Tandem type composite sterilization treatment system for mineral water processing

Abstract

The invention relates to the field of composite sterilization, and particularly discloses a mineral water processing tandem type composite sterilization treatment system which comprises a UVC sterilizer, a plurality of micro-nano sterilizers and an efficient activated carbon sterilization filter which are communicated in sequence, each of the UVC sterilizer, the micro-nano sterilizers and the efficient activated carbon sterilization filter comprises a catalysis tube, a bottom bin and a top bin, and a composite flow driving paddle is rotationally connected in each bottom bin; a UVC lamp tube is arranged in a catalytic tube of the UVC sterilizer; and a bubble generator is arranged in the bottom bin of the micro-nano sterilizer. When mineral water enters the micro-nano bubble sterilizer, part of the mineral water is compressed along the brewing channel to increase the flow rate, bubbles attached to the UVA lamp tube are scoured, and the attachment amount is reduced, so that the catalytic efficiency is enhanced, and the other part of the mineral water is directly mixed with micro-nano ozone bubbles and then directly enters the catalytic tube, so that the service life of the micro-nano bubble sterilizer is prolonged. And the accelerated flowing mineral water can also stir the part to generate mixed flow, so that more bubbles are irradiated by the UVA lamp tube, and the catalytic efficiency is further enhanced.

Description

TECHNICAL FIELD

[0001] The present application relates to composite sterilization technology, in particular to a mineral water processing series composite sterilization treatment system. BACKGROUND

[0002] It is known that mineral water needs to go through water taking, filtering, disinfection and packaging in the production process, and the disinfection step is the focus of production. The disinfection methods commonly used are ultraviolet (over-flow type ultraviolet sterilizer), ozone (micro-nano ozone bubbles) and high-efficiency activated carbon, which do not have chemical residues and are suitable for food-grade disinfection and sterilization.

[0003] For example, the application publication No. CN105293622B, application publication date is March 27, 2018, and the name is "a punch forming over-flow type ultraviolet disinfection device", which includes a disinfection device, including a main body provided with a water inlet and a water outlet provided with a water inlet device and a water outlet device; each end of the main body is provided with a structure symmetrical end head, the end head is a punch forming end head, the end head is provided with a plurality of uniformly distributed reference tables, each reference table is provided with a through hole, and each reference table is provided with a wire head for setting a sealing sleeve through welding; the ultraviolet lamp sleeve is arranged on the two reference tables symmetrically arranged on the two end heads; the distribution box is connected with the ultraviolet lamp sleeve, and is arranged below the main body through the barrel support. The disinfection device manufacturing process includes one-time punch forming and secondary punch forming of the end head, end head spinning forming, water inlet and water outlet punch forming, welding, assembly and other steps. Through the above design, the disinfection device realizes batch production, improves the quality of the equipment, reduces the production cost, and is beneficial to the later maintenance.

[0004] The existing technology has the following disadvantages: when the mineral water is deeply treated, the ultraviolet, high-efficiency activated carbon and micro-nano ozone bubbles are combined in series to carry out composite sterilization and filtration on the mineral water to ensure the quality of the mineral water. The ultraviolet sterilization includes UVC (short-wave ultraviolet) and UVA (long-wave ultraviolet), and when the UVA ultraviolet catalyzes the micro-nano ozone bubbles, the water flow is limited based on the over-flow type ultraviolet sterilizer. However, the high-concentration micro-nano ozone bubbles are easily adsorbed on the glass cover of the ultraviolet lamp during the movement with the water flow, which affects the catalysis of the UVA ultraviolet lamp on the micro-nano ozone bubbles. SUMMARY

[0005] The purpose of the present application is to provide a mineral water processing series composite sterilization treatment system to solve the above-mentioned deficiencies in the prior art.

