Quick-mixing water mixing furnace

Abstract

The utility model provides a mixed water furnace of quick mixed water, including mixed furnace, and be located mixed furnace side portion, and present upper and lower distribution to form the height difference's cold water inlet and hot water inlet, cold water inlet department is provided with first dispersion mechanism, first dispersion mechanism makes the cold water that enters mixed boiler form a plurality of downward hot water flow's guide mixed track, be located the second dispersion mechanism of hot water inlet department, second dispersion mechanism forms the outward expansion type mixed track that a plurality of directions spread to the periphery with hot water inlet as midpoint, to interfere with the water temperature of hot water inlet periphery, the utility model discloses through the setting of height difference's water inlet setting and dispersion mechanism, make the distribution of cold water and hot water more uniform, promote the even mixing of quick.

Description

Technical Field

[0001] This utility model relates to the field of mixing technology for water of different temperatures, such as hot and cold water, and particularly to a water mixing furnace for rapid water mixing. Background Technology

[0002] In existing technologies, in the preparation of various beverages or cooking, there are situations where ingredients or water at different temperatures are mixed. The existing mixing method is to directly pour hot and cold water into the inlet at the same height and then mix them. However, this method of setting up the cold and hot water directly contact each other, which lacks a height difference and results in poor mixing effect. Utility Model Content

[0003] The purpose of this invention is to provide a water mixing furnace for rapid water mixing, which utilizes height difference and dispersion mechanism to allow hot and cold water to be better dispersed and then mixed, thereby improving the mixing effect.

[0004] To achieve the above objectives, this utility model is implemented through the following technical solution.

[0005] Rapid water mixing boilers, including, A mixing furnace, and cold water inlet and hot water inlet located on the side of the mixing furnace and distributed vertically to form a height difference; A first dispersing mechanism is provided at the cold water inlet, which causes the cold water entering the mixing boiler to form several downward hot water flow guiding mixing trajectories. The second dispersion mechanism located at the hot water inlet forms an outward-expanding mixing trajectory that spreads outward in several directions from the hot water inlet as the center point, thereby interfering with the water temperature around the hot water inlet.

[0006] Furthermore, the cold water inlet is vertically disposed on the outside of the mixing furnace, and a recess is provided on the inner wall of the mixing furnace at a position corresponding to the inlet to form the first dispersing mechanism, and the recess has a downward inclined guiding tendency.

[0007] Furthermore, the recess forms an elliptical structure that covers the cold water inlet. Starting from the cold water inlet, the guiding trend gradually increases in thickness from the cold water inlet to the downward direction until it is flush with the inner wall of the mixing furnace.

[0008] Furthermore, the guiding trend forms an angle of 30°-60° with the horizontal direction at the cold water inlet.

[0009] Furthermore, the hot water inlet is vertically positioned near the bottom of the mixing furnace, and the inner wall of the mixing furnace is recessed at the hot water inlet, forming several outwardly diffusing inclined paths at the recess to constitute the second dispersion mechanism.

[0010] Furthermore, the recessed area is centered on the hot water inlet, with several guide lines radiating outwards.

[0011] Furthermore, the thickness of the guide sloping line gradually increases from near the hot water inlet to the other end.

[0012] Furthermore, there is at least one cold water inlet and at least two hot water inlets, and the two hot water inlets are symmetrically arranged with respect to the extension line formed by the cold water inlet along the height direction of the mixing furnace as the axis of symmetry.

[0013] Furthermore, it also includes a probe located on the mixing furnace and near the cold water inlet, the guiding mixing trajectory forming an avoidance route around the probe.

[0014] Furthermore, the probe is a temperature sensor probe or a water level sensor probe.

[0015] The beneficial effects of this utility model are as follows: In this invention, the height difference is utilized, and during mixing, the density difference between hot and cold water is taken into account. Due to the density difference, the denser water moves downwards, and the less dense water moves upwards, promoting rapid and uniform mixing. This principle can be explained further, and the mixture can be dispersed and guided before mixing, allowing for mixing in multiple directions and improving mixing efficiency. Attached Figure Description

[0016] Figure 1 One of the structural schematic diagrams of the rapid water mixing furnace provided by this utility model; Figure 2 The second structural schematic diagram of the rapid water mixing furnace provided by this utility model; Figure 3 A cross-sectional view of the rapid water mixing furnace provided by this utility model; Figure 4 The path direction diagram of the dispersive mechanism provided by this utility model; In the picture: 1. Mixing furnace; 2. Cold water inlet; 3. Hot water inlet; 4. First dispersion mechanism; 5. Second dispersion mechanism; 6. Probe; 7. First circulation pipe; 8. Second circulation pipe. Detailed Implementation

[0017] The present invention will now be described in detail with reference to the embodiments shown in the accompanying drawings. However, it should be noted that these embodiments are not intended to limit the present invention. Equivalent transformations or substitutions in function, method, or structure made by those skilled in the art based on these embodiments are all within the protection scope of the present invention.

