CN211585907U - Be used for organic waste gas oxidation and adsorption treatment device - Google Patents
Be used for organic waste gas oxidation and adsorption treatment device Download PDFInfo
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- CN211585907U CN211585907U CN201921935098.4U CN201921935098U CN211585907U CN 211585907 U CN211585907 U CN 211585907U CN 201921935098 U CN201921935098 U CN 201921935098U CN 211585907 U CN211585907 U CN 211585907U
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- adsorption
- adsorption tower
- waste gas
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- 238000001179 sorption measurement Methods 0.000 title claims abstract description 102
- 239000007789 gas Substances 0.000 title claims abstract description 50
- 239000010815 organic waste Substances 0.000 title claims abstract description 29
- 230000003647 oxidation Effects 0.000 title claims abstract description 14
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 39
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 17
- 239000002912 waste gas Substances 0.000 claims description 22
- 230000001590 oxidative effect Effects 0.000 claims description 3
- 238000001914 filtration Methods 0.000 abstract description 8
- 238000000746 purification Methods 0.000 abstract description 7
- 230000007246 mechanism Effects 0.000 abstract description 6
- 238000013461 design Methods 0.000 abstract description 3
- 230000006978 adaptation Effects 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 239000000945 filler Substances 0.000 description 4
- 230000007774 longterm Effects 0.000 description 4
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 238000013475 authorization Methods 0.000 description 2
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 230000003044 adaptive effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- DALDUXIBIKGWTK-UHFFFAOYSA-N benzene;toluene Chemical compound C1=CC=CC=C1.CC1=CC=CC=C1 DALDUXIBIKGWTK-UHFFFAOYSA-N 0.000 description 1
- 150000001555 benzenes Chemical class 0.000 description 1
- GMGLYSIINJPYLI-UHFFFAOYSA-N butan-2-one;propan-2-one Chemical compound CC(C)=O.CCC(C)=O GMGLYSIINJPYLI-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
The utility model discloses a be used for organic waste gas oxidation and adsorption treatment device, including adsorption tower and No. two adsorption towers, the active carbon adsorption piece is from getting put mouthful (not marked in the picture) the sealed space that forms between inserting the support filter and the under bracing filter of department adaptation and the tip of active carbon adsorption piece has linked firmly the hand (hold), install a switch on the body of inlet lateral pipe No. one, install No. two switches on the body of inlet lateral pipe No. two inlet lateral pipes, the top of inlet lateral pipe and the top of No. two inlet lateral pipes upwards communicate to on the inlet manifold jointly, the bottom gas outlet of adsorption tower and the top of No. one outlet lateral pipe communicate together, the bottom gas outlet of No. two adsorption towers communicates with the top of No. two outlet lateral pipes together. The utility model discloses an aspect can two mechanisms the purification ability reinforce, and on the other hand in case inside activated carbon layer takes place to block up inefficacy, structural design is reasonable because of long-time filtration very easily.
Description
Technical Field
The utility model relates to a relevant technical field of exhaust-gas treatment specifically is a be used for organic waste gas oxidation and adsorption treatment device.
Background
The organic waste gas treatment refers to the treatment work of adsorption, filtration and purification of organic waste gas generated in the industrial production process. The organic waste gas treatment is generally carried out by air purification of organic substances containing carbon, such as carbon-hydrogen oxygen, such as formaldehyde organic waste gas treatment, benzene series organic waste gas treatment such as benzene toluene xylene, acetone butanone organic waste gas treatment, ethyl acetate waste gas treatment, oil mist organic waste gas treatment, furfural organic waste gas treatment, styrene and acrylic acid organic waste gas treatment, resin organic waste gas treatment, additive organic waste gas treatment, paint mist organic waste gas treatment, and Tianna water organic waste gas treatment.
Referring to fig. 1, reference numeral 1 indicates a schematic structural diagram of a device for oxidation and adsorption treatment of organic waste gas in the prior art, and a patent with an authorization number of CN201820841657 disclosed in the patent publication includes an adsorption tower 101, wherein a porous filler 102 is fixedly disposed inside the adsorption tower 101, the porous filler 102 is specifically an activated carbon layer, the waste gas treated by the preamble is finally introduced into the adsorption tower 101, and the activated carbon layer is used for adsorption treatment of the final waste gas, although the prior art device can perform the final adsorption treatment of the waste gas, there is a problem that the adsorption tower 101 is only provided with one activated carbon layer fixed inside the adsorption tower 101 and is not detachable, on one hand, the purification capacity of a single mechanism is limited, and on the other hand, once the activated carbon layer inside is easily blocked due to long-term filtration, the complete blockage is that the whole activated carbon layer fails, waste gas cannot be filtered and permeated, the accumulation phenomenon is easy to occur, the safety of equipment is further reduced, and the waste gas purification effect is poor, so that the related structure of the last adsorption process of waste gas treatment is necessarily improved to ensure the treatment effect.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a be used for organic waste gas oxidation and adsorb processing apparatus to solve the problem that proposes among the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme:
a device for oxidizing and adsorbing organic waste gas comprises a first adsorption tower and a second adsorption tower, wherein an upper support filter plate and a lower support filter plate are respectively and correspondingly arranged in the tower cavities of the first adsorption tower and the second adsorption tower, a taking and placing opening is formed in the tower wall between the upper support filter plate and the lower support filter plate and corresponding to the first adsorption tower and the second adsorption tower, an active carbon adsorption block is fittingly and hermetically inserted into a gap formed between the upper support filter plate and the lower support filter plate from the taking and placing opening, a handle is fixedly connected with the end part of the active carbon adsorption block, a top air inlet of the first adsorption tower is communicated with the bottom end of a first air inlet branch pipe, a top air inlet of the second adsorption tower is communicated with the bottom end of a second air inlet branch pipe, a first conduction switch is installed on the body of the first air inlet branch pipe, and a second conduction switch is installed on the body of the second air inlet branch pipe, the top end of the first branched gas inlet pipe and the top end of the second branched gas inlet pipe are communicated with the gas inlet main pipe together, the bottom gas outlet of the first adsorption tower is communicated with the top end of the first branched gas outlet pipe, the bottom gas outlet of the second adsorption tower is communicated with the top end of the second branched gas outlet pipe, and the first branched gas outlet pipe and the second branched gas outlet pipe are converged and then communicated with the gas outlet main pipe together.
As a further aspect of the present invention: the structure of the preamble of the device for treating exhaust gas is the same as that of the preamble of the prior art device.
As a further aspect of the present invention: the first adsorption tower and the second adsorption tower are identical in structure and are located at the same height.
Compared with the prior art, the beneficial effects of the utility model are that: the utility model discloses a be provided with an adsorption tower, No. two adsorption towers, go up the support filter, the under bracing filter, get and put the mouth, the active carbon adsorption piece, the hand (hold), inlet branch pipe, a switch on, No. two inlet branch pipes, No. two switch on, a bleeder and No. two bleeder of giving vent to anger, the purifying power that can two mechanisms on the one hand becomes strong, on the other hand in case inside active carbon layer takes place to block up the inefficacy because of filtering for a long time very easily, still can provide another circuit and carry out the processing of waste gas, whole journey does not need to shut down completely and overhauls again, the drawback of the security because of gaseous piling up the phenomenon and then reducing equipment more can not appear, structural design is reasonable, safety and ingeniousness, the reliability of equipment operation has been guaranteed, good popularization and application prospect has.
Drawings
Fig. 1 is a schematic structural diagram of a device for oxidation and adsorption treatment of organic waste gas in the prior art.
Fig. 2 is a schematic structural diagram of an improved device for oxidation and adsorption treatment of organic waste gas.
Fig. 3 is an enlarged schematic structural diagram of a modified apparatus for oxidation and adsorption treatment of organic waste gas at a.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1, reference numeral 1 indicates a schematic structural diagram of a device for oxidation and adsorption treatment of organic waste gas in the prior art, and a patent with an authorization number of CN201820841657 disclosed in the patent publication includes an adsorption tower 101, wherein a porous filler 102 is fixedly disposed inside the adsorption tower 101, the porous filler 102 is specifically an activated carbon layer, the waste gas treated by the preamble is finally introduced into the adsorption tower 101, and the activated carbon layer is used for adsorption treatment of the final waste gas, although the prior art device can perform the final adsorption treatment of the waste gas, there is a problem that the adsorption tower 101 is only provided with one activated carbon layer fixed inside the adsorption tower 101 and is not detachable, on one hand, the purification capacity of a single mechanism is limited, and on the other hand, once the activated carbon layer inside is easily blocked due to long-term filtration, the complete blockage is that the whole activated carbon layer fails, waste gas cannot be filtered and permeated, the accumulation phenomenon is easy to occur, the safety of equipment is further reduced, and the waste gas purification effect is poor, so that the related structure of the last adsorption process of waste gas treatment is necessarily improved to ensure the treatment effect.
Referring to fig. 2-3, reference numeral 2 indicates an improved structural schematic diagram of an organic waste gas oxidation and adsorption treatment device, in the embodiment of the present invention, the structure of the preorder waste gas treatment is the same as the preorder waste gas treatment structure in the prior art device, except that, one adsorption tower 101 is modified into two adsorption towers, the two adsorption towers are named as a first adsorption tower 201 and a second adsorption tower 202 respectively, the first adsorption tower 201 and the second adsorption tower 202 have the same structure and are at the same height, the tower cavities of the first adsorption tower 201 and the second adsorption tower 202 are respectively provided with an upper support filter plate 8 and a lower support filter plate 9, an access opening is provided between the upper support filter plate 8 and the lower support filter plate 9 and on the tower wall corresponding to the first adsorption tower 201 and the second adsorption tower 202, and an active carbon adsorption block 10 is inserted into the upper support filter plate 8 and the lower support filter plate 9 from the access opening in an adaptive seal manner A handle 11 is fixedly connected with the end part of the active carbon adsorption block 10 in the gap, the top air inlet of the first adsorption tower 201 is communicated with the bottom end of the first air inlet branch pipe 4, the top air inlet of the second adsorption tower 202 is communicated with the bottom end of the second air inlet branch pipe 6, a first conducting switch 5 is arranged on the pipe body of the first air inlet branch pipe 4, a second conducting switch 7 is arranged on the pipe body of the second air inlet branch pipe 6, the top end of the first air inlet branch pipe 4 and the top end of the second air inlet branch pipe 6 are communicated with the air inlet main pipe 3 upwards together, the bottom air outlet of the first adsorption tower 201 is communicated with the top end of the first air outlet branch pipe 12, the bottom air outlet of the second adsorption tower 202 is communicated with the top end of the second air outlet branch pipe 13, and the first air outlet branch pipe 12 and the second air outlet branch pipe 13 are converged and then communicated to the air outlet header pipe 14.
