Fuel reaction device and reaction method

By designing a fuel reaction device including a guide groove, a spiral plate and a circulation channel, the problem of low reaction efficiency caused by the fast upward speed of hydrogen is solved, and the full mixing of hydrogen and oil and efficient hydrotreatment are achieved.

CN119075890BActive Publication Date: 2025-04-18LUOYANG HENGJIU BIOENERGY CO LTD +1
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Patent Information

Application Number
CN202411570178.X
Authority / Receiving Office
CN · China
Patent Type
Patents(China)
Current Assignee / Owner
Filing Date
2024-11-06
Publication Date
2025-04-18
Estimated Expiration
2044-11-06

AI Technical Summary

Technical Problem

In existing fuel hydrogenation reaction equipment, the fast hydrogen rise rate leads to a lower contact rate between the oil and hydrogen and a lower reaction efficiency.

Method used

A fuel reaction device is designed, including a tank body, a mixing mechanism and a reaction mechanism. The mixing mechanism promotes the full mixing and reaction of hydrogen and oil through the guide groove, spiral plate and circulation channel. The reaction mechanism improves the reaction efficiency through stirring and separation of the catalyst.

Benefits of technology

By increasing the contact range between hydrogen and oil and repeated mixing, the efficiency of hydrotreatment is significantly improved, the hydrogen upflow rate is reduced, and the efficient hydrotreatment of oil is ensured.

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Abstract

The invention relates to the technical field of chemical reaction equipment, and specifically discloses a fuel reaction device and a reaction method. The fuel device comprises a tank body, a liquid inlet and a liquid outlet are provided on the tank body, a mixing mechanism is provided in the tank body, the mixing mechanism comprises a guide piece, a mixing piece and an air intake assembly, a mixing chamber is formed inside the guide piece, the mixing piece is arranged in the mixing chamber, a spiral guide groove is formed between the guide piece and the mixing piece, the liquid inlet is communicated with the upper end of the guide groove, an opening is provided at the bottom of the mixing chamber, the air intake assembly comprises an air intake pipe, an air outlet channel and an air outlet pipe, the air outlet pipe is spirally arranged in the guide groove, the air outlet end of the air outlet pipe is communicated with the inside of the mixing piece, the air outlet channel is respectively connected to the mixing piece and the air outlet pipe, the guide groove is unidirectionally connected with the air outlet channel through a circulation channel, the reaction method comprises raw material preparation, mixing, separation and purification, and the fuel reaction device and the reaction method provided by the invention improve the reaction efficiency of oil and hydrogen.
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Description

Technical Field

[0001] The present invention relates to the technical field of chemical reaction equipment, and in particular to a fuel reaction device and a reaction method. Background Art

[0002] Fuel hydrogenation is a chemical reaction that aims to improve the quality and performance of fuel. The reaction between fuel and hydrogen is used to remove impurities in the fuel, reduce the content of sulfur and other harmful elements, and improve the quality of the fuel. The fuel hydrogenation reaction needs to be carried out in a reaction vessel. To ensure the reaction effect, it is necessary to ensure that the fuel and hydrogen are in full contact in the reaction vessel.

[0003] The patent document with the authorization announcement number CN215693847U discloses a hydrogenation reaction equipment for fuel production, including a reaction tank and a hydrogen recovery system, the hydrogen recovery system includes an expander and a gas cylinder system, the outer side of the reaction tank is wrapped with a jacket, the lower end of the jacket is provided with a heat medium inlet, the upper end of the jacket is provided with a heat medium outlet, the interior of the reaction tank is filled with a solution containing a catalyst, the bottom of the reaction tank is provided with a distributor, the distributor is respectively connected to the reactant delivery pipeline and the hydrogen generator; the input end of the expander is connected to the gas outlet of the reaction tank through a pipeline, the output end of the expander is connected to the product delivery pipeline, the separation end of the expander is connected to a pressurizing device, and the pressurizing device is connected to the gas cylinder system through a pipeline. According to the relative boiling point difference of each component in the reaction product gas phase, the expander can recover extremely high-purity hydrogen from the reaction product gas phase, and the hydrogen is then stored in the gas cylinder system through the pressurizing device, reducing hydrogen consumption and energy consumption.

