Up-flow liquid hydro-conversion reactor

Abstract

The utility model relates to the technical field of reactors, and discloses an up-flow type liquid hydro-conversion reactor which is characterized in that an oil gas inlet is formed in the side end of the upper half part of a reactor main body, a cold hydrogen inlet is formed in the side end of the middle of the reactor main body, a plurality of fixing pieces are fixedly mounted on the upper surface of the reactor main body, and a motor is mounted among the fixing pieces; the lower end of the motor is connected with a rotating shaft, the other end of the rotating shaft penetrates through the surface of the reactor main body and extends into the reactor main body, a first rotating blade is installed in the middle of the rotating shaft, and a second rotating blade is installed at the lower end of the rotating shaft; the motor drives the rotating shaft and the first rotating blade and the second rotating blade mounted on the rotating shaft, so that materials in the reactor can be fully mixed, the uniformity of the materials in the reaction process is ensured, and the reaction efficiency and the product quality are improved.

Description

Technical Field

[0001] The utility model relates to the technical field of reactors, in particular to an upflow liquid hydrogenation conversion reactor. Background Art

[0002] An upflow liquid hydrogenation conversion reactor is a device with important applications in the chemical industry, especially in liquid reactions that require hydrogenation conversion. This reactor adopts an upflow design so that the reactant flow flows from bottom to top, thereby bringing a series of unique advantages. The upflow liquid hydrogenation conversion reactor has good adaptability to high-metal inferior raw materials. Since the reactant flow flows from bottom to top, the residence time of the raw materials in the reactor is relatively long, which is conducive to fully carrying out the hydrogenation conversion reaction. At the same time, this design can also effectively reduce the pressure loss in the reactor and improve the overall operating efficiency of the equipment. The upflow liquid hydrogenation conversion reactor has a high space utilization rate. Since the flow direction of the reactants is opposite to the gravity direction, the mass transfer and heat transfer effects inside the reactor are improved, which is conducive to accelerating the reaction speed and improving the conversion rate. In addition, the spatial layout inside the reactor is more reasonable, which can accommodate more catalyst beds and further improve the processing capacity of the equipment.

[0003] In the operation process of the existing reactor, the mixed gas generally has a large flow rate and is concentrated in the center of the reactor cross section and directly rushes onto the distribution plate, which can easily damage the portion of the distributor corresponding to the gas inlet, rendering the entire distributor unusable. The distributor needs to be replaced frequently, which not only increases production costs but also delays the desulfurization process, that is, reduces work efficiency. In addition, the mixed gas in the reactor cannot fully and quickly contact the catalyst, resulting in a low reaction rate. For this reason, we propose an upflow liquid hydrogenation conversion reactor. Utility Model Content

[0004] 1. Technical issues to be resolved

[0005] In view of the deficiencies in the prior art, the utility model provides an upflow liquid hydrogenation conversion reactor to solve the above-mentioned problems.

[0006] (II) Technical solution

[0007] To achieve the above-mentioned purpose, the utility model provides the following technical solutions: an upflow liquid hydrogenation conversion reactor, comprising a reactor body, a plurality of thermocouple nozzles are installed at the side end of the reactor body, one end of the thermocouple nozzles penetrates the inner wall of the reactor body, a feed port is installed at the side end of the upper half of the reactor body, and a cold hydrogen inlet is installed at the middle side end of the reactor body, and further comprising:

[0008] A fixing part, wherein a plurality of fixing parts are fixedly installed on the upper surface of the reactor body, a motor is installed in the middle of the plurality of fixing parts, and a support column is arranged on the surface of the plurality of fixing parts, the support column is movably connected with the motor, the lower end of the motor is connected with the rotating shaft, the other end of the rotating shaft passes through the surface of the reactor body and extends to the inside of the reactor body, a first rotating blade is installed in the middle of the rotating shaft, and a second rotating blade is installed at the lower end of the rotating shaft;

[0009] The structure for driving the rotating shaft to rotate comprises at least one set of stirring structures.

[0010] Preferably, a first baffle is arranged inside the reactor body corresponding to the lower end of the second rotating blade, and a second baffle is arranged inside the reactor body corresponding to the lower end of the first rotating blade.

[0011] Preferably, holes are arranged on the surfaces of the first partition plate and the second partition plate, and a funnel is installed at the lower end of the reactor body.

[0012] Preferably, a through hole is provided on the upper surface of the reactor body corresponding to the side end of the support column, a seal is installed inside the through hole, a ball valve is installed inside the seal, the upper end of the ball valve is connected to the hanging hole, and the lower end of the ball valve extends to the interior of the reactor body.

[0013] Preferably, a discharge port is installed at the center of the lower end of the reactor body, and one end of the discharge port penetrates the surface of the reactor body and is connected to the funnel.

[0014] Preferably, the thermocouple tube opening, feed inlet and cold hydrogen inlet are symmetrically arranged with the reactor body as the center.

[0015] (III) Beneficial effects

[0016] Compared with the prior art, the utility model provides an upflow liquid hydrogenation conversion reactor, which has the following beneficial effects:

[0017] 1. By driving the rotating shaft and the first rotating blade and the second rotating blade installed thereon by a motor, the materials inside the reactor can be fully mixed. This design ensures the uniformity of the materials during the reaction, thereby improving the reaction efficiency and product quality. The through holes arranged on the upper surface of the reactor and the seals installed inside, as well as the connection with the hanging hole through the ball valve, make the hoisting and sealing of the reactor convenient and quick, which not only improves the operability of the equipment, but also ensures the sealing during the reaction, preventing material leakage and environmental pollution.

[0018] 2. The discharge port at the center of the lower end of the reactor is connected to the internal funnel, so that the material can be discharged smoothly after the reaction is completed. The symmetrical layout of the feed port and the cold hydrogen inlet ensures that the material and the cooling medium can enter the reactor evenly, further improving the reaction efficiency and safety. This design also helps to reduce material residue and waste and reduce production costs. BRIEF DESCRIPTION OF THE DRAWINGS

[0019] Figure 1 It is a schematic diagram of the utility model;

[0020] Figure 2 It is a side sectional schematic diagram of the utility model;

[0021] Figure 3 This is a schematic diagram of the stirring structure of the utility model.

[0022] In the figure: 1. Reactor body; 2. Through hole; 3. Seal; 4. Hanging hole; 5. Fixing piece; 6. Support column; 7. Motor; 8. Thermocouple tube mouth; 9. Inlet; 10. Cold hydrogen inlet; 11. Outlet; 12. Support foot; 13. Ball valve; 14. First partition; 15. Second partition; 16. Leakage hole; 17. Funnel; 18. Rotating shaft; 19. First rotating blade; 20. Second rotating blade. DETAILED DESCRIPTION

[0023] The following will be combined with the drawings in the embodiments of the utility model to clearly and completely describe the technical solutions in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments in the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.

[0024] See also Figure 1-3 , an upflow liquid hydrogenation conversion reactor, comprising a reactor body 1, a plurality of thermocouple tube ports 8 are installed at the side end of the reactor body 1, one end of the thermocouple tube port 8 penetrates the inner wall of the reactor body 1, a feed port 9 is installed at the side end of the upper half of the reactor body 1, and a cold hydrogen inlet 10 is installed at the middle side end of the reactor body 1, and also includes: a fixing member, a plurality of fixing members 5 are fixedly installed on the upper surface of the reactor body 1, a motor 7 is installed in the middle of the plurality of fixing members 5, and a support column 6 is arranged on the surface of the plurality of fixing members 5, the support column 6 is movably connected to the motor 7, the lower end of the motor 7 is connected to a rotating shaft 18, the other end of the rotating shaft 18 passes through the surface of the reactor body 1 and extends to the interior of the reactor body 1, a first rotating blade 19 is installed in the middle of the rotating shaft 18, and a second rotating blade 20 is installed at the lower end of the rotating shaft 18, a structure for driving the rotating shaft 18 to rotate, which includes at least one group of stirring structures, the basic composition of the reactor.

[0025] Furthermore, a first baffle 14 is provided inside the reactor body 1 corresponding to the lower end of the second rotating blade 20, and a second baffle 15 is provided inside the reactor body 1 corresponding to the lower end of the first rotating blade 19, and the rotating blade scrapes the surface of the baffle while rotating.

[0026] Furthermore, holes 16 are provided on the surfaces of the first partition 14 and the second partition 15, and a funnel 17 is installed at the lower end of the reactor body 1, and liquid leaks from the holes 16 on the surfaces of the first partition 14 and the second partition 15, and the funnel 17 collects the fallen liquid.

