Testing device for glycerol hydrogenolysis catalyst

By designing a testing device that includes a glyceride hydrogen hydrogen hydrogen hydrogen hydrogen hydrogen hydrogen hydrogen hydrogen hydrogen hydrogen dismissal catalyst test device that includes frame components, raw materials storage components, liquid hybrid components, reaction components, hybrid mixing components, and reaction driving components, it solves the effects of the effects of the effects of hybrid glycerin and solutions and testing agents. The problem realizes the safe and efficient carrion of glycerin hydrolysis test and the controllability of catalyst effects.

CN119375392AInactive Publication Date: 2025-01-28CHONGQING VOCATIONAL COLLEGE OF SAFETY TECH
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Patent Information

Application Number
CN202411741645.0
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2024-11-29
Publication Date
2025-01-28
Estimated Expiration
Not applicable · inactive patent

AI Technical Summary

Technical Problem

The existing glycerol hydrogenolysis test device is difficult to efficiently mix glycerol with solution, and it is difficult to test the effect of different catalysts on glycerol hydrogenolysis reaction.

Method used

A test device includes a test device that includes frame structures, raw materials storage components, liquid hybrid components, reaction components, hybrid mixing components, and reaction drive components. The device adds glycerin and solution to the mixed tank through the raw material storage component connected to the mixed tank to the mixed tank, and forms a switching connection between the liquid mixed component, the reaction component and the mixing component through the reaction driver component to achieve the hydrogen hydrogen hydrogen disintegration The test of the test is safe and efficient.

Benefits of technology

The efficient mixing of glycerin and solutions can be safely tested to the impact of different catalysts on the disintegration of glycerin hydrogen, which improves the controllability and efficiency of glycerin hydrogenation process.

✦ Generated by Eureka AI based on patent content.

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Abstract

The invention provides a glycerin hydrogenolysis catalyst testing device, and belongs to the technical field of glycerin hydrogenolysis testing devices.The glycerin hydrogenolysis catalyst testing device comprises a frame component, a raw material storage assembly, a liquid mixing assembly, a reaction assembly, a mixing and stirring component and a reaction driving component; the raw material storage assembly is used for storing glycerol and different solutions and can supply materials to the mixing tank in a non-contact manner; the reaction assembly is located on the other side of the mixing tank, and under the state that the transverse movement connecting base drives the liquid outlet plug not to be inserted into the flaring connecting pipe, the transverse movement sliding sleeve and the first rotating bevel gear can just synchronously form matched transmission. On the other hand, inner stirring blades in the mixing tank are driven to rotate passively, and the glycerol and the solution are mixed; after the liquid outlet plug is inserted into the flaring connecting pipe in place, the transverse sliding sleeve and the second rotating bevel gear are in transmission, and rotation of the reaction mixing lantern ring can be formed.
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Description

Technical Field

[0001] The invention relates to the technical field of glycerol hydrogenolysis test devices, in particular to a test device for a glycerol hydrogenolysis catalyst. Background Art

[0002] Glycerol, also known as propylene glycol, is a non-toxic and biodegradable compound with a melting point of 17.8°C and a boiling point of 290.0°C. It is miscible with water and ethanol, but insoluble in benzene, chloroform, carbon tetrachloride, carbon disulfide, petroleum ether and other oils. It is a very important chemical raw material and is widely used in food, medicine, cosmetics, tobacco and other industries.

[0003] Hydrogenolysis refers to the reaction in which part of the oxygen atoms in an organic molecule are replaced by hydrogen atoms. Glycerol hydrogenolysis can produce propylene glycol, which is also an important chemical raw material, mainly used in the production of polyester resins, detergents, cosmetics, plasticizers, surfactants, emulsifiers, etc.

[0004] Glycerol hydrogenolysis refers to the process in which the hydroxyl groups of glycerol break under the action of a catalyst to form propylene glycol. Glycerol hydrogenolysis reactions under different conditions and factors will produce different results. Testing these processes can lead to a more reasonable glycerol hydrogenolysis process and guide the industrial production of propylene glycol. Summary of the invention

[0005] The purpose of the present invention is to provide a testing device for a glycerol hydrogenolysis catalyst. By utilizing an array of raw material storage components connected to a mixing tank, glycerol and different solutions can be added to the mixing tank. By forming a switching transmission connection between the liquid mixing component, the reaction component and the mixing and stirring component through a reaction driving component, the glycerol hydrogenolysis test can be carried out safely and efficiently.

[0006] The objective of the present invention is achieved through such a technical solution. A testing device for a glycerol hydrogenolysis catalyst comprises a frame component, a raw material storage component, a liquid mixing component, a reaction component, a mixing and stirring component and a reaction drive component. The liquid mixing component comprises a mixing tank, a liquid outlet plug and a liquid outlet hose. The reaction component comprises a reaction tower, a flared connecting pipe and a reaction tower mixing shaft. The mixing and stirring component comprises an inner stirring shaft, a stirring gear and a fixed rack. The reaction drive component comprises an inner horizontal shaft, a first rotating bevel gear and a second rotating bevel gear.