[0006] In order to achieve the above object, the present application provides the following technical scheme: a mineral water processing series composite sterilization treatment system, comprising a UVC sterilizer, a plurality of micro-nano sterilizers and a high-efficiency activated carbon sterilization filter which are sequentially communicated, all of which comprise a catalytic pipe, a bottom bin and a top bin, and a composite flow driving paddle is rotatably connected in the bottom bin;

[0007] A UVC lamp tube is arranged in the catalytic pipe of the UVC sterilizer;

[0008] A bubble generator is arranged in the bottom bin of the micro-nano sterilizer, and a UVA lamp tube is arranged in the catalytic pipe, the composite flow driving paddle comprises a middle outlet pipe and an inner paddle plate arranged in the middle outlet pipe, the UVA lamp tube extends into the middle outlet pipe, and a brewing channel is formed between the UVA lamp tube and the middle outlet pipe;

[0009] An activated carbon sterilization rod is arranged in the catalytic pipe of the high-efficiency activated carbon sterilization filter.

[0010] As a further description of the above technical scheme: the bottom bin is provided with a water inlet which is tangent to the inner wall, the top bin of the micro-nano sterilizer is provided with a water outlet pipe which leads to the next container, and a shunt pipe is fixedly communicated between the bottom bin of the micro-nano sterilizer and the water outlet pipe.

[0011] As a further description of the above technical scheme: an outer paddle plate is arranged outside the middle outlet pipe, and the outer paddle plate rotates with the middle outlet pipe to transport mixed gas bubbles and liquid to the shunt pipe.

[0012] As a further description of the above technical scheme: a limiting spiral piece is arranged in the bottom bin of the micro-nano sterilizer, an ascending channel is formed between the limiting spiral piece and the outer paddle plate, and the ascending channel is used for ascending large bubbles.

[0013] As a further description of the above technical scheme: a coupling is rotatably connected to the bottom of the bottom bin, the composite flow driving paddle is arranged on the coupling, and an opening which leads to the middle outlet pipe is formed in the coupling.

[0014] As a further description of the above technical scheme: a coarse-hole active filter plate and an inverted middle outlet pipe are arranged in the bottom bin of the UVC sterilizer, and an outer paddle plate which faces the catalytic pipe is arranged on the middle outlet pipe.

[0015] As a further description of the above technical scheme: a middle outlet pipe is arranged in the bottom bin of the high-efficiency activated carbon sterilization filter, an outer paddle plate is arranged on the middle outlet pipe, and a partition plate is arranged on the outer layer of the outer paddle plate.

[0016] As a further description of the above technical scheme: a separation mechanism is arranged on the top bin of the UVC sterilizer, the separation mechanism comprises a secondary cover which is rotatably connected to the top bin, and the secondary cover is driven to rotate to drive the gas to converge along the axis.

[0017] As a further description of the above technical solution: the inner wall of the sub-cover is provided with a high position and a low position, the low position is provided with a liquid outlet groove, and the top bin of the UVC sterilizer and the sub-cover form a liquid outlet channel.

[0018] As a further description of the above technical solution: the middle outlet pipe is provided with a pressure relief port, and the pressure relief port is provided with a circular arc corner towards the outer wall of the middle outlet pipe.

[0019] In the above technical solution, the mineral water processing series composite sterilization treatment system provided by the application is used. When the mineral water enters the micro-nano bubble sterilizer, part of the mineral water output along the middle outlet pipe is compressed along the brewing channel to increase the flow rate, the bubbles attached to the UVA lamp tube are washed, the attachment amount is reduced, and the catalytic efficiency is enhanced. Another part of the mineral water directly mixes with the micro-nano ozone bubbles and then directly enters the catalytic pipe. The flowing mineral water can also stir this part, produce mixed flow, make more bubbles irradiated by the UVA lamp tube, and further enhance the catalytic efficiency. BRIEF DESCRIPTION OF DRAWINGS

[0020] In order to more clearly illustrate the technical solutions in the embodiments of the present application or the prior art, the drawings needed in the embodiments will be briefly introduced. Obviously, the drawings in the following description are only some embodiments described in the present application, and other drawings can also be obtained by those skilled in the art according to these drawings.

[0021] Figure 1 The overall structure schematic diagram provided by the embodiment of the present application is shown in the figure.

[0022] Figure 2 The overall structure cross-sectional schematic diagram provided by the embodiment of the present application is shown in the figure.

[0023] Figure 3 The Figure 2 The enlarged schematic diagram of the middle A is shown in the figure.

[0024] Figure 4 The Figure 2 The enlarged schematic diagram of the middle B is shown in the figure.

[0025] Figure 5 The Figure 2 The enlarged schematic diagram of the middle C is shown in the figure.

[0026] Figure 6 The Figure 2 The enlarged schematic diagram of the middle D is shown in the figure.

[0027] Figure 7 The UVC sterilizer structure explosion schematic diagram provided by the embodiment of the present application is shown in the figure.

[0028] Figure 8 TheFigure 7 Amplification intention at E;

[0029] Figure 9 The micro-nano sterilizer structure explosion schematic diagram provided for the embodiment of the present application;

[0030] Figure 10 The high-efficiency activated carbon sterilization filter structure explosion schematic diagram provided for the embodiment of the present application.

[0031] Mark explanation:

[0032] 1, UVC sterilizer; 11, catalytic pipe; 12, bottom bin; 121, water inlet; 13, top bin; 14, UVC lamp; 15, composite drive flow paddle; 151, outer paddle; 152, middle outlet pipe; 153, pressure relief port; 154, inner paddle plate; 16, water outlet pipe; 161, shunt pipe; 17, coarse hole active filter plate; 18, shaft coupling; 2, micro-nano sterilizer; 21, limiting spiral piece; 22, auxiliary sub-cover; 221, liquid outlet groove; 222, coupling ring; 23, UVA lamp; 24, drive source; 25, guide plate; 26, bubble generator; 3, high-efficiency activated carbon sterilization filter; 31, activated carbon sterilization rod; 32, partition plate; 4, separation mechanism. DETAILED DESCRIPTION

[0033] In order to make the technical personnel in the art better understand the technical solutions of the present application, the present application will be further described in detail below with reference to the drawings.

[0034] Please refer to Figures 1-10 The embodiment of the present application provides a technical scheme: a mineral water processing series composite sterilization treatment system, comprising a UVC sterilizer 1, a plurality of micro-nano sterilizers 2 and a high-efficiency activated carbon sterilization filter 3 connected in sequence, all of which comprise a catalytic pipe 11, a bottom bin 12 and a top bin 13, the top bin 13 is fixedly connected with a water outlet pipe 16, the water outlet pipe 16 is connected with the bottom bin 12 of the next sterilizer in series, the bottom bin 12 is rotatably connected with a composite drive flow paddle 15, the number of micro-nano sterilizers 2 is 2-8, the UVC sterilizer 1 is used as the first sterilization equipment in series, and the mineral water is pumped into the bottom bin 12 of the UVC sterilizer 1 by a water pump.

[0035] The catalytic pipe 11 of the UVC sterilizer 1 is provided with a UVC lamp 14, the UVC lamp 14 is a short-wave ultraviolet lamp, and the purpose is to kill bacteria in the mineral water by short-wave ultraviolet rays, so as to achieve the effect of water purification, and the composite drive flow paddle 15 in the bottom bin 12 of the UVC sterilizer 1 is driven to rotate to assist the flow of mineral water into the catalytic pipe 11.

