CN212538903U - Carbon black tail gas dewatering device - Google Patents
Carbon black tail gas dewatering device Download PDFInfo
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- CN212538903U CN212538903U CN202020355830.7U CN202020355830U CN212538903U CN 212538903 U CN212538903 U CN 212538903U CN 202020355830 U CN202020355830 U CN 202020355830U CN 212538903 U CN212538903 U CN 212538903U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
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Abstract
The application discloses carbon black tail gas dewatering device includes: the waste heat recovery mechanism is provided with a heat exchange tube for exchanging heat with the carbon black tail gas; the temperature of the carbon black tail gas discharged from the waste heat recovery mechanism is higher than the flue gas dew point of the carbon black tail gas; the spraying container is positioned at the downstream of the waste heat recovery mechanism and is provided with an inlet and an outlet, the inlet is positioned at the lower half part of the spraying container, and the outlet is positioned at the top of the spraying container; a filling part and a spraying part are arranged in the spraying container, the filling part is positioned between the inlet and the outlet, and the spraying part is positioned between the filling part and the outlet; and the circulating mechanism is connected with the spraying part and comprises a liquid storage part arranged at the bottom of the spraying container and a circulating pump used for conveying the liquid in the liquid storage part to the spraying part. The application provides a carbon black tail gas dewatering device can dewater carbon black tail gas, can carry out recycle to the waste heat of carbon black tail gas simultaneously.
Description
Technical Field
The application relates to the technical field of carbon black tail gas treatment, in particular to a carbon black tail gas dehydration device.
Background
The statements in this section merely provide background information related to the present disclosure and may not constitute prior art.
Carbon black is an important chemical raw material and is widely applied to various fields of rubber, plastics, coatings, printing ink, war industry, communication, electronics, telecommunication, household appliances, cables, optical cables, high-energy batteries, electrostatic copying, photosensitive materials, printing and dyeing, papermaking, metallurgy and the like. The development of the carbon black industry promotes the social progress, but also increases the pollution to the living environment of human beings.
The carbon black industry has always been an industry with high energy consumption and high pollution. With the rapid development of the automotive industry, the demand for carbon black is also increasing. For the development of the carbon black industry, the carbon black production method not only continuously adapts to the market requirement, but also needs to excavate the internal potential of the carbon black, reduce the energy consumption of the carbon black production, fully utilize the waste heat in the carbon black production, realize the cyclic utilization of resources and reduce the pollution.
The carbon black tail gas is a byproduct generated in the carbon black production process, and in the carbon black production process, the CO and H can be generated through pyrolysis of raw oil2And waiting for the waste gas of the combustible gas, wherein the waste gas is the carbon black tail gas. The carbon black tail gas comes from a carbon black reaction furnace, contains carbon black powder, and is generally discharged after being purified by a main bag filter. Due to the technological requirements of carbon black production, a large amount (about 10-15 m) of carbon black needs to be sprayed3And/h) cooling by using quenching water, so that the water content in the carbon black tail gas is higher and is about 36-40%. The carbon black tail gas has high water content, low heat value, more complex components, water content and NH3Dust, etc. In order to avoid pollution, the carbon black tail gas needs to be recycled.
The carbon black tail gas is mainly used as a drying furnace fuel or a tail gas boiler fuel in the carbon black industry. The carbon black tail gas boiler can recover tail gas discharged in the carbon black production process and convert chemical energy in the carbon black tail gas into heat energy. By this conversion, substances such as hydrogen, methane, and carbon monoxide in the carbon black off-gas are converted into water and carbon dioxide.
However, when the carbon black tail gas is utilized, the amount of coal gas used for recovering the carbon black tail gas is increased, the power consumption is increased and the partition wall of the regenerator of the coke oven is seriously corroded due to the high water content of the carbon black tail gas. Therefore, the dehydration of the carbon black tail gas is particularly important.
It should be noted that the above background description is only for the convenience of clear and complete description of the technical solutions of the present application and for the understanding of those skilled in the art. Such solutions are not considered to be known to the person skilled in the art merely because they have been set forth in the background section of the present application.
SUMMERY OF THE UTILITY MODEL
In view of the deficiencies of the prior art, one of the objectives of the present application is to provide a carbon black tail gas dehydration device, which can dehydrate carbon black tail gas and recycle the waste heat of the carbon black tail gas.
In order to achieve the purpose, the technical scheme is as follows:
a carbon black tail gas dehydration device comprises:
the waste heat recovery mechanism is provided with a heat exchange tube for exchanging heat with the carbon black tail gas; the temperature of the carbon black tail gas discharged from the waste heat recovery mechanism is higher than the flue gas dew point of the carbon black tail gas;
the spraying container is positioned at the downstream of the waste heat recovery mechanism and is provided with an inlet and an outlet, the inlet is positioned at the lower half part of the spraying container, and the outlet is positioned at the top of the spraying container; a filling part and a spraying part are arranged in the spraying container, the filling part is positioned between the inlet and the outlet, and the spraying part is positioned between the filling part and the outlet;
and the circulating mechanism is connected with the spraying part and comprises a liquid storage part arranged at the bottom of the spraying container and a circulating pump used for conveying the liquid in the liquid storage part to the spraying part.
In a preferred embodiment, a heat exchanging portion is provided between the circulation pump and the spraying portion, so that the liquid in the liquid storage portion is circulated in a closed manner.
As a preferred embodiment, a pressurizing part is arranged at the upstream of the waste heat recovery mechanism, and the carbon black tail gas entering the waste heat recovery mechanism can be pressurized to 10-16 kilopascals by the pressurizing part; the waste heat recovery mechanism can produce 0.5 MPa steam or deoxygenated water.
In a preferred embodiment, the outer wall of the heat exchange tube is provided with a fin, and the pitch of the fin has a preset width; and the flowing direction of at least part of liquid in the heat exchange pipe is vertical to the flowing direction of the carbon black tail gas in the waste heat recovery mechanism.
As a preferred embodiment, the waste heat recovery mechanism is provided with an upper header, a lower header, an external header and a steam drum; the upper header and the lower header are connected to form the outer wall of the waste heat recovery mechanism, and the upper header and the lower header are respectively connected with the steam drum through the outer connecting pipes.
As a preferred embodiment, the shower section includes a trough distributor; an airflow uniform distributor is arranged between the filling part and the inlet.
As a preferred embodiment, the spraying part is provided with three layers; a washing part is arranged between the spraying part and the outlet, and the washing part is provided with two layers; and ceramic filler is arranged in the filler part.
In a preferred embodiment, the wall surface and the inlet of the spray container are made of carbon steel and corrosion-resistant or glass fiber reinforced plastics; the spray nozzle of the spraying part is made of ceramic or polypropylene material; the nozzle of the flushing part is made of polypropylene material.
In a preferred embodiment, the top of the spraying container is provided with a ridge type demister.
In a preferred embodiment, the temperature of the carbon black tail gas discharged from the waste heat recovery mechanism is 160 ℃; the temperature of the carbon black tail gas discharged from the outlet of the spraying container is 50 ℃, and the water content is 10-12%.
Has the advantages that:
the carbon black tail gas dewatering device that this application embodiment provided sprays container and waste heat recovery mechanism through setting up, makes this device not only can dewater, improve the calorific value of carbon black tail gas to carbon black tail gas, can carry out recycle to the waste heat of carbon black tail gas simultaneously, can also reduce impurity such as dust, ammonia in the carbon black tail gas, improves the cleanliness factor of carbon black tail gas.
And the temperature of the carbon black tail gas discharged from the waste heat recovery mechanism is higher than the flue gas dew point of the carbon black tail gas, so that the waste heat recovery mechanism cannot be corroded at low temperature.
In addition, by arranging the circulating mechanism, the liquid in the liquid storage part can be recycled, and the leakage of volatile smell such as ammonia contained in the condensed water in the carbon black tail gas is avoided.
Specific embodiments of the present application are disclosed in detail with reference to the following description and drawings, indicating the manner in which the principles of the application may be employed. It should be understood that the embodiments of the present application are not so limited in scope.
Features that are described and/or illustrated with respect to one embodiment may be used in the same way or in a similar way in one or more other embodiments, in combination with or instead of the features of the other embodiments.
It should be emphasized that the term "comprises/comprising" when used herein, is taken to specify the presence of stated features, integers, steps or components but does not preclude the presence or addition of one or more other features, integers, steps or components.
Drawings
In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings needed to be used in the description of the embodiments or the prior art will be briefly introduced below, it is obvious that the drawings in the following description are only some embodiments of the present application, and for those skilled in the art, other drawings can be obtained according to the drawings without inventive exercise.
Fig. 1 is a schematic structural diagram of a carbon black tail gas dehydration device provided in an embodiment of the present application.
Description of reference numerals:
1. a main bag filter; 2. a waste heat recovery mechanism; 3. a spray container; 4. a filler section; 5. a heat exchanging part; 6. a circulation pump; 7. a steam drum; 8. a booster fan; 9. a spraying part; 10. an outlet; 11. an inlet; 12. a heat exchange tube.
Detailed Description
In order to make those skilled in the art better understand the technical solutions in the present application, the technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application, and it is obvious that the described embodiments are only a part of the embodiments of the present application, 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 application.
It will be understood that when an element is referred to as being "disposed on" another element, it can be directly on the other element or intervening elements may also be present. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or intervening elements may be present. The terms "vertical," "horizontal," "left," "right," and the like as used herein are for illustrative purposes only and do not represent the only embodiments.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this application belongs. The terminology used herein in the description of the present application is for the purpose of describing particular embodiments only and is not intended to be limiting of the application. As used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.
Please refer to fig. 1. The embodiment of the application provides a carbon black tail gas dewatering device, and the device comprises a waste heat recovery mechanism 2, a spraying container 3 and a circulating mechanism. The carbon black tail gas treated by the method can be generated after being filtered by the main bag filter 1, the water content of the carbon black tail gas is about 36%, and the temperature of the carbon black tail gas is about 230 ℃. Of course, the carbon black tail gas water content and the temperature that produce under different operating modes are different, and the device that produces carbon black tail gas also can be different, and this application embodiment does not do the restriction to this.
The waste heat recovery mechanism 2 is provided with a heat exchange tube 12 for exchanging heat with the carbon black tail gas. The temperature of the carbon black tail gas discharged from the waste heat recovery mechanism 2 is higher than the flue gas dew point of the carbon black tail gas. The flue gas dew point refers to the temperature at which the acidic species (e.g., hydrogen sulfide) in the carbon black tail gas begin to condense. The spraying container 3 is positioned at the downstream of the waste heat recovery mechanism 2. The spray container 3 has an inlet 11 and an outlet 10. The inlet 11 is located in the lower half of the spray container 3. The outlet 10 is located at the top of the spray container 3. The spraying container 3 is internally provided with a filling part 4 and a spraying part 9. The filler part 4 is located between the inlet 11 and the outlet 10. The shower portion 9 is located between the filler portion 4 and the outlet 10. The circulating mechanism is connected with the spraying part 9. The circulating mechanism comprises a liquid storage part arranged at the bottom of the spraying container 3 and a circulating pump 6 used for conveying the liquid in the liquid storage part to the spraying part 9. The number of circulation pumps 6 is not limited by the present application.
The carbon black tail gas dewatering device that this application embodiment provided sprays container 3 and waste heat recovery mechanism 2 through setting up, makes this device not only can dewater, improve the calorific value of carbon black tail gas to carbon black tail gas, can carry out recycle to the waste heat of carbon black tail gas simultaneously, can also reduce impurity such as dust, ammonia in the carbon black tail gas, improves the cleanliness factor of carbon black tail gas.
Moreover, the temperature of the carbon black tail gas discharged from the waste heat recovery mechanism 2 is higher than the flue gas dew point of the carbon black tail gas, so that the waste heat recovery mechanism 2 cannot be corroded at low temperature.
In addition, by arranging the circulating mechanism, the liquid in the liquid storage part can be recycled, and the leakage of volatile smell such as ammonia contained in the condensed water in the carbon black tail gas is avoided.
In the embodiment of the present application, the carbon black tail gas dehydration device washes the carbon black tail gas by the spray container 3, and cools and dehydrates the carbon black tail gas. Thus, the heat in the carbon black off-gas is replaced into the circulating water (i.e., the liquid sprayed by the spraying section 9), so that the temperature of the circulating water in the spraying container 3 is increased. In order to effectively cool and dehydrate the carbon black tail gas by the circulating water, the heat in the circulating water must be replaced again.
Therefore, a heat exchanging part 5 can be arranged between the circulating pump 6 and the spraying part 9, so that the liquid in the liquid storage part can realize closed circulation. Specifically, the heat exchanging portion 5 may be a plate heat exchanger. Other cooling water pipe networks are introduced into the plate heat exchanger, and heat in circulating water in the spraying container 3 is replaced, so that the circulating water in the spraying container 3 is cooled, carbon black tail gas can be cooled and dehydrated circularly, and leakage of carbon black tail gas condensate water odor (pungent odor of volatile gases such as ammonia gas) is avoided.
