CN212167756U

CN212167756U - Medium-speed grinding dynamic pulverized coal separator

Info

Publication number: CN212167756U
Application number: CN201922411729.9U
Authority: CN
Inventors: 曹凤英; 吴汉周; 张�杰
Original assignee: Nanjing Chuqing Electronic Technology Co Ltd
Current assignee: Sinoma Nanjing Mining Research Institute Co ltd
Priority date: 2019-12-28
Filing date: 2019-12-28
Publication date: 2020-12-18
Anticipated expiration: 2029-12-28

Abstract

The utility model discloses a medium-speed grinding dynamic pulverized coal separator in the technical field of pulverized coal separation, which comprises a separation shell, a dynamic separation barrel and a coal dropping pipe, the dynamic separation cylinder is arranged at the top of the inner cavity of the separation shell, the coal dropping pipe penetrates through the center of the dynamic separation cylinder, the bottom and the top of the separation shell are respectively provided with a coal inlet and a coal outlet, the inner cavity of the separation shell is provided with separation channels at two sides of the movable separation cylinder, the movable impeller sleeved outside the coal dropping pipe is arranged inside the movable separation barrel, the top of the separation shell is provided with a reduction gearbox and a driving motor for driving the reduction gearbox, the periphery of movable impeller is equipped with the cylinder, all be equipped with the baffle on the inner chamber of separation passageway and the outer wall of coal breakage pipe, it is less to guarantee to enter into the heavy buggy of waiting to burn of buggy storehouse and contain the gas powder, has improvement buggy rate of recovery, buggy thickness separation even.

Description

Medium-speed grinding dynamic pulverized coal separator

Technical Field

The utility model relates to a buggy separation technical field specifically is a dynamic buggy separator is ground to intermediate speed.

Background

At present, coal quality of thermal power plants in China changes frequently, a plurality of power plants are subjected to coal blending and combustion, and a coal mill has to have the capability of adjusting the fineness of coal powder in time in order to meet the requirement of peak regulation of a unit; and with the increasing requirements of countries in the world on energy conservation and environmental protection of power plants, a plurality of units use low NOx emission technology, in order to reduce the discharge amount of NOx and fly ash without increasing the operation cost, the fineness and uniformity of the pulverized coal must meet higher requirements,

the coal powder separator is one of the most important components in a coal pulverizing system of a coal mill, and the advantages and disadvantages of the structure and the performance of the coal powder separator have great influence on the service life, the power consumption, the boiler combustion efficiency and the like of the coal mill. A reasonably designed coal dust separator can timely send qualified coal dust to a boiler on one hand, and screens out coal dust with unqualified fineness to return the coal dust to a coal mill for continuous grinding on the other hand.

The medium-speed pulverized coal separators used in various industries at present are basically of baffle type, static separation technology is adopted, separation effect and fineness of pulverized coal after separation can only be realized by the change of the corner of a baffle and ventilation quantity, the pulverized coal is mainly separated by centrifugal force generated by rotation, when the centrifugal force is too large, coarse pulverized coal is easily discharged from a powder outlet, and when the centrifugal force is too small, the pulverized coal is easily separated incompletely, the separation efficiency is low, the pulverized coal fineness adjustment difficulty is large, and the separated pulverized coal gas easily causes environmental pollution.

Based on this, the utility model designs an intermediate speed grinds developments buggy separator to solve above-mentioned problem.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide a guarantee to enter into the buggy storehouse and heavily treat the buggy that burns and contain the gas powder less, have the even intermediate speed of improvement buggy rate of recovery, buggy thickness separation and grind dynamic buggy separator to solve the problem of proposing in the above-mentioned background art.

