Liquid storage device for oxidized wax

Abstract

The utility model relates to a liquid storage device for oxidized wax. The liquid storage device comprises a buffer tank, a gas inlet pipeline and a heat exchange tube nest. Wherein the buffer tank is configured to store liquid oxidized wax; one end of the air inlet pipeline is located in the buffer tank, the other end of the air inlet pipeline is located outside the buffer tank, and the air inlet pipeline is configured to introduce air into the buffer tank; and heat exchange tube nests are arranged on the peripheral side of the buffer tank, and the heat exchange tube nests are configured to be used for controlling the temperature of the buffer tank. According to the liquid storage device of the oxidized wax, air is introduced into the buffer tank through the air inlet pipeline, the reversible reaction of the oxidized wax is inhibited, the temperature in the buffer tank is controlled through the heat exchange tube nest, the excessive reaction of the oxidized wax is prevented, a stable storage environment is provided for the oxidized wax, and the storage efficiency of the oxidized wax is improved. The stability of the oxidized wax in the storage process is ensured.

Description

Technical Field

[0001] The present disclosure relates to the field of chemical technology, and more specifically, to a liquid storage device for oxidized wax. Background Art

[0002] Oxidized wax, as a wax material that has undergone special oxidation treatment, is widely used in many fields, such as cosmetics, packaging materials, printing inks, etc. The color of oxidized wax directly affects the appearance quality of the final product. Clear or specific color oxidized wax can ensure that the product has a good visual effect, while inappropriate color tone may be regarded as a defect and affect the market acceptance of the product.

[0003] However, in the prior art, oxidized wax is prone to reversible reactions during storage, resulting in color changes and quality degradation. Utility Model Content

[0004] In view of this, an embodiment of the present disclosure provides a liquid storage device for oxidized wax to solve the technical defects existing in the prior art.

[0005] To achieve the above objectives, the present disclosure adopts the following technical solutions:

[0006] The present disclosure provides a liquid storage device for oxidized wax, the liquid storage device for oxidized wax comprising:

[0007] a buffer tank configured to store liquid oxidized wax;

[0008] an air intake pipe, one end of which is located inside the cache tank and the other end of which is located outside the cache tank, and the air intake pipe is configured to introduce air into the cache tank;

[0009] Heat exchange tubes are arranged on the peripheral side of the cache tank, and the heat exchange tubes are configured to control the temperature of the cache tank.

[0010] In one embodiment of the present disclosure, a heat exchange inlet and a heat exchange outlet are provided on the periphery of the cache tank, and the heat exchange inlet and the heat exchange outlet are connected with the heat exchange tubes, and the heat exchange medium enters the heat exchange tubes through the heat exchange inlet and is output from the heat exchange outlet.

[0011] In one embodiment of the present disclosure, a gas distributor is connected to the air inlet pipeline, a gas distribution pipe is arranged on the gas distributor, and the gas distribution pipe is arranged as an annular structure with the gas distributor as the center and the inner diameter gradually increases.

[0012] In one embodiment of the present disclosure, filter elements are correspondingly arranged on the gas distribution pipes, the filter element on the gas distribution pipe with the largest inner diameter is perpendicular to the plane of the bottom of the cache tank, and the remaining filter elements are parallel to the plane of the bottom of the cache tank.

[0013] In one embodiment of the present disclosure, a stirring shaft is provided inside the cache tank, the stirring shaft extends from the top of the cache tank to the bottom of the cache tank, and an agitator is provided on the stirring shaft.

[0014] In one embodiment of the present disclosure, a manhole is provided on the top of the cache tank, and the manhole is configured to be used for observing the conditions inside the cache tank.

[0015] In one embodiment of the present disclosure, an on-site liquid level meter and a remote liquid level meter are provided in the cache tank, and the on-site liquid level meter and the remote liquid level meter are symmetrically distributed along the central axis of the cache tank, and the on-site liquid level meter and the remote liquid level meter are both configured to monitor the liquid level in the cache tank.

[0016] In one embodiment of the present disclosure, an on-site thermometer and a remote thermometer are provided at the lower portion of the cache tank, and the on-site thermometer and the remote thermometer are symmetrically distributed along the central axis of the cache tank, and both the on-site thermometer and the remote thermometer are configured to monitor the temperature inside the cache tank.

[0017] In one embodiment of the present disclosure, an on-site pressure gauge and a remote pressure gauge are provided on the top of the cache tank, and the on-site pressure gauge and the remote pressure gauge are symmetrically distributed along the central axis of the cache tank, and the on-site pressure gauge and the remote pressure gauge are both configured to monitor the pressure inside the cache tank.

[0018] In one embodiment of the present disclosure, a steam pipe and a condensation pipe are provided on both sides of the air intake pipe, the steam pipe is located higher than the condensation pipe, and both the steam pipe and the condensation pipe are connected to the air intake pipe.

[0019] The liquid storage device for oxidized wax provided in the present invention provides an air intake pipe to introduce air into a buffer tank to inhibit the reversible reaction of the oxidized wax, and controls the temperature in the buffer tank by providing heat exchange tubes to prevent the oxidized wax from overreacting, thereby providing a stable storage environment for the oxidized wax and ensuring the stability of the oxidized wax during storage.

[0020] Other features and advantages of the present disclosure will become apparent from the following detailed description of exemplary embodiments of the present disclosure with reference to the accompanying drawings. BRIEF DESCRIPTION OF THE DRAWINGS

[0021] Figure 1It is a schematic structural diagram of a liquid storage device for oxidized wax provided in one embodiment of the present disclosure;

[0022] Figure 2 is a schematic structural diagram of a liquid storage device for oxidized wax provided in another embodiment of the present disclosure;

[0023] Figure 3 is a top view of a liquid storage device for oxidized wax provided by another embodiment of the present disclosure;

[0024] Figure 4 is a partial schematic diagram of an air intake duct of a liquid storage device for oxidized wax provided in another embodiment of the present disclosure;

[0025] Figure 5 It is a schematic diagram of a gas distributor of a liquid storage device for oxidized wax provided in another embodiment of the present disclosure.

[0026] 1-buffer tank; 2-air inlet pipe; 3-heat exchange tubes; 31-heat exchange inlet; 32-heat exchange outlet; 4-gas distributor; 5-agitation shaft; 51-agitation machine; 6-manhole; 7-local level gauge; 8-remote level gauge; 9-local thermometer; 10-remote thermometer; 11-local pressure gauge; 12-remote pressure gauge; 13-steam pipe; 14-condensation pipe; 15-filter element. DETAILED DESCRIPTION

[0027] Various exemplary embodiments of the present disclosure will now be described in detail with reference to the accompanying drawings. It should be noted that the relative arrangement of components and steps, numerical expressions and numerical values ​​set forth in these embodiments do not limit the scope of the present disclosure unless otherwise specifically stated.

[0028] The following description of at least one exemplary embodiment is merely illustrative in nature and is in no way intended to limit the present disclosure, its application, or uses.

[0029] Technologies, methods, and equipment known to ordinary technicians in the relevant art may not be discussed in detail, but where appropriate, the technologies, methods, and equipment should be considered as part of the specification.

[0030] It should be noted that like reference numerals and letters refer to similar items in the following figures, and therefore, once an item is defined in one figure, it need not be further discussed in subsequent figures.

[0031] The specific embodiments of the present disclosure are described below in conjunction with the accompanying drawings.

[0032] In this document, “upper”, “lower”, “front”, “back”, “left”, “right”, etc. are only used to indicate the relative position relationship between related parts, rather than to limit the absolute positions of these related parts.

[0033] In this article, "first", "second", etc. are only used to distinguish each other, and do not indicate the importance and order, or the premise of each other's existence.

[0034] In this document, “equal”, “same”, etc. are not strictly limited in a mathematical and / or geometric sense, but also include errors that can be understood by those skilled in the art and are allowed in manufacturing or use.

[0035] The present disclosure provides a liquid storage device for oxidized wax, comprising a buffer tank, an air intake pipe and a heat exchange tube. The buffer tank is configured to store liquid oxidized wax; one end of the air intake pipe is located inside the buffer tank, and the other end is located outside the buffer tank, and the air intake pipe is configured to pass air into the buffer tank; the heat exchange tube is arranged on the peripheral side of the buffer tank, and the heat exchange tube is configured to control the temperature of the buffer tank.