[0004] The reaction equipment provided by the above patent document passes hydrogen into the reaction tank through a distributor at the bottom of the reaction tank. Due to the low density of hydrogen, hydrogen will quickly float up in the reaction tank, resulting in a relatively low contact rate between the oil and hydrogen. In actual production, it is necessary to repeatedly recover the upper layer of hydrogen and repeatedly pressurize it into the reaction tank, resulting in low efficiency of oil hydrogenation treatment. Summary of the invention

[0005] The present invention provides a fuel reaction device and a reaction method, aiming to solve the problem in the related art that when the fuel is hydrogenated, the reaction efficiency between the oil and hydrogen is low due to the fast floating speed of hydrogen.

[0006] A fuel reaction device of the present invention comprises a tank body, wherein the tank body is provided with a liquid inlet and a liquid outlet, wherein the tank body is provided with a mixing mechanism, wherein the mixing mechanism comprises a guide member, a mixing member and an air intake assembly, wherein a mixing chamber is formed inside the guide member, wherein the mixing member is arranged in the mixing chamber, wherein a spiral guide groove is formed between the guide member and the mixing member, wherein the liquid inlet is communicated with the upper end of the guide groove, and wherein an opening is provided at the bottom of the mixing chamber;

[0007] The air intake assembly includes an air intake pipe, an air outlet channel and an air outlet pipe. The air outlet pipe is spirally arranged in the guide groove. A plurality of air outlet holes are evenly spaced on the air outlet pipe. A cavity is formed inside the mixing element. The air outlet end of the air outlet pipe is connected to the interior of the mixing element. One end of the air outlet channel is connected to the interior of the mixing element. The other end of the air outlet channel is connected to the air outlet pipe through a connecting structure, and the gas in the mixing element is introduced into the air outlet pipe. The mixing element is also provided with a circulation channel. One end of the circulation channel is connected to the guide groove, and the other end of the circulation channel is unidirectionally connected to the air outlet channel.

[0008] The beneficial effects are: promoting full mixing and reaction of oil and hydrogen. After the oil is introduced into the tank body, it flows in the guide groove. The feed component introduces hydrogen into the guide groove and fully mixes it with the oil in the guide groove. Compared with the traditional method of directly introducing hydrogen into the tank body, the contact range of hydrogen and oil is improved, and the floating hydrogen can enter the outlet pipe again from the outlet channel through the circulation channel, thereby realizing repeated mixing and reaction of the floating hydrogen and oil, improving the mixing and reaction efficiency of hydrogen and oil, and ensuring the hydrogenation treatment effect of the oil.

[0009] Preferably, a spiral plate 1 is provided on the inner side of the guide member, and a spiral plate 2 is provided on the outer side of the mixing member, and the spiral directions of the spiral plates 1 and 2 are consistent. The mixing mechanism also includes a driving member, and the driving member drives the mixing member to rotate, and the air outlet pipe is rotatably matched with the spiral plate 1, and the connecting structure is arranged on the spiral plate 2.

[0010] Preferably, a blocking block is respectively provided at the upper and lower ends of the guide groove, a groove body is provided on the spiral plate 2, the upper end of the blocking block is elastically connected to the groove body, the lower end of the blocking block abuts against the spiral plate 2, a notch is provided in the middle of the blocking block, and when the spiral plate 2 approaches the spiral plate 1, the blocking block is squeezed into the groove body and the notch is staggered with the guide groove.

[0011] The beneficial effects are: reducing the floating speed of hydrogen in the oil, promoting the mixing and reaction of hydrogen and oil, when the driving member drives the mixing member to rotate, the space of the guide groove formed by the spiral plate 2 and the spiral plate 1 changes with the rotation of the mixing member, when the guide groove space is reduced, the pressure in the guide groove increases, slowing down the floating speed of hydrogen, promoting the full contact between hydrogen and oil, and further improving the reaction efficiency of oil and hydrogen.

[0012] Preferably, the connecting structure includes a connecting groove, a connecting piece and an elastic piece, the connecting groove is opened on the second spiral plate, the outlet end of the air outlet channel is connected to the connecting groove, the connecting piece is hollow inside, an air inlet is provided at the upper end of the connecting piece, the upper end of the connecting piece extends into the connecting groove, the elastic piece is arranged in the connecting groove and abuts against the upper end of the connecting piece, the side wall of the connecting piece is slidingly and closedly connected to the connecting groove, and the lower end of the connecting piece is connected to the outlet pipe.

[0013] Preferably, a spiral groove is provided on the outer wall of the connecting member, a slider slidably matched with the spiral groove is provided on the connecting groove, the lower end of the connecting member is sealingly and rotatably connected to the air outlet, and a blade is fixed on the connecting member.