In order to achieve the above object, the utility model provides a following technical scheme: a medium-speed grinding dynamic pulverized coal separator comprises a separation shell, a dynamic separation barrel and a coal dropping pipe, wherein the dynamic separation barrel is arranged at the top of an inner cavity of the separation shell, the coal dropping pipe penetrates through the center of the dynamic separation barrel, a coal inlet and a coal outlet are respectively arranged at the bottom and the top of the separation shell, separation channels are arranged at two sides of the inner cavity of the separation shell, which are positioned on the dynamic separation barrel, a movable impeller sleeved outside the coal dropping pipe is arranged inside the dynamic separation barrel, a reduction gearbox and a driving motor used for driving the reduction gearbox are arranged at the top of the separation shell, the output end of the reduction gearbox is connected with a rotating shaft, the rotating shaft penetrates through the inside of the separation shell and is fixedly connected with the bottom of the movable impeller, the top of the movable impeller is connected to the top of the inner cavity of the separation shell in a sliding manner through a connecting ring, the movable impeller rotates around the driving motor under the driving of, the inner cavity of the separation channel and the outer wall of the coal dropping pipe are both provided with a baffle plate; the separation cylinder comprises a lower blade connecting plate fixed at the top of the inner cavity of the separation shell and an upper blade connecting plate fixed at the top of the movable separation cylinder, the top of the coal outlet is connected with the input end of a negative pressure machine through an air suction pipe, and the output end of the negative pressure machine is connected with the spray tower.

Preferably, the movable impeller is a conical rotor movable impeller, and the vane material is a low-alloy wear-resistant material.

Preferably, a plurality of stationary blades are uniformly distributed in the circumferential direction between the lower blade connecting plate and the upper blade connecting plate.

Preferably, the plurality of stationary blades are provided with the same stationary blade included angle in the radial direction of the circle where the stationary blades are located, and the stationary blade included angle is 45 °.

Preferably, the drive motor is an MB series stepless speed change speed regulation motor.

Preferably, an air seal piece is further installed between the reduction gearbox and the coal outlet.

Preferably, the baffle that slopes to set up on the separation shells inner wall sets up with the baffle looks interval that slopes to set up on the coal breakage pipe outer wall.

Preferably, the baffle is a stainless steel metal filter plate with dense hollows.

Preferably, the bottom of the separation shell is also provided with a coal return port.

Preferably, a coal filtering net is further installed at the connection position of the air suction pipe and the coal outlet.

Compared with the prior art, the beneficial effects of the utility model are that: the utility model discloses a cylinder and movable separation barrel realize the dynamic separation to the buggy to carry out the first separation through the baffle, the buggy after twice separation is carrying out the gas powder and is handling, realize separating once more to the buggy, it is less to guarantee to enter into the buggy storehouse and heavily treat the buggy that burns and contain the gas powder, has the advantage that improves the buggy rate of recovery, buggy thickness separation is even, is favorable to solving the problem that separation efficiency is low, the degree of difficulty is big is adjusted to the buggy fineness.

Drawings

In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings used in the description of the embodiments will be briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained according to these drawings without creative efforts.

FIG. 1 is a schematic structural view of the present invention;

fig. 2 is a schematic view of the structure of the separation cylinder of the present invention.

In the drawings, the components represented by the respective reference numerals are listed below:

1-separation shell, 2-dynamic separation cylinder, 3-coal dropping pipe, 4-coal inlet, 5-coal outlet, 6-separation channel, 7-movable impeller, 8-separation cylinder, 8-1-lower blade connecting plate, 8-2-upper blade connecting plate, 8-3-stationary blade, 9-driving motor, 10-reduction box, 11-air seal piece, 12-baffle, 13-coal return port, 14-rotating shaft, 15-air suction pipe, 16-negative pressure machine and 17-coal filtering net.

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 of the present invention, all other embodiments obtained by a person of ordinary skill in the art without creative efforts belong to the protection scope of the present invention.

Referring to fig. 1-2, the present invention provides a technical solution: a medium-speed grinding dynamic pulverized coal separator comprises a separation shell 1, a dynamic separation barrel 2 and a coal dropping pipe 3, wherein the dynamic separation barrel 2 is installed at the top of an inner cavity of the separation shell 1, the coal dropping pipe 3 penetrates through the center of the dynamic separation barrel 2, a coal inlet 4 and a coal outlet 5 are respectively arranged at the bottom and the top of the separation shell 1, a separation channel 6 is arranged at two sides of the dynamic separation barrel 2 in the inner cavity of the separation shell 1, a movable impeller 7 sleeved outside the coal dropping pipe 3 is arranged inside the dynamic separation barrel 2, a reduction gearbox 10 and a driving motor 9 for driving the reduction gearbox 10 are installed at the top of the separation shell 1, the output end of the reduction gearbox 10 is connected with a rotating shaft 14, the rotating shaft 14 penetrates through the inside of the separation shell 1 and is fixedly connected with the bottom of the movable impeller 7, the top of the movable impeller 7 is slidably connected with the top of the inner cavity of the separation shell 1 through a connecting, driven by a reduction gearbox 10, the movable impeller 7 rotates around a driving motor 9, a separation barrel 8 is arranged on the periphery of the movable impeller 7, and baffles 12 are arranged on the inner cavity of the separation channel 6 and the outer wall of the coal dropping pipe 3.

