CN220002322U

CN220002322U - Volcanic mud bath treatment device

Info

Publication number: CN220002322U
Application number: CN202321684663.0U
Authority: CN
Inventors: 高亚民; 杨帅; 程世哲; 闫首弟
Original assignee: Shenyang Hong Cheng Shiji Refrigeration Equipment Co ltd
Current assignee: Shenyang Hong Cheng Shiji Refrigeration Equipment Co ltd
Priority date: 2023-06-29
Filing date: 2023-06-29
Publication date: 2023-11-14
Anticipated expiration: 2033-06-29

Abstract

The utility model discloses a volcanic mud bath treatment device, relates to the technical field of mud bath equipment, and aims to solve the problems of inconvenience in temperature control and filtration of the mud bath equipment. The utility model is provided with a heat exchange system with an evaporator and a condenser, then the condenser is communicated with a first heat exchanger, and under the heating state, the heat released by the condenser is transferred to the first heat exchanger to heat mud; under the cooling state, pipeline switching is carried out through the valve, the condenser is cooled by source water, the evaporator is communicated with the first heat exchanger, the heat release and cooling of the evaporator are utilized to transfer the cooling capacity to the first heat exchanger, and then the mud is cooled. On the basis, the blast is used for overturning the slurry to prevent hardening, meanwhile, the blast can also control the temperature, and the temperature change of the first heat exchanger is used for assisting the temperature rise and the temperature reduction of the slurry.

Description

Volcanic mud bath treatment device

Technical Field

The utility model relates to the technical field of mud bath equipment, in particular to a volcanic mud bath treatment device.

Background

The volcanic mud bath is a brand new bath seed, which means that people are soaked in the volcanic mud, and the volcanic mud has a plurality of mineral elements beneficial to human bodies, so the volcanic mud bath has a health care effect.

The prior volcanic mud bath technology mainly has the problems that heating and constant temperature can only be carried out and filtering are difficult, specifically, on one hand, the prior equipment can only be heated to keep constant temperature, which is feasible for artificial mud, but for a part of natural volcanic mud, the temperature is required to be reduced when the volcanic mud bath is used, because the volcanic mud bath is usually used in a high-end bathing place, customer satisfaction is critical, and supercooling or overheating can influence experience or complain, so that the prior equipment which can only be heated obviously has limitations; on the other hand, volcanic mud is easy to harden, so that certain obstacle is caused to filtration. The current equipment does not better address the above-mentioned needs, thus limiting the popularization of volcanic mud baths.

Disclosure of Invention

The utility model provides a volcanic mud bath treatment device, which comprises: the system comprises a first heat exchanger, an evaporator, a condenser, a heat exchange pump and a slurry pump; the device comprises a first heating pipeline, a second heating pipeline, a first refrigerating pipeline and a second refrigerating pipeline;

the heat release side of the evaporator is connected with the first heating pipeline, and the other end of the first heating pipeline is used as an inlet and an outlet of a water source;

the two pipelines of the first heating pipeline are respectively provided with a first heating valve;

the heat absorption side of the evaporator is connected with the heat release side of the condenser through a pipeline, and a compressor is arranged between the heat absorption side and the heat release side of the condenser;

the heat absorption side of the condenser is connected with one side of the first heat exchanger through the second heating pipeline;

the other side of the first heat exchanger is connected with a filtering pipeline, and the slurry pump is arranged on the filtering pipeline;

the two pipelines of the second heating pipeline are respectively provided with a second heating valve; the heat exchange pump is arranged on the second heating pipeline;

the first refrigeration pipeline and the second refrigeration pipeline are connected with the heat absorption side of the condenser and the first heating pipeline;

the first refrigeration pipeline is connected to one side of the second heating valve close to the condenser, and the second refrigeration pipeline is connected to one side of the second heating valve close to the first heat exchanger;

the first refrigeration pipeline is connected to one side of the first heating valve, which is far away from the evaporator, and the second refrigeration pipeline is connected to one side of the first heating valve, which is close to the evaporator.

