Disc type heating foaming agent vaporization device
By combining a disc heating element with a spiral liquid tube and using an automatic cleaning component, the problems of uneven temperature and scaling during the vaporization of the foaming agent are solved, achieving efficient and stable vaporization and reducing operation and maintenance costs.
Patent Information
- Application Number
- CN202511627357.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-11-07
- Publication Date
- 2026-02-27
AI Technical Summary
The existing device exhibits uneven effects of temperature changes on different types of foaming agents during the vaporization process, resulting in low vaporization efficiency. Furthermore, the inner wall of the spiral liquid pipe is prone to scaling, which affects heat transfer efficiency.
The design combines a disc heating element with a spiral liquid tube. Temperature control is achieved through a temperature sensor and control module. Combined with a motor-driven cleaning component, the spiral liquid tube is automatically cleaned to ensure uniform heating of the liquid and prevent scaling.
It achieves rapid and complete vaporization of the foaming agent, reduces energy waste and maintenance costs, and ensures stable operation of the equipment under complex working conditions.
Smart Images
Figure CN121576818A_ABST
Abstract
Description
Technical Field
[0001] This invention relates to the field of foaming agent processing technology, specifically to a disc-type heated foaming agent vaporization device. Background Technology
[0002] Traditional reagent addition methods in coal slime flotation have many technical bottlenecks in industrial applications. These mainly manifest in the large droplet size and uneven dispersion, leading to low contact efficiency between reagents and targets. At the same time, competitive adsorption makes reagents easily adsorbed on non-target surfaces, resulting in resource waste. Furthermore, existing technologies lack selective adsorption capabilities and cannot accurately act on specific targets. Excessive use of reagents further exacerbates economic costs and environmental burdens. Although emulsification and atomization technologies have partially alleviated the above problems by reducing droplet size and improving dispersibility, the inherent drawbacks of external adsorption, such as competitive adsorption, non-selective adsorption, and reagent excess, have not been fundamentally resolved.
[0003] Existing technologies such as ultra-high pressure air atomization and electrothermal atomization can improve the atomization effect, but they still cannot completely avoid the non-target adsorption of the agent on the outside of the bubble. They also have problems such as high energy consumption and insufficient control precision, making it difficult to meet the needs of efficient and precise dosing. The prerequisite problem that the foaming agent vaporization dosing solution needs to solve is how to vaporize the foaming agent and make it reach the ideal vaporization form.
[0004] Existing methods use specialized equipment, such as vaporization tanks and heating components, to heat liquid foaming agents to vaporize them before introducing them into the flotation system. However, temperature changes during vaporization can have different effects on different types of foaming agents, requiring real-time monitoring. Directly heating the foaming agent with heating components can easily lead to uneven heating, resulting in poor vaporization and low vaporization efficiency. Summary of the Invention
[0005] This invention provides a disc-type heated foaming agent vaporization device to solve the problems mentioned in the background art, where temperature changes during the vaporization process of existing devices have different effects on different types of foaming agents, requiring real-time control. Directly using heating components to heat the foaming agent can easily lead to uneven heating, resulting in poor vaporization effect and low vaporization efficiency.
[0006] This invention provides a disc-type heated foaming agent vaporization device, including a vaporization box, an inlet pipe fixedly connected to the top side of the vaporization box, an outlet pipe fixedly connected to the bottom side of the vaporization box, a control module fixedly installed on the outer wall of the vaporization box, and a temperature sensor fixedly installed on the inner wall of the vaporization box. The control module and the temperature sensor work together to ensure that the vaporization process is controllable and adapt to the foaming agent vaporization requirements under different working conditions. The vaporization box is provided with disc type heating pipes, a plurality of fixing frames are fixedly connected to the disc type heating pipes, the side walls of the fixing frames are fixedly connected to the inner wall of the vaporization box, a spiral liquid pipe is arranged in the middle of the disc type heating pipe, a plurality of auxiliary rods are fixedly connected between the spiral liquid pipe and the disc type heating pipe, a liquid inlet hopper is fixedly connected to the top of the spiral liquid pipe, the liquid inlet hopper is arranged directly below the liquid inlet pipe, and a gas outlet groove is formed in the top wall of the spiral liquid pipe.