[0027] Furthermore, a through hole 2 is provided on the upper surface of the reactor body 1 corresponding to the side end of the support column 6, a seal 3 is installed inside the through hole 2, a ball valve 13 is installed inside the seal 3, and the upper end of the ball valve 13 is connected to the hanging hole 4, and the lower end of the ball valve 13 extends to the interior of the reactor body 1, a catalyst is placed inside the ball valve 13, the ball valve 3 is movable and can be replaced, and the seal 3 keeps the ball valve 3 in a sealed state during installation.

[0028] Furthermore, a discharge port 11 is installed at the center of the lower end of the reactor body 1 , and one end of the discharge port 11 penetrates the surface of the reactor body 1 and is connected to a funnel 17 . The funnel 17 allows the fallen liquid to slide to the middle and then flow out from the discharge port 11 .

[0029] Furthermore, the thermocouple tube opening 8, the feed opening 9 and the cold hydrogen inlet 10 are symmetrically arranged with the reactor body 1 as the center. Two groups of the thermocouple tube opening 8, the feed opening 9 and the cold hydrogen inlet 10 are arranged and are symmetrically installed with respect to each other.

[0030] Working principle: The catalyst is placed inside the ball valve 13, and the ball valve 13 is installed on top of 1 through the seal 3. The liquid to be processed enters from the feed port 9, and the liquid flows through the ball valve 13. The liquid combines with the catalyst inside the ball valve 13, and the liquid reaches the surface of the first partition 14. The motor 7 is turned on, and the motor 7 drives the rotating shaft 18 to rotate. The rotating shaft 18 drives the first rotating blade 19 and the second rotating blade 20 to rotate. The first stirring blade 19 stirs the liquid and the catalyst. At the same time, the first stirring blade 19 pushes the liquid to fall from the hole 16, and the liquid falls to the surface of the second partition 15. Cold hydrogen enters from the cold hydrogen inlet 10, and the hydrogen is mixed with the liquid. The second rotating blade 20 stirs the liquid to make the liquid react fully. The liquid falls from the hole 16 on the surface of the second partition 15 to the inside of the funnel 17, and the liquid flows out from the discharge port 11.

[0031] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. An upflow liquid hydroconversion reactor, comprising a reactor body (1), a plurality of thermocouple tube ports (8) are installed at the side end of the reactor body (1), one end of the thermocouple tube port (8) penetrates the inner wall of the reactor body (1), a feed port (9) is installed at the side end of the upper half of the reactor body (1), and a cold hydrogen inlet (10) is installed at the middle side end of the reactor body (1), characterized in that: Also includes: A fixing member, wherein a plurality of fixing members (5) are fixedly mounted on the upper surface of the reactor body (1), a motor (7) is mounted in the middle of the plurality of fixing members (5), and a support column (6) is arranged on the surface of the plurality of fixing members (5), the support column (6) is movably connected to the motor (7), the lower end of the motor (7) is connected to a rotating shaft (18), the other end of the rotating shaft (18) passes through the surface of the reactor body (1) and extends into the interior of the reactor body (1), a first rotating blade (19) is mounted in the middle of the rotating shaft (18), and a second rotating blade (20) is mounted at the lower end of the rotating shaft (18); The structure is used to drive the rotating shaft (18) to rotate, and comprises at least one set of stirring structures.

2. An upflow liquid hydroconversion reactor according to claim 1, characterized in that: A first baffle (14) is arranged inside the reactor body (1) corresponding to the lower end of the second rotating blade (20), and a second baffle (15) is arranged inside the reactor body (1) corresponding to the lower end of the first rotating blade (19).

3. An upflow liquid hydroconversion reactor according to claim 2, characterized in that: Holes (16) are provided on the surfaces of the first baffle (14) and the second baffle (15), and a funnel (17) is installed at the lower end of the reactor body (1).

4. The upflow liquid hydroconversion reactor according to claim 1, characterized in that: A through hole (2) is provided on the upper surface of the reactor body (1) corresponding to the side end of the support column (6), a sealing member (3) is installed inside the through hole (2), a ball valve (13) is installed inside the sealing member (3), and the upper end of the ball valve (13) is connected to the hanging hole (4), and the lower end of the ball valve (13) extends into the interior of the reactor body (1).

5. The upflow liquid hydroconversion reactor according to claim 1, characterized in that: A discharge port (11) is installed at the center of the lower end of the reactor body (1), and one end of the discharge port (11) penetrates the surface of the reactor body (1) and is connected to the funnel (17).

6. The upflow liquid hydroconversion reactor according to claim 1, characterized in that: The thermocouple tube port (8), the feed port (9) and the cold hydrogen inlet (10) are symmetrically arranged with the reactor body (1) as the center.

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