange effect | |
CN202119298U (en) | Composite type heat exchanger | |
CN201433876Y (en) | Cooler core body structure employing compressed air and water-heat exchange for heat dissipation | |
CN213746687U (en) | Surface type heat exchanger applied to low-temperature economizer system | |
CN206860267U (en) | Heat exchanging silencer | |
CN212057671U (en) | A heat recovery and utilization device for HVAC | |
CN115164618A (en) | A multi-heat source solar heat exchanger with adjustable heat exchange area | |
CN222617675U (en) | A waterproof heat exchanger capable of uniform heat exchange | |
CN213778725U (en) | High-efficiency brazing type pipe shell heat exchanger | |
CN109482369B (en) | An energy-saving heating device for coal slime water | |
CN212390399U (en) | Multi-tube type efficient energy-saving environment-friendly boiler | |
CN204478872U (en) | A kind of gas-liquid heat-exchange | |
CN201803617U (en) | Novel heat exchanger | |
CN201199137Y (en) | Brazing sheet type heat exchanger | |
CN2893618Y (en) | Tractor Exhaust Gas Waste Heat Utilization Heat Exchanger | |
CN2856908Y (en) | Steam/water directly mixed heat exchanger | |
CN204043446U (en) | A kind of compact tubular type finned heat exchanger | |
CN222256502U (en) | Plate-type coal economizer with flow field adjusting structure | |
CN219656679U (en) | Energy-saving efficient heat exchanger | |
CN218066056U (en) | Energy-saving multiplier | |
CN221882277U (en) | A low-carbon energy-saving heat exchanger |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |