Homogenizing system
By setting a cooler in the hydraulic system to maintain the hydraulic oil temperature, the problem of unstable hydraulic oil pressure is solved, the homogenization effect and equipment safety are ensured, and the stability of pressure and viscosity is achieved.
Patent Information
- Application Number
- CN202422321541.6
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-09-23
- Publication Date
- 2025-07-22
- Estimated Expiration
- 2034-09-23
AI Technical Summary
Poor homogenization results from unstable hydraulic oil pressure and equipment damage problems, especially when the hydraulic oil temperature rises, the viscosity drops and the working rated pressure cannot be maintained.
By setting a cooler in the pipeline of the hydraulic system, the hydraulic oil temperature is maintained between 30°C and 40°C, and the viscosity of the hydraulic oil is stabilized, thereby maintaining the pressure at the homogeneous gap between 245°C and 255bar to prevent equipment damage.
Effectively maintain the pressure stability of the homogenization gap, avoid equipment damage, ensure homogeneity effect, avoid frequent adjustment of hydraulic oil pressure, and improve the operating reliability of the equipment.
Smart Images
Figure CN223127867U_ABST
Abstract
Description
Technical Field
[0001] The present application relates to the technical field of homogenizers, and in particular to a homogenizing system. Background Art
[0002] The high-pressure homogenizer uses a plunger pump to generate high pressure to transport the material into the high-pressure homogenization chamber. Under the action of high pressure, the material is forced to pass through the homogenization gap to form a high-speed jet flow. In this process, the material is subjected to strong pressure, which helps to break and disperse its particles.
[0003] The hydraulic oil provides pressure to the hydraulic head. However, as the operation time of the device increases, the hydraulic oil circulates continuously, and its temperature gradually increases, resulting in a decrease in viscosity, which in turn causes a decrease in the pressure transmitted to the hydraulic head, and fails to reach the minimum process requirement standard pressure of 245 bar. When it is lower than 245 bar, the equipment automatically stops production. Therefore, the relevant technology is to increase the initial hydraulic oil pressure to 280 bar. During the operation, even if the hydraulic oil temperature increases, the viscosity decreases, and the pressure decreases, it can be guaranteed not to drop below 245 bar to ensure normal production. However, when the hydraulic oil pressure reaches 280 bar, it will cause damage to the internal components of the equipment. Utility Model Content
[0004] In view of this, the present application provides a homogenizing system to solve or improve the problem of unstable hydraulic oil pressure.
[0005] The present application provides a homogenizing system, comprising:
[0006] The homogenizer is provided with a pressurizing chamber, a feeding channel and a homogenizing channel. A feeding port is provided on the wall of the pressurizing chamber. The feeding channel is connected with the feeding port through a one-way valve. The pressurizing chamber is provided with a pressurizing port and an output port. The homogenizing channel is connected with the output port.
[0007] The driving device is provided with a telescopic driving rod, which penetrates into the pressurizing chamber from the pressurizing port and reciprocates in the pressurizing chamber, and the telescopic driving rod is sealingly and slidably connected with the pressurizing port, and is used to suck the material in the feed channel into the pressurizing chamber and convey it to the homogenizing channel;
[0008] A hydraulic cylinder, wherein the rodless chamber is provided with an oil inlet and an oil outlet, the hydraulic rod of the hydraulic cylinder is arranged correspondingly to the outlet, a homogenous gap is formed between the hydraulic rod and the outlet, and the homogenous gap is connected to the homogenous channel;
[0009] The hydraulic system is provided with an output port and a return port, which are respectively connected to the oil inlet and the oil outlet through pipelines. The hydraulic system transports the hydraulic oil to the rodless cavity so that the hydraulic rod can adjust the size of the homogenizing gap. A cooler is installed on the pipeline to control the hydraulic oil in the pipeline at a rated temperature.
