A separation mechanism and a reaction kettle having the same

By designing the separation mechanism and pretreatment structure in the distillation reactor, the problem of incomplete steam condensation and solid particles mixed in is solved, and the purity and condensation efficiency of the extracted material are improved.

CN119034238BActive Publication Date: 2025-01-03GUANGDONG LINTON HEAVY IND CO LTD
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Patent Information

Application Number
CN202411499874.6
Authority / Receiving Office
CN · China
Patent Type
Patents(China)
Current Assignee / Owner
Filing Date
2024-10-25
Publication Date
2025-01-03
Estimated Expiration
2044-10-25

AI Technical Summary

Technical Problem

The steam in the existing distillation reactor needs to be liquefied through an external condenser, but the steam flow rate is too large or the internal surface area of ​​the condenser is not completely condensed, and the presence of solid impurities in the reactants leads to insufficient purity of the extracted material.

Method used

A separation mechanism is designed, including a separation housing, a separation unit, a pretreatment structure, to separate solid particles in the steam by a separation unit and a secondary separation assembly in the separation housing, and to use first and second stages in the pretreatment structure The second guide plate is pre-treated to ensure complete condensation of the steam.

Benefits of technology

It effectively avoids the problem of incomplete steam condensation, improves the purity of the extracted material, prevents solid particles from sticking to the inner wall of the pretreatment structure, extends the service life of the equipment and improves the condensation efficiency.

✦ Generated by Eureka AI based on patent content.

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Abstract

The present invention provides a separation mechanism and a reactor with the mechanism, belonging to the technical field of reactor separation devices. It comprises a separation shell; a separation structure, which is located in the separation shell and connected to the separation shell, and the separation structure is used to separate solid particles in the vaporized separation steam inside the reactor; the separation structure comprises a partition unit connected to the bottom of the separation shell, and the partition unit is connected to a secondary separation component. The present invention sets a pretreatment structure and a separation structure. The pretreatment structure is used to condense and pretreat the material steam, which greatly alleviates the condensation pressure of the external condenser and avoids the incomplete condensation of the steam during the distillation process. The separation structure is used to separate the solid particles in the material steam that is vaporized and separated inside the lower kettle body, so as to avoid the solid particles from mixing with the distilled steam, and the purity of the distilled material after condensation is insufficient.
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Description

Technical Field

[0001] The invention relates to the technical field of reactor separation devices, and in particular to a separation mechanism and a reactor with the mechanism. Background Art

[0002] The distillation reactor is a device used for the distillation process, commonly used in the chemical, pharmaceutical and food industries. It combines the functions of reaction and distillation, and can simultaneously separate and purify products during the reaction process. The function of the distillation reactor is to vaporize the liquid to be distilled and provide the necessary amount of rising steam in the tower. The types of distillations include jacketed, coiled tube and shell-and-tube types. Jacketed and coiled tube types are mostly used in small-scale production due to their smaller heating area, while shell-and-tube distillations are mostly used in large-scale production.

[0003] The steam of the existing distillation reactor needs to be liquefied through an external condenser. When the steam flow is too large or dirt accumulates on the internal surface of the condenser, the condenser will not condense completely. At the same time, if there are solid impurities or undissolved solids in the reactants, the steam formed by the reactants will carry these solid particles, resulting in insufficient purity of the extracted material. Therefore, the present application provides a separation mechanism and a reactor with the mechanism to meet the needs. Summary of the invention

[0004] The technical problem to be solved by the present invention is to provide a separation mechanism and a reactor with the mechanism to solve the problem that the steam of the existing distillation reactor needs to be liquefied through an external condenser. When the steam flow is too large or dirt accumulates on the internal surface of the condenser, the condenser will not condense completely. At the same time, if there are solid impurities or undissolved solids in the reactants, the steam formed by the reactants will carry these solid particles, resulting in the problem of insufficient purity of the extracted material.

[0005] The present invention solves the above technical problems through the following technical solutions, which include:

[0006] Separate the shell;

[0007] A separation structure is located in the separation shell and connected to the separation shell, and is used to separate solid particles in the gasified separation steam inside the reactor; the separation structure includes a separation unit connected to the bottom of the separation shell, and the separation unit is connected to a secondary separation component; a pretreatment structure is located at the top of the separation shell, and is connected to the separation shell, and is used to condense and pretreat the material steam separated by the separation structure.

[0008] Preferably, the interior of the separation shell is hollow, one end of the separation shell is provided with an outward-turned mounting opening penetrating therethrough, an outward-turned ring piece is fixedly connected to the outward-turned mounting opening, and the top of the separation shell away from the outward-turned mounting opening is provided with an outlet penetrating therethrough.

[0009] Preferably, the separation unit includes a bottom plate fixedly connected to the bottom of the separation shell, a group of air guide modules are fixedly connected to one side of the bottom plate, the air guide module is composed of a plurality of diverter plates, the spacing between each two adjacent diverter plates near the outward-turned mounting port is greater than the spacing near the guide port, the two outermost diverter plates of the air guide module are fixedly connected with an outward-turned partition near the outward-turned mounting port, a plurality of protrusions with uniform spacing are fixedly connected to the two side surfaces of the diverter plates, and the protrusions on the opposite surfaces of each two diverter plates are staggered, a separation mounting groove is provided on the surface of the diverter plate near each two adjacent protrusions, and a first-level separation unit is connected to the separation mounting groove.

[0010] Preferably, the primary separation unit includes a primary separation plate fixedly connected to the surface wall of the separation mounting groove, a plurality of evenly arranged columns are fixedly connected to one side of the primary separation plate, and a plush pad is laid on the surface of the primary separation plate near the bottom of the columns.

[0011] Preferably, the secondary separation component includes a guide block fixedly connected to one side of the bottom plate, a steam guide groove is provided on the side of the guide block close to the diverter plate, and a diverter plate groove adapted to the diverter plate is provided on one side of the guide block; the steam guide groove is composed of a square groove and a fan-shaped groove that are interconnected, the square groove is opened at the bottom end of the guide block, and the fan-shaped groove is opened at the top end of the guide block, a secondary separation unit is connected to the square groove, and the fan-shaped groove corresponds to the position of the guide outlet; and also includes a connecting unit for fixedly connecting the secondary separation unit to the square groove.

[0012] Preferably, the secondary separation unit includes a secondary separation plate fixedly connected to the two diagonals of the square groove, the secondary separation plate is provided with a plurality of evenly arranged separation holes, and the inner walls of the separation holes are connected to the collecting units; the connecting unit includes a clamping strip fixedly connected to both sides of the secondary separation plate, the inner walls of both sides of the square groove are provided with clamping slots matched with the clamping strips, and the bottom of the square groove is provided with a placement slot matched with the bottom end of the secondary separation plate; the collecting unit includes a collecting ring fixedly connected to the inner surface wall of the separation hole, one side of the collecting ring is fixedly connected with a collecting bend pipe, the end of the collecting bend pipe away from the collecting ring is fixedly connected with a stop pipe, the collecting ring is connected with the collecting bend pipe, and the collecting bend pipe is connected with the stop pipe.

[0013] Preferably, the pretreatment structure includes an inlet pipe fixedly connected to the separation shell, one end of the inlet pipe passes through the outlet and extends into the separation shell, the other end of the inlet pipe is fixedly connected to a pre-condensing pipe, one end of the pre-condensing pipe away from the inlet pipe is fixedly connected to a tail pipe, and the bottom of the tail pipe is fixedly connected to an outlet pipe.

[0014] Preferably, the inner wall of the pre-condensing tube is fixedly connected with a first-level guide plate and a second guide plate in sequence from the inlet pipe to the tail pipe, and air outlets are provided on the second guide plate and the first-level guide plate. The first-level guide plate is fixed to the inner wall at the bottom end and the side of the bottom end of the pre-condensing tube, and the second guide plate is fixed to the inner wall at the top end and the side of the top end of the pre-condensing tube. The pre-condensing tube is provided with an external contact groove at the position corresponding to the second guide plate.

[0015] Preferably, the first-level guide plate is composed of a first guide section with an outward convex shape and an anti-backflow section with an outward-turned shape, one end of the first guide section is fixedly connected to the inner surface wall of the pre-condensing tube, and the other end of the first guide section is fixedly connected to the anti-backflow section; the second guide plate is composed of a second guide section, a connecting section and a surface-increasing section, the second guide section and the surface-increasing section are both concave structures, the connecting section is a convex structure, the two ends of the connecting section are fixedly connected to the second guide section and the surface-increasing section respectively, and the other ends of the second guide section and the surface-increasing section are both fixedly connected to the inner wall of the pre-condensing tube; the first-level guide plate and the second guide plate are provided with a plurality of annularly distributed guide grooves on the opposing surfaces.

[0016] The present invention also proposes a reaction kettle, comprising a lower kettle body, an upper kettle body and a driving device, wherein the top of the lower kettle body is fixedly connected to the upper kettle body, the top of the upper kettle body is fixedly connected to the driving device, the output end of the driving device passes through the upper kettle body and extends to the interior of the lower kettle body, the output end of the driving device is fixedly connected to the first stirring blade, the second stirring blade and the third stirring blade in sequence, and also includes the separation mechanism described above, the separation shell is fixedly connected to the inner surface wall of the upper kettle body, the upper kettle body is provided with an inlet hole, and the outer wall of the inlet pipe is fixedly connected to the inner wall of the inlet hole.

[0017] Compared with the prior art, the present invention has at least the following beneficial effects:

[0018] In the above scheme, a pretreatment structure and a separation structure are set up. The pretreatment structure is used to perform condensation pretreatment on the material vapor, which greatly alleviates the condensation pressure of the external condenser and avoids incomplete condensation of the steam during the distillation process. The separation structure is used to separate the solid particles in the material vapor separated by gasification inside the lower kettle body to avoid the solid particles from mixing with the distilled steam, which may result in insufficient purity of the distilled material after condensation. At the same time, it can prevent the solid particles from sticking to the inner wall of the pretreatment structure, which may cause the inner wall of the pretreatment structure to be blocked or accumulate dirt for a long time, affecting the heat exchange effect and causing a decrease in condensation efficiency.

[0019] By setting up diverter plates and a primary separation unit, several diverter plates separate several channels to divert the steam entering the separation shell, and the protrusions are used to guide the passing steam so that it flows in a wave shape in the channel between every two diverter plates, and then the primary separation unit is used to perform initial separation on the solid particles passing through the steam.

