Suitable for combined homogenizing crushing devices with ultra-high pressure micro-jet homogenizing chamber.

Abstract

This invention discloses a combined homogenizing crushing device suitable for ultra-high pressure micro-jet homogenizing chambers, relating to the field of micro-jet homogenizing chamber technology. It includes a valve body, a feeding mechanism, a discharging mechanism, and a crusher. A processing chamber is formed within the valve body, and an impact ring is installed within the processing chamber. The crusher includes an inlet substrate and an outlet substrate, which are respectively embedded in the feeding mechanism and the discharging mechanism. Inlet and outlet channels are respectively formed on the inlet and outlet substrates. When the feeding mechanism and the discharging mechanism are installed, the inlet and outlet substrates abut against each other to form an integral crusher structure, and the inlet and outlet channels are interconnected. This invention allows for multiple collisions and crushing of materials by the crusher, achieving a higher degree of material crushing and preventing material from easily agglomerating within the crusher.

Description

Technical Field

[0001] This invention relates to the field of microjet homogenizing cavity technology, and more specifically to a combined homogenizing and crushing device suitable for use in ultra-high pressure microjet homogenizing cavities. Background Technology

[0002] A homogenizer is a device that uses ultra-high pressure micro-jet to disperse and break down tissues in the field of biotechnology. It has a wide range of applications in the fine industries such as biopharmaceuticals, food chemicals, and daily chemical care products. It can achieve a material grade of nanometer and micrometer after dispersion and crushing, and the material distribution is uniform. Therefore, the dispersion and crushing structure used in the homogenizer is also an important component that determines the uniformity of the material.

[0003] The existing utility model patent with authorization announcement number CN219482456U discloses a micro-jet homogenizing cavity and homogenizer. The homogenizing cavity includes a shell, a first retainer, a second retainer, and an interactive body. The shell includes a first housing and a second housing. A groove is formed on the second housing. The groove abuts against the first housing through the second retainer, the interactive body, and the first retainer in sequence. The interactive body is narrow at the top and wide at the bottom. The upper part and the groove form a third diversion channel and a fourth diversion channel. A collision channel is provided between the upper and lower parts. A converging channel is provided at the bottom. The third diversion channel and the fourth diversion channel are connected to the converging channel through the collision channel. The first retainer has a channel that is connected to the inlet channel, the third diversion channel, and the fourth diversion channel respectively. The second retainer has a channel that connects the converging channel and the outlet channel.

[0004] The aforementioned homogenizer's micro-jet homogenizing chamber incorporates a first holding member, a second holding member, and an interaction body. Diversion channels are located on both sides of the interaction body, and a collision channel is situated in the middle of the interaction body. This allows materials to collide and break down within the collision channel, achieving homogenized output under ultra-high pressure. However, the overall structure of the interaction body, where collision and breaking occur only in the middle collision channel, allows for only one-time crushing. This can easily result in particles that do not achieve the expected nanometer or micrometer level of uniform crushing. Furthermore, the collision channels still need to be aligned; otherwise, materials may agglomerate within the interaction body. Therefore, this invention provides a processor for uniformly dispersing and crushing materials, improving the degree of material breakage. Summary of the Invention

[0005] To address the shortcomings of existing technologies, the present invention aims to provide a combined homogenizing crushing device suitable for ultra-high pressure micro-jet homogenizing chambers, which features multiple collision crushing of materials by a crushing processor, thereby improving the degree of material crushing and preventing material from agglomerating in the processor.

