CN115228389A - Reactor capable of improving heat transfer capacity - Google Patents

Reactor capable of improving heat transfer capacity Download PDF

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Publication number
CN115228389A
CN115228389A CN202210886522.0A CN202210886522A CN115228389A CN 115228389 A CN115228389 A CN 115228389A CN 202210886522 A CN202210886522 A CN 202210886522A CN 115228389 A CN115228389 A CN 115228389A
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China
Prior art keywords
box
guide
air flow
cylinder
catalyst
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CN202210886522.0A
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Chinese (zh)
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CN115228389B (en
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刘志鹤
武玉利
揭念国
王垒
相文静
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Qingdao Haiwan Chemical Engineering Design & Research Institute Co ltd
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Qingdao Haiwan Chemical Engineering Design & Research Institute Co ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005Separating solid material from the gas/liquid stream
    • B01J8/006Separating solid material from the gas/liquid stream by filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/087Heating or cooling the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/10Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by stirrers or by rotary drums or rotary receptacles or endless belts

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

The invention discloses a reactor capable of improving heat transfer capacity, which comprises a support, wherein a reaction cylinder is arranged at the top of the support, a feeding hopper is arranged on the slope surface of the top of the reaction cylinder, a catalyst placing mechanism is arranged in the reaction cylinder, the catalyst placing mechanism comprises a catalyst feeding component and a catalyst recovery component, a driving motor is arranged at the top of the reaction cylinder, and a feeding box is embedded and arranged at the top end of the reaction cylinder.

Description

Reactor capable of improving heat transfer capacity
Technical Field
The invention relates to the technical field of reactors, in particular to a reactor capable of improving heat transfer capacity.
Background
The reactor is a device for realizing the reaction process, and is widely applied to the fields of chemical industry, oil refining, metallurgy and the like, the reactor is used for realizing the liquid phase single phase reaction process and the liquid-liquid, gas-liquid, liquid-solid, gas-liquid-solid and other multiphase reaction processes, the application of the reactor is started in ancient times, a kiln for manufacturing ceramics is an original reactor, the form of the reactor in the recent industry is various, blast furnaces and converters in the metallurgical industry, fermentation tanks and various combustors in bioengineering are all reactors in different forms, and along with the maturity and development of the reactor technology, higher requirements are put forward on the reactor in practical application;
however, in the reactor on the market at present, the catalyst is usually added at the beginning of the reaction, in the reaction process, a reasonable mechanism is not provided, the catalyst is timely supplemented and uniformly distributed, and a reasonable mechanism is also not provided, so that the lost catalyst is timely transported and recovered in the reaction process, the catalyst cannot be timely supplemented, the subsequent reaction efficiency is lower and lower, even the subsequent reactant cannot completely and thoroughly react, the reaction efficiency is low, the lost catalyst cannot be timely transported, the catalyst with the particles reduced after loss is mixed into the reactant, and the purity of the reaction product and the waste of the catalyst are influenced.
Disclosure of Invention
The invention provides a reactor capable of improving heat transfer capacity, which can effectively solve the problems that the reactor in the current market proposed in the background technology usually only puts in a catalyst at the beginning of a reaction, a reasonable mechanism is not provided in the reaction process, the catalyst is timely supplemented and uniformly distributed, a reasonable mechanism is not provided, the lost catalyst is timely transported and recovered in the reaction process, the catalyst cannot be timely supplemented, the subsequent reaction efficiency is lower and lower, even the subsequent reactants cannot completely and thoroughly react, the reaction efficiency is low, the lost catalyst cannot be timely transported, the lost catalyst with small particles is mixed in the reactants, and the purity of reaction products and the waste of the catalyst are influenced.
In order to achieve the purpose, the invention provides the following technical scheme: a reactor capable of improving heat transfer capacity comprises a support, wherein a reaction cylinder is installed at the top of the support, a feeding hopper is installed on the slope surface of the top of the reaction cylinder, a catalyst placing mechanism is installed inside the reaction cylinder, and the catalyst placing mechanism comprises a catalyst feeding assembly and a catalyst recovery assembly;
the catalyst feeding assembly comprises a driving motor, a material supplementing box, a hollow shaft seat, a hollow rotating rod, a material supplementing opening, a material guide box, a material discharge opening, a material distribution plate, a material guide ring, a material separating strip, a material blocking block, a material blocking ring, a mounting frame, a limiting net and a material supplementing hopper;
the device comprises a reaction barrel, a driving motor, a feeding box, a hollow rotating rod, a driving motor output shaft, a plurality of feeding ports and a plurality of discharging ports, wherein the driving motor is installed at the top of the reaction barrel;
the middle part of the outer surface of the hollow rotating rod is provided with a material guide box, a plurality of material discharge ports are formed in the position, located inside the material guide box, of the outer surface of the hollow rotating rod at equal angles along the circumferential direction, a plurality of material distribution ports are formed in the bottom of the outer surface of the material guide box at equal angles along the circumferential direction, a material distribution disk is arranged on the outer side of the material guide box, a material guide ring is arranged at the top end of the material distribution disk, and a plurality of material separation strips are arranged at the top end of the material distribution disk at equal angles along the circumferential direction;
a material blocking block is arranged in the hollow rotating rod and positioned at the bottom of the discharge port, a material blocking ring is arranged on the edge of the top end of the material distribution plate, an installation frame is arranged on the outer side of the material guide box and positioned at the top end of the material blocking ring, a plurality of limiting nets are embedded at equal angles along the circumferential direction at the top end of the installation frame, and a material supplementing hopper is arranged at the top of the side end face of the material supplementing box;
the outer surface of the hollow rotating rod is uniformly provided with a plurality of stirring rods at equal distances at positions on two sides of the material distribution disc, and the bottom of the material distribution disc is provided with a catalyst recovery assembly.
Preferably, the catalyst recovery assembly comprises a material guide disc, a flow guide net, a flow guide ring, a collecting groove, a guide groove, a feed inlet, a transfer box, a hollow bearing seat, a material collecting box, a discharge partition plate, a material collecting partition plate, a screen, a collecting box, a sampling barrel and a three-way pipe;
the cloth disc is characterized in that a flow guide net is installed on the edge portion of the bottom end of the cloth disc, a guide disc is installed at the bottom end of the flow guide net, a flow guide ring is installed at the top end of the guide disc, a gathering groove is formed in the middle of the top end of the guide disc, a plurality of guide grooves are formed in the top end of the gathering groove at equal angles along the circumferential direction, and a plurality of feed inlets are formed in the outer surface of the hollow rotating rod, located in the gathering groove, at equal angles along the circumferential direction;
the improved reaction barrel comprises a reaction barrel bottom, a transfer box, a hollow bearing seat, a hollow rotary rod, a material collecting box, a discharging baffle plate, a material collecting box side end face, a material collecting baffle plate, a material collecting box side end face, a material collecting box, a three-way pipe, a collecting box, a sampling barrel and a sampling barrel, wherein the transfer box is embedded in the middle of the bottom of the reaction barrel, the hollow bearing seat is rotatably mounted at the top of the transfer box, the material collecting box side end face, the material collecting baffle plate is embedded in the bottom of the material collecting box, the three-way pipe is mounted in the middle of the bottom of the material collecting box, the collecting box is mounted on one side of the bottom of the material collecting box, the sampling barrel is connected with the material collecting box through the three-way pipe, and a screen is mounted in the connecting position of the three-way pipe and the sampling barrel.