The utility model is further provided with: the device comprises an exhaust pipeline, wherein an air pump is arranged on the exhaust pipeline, one end of the exhaust pipeline is communicated with the natural environment, and the other end of the exhaust pipeline is arranged in a mud pit.

The utility model is further provided with: the exhaust pipeline is provided with a second heat exchanger; the other side of the second heat exchanger is connected with one side of the first heat exchanger connected with a second heating pipeline through a hot air pipeline; and a hot air valve is arranged on the hot air pipeline.

The utility model is further provided with: still include cold air pipeline, cold air pipeline connect first heating pipeline with hot-blast pipeline, be provided with the cold air valve on the cold air pipeline.

The utility model is further provided with: the filter pipeline is also provided with a hair filter and a filter sand cylinder.

The utility model is further provided with: the filter pipeline is also provided with an ultraviolet sterilizer and a dosing pump, and an inlet of the dosing pump is connected with a dosing box.

The beneficial effects of the utility model are as follows:

the temperature rising and reducing regulation can be realized in the scheme, the temperature rising and reducing regulation is not limited to the control process which can only be used for temperature rising, the temperature can be better controlled, the slurry is stably maintained in a proper temperature range, and the method can be applied no matter the temperature of the newly filled slurry.

Under the continuous action of exhaust, the slurry can be continuously turned over, so that the slurry is not easy to harden, the filtering process is facilitated, and the slurry temperature is more uniform.

As the exhaust air has cold and hot conditions, the temperature rise and the temperature drop of the slurry can be assisted.

Drawings

FIG. 1 is a schematic diagram of the structure of the present utility model;

FIG. 2 is a schematic view of the structure of the present utility model in a heated state;

fig. 3 is a schematic view of the structure of the present utility model in a cold state.

Reference numerals: 11. a compressor; 12. an evaporator; 13. a condenser; 14. a throttle valve; 15. an electromagnetic valve; 16. a filter; 17. a ball valve; 21. a first heating line; 22. a second heating line; 31. a first refrigeration line; 32. a second refrigeration line; 4. a filter pipeline; 51. a hot air pipeline; 52. a cold air pipeline; 61. a first heat exchanger; 62. a second heat exchanger; 71. a hair filter; 72. a slurry pump; 73. filtering a sand cylinder; 74. an ultraviolet sterilizer; 75. a medicine-throwing box; 76. a drug administration pump; 81. a heat exchange pump; 82. an air pump; 9. an exhaust line; 101. a first heating valve; 102. a second heating valve; 103. a first refrigeration valve; 104. a second refrigeration valve; 105. a hot air valve; 106. and a cold air valve.

Detailed Description

Preferred embodiments of the present utility model are described below with reference to the accompanying drawings. It should be understood by those skilled in the art that these embodiments are merely for explaining the technical principles of the present utility model, and are not intended to limit the scope of the present utility model.

In the drawing, solid dots are arranged at the line crossing positions to indicate that the pipelines are communicated, and no solid dots at the line crossing positions indicate that the pipelines are not communicated.

The utility model provides a volcanic mud bath treatment device,

comprising the following steps: an evaporator 12, a condenser 13, a first heat exchanger 61, a second heat exchanger 62;

comprising the following steps: a first heating line 21, a second heating line 22, a first cooling line 31, and a second cooling line 32;

comprising the following steps: a filter pipeline 4 and an exhaust pipeline 9.

The heat absorbing side of the evaporator 12 and the heat releasing side of the condenser 13 are connected by a pipeline, a compressor 11 is arranged on a pipeline between an outlet of the heat absorbing side of the evaporator 12 and an inlet of the heat releasing side of the condenser 13, and a ball valve 17, a filter 16, an electromagnetic valve 15 and a throttle valve 14 are sequentially arranged on a pipeline between an outlet of the heat releasing side of the condenser 13 and an inlet of the heat absorbing side of the evaporator 12. The part is not different from the current heat exchange system, the operation process mainly comprises the steps of absorbing heat at the evaporator 12, doing work through the compressor 11 and then releasing heat at the condenser 13, and the part can be applied to an air conditioner and a heat pump, and the principle and the technology are mature, so that the description is omitted.