[0007] The raw material storage assembly is installed on one side of the frame member, the bottom end of the mixing tank is slidably connected to the inner middle part of the frame member, one end of the liquid outlet hose is connected to the top outlet of the mixing tank, and the other end is connected to the liquid outlet plug, the reaction tower is installed on the other side of the frame member, the flared connecting pipe is connected to one side of the upper end of the reaction tower, and the flared part faces the liquid outlet plug upward, the reaction tower mixing shaft is screwed to the inner middle part of the reaction tower, the inner stirring shaft is screwed to the inner middle part of the mixing tank, the stirring gear is inserted and fixed to the outer top end of the inner stirring shaft, the inner top end of the frame member body is fixed with a fixed rack, and the stirring gear is meshed with the fixed rack;

[0008] The inner horizontal shaft is laterally rotated above the reaction tower, the first rotating bevel gear and the second rotating bevel gear are both rotationally connected in the inner horizontal shaft, and the second rotating bevel gear is transmission connected to the mixing shaft of the reaction tower, the first rotating bevel gear is transmission connected to the mechanism that drives the mixing tank to reciprocate, and a transverse sliding sleeve is also slidably inserted in the middle of the main body of the inner horizontal shaft, and the two ends of the transverse sliding sleeve can respectively form an engagement with the first rotating bevel gear or the second rotating bevel gear, and a transverse connecting seat that can automatically move laterally is provided on the other side of the top end of the frame member, the upper end of the transverse connecting seat is rotationally connected to the transverse sliding sleeve, and the lower end is fixedly connected to the liquid outlet plug.

[0009] The use process of the technical solution of the present invention is as follows:

[0010] The mixing tank is a container for mixing glycerin and solutions. Glycerin and other different solutions can be injected into the mixing tank from various raw material storage components according to the test requirements, so that the glycerin and the solution are fully contacted and mixed. In this process, the automatically movable transverse connecting seat can drive the transverse sliding sleeve to form a transmission connection with the first rotating bevel gear separately. The first rotating bevel gear can drive the mixing tank to move back and forth within a certain range through the transmission mechanism, thereby improving the mixing efficiency.

[0011] And synchronously, it can also drive the stirring gear in a freely rotating state to form a matching transmission with the fixed rack at a fixed position, so that as the mixing tank reciprocates horizontally, the inner stirring shaft fixedly connected to the stirring gear can rotate, thereby stirring the mixture in the mixing tank, further improving the mixing efficiency;

[0012] After the glycerol and the solution are fully contacted and mixed, they can be transferred to the reaction tower for catalytic heating reaction. The liquid outlet plug can be moved by the automatically movable transverse connecting seat, so that the liquid outlet plug can be inserted into the expanded connecting pipe, so that the mixing tank and the reaction tower are connected, and a channel for the mixture in the mixing tank to be transferred to the reaction tower can be formed;

[0013] Synchronously, the transverse sliding sleeve independently forms a transmission connection with the second rotating bevel gear, so that the second rotating bevel gear can drive the rotation of the reaction mixing ring in the reaction tower through the transmission mechanism, and cooperate with the heating of the reaction tower and the addition of hydrogen and catalyst at a certain pressure into the reaction tower to form a glycerol hydrogenolysis reaction. Not only can the glycerol hydrogenolysis reaction after glycerol is mixed with different solutions be tested, but also the glycerol hydrogenolysis reaction under the action of different catalysts can be tested.

[0014] By adopting the above technical solution, the present invention can achieve the following beneficial effects:

[0015] (1) Before glycerol hydrogenolysis, in order to test the effects of different solvents, glycerol can be mixed with any one of the solvents, or glycerol can be mixed with a plurality of solvents. To achieve this purpose, the present invention provides a plurality of raw material storage components connected to the mixing tank, which can be used to store different raw materials, thereby forming test effects with different raw material ratios;

[0016] (2) The mixing tank of the present invention is a container for mixing glycerol and solution. In order to improve the mixing efficiency, the present invention sets the bottom end of the mixing tank in a sliding connection state, and sets an internal stirring shaft inside the mixing tank, and the stirring gear connected to the top end of the internal stirring shaft is meshed with a fixed rack at a fixed position, so that the lateral movement seat can move automatically, so that the lateral movement sleeve is independently connected to the first rotating bevel gear for transmission. After the liquid outlet plug is synchronously disconnected from the flared connecting pipe, the first rotating bevel gear can not only drive the reciprocating lateral movement of the mixing tank through the transmission mechanism, but also drive the passive rotation of the internal stirring shaft located in the mixing tank, thereby achieving the purpose of efficient mixing, and also achieving the purpose of safely cutting off the connection between the mixing tank and the reaction tower during the mixing process;

[0017] (3) The reaction tower is used as a container for catalytic reaction. The liquid outlet plug can be driven to move horizontally by the transverse connecting seat, and the liquid outlet plug is connected with the flared connecting pipe to establish a connecting channel between the mixing tank and the reaction tower, so that the glycerol solution after mixing can enter the reaction tower. After the catalyst and hydrogen are added, a hydrogenolysis reaction can be formed. At the same time, the transverse sliding sleeve can be connected to the second rotating bevel gear transmission separately, so that the reaction tower mixing shaft located in the reaction tower rotates, which can also achieve the purpose of accelerating the catalytic hydrogenolysis reaction process. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required for use in the embodiments or the description of the prior art will be briefly introduced below. Obviously, the drawings described below are some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying creative labor.