Preferably, the net that leaks is installed in cloth dish bottom embedding, cloth dish and mounting bracket all are the boss form, the guide ring is the toper heliciform, discharge gate and cloth mouth wait high, the discharge gate bottom flushes with the fender material piece top, the feed supplement mouth bottom flushes with feed supplement box bottom, the cloth mouth is located position department between spacing net and the cloth dish, the bleeder valve is installed to the domatic position of reaction cylinder bottom, driving motor input and external power supply output electric connection.
Preferably, the filter screen is installed in the embedding of baffle disc bottom, the filter screen aperture is less than the screen aperture of leaking, the filter screen aperture is the same with the screen aperture, the baffle disc is the inversion boss form, the water conservancy diversion circle is the inversion coniform heliciform, water conservancy diversion circle screw direction is opposite with water conservancy diversion circle screw direction, it all reduces to hollow bull stick direction along the water conservancy diversion net gradually to gather groove and guide way bottom domatic, sampling barrel side end face mid-mounting has the sampling valve, it has the transportation drawer to collect box side end face mid-embedding slidable mounting.
Preferably, one side of the reaction cylinder is provided with a temperature control mechanism, and the temperature control mechanism comprises an adjusting mechanism, a mixing mechanism and a circulating conveying mechanism;
the adjusting mechanism comprises an adjusting cylinder, a hot air flow fixing cylinder, a hot air flow sleeve, a hot air flow outlet hole, a hot air flow air adjusting hole, a cold air flow fixing cylinder, a cold air flow sleeve, a cold air flow outlet hole, a cold air flow air adjusting hole, a limiting mounting plate, a piston, a connecting rod, a spring, a hot air flow outlet pipe and a cold air flow outlet pipe;
an adjusting cylinder is installed on one side of the reaction cylinder, a hot air fixing cylinder is installed on the side end face of the adjusting cylinder in an embedded mode, a hot air sleeve is installed on the outer side of the hot air fixing cylinder in a sliding mode, a plurality of hot air outlet holes are formed in the outer surface of the hot air fixing cylinder at equal angles along the circumferential direction, and a plurality of hot air adjusting holes are formed in the outer surface of the hot air sleeve at equal angles along the circumferential direction;
a cold air flow fixing barrel is embedded in the end face of the other side of the adjusting barrel, a cold air flow sleeve is slidably mounted on the outer side of the cold air flow fixing barrel, a plurality of cold air flow outlet holes are formed in the outer surface of the cold air flow fixing barrel at equal angles along the circumferential direction, and a plurality of cold air flow adjusting holes are formed in the outer surface of the cold air flow sleeve at equal angles along the circumferential direction;
the piston is embedded in the middle of the adjusting cylinder in a sliding mode, the limiting mounting plates are fixedly mounted at positions, located on two sides of the piston, in the adjusting cylinder, connecting rods are mounted in the middle of end faces of two sides of the piston, springs are sleeved on the outer sides of the connecting rods, a hot air outlet pipe is mounted at the top of the adjusting cylinder, located on one side of the piston, and a cold air outlet pipe is mounted at the top of the adjusting cylinder, located on the other side of the piston;
compared with the prior art, the invention has the beneficial effects that: the invention has scientific and reasonable structure and safe and convenient use;
1. the catalyst feeding component is arranged, and the catalyst can be conveyed to the surface of the material distribution disc in real time in the reaction process through the matching of the material supplementing hopper, the material supplementing box, the hollow shaft seat, the hollow rotating rod, the material supplementing port, the material discharging port, the material guide box and the material distribution port, so that the catalyst can be timely supplemented, the loss of the catalyst caused by reaction is avoided, the catalyst cannot be timely supplemented, the reaction rate is slower and slower, even partial reactants are caused, the subsequent reaction is incomplete, and the reaction quality is poor;
provide drive power through driving motor, through hollow bull stick, the cloth material mouth, the cloth dish, lead material circle and parting bead and cooperate, make the catalyst under centrifugal force, it is spacing to lead to the catalyst, make catalyst evenly distributed at cloth dish surface, make more abundant even and the reactant contact of catalyst, reaction efficiency and reaction quality have effectively been improved, and through keeping off the material circle, mounting bracket and spacing net, then can limit the catalyst at cloth dish surface, avoid it to scatter inside the reaction section of thick bamboo, when causing the inconvenient recovery of catalyst, collect the production of reaction and disturb, also avoid the catalyst to pile up cloth dish surface edge portion under centrifugal force effect simultaneously, cause the catalyst to utilize inadequately.
2. The catalyst recovery assembly is arranged, the small-particle catalyst after loss is limited and guided through the guide plate and the guide net, guided and collected through the guide ring, the collection groove and the guide groove, and then guided into the transfer box through the matching of the feed inlet and the hollow rotating rod, so that the small-particle catalyst after loss is timely transferred and collected in the reaction process, the continuous loss of the small-particle catalyst is avoided, the small-particle catalyst is scattered into a reaction liquid, reaction products are impure, and adverse effects are caused on the reaction;
and through the transfer box, the material collecting box, ejection of compact baffle and receipts material baffle cooperate, can avoid in the tiny particle catalyst collection process after to the loss, cause reaction liquid to leak excessively, cooperate through three-way pipe and screen cloth, can realize solid-liquid separation, make the reaction liquid along with the catalyst outflow get into the sampling bucket and sample and collect, the staff of being convenient for is follow-up samples through the sampling valve, in real time to the reaction process condition of accuse current stage reactant, with the supplementary catalytic dose of control, and the catalyst then gets into and collects the box and save, so that follow-up through transporting the drawer, retrieve the transportation.
In conclusion, the catalyst placing mechanism and the catalyst feeding assembly can supplement and feed the catalyst in real time in the reaction process, the catalyst is uniformly distributed, the reaction efficiency is ensured, incomplete reaction caused by catalyst loss of reactants is avoided, the reaction quality is poor, the catalyst recovery assembly can recover and transport the lost catalyst in real time in the reaction process, the loss catalyst is prevented from influencing the purity of reaction products, synchronous sampling can be realized, the catalyst supplementing amount is controlled, and the catalyst waste is avoided.
3. The adjusting mechanism is arranged, the hot air flow sleeve and the cold air flow sleeve can be driven to displace in real time according to air pressure through the matching of the adjusting cylinder, the limiting mounting plate, the piston, the connecting rod and the spring, the effective number of the hot air flow outlet hole, the hot air flow adjusting hole, the cold air flow outlet hole and the cold air flow adjusting hole can be adjusted in real time through the matching of the hot air flow fixing cylinder, the hot air flow sleeve, the cold air flow fixing cylinder and the cold air flow sleeve, so that the conveying amount of cold and hot air flows can be respectively adjusted, the temperature of mixed air can be adjusted in real time, the temperature of the mixed air flow is suitable for reaction, the temperature in the reaction cylinder is kept at a proper temperature, and the heat exchange efficiency is improved.