[0018] See attached document Figure 1-4As shown, the rapid water mixing furnace in this embodiment includes a mixing furnace 1, and a cold water inlet 2 and a hot water inlet 3 located on the side of the mixing furnace and distributed vertically to form a height difference. In this embodiment, by utilizing this height difference, the denser cold water will move downwards due to its relative weight, thus accelerating the addition speed of the cold water. The hot water, due to its lower density, tends to move upwards when mixing with the cold water. That is, the denser water moves downwards and the less dense water moves upwards, thus accelerating the mixing efficiency.

[0019] A first dispersing mechanism 4 is provided at the cold water inlet 2. The first dispersing mechanism 4 causes the cold water entering the mixing boiler to form several downward hot water flow guiding mixing trajectories. For cold water, it mainly moves downwards towards the hot water, and at this time it only needs to be dispersed first to avoid accumulation mixing. The second dispersion mechanism 5 is located at the hot water inlet 3. The second dispersion mechanism 5 forms an outward diffusion mixing trajectory that spreads outward in several directions from the hot water inlet as the center point, thereby interfering with the water temperature around the hot water inlet. In this embodiment, the second dispersion mechanism 5 diffuses the hot water outward in an outward diffusion manner, so that it can be well dispersed, thereby mixing with more cold water as soon as possible. At the same time, some of it moves downward, increasing the mixing temperature around its periphery.

[0020] Furthermore, the cold water inlet 2 is vertically positioned on the outside of the mixing furnace 1, and a recess is provided on the inner wall of the mixing furnace 1 at a position corresponding to the inlet 2 to form the first dispersing mechanism 4. The recess has a downward-sloping guiding tendency. In this embodiment, the vertical positioning here causes the cold water to flow into the furnace, which is already moving downwards faster due to gravity. Combined with the guiding tendency, its downward flow speed will be even faster.

[0021] Specifically, the recess forms an elliptical structure that completely covers the cold water inlet 2. Furthermore, starting from the cold water inlet 2, the thickness gradually increases downwards until it is flush with the inner wall of the mixing furnace 1. This design ensures that the final thickness is equal to that of the mixing furnace 1, resulting in a relatively smooth inner wall.

[0022] Furthermore, the guiding trend forms an angle of 30°-60° with the horizontal direction at the cold water inlet 2.

[0023] In this embodiment, the hot water inlet 3 is vertically located near the bottom of the mixing furnace, and the inner wall of the mixing furnace 1 is recessed at the hot water inlet 3, forming several outwardly diffusing inclined paths at the recess to constitute the second dispersion mechanism 5.

[0024] Furthermore, the recessed area is radiating outwards from the hot water inlet 3 as the center, with several guide lines pointing outwards. In this embodiment, the thickness of the guide lines gradually increases from near the hot water inlet 3 to the other end.

[0025] In this embodiment, there is at least one cold water inlet 2 and at least two hot water inlets 3, with the two hot water inlets 3 symmetrically arranged about the extension line formed by the cold water inlets 2 along the height direction of the mixing furnace 1. With more hot water inlets and fewer cold water inlets, the bottom is primarily heated, thus accelerating the overall mixing speed. Simultaneously, the symmetrical arrangement of the hot water inlets on both sides of the cold water inlets allows for a larger influx of hot water, which then flows from both sides towards the cold water inlet in the center.

[0026] To prevent overflow, a probe 6 is also provided on the mixing furnace 1 and near the cold water inlet 2. The guiding mixing trajectory forms an avoidance route around the probe 6, so that the cold water flows into the furnace and the water outlet direction is parallel to the boiler, so as to avoid water spraying towards the probe, which would cause the water level probe to misjudge and affect cooking.

[0027] Specifically, the probe 6 is a temperature sensor probe or a water level sensor probe.

[0028] In this embodiment, the height difference and density difference are cleverly utilized so that the denser cold water, which can be drawn in from the top by gravity, will move rapidly downwards and mix with the hot water. Meanwhile, the hot water, which has a relatively lower density, will be forced to move upwards and mix with the hot water at the higher position. Compared with other mixing methods, this mixing method has a faster mixing speed and better mixing efficiency.