Wherein, the movable impeller 7 adopts a conical rotor movable impeller, the best separation effect is ensured according to the separation space of the separator, the blade material adopts low-alloy wear-resistant material 16Mn, the erosion and abrasion of the pulverized coal to the movable impeller 7 are effectively prevented, the separating cylinder 8 comprises a lower blade connecting plate 8-1 fixed at the top of the inner cavity of the separating shell 1 and an upper blade connecting plate 8-2 fixed at the top of the movable separating cylinder 2, a plurality of stationary blades 8-3 are circumferentially and uniformly distributed between the lower blade connecting plate 8-1 and the upper blade connecting plate 8-2, the plurality of stationary blades 8-3 and the radial direction of the circle where the stationary blades are positioned are provided with the same stationary blade included angle which is 45 degrees, the tangential force borne by the pulverized coal particles is directly influenced by the stationary blade included angle, the pulverized coal fineness is reduced along with the increase of the stationary blade included angle, and the separation efficiency is increased, the included angle of the stator blades of 45 degrees is considered to be the best angle comprehensively, the driving motor 9 adopts an MB series stepless speed change speed regulation motor, the structure is simple, the regulation is more convenient and accurate, an airtight sealing piece 11 is further installed between the reduction gearbox 10 and the coal outlet 5, a better sealing effect is achieved, the pulverized coal is effectively prevented from floating to the outside, the baffle 12 obliquely arranged on the inner wall of the separation shell 1 and the baffle 12 obliquely arranged on the outer wall of the coal dropping pipe 3 are arranged at intervals, the baffle 12 is a stainless steel metal filter plate with dense hollowed-out holes and can separate the pulverized coal, large-particle pulverized coal passing through the baffle 12 is blocked, the pulverized coal not blocked continuously enters the separation channel 6 and the movable separation cylinder 2 to be separated again, the coal return port 13 is further installed at the bottom of the separation shell 1, and the large particles separated twice can be conveniently returned to the coal mill through the coal return port 13 to be re-milled again, the top of the coal outlet 5 is connected with the input end of a negative pressure machine 16 through an air suction pipe 15, the output end of the negative pressure machine 16 is connected with a spray tower, and a coal filtering net 17 is further installed at the joint of the air suction pipe 15 and the coal outlet 5.

One specific application of this embodiment is: the gas-powder mixture ground by the coal grinding device enters the separation shell 1 through the coal inlet 4, the coal powder firstly passes through the baffle 12 to block and separate larger particle coal powder, the larger particle coal powder flows back to the coal grinding machine to be ground again, the unblocked coal powder continuously enters the separation channel 6 and the movable separation barrel 2, the static blades 8-3 can generate secondary separation in the process under the action of gravity, when the coal powder airflow enters the movable separation barrel 2, the centripetal force applied to the coal powder particles is smaller than the centrifugal force under the action of the movable impeller 7, the coal powder particles can escape from the static blade included angle of the static blades 8-3 to the separation channel 6, and when larger particle coal powder collides with the movable impeller, the coal powder particles also return to the separation channel 6 due to larger inertia force and slide to the inclined baffle 12 to the coal return opening 13, the large-particle coal dust separated twice conveniently returns to the coal mill through the coal return port 13 to be milled again, the coal dropping pipe 3 is used for adding the coal dust, the centrifugal separation effect is more uniform and accurate, qualified coal dust particles can leave the separation shell 1 through the coal outlet 5 under the action of airflow generated by the movable impeller 7 and the negative pressure machine 16 and enter the coal dust bin, wherein in order to avoid that coal dust gas contained in the coal dust bin is larger and is diffused in the coal dust bin, the combustion of the coal dust is not only influenced, but also the subsequent operation is influenced, the air powder in the coal dust separated twice is absorbed through the negative pressure machine 16 and the air suction pipe 15 at the coal outlet 5 and is conveyed to the spray tower for processing, wherein the coal filter screen 17 is used for separating the coal dust and the air powder, the third separation is carried out, the coal dust which enters the coal dust bin and is heavy to be combusted is ensured to contain less air powder, the recovery rate of the coal dust is improved, The advantage of even separation of the fineness of the coal dust is favorable for solving the problems of low separation efficiency and high difficulty in adjusting the fineness of the coal dust.

