TWI815206B - Apparatus for producing an oxidation complex gas solution - Google Patents

Abstract

A pipeline module, a mixing tank, a storage tank, an electrolytic tank, a gas-liquid mixing device and electric control module are assembled in a cabinet body. The pipeline module is provided with a water pipeline, a salt-water pipeline and an aqueous solution pipeline. Wherein, a water supply is connected to an inlet water pipe of the storage tank and an inlet pipe of the salt-water pipeline through the salt-water pipeline. A outlet pipe of the mixing tank is connected to the storage tank and a reflow pipe of the mixing tank. The gas-liquid mixing device is connected to the inlet pipe through the aqueous solution pipeline. Therefore, the mixture of water and salt, the electrolysis of salt-water, and the mixture of gas and liquid are integrated into a miniaturized cabinet, so that the apparatus can be moved and transported conveniently and the pipelines of the apparatus can be simplified.

Description

Production equipment configuration of oxidation-based composite gaseous aqueous solution

The present invention relates to a production equipment capable of producing an oxidation-based composite gaseous aqueous solution, in particular to a miniaturized production equipment that integrates salt water mixing, salt water electrolysis, gas-liquid mixing and other devices into the same cabinet.

Since the oxidizing complex gas itself has an unpaired free active electron, the oxidizing complex gas aqueous solution has strong oxidizing ability and can be used to oxidize proteins, peptides, DNA or RNA of bacteria, viruses, molds and other pathogens. In order to eliminate these pathogens, and because the gaseous oxidation complex gas cannot provide users with convenience, it is currently used in medical and health, food processing, environmental protection, industrial water, Xumu breeding and sewage treatment: In other industries, most of them dissolve oxidizing complex gases in water to form oxidizing complex gaseous aqueous solutions, so that users can conveniently use oxidizing complex aqueous solutions for disinfection, sterilization, and deodorization.

Among them, the current manufacturing method of the oxidation-based composite gaseous aqueous solution mainly uses a conventional electrolysis device to electrolyze salt water to generate the aforementioned oxidation-system composite gas, and then the conventional electrolysis device dissolves the oxidation-system composite gas in water to form Oxidation-based composite gaseous aqueous solution, however, the overall volume of the conventional electrolysis device is too large, so that medical institutions that need to use the oxidation-system composite gaseous aqueous solution for a long time do not have enough space to place the conventional electrolysis device, making it impossible for medical institutions to Produce the oxidation-based complex gaseous aqueous solution by yourself, and then the medical institution must regularly purchase the oxidation-based complex gaseous aqueous solution from the manufacturer of the oxidation-based complex gaseous aqueous solution. Once the market encounters an unexpected situation, When the supply of oxidizing compound gaseous aqueous solution exceeds demand, medical institutions often do not have enough oxidizing compound gaseous aqueous solution for use.

Traditional production equipment requires a large volume for each device and requires many pipe connections between the devices. As a result, the equipment requires a large-scale site to be placed for production. Therefore, it is not suitable for ordinary consumers or some people who only need it. Manufacturers with small fields have caused most users with small needs to directly look for large manufacturing plants to purchase directly. However, the traditional business model of letting others produce and then purchase, once the market encounters a sudden shortage of supply, There may be a crisis of out-of-stock, so for some users such as hospitals who cannot lack disinfectant, a small and convenient disinfectant production device is needed.

The main purpose of the present invention is to provide a cabinet-type production equipment for the storage of oxidation-type composite gaseous aqueous solutions, so that three different processes such as brine mixing, electrolytic brine and gas-liquid mixing are integrated into a miniaturized cabinet, allowing the production equipment to It can be easily moved and transported, and can simplify the installation and configuration of pipelines between various components.

The secondary purpose of the present invention is to use the transportation pipeline module to return and connect multiple pipelines, and to operate the switching of multiple solenoid valves on each pipeline through the electronic control module, so that the production equipment can respond to different production procedures. Automatic production of oxidation system composite gaseous aqueous solution.

In order to achieve the above object, the production equipment configuration of the oxidation-based composite gaseous aqueous solution of the present invention includes: a cabinet, the interior of which is divided into a front space and a rear space. The front space is blocked by a movable first door panel, and the rear space The two sides are respectively covered by a movable second door panel and a third door panel, and the rear space is further divided into a lower passage, an upper right area, a lower right area and a left area.