[0006] To achieve the above objectives, the present invention provides the following technical solution:

[0007] A combined homogenizing and crushing device suitable for ultra-high pressure micro-jet homogenizing chamber, comprising:

[0008] Valve body, wherein a processing cavity is formed in the valve body;

[0009] An impact ring, which is coaxially disposed within the processing cavity;

[0010] The feeding mechanism includes a feeding pipe, which is disposed inside the processing chamber and one end abuts against the impact ring;

[0011] The discharge mechanism includes a discharge pipe, which is disposed inside the processing chamber and one end abuts against the impact ring;

[0012] The feed pipe and the discharge pipe have a homogenized cavity formed at the end that abuts against the impact ring;

[0013] A crusher, comprising an inlet substrate and an outlet substrate, wherein one end of the inlet substrate is embedded in a feed pipe and one end of the outlet substrate is embedded in a discharge pipe;

[0014] When the feed pipe is installed into the processing chamber, the end of the inflow substrate away from the feed pipe extends into the homogenization chamber. When the discharge pipe is installed into the processing chamber, the end of the discharge substrate away from the discharge pipe extends into the homogenization chamber. The inflow substrate located in the homogenization chamber abuts against the discharge substrate.

[0015] The inlet substrate has an inlet channel, and the outlet substrate has an outlet channel. When the inlet substrate and the outlet substrate come into contact, the inlet channel and the outlet channel are connected.

[0016] As a further improvement of the present invention, an impact flow channel is formed between the crusher and the impact ring, and the inflow channel and the outflow channel are respectively connected to the impact flow channel.

[0017] As a further improvement of the present invention, the inlet substrate has an expansion cavity one at one end away from the feed pipe, the expansion cavity one being connected to the inlet channel, and the outlet substrate has an expansion cavity two at one end away from the outlet pipe, the expansion cavity two being connected to the outlet channel. When the inlet substrate and the outlet substrate abut, the expansion cavity one and the expansion cavity two are coaxially spliced.

[0018] As a further improvement of the present invention, the inflow channels are opened along the axial direction of the inflow substrate and are arranged in a plurality of arrays along the circumferential direction of the inflow substrate, and the outflow channels are opened along the axial direction of the outflow substrate and are arranged in a plurality of arrays along the circumferential direction of the outflow substrate.

[0019] As a further improvement of the present invention, the inflow channel includes an inflow port and a branch port one. The inflow port is opened along the axial direction of the inflow substrate, and the branch port one is opened along the radial direction of the inflow substrate. The inflow port and the branch port one are connected.

[0020] The outflow channel includes an outflow port and a second branch port. The outflow port is opened along the axial direction of the outflow base, and the second branch port is opened along the radial direction of the outflow base. The outflow port and the second branch port are connected.

[0021] Both the first and second diversion ports are connected to the impact flow channel.

[0022] As a further improvement of the present invention, the inlet is formed as a single flow channel along the axial direction of the inlet substrate, and the outlet is formed as a single flow channel along the axial direction of the outlet substrate.

[0023] As a further improvement of the present invention, the inlet is arranged in a plurality of arrays along the circumferential direction of the inlet substrate, and the outlet is arranged in a plurality of arrays along the circumferential direction of the outlet substrate.

[0024] As a further improvement of the present invention, the first diversion port is arranged in a plurality of arrays along the circumference of the inflow substrate, and the second diversion port is arranged in a plurality of arrays along the circumference of the outflow substrate.

[0025] As a further improvement of the present invention, the crusher and the impact ring are both made of polycrystalline diamond.

[0026] As a further improvement to the present invention, it also includes:

[0027] A housing, which is disposed outside the valve body;

[0028] Liquid inlet, the housing is provided with a liquid inlet chamber, and the liquid inlet is connected to the liquid inlet chamber;

[0029] The liquid outlet pipe is connected to the liquid outlet chamber inside the housing.

[0030] The inlet chamber and outlet chamber are respectively located at both ends of the valve body, and the housing is also provided with a liquid flow channel for connecting the inlet chamber and the outlet chamber.