[0036] The bottom chamber 12 of the micro-nano sterilizer 2 is equipped with a bubble generator 26, which outputs micro-nano ozone bubbles to disinfect the mineral water. The catalytic tube 11 of the micro-nano sterilizer 2 is equipped with a UVA lamp 23, a long-wave ultraviolet lamp. Long-wave ultraviolet light catalyzes the collapse of the micro-nano ozone bubbles, increasing their disinfection effect and deodorizing capabilities. The composite propeller 15 includes a central outlet pipe 152 and an inner propeller plate 154 disposed within the central outlet pipe 152. The central outlet pipe 152 is positioned upright within the bottom chamber 12 of the micro-nano sterilizer 2. Figure 5 The UVA lamp tube 23 is locked and extends into the middle outlet tube 152, forming a brewing channel between them. This allows some of the mineral water output along the middle outlet tube 152 to be compressed and its flow rate increased along the brewing channel, flushing the bubbles attached to the UVA lamp tube 23 and reducing the amount of attached water, thereby enhancing the catalytic efficiency. Meanwhile, the other part of the mineral water is directly mixed with micro-nano ozone bubbles and enters the catalytic tube 11. The accelerated flow of the mineral water also agitates this part, creating turbulence, which allows more bubbles to be irradiated by the UVA lamp tube 23, further enhancing the catalytic efficiency.

[0037] The catalytic tube 11 of the high-efficiency activated carbon sterilization filter 3 is equipped with an activated carbon sterilization rod 31. The activated carbon sterilization rod 31 is composed of multiple high-efficiency activated carbon rings stacked together. It is used to filter the remaining solid particulate impurities in the mineral water and at the same time to catalytically absorb the residual ozone, thereby reducing the content of residual micro-nano ozone bubbles in the mineral water after sterilization.

[0038] Both the high-efficiency activated carbon sterilization filter 3 and the micro-nano sterilizer 2 have guide plates 25 on the top of their bottom chambers 12. The guide plates 25 are circular rings with slopes that guide the liquid into the catalytic tube 11.

[0039] In another embodiment of the present invention, multiple bottom chambers 12 are each provided with an inlet 121 tangential to the inner wall, allowing the liquid entering the bottom chamber 12 to flow along the inner wall of the bottom chamber 12. When mineral water enters the micro-nano sterilizer 2, the mineral water flowing along the inner wall of the bottom chamber 12 will generate a swirling flow, causing the micro-nano ozone bubbles and mineral water to mix. The top chamber 13 of the micro-nano sterilizer 2 is provided with an outlet pipe 16 leading to the next container. A diversion pipe 161 is fixedly connected between the bottom chamber 12 of the micro-nano sterilizer 2 and the outlet pipe 16. When the bubble generator 26 generates micro-nano ozone bubbles, it will generate large normal bubbles. These normal bubbles will rise quickly and are large in size. The micro-nano ozone bubbles cause a higher bubble content in the first micro-nano sterilizer 2 (only the first micro-nano sterilizer 2 has a bubble generator 26). The large normal bubbles will block (reflection, refraction, etc.) the ultraviolet rays emitted by the UVA lamp tube 23. At this time, some of the mineral water mixed with micro-nano ozone bubbles enters the outlet pipe 16 ahead of time along the diversion pipe 161 of the bottom chamber 12 of the micro-nano sterilizer 2, and reaches the next micro-nano sterilizer 2. This reduces the time that part of the mineral water and the large normal bubbles coexist, and enhances the catalytic efficiency. The large bubbles burst in the top chamber 13 after rising, and the waste gas is recovered.

[0040] Preferably, an outer paddle plate 151 is provided on the outer side of the outlet pipe 152, such as... Figure 5 As shown, the outer paddle plate 151 delivers liquid to the bottom as the middle outlet pipe 152 rotates, so as to promote the mineral water mixed with micro-nano ozone bubbles to be transported to the bottom chamber 12 of the micro-nano sterilizer 2, so that part of the mineral water mixed with micro-nano ozone bubbles flows along the diversion pipe 161 to the outlet pipe 16 for mixing.