[0020] By arranging a primary guide plate and a second guide plate, a large amount of steam flowing from the primary guide plate to the second guide plate forms turbulence on the surface of the second guide plate, which reduces the steam flow rate and makes the steam entering between the primary guide plate and the second guide plate mix more evenly, so that part of the steam is pre-condensed into liquid on the surface of the second guide plate. The primary guide plate and the second guide plate are both integrally formed by die-casting, and the manufacturing process is simple and low-cost.

[0021] The external contact groove is provided so that the second guide plate is in direct contact with the external air, and the second guide plate is further cooled by external blowing, thereby increasing the condensation efficiency of the second guide plate. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] The accompanying drawings, which are incorporated herein and constitute a part of the specification, illustrate embodiments of the invention and, together with the description, further serve to explain the principles of the invention and to enable those skilled in the relevant art to make and use the invention.

[0023] Figure 1 It is a schematic diagram of the three-dimensional structure of the separation mechanism;

[0024] Figure 2 It is a schematic diagram of the three-dimensional structure of the separation mechanism and the reactor assembly having the mechanism;

[0025] Figure 3 It is a schematic diagram of a three-dimensional structure of a separation mechanism and a reactor having the mechanism;

[0026] Figure 4 A schematic diagram of the three-dimensional structure of the upper kettle body, pretreatment structure and separation structure;

[0027] Figure 5It is a schematic diagram of the three-dimensional structure of the separation structure;

[0028] Figure 6 The schematic diagram of the three-dimensional structure is a separation structure decomposition;

[0029] Figure 7 for Figure 6 Schematic diagram of the three-dimensional structure at A in the middle;

[0030] Figure 8 A schematic diagram of a three-dimensional structure cut out for the separation structure;

[0031] Fig. 9 Schematic diagram of the three-dimensional structure of the guide block;

[0032] Fig.10 It is a schematic diagram of the three-dimensional structure of the secondary separation unit;

[0033] Fig.11 It is a schematic diagram of the three-dimensional structure of the collection unit;

[0034] Fig.12 It is a schematic diagram of the three-dimensional structure of the pretreatment structure;

[0035] Fig.13 A schematic diagram of a three-dimensional structure cut out for a pretreatment structure;

[0036] Fig.14 for Fig.13 Schematic diagram of the three-dimensional structure at B in the middle;

[0037] Fig.15 for Fig.13 Schematic diagram of the three-dimensional structure at C in the middle;

[0038] Fig.16 It is a schematic diagram of the three-dimensional structure of the first-stage guide vane and the second guide vane.

[0039] Reference numerals:

[0040] 1. Lower kettle body; 2. Upper kettle body; 3. Driving device; 31. First stirring blade; 32. Second stirring blade; 33. Third stirring blade; 4. Pretreatment structure; 41. Pre-condensing tube; 411. External contact groove; 42. Inlet pipe; 43. Outlet pipe; 44. Tail pipe; 45. Second guide vane; 451. Guide groove; 452. Second guide section; 453. Connecting section; 454. Surface increase section; 46. Primary guide vane; 461. First guide section; 462. Anti-backflow section; 5. Separation structure; 51. Separation shell; 511. Outward-turned ring piece; 512. Outward-turned mounting port; 513. Guide outlet; 52. Separation unit; 521, bottom plate; 522, diverter plate; 5221, separation installation groove; 523, partition; 53, secondary separation assembly; 531, guide block; 5312, card slot; 5313, placement slot; 5314, diverter plate slot; 5315, steam guide slot; 5316, fan-shaped slot; 5317, square slot; 532, secondary separation unit; 5321, secondary separation plate; 5322, card strip; 5323, separation hole; 54, collection unit; 541, collection ring; 542, collection elbow; 543, stop pipe; 6, primary separation unit; 61, primary separation plate; 62, column; 63, plush pad.

[0041] As shown in the figure, in order to clearly implement the structure of the embodiment of the present invention, specific structures and devices are marked in the figure, but this is only for illustrative purposes and is not intended to limit the present invention to the specific structure, device and environment. According to specific needs, ordinary technicians in this field can adjust or modify these devices and environments. DETAILED DESCRIPTION

[0042] The following is a detailed description of a separation mechanism and a reactor having the mechanism provided by the present invention in conjunction with the accompanying drawings and specific embodiments. At the same time, it is explained here that in order to make the embodiments more detailed, the following embodiments are the best and preferred embodiments, and those skilled in the art may also adopt other alternatives to implement some known technologies; and the accompanying drawings are only for a more specific description of the embodiments, and are not intended to specifically limit the present invention.

[0043] It should be noted that the references to "one embodiment", "embodiment", "exemplary embodiments", "some embodiments" and the like in the specification indicate that the embodiments described may include specific features, structures or characteristics, but not every embodiment may include the specific features, structures or characteristics. In addition, when a specific feature, structure or characteristic is described in conjunction with an embodiment, it should be within the knowledge of a person skilled in the art to implement such feature, structure or characteristic in conjunction with other embodiments (whether or not explicitly described).

[0044] In general, a term can be understood, at least in part, from its use in context. For example, depending, at least in part, on the context, the term "one or more" as used herein can be used to describe any feature, structure, or characteristic in the singular sense, or can be used to describe a combination of features, structures, or characteristics in the plural sense. Additionally, the term "based on" can be understood as not necessarily intended to convey an exclusive set of factors, but can instead, depending, at least in part, on the context, allow for the presence of other factors that are not necessarily explicitly described.