4. The temperature-variable bimetallic strip, the plugging plate, the sealing strip and the adjusting groove are matched, so that the plugging degree of a hot airflow outlet pipe and a cold airflow outlet pipe can be regulated and controlled in real time, the flow of cold airflow and hot airflow can be adjusted, the temperature of mixed gas can be corrected in time, the internal temperature of the reaction cylinder can be kept stable, and the stability and reliability of reaction can be improved;
can lead at the shutoff board displacement in-process through the guide arm, cooperate through ball, spin and guide pulley, can effectively reduce frictional resistance, make the accommodation process more sensitive.
5. Be provided with circulating transport mechanism, through the air feed chamber, the air duct cooperatees, can make the gaseous filter box that gets into that the reaction produced filter, cooperate through heating cabinet and heating strip, can heat the gaseous of reaction production, cooperate through air pump and filter box, can make the air after the purification get into the cooling tube and cool down through the inside coolant liquid of cooling box, through the air feed chamber, the cloth gas seat, inlet port and jet head cooperate, can make the gaseous and the clean air after the cooling that the reaction produced after the heating, spray inside the reaction cylinder after mixing, effectively improved the reaction in-process, the inside heat transfer volume and the heat transfer volume of reaction cylinder, make the inside temperature of reaction cylinder maintain dynamic balance, effectively improved reaction efficiency and quality.
Drawings
The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the principles of the invention and not to limit the invention.
In the drawings:
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a cross-sectional view of the present invention;
FIG. 3 is a schematic view of the structure of the reaction cylinder of the present invention;
FIG. 4 is a schematic diagram of the catalyst placement mechanism of the present invention;
FIG. 5 is a schematic view of the cloth disk structure of the present invention;
FIG. 6 is a schematic view of the hollow rotating shaft of the present invention;
FIG. 7 is a schematic view of the receiving partition of the present invention;
FIG. 8 is a schematic view of the temperature control mechanism of the present invention;
FIG. 9 is a schematic view of the hot gas flow sleeve configuration of the present invention;
FIG. 10 is a schematic view of the construction of the plugging plate of the present invention;
FIG. 11 is a schematic view of the idler construction of the present invention;
FIG. 12 is a schematic view of the gas distribution base of the present invention;
reference numbers in the figures: 1. a support; 2. a reaction cylinder; 3. a feeding hopper; 4. a stirring rod; 5. a catalyst placement mechanism; 6. a temperature control mechanism;
50. a catalyst delivery assembly; 501. a drive motor; 502. a material supplementing box; 503. a hollow shaft seat; 504. a hollow rotating rod; 505. a material supplementing port; 506. a material guide box; 507. a discharge port; 508. a material distribution port; 509. a material distribution disc; 5010. a material guiding ring; 5011. separating the material strip; 5012. a material blocking block; 5013. a material blocking ring; 5014. a mounting frame; 5015. a limiting net; 5016. a material supplementing hopper;
51. a catalyst recovery assembly; 511. a material guide plate; 512. a flow guide net; 513. a flow guide ring; 514. a collecting groove; 515. a guide groove; 516. a feed inlet; 517. a transfer box; 518. a hollow bearing seat; 519. a material collecting box; 5110. a discharge partition plate; 5111. a material receiving clapboard; 5112. screening a screen; 5113. a collection box; 5114. a sampling barrel; 5115. a three-way pipe;
60. an adjustment mechanism; 601. an adjusting cylinder; 602. a hot air flow fixing cylinder; 603. a hot gas flow sleeve; 604. hot air outlet holes; 605. a hot air flow air adjusting hole; 606. a cold airflow fixing cylinder; 607. a cold airflow sleeve; 608. a cold airflow outlet; 609. a cold airflow register; 6010. a limiting mounting plate; 6011. a piston; 6012. a connecting rod; 6013. a spring; 6014. a hot air outlet pipe; 6015. a cold airflow outlet pipe;
61. a mixing mechanism; 611. a mixing box; 612. an adjustment groove; 613. a plugging plate; 614. a sealing strip; 615. a ball bearing; 616. a linkage rod; 617. connecting blocks; 618. a guide bar; 619. rolling a ball; 6110. a drive block; 6111. a temperature-variable bimetal; 6112. a guide wheel; 6113. a rolling groove; 6114. a booster magnet; 6115. a drive magnet; 6116. a delivery pipe;
62. a circulating conveying mechanism; 621. an air delivery cavity; 622. an air delivery cavity; 623. an air distribution seat; 624. an air inlet; 625. a gas showerhead; 626. a guide plate; 627. an air pump; 628. a cooling tank; 629. a cooling pipe; 6210. a heating box; 6211. heating the strip; 6212. a filter cartridge; 6213. an air duct.
Detailed Description
The preferred embodiments of the present invention will be described in conjunction with the accompanying drawings, and it should be understood that they are presented herein only to illustrate and explain the present invention and not to limit the present invention.
Example (b): as shown in fig. 1-12, the present invention provides a technical solution, a reactor capable of increasing heat transfer capacity, comprising a support 1, a reaction cylinder 2 installed on the top of the support 1, a hopper 3 installed on the slope surface of the top of the reaction cylinder 2, a catalyst placement mechanism 5 installed inside the reaction cylinder 2, the catalyst placement mechanism 5 comprising a catalyst feeding component 50 and a catalyst recovery component 51;
the catalyst feeding assembly 50 comprises a driving motor 501, a feeding box 502, a hollow shaft seat 503, a hollow rotating rod 504, a feeding port 505, a guide box 506, a discharge port 507, a material distribution port 508, a material distribution disc 509, a guide ring 5010, a material separation strip 5011, a material blocking block 5012, a material blocking ring 5013, a mounting frame 5014, a limiting net 5015 and a feeding hopper 5016;
the top of the reaction barrel 2 is provided with a driving motor 501, the top end of the reaction barrel 2 is embedded with a feeding box 502, the middle parts of the top end and the bottom end of the feeding box 502 are respectively rotatably provided with a hollow shaft seat 503, the middle part of the feeding box 502 is rotatably provided with a hollow rotating rod 504, the output shaft of the driving motor 501 is connected with the hollow rotating rod 504 through the hollow shaft seat 503, and the outer surface of the hollow rotating rod 504, which is positioned at the inner position of the feeding box 502, is provided with a plurality of feeding ports 505 at equal angles along the circumferential direction;
a material guide box 506 is arranged in the middle of the outer surface of the hollow rotating rod 504, a plurality of material outlet openings 507 are formed in the position, located inside the material guide box 506, of the outer surface of the hollow rotating rod 504 at equal angles along the circumferential direction, a plurality of material distribution openings 508 are formed in the bottom of the outer surface of the material guide box 506 at equal angles along the circumferential direction, a material distribution plate 509 is arranged outside the material guide box 506, a material guide ring 5010 is arranged at the top end of the material distribution plate 509, and a plurality of material separation strips 5011 are arranged at the top end of the material distribution plate 509 at equal angles along the circumferential direction;
a material blocking block 5012 is arranged at the bottom of a material outlet 507 in the hollow rotating rod 504, a material blocking ring 5013 is arranged at the top end of a material distribution disc 509, a mounting frame 5014 is arranged at the top end of the material blocking ring 5013 on the outer side of the material guiding box 506, a plurality of limiting nets 5015 are embedded into the top end of the mounting frame 5014 at equal angles along the circumferential direction, a leakage net is embedded into the bottom of the material distribution disc 509, the material distribution disc 509 and the mounting frame 5014 are both in a boss shape, the material guiding ring 5010 is in a conical spiral shape, the material outlet 507 and a material distribution port 508 are equal in height, the bottom end of the material outlet 507 is flush with the top end of the material blocking block 5012, the bottom end of a material supplementing port 505 is flush with the bottom end of the material distribution box 502, the material distribution port 508 is arranged at a position between the limiting net 5015 and the material distribution disc 509, a discharge valve is arranged at the slope surface at the bottom of the reaction cylinder 2, an input end of a driving motor 501 is electrically connected with an external power supply output end so as to supplement catalyst in time, and a material supplementing hopper 5016 is arranged at the top of the side end surface of the material distribution box 502;
the outer surface of the hollow rotating rod 504 is provided with a plurality of stirring rods 4 at equal distance at the two sides of the material distribution disk 509, and the bottom of the material distribution disk 509 is provided with the catalyst recovery component 51.