[0007] Preferably, the control module comprises an adjusting knob, a control key and a display screen, which are fixedly installed on the outer wall of the vaporization box, and electric control valves are fixedly installed on the liquid inlet pipe and the gas outlet pipe.
[0008] Preferably, a protective shell is fixedly connected to the top of the vaporization box, a motor is installed on the inner wall of the protective shell, a screw rod is connected to the bottom output end of the motor, the bottom end of the screw rod extends downward through the top wall of the vaporization box, a protective cylinder is fixedly connected to the top inner surface of the vaporization box, and the protective cylinder is sleeved on the outer wall of the screw rod.
[0009] Preferably, a cleaning assembly is arranged on the screw rod, the cleaning assembly comprises a first supporting pipe, a second supporting pipe and a cleaner, one end of each of the first supporting pipe and the second supporting pipe is fixedly connected to the protective cylinder, the other end of each of the first supporting pipe and the second supporting pipe is fixedly connected to the spiral liquid pipe, the first supporting pipe is arranged directly above the second supporting pipe, and the first supporting pipe and the second supporting pipe are oppositely inclined.
[0010] Preferably, the cleaner is arranged in the spiral liquid pipe, a sliding seat is movably connected to the screw rod, a lifting shell is fixedly connected to one side of the sliding seat, and the length, width and height of the interior of the lifting shell are all greater than the diameter of the cleaner.
[0011] Preferably, a sliding block is fixedly connected to the other side of the sliding seat, a sliding groove is formed in the inner wall of the protective cylinder, and the sliding groove is slidably connected with the sliding block.
[0012] Preferably, the cleaner comprises a counterweight ball and a cleaning disc, the side wall of the counterweight ball is fixedly connected with the cleaning disc, the diameter of the cleaning disc is slightly smaller than the inner diameter of the spiral liquid pipe, and a plurality of brushes are fixedly connected to the outer wall of the cleaning disc.
[0013] Preferably, the inner diameters of the first supporting pipe and the second supporting pipe are both greater than the diameter of the cleaner.
[0014] Preferably, a rotating assembly is arranged at the bottom end of the screw rod, the rotating assembly comprises a rotating rod, the top end of the rotating rod is fixedly connected to the bottom of the screw rod, the bottom end of the rotating rod is connected to the bottom inner surface of the vaporization box through a bearing, a plurality of cleaning rods are fixedly connected to the outer wall of the rotating rod, a scraper is fixedly connected to the bottom of each cleaning rod, and the bottom of the scraper abuts against the bottom inner surface of the vaporization box.
[0015] Compared with the prior art, the present application has the following advantages: The present application adopts the technical means of spiral liquid pipe and disc type heating pipe cooperation, improves the vaporization efficiency from two aspects of liquid distribution and heat transfer, the spiral liquid pipe prolongs the flow path of the foaming agent liquid in the vaporization box, and the liquid is uniformly distributed along the inner wall of the spiral pipe, there is no local liquid accumulation, so that each part of the liquid can fully contact the heating environment, the annular layout of the disc type heating pipe maximizes the heating area, compared with the traditional straight heating pipe, it can form a more uniform temperature field in the vaporization box, avoid the problem that local heating is insufficient, the liquid is not vaporized or local overheating waste heat, finally realize the rapid and sufficient vaporization of the foaming agent liquid, reduce the energy loss and material waste, the pipe diameter of the spiral liquid pipe and the power of the disc type heating pipe can be adjusted according to the vaporization demand, such as larger pipe diameter of the liquid pipe and higher power of the heating pipe for large-scale production, which takes into account the small flow precision vaporization and large flow continuous vaporization scene.