A delivery pipeline module is disposed in the front space and can obtain clean water from a clean water supply source located outside the cabinet.

A salt water mixing tank is arranged in the upper right area of the rear space, connected to the delivery pipeline module to obtain the clean water, and mixes the clean water with a plurality of salt particles to form a salt water solution.

A salt water storage tank is arranged in the rear space and connected to the salt water mixing tank to obtain the salt water solution storage.

An electrolytic tank is arranged in the rear space and is connected to the brine mixing tank and the delivery pipeline module. It can obtain the brine solution from the brine storage tank and electrolyze the brine solution to form an oxidation-based composite gas.

A gas-liquid mixing device is disposed in the left area of the rear space and is connected to the electrolyzer and the delivery pipeline module to obtain the oxidation-based composite gas and the clean water respectively, and mix the oxidation-based composite gas with the Clean water forms an oxidation-type composite gaseous aqueous solution for storage; and an electronic control module is disposed in the front space and has a power supply electrically connected to the delivery pipeline module, the electrolyzer and the gas-liquid mixing device, and form an operation interface on the first door panel.

Wherein, the delivery pipeline module has a clean water delivery pipeline, a salt water delivery pipeline and an aqueous solution delivery pipeline. The clean water supply source is connected to an inlet pipe of the salt water mixing tank and the gas through the clean water delivery pipeline. An input pipe of the liquid mixing device, an outlet pipe of the brine mixing tank is connected to the brine storage tank and a return pipe of the brine mixing tank through the brine transport pipeline, and an output pipe of the gas-liquid mixing device passes through the aqueous solution The conveying pipeline is connected to the input pipe. In addition, the brine mixing tank has an inlet for adding the plurality of salt particles, and the inside of the brine mixing tank is divided into an inlet adjacent to the inlet by a baffle. space and a suction space connected to the outlet pipe. The feed space stores the plurality of salt particles and is connected to the return pipe and the input pipe, so that the plurality of salt particles can interact with the cleaning The water is mixed to form the brine solution, the suction space obtains the brine solution filtered out of the salt particles by the partition, and can transport the brine solution to the brine storage tank.

Wherein, the input pipe of the gas-liquid mixing device and the outlet pipe of the salt water mixing tank are respectively provided with a first motor and a second motor. The first motor can transport the salt water solution inside the salt water mixing tank to different height positions. The brine storage tank, and the first motor can transport the clean water or the oxidation system composite gaseous aqueous solution to the gas-liquid mixing device at different height positions.

Wherein, the clean water delivery pipeline further connects the clean water supply source to a first tank body of the electrolytic tank and a second tank body of the electrolytic tank, so that the electrolytic tank can be directly used by the clean water when no electrolysis treatment is performed. Flush the inside.

Furthermore, a connecting pipe is provided between the clean water delivery pipeline and the salt water delivery pipeline, so that the salt water solution in the salt water mixing tank can be directly input to the first tank body and the second tank body.

Furthermore, the production equipment configuration of the above-mentioned oxidation-based composite gaseous aqueous solution further has an adding plate capable of adding a plurality of the above-mentioned salt particles into the inside of the above-mentioned feed space, the adding plate has a connection portion fixed on the feed inlet and An inclined portion extending to the outside of the rear space.

The characteristic of this invention is to change the internal configuration of the cabinet and add a salt water mixing tank at the same time, so that the production equipment can simultaneously integrate three different processes such as salt water mixing, electrolytic salt water and gas-liquid mixing inside a miniaturized cabinet; in terms of configuration, The interfaces, valve bodies and switches that require manual operation by users are presented in the space directly in front of the cabinet, making it convenient for users to control and repair subsequent damage.

