Biological aviation kerosene recovery and separation device

Abstract

The invention relates to the technical field of distillation recovery, and discloses a biological aviation kerosene recovery and separation device, which comprises a support assembly, the support assembly comprises a transverse plate, a vertical plate and a bottom plate, the vertical plate is fixed at the bottom of the transverse plate, and the bottom plate is fixed at the bottom of the vertical plate; the heating assembly is fixed to the supporting assembly and comprises a box body, a heat insulation plate, a fixing plate, a heating box and a heating plate. According to the scheme, waste heat generated in the distillation process can be recycled, the condensation assembly and the heat exchange assembly serve as key parts of the energy recycling system, and heat can be transferred from high-temperature gas to a low-temperature biological aviation kerosene raw material or other links needing to be heated; the recycling of the heat can remarkably reduce the input of external energy, so that the energy utilization efficiency of the whole device is improved, the production cost is reduced, the reduction of thermal pollution to the environment is facilitated, and the biological aviation kerosene industry is promoted to develop towards a greener and sustainable direction.

Description

Technical Field

[0001] The invention relates to the technical field of distillation recovery, in particular to a bio-aviation kerosene recovery and separation device. Background Art

[0002] With the rapid development of the global aviation industry, the demand for aviation kerosene continues to increase. At the same time, due to considerations of environmental sustainability and efficient use of resources, bio-jet kerosene has received widespread attention as a more environmentally friendly alternative energy source. The production of bio-jet kerosene involves multiple complex processes, among which the recovery and separation links are crucial. The quality and efficiency of the recovery and separation links directly affect the final performance and production cost of bio-jet kerosene.

[0003] There are many technical challenges in the recovery and separation process of bio-jet fuel, among which the energy consumption problem is particularly prominent. Take distillation operation as an example. It is one of the commonly used methods in the recovery and separation process of bio-jet fuel. Distillation is based on the difference in boiling points of different substances. The mixture is vaporized by heating and then separated into different components by condensation. However, this heating and vaporization process requires a lot of energy, which not only increases production costs, but also puts great pressure on energy supply.

[0004] From the perspective of the entire energy utilization, traditional bio-jet fuel recovery and separation devices are often not fully considered in their design for energy recovery and utilization. The waste heat generated during the distillation process is usually directly discharged into the environment, resulting in a huge waste of energy. This is neither in line with the development trend of energy conservation and emission reduction in modern industry nor conducive to improving the economic benefits of bio-jet fuel production. Therefore, how to effectively reduce energy consumption and improve energy utilization efficiency has become an urgent problem to be solved in the field of bio-jet fuel recovery and separation technology. Summary of the invention

[0005] The purpose of this section is to summarize some aspects of embodiments of the present invention and briefly introduce some preferred embodiments. Some simplifications or omissions may be made in this section and the specification abstract and the invention title of this application to avoid blurring the purpose of this section, the specification abstract and the invention title, and such simplifications or omissions cannot be used to limit the scope of the present invention.

[0006] In view of the above problems and / or the problems existing in the existing bio-jet kerosene recovery and separation devices, the present invention is proposed.

[0007] Therefore, the problem to be solved by the present invention is that the waste heat generated during the distillation process is usually directly discharged into the environment, resulting in a huge waste of energy.