[0016] The present application adopts the technical means of cleaning assembly, motor and spiral liquid pipe cooperation, through the automatic design of motor driving, screw transmission and brush cleaning, solves the scaling problem of spiral liquid pipe in long-term use, overcomes the technical defects that the inner wall of spiral liquid pipe is easy to leave foaming agent impurities or scaling for a long time in the existing device, which reduces the heat transfer efficiency and reduces the pipe cavity, which not only guarantees the stability of vaporization efficiency, but also reduces the maintenance cost, so that the device is more practical in continuous operation, complex material processing and other scenes, regular cleaning avoids local overheating, corrosion or blockage caused by scaling of liquid pipe, reduces the replacement frequency of core components, spiral liquid pipe and disc type heating pipe, and reduces the long-term operation and maintenance cost. BRIEF DESCRIPTION OF DRAWINGS
[0017] Figure 1 It is the overall structure schematic diagram of the present application; Figure 2 It is the overall structure schematic diagram of the vaporization box outside of the present application; Figure 3 It is the overall structure schematic diagram of the disc type heating pipe and spiral liquid pipe of the present application; Figure 4 It is the overall structure schematic diagram of the disc type heating pipe of the present application; Figure 5 It is the overall structure schematic diagram of the spiral liquid pipe of the present application; Figure 6 It is the overall structure schematic diagram of the inside of the vaporization box of the present application; Figure 7 It is the overall structure schematic diagram of the present application Figure 6 It is the enlarged structure schematic diagram of structure A in the present application; Figure 8 It is the enlarged structure schematic diagram of structure B in the present application; Figure 6 Figure 9 It is the overall structure schematic diagram of the cleaner of the present application.
[0018] In the diagram: 100, vaporization chamber; 101, liquid inlet pipe; 102, gas outlet pipe; 103, control module; 104, temperature sensor; 200. Disc heating element; 201. Mounting bracket; 300. Spiral liquid pipe; 301. Liquid inlet hopper; 302. Gas outlet trough; 400, Protective housing; 500, Motor; 501, Screw; 600. Protective casing; 601. Slide groove; 700. Cleaning component; 710. First support tube; 720. Second support tube; 730. Cleaner; 731. Counterweight ball; 732. Cleaning disc; 733. Brush; 740. Slide; 750. Lifting housing; 760. Slider; 800, Rotating assembly; 810, Rotating rod; 820, Cleaning rod; 830, Scraper. Detailed Implementation
[0019] The technical solutions of the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some embodiments of the present invention, and not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of the present invention.
[0020] This invention discloses a disc-type heated foaming agent vaporization device, such as... Figures 1-9 As shown, it includes a vaporization box 100, an inlet pipe 101 fixedly connected to the top side of the vaporization box 100, an outlet pipe 102 fixedly connected to the bottom side of the vaporization box 100, a control module 103 fixedly installed on the outer wall of the vaporization box 100, and a temperature sensor 104 fixedly installed on the inner wall of the vaporization box 100. Furthermore, the temperature sensor 104 monitors the temperature inside the chamber in real time and transmits the temperature signal to the control module 103. The control module 103 automatically adjusts the heating power of the disc heating tube 200 according to the preset vaporization temperature threshold, such as the optimal vaporization temperature of the foaming agent. If the temperature is lower than the threshold, the power is increased; if it is higher than the threshold, the power is reduced, so as to achieve constant temperature vaporization and ensure stable vaporization effect.
[0021] It should be noted that the vaporization tank 100 is provided with a disc type heating pipe 200, a plurality of fixing frames 201 are fixedly connected to the disc type heating pipe 200, the side wall of the fixing frame 201 is fixedly connected to the inner wall of the vaporization tank 100, a spiral liquid pipe 300 is arranged in the middle of the disc type heating pipe 200, a plurality of auxiliary rods are fixedly connected between the spiral liquid pipe 300 and the disc type heating pipe 200, a liquid inlet hopper 301 is fixedly connected to the top of the spiral liquid pipe 300, and the liquid inlet hopper 301 is arranged directly below the liquid inlet pipe 101, and a gas outlet groove 302 is formed in the top wall of the spiral liquid pipe 300.
[0022] Further, the gas outlet groove 302 formed in the top wall of the spiral liquid pipe 300 is a key outlet for gaseous products, and the gas bubbles generated by vaporization can directly escape from the liquid pipe through the gas outlet groove 302 and enter the gas phase space inside the vaporization tank 100. Since the spiral liquid pipe 300 is provided with the gas outlet groove 302 along the length direction, it ensures the release of all vaporization products and avoids the flow obstruction caused by the accumulation of gas bubbles in the liquid pipe.