[0036] The liquid storage device for oxidized wax provided in the present invention provides an air intake pipe to introduce air into a buffer tank to inhibit the reversible reaction of the oxidized wax, and controls the temperature in the buffer tank by providing heat exchange tubes to prevent the oxidized wax from overreacting, thereby providing a stable storage environment for the oxidized wax and ensuring the stability of the oxidized wax during storage.

[0037] For ease of understanding, refer to Figures 1 to 5 , the specific structure and working principle of the liquid storage device for oxidized wax disclosed in the present invention are explained in detail in combination with an embodiment.

[0038] like Figure 1 As shown, the present disclosure provides a liquid storage device for oxidized wax, comprising a buffer tank 1, an air intake pipe 2, and a heat exchange tube 3. The buffer tank 1 is configured to store liquid oxidized wax, one end of the air intake pipe 2 is located inside the buffer tank 1, and the other end is located outside the buffer tank 1, the air intake pipe 2 is configured to pass air into the buffer tank 1, and the heat exchange tube 3 is provided on the peripheral side of the buffer tank 1, and the heat exchange tube 3 is configured to control the temperature of the buffer tank 1.

[0039] Specifically, the buffer tank 1 is used to store a large amount of liquid oxidized wax. Due to the special properties of the oxidized wax itself, a reversible reaction is prone to occur during the storage process, causing the color to turn yellow, affecting the final performance of the product. Therefore, an air intake pipe 2 is also provided. One end of the air intake pipe 2 is connected to the external air source, and the other end is passed into the buffer tank 1 to provide air to the buffer tank 1, inhibiting the occurrence of reversible reactions, so that the color of the oxidized wax is not easy to change during the storage process. In addition, in order to prevent the introduction of air from causing the oxidized wax to over-react and the acid value to be too high, the reaction temperature needs to be controlled. Therefore, a heat exchange tube 3 is also provided on the peripheral side of the buffer tank 1. The heat exchange tube 3 can control the temperature of the buffer tank 1 at 110°C, which can not only inhibit the reversible reaction, but also prevent the oxidized wax from over-reacting with the air, and the acid value is too high, affecting the index.

[0040] like Figures 2 to 3 As shown, in one embodiment of the present disclosure, a heat exchange inlet 31 and a heat exchange outlet 32 ​​are provided on the side of the cache tank 1, and the heat exchange inlet 31 and the heat exchange outlet 32 ​​are connected to the heat exchange tube 3, and the heat exchange medium enters the heat exchange tube 3 through the heat exchange inlet 31 and is output from the heat exchange outlet 32.

[0041] Specifically, by respectively arranging a heat exchange inlet 31 and a heat exchange outlet 32 ​​on the side of the buffer tank 1, the system can realize directional flow of the heat exchange medium. In this embodiment, the heat exchange medium is selected to be heat transfer oil. Heat transfer oil can obtain a higher operating temperature under almost normal pressure conditions, and can greatly reduce the operating pressure in a high-temperature heating system, thereby improving the safety of the system and equipment. In addition, heat transfer oil has good thermal conductivity, can quickly and evenly transfer heat, improve heating efficiency, reduce energy loss, and thus achieve energy saving.

[0042] In this embodiment, the number of heat exchange inlets 31 and heat exchange outlets 32 can be set on the periphery of the buffer tank 1 according to actual needs. The heat exchange inlet 31 enables the heat exchange medium to be introduced into the heat exchange tube 3, while the heat exchange outlet 32 ​​is used to discharge the medium that has completed heat exchange with the oxidized wax in the tank. This design ensures the continuity and efficiency of the heat exchange process. The heat exchange inlet 31 and the outlet are directly connected to the heat exchange tube 3, so that the heat exchange medium circulates in a closed loop, which neither directly contacts the stored liquid oxidized wax nor effectively regulates the temperature in the tank. This indirect heat exchange method is conducive to maintaining the purity of the oxidized wax and avoiding contamination problems that may be caused by direct contact. After the heat exchange medium enters the heat exchange tube 3 from the inlet, it flows in the tube, and heat is exchanged with the oxidized wax in the tank through the tube wall. According to the required operating temperature, the heat exchange medium absorbs or releases heat, and then flows out through the heat exchange outlet 32 ​​to complete a cycle. The external heat exchange medium circulation pump and temperature control system will adjust the medium flow and temperature according to the set parameters to maintain the storage conditions required for the oxidized wax in the tank.

