The novel gas-liquid heat-exchanger rig
Technical field
The present invention relates to a kind of refrigeration technology field that belongs to, be specifically related to a kind of novel gas-liquid heat-exchanger rig.
Background technology
Heat exchanger is the vitals of temperature controlling instruments such as air-conditioning, heat exchanger, and the power of its performance and function directly has influence on the operating efficiency and the service life of temperature controlling instruments.Use form to be mainly pipe type heat exchanger and parallel-flow heat exchanger at present at the gas-liquid heat-exchange aspect cabinet air conditioner and the heat exchanger, basically combine by piping and sheet system, because this type of heat exchanger self structure limits, when heat exchange, need reach final heat exchange purpose by the convection current that fan is strengthened air.Plant maintenance and operation cost height also are subjected to the influence of fan life the service life of complete equipment.Improve heat exchange efficiency, the reduction equipment volume prolongs service life of equipment, reduces the equipment cost expense, is the important proposition that improves the heat exchanger quality, also is simultaneously one of main contents of temperature controlling instruments refrigeration system development.
Summary of the invention
The present invention seeks to: a kind of novel gas-liquid heat-exchanger rig that only depends on self structure and can reach the heat exchange purpose by the free convection of air is provided, must carry out the fluid media (medium) heat exchange and cause volume big by auxiliary equipment such as fan and heat exchange pipings, the problem that cost is high in order to solve current heat exchanger.
Technical scheme of the present invention is: a kind of novel gas-liquid heat-exchanger rig comprises main heat exchange plate and some auxiliary heat exchange fins; It is characterized in that: described main heat exchange plate is provided with liquid inlet and outlet, inner then be provided with the liquid inlet and outlet sprue that links to each other with liquid inlet and outlet respectively, and the vertical parallel interval of described auxiliary heat exchange fin is arranged on the main heat exchange plate, be provided with the liquid inlet and outlet runner that links to each other with the liquid inlet and outlet sprue respectively in the every auxiliary heat exchange fin, in every auxiliary heat exchange fin, also be provided with the inferior runner that some vertical perforations connect aforementioned liquid inlet and outlet runner simultaneously.
Further, the sprue of liquid inlet and outlet described in the present invention be arranged in parallel up and down in the main heat exchange intralamellar part, and described liquid inlet and outlet runner also be arranged in parallel up and down in every auxiliary heat exchange fin inside.
Further, liquid inlet and outlet described in the present invention is located at the side of main heat exchange plate.
Preferably, liquid inlet and outlet described in the present invention is located at the homonymy of main heat exchange plate.
Preferably, every auxiliary heat exchange fin is provided with the main heat exchange plate is vertical described in the present invention, and the feed liquor runner in the described every auxiliary heat exchange fin is vertical with the feed liquor sprue, and the fluid runner is vertical with the fluid sprue.
Preferably, the surface of auxiliary heat exchange fin is corrugated described in the present invention, with further increase heat exchange area, improves radiating effect.
The sprue of liquid inlet and outlet described in the present invention, the cross section of liquid inlet and outlet runner and time runner can be circle, and is perhaps oval, perhaps rectangle, perhaps triangle.
Liquid inlet and outlet runner in liquid inlet and outlet sprue in the main heat exchange plate of the present invention and the every auxiliary heat exchange fin and time runner be common to constitute a circuitous parallel flow passages of connect, supplies the fluid media (medium) circulation.When the present invention specifically works, liquid inlet and outlet links to each other with the pipeline of conventional cooling cycle system respectively, fluid media (medium) is flowed into by the inlet of main heat exchange plate one side, after in the feed liquor sprue, compiling, in the feed liquor runner in every auxiliary heat exchange fin of parallel again inflow, and then flow in the fluid runner through some vertical inferior runners, be collected to the fluid sprue again, flow out by liquid outlet at last.When fluid media (medium) flows, carry out heat exchange by the surface and the outside air of assisting the heat exchange fin in auxiliary heat exchange fin.
Advantage of the present invention is:
1. this novel gas-liquid heat-exchanger rig provided by the invention, it comes the water conservancy diversion heat exchange by the multi-channel structure of specialized designs in main heat exchange plate and auxiliary heat exchange fin, and need not heat exchange piping in the routine techniques, also need not to be aided with fan, so not only dwindled volume, save cost, also prolonged service life.And, reduce the cost of temperature controlling instruments when integral installation of the present invention can significantly have been dwindled the temperature controlling instruments volume inside to temperature controlling instruments inside.
