A high-efficiency vaporization device for TMA recovery
By combining the carrier component and the shaking component, the problem of reduced purity during trimethylamine recovery was solved, achieving efficient trimethylamine recovery and impurity removal, and improving recovery efficiency.
Patent Information
- Application Number
- CN202511500631.4
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2025-10-21
- Publication Date
- 2025-12-16
- Estimated Expiration
- 2045-10-21
AI Technical Summary
In the existing technology for trimethylamine recovery, as the vaporization process is prolonged, the concentration of impurities in the wastewater increases, resulting in a decrease in the purity of the recovered trimethylamine and low recovery efficiency.
The carrier assembly includes a carrier frame, a heating carrier, and a shaking component. By heating, trimethylamine is preferentially vaporized into a gaseous state, impurities are crystallized and shaken off, wastewater is adsorbed by hydrophilic modified PAN material, wastewater is stored by silicon carbide nanowire-reinforced ceramic cotton, graphene-coated aramid material is used to increase the heating rate, and a rotating shaft drives the carrier frame to shake and remove impurities.
This improved the purity and efficiency of trimethylamine recovery, reduced the impurity content in wastewater, and achieved highly efficient trimethylamine recovery.
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Figure CN120964920B_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The present application relates to the technical field of TMA recovery, in particular to a high-efficiency vaporization equipment for TMA recovery. BACKGROUND
[0002] Trimethylamine, referred to as TMA, is an organic amine compound with strong odor, which is a colorless gas at normal temperature and pressure, has a pungent odor similar to fishy or ammonia, is usually stored in the form of pressurized liquefaction or aqueous solution, is released by biological metabolites and decomposed products of rotten fish, algae and bacteria, and is mainly applied to chemical synthesis to produce choline chloride, synthesize quaternary ammonium salt, pesticide and pharmaceutical intermediates, and can be used as a gas warning agent. When wastewater is treated, TMA in the wastewater needs to be extracted, so professional equipment is needed for TMA recovery.
[0003] The patent with publication number CN104888595A discloses a trimethylamine odor recovery system and method, which sets a two-stage odor recovery module and a water tank odor absorption module, can further recover or absorb excess trimethylamine gas in the recovery tank one in the first-stage odor recovery module, can ensure that there is no trimethylamine gas leakage, and after one or two times of odor recovery, the amount of trimethylamine gas absorbed by water in the water tank is small, so that odor is not formed again due to a large amount of trimethylamine dissolved in water; the self-suction type magnetic pump and the ammonia stop valve have no leakage, so that good trimethylamine odor recovery effect can be ensured; the mass fraction of hydrochloric acid solution is required to be 30%, so that trimethylamine gas can be effectively recovered, the concentration of trimethylamine hydrochloride generated after reaction is also appropriate, and the trimethylamine hydrochloride can directly enter the liquid preparation tank.
[0004] In the use process of the water and the like, when the conventional vaporization recovery method is used to heat the wastewater containing trimethylamine to vaporize the trimethylamine, there are not only trimethylamine but also other sulfides or chlorides in the wastewater. When the trimethylamine is continuously vaporized and reduced, the concentration of impurities in the residual wastewater is also continuously increased. With the prolongation of the vaporization process, more than one kind of substance will be vaporized from the wastewater, thereby reducing the recovery purity of trimethylamine and the recovery efficiency. SUMMARY
[0005] The present application aims to provide a high-efficiency vaporization equipment for TMA recovery to solve the problems in the background art.
[0006] In order to achieve the above object, the present application provides the following technical scheme: a high-efficiency vaporization equipment for TMA recovery, comprising a main body assembly and a top cover assembly, the main body assembly comprises a main cylinder, and the top cover assembly comprises a top cover body, a carrier assembly for absorbing and heating wastewater is arranged on the top cover body, a shaking assembly for driving the carrier assembly to shake and a storage assembly for impurity recovery are arranged in the main cylinder, and a water spraying assembly for wastewater conveying is arranged in the main cylinder;
[0007] The carrier assembly comprises a carrier frame and a heating carrier arranged on the carrier frame, a water absorbing carrier is arranged on the heating carrier, a rotating shaft is arranged between the top cover body and the main cylinder, a fixing sleeve is arranged on the rotating shaft, the carrier frame is arranged on the fixing sleeve, and a driving motor fixedly connected with the rotating shaft is arranged on the top cover body;
[0008] The driving motor drives the rotating shaft to rotate, the water spraying assembly conveys and sprays the wastewater at the bottom of the main cylinder on the water absorbing carrier, the water absorbing carrier stores the wastewater, and the heating carrier heats the water absorbing carrier, so that the trimethylamine in the water absorbing carrier is evaporated, and the trimethylamine is recovered; the heating carrier further heats the water absorbing carrier, so that the remaining impurities in the water absorbing carrier are crystallized, the shaking assembly shakes the carrier frame up and down as a whole, and the crystallized impurities are shaken off, so that the content of the impurities in the wastewater at the bottom of the main cylinder is reduced.
[0009] Further, a supporting bottom ring and a supporting top ring are arranged in the main cylinder, a first supporting rod is arranged between the supporting bottom ring and the main cylinder, a second supporting rod is arranged between the supporting top ring and the top cover body, the supporting bottom ring and the supporting top ring are in contact with the carrier frame, the rotating shaft drives the carrier frame to rotate and shake, and the supporting bottom ring and the supporting top ring are used for limiting the carrier frame.
[0010] Further, the shaking assembly comprises a clamping plate and a guide ball arranged on the clamping plate, an expansion plate is arranged on the supporting bottom ring and the supporting top ring, a guide spring is arranged on the expansion plate, the clamping plate is arranged on the guide spring, a guide inclined groove is formed in the clamping plate, the number of the guide balls on different clamping plates is different, a limiting frame is arranged on the fixing sleeve, a limiting rod is arranged on the limiting frame, a lifting block is arranged on the carrier frame and sleeved on the limiting rod, the lifting block is electrically connected with the fixing sleeve, a shaking spring is arranged on the lifting block, the rotating shaft drives the carrier frame to rotate, the carrier frame enters between the clamping plates under the guidance of the guide inclined groove, the carrier frame is in a shaking state under the limiting action of the guide balls and the elastic force of the shaking spring, the shaking of the carrier frame is intensified under the action of the guide spring, and the crystallized impurities are shaken and removed.
[0011] Further, the water absorption carrier comprises a liquid-approaching layer, an intermediate layer and a heat-conducting layer, the liquid-approaching layer is made of hydrophilic modified PAN material and is used for quickly absorbing wastewater, the intermediate layer is made of silicon carbide nanowire reinforced ceramic cotton material and is used for storing wastewater, and the heat-conducting layer is made of graphene-coated aramid material and is used for improving the heating rate.
[0012] Further, the top cover body is provided with a brush ring and an electricity connection assembly, the electricity connection assembly is electrically connected with the brush ring, the brush ring is sleeved on the rotating shaft, and the electricity connection assembly is used for connecting an external power supply, converting voltage and delivering electric energy to the brush ring.
[0013] Further, the water spraying assembly comprises a flow distribution plate, the flow distribution plate is arranged on the top cover body and is electrically connected with the electricity connection assembly, the flow distribution plate is provided with a water suction pipe, the water suction pipe is provided with a water suction pump, a plurality of water spraying holes are formed in the flow distribution plate, when the carrier assembly is driven by the rotating shaft to rotate to the middle position of the flow distribution plate, the water suction pump sucks wastewater at the bottom of the main cylinder through the water suction pipe and sprays the wastewater through the water spraying holes to the water absorption carriers on both sides of the carrier frame, so that the wastewater is uniformly sprayed.
[0014] Further, the top cover body is provided with a first gas outlet pipe and a second gas outlet pipe, the main cylinder is provided with a feeding pipe, wastewater enters the main cylinder through the feeding pipe, and the heating carrier is heated in a segmented mode, that is, the heating carrier is first heated at low temperature to evaporate trimethylamine and then heated at high temperature to crystallize the remaining impurities, and the gas impurities generated in the crystallization process are discharged through the second gas outlet pipe.
[0015] Further, the material storage assembly comprises a material collecting box, the material collecting box is arranged on the supporting bottom ring, the material collecting box is provided with a dismounting plate, the dismounting plate is provided with a dismounting rod, the material collecting box is below the clamping plate, the crystallized impurities shaken off during the shaking of the carrier frame fall into the material collecting box, and when the impurities need to be cleaned, the dismounting plate is pulled out of the material collecting box through the dismounting rod for impurity cleaning.
[0016] Further, the main cylinder bottom is provided with an anti-falling rod, and the bottom of the rotating shaft is provided with a butt joint hole, when the main cylinder and the top cover body are installed, the rotating shaft is sleeved on the anti-falling rod through the butt joint hole, and the rotating shaft is used for keeping stable during rotation.
[0017] Compared with the prior art, the present application has the following advantages:
[0018] The efficient vaporization equipment of the TMA recovery device stores the waste water in the water-absorbing carrier, and the water-absorbing carrier is heated by the heating carrier. Since the boiling point of trimethylamine is much lower than that of water, the trimethylamine is vaporized into a gaseous state by heating the waste water, while the water and other high-boiling-point components remain in the liquid phase. Thus, the trimethylamine in the water-absorbing carrier is evaporated, thereby achieving the recovery effect of trimethylamine. After the recovery of trimethylamine is completed, the heating carrier further heats the water-absorbing carrier. At this time, under the action of high temperature, the remaining impurities in the water-absorbing carrier are crystallized, and the crystallized impurities are stored in the water-absorbing carrier. As the rotating shaft continuously drives the water-absorbing carrier and the heating carrier to rotate, the water-absorbing carrier and the heating carrier come into contact with the shaking assembly, thereby causing the carrier frame to shake up and down as a whole, and the crystallized impurities are shaken off, thereby reducing the content of impurities in the sewage at the bottom of the main cylinder and improving the recovery efficiency of trimethylamine.
[0019] Meanwhile, the water-absorbing carrier includes a liquid-approaching layer, an intermediate layer and a heat-conducting layer. The liquid-approaching layer is made of hydrophilic modified PAN material and is used for quickly absorbing waste water. The intermediate layer is made of silicon carbide nanowire reinforced ceramic cotton material and is used for storing waste water. The heat-conducting layer is made of graphene-coated aramid material and is used for improving the heating rate.
[0020] Furthermore, when the rotating shaft drives the carrier frame to rotate, the carrier frame enters between the clamping plates under the guidance of the guide chute. Since the number of guide balls on different clamping plates is different, the number of clamping plates is two, one of which is arranged on the support bottom ring and the other of which is arranged at the bottom of the support top ring. The guide balls are distributed in a staggered manner. Under the limiting action of the guide balls and the elastic force of the shaking spring, the carrier frame is in an up-and-down shaking state, and the crystallized impurities are shaken and removed. Under the action of the guide spring, the elastic force of the clamping plate increases, thereby intensifying the shaking of the carrier frame and more effectively shaking and removing the crystallized impurities. BRIEF DESCRIPTION OF DRAWINGS
[0021] Figure 1 It is a schematic diagram of the overall structure of the present application;
[0022] Figure 2 It is a schematic diagram of the internal structure of the main cylinder of the present application;
[0023] Figure 3 It is a schematic diagram of the structure of the shaking assembly of the present application;
[0024] Figure 4 It is a schematic diagram of the structure of the material storage assembly of the present application;
[0025] Figure 5 It is a schematic diagram of the structure of the rotating shaft of the present application;
[0026] Figure 6 It is a schematic diagram of the structure of the carrier frame of the present application;
[0027] Figure 7 Structure diagram of the heating carrier and water absorption carrier of the present application;
[0028] Figure 8 Structure diagram of the water spraying assembly of the present application;
[0029] Figure 9 Structure diagram of the internal structure of the water absorption carrier of the present application.
[0030] In the figure: 1, main body assembly; 101, main cylinder; 102, feeding pipe; 103, supporting bottom ring; 104, first supporting rod; 2, top cover assembly; 201, top cover body; 202, first air outlet pipe; 203, second air outlet pipe; 204, supporting top ring; 205, second supporting rod; 3, carrier assembly; 301, driving motor; 302, rotating shaft; 303, power connection assembly; 304, brush ring; 305, fixed sleeve; 306, carrier frame; 307, heating carrier; 308, water absorption carrier; 309, lifting block; 310, limiting frame; 4, storage assembly; 401, material collecting box; 402, disassembly plate; 403, disassembly rod; 5, water spraying assembly; 501, flow dividing plate; 502, water absorption pipe; 503, water absorption pump; 6, shaking assembly; 601, expanding plate; 602, clamping plate; 603, guide ball; 604, guide spring; 605, shaking spring; 606, limiting rod. DETAILED DESCRIPTION
[0031] The technical solutions in the embodiments of the present application will be described clearly and completely below with reference to the accompanying drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments of the present application. Based on the embodiments in the present application, all the other embodiments obtained by those of ordinary skill in the art without any creative work fall within the scope of protection of the present application.
[0032] In industrial production, the commonly used vaporization recovery method is to vaporize trimethylamine by heating, so as to realize the purpose of separation and recovery from wastewater. However, in practical application, this method has a significant defect, that is, with the progress of the vaporization process, the recovery purity of trimethylamine will gradually decrease, and the recovery efficiency is not ideal. Industrial wastewater is complex, and usually contains not only trimethylamine, but also sulfides, chlorides and other impurities. The presence of these impurities is the fundamental reason for the decrease of the recovery purity of trimethylamine. Secondly, in the initial stage of vaporization recovery, since trimethylamine accounts for a relatively high proportion in wastewater, the main component of the vaporized gas is trimethylamine, and the purity of the recovered product is high at this time. However, with the continuation of the vaporization process, the content of trimethylamine in wastewater gradually decreases, while the concentration of sulfides, chlorides and other impurities relatively increases. Thirdly, when the concentration of trimethylamine in wastewater decreases to a certain extent, the composition of the gas produced by heating vaporization will change. Since part of the impurities also have a certain volatility, they will also gradually vaporize under high temperature conditions. At this time, the recovered gas will no longer contain only trimethylamine, but also contain a variety of impurities, thereby significantly reducing the recovery purity of trimethylamine. In addition, the prolongation of the vaporization process will further exacerbate this problem. With the increase of vaporization time, the concentration of impurities in wastewater will further increase, so that more impurities will vaporize, further reducing the recovery purity of trimethylamine.
[0033] As Figures 1-9 The present application provides a technical scheme: an efficient vaporization equipment for TMA recovery, comprising a main body assembly 1 and a top cover assembly 2, the main body assembly 1 comprising a main cylinder 101, the top cover assembly 2 comprising a top cover body 201, the top cover body 201 being provided with a carrier assembly 3 for absorbing wastewater and heating the wastewater, the main cylinder 101 being provided with a shaking assembly 6 for driving the carrier assembly 3 to vibrate and a storage assembly 4 for impurity recovery, and the main cylinder 101 being provided with a water spraying assembly 5 for wastewater conveying; the carrier assembly 3 comprising a carrier frame 306 and a heating carrier 307 provided on the carrier frame 306, the heating carrier 307 being provided with a water absorbing carrier 308, a rotating shaft 302 being arranged between the top cover body 201 and the main cylinder 101, the rotating shaft 302 being provided with a fixing sleeve 305, the carrier frame 306 being arranged on the fixing sleeve 305, and the top cover body 201 being provided with a driving motor 301 fixedly connected with the rotating shaft 302.
[0034] It should be noted that when the driving motor 301 starts and drives the rotating shaft 302 to rotate, the water spraying assembly 5 first transports the wastewater at the bottom of the main cylinder 101 upward and sprays it on the water absorbing carrier 308, the water absorbing carrier 308 stores the wastewater, and the heating carrier 307 heats the water absorbing carrier 308, because the boiling point of trimethylamine is much lower than that of water, so by heating the wastewater containing wastewater, trimethylamine is preferentially vaporized into a gaseous state, while water and other high-boiling components remain in a liquid phase, thereby evaporating the trimethylamine in the water absorbing carrier 308, thereby achieving the effect of recycling trimethylamine. When the trimethylamine recycling is completed, the heating carrier 307 further heats the water absorbing carrier 308, at which time under the action of high temperature, the remaining impurities in the water absorbing carrier 308 are crystallized, and the crystallized impurities are stored in the water absorbing carrier 308. As the rotating shaft 302 continuously drives the water absorbing carrier 308 and the heating carrier 307 to rotate, the water absorbing carrier 308 and the heating carrier 307 come into contact with the shaking assembly 6, thereby causing the carrier frame 306 to shake up and down as a whole, and the crystallized impurities are shaken off, thereby reducing the content of impurities in the wastewater at the bottom of the main cylinder 101, and thereby improving the recycling efficiency of trimethylamine.
[0035] As shown in Figure 2 , the main cylinder 101 is provided with a support bottom ring 103 and a support top ring 204, the support bottom ring 103 and the main cylinder 101 are provided with a first support rod 104, the support top ring 204 and the top cover body 201 are provided with a second support rod 205, and the support bottom ring 103 and the support top ring 204 are in contact with the carrier frame 306.
[0036] It should be noted that in the process of rotating and shaking the carrier frame 306 by the rotating shaft 302, the support bottom ring 103 and the support top ring 204 are used to limit the rotation of the carrier frame 306 and reset during the shaking process, that is, after the carrier frame 306 is shaken, the support bottom ring 103 and the support top ring 204 limit the carrier frame 306 again, keeping the carrier frame 306 moving normally.
[0037] As shown in Figure 3 , Figure 6 and Figure 7As shown, the shaking assembly 6 comprises a clamping plate 602 and a guide ball 603 arranged on the clamping plate 602, the support bottom ring 103 and the support top ring 204 are provided with an expansion plate 601, the expansion plate 601 is provided with a guide spring 604, the clamping plate 602 is arranged on the guide spring 604, the clamping plate 602 is provided with a guide inclined groove, the number of guide balls 603 on different clamping plates 602 is different, the fixed sleeve 305 is provided with a limiting frame 310, the limiting frame 310 is provided with a limiting rod 606, the carrier frame 306 is provided with a lifting block 309 sleeved on the limiting rod 606, the lifting block 309 is electrically connected with the fixed sleeve 305, and the lifting block 309 is provided with a shaking spring 605.
[0038] It should be noted that when the rotating shaft 302 drives the carrier frame 306 to rotate, the carrier frame 306 enters between the clamping plates 602 under the guidance of the guide inclined groove. Since the number of guide balls 603 on different clamping plates 602 is different, the number of clamping plates 602 is two, one of which is arranged on the support bottom ring 103 and the other is arranged at the bottom of the support top ring 204. The guide balls 603 are distributed in a staggered manner. Under the limiting action of the guide balls 603 and the elastic force of the shaking spring 605, the carrier frame 306 is in an up-down shaking state. The crystallized impurities are shaken and removed. Under the action of the guide spring 604, the elastic force received by the clamping plate 602 increases, thereby intensifying the shaking of the carrier frame 306 and removing the crystallized impurities with stronger effect.
[0039] As shown in Figure 9 The water absorption carrier 308 comprises a liquid receiving layer, an intermediate layer and a heat conducting layer. The liquid receiving layer is made of hydrophilic modified PAN material for quickly absorbing wastewater. The intermediate layer is made of silicon carbide nanowire reinforced ceramic cotton material for storing wastewater. The heat conducting layer is made of graphene coated aramid material for improving the heating rate.
[0040] As shown in Figure 5 The top cover body 201 is provided with a brush ring 304 and an electrical connection assembly 303. The electrical connection assembly 303 is electrically connected with the brush ring 304. The brush ring 304 is sleeved on the rotating shaft 302.
[0041] It should be noted that the electrical connection assembly 303 is used for connecting an external power source and converting voltage to deliver electric energy to the brush ring 304. When the rotating shaft 302 rotates, the brush ring 304 is used for supplying power to the fixed sleeve 305.
[0042] As shown in Figure 8 The water spraying assembly 5 comprises a flow divider 501 arranged on the top cover body 201. The flow divider 501 is electrically connected with the electrical connection assembly 303. The flow divider 501 is provided with a water suction pipe 502 and a water suction pump 503. The flow divider 501 is provided with a plurality of water spraying holes.
[0043] It should be noted that when the rotating shaft 302 drives the carrier assembly 3 to rotate to the middle position of the flow divider 501, the water suction pump 503 sucks the wastewater at the bottom of the main cylinder 101 through the water suction pipe 502 and sprays it through the water spraying hole to the water suction carrier 308 on both sides of a carrier frame 306, respectively, to uniformly spray the wastewater.
[0044] As shown in Figure 2 The top cover body 201 is provided with a first air outlet pipe 202 and a second air outlet pipe 203, and the main cylinder 101 is provided with a feeding pipe 102, through which the wastewater enters the main cylinder 101.
[0045] It should be noted that when the heating carrier 307 heats the water suction carrier 308, it is heated in a segmented manner. Since the boiling point of trimethylamine is low, it is first heated at a low temperature to evaporate the trimethylamine and recover it through the first air outlet pipe 202. After the trimethylamine is recovered, it is heated at a high temperature, which promotes the crystallization of the remaining impurities under the action of high temperature. In the process of crystallization, the gas impurities generated are discharged through the second air outlet pipe 203. The first air outlet pipe 202 is provided with a molecular sieve membrane, which is made of graphene oxide composite material with a pore size of 0.39 nm, accurately trapping macromolecules and allowing trimethylamine to pass normally. The first air outlet pipe 202 and the second air outlet pipe 203 are in an alternating working state. When low-temperature heating is performed, the first air outlet pipe 202 works and the second air outlet pipe 203 is closed. When low-temperature heating is completed, the second air outlet pipe 203 works and the first air outlet pipe 202 is closed. Therefore, the gas impurities cannot be discharged through the first air outlet pipe 202.
[0046] As shown in Figure 4 The storage assembly 4 includes a material collecting box 401, which is arranged on the supporting bottom ring 103. The material collecting box 401 is provided with a dismounting plate 402, and the dismounting plate 402 is provided with a dismounting rod 403. The material collecting box 401 is below the clamping plate 602.
[0047] It should be noted that when the carrier frame 306 is shaken, the crystallized impurities shaken off fall into the material collecting box 401. When it is necessary to clean the impurities, the dismounting plate 402 is pulled out of the material collecting box 401 through the dismounting rod 403 for impurity cleaning.
[0048] As shown in Figure 3 The bottom of the main cylinder 101 is provided with an anti-falling rod, and the bottom of the rotating shaft 302 is provided with a butt joint hole. When the main cylinder 101 and the top cover body 201 are installed, the rotating shaft 302 is sleeved on the anti-falling rod through the butt joint hole to keep stable when the rotating shaft 302 rotates.
[0049] It should be noted that when installing the main cylinder 101 and the top cover body 201, the rotating shaft 302 is sleeved on the anti-off rod through the butt joint hole, when the rotating shaft 302 drives the carrier assembly 3 to rotate to the middle position of the flow divider 501, the water suction pump 503 sucks the wastewater at the bottom of the main cylinder 101 through the water suction pipe 502, and sprays out through the water spray hole, respectively to the water suction carrier 308 on both sides of a carrier frame 306, the water suction carrier 308 stores the wastewater, and the heating carrier 307 heats the water suction carrier 308, because the boiling point of trimethylamine is much lower than that of water, by heating the wastewater containing water, the trimethylamine is preferentially vaporized into a gaseous state, and the water and other high-boiling-point components remain in the liquid phase, thereby evaporating the trimethylamine in the water suction carrier 308, and recycling through the first gas outlet pipe 202, thereby realizing the recycling effect of trimethylamine, when the trimethylamine recycling is completed, the heating carrier 307 further heats the water suction carrier 308, at this time, under the action of high temperature, the remaining impurities in the water suction carrier 308 are crystallized, and the crystallized impurities are stored in the water suction carrier 308, in the process of crystallization, the gas impurities generated are discharged through the second gas outlet pipe 203, as the rotating shaft 302 continuously drives the water suction carrier 308 and the heating carrier 307 to rotate, the water suction carrier 308 and the heating carrier 307 contact the shaking assembly 6, and enter between the clamping plates 602 under the guidance of the guide chute, because the number of guide balls 603 on different clamping plates 602 is different, the number of clamping plates 602 is two, one of which is arranged on the support bottom ring 103, and the other is arranged at the bottom of the support top ring 204, the guide balls 603 are distributed in a staggered manner, under the limiting action of the guide balls 603 and the elastic force of the shaking spring 605, the carrier frame 306 is in an up-down shaking state, and the crystallized impurities are shaken off, under the action of the guide spring 604, the clamping plate 602 receives an increased elastic force, thereby intensifying the shaking of the carrier frame 306, and shaking off the crystallized impurities, in the process of rotating and shaking the carrier frame 306 driven by the rotating shaft 302, the support bottom ring 103 and the support top ring 204 are used for limiting the carrier frame 306 in the rotating process and resetting the carrier frame 306 in the shaking process, that is, when the carrier frame 306 finishes shaking, the support bottom ring 103 and the support top ring 204 limit the carrier frame 306 again, keep the normal movement of the carrier frame 306, and reduce the content of impurities in the wastewater at the bottom of the main cylinder 101, when the carrier frame 306 is shaken, the shaken-off crystallized impurities fall into the material collecting box 401, when it is necessary to clean the impurities, the disassembly plate 402 is pulled out from the material collecting box 401 through the disassembly rod 403 for cleaning the impurities.
[0050] While embodiments of the application have been shown and described, it is to be understood that the embodiments described are merely exemplary of the principles and application of the present application. Numerous modifications and adaptions can be effected without departing from the spirit and scope of the present application, which is not limited to the embodiments disclosed except insofar as recited in the claims.
Claims
1. A high efficiency vaporization apparatus for TMA recovery, comprising a main body assembly (1) and a top cover assembly (2), characterized in that: The main body assembly (1) comprises a main cylinder (101), the top cover assembly (2) comprises a top cover body (201), the top cover body (201) is provided with a carrier assembly (3) for absorbing and heating wastewater, the main cylinder (101) is provided with a shaking assembly (6) for driving the carrier assembly (3) to vibrate and a storage assembly (4) for impurity recovery, and the main cylinder (101) is provided with a water spraying assembly (5) for wastewater conveying; The carrier assembly (3) comprises a carrier frame (306) and a heating carrier (307) arranged on the carrier frame (306), the heating carrier (307) is provided with a water absorbing carrier (308), the top cover body (201) and the main cylinder (101) are provided with a rotating shaft (302), the rotating shaft (302) is provided with a fixing sleeve (305), the carrier frame (306) is arranged on the fixing sleeve (305), and the top cover body (201) is provided with a driving motor (301) fixedly connected with the rotating shaft (302); The driving motor (301) drives the rotating shaft (302) to rotate, the water spraying assembly (5) conveys and sprays the wastewater at the bottom of the main cylinder (101) on the water absorbing carrier (308), the water absorbing carrier (308) stores the wastewater, and the heating carrier (307) heats the water absorbing carrier (308), so that trimethylamine in the water absorbing carrier (308) evaporates, and then the trimethylamine is recovered, the heating carrier (307) further heats the water absorbing carrier (308), so that the remaining impurities in the water absorbing carrier (308) are crystallized, the shaking assembly (6) shakes the carrier frame (306) up and down as a whole, and the crystallized impurities are shaken off, so that the content of impurities in the wastewater at the bottom of the main cylinder (101) is reduced; The main cylinder (101) is provided with a supporting bottom ring (103) and a supporting top ring (204), the supporting bottom ring (103) and the main cylinder (101) are provided with a first supporting rod (104), the supporting top ring (204) and the top cover body (201) are provided with a second supporting rod (205), the supporting bottom ring (103) and the supporting top ring (204) are in contact with the carrier frame (306), the rotating shaft (302) drives the carrier frame (306) to rotate and shake, and the supporting bottom ring (103) and the supporting top ring (204) are used for limiting the carrier frame (306). The shaking component (6) comprises a clamping plate (602) and a guide ball (603) arranged on the clamping plate (602), an expansion plate (601) arranged on a supporting bottom ring (103) and a supporting top ring (204), a guide spring (604) arranged on the expansion plate (601), the clamping plate (602) arranged on the guide spring (604), a guide inclined slot opened on the clamping plate (602), different numbers of the guide balls (603) on different clamping plates (602), a limiting frame (310) arranged on a fixed sleeve (305), a limiting rod (606) arranged on the limiting frame (310), a lifting block (309) arranged on a carrier frame (306) and sleeved on the limiting rod (606), the lifting block (309) in electric connection with the fixed sleeve (305), a shaking spring (605) arranged on the lifting block (309), the rotating shaft (302) driving the carrier frame (306) to rotate, the carrier frame (306) entering between the clamping plates (602) under the guidance of the guide inclined slot, the carrier frame (306) in a shaking state due to the different numbers of the guide balls (603) on different clamping plates (602) and the limiting effect of the guide balls (603) and the elastic effect of the shaking spring (605), and the shaking of the carrier frame (306) being intensified under the effect of the guide spring (604), so as to shake and remove the crystallized impurities. The water absorption carrier (308) comprises a liquid receiving layer, an intermediate layer and a heat conducting layer, the liquid receiving layer is a hydrophilic modified PAN material, is used for quickly absorbing wastewater, the intermediate layer is a silicon carbide nanowire reinforced ceramic cotton material, is used for storing wastewater, and the heat conducting layer is a graphene coated aramid material, is used for improving the heating rate. The top cover body (201) is provided with a first gas outlet pipe (202) and a second gas outlet pipe (203), and the main cylinder (101) is provided with a feeding pipe (102), the wastewater enters into the main cylinder (101) through the feeding pipe (102), the heating carrier (307) is in a segmented heating mode when heating the water absorption carrier (308), the heating carrier (307) heats the water absorption carrier (308), the boiling point of trimethylamine is lower than that of water, the trimethylamine is preferentially vaporized into a gaseous state by heating the wastewater containing wastewater, and is recovered through the first gas outlet pipe (202), when the trimethylamine recovery is completed, the heating carrier (307) further heats the water absorption carrier (308), at this time, under the action of high temperature, the remaining impurities in the water absorption carrier (308) are crystallized, at this time, the remaining impurities are crystallized, in the process of crystallization, the gas impurities generated are discharged through the second gas outlet pipe (203).
2. A high efficiency vaporization apparatus for TMA recovery according to claim 1, characterized by: The top cover body (201) is provided with a brush ring (304) and an electricity connection assembly (303), the electricity connection assembly (303) and the brush ring (304) are electrically connected, the brush ring (304) is sleeved on the rotating shaft (302), the electricity connection assembly (303) is used for connecting an external power supply and converting voltage, and the electricity connection assembly (303) is used for transmitting electric energy to the brush ring (304); when the rotating shaft (302) rotates, the brush ring (304) is used for supplying energy to the fixed sleeve (305).
3. A high efficiency vaporizing apparatus for TMA recovery according to claim 2, characterized by: The water spraying assembly (5) comprises a flow distribution plate (501), the flow distribution plate (501) is arranged on the top cover body (201), the flow distribution plate (501) is electrically connected with the electricity connection assembly (303), the flow distribution plate (501) is provided with a water suction pipe (502), the water suction pipe (502) is provided with a water suction pump (503), a plurality of water spraying holes are formed in the flow distribution plate (501), when the rotating shaft (302) drives the carrier assembly (3) to rotate to the middle position of the flow distribution plate (501), the water suction pump (503) sucks the waste water at the bottom of the main cylinder (101) through the water suction pipe (502) and sprays the waste water through the water spraying holes to the water suction carriers (308) on both sides of one carrier frame (306) respectively, and the waste water is uniformly sprayed.
4. The high efficiency vaporizing apparatus for TMA recovery according to claim 1, characterized by: The material storage assembly (4) comprises a material collecting box (401), the material collecting box (401) is arranged on the supporting bottom ring (103), the material collecting box (401) is provided with a dismounting plate (402), the dismounting plate (402) is provided with a dismounting rod (403), and the material collecting box (401) is below the clamping plate (602); when the carrier frame (306) is shaken, the crystallized impurities are shaken and fall into the material collecting box (401); when the impurities need to be cleaned, the dismounting plate (402) is pulled out from the material collecting box (401) through the dismounting rod (403), and the impurities are cleaned.
5. A high efficiency vaporizing apparatus for TMA recovery according to claim 1, characterized by: The main cylinder (101) is provided with an anti-falling rod at the bottom, the rotating shaft (302) is provided with a butt joint hole at the bottom, and when the main cylinder (101) and the top cover body (201) are installed, the rotating shaft (302) is sleeved on the anti-falling rod through the butt joint hole, and the rotating shaft (302) is used for keeping stable when rotating.
Citation Information
Patent Citations
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