100:Production equipment

1: Cabinet

1a: First longitudinal partition

1b: Second longitudinal partition

1c: First transverse partition

1d: Second transverse partition

1e: The third transverse partition

11: Space ahead

11a: Upper area

11b:Lower area

11c: First door panel

12: Rear space

121:Left area

121a: Second door panel

13:Right area

13a: Upper right area

13b: Lower right area

13c:Third door panel

14: Lower channel

2: Salt water mixing tank

2a: Clean water supply source

21:Inlet port

22:Baffle

221: Feeding space

222:Suction space

23:Add board

231:Connection part

232: Inclined part

24:Exit pipe

25:Small round hole

26:Inlet pipe

3:Conveying pipeline module

31: First solenoid valve

32: Second solenoid valve

33:Third solenoid valve

34: The fourth solenoid valve

35:Fifth solenoid valve

36:Sixth solenoid valve

37:Seventh solenoid valve

38:The eighth solenoid valve

39: Ninth solenoid valve

4: Salt water storage tank

5:Electrolyzer

6: Gas-liquid mixing device

7:Electronic control module

7a:Power supply

7b: Circuit board

7c: Operation interface

8:First motor

81: Second motor

A: Clean water delivery pipeline

A1: The first clean water delivery pipeline

A2: Second clean water delivery pipeline

A3: The third clean water delivery pipeline

B: Salt water delivery pipeline

B1: The first brine transport pipeline

B2: Second brine delivery pipeline

B3: The third brine transportation pipeline

C: Aqueous solution delivery pipeline

Figure 1 is a schematic diagram of the hardware settings of the present invention;

Figure 2A is a three-dimensional schematic diagram of the present invention;

Figure 2B is a schematic perspective view of the other side of the present invention;

Figure 3 is a schematic diagram of the interior of the brine mixing tank and the installation location of the adding plate;

Figure 4 shows the detailed configuration of the transportation pipeline module;

Figure 5 is a right side view of the present invention;

Figure 6 is a left side view of the present invention;

Figure 7 is a front view of the present invention.

In order to facilitate a further clear and detailed understanding of the structure, use and characteristics of the present invention, preferred embodiments are enumerated and detailed descriptions are as follows with reference to the drawings: Please refer to Figures 1 to 2B. In a preferred embodiment, the cabinet-type production equipment 100 of the present invention includes a cabinet 1, a brine mixing tank 2, a transportation pipeline module 3, a brine storage tank 4, an electrolytic tank 5, and a gas-liquid mixing tank. Device 6 and an electronic control module 7.

The interior of the cabinet 1 has a first longitudinal partition 1a perpendicular to the ground, a second longitudinal partition 1b perpendicular to the first longitudinal partition 1a and the ground, and a second longitudinal partition 1b parallel to the ground and connected to the ground. The first transverse partition 1c of the board 1b is vertical, and through these longitudinal and transverse partitions, the interior is divided into a front space 11 and a rear space 12. The rear space 12 is further divided into a left area 121, a right area 13 and A lower passage 14. A movable first door panel 11c, a second door panel 121a and a third door panel 13c are respectively provided corresponding to the front space 11, the left area 121, the right area 13 and the lower passage 14, so that the front space 11 Blocked by the first door panel 11c, both sides of the rear space 12 are blocked by the second door panel 121a and the third door panel 13c respectively.

Furthermore, a second transverse partition 1d parallel to the ground and perpendicular to one side of the first longitudinal partition 1a is provided in the front space 11. The second transverse partition 1d divides the front space 11 into a An upper area 11a, a lower area 11b; and a third transverse partition 1e parallel to the ground and perpendicular to the first longitudinal partition 1a and the second longitudinal partition 1b is provided in the right area 13, dividing the right area 13 is divided into an upper right area 13a and a lower right area 13b.

Among them, the right area 13, the left area 121, and the lower channel 14 are not connected to each other. There are only small openings on the wall that allow only the pipelines and lines connecting the equipment to pass through, so that the electrolytic tank 5 The generated gas that may be harmful to the human body will not flow directly from the left area 121 to the right area 13 or the lower channel 14 as much as possible, but will flow in a preset pipeline.