[0041] Preferably, the bottom chamber 12 of the micro-nano sterilizer 2 is provided with a limiting spiral plate 21, such as... Figure 5 As shown, an upward channel is formed between the limiting spiral plate 21 and the outer paddle plate 151. The length of the upward channel is between 3mm and 7mm. The cross-section of the limiting spiral plate 21 is inclined. When large-sized bubbles are pushed to the bottom of the bottom chamber 12 of the micro-nano sterilizer 2 by the outer paddle plate 151, they can float up along the limiting spiral plate 21. However, micro-nano ozone bubbles do not float easily. When water enters through the inlet 121, it will fill the bottom chamber 12 to increase the mineral water pressure at the limiting spiral plate 21, causing the mineral water mixed with micro-nano ozone bubbles to enter the diversion pipe 161.

[0042] In another embodiment of the present invention, a coupling 18 is rotatably connected to the bottom of the bottom chamber 12. The coupling 18 is connected to a drive unit (which can be a motor and a reducer). A composite propeller 15 is disposed on the coupling 18. An opening leading to the outlet pipe 152 is provided on the coupling 18. When the coupling 18 is located in the bottom chamber 12 of the micro-nano sterilizer (e.g.) Figure 5As shown), the mineral water entering the bottom of the bottom chamber 12 will enter the middle outlet pipe 152 through the opening, and will be driven by the inner paddle plate 154 in the middle outlet pipe 152 to flow along the brewing channel.

[0043] In another embodiment of the present invention, the bottom chamber 12 of the UVC sterilizer 1 is provided with a coarse-pore activated filter plate 17 and an inverted outlet pipe 152, as shown below. Figure 3 As shown, the outlet pipe 152 is inverted, and the outer paddle plate 151 of the outlet pipe 152 is set at the top. As the outlet pipe 152 rotates, it delivers mineral water to the catalytic tube 11 of the UVC sterilizer 1. The water inlet 121 on the bottom chamber 12 of the UVC sterilizer 1 is located below the coarse pore activated filter plate 17, so that the mineral water entering the bottom chamber 12 of the UVC sterilizer 1 will be filtered by the coarse pore activated filter plate 17 (the coarse pore activated filter plate 17 is made of high-efficiency activated carbon). When the opening of the coupling 18 is located in the bottom chamber 12 of the UVC sterilizer 1, it has the ability to discharge liquid, thereby agitating the mineral water in the bottom chamber 12 of the UVC sterilizer 1, reducing the deposition of impurities, and making the impurities suspended and adsorbed and filtered by the coarse pore activated filter plate 17.

[0044] In another embodiment of the present invention, the composite flow-driving impeller 15 in the bottom chamber 12 of the high-efficiency activated carbon sterilization filter 3 is upright, as shown below. Figure 6 As shown, the bottom chamber 12 of the high-efficiency activated carbon sterilization filter 3 is equipped with a central outlet pipe 152, an outer paddle plate 151 is installed on the central outlet pipe 152, and a partition plate 32 is installed on the outer layer of the outer paddle plate 151. The bottom chamber 12 of the high-efficiency activated carbon sterilization filter 3 is not opened with a diversion pipe 161 and is in a closed state, so that the mineral water driven by the outer paddle plate 151 enters the central outlet pipe 152 and is output, thereby increasing the flow rate of the liquid output from the central outlet pipe 152 and accelerating the mineral water through the activated carbon sterilization rod 31 with resistance. The partition plate 32 prevents the liquid from flowing back into the bottom, so that the mineral water driven by the outer paddle plate 151 can only be output from the central outlet pipe 152.

[0045] In another embodiment of the present invention, a separation mechanism 4 is provided on the top chamber 13 of the UVC sterilizer 1. The separation mechanism 4 can be provided on the top chamber 13 of the first UVC sterilizer 1 or the top chamber 13 of the first two UVC sterilizers 1, and it is not necessary to provide it on the top chamber 13 of each UVC sterilizer 1. The separation mechanism 4 includes a secondary separator 22 rotatably connected to the top chamber 13, such as... Figure 4 As shown, the sub-distribution hood 22 is provided with a coupling ring 222 extending out of the top chamber 13. The coupling ring 222 is coupled to the drive source 24 (the drive source 24 can be a motor or a motor with a reducer) to make the sub-distribution hood 22 rotate. When rotating, the liquid moves towards the inner wall of the sub-distribution hood 22 due to inertial centrifugal force. The large bubbles that rise and burst, as well as the micro-nano ozone bubbles that burst with the water surface, will generate gas. After the water moves along both sides, the gas will converge along the axis to facilitate the recovery of waste gas.