In the embodiment of the present application, a pressurizing portion may be disposed upstream of the waste heat recovery mechanism 2, so that the carbon black tail gas overcomes the resistance in the conveying process. The carbon black tail gas entering the waste heat recovery mechanism 2 can be pressurized to 10-16 kPa by the pressurizing part. The pressurizing part may be a pressurizing fan 8.
In order to increase the heat exchange area of the heat exchange tube 12 and improve the heat exchange coefficient, the outer wall of the heat exchange tube 12 may be provided with fins. However, the dust content of the carbon black tail gas is about 18mg/m3Most of the components are carbon black dust and the like escaping after being filtered by the main bag filter 1 and are easy to attach to fins of the heat exchange tube 12, the water content of carbon black tail gas reaches 36%, carbon black mud is easy to wrap the inner surface of the waste heat recovery mechanism 2 and is hung on the wall in the cooling process, and therefore blocking is aggravated. In this regard, the pitch of the fins may have a predetermined width to reduce the occurrence of clogging. Specifically, the pitch of the fins is not less than 10 mm.
The arrangement of the heat exchange tubes 12 is not limited in the embodiments of the present application. Preferably, the flowing direction of at least part of the liquid in the heat exchange tube 12 is perpendicular to the flowing direction of the carbon black tail gas in the waste heat recovery mechanism 2, so as to enhance the heat exchange effect.
In the embodiment of the present application, the waste heat recovery mechanism 2 may be provided with an upper header, a lower header, an outer header, and a steam drum 7. The upper header and the lower header are connected to form the outer wall of the waste heat recovery mechanism 2, and the heat exchange tubes 12 are arranged in the upper header and the lower header. The upper header and the lower header are respectively connected with the steam pocket 7 through the external connecting pipes, so that the equipment is prevented from being washed by fluid. The structure of upper and lower header has reduced the manufacturing degree of difficulty, has reduced the installation work volume on the scene, and is also comparatively simple to the sealed of equipment, can effectually prevent to leak. A steam-water separation part can be arranged in the steam drum 7. The liquid in the heat exchange tube 12 absorbs the heat of the carbon black tail gas, the heat is increased, the liquid flows to the steam drum 7 at the top, and the steam-water separation part in the steam drum 7 processes the product flowing into the steam drum, so that the finally generated steam has higher quality. Meanwhile, the steam pocket 7 can also have a deoxidizing function, so that the waste heat recovery mechanism 2 can produce 0.5 MPa steam or deoxidized water, and the energy of carbon black tail gas is fully utilized.
In the embodiment of the present application, the spraying container 3 may be a spraying tower, which can cool the temperature of the carbon black tail gas and remove a large amount of moisture in the carbon black tail gas. An air flow distributor, such as a tubular air flow distributor, can be arranged between the packing part 4 and the inlet 11, so that the carbon black tail gas is distributed more uniformly in the whole spray tower. The spray section 9 may include a trough distributor to provide a more uniform distribution of spray throughout the spray tower. This spray container 3 has strengthened the abundant contact of carbon black tail gas and circulating water, and carbon black tail gas has sufficient dwell time to make cooling effect good, the dehydration is more abundant.
In the embodiment of the present application, the spraying part 9 may have three layers, and the spraying nozzle may be made of ceramic or polypropylene. A flushing part can be arranged between the spraying part 9 and the outlet 10 and is used for flushing impurities in the carbon black tail gas and taking away heat in the carbon black tail gas. The washing part can be provided with two layers for spraying washing water, and the nozzle can be made of polypropylene materials. The filler part 4 can be internally provided with ceramic filler, which not only resists corrosion, but also reduces resistance. The wall surface of the spray container 3 and the inlet 11 can be made of carbon steel and corrosion-resistant or glass fiber reinforced plastics. The top of the spraying container 3 can be provided with a ridge type demister so as to eliminate fog drops in the carbon black tail gas.
The spray container 3 in the embodiment of the application adopts the circulating spray design, so that spray water is recycled, the water consumption and the sewage discharge are greatly reduced, and the economical efficiency of system operation is ensured. The carbon black tail gas enters from the middle lower part of the spraying container 3, sequentially passes through the gas flow uniform distributor, the packing part 4, the spraying part 9 and the washing part, and is discharged from the top of the spraying container 3. The temperature of the carbon black tail gas is about 160 ℃ from the inlet 11, the temperature is reduced to about 50 ℃ after the carbon black tail gas passes through the spraying container 3, meanwhile, the water content is reduced to about 12% from 36.31%, and a large amount of condensed water is separated out in the period.