[0014] The beneficial effects are as follows: hydrogen is promoted to fully contact with the oil in the guide groove. After hydrogen enters the connecting groove from the outlet channel, it further enters the connecting piece from the air inlet of the connecting piece, and further enters the outlet pipe, and is finally discharged from each outlet on the outlet pipe; in addition, when the mixing piece rotates, the spacing between the spiral plate 1 and the spiral plate 2 is changed, and the connecting piece rotates in coordination with the rotation of the sliding block at the spiral groove and the connecting groove, and drives the blades to rotate, stirring the oil around the connecting piece, causing disturbance to the oil, and thereby allowing the oil to further fully contact and react with the hydrogen.

[0015] Preferably, a reaction mechanism is also provided in the tank body, and the reaction mechanism is located at the lower side of the mixing mechanism. The reaction mechanism includes an outer cylinder and a rotating part. The outer cylinder is unidirectionally rotatably matched with the tank body. The rotating part is provided on the inner side of the outer cylinder. A gap for accommodating a catalyst is formed between the rotating part and the outer cylinder. A bottom plate is provided at the bottom of the outer cylinder, and a plurality of filter holes are provided on the bottom plate. The rotating part is fixed relative to the mixing part, and the rotating part is frictionally rotatably matched with the bottom of the outer cylinder.

[0016] Preferably, a tooth portion is provided on the outer circumferential side of the outer cylinder, and a spring block is elastically connected to the inner wall of the tank body. The spring block is located between two adjacent tooth portions, and the end faces of the spring block opposite to the two adjacent tooth portions are a straight face and an inclined face respectively. When the tooth portion squeezes the inclined face side of the spring block, the spring block is pushed to retract into the inner wall of the tank body and avoid the tooth portion.

[0017] The beneficial effects are: providing catalytic reaction space for the mixed oil, improving the purification effect of the oil, and during the reaction process, by driving the rotating part and the outer cylinder to move in relative reverse directions, rubbing the catalyst and separating impurities attached to the catalyst surface, thereby ensuring the catalytic effect of the catalyst.

[0018] Preferably, the upper end surface of the rotating member decreases in height in a direction away from the axial direction of the tank body.

[0019] The beneficial effect is that the height change of the upper end surface of the rotating part facilitates the diversion of the mixed solution, so that the solution smoothly enters between the outer cylinder and the rotating part to react with the catalyst.

[0020] Preferably, the width of the outer cylinder decreases from top to bottom, and the width of the rotating member decreases from top to bottom.

[0021] A fuel reaction method comprises the following steps:

[0022] S1. Raw material preparation: crude oil is initially refined to obtain semi-finished fuel oil;

[0023] S2, mixing, mixing and reacting the semi-finished fuel oil and hydrogen through the fuel oil reaction device provided by the present invention;

[0024] S3, separation and purification, after the reaction is completed, the product is separated from the unreacted raw materials, and the unreacted raw materials are returned to the mixing step for mixing treatment, and the product is further purified and then cooled to room temperature for storage.

[0025] The beneficial effects are: promoting full mixing and reaction of oil and hydrogen. After the oil is introduced into the tank body, it flows in the guide groove. The feed component introduces hydrogen into the guide groove and fully mixes it with the oil in the guide groove, thereby increasing the contact range of hydrogen and oil. The floating hydrogen can enter the outlet pipe again from the outlet channel through the circulation channel, thereby achieving repeated mixing and reaction of the floating hydrogen and oil, and improving the mixing and reaction efficiency of hydrogen and oil.

[0026] The beneficial effects of the present invention are:

[0027] (1) Promote the full mixing and reaction of oil and hydrogen. After the oil is introduced into the tank body, it flows in the guide groove. The feed component introduces hydrogen into the guide groove and fully mixes it with the oil in the guide groove. Compared with the traditional method of directly introducing hydrogen into the tank body, the contact range of hydrogen and oil is improved, and the floating hydrogen can enter the outlet pipe again through the outlet channel through the circulation channel, thereby realizing repeated mixing and reaction of the floating hydrogen and oil, improving the mixing and reaction efficiency of hydrogen and oil, and ensuring the hydrogenation treatment effect of the oil.