[0023] Further, the design of the gas outlet groove 302 of the spiral liquid pipe 300 allows the gas bubbles to be released immediately, avoiding the accumulation of a large number of gas bubbles in the liquid pipe, which can cause the pressure in the pipe to rise suddenly. At the same time, the gas phase space in the vaporization tank 100 can buffer the pressure fluctuation, reducing the risk of device leakage or damage caused by excessive pressure The present application is around the core process of inputting the foaming agent liquid, accurately heating vaporization, and outputting the gaseous product, and realizes efficient and controllable vaporization by combining the structural design. In the use process, the external foaming agent liquid enters the vaporization box 100 through the liquid inlet pipe 101 at the top of the device. Since the liquid inlet bucket 301 is accurately arranged below the liquid inlet pipe 101, the liquid can directly fall into the liquid inlet bucket 301, avoiding splashing to the inner wall of the vaporization box 100 to cause waste or local residue. The liquid inlet bucket 301 serves as a transition structure to smoothly guide the liquid into the spiral liquid pipe 300 below. The spiral pipe design prolongs the flow path of the liquid in the vaporization box 100, and at the same time realizes the uniform distribution of the liquid, avoiding local liquid accumulation, laying a foundation for subsequent step-by-step vaporization. The disc-type heating pipe 200 is connected with the external power source before work to realize power heating. Compared with the traditional straight heating pipe, the disc-type layout can maximize the contact area of the heating pipe with the internal space of the vaporization box 100, making the temperature field in the box more uniform, avoiding problems such as low vaporization efficiency, foaming agent decomposition caused by local overheating or insufficient temperature, etc. The foaming agent liquid in the spiral liquid pipe 300 gradually increases in temperature to the vaporization temperature under the continuous and uniform heating of the disc-type heating pipe 200, and the liquid is converted into gaseous foaming agent. The gaseous foaming agent generated by vaporization can directly escape from the gas outlet groove 302 into the gas phase space inside the vaporization box 100, ensuring the release of the entire vaporization product and avoiding flow obstruction caused by bubble accumulation in the liquid pipe. The gaseous foaming agent entering the gas phase space of the vaporization box 100 flows towards the gas outlet pipe 102 at the bottom, and is finally transported to the subsequent flotation system through the gas outlet pipe 102, completing the entire liquid-to-gas conversion and transportation process. Through the cooperative design of spiral liquid distribution and disc-type uniform heating, the present application realizes efficient and stable vaporization of the foaming agent. Through the linkage of the control module 103 and the temperature sensor 104, the vaporization process is controllable, and the foaming agent vaporization demand under different working conditions is adapted.
[0024] The present application adopts the technical means of spiral liquid pipe 300 and disc-type heating pipe 200 cooperation to improve the vaporization efficiency from two aspects of liquid distribution and heat transfer. The spiral liquid pipe 300 prolongs the flow path of the foaming agent liquid in the vaporization box 100, and the liquid is uniformly distributed along the inner wall of the spiral pipe without local liquid accumulation, so that each part of the liquid can fully contact the heating environment. The annular layout of the disc-type heating pipe 200 maximizes the heating area. Compared with the traditional straight heating pipe, it can form a more uniform temperature field in the vaporization box 100, avoiding problems such as incomplete vaporization of liquid or local overheating and waste of heat caused by insufficient local heating. Finally, the rapid and sufficient vaporization of the foaming agent liquid is realized, reducing energy consumption and material waste. The pipe diameter of the spiral liquid pipe 300 and the power of the disc-type heating pipe 200 can be adjusted according to the vaporization demand, such as using larger-diameter liquid pipes and higher-power heating pipes for large-scale production, considering both small-flow precise vaporization and large-flow continuous vaporization scenarios.
