CN116617810B - Granulator exhaust treatment equipment - Google Patents
Granulator exhaust treatment equipment Download PDFInfo
- Publication number
- CN116617810B CN116617810B CN202310901331.1A CN202310901331A CN116617810B CN 116617810 B CN116617810 B CN 116617810B CN 202310901331 A CN202310901331 A CN 202310901331A CN 116617810 B CN116617810 B CN 116617810B
- Authority
- CN
- China
- Prior art keywords
- drawer
- box
- fixedly connected
- split half
- box body
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 141
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 45
- 229920001971 elastomer Polymers 0.000 claims abstract description 11
- 239000003610 charcoal Substances 0.000 claims description 9
- 230000000149 penetrating effect Effects 0.000 claims description 5
- 239000002912 waste gas Substances 0.000 abstract description 39
- 239000000203 mixture Substances 0.000 abstract description 14
- 238000003795 desorption Methods 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 9
- 230000008929 regeneration Effects 0.000 abstract description 5
- 238000011069 regeneration method Methods 0.000 abstract description 5
- 238000001125 extrusion Methods 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 15
- 238000007789 sealing Methods 0.000 description 15
- 239000000126 substance Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- 238000001179 sorption measurement Methods 0.000 description 6
- 230000000670 limiting effect Effects 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 230000002035 prolonged effect Effects 0.000 description 3
- 238000003915 air pollution Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000010355 oscillation Effects 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007084 catalytic combustion reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3416—Regenerating or reactivating of sorbents or filter aids comprising free carbon, e.g. activated carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3483—Regenerating or reactivating by thermal treatment not covered by groups B01J20/3441 - B01J20/3475, e.g. by heating or cooling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
Landscapes
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Materials Engineering (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention relates to a granulator waste gas treatment device, which belongs to the technical field of waste gas treatment and comprises a box body; end covers are fixedly connected to two ends of the box body through screws; the inside of the box body is connected with a plurality of carbon boxes in a sliding way, and the carbon boxes are arranged in parallel up and down; through setting up the piston rod in the branch pipe of steam line, and the piston rod can produce thrust when the internal atmospheric pressure of branch increases, make the piston rod drive the contact plate outwards remove, and with the baffle contact, at the baffle of not leading-in high temperature steam formula and guide module separation, remove to guide module one side through the contact plate extrusion this moment, and laminate on guide module, because the bottom of baffle still peg graft and cooperate with the rubber strip, consequently when the baffle removes and contacts guide module, can realize the seal of box both sides through the rubber strip, make high temperature steam when realizing the thermal desorption regeneration effect to the active carbon, can avoid the steam mixture of production to discharge to the atmosphere through the pipeline of giving vent to anger, cause atmospheric pollution.
Description
Technical Field
The invention relates to the technical field of waste gas treatment, in particular to waste gas treatment equipment of a granulator.
Background
Injection molding and granulation are a common process for processing plastics in modern times, and a large amount of waste gas is generated in the process, if the waste gas is directly discharged to the atmosphere or affects the surrounding environment, meanwhile, the problem of human health is caused; therefore, the waste gas produced by the granulation process needs to be treated;
the existing treatment modes of waste gas generated in the plastic processing process such as a granulating process generally comprise activated carbon adsorption, photocatalytic oxidation, plasma oxidation, catalytic combustion technology and the like; aiming at activated carbon adsorption, the device is suitable for waste gas with low content of harmful substances and large amount, and accords with the type of waste gas generated by a granulating process, so that the prior art mostly adopts an activated carbon box to treat the waste gas in combination with other waste gas treatment processes, the conventional activated carbon box generally comprises an external box body and internal activated carbon, the activated carbon is placed in the box body in a horizontal or vertical arrangement mode by taking a drawer as a bearing structure, and the contact area between the waste gas and the activated carbon can be increased by horizontal arrangement, and the device is more popular.
In the prior art, when the activated carbon box is used for treating waste gas, as the activated carbon belongs to a physical adsorption means when the activated carbon adsorbs waste gas, the saturated phenomenon can be generated after the activated carbon works for a period of time, the adsorption effect provided by the activated carbon is very small, the activated carbon needs to be replaced, however, when the activated carbon is replaced, the activated carbon in the drawer at the top needs to be replaced more conveniently by keeping the drawer inclined, the activated carbon needs to slide out of the adjacent drawer and is used for bearing the drawer above, and in the prior art, the activated carbon can be realized only by sliding out of the drawer below again by an operator, so that the activated carbon is more convenient to replace; meanwhile, the saturated activated carbon can be desorbed and regenerated by introducing hot steam, and the generated steam mixture is easily discharged into the atmosphere through an air outlet pipeline of the device when the regeneration mode works, so that the problem of atmosphere pollution is caused.
To this end, the invention provides a granulator exhaust gas treatment apparatus.
Disclosure of Invention
Therefore, the invention aims to solve the technical problem that when the saturated activated carbon is regenerated by thermal desorption in the prior art, the steam mixture combined with the hot steam is easily discharged into the atmosphere through the air outlet pipeline, so that pollution is caused.
In order to solve the technical problems, the invention provides a granulator waste gas treatment device, which comprises a box body; end covers are fixedly connected to two ends of the box body through screws; the inside of the box body is connected with a plurality of carbon boxes in a sliding way, and the carbon boxes are arranged in parallel up and down;
the top and the bottom of the box body are connected with steam pipelines in a penetrating way, and the steam pipelines comprise a main pipe and branch pipes; the main pipes are transversely arranged, and the branch pipes are perpendicularly arranged in a crossing manner; the bottom of the branch pipe is provided with a steam outlet, and the steam outlet is right opposite to the carbon box; the middle part of the main pipe is communicated with a connecting pipe vertical to the main pipe and the branch pipes; the root of the connecting pipe is communicated with the main pipe, and the end part of the connecting pipe is fixedly connected with a flange plate; the connecting pipe penetrates through the box body.
In one embodiment of the invention, the box body consists of two split half boxes, and the two split half boxes are fixedly connected through screws; the inner side wall of the split half box is vertically fixedly connected with a guide module adjacent to the end cover; the inner side wall of the split half-box is adjacent to the guide module, and a baffle is movably connected between the charcoal box and the guide module; rubber strips are inserted and matched at the bottom of the baffle; the two baffles are arranged up and down symmetrically and are arranged obliquely.
In one embodiment of the invention, the end part of the branch pipe is in sliding fit with a piston rod, and a contact plate is fixedly connected with one side of the piston rod, which faces the baffle; the piston rod is fixedly connected with one end in the branch pipe, and the piston rod is sleeved with a second spring.
In one embodiment of the invention, a connecting rod is fixedly connected to the inner side of the side wall of one end of the split half box, which is contacted with the end cover, and a first spring is sleeved on the connecting rod; the two connecting rods are symmetrically arranged about the contact surface of the two split half boxes; both connecting rods penetrate through the baffle.
In one embodiment of the invention, one split half box is connected with the carbon box in a penetrating way, and the middle part of the other split half box is communicated with an exhaust pipe.
In one embodiment of the invention, the charcoal box comprises a first drawer, a second drawer and a third drawer; the first drawer, the second drawer and the third drawer are sequentially arranged in the box body up and down; the inner side of one split half box is fixedly connected with a plurality of bearing frames through screws; the first drawer, the second drawer and the third drawer respectively slide on the bearing frame.
In one embodiment of the invention, one end of the first drawer, the second drawer and the third drawer, which is positioned outside the box body, is fixedly connected with an end plate, and the end plate is connected with the side wall of the split half box in an embedded way; and one side of the first drawer, one side of the second drawer and one side of the third drawer are fixedly connected with connecting shafts, and the first drawer, the second drawer and the third drawer are in sliding fit with the bearing frame through the connecting shafts.
In one embodiment of the invention, a first connecting angle is fixedly connected to the bottom of one end of the first drawer positioned in the split half box, and a second connecting angle is correspondingly fixedly connected to the bottom of one end of the second drawer positioned in the split half box; the middle part above the second drawer is rotationally connected with a swinging angle through a rotating shaft, and the swinging angle is arranged corresponding to the first connecting angle; the two swing angles are symmetrically arranged about the middle of the second drawer, and a movable rod is in sliding fit between the two swing angles; and a torsion spring is clamped between the swinging angle and the inner side wall of the second drawer and sleeved on the rotating shaft.
In one embodiment of the invention, the upper middle part of the third drawer is also connected with a swinging angle corresponding to the second drawer through the rotating shaft, and a movable rod is also matched between the two swinging angles in a sliding way.
In one embodiment of the invention, the first drawer is positioned at the top of the split half box, the third drawer is positioned at the bottom of the split half box, and the second drawers are arranged in plurality and are positioned between the first drawer and the third drawer in an equidistant array.
Compared with the prior art, the technical scheme of the invention has the following advantages:
1. according to the exhaust gas treatment equipment of the granulator, the piston rod is arranged in the branch pipe of the steam pipeline, the piston rod can generate thrust when the air pressure in the branch pipe is increased, so that the piston rod drives the contact plate to move outwards and contact with the baffle, when high-temperature steam is not introduced, the baffle separated from the guide module moves to one side of the guide module through the extrusion of the contact plate and is tightly attached to the guide module, and as the bottom of the baffle is also spliced and matched with the rubber strip, when the baffle moves and contacts the guide module, the sealing of the two sides of the box body is realized through the rubber strip, so that the high-temperature steam can be prevented from being discharged to the atmosphere through the air outlet pipeline when the thermal desorption regeneration effect on active carbon is realized, the air pollution is caused, meanwhile, the generated steam mixture can be pumped by adopting the air outlet pipe arranged on the other split half box, the condenser arranged outside is matched for condensing the steam mixture to prepare liquid, and the liquid containing harmful substances is treated;
2. according to the exhaust gas treatment equipment for the granulator, the service life of the active carbon is limited, the active carbon is required to be replaced at the moment after repeated thermal desorption for a plurality of times, when the first drawer slides out, the first connecting angle of the bottom surface of the inner end part of the first drawer is clamped with the swinging angle on the second drawer after sliding for a certain distance, and the swinging angle cannot rotate towards the direction close to the end plate due to the limitation of the torsion spring, the second drawer can synchronously slide along the first drawer under the contact action of the first connecting angle and the swinging angle, at the moment, the first drawer is released, and the first drawer can be inclined downwards under the action of center deviation and gravity and takes the second drawer end plate with a part of sliding distance as a support, so that the second drawer is kept in an inclined state without being pulled out by an operator alone, and the exhaust gas treatment equipment has the advantages of time and labor relatively saving.
Drawings
In order that the invention may be more readily understood, a more particular description of the invention will be rendered by reference to specific embodiments thereof that are illustrated in the appended drawings.
FIG. 1 is a perspective view of a first embodiment of the present invention;
FIG. 2 is a partial perspective view of a first embodiment of the present invention;
FIG. 3 is a perspective view of a steam line according to a first embodiment of the present invention;
FIG. 4 is a side view of a first embodiment of the invention;
FIG. 5 is a schematic view of a cross-section AA in a first embodiment of the invention;
FIG. 6 is a schematic view of an exhaust gas flow path according to a first embodiment of the present invention;
FIG. 7 is a cross-sectional perspective view of a first embodiment of the present invention;
FIG. 8 is a perspective view of a first drawer, a second drawer, and a third drawer according to a first embodiment of the present invention;
FIG. 9 is a perspective view showing the cooperation of a first drawer and a second drawer according to the first embodiment of the present invention;
FIG. 10 is a perspective view of a third drawer in accordance with a first embodiment of the present invention;
FIG. 11 is a perspective view of a second drawer according to a second embodiment of the present invention;
description of the specification reference numerals: 1. a case; 11. split half-box; 12. a guide module; 13. a baffle; 141. a connecting rod; 142. a first spring; 15. a rubber strip; 2. an end shield; 3. a charcoal box; 31. a first drawer; 311. a first connection angle; 32. a second drawer; 321. a second connection angle; 322. a chute; 33. a third drawer; 34. a carrier; 35. a connecting shaft; 36. an end plate; 371. a swing angle; 372. a movable rod; 38. a holding plate; 39. a push plate; 4. a steam line; 41. a header pipe; 42. a branch pipe; 43. a contact plate; 44. a piston rod; 45. a second spring; 46. and a flange plate.
Detailed Description
The present invention will be further described with reference to the accompanying drawings and specific examples, which are not intended to be limiting, so that those skilled in the art will better understand the invention and practice it.
Example 1
As shown in fig. 1 to 2, a granulator exhaust gas treatment apparatus according to an embodiment of the present invention comprises a housing 1; the two ends of the box body 1 are fixedly connected with end covers 2 through screws; the inside of the box body 1 is connected with a plurality of carbon boxes 3 in a sliding manner, the carbon boxes 3 are arranged in parallel up and down, and the carbon boxes 3 are used for placing activated carbon; the case body 1 is used as an external container for bearing active carbon, the end cover 2 can be communicated with an external air inlet pipeline and an air outlet pipeline, when the waste gas generated by the granulator is filtered, the air inlet pipeline is communicated with one end cover 2, the air outlet pipeline is communicated with the opposite end cover 2, after the waste gas is sent into the case body 1 through the air inlet pipeline, the harmful gas in the waste gas can be adsorbed and captured through a porous structure on the active carbon, so that the waste gas fully contacted with the active carbon is purified, and the purified waste gas is discharged through the air outlet pipeline, so that the air pollution and the harmful physical health caused by the direct discharge of the waste gas are avoided;
the box body 1 consists of two split half boxes 11, and the two split half boxes 11 are fixedly connected through screws; in order to facilitate overhaul and maintenance in the box body 1, two split half boxes 11 are arranged, the split half boxes 11 are spliced through screws and sealing strips, and the split structure is beneficial to transportation and later overhaul work.
The top and the bottom of the box body 1 are connected with a steam pipeline 4 in a penetrating way, and the steam pipeline 4 comprises a main pipe 41 and branch pipes 42; the main pipe 41 is transversely arranged, and the branch pipes 42 are vertically arranged with the main pipe 41 and extend to two sides of the main pipe 41 in the horizontal direction; the bottom of the branch pipe 42 is provided with a steam outlet, and the steam outlet is opposite to the carbon box 3; because the active carbon adopts a porous structure to adsorb harmful substances in the waste gas, and belongs to physical reaction, the active carbon can generate saturation phenomenon after working for a period of time, at the moment, the problem of poor active carbon adsorption efficiency can be solved by changing the active carbon, meanwhile, the saturated active carbon can be desorbed and regenerated, the recycling of the active carbon is realized, specifically, a steam outlet in a steam pipeline 4 is utilized to introduce high-temperature steam, the harmful substances adsorbed in the active carbon are released through high-temperature steam stripping, so that the harmful substances are combined with the steam to form a steam mixture, and the steam mixture leaves the active carbon together, so that the recycling of the active carbon is realized, and the formed steam mixture can be condensed and collected by an external condenser; the middle part of the main pipe 41 is communicated with a connecting pipe which extends upwards; the end part of the connecting pipe extends out of the box body 1, the end part of the connecting pipe is fixedly connected with a flange 46, and the connecting pipe is used for introducing high-temperature steam; the header pipes 41 which are transversely arranged can uniformly disperse the introduced high-temperature steam into the branch pipes 42 on the two sides, and the activated carbon placed in the carbon box 3 is thermally desorbed through the steam outlets on the branch pipes 42 on the two sides, so that the desorption regeneration of the saturated activated carbon is realized.
As shown in fig. 1 to 5, a plurality of carbon boxes 3 are arranged inside one split half box 11, and the middle part of the other split half box 11 is communicated with an exhaust pipe; after the high-temperature steam is combined with harmful substances in the saturated activated carbon in the carbon box 3, the combined steam mixture can be sucked out of the box body 1 through an exhaust pipe, and a condenser is additionally arranged outside the box body, so that the sucked steam mixture is condensed into liquid, and different harmful substance liquids, namely waste water, are treated.
As shown in fig. 6, the inner side wall of the split half box 11 is vertically and fixedly connected with a guide module 12 adjacent to the end cover 2; the inner side wall of the split half-box 11 is adjacent to the guide module 12, and a baffle 13 is movably connected between the charcoal box 3 and the guide module 12; the bottom of the baffle 13 is inserted and matched with a rubber strip 15; the two baffles 13 are symmetrically arranged up and down and are obliquely arranged; a sealing plate is vertically fixedly connected to the inner side wall of the split half-box 11, one side of the carbon box 3 is attached to the sealing plate, an airflow passage is formed between two adjacent carbon boxes, a sealing plate is arranged between one ends of the two adjacent carbon boxes corresponding to the inlet of waste gas and used for blocking the waste gas from directly entering the airflow passage, one ends of the two adjacent carbon boxes corresponding to the outlet of the waste gas are provided with half-sealing plates, the half-sealing plates are connected with the inner wall of the box body and used for blocking the waste gas from being directly discharged through the outlet of the waste gas without being purified by activated carbon, after the waste gas enters the box body, the waste gas can penetrate through the carbon box through the surfaces of the two adjacent carbon boxes, wherein vent holes are formed in the bottoms of the carbon boxes, and after the waste gas absorbs harmful substances by the activated carbon, the waste gas is collected in the airflow passage and finally discharged out of the box body, so that the waste gas is purified;
specifically, as shown in fig. 4, four half sealing plates are arranged on the left side of the split half tank 11, and the middle two half sealing plates are aligned and spliced, two sealing plates are arranged on the right side, and the arrangement of the guide template and the baffle 13 is matched, so that the exhaust gas flowing path from the air inlet pipeline into the tank body 1 can be changed, the path of the exhaust gas into the tank body 1 is prolonged, the time for the exhaust gas to pass through the tank body 1 is prolonged, the adsorption effect of the active carbon on harmful substances in the exhaust gas is improved, the exhaust gas enters from the right side, moves in the tank body 1 according to the direction shown by an arrow, the contact time of the exhaust gas in the carbon tank 3 is prolonged through the separation of the sealing plates and the half sealing plates, the contact area is larger, and the treatment effect of the exhaust gas is better.
As shown in fig. 4 to 5, the end of the branch pipe 42 is slidably fitted with a piston rod 44, and a contact plate 43 is fixedly connected to one side of the piston rod 44 facing the baffle 13; a piston is fixedly connected to one end of the piston rod 44 positioned in the main pipe 41, and a second spring 45 is sleeved on the piston rod 44; when high-temperature steam is fed into the main pipe 41, the valve of the exhaust pipe is closed, at the moment, the piston is pushed to move outwards due to the increase of the air pressure in the branch pipe 42, when the piston moves, the second spring 45 is extruded, the contact plate 43 connected with the outside of the piston rod 44 is contacted with and abutted against the baffle plate 13, the baffle plate 13 is pushed finally, and the baffle plate 13 moves towards one side of the guide module 12, and the rubber strip 15 is fixedly connected to the bottom of the baffle plate 13 and is obliquely arranged, so that the baffle plate 13 can be abutted against the guide module 12 when moving towards one side of the guide module 12, the relative sealing in the box body 1 is kept, the failure of the valves on an air inlet pipeline and an air outlet pipeline is prevented, the steam mixture carrying harmful substances is discharged into the atmosphere through the air inlet pipeline or the air outlet pipeline, and pollution is caused, and meanwhile, the closed box body 1 can fully exert the thermal desorption effect of the high-temperature steam on saturated activated carbon in the carbon box 3.