Please refer to Figure 3. In this embodiment, the brine mixing tank 2 has an inlet 21 for adding the plurality of salt particles, a baffle 22 and an adding plate 23 assembled on the inlet 21. The salt water mixing tank 2 is disposed in the lower channel 14 of the rear space 12, and the delivery pipeline module 3 is disposed in the front space 11 and can obtain clean water from a clean water supply source 2a located outside the cabinet 1. The salt water mixing tank 2 is connected to the delivery pipeline module 3, so that the clean water supply source 2a can transport the clean water to the salt water mixing tank 2 through the delivery pipeline module 3, so that the salt water mixing tank 2 can contain the salt water mixing tank 2. The clean water delivered by the clean water supply source 2a has the baffle 22 inside the brine mixing tank 2 so that the brine mixing tank 2 is divided into an inlet space 221 adjacent to the inlet 21 and a connecting space 221 connected to the brine mixing tank 2. A suction space 222 of the outlet pipe 24, and the baffle 22 has a plurality of small round holes 25 so that the feeding space 221 is connected to the suction space 222 through the plurality of small round holes 25. In addition, the adding plate 23 has a connecting portion 231 fixed on the feed inlet 21 and an inclined portion 232 extending to the outside of the rear space 12 .

Please refer to Figure 4 as shown in which the delivery pipeline module 3 is located in the lower area 11b. In this embodiment, the delivery pipeline module 3 has a clean water delivery pipeline A, a salt water delivery pipeline B and a The aqueous solution transport pipeline C, the clean water supply source 2a is connected to an inlet pipe 26 of the brine mixing tank 2 and an input pipe of the gas-liquid mixing device 6 through the clean water transport pipeline A, and the outlet of the brine mixing tank 2 tube 24 through The brine transport pipeline B is connected to the brine storage tank 4 and a return pipe of the brine mixing tank 2, and an output pipe of the gas-liquid mixing device 6 is connected to the input pipe through the aqueous solution transport pipeline C, wherein, the The feed space 221 stores the plurality of salt particles and is connected to the return pipe and the input pipe, so that the plurality of salt particles can be mixed with the clean water inside the salt water mixing tank 2 to form a salt water solution, and then the salt water solution can pass through The plurality of small round holes 25 flows between the feeding space 221 and the suction space 222 , and the suction space 222 is connected to the conveying pipeline module 3 , and the suction space 222 is obtained by the baffle 22 The brine solution is filtered out of the salt particles, and the brine solution can be transported to the brine storage tank 4 so that the brine solution in the suction space 222 can flow into the delivery pipeline module 3. In addition, the clean water is transported The pipeline A further connects the clean water supply source 2a to a first tank body of the electrolytic tank 5 and a second tank body of the electrolytic tank 5, so that the electrolytic tank 5 can be directly used by the clean water when no electrolysis treatment is performed. Rinse the inside, and a connecting pipe is provided between the clean water delivery pipeline A and the salt water delivery pipeline B, so that the salt water solution in the salt water mixing tank 2 can be directly input to the first tank and the second tank. , in addition, the clean water delivery pipeline A is provided with a first clean water delivery pipeline A1, a second clean water delivery pipeline A2 and a third clean water delivery pipeline A3; the salt water delivery pipeline B is provided with a first salt water delivery pipe Road B1, a second salt water delivery pipeline B2 and a third salt water delivery pipeline B3; among them, a first solenoid valve 31, a second solenoid valve 32 and a third solenoid valve 33 are respectively provided to control the flow of clean water; A fourth solenoid valve 34, a fifth solenoid valve 35, a sixth solenoid valve 36, a seventh solenoid valve 37 and an eighth solenoid valve 38 control the flow of salt water; a ninth solenoid valve 39 controls the compound aqueous solution flow.

The detailed operation of the delivery pipeline module 3 is that the second clean water delivery pipeline A2 is provided with the second solenoid valve 32 to control the delivery of clean water to the salt water mixing tank 2 and the plurality of water placed in the feed space 221. After the salt particles are mixed into the brine solution, the first brine transport pipeline B1 is connected to an outlet of the brine mixing tank 2. The first brine transport pipeline B1 is provided with the fourth solenoid valve 34 to control the transport of salt water to the brine solution. In the brine storage tank 4, the fifth solenoid valve 35 is used to control the brine to be transported to the electrolytic tank 5 through the second brine transport pipeline B2. When the amount of salt water stored in the brine storage tank 4 is too late for the electrolytic tank 5 to use When the sixth solenoid valve 36 is triggered to start a first motor 8 provided in the input pipe of the gas-liquid mixing device 6, the brine solution inside the brine mixing tank 2 is directly transported to the The electrolytic tank 5 is used so that the brine solution is transported to the brine storage tank 4 at different heights, and the first motor can transport the clean water or the oxidation system composite gaseous aqueous solution to the gas-liquid mixture at different heights. Device 6.