In the description herein, references to the description of "one embodiment," "an example," "a specific example," etc., mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.

The preferred embodiments of the present invention disclosed above are intended only to help illustrate the present invention. The preferred embodiments are not intended to be exhaustive or to limit the invention to the precise embodiments disclosed. Obviously, many modifications and variations are possible in light of the above teaching. The embodiments were chosen and described in order to best explain the principles of the invention and its practical applications, to thereby enable others skilled in the art to best understand the invention for and utilize the invention. The present invention is limited only by the claims and their full scope and equivalents.

Claims

1. The utility model provides a medium speed grinds dynamic buggy separator, includes separation casing (1), moves separating cylinder (2) and coal breakage pipe (3), its characterized in that: the coal separating device is characterized in that the movable separating cylinder (2) is arranged at the top of an inner cavity of the separating shell (1), the coal dropping pipe (3) penetrates through the center of the movable separating cylinder (2), a coal inlet (4) and a coal outlet (5) are respectively arranged at the bottom and the top of the separating shell (1), separating channels (6) are arranged at two sides of the inner cavity of the separating shell (1) which are positioned on the movable separating cylinder (2), a movable impeller (7) sleeved outside the coal dropping pipe (3) is arranged inside the movable separating cylinder (2), a reduction gearbox (10) and a driving motor (9) for driving the reduction gearbox (10) are arranged at the top of the separating shell (1), the output end of the reduction gearbox (10) is connected with a rotating shaft (14), the rotating shaft (14) penetrates through the inside of the separating shell (1) and is fixedly connected with the bottom of the movable impeller (7), the top of the movable impeller (7) is connected with the top of the inner cavity of the separating shell (1) in, driven by a reduction box (10), the movable impeller (7) rotates around a driving motor (9), a separation cylinder (8) is arranged on the periphery of the movable impeller (7), and baffles (12) are arranged on the inner cavity of the separation channel (6) and the outer wall of the coal dropping pipe (3); the coal outlet (5) is connected with the input end of a negative pressure machine (16) through an air suction pipe (15), and the output end of the negative pressure machine (16) is connected with a spray tower.

2. The medium-speed grinding dynamic pulverized coal separator according to claim 1, characterized in that: the movable impeller (7) is a conical rotor movable impeller, and the vane material is low-alloy wear-resistant material.

3. The medium-speed grinding dynamic pulverized coal separator according to claim 1, characterized in that: a plurality of stationary blades (8-3) are uniformly distributed between the lower blade connecting plate (8-1) and the upper blade connecting plate (8-2) in the circumferential direction.

4. The medium-speed grinding dynamic pulverized coal separator according to claim 3, characterized in that: the plurality of stationary blades (8-3) and the radial direction of the circle where the stationary blades are located are provided with the same stationary blade included angle which is 45 degrees.

5. The medium-speed grinding dynamic pulverized coal separator according to claim 1, characterized in that: the drive motor (9) adopts an MB series stepless speed change speed regulation motor.

6. The medium-speed grinding dynamic pulverized coal separator according to claim 1, characterized in that: an air seal piece (11) is also arranged between the reduction gearbox (10) and the coal outlet (5).

7. The medium-speed grinding dynamic pulverized coal separator according to claim 1, characterized in that: baffle (12) that slope set up on separation casing (1) inner wall and baffle (12) looks interval that slope set up on coal breakage pipe (3) outer wall set up.

8. The medium-speed grinding dynamic pulverized coal separator according to claim 1, characterized in that: the baffle (12) is a stainless steel metal filter plate with dense hollows.

9. The medium-speed grinding dynamic pulverized coal separator according to claim 1, characterized in that: and a coal return port (13) is also arranged at the bottom of the separation shell (1).

10. The medium-speed grinding dynamic pulverized coal separator according to claim 1, characterized in that: and a coal filtering net (17) is also arranged at the joint of the air suction pipe (15) and the coal outlet (5).