The catalyst recovery component 51 comprises a material guide disc 511, a flow guide net 512, a flow guide ring 513, a collection groove 514, a guide groove 515, a feed inlet 516, a transfer box 517, a hollow shaft bearing 518, a collection box 519, a discharge partition plate 5110, a material receiving partition plate 5111, a screen 5112, a collection box 5113, a sampling barrel 5114 and a three-way pipe 5115;
a flow guide net 512 is installed at the edge part of the bottom end of the cloth disc 509, a guide disc 511 is installed at the bottom end of the flow guide net 512, a flow guide ring 513 is installed at the top end of the guide disc 511, a collection groove 514 is formed in the middle of the top end of the guide disc 511, a plurality of guide grooves 515 are formed in the top end of the collection groove 514 at equal angles along the circumferential direction, and a plurality of feed inlets 516 are formed in the outer surface of the hollow rotating rod 504, which is located in the collection groove 514, at equal angles along the circumferential direction;
a transit box 517 is embedded in the middle of the bottom end of the reaction barrel 2, a hollow shaft bearing 518 is rotatably arranged at the top end of the transit box 517, the transit box 517 is connected with the hollow rotating rod 504 through the hollow shaft bearing 518, a material collecting box 519 is arranged at the bottom end of the transit box 517, a discharging partition plate 5110 is embedded in the top of the side end face of the material collecting box 519 in a sliding manner, a material collecting partition plate 5111 is embedded in the bottom of the side end face of the material collecting box 519 in a sliding manner, a three-way pipe 5115 is arranged in the middle of the bottom end of the material collecting box 519, a collecting box 5113 is arranged on one side of the bottom of the material collecting box 519, a sampling barrel 5114 is arranged on the other side of the bottom of the material collecting box 519, both the collecting box 5113 and the sampling barrel 5114 are connected with the material collecting box 519 through the three-way pipe 5115, a screen 5112 is arranged at the connecting position of the inside of the three-way pipe 5115 and the sampling barrel 5114, a filter screen is embedded in the bottom of the guide plate 511, the diameter of the filter screen is smaller than the aperture of the screen 5112, the aperture of the filter screen is the same as that of the screen 5112, the guide plate 511 is in an inverted boss shape, the guide ring 513 is in an inverted conical spiral shape, the spiral direction of the guide ring 513 is opposite to that of the guide ring 5010, the bottom slopes of the collecting groove 514 and the guide groove 515 are gradually reduced from the guide net 512 to the hollow rotating rod 504, a sampling valve is arranged in the middle of the side end face of the sampling barrel 5114, and a transfer drawer is embedded in the middle of the side end face of the collecting box 5113 and slidably mounted in order to transfer and recover lost catalyst in time.
A temperature control mechanism 6 is arranged on one side of the reaction cylinder 2, and the temperature control mechanism 6 comprises an adjusting mechanism 60, a mixing mechanism 61 and a circulating conveying mechanism 62;
the adjusting mechanism 60 comprises an adjusting cylinder 601, a hot air flow fixing cylinder 602, a hot air flow sleeve 603, a hot air flow outlet 604, a hot air flow adjusting hole 605, a cold air flow fixing cylinder 606, a cold air flow sleeve 607, a cold air flow outlet 608, a cold air flow adjusting hole 609, a limiting mounting plate 6010, a piston 6011, a connecting rod 6012, a spring 6013, a hot air flow outlet 6014 and a cold air flow outlet 6015;
an adjusting cylinder 601 is installed on one side of the reaction cylinder 2, a hot air flow fixing cylinder 602 is installed on the end face of the adjusting cylinder 601 in an embedded manner, a hot air flow sleeve 603 is installed outside the hot air flow fixing cylinder 602 in a sliding manner, a plurality of hot air flow outlet holes 604 are formed in the outer surface of the hot air flow fixing cylinder 602 at equal angles along the circumferential direction, and a plurality of hot air flow adjusting holes 605 are formed in the outer surface of the hot air flow sleeve 603 at equal angles along the circumferential direction;
the other side end face of the adjusting cylinder 601 is embedded with a cold air flow fixing cylinder 606, the outer side of the cold air flow fixing cylinder 606 is slidably provided with a cold air flow sleeve 607, the outer surface of the cold air flow fixing cylinder 606 is provided with a plurality of cold air flow outlet holes 608 at equal angles along the circumferential direction, and the outer surface of the cold air flow sleeve 607 is provided with a plurality of cold air flow adjusting holes 609 at equal angles along the circumferential direction;
a piston 6011 is embedded in the middle of the adjusting cylinder 601 in a sliding manner, limiting mounting plates 6010 are fixedly mounted at positions, located on two sides of the piston 6011, in the adjusting cylinder 601, connecting rods 6012 are mounted in the middle of end faces of the two sides of the piston 6011, a spring 6013 is sleeved outside the connecting rods 6012, the hot air flow sleeve 603 and the cold air flow sleeve 607 are connected with the piston 6011 through the connecting rods 6012, the piston 6011 is connected with the limiting mounting plates 6010 through the spring 6013 so as to adjust the cold and hot air flow ratio in time, a hot air flow outlet pipe 6014 is mounted at one side, located on the piston 6011, of the top of the adjusting cylinder 601, and a cold air flow outlet pipe 6015 is mounted at the other side, located on the piston 6011, of the top of the adjusting cylinder 601;
the top of the adjusting cylinder 601 is provided with a mixing mechanism 61, and the top of the adjusting cylinder 601 is provided with a circulating conveying mechanism 62.
