Device for controlling uniform discharging of activated carbon in activated coke system
By designing a combination device of polygonal feeder and ultrasonic speed detector in the adsorption tower of the activated coke system, uniform feeding of activated carbon is achieved, and the problems of ignition and flue gas exceeding standards caused by uneven feeding of activated carbon are solved, thereby increasing pollution Material processing efficiency.
Patent Information
- Application Number
- CN202421120804.0
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-05-22
- Publication Date
- 2024-12-20
- Estimated Expiration
- 2034-05-22
AI Technical Summary
In the adsorption tower of the activated coke system, the activated carbon is unevenly discharged, resulting in a fast drop in the middle area and a slow drop in the side wall activated carbon, which may cause ignition and reduce the pollutant treatment capacity, and there is a risk of sintered flue gas exceeding the standard.
A device including a feeding silo shell, a small triangular prismatic feeder on the left, a small triangular prismatic feeder on the right and a large triangular prismatic feeder on the ultrasonic speed detector is designed to monitor the feeding port speed and drive the The machine drives the baffle to adjust the angle to achieve a uniform drop in the activated carbon at the four cutting ports.
It effectively solves the problem of uneven cutting of activated carbon, reduces the risk of fire and sintered flue gas exceeding the standard, reduces the activated carbon evenly, and improves the pollutant treatment capacity.
Smart Images

Figure CN222204105U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of metallurgical sintering fume treatment, in particular to a device for controlling uniform feeding of activated carbon in an activated coke system. Background Art
[0002] Activated coke desulfurization and denitrification technology can simultaneously treat multiple pollutants, that is, remove SO2, NOx, dioxins and other pollutants at the same time. This technology is widely used in the steel industry, especially in sintering flue gas desulfurization and denitrification. This technology uses the non-selective adsorption and catalytic effects of activated coke to absorb and remove multiple pollutants, thereby achieving the purpose of purifying flue gas. Activated carbon for desulfurization and denitrification for sintering is a cylindrical activated carbon made of coal. It uses high-quality anthracite as raw material, adds a binder to extrude and then undergoes carbonization, cooling, activation, washing and other processes. It has a developed void structure, good adsorption performance, high mechanical strength, fast absorption speed, high capacity, large specific surface area, strong regeneration and other characteristics. Activated carbon is the main adsorption catalyst. Before the activated coke desulfurization and denitrification system works normally, a large amount of activated carbon needs to be added to the adsorption tower. The adsorption tower is filled with activated carbon to start normally according to the program. After filling with activated carbon, the temperature in the adsorption tower is controlled not to exceed 130°C, and the activated carbon adsorption catalysis works normally. Activated carbon moves from the top to the bottom of the tower with gravity. Ideally, activated carbon at different positions falls evenly until it is removed from the adsorption tower. However, in actual operation, the activated carbon in the middle falls quickly, while the activated carbon in contact with the side wall of the adsorption tower falls slowly, which results in a high heat storage temperature of the activated carbon on the side wall, which may cause fire in serious cases. In addition, the activated carbon in the middle area falls quickly, while the activated carbon on the side wall falls slowly or does not move, which reduces the processing capacity of the activated coke system to remove multiple pollutants, and there is a risk of excessive pollutants in the sintering flue gas after treatment.
[0003] Patent No. CN201721325423.6 discloses a uniform activated carbon feeding device. This utility model mainly aims at the problem of uneven activated carbon feeding after the activated carbon discharged from the adsorption tower enters the vibrating screen to screen out the powder, and a round roller feeder is added to make the activated carbon feeding uniform. This method is suitable for controlling the uniform feeding of activated carbon in an open space, while the activated coke system adsorption tower is filled with activated carbon, which is a confined space, so this method is not suitable for controlling the feeding speed of activated carbon in the adsorption tower. Utility Model Content
[0004] The utility model provides a device for controlling the uniform feeding of activated carbon in an activated coke system, so as to solve the problems raised in the above background technology.
[0005] In order to solve the above technical problems, the technical solution adopted by the utility model is:
[0006] A device for controlling the uniform feeding of activated carbon in an activated coke system comprises a feeding bin shell, the lower part of which is a V-shaped structure, and the lower inner cavity of the feeding bin shell is provided with a left small triangular prism distributor, a right small triangular prism distributor and a large triangular prism distributor, the large triangular prism distributor is located in the middle of the feeding bin shell, the left small triangular prism distributor and the right small triangular prism distributor are symmetrically arranged with the large triangular prism distributor as the symmetry axis, the left small triangular prism distributor, the large triangular prism distributor and the right small triangular prism distributor divide the lower inner cavity of the feeding bin shell from left to right in sequence It is divided into four discharge ports, and a left-side rotating shaft is provided at the bottom center line of the left small triangular prism-shaped divider, and a left-side baffle is fixedly connected to the left-side rotating shaft, and a right-side rotating shaft is provided at the bottom center line of the right small triangular prism-shaped divider, and a right-side baffle is fixedly connected to the right-side rotating shaft, a long-axis discharger is connected to the bottom of the discharge bin shell, and the inner cavity of the discharge bin shell is provided with an ultrasonic velocimeter for monitoring the four discharge ports, and two driving machines are fixedly installed on the outer side of the discharge bin shell, and the output ends of the two driving machines are respectively connected to the left-side rotating shaft and the left-side baffle.
[0007] Preferably, the sizes of the left small triangular prism-shaped distributor and the right small triangular prism-shaped distributor are respectively proportionally reduced sizes of the large triangular prism-shaped distributor.
[0008] Preferably, the cross-sections of the left small triangular prism-shaped distributor, the right small triangular prism-shaped distributor and the large triangular prism-shaped distributor are all equilateral triangles.
[0009] Preferably, the cross-sectional side lengths of the left small triangular prism-shaped distributor and the right small triangular prism-shaped distributor are equal.
[0010] Preferably, the opening and closing angle between the bottom edge of the left small triangular prism-shaped distributor and the left baffle is 30° to 150°.
[0011] Preferably, the opening and closing angle between the bottom edge of the right small triangular prism-shaped distributor and the right baffle is 30°~150°.
[0012] Preferably, the lengths of the left baffle and the right baffle are respectively the length of the side of the cross section of the left small triangular prism distributor. .
[0013] Preferably, the sizes of the left small triangular prism-shaped divider and the right small triangular prism-shaped divider are respectively 1 / 4 of the size of the large triangular prism-shaped divider.
[0014] Preferably, the cross-sectional vertices of the left small triangular prism-shaped distributor, the right small triangular prism-shaped distributor and the large triangular prism-shaped distributor are all on the same horizontal plane.
[0015] By adopting the above technical solution, the beneficial effects achieved by the utility model are as follows:
[0016] In the utility model, the four discharge ports are monitored by an ultrasonic velocimeter, so that the driving machine can drive the left rotating shaft and the right rotating shaft to rotate according to the monitoring data. After the left baffle and the right baffle are adjusted in angle, the activated carbon at the four discharge ports can be uniformly lowered at a speed of 1m / min, effectively solving the problem of uneven discharge of activated carbon, reducing the risk of activated carbon ignition and excessive discharge of sintering flue gas. The utility model is simple, practical and effective. BRIEF DESCRIPTION OF THE DRAWINGS
[0017] Figure 1 This is a schematic diagram of the front cross-sectional structure of the lower silo shell of the utility model;
[0018] Figure 2 for Figure 1 Schematic diagram of the structure of the AA section;
[0019] Figure 3 It is a schematic diagram of the top view of the lower silo shell structure of the utility model.
[0020] In the figure: 1. lower hopper shell; 2. left small triangular prism-shaped distributor; 3. left rotating shaft; 4. left baffle; 5. long-axis discharger; 6. right small triangular prism-shaped distributor; 7. right rotating shaft; 8. right baffle; 9. large triangular prism-shaped distributor; 10. ultrasonic tachometer; 11. driving machine. DETAILED DESCRIPTION
[0021] In order to more clearly understand the above-mentioned purpose, features and advantages of the utility model, the utility model is further described below in conjunction with the accompanying drawings and embodiments. It should be noted that the embodiments of the present application and the features in the embodiments can be combined with each other without conflict.
[0022] In the following description, many specific details are set forth to facilitate a full understanding of the present invention. However, the present invention may also be implemented in other ways than those described herein. Therefore, the present invention is not limited to the specific embodiments of the following disclosure.
[0023] like Figure 1-3As shown, the utility model provides a device for controlling the uniform feeding of activated carbon in an activated coke system, comprising a feeding bin shell 1, the lower part of the feeding bin shell 1 is a V-shaped structure, and the lower inner cavity of the feeding bin shell 1 is provided with a left small triangular prism-shaped distributor 2, a right small triangular prism-shaped distributor 6 and a large triangular prism-shaped distributor 9, the large triangular prism-shaped distributor 9 is located in the middle of the feeding bin shell 1, the left small triangular prism-shaped distributor 2 and the right small triangular prism-shaped distributor 6 are symmetrically arranged with the large triangular prism-shaped distributor 9 as the symmetry axis, and the left small triangular prism-shaped distributor 2, the large triangular prism-shaped distributor 9 and the right small triangular prism-shaped distributor 6 divide the lower inner cavity of the feeding bin shell 1 from From left to right, it is divided into four discharge ports in sequence, and a left rotating shaft 3 is arranged at the bottom center line of the left small triangular prism divider 2, and a left baffle 4 is fixedly connected to the left rotating shaft 3, and a right rotating shaft 7 is arranged at the bottom center line of the right small triangular prism divider 6, and a right baffle 8 is fixedly connected to the right rotating shaft 7, a long-axis discharger 5 is connected to the bottom of the discharge bin shell 1, and an ultrasonic velocimeter 10 for monitoring the four discharge ports is provided in the inner cavity of the discharge bin shell 1, and two driving machines 11 are fixedly installed on the outer side of the discharge bin shell 1, and the output ends of the two driving machines 11 are respectively connected to the left rotating shaft 3 and the left baffle 4.
[0024] Specifically, the device also includes an external control device, and the control device is used to receive the monitoring data of the ultrasonic velocimeter 10 in real time, and prompt the driving machine 11 to drive the left rotating shaft 3 or the right rotating shaft 7 to rotate according to the monitoring data, which is conducive to the unification of the activated carbon discharge speeds of the four discharge ports, reducing the risks of activated carbon ignition and excessive discharge of sintering flue gas, and the ultrasonic velocimeter 10 is a conventional device currently on the market, and has not been improved. Its principle is mainly based on the propagation speed of ultrasonic waves and the reception time difference, and the device is already well known to technical personnel in various industries, and is installed and applied according to the actual installation environment during installation and use. This article does not elaborate on this, and this article only aims to protect the physical structure. For the existing control devices in the outside world, their receiving and sending operations are well known to technical personnel in this field, and can be independently completed according to computer program programming. Therefore, this article does not elaborate on this.
[0025] The sizes of the left small triangular prismatic divider 2 and the right small triangular prismatic divider 6 are respectively proportionally reduced sizes of the large triangular prismatic divider 9, the cross-sections of the left small triangular prismatic divider 2, the right small triangular prismatic divider 6 and the large triangular prismatic divider 9 are all equilateral triangles, the cross-sectional side lengths of the left small triangular prismatic divider 2 and the right small triangular prismatic divider 6 are equal, and the sizes of the left small triangular prismatic divider 2 and the right small triangular prismatic divider 6 are respectively 1 / 4 of the size of the large triangular prismatic divider 9.
[0026] The opening and closing angle value of the bottom edge of the left small triangular prism divider 2 and the left baffle 4 is 30°~150°, and the opening and closing angle value of the bottom edge of the right small triangular prism divider 6 and the right baffle 8 is 30°~150°.
[0027] According to the above example: when the opening and closing angle value of the bottom edge of the left baffle plate 4 and the left small triangular prism-shaped divider 2 is 120°, the opening and closing angle of the bottom edge of the right baffle plate 8 and the right small triangular prism-shaped divider 6 is 60°, and at this time, the left baffle plate 4 and the right baffle plate 8 are symmetrically arranged with the large triangular prism-shaped divider 9 as the central axis, and when the opening and closing angle values of the left baffle plate 4 and the right baffle plate 8 are adjusted, the total opening and closing angle of the two is 180°.
[0028] The lengths of the left baffle plate 4 and the right baffle plate 8 are respectively the length of the side of the cross section of the left small triangular prism distributor 2 .
[0029] The cross-sectional vertices of the left small triangular prism divider 2, the right small triangular prism divider 6 and the large triangular prism divider 9 are all on the same horizontal plane, and the inner width values of the four discharge openings separated from left to right are equal. The four discharge openings separated from left to right are discharge opening a, discharge opening b, discharge opening c and discharge opening d.
[0030] Before the installation of this device, the discharge speed of the activated carbon in the adsorption tower is controlled by the rotation frequency of the long-axis discharger 5, and its discharge speed is much lower than the discharge speed of the activated carbon in the adsorption tower. The activated carbon in the middle of the lower bin of the adsorption tower moves downward at a speed of 2m / min, while the activated carbon near the side wall moves downward at a speed of 0.5m / min, and the discharge is uneven.
[0031] like Figure 1-Figure 3 As shown, the use process of the utility model is as follows: since the large triangular prism divider 9 is located in the middle of the discharge bin shell 1, the two small triangular prism dividers on the left and right are placed on both sides of the large triangular prism divider 9, so that the discharge port is evenly divided into four equal parts, and the discharge speeds of the four discharge ports are monitored by the ultrasonic velocimeter 10, and when the discharge speeds of discharge ports a and d are 0.8m / min, and the discharge speeds of discharge ports b and c are 1.5m / min, the left rotating shaft 3 and the right rotating shaft 7 are driven by the driving machine 11 to achieve the adjustment angle of the left baffle 4 to 120° and the adjustment angle of the right baffle 8 to 60°. It is then known through actual use that at this time, the activated carbon at the four discharge ports all descends evenly at a speed of 1m / min, which effectively solves the problem of uneven discharge of activated carbon and reduces the risk of activated carbon ignition and excessive discharge of sintering flue gas.
[0032] In the present utility model, the term "plurality" refers to two or more than two, unless otherwise clearly defined. The term "and / or" used in this article includes any and all combinations of one or more related listed items. The terms "install", "connect", "connect", "fix" and the like should be understood in a broad sense. For example, "connection" can be a fixed connection, a detachable connection, or an integral connection; "connection" can be a direct connection or an indirect connection through an intermediate medium. For those of ordinary skill in the art, the specific meanings of the above terms in the present utility model can be understood according to the specific circumstances.
[0033] It should be noted that when an element is referred to as being "assembled on", "installed on", "fixed on" or "disposed on" another element, it may be directly on the other element or there may be a central element. When an element is considered to be "connected to" another element, it may be directly connected to the other element or there may be a central element at the same time. The terms "vertical", "horizontal", "upper", "lower", "left", "right" and similar expressions used herein are for illustrative purposes only and do not represent the only implementation method.
[0034] In the description of this specification, the description of the terms "one embodiment", "some embodiments", "specific embodiments", etc. means that the specific features, structures, materials or characteristics described in conjunction with the embodiment or example are included in at least one embodiment or example of the utility model. In this specification, the schematic representation of the above terms does not necessarily refer to the same embodiment or example. Moreover, the specific features, structures, materials or characteristics described can be combined in any one or more embodiments or examples in a suitable manner.
[0035] Although the embodiments of the present invention have been shown and described, those skilled in the art will appreciate that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the claims and their equivalents.
Claims
1. A device for controlling the uniform feeding of activated carbon in an activated coke system, characterized in that: The invention comprises a lower material bin shell (1), the lower part of which is a V-shaped structure, and the lower inner cavity of the lower material bin shell (1) is provided with a left small triangular prism-shaped distributor (2), a right small triangular prism-shaped distributor (6) and a large triangular prism-shaped distributor (9), the large triangular prism-shaped distributor (9) being located in the middle of the lower material bin shell (1), the left small triangular prism-shaped distributor (2) and the right small triangular prism-shaped distributor (6) being symmetrically arranged with the large triangular prism-shaped distributor (9) as a symmetry axis, the left small triangular prism-shaped distributor (2), the large triangular prism-shaped distributor (9) and the right small triangular prism-shaped distributor (6) dividing the lower inner cavity of the lower material bin shell (1) into four material discharge openings from left to right in sequence, and the left small triangular prism-shaped distributor (2) and the right small triangular prism-shaped distributor (6) are arranged in a symmetrical manner with the large triangular prism-shaped distributor (9) as a symmetry axis. A left rotating shaft (3) is arranged at the bottom center line of the prism-shaped distributor (2), and a left baffle (4) is fixedly connected to the left rotating shaft (3); a right rotating shaft (7) is arranged at the bottom center line of the right small triangular prism-shaped distributor (6), and a right baffle (8) is fixedly connected to the right rotating shaft (7); a long-axis discharger (5) is connected to the bottom of the lower bin shell (1); an ultrasonic velocimeter (10) for monitoring four discharge ports is arranged in the inner cavity of the lower bin shell (1); and two driving machines (11) are fixedly installed on the outer side of the lower bin shell (1); the output ends of the two driving machines (11) are respectively connected to the left rotating shaft (3) and the left baffle (4).
2. The device for controlling uniform discharge of activated carbon in an activated coke system according to claim 1, characterized in that: The sizes of the left small triangular prism-shaped distributor (2) and the right small triangular prism-shaped distributor (6) are respectively proportionally reduced sizes of the large triangular prism-shaped distributor (9).
3. The device for controlling uniform discharge of activated carbon in an activated coke system according to claim 2, characterized in that: The cross-sections of the left small triangular prism-shaped distributor (2), the right small triangular prism-shaped distributor (6) and the large triangular prism-shaped distributor (9) are all equilateral triangles.
4. The device for controlling uniform discharge of activated carbon in an activated coke system according to claim 3, characterized in that: The cross-sectional side lengths of the left small triangular prism-shaped distributor (2) and the right small triangular prism-shaped distributor (6) are equal.
5. The device for controlling uniform discharge of activated carbon in an activated coke system according to claim 1, characterized in that: The opening and closing angle between the bottom edge of the left small triangular prism-shaped distributor (2) and the left baffle plate (4) is 30° to 150°.
6. The device for controlling uniform discharge of activated carbon in an activated coke system according to claim 1, characterized in that: The opening and closing angle between the bottom edge of the right small triangular prism-shaped distributor (6) and the right baffle (8) is 30° to 150°.
7. The device for controlling uniform discharge of activated carbon in an activated coke system according to claim 4, characterized in that: The lengths of the left baffle plate (4) and the right baffle plate (8) are respectively the length of the side of the cross section of the left small triangular prism-shaped distributor (2). .
8. The device for controlling uniform discharge of activated carbon in an activated coke system according to claim 4, characterized in that: The sizes of the left small triangular prism-shaped distributor (2) and the right small triangular prism-shaped distributor (6) are respectively 1 / 4 of the size of the large triangular prism-shaped distributor (9).
9. The device for controlling uniform discharge of activated carbon in an activated coke system according to claim 1, characterized in that: The cross-sectional vertices of the left small triangular prism-shaped distributor (2), the right small triangular prism-shaped distributor (6) and the large triangular prism-shaped distributor (9) are all located on the same horizontal plane, and the inner widths of the four feed openings sequentially separated from left to right are all equal.