[0046] Preferred, such as Figure 4 As shown, the inner wall of the sub-distribution hood 22 is provided with a high position and a low position. A liquid outlet trough 221 is opened at the low position. A liquid outlet channel is formed between the top chamber 13 of the UVC sterilizer 1 and the sub-distribution hood 22. As the sub-distribution hood 22 rotates, the liquid will enter the liquid outlet trough 221 at the low position and then enter the liquid outlet channel. As the outer wall of the sub-distribution hood 22 rotates, it will accelerate into the water outlet pipe 16, increasing the flow rate and pressure entering the water outlet pipe 16.

[0047] In another embodiment of the present invention, a pressure relief port 153 is provided on the outlet pipe 152. Because of the rounded corners on the pressure relief port 153, the inner wall opening of the pressure relief port 153 is smaller than the outer wall opening. When the pressure relief port 153 is in the UVC sterilizer 1, such as Figure 3 As shown, a portion of the mineral water enters the bottom chamber 12 in advance to contact the coarse-pore activated filter plate 17 for filtration. When the pressure relief port 153 is in the micro-nano sterilizer 2, as... Figure 5 As shown, due to the limitation of the brewing channel, the internal liquid can be discharged from the pressure relief port 153 into the bottom chamber 12 when the pressure is high, assisting in the mixing of micro-nano bubbles and mineral water. When the pressure relief port 153 is in the high-efficiency activated carbon sterilization filter 3, such as... Figure 6 As shown, the mineral water that quickly passes through the pressure relief port 153 will carry the mineral water in the bottom tank 12 into the tank, increasing the output flow of the middle outlet pipe 152.

[0048] First, the mineral water is pumped into the bottom chamber 12 of the UVC sterilizer 1 and pre-filtered by the coarse-pore active filter plate 17. Then, it is sterilized by short-wave ultraviolet light emitted by the UVC lamp tube along the catalytic tube 11 of the UVC sterilizer 1. After sterilization, the mineral water enters the bottom chamber 12 of the first micro-nano sterilizer 2 along the top chamber 13 of the UVC sterilizer 1.

[0049] The mineral water mixed with the bubble generator 26 in the bottom chamber 12 of the first micro-nano sterilizer 2 emits micro-nano ozone bubbles. At this time, some mineral water mixed with normal bubbles and micro-nano bubbles enters the catalytic tube 11 of the micro-nano sterilizer 2 and is irradiated by the UVA lamp tube for sterilization. At the same time, the liquid out of the middle outlet pipe 152 washes the glass tube on the outer wall of the UVA lamp tube along the rinsing channel. After the mineral water entering the catalytic tube 11 flows to the top, it is separated from the broken bubbles by the rotation of the sub-distribution hood 22 and enters the next sterilizer through the inlet 121. Meanwhile, another part of the mineral water mixed with micro-nano bubbles (and a small amount of normal bubbles, because normal bubbles will float and are not easy to be pumped away) is restricted by the outer paddle 151 and transported to the bottom chamber 12 of the next micro-nano sterilizer 2 for continued sterilization.

[0050] The last micro-nano sterilizer 2 outputs mineral water to the high-efficiency activated carbon sterilization filter 3, so that it passes through the activated carbon sterilization rod 31 to complete the composite sterilization work.

[0051] The foregoing has only described certain exemplary embodiments of the present invention by way of illustration. Undoubtedly, those skilled in the art can modify the described embodiments in various ways without departing from the spirit and scope of the present invention. Therefore, the foregoing drawings and descriptions are illustrative in nature and should not be construed as limiting the scope of protection of the claims of the present invention.

Claims

1. A series-connected composite sterilization system for mineral water processing, comprising a UVC sterilizer (1), several micro / nano sterilizers (2), and a high-efficiency activated carbon sterilization filter (3) connected in sequence, characterized in that, All three include a catalyst tube (11), a bottom chamber (12) and a top chamber (13), and a composite propeller (15) is rotatably connected inside the bottom chamber (12). The UVC sterilizer (1) has a UVC lamp tube (14) installed inside the catalytic tube (11). The micro-nano sterilizer (2) has a bubble generator (26) installed in the bottom chamber (12) and a UVA lamp (23) installed in the catalytic tube (11). The composite flow propeller (15) includes a central outlet pipe (152) and an inner propeller plate (154) installed in the central outlet pipe (152). The UVA lamp (23) extends into the central outlet pipe (152), and a bubbling channel is formed between the two. The high-efficiency activated carbon sterilization filter (3) has an activated carbon sterilization rod (31) installed inside the catalytic tube (11).

2. The mineral water processing series composite sterilization system according to claim 1, characterized in that, Each of the bottom chambers (12) is provided with a water inlet (121) tangent to the inner wall. The top chamber (13) of the micro-nano sterilizer (2) is provided with a water outlet pipe (16) leading to the next container. A diversion pipe (161) is fixedly connected between the bottom chamber (12) of the micro-nano sterilizer (2) and the water outlet pipe (16).

3. The series-connected composite sterilization system for mineral water processing according to claim 2, characterized in that, An outer paddle plate (151) is provided on the outside of the outlet pipe (152). The outer paddle plate (151) rotates with the outlet pipe (152) to deliver liquid containing mixed bubbles to the diversion pipe (161).

4. The mineral water processing series composite sterilization system according to claim 3, characterized in that, The bottom chamber (12) of the micro-nano sterilizer (2) is provided with a limiting spiral plate (21), and an upward channel is formed between the limiting spiral plate (21) and the outer paddle plate (151), which allows large air bubbles to rise.

5. The series-connected composite sterilization system for mineral water processing according to claim 1, characterized in that, The bottom of the hopper (12) is rotatably connected to a coupling (18), and the composite propeller (15) is mounted on the coupling (18). The coupling (18) has an opening leading to the outlet pipe (152).

6. The mineral water processing series composite sterilization system according to claim 1, characterized in that, The bottom chamber (12) of the UVC sterilizer (1) is provided with a coarse-pore active filter plate (17) and an inverted central outlet pipe (152), and an outer paddle plate (151) facing the catalyst tube (11) is provided on the central outlet pipe (152).

7. The series-connected composite sterilization system for mineral water processing according to claim 1, characterized in that, The high-efficiency activated carbon sterilization filter (3) has a central outlet pipe (152) in the bottom chamber (12), an outer paddle plate (151) on the central outlet pipe (152), and a partition plate (32) on the outer layer of the outer paddle plate (151).

8. The series-connected composite sterilization system for mineral water processing according to claim 1, characterized in that, The UVC sterilizer (1) has a separation mechanism (4) on its top chamber (13). The separation mechanism (4) includes a sub-distribution hood (22) rotatably connected to the top chamber (13). The sub-distribution hood (22) is driven to rotate, causing the gas to converge along the axis.

9. A series-type composite sterilization system for mineral water processing according to claim 8, characterized in that, The inner wall of the sub-hood (22) is provided with a high position and a low position. A liquid outlet groove (221) is opened at the low position. A liquid outlet channel is formed between the top chamber (13) of the UVC sterilizer (1) and the sub-hood (22).

10. A series-type composite sterilization system for mineral water processing according to claim 1, characterized in that, The outlet pipe (152) is provided with a pressure relief port (153), and the pressure relief port (153) is provided with an arc angle in the direction of the outer wall of the outlet pipe (152).

Images