[0010] Beneficial effects: The telescopic drive rod passes through the pressurizing port and reciprocates in the pressurizing cavity. When the telescopic drive rod is withdrawn from the pressurizing cavity, the pressure inside the pressurizing cavity decreases. Under the action of the one-way valve, the dairy product in the feed channel enters the pressurizing cavity. When the telescopic drive rod extends and squeezes the pressurizing cavity, the pressure inside the pressurizing cavity increases. Under the action of the one-way valve, the dairy product cannot enter the feed channel and can only enter the homogenization channel through the output port and the homogenization gap. When the dairy product passes through the homogenization gap, it passes through a tiny homogenization gap under high pressure, and the dairy product experiences shearing, impact, and cavitation effects, forcing the particles to be refined and evenly distributed. During this period, the hydraulic cylinder needs to maintain the pressure at the homogenization gap between 245 and 255 bar for a long time. Otherwise, an increase in the homogenization gap will reduce the homogenization effect. The temperature of the hydraulic oil is inversely proportional to its viscosity. As the homogenization time increases, the hydraulic oil circulates continuously, and its temperature will gradually rise, resulting in a decrease in viscosity, and then a decrease in the pressure transmitted to the hydraulic rod. The hydraulic rod cannot reach the working rated pressure of 245 - 255 bar, resulting in poor homogenization effect. By installing a cooler in the pipeline of the hydraulic system, the hydraulic oil is stabilized between 30°C and 40°C. When the hydraulic oil is between 30°C and 40°C, its viscosity is stable, which can make the pressure at the homogenization gap between 245 and 255 bar. There is no need to adjust the pressure of the hydraulic oil very high at the initial stage of homogenization to prevent the pressure from decreasing below the working rated pressure after the temperature of the hydraulic oil rises, resulting in problems that cannot work properly. And the initial pressure is below 280 bar to prevent damage to the equipment in the homogenization system.
[0011] In an alternative embodiment, the hydraulic system includes a box body, a hydraulic pump, and a cooler. The box body, the hydraulic pump, the hydraulic cylinder, and the cooler are connected in series through pipes end to end.
[0012] In an alternative embodiment, the hydraulic system further includes a pressure regulating valve, and the pressure regulating valve is installed on the pipeline.
[0013] In an alternative embodiment, the cooler includes a shell and heat exchange tubes arranged inside the shell. The shell is provided with a cooling water inlet and a cooling water outlet. One end of the heat exchange tube is communicated with the cooling water inlet, and the other end is communicated with the cooling water outlet. A heat exchange space is formed between the heat exchange tube and the inner cavity of the shell.
[0014] In an alternative embodiment, the driving device is a driving oil cylinder, and the telescopic drive rod is adapted to telescopically switch between a first position and a second position. During the movement from the first position to the second position, the pressure in the pressurizing cavity decreases, sucking the material in the feed channel into the pressurizing cavity. During the movement from the second position to the first position, the pressure in the pressurizing cavity increases, transporting the material in the pressurizing cavity to the homogenization gap.
[0015] In an alternative embodiment, the pressurizing chamber is provided with a plurality of feed ports, and the side wall of the feed channel is provided with a plurality of communication ports corresponding to the plurality of feed ports. The plurality of feed ports and the plurality of communication ports are communicated through a plurality of one-way valves.
[0016] In an alternative embodiment, the side wall of the homogenization channel is provided with perforations, and the hydraulic rod is hermetically and slidably connected to the perforations.
[0017] In an alternative embodiment, corresponding to the output port, a stepped groove is formed in the inner wall of the end portion of the feed channel, and a homogenization gap is formed between the end portion of the hydraulic rod and the stepped groove.
[0018] In an alternative embodiment, the end portion of the hydraulic rod protrudes radially outward to form a homogenization head, and a homogenization gap is formed between the outer wall of the homogenization head and the inner wall of the stepped groove.