[0043] like Figures 2 to 3 As shown, in one embodiment of the present disclosure, a gas distributor 4 is connected to the air inlet pipe 2, a gas distribution pipe is arranged on the gas distributor 4, and the gas distribution pipe is arranged as an annular structure with the gas distributor 4 as the center and the inner diameter gradually increases.

[0044] Specifically, the gas distribution pipe provided on the gas distributor 4 adopts an annular structure with a gradually increasing inner diameter centered on the gas distributor 4, and the gradually increasing annular structure can help the gas to be more evenly dispersed throughout the tank. As the gas diffuses outward from the center of the gas distributor 4, the gradually increasing inner diameter can promote the adjustment of the gas flow rate, ensure that the gas flow rate in each area tends to be consistent, and avoid the problem of local bubbles being too large or too small, which is crucial for reactions or storage processes that require uniform gas contact. The design of the gradual change in the inner diameter helps to better mix the gas and the oxidized wax. The larger surface area promotes the dissolution and dispersion of the gas, especially in an environment where there is a chemical reaction or a specific gas saturation needs to be maintained, which can improve the reaction efficiency or storage stability. In addition, the gradually increasing annular structure can also smooth the flow path of the gas, reduce the possibility of turbulence, protect the quality of the oxidized wax, and help control the reaction process to avoid overreaction or underreaction.

[0045] like Figure 5 As shown, in one embodiment of the present disclosure, filter elements 15 are correspondingly arranged on the gas distribution pipes, the filter element 15 on the gas distribution pipe with the largest inner diameter is perpendicular to the plane of the bottom of the cache tank 1, and the remaining filter elements 15 are parallel to the plane of the bottom of the cache tank 1.

[0046] Specifically, a filter element 15 is provided on the gas distribution pipe, and different installation angles are set according to the position of the gas distribution pipe. The main function of the filter element 15 is to filter out impurities, moisture or particles in the gas, and prevent these impurities from entering the cache tank 1 along with the gas, contaminating the oxidized wax or affecting the purity inside the storage tank, thereby maintaining the quality of the oxidized wax and preventing adverse reactions caused by foreign matter. The filter element 15 on the gas distribution pipe with the largest inner diameter is installed vertically, which can help the filtered gas to diffuse downward more smoothly, while reducing the resistance of the gas when passing through the filter element 15, ensuring the gas flow efficiency in the maximum flow area, and thus achieving a more uniform gas distribution effect. The remaining filter elements 15 are parallel to the bottom plane of the cache tank 1, which helps the gas to form a more uniform lateral distribution pattern in the cache tank 1, which can promote full contact between the gas and the liquid, and improve the gas utilization efficiency or reaction uniformity.

[0047] like Figures 2 to 3 As shown, in one embodiment of the present disclosure, a stirring shaft 5 is provided inside the cache tank 1 , the stirring shaft 5 extends from the top of the cache tank 1 to the bottom of the cache tank 1 , and an agitator 51 is provided on the stirring shaft 5 .

[0048] Specifically, a stirring shaft 5 and an agitator 51 are arranged inside the buffer tank 1. The agitator 51 can stir the liquid oxidized wax in the buffer tank 1 evenly through rotational motion, avoid stratification or precipitation, ensure the consistent distribution of the components of the oxidized wax, maintain product quality, and prevent local overheating or uneven composition. In the process where chemical reactions or physical changes are required, stirring can significantly increase the contact opportunities between reactants, speed up the reaction rate, and improve reaction efficiency and output. In addition, in an environment where temperature control is required, stirring can accelerate the uniform distribution of temperature in the tank and ensure heat exchange efficiency. Oxidized wax liquid that has been left standing for a long time tends to form lumps or deposit at the bottom of the tank. Stirring can effectively break up these aggregates, maintain the fluidity of the material in the tank, and facilitate subsequent processing and transfer.

[0049] like Figures 2 to 3 As shown, in one embodiment of the present disclosure, a manhole 6 is provided on the top of the cache tank 1 , and the manhole 6 is configured to be used for observing the conditions inside the cache tank 1 .