[0008] In order to solve the above technical problems, the present invention provides the following technical solutions: a bio-jet kerosene recovery and separation device, comprising a support assembly, including a horizontal plate, a vertical plate and a bottom plate, the vertical plate is fixed to the bottom of the horizontal plate, and the bottom plate is fixed to the bottom of the vertical plate; A heating assembly is fixed on the supporting assembly, comprising a box body, a heat insulating plate, a fixing plate, a heating box and a heating plate, wherein the heat insulating plate is fixed to the inner wall of the box body, the fixing plate is fixedly connected to the bottom of the inner cavity of the box body, the fixing plate is fixedly connected to the bottom of the heating box at one side away from the inner wall of the box body, and the heating plate is arranged through the bottom of the heating box; A condensation assembly is arranged on one side of the heating assembly, and includes a condensation box, a condensation pipe, a first delivery pump and a guide plate, wherein the condensation pipe is fixed to the inner cavity of the condensation box, the first delivery pump is fixed to the bottom of the condensation box, the first delivery pump is connected to the condensation pipe, and the guide plate is fixed to the inner wall of the condensation box; A recovery component is arranged below the condensation component, comprising a recovery box and a connection plate, wherein the connection plate is fixed to the top of the recovery box, and the top of the connection plate is fixedly connected to the condensation component; A heat exchange component is fixed to one side of the condensing component, comprising a heat exchange box, a mesh plate and a heat exchange component, wherein the mesh plate is arranged through the top of the heat exchange box, and the heat exchange component is arranged through one side of the heat exchange box, the mesh plate comprises a mesh plate body and a sealing plate, the sealing plate is fixed to the top of the mesh plate body, and the top of the sealing plate is penetrated with evenly distributed fixing screws, and the top of the heat exchange box is provided with fixing screw holes used in conjunction with the fixing screws, and the sealing plate is fixedly connected to the heat exchange box through the fixing screws and the fixing screw holes, and the heat exchange component comprises a first heat conducting plate, a second heat conducting plate, a heat exchanging sheet and a heat conducting rod, the second heat conducting plate is fixed to one side of the first heat conducting plate, the heat exchanging sheet is evenly fixed to the other side of the first heat conducting plate, and the heat conducting rod is evenly fixed to the side of the second heat conducting plate away from the first heat conducting plate; A water bath assembly is fixed on the support assembly, and includes a water tank and an oil tank. The oil tank is fixed to the bottom of the inner cavity of the water tank. One side of the oil tank is connected to a refueling pipe. The end of the refueling pipe away from the oil tank passes through the outside of the water tank. The heating box is connected to the condensing box, the condensing box is connected to the heat exchange box, one side of the top of the heat exchange box is connected to an exhaust pipe, one side of the heat exchange component is connected to the inner cavity of the water storage tank through a heat conducting rod, and is used to transfer the heat absorbed by the heat exchange component to the water storage tank.

[0009] As a preferred solution of the bio-jet fuel recovery and separation device of the present invention, temperature sensors are provided on both sides of the top of the heating box surface, a liquid level sensor is provided on the surface of the heating box and between the two temperature sensors, a vertical pipe is connected to the top of the heating box, a waste pipe is connected to one side of the heating box, and the waste pipe extends to the outside of the box body.

[0010] As a preferred solution of the bio-jet fuel recovery and separation device of the present invention, the top of the base plate is respectively fixedly connected with a junction box, a controller and a backup power supply, the junction box is located on one side of the controller, the backup power supply is located on the other side of the controller, and anti-slip pads are fixedly connected on both sides of the bottom of the base plate.

[0011] As a preferred solution of the bio-jet fuel recovery and separation device of the present invention, a second delivery pump is fixedly connected to the bottom of the horizontal plate, the second delivery pump is connected to the oil storage tank, the second delivery pump is connected to a delivery pipe, and the delivery pipe is connected to the heating box.

[0012] As a preferred solution of the bio-jet fuel recovery and separation device of the present invention, a liquid guide groove and a conveying groove are respectively provided at the bottom of the inner cavity of the condensing box, the liquid guide groove is connected to the conveying groove, the inner wall of the conveying groove is connected to a recovery pipe, and the recovery pipe is connected to the recovery box.

[0013] As a preferred solution of the bio-jet fuel recovery and separation device of the present invention, wherein: the surface of the condenser tube is provided with a fixed sleeve, the surface of the fixed sleeve is fixedly connected with a support plate, the support plate is fixedly connected to the inner wall of the condenser box, the end of the condenser tube away from the first delivery pump is connected with a horizontal pipe, and the horizontal pipe is connected to the water storage tank.

[0014] As a preferred solution of the bio-jet fuel recovery and separation device of the present invention, the surface of the box body is movably connected to a door body through a hinge, a nameplate is fixedly connected to one side of the top front of the box body, an observation window is provided through the left side of the front of the water tank, and a control panel is fixedly connected to the right side of the front of the water tank.

[0015] The beneficial effects of the present invention are as follows: through this scheme, the waste heat generated in the distillation process can be recovered. The condensation component and the heat exchange component, as key parts of the energy recovery system, can realize the transfer of heat from the high-temperature gas to the low-temperature bio-jet fuel raw materials or other links that require heating. The reuse of this heat can significantly reduce the input of external energy, thereby improving the energy utilization efficiency of the entire device and reducing production costs. At the same time, it also helps to reduce thermal pollution to the environment and promote the development of the bio-jet fuel industry in a greener and more sustainable direction. BRIEF DESCRIPTION OF THE DRAWINGS

[0016] In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following briefly introduces the drawings required for describing the embodiments. Obviously, the drawings described below are only some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without creative labor. Among them: Figure 1 This is a first-person perspective structural stereogram of the bio-jet fuel recovery and separation device.