In the embodiment of the present application, the temperature of the carbon black off-gas discharged from the heat recovery mechanism 2 may be 160 ℃. The temperature of the carbon black tail gas discharged from the outlet 10 of the spray container 3 can be 50 ℃, and the water content can be 10-12%.
In a specific application scenario, carbon black tail gas with the temperature of 230 ℃ and the water content of 36.31% flows out of the main bag filter 1, is pressurized and boosted to 10-16 kilopascals through the booster fan 8, enters the waste heat recovery mechanism 2, and the waste heat recovery mechanism 2 can produce 0.5 MPa steam or deoxygenated water to be supplied to a boiler in front of the boiler for use, so that the service life of equipment can be prolonged. The temperature of the carbon black tail gas discharged from the waste heat recovery mechanism 2 is about 160 ℃, so that the waste heat is fully utilized, and a smoke dew point low-temperature corrosion area is avoided. The carbon black tail gas from the waste heat recovery mechanism 2 enters the spraying container 3, directly contacts with the circulating liquid (namely the liquid sprayed by the spraying part 9) to exchange heat, and is discharged out of the top of the container at 50 ℃. Circulating pump 6 is utilized as the power supply to the circulating liquid, gets into filler portion 4 after trough distributor evenly distributed from 3 upper portions of spraying container, and carbon black tail gas and circulating liquid are here abundant heat transfer back, and the circulating liquid gets into the stock solution portion of spraying container 3 bottom, and the water that appears can be drained to the sedimentation tank after deposiing, arrange the external processing water retrieval and utilization that carries on, has realized the saving of water resource and has utilized.
It should be noted that, in the description of the present application, the terms "first", "second", and the like are used for descriptive purposes only and for distinguishing similar objects, and no precedence between the two is intended or should be construed to indicate or imply relative importance. In addition, in the description of the present application, "a plurality" means two or more unless otherwise specified.
Any numerical value recited herein includes all values from the lower value to the upper value, in increments of one unit, provided that there is a separation of at least two units between any lower value and any higher value. For example, if it is stated that the number of a component or a value of a process variable (e.g., temperature, pressure, time, etc.) is from 1 to 90, preferably from 20 to 80, and more preferably from 30 to 70, it is intended that equivalents such as 15 to 85, 22 to 68, 43 to 51, 30 to 32 are also expressly enumerated in this specification. For values less than 1, one unit is suitably considered to be 0.0001, 0.001, 0.01, 0.1. These are only examples of what is intended to be explicitly recited, and all possible combinations of numerical values between the lowest value and the highest value that are explicitly recited in the specification in a similar manner are to be considered.
Unless otherwise indicated, all ranges include the endpoints and all numbers between the endpoints. The use of "about" or "approximately" with a range applies to both endpoints of the range. Thus, "about 20 to about 30" is intended to cover "about 20 to about 30", including at least the endpoints specified.
All articles and references disclosed, including patent applications and publications, are hereby incorporated by reference for all purposes. The term "consisting essentially of …" describing a combination shall include the identified element, ingredient, component or step as well as other elements, ingredients, components or steps that do not materially affect the basic novel characteristics of the combination. The use of the terms "comprising" or "including" to describe combinations of elements, components, or steps herein also contemplates embodiments that consist essentially of such elements, components, or steps. By using the term "may" herein, it is intended to indicate that any of the described attributes that "may" include are optional.
A plurality of elements, components, parts or steps can be provided by a single integrated element, component, part or step. Alternatively, a single integrated element, component, part or step may be divided into separate plural elements, components, parts or steps. The disclosure of "a" or "an" to describe an element, ingredient, component or step is not intended to foreclose other elements, ingredients, components or steps.
It is to be understood that the above description is intended to be illustrative, and not restrictive. Many embodiments and many applications other than the examples provided will be apparent to those of skill in the art upon reading the above description. The scope of the present teachings should, therefore, be determined not with reference to the above description, but should instead be determined with reference to the appended claims, along with the full scope of equivalents to which such claims are entitled. The disclosures of all articles and references, including patent applications and publications, are hereby incorporated by reference for all purposes. The omission in the foregoing claims of any aspect of the subject matter that is disclosed herein is not intended to forego such subject matter, nor should the inventors be construed as having contemplated such subject matter as being part of the disclosed inventive subject matter.