[0025] AsFigures 5-9 As shown, in one specific embodiment: the control module 103 includes an adjustment knob, control keys and a display screen, all fixedly installed on the outer wall of the vaporization tank 100, and the inlet pipe 101 and the outlet pipe 102 are both fixedly installed with electric control valves.
[0026] Further, the control module 103 supports precise setting of heating temperature, such as low-boiling-point foaming agent can reduce heating power, high-viscosity foaming agent can appropriately increase temperature to accelerate flow and vaporization, and adapt to foaming agents of different components.
[0027] It should be noted that the protective shell 400 is fixedly connected to the top of the vaporization tank 100, the motor 500 is installed on the inner wall of the protective shell 400, the bottom output end of the motor 500 is connected with the screw rod 501, the bottom end of the screw rod 501 extends downward through the top wall of the vaporization tank 100, the protective cylinder 600 is fixedly connected to the inner top surface of the vaporization tank 100, and the protective cylinder 600 is sleeved outside the screw rod 501.
[0028] It should be noted that the screw rod 501 is provided with a cleaning assembly 700, the cleaning assembly 700 includes a first support pipe 710, a second support pipe 720 and a cleaner 730, one end of the first support pipe 710 and the second support pipe 720 are fixedly connected to the protective cylinder 600, the other end of the first support pipe 710 and the second support pipe 720 are fixedly connected to the spiral liquid pipe 300, the first support pipe 710 is arranged directly above the second support pipe 720, and the inclination directions of the first support pipe 710 and the second support pipe 720 are opposite.
[0029] Further, the first support pipe 710 and the second support pipe 720 are opposite in inclination direction, one end is fixed to the protective cylinder 600, and the other end is fixed to the spiral liquid pipe 300, which not only enhances the structural stability of the liquid pipe and offsets the impact force when the cleaner 730 moves, but also because the inner diameter is greater than the diameter of the cleaner 730, it can be used as a channel node for the cleaner 730 to move up and down, ensuring smooth transition of the cleaner 730 at the bend of the spiral pipe and avoiding jamming.
[0030] In addition, the cleaner 730 is placed in the spiral liquid pipe 300, the screw rod 501 is movably connected with a sliding seat 740, one side of the sliding seat 740 is fixedly connected with a lifting shell 750, and the inside length, width and height of the lifting shell 750 are all greater than the diameter of the cleaner 730.
[0031] Specifically, the other side of the sliding seat 740 is fixedly connected with a sliding block 760, and a sliding groove 601 is formed in the inner side wall of the protective cylinder 600, and the sliding groove 601 is slidably connected with the sliding block 760.
[0032] It should be noted that the cleaner 730 includes a counterweight ball 731 and a cleaning disc 732, the sidewall of the counterweight ball 731 is fixedly connected with the cleaning disc 732, the diameter of the cleaning disc 732 is slightly smaller than the inner diameter of the spiral liquid pipe 300, and the outer wall of the cleaning disc 732 is fixedly connected with a brush 733.
[0033] In addition, the inner diameters of the first support pipe 710 and the second support pipe 720 are greater than the diameter of the cleaner 730.
[0034] The above technical scheme further realizes automatic cleaning of the spiral liquid pipe 300 on the basis of the original vaporization function, and the working principle is as follows: in the use process of the present application, the motor 500 in the protective shell 400 provides power for the cleaning action, the screw rod 501 connected to the bottom output end penetrates the top wall of the vaporization box 100 and extends to the inside, and the protective cylinder 600 is externally sleeved, which not only protects the screw rod 501 from being corroded by the gaseous blowing agent, but also provides a guide reference for the movement of the sliding seat 740. When the screw rod 501 rotates, the sliding seat 740 connected therewith is limited by the sliding cooperation of the sliding block 760 and the inner sliding groove 601 of the protective cylinder 600, and converts the rotary motion of the screw rod 501 into the lifting motion in the vertical direction. The lifting shell 750 on one side of the sliding seat 740 synchronously rises and falls with the sliding seat 740. The cleaner 730 may be positioned at a certain position in the spiral liquid pipe 300 by gravity or initial position under normal circumstances. With the inclined arrangement of the spiral liquid pipe 300, the cleaner 730 will roll down. When the lifting shell 750 descends to the bottom, the cleaner 730 rolls to the bottom, and then enters the lifting shell 750 through the second support pipe 720. The motor 500 reverses to drive the screw rod 501 to rotate, the sliding seat 740 moves upward, and the cleaner 730 is reset upward to the position of the first support pipe 710. During the cleaning process, the brush 733 on the outer wall of the cleaning disc 732 closely contacts the inner wall of the liquid pipe, and scrapes off the adhered residual materials, such as impurities and scale, which may be left after the vaporization of the blowing agent, with the movement of the cleaner 730. After long-term use, the inner wall of the spiral liquid pipe 300 is easy to form scale due to impurities in the blowing agent or trace decomposition under high temperature, which reduces the heat conduction efficiency, affects the vaporization speed, narrows the pipe cavity, and hinders the flow of liquid. The cleaner 730 regularly cleans the inner wall through the brush 733, which can keep the surface of the liquid pipe clean and ensure the long-term stability of the heating efficiency and the liquid flowability.