The first heating pipeline 21 is connected with an inlet and an outlet of the heat release side of the evaporator 12, and a first heating valve 101 is respectively arranged on the first heating pipeline 21 corresponding to the inlet and the outlet of the evaporator 12, and the pipe orifice at the other end of the first heating pipeline 21 is respectively used as an inlet and an outlet of a water source. The second heating pipeline 22 connects the heat absorbing side of the condenser 13 with one side of the first heat exchanger 61, two pipelines of the second heating pipeline 22 are respectively provided with a second heating valve 102, and in addition, the second heating pipeline 22 is also provided with a heat exchange pump 81 for providing power for the circulation of heat exchange medium between the condenser 13 and the first heat exchanger 61. The other side of the first heat exchanger 61 is connected to the filter line 4.

A hair filter 71, a slurry pump 72 and a filtering sand cylinder 73 are sequentially arranged on a pipeline of the filtering pipeline 4 corresponding to the inlet of the first heat exchanger 61 according to the flowing direction; an ultraviolet sterilizer 74 and a dosing pump 76 are sequentially arranged on a pipeline of the filtering pipeline 4 corresponding to the outlet of the first heat exchanger 61 according to the flowing direction, and the inlet of the dosing pump 76 is connected with a dosing box 75. The slurry pump 72 is operated to circulate and convey slurry through the filter tube, and to filter, exchange heat and sterilize the slurry during operation. Wherein the hair filter 71 (model HK-SED), the filter sand cylinder 73 (model JJBQ-600), the ultraviolet sterilizer 74 (model SYZW-80-N), the dosing pump 76 and the dosing tank 75 are all the prior art products in the bath equipment field.

The first refrigeration line 31 connects the first heating line 21 and the second heating line 22, and one first refrigeration valve 103 is provided on each of the two pipes of the first refrigeration line 31. The second cooling line 32 connects the first heating line 21 and the second heating line 22, and a second cooling valve 104 is provided in each of the two pipes of the second cooling line 32. The differences are: the connection position of the first refrigeration pipeline 31 and the second heating pipeline 22 is positioned on a pipeline of the second heating valve 102, which is close to one side of the first heat exchanger 61; the connection position of the second cooling pipeline 32 and the second heating pipeline 22 is located on a pipeline of one side of the second heating valve 102, which is close to the condenser 13. The first refrigeration pipeline 31 is connected with the first heating pipeline 21 and is positioned at one side of the first heating valve 101 far away from the evaporator 12, and the second refrigeration pipeline 32 is connected with the first heating pipeline 21 and is positioned at one side of the first heating valve 101 near the evaporator 12.

One end of the exhaust pipeline 9 is communicated with the natural environment, the other end of the exhaust pipeline is arranged in a mud pit, and the second heat exchanger 62 and the air pump 82 are sequentially arranged according to the flow direction. First, the action of the exhaust pipe 9 will be described, and when the air pump 82 is operated, air can be blown into the slurry tank, and a large amount of generated air bubbles can cause slurry to tumble, so that slurry hardening can be suppressed, and the filtering difficulty can be solved. In addition, the slurry is beneficial to heat transfer of the slurry after the slurry is turned over, so that the temperature of the slurry is more uniform. A second heat exchanger 62 is provided to assist in the warming and cooling of the slurry. Specifically: the other side of the second heat exchanger 62 is connected to the first heat exchanger 61 via the hot air line 51 and to one side of the second heating line 22. A hot air valve 105 is provided in each of the two pipes of the hot air line 51.

The cold air pipeline 52 is connected with the hot air pipeline 51 and the first heating pipeline 21, and two cold air valves 106 are respectively arranged on two pipelines of the cold air pipeline 52. The connection position of the cold air pipeline 52 and the hot air pipeline 51 is positioned on one side of the hot air valve 105 close to the second heat exchanger 62.