[0019] Figure 1 A schematic diagram of the overall structure of a testing device for a glycerol hydrogenolysis catalyst provided by the present invention;

[0020] Figure 2 It is a schematic diagram of the installation structure of the raw material storage component and the liquid mixing component of the present invention;

[0021] Figure 3 A schematic diagram of the connection between the raw material storage component and the liquid mixing component of the present invention from a first perspective;

[0022] Figure 4 A schematic diagram of the connection between the raw material storage component and the liquid mixing component of the present invention from a second viewing angle;

[0023] Figure 5 It is a structural schematic diagram of the inner tube part of the present invention;

[0024] Figure 6 It is a schematic structural diagram of the elastic airbag part of the present invention;

[0025] Figure 7 This is a schematic structural diagram of the reaction assembly of the present invention from a first perspective;

[0026] Figure 8 This is a schematic structural diagram of the reaction assembly of the present invention from a second viewing angle;

[0027] Fig. 9 It is a cross-sectional schematic diagram of the reaction tower part of the present invention;

[0028] Fig.10 It is a schematic structural diagram of the mixing and stirring component of the present invention;

[0029] Fig.11 It is a structural schematic diagram of the driving box part of the reaction driving component of the present invention;

[0030] Fig.12 It is a schematic diagram of the structure of the transverse sliding sleeve and the moving face gear part of the present invention;

[0031] Fig.13 It is a structural schematic diagram of the lower connecting frame part of the present invention;

[0032] Fig.14 It is a structural schematic diagram of the eccentric wheel part of the present invention from a first viewing angle;

[0033] Fig.15 It is a structural schematic diagram of the eccentric wheel part of the present invention from a second viewing angle.

[0034] Reference numerals:

[0035] 1. Frame components;

[0036] 2. Raw material storage assembly; 201. Storage tank; 202. Feed pipe; 203. Discharge connecting pipe; 204. Pump body bottom plate; 205. Pump housing; 206. Discharge connecting hose; 207. Suction connecting hose; 208. Rotating pulley; 209. Pump shaft; 210. Driving pulley; 211. Connecting belt; 212. Inner tube; 213. Triangular seat; 214. Push wheel; 215. Pump body motor; 216. Elastic airbag;

[0037] 3. Liquid mixing assembly; 301. Mixing tank; 302. Bottom slide rail; 303. Bottom slide plate; 304. Liquid outlet pipe; 305. Liquid outlet plug; 306. Liquid outlet hose; 307. Liquid inlet pipe; 308. Liquid outlet valve; 309. Air blowing pipe;

[0038] 4. Reaction assembly; 401. Constant temperature baffle; 402. Reaction tower; 403. Expanded connecting pipe; 404. Dosing pipe; 405. Dosing cap; 406. Heating pipe; 407. Reaction liquid inlet valve; 408. Reaction tower top seat; 409. Reaction tower mixing shaft; 410. Reaction mixing collar; 411. Test liquid outlet pipe; 412. Hydrogen gas connection pipe;

[0039] 5. Mixing and stirring member; 501. Top seat of mixing tank; 502. Internal stirring shaft; 503. Internal stirring blade; 504. Stirring gear; 505. Fixed rack;

[0040] 6. Reaction drive component; 601. Drive box; 602. Main drive motor; 603. Inner seat; 604. Inner horizontal shaft; 605. First rotating bevel gear; 606. Second rotating bevel gear; 607. Fixed face gear; 608. Transverse slideway; 609. Transverse slide sleeve; 610. Moving face gear; 611. Fork rotation groove; 612. Transverse electric cylinder; 613. Transverse connecting seat; 614. Fork sleeve; 615. Auxiliary slide rail; 616. Auxiliary pulley; 617, lower connecting frame; 618, hanging seat; 619, hanging rod; 620, lifting ring; 621, reaction mixing gear; 622, compound connecting shaft; 623, compound connecting bevel gear; 624, transmission shaft; 625, transmission bevel gear; 626, coaxial fixed gear; 627, vertical shaft seat; 628, vertical shaft; 629, upper connecting gear; 630, eccentric wheel; 631, eccentric shaft; 632, eccentric connecting rod; 633, bottom fixed rotating seat; 634, push connecting rod;

[0041] 7. Test analyzer. DETAILED DESCRIPTION

[0042] In order to make the purpose, technical solution and advantages of the embodiments of the present invention clearer, the technical solution in the embodiments of the present invention will be clearly and completely described below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments are part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0043] In the description of the present invention, it should be noted that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside" and the like indicate positions or positional relationships based on the positions or positional relationships shown in the accompanying drawings, and are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as limiting the present invention. In addition, the terms "first" and "second" are used for descriptive purposes only and cannot be understood as indicating or implying relative importance.

[0044] like Figure 1-Figure 15 As shown, a test device for a glycerol hydrogenolysis catalyst, wherein a raw material storage assembly 2 is installed on one side of a frame member 1 for storing glycerol and other different solvents, a bottom end of a mixing tank 301 is laterally slidably connected to an inner middle portion of the frame member 1, one end of a liquid outlet hose 306 is connected to a top outlet of the mixing tank 301, and the other end is connected to a liquid outlet plug 305, a reaction tower 402 is installed on the other side of the frame member 1, and a heating source is provided on the outside, a flared connecting pipe 403 is connected to one side of an upper end of the reaction tower 402, and the flared portion faces upward to the liquid outlet plug 305, a reaction tower mixing shaft 409 is screwed to an inner middle portion of the reaction tower 402, an inner stirring shaft 502 is screwed to an inner middle portion of the mixing tank 301, a stirring gear 504 is inserted and fixed to an outer top end of the inner stirring shaft 502, a fixed rack 505 is fixed to an inner top end of a main body of the frame member 1, and the stirring gear 504 is meshed with the fixed rack 505;