Through the improved device for oxidizing and adsorbing organic waste gas, the subsequent treatment structure of the oxidation and adsorption treatment device in the prior art is redesigned, and the device is provided with a first adsorption tower 201, a second adsorption tower 202, an upper support filter plate 8, a lower support filter plate 9, a pick-and-place opening, an active carbon adsorption block 10, a handle 11, a first branched gas inlet pipe 4, a first conducting switch 5, a second branched gas inlet pipe 6, a second conducting switch 7, a branched gas outlet pipe 12 and a second branched gas outlet pipe 13, when the device is used in particular, the first conducting switch 5 and the second conducting switch 7 are simultaneously opened, waste gas can be purified under the combined action of the first adsorption tower 201 and the second adsorption tower 202, the adsorption efficiency is improved, once the active carbon adsorption block 10 in the first adsorption tower 201 is easy to be blocked and completely loses efficacy due to long-time filtration, at the moment, the first conducting switch 5 is closed, the second conducting switch 7 is opened, the first adsorption tower 201 is stopped and isolated, the second adsorption tower 202 still can adsorb the waste gas, the active carbon adsorption block 10 in the first adsorption tower 201 is pulled out through the handle 11 for replacement, once the active carbon adsorption block 10 in the second adsorption tower 202 is easily blocked and completely fails due to long-term filtration, the second conducting switch 7 is closed, the first conducting switch 5 is opened, the second adsorption tower 202 is stopped and isolated, the first adsorption tower 202 still can adsorb the waste gas, the active carbon adsorption block 10 in the second adsorption tower 202 is pulled out through the handle 11 for replacement, the operation is set, on one hand, the purification capacity of the two mechanisms is enhanced, on the other hand, once the active carbon layer in the two mechanisms is easily blocked and fails due to long-term filtration, still can provide another circuit and carry out the processing of waste gas, whole journey does not need to shut down completely and overhauls again, more can not appear because of the accumulational phenomenon of gas and then the drawback of the security that reduces equipment, and structural design is reasonable, and is safe ingenious, has guaranteed the reliability of equipment operation, has good popularization and application prospect.
Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments or portions thereof without departing from the spirit and scope of the invention.
Claims (3)
1. A device for oxidizing and adsorbing organic waste gas comprises a first adsorption tower (201) and a second adsorption tower (202), and is characterized in that an upper supporting filter plate (8) and a lower supporting filter plate (9) are respectively and correspondingly arranged in tower cavities of the first adsorption tower (201) and the second adsorption tower (202), a taking and placing opening is formed in a tower wall corresponding to the first adsorption tower (201) and the second adsorption tower (202) between the upper supporting filter plate (8) and the lower supporting filter plate (9), an active carbon adsorption block (10) is fittingly and hermetically inserted into a gap formed between the upper supporting filter plate (8) and the lower supporting filter plate (9) from the taking and placing opening, the end part of the active carbon adsorption block (10) is fixedly connected with a handle (11), a top air inlet of the first adsorption tower (201) is communicated with the bottom end of a first air inlet branch pipe (4), a top air inlet of the second adsorption tower (202) is communicated with the bottom end of a second air inlet branch pipe (6), install one on the body of inlet lateral pipe (4) and switch (5) that lead to No. one, install No. two on the body of No. two inlet lateral pipes (6) and lead to switch (7), the top of inlet lateral pipe (4) and the top of No. two inlet lateral pipes (6) upwards communicate to on air intake manifold (3) jointly, the bottom gas outlet of adsorption tower (201) and the top of No. one outlet lateral pipe (12) communicate together, the bottom gas outlet of No. two adsorption towers (202) and the top of No. two outlet lateral pipes (13) communicate together, No. one outlet lateral pipe (12) and No. two outlet lateral pipes (13) converge the back and communicate to on air outlet manifold (14) jointly.
2. The oxidation and adsorption treatment device for organic waste gas according to claim 1, wherein the structure of the device for treating waste gas in the preamble is the same as the structure of the device for treating waste gas in the preamble of the prior art.
3. The device for oxidation and adsorption treatment of organic waste gas according to claim 1, wherein the first adsorption tower (201) and the second adsorption tower (202) have the same structure and are at the same height.
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CN201921935098.4U CN211585907U (en) | 2019-11-11 | 2019-11-11 | Be used for organic waste gas oxidation and adsorption treatment device |
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CN201921935098.4U CN211585907U (en) | 2019-11-11 | 2019-11-11 | Be used for organic waste gas oxidation and adsorption treatment device |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN112657309A (en) * | 2020-12-03 | 2021-04-16 | 淮北市森化碳吸附剂有限责任公司 | High-efficiency conversion rate adsorption tower |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN112657309A (en) * | 2020-12-03 | 2021-04-16 | 淮北市森化碳吸附剂有限责任公司 | High-efficiency conversion rate adsorption tower |
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Granted publication date: 20200929 |