The first clean water delivery pipeline A1 is provided with the first solenoid valve 31 to control the clean water to be continuously delivered to the gas-liquid mixing device 6 and the electrolyzer through a second motor 81 provided in the outlet pipe 24 of the brine mixing tank 2 The gas generated after the tank 5 is decomposed is mixed into a composite aqueous solution. When the concentration of the aqueous solution is insufficient, the ninth solenoid valve 39 will be triggered to flow the aqueous solution back to the second motor 81 through the aqueous solution delivery pipeline C, and then use the The second motor 81 drives back the gas-liquid mixing device 6 for multiple times of mixing until the aqueous solution reaches the concentration required by the user.

The third clean water delivery pipeline A3 is provided with the third solenoid valve 33 to control the delivery of clean water to the electrolytic tank 5. After the electrolytic tank 5 is used, the clean water is delivered to the electrolytic tank 5 for cleaning. The cabinet 1 has There are two water outlets, and each tank body of the electrolytic tank 5 is connected to a drainage pipe. The two drainage pipes pass through the water outlets respectively to discharge the cleaned sewage out of the electrolytic tank 5 .

Please refer to Figure 5. The brine storage tank 4 is located in the upper right area 13a of the rear space 12. The brine storage tank 4 is connected to the delivery pipeline module 3, the brine mixing tank 2 and the electrolytic tank 5. To obtain the salt water solution storage, a plurality of sensors (not shown) are provided in the tank to detect the height of the salt water in the tank. When the detected salt water height is lower than the set value, the third solenoid valve 33 will be triggered. The brine in the brine mixing tank 2 is transported up until it is higher than the set value.

The electrolytic tank 5 is disposed in the lower right area 13b of the rear space 12. The electrolytic tank 5 is connected to the brine mixing tank 2, the delivery pipeline module 3, the brine storage tank 4, and the gas-liquid mixing device 6 and an exhaust device (not shown) that can generate monoxide-based composite gas by electrolyzing the brine solution transmitted from the brine storage tank 4 through the delivery pipeline module 3 .

Please refer to Figure 6. The gas-liquid mixing device 6 is located in the left area 121 of the rear space 12. The gas-liquid mixing device 6 is connected to the electrolytic cell 5 and the delivery pipeline module 3 to obtain the respective The oxidation system composite gas and the clean water are mixed with the clean water to form an oxidation system composite gaseous aqueous solution for storage, and the clean water is injected from the clean water supply source 2a to mix with the gas generated by the electrolytic cell 5 A compound aqueous solution with disinfection function is prepared for users to use.

Please refer to Figure 7. The electronic control module 7 is disposed in the front space 11 and has a power supply 7a, a circuit board 7b and an operating interface 7c, which are electrically connected to the delivery pipeline module 3, The electrolytic cell 5 and the gas-liquid mixing device 6, wherein the circuit board is electrically connected to the power supply 7a and is located in the upper area 11a and is electrically connected to the operating interface 7c and is located on the first door panel 11c .

The present invention considers that the electronic control module 7 and the conveying pipeline module 3, which operate in a more complex manner or require frequent repairs and maintenance, are integrated in the front space 11 to facilitate the user to complete the maintenance by opening the first door panel 11c. , maintenance and other operations.