[0045] It will be understood that the meanings of “on,” “over,” and “above” in the present invention should be interpreted in the broadest manner, so that “on” not only means “directly on” something, but also includes the meaning of being “on” something with intervening features or layers therebetween, and “on” or “over” not only means “on” or “above” something, but also includes the meaning of being “on” or “above” something with no intervening features or layers therebetween.

[0046] Additionally, spatially relative terms such as "under," "beneath," "lower," "above," "upper," and the like may be used herein for descriptive convenience to describe the relationship of one element or feature to another element or features, as shown in the accompanying drawings. Spatially relative terms are intended to encompass different orientations of the device in use or operation in addition to the orientation depicted in the accompanying drawings. The device may be oriented in other ways, and the spatially relative descriptors used herein may be similarly interpreted accordingly.

[0047] like Figures 1 to 6 As shown, an embodiment of the present invention provides a separation mechanism, including a separation shell 51; a separation structure 5, which is located in the separation shell 51 and is connected to the separation shell 51, and the separation structure 5 is used to separate solid particles in the gasified separation steam inside the reactor to avoid mixing of the solid particles with the distilled steam, and the purity of the distilled material after condensation is insufficient. At the same time, it can prevent the solid particles from sticking to the inner wall of the pretreatment structure 4, causing the inner wall of the pretreatment structure 4 to be blocked or accumulate dirt for a long time, affecting the heat exchange effect, and causing the condensation efficiency to decrease; the separation structure 5 includes a separation unit 52 connected to the bottom of the separation shell 51, and the separation unit 52 is connected to a secondary separation component 53; the pretreatment structure 4 is located at the top of the separation shell 51, and the pretreatment structure 4 is connected to the separation shell 51, and the pretreatment structure 4 is used to condense and pretreat the material steam separated by the separation structure 5, which greatly relieves the condensation pressure of the external condenser and avoids the situation where the steam is not completely condensed during the distillation process.

[0048] During operation, the distillation raw materials are discharged into the lower kettle body 1 from the raw material inlet at the top of the upper kettle body 2, and then the lower kettle body 1 is heated. The various raw materials are stirred and mixed by the second stirring blade 32 and the third stirring blade 33. By utilizing the principle of different boiling points of different raw materials, the material with a lower boiling point in the lower kettle body 1 forms steam, which is driven by the first stirring blade 31 and enters the separation structure 5 for separation of solid particles. The steam separated by the separation structure 5 enters the pretreatment structure 4 for pretreatment.

[0049] like Figures 2 to 6 and Figure 8 As shown, the interior of the separation shell 51 is hollow, and the separation shell 51 with a hollow interior provides installation space for the separation unit 52 and the secondary separation component 53. One end of the separation shell 51 is provided with an outward-turned installation port 512 that penetrates the interior thereof, and an outward-turned ring piece 511 is fixedly connected to the outward-turned installation port 512. The separation shell 51 with a hollow interior is used to guide the distilled steam, and the outward-turned installation port 512 is used to provide an installation position for the outward-turned ring piece 511. At the same time, the interior of the separation shell 51 is connected to the interior of the upper kettle body 2 through the outward-turned installation port 512, and more steam can be introduced through the outward-turned ring piece 511. The top of the separation shell 51 away from the outward-turned installation port 512 is provided with an outflow port 513 that penetrates the interior thereof, and the outflow port 513 is used to guide the steam after separation in the separation shell 51.

[0050] The partition unit 52 is used to divert the steam entering the separation shell 51, so that the steam passing through the partition unit 52 can contact with the primary separation unit 6 more thoroughly. The partition unit 52 includes a bottom plate 521 fixedly connected to the bottom of the separation shell 51, the bottom plate 521 provides an installation position for the air guide module, and seals the bottom of the separation shell 51. A group of air guide modules is fixedly connected to one side of the bottom plate 521. The air guide module is composed of a plurality of diverter plates 522 arranged in an array. The plurality of diverter plates 522 separate a plurality of channels from the inside of the separation shell 51, so that the steam entering the separation shell 51 is diverted. The distance between each two adjacent diverter plates 522 near the end of the outward-turned installation port 512 is greater than the distance near the end of the guide outlet 513. The two outermost diverter plates 522 of the air guide module are fixedly connected with an outward-turned partition plate 523 near the end of the outward-turned installation port 512. The partition plate 523 fits the surface of the outward-turned ring sheet 511, so that the steam entering The steam entering the separation shell 51 will not flow out through the gap between the partition 523 and the outward-turned ring sheet 511. The two side surfaces of the diverter plate 522 are fixedly connected with a plurality of protrusions with uniform spacing. The protrusions are used to guide the passing steam so that it flows in a wave-like manner in the channel between every two diverter plates 522, thereby increasing the contact with the primary separation unit 6. The protrusions on the opposite surfaces of every two diverter plates 522 are staggered with each other. A separation mounting groove 5221 is provided on the surface of the diverter plate 522 near every two adjacent protrusions. The separation mounting groove 5221 is used to provide an installation position for the primary separation unit 6. The primary separation unit 6 is connected to the separation mounting groove 5221. The primary separation unit 6 is used to initially separate solid particles passing through the steam. A secondary separation component 53 is connected to the side of the bottom plate 521 near the guide outlet 513. The secondary separation component 53 is used to further separate solid particles passing through the steam.