[0029] The working principle of this invention is that during mixing, cold water flows from top to bottom, and combined with gravity, it forms a strong impact force. At this time, through its own gravity and impact force, it can flow downward through fewer pipes. When hot water is added, it flows from bottom to top, and at this time, the hot water diffuses to the side. The whole process relies entirely on itself, which makes the temperature of the mixing furnace uniform. In this embodiment, the gravity difference between cold water and hot water is used to form many diffusion holes. Then, with the addition of r-angle on the pipe, a diffusion mechanism is formed, thereby forming multiple impacts and mixing, and accelerating the mixing efficiency.

[0030] In practical use, a cold water inlet 2 and a hot water inlet 3 are respectively installed on the side of the mixing furnace 1. Then, a first dispersion mechanism 4 and a second dispersion mechanism 6 are installed inside the mixing furnace 1. A connecting pipe is installed at the bottom of the first dispersion mechanism 4, which is directly connected to the drain outlet below. However, the dispersion range formed by the dispersion mechanism is larger than the drainage area at the drain outlet, that is, the dispersed water is relatively more than the discharged water. Then, the discharged water flows back to the cold water inlet 2 through the first circulation pipe 7 for repeated circulation and cold water addition. Of course, it can also be directly discharged into the recovery tank. As for the hot water inlet 3, it is connected to the second dispersion mechanism 6 inside the mixing furnace 1. After being dispersed, some of the water flows back to the hot water inlet 3 through the second circulation pipe 8, or is discharged into the recovery tank through the pipe.

[0031] The detailed descriptions listed above are merely specific descriptions of feasible implementations of this utility model, and are not intended to limit the scope of protection of this utility model. All equivalent implementations or modifications made without departing from the spirit of this utility model should be included within the scope of protection of this utility model.

[0032] It will be apparent to those skilled in the art that this invention is not limited to the details of the exemplary embodiments described above, and that it can be implemented in other specific forms without departing from the spirit or essential characteristics of this invention. Therefore, the embodiments should be considered illustrative and non-limiting in all respects, and the scope of this invention is defined by the appended claims rather than the foregoing description. Thus, it is intended that all variations falling within the meaning and scope of equivalents of the claims be included within this invention. No reference numerals in the claims should be construed as limiting the scope of the claims.

[0033] Furthermore, it should be understood that although this specification describes embodiments, not every embodiment contains only one independent technical solution. This narrative style is merely for clarity. Those skilled in the art should consider the specification as a whole, and the technical solutions in each embodiment can also be appropriately combined to form other embodiments that can be understood by those skilled in the art.

Claims

1. A rapid water mixing furnace, characterized in that, include, A mixing furnace, and cold water inlet and hot water inlet located on the side of the mixing furnace and distributed vertically to form a height difference; A first dispersing mechanism is provided at the cold water inlet, which causes the cold water entering the mixing boiler to form several downward hot water flow guiding mixing trajectories. The second dispersion mechanism located at the hot water inlet forms an outward-expanding mixing trajectory that spreads outward in several directions from the hot water inlet as the center point, thereby interfering with the water temperature around the hot water inlet.

2. The rapid water mixing furnace according to claim 1, characterized in that, The cold water inlet is vertically disposed on the outside of the mixing furnace, and a recess is provided on the inner wall of the mixing furnace at the position corresponding to the inlet to form the first dispersing mechanism, and the recess forms a downward inclined guiding trend.

3. The rapid water mixing furnace according to claim 2, characterized in that, The recess forms an elliptical structure that covers the cold water inlet. Starting from the cold water inlet, the guiding trend gradually increases in thickness from the cold water inlet downwards until it is flush with the inner wall of the mixing furnace.

4. The rapid water mixing furnace according to claim 3, characterized in that, The guiding trend forms an angle of 30°-60° with the horizontal direction at the cold water inlet.

5. The rapid water mixing furnace according to claim 1, characterized in that, The hot water inlet is vertically located near the bottom of the mixing furnace. The inner wall of the mixing furnace is recessed at the hot water inlet, and several outwardly diffusing inclined paths are formed at the recess to constitute the second dispersion mechanism.

6. The rapid water mixing furnace according to claim 5, characterized in that, The recessed area has several guide lines radiating outwards from the hot water inlet.

7. The rapid water mixing furnace according to claim 6, characterized in that, The thickness of the guide line gradually increases from near the hot water inlet to the other end.

8. The rapid water mixing furnace according to claim 1, characterized in that, There is at least one cold water inlet and at least two hot water inlets, and the two hot water inlets are symmetrically arranged with the extension line formed by the cold water inlet along the height direction of the mixing furnace as the axis of symmetry.

9. The rapid water mixing furnace according to claim 1, characterized in that, It also includes a probe located on the mixing furnace and near the cold water inlet, the guiding mixing trajectory forming an avoidance route around the probe.

10. The rapid water mixing furnace according to claim 9, characterized in that, The probe is a temperature sensor probe or a water level sensor probe.

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