As shown in fig. 2 and 6, a connecting rod 141 is fixedly connected to the inner side of the side wall of one end of the split half-box 11, which is in contact with the end cover 2, and a first spring 142 is sleeved on the connecting rod 141; the two connecting rods 141 are symmetrically arranged about the contact surfaces of the two split half boxes 11; both the connecting rods 141 penetrate through the baffle 13; the baffle 13 is separated from the guide module 12 when high-temperature steam is not introduced, the gap between the baffle 13 and the guide module 12 is used for allowing waste gas to enter the box body 1 and contact activated carbon, the split half box 11 is connected with the baffle 13 through the connecting rod 141 at the moment, the baffle 13 is separated from the guide module 12 when high-temperature steam is not introduced, the piston rod 44 drives the contact plate 43 to extrude outwards due to air pressure when high-temperature steam is introduced into the main pipe 41, the pressure of the first spring 142 can be counteracted by the air pressure provided by the contact plate 43 in the process, and when the contact plate 43 contacts with the baffle 13 and extrudes the baffle 13 to move, the baffle 13 can be made to move towards one side of the guide module 12 and be attached tightly, so that the sealing effect on the box body 1 is achieved, and the effective thermal desorption effect on the activated carbon is maintained.
As shown in fig. 7 to 8, the charcoal box 3 includes a first drawer 31, a second drawer 32, and a third drawer 33; the first drawer 31, the second drawer 32 and the third drawer 33 are arranged in the box body 1 in sequence from top to bottom; a plurality of bearing frames 34 are fixedly connected on the inner side of one split half box 11 through screws; the first drawer 31, the second drawer 32 and the third drawer 33 slide on the bearing frame 34 respectively; the first drawer 31, the second drawer 32 and the third drawer 33 are all used for bearing activated carbon, and are sequentially arranged up and down, the bearing frame 34 is fixedly connected on the split half box 11 in advance through screws, and the bearing frame 34 can be used for bearing the first drawer 31, the second drawer 32 and the third drawer 33, so that the first drawer 31, the second drawer 32 and the third drawer 33 can slide on the bearing frame 34 under the action of manpower, and the activated carbon can be replaced conveniently.
As shown in fig. 7-9, one end of the first drawer 31, the second drawer 32 and the third drawer 33, which is positioned outside the box body 1, is fixedly connected with an end plate 36, and the end plate 36 is connected with the side wall of the split half box 11 in an embedded manner; a connecting shaft 35 is fixedly connected to one side of the first drawer 31, the second drawer 32 and the third drawer 33, and the first drawer 31, the second drawer 32 and the third drawer 33 are in sliding fit with the bearing frame 34 through the connecting shaft 35; the end plate 36 can be used for connecting the first drawer 31, the second drawer 32 and the third drawer 33, and the end plate 36 is connected with one side of the split half box 11 in an embedded manner, so that the limiting effect on the first drawer 31, the second drawer 32 and the third drawer 33 can be realized, the connecting shaft 35 arranged in the second side can be in sliding fit with the bearing frame 34, the limiting effect on the first drawer 31, the second drawer 32 and the third drawer 33 is improved, when one of the first drawer 31, the second drawer 32 and the third drawer 33 slides to the tail end, deflection can be realized by utilizing the connecting shaft 35, one of the first drawer 31, the second drawer 32 and the third drawer 33 is in a state shown in an attached figure 5, and the first drawer 31, the second drawer 32 or the third drawer 33 which are obliquely arranged can be convenient for an operator to replace active carbon.
As shown in fig. 9, a first connecting angle 311 is fixedly connected to the bottom of one end of the first drawer 31 located in the split half-box 11, and a second connecting angle 321 is correspondingly fixedly connected to the bottom of one end of the second drawer 32 located in the split half-box 11; a swing angle 371 is rotatably connected to the upper middle part of the second drawer 32 through a rotating shaft, and the swing angle 371 is arranged corresponding to the first connection angle 311; the two swinging angles 371 are symmetrically arranged about the middle of the second drawer 32, and a movable rod 372 is in sliding fit between the two swinging angles 371; a torsion spring is clamped between the swing angle 371 and the inner side wall of the second drawer 32, and is sleeved on the rotating shaft, and the torsion spring limits the swing angle 371 to rotate only in a direction away from the end plate 36; because the service life of the activated carbon is limited, after repeated thermal desorption is carried out repeatedly for a plurality of times, the service life of the activated carbon is reduced, at this time, the activated carbon needs to be replaced, in general, when the activated carbon in the carbon tank 3 is replaced, the first drawer 31, the second drawer 32 or the third drawer 33 is slipped out, and the activated carbon carried by the activated carbon is enabled to be in an inclined state, at this time, in order to enable the first drawer 31, the second drawer 32 or the third drawer 33 to keep inclined, a support needs to be given, the second drawer 32 or the third drawer 33 of the next layer is usually slipped out by hand, and is used for carrying the first drawer 31 or the second drawer 32 above, in the device, when the first drawer 31 is slipped out again, the first drawer 32 is in an inclined state, as a first connection angle 311 of the bottom surface of the inner end part of the first drawer 31 is blocked with an oscillation angle 371 on the second drawer 32 after a sliding distance, and because the oscillation angle 371 cannot rotate towards the direction close to 36 due to the limitation of a torsion spring, the second drawer 32 can be in a certain degree, and the second drawer 32 can be in a certain inclined state is enabled to be in a state, and the second drawer 31 is in a certain degree of inclination angle is enabled to be in a state, and the second drawer 32 can be in a certain degree of being in a state, and the first end plate 31 is in an inclined state is in a state and a certain degree of the first connection angle is used as a drawer 31 is in the bottom end plate 31, and an inner end face of the first connection angle is used, and a bottom end plate 31 is in the first connection angle is used, when the first drawer 31 is in the bottom end plate 31 is in the bottom end face; when the second drawer 32 is withdrawn, the swing angle 371 is rotated and contracted inward, and the movable rod 372 is also slid for restricting the synchronous movement of the two swing angles 371.