[0028] (2) Reduce the speed of hydrogen rising in the oil and promote the mixing and reaction of hydrogen and oil. When the driving element drives the mixing element to rotate, the space of the guide groove formed by spiral plate 2 and spiral plate 1 changes with the rotation of the mixing element. When the space of the guide groove decreases, the pressure in the guide groove increases, slowing down the speed of hydrogen rising, promoting the full contact between hydrogen and oil, and further improving the reaction efficiency of oil and hydrogen.

[0029] (3) The hydrogen is promoted to fully contact with the oil in the guide groove. After the hydrogen enters the connecting groove from the outlet channel, it further enters the connecting piece from the air inlet of the connecting piece, and further enters the outlet pipe, and is finally discharged from the outlets on the outlet pipe. In addition, when the mixing element rotates, the distance between the spiral plate 1 and the spiral plate 2 is changed. The connecting piece rotates in coordination with the rotation of the spiral groove on it and the slider at the connecting groove, and drives the blades to rotate, stirring the oil around the connecting piece, causing disturbance to the oil, thereby allowing the oil to further fully contact and react with the hydrogen. BRIEF DESCRIPTION OF THE DRAWINGS

[0030] Figure 1 It is a schematic diagram of the structure inside the tank body of the present invention.

[0031] Figure 2 It is a schematic structural diagram of the connection between the mixing element and the reaction mechanism in the present invention.

[0032] Figure 3 It is a schematic diagram of the structure of the mixing element in the present invention.

[0033] Figure 4 It is a structural schematic diagram of the connection between the air outlet pipe and the mixing element in the present invention.

[0034] Figure 5 yes Figure 4 Enlarged view of part A.

[0035] Reference numerals:

[0036] 1. Tank body; 11. Liquid inlet; 12. Liquid outlet; 2. Driving member; 21. Guide member; 211. Spiral plate 1; 22. Mixing member; 221. Spiral plate 2; 3. Air inlet pipe; 31. Air outlet channel; 311. Connecting groove; 32. Air outlet pipe; 33. Connecting member; 34. Blade; 35. Circulation channel; 4. Rotating member; 41. Outer cylinder; 411. Tooth; 412. Spring block. DETAILED DESCRIPTION

[0037] Embodiments of the present invention are described in detail below, and examples of the embodiments are shown in the accompanying drawings. The embodiments described below with reference to the accompanying drawings are exemplary and intended to be used to explain the present invention, but should not be understood as limiting the present invention.

[0038] like Figure 1 As shown, the fuel reaction device of the present invention comprises a tank body 1, on which a liquid inlet 11 and a liquid outlet 12 are provided. Untreated fuel enters the tank body 1 from the liquid inlet 11, and the fuel treated with hydrogen is discharged from the liquid outlet 12 and collected. A mixing mechanism for mixing fuel and hydrogen is provided in the tank body 1.

[0039] The mixing mechanism includes a guide member 21, a mixing member 22 and an air intake assembly. A mixing chamber is formed inside the guide member 21. The mixing member 22 is arranged in the mixing chamber. The guide member 21, the mixing member 22 and the tank body 1 are coaxially arranged. A spiral plate 1 211 is provided on the inner wall of the guide member 21. A spiral plate 221 is provided on the outer side of the mixing member 22. The spiral plates 1 211 and 221 overlap and have the same spiral direction. The spiral plates 1 211 and 221 form a spiral guide groove between the guide member 21 and the mixing member 22. The liquid inlet 11 is connected to the upper end of the guide groove. The oil flows from top to bottom along the guide groove. The bottom diameter of the guide member 21 is reduced to form a cone. An opening is provided at the bottom of the guide member 21. After the oil is mixed in the mixing chamber, it flows out from the opening at the bottom of the guide member 21.

[0040] The mixing element 22 is also connected to a driving element 2, which may be a motor. The driving element 2 is fixed to the mixing element 22 via a driving shaft. The driving element 2 drives the mixing element 22 to rotate. When the mixing element 22 rotates, the spacing between the spiral plate 1 211 and the spiral plate 221 changes, and the space size of the guide groove changes. When the space in the guide groove decreases, the gas inside it is compressed and the pressure increases, which facilitates the mixing of hydrogen and oil.