[0031] The beneficial effects of this invention are:

[0032] 1. By setting an impact ring in the processing chamber, a homogeneous cavity is formed between the feeding mechanism and the discharge mechanism and the impact ring after installation. The inlet matrix and outlet matrix of the crusher are respectively embedded in the feed pipe and the discharge pipe, so that when the feed pipe and the discharge pipe are installed, the inlet matrix and the outlet matrix abut against each other in the homogeneous cavity, thereby forming the crusher structure. The inlet flow channel opened in the inlet matrix and the outlet flow channel opened in the outlet matrix are interconnected, so that when the material is pumped in, the material is squeezed into the crusher through the inlet flow channel under the action of ultra-high pressure and pumped out uniformly from the outlet flow channel.

[0033] 2. Due to the split structure of the crusher, and after the inlet and outlet substrates are spliced ​​together to form an integral crusher, the inlet and outlet channels are connected. This eliminates the need to consider whether the channels used for material crushing correspond during docking. In this invention, when the material is pumped in, it can be smoothly crushed through the inlet and outlet channels. Due to the structure of the crusher, the material undergoes multiple impacts and compressions during the pumping process, resulting in a uniform distribution of the crushed material. It can also be smoothly pumped out through the inlet and outlet channels along the discharge pipe, realizing multiple collision crushing of the material and improving the degree of material crushing, which is not easily caused by the material clumping together in the processor. Attached Figure Description

[0034] Figure 1 This is a schematic diagram of the first three-dimensional structure of a crushing processor;

[0035] Figure 2 for Figure 1 Enlarged view of part A in the middle;

[0036] Figure 3 This is a schematic diagram of the second three-dimensional structure of the crushing processor;

[0037] Figure 4 A schematic diagram of a crusher structure with a single inflow channel;

[0038] Figure 5 for Figure 4 A cross-sectional view;

[0039] Figure 6 A schematic diagram of a crusher with multiple inflow channels;

[0040] Figure 7 for Figure 6 A cross-sectional view;

[0041] Figure 8 A schematic diagram of a crusher structure with a single inlet.

[0042] Figure 9 for Figure 8 A cross-sectional view;

[0043] Figure 10 A schematic diagram of a crusher with multiple inlets;

[0044] Figure 11 for Figure 10 A cross-sectional view.

[0045] Reference numerals: 1. Valve body; 11. Processing chamber; 12. Homogenizing chamber; 2. Impact ring; 3. Feeding mechanism; 31. Feed pipe; 32. Preload nut one; 4. Discharge mechanism; 41. Discharge pipe; 42. Preload nut two; 5. Crusher; 51. Inlet body; 52. Outlet body; 53. Inlet channel; 531. Inlet; 532. Diverter port one; 54. Outlet channel; 541. Outlet; 542. Diverter port two; 55. Impact channel; 56. Expanding cavity one; 57. Expanding cavity two; 6. Shell; 61. Liquid inlet; 62. Liquid outlet pipe; 63. Liquid flow channel; 7. Sealing assembly; 71. Sealing ring; 72. Support ring. Detailed Implementation

[0046] The present invention will be further described in detail below with reference to the accompanying drawings and embodiments. Identical components are denoted by the same reference numerals. It should be noted that the terms "front," "rear," "left," "right," "upper," and "lower" used in the following description refer to directions in the accompanying drawings, and the terms "bottom surface," "top surface," "inner," and "outer" refer to directions toward or away from the geometric center of a specific component, respectively.

[0047] Example 1:

[0048] refer to Figures 1 to 5The diagram illustrates a specific embodiment of the present invention applicable to a combined homogenizing crushing device within an ultra-high pressure micro-jet homogenizing chamber. It includes a valve body 1, an impact ring 2, a feeding mechanism 3, and a discharging mechanism 4. The valve body 1 contains a processing chamber 11. The impact ring 2 is coaxially disposed within the processing chamber 11. The feeding mechanism 3 includes a feeding pipe 31 and a pre-tightening nut 32. The feeding pipe 31 is coaxially disposed within the processing chamber 11 and one end abuts against the impact ring 2. The pre-tightening nut 32 is used to lock and fix the feeding pipe 31 to the valve body 1. The discharging mechanism 4 includes a discharging pipe 41 and a pre-tightening nut 42. The discharging pipe 41 is coaxially disposed within the processing chamber 11 and one end abuts against the impact ring 2. The pre-tightening nut 42 is used to discharge the material from the valve body 1. The feed pipe 41 is locked and fixed to the valve body 1. The ends of the feed pipe 31 and the discharge pipe 41 that abut against the impact ring 2 form a homogenized cavity 12. The feed pipe 31 and the discharge pipe 41 are sealed to the processing cavity 11 by the sealing assembly 7. The sealing assembly 7 includes a sealing ring 71 and a support ring 72. The sealing ring 71 is sleeved on the outside of the feed pipe 31 and the discharge pipe 41 to form a seal under the action of the sealing ring 71. The support ring 72 is used to press the sealing ring 71 into the processing cavity 11 when the pre-tightening nut 1 32 locks the feed pipe 31, and to press the sealing ring 71 into the processing cavity 11 when the pre-tightening nut 2 42 locks the discharge pipe 41, thereby forming a tight seal.

[0049] It also includes a crusher 5, which includes an inlet substrate 51 and an outlet substrate 52. One end of the inlet substrate 51 is embedded in the feed pipe 31, and one end of the outlet substrate 52 is embedded in the discharge pipe 41. When the feed pipe 31 is installed into the processing chamber 11, the end of the inlet substrate 51 facing away from the feed pipe 31 extends into the homogenization chamber 12. When the discharge pipe 41 is installed into the processing chamber 11, the end of the outlet substrate 52 facing away from the discharge pipe 41 extends into the homogenization chamber 12. At this time, the inlet substrate 51 and the outlet substrate 52 located in the homogenization chamber 12 abut against each other. An inlet flow channel 53 is opened in the inlet substrate 51. An outflow channel 54 is provided in the outflow base 52. When the inflow base 51 and the outflow base 52 come into contact, the inflow channel 53 and the outflow channel 54 are connected. Since the inflow base 51 is embedded in the feed pipe 31 and the outflow base 52 is embedded in the discharge pipe 41, the inflow base 51 and the outflow base 52 are pressed together and pressed after the feed pipe 31 and the discharge pipe 41 are locked by the first preload nut 32 and the second preload nut 42 respectively, thereby forming an integral crusher 5 and making the inflow channel 53 and the outflow channel 54 connected. The crusher 5 and the impact ring 2 are made of polycrystalline diamond.

[0050] It also includes a housing 6, which covers the valve body 1. The housing 6 is connected to an inlet 61 and an outlet pipe 62. The housing 6 is provided with an inlet chamber communicating with the inlet 61 and an outlet chamber communicating with the outlet pipe 62. The inlet chamber and the outlet chamber are respectively located at both ends of the valve body 1. The housing 6 is also provided with a liquid flow channel 63 for connecting the inlet chamber and the outlet chamber, so that condensate is introduced through the inlet 61 and the condensate is circulated through the inlet chamber, the liquid flow channel 63 and the outlet chamber, thereby cooling the valve body 1.