The mixing mechanism 61 comprises a mixing box 611, an adjusting groove 612, a blocking plate 613, a sealing strip 614, a ball 615, a linkage 616, a connecting block 617, a guide rod 618, a rolling ball 619, a driving block 6110, a temperature-variable bimetallic strip 6111, a guide wheel 6112, a rolling groove 6113, a power-assisted magnet 6114, a driving magnet 6115 and a conveying pipe 6116;
a mixing box 611 is installed at the top of the adjusting cylinder 601, the mixing box 611 is connected with the adjusting cylinder 601 through a hot air outlet pipe 6014 and a cold air outlet pipe 6015, an adjusting groove 612 is formed in the bottom end of the mixing box 611, a blocking plate 613 is installed in the adjusting groove 612 in a sliding mode, a sealing strip 614 is installed in the middle of the bottom end of the blocking plate 613, and a plurality of balls 615 are evenly installed at the bottom end of the blocking plate 613, located on two sides of the sealing strip 614, in a rolling mode at equal intervals;
the middle part of the top end of the blocking plate 613 is provided with a linkage lever 616, the top end of the linkage lever 616 is provided with a connecting block 617, the end surfaces of two sides of the connecting block 617 are provided with guide rods 618, the middle part of the end surface of the side of the guide rod 618 is provided with a rolling ball 619 in a rolling manner, the top end of the connecting block 617 is provided with a driving block 6110, the middle part of the top end of the inner side of the mixing box 611 is provided with a temperature-variable bimetallic strip 6111, the temperature-variable bimetallic strip 6111 is deformed due to the different thermal expansion coefficients of all component layers, when the temperature changes, the deformation of the driving layer is larger than the deformation of the driven layer, so that the whole temperature-variable bimetallic strip 6111 is bent towards one side of the driven layer, the curvature of the composite material is changed to generate deformation, the layer with higher expansion coefficient is called as the driving layer, and the layer with lower expansion coefficient is called as the driven layer, guide wheel 6112 is rotatably mounted at the bottom end of temperature-variable bimetallic strip 6111, after temperature-variable bimetallic strip 6111 deforms, the movable end of temperature-variable bimetallic strip can abut against guide wheel 6112, drive guide wheel 6112 displaces, rolling groove 6113 is formed in the middle of drive block 6110 corresponding to guide wheel 6112, booster magnets 6114 are mounted in the middle of end faces on two sides of drive block 6110, booster magnets 6114 and drive magnets 6115 are opposite magnets, sliding grooves are formed in the end faces on two sides inside mixing box 611 corresponding to guide rod 618, pressure relief valves are mounted on the edge of the top end of mixing box 611, so that guiding and pressure relief can be performed, drive magnets 6115 are mounted in the middle of end faces on two sides of mixing box 611 corresponding to booster magnets 6114 through supporting rods, and conveying pipe 6116 is mounted in the middle of the top end outside mixing box 611.
The circulating conveying mechanism 62 comprises an air conveying cavity 621, an air feeding cavity 622, an air distribution seat 623, an air inlet hole 624, an air spraying head 625, a guide plate 626, an air pump 627, a cooling box 628, a cooling pipe 629, a heating box 6210, a heating strip 6211, a filter box 6212 and an air guide pipe 6213;
an air conveying cavity 621 is formed in the middle of the side wall of the reaction barrel 2, an air feeding cavity 622 is formed in the side wall of the reaction barrel 2 and located at the top of the air conveying cavity 621, an air distribution seat 623 is rotatably mounted inside the air feeding cavity 622, a plurality of air inlet holes 624 are formed in the middle of the end face of the side of the air distribution seat 623 in an equiangular manner along the circumferential direction, a plurality of air nozzles 625 are mounted at the bottom end of the air distribution seat 623 in an equiangular manner along the circumferential direction, and guide plates 626 are mounted at the top end edge and the bottom end edge of the air distribution seat 623;
an air pump 627 is installed on one side of the adjusting cylinder 601, a cooling box 628 is installed at the bottom of the air pump 627, a cooling pipe 629 is installed inside the cooling box 628, a heating box 6210 is installed at the position of the bottom of the adjusting cylinder 601, which is located on one side of the cooling pipe 629, a heating strip 6211 is installed inside the heating box 6210, filter boxes 6212 are installed in the middle of the side end face of the cooling box 628 and in the middle of the side end face of the heating box 6210, an air guide pipe 6213 is installed at the top end of the filter box 6212 in the middle of the side end face of the heating box 6210, a guide chute is formed in the air feeding cavity 622 corresponding to the position of the guide plate 626, the guide plate 626 and the guide chute are both annular, the cross sections of the guide plate 626 and the guide chute are both T-shaped, the top of the inner wall of the reaction cylinder 2 is provided with a communicating hole corresponding to the position of the air delivery cavity 621, the air delivery cavity 621 is connected with a filter box 6212 through an air duct 6213, a cooling pipe 629 is connected with the air inlet end of an air pump 627 through a pipeline, the air outlet end of the air pump 627 is connected with the cold air flow fixing cylinder 606 through a pipeline, the middle part of the top end of the heating box 6210 is connected with the hot air flow fixing cylinder 602 through a pipeline, the air delivery cavity 622 is connected with the mixing box 611 through a conveying pipe 6116, the cooling box 628 is internally filled with cooling liquid, the input end of the air pump 627 is electrically connected with the output end of an external power supply, so that the air flow circulation is realized, and the heat exchange rate and the heat transfer amount are improved.
The working principle and the using process of the invention are as follows: when the reactor is actually used, firstly, the support 1 is stably placed on the ground, then materials are put into the reaction cylinder 2 through the feeding hopper 3, then the catalyst is put into the feeding box 502 through the feeding hopper 5016, then the driving motor 501 is started, and in the initial stage of reaction, the driving motor 501 is controlled to rotate at a low speed;
an output shaft of the driving motor 501 drives the hollow shaft seat 503 to rotate through rotation, then the hollow shaft seat 503 drives the hollow rotating rod 504 to rotate, in the rotation process of the hollow rotating rod 504, a catalyst in the material supplementing box 502 enters a cavity in the hollow rotating rod 504 through the material supplementing opening 505 and then enters the material guide box 506 through the material outlet 507, the material blocking block 5012 blocks the catalyst and prevents the catalyst from entering the middle rotating box 517, the material guide box 506 rotates along with the hollow rotating rod 504, and in the rotation process of the material guide box 506, the catalyst in the material guide box 506 rolls down to the surface of the material distribution disk 509 through the material distribution opening 508 under the action of centrifugal force;
the catalyst rolled on the surface of the distribution plate 509 rolls from inside to outside along the guide ring 5010 under the action of centrifugal force and is uniformly dispersed on the surface of the distribution plate 509 under the grid spacing action of the material separating strips 5011 by the limiting guide of the guide ring 5010, and the catalyst can be prevented from being thrown out of the surface of the distribution plate 509 and scattering into the reaction cylinder 2 under the limiting action of the material blocking ring 5013, the mounting rack 5014 and the limiting net 5015, and meanwhile, the catalyst can be limited between the limiting net 5015 and the distribution plate 509, so that the catalyst is prevented from being accumulated on the edge part of the surface of the distribution plate 509 due to centrifugal force;
along with the reaction of materials, the catalyst is lost, so that part of catalyst particles become small, the catalyst with the small part of particles falls onto the surface of the material guide plate 511 through the leakage net, and the flow guide net 512 can limit and guide the catalyst particles in the falling process of the catalyst, so that the catalyst particles are prevented from falling into the reaction cylinder 2 after being separated from the material distribution plate 509;