[0050] Specifically, a manhole 6 is provided on the top of the buffer tank 1, and the operator can observe the state of the oxidized wax in the tank, such as the liquid level, color, whether there is precipitation or foreign matter, etc. through the manhole 6, so as to effectively monitor the material quality. In addition, the manhole 6 can also be a passage for personnel to enter and exit the buffer tank 1 for internal cleaning, maintenance or emergency treatment. When installing or replacing equipment in the tank, the manhole 6 provides a necessary access point to facilitate the installation, adjustment or troubleshooting of the equipment.

[0051] like Figures 2 to 3 As shown, in one embodiment of the present disclosure, a local liquid level meter 7 and a remote liquid level meter 8 are provided in the cache tank 1. The local liquid level meter 7 and the remote liquid level meter 8 are symmetrically distributed along the central axis of the cache tank 1. The local liquid level meter 7 and the remote liquid level meter 8 are both configured to monitor the liquid level in the cache tank.

[0052] Specifically, an on-site liquid level meter 7 and a remote liquid level meter 8 are arranged in the buffer tank 1 and symmetrically distributed along the central axis of the tank, which can provide reliable and accurate liquid level monitoring to ensure operational safety and production efficiency. The on-site liquid level meter 7 is convenient for on-site operators to read the liquid level data intuitively and immediately understand the material situation in the tank. The remote liquid level meter 8 sends the liquid level information to the control room or monitoring system through electrical signals or other remote transmission methods to achieve real-time remote monitoring. The combination of the two can not only improve the accuracy of liquid level measurement, but also calibrate each other to enhance the reliability of liquid level meter monitoring data. In addition, if one of the liquid level meters fails, the other can continue to work to provide the necessary liquid level data for the operation, reducing the risk of production interruption caused by failure of the monitoring equipment. The two symmetrically distributed liquid level meters are convenient for mutual calibration. By comparing the measurement results of the two, deviations can be discovered and corrected in time to ensure the accuracy of liquid level monitoring. Through the liquid level monitoring system, not only can the material inventory in the buffer tank 1 be effectively managed to avoid accidents such as overflow or emptying, but it can also improve the automation level and response speed of the entire production process to ensure the continuity and safety of the production process.

[0053] like Figures 2 to 3 As shown, in one embodiment of the present disclosure, an on-site thermometer 9 and a remote thermometer 10 are provided at the lower portion of the cache tank 1. The on-site thermometer 9 and the remote thermometer 10 are symmetrically distributed along the central axis of the cache tank 1. The on-site thermometer 9 and the remote thermometer 10 are both configured to monitor the temperature inside the cache tank.

[0054] Specifically, an on-site thermometer 9 and a remote thermometer 10 are arranged at the lower part of the buffer tank 1 and are symmetrically distributed along the central axis, so that the temperature in the tank can be monitored and controlled. The on-site thermometer 9 is convenient for on-site personnel to directly view and grasp the actual temperature in the tank in real time. The remote thermometer 10 transmits the temperature signal remotely to the control room or monitoring system to realize remote monitoring and automatic control. The dual monitoring mechanism improves the accuracy and reliability of temperature monitoring. The symmetrically distributed design helps to cover the temperature gradient that may exist in the tank, especially when the tank body is large and the temperature difference is sensitive, to ensure that any local abnormal temperature rise can be discovered in time to avoid local overheating or overcooling. If a thermometer fails, the other thermometer can still work normally, ensuring uninterrupted temperature monitoring, reducing the risk of production interruption, and enhancing the stability and safety of the system. Through the two sets of symmetrically distributed thermometers, the operator can cross-verify, confirm the accuracy of the measurement by comparing the readings of the two, and promptly discover and adjust possible deviations to improve the accuracy of temperature control. Combined with the data from the local and remote thermometers 10, the control system can more flexibly adjust the working state of the heat exchange system, such as adjusting the flow rate and temperature of the heat exchange medium, so as to quickly respond to changes in the temperature in the tank and maintain the required temperature conditions. Not only can it effectively monitor and control the temperature in the buffer tank 1 to avoid product quality degradation or safety problems caused by improper temperature control, but it can also improve the automation level and efficiency of the entire storage system, ensuring the stability and efficiency of the entire system.