[0017] Figure 2 This is a second perspective structural stereogram of the bio-jet fuel recovery and separation device.

[0018] Figure 3 This is a three-dimensional cutaway view of the box of the bio-jet fuel recovery and separation device.

[0019] Figure 4 This is a three-dimensional diagram of the partial structure of the bio-jet fuel recovery and separation device.

[0020] Figure 5 This is a cutaway perspective view of the condensate box of the bio-jet fuel recovery and separation device.

[0021] Figure 6 This is a cutaway perspective view of the heat exchange box of the bio-jet fuel recovery and separation device.

[0022] Figure 7 This is a cutaway perspective view of the water tank of the bio-jet fuel recovery and separation device.

[0023] Figure 8 This is a three-dimensional diagram of the recovery box of the bio-jet fuel recovery and separation device. DETAILED DESCRIPTION

[0024] In order to make the above-mentioned objects, features and advantages of the present invention more obvious and easy to understand, the specific implementation methods of the present invention are described in detail below in conjunction with the accompanying drawings.

[0025] In the following description, many specific details are set forth to facilitate a full understanding of the present invention, but the present invention may also be implemented in other ways different from those described herein, and those skilled in the art may make similar generalizations without violating the connotation of the present invention. Therefore, the present invention is not limited to the specific embodiments disclosed below.

[0026] Secondly, the term "one embodiment" or "embodiment" as used herein refers to a specific feature, structure, or characteristic that may be included in at least one implementation of the present invention. The term "in one embodiment" that appears in different places in this specification does not necessarily refer to the same embodiment, nor does it refer to a separate or selective embodiment that is mutually exclusive with other embodiments. Example 1

[0027] Reference Figure 1-Figure 8 , which is the first embodiment of the present invention, and provides a bio-jet fuel recovery and separation device. The bio-jet fuel recovery and separation device includes a support assembly 100, including a horizontal plate 101, a vertical plate 102 and a bottom plate 103. The vertical plate 102 is fixed to the bottom of the horizontal plate 101, and the bottom plate 103 is fixed to the bottom of the vertical plate 102.

[0028] The support assembly 100 is used for supporting and fixing. The bottom of the horizontal plate 101 and the top of the vertical plate 102 are fixedly connected by welding. The bottom of the vertical plate 102 and the top of the bottom plate 103 are fixedly connected by welding. The welding connection method can ensure the firmness of the workpiece connection, thereby improving the bearing capacity of the support assembly 100.

[0029] The heating assembly 200 is fixed on the supporting assembly 100, and includes a box body 201, an insulating plate 202, a fixing plate 203, a heating box 204 and a heating plate 205. The insulating plate 202 is fixed to the inner wall of the box body 201, the fixing plate 203 is fixedly connected to the bottom of the inner cavity of the box body 201, the fixing plate 203 is fixedly connected to the bottom of the heating box 204 on one side away from the inner wall of the box body 201, and the heating plate 205 is arranged through the bottom of the heating box 204.

[0030] The heating assembly 200 is used to heat the bio-jet fuel. The box body 201 cooperates with the heat insulation plate 202 to block the heat, thereby preventing heat loss during the heating process, improving the thermal energy utilization rate, and saving heating energy. The fixing plate 203 is used to connect the heating box 204 and the box body 201, and is also used to stably support the heating box 204. The heating plate 205 cooperates with the heating box 204 to heat the bio-jet fuel.

[0031] The condensation component 300 is arranged on one side of the heating component 200, and includes a condensation box 301, a condensation pipe 302, a first delivery pump 303 and a guide plate 304. The condensation pipe 302 is fixed to the inner cavity of the condensation box 301, the first delivery pump 303 is fixed to the bottom of the condensation box 301, the first delivery pump 303 is connected to the condensation pipe 302, and the guide plate 304 is fixed to the inner wall of the condensation box 301.

[0032] The condensation component 300 is used to condense steam. The surface of the first delivery pump 303 is connected to a water inlet pipe. The user connects the water inlet pipe to an external water source at normal temperature and starts the first delivery pump 303. The first delivery pump 303 works to deliver water to the condenser 302. The steam is cooled by the condenser 302 and the water. At this time, the water is heated, and the guide plate 304 can guide the flow of steam to increase the contact area between the steam and the condenser 302, thereby ensuring the condensation effect.