As shown in fig. 10, the upper middle part of the third drawer 33 is also rotatably connected with a swinging angle 371 corresponding to the second drawer 32 through a rotating shaft, and a movable rod 372 is also slidingly matched between the two swinging angles 371;
the first drawers 31 are located at the top of the split half box 11, the third drawers 33 are located at the bottom of the split half box 11, and the second drawers 32 are arranged in plurality and are located between the first drawers 31 and the third drawers 33 in an equidistant array; the third drawer 33 is driven by the second drawer 32 above and is located at the bottommost part, so that the bottom of the third drawer 33 is not provided with the first connection angle 311 or the second connection angle 321 corresponding to the first drawer 31 and the second drawer 32, and only the top of the third drawer is provided with the swinging angle 371, so that when the adjacent second drawer 32 slides out, the corresponding sliding-out part distance can realize the support of the adjacent second drawer 32, and when the third drawer 33 slides out, only the third drawer 33 only needs to slide out, and the third drawer is closer to the ground, so that the ground can be used as the support.
Example two
As shown in fig. 11, in order to more facilitate the replacement of activated carbon and avoid the existence of the swing angle 371 from affecting the vertical placement of activated carbon, in comparative example one, another embodiment of the present invention is as follows: the two sides of the second drawer 32 are provided with sliding grooves 322, and a push plate 39 is connected to one side of the second drawer 32 adjacent to the end plate 36 in a sliding manner; the two ends of the push plate 39 are fixedly connected with sliding blocks which are in sliding fit with the sliding grooves 322; a holding plate 38 is fixedly connected in the middle of the top of the push plate 39; when the device is used, the swing angle 371 exists on the second drawer 32, so that the activated carbon corresponding to one side of the swing angle 371 is difficult to vertically place on the second drawer 32, at the moment, the activated carbon can be placed in the end, adjacent to the end plate 36, of the second drawer 32, and the push plate 39 is driven to move towards the end far away from the end plate 36 by the holding plate 38, so that the activated carbon can be placed in order without being influenced by the swing angle 371.
Working principle: in the prior art, when thermal desorption is adopted to regenerate saturated activated carbon, a steam mixture combined with the hot steam is easily discharged into the atmosphere through an air outlet pipeline to cause pollution, so in order to prevent the situation, when the waste gas generated by a granulator is filtered, the air outlet pipeline is communicated with one end cover 2 and the opposite end cover 2, after the waste gas is sent into a box body 1 through the air inlet pipeline, the porous structure on the activated carbon can be used for absorbing and capturing harmful gas in the waste gas, so that the waste gas fully contacted with the activated carbon is purified, and the purified waste gas is discharged through the air outlet pipeline; meanwhile, a piston rod 44 is arranged in a branch pipe 42 of a steam pipeline 4, when the air pressure in the branch pipe 42 is increased, thrust is generated by the piston rod 44, the piston rod 44 drives a contact plate 43 to move outwards and contact with a baffle 13, so that the baffle 13 separated from the guide module 12 when high-temperature steam is not introduced is extruded to one side of the guide module 12 through the contact plate 43 and is tightly adhered to the guide module 12, and as the bottom of the baffle 13 is also spliced and matched with a rubber strip 15, when the baffle 13 moves and contacts with the guide module 12, sealing of two sides of the box body 1 is realized through the rubber strip 15, so that the high-temperature steam can be prevented from being discharged to the atmosphere through an air outlet pipeline when the thermal desorption regeneration effect of active carbon is realized, atmospheric pollution is caused, meanwhile, the generated steam mixture can be pumped by adopting an air outlet pipe arranged on the other split half box 11, the steam mixture is condensed by being matched with a condenser arranged outside, liquid is prepared, the liquid is treated, and the liquid containing harmful substances is removed by adopting a corresponding treatment mode, and the harmful substances in the waste water is removed relatively lower in cost;
because the service life of the activated carbon is limited, after repeated thermal desorption is carried out repeatedly for a plurality of times, the service life of the activated carbon is reduced, at this time, the activated carbon needs to be replaced, in general, when the activated carbon in the carbon tank 3 is replaced, the first drawer 31, the second drawer 32 or the third drawer 33 can be slipped out, and the activated carbon carried by the activated carbon is enabled to be in an inclined state, at this time, in order to enable the first drawer 31, the second drawer 32 or the third drawer 33 to keep inclined, a support needs to be given, the second drawer 32 or the third drawer 33 of the next layer is usually manually slipped out, and is used for carrying the first drawer 31 or the second drawer 32 above, in the device, when the first drawer 31 is slipped out, the first drawer 32 is used as an example, due to the first connection angle 311 of the bottom surface of the inner end part of the first drawer 31, the second drawer 32 is clamped after a sliding distance, and the swing angle 371 cannot rotate towards the direction close to 36 due to the limitation of the torsion spring, the second drawer 32 can be in the inclined state, the second drawer 32 can be enabled to be in the inclined state, the first drawer 31 is in the inclined state and the first connection angle 311 is enabled to be in the inclined state, and the first drawer 31 is enabled to be in the inclined state and the first connection angle is enabled to be in the inclined state, and the first connection angle is not to be separated from the first connection angle 311 and the first connection angle is used as an end plate 31, and the end plate 31 is required to be in the inclined state, and the first end plate 31 is required to be in the inclined state and the end plate 31 is required to be independently in the opposite a corresponding position to be in the inclined state.