[0035] The cleaning assembly 700, the motor 500 and the spiral liquid pipe 300 are matched, the motor 500 is driven, the screw rod 501 is driven to cooperate with the brush 733 to realize automatic cleaning, the scaling problem of the spiral liquid pipe 300 in long-term use is solved, the technical defects that the inner wall of the spiral liquid pipe 300 is easy to remain foaming agent impurities or scale in long-term use, and the heat conduction efficiency is reduced and the pipe cavity is reduced are overcome, the stability of the vaporization efficiency is ensured, the maintenance cost is reduced, the device is more practical in continuous operation, complex material processing and the like, regular cleaning avoids local overheating, corrosion or blockage of the liquid pipe caused by scaling, the replacement frequency of the core components, the spiral liquid pipe 300 and the disc type heating pipe 200 is reduced, and the long-term operation and maintenance cost is reduced.
[0036] As shown in Figure 5 In one specific embodiment, the screw rod 501 is provided with a rotating assembly 800, the rotating assembly 800 comprises a rotating rod 810, the rotating rod 810 is fixedly connected to the bottom of the screw rod 501, the bottom of the rotating rod 810 is connected to the inner bottom surface of the vaporization box 100 through a bearing, a plurality of cleaning rods 820 are fixedly connected to the outer wall of the rotating rod 810, a scraper 830 is fixedly connected to the bottom of the cleaning rod 820, and the bottom of the scraper 830 abuts against the inner bottom surface of the vaporization box 100.
[0037] The working principle of the above technical scheme is as follows: in the use process of the present application, the rotating rod 810 rotates synchronously with the screw rod 501, drives the cleaning rod 820 on the outer wall and the scraper 830 at the bottom to rotate, the scraper 830 is in close contact with the inner bottom surface of the vaporization box 100, and can scrape off the residual materials that may accumulate on the bottom, such as liquid droplets of unvaporized foaming agent, impurity deposits or scale, avoid the bottom corrosion, heat conduction obstruction, influence on the uniformity of the temperature in the box or blockage of the gas outlet pipe 102 caused by long-term accumulation, compared with manual cleaning of the bottom of the box, synchronous cleaning is realized by driving the screw rod 501, without the need of an additional power source, energy consumption is saved and operation is convenient.
[0038] The contents not described in detail in the description belong to the prior art known to those skilled in the art, although the present application has been described in detail with reference to the foregoing embodiments, those skilled in the art can still modify the technical solutions recorded in the foregoing embodiments, or make equivalent replacement for part of the technical features, any modification, equivalent replacement, improvement and the like made within the spirit and principles of the present application shall be included in the protection scope of the present application.