[0051] An expansion cavity 56 is formed at the end of the inlet substrate 51 opposite to the feed pipe 31, and the expansion cavity 56 is connected to the inlet channel 53. An expansion cavity 57 is formed at the end of the outlet substrate 52 opposite to the outlet pipe 41, and the expansion cavity 57 is connected to the outlet channel 54. When the inlet substrate 51 and the outlet substrate 52 come into contact, the expansion cavity 56 and the expansion cavity 57 are coaxially connected, so that when the material is pumped in through the feed pipe 31, the material is squeezed and crushed through the inlet channel 53, enters the expansion cavity 56 through the inlet channel 53, and diffuses evenly in the expansion cavity 56. Since the expansion cavity 56 and the expansion cavity 57 are connected, and the feed pipe 31 continuously feeds in the material, the nanomaterials crushed by the extrusion through the inlet channel 53 are further processed. The nanomaterials are uniformly mixed in the expansion chamber 1 56 and expansion chamber 2 57, and the continuous ultra-high pressure at the inlet channel 53 causes the nanomaterials mixed in the expansion chamber 1 56 and expansion chamber 2 57 to collide and break each other. They are then squeezed and broken again at the outlet channel 54 before being pumped out. This achieves the effect of multiple crushing and uniform mixing of nanomaterials, resulting in uniform pumping out of the crushed nanomaterials. Furthermore, the design of the inlet channel 53, expansion chamber 1 56, expansion chamber 2 57, and outlet channel 54 ensures that the material pumped in through the feed pipe 31 will definitely be pumped out through the discharge pipe 41. Since the inlet substrate 51 and the outlet substrate 52 are connected in a spliced ​​manner, it is convenient to clean the inlet substrate 51 and the outlet substrate 52.

[0052] Example 2:

[0053] refer to Figure 6 and Figure 7 The diagram shows a specific implementation of the present invention applicable to a combined homogenizing crushing device within an ultra-high pressure micro-jet homogenizing chamber. The difference from Embodiment 1 is that: the inlet channel 53 is opened along the axial direction of the inlet substrate 51 and is arranged in multiple arrays along the circumferential direction of the inlet substrate 51; the outlet channel 54 is opened along the axial direction of the outlet substrate 52 and is arranged in multiple arrays along the circumferential direction of the outlet substrate 52. Under the action of multiple inlet channels 53, the efficiency of material crushing in the inlet is improved, and the multiple outlet channels 54 also improve the effect of uniformly pumping out the material after processing, crushing and extrusion.

[0054] Example 3:

[0055] refer to Figure 1 , Figure 2 , Figure 8 and Figure 9 The diagram illustrates a specific embodiment of the present invention applicable to a combined homogenizing crusher within an ultra-high pressure micro-jet homogenizing chamber. The difference from the previous embodiment lies in the following: an impact channel 55 is formed between the crusher 5 and the impact ring 2. An inlet channel 53 and an outlet channel 54 are respectively connected to the impact channel 55. The inlet channel 53 includes an inlet 531 and a first branch port 532. The inlet 531 is axially oriented along the inlet substrate 51, and the first branch port 532 is radially oriented along the inlet substrate 51. The inlet 531 and the first branch port 532 are connected. The outlet channel 54 includes an outlet 541 and a second branch port 542. The outlet 541 is axially oriented along the outlet substrate 52, and the second branch port 542 is radially oriented along the outlet substrate 52. The outlet 541 and the second branch port 542 are connected. Both the first diversion port 532 and the second diversion port 542 are connected to the impact channel 55. The inlet port 531 is opened as a single channel along the axial direction of the inlet substrate 51, and the outlet port 541 is opened as a single channel along the axial direction of the outlet substrate 52. This allows the nanomaterials to be pumped in through the feed pipe 31, crushed by compression through the inlet port 531, and then enter the first diversion port 532. The material is crushed by impact at the connection between the inlet port 531 and the first diversion port 532. After the impact crushing, the material is guided into the impact channel 55 through the first diversion port 532 and crushed again by impact with the impact ring 2 at the outlet of the impact channel 55. The material after impact crushing is guided into the outlet substrate 52 through the second diversion port 542 and pumped out through the outlet port 541, thereby achieving uniform pumping out of the material after multiple impacts.

[0056] Diverter port 1 532 includes a single flow channel opened along the inlet substrate 51 and a plurality of channels arranged in an array along the circumferential direction of the inlet substrate 51; Diverter port 2 542 includes a single flow channel opened along the outlet substrate 52 and a plurality of channels arranged in an array along the circumferential direction of the outlet substrate 52.