It is apparent that the above examples are given by way of illustration only and are not limiting of the embodiments. Other variations and modifications of the present invention will be apparent to those of ordinary skill in the art in light of the foregoing description. It is not necessary here nor is it exhaustive of all embodiments. And obvious variations or modifications thereof are contemplated as falling within the scope of the present invention.
Claims (6)
1. A granulator exhaust gas treatment device, characterized in that: comprises a box body (1); the two ends of the box body (1) are fixedly connected with end covers (2) through screws; a plurality of carbon boxes (3) are connected inside the box body (1) in a sliding manner, and the carbon boxes (3) are arranged in parallel up and down;
the top and the bottom of the box body (1) are connected with steam pipelines (4) in a penetrating way, and the steam pipelines (4) comprise a main pipe (41) and branch pipes (42); the main pipes (41) are transversely arranged, and the branch pipes (42) are perpendicularly arranged in a crossing manner with the main pipes (41); the bottom of the branch pipe (42) is provided with a steam outlet, and the steam outlet is right opposite to the charcoal box (3); the middle part of the main pipe (41) is communicated with connecting pipes perpendicular to the main pipe (41) and the branch pipes (42); the root of the connecting pipe is communicated with the main pipe (41), and the end of the connecting pipe is fixedly connected with a flange plate (46); the connecting pipe penetrates through the box body (1);
the box body (1) consists of two split half boxes (11), and the two split half boxes (11) are fixedly connected through screws; the inner side wall of the split half box (11) is vertically fixedly connected with a guide module (12) adjacent to the end cover (2); the inner side wall of the split half-box (11) is adjacent to the guide module (12), and a baffle (13) is movably connected between the charcoal box (3) and the guide module (12); the bottom of the baffle (13) is inserted and matched with a rubber strip (15); the two baffles (13) are symmetrically arranged up and down and are obliquely arranged;
the charcoal box (3) comprises a first drawer (31), a second drawer (32) and a third drawer (33); the first drawer (31), the second drawer (32) and the third drawer (33) are sequentially arranged in the box body (1) up and down; the inner side of one split half box (11) is fixedly connected with a plurality of bearing frames (34) through screws; the first drawer (31), the second drawer (32) and the third drawer (33) slide on the bearing frame (34) respectively;
an end plate (36) is fixedly connected to one end of the first drawer (31), the second drawer (32) and the third drawer (33) which are positioned outside the box body (1), and the end plate (36) is connected with the side wall of the split half box (11) in an embedded manner; one side of the first drawer (31), one side of the second drawer (32) and one side of the third drawer (33) are fixedly connected with a connecting shaft (35), and the first drawer (31), the second drawer (32) and the third drawer (33) are in sliding fit with the bearing frame (34) through the connecting shaft (35);
the bottom of one end of the first drawer (31) positioned in the split half box (11) is fixedly connected with a first connecting angle (311), and the bottom of one end of the second drawer (32) positioned in the split half box (11) is correspondingly fixedly connected with a second connecting angle (321); a swing angle (371) is rotatably connected to the upper middle part of the second drawer (32) through a rotating shaft, and the swing angle (371) is arranged corresponding to the first connection angle (311); two swing angles (371) are symmetrically arranged about the middle of the second drawer (32), and a movable rod (372) is in sliding fit between the two swing angles (371); a torsion spring is clamped between the swing angle (371) and the inner side wall of the second drawer (32), and the torsion spring is sleeved on the rotating shaft.
2. A granulator exhaust gas treatment apparatus according to claim 1, characterized in that: the end part of the branch pipe (42) is in sliding fit with a piston rod (44), and a contact plate (43) is fixedly connected to one side of the piston rod (44) facing the baffle (13); one end of the piston rod (44) positioned in the branch pipe (42) is fixedly connected with a piston, and the piston rod (44) is sleeved with a second spring (45).
3. A granulator exhaust gas treatment apparatus according to claim 2, characterized in that: a connecting rod (141) is fixedly connected to the inner side of the side wall of one end, which is contacted with the end cover (2), of the split half box (11), and a first spring (142) is sleeved on the connecting rod (141); the two connecting rods (141) are symmetrically arranged about the contact surface of the two split half boxes (11); both connecting rods (141) penetrate through the baffle plate (13).
4. A granulator exhaust gas treatment apparatus according to claim 3, characterized in that: one split half box (11) is connected with the charcoal box (3) in a penetrating way, and the middle part of the other split half box (11) is communicated with an exhaust pipe.