[0033] The recovery component 400 is arranged below the condensation component 300 and includes a recovery box 401 and a connecting plate 402 . The connecting plate 402 is fixed to the top of the recovery box 401 , and the top of the connecting plate 402 is fixedly connected to the condensation component 300 .

[0034] The condensed liquid is collected by the recovery component 400, the bottom of the connecting plate 402 is fixedly connected to the top of the recovery box 401 by welding, and the top of the connecting plate 402 is fixedly connected to the bottom of the condensation box 301 by welding. The welding connection method can ensure the firmness of the workpiece connection. The recovery box 401 is used for temporary storage of the recovered liquid.

[0035] The heat exchange assembly 500 is fixed to one side of the condensing assembly 300 and includes a heat exchange box 501 , a mesh plate 502 and a heat exchange component 503 . The mesh plate 502 is disposed through the top of the heat exchange box 501 , and the heat exchange component 503 is disposed through one side of the heat exchange box 501 .

[0036] The condensation box 301 transports the condensed gas to the heat exchange box 501. At this time, the gas still has residual heat. The gas is refined by the mesh plate 502 so that the gas is evenly transported to the surface of the heat exchange element 503 to ensure the heat exchange effect. The heat exchange element 503 can absorb the residual heat of the gas.

[0037] The water bath assembly 600 is fixed on the support assembly 100, and includes a water tank 601 and an oil tank 602. The oil tank 602 is fixed to the bottom of the inner cavity of the water tank 601. One side of the oil tank 602 is connected to a refueling pipe 6021, and the refueling pipe 6021 extends from one end away from the oil tank 602 to the outside of the water tank 601.

[0038] The water heated by the condensing component 300 is transported to the water tank 601, and the heat absorbed by the heat exchange component 503 reheats the water inside the water tank 601. The hot water inside the water tank 601 can preheat the bio-jet fuel in the fuel tank 602, thereby reducing the heat required for the heating component 200 to heat the bio-jet fuel. In addition, the hot water inside the water tank 601 can also be transported to a designated location through a water delivery device for use, thereby improving energy utilization. The refueling pipe 6021 is used to replenish the bio-jet fuel. Example 2

[0039] Reference Figure 1-Figure 8 , which is the second embodiment of the present invention, and this embodiment is based on the previous embodiment.

[0040] Specifically, temperature sensors 2041 are provided on both sides of the top of the surface of the heating box 204, a liquid level sensor 2042 is provided on the surface of the heating box 204 and between the two temperature sensors 2041, a vertical pipe 2043 is connected to the top of the heating box 204, a waste pipe 2044 is connected to one side of the heating box 204, and the waste pipe 2044 extends to the outside of the box body 201.

[0041] There are two temperature sensors 2041. The two temperature sensors 2041 can accurately detect the temperature inside the heating box 204, so as to achieve precise temperature control. The liquid level sensor 2042 is used to detect the liquid level inside the heating box 204, so as to replenish the bio-jet fuel in time and avoid damage to the heating box 204 and the heating plate 205 due to empty burning. Opening the vertical pipe 2043 can balance the internal and external pressures when adding bio-jet fuel, and the residual pipe 2044 can discharge the residual liquid.

[0042] Specifically, a junction box 1031, a controller 1032 and a backup power supply 1033 are fixedly connected to the top of the base plate 103, respectively. The junction box 1031 is located on one side of the controller 1032, and the backup power supply 1033 is located on the other side of the controller 1032. Anti-slip pads 1034 are fixedly connected to both sides of the bottom of the base plate 103.

[0043] The junction box 1031 is used to connect and transmit electric energy, the controller 1032 is used to perform circuit control, the circuit connection method and the control procedure belong to the prior art, and therefore will not be described in detail in this application document, the backup power supply 1033 is used to store and provide electric energy, so that temporary power supply can be provided during a power outage, and the anti-slip pad 1034 can increase friction, thereby improving the stability of the bio-jet fuel recovery and separation device during use.

[0044] Specifically, a second delivery pump 1011 is fixedly connected to the bottom of the transverse plate 101 , the second delivery pump 1011 is connected to the oil storage tank 602 , the second delivery pump 1011 is connected to a delivery pipe 1012 , and the delivery pipe 1012 is connected to the heating box 204 .

