Pipe type high-voltage pulsed electric field sludge cell wall breaking treatment equipment

Abstract

The application provides a tubular high-voltage pulsed electric field sludge cell wall breaking treatment device and relates to the technical field of sludge treatment. The device comprises a tubular shell, a high-voltage pulsed electric field wall breaking structure, a steady flow structure, a turbulence element and a high-voltage pulse power supply. The high-voltage pulsed electric field wall breaking structure is fixed in the tubular shell through a support and the length direction of the high-voltage pulsed electric field wall breaking structure is consistent with the length direction of the tubular shell. The turbulence element and the steady flow structure are both sleeved on the high-voltage pulsed electric field wall breaking structure and the steady flow structure is located above the turbulence element. The high-voltage pulsed electric field wall breaking structure is electrically connected with the high-voltage pulse power supply. The high-voltage pulsed electric field wall breaking structure can generate a non-uniform high-voltage pulsed electric field in the region where the turbulence element is located.

Description

TECHNICAL FIELD

[0001] The present application relates to the technical field of sludge treatment, in particular to a tubular high-voltage pulsed electric field sludge cell wall breaking treatment equipment. BACKGROUND

[0002] With the gradual development and improvement of urbanization in China, sewage treatment facilities are increasingly improved, and the demand for sludge treatment is also gradually increasing. In order to improve the efficiency of sludge treatment and increase the resource utilization of sludge, ultrasonic, digestion, electric field and oxidation treatment technologies have been widely applied. However, there is a common problem of insufficient carbon source and C / N value imbalance in the currently operated sewage plants in China, which affects the efficiency of nitrogen and phosphorus removal. In order to ensure the efficiency of nitrogen and phosphorus removal, it is a common way to use the residual sludge in the sewage treatment process to supplement the carbon source, that is, to destroy the microbial cells in the sludge and dissolve the organic carbon source in the content. This treatment method not only increases the carbon source of the influent, which is beneficial to the anaerobic digestion reaction of microorganisms, but also effectively solves the disposal dilemma of large amount of residual sludge and significantly reduces the pressure of sludge treatment.

[0003] The existing sludge cell wall breaking equipment mainly has the problems of complex internal structure, high energy consumption, and difficulty in engineering scale-up design. Moreover, it is difficult to improve the sludge treatment capacity while ensuring the cell wall breaking effect. Therefore, how to improve the wall breaking effect in the engineering scale-up design with large treatment capacity while maintaining compact structure and sufficient electric field strength is a technical problem to be solved. SUMMARY

[0004] The present application provides a tubular high-voltage pulsed electric field sludge cell wall breaking treatment equipment. The preferred technical solutions in the many technical solutions provided by the present application can produce many technical effects, which are described in detail below.

[0005] To achieve the above-mentioned purpose, the present application provides the following technical solutions:

[0006] The present application provides a tubular high-voltage pulsed electric field sludge cell wall breaking treatment equipment, which comprises a tubular shell, a high-voltage pulsed electric field wall breaking structure, a flow stabilizing structure, a turbulence element and a high-voltage pulse power supply. The high-voltage pulsed electric field wall breaking structure is fixed in the tubular shell by a support, and the length direction of the high-voltage pulsed electric field wall breaking structure is consistent with the length direction of the tubular shell. The turbulence element and the flow stabilizing structure are both sleeved on the high-voltage pulsed electric field wall breaking structure, and the flow stabilizing structure is located above the turbulence element. The high-voltage pulsed electric field wall breaking structure is electrically connected with the high-voltage pulse power supply, and can generate a non-uniform high-voltage pulsed electric field in the area where the turbulence element is located.

[0007] Optionally, the high-voltage pulsed electric field cell wall breaking structure comprises a plurality of honeycomb flow channel unit bodies, all of the honeycomb flow channel unit bodies are electrically connected with the high-voltage pulsed power supply, and side walls of two adjacent honeycomb flow channel unit bodies are connected.

[0008] Optionally, the honeycomb flow channel unit body comprises a metal straight pipe and a cylindrical insulating electrode rod, the metal straight pipe is sleeved on the cylindrical insulating electrode rod, and a flow channel space exists between the metal straight pipe and the cylindrical insulating electrode rod, the length of the cylindrical insulating electrode rod is longer than the length of the metal straight pipe, the flow disturbing element is sleeved on the cylindrical insulating electrode rod and located in the flow channel space, and an upper end section of the cylindrical insulating electrode rod penetrates through the flow stabilizing structure and the flow stabilizing structure is located above the metal straight pipe.