When the temperature raising process is performed: the first refrigeration valve 103, the second refrigeration valve 104 and the cool air valve 106 are closed, and the first heating valve 101, the second heating valve 102 and the hot air valve 105 are opened. The source water enters the evaporator 12 through the first heating pipeline 21 and releases heat, and according to the above, the heat released by the evaporator 12 is released at the condenser 13 and transferred to the first heat exchanger 61 through the second heating pipeline 22, and the mud also enters the first heat exchanger 61 under the action of the mud pump 72, so that the heat released by the condenser 13 acts on the mud to heat the mud. Meanwhile, referring to fig. 2, in order to facilitate understanding of the temperature raising process, the pipes and valves involved in the temperature lowering related process are omitted appropriately in fig. 2. Under the action of the heat exchange pump 81, the fluid medium after absorbing heat from the condenser 13 also reaches the second heat exchanger 62 through the hot air pipeline 51, and the air flow is released at the second heat exchanger 62, so that the air flow is heated, and the temperature rising speed of the slurry is higher.

When the temperature reduction process is performed: the first heating valve 101, the second heating valve 102 and the hot air valve 105 are closed, and the first refrigeration valve 103, the second refrigeration valve 104 and the cold air valve 106 are opened. Referring to fig. 3, for ease of understanding the cooling process, the piping and valves involved in the temperature rise related process are omitted from fig. 3 as appropriate. The source water is directly conveyed to the heat absorbing side of the condenser 13 through the first refrigerating pipeline 31, and plays a role of cooling water for cooling the condenser 13. The first heat exchanger 61 and the evaporator 12 are connected through the second refrigeration pipeline 32, and the medium in the pipeline circulates and continuously releases heat and cools at the heat release side of the evaporator 12 under the action of the heat exchange pump 81, so that the direction of heat transfer at the first heat exchanger 61 is changed, and in this case, the mud entering the first heat exchanger 61 is not heat-released but heat-released, thereby realizing the cooling function of the mud. At the same time, the low-temperature medium enters the cold air line 52 and reaches the second heat exchanger 62 by the heat exchange pump 81. The second heat exchanger 62 absorbs heat from the air stream and cools the air stream, thereby increasing the cooling rate of the slurry.

To sum up. The temperature rising and reducing regulation can be realized in the scheme, the temperature rising and reducing regulation is not limited to the control process which can only be used for temperature rising, the temperature can be better controlled, the slurry is stably maintained in a proper temperature range, and the method can be applied no matter the temperature of the newly filled slurry.

As the exhaust air has cold and hot conditions, the temperature rise and the temperature drop of the slurry can be assisted. It is important to note here that the heat exchange power of the heat exchanger is limited, and the heat exchange performance is further crushed after the second heat exchanger 62 is introduced. Taking the heating process as an example, after the first heat exchanger 61 reaches the rated heat exchange power, the second heat exchanger 62 can further extract the heat released by the condenser 13, so that the temperature of the heat absorbing side of the condenser 13 is lower, which is beneficial to the working efficiency of the heat exchange system of the evaporator 12 and the condenser 13. Taking the cooling process as an example, the second heat exchanger 62 can absorb more heat in the heat exchange process, so that the temperature of the heat release side of the evaporator 12 is higher, which is also beneficial to the working efficiency of the heat exchange system, namely the evaporator 12 and the condenser 13. In other words, more energy is saved.

While the utility model has been described with reference to a preferred embodiment, various modifications may be made and equivalents may be substituted for elements thereof without departing from the scope of the utility model, and in particular, the technical features set forth in the various embodiments may be combined in any manner so long as there is no structural conflict. The present utility model is not limited to the specific embodiments disclosed herein, but encompasses all technical solutions falling within the scope of the claims.