[0057] Example 4:

[0058] refer to Figure 10 and Figure 11 The figure shows a specific implementation of the present invention applicable to the combined homogenizing crushing device in the ultra-high pressure micro-jet homogenizing cavity. The difference from embodiment three is that: the inlet 531 is arranged in multiple arrays along the circumferential direction of the inlet substrate 51, the outlet 541 is arranged in multiple arrays along the circumferential direction of the outlet substrate 52, the first diversion port 532 is arranged in multiple arrays along the circumferential direction of the inlet substrate 51, and the second diversion port 542 is arranged in multiple arrays along the circumferential direction of the outlet substrate 52.

[0059] Working principle and its effects:

[0060] By setting an impact ring 2 in the processing chamber 11, a homogeneous chamber 12 is formed between the feeding mechanism 3 and the discharging mechanism 4 and the impact ring 2 after installation. The inlet substrate 51 and the outlet substrate 52 in the crusher 5 are respectively embedded in the feed pipe 31 and the discharge pipe 41, so that when the feed pipe 31 and the discharge pipe 41 are installed, the inlet substrate 51 and the outlet substrate 52 abut against each other in the homogeneous chamber 12, thereby forming the structure of the crusher 5. The inlet channel 53 opened in the inlet substrate 51 and the outlet channel 54 opened in the outlet substrate 52 are interconnected, so that when the nanomaterial is pumped in, the nanomaterial is squeezed into the crusher 5 by the inlet channel 53 under the action of ultra-high pressure, and is uniformly pumped out from the outlet channel 54. Due to the split structure of the crusher 5, and after the inlet base 51 and the outlet base 52 are spliced ​​together to form the integral crusher 5, the inlet channel 53 and the outlet channel 54 are connected. This eliminates the need to consider whether the channels used for crushing materials correspond during docking. In this invention, when the material is pumped in, it can be smoothly crushed through the inlet channel 53 and the outlet channel 54. Due to the structure of the crusher 5, the material will undergo multiple impacts and compressions during the pumping process, thereby achieving a uniform distribution of the crushed material. It can also be smoothly pumped out through the inlet channel 53 and the outlet channel 54 along the discharge pipe 41, realizing multiple collision crushing of the material and improving the degree of material crushing, which is not easy to cause agglomeration in the processor.

[0061] The above description is merely a preferred embodiment of the present invention. The scope of protection of the present invention is not limited to the above embodiments. All technical solutions falling within the scope of the present invention's concept are within the scope of protection of the present invention. It should be noted that for those skilled in the art, any improvements and modifications made without departing from the principles of the present invention should also be considered within the scope of protection of the present invention.

Claims

1. A combined homogenizing and crushing device suitable for ultra-high pressure micro-jet homogenizing chamber, characterized in that, include: Valve body (1), wherein a processing chamber (11) is formed in the valve body (1); Impact ring (2), which is coaxially disposed in the processing cavity (11); The feeding mechanism (3) includes a feeding pipe (31), which is disposed in the processing chamber (11) and one end abuts against the impact ring (2); The discharge mechanism (4) includes a discharge pipe (41), which is disposed in the processing chamber (11) and one end abuts against the impact ring (2); The feed pipe (31) and the discharge pipe (41) have a homogenized cavity (12) at the end that abuts against the impact ring (2); The crusher (5) includes an inlet substrate (51) and an outlet substrate (52). One end of the inlet substrate (51) is embedded in the feed pipe (31), and one end of the outlet substrate (52) is embedded in the discharge pipe (41). When the feed pipe (31) is installed into the processing chamber (11), the end of the inlet substrate (51) facing away from the feed pipe (31) extends into the homogenization chamber (12). When the outlet pipe (41) is installed into the processing chamber (11), the end of the outlet substrate (52) facing away from the outlet pipe (41) extends into the homogenization chamber (12). The inlet substrate (51) located in the homogenization chamber (12) abuts against the outlet substrate (52). The inlet substrate (51) has an inlet channel (53), and the outlet substrate (52) has an outlet channel (54). When the inlet substrate (51) and the outlet substrate (52) come into contact, the inlet channel (53) and the outlet channel (54) are connected. An impact channel (55) is also formed between the crusher (5) and the impact ring (2), and the inflow channel (53) and the outflow channel (54) are respectively connected to the impact channel (55); The inflow channel (53) includes an inflow port (531) and a branch port (532). The inflow port (531) is opened along the axial direction of the inflow substrate (51), and the branch port (532) is opened along the radial direction of the inflow substrate (51). The inflow port (531) and the branch port (532) are connected. The outflow channel (54) includes an outflow port (541) and a second branch port (542). The outflow port (541) is opened along the axial direction of the outflow base (52), and the second branch port (542) is opened along the radial direction of the outflow base (52). The outflow port (541) and the second branch port (542) are connected. Both the first diversion port (532) and the second diversion port (542) are connected to the impact channel (55).