[0019] In an alternative embodiment, the homogenization head is provided with a blocking surface corresponding to the output port, and the area of the blocking surface is larger than the cross-sectional area of the output port. Description of the Drawings
[0020] In order to more clearly illustrate the specific embodiments of the present application or the technical solutions in the prior art, the following will briefly introduce the drawings required for the description of the specific embodiments or the prior art. Obviously, the drawings in the following description are some embodiments of the present application. For those of ordinary skill in the art, other drawings can be obtained based on these drawings without creative efforts.
[0021] Figure 1 It is a schematic structural diagram of a homogenizer and a hydraulic cylinder in a homogenization system according to an embodiment of the present application;
[0022] Figure 2 It is a schematic structural diagram of a hydraulic system in a homogenization system according to an embodiment of the present application.
[0023] Description of the Reference Numerals:
[0024] 1. Homogenizer; 101. Pressurizing chamber; 1011. Output port; 1012. Feed port; 102. Feed channel; 103. Homogenization channel; 2. Hydraulic cylinder; 201. Hydraulic rod; 3. One-way valve; 4. Homogenization gap; 5. Hydraulic system; 501. Cooler; 502. Box body; 503. Hydraulic pump; 504. Pressure regulating valve; 6. Stepped groove; 7. Homogenization head; 8. First annular protrusion; 9. Second annular protrusion; 10. Communication channel; 11. Compression spring. Detailed Embodiments
[0025] To make the objectives, technical solutions, and advantages of the embodiments of this application clearer, the following will clearly and completely describe the technical solutions in the embodiments of this application with reference to the accompanying drawings in the embodiments of this application. Apparently, the described embodiments are some, but not all, of the embodiments of this application. All other embodiments obtained by those skilled in the art based on the embodiments in this application without creative efforts fall within the scope of protection of this application.
[0026] A plurality of hydraulic cylinders 2 are arranged in a homogeneous system. The plurality of hydraulic cylinders 2 are connected in series through oil pipes. The hydraulic system 5 supplies hydraulic oil to the plurality of hydraulic cylinders 2 simultaneously. Therefore, the hydraulic oil needs to circulate in the oil pipes.
[0027] The following combines Figures 1 to 2 , to describe the embodiments of this application.
[0028] According to an embodiment of this application, a homogeneous system is provided, including a homogenizer 1, a driving device, a hydraulic cylinder 2, and a hydraulic system 5;
[0029] Specifically, the homogenizer 1 is provided with a pressurizing chamber 101, a feed channel 102, and a homogenizing channel 103. A feed port 1012 is formed on the chamber wall of the pressurizing chamber 101. The feed channel 102 and the feed port 1012 are connected through a one-way valve 3. The pressurizing chamber 101 is provided with a pressurizing port and an output port 1011. The homogenizing channel 103 is connected to the output port 1011;
[0030] The driving device is provided with a telescopic driving rod. The telescopic driving rod penetrates into the pressurizing chamber 101 from the pressurizing port and reciprocates in the pressurizing chamber 101. The telescopic driving rod is hermetically and slidably connected to the pressurizing port, and is used to suck the material in the feed channel 102 into the pressurizing chamber 101 and transport it to the homogenizing channel 103;
[0031] The rodless chamber of the hydraulic cylinder 2 is provided with an oil inlet and an oil outlet. The hydraulic rod 201 of the hydraulic cylinder 2 is arranged corresponding to the output port 1011. A homogenizing gap 4 is formed between the hydraulic rod 201 and the output port 1011. The homogenizing gap 4 is connected to the homogenizing channel 103;
[0032] The hydraulic system 5 is provided with an output port 1011 and a return port. The output port 1011 and the return port are respectively connected to the oil inlet and the oil outlet through pipelines. The hydraulic system 5 transports hydraulic oil into the rodless chamber to enable the hydraulic rod 201 to adjust the size of the homogenizing gap 4. A cooler 501 for controlling the hydraulic oil in the pipeline at a rated temperature is installed on the pipeline.