[0045] When the liquid level sensor 2042 detects that the bio-jet fuel in the heating box 204 is lacking, the second delivery pump 1011 is started, and the second delivery pump 1011 delivers the preheated bio-jet fuel to the delivery pipe 1012, and the delivery pipe 1012 delivers the preheated bio-jet fuel to the inner cavity of the heating box 204, thereby replenishing the bio-jet fuel.

[0046] Specifically, a liquid guiding groove 3011 and a conveying groove 3012 are respectively opened at the bottom of the inner cavity of the condensation box 301 . The liquid guiding groove 3011 is connected to the conveying groove 3012 . The inner wall of the conveying groove 3012 is connected to a recovery pipe 3013 . The recovery pipe 3013 is connected to the recovery box 401 .

[0047] The liquid condensed by the condenser 302 is transported to the conveying groove 3012 through the liquid guiding groove 3011, and the conveying groove 3012 transports the liquid to the recovery pipe 3013. The recovery pipe 3013 transports the liquid to the recovery box 401, and the recovery box 401 collects and temporarily stores the liquid. The surface of the recovery box 401 is connected to a valve, which can discharge the recovered liquid.

[0048] Specifically, a fixed sleeve 3021 is provided on the surface of the condenser 302, a support plate 3022 is fixedly connected to the surface of the fixed sleeve 3021, the support plate 3022 is fixedly connected to the inner wall of the condenser box 301, and the end of the condenser 302 away from the first delivery pump 303 is connected to a transverse pipe 3023, and the transverse pipe 3023 is connected to the water storage tank 601.

[0049] The fixing sleeve 3021 is fixedly connected to the condensing tube 302 , and is used to support and fix the condensing tube 302 . The support plate 3022 is used to install the fixing sleeve 3021 on the inner wall of the condensing box 301 . The transverse pipe 3023 is used to transport hot water to the inner cavity of the water storage tank 601 . Example 3

[0050] Reference Figure 1-Figure 8 , which is the third embodiment of the present invention, and is based on the first two embodiments.

[0051] Specifically, the mesh plate part 502 includes a mesh plate body 5021 and a sealing plate 5022. The sealing plate 5022 is fixed to the top of the mesh plate body 5021. Evenly distributed fixing screws 5023 are arranged through the top of the sealing plate 5022. A fixing screw hole used in conjunction with the fixing screw 5023 is opened on the top of the heat exchange box 501. The sealing plate 5022 is fixedly connected to the heat exchange box 501 through the fixing screw 5023 and the fixing screw hole.

[0052] The gas is guided and dispersed through the mesh body 5021 to ensure the heat exchange effect. The sealing plate 5022 is used to seal the heat exchange box 501. When the mesh body 5021 is not needed, the user can remove the fixing screws 5023 with tools, so that the sealing plate 5022 and the mesh body 5021 can be disassembled, and then the sealing plate 5022 can be installed alone.

[0053] Specifically, the heat exchange element 503 includes a first heat conducting plate 5031, a second heat conducting plate 5032, a heat exchange sheet 5033 and a heat conducting rod 5034. The second heat conducting plate 5032 is fixed to one side of the first heat conducting plate 5031, the heat exchange sheet 5033 is evenly fixed to the other side of the first heat conducting plate 5031, and the heat conducting rod 5034 is evenly fixed to the side of the second heat conducting plate 5032 away from the first heat conducting plate 5031.

[0054] The evenly distributed heat exchange plates 5033 can efficiently absorb the residual heat in the exhaust gas, and transfer the heat to the first heat conduction plate 5031 through the heat exchange plates 5033, the first heat conduction plate 5031 transfers the heat to the second heat conduction plate 5032, and the second heat conduction plate 5032 transfers the heat to the heat conduction rod 5034. The evenly distributed heat conduction rod 5034 can heat the water body, thereby realizing the recovery of waste heat.

[0055] Specifically, the heating box 204 is connected to the condensing box 301 , the condensing box 301 is connected to the heat exchange box 501 , and one side of the top of the heat exchange box 501 is connected to an exhaust pipe 5011 .

[0056] The exhaust pipe 5011 is used to discharge the gas recovered from the waste heat.

[0057] Specifically, the surface of the box body 201 is movably connected to a door body 2011 through a hinge, a nameplate 2012 is fixedly connected to one side of the top front of the box body 201, an observation window 6011 is provided on the left side of the front of the water tank 601, and a control panel 6012 is fixedly connected to the right side of the front of the water tank 601.