[0009] Optionally, the bracket comprises a lower bracket and an upper bracket, a lower end of the metal straight pipe is connected with the inner wall of the tubular shell through the lower bracket, and an upper end of the cylindrical insulating electrode rod is connected with the inner wall of the tubular shell through the upper bracket, and the upper bracket is located above the flow stabilizing structure.

[0010] Optionally, the bracket comprises a lower bracket and an upper bracket, a lower end of the metal straight pipe is connected with the inner wall of the tubular shell through the lower bracket, and an upper end of the cylindrical insulating electrode rod is connected with the inner wall of the tubular shell through the upper bracket, and the upper bracket is located above the flow stabilizing structure.

[0011] An outer wall of an upper end of the tubular shell is provided with a wiring pipe.

[0012] Optionally, an insulating layer is arranged on an outer surface of the cylindrical insulating electrode rod, the thickness of the insulating layer is 1-2 mm, and the cross-sectional shape of the metal straight pipe is a regular polygon or a circle.

[0013] Optionally, the number of the flow disturbing elements is consistent with the number of the cylindrical insulating electrode rods, the flow disturbing element comprises a sleeve and a flow disturbing part, the flow disturbing part is fixedly connected with a side wall of the sleeve, and the sleeve is sleeved on the cylindrical insulating electrode rod.

[0014] The flow disturbing part is a dendritic structure, a continuous spiral blade structure or an intermittent spiral blade structure.

[0015] Optionally, the flow stabilizing structure comprises flow stabilizing vanes and positioning cylinders, the number of the flow stabilizing vanes and the positioning cylinders is multiple, the number of the positioning cylinders is consistent with the number of the cylindrical insulated electrode rods, the cylindrical insulated electrode rods pass through the positioning cylinders, the adjacent flow stabilizing vanes are connected with each other through the positioning cylinders, and the free end of the flow stabilizing vane at the outer end is connected with the inner wall of the tubular shell.

[0016] Optionally, the bottom of the tubular shell is provided with a sludge inlet pipe and an inlet expansion section, the upper end side wall of the tubular shell is provided with a sludge outlet pipe, and the height of the sludge outlet pipe is higher than the height of the flow stabilizing structure.

[0017] The pipe type high-voltage pulsed electric field sludge cell wall breaking treatment equipment provided by the application is of a compact pipe type structure, the high-voltage pulsed electric field wall breaking structure, the flow stabilizing structure and the turbulence element are all installed in the tubular shell, and the flow stabilizing structure and the turbulence element are both sleeved on the high-voltage pulsed electric field wall breaking structure, so that the structure is simple and compact, the overall space volume is compressed, the modular design makes transportation and installation and maintenance more convenient, the sludge enters the high-voltage pulsed electric field wall breaking structure from the bottom of the tubular shell, is broken by the non-uniform high-voltage pulsed electric field generated thereby, and the organic matter is dissolved out, and under the strong turbulent flow of the turbulence element, the wall of the sludge is broken and dewatered, then the sludge passes through the flow stabilizing structure again, the sludge is stabilized and vortex broken, and finally the broken wall sludge is discharged from the upper end of the tubular shell, so that the wall of the sludge is broken and dewatered, and the ability of further improving the sludge wall breaking effect is realized under the condition of ensuring the compact structure. The pipe type high-voltage pulsed electric field sludge cell wall breaking treatment equipment is especially suitable for municipal sewage treatment plants.

[0018] The preferred technical scheme of the application can at least produce the following technical effects:

[0019] (1) The high-voltage pulsed electric field wall breaking technology is applied to the inside of the pipe type structure, the cylindrical insulated electrode rod is sleeved with the turbulence element, the turbulent flow intensity of the sludge flow is increased, and the efficiency of sludge wall breaking and dewatering is effectively improved.

[0020] (2) The high-voltage pulsed electric field wall breaking structure adopts the structure form of a honeycomb flow channel unit body combination, which is convenient for engineering scale-up design in large processing capacity, and the structure after engineering scale-up still has high compactness.