[0033] The telescopic drive rod passes through the pressurizing port and reciprocates within the pressurizing chamber 101. When the telescopic drive rod is withdrawn from the pressurizing chamber 101, the pressure inside the pressurizing chamber 101 decreases. Under the action of the one-way valve 3, the dairy product in the feed channel 102 enters the pressurizing chamber 101. When the telescopic drive rod extends and squeezes the pressurizing chamber 101, the pressure inside the pressurizing chamber 101 increases. Under the action of the one-way valve 3, the dairy product cannot enter the feed channel 102 and can only pass through the output port 1011 and the homogenization gap 4 into the homogenization channel 103. When the dairy product passes through the homogenization gap 4, it passes through a tiny homogenization gap 4 under high pressure. The dairy product undergoes shearing, impact, and cavitation effects, forcing the particles to be refined and evenly distributed. During this period, the hydraulic cylinder 2 needs to maintain the pressure at the homogenization gap 4 between 245 and 255 bar for a long time. Otherwise, an increase in the homogenization gap 4 will reduce the homogenization effect. The temperature of the hydraulic oil is inversely proportional to its viscosity. As the homogenization time increases, the hydraulic oil circulates continuously, and its temperature will gradually rise, resulting in a decrease in viscosity, and then a decrease in the pressure transmitted to the hydraulic rod 201. The hydraulic rod 201 cannot reach the working rated pressure of 245 to 255 bar, resulting in poor homogenization effect. By setting a cooler 501 in the pipeline of the hydraulic system 5, the hydraulic oil is stabilized between 30°C and 40°C. When the hydraulic oil is between 30°C and 40°C, the viscosity is stable, which can make the pressure at the homogenization gap 4 between 245 and 255 bar. There is no need to adjust the pressure of the hydraulic oil very high at the initial stage of homogenization to prevent the pressure from decreasing below the working rated pressure after the temperature of the hydraulic oil rises, resulting in the problem of abnormal operation. And the initial pressure is below 280 bar to prevent the equipment in the homogenization system from being damaged.
[0034] It should be noted that the hydraulic oil is cooled in the cooler 501. The cooler 501 maintains the temperature of the hydraulic oil between 30°C and 40°C, which can stabilize the viscosity of the hydraulic oil, prevent its temperature from rising and causing a decrease in viscosity, and then a decrease in pressure, so that the working rated pressure required for homogenization cannot be maintained.
[0035] Further explanation is as follows. A communication channel 10 communicating with the feed channel 102 is provided on the wall of the pressurization chamber 101. First annular protrusions 8 and second annular protrusions 9 are respectively provided on the inner walls at both ends of the communication channel 10. The first annular protrusion 8 is arranged close to the pressurization chamber 101, and the second annular protrusion 9 is arranged close to the feed channel 102. The one-way valve 3 is arranged between the first annular protrusion 8 and the second annular protrusion 9. The one-way valve 3 includes a sealing head and a connection head fixedly connected. The compression spring 11 is sleeved on the sealing head, and the other end abuts against the first annular protrusion 8. The sealing head abuts against the inner hole wall of the second annular protrusion 9. When the telescopic drive rod is withdrawn from the pressurization chamber 101, the pressure inside the pressurization chamber 101 decreases, the sealing head moves away from the second annular protrusion 9, opening the inner hole of the second annular protrusion 9, and the dairy product enters the pressurization chamber 101 from the feed channel 102. When the telescopic drive rod extends into and squeezes the pressurization chamber 101, the pressure inside the pressurization chamber 101 increases, and the sealing head seals the inner hole of the second annular protrusion 9 to prevent the dairy product in the pressurization chamber 101 from flowing back to the feed channel 102.
[0036] It needs to be further explained that the inner hole of the second annular protrusion 9 is the feed port 1012.