[0058] A sealing body is provided at the connection between the door body 2011 and the box body 201, and the sealing body can ensure the sealing of the connection between the door body 2011 and the box body 201, thereby avoiding heat loss. The user can open the door body 2011 to inspect the components in the inner cavity of the box body 201. The surface of the nameplate 2012 is marked with relevant information of the bio-jet fuel recovery and separation device, so as to facilitate the user to understand and use the bio-jet fuel recovery and separation device. The observation window is used to observe the liquid level of the water body, so that the excess hot water can be transported to the designated use place in time to avoid excessive water. The control panel 6012 is used to input control signals and display working information.

[0059] When in use, the box body 201 cooperates with the heat insulation plate 202 to block the heat, thereby preventing heat loss during the heating process, improving the thermal energy utilization rate, and saving heating energy. The fixing plate 203 is used to connect the heating box 204 and the box body 201, and is also used to stably support the heating box 204. The heating plate 205 cooperates with the heating box 204 to heat the bio-jet fuel. The steam generated inside the heating box 204 is transported to the condensing box 301. The surface of the first delivery pump 303 is connected with a water inlet pipe. The user connects the water inlet pipe to an external water source at normal temperature, starts the first delivery pump 303, and the first delivery pump 303 works to transport water to the condensing pipe 302. The condensing pipe 302 cooperates with the water to cool the steam. At this time, the water is heated, and the guide plate 304 can guide the flow of the steam to increase the steam and condensing pipe 302. The contact area ensures the condensation effect. The condensed liquid is collected by the recovery component 400. The condensation box 301 transports the condensed gas to the heat exchange box 501. At this time, the gas still has residual heat. The gas is refined by the mesh plate 502, so that the gas is evenly transported to the surface of the heat exchange component 503 to ensure the heat exchange effect. The heat exchange component 503 can absorb the residual heat of the gas. The water heated by the condensation component 300 is transported to the water storage tank 601. The heat absorbed by the heat exchange component 503 reheats the water inside the water storage tank 601. The hot water inside the water storage tank 601 can preheat the bio-jet fuel in the fuel storage tank 602, thereby reducing the heat required for the heating component 200 to heat the bio-jet fuel. In addition, the hot water inside the water storage tank 601 can also be transported to a designated location through a water delivery device for use, thereby improving energy utilization.

[0060] It should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention rather than to limit it. Although the present invention has been described in detail with reference to the preferred embodiments, those skilled in the art should understand that the technical solutions of the present invention may be modified or replaced by equivalents without departing from the spirit and scope of the technical solutions of the present invention, which should all be included in the scope of the claims of the present invention.