[0021] (3) The single central cylindrical insulated electrode rod and the single regular hexagonal metal straight pipe in the honeycomb flow channel unit form a unit body, a non-uniform high-voltage pulsed electric field is formed between the cylindrical insulated electrode rod and the regular hexagonal metal straight pipe, sufficient electric field strength can be ensured, and the cell wall or basic unit structure in the sludge is broken. BRIEF DESCRIPTION OF DRAWINGS

[0022] To more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the drawings used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the present invention. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0023] Figure 1 This is a schematic diagram of the structure of a tubular high-voltage pulsed electric field sludge cell wall disruption treatment device provided in an embodiment of the present invention;

[0024] Figure 2 yes Figure 1 Cross-sectional view of AA in the middle;

[0025] Figure 3 yes Figure 1 Cross-sectional view of BB in the middle;

[0026] Figure 4 This is a schematic diagram of the current stabilization structure of a tubular high-voltage pulse electric field sludge cell wall breaking treatment device provided in an embodiment of the present invention;

[0027] Figure 5 This is a schematic diagram of the cylindrical high-voltage pulse electric field cell disruption structure of a tubular high-voltage pulse electric field sludge cell disruption treatment device provided in an embodiment of the present invention.

[0028] Figure 6 This is a schematic diagram of the structure of a type one of the turbulence element in a tubular high-voltage pulse electric field sludge cell wall breaking treatment device provided in an embodiment of the present invention;

[0029] Figure 7 This is a schematic diagram of the second type of turbulence element in a tubular high-voltage pulsed electric field sludge cell wall breaking treatment device provided in an embodiment of the present invention;

[0030] Figure 8 This is a schematic diagram of the third type of turbulence element in a tubular high-voltage pulsed electric field sludge cell wall breaking treatment device provided in an embodiment of the present invention;

[0031] Figure 9 This is a schematic diagram of the fourth type of turbulence element in a tubular high-voltage pulse electric field sludge cell wall breaking treatment device provided in an embodiment of the present invention.

[0032] 1, wiring chamber; 2, sludge outlet pipe; 3, steady flow structure; 4, high-voltage pulsed electric field wall-breaking structure; 5, cylindrical insulating electrode rod; 6, tubular shell; 7, inlet expansion section; 8, sludge inlet pipe; 9, steady flow blade; 10, upper support; 11, wiring pipe; 12, high-voltage pulse power supply; 13, wiring stud; 14, wiring board; 15, metal straight pipe; 16, spoiler element; 17, lower support; 18, sleeve; 19, branch structure; 20, continuous spiral blade structure; 21, intermittent spiral blade structure; 22, positioning cylinder. DETAILED DESCRIPTION

[0033] In order to make the objects, technical solutions and advantages of the present application clearer, the technical solutions of the present application will be described in detail below. Obviously, the described embodiments are only some of the embodiments of the present application, not all the embodiments. Based on the embodiments in the present application, all other embodiments obtained by those of ordinary skill in the art without creative work fall within the scope of protection of the present application.

[0034] In the description of the present application, it should be noted that, unless otherwise specified, the meaning of "a plurality of" is two or more; the orientations or positional relationships indicated by the terms "upper", "lower", "left", "right", "inner", "outer", "front end", "rear end", "head", "tail" and the like are based on the orientations or positional relationships shown in the drawings, and are only for the purpose of facilitating the description of the present application and simplifying the description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore cannot be understood as a limitation on the present application. In addition, the terms "first", "second", "third" and the like are only for the purpose of description and cannot be understood as indicating or implying relative importance.

[0035] In the description of the present application, it should also be noted that, unless otherwise specified and limited, the terms "mounting", "connecting", "connection" should be understood broadly, for example, it can be fixed connection, or detachable connection, or integral connection; it can be mechanical connection, or electrical connection; it can be directly connected, or indirectly connected through an intermediate medium. For those of ordinary skill in the art, the specific meaning of the above terms in the present application can be understood according to the specific circumstances.