[0037] In one embodiment, the hydraulic system 5 includes a box body 502, a hydraulic pump 503 and a cooler 501. The box body 502, the hydraulic pump 503, the hydraulic cylinder 2 and the cooler 501 are connected in series through pipes end to end. The box body 502 is communicated with the input port of the hydraulic pump 503 through a first pipe. The output port 1011 of the hydraulic pump 503 is communicated with the oil inlet of the rodless cavity through a second pipe. The oil outlet of the rodless cavity is communicated with the liquid inlet of the cooler 501 through a third pipe. The liquid outlet of the cooler 501 is communicated with the box body 502 through a fourth pipe. The hydraulic pump 503 transports the hydraulic oil in the box body 502 into the rodless cavity in the hydraulic rod 201, pushing the hydraulic rod 201 so that the end of the hydraulic rod 201 corresponds to the output port 1011. A homogenization gap 4 is formed between the end of the hydraulic rod 201 and the output port 1011. The end of the hydraulic rod 201 presses against the dairy product output from the pressurization chamber 101, and the dairy product is homogenized through the homogenization gap 4.
[0038] It needs to be further explained that when the cooler 501 maintains the temperature of the hydraulic oil at 30°C, 35°C and 40°C, the viscosity of the hydraulic oil is stable, the same as the pressure output by the hydraulic pump 503, and no pressure loss will be caused.
[0039] In one embodiment, the hydraulic system 5 further includes a pressure regulating valve 504, and the pressure regulating valve 504 is installed on the pipe.
[0040] It should be noted that the pressure regulating valve 504 can be installed on any one of the first pipeline, the second pipeline, the third pipeline and the fourth pipeline in the hydraulic system 5. The pressure regulating valve 504 can adjust the return flow of the hydraulic oil to control the pressure of the hydraulic oil. However, when the temperature of the hydraulic oil rises, the pressure drop is a continuous process. Therefore, workers need to frequently adjust the pressure regulating valve 504. After the pressure regulating valve 504 adjusts the pressure of the hydraulic oil to 245-255 bar, the cooler 501 maintains the temperature of the hydraulic oil between 30°C and 40°C, and then the pressure of the hydraulic oil will be maintained between 245-255 bar.
[0041] Furthermore, the box body 502, the hydraulic pump 503, the pressure regulating valve 504 and the cooler 501 are connected in series through the first pipeline, the second pipeline and the third pipeline.
[0042] In one embodiment, the cooler 501 includes a shell and heat exchange tubes arranged in the shell. The shell is provided with a cooling water inlet and a cooling water outlet. One end of the heat exchange tube is communicated with the cooling water inlet, and the other end is communicated with the cooling water outlet. A heat exchange space is formed between the heat exchange tube and the inner cavity of the shell.
[0043] In a specific embodiment, the heat exchange tubes are spirally wound, which can increase the storage capacity of cold water and improve the cooling effect.
[0044] In one embodiment, the driving device is a driving oil cylinder. The telescopic driving rod is adapted to telescopically switch between a first position and a second position. During the movement from the first position to the second position, the pressure in the pressurizing chamber 101 decreases, and the material in the feeding channel 102 is sucked into the pressurizing chamber 101. During the movement from the second position to the first position, the pressure in the pressurizing chamber 101 increases, and the material in the pressurizing chamber 101 is conveyed to the homogenization gap 4. When the telescopic driving rod moves from the first position to the second position, it is equivalent to the telescopic driving rod being withdrawn from the pressurizing chamber 101, and the pressure in the pressurizing chamber 101 decreases. Under the action of the one-way valve 3, the dairy product in the feeding channel 102 is sucked into the pressurizing chamber 101. Subsequently, when the telescopic driving rod moves from the second position to the first position, it is equivalent to the telescopic driving rod extending into and squeezing the pressurizing chamber 101, and the pressure inside the pressurizing chamber 101 increases. Under the action of the one-way valve 3, the dairy product cannot enter the feeding channel 102, and the high-pressure dairy product is conveyed to the homogenization gap 4 for homogenization.
[0045] In one embodiment, the pressurizing chamber 101 is provided with a plurality of feeding ports 1012. The side wall of the feeding channel 102 is provided with a plurality of communication ports corresponding to the plurality of feeding ports 1012. The plurality of feeding ports 1012 and the plurality of communication ports are communicated through a plurality of one-way valves 3. The arrangement of the plurality of feeding ports 1012 and the plurality of communication ports can improve the working efficiency and increase the single-time homogenization output of the dairy product when the telescopic driving rod makes a reciprocating movement once.