Claims

1. A bio-jet fuel recovery and separation device, characterized in that: include, A support assembly (100) comprises a transverse plate (101), a vertical plate (102) and a bottom plate (103), wherein the vertical plate (102) is fixed to the bottom of the transverse plate (101), and the bottom plate (103) is fixed to the bottom of the vertical plate (102); A heating assembly (200) is fixed on the supporting assembly (100), comprising a box body (201), a heat insulating plate (202), a fixing plate (203), a heating box (204) and a heating plate (205), wherein the heat insulating plate (202) is fixed to the inner wall of the box body (201), the fixing plate (203) is fixedly connected to the bottom of the inner cavity of the box body (201), the side of the fixing plate (203) away from the inner wall of the box body (201) is fixedly connected to the bottom of the heating box (204), and the heating plate (205) is arranged through the bottom of the heating box (204); A condensation component (300) is arranged on one side of the heating component (200), comprising a condensation box (301), a condensation pipe (302), a first delivery pump (303) and a guide plate (304), wherein the condensation pipe (302) is fixed to the inner cavity of the condensation box (301), the first delivery pump (303) is fixed to the bottom of the condensation box (301), the first delivery pump (303) is connected to the condensation pipe (302), and the guide plate (304) is fixed to the inner wall of the condensation box (301); A recovery component (400) is arranged below the condensation component (300), comprising a recovery box (401) and a connection plate (402), wherein the connection plate (402) is fixed to the top of the recovery box (401), and the top of the connection plate (402) is fixedly connected to the condensation component (300); The heat exchange component (500) is fixed to one side of the condensing component (300), and comprises a heat exchange box (501), a mesh plate component (502) and a heat exchange component (503), wherein the mesh plate component (502) is arranged through the top of the heat exchange box (501), and the heat exchange component (503) is arranged through one side of the heat exchange box (501), the mesh plate component (502) comprises a mesh plate body (5021) and a sealing plate (5022), the sealing plate (5022) is fixed to the top of the mesh plate body (5021), and the top of the sealing plate (5022) is provided with evenly distributed fixing screws (5023), and the top of the heat exchange box (501) is provided with a sealing plate (5022) for connecting with the fixing screws (5023). The sealing plate (5022) is fixedly connected to the heat exchange box (501) by means of the fixing screws (5023) and the fixing screw holes, the heat exchange element (503) comprising a first heat conducting plate (5031), a second heat conducting plate (5032), a heat exchanging sheet (5033) and a heat conducting rod (5034), the second heat conducting plate (5032) being fixed to one side of the first heat conducting plate (5031), the heat exchanging sheet (5033) being evenly fixed to the other side of the first heat conducting plate (5031), and the heat conducting rod (5034) being evenly fixed to the side of the second heat conducting plate (5032) away from the first heat conducting plate (5031); The water bath assembly (600) is fixed on the support assembly (100), and comprises a water storage tank (601) and an oil storage tank (602), wherein the oil storage tank (602) is fixed to the bottom of the inner cavity of the water storage tank (601), and one side of the oil storage tank (602) is connected to a refueling pipe (6021), and the end of the refueling pipe (6021) away from the oil storage tank (602) passes through the outside of the water storage tank (601); The heating box (204) is in communication with the condensing box (301), the condensing box (301) is in communication with the heat exchange box (501), one side of the top of the heat exchange box (501) is in communication with an exhaust pipe (5011), and one side of the heat exchange component (503) is in communication with the inner cavity of the water storage tank (601) via a heat conducting rod (5034), so as to transfer the heat absorbed by the heat exchange component (500) to the water storage tank (601).

2. The bio-jet fuel recovery and separation device according to claim 1, characterized in that: Temperature sensors (2041) are provided on both sides of the top of the surface of the heating box (204); a liquid level sensor (2042) is provided on the surface of the heating box (204) and between the two temperature sensors (2041); a vertical pipe (2043) is connected to the top of the heating box (204); a residual discharge pipe (2044) is connected to one side of the heating box (204); and the residual discharge pipe (2044) extends to the outside of the box body (201).

3. The bio-jet fuel recovery and separation device according to claim 1, characterized in that: The top of the base plate (103) is respectively fixedly connected with a junction box (1031), a controller (1032) and a backup power supply (1033); the junction box (1031) is located on one side of the controller (1032), and the backup power supply (1033) is located on the other side of the controller (1032); and both sides of the bottom of the base plate (103) are fixedly connected with anti-slip pads (1034).

4. The bio-jet fuel recovery and separation device according to claim 1, characterized in that: A second delivery pump (1011) is fixedly connected to the bottom of the transverse plate (101), the second delivery pump (1011) is in communication with the oil storage tank (602), the second delivery pump (1011) is in communication with a delivery pipe (1012), and the delivery pipe (1012) is in communication with the heating box (204).

5. The bio-jet fuel recovery and separation device according to claim 1, characterized in that: A liquid guide groove (3011) and a conveying groove (3012) are respectively provided at the bottom of the inner cavity of the condensing box (301), the liquid guide groove (3011) is in communication with the conveying groove (3012), the inner wall of the conveying groove (3012) is in communication with a recovery pipe (3013), and the recovery pipe (3013) is in communication with the recovery box (401).

6. The bio-jet fuel recovery and separation device according to claim 1, characterized in that: The surface of the condensing pipe (302) is sleeved with a fixing sleeve (3021), the surface of the fixing sleeve (3021) is fixedly connected with a supporting plate (3022), the supporting plate (3022) is fixedly connected to the inner wall of the condensing tank (301), and one end of the condensing pipe (302) away from the first delivery pump (303) is connected with a transverse pipe (3023), and the transverse pipe (3023) is connected with the water storage tank (601).

7. The bio-jet fuel recovery and separation device according to claim 1, characterized in that: The surface of the box body (201) is movably connected to a door body (211) via a hinge, a nameplate (212) is fixedly connected to one side of the top of the front face of the box body (201), an observation window is provided through the left side of the front face of the water storage tank (601), and a control panel (6012) is fixedly connected to the right side of the front face of the water storage tank (601).

Images