[0036] The present application provides a kind of tubular high pressure pulsed electric field sludge cell wall breaking treatment equipment, including tubular shell 6, high pressure pulsed electric field wall breaking structure 4, steady flow structure 3, turbulence element 16 and high voltage pulse power supply 12, wherein high pressure pulsed electric field wall breaking structure 4 is fixed in tubular shell 6 by support and the length direction of high pressure pulsed electric field wall breaking structure 4 is consistent with the length direction of tubular shell 6, turbulence element 16 and steady flow structure 3 are all covered on high pressure pulsed electric field wall breaking structure 4 and steady flow structure 3 is located above turbulence element 16, high pressure pulsed electric field wall breaking structure 4 is electrically connected with high voltage pulse power supply 12, and high pressure pulsed electric field wall breaking structure 4 can generate non-uniform high pressure pulsed electric field in the area where turbulence element 16 is located.The present application provides a kind of tubular high pressure pulsed electric field sludge cell wall breaking treatment equipment, and the whole is compact tubular structure, high pressure pulsed electric field wall breaking structure 4, steady flow structure 3 and turbulence element 16 are all installed in tubular shell 6, and steady flow structure 3 and turbulence element 16 are all covered on high pressure pulsed electric field wall breaking structure 4, which is simple and compact, compresses the overall space volume, and modular design makes transportation and installation and maintenance more convenient, sludge enters high pressure pulsed electric field wall breaking structure 4 from bottom to top from the bottom of tubular shell 6, is destroyed by non-uniform high pressure pulsed electric field generated thereby, and the cell wall in sludge is destroyed, and organic matter is dissolved, and under the strong turbulent action of turbulence element 16, the wall of sludge is broken and dewatered, then sludge passes through steady flow structure 3 again, and sludge is stabilized and vortex is broken, finally the broken wall sludge is discharged from the upper end of tubular shell 6, realizes the wall breaking and dewatering of sludge, and has the ability to further improve the sludge wall breaking effect under the condition of guaranteeing compact structure.Especially suitable for urban sewage treatment plant.

[0037] As an optional implementation, high pressure pulsed electric field wall breaking structure 4 includes a plurality of honeycomb flow channel unit bodies, all honeycomb flow channel unit bodies are electrically connected with high voltage pulse power supply 12, and the side walls of adjacent two honeycomb flow channel unit bodies are connected.Referring to Figure 2 The number of honeycomb flow channel unit bodies is seven, and a regular hexagon is adopted, one honeycomb flow channel unit body is located at the center, and the other six honeycomb flow channel unit bodies are distributed around the center honeycomb flow channel unit body and are connected with each other.

[0038] As an optional implementation, the honeycomb flow channel unit body comprises a metal straight pipe 15 and a cylindrical insulating electrode rod 5, the metal straight pipe 15 is sleeved on the cylindrical insulating electrode rod 5 and there is a flow channel space between the metal straight pipe 15 and the cylindrical insulating electrode rod 5, the length of the cylindrical insulating electrode rod 5 is longer than the length of the metal straight pipe 15, the spoiler element 16 is sleeved on the cylindrical insulating electrode rod 5 and located in the flow channel space, a non-uniform high-voltage pulse electric field is generated in the flow channel space, the upper end section of the cylindrical insulating electrode rod 5 passes through the flow stabilizing structure 3 and the flow stabilizing structure 3 is located above the metal straight pipe 15. The cross-sectional shape of the metal straight pipe 15 is a regular polygon or a circle, that is, the cross-sectional shape of the metal straight pipe 15 can be a regular quadrilateral, a regular pentagon, a regular hexagon, a regular dodecagon or a circle, etc. In the enlarged design, through the multi-layer flow channel, the compact structure and sufficient electric field strength can be ensured. At the same time, the effective space utilization rate of the flow channel of the metal straight pipe 15 is not less than 50%, and the effective space utilization rates of the flow channel of the metal straight pipe 15 are 63.69% for a regular quadrilateral, 50.14% for a regular pentagon, 82.74% for a regular hexagon, 78.85% for a regular dodecagon and 77.78% for a circle, respectively. The regular hexagonal metal straight pipe is preferably used. The outer diameter of the cylindrical insulating electrode rod 5 can be φ16mm, φ20mm and φ40mm and other different size series according to the processing capacity of the equipment. When the diameter of φ16mm and φ20mm is used, the distance between the wall surface of the metal straight pipe 15 and the center of the cylindrical insulating electrode rod 5 is recommended to be between 15-20mm; when the diameter of φ40mm is used, the corresponding distance is recommended to be between 30-35mm, so as to ensure the electric field strength and space utilization rate. The outer diameter of the cylindrical insulating electrode rod 5 is usually φ16, φ20 or φ40mm, etc. The distance on the regular hexagonal metal straight pipe matched therewith is usually 17, 29, 34mm, etc. The metal straight pipe 15 can be made of alloy steel.