Claims
1. A disc-type heated foaming agent vaporization device, characterized in that, The device includes a vaporization chamber (100), with an inlet pipe (101) fixedly connected to the top side of the vaporization chamber (100), an outlet pipe (102) fixedly connected to the bottom side of the vaporization chamber (100), a control module (103) fixedly installed on the outer wall of the vaporization chamber (100), and a temperature sensor (104) fixedly installed on the inner wall of the vaporization chamber (100). The control module (103) and the temperature sensor (104) work together to ensure that the vaporization process is controllable and adapts to the vaporization requirements of the foaming agent under different working conditions. The vaporization chamber (100) is equipped with a disc heating tube (200), and multiple fixing brackets (201) are fixedly connected to the disc heating tube (200). The side wall of the fixing bracket (201) is fixedly connected to the inner wall of the vaporization chamber (100). A spiral liquid tube (300) is provided in the middle of the disc heating tube (200). Multiple auxiliary rods are fixedly connected between the spiral liquid tube (300) and the disc heating tube (200). A liquid inlet hopper (301) is fixedly connected to the top of the spiral liquid tube (300), and the liquid inlet hopper (301) is located directly below the liquid inlet tube (101). An air outlet groove (302) is opened on the top wall of the spiral liquid tube (300).
2. The disc-type heated foaming agent vaporization device according to claim 1, characterized in that: The control module (103) includes an adjustment knob, control keys and a display screen, all of which are fixedly installed on the outer wall of the vaporization box (100). Electrically controlled valves are fixedly installed on the liquid inlet pipe (101) and the gas outlet pipe (102).
3. The disc-type heated foaming agent vaporization device according to claim 1, characterized in that: A protective shell (400) is fixedly connected to the top of the vaporization box (100). A motor (500) is installed on the inner wall of the protective shell (400). A screw (501) is connected to the bottom output end of the motor (500). The bottom end of the screw (501) extends downward through the top wall of the vaporization box (100). A protective cylinder (600) is fixedly connected to the top surface of the vaporization box (100). The protective cylinder (600) is sleeved on the outside of the screw (501).
4. The disc-type heated foaming agent vaporization device according to claim 3, characterized in that: A cleaning assembly (700) is provided on the screw (501). The cleaning assembly (700) includes a first support tube (710), a second support tube (720), and a cleaner (730). One end of the first support tube (710) and the second support tube (720) are fixedly connected to the protective cylinder (600). The other end of the first support tube (710) and the second support tube (720) are fixedly connected to the spiral liquid tube (300). The first support tube (710) is located directly above the second support tube (720), and the first support tube (710) and the second support tube (720) are inclined in opposite directions.
5. The disc-type heated foaming agent vaporization device according to claim 4, characterized in that: The cleaner (730) is placed inside the spiral liquid tube (300). A slide (740) is movably connected to the screw (501). A lifting shell (750) is fixedly connected to one side of the slide (740). The length, width and height of the lifting shell (750) are all greater than the diameter of the cleaner (730).
6. The disc-type heated foaming agent vaporization device according to claim 5, characterized in that: A slider (760) is fixedly connected to the other side of the slide block (740), and a groove (601) is provided on the inner wall of the protective cylinder (600). The groove (601) is slidably connected to the slider (760).
7. The disc-type heated foaming agent vaporization device according to claim 5, characterized in that: The cleaner (730) includes a counterweight ball (731) and a cleaning disc (732). The cleaning disc (732) is fixedly connected to the side wall of the counterweight ball (731). The diameter of the cleaning disc (732) is slightly smaller than the inner diameter of the spiral liquid tube (300). A brush (733) is fixedly connected around the outer wall of the cleaning disc (732).
8. The disc-type heated foaming agent vaporization device according to claim 4, characterized in that: The inner diameters of the first support tube (710) and the second support tube (720) are both larger than the diameter of the cleaner (730).
9. A disc-type heated foaming agent vaporization device according to claim 3, characterized in that: The bottom end of the screw (501) is provided with a rotating assembly (800), the rotating assembly (800) includes a rotating rod (810), the top end of the rotating rod (810) is fixedly connected to the bottom of the screw (501), the bottom end of the rotating rod (810) is connected to the inner bottom surface of the vaporization box (100) through a bearing, a plurality of cleaning rods (820) are fixedly connected to the outer wall of the rotating rod (810), a scraper (830) is fixedly connected to the bottom of the cleaning rod (820), and the bottom of the scraper (830) abuts against the inner bottom surface of the vaporization box (100).