[0041] like Figures 3 to 5 As shown, the air intake assembly is used to introduce hydrogen into the guide groove. The air intake assembly includes an air intake pipe 3, an air outlet channel 31 and an air outlet pipe 32. The air outlet pipe 32 is spirally arranged in the guide groove. A plurality of air outlet holes are evenly spaced on the air outlet pipe 32. A cavity is formed inside the mixing element 22. The air outlet end of the air outlet pipe 32 is connected to the inside of the mixing element 22. One end of the air outlet channel 31 is connected to the inside of the mixing element 22. The other end of the air outlet channel 31 is connected to the air outlet pipe 32 through a connecting structure, and the gas in the mixing element 22 is introduced into the air outlet pipe 32. 2. The outlet pipe 32 is slidably matched with the spiral plate 1 211 and does not separate from the spiral plate 1 211. The outlet pipe 32 rotates with the spiral plate 221. The hydrogen enters the interior of the mixing element 22 from the intake pipe 3, and is further introduced into the outlet pipe 32 through the outlet channel 31, and is finally discharged from the outlet holes in the outlet pipe 32, so that the hydrogen is fully mixed with the oil in the guide groove. The rotation operation of the mixing element 22 further promotes the pressure change in the guide groove, so that the mixing effect of the hydrogen and the oil is improved when the space in the guide groove is squeezed.

[0042] The connecting structure includes a connecting groove 311, a connecting piece 33 and an elastic piece. The connecting groove 311 is arranged on the spiral plate 221. The outlet end of the gas outlet channel 31 is connected to the connecting groove 311. The connecting piece 33 is hollow inside. An air inlet is arranged on the upper end of the connecting piece 33. The upper end of the connecting piece 33 extends into the connecting groove 311. The elastic piece is arranged in the connecting groove 311 and abuts against the upper end of the connecting piece 33. The side wall of the connecting piece 33 is slidably and closedly connected to the connecting groove 311. The lower end of the connecting piece 33 is connected to the gas outlet pipe 32. The gas in the mixing element 22 enters the connecting groove 311 through the gas outlet channel 31, and further enters the air inlet at the upper end of the connecting piece 33 in the connecting groove 311, and finally enters the gas outlet pipe 32 through the connecting piece 33. In order to improve the efficiency of hydrogen introduction, a plurality of gas outlet channels 31 and a plurality of connecting structures can be provided, and each gas outlet channel 31 corresponds to each connecting structure one by one.

[0043] In order to further promote the mixing of oil and hydrogen, a spiral groove is provided on the outer wall of the connecting member 33, and a slider that slides with the spiral groove is provided on the connecting groove 311. The lower end of the connecting member 33 is sealed and rotatably connected to the air outlet. A blade 34 is fixed on the connecting member 33. When the relative spacing between the spiral plate 1 211 and the spiral plate 2 221 changes, the connecting member 33 rotates with the cooperation of the slider and the spiral groove, and drives the blade 34 to rotate, thereby stirring the oil around the connecting member 33, promoting oil disturbance, making the oil fully contact with the hydrogen, and improving the mixing effect of the oil and hydrogen.

[0044] A sealing block is provided at the upper and lower ends of the guide groove, and a groove body is provided on the spiral plate 221. The upper end of the sealing block is elastically connected to the groove body, and the lower end of the sealing block abuts against the spiral plate 221. A notch is provided in the middle of the sealing block. When the spiral plate 221 approaches the spiral plate 1 211, the sealing block is squeezed into the groove body and the notch is staggered with the guide groove. When the spiral plate 221 and the spiral plate 1 211 are relatively far apart, the notch on the sealing block is in the guide groove, and the oil can flow through the notch. When the spacing between the spiral plate 221 and the spiral plate 1 211 is reduced, the sealing block is squeezed until the notch is staggered with the guide groove, and the guide groove is in a relatively closed state in the area between the two sealing blocks, so that when the spiral plate 221 approaches the spiral plate 1 211, the pressure in the guide groove is adjusted according to the spatial change, thereby promoting the full mixing and reaction of the oil and hydrogen in this area.

[0045] A circulation channel 35 is also provided on the mixing element 22, one end of the circulation channel 35 is connected to the guide groove, and the other end of the circulation channel 35 is unidirectionally connected to the gas outlet channel 31. The circulation channel 35 can be connected to the gas outlet channel 31 through a one-way valve. When the oil and hydrogen are mixed, the hydrogen flowing above the oil level enters the gas outlet channel 31 through the circulation channel 35, and further re-enters the gas outlet pipe 32 through the connecting structure, so that the upper layer of hydrogen automatically circulates in the mixing operation of the oil and hydrogen, so that the hydrogen is fully in contact with the oil, thereby improving the utilization efficiency of the hydrogen.