[0055] like Figures 2 to 3 As shown, in one embodiment of the present disclosure, a local pressure gauge 11 and a remote pressure gauge 12 are provided on the top of the cache tank 1. The local pressure gauge 11 and the remote pressure gauge 12 are symmetrically distributed along the central axis of the cache tank 1. The local pressure gauge 11 and the remote pressure gauge 12 are both configured to monitor the pressure inside the cache tank.

[0056] Specifically, an on-site pressure gauge 11 and a remote pressure gauge 12 are arranged on the top of the cache tank 1 and are symmetrically distributed along the central axis. The on-site pressure gauge 11 provides instant pressure readings on site, so that the operator can directly observe the pressure status in the tank. The remote pressure gauge 12 transmits the pressure information to the control room or remote monitoring system through electronic signals or networks to realize remote monitoring and automatic alarm functions. The dual monitoring mechanism enhances the system safety and response speed. The pressure parameter is directly related to the stability and safety of the cache tank 1. The symmetrically distributed on-site pressure gauge 11 and the remote pressure gauge 12 can more accurately reflect the pressure situation of the cache tank 1, whether it is static pressure or dynamic changes, which helps to adjust the operation in time and maintain the pressure within a safe range. Any single measuring device may have the risk of false alarm or failure. By setting up two sets of pressure gauges, even if one of them fails, the other can still continue to work, providing reliable pressure data for the operator and reducing the occurrence of misoperation and safety accidents. Convenient for calibration and maintenance: The two sets of pressure gauges arranged symmetrically are convenient for mutual verification to ensure the accuracy of the measurement data. At the same time, this layout also facilitates daily maintenance and calibration work and improves maintenance efficiency. By installing the local pressure gauge 11 and the remote pressure gauge 12, the pressure management of the buffer tank 1 is made more accurate and safer, and can effectively prevent accidents such as tank damage and material leakage caused by overpressure or vacuum, thereby ensuring the safety of the entire system.

[0057] like Figure 2 and Figure 4 As shown, in one embodiment of the present disclosure, a steam pipe 13 and a condensing pipe 14 are provided on both sides of the air intake pipe 2 , the steam pipe 13 is located higher than the condensing pipe 14 , and both the steam pipe 13 and the condensing pipe 14 are connected to the air intake pipe 2 .

[0058] Specifically, a steam pipe 13 and a condensation pipe 14 are arranged on both sides of the air intake pipe 2, and the steam pipe 13 is located higher than the condensation pipe 14. The steam pipe 13 is used to add steam to the air intake pipe 2, which can increase the temperature and humidity of the incoming air. It can effectively adjust the internal environment of the buffer tank 1 to prevent the oxidized wax from solidifying due to low temperature or changing in quality due to high temperature. The addition of steam can accurately control the temperature of the gas in the buffer tank 1 and maintain suitable storage conditions. The condensation pipe 14 is located below the steam pipe 13 and is used to remove excess moisture, reduce the relative humidity of the intake air through condensation, and control the dryness of the intake air to avoid the formation of condensed water in the tank, which may cause quality problems of the oxidized wax. The layout of the steam pipe 13 being higher than the condensation pipe 14 utilizes the natural law that hot air rises and cold air sinks, which helps to promote a more uniform distribution of temperature and humidity in the airflow, improve the control efficiency, reduce energy consumption, and improve the efficiency of the entire system.

[0059] The liquid storage device for oxidized wax provided in the present invention provides an air intake pipe to introduce air into a buffer tank to inhibit the reversible reaction of the oxidized wax, and controls the temperature in the buffer tank by providing heat exchange tubes to prevent the oxidized wax from overreacting, thereby providing a stable storage environment for the oxidized wax and ensuring the stability of the oxidized wax during storage.

[0060] It should be noted that, for the above-mentioned method embodiments, for the sake of simplicity of description, they are all expressed as a series of action combinations, but those skilled in the art should know that the present disclosure is not limited by the described action sequence, because according to the present disclosure, certain steps can be performed in other sequences or simultaneously. Secondly, those skilled in the art should also know that the embodiments described in the specification are all preferred embodiments, and the actions and modules involved are not necessarily required by the present disclosure.

[0061] In the above embodiments, the description of each embodiment has its own emphasis. For parts that are not described in detail in a certain embodiment, reference can be made to the relevant descriptions of other embodiments.

