CN215676574U - Powdered activated carbon cooling and collecting device - Google Patents
Powdered activated carbon cooling and collecting device Download PDFInfo
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- CN215676574U CN215676574U CN202121819618.2U CN202121819618U CN215676574U CN 215676574 U CN215676574 U CN 215676574U CN 202121819618 U CN202121819618 U CN 202121819618U CN 215676574 U CN215676574 U CN 215676574U
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Abstract
The utility model belongs to the technical field of processing of powdered activated carbon, and particularly relates to a powdered activated carbon cooling and collecting device which comprises a coil collecting mechanism, two separators and a dust remover which are connected in series and also comprises a draught fan, wherein the coil collecting mechanism is sequentially communicated from left to right; the coil collecting mechanism comprises a cooling bin and a material cooling coil arranged in the cooling bin, the inner space of the cooling bin is a cooling chamber, and a water inlet and a water outlet which are communicated with the cooling chamber are respectively formed in the cooling bin; according to the collecting device, the material cooling coil with the spiral structure is arranged in the cooling bin, cooling water is introduced to the material cooling coil for cooling the powdered activated carbon, so that the reliability of collection is guaranteed, and the cyclone separator and the bag-type dust collector are used for grading the powdered activated carbon and removing impurities in the powdered activated carbon, so that the effect of purifying the powdered activated carbon is achieved, the yield of the powdered activated carbon is guaranteed, the processing efficiency is improved, and the service life of equipment is prolonged.
Description
Technical Field
The utility model belongs to the technical field of powdered activated carbon processing, and particularly relates to a powdered activated carbon cooling and collecting device.
Background
The powdery active carbon takes high-quality sawdust and shells as raw materials, is produced by a zinc chloride method, has a developed mesoporous structure, large adsorption capacity, rapid filtration and other characteristics, has good application in the aspects of sudden odor and industrial pollutants in water treatment, has a caramel decolorization rate which is the adsorption performance of the reactive powdery active carbon on colored substances, has a good performance and an adsorption value which can reach 100 plus 110, and is widely applied to the pharmaceutical industry, the fine chemical industry, such as crude drug decolorization, oral medicine (silicon carbon silver, antidote and bowel clearing agent), chemical raw materials, medical intermediates, chemical bulk drugs, the biological pharmacy, the biochemical technology and decolorization, purification and refining of injection of various preparations; the product is suitable for medical industry such as antibiotics, streptomycin, lincomycin, gentamicin, penicillin, chloramphenicol, sulfonamides, alkaloids, hormones, ibuprofen, paracetamol, vitamin B1, vitamin B6, vitamin C, metronidazole, gallic acid, etc., can also be used for decoloring, impurity removing and peculiar smell removing of fine chemical products such as glyoxal, benzotriazole, methyl ester, glycerol, etc., is mainly used for decoloring, refining and removing 'heat source' of various injection medicaments, can also be used for decoloring vitamin C and other raw material medicaments, has strong decoloring capability and fast filtration speed, is suitable for decoloring and refining medicines, pesticides and Chinese and western raw materials, and has the effects of absorbing intestinal pathogens and detoxifying.
Suitable collection means are important conditions for the processing of powdered activated carbon.
Traditional powdered activated carbon collection device is when putting into use, because the powdered activated carbon temperature after the processing is very high, directly emits into fragile collection device in the collection device, reduces the temperature to powdered activated carbon earlier and then emits into collection device, has improved the processing cost undoubtedly to machining efficiency has been reduced.
SUMMERY OF THE UTILITY MODEL
In order to solve the problems in the prior art, the utility model provides a powdered activated carbon cooling and collecting device which has the characteristics of convenience in use and high processing efficiency.
In order to achieve the purpose, the utility model provides the following technical scheme: the powdery active carbon cooling and collecting device comprises a coil pipe collecting mechanism, two separators and a dust remover which are sequentially communicated from left to right, and also comprises an induced draft fan, wherein an air outlet nozzle of the induced draft fan is communicated with the dust remover by a pipeline; the coil collecting mechanism comprises a cooling bin and a material cooling coil arranged in the cooling bin, the inner space of the cooling bin is a cooling chamber, and a water inlet and a water outlet which are communicated with the cooling chamber are respectively formed in the cooling bin.
As a preferable technical scheme of the utility model, the material cooling coil is of a spiral structure.
As a preferable technical scheme of the utility model, the separator is a conical cyclone separator, and the processing air volume of the separator is 2000m3/h-5000m3/h。
As a preferred technical scheme of the utility model, the dust remover is a bag-type dust remover, and the processing air volume of the dust remover is 10000m3/h-16000m3/h。
As a preferable technical scheme of the utility model, the bottom end of the separator is provided with a trash discharge port and a valve.
As a preferred technical scheme of the present invention, a metal heat exchange water pipe having a spiral structure is wound around an outer wall of the separator, and the metal heat exchange water pipe is an aluminum pipe.
Compared with the prior art, the utility model has the beneficial effects that:
1. according to the collecting device, the material cooling coil with the spiral structure is arranged in the cooling bin, cooling water is introduced to the material cooling coil for cooling the powdered activated carbon, so that the reliability of collection is guaranteed, and the cyclone separator and the bag-type dust collector are applied to grading the powdered activated carbon and removing impurities in the powdered activated carbon, so that the effect of purifying the powdered activated carbon is achieved, the yield of the powdered activated carbon is guaranteed, the processing efficiency is improved, and the service life of equipment is prolonged;
2. because the temperature of the powdery active carbon after high-temperature oxygen-insulation regeneration can reach about 800 ℃, the powdery active carbon can be burnt out when oxygen is found, the danger coefficient is high, the device can rapidly cool the powdery active carbon with extremely high temperature to 60-80 ℃ and is lower than the ignition point of the powdery active carbon, thereby improving the controllability of the powdery active carbon, reducing the burning out of the powdery active carbon and improving the regeneration yield of the powdery active carbon.
Drawings
The accompanying drawings, which are included to provide a further understanding of the utility model and are incorporated in and constitute a part of this specification, illustrate embodiments of the utility model and together with the description serve to explain the principles of the utility model and not to limit the utility model. In the drawings:
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a front cross-sectional structural schematic view of a coil collection mechanism of the present invention;
in the figure: 1. a coil collecting mechanism; 2. a separator; 3. a dust remover; 4. an induced draft fan; 5. a cooling bin; 6. a material cooling coil; 7. a cooling chamber; 8. a water inlet; 9. and (7) a water outlet.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1-2, the present invention provides the following technical solutions: the powdery active carbon cooling and collecting device comprises a coil pipe collecting mechanism 1, two separators 2 and a dust remover 3 which are connected in series and are sequentially communicated from left to right, and also comprises an induced draft fan 4, wherein an air outlet nozzle of the induced draft fan 4 is communicated with the dust remover 3 by a pipeline; coil pipe collection mechanism 1 includes cooling chamber 5 and installs material cooling coil 6 in cooling chamber 5, the inner space of cooling chamber 5 is cooling chamber 7, water inlet 8 and delivery port 9 that are linked together with cooling chamber 7 have been seted up respectively on cooling chamber 5, when using, utilize water inlet 8 to let in the cooling water in the cooling chamber 7, powdered activated carbon passes through in the material import feeding material cooling coil 6, cooling water and material cooling coil 6 in the cooling chamber 7 produce the heat exchange, and cool down powdered activated carbon through material cooling coil 6, start draught fan 4 back, draught fan 4 produces and attracts the wind, separator 2 and the dust remover 3 that utilize two series connections remove dust and classify powdered activated carbon, guarantee the yield of powdered activated carbon.
Specifically, as shown in fig. 1 and fig. 2, in this embodiment, the material cooling coil 6 has a spiral structure, so that the contact area between the material cooling coil 6 and the powdered activated carbon is increased, the material cooling time is prolonged, and the cooling efficiency is improved.
Specifically, according to the embodiment shown in FIG. 1, the separator 2 is a conical cyclone separator, and the processing air volume of the separator 2 is 2000m3/h-5000m3H, can be 2000m3/h、3500m3H or 5000m3The treated air volume of this example was 3500m3And h, dedusting and grading the powdered activated carbon, and ensuring the yield of the powdered activated carbon.
Specifically, as shown in fig. 1, in this embodiment, the dust remover 3 is a bag-type dust remover, and the processing air volume of the dust remover 3 is 10000m3/h-16000m3H, can be 10000m3/h、13000m3H or 16000m3The treated air volume of this example was 3500m3H, dedusting the powdered activated carbon, and ensuring the yield of the powdered activated carbon to be 13000m3/h。
Specifically, according to the illustration in fig. 1, in this embodiment, the bottom end of the separator 2 is a trash discharge port and is provided with a valve, so as to facilitate discharging of the trash.
Specifically, as shown in fig. 1, in this embodiment, the outer wall of the separator 2 is wound with a metal heat exchange water pipe having a spiral structure, and the metal heat exchange water pipe is an aluminum pipe, so that the powdered activated carbon can be further cooled, and the safe operation of the separator 2 is ensured.
The working principle and the using process of the utility model are as follows: when the collecting device is used, cooling water is introduced into the cooling chamber 7 through the water inlet 8, the powdery active carbon is fed into the material cooling coil 6 through the material inlet, the cooling water in the cooling chamber 7 and the material cooling coil 6 generate heat exchange, the powdery active carbon is cooled through the material cooling coil 6, after the draught fan 4 is started, the draught fan 4 generates suction air, and the powdery active carbon is dedusted and classified by the two separators 2 and the deduster 3 which are connected in series, so that the yield of the powdery active carbon is ensured.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that changes may be made in the embodiments and/or equivalents thereof without departing from the spirit and scope of the utility model. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (6)
1. Powdered activated carbon cooling collection device, its characterized in that: the device comprises a coil pipe collecting mechanism (1), two separators (2) and a dust remover (3) which are connected in series and are sequentially communicated from left to right, and further comprises an induced draft fan (4), wherein an air outlet nozzle of the induced draft fan (4) is communicated with the dust remover (3) by a pipeline; the coil collecting mechanism (1) comprises a cooling bin (5) and a material cooling coil (6) arranged in the cooling bin (5), the inner space of the cooling bin (5) is a cooling chamber (7), and a water inlet (8) and a water outlet (9) communicated with the cooling chamber (7) are respectively formed in the cooling bin (5).
2. A powdered activated carbon cooling collection device as set forth in claim 1, characterized in that: the material cooling coil (6) is of a spiral structure.
3. Root of herbaceous plantA cooling collection device for powdered activated carbon as claimed in claim 1, characterized in that: the separator (2) is a conical cyclone separator, and the processing air volume of the separator (2) is 2000m3/h-5000m3/h。
4. A powdered activated carbon cooling collection device as set forth in claim 1, characterized in that: the dust remover (3) is a bag-type dust remover, and the processing air volume of the dust remover (3) is 10000m3/h-16000m3/h。
5. A powdered activated carbon cooling collection device as set forth in claim 1, characterized in that: the bottom end of the separator (2) is provided with a trash discharge port and a valve.
6. A powdered activated carbon cooling collection device as set forth in claim 1, characterized in that: the outer wall of the separator (2) is wound with a metal heat exchange water pipe of a spiral structure, and the metal heat exchange water pipe is an aluminum pipe.
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CN202121819618.2U CN215676574U (en) | 2021-08-05 | 2021-08-05 | Powdered activated carbon cooling and collecting device |
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CN202121819618.2U CN215676574U (en) | 2021-08-05 | 2021-08-05 | Powdered activated carbon cooling and collecting device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115555000A (en) * | 2022-10-11 | 2023-01-03 | 山东格瑞德环保科技有限公司 | Activated carbon water-cooling scraper type discharge opening device |
CN117339585A (en) * | 2023-11-23 | 2024-01-05 | 青岛冠宝林活性炭有限公司 | Pyrolysis device for powdered activated carbon |
-
2021
- 2021-08-05 CN CN202121819618.2U patent/CN215676574U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115555000A (en) * | 2022-10-11 | 2023-01-03 | 山东格瑞德环保科技有限公司 | Activated carbon water-cooling scraper type discharge opening device |
CN117339585A (en) * | 2023-11-23 | 2024-01-05 | 青岛冠宝林活性炭有限公司 | Pyrolysis device for powdered activated carbon |
CN117339585B (en) * | 2023-11-23 | 2024-04-30 | 青岛冠宝林活性炭有限公司 | Pyrolysis device for powdered activated carbon |
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