the catalyst falling on the surface of the material guide disc 511 rolls from outside to inside along the flow guide ring 513 due to the opposite spiral direction of the flow guide ring 513 and the material guide ring 5010, and finally is collected on the surface of the collection groove 514, and under the flow guide effect of the collection groove 514 and the guide groove 515, part of the catalyst with reduced particles enters the cavity inside the hollow rotating rod 504 through the feed port 516, then enters the transfer box 517 through the cavity inside the hollow rotating rod 504, enters the catalyst inside the transfer box 517, is blocked by the discharge partition plate 5110, and is temporarily stored inside the transfer box 517;
after the reaction lasts for a period of time, the discharging partition plate 5110 is pulled to enable the discharging partition plate 5110 to displace and leak out of the through hole at the bottom of the transit box 517, then a part of the catalyst with smaller particles enters the material collecting box 519 through the transit box 517 for temporary storage, then the discharging partition plate 5110 is pushed to reset and seal the through hole at the bottom of the transit box 517, then the material collecting partition plate 5111 is pulled and leaks out of the through hole at the bottom of the material collecting box 519, the catalyst entering the material collecting box 519 enters the three-way pipe 5115 through the through hole, under the sieving action of the screen 5112, the reaction liquid flowing out along with the catalyst enters the sampling barrel 5114 through the three-way pipe 5115 for sampling and collection, so that a worker can sample through the sampling valve subsequently, control the reaction progress of the reactant at the current stage in real time, and the catalyst enters the collecting box 5113 through the three-way pipe 5115 for storage, so that the catalyst can be recovered and transported subsequently;
after the reaction lasts for a period of time, the catalyst with reduced partial particles is transported and recovered, meanwhile, the catalyst is put into the feeding box 502 through the feeding hopper 5016, the catalyst in the feeding box 502 enters the cavity in the hollow rotating rod 504 through the feeding port 505 and then enters the material guide box 506 through the discharging port 507, the material guide box 506 rotates along with the hollow rotating rod 504, and then the catalyst in the material guide box 506 rolls down to the surface of the material distribution disk 509 through the material distribution port 508 under the action of centrifugal force in the rotating process of the material guide box 506, so that the catalyst can be supplemented in real time, and the reaction efficiency is ensured;
in the reaction process, gas is generated in real time along with the reaction of reactants, the generated gas enters the gas transmission cavity 621 through the communicating hole, the gas entering the gas transmission cavity 621 enters the filter box 6212 through the gas guide pipe 6213, the gas enters the heating box 6210 through the filter box 6212 after being filtered by the filter box 6212 and is heated through the heating strip 6211, the gas generated by the reaction has certain heat, the phase change has a preheating effect, the heating difficulty is effectively reduced, the heating efficiency is improved, the heated hot gas flows enter the hot gas flow fixing cylinder 602 through the pipeline, and then enters the adjusting cylinder 601 through the gas outlet hole 604 and the hot gas flow adjusting hole 605 at the overlapped part of the hot gas flow fixing cylinder 602 and the hot gas flow sleeve 603, and then the hot gas flows enter the mixing box 611 through the hot gas outlet pipe 6014;
when hot air flow enters the adjusting cylinder 601, the air pump 627 can pump external air in real time, the external air becomes clean air flow under the filtering action of the filter box 6212, the clean air flow can be pumped to the cooling pipe 629 by the air pump 627, and then the clean air flow is cooled by the cooling liquid in the cooling box 628 to become cold air flow, the cold air flow can be conveyed to the cold air flow fixing cylinder 606 by the air pump 627, and then enters the adjusting cylinder 601 through the cold air flow outlet hole 608 and the cold air flow adjusting hole 609 at the overlapping part of the cold air flow fixing cylinder 606 and the cold air flow sleeve 607, and then enters the mixing box 611 through the cold air flow outlet pipe 6015;
the cold air flow and the hot air flow entering the mixing box 611 are mixed in the mixing box 611, so that the temperature of the air flow is neutralized, the temperature of the air flow is changed into a temperature suitable for reaction, the air flow with the over-neutralized temperature enters the air supply cavity 622 through the air guide tube 6213, then enters the air distribution seat 623 through the air inlet hole 624 and finally is ejected out through the air nozzle 625, and the air flow ejected out of the air nozzle 625 can be uniformly sprayed into the reaction cylinder 2 under the guiding action of the guide plate 626 and rotates along with the hollow rotating rod 504, so that the air temperature in the reaction cylinder 2 can be adjusted in real time;
in the reaction process, along with the fluctuation of the reaction speed, the generated gas velocity also fluctuates, which causes the ratio of the cold air flow and the hot air flow entering the mixing box 611 to change, at this time, the temperature of the mixed air flow changes correspondingly, and along with the change of the temperature of the mixed air flow, the mixed air flow blows to the surface of the temperature-variable bimetallic strip 6111, so that the temperature-variable bimetallic strip 6111 is bent to different degrees;
when the temperature of the mixed gas is high, the temperature-variable bimetallic strip 6111 bends towards one side of the hot gas outlet pipe 6014, when the temperature of the mixed gas is low, the temperature-variable bimetallic strip 6111 bends towards one side of the cold gas outlet pipe 6015, the bending degree of the temperature-variable bimetallic strip 6111 is changed correspondingly due to different temperatures, the bending of the temperature-variable bimetallic strip 6111 drives the guide wheel 6112 to displace, the guide wheel 6112 rolls in the rolling groove 6113 and simultaneously pushes the driving block 6110 to displace, the driving block 6110 displaces to shorten the distance between the driving magnet 6115 and the assisting magnet 6114, and under the attraction effect of magnetic force, the driving block 6110 can be assisted to displace, so that the displacement difficulty is reduced;
the driving block 6110 can drive the connecting block 617 to displace, the connecting block 617 can displace in a fixed direction under the guiding action of the guide rod 618, the rolling ball 619 reduces the displacement difficulty of the guide rod 618, the connecting block 617 can drive the linkage rod 616 to displace, and further drive the blocking plate 613 to displace in the adjusting groove 612, the rolling ball 615 effectively reduces the friction force of the blocking plate 613 during the displacement in the adjusting groove 612, so that the displacement is smoother, the reaction is more sensitive, the sealing strip 614 prevents cold and hot air from being mixed in advance, the blocking plate 613 displaces in the adjusting groove 612, the blocking degree of the blocking plate 613 on the hot air outlet pipe 6014 and the cold air outlet pipe 6015 can be changed, and further the air pressure on two sides of the piston 6011 can be changed;
when the temperature is higher, the hot air outlet pipe 6014 is blocked to a greater degree, which causes a larger air pressure at one side of the hot air sleeve 603 in the adjusting cylinder 601, and due to the unbalanced air pressure, the air flow pushes the piston 6011 to displace towards one side of the cold air fixed cylinder 606, and further drives the connecting rod 6012 to drive the hot air sleeve 603 and the cold air sleeve 607 to synchronously displace;
further, the overlapping portion of the hot air flow fixing cylinder 602 and the hot air flow sleeve 603 becomes smaller, while the overlapping portion of the cold air flow fixing cylinder 606 and the cold air flow sleeve 607 becomes larger, because the overlapping portion of the hot air flow outlet hole 604 and the hot air flow adjusting hole 605, and the cold air flow outlet hole 608 and the cold air flow adjusting hole 609 is an effective portion, the effective number of the hot air flow outlet hole 604 and the hot air flow adjusting hole 605 is reduced, and the effective number of the cold air flow outlet hole 608 and the cold air flow adjusting hole 609 is increased, so that the hot air flow conveying amount is reduced, and the cold air flow conveying amount is increased;