2. The combined homogenizing crushing device suitable for ultra-high pressure micro-jet homogenizing chambers according to claim 1, characterized in that: The inlet substrate (51) has an expansion cavity one (56) at one end away from the feed pipe (31), and the expansion cavity one (56) is connected to the inlet channel (53). The outlet substrate (52) has an expansion cavity two (57) at one end away from the outlet pipe (41), and the expansion cavity two (57) is connected to the outlet channel (54). When the inlet substrate (51) and the outlet substrate (52) come into contact, the expansion cavity one (56) and the expansion cavity two (57) are coaxially spliced.

3. The combined homogenizing crushing device suitable for ultra-high pressure micro-jet homogenizing chambers according to claim 2, characterized in that: The inlet channel (53) is opened along the axial direction of the inlet substrate (51) and is arranged in multiple arrays along the circumferential direction of the inlet substrate (51). The outlet channel (54) is opened along the axial direction of the outlet substrate (52) and is arranged in multiple arrays along the circumferential direction of the outlet substrate (52).

4. The combined homogenizing crushing device suitable for ultra-high pressure micro-jet homogenizing chambers according to claim 1, characterized in that: The inlet (531) is formed as a single flow channel along the axial direction of the inlet substrate (51), and the outlet (541) is formed as a single flow channel along the axial direction of the outlet substrate (52).

5. The combined homogenizing crushing device suitable for ultra-high pressure micro-jet homogenizing chambers according to claim 1, characterized in that: The inlet (531) is arranged in a plurality of arrays along the circumferential direction of the inlet substrate (51), and the outlet (541) is arranged in a plurality of arrays along the circumferential direction of the outlet substrate (52).

6. The combined homogenizing crushing device suitable for ultra-high pressure micro-jet homogenizing chambers according to claim 1 or 4, characterized in that: The first diversion port (532) is arranged in a circumferential array along the inlet substrate (51), and the second diversion port (542) is arranged in a circumferential array along the outlet substrate (52).

7. The combined homogenizing crushing device suitable for ultra-high pressure micro-jet homogenizing chambers according to claim 1, characterized in that: The crusher (5) and the impact ring (2) are made of polycrystalline diamond.

8. The combined homogenizing crushing device suitable for ultra-high pressure micro-jet homogenizing chambers according to claim 7, characterized in that, Also includes: Housing (6), which covers the valve body (1); Liquid inlet (61), the housing (6) is provided with a liquid inlet chamber, and the liquid inlet (61) is connected to the liquid inlet chamber; The liquid outlet pipe (62) is provided in the housing (6), and the liquid outlet chamber is connected to the liquid outlet pipe (62); The inlet chamber and outlet chamber are respectively located at both ends of the valve body (1), and the housing (6) is also provided with a liquid flow channel (63) for connecting the inlet chamber and the outlet chamber.

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