[0046] like Figure 1 and Figure 2 As shown, a reaction mechanism is also provided in the tank body 1, and the reaction mechanism is located at the lower side of the mixing mechanism. The reaction mechanism includes an outer cylinder 41 and a rotating member 4. The rotating member 4 is provided on the inner side of the outer cylinder 41. A gap for accommodating a catalyst is formed between the rotating member 4 and the outer cylinder 41. In order to facilitate the mixed oil to smoothly enter the gap between the outer cylinder 41 and the rotating member 4, the upper end surface of the rotating member 4 is lowered in height along the direction away from the axial direction of the tank body 1. A bottom plate is provided at the bottom of the outer cylinder 41, and a plurality of filter holes are provided on the bottom plate. The rotating member 4 is fixed relative to the mixing member 22.

[0047] When the mixed oil reacts with the catalyst, impurities will be separated. The impurities adhered to the catalyst and will affect the reaction of the catalyst with the subsequent oil. In order to reduce the influence of the impurity adhesion on the catalytic reaction, the outer cylinder 41 is matched with the tank body 1 for unidirectional rotation, and the rotating part 4 is matched with the bottom of the outer cylinder 41 for frictional rotation. When the rotating part 4 rotates in one direction, the outer cylinder 41 is driven to rotate synchronously by the action of friction. When the rotating part 4 rotates in the other direction, the rotation of the outer cylinder 41 is restricted. In the process of the reaction between the oil and the catalyst, the rotation direction of the rotating part 4 is adjusted at intervals so that the rotating part 4 rubs the catalyst to ensure the catalytic effect of the catalyst.

[0048] Specifically, the one-way rotation of the outer tube 41 can be limited by the cooperation between the tooth portion 411 and the spring block 412. The outer circumference of the outer tube 41 is evenly provided with tooth portions 411. The inner wall of the tank body 1 is elastically connected with a plurality of spring blocks 412. Each spring block 412 is respectively located between two adjacent tooth portions 411. The end faces of the spring block 412 opposite to the two adjacent tooth portions 411 are respectively a straight face and an inclined face. When the tooth portion 411 squeezes the inclined face of the spring block 412, the spring block 412 is pushed back to the inner wall of the tank body 1 and avoids the tooth portion 411.

[0049] A fuel reaction method comprises the following steps:

[0050] S1. Raw material preparation: crude oil is initially refined to remove most impurities and water in the oil to obtain semi-finished fuel oil suitable for hydrotreating;

[0051] S2, mixing, mixing the semi-finished fuel oil and hydrogen in a certain proportion and passing through the fuel oil reaction device provided by the present invention to mix and react;

[0052] S3, separation and purification, after the reaction is completed, the product is separated from the unreacted raw materials, and the unreacted raw materials are returned to the mixing step for mixing treatment, and the product is further purified and then cooled to room temperature for storage.

[0053] The fuel reaction device and method provided by the present invention promote the full mixing of oil and hydrogen, and improve the reaction efficiency of oil and hydrogen.

[0054] In the description of the present invention, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", "clockwise", "counterclockwise", "axial", "radial", "circumferential" and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the accompanying drawings, and are only for the convenience of describing the present invention and simplifying the description, and do not indicate or imply that the referred device or element must have a specific orientation, be constructed and operated in a specific orientation, and therefore should not be understood as limiting the present invention.

[0055] In addition, the terms "first" and "second" are used for descriptive purposes only and should not be understood as indicating or implying relative importance or implicitly indicating the number of the indicated technical features. Therefore, the features defined as "first" and "second" may explicitly or implicitly include at least one of the features. In the description of the present invention, the meaning of "plurality" is at least two, such as two, three, etc., unless otherwise clearly and specifically defined.

[0056] Although the embodiments of the present invention have been shown and described above, it is to be understood that the above embodiments are exemplary and are not to be construed as limitations of the present invention. A person skilled in the art may change, modify, replace and vary the above embodiments within the scope of the present invention.