[0039] As an optional implementation, the bracket comprises a lower bracket 17 and an upper bracket 10, the lower end of the metal straight pipe 15 is connected with the inner wall of the tubular shell 6 through the lower bracket 17, a plurality of first fixing holes are arranged on the lower bracket 17, the number of the first fixing holes is consistent with the number of the metal straight pipes 15, the first fixing holes are matched with the metal straight pipes 15 and fixedly connected, the lower bracket 17 is used for positioning and fixing the metal straight pipes 15, the upper end of the cylindrical insulating electrode rod 5 is connected with the inner wall of the tubular shell 6 through the upper bracket 10, a plurality of second fixing holes are arranged on the upper bracket 10, the number of the second fixing holes is consistent with the number of the cylindrical insulating electrode rods 5, the second fixing holes are matched with the cylindrical insulating electrode rods 5, the upper bracket 10 is used for positioning and fixing the cylindrical insulating electrode rods 5, the upper bracket 10 is located above the flow stabilizing structure 3 and the height of the upper bracket 10 is higher than the height of the sludge outlet pipe 2.

[0040] As an optional implementation, the wire board 14 and the wire studs 13 are further included, the number of the wire studs 13 is consistent with the number of the cylindrical insulated electrode rods 5 and is connected one by one, the wire board 14 is connected with all the wire studs 13, the upper support 10 forms the wire chamber 1 with the upper end region of the tubular shell 6, the wire board 14 is located in the wire chamber 1, the positive pole of the high-voltage pulse power supply 12 is electrically connected with the wire board 14, and the negative pole of the high-voltage pulse power supply 12 is electrically connected with the metal straight pipe 15; the cylindrical insulated electrode rods 5 serve as high-voltage poles, the metal straight pipe 15 serves as a grounding pole, and a non-uniform high-voltage pulse electric field is formed between the cylindrical insulated electrode rods 5 and the metal straight pipe 15. The wire board 14 can be connected with all the cylindrical insulated electrode rods 5 through the wire studs 13, thereby saving the wires, and the high-voltage pulse power supply 12 only needs to be connected with the wire board 14, so that the high-voltage pulse power supply 12 can be connected with all the cylindrical insulated electrode rods 5, without using multiple wires to connect multiple cylindrical insulated electrode rods 5, thereby saving the amount of wires.

[0041] The upper end outer wall of the tubular shell 6 is provided with the wire pipe 11, which is used to facilitate the wire to pass through. The high-voltage pulse power supply 12 can adopt a high-frequency high-voltage pulse alternating current power supply or a high-frequency high-voltage pulse direct current power supply, the voltage is 0-20 kV, the frequency is 50-5000 Hz, the duty cycle is 0-30%, and the waveform is a square wave. The optimal frequency, voltage and duty cycle to be applied need to be selected according to the specific sludge physicochemical property test. The operating parameters of the high-voltage pulse power supply 12 are recommended parameters, and the adjustable parameters can adapt to different working conditions.

[0042] As an optional implementation, an insulating layer is arranged on the outer surface of the cylindrical insulated electrode rod 5, the thickness of the insulating layer is 1-2 mm, the cylindrical insulated electrode rod 5 can form the insulating layer by means of spraying ceramic powder on the surface, hot setting a soft plastic pipe or the like, or by using a hot-dip plastic steel pipe.

[0043] As an optional implementation, the material of the spoiler element 16 can be polytetrafluoroethylene insulating material, the number of the spoiler elements 16 is consistent with the number of the cylindrical insulated electrode rods 5, the spoiler element 16 includes a sleeve 18 and a spoiler part, the spoiler part is fixedly connected with the side wall of the sleeve 18, the sleeve 18 is sleeved on the cylindrical insulated electrode rod 5, and the sleeve 18 is used to position and fix the cylindrical insulated electrode rod 5.

[0044] The spoiler part is a dendritic structure 19 or a continuous spiral blade structure 20 or an intermittent spiral blade structure 21, which has the effect that when the sludge passes through the flow channel space, the spoiler part will interfere with the flow of the sludge, causing strong turbulence, which is helpful for the wall breaking and dewatering of the sludge. Figure 6 The sleeve 18 has multiple branch rods, the free ends of the branch rods are directed upward and are in the same direction as the sludge flow direction. Figure 7The sleeve 18 has a plurality of branch rods, the free end of the branch rod is directed downward, opposite to the flow direction of the sludge; see Figure 8 It is an intermittent spiral blade structure 21, the blade is discontinuous and distributed upward along the sleeve 18 in a spiral manner; see Figure 9 It is a continuous spiral blade structure 20, the blade is continuous and distributed upward along the sleeve 18 in a spiral manner.

[0045] As an optional embodiment, the flow stabilizing structure 3 comprises a plurality of flow stabilizing blades 9 and a plurality of positioning cylinders 22, the number of the positioning cylinders 22 is consistent with the number of the cylindrical insulating electrode rods 5, the cylindrical insulating electrode rods 5 pass through the positioning cylinders 22, the adjacent flow stabilizing blades 9 are connected to each other through the positioning cylinders 22, and the free end of the flow stabilizing blade 9 at the outer end is connected to the inner wall of the tubular shell 6. Optionally, the number of the positioning cylinders 22 is seven, one of which is located at the center, and the other six are distributed around the center positioning cylinder 22, the six positioning cylinders 22 are fixedly connected through the corresponding flow stabilizing blades 9 at the center of the positioning cylinder 22, the adjacent two of the six positioning cylinders 22 are fixedly connected through the flow stabilizing blades 9, and the six positioning cylinders 22 are fixedly connected to the inner wall of the tubular shell 6 through the corresponding flow stabilizing blades 9. After the sludge is broken by the high-voltage pulse electric field wall-breaking structure 4, the sludge is subjected to flow stabilization and vortex breaking under the action of the blades of the flow stabilizing blades 9, and finally flows out through the sludge outlet pipe 2 for subsequent sludge treatment process.

[0046] As an optional embodiment, the bottom of the tubular shell 6 is provided with a sludge inlet pipe 8 and an inlet expansion section 7, the sludge inlet pipe 8 is located below the inlet expansion section 7, the diameter of the inlet expansion section 7 gradually increases from bottom to top, the upper end side wall of the tubular shell 6 is provided with a sludge outlet pipe 2, and the height of the sludge outlet pipe 2 is higher than the height of the flow stabilizing structure 3.

[0047] The working principle of the present application is as follows: the sludge enters the high-voltage pulse electric field wall-breaking structure 4 from the bottom of the tubular shell 6 through the sludge inlet pipe 8, the electric energy generated by the high-voltage pulse power supply 12 forms a non-uniform high-voltage pulse electric field between the cylindrical insulating electrode rods 5 and the metal straight pipe 15, the cell wall in the sludge is broken and the organic matter is dissolved when the sludge passes through the non-uniform high-voltage pulse electric field, and the sludge is dehydrated by the strong turbulent flow of the flow disturbing element 16. When the sludge passes through the flow stabilizing structure 3, the flow stabilizing blades 9 stabilize the flow of the sludge and break the vortex, and finally the broken wall sludge flows out through the sludge outlet pipe 2.

[0048] The above merely illustrates the specific embodiments of the present application, but the protection scope of the present application is not limited thereto, any person skilled in the art can easily think of the changes or replacements within the technical range disclosed by the present application, which should be covered in the protection scope of the present application. Therefore, the protection scope of the present application should be subject to the protection scope of the claims.

Claims

1. A tubular high-voltage pulsed electric field sludge cell disintegration device, characterized by, The device comprises a tubular shell (6), a high-voltage pulsed electric field cell wall breaking structure (4), a flow stabilizing structure (3), a flow disturbing element (16) and a high-voltage pulse power supply (12), wherein, The high-voltage pulsed electric field cell wall breaking structure (4) is fixed in the tubular shell (6) by a bracket, and the length direction of the high-voltage pulsed electric field cell wall breaking structure (4) is consistent with the length direction of the tubular shell (6), the flow disturbing element (16) and the flow stabilizing structure (3) are both sleeved on the high-voltage pulsed electric field cell wall breaking structure (4), and the flow stabilizing structure (3) is located above the flow disturbing element (16), the high-voltage pulsed electric field cell wall breaking structure (4) is electrically connected with the high-voltage pulse power supply (12), and the high-voltage pulsed electric field cell wall breaking structure (4) can generate a non-uniform high-voltage pulsed electric field in the area where the flow disturbing element (16) is located; The high-voltage pulsed electric field cell wall breaking structure (4) comprises a plurality of honeycomb flow channel unit bodies, all the honeycomb flow channel unit bodies are electrically connected with the high-voltage pulse power supply (12), and the side walls of two adjacent honeycomb flow channel unit bodies are connected. The honeycomb flow channel unit body comprises a metal straight pipe (15) and a cylindrical insulating electrode rod (5), the metal straight pipe (15) is sleeved on the cylindrical insulating electrode rod (5), and there is a flow channel space between the metal straight pipe (15) and the cylindrical insulating electrode rod (5), the length of the cylindrical insulating electrode rod (5) is longer than the length of the metal straight pipe (15), the flow disturbing element (16) is sleeved on the cylindrical insulating electrode rod (5), and the flow disturbing element (16) is located in the flow channel space, the upper end section of the cylindrical insulating electrode rod (5) penetrates through the flow stabilizing structure (3), and the flow stabilizing structure (3) is located above the metal straight pipe (15); The flow stabilizing structure (3) comprises a flow stabilizing blade (9) and a positioning cylinder (22), the number of the flow stabilizing blade (9) and the positioning cylinder (22) is both plural, the number of the positioning cylinder (22) is consistent with the number of the cylindrical insulating electrode rod (5), the cylindrical insulating electrode rod (5) penetrates through the positioning cylinder (22), the adjacent flow stabilizing blades (9) are connected with each other through the positioning cylinder (22), and the free end of the flow stabilizing blade (9) at the outer end is connected with the inner wall of the tubular shell (6).

2. The tubular high-voltage pulsed electric field sludge cell disintegration device according to claim 1, characterized in that The bracket comprises a lower bracket (17) and an upper bracket (10), the lower end of the metal straight pipe (15) is connected with the inner wall of the tubular shell (6) through the lower bracket (17), the upper end of the cylindrical insulating electrode rod (5) is connected with the inner wall of the tubular shell (6) through the upper bracket (10), and the upper bracket (10) is located above the flow stabilizing structure (3).

3. The tubular high-voltage pulsed electric field sludge cell disintegration device according to claim 2, characterized in that It also includes a terminal board (14) and terminal studs (13), the number of terminal studs (13) is consistent with the number of cylindrical insulated electrode rods (5) and one-to-one corresponding connection, the terminal board (14) is connected with all the terminal studs (13), the upper support (10) and the upper end region of the tubular shell (6) form a wiring chamber (1), the terminal board (14) is located in the wiring chamber (1), the positive of the high-voltage pulse power supply (12) is electrically connected with the terminal board (14), the negative of the high-voltage pulse power supply (12) is electrically connected with the metal straight pipe (15); The upper end outer wall of the tubular shell (6) is provided with a wiring pipe (11).

4. The tubular high-voltage pulsed electric field sludge cell wall breaking treatment apparatus according to claim 1, characterized by, The outer surface of the cylindrical insulated electrode rod (5) is provided with an insulating layer, the thickness of the insulating layer is 1-2mm, the cross-sectional shape of the metal straight pipe (15) is a regular polygon or a circle.

5. The tubular high-voltage pulsed electric field sludge cell disintegration device according to claim 1, characterized in that The number of the spoiler elements (16) is consistent with the number of the cylindrical insulated electrode rods (5), the spoiler element (16) includes a sleeve (18) and a spoiler part, the spoiler part is fixedly connected with the side wall of the sleeve (18), the sleeve (18) is sleeved on the cylindrical insulated electrode rod (5); The spoiler part is a dendritic structure (19) or a continuous spiral blade structure (20) or an intermittent spiral blade structure (21).

6. The tubular high-voltage pulsed electric field sludge cell disintegration device according to claim 1, characterized in that The bottom of the tubular shell (6) is provided with a sludge inlet pipe (8) and an inlet expansion section (7), the upper end side wall of the tubular shell (6) is provided with a sludge outlet pipe (2), the height of the sludge outlet pipe (2) is higher than the height of the flow stabilizing structure (3).

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