when the temperature is relatively low, the piston 6011 will displace towards one side of the hot air flow fixing cylinder 602, so that the hot air flow delivery rate is increased, and the cold air flow delivery rate is decreased, thereby realizing real-time adjustment of the cold and hot air flow, correcting the mixed gas temperature in time, ensuring that the mixed air flow temperature becomes the temperature suitable for reaction, ensuring that the reaction in the reaction cylinder 2 is carried out at a proper temperature in real time, effectively improving the heat transfer rate, and improving the reaction efficiency and quality;
in the reaction process, when atmospheric pressure was too high, can carry out the pressure release through the relief valve, guaranteed work safety, because the gas has been filtered this moment, also effectively avoided causing the pollution.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that changes may be made in the embodiments and/or equivalents thereof without departing from the spirit and scope of the invention. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (10)

1. A reactor capable of increasing the heat transfer capacity, comprising a support (1), characterized in that: the top of the support (1) is provided with a reaction cylinder (2), the top slope surface of the reaction cylinder (2) is provided with a feeding hopper (3), a catalyst placing mechanism (5) is arranged in the reaction cylinder (2), and the catalyst placing mechanism (5) comprises a catalyst feeding component (50) and a catalyst recovery component (51);
the catalyst feeding assembly (50) comprises a driving motor (501), a feeding box (502), a hollow shaft seat (503), a hollow rotating rod (504), a feeding port (505), a material guide box (506), a material outlet (507), a material distribution port (508), a material distribution disc (509), a material guide ring (5010), a material separation strip (5011), a material blocking block (5012), a material blocking ring (5013), an installation rack (5014), a limiting net (5015) and a feeding hopper (5016);
the reaction barrel (2) is provided with a driving motor (501) at the top, a material supplementing box (502) is embedded into the top end of the reaction barrel (2), hollow shaft seats (503) are rotatably arranged in the middle of the top end and the middle of the bottom end of the material supplementing box (502), a hollow rotating rod (504) is rotatably arranged in the middle of the material supplementing box (502), an output shaft of the driving motor (501) is connected with the hollow rotating rod (504) through the hollow shaft seats (503), and a plurality of material supplementing ports (505) are arranged on the outer surface of the hollow rotating rod (504) at positions inside the material supplementing box (502) at equal angles along the circumferential direction;
the middle part of the outer surface of the hollow rotating rod (504) is provided with a material guide box (506), the outer surface of the hollow rotating rod (504) is provided with a plurality of material outlets (507) at equal angles along the circumferential direction at the position located inside the material guide box (506), the bottom of the outer surface of the material guide box (506) is provided with a plurality of material distribution ports (508) at equal angles along the circumferential direction, a material distribution disk (509) is arranged outside the material guide box (506), the top end of the material distribution disk (509) is provided with a material guide ring (5010), and the top end of the material distribution disk (509) is provided with a plurality of material separation strips (5011) at equal angles along the circumferential direction;
a material blocking block (5012) is arranged in the hollow rotating rod (504) and located at the bottom of the discharge port (507), a material blocking ring (5013) is arranged on the edge of the top end of the cloth disc (509), a mounting frame (5014) is arranged on the outer side of the material guide box (506) and located at the top of the material blocking ring (5013), a plurality of limiting nets (5015) are embedded into the top of the mounting frame (5014) at equal angles along the circumferential direction, and a material supplementing hopper (5016) is arranged at the top of the side end face of the material supplementing box (502);
a plurality of stirring rods (4) are uniformly arranged on the outer surface of the hollow rotating rod (504) at equal distances at the positions on two sides of the distribution plate (509), and the catalyst recovery assembly (51) is arranged at the bottom of the distribution plate (509).
2. The reactor capable of improving heat transfer capacity of claim 1, wherein the catalyst recovery assembly (51) comprises a material guide disc (511), a flow guide net (512), a flow guide ring (513), a collecting groove (514), a guide groove (515), a material inlet (516), a transfer box (517), a hollow shaft bearing seat (518), a collecting box (519), a discharging partition plate (5110), a material collecting partition plate (5111), a screen (5112), a collecting box (5113), a sampling barrel (5114) and a three-way pipe (5115);
a guide net (512) is installed on the edge portion of the bottom end of the distribution disc (509), a guide disc (511) is installed at the bottom end of the guide net (512), a guide ring (513) is installed at the top end of the guide disc (511), a gathering groove (514) is formed in the middle of the top end of the guide disc (511), a plurality of guide grooves (515) are formed in the top end of the gathering groove (514) at equal angles along the circumferential direction, and a plurality of feed inlets (516) are formed in the position, located inside the gathering groove (514), of the outer surface of the hollow rotating rod (504) at equal angles along the circumferential direction;
the reaction cylinder (2) bottom middle part embedding is installed with transit box (517), transit box (517) top is rotated and is installed hollow bearing frame (518), transit box (517) is connected with hollow bull stick (504) through hollow shaft bearing frame (518), the collection box (519) is installed to transit box (517) bottom, the embedding slidable mounting of collection box (519) side end surface top has ejection of compact baffle (5110), the embedding slidable mounting of collection box (519) side end surface bottom has receipts material baffle (5111), collection box (519) bottom middle part installs three-way pipe (5115), collection box (5113) is installed to collection box (519) bottom one side, collection box (5114) is installed to collection box (519) bottom opposite side, collection box (5113) and sampling bucket (5114) all are connected with collection box (519) through three-way pipe (5115), screen cloth (5112) are installed to the inside and sampling bucket (5114) the hookup location of three-way pipe (5115).
3. The reactor capable of improving the heat transfer quantity according to claim 1, wherein a leakage net is embedded in the bottom of the material distribution disc (509), the material distribution disc (509) and the mounting frame (5014) are both in a boss shape, the material guide ring (5010) is in a conical spiral shape, the height of the material outlet (507) and the height of the material distribution opening (508) are equal, the bottom end of the material outlet (507) is flush with the top end of the material blocking block (5012), the bottom end of the material supplementing opening (505) is flush with the bottom end of the material supplementing box (502), the material distribution opening (508) is located at a position between the limiting net (5015) and the material distribution disc (509), a discharge valve is installed at the slope position of the bottom of the reaction cylinder (2), and the input end of the driving motor (501) is electrically connected with the output end of an external power supply.
4. The reactor capable of improving the heat transfer capacity as claimed in claim 2, wherein a filter screen is embedded in the bottom of the guide plate (511), the aperture of the filter screen is smaller than that of the filter screen, the aperture of the filter screen is the same as that of the screen (5112), the guide plate (511) is in an inverted boss shape, the guide ring (513) is in an inverted cone-shaped spiral shape, the spiral direction of the guide ring (513) is opposite to that of the guide ring (5010), the slope surfaces at the bottom ends of the collection groove (514) and the guide groove (515) are gradually reduced along the direction from the guide net (512) to the hollow rotating rod (504), the sampling barrel (5114) is provided with a sampling valve at the middle part of the side end surface, and a transfer drawer is embedded in the middle part of the side end surface of the collection box (5113) and slidably provided with a transfer drawer.