[0051] When the distilled steam enters the separation shell 51 through the outward-turned ring sheet 511, the steam is intercepted by the partition 523, so that it moves in the direction of the air guide module. The steam in the flow process flows in a wave shape in the channel between every two diverter plates 522 under the guidance of the protrusions. During the flow, it contacts the primary separation unit 6 for initial separation. After the initial separation, the steam flows to the secondary separation component 53 for further separation, until it flows from the outlet 513 to the pretreatment structure 4 after separation.

[0052] like Figures 6 to 11As shown, the primary separation unit 6 includes a primary separation plate 61 fixedly connected to the surface wall of the separation installation groove 5221, the primary separation plate 61 is used to provide installation space for the column 62 and the plush pad 63, and can be more conveniently fixed on the separation installation groove 5221 through the primary separation plate 61, one side of the primary separation plate 61 is fixedly connected with a plurality of evenly arranged columns 62, the columns 62 are used to intercept the steam and slow it down so that it can fully contact the surface of the plush pad 63, the surface of the primary separation plate 61 is paved with a plush pad 63 near the bottom of the column 62, and the surface of the plush pad 63 is provided with dense high-temperature resistant plastic plush, which can intercept solid particles in the steam, and the secondary separation component 53 includes a guide block 531 fixedly connected to one side of the bottom plate 521, the outer wall of the guide block 531 is tightly fitted with the separation shell 51, and a steam guide groove 5315 is provided on the side of the guide block 531 close to the diverter plate 522, and the steam guide groove 5315 is used The steam passing through the channel between the two diverter plates 522 is guided so that it is secondary separated and guided to the outlet 513 at the top of the separation shell 51. A diverter plate groove 5314 adapted to the diverter plate 522 is provided on one side of the guide block 531. The diverter plate groove 5314 is used to make the guide block 531 fit closely with one end of the diverter plate 522. The steam guide groove 5315 is composed of a square groove 5317 and a fan-shaped groove 5316 connected to each other. The square groove 5317 is connected to the fan-shaped groove 5316. It is opened at the bottom end of the guide block 531, and the fan-shaped groove 5316 is opened at the top end of the guide block 531. Every two diverter plates 522 are sealed near the top of the fan-shaped groove 5316, so that the steam can only enter the square groove 5317. The steam flowing out from the channel between the diverter plates 522 enters the secondary separation unit 532 in the square groove 5317 at the first time, and after separation by the secondary separation unit 532, it flows along the arc surface of the fan-shaped groove 5316 to the guide outlet 513.

[0053] The square groove 5317 is connected with a secondary separation unit 532, and the fan-shaped groove 5316 corresponds to the position of the outlet 513; it also includes a connecting unit for fixing the secondary separation unit 532 to the square groove 5317, and the secondary separation unit 532 includes a secondary separation plate 5321 fixedly connected to two diagonal portions of the square groove 5317, and a plurality of evenly arranged separation holes 5323 are opened on the secondary separation plate 5321, and the separation holes 5323 are oriented to flow out steam from the channel between the diverter plate 522. The flow direction of the square groove 5317 is parallel to that of the secondary separation plate 5321, so that the outflowing steam can directly enter the separation hole 5323. The inner wall of the separation hole 5323 is connected to a collecting unit 54, and the collecting unit 54 is used to separate and collect solid particles inside the steam; the connecting unit includes a clamping strip 5322 fixedly connected to both sides of the secondary separation plate 5321, and the inner walls of both sides of the square groove 5317 are provided with a clamping slot 5312 adapted to the clamping strip 5322, and the bottom of the square groove 5317 is provided with a placement slot adapted to the bottom end of the secondary separation plate 5321 5313, when installing the secondary separation plate 5321, the bottom of the secondary separation plate 5321 is inserted into the placement groove 5313, and then the secondary separation plate 5321 is pressed, and the clamping strips 5322 on both sides of the secondary separation plate 5321 are inserted into the clamping groove 5312, so as to limit and fix the secondary separation plate 5321. The collecting unit 54 includes a collecting ring 541 fixedly connected to the inner surface wall of the separation hole 5323, and a collecting elbow 542 is fixedly connected to one side of the collecting ring 541, and the collecting elbow 542 is away from the collecting ring 54 1 is fixedly connected with a stop pipe 543, the collecting ring 541 is connected with the collecting elbow 542, and the collecting elbow 542 is connected with the stop pipe 543. When the collecting unit 54 is working, the steam enters the collecting ring 541 from the separation hole 5323, and then enters the stop pipe 543 along the collecting elbow 542 connected with the collecting ring 541, until it enters the square groove 5317, reducing the flow speed of the steam, so that the steam does not have enough kinetic energy to drive the solid particles, so that the solid particles fall under the action of gravity.

[0054] like Fig.12 and Fig.13As shown, the pretreatment structure 4 includes an inlet pipe 42 fixedly connected to the upper kettle body 2, one end of the inlet pipe 42 passes through the upper kettle body 2 and extends to the outlet 513, the steam flowing out of the outlet 513 enters the pre-condensing pipe 41 along the inlet pipe 42, the other end of the inlet pipe 42 is fixedly connected to the pre-condensing pipe 41, the pre-condensing pipe 41 is used to condense the steam entering the pre-condensing pipe 41, the end of the pre-condensing pipe 41 away from the inlet pipe 42 is fixedly connected to the tail pipe 44, the bottom of the tail pipe 44 is fixedly connected to the outlet pipe 43, the tail pipe 44 It is used to collect the liquid after the pre-condensation treatment. The outlet pipe 43 is used to introduce the steam and liquid after the pre-condensation treatment into the external condenser. The inner wall of the pre-condensation pipe 41 is fixedly connected with a first-level guide plate 46 and a second guide plate 45 in sequence from the inlet pipe 42 to the tail pipe 44. The first-level guide plate 46 is used to guide the steam entering the pre-condensation pipe 41 to flow to the surface of the second guide plate 45. The second guide plate 45 and the first-level guide plate 46 are all provided with air outlets. The air outlet on the first-level guide plate 46 The opening angle is 120°, so that the steam can flow quickly and in large quantities to the second guide vane 45. The opening angle of the air outlet on the second guide vane 45 is 90°. A large amount of steam flows to the second guide vane 45 through the first-level guide vane 46, and forms turbulence on the surface of the second guide vane 45, which reduces the steam flow rate and makes the steam entering between the first-level guide vane 46 and the second guide vane 45 more evenly mixed. Part of the steam is pre-condensed into liquid on the surface of the second guide vane 45. The first-level guide vane 46 is fixed to the bottom end and bottom end of the pre-condensing pipe 41. The inner wall of the end side, the second guide vane 45 is fixed to the top of the pre-condensing tube 41 and the inner wall of the top side, and the pre-condensing tube 41 and the second guide vane 45 are provided with an outer contact groove 411 at the corresponding position. The opened outer contact groove 411 allows the second guide vane 45 to directly contact the external air, and at the same time cooperate with the external blowing to further cool the second guide vane 45, which can increase the condensation efficiency of the second guide vane 45. The first-stage guide vane 46 and the second guide vane 45 are both integrally formed by die-casting, and the manufacturing process is simple and low-cost.

[0055] like Figures 13 to 16As shown, the first-level guide plate 46 is composed of a first guide section 461 with an outward convex shape and an anti-backflow section 462 with an outward eversion shape. One end of the first guide section 461 is fixedly connected to the inner surface wall of the pre-condensing tube 41, and the other end of the first guide section 461 is fixedly connected to the anti-backflow section 462; the second guide plate 45 is composed of a second guide section 452, a connecting section 453 and a surface-increasing section 454. The surface-increasing section 454 is used to increase the contact area between the second guide plate 45 and the outside. The second guide section 452 and the surface-increasing section 454 are both concave structures, and the connecting section 453 is a convex structure. The two ends of the connecting section 453 are fixedly connected to the second guide section 452 and the surface-increasing section 454 respectively, and the other ends of the second guide section 452 and the surface-increasing section 454 are both fixedly connected to the inner wall of the pre-condensing tube 41; the first-level guide plate 46 and the second guide plate 45 are both provided with a plurality of guide grooves 451 distributed in an annular shape on the opposing surfaces.

[0056] The steam enters the pre-condensing tube 41 from the inlet pipe 42, and first contacts the first guide section 461. The steam is guided by the arc surface of the first guide section 461, and is directed from the air outlet to the surface of the second guide section 452, so that the steam flows from the outside to the inside of the surface of the second guide section 452. Since the second guide section 452 is in contact with the outside and the surface temperature of the second guide section 452 is low under the operation of external blowing, the steam condenses into liquid by contacting the surface of the second guide section 452, and flows along the guide groove 451 to the bottom of the inner wall of the pre-condensing tube 41. The temperature of the uncondensed steam will decrease, and under the guidance of the second guide section 452, it will flow back to the outer surface of the first guide section 461, and under the guidance of the anti-backflow section 462, it will flow to the air outlet of the second guide section 452, and then enter the tail pipe 44 along the pre-condensing tube 41, and finally flow to the outlet pipe 43.

[0057] The present invention also provides a technical solution: a reaction kettle, such as Figures 1 to 16 As shown, it includes a lower kettle body 1, an upper kettle body 2 and a driving device 3, the top of the lower kettle body 1 is fixedly connected to the upper kettle body 2, the top of the upper kettle body 2 is fixedly connected to the driving device 3, the output end of the driving device 3 passes through the upper kettle body 2 and extends to the interior of the lower kettle body 1, the output end of the driving device 3 is fixedly connected to the first stirring blade 31, the second stirring blade 32 and the third stirring blade 33 in sequence, the separation shell 51 is fixedly connected to the inner surface wall of the upper kettle body 2, one side and the top of the separation shell 51 are adapted to the inner surface wall and the top of the upper kettle body 2, an inlet hole is opened on the upper kettle body 2, and the outer wall of the inlet pipe 42 is fixedly connected to the inner wall of the inlet hole.

[0058] The lower kettle body 1 has an upper kettle body 2 fixedly connected to the top of the lower kettle body 1, and a driving device 3 fixedly connected to the top of the upper kettle body 2. The output end of the driving device 3 passes through the upper kettle body 2 and extends to the interior of the lower kettle body 1. The upper kettle body 2, the lower kettle body 1 and the driving device 3 are prior art. The output end of the driving device 3 is fixedly connected with a first stirring blade 31, a second stirring blade 32 and a third stirring blade 33 in sequence. The third stirring blade 33 is arranged in parallel with the vertical direction of the output end. The mixed material at the bottom of the lower kettle body 1 is driven to stir by the third stirring blade 33, so that the mixed material is stirred more evenly. The second stirring blade 32 is arranged at an angle of 30° to the vertical direction of the output end, and is used to drive the mixed material at the top of the lower kettle body 1 to move to the bottom of the lower kettle body 1 during the stirring process. The deflection angle of the first stirring blade 31 is opposite to that of the second stirring blade 32, and is used to drive the steam evaporated by heating the lower kettle body 1 toward the upper kettle body 2, so that the steam quickly enters the separation structure 5.

[0059] The working principle of the technical solution provided by the present invention is as follows: when working, the distillation raw materials are discharged into the lower kettle body 1 from the raw material inlet at the top of the upper kettle body 2, and then the lower kettle body 1 is heated, and the various raw materials are stirred and mixed by the second stirring blade 32 and the third stirring blade 33. By utilizing the principle that different raw materials have different boiling points, the material with a lower boiling point in the lower kettle body 1 forms steam, and enters the separation structure 5 driven by the first stirring blade 31 to separate the solid particles.

[0060] When the distilled steam enters the separation shell 51 through the outward-turned ring sheet 511, the steam is intercepted by the partition 523, so that the steam moves in the direction of the wind guide module. The steam in the flow process flows in a wave shape in the channel between every two diverter plates 522 under the guidance of the protrusion. During the flow, it contacts the primary separation unit 6 for initial separation. The steam passes through the column 62 to intercept the steam and slow it down. The steam can fully contact the surface of the plush pad 63 to intercept the solid particles in the steam. The steam passing through the channel between the diverter plates 522 enters the square groove 5317 through the secondary separation plate 5321. When passing through the secondary separation plate 5321, the steam enters the collecting ring 541 from the separation hole 5323, and then enters the stop pipe 543 along the collecting bend 542 connected to the collecting ring 541, until it enters the square groove 5317. After separation by the secondary separation unit 532, it flows toward the outlet 513 along the arc surface of the fan-shaped groove 5316.

[0061] The steam enters the pre-condensing tube 41 from the inlet pipe 42, and first contacts the first guide section 461. The steam is guided by the arc surface of the first guide section 461, and is directed from the air outlet to the surface of the second guide section 452, so that the steam flows from the outside to the inside of the surface of the second guide section 452. Since the second guide section 452 is in contact with the outside and the surface temperature of the second guide section 452 is low under the operation of external blowing, the steam condenses into liquid by contacting the surface of the second guide section 452, and flows along the guide groove 451 to the bottom of the inner wall of the pre-condensing tube 41. The temperature of the uncondensed steam will decrease, and under the guidance of the second guide section 452, it will flow back to the outer surface of the first guide section 461, and under the guidance of the anti-backflow section 462, it will flow to the air outlet of the second guide section 452, and then enter the tail pipe 44 along the pre-condensing tube 41, and finally flow to the outlet pipe 43.

[0062] The present invention covers any substitution, modification, equivalent method and scheme made on the essence and scope of the present invention. In order to make the public have a thorough understanding of the present invention, specific details are described in detail in the following preferred embodiments of the present invention, but those skilled in the art can fully understand the present invention without the description of these details. In addition, in order to avoid unnecessary confusion about the essence of the present invention, well-known methods, processes, procedures, components and circuits are not described in detail.

[0063] The above is only a preferred embodiment of the present invention. It should be pointed out that for ordinary technicians in this technical field, several improvements and modifications can be made without departing from the principle of the present invention. These improvements and modifications should also be regarded as the scope of protection of the present invention.

Claims

1. A separation mechanism, characterized in that: include: Separate the housing (51); A separation structure (5) is located inside the separation shell (51), and the separation structure (5) is connected to the separation shell (51), and the separation structure (5) is used to separate solid particles in the gasified separation steam inside the reactor; The separation structure (5) comprises a separation unit (52) connected to the interior of the separation housing (51), and a secondary separation component (53) is connected to the separation unit (52); A pretreatment structure (4) is located on the top of the separation shell (51), the pretreatment structure (4) is connected to the separation shell (51), and the pretreatment structure (4) is used to condense and pretreat the material vapor separated by the separation structure (5); The interior of the separation shell (51) is hollow, one end of the separation shell (51) is provided with an outward-turned mounting opening (512) penetrating the interior thereof, an outward-turned ring sheet (511) is fixedly connected to the outward-turned mounting opening (512), and a guide outlet (513) penetrating the interior thereof is provided at the top end of the separation shell (51) away from the outward-turned mounting opening (512); The separation unit (52) comprises a bottom plate (521) fixedly connected to the bottom of the separation shell (51); a group of air guide modules are fixedly connected to one side of the bottom plate (521); the air guide module is composed of a plurality of flow dividers (522) arranged in an array; the spacing between each two adjacent flow dividers (522) near the end of the outward-turned installation opening (512) is greater than the spacing between each two adjacent flow dividers (522) near the end of the guide outlet (513); the two outermost flow dividers (522) of the air guide module are fixedly connected to an outward-turned partition plate (523) at one end near the outward-turned installation opening (512); a plurality of protrusions with the same spacing are fixedly connected to the surfaces of both sides of the flow divider (522); the protrusions on the opposite surfaces of each two flow dividers (522) are staggered; a separation installation groove (5221) is provided on the surface of the flow divider (522) near each two adjacent protrusions; the separation installation groove (5221) is connected to a primary separation unit (6).

2. The separation mechanism according to claim 1, characterized in that: The primary separation unit (6) comprises a primary separation plate (61) fixedly connected to the surface wall of the separation installation groove (5221), a plurality of evenly arranged upright posts (62) being fixedly connected to one side of the primary separation plate (61), and a plush pad (63) being laid on the surface of the primary separation plate (61) near the bottom of the upright posts (62).

3. The separation mechanism according to claim 1, characterized in that: The secondary separation component (53) comprises a guide block (531) fixedly connected to one side of the bottom plate (521); a steam guide groove (5315) is provided on a side of the guide block (531) close to the diverter plate (522); and a diverter plate groove (5314) adapted to the diverter plate (522) is provided on one side of the guide block (531); The steam guide groove (5315) is composed of a square groove (5317) and a fan-shaped groove (5316) which are connected to each other, the square groove (5317) is opened at the bottom end of the guide block (531), and the fan-shaped groove (5316) is opened at the top end of the guide block (531), the square groove (5317) is connected to a secondary separation unit (532), and the fan-shaped groove (5316) corresponds to the position of the guide outlet (513); It also includes a connection unit for fixedly connecting the secondary separation unit (532) to the square groove (5317).

4. The separation mechanism according to claim 3, characterized in that: The secondary separation unit (532) comprises a secondary separation plate (5321) fixedly connected to two diagonal corners of the square groove (5317); a plurality of evenly arranged separation holes (5323) are formed on the secondary separation plate (5321); and the inner walls of the separation holes (5323) are connected to the collection units (54); The connection unit comprises a clamping strip (5322) fixedly connected to both sides of the secondary separation plate (5321); inner walls on both sides of the square groove (5317) are provided with clamping slots (5312) adapted to the clamping strip (5322); and a placement slot (5313) adapted to the bottom end of the secondary separation plate (5321) is provided at the bottom of the square groove (5317); The collecting unit (54) comprises a collecting ring (541) fixedly connected to the inner surface wall of the separation hole (5323); a collecting elbow (542) is fixedly connected to one side of the collecting ring (541); an end of the collecting elbow (542) away from the collecting ring (541) is fixedly connected to a stop tube (543); the collecting ring (541) is communicated with the collecting elbow (542); and the collecting elbow (542) is communicated with the stop tube (543).

5. The separation mechanism according to claim 1, characterized in that: The pretreatment structure (4) comprises an inlet pipe (42) fixedly connected to the separation shell (51), one end of the inlet pipe (42) passes through the outlet (513) and extends into the separation shell (51), the other end of the inlet pipe (42) is fixedly connected to a pre-condensing pipe (41), one end of the pre-condensing pipe (41) away from the inlet pipe (42) is fixedly connected to a tail pipe (44), and the bottom of the tail pipe (44) is fixedly connected to an outlet pipe (43).

6. The separation mechanism according to claim 5, characterized in that: The inner wall of the pre-condensing tube (41) is fixedly connected with a first guide plate (46) and a second guide plate (45) in sequence from the inlet pipe (42) toward the tail pipe (44); the second guide plate (45) and the first guide plate (46) are both provided with air outlets; the first guide plate (46) is fixed to the inner wall at the bottom end and the side of the bottom end inside the pre-condensing tube (41); the second guide plate (45) is fixed to the inner wall at the top end and the side of the top end inside the pre-condensing tube (41); and the pre-condensing tube (41) and the second guide plate (45) are provided with external contact grooves (411) at positions corresponding to the second guide plate (45).

7. The separation mechanism according to claim 6, characterized in that: The first-stage guide plate (46) is composed of a first guide section (461) in an outward convex shape and an anti-backflow section (462) in an outward everted shape, one end of the first guide section (461) is fixedly connected to the inner surface wall of the pre-condensing tube (41), and the other end of the first guide section (461) is fixedly connected to the anti-backflow section (462); The second guide plate (45) is formed by connecting a second guide section (452), a connecting section (453) and a surface increasing section (454); the second guide section (452) and the surface increasing section (454) are both concave structures; the connecting section (453) is a convex structure; two ends of the connecting section (453) are respectively fixedly connected to the second guide section (452) and the surface increasing section (454); and the other ends of the second guide section (452) and the surface increasing section (454) are both fixedly connected to the inner wall of the pre-condensing tube (41); The surfaces of the first-stage guide vane (46) and the second guide vane (45) facing each other are both provided with a plurality of guide grooves (451) distributed in an annular shape.

8. A reaction kettle, comprising a lower kettle body (1), an upper kettle body (2) and a driving device (3), wherein the top of the lower kettle body (1) is fixedly connected to the upper kettle body (2), the top of the upper kettle body (2) is fixedly connected to the driving device (3), the output end of the driving device (3) passes through the upper kettle body (2) and extends to the interior of the lower kettle body (1), and the output end of the driving device (3) is fixedly connected to a first stirring blade (31), a second stirring blade (32) and a third stirring blade (33) in sequence, characterized in that: It also comprises the separation mechanism according to any one of claims 5 to 7, wherein the separation shell (51) is fixedly connected to the inner surface wall of the upper kettle body (2), an inlet hole is provided on the upper kettle body (2), and the outer surface wall of the inlet pipe (42) is fixedly connected to the inner wall of the inlet hole.