31: First solenoid valve

32: Second solenoid valve

33:Third solenoid valve

34: The fourth solenoid valve

35:Fifth solenoid valve

36:Sixth solenoid valve

37:Seventh solenoid valve

38:The eighth solenoid valve

39: Ninth solenoid valve

8:First motor

81: Second motor

A: Clean water delivery pipeline

A1: The first clean water delivery pipeline

A2: Second clean water delivery pipeline

A3: The third clean water delivery pipeline

B: Salt water delivery pipeline

B1: The first brine transport pipeline

B2: Second brine delivery pipeline

B3: The third brine transportation pipeline

C: Aqueous solution delivery pipeline

Claims (7)

A production equipment configuration for an oxidizing compound gaseous aqueous solution, including: a cabinet, the interior of which is divided into a front space and a rear space. The front space is blocked by a movable first door panel, and both sides of the rear space are respectively protected by movable doors. A second movable door panel and a third door panel are provided for shielding; a delivery pipeline module is disposed in the front space and can obtain clean water from a clean water supply source located outside the cabinet; a salt water mixing tank is disposed in The rear space is connected to the delivery pipeline module to obtain the clean water, and the clean water and a plurality of salt particles are mixed to form a salt water solution; a salt water storage tank is arranged in the rear space and is connected to the salt water mixing tank to obtain the clean water. The brine solution is stored; an electrolytic tank is disposed in the rear space, connected to the brine mixing tank and the delivery pipeline module, and can obtain the brine solution from the brine storage tank, and electrolyze the brine solution to form an oxidation It is a composite gas; a gas-liquid mixing device is arranged in the rear space and is connected to the electrolytic cell and the delivery pipeline module to respectively obtain the oxidation-system composite gas and the clean water, and mix the oxidation-system composite gas The clean water forms an oxidation-type composite gaseous aqueous solution for storage; and an electronic control module is disposed in the front space and has a power supply electrically connected to the delivery pipeline module, the electrolyzer and the gas-liquid Mixing device and forming an operating interface on the first door panel; wherein, the delivery pipeline module has a clean water delivery pipeline, a salt water delivery pipeline and an aqueous solution delivery pipeline, and the clean water supply source passes through the clean water delivery pipeline The path is connected to an inlet pipe of the brine mixing tank and an input pipe of the gas-liquid mixing device, and an outlet pipe of the brine mixing tank is transported through the brine. The pipeline is connected to a return pipe of the brine storage tank and the brine mixing tank, and an output pipe of the gas-liquid mixing device is connected to the input pipe through the aqueous solution delivery pipe. The production equipment configuration of the oxidation-type composite gaseous aqueous solution as described in claim 1, wherein the input pipe of the gas-liquid mixing device and the outlet pipe of the brine mixing tank are respectively equipped with a first motor and a second motor, and the first motor The motor can transport the brine solution inside the brine mixing tank to the brine storage tanks at different heights, and the first motor can transport the clean water or the oxidation system composite gaseous aqueous solution to the gas-liquid mixing device at different heights. . The production equipment configuration of the oxidation system composite gaseous aqueous solution as described in claim 2, wherein the rear space of the cabinet is further divided into a lower channel, an upper right area, a lower right area and a left area, and the gas-liquid mixing The device is installed in the left area, and the brine mixing tank is located in the upper right area. The production equipment configuration of the oxidation-type composite gaseous aqueous solution as described in claim 1, wherein the clean water delivery pipeline further connects the clean water supply source to a first tank body of the electrolytic tank and a second tank of the electrolytic tank body, so that the inside of the electrolytic cell can be directly flushed by the clean water when no electrolysis treatment is performed. The production equipment configuration of the oxidation system composite gaseous aqueous solution as described in claim 4, wherein a connecting pipe is provided between the clean water transportation pipeline and the brine transportation pipeline so that the brine solution in the brine mixing tank can be directly input to the first tank body and the second tank body. The production equipment configuration of the oxidation system composite gaseous aqueous solution as described in claim 1, wherein the brine mixing tank has an inlet for adding the plurality of salt particles, and the inside of the brine mixing tank is divided into one phase by a baffle. There is a feed space adjacent to the feed inlet and a suction space connected to the outlet pipe. The feed space stores the plurality of salt particles and is connected to the return pipe and the input pipe, so that The plurality of salt particles can be mixed with the clean water to form the brine solution. The suction space obtains the brine solution in which the salt particles are filtered out by the baffle, and can transport the brine solution to the brine storage tank. The production equipment configuration of the oxidation-based composite gaseous aqueous solution as described in claim 6, wherein the brine mixing tank further includes an adding plate assembled at the feed inlet, and the adding plate has a connection portion fixed at the feed inlet. and an inclined portion extending to the outside of the above-mentioned rear space.

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