5. The reactor capable of improving heat transfer capacity according to claim 1, wherein a temperature control mechanism (6) is installed on one side of the reaction cylinder (2), and the temperature control mechanism (6) comprises an adjusting mechanism (60), a mixing mechanism (61) and a circulating conveying mechanism (62);
the adjusting mechanism (60) comprises an adjusting cylinder (601), a hot air flow fixing cylinder (602), a hot air flow sleeve (603), a hot air flow outlet hole (604), a hot air flow adjusting hole (605), a cold air flow fixing cylinder (606), a cold air flow sleeve (607), a cold air flow outlet hole (608), a cold air flow adjusting hole (609), a limiting mounting plate (6010), a piston (6011), a connecting rod (6012), a spring (6013), a hot air flow outlet pipe (6014) and a cold air flow outlet pipe (6015);
an adjusting cylinder (601) is installed on one side of the reaction cylinder (2), a hot air flow fixing cylinder (602) is installed on the end face of the side of the adjusting cylinder (601) in an embedded mode, a hot air flow sleeve (603) is installed on the outer side of the hot air flow fixing cylinder (602) in a sliding mode, a plurality of hot air flow outlet holes (604) are formed in the outer surface of the hot air flow fixing cylinder (602) at equal angles along the circumferential direction, and a plurality of hot air flow air adjusting holes (605) are formed in the outer surface of the hot air flow sleeve (603) at equal angles along the circumferential direction;
a cold air flow fixing cylinder (606) is embedded in the end face of the other side of the adjusting cylinder (601), a cold air flow sleeve (607) is slidably mounted on the outer side of the cold air flow fixing cylinder (606), a plurality of cold air flow outlet holes (608) are formed in the outer surface of the cold air flow fixing cylinder (606) at equal angles along the circumferential direction, and a plurality of cold air flow adjusting holes (609) are formed in the outer surface of the cold air flow sleeve (607) at equal angles along the circumferential direction;
a piston (6011) is embedded in the middle of the adjusting cylinder (601) in a sliding mode, limiting mounting plates (6010) are fixedly mounted at positions, located on two sides of the piston (6011), in the adjusting cylinder (601), connecting rods (6012) are mounted in the middle of end faces on two sides of the piston (6011), springs (6013) are sleeved on the outer sides of the connecting rods (6012), a hot air outlet pipe (6014) is mounted at the top of the adjusting cylinder (601) and located on one side of the piston (6011), and a cold air outlet pipe (6015) is mounted at the top of the adjusting cylinder (601) and located on the other side of the piston (6011);
the mixing mechanism (61) is installed at the top of the adjusting cylinder (601), and the circulating conveying mechanism (62) is installed at the top of the adjusting cylinder (601).
6. The reactor capable of improving the heat transfer capacity according to claim 5, wherein the mixing mechanism (61) comprises a mixing box (611), an adjusting groove (612), a blocking plate (613), a sealing strip (614), a ball (615), a linkage rod (616), a connecting block (617), a guide rod (618), a rolling ball (619), a driving block (6110), a temperature-variable bimetallic strip (6111), a guide wheel (6112), a rolling groove (6113), a power-assisted magnet (6114), a driving magnet (6115) and a conveying pipe (6116);
a mixing box (611) is installed at the top of the adjusting cylinder (601), the mixing box (611) is connected with the adjusting cylinder (601) through a hot air outlet pipe (6014) and a cold air outlet pipe (6015), an adjusting groove (612) is formed in the bottom end of the mixing box (611), a blocking plate (613) is installed in the adjusting groove (612) in a sliding mode, a sealing strip (614) is installed in the middle of the bottom end of the blocking plate (613), and a plurality of balls (615) are evenly installed on the bottom end of the blocking plate (613) on two sides of the sealing strip (614) in a rolling mode at equal intervals;
the utility model discloses a temperature-variable double-metal sheet (6111), including shutoff board (613) top end mid-mounting have trace (616), trace (617) are installed on trace (616) top, guide arm (618) are all installed to connecting block (617) both sides terminal surface, guide arm (618) side end face middle part is rolled and is installed spin (619), driving block (6110) are installed on connecting block (617) top, mixing box (611) inboard top mid-mounting has temperature-variable double-metal sheet (6111), guide pulley (6112) are installed in temperature-variable double-metal sheet (6111) bottom rotation, driving block (6110) middle part corresponds guide pulley (6112) position department and has seted up rolling groove (6113), helping hand magnet (6114) are all installed at driving block (6110) both sides terminal surface middle part, mixing box (611) both sides terminal surface middle part corresponds helping hand magnet (6114) position department and installs driving magnet (6115) through branch, mixing box (611) outside top mid-mounting has conveyer pipe (6116).
7. The reactor capable of improving heat transfer capacity according to claim 5, wherein the circulating conveying mechanism (62) comprises an air conveying cavity (621), an air feeding cavity (622), an air distribution seat (623), an air inlet hole (624), an air nozzle (625), a guide plate (626), an air pump (627), a cooling box (628), a cooling pipe (629), a heating box (6210), a heating strip (6211), a filter box (6212) and an air guide pipe (6213);
an air conveying cavity (621) is formed in the middle of the side wall of the reaction cylinder (2), an air sending cavity (622) is formed in the side wall of the reaction cylinder (2) and located at the top of the air conveying cavity (621), an air distribution seat (623) is rotatably installed inside the air sending cavity (622), a plurality of air inlet holes (624) are formed in the middle of the side end face of the air distribution seat (623) at equal angles along the circumferential direction, a plurality of air nozzles (625) are installed at the bottom end of the air distribution seat (623) at equal angles along the circumferential direction, and guide plates (626) are installed on the top end edge portion and the bottom end edge portion of the air distribution seat (623);
air pump (627) are installed to regulation section of thick bamboo (601) one side, cooler bin (628) are installed to air pump (627) bottom, cooler bin (628) internally mounted has cooling tube (629), it installs heating cabinet (6210) to be located cooling tube (629) one side position department to adjust section of thick bamboo (601) bottom, heating cabinet (6210) internally mounted has heating strip (6211), filter cartridge (6212) are all installed in cooler bin (628) side end face middle part and heating cabinet (6210) side end face middle part, air duct (6213) are installed on filter cartridge (6212) top at heating cabinet (6210) side end face middle part.
8. The reactor capable of increasing the heat transfer capacity as claimed in claim 5, wherein the hot air flow sleeve (603) and the cold air flow sleeve (607) are connected with a piston (6011) through a connecting rod (6012), and the piston (6011) is connected with a limiting mounting plate (6010) through a spring (6013).
9. The reactor capable of improving heat transfer capacity according to claim 6, wherein the booster magnet (6114) and the driving magnet (6115) are opposite magnets, sliding grooves are formed in the end faces of two sides of the interior of the mixing box (611) corresponding to the guide rod (618), and a pressure release valve is installed on the edge of the top end of the mixing box (611).
10. The reactor capable of improving heat transfer capacity according to claim 7, wherein a guide chute is formed in the air sending chamber (622) corresponding to the position of the guide plate (626), the guide plate (626) and the guide chute are both annular, the cross sections of the guide plate (626) and the guide chute are both T-shaped, a communication hole is formed in the top of the inner wall of the reaction cylinder (2) corresponding to the position of the air sending chamber (621), the air sending chamber (621) is connected with the filter box (6212) through an air duct (6213), the cooling pipe (629) is connected with the air inlet end of the air pump (627) through a pipeline, the air outlet end of the air pump (627) is connected with the cold air flow fixing cylinder (606) through a pipeline, the middle part of the top end of the heating chamber (6210) is connected with the hot air flow fixing cylinder (602) through a pipeline, the air sending chamber (622) is connected with the mixing chamber (611) through a conveying pipe (6116), the cooling liquid is filled in the cooling chamber (628), and the input end of the air pump (627) is electrically connected with the output end of an external power supply.
CN202210886522.0A 2022-07-26 2022-07-26 Reactor capable of improving heat transfer capacity Active CN115228389B (en)

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