2. this novel gas-liquid heat-exchanger rig provided by the invention, liquid inlet and outlet runner in liquid inlet and outlet sprue in its main heat exchange plate and the every auxiliary heat exchange fin and time runner be common to constitute a circuitous parallel flow passages of connecting, for the fluid media (medium) circulation, and by the surface of a plurality of auxiliary heat exchange fins and the free convection enforcement heat exchange of outside air, heat exchange area is big, the heat exchange efficiency height.Especially when auxiliary heat exchange fin surface design became corrugated, heat exchange area was bigger, and heat exchange efficiency is higher.
Description of drawings
Below in conjunction with drawings and Examples the present invention is further described:
Fig. 1 is the perspective view of a kind of specific embodiment of the present invention;
Fig. 2 is another visual angle view of Fig. 1;
Fig. 3 is the rearview of the embodiment of Fig. 1;
Fig. 4 is the A-A profile of Fig. 3;
Fig. 5 is the B-B profile of Fig. 3;
Fig. 6 is the vertical view of Fig. 3;
Fig. 7 is the partial sectional perspective view of Fig. 2.
Wherein: 1, main heat exchange plate; 2, auxiliary heat exchange fin; 3, inlet; 4, liquid outlet; 5, feed liquor sprue; 6, fluid sprue; 7, feed liquor runner; 8, fluid runner; 9, inferior runner.
The specific embodiment
Embodiment: in conjunction with Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6 and shown in Figure 7, this novel gas-liquid heat-exchanger rig that present embodiment provides, it together is made of main heat exchange plate 1 and 10 auxiliary heat exchange fins 2 being fixed on the main heat exchange plate 1, the side homonymy of described main heat exchange plate 1 is provided with liquid inlet and outlet 3,4, inner then be provided with the liquid inlet and outlet sprue 5,6 that links to each other with liquid inlet and outlet 3,4 respectively, and liquid inlet and outlet sprue 5,6 be arranged in parallel up and down in main heat exchange plate 1 inside in the present embodiment.Described 10 auxiliary heat exchange fin 2 vertical parallel interval are arranged on the main heat exchange plate 1, be provided with the liquid inlet and outlet runner 7,8 that links to each other with liquid inlet and outlet sprue 5,6 respectively in the every auxiliary heat exchange fin 2, and the runner of liquid inlet and outlet described in the present embodiment 7,8 be arranged up and down in every auxiliary heat exchange fin 2 inside also in parallel.Simultaneously in every auxiliary heat exchange fin 2, also be provided with the inferior runner 9 that some vertical perforations connect aforementioned liquid inlet and outlet runner 7,8.And the feed liquor runner 7 in the every auxiliary heat exchange fin 2 and the 1 vertical setting of main heat exchange plate in the present embodiment, every auxiliary heat exchange fin 2 is vertical with feed liquor sprue 5, and fluid runner 8 is vertical with fluid sprue 6.The surface of described every auxiliary heat exchange fin 2 is corrugated.Described liquid inlet and outlet sprue 5,6, the cross section of liquid inlet and outlet runner 7,8 and time runner 9 is circular.
Liquid inlet and outlet runner 7,8 in liquid inlet and outlet sprue 5,6 in the main heat exchange plate 1 of present embodiment and the every auxiliary heat exchange fin 2 and inferior runner 9 be common to constitute a circuitous parallel flow passages of connect, confession fluid media (medium) circulation.When present embodiment is specifically worked, liquid inlet and outlet 3,4 links to each other with the pipeline of conventional cooling cycle system respectively, fluid media (medium) is flowed into by the inlet 3 of main heat exchange plate 1 one sides, after in feed liquor sprue 5, compiling, in the feed liquor runner 7 in every auxiliary heat exchange fin 2 of parallel again inflow, and then flow in the fluid runner 8 through some vertical inferior runners 9, be collected to fluid sprue 6 again, at last by liquid outlet 4 outflows.When fluid media (medium) flows, carry out heat exchange by the surface and the outside air of assisting heat exchange fin 2 in auxiliary heat exchange fin 2.
Certainly, more than only be concrete exemplary applications of the present invention, protection scope of the present invention is not constituted any limitation.In addition to the implementation, the present invention can also have other embodiment.All employings are equal to the technical scheme of replacement or equivalent transformation formation, all drop within the present invention's scope required for protection.