Claims (10)
1. A carbon black tail gas dewatering device is characterized by comprising:
the waste heat recovery mechanism is provided with a heat exchange tube for exchanging heat with the carbon black tail gas; the temperature of the carbon black tail gas discharged from the waste heat recovery mechanism is higher than the flue gas dew point of the carbon black tail gas;
the spraying container is positioned at the downstream of the waste heat recovery mechanism and is provided with an inlet and an outlet, the inlet is positioned at the lower half part of the spraying container, and the outlet is positioned at the top of the spraying container; a filling part and a spraying part are arranged in the spraying container, the filling part is positioned between the inlet and the outlet, and the spraying part is positioned between the filling part and the outlet;
and the circulating mechanism is connected with the spraying part and comprises a liquid storage part arranged at the bottom of the spraying container and a circulating pump used for conveying the liquid in the liquid storage part to the spraying part.
2. The carbon black tail gas dehydration device according to claim 1, characterized in that a heat exchanging part is provided between the circulation pump and the spraying part, so that the liquid in the liquid storage part is circulated in a closed manner.
3. The carbon black tail gas dehydration device according to claim 1, characterized in that a pressurizing part is arranged at the upstream of the waste heat recovery mechanism, and the carbon black tail gas entering the waste heat recovery mechanism can be pressurized to 10-16 kPa by the pressurizing part; the waste heat recovery mechanism can produce 0.5 MPa steam or deoxygenated water.
4. The carbon black tail gas dehydration device of claim 1, characterized in that the outer wall of the heat exchange tube is provided with a fin, and the pitch of the fin has a preset width; and the flowing direction of at least part of liquid in the heat exchange pipe is vertical to the flowing direction of the carbon black tail gas in the waste heat recovery mechanism.
5. The carbon black tail gas dehydration device according to claim 1, characterized in that said waste heat recovery mechanism is provided with an upper header, a lower header, an external header and a steam drum; the upper header and the lower header are connected to form the outer wall of the waste heat recovery mechanism, and the upper header and the lower header are respectively connected with the steam drum through the outer connecting pipes.
6. The carbon black tail gas dehydration device according to claim 1, characterized in that the spraying section comprises a trough distributor; an airflow uniform distributor is arranged between the filling part and the inlet.
7. The carbon black tail gas dehydration device according to claim 1, characterized in that the spraying section is provided with three layers; a washing part is arranged between the spraying part and the outlet, and the washing part is provided with two layers; and ceramic filler is arranged in the filler part.
8. The carbon black tail gas dehydration device according to claim 7, characterized in that the spray container wall and inlet are made of carbon steel plus corrosion protection or glass fiber reinforced plastic; the spray nozzle of the spraying part is made of ceramic or polypropylene material; the nozzle of the flushing part is made of polypropylene material.
9. The carbon black tail gas dehydration device of claim 1, characterized in that a ridge demister is arranged on the top of the spray container.
10. The carbon black tail gas dehydration device according to claim 1, characterized in that the temperature of the carbon black tail gas discharged from the waste heat recovery mechanism is 160 ℃; the temperature of the carbon black tail gas discharged from the outlet of the spraying container is 50 ℃, and the water content is 10-12%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020355830.7U CN212538903U (en) | 2020-03-19 | 2020-03-19 | Carbon black tail gas dewatering device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202020355830.7U CN212538903U (en) | 2020-03-19 | 2020-03-19 | Carbon black tail gas dewatering device |
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| CN212538903U true CN212538903U (en) | 2021-02-12 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114562905A (en) * | 2022-01-25 | 2022-05-31 | 杭州制氧机集团股份有限公司 | Dividing wall type and contact type combined cooling device |
| CN115046356A (en) * | 2022-06-08 | 2022-09-13 | 南京交通职业技术学院 | Tail gas absorption device for asphalt modifier production and working method thereof |
-
2020
- 2020-03-19 CN CN202020355830.7U patent/CN212538903U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114562905A (en) * | 2022-01-25 | 2022-05-31 | 杭州制氧机集团股份有限公司 | Dividing wall type and contact type combined cooling device |
| CN115046356A (en) * | 2022-06-08 | 2022-09-13 | 南京交通职业技术学院 | Tail gas absorption device for asphalt modifier production and working method thereof |
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