5. A granulator exhaust gas treatment apparatus according to claim 1, characterized in that: the middle part above the third drawer (33) is also connected with a swinging angle (371) corresponding to the second drawer (32) through a rotating shaft, and a movable rod (372) is also matched between the two swinging angles (371) in a sliding way.
6. A granulator exhaust gas treatment apparatus according to claim 5, characterized in that: the first drawers (31) are arranged at the top of the split half box (11), the third drawers (33) are arranged at the bottom of the split half box (11), and the second drawers (32) are arranged in a plurality and are arranged between the first drawers (31) and the third drawers (33) in an equidistant array.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202310901331.1A CN116617810B (en) | 2023-07-21 | 2023-07-21 | Granulator exhaust treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202310901331.1A CN116617810B (en) | 2023-07-21 | 2023-07-21 | Granulator exhaust treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
CN116617810A CN116617810A (en) | 2023-08-22 |
CN116617810B true CN116617810B (en) | 2023-10-31 |
Family
ID=87617380
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202310901331.1A Active CN116617810B (en) | 2023-07-21 | 2023-07-21 | Granulator exhaust treatment equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN116617810B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN117088005B (en) * | 2023-10-13 | 2024-01-23 | 泉州海关综合技术服务中心 | Tealeaves storage cabinet of humidity independent control |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN206699828U (en) * | 2016-12-15 | 2017-12-05 | 合富国际股份有限公司 | Sliding rail structure of drawer |
CN110585855A (en) * | 2019-10-18 | 2019-12-20 | 郭渊明 | Movable waste gas treatment device |
CN212915068U (en) * | 2020-08-11 | 2021-04-09 | 浙江碧连天环境技术有限公司 | A exhaust treatment device for car spray booth |
CN215276506U (en) * | 2021-07-23 | 2021-12-24 | 天津益澈环保工程有限公司 | VOCs removes desorption equipment |
CN217288435U (en) * | 2022-04-29 | 2022-08-26 | 浙江悦胜环境科技有限公司 | Efficient honeycomb activated carbon regeneration treatment equipment |
-
2023
- 2023-07-21 CN CN202310901331.1A patent/CN116617810B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN206699828U (en) * | 2016-12-15 | 2017-12-05 | 合富国际股份有限公司 | Sliding rail structure of drawer |
CN110585855A (en) * | 2019-10-18 | 2019-12-20 | 郭渊明 | Movable waste gas treatment device |
CN212915068U (en) * | 2020-08-11 | 2021-04-09 | 浙江碧连天环境技术有限公司 | A exhaust treatment device for car spray booth |
CN215276506U (en) * | 2021-07-23 | 2021-12-24 | 天津益澈环保工程有限公司 | VOCs removes desorption equipment |
CN217288435U (en) * | 2022-04-29 | 2022-08-26 | 浙江悦胜环境科技有限公司 | Efficient honeycomb activated carbon regeneration treatment equipment |
Also Published As
Publication number | Publication date |
---|---|
CN116617810A (en) | 2023-08-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106163636B (en) | For removing CO from the atmosphere2Rotary multiple material bed moving system | |
CN116617810B (en) | Granulator exhaust treatment equipment | |
US20230211278A1 (en) | Continuous-motion direct air capture system | |
CN101584960A (en) | Separator and separation and purification method of gas-liquid phase absorbing membrane | |
CN211328803U (en) | New-type absorption steam desorption regeneration facility | |
JP2018058042A (en) | Purification treatment method of syngas and device | |
CN109731448B (en) | Integrated VOCs treatment device combining excimer radiation | |
CN102527186A (en) | Technology and system for recycling solvent oil from oil gas of butadiene prepared from butane under oxidative dehydrogenation effect | |
CN103830983A (en) | Process method for removing dust in waste gas | |
CN115228257A (en) | Intelligent desulfurization and denitrification device for atmospheric treatment | |
CN210665172U (en) | High-purity anhydrous hydrofluoric acid sampling equipment | |
CN218795962U (en) | Active carbon adsorption catalytic combustion device | |
CN213528027U (en) | Waste gas adsorption treatment tower | |
CN117563384B (en) | Furanol organic waste gas efficient recovery process and equipment | |
CN221385815U (en) | Organic waste gas purifying, adsorbing and recycling device | |
CN115445395B (en) | Gas collecting and filtering device for fermentation workshop | |
CN114887447B (en) | Chemical production line organic matter recovery processing device | |
CN110523263A (en) | Utilize the exhaust gas processing device and method of mineralized waste processing gas phase extracting tail gas | |
CN218166327U (en) | High-adsorptivity organic waste gas absorption device | |
RU51898U1 (en) | ABSORPTION AND DESORPTION DEVICE | |
CN116571226B (en) | Continuous operation device and process for desorbing and recycling VOCs (volatile organic compounds) adsorption material | |
CN220495975U (en) | Carbon dioxide trapping device | |
CN219815848U (en) | Biological trickling filter treatment equipment for VOC (volatile organic compound) -containing organic waste gas | |
CN219804411U (en) | Direct air carbon trapping and adsorbing device and system | |
CN118577118B (en) | Stainless steel spray tower for industrial waste gas treatment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |