CN212712768U - Continuous production system of high SOx/NOx control active coke - Google Patents
Continuous production system of high SOx/NOx control active coke Download PDFInfo
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- CN212712768U CN212712768U CN202021016735.0U CN202021016735U CN212712768U CN 212712768 U CN212712768 U CN 212712768U CN 202021016735 U CN202021016735 U CN 202021016735U CN 212712768 U CN212712768 U CN 212712768U
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Abstract
The utility model provides a continuous production system of active burnt of high SOx/NOx control, include raw materials conveying mechanism, dosing mechanism, crocus mechanism, mediate granulation mechanism, carbomorphism mechanism, activation mechanism, finished product packagine machine and construct, raw materials conveying mechanism's ejection of compact department is connected with dosing mechanism's feeding department, and dosing mechanism's ejection of compact department is connected with the feeding department of crocus mechanism, and the ejection of compact department of crocus mechanism is connected with the feeding department of mediating granulation mechanism, and the ejection of compact department of mediating granulation mechanism is connected with the feeding department of carbomorphism mechanism, and the ejection of compact department of carbomorphism mechanism is connected with the feeding department of activation mechanism, and the ejection of compact department of activation mechanism is connected with the feeding department of finished product packagine. The utility model discloses a raw materials of well full automatization integrated control active coke production is carried, batching, crocus, is mediated granulation, carbomorphism, activation, finished product packaging process, has improved production efficiency greatly, and the active coke abrasion strength who obtains simultaneously from this reaches 98%, and compressive strength reaches 40Kgf, and the desulfurization value reaches 20mg/g, and the denitration value reaches 65%.
Description
Technical Field
The utility model belongs to the technical field of active burnt production, concretely relates to high SOx/NOx control active burnt continuous production system.
Background
The special active coke product for industrial flue gas desulfurization and denitration adopts bituminous coal or anthracite as main raw material, other auxiliary coal for conditioning and adding solid or liquid binder, after fully mixing, the granular material with uniform granularity and regular appearance is prepared by pelleting or strip extrusion molding equipment, and then the granular material is subjected to high-temperature carbonization, steam shallow activation, post oxidation and other procedures to prepare the regular granular product active coke meeting the established technical quality requirements.
With the continuous improvement of the environmental protection requirement, the active coke dry method integrated desulfurization and denitrification technology can be well-mastered in the domestic flue gas treatment industry, the traditional active coke production line has low automation degree, poor field environment and insufficient mechanization level, and a full-automatic integrated and remote centralized control production system cannot be formed, so that the quality of the active coke product in the current market is poor and the production efficiency is low.
SUMMERY OF THE UTILITY MODEL
The utility model aims at overcoming the problems of poor automation degree and product quality and low production efficiency of the existing active coke production line.
For this reason, the utility model provides a continuous production system of active burnt of high SOx/NOx control, include raw materials conveying mechanism, feed mechanism, crocus mechanism, mediate granulation mechanism, carbomorphism mechanism, activation mechanism, finished product packagine machine and construct, raw materials conveying mechanism's ejection of compact department is connected with feed department of feed mechanism, feed mechanism's ejection of compact department is connected with feed department of crocus mechanism, ejection of compact department and the feed department of mediating granulation mechanism of crocus mechanism are connected, the ejection of compact department of mediating granulation mechanism is connected with feed department of carbomorphism mechanism, the ejection of compact department of carbomorphism mechanism is connected with feed department of activation mechanism, the ejection of compact department of activation mechanism is connected with feed department of finished product packagine machine.
Furthermore, the raw material conveying mechanism comprises a bridge type grab bucket machine, a coal receiving bucket, an inertial vibration coal feeder and a toothed roller crusher, a discharge port of the coal receiving bucket is positioned right above a feed port of the inertial vibration coal feeder, a discharge port of the inertial vibration coal feeder is positioned right above a feed port of the toothed roller crusher, and a discharge port of the toothed roller crusher is connected with a feed part of the batching mechanism.
Furthermore, the batching mechanism comprises a raw material silo, a batching and weighing coal feeder, a first belt weighing machine, a bucket elevator and a second belt weighing machine, wherein the raw material silo and the batching and weighing coal feeder are arranged in a one-to-one correspondence manner, a feed inlet of the batching and weighing coal feeder is arranged right opposite to a discharge outlet of the raw material silo, the first belt weighing machine is positioned below the batching and weighing coal feeder and penetrates through the batching and weighing coal feeders, the bucket elevator is arranged at one end part of the first belt weighing machine, an upper hopper of the bucket elevator is positioned under the first belt weighing machine, the second belt weighing machine is positioned at the upper part of the bucket elevator and is arranged in parallel with the first belt weighing machine, and a discharge end of the second belt weighing machine is connected with a feed inlet of the milling mechanism.
Furthermore, the powder grinding mechanism comprises a proportioning bin, a powder grinding weighing coal feeder, a vertical roller type coal mill, a fine powder separator and a buffer powder bin, wherein the proportioning bin, the powder grinding weighing coal feeder and the vertical roller type coal mill are sequentially arranged from top to bottom, a discharge port of the vertical roller type coal mill is connected with a feed port of the fine powder separator, a discharge port of the fine powder separator is positioned right above a feed port of the buffer powder bin, and a discharge port of the buffer powder bin is connected with a feed position of the kneading granulation mechanism.
Further, knead granulation mechanism including weigh feed bin, kneading machine, double screw conveyer and granulator, the discharge gate of the feed bin of weighing is located directly over the feed inlet of kneading machine, the discharge gate of kneading machine is located directly over the feed end of double screw conveyer, the discharge end of double screw conveyer is located directly over the feed inlet of granulator, the discharge gate of granulator is connected with the feeding department of carbomorphism mechanism.
Further, the carbonization mechanism comprises a third belt conveyor, a dryer, a carbonization feeding buffer bin, a carbonization furnace and a carbonization roller cooler, the feeding end of the third belt conveyor is connected with the discharging part of the kneading granulation mechanism, the discharging end of the third belt conveyor is connected with the feeding hole of the dryer, the discharging hole of the dryer is positioned right above the feeding hole of the carbonization feeding buffer bin, the discharging hole of the carbonization feeding buffer bin is positioned right above the feeding hole of the carbonization furnace, the discharging hole of the carbonization furnace is connected with the feeding hole of the carbonization roller cooler, and the discharging hole of the carbonization roller cooler is connected with the feeding part of the activation mechanism.
Further, the activation mechanism comprises a fourth belt conveyor, an activation feeding hopper type elevator, an activation furnace and an activation roller cooler, the feeding end of the fourth belt conveyor is connected with the discharging part of the carbonization mechanism, the discharging end of the fourth belt conveyor is located at the lower part of the activation feeding hopper type elevator and corresponds to the hopper inlet of the activation feeding hopper type elevator, the discharging end of the upper part of the activation feeding hopper type elevator is connected with the feeding hole of the activation furnace, the discharging hole of the activation furnace is connected with the feeding hole of the activation roller cooler, and the discharging hole of the activation roller cooler is connected with the feeding part of the finished product packaging mechanism.
Further, finished product packagine machine constructs including fifth belt conveyor, finished product bucket elevator, finished product feed bin and packagine machine, the feed end of fifth belt conveyor is connected with the ejection of compact department of activation mechanism, the discharge end of fifth belt conveyor is located finished product bucket elevator's lower part, and corresponding with finished product bucket elevator's hopper import, the upper portion discharge end of finished product bucket elevator is connected with the feed inlet of finished product feed bin, the bottom discharge mouth of finished product feed bin is connected with packagine machine's feed inlet.
Compared with the prior art, the beneficial effects of the utility model are that:
the utility model provides a process such as the transport of full automatization integrated control raw materials, batching, crocus, mediate granulation, carbomorphism, activation, finished product packing among this kind of high SOx/NOx control active burnt continuous production system has improved production efficiency greatly, and the active burnt abrasive resistance that obtains of production system production simultaneously can reach 98%, and compressive strength can reach 40Kgf, and the desulfurization value can reach 20mg/g, and the denitration value can reach 65%.
The present invention will be described in further detail with reference to the accompanying drawings.
Drawings
FIG. 1 is a schematic structural diagram of a continuous production system for high desulfurization and denitrification active coke.
Description of reference numerals: 1. a bridge grab machine; 2. a coal receiving hopper; 3. an inertial vibration coal feeder; 4. a toothed roll crusher; 5. a raw material silo; 6. a material-proportioning, weighing and coal-feeding machine; 7. a first belt weigher; 8. a bucket elevator; 9. a second belt weigher; 10. a proportioning bin; 11. a pulverized coal weighing feeder; 12. a vertical roll coal mill; 13. a fine powder separator; 14. caching a powder bin; 15. a weighing bin; 16. a kneader; 17. a double screw conveyor; 18. a granulator; 19. a third belt conveyor; 20. a dryer; 21. a carbonization feeding buffer bin; 22. a carbonization furnace; 23. a charring roller cooler; 24. a fourth belt conveyor; 25. activating the feeding hopper type hoister; 26. an activation furnace; 27. an activation drum cooler; 28. a fifth belt conveyor; 29. a finished product bucket elevator; 30. a finished product bin; 31. a packaging machine.
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 efforts belong to the protection scope of the present invention.
In the description of the present invention, it is to be understood that the terms "center", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like indicate orientations or positional relationships based on those shown in the drawings, and are merely for convenience of description and simplicity of description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, are not to be construed as limiting the present invention.
The terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature; in the description of the present invention, "a plurality" means two or more unless otherwise specified.
As shown in fig. 1, the present embodiment provides a continuous production system of high-desulfurization-denitrification active coke, which includes a raw material conveying mechanism, a batching mechanism, a milling mechanism, a kneading and granulating mechanism, a carbonizing mechanism, an activating mechanism, and a finished product packaging mechanism, wherein a discharge position of the raw material conveying mechanism is connected with a feed position of the batching mechanism, a discharge position of the batching mechanism is connected with a feed position of the milling mechanism, a discharge position of the milling mechanism is connected with a feed position of the kneading and granulating mechanism, a discharge position of the kneading and granulating mechanism is connected with a feed position of the carbonizing mechanism, a discharge position of the carbonizing mechanism is connected with a feed position of the activating mechanism, and a discharge position of the activating mechanism is connected with a feed position of the finished product packaging mechanism. In this embodiment, four raw materials, namely long flame coal, coke powder, coke coal and pitch, for producing active coke are conveyed and crushed by a raw material conveying mechanism in several times, mixed into a mixed material by a batching mechanism according to a designed proportion, then the mixed material is conveyed into a grinding mechanism to be ground into mixed powder, then a certain amount of the mixed powder is accurately weighed by a kneading and granulating mechanism, mixed and kneaded with tar and water according to a designed proportion to form a kneaded material, and the kneaded material is rolled and granulated to form a granulated material; the granulated material is conveyed to a carbonization mechanism for carbonization treatment to form carbonized material; conveying the carbonized material to an activation mechanism for pore-forming activation to form active coke, bagging and packaging the finished active coke by a packaging mechanism after cooling the active coke, and transporting the active coke to a warehouse for storage. The utility model provides a process such as the transport of full automatization integrated control raw materials, batching, crocus, mediate granulation, carbomorphism, activation, finished product packing among this kind of high SOx/NOx control active burnt continuous production system has improved production efficiency greatly, and the active burnt abrasive resistance that obtains of production system production simultaneously can reach 98%, and compressive strength can reach 40Kgf, and the desulfurization value can reach 20mg/g, and the denitration value can reach 65%.
In a detailed embodiment, the raw material conveying mechanism comprises a bridge type grab bucket machine 1, a coal receiving bucket 2, an inertial vibration coal feeder 3 and a toothed roller crusher 4, wherein a discharge port of the coal receiving bucket 2 is positioned right above a feed port of the inertial vibration coal feeder 3, a discharge port of the inertial vibration coal feeder 3 is positioned right above a feed port of the toothed roller crusher 4, and a discharge port of the toothed roller crusher 4 is connected with a feed position of the batching mechanism; the bridge type grab bucket machine 1 sends four raw materials (long flame coal, coke powder, coke coal and coke tar) into a coal receiving bucket 2 in a grading way, the raw materials are sent into a toothed roller crusher 4 by an inertia vibration coal feeder 3 to be crushed, the granularity of the crushed raw materials is below 30mm, and the crushed raw materials respectively enter a batching mechanism.
The material distribution mechanism comprises a plurality of raw material silos 5, a material distribution weighing and coal feeding machine 6, a first belt weighing machine 7, a bucket elevator 8 and a second belt weighing machine 9, the raw material silos 5 and the material distribution weighing and coal feeding machine 6 are arranged in a one-to-one correspondence manner, the number of the raw material silos 5 and the material distribution weighing machines 6 corresponds to the number of the raw materials, and the crushed raw materials enter the corresponding raw material silos 5 respectively for standby; the feed inlet of the batching and weighing coal feeder 6 is arranged over against the discharge outlet of the raw material silo 5, the first belt-type weighing machine 7 is positioned below the batching and weighing coal feeder 6 and penetrates through a plurality of batching and weighing coal feeders 6, the bucket elevator 8 is arranged at the end part of the discharge end of the first belt-type weighing machine 7, the upper hopper of the bucket elevator 8 is positioned under the first belt-type weighing machine 7, the second belt-type weighing machine 9 is positioned at the upper part of the bucket elevator 8 and is arranged in parallel with the first belt-type weighing machine 7, and the discharge end of the second belt-type weighing machine 9 is connected with the feed inlet of the powder grinding mechanism; the material proportioning and weighing feeder 6 conveys the raw materials in the raw material silo 5 to a first belt-type weighing machine 7 according to a certain proportion, simultaneously, the four raw materials are uniformly mixed on the first belt-type weighing machine 7, the mixed materials are conveyed to a hopper of a bucket elevator 8 after being uniformly mixed, then the mixed materials are lifted to a second belt-type weighing machine 9, and the mixed materials are conveyed to a powder grinding mechanism through the second belt-type weighing machine 9.
The powder grinding mechanism comprises a proportioning bin 10, a powder grinding weighing coal feeder 11, a vertical roller type coal mill 12, a fine powder separator 13 and a buffer powder bin 14, wherein the proportioning bin 10, the powder grinding weighing coal feeder 11 and the vertical roller type coal mill 12 are sequentially arranged from top to bottom, a discharge port of the vertical roller type coal mill 12 is connected with a feed port of the fine powder separator 13, a discharge port of the fine powder separator 13 is positioned right above a feed port of the buffer powder bin 14, and a discharge port of the buffer powder bin 14 is connected with a feed position of the kneading granulation mechanism; the mixed materials are conveyed to a batching bin 10 for standby through a second belt type weighing machine 9, the mixed materials are conveyed to a vertical roller type coal mill 12 at a constant speed through a grinding weighing coal feeder 11, the mixed materials are ground into fine powder of 200-300 meshes and then conveyed to a fine powder separator 13 through pneumatic conveying for separation, and finally the mixed powder falls into a cache powder bin 14 for standby.
The kneading and granulating mechanism comprises a weighing bin 15, a kneader 16, a double-screw conveyer 17 and a granulator 18, wherein a discharge port of the weighing bin 15 is positioned right above a feed port of the kneader 16, a discharge port of the kneader 16 is positioned right above a feed end of the double-screw conveyer 17, a discharge end of the double-screw conveyer 17 is positioned right above a feed port of the granulator 18, and a discharge port of the granulator 18 is connected with a feed position of the carbonization mechanism; the mixture powder in the cache powder bin 14 is sent to a weighing bin 15, the weighing bin 15 accurately weighs a certain amount of the mixture powder to a kneader 16, then a certain proportion of tar and water are added, after the mixture powder is kneaded for 5-10 minutes by the kneader 16, the kneaded material is continuously conveyed to a granulator 18 at a constant speed by a double-screw conveyor 17, and then the kneaded material is rolled and granulated by the granulator 18 to form a molded granulated material.
The carbonization mechanism comprises a third belt conveyor 19, a dryer 20, a carbonization feeding buffer bin 21, a carbonization furnace 22 and a carbonization roller cooler 23, wherein the feeding end of the third belt conveyor 19 is connected with the discharging part of the kneading granulation mechanism, the discharging end of the third belt conveyor 19 is connected with the feeding hole of the dryer 20, the discharging hole of the dryer 20 is positioned right above the feeding hole of the carbonization feeding buffer bin 21, the discharging hole of the carbonization feeding buffer bin 21 is positioned right above the feeding hole of the carbonization furnace 22, the discharging hole of the carbonization furnace 22 is connected with the feeding hole of the carbonization roller cooler 23, and the discharging hole of the carbonization roller cooler 23 is connected with the feeding part of the activation mechanism. The granulated material made by the granulator 18 is sent to a dryer 20 by a third belt conveyor 19, partial moisture in the granulated material is removed through steam drying, the hardness of the granulated material is improved, then the granulated material is sent to a carbonization feeding buffer bin 21 for standby use, when the granulated material is carbonized, the granulated material falls into a carbonization furnace 22 from the carbonization feeding buffer bin 21, most of volatile components in the granulated material are removed by heating to about 500-550 ℃, a carbonized material is formed, and the carbonized material is sent to a carbonization roller cooler 23 to be cooled to normal temperature.
Activation mechanism includes fourth belt conveyor 24, activation feeding hopper formula lifting machine 25, activation furnace 26 and activation cylinder cooler 27, fourth belt conveyor 24's feed end is connected with the ejection of compact department of carbomorphism mechanism, fourth belt conveyor 24's discharge end is located the lower part of activation feeding hopper formula lifting machine 25, and is corresponding with the hopper import of activation feeding hopper formula lifting machine 25, the upper portion discharge end of activation feeding hopper formula lifting machine 25 is connected with activation furnace 26's feed inlet, activation furnace 26's discharge gate with activation cylinder cooler 27's feed inlet is connected, activation cylinder cooler 27's discharge gate is connected with finished product packagine machine's feed inlet department. And conveying the cooled carbonized material to a hopper of an activation feeding hopper type lifter 25 through a fourth belt conveyor 24, then lifting and conveying the carbonized material to an activation furnace 26, heating the carbonized material in the activation furnace 26 to 900-950 ℃, introducing water gas to perform pore-forming activation on the carbonized material to form activated coke, and then conveying the activated coke to an activation roller cooler 27 for cooling to form the final finished activated coke.
Finished product packagine machine constructs including fifth belt conveyor 28, finished product bucket elevator 29, finished product feed bin 30 and packagine machine 31, fifth belt conveyor 28's feed end is connected with the ejection of compact department of activation mechanism, fifth belt conveyor 28's discharge end is located finished product bucket elevator 29's lower part, and is corresponding with finished product bucket elevator 29's hopper import, finished product bucket elevator 29's upper portion discharge end is connected with finished product feed bin 30's feed inlet, finished product feed bin 30's bottom discharge gate and packagine machine 31's feed inlet are connected. The finished active coke formed above is conveyed to the hopper of a finished bucket elevator 29 by a fifth belt conveyor 28, then the finished active coke is lifted and conveyed to a finished product bin 30 for standby, and finally the finished active coke in the finished product bin 30 falls to a packaging machine 31 for bagging and packaging, and is transported to a warehouse for storage.
The above illustration is merely an illustration of the present invention, and does not limit the scope of the present invention, and all designs identical or similar to the present invention are within the scope of the present invention.
Claims (8)
1. The utility model provides a continuous production system of high SOx/NOx control active coke which characterized in that: the material mixing and packaging device comprises a raw material conveying mechanism, a batching mechanism, a powder grinding mechanism, a kneading and granulating mechanism, a carbonizing mechanism, an activating mechanism and a finished product packaging mechanism, wherein the discharging position of the raw material conveying mechanism is connected with the feeding position of the batching mechanism, the discharging position of the batching mechanism is connected with the feeding position of the powder grinding mechanism, the discharging position of the powder grinding mechanism is connected with the feeding position of the kneading and granulating mechanism, the discharging position of the kneading and granulating mechanism is connected with the feeding position of the carbonizing mechanism, the discharging position of the carbonizing mechanism is connected with the feeding position of the activating mechanism, and the discharging position of the activating mechanism is connected with the feeding position of the finished product packaging mechanism.
2. The continuous production system of high desulfurization and denitrification active coke as claimed in claim 1, wherein: the raw material conveying mechanism comprises a bridge type grab bucket machine, a coal receiving bucket, an inertial vibration coal feeder and a toothed roller crusher, wherein a discharge port of the coal receiving bucket is positioned right above a feed port of the inertial vibration coal feeder, a discharge port of the inertial vibration coal feeder is positioned right above a feed port of the toothed roller crusher, and a discharge port of the toothed roller crusher is connected with a feed part of the batching mechanism.
3. The continuous production system of high desulfurization and denitrification active coke as claimed in claim 1, wherein: the batching mechanism comprises a raw material silo, a batching weighing coal feeder, a first belt-type weighing machine, a bucket elevator and a second belt-type weighing machine, wherein the raw material silo and the batching weighing coal feeder are arranged in a one-to-one correspondence manner, a feed inlet of the batching weighing coal feeder is arranged right opposite to a discharge outlet of the raw material silo, the first belt-type weighing machine is positioned below the batching weighing coal feeder and penetrates through a plurality of batching weighing coal feeders, the bucket elevator is arranged at one end part of the first belt-type weighing machine, a feed hopper of the bucket elevator is positioned under the first belt-type weighing machine, the second belt-type weighing machine is positioned at the upper part of the bucket elevator and is arranged in parallel with the first belt-type weighing machine, and a discharge end of the second belt-type weighing machine is connected with a feed inlet of the milling mechanism.
4. The continuous production system of high desulfurization and denitrification active coke as claimed in claim 1, wherein: the powder grinding mechanism comprises a proportioning bin, a powder grinding weighing coal feeder, a vertical roller type coal mill, a fine powder separator and a buffer powder bin, the proportioning bin, the powder grinding weighing coal feeder and the vertical roller type coal mill are sequentially arranged from top to bottom, a discharge port of the vertical roller type coal mill is connected with a feed port of the fine powder separator, a discharge port of the fine powder separator is located right above a feed port of the buffer powder bin, and a discharge port of the buffer powder bin is connected with a feed part of the kneading granulation mechanism.
5. The continuous production system of high desulfurization and denitrification active coke as claimed in claim 1, wherein: kneading granulation mechanism includes the feed bin of weighing, kneading machine, double screw conveyer and granulator, the discharge gate of the feed bin of weighing is located directly over the feed inlet of kneading machine, the discharge gate of kneading machine is located directly over the feed end of double screw conveyer, the discharge end of double screw conveyer is located directly over the feed inlet of granulator, the discharge gate of granulator is connected with the feeding department of carbomorphism mechanism.
6. The continuous production system of high desulfurization and denitrification active coke as claimed in claim 1, wherein: the carbonization mechanism comprises a third belt conveyor, a dryer, a carbonization feeding buffer bin, a carbonization furnace and a carbonization roller cooler, wherein the feeding end of the third belt conveyor is connected with the discharging part of the kneading granulation mechanism, the discharging end of the third belt conveyor is connected with the feeding hole of the dryer, the discharging hole of the dryer is positioned right above the feeding hole of the carbonization feeding buffer bin, the discharging hole of the carbonization feeding buffer bin is positioned right above the feeding hole of the carbonization furnace, the discharging hole of the carbonization furnace is connected with the feeding hole of the carbonization roller cooler, and the discharging hole of the carbonization roller cooler is connected with the feeding part of the activation mechanism.
7. The continuous production system of high desulfurization and denitrification active coke as claimed in claim 1, wherein: the activation mechanism comprises a fourth belt conveyor, an activation feeding hopper type elevator, an activation furnace and an activation roller cooler, the feeding end of the fourth belt conveyor is connected with the discharging part of the carbonization mechanism, the discharging end of the fourth belt conveyor is positioned at the lower part of the activation feeding hopper type elevator and corresponds to the hopper inlet of the activation feeding hopper type elevator, the upper discharging end of the activation feeding hopper type elevator is connected with the feeding hole of the activation furnace, the discharging hole of the activation furnace is connected with the feeding hole of the activation roller cooler, and the discharging hole of the activation roller cooler is connected with the feeding part of the finished product packaging mechanism.
8. The continuous production system of high desulfurization and denitrification active coke as claimed in claim 1, wherein: finished product packagine machine constructs including fifth belt conveyor, finished product bucket elevator, finished product feed bin and packagine machine, the feed end of fifth belt conveyor is connected with the ejection of compact department of activation mechanism, the discharge end of fifth belt conveyor is located finished product bucket elevator's lower part, and corresponding with finished product bucket elevator's hopper import, finished product bucket elevator's upper portion discharge end is connected with the feed inlet of finished product feed bin, the bottom discharge mouth of finished product feed bin is connected with packagine machine's feed inlet.
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| CN111689498A (en) * | 2020-06-05 | 2020-09-22 | 中冶南方都市环保工程技术股份有限公司 | Continuous production system and method for high-desulfurization and denitrification active coke |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111689498A (en) * | 2020-06-05 | 2020-09-22 | 中冶南方都市环保工程技术股份有限公司 | Continuous production system and method for high-desulfurization and denitrification active coke |
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