Claims

1. A fuel reaction device, comprising a tank body, the tank body being provided with a liquid inlet and a liquid outlet, characterized in that: A mixing mechanism is provided in the tank body, and the mixing mechanism includes a guide member, a mixing member and an air inlet assembly. A mixing chamber is formed inside the guide member, and the mixing member is arranged in the mixing chamber. A spiral guide groove is formed between the guide member and the mixing member. The liquid inlet is communicated with the upper end of the guide groove, and an opening is provided at the bottom of the mixing chamber. The air intake assembly includes an air intake pipe, an air outlet channel and an air outlet pipe. The air outlet pipe is spirally arranged in the guide groove. A plurality of air outlet holes are evenly spaced on the air outlet pipe. A cavity is formed inside the mixing element. The air outlet end of the air outlet pipe is connected to the inside of the mixing element. One end of the air outlet channel is connected to the inside of the mixing element. The other end of the air outlet channel is connected to the air outlet pipe through a connecting structure, and the gas in the mixing element is introduced into the air outlet pipe. The mixing element is also provided with a circulation channel. One end of the circulation channel is connected to the guide groove, and the other end of the circulation channel is unidirectionally connected to the air outlet channel. A spiral plate 1 is provided on the inner side of the guide member, and a spiral plate 2 is provided on the outer side of the mixing member. The spiral directions of the spiral plates 1 and 2 are consistent. The mixing mechanism also includes a driving member, which drives the mixing member to rotate. The air outlet pipe rotates in coordination with the spiral plate 1, and the connecting structure is provided on the spiral plate 2. A blocking block is provided at the upper and lower ends of the guide groove, a groove body is provided on the spiral plate 2, the upper end of the blocking block is elastically connected to the groove body, the lower end of the blocking block abuts against the spiral plate 2, and a notch is provided in the middle of the blocking block. When the spiral plate 2 approaches the spiral plate 1, the blocking block is squeezed into the groove body and the notch is staggered with the guide groove.

2. The fuel reaction device according to claim 1, characterized in that: The connecting structure includes a connecting groove, a connecting piece and an elastic piece. The connecting groove is opened on the second spiral plate. The outlet end of the air outlet channel is connected to the connecting groove. The interior of the connecting piece is hollow. An air inlet is arranged at the upper end of the connecting piece. The upper end of the connecting piece extends into the connecting groove. The elastic piece is arranged in the connecting groove and abuts against the upper end of the connecting piece. The side wall of the connecting piece is slidingly and closedly connected to the connecting groove. The lower end of the connecting piece is connected to the air outlet pipe.

3. The fuel reaction device according to claim 2, characterized in that: The outer wall of the connecting piece is provided with a spiral groove, the connecting groove is provided with a sliding block which is slidably matched with the spiral groove, the lower end of the connecting piece is sealingly and rotatably connected with the air outlet, and a blade is fixed on the connecting piece.

4. The fuel reaction device according to claim 1, characterized in that: A reaction mechanism is also provided in the tank body, and the reaction mechanism is located at the lower side of the mixing mechanism. The reaction mechanism includes an outer cylinder and a rotating part. The outer cylinder and the tank body are unidirectionally rotated together. The rotating part is provided on the inner side of the outer cylinder. A gap for accommodating the catalyst is formed between the rotating part and the outer cylinder. A bottom plate is provided at the bottom of the outer cylinder, and a plurality of filter holes are provided on the bottom plate. The rotating part is fixed relative to the mixing part, and the rotating part and the bottom of the outer cylinder are frictionally rotated together.

5. The fuel reaction device according to claim 4, characterized in that: A tooth portion is provided on the outer circumference of the outer cylinder, and a spring block is elastically connected to the inner wall of the tank body. The spring block is located between two adjacent tooth portions. The end faces of the spring block opposite to the two adjacent tooth portions are a straight face and an inclined face respectively. When the tooth portion squeezes the inclined face of the spring block, the spring block is pushed back to the inner wall of the tank body and avoids the tooth portion.

6. The fuel reaction device according to claim 4, characterized in that: The upper end surface of the rotating member decreases in height in a direction away from the axial direction of the tank body.

7. The fuel reaction device according to claim 4, characterized in that: The width of the outer cylinder decreases from top to bottom, and the width of the rotating member decreases from top to bottom.

8. A fuel reaction method, characterized in that: The following steps are involved: S1. Raw material preparation: crude oil is initially refined to obtain semi-finished fuel oil; S2, mixing, mixing and reacting the semi-finished fuel oil and hydrogen through the fuel oil reaction device according to any one of claims 1 to 7; S3, separation and purification, after the reaction is completed, the product is separated from the unreacted raw materials, and the unreacted raw materials are returned to the mixing step for mixing treatment, and the product is further purified and then cooled to room temperature for storage.

Citation Information

Patent Citations

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    CN215693847U

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