[0046] It should be further noted that a plurality of communication channels 10 communicating with the feed channel 102 are provided on the chamber wall of the pressurizing chamber 101, and a one-way valve 3 is installed in each communication channel 10.
[0047] In one embodiment, a perforation is provided on the side wall of the homogenization channel 103, and the hydraulic rod 201 is in sealed sliding connection with the perforation.
[0048] In one embodiment, corresponding to the outlet 1011, a stepped groove 6 is provided on the inner wall of the end of the feed channel 102, and a homogenization gap 4 is formed between the end of the hydraulic rod 201 and the stepped groove 6. This can extend the path that the dairy product passes through in the homogenization gap 4 and improve the homogenization effect.
[0049] In one embodiment, the end of the hydraulic rod 201 protrudes radially outward to form a homogenization head 7, and a homogenization gap 4 is formed between the outer wall of the homogenization head 7 and the inner wall of the stepped groove 6.
[0050] In one embodiment, the homogenization head 7 is provided with a blocking surface corresponding to the outlet 1011, and the area of the blocking surface is larger than the cross-sectional area of the outlet 1011.
[0051] Next, taking an embodiment as an example, in combination with Figures 1 to 2 the above all solutions will be comprehensively elaborated.
[0052] Taking the homogenization of dairy products as an example:
[0053] The dairy product is conveyed through the feeding channel 102. During the movement of the telescopic driving rod from the first position to the second position, the pressure in the pressurizing chamber 101 decreases, the sealing head moves away from the second annular protrusion 9, and the compression spring 11 is compressed, opening the inner hole of the second annular protrusion 9. The dairy product passes through the inner hole of the second annular protrusion 9, the communication channel 10, and the inner hole of the first annular protrusion 8 from the feeding channel 102 and enters the pressurizing chamber 101. During the movement of the telescopic driving rod from the second position to the first position, when the telescopic driving rod extends into and squeezes the pressurizing chamber 101, the pressure inside the pressurizing chamber 101 increases, and the sealing head seals the inner hole of the second annular protrusion 9 to prevent the dairy product in the pressurizing chamber 101 from flowing back to the feeding channel 102, and conveys the dairy product to the homogenization gap 4 through the output port 1011 for homogenization. During this period, the hydraulic cylinder 2 needs to maintain the pressure at the homogenization gap 4 between 245 and 255 bar for a long time. Otherwise, an increase in the homogenization gap 4 will reduce the homogenization effect. The temperature of the hydraulic oil is inversely proportional to its viscosity. As the homogenization time increases, the hydraulic oil circulates continuously, and its temperature will gradually rise, resulting in a decrease in viscosity, and further resulting in a decrease in the pressure transmitted to the hydraulic rod 201. The hydraulic rod 201 cannot reach the working rated pressure of 245 to 255 bar, resulting in poor homogenization effect. By setting a cooler 501 in the pipeline of the hydraulic system 5, the hydraulic oil is stabilized at 35°C. When the hydraulic oil is at 35°C, its viscosity is stable, which can make the pressure at the homogenization gap 4 between 245 and 255 bar, and there is no need to adjust the pressure of the hydraulic oil very high at the initial stage of homogenization to prevent the pressure from decreasing below 245 bar after the temperature of the hydraulic oil rises, resulting in the problem of abnormal operation, and the initial pressure is below 280 bar to prevent the equipment in the homogenization system from being damaged.
[0054] Although the embodiments of the present application have been described in conjunction with the accompanying drawings, those skilled in the art can make various modifications and variations without departing from the spirit and scope of the present application, and such modifications and variations all fall within the scope defined by the appended claims of the present application.