[0045] The inner horizontal shaft 604 is laterally screwed on the top of the reaction tower 402 and can rotate automatically. The first rotating bevel gear 605 and the second rotating bevel gear 606 are both rotatably connected in the inner horizontal shaft 604, and the second rotating bevel gear 606 is transmission-connected to the reaction tower mixing shaft 409, and the first rotating bevel gear 605 is transmission-connected to the mechanism that drives the mixing tank 301 to reciprocate. A transverse sliding sleeve 609 is also slidably inserted in the middle of the main body of the inner horizontal shaft 604, and the two ends of the transverse sliding sleeve 609 are The ends can respectively form an engagement with the first rotating bevel gear 605 or the second rotating bevel gear 606. The other side of the top of the frame member 1 is provided with a transverse connecting seat 613 which can automatically move laterally. The upper end of the transverse connecting seat 613 is screwed to the transverse sliding sleeve 609, and the lower end is fixed to the liquid outlet plug 305. After the transverse connecting seat 613 drives the liquid outlet plug 305 to be inserted into the flared connecting pipe 403 and into place, the transverse sliding sleeve 609 just forms an engagement with the second rotating bevel gear 606 alone.

[0046] Here’s how it works:

[0047] Glycerol hydrogenolysis refers to the process in which glycerol hydroxyl groups are broken to form propylene glycol under the action of a catalyst using glycerol as a raw material.

[0048] The mixing tank 301 is a container for mixing glycerin and solution. According to the test requirements, glycerin and other different solutions can be injected into the mixing tank 301 from each group of raw material storage components 2 so that the glycerin and solution are fully contacted and mixed;

[0049] In this process, the automatically movable transverse connecting seat 613 can drive the transverse sliding sleeve 609 to form a transmission connection with the first rotating bevel gear 605. The first rotating bevel gear 605 can drive the mixing tank 301 to move back and forth within a certain range through the transmission mechanism, thereby improving the mixing efficiency.

[0050] And synchronously, it can also drive the stirring gear 504 in a freely rotating state to form a matching transmission with the fixed rack 505 in a fixed position, so that as the mixing tank 301 reciprocates horizontally, the inner stirring shaft 502 fixedly connected to the stirring gear 504 can rotate, thereby stirring the mixture in the mixing tank 301, and further improving the mixing efficiency;

[0051] After the glycerol is fully contacted and mixed with the solution, it can be transferred to the reaction tower 402 for catalytic heating reaction. The liquid outlet plug 305 can be moved by the automatically movable transverse connecting seat 613, so that the liquid outlet plug 305 can be inserted into the expanded connecting pipe 403, so that the mixing tank 301 and the reaction tower 402 are connected to form a channel for the mixture in the mixing tank 301 to transfer to the reaction tower 402.

[0052] Synchronously, the transverse sliding sleeve 609 forms a transmission connection with the second rotating bevel gear 606 alone, so that the second rotating bevel gear 606 can drive the rotation of the reaction mixing ring 410 in the reaction tower 402 through the transmission mechanism, and cooperate with the heating of the reaction tower 402 and the addition of a certain pressure of hydrogen and a catalyst into the reaction tower 402 to form a glycerol hydrogenolysis reaction. Not only can the glycerol hydrogenolysis reaction after mixing glycerol with different solutions be tested, but also the glycerol hydrogenolysis reaction under the action of different catalysts can be tested.

[0053] The specific structures of the raw material storage component 2 and the liquid mixing component 3 are as follows: Figure 2 , Figure 3 , Figure 4 , Figure 5 and Figure 6 As shown, the frame member 1 is a frame-shaped structure as a whole, and different storage tanks 201 are placed and fixed on one side of the inner frame of the frame member 1. One end of each group of storage tanks 201 is connected to a feed pipe 202, and a valve is installed at the liquid inlet end of the feed pipe 202, so that glycerin and other different solutions can be added to each group of storage tanks 201;

[0054] One side of the mixing tank 301 is connected with an array of liquid inlet pipes 307, and the liquid outlet end of each group of storage tanks 201 is connected to the pump housing 205 through the discharge connecting pipe 203 and the discharge connecting hose 206, and the liquid outlet end of each group of pump housings 205 is connected to a different liquid inlet pipe 307 through the suction connecting hose 207, so as to form a connection channel between each group of storage tanks 201 and the mixing tank 301;

[0055] The bottom of the pump housing 205 is fixedly connected to the frame member 1 through the pump body bottom plate 204, and the rotating pulley 208 is laterally screwed into the main body of the pump housing 205. A pump body motor 215 is also installed and fixed on the top of each group of pump body bottom plates 204. A driving pulley 210 is inserted and fixed in the rotating shaft of the pump body motor 215. A pump shaft 209 is inserted and fixed on the outer end of the rotating pulley 208. A connecting belt 211 is sleeved and installed between the pump shaft 209 and the driving pulley 210.

[0056] Each pump housing 205 is provided with an inner tube 212, and both ends of the inner tube 212 are connected to a discharge connection hose 206 and a suction connection hose 207 respectively;

[0057] The triangular seat 213 is inserted and fixed in the rotating pulley 208, and the push wheel 214 is rotatably connected to the sharp corner of the main body of the triangular seat 213. The inner side of the inner tube 212 is connected with the same number of elastic air bags 216 as the push wheels 214. When the rotating pulley 208 drives the triangular seat 213 to rotate, three different push wheels 214 can simultaneously squeeze and release the elastic air bags 216 on the same side.