[0062] The preferred embodiments of the present disclosure disclosed above are only used to help explain the present disclosure. The optional embodiments do not describe all the details in detail, nor do they limit the invention to only the specific implementation methods described. Obviously, many modifications and changes can be made according to the content of the present disclosure. The present disclosure selects and specifically describes these embodiments in order to better explain the principles and practical applications of the present disclosure, so that those skilled in the art can well understand and use the present disclosure. The present disclosure is limited only by the claims and their full scope and equivalents.

Claims

1. A liquid storage device for oxidized wax, characterized in that: include: A cache tank (1), wherein the cache tank (1) is configured to store liquid oxidized wax; an air intake pipe (2), one end of the air intake pipe (2) being located inside the cache tank (1) and the other end of the air intake pipe (2) being located outside the cache tank (1), the air intake pipe (2) being configured to introduce air into the cache tank (1); Heat exchange tubes (3) are arranged on the peripheral side of the cache tank (1), and the heat exchange tubes (3) are configured to control the temperature of the cache tank (1).

2. The liquid storage device for oxidized wax according to claim 1, characterized in that: The cache tank (1) is provided with a heat exchange inlet (31) and a heat exchange outlet (32) on its circumference; the heat exchange inlet (31) and the heat exchange outlet (32) are connected to the heat exchange tubes (3); the heat exchange medium enters the heat exchange tubes (3) through the heat exchange inlet (31) and is output from the heat exchange outlet (32).

3. The liquid storage device for oxidized wax according to claim 1, characterized in that: The air inlet pipeline (2) is connected to a gas distributor (4), and a gas distribution pipe is arranged on the gas distributor (4). The gas distribution pipe is arranged as an annular structure with a gradually increasing inner diameter centered on the gas distributor (4).

4. The liquid storage device for oxidized wax according to claim 3, characterized in that: A filter element (15) is correspondingly arranged on the gas distribution pipe, the filter element (15) on the gas distribution pipe with the largest inner diameter is perpendicular to the plane of the bottom of the cache tank (1), and the remaining filter elements (15) are parallel to the plane of the bottom of the cache tank (1).

5. The liquid storage device for oxidized wax according to claim 1, characterized in that: A stirring shaft (5) is arranged inside the cache tank (1), and the stirring shaft (5) extends from the top of the cache tank (1) to the bottom of the cache tank (1), and an agitator (51) is arranged on the stirring shaft (5).

6. The liquid storage device for oxidized wax according to claim 1, characterized in that: A manhole (6) is provided on the top of the cache tank (1), and the manhole (6) is configured to be used for observing the conditions inside the cache tank (1).

7. The liquid storage device for oxidized wax according to claim 1, characterized in that: The cache tank (1) is provided with an on-site liquid level meter (7) and a remote liquid level meter (8), the on-site liquid level meter (7) and the remote liquid level meter (8) are symmetrically distributed along the central axis of the cache tank (1), and the on-site liquid level meter (7) and the remote liquid level meter (8) are both configured to monitor the liquid level in the cache tank.

8. The liquid storage device for oxidized wax according to claim 1, characterized in that: An on-site thermometer (9) and a remote thermometer (10) are provided at the lower part of the cache tank (1); the on-site thermometer (9) and the remote thermometer (10) are symmetrically distributed along the central axis of the cache tank (1); and the on-site thermometer (9) and the remote thermometer (10) are both configured to monitor the temperature inside the cache tank.

9. The liquid storage device for oxidized wax according to claim 1, characterized in that: The top of the cache tank (1) is provided with an on-site pressure gauge (11) and a remote pressure gauge (12), and the on-site pressure gauge (11) and the remote pressure gauge (12) are symmetrically distributed along the central axis of the cache tank (1), and the on-site pressure gauge (11) and the remote pressure gauge (12) are both configured to monitor the pressure in the cache tank.

10. The liquid storage device for oxidized wax according to claim 1, characterized in that: A steam pipe (13) and a condensing pipe (14) are provided on both sides of the air intake pipe (2); the steam pipe (13) is located higher than the condensing pipe (14); and both the steam pipe (13) and the condensing pipe (14) are connected to the air intake pipe (2).

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