In the description of the present utility model, terms such as "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", and the like, which indicate a direction or a positional relationship, are based on the direction or the positional relationship shown in the drawings, are merely for convenience of description, and do not indicate or imply that the apparatus or elements must have a specific orientation, be constructed and operated in a specific orientation, and thus are not to be construed as limiting the present utility model. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.

Furthermore, it should be noted that, in the description of the present utility model, unless explicitly specified and limited otherwise, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be either fixedly connected, detachably connected, or integrally connected, for example; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present utility model can be understood by those skilled in the art according to the specific circumstances.

The terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, article, or apparatus/means that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, article, or apparatus/means.

Thus far, the technical solution of the present utility model has been described in connection with the preferred embodiments shown in the drawings, but it is easily understood by those skilled in the art that the scope of protection of the present utility model is not limited to these specific embodiments. Equivalent modifications and substitutions for related technical features may be made by those skilled in the art without departing from the principles of the present utility model, and such modifications and substitutions will fall within the scope of the present utility model.

Claims

1. A volcanic mud bath treatment device, comprising: a first heat exchanger (61), an evaporator (12), a condenser (13), a heat exchange pump (81) and a slurry pump (72); a first heating pipeline (21), a second heating pipeline (22), a first refrigerating pipeline (31) and a second refrigerating pipeline (32);

the heat release side of the evaporator (12) is connected with the first heating pipeline (21), and the other end of the first heating pipeline (21) is used as an inlet and an outlet of a water source;

the two pipelines of the first heating pipeline (21) are respectively provided with a first heating valve (101);

the heat absorption side of the evaporator (12) is connected with the heat release side of the condenser (13) through a pipeline, and a compressor (11) is arranged between the heat absorption side and the heat release side;

the heat absorption side of the condenser (13) is connected with one side of the first heat exchanger (61) through the second heating pipeline (22);

the other side of the first heat exchanger (61) is connected with a filtering pipeline (4), and the slurry pump (72) is arranged on the filtering pipeline (4);

two pipelines of the second heating pipeline (22) are respectively provided with a second heating valve (102); the heat exchange pump (81) is arranged on the second heating pipeline (22);

the first refrigeration pipeline (31) and the second refrigeration pipeline (32) are connected with the heat absorption side of the condenser (13) and the first heating pipeline (21);

the first refrigeration pipeline (31) is connected to one side of the second heating valve (102) close to the condenser (13), and the second refrigeration pipeline (32) is connected to one side of the second heating valve (102) close to the first heat exchanger (61);

the first refrigerating pipeline (31) is connected to one side, far away from the evaporator (12), of the first heating valve (101), and the second refrigerating pipeline (32) is connected to one side, close to the evaporator (12), of the first heating valve (101).

2. The volcanic mud bath treatment device according to claim 1, wherein: the device comprises an exhaust pipeline, wherein an air pump is arranged on the exhaust pipeline, one end of the exhaust pipeline is communicated with the natural environment, and the other end of the exhaust pipeline is arranged in a mud pit.

3. The volcanic mud bath treatment device according to claim 2, wherein: a second heat exchanger (62) is arranged on the exhaust pipeline; the other side of the second heat exchanger (62) is connected with one side of the first heat exchanger (61) and connected with one side of the second heating pipeline (22) through a hot air pipeline (51); a hot air valve (105) is arranged on the hot air pipeline (51).

4. A volcanic mud bath treatment device according to claim 3, characterized in that: still include cold air pipeline (52), cold air pipeline (52) connect first heating pipeline (21) with hot-blast pipeline (51), be provided with cold air valve (106) on cold air pipeline (52).

5. The volcanic mud bath treatment device according to claim 1, wherein: the filtering pipeline (4) is also provided with a hair filter (71) and a filtering sand cylinder (73).

6. The volcanic mud bath treatment device according to claim 1, wherein: the filter pipeline (4) is also provided with an ultraviolet sterilizer (74) and a dosing pump (76), and an inlet of the dosing pump (76) is connected with a dosing box (75).