[0058] The purpose of using the rotating triangular seat 213 to drive the push wheel 214 to squeeze and release the elastic airbag 216 is to achieve non-contact driving of various raw material liquids in the inner tube 212 and the elastic airbag 216, so that the raw material liquid will not damage the pump body structure;

[0059] The bottom of the inner frame of the frame member 1 is fixedly connected in pairs with bottom rails 302, the bottom of the bottom slide plate 303 is slidably connected to the bottom rails 302, and the outer bottom of the mixing tank 301 is fixedly connected to the bottom slide plate 303;

[0060] A liquid outlet pipe 304 is connected to one side of the top of the mixing tank 301. The main body of the liquid outlet pipe 304 extends into the bottom of the inner cavity of the mixing tank 301, and the inlet of the liquid outlet pipe 304 is connected to the inner cavity of the mixing tank 301.

[0061] The liquid outlet valve 308 is installed at one end of the liquid outlet plug 305 and is in a normally closed state. It is opened only after the liquid outlet plug 305 and the flared connecting pipe 403 are plugged into place.

[0062] A gas blowing pipe 309 is also connected to one side of the top of the mixing tank 301, and an air valve is installed in the gas blowing pipe 309. The gas blowing pipe 309 is connected to an external gas source for pressurizing the inner cavity of the mixing tank 301, so that after the glycerol and solution in the mixing tank 301 are mixed, they can enter the reaction tower 402, and the gas source gas connected to the gas blowing pipe 309 can be selected from inert gas or other gases that do not participate in the glycerol hydrogenolysis reaction at all.

[0063] The specific structure of the reaction component 4 is as follows Figure 7 , Figure 8 and Fig. 9 As shown, the thermostatic baffle 401 is fixedly connected to the other side of the frame member 1 and can surround and fix the reaction tower 402. A heating pipe 406 is installed between the outer wall of the reaction tower 402 and the inner cavity of the thermostatic baffle 401 to provide a heat source for the reaction process in the reaction tower 402.

[0064] A dosing tube 404 is also installed on one side of the top of the reaction tower 402, and an openable and closable dosing cap 405 is connected to the top of the dosing tube 404 to facilitate adding a catalyst for the reaction into the reaction tower 402;

[0065] A reaction liquid inlet valve 407 is also installed in the main pipe of the expanded connecting pipe 403, which can play the role of closing the inner cavity of the reaction tower 402;

[0066] The reaction liquid inlet valve 407 is in a normally open state, and is closed only after the glycerol solution in the mixing tank 301 is completely transferred to the inner cavity of the reaction tower 402;

[0067] A hydrogen pipe 412 is also connected to one side of the top of the reaction tower 402. A gas valve is also installed in the hydrogen pipe 412 to provide hydrogen with a certain pressure into the reaction tower 402.

[0068] A reaction tower top seat 408 is fixedly installed in the middle of the top of the reaction tower 402, the upper end body of the reaction tower mixing shaft 409 is rotatably connected in the reaction tower top seat 408, and the reaction mixing ring 410 is fixedly connected to the outer lower end of the reaction tower mixing shaft 409 and is completely located in the inner cavity of the reaction tower 402.

[0069] The specific structure of the mixing and stirring member 5 is as follows: Fig.10 As shown, the mixing tank top seat 501 is fixedly installed at the top middle part of the mixing tank 301, the upper end body of the inner stirring shaft 502 is rotatably connected in the mixing tank top seat 501, and the inner stirring blade 503 is fixedly connected to the outer lower end of the inner stirring shaft 502 and is completely located in the inner cavity of the mixing tank 301;

[0070] The inner stirring blade 503 and the reaction mixing ring 410 play the same role, which is to mix the reaction contact process to improve efficiency.

[0071] The specific structure of the reaction drive component 6 is as follows Fig.11 , Fig.12 , Fig.13 , Fig.14 and Fig.15 As shown, the drive box 601 is fixedly connected to the other side of the top of the frame member 1, and is used to provide a position for the transmission mechanism disposed therein, the main drive motor 602 is installed and fixed to one end of the outside of the drive box 601, and an inner seat 603 is fixed to the other end of the inner cavity of the drive box 601, one end of the inner horizontal shaft 604 is rotatably connected to the inner seat 603, and the other end passes through the side wall of the drive box 601 and is fixedly connected to the rotating shaft of the main drive motor 602;

[0072] Fixed face gears 607 are fixed inside the first rotating bevel gear 605 and the second rotating bevel gear 606, movable face gears 610 are fixed at both ends of the transverse sliding sleeve 609, the transverse slideway 608 is fixedly connected to the middle part of the outer side of the inner transverse shaft 604, the transverse sliding sleeve 609 is slidably connected in the transverse slideway 608, and the movable face gears 610 will not interfere with the sliding action of the transverse sliding sleeve 609 in the transverse slideway 608;

[0073] The movable face gear 610 can gradually form a meshing connection with the fixed face gear 607 as the lateral movement of the lateral sliding sleeve 609 progresses;

[0074] The shift fork rotation groove 611 is opened in the middle of the main body of the transverse sliding sleeve 609, and the transverse electric cylinder 612 is also installed and fixed on the other side of the top of the frame member 1. The transverse connecting seat 613 is fixedly connected to the telescopic rod of the transverse electric cylinder 612. One end of the shift fork sleeve 614 is rotationally connected to the shift fork rotation groove 611, and the other end passes through the side wall of the driving box 601 and is fixedly connected to the upper end of the transverse connecting seat 613;

[0075] In order to improve the stability of the lateral movement of the lateral movement seat 613, an auxiliary slide rail 615 and an auxiliary pulley 616 are further provided between the lateral movement seat 613 and the outer side of the driving box 601. The auxiliary slide rails 615 are fixedly connected to the outer side of the driving box 601 in pairs, and the auxiliary pulley 616 is rotatably connected to the lateral movement seat 613 and rollingly connected in the auxiliary slide rails 615.

[0076] The lower end of the transverse connecting seat 613 is fixedly connected with a lower connecting frame 617, and the other end of the lower connecting frame 617 passes through the main body of the frame member 1 and is fixedly connected to the outside of the liquid outlet plug 305, so that when the transverse electric cylinder 612 drives the transverse connecting seat 613 to move transversely, the transverse movement of the liquid outlet plug 305 and the fork sleeve 614 can be synchronously formed, and the liquid outlet plug 305 and the flared connecting pipe 403 can be plugged and matched with the moving face gears 610 at both ends of the transverse sliding sleeve 609 to form a synchronous action of meshing with the first rotating bevel gear 605 and the fixed face gear 607 inside the second rotating bevel gear 606;

[0077] The frame member 1 and the main body of the drive box 601 are also provided with through grooves to provide space for the lateral movement of the lower connecting frame 617 and the fork sleeve 614;

[0078] In order to improve the dynamic and static stability of the liquid outlet plug 305, a hanging seat 618, a hanging rod 619 and a hanging ring 620 are further provided between the inner top of the frame member 1 and the liquid outlet plug 305. The hanging rod 619 is fixedly connected to the inner top of the frame member 1 through the hanging seats 618 at both ends, and the hanging ring 620 is slidably connected in the hanging rod 619, and the bottom of the hanging ring 620 is sleeved and fixed on the outside of the liquid outlet plug 305. The number of the hanging rings 620 can be increased or decreased according to the length of the liquid outlet plug 305 to form the optimal static and mobile state of the liquid outlet plug 305.

[0079] The reaction mixing gear 621 is plugged and fixed on the top of the reaction tower mixing shaft 409. The bottom surface of the inner cavity of the driving box 601 is fixed with a composite connection shaft 622. The composite connection bevel gear 623 is rotatably connected in the composite connection shaft 622. One end of the composite connection bevel gear 623 is a bevel gear structure and the other end is a spur gear structure. The spur gear structure part is meshed with the reaction mixing gear 621, and the bevel gear part is meshed with the second rotating bevel gear 606.

[0080] After the second rotating bevel gear 606 is driven to rotate, the reaction tower mixing shaft 409 can be driven to rotate through the matching transmission formed by the composite connecting bevel gear 623 and the reaction mixing gear 621, thereby forming a reaction mixing action of the reaction mixing collar 410;

[0081] A transmission shaft 624 is also fixed to the bottom surface of the inner cavity of the driving box 601, a transmission bevel gear 625 is rotatably connected to the top end of the transmission shaft 624, a coaxial fixed gear 626 is coaxially fixed to the bottom end of the transmission bevel gear 625, and the first rotating bevel gear 605 is meshed with the transmission bevel gear 625;

[0082] A vertical shaft seat 627 is also installed and fixed at the bottom of the inner cavity of the driving box 601. A vertical shaft 628 is rotatably connected in the vertical shaft seat 627. An upper connecting gear 629 is plugged and fixed on the top of the vertical shaft 628 and meshes with the coaxial fixed gear 626.

[0083] An eccentric wheel 630 is fixed to the bottom end of the vertical shaft 628 after passing through the main body of the constant temperature partition 401. In order to improve the rotation stability of the vertical shaft 628, a rotating connection mechanism can be installed in the constant temperature partition 401 to form a support for the rotation of the vertical shaft 628 together with the vertical shaft seat 627;

[0084] An eccentric shaft 631 is eccentrically fixed to the bottom end of the eccentric wheel 630, a bottom fixed rotating seat 633 is fixed to the middle of the bottom end of the bottom slide plate 303, an eccentric connecting rod 632 is rotatably connected in the eccentric shaft 631, a push connecting rod 634 is rotatably connected in the bottom fixed rotating seat 633, and the other end of the eccentric connecting rod 632 is rotatably connected to the other end of the push connecting rod 634;

[0085] After the first rotating bevel gear 605 is driven to rotate, it forms a matching transmission with the transmission bevel gear 625. The transmission bevel gear 625 drives the rotation of the coaxial fixed gear 626, so that the coaxial fixed gear 626 and the upper connecting gear 629 form a matching transmission. The upper connecting gear 629 drives the rotation of the eccentric wheel 630 coaxially through the vertical shaft 628, and can drive the bottom slide plate 303 to reciprocate within a certain range through the eccentric rotational connection formed by the eccentric connecting rod 632 and the eccentric shaft 631 and the rotational connection formed with the push connecting rod 634.

[0086] Preferably, if Figure 1 and Fig. 9 As shown, a test liquid outlet pipe 411 is also connected to the middle of the bottom end of the reaction tower 402, and a test analyzer 7 is provided at the inner lower end of the other side of the frame member 1. The test liquid outlet pipe 411 is connected to the sample liquid inlet end of the test analyzer 7, and a valve is installed at the connection. The test analyzer 7 includes a solid-liquid separator and a chromatograph analyzer, which can purify propylene glycol and perform gas chromatography analysis using the chromatograph analyzer, thereby forming glycerol hydrogenolysis tests under different solutions and different catalyst conditions.

[0087] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit it. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the aforementioned embodiments, or replace some or all of the technical features therein with equivalents. However, these modifications or replacements do not cause the essence of the corresponding technical solutions to deviate from the scope of the technical solutions of the embodiments of the present invention.

Claims

1. A testing device for a glycerol hydrogenolysis catalyst, comprising a frame member (1) and a raw material storage assembly (2), characterized in that: It also includes a liquid mixing component (3), a reaction component (4), a mixing and stirring component (5) and a reaction driving component (6); The liquid mixing component (3) includes a mixing tank (301), a liquid outlet plug (305) and a liquid outlet hose (306); the reaction component (4) includes a reaction tower (402), a flared connecting pipe (403) and a reaction tower mixing shaft (409); the raw material storage component (2) is installed on one side of the frame component (1); the bottom end of the mixing tank (301) is slidably connected to the inner middle part of the frame component (1); one end of the liquid outlet hose (306) is connected to the top outlet of the mixing tank (301) and the other end is connected to the liquid outlet plug (305); the reaction tower (402) is installed on the frame component (1), the flared connecting pipe (403) is connected to one side of the upper end of the reaction tower (402), and the flared portion faces the liquid outlet plug (305) upwards, the reaction tower mixing shaft (409) is screwed to the inner middle part of the reaction tower (402), the mixing and stirring component (5) is installed in the mixing tank (301), and the reaction driving component (6) can not only drive the mixing tank (301) to move back and forth horizontally and the mixing and stirring component (5) to move synchronously, but also drive the reaction tower mixing shaft (409) to rotate after the liquid outlet plug (305) is inserted into the flared connecting pipe (403) in place.

2. A testing device for a glycerol hydrogenolysis catalyst according to claim 1, characterized in that: The mixing and stirring component (5) comprises an inner stirring shaft (502), a stirring gear (504) and a fixed rack (505); the reaction drive component (6) comprises an inner horizontal shaft (604), a first rotating bevel gear (605) and a second rotating bevel gear (606); the inner stirring shaft (502) is screwed to the inner middle part of the mixing tank (301); the stirring gear (504) is inserted and fixed to the outer top end of the inner stirring shaft (502); a fixed rack (505) is fixed to the inner top end of the main body of the frame component (1); the stirring gear (504) is meshed with the fixed rack (505); the inner horizontal shaft (604) is screwed to the top of the reaction tower (402); the first rotating bevel gear (605) and the second rotating bevel gear (606) are screwed to the inner middle part of the mixing tank (301); the stirring gear (504) is inserted and fixed to the outer top end of the inner stirring shaft (502); a fixed rack (505) is fixed to the inner top end of the main body of the frame component (1); the stirring gear (504) is meshed with the fixed rack (505); the inner horizontal shaft (604) is screwed to the top of the reaction tower (402); the first rotating bevel gear (605) and the second rotating bevel gear (606) are all rotatably connected in the inner transverse shaft (604), and the second rotating bevel gear (606) is transmission-connected to the mixing shaft (409) of the reaction tower, and the first rotating bevel gear (605) is transmission-connected to the mechanism that drives the mixing tank (301) to move back and forth. A transverse sliding sleeve (609) is also slidably inserted in the middle of the main body of the inner transverse shaft (604), and the two ends of the transverse sliding sleeve (609) can respectively form an engagement with the first rotating bevel gear (605) or the second rotating bevel gear (606). An automatically movable transverse connecting seat (613) is provided on the other side of the top end of the frame member (1), and the upper end of the transverse connecting seat (613) is rotationally connected to the transverse sliding sleeve (609), and the lower end is fixedly connected to the liquid outlet plug (305).

3. A testing device for a glycerol hydrogenolysis catalyst according to claim 1 or 2, characterized in that: The liquid mixing assembly (3) further comprises a bottom slide plate (303) and a liquid outlet valve (308); one side of the mixing tank (301) is connected to a liquid inlet pipe (307); the bottom of the inner frame of the frame member (1) is fixedly connected to bottom slide rails (302) in pairs; the bottom of the bottom slide plate (303) is slidably connected to the bottom slide rails (302); the outer bottom of the mixing tank (301) is fixedly connected to the bottom slide plate (303); one side of the top end of the mixing tank (301) is connected to a liquid outlet pipe (304); the liquid outlet valve (308) is mounted on one end of a liquid outlet plug (305); and one side of the top end of the mixing tank (301) is also connected to an air blowing pipe (309).

4. A testing device for a glycerol hydrogenolysis catalyst according to claim 3, characterized in that: The raw material storage component (2) comprises a storage tank (201), a discharge connecting pipe (203), a pump body bottom plate (204), a pump housing (205), a discharge connecting hose (206), and a suction connecting hose (207). Different storage tanks (201) are placed and fixed on one side of the inner frame of the frame component (1). The liquid outlet end of each group of storage tanks (201) is connected to the pump housing (205) through the discharge connecting pipe (203) and the discharge connecting hose (206). The liquid outlet end of each group of pump housings (205) is connected to different liquid inlet pipes (307) through the suction connecting hose (207). The bottom of the pump housing (205) is fixedly connected to the frame component (1) through the pump body bottom plate (204).

5. A testing device for a glycerol hydrogenolysis catalyst according to claim 4, characterized in that: The raw material storage assembly (2) further comprises a rotating pulley (208), a triangular seat (213) and a push wheel (214); the rotating pulley (208) is screwed into the main body of the pump housing (205); a pump motor (215) is also installed and fixed on the top of each pump body bottom plate (204); a driving pulley (210) is inserted and fixed in the rotating shaft of the pump body motor (215); a pump shaft (209) is inserted and fixed at the outer end of the rotating pulley (208); a pump shaft (209) and a driving pulley (210) are connected between the pump shaft (209) and the driving pulley (210). A connecting belt (211) is sleeved and installed, and an inner tube (212) is installed inside each group of pump shells (205). The two ends of the inner tube (212) are respectively connected to the discharge connection hose (206) and the suction connection hose (207). The triangular seat (213) is inserted and fixed in the rotating pulley (208), and the push wheel (214) is rotatably connected to the sharp corner position of the main body of the triangular seat (213). The inner side of the inner tube (212) is connected to elastic air bags (216) of the same number as the push wheel (214).

6. A testing device for a glycerol hydrogenolysis catalyst according to claim 1, 2, 3 or 5, characterized in that: The reaction assembly (4) further comprises a constant temperature partition (401) and a reaction mixing collar (410). The constant temperature partition (401) is fixedly connected to the other side of the frame member (1) and can surround and fix the reaction tower (402). A heating pipe (406) is installed in a surrounding manner between the outer wall of the reaction tower (402) and the inner cavity of the constant temperature partition (401). A dosing pipe (404) is also installed on one side of the top end of the reaction tower (402). The top end of the dosing pipe (404) is connected to an openable and closable A dosing cap (405) is provided, a reaction liquid inlet valve (407) is also installed in the main pipeline of the flared connecting pipe (403), a hydrogen connecting pipe (412) is also connected to one side of the top of the reaction tower (402), a reaction tower top seat (408) is fixedly installed in the middle of the top of the reaction tower (402), the upper end body of the reaction tower mixing shaft (409) is rotatably connected to the reaction tower top seat (408), and a reaction mixing collar (410) is fixedly connected to the outer lower end of the reaction tower mixing shaft (409).

7. A testing device for a glycerol hydrogenolysis catalyst according to claim 2, 3 or 5, characterized in that: The mixing and stirring member (5) further comprises a mixing tank top seat (501) and an inner stirring blade (503), wherein the mixing tank top seat (501) is fixedly mounted at the middle of the top end of the mixing tank (301), the upper end body of the inner stirring shaft (502) is rotatably connected to the mixing tank top seat (501), and the inner stirring blade (503) is fixedly connected to the outer lower end of the inner stirring shaft (502) and is completely located in the inner cavity of the mixing tank (301).

8. A testing device for a glycerol hydrogenolysis catalyst according to claim 2, 3 or 5, characterized in that: The reaction drive component (6) also includes a drive box (601), a main drive motor (602), a transverse slideway (608), a fork rotation groove (611), and a fork sleeve (614). The drive box (601) is fixedly connected to the other side of the top end of the frame component (1). The main drive motor (602) is installed and fixed to the outer end of the drive box (601). The other end of the inner cavity of the drive box (601) is fixed with an inner seat (603). One end of the inner transverse shaft (604) is rotatably connected to the inner seat (603), and the other end is fixedly connected to the rotating shaft of the main drive motor (602). The first rotating bevel gear (605) and the second rotating bevel gear (606) are both fixed with A fixed face gear (607), movable face gears (610) are fixed at both ends of the transverse sliding sleeve (609), the transverse sliding track (608) is fixedly connected to the middle part of the outer side of the inner transverse shaft (604), the transverse sliding sleeve (609) is slidably connected in the transverse sliding track (608), a shift fork rotation groove (611) is provided in the middle part of the main body of the transverse sliding sleeve (609), a transverse electric cylinder (612) is also fixedly installed on the other side of the top of the frame component (1), the transverse connecting seat (613) is fixedly connected to the telescopic rod of the transverse electric cylinder (612), one end of the shift fork sleeve (614) is rotationally connected to the shift fork rotation groove (611), and the other end is fixedly connected to the upper end of the transverse connecting seat (613).

9. The testing device for a glycerol hydrogenolysis catalyst according to claim 8, characterized in that: The reaction drive component (6) further comprises a reaction mixing gear (621), a composite connecting bevel gear (623), a transmission bevel gear (625), a coaxial fixed gear (626) and a bottom fixed rotating seat (633). The lower end of the transverse connecting seat (613) is fixedly connected to a lower connecting frame (617). The other end of the lower connecting frame (617) is fixedly connected to the outside of the liquid outlet plug (305). The reaction mixing gear (621) is plugged and fixed to the top end of the reaction tower mixing shaft (409). A composite connecting shaft (622) is fixed to the bottom surface of the inner cavity of the driving box (601), and a composite connecting bevel gear (623) is rotatably connected to the composite connecting shaft (622). One end of the composite connecting bevel gear (623) is meshed with the reaction mixing gear (621), and the other end is meshed with the second rotating bevel gear (606). A transmission shaft (624) is also fixed to the bottom surface of the inner cavity of the driving box (601), and a transmission bevel gear (625) is rotatably connected to the top end of the transmission shaft (624). The coaxial fixed gear (626) is fixed to the bottom end of the transmission bevel gear (625), and the first rotating bevel gear (605) is meshed with the transmission bevel gear (625). The bottom end of the inner cavity of the driving box (601) is also fixed with a vertical shaft seat (627), and a vertical shaft (628) is rotatably connected in the vertical shaft seat (627). The upper connecting gear (629) is plugged and fixed to the top end of the vertical shaft (628) and meshed with the coaxial fixed gear (626). The vertical shaft (628) passes through the constant temperature An eccentric wheel (630) is fixed to the bottom end behind the main body of the partition (401), an eccentric shaft (631) is eccentrically fixed to the bottom end of the eccentric wheel (630), a bottom fixed rotating seat (633) is fixed to the middle part of the bottom end of the bottom slide plate (303), an eccentric connecting rod (632) is rotatably connected in the eccentric shaft (631), a push connecting rod (634) is rotatably connected in the bottom fixed rotating seat (633), and the other end of the eccentric connecting rod (632) is rotatably connected to the other end of the push connecting rod (634).