Claims
1. A homogenization system, characterized in that, Comprising: A homogenizer (1) provided with a pressurizing chamber (101), a feed channel (102) and a homogenization channel (103). An inlet (1012) is formed in the wall of the pressurizing chamber (101). The feed channel (102) is communicated with the inlet (1012) through a check valve (3). The pressurizing chamber (101) is provided with a pressurizing port and an outlet (1011). The homogenization channel (103) is communicated with the outlet (1011). A driving device provided with a telescopic driving rod. The telescopic driving rod penetrates into the pressurizing chamber (101) from the pressurizing port and reciprocates in the pressurizing chamber (101). The telescopic driving rod is in sealed sliding connection with the pressurizing port and is used for sucking the material in the feed channel (102) into the pressurizing chamber (101) and conveying it to the homogenization channel (103). A hydraulic cylinder (2) whose rodless chamber is provided with an oil inlet and an oil outlet. The hydraulic rod (201) of the hydraulic cylinder (2) is arranged corresponding to the outlet (1011). A homogenization gap (4) is formed between the hydraulic rod (201) and the outlet (1011). The homogenization gap (4) is communicated with the homogenization channel (103). A hydraulic system (5) provided with an outlet (1011) and a return port. The outlet (1011) and the return port are respectively communicated with the oil inlet and the oil outlet through pipelines. The hydraulic system (5) conveys hydraulic oil into the rodless chamber to enable the hydraulic rod (201) to adjust the size of the homogenization gap (4). A cooler (501) for controlling the hydraulic oil in the pipeline at a rated temperature is installed on the pipeline.
2. The homogenization system according to claim 1, characterized in that, The hydraulic system (5) includes a box body (502), a hydraulic pump (503) and the cooler (501). The box body (502), the hydraulic pump (503), the hydraulic cylinder (2) and the cooler (501) are connected in series through pipelines end to end.
3. The homogenization system according to claim 2, characterized in that The hydraulic system (5) further includes a pressure regulating valve (504). The pressure regulating valve (504) is installed on the pipeline.
4. The homogenization system according to claim 2, characterized in that The cooler (501) includes a shell and heat exchange tubes arranged in the shell. A cooling water inlet and a cooling water outlet are formed in the shell. One end of the heat exchange tube is communicated with the cooling water inlet, and the other end is communicated with the cooling water outlet. A heat exchange space is formed between the heat exchange tube and the inner cavity of the shell.
5. The homogenization system according to claim 2, characterized in that, The driving device is a driving oil cylinder. The telescopic driving rod is adapted to telescopically switch between a first position and a second position. During the movement from the first position to the second position, the pressure in the pressurizing chamber (101) decreases, sucking the material in the feed channel (102) into the pressurizing chamber (101). During the movement from the second position to the first position, the pressure in the pressurizing chamber (101) increases, conveying the material in the pressurizing chamber (101) to the homogenization gap (4).
6. The homogenization system according to claim 1, characterized in that, The pressurization chamber (101) is provided with a plurality of the feed ports (1012), and the side wall of the feed channel (102) is provided with a plurality of communication ports corresponding to the plurality of the feed ports (1012), and the plurality of the feed ports (1012) and the plurality of the communication ports are communicated through a plurality of the one-way valves (3).
7. The homogenization system according to claim 1, characterized in that The side wall of the homogenization channel (103) is provided with perforations, and the hydraulic rod (201) is in sealed sliding connection with the perforations.
8. The homogenization system according to claim 7, characterized in that, Corresponding to the output port (1011), a stepped groove (6) is formed in the inner wall of the end of the feed channel (102), and a homogenization gap (4) is formed between the end of the hydraulic rod (201) and the stepped groove (6).
9. The homogenization system according to claim 8, characterized in that, The end of the hydraulic rod (201) protrudes radially outward to form a homogenization head (7), and the homogenization gap (4) is formed between the outer wall of the homogenization head (7) and the inner wall of the stepped groove (6).
10. The homogenization system according to claim 9, characterized in that, The homogenization head (7) is provided with a blocking surface corresponding to the output port (1011), and the area of the blocking surface is larger than the cross-sectional area of the output port (1011).