CN202453271U - Fluidizing device for air separation experiment of pulverized coal - Google Patents

Fluidizing device for air separation experiment of pulverized coal Download PDF

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Publication number
CN202453271U
CN202453271U CN2011205558961U CN201120555896U CN202453271U CN 202453271 U CN202453271 U CN 202453271U CN 2011205558961 U CN2011205558961 U CN 2011205558961U CN 201120555896 U CN201120555896 U CN 201120555896U CN 202453271 U CN202453271 U CN 202453271U
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CN
China
Prior art keywords
jar
fluidized
distribution plate
air distribution
air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2011205558961U
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Chinese (zh)
Inventor
李顺
徐阳
谢国威
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Sinosteel Anshan Research Institute of Thermo Energy Co Ltd
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Sinosteel Anshan Research Institute of Thermo Energy Co Ltd
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Priority to CN2011205558961U priority Critical patent/CN202453271U/en
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Publication of CN202453271U publication Critical patent/CN202453271U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to the field of fluidized bed experimental study and particularly relates to a fluidizing device for an air separation experiment of pulverized coal. The device comprises a fluidized jar, an air distribution plate and an air pipe, wherein one end of the air pipe is connected with the bottom of the fluidized jar, the air distribution plate is arranged on the upper portion of an inlet port of the air pipe at the bottom of the fluidized jar, the top of the fluidized jar is provided with an air outlet port, and a middle section of the fluidized jar above the air distribution plate is a fluidization zone. The device is characterized in that the fluidized jar is made of organic glass, three or more openings are arranged uniformly up and down on one side of the jar wall of the fluidization zone, reverse leakage-proof rubber curtains are arranged at positions of the openings, the opening side jar wall is provided with a fixing support, a rotating shaft is arranged on the fixing support, coal receiving rotating plates which corresponds to the openings are arranged on the rotating shaft, and pressure tapping holes are arranged on the jar wall of the fluidized jar. Compared with the prior art, the device has the advantages that the scheme is feasible, the fluidizing situation of the pulverized coal can be clearly observed, the operation is convenient, the data is accurate and the fluidizing conditions of pulverized coal is visual, and the problem that basic data of air separation of the pulverized coal is difficult to acquire is solved effectively.

Description

A kind of fluidizer of coal dust selection by winnowing experiment usefulness
Technical field
The utility model relates in the fluidized bed experimental study observing with the fluidisation basic data about the fluidized state of medium in the fluidized bed and obtains the field, relates in particular to the fluidizer that a kind of coal dust selection by winnowing is tested usefulness.
Background technology
Domestic iron and steel enterprises adopts traditional wet coal coking technology mostly at present; Basic technology is that several kinds of coal for cokings are broken by certain requirement, mixes the back more by a certain percentage and gets into coking by coke oven, and this technological advantage is a technology maturation; Simple to operate; But owing to contain 10% outside moisture approximately in the coal, cause the defective that is difficult to overcome below traditional wet coal coking technology existence: (1) productive capacity is low; This part moisture of evaporation need consume the plenty of time in process of coking, prolongs total coking cycle; (2) coke quality is difficult to guarantee, outside moisture will make the bulk density of coal reduce, and contact is not tight between the coal grain in process of coking, and the cohesive action of plastic mass is difficult for performance, therefore is difficult to obtain the high-quality smelter coke; (3) external water is divided through process of coking becomes coking chemical waste water, has increased carrying capacity of environment; (4) energy-output ratio is big, because the outside moisture of evaporation certainly will increase thermal energy consumption.
The selection by winnowing humidifying technology is the coking shove charge coal pre-service new technology that the pneumatic selection crushing technology of coking coal and moisture Control technology are integrated in one; It is to utilize the energy that blasts wind to make coal dust be in fluidized state that wherein pneumatic selection is pulverized; Height according to the coal dust buoyance lift is divided into some batches; The specific aim technology of different disposal in addition, so the fluidized state of coal dust more how and coal dust selection by winnowing basic data how accurately to obtain just to become the key of dealing with problems.
Summary of the invention
The purpose of the utility model provides the fluidizer of a kind of coal dust selection by winnowing experiment usefulness, and handled easily can clearly be observed the fluidisation situation of coal dust, solves the problem that coal dust selection by winnowing basic data is accurately obtained.
For solving the problems of the technologies described above, the technical scheme of the utility model is:
A kind of fluidizer of coal dust selection by winnowing experiment usefulness comprises streaming tank, air distribution plate and airduct, and airduct one end links to each other with the streaming tank bottom; Air distribution plate is located at airduct inlet top, streaming tank bottom, and the streaming tank top is provided with air outlet, and streaming tank stage casing, air distribution plate top is a fluidization regions; Said streaming tank is an organic glass matter; Tank skin one side of fluidization regions evenly is provided with the horizontal opening more than three from top to bottom, and opening part is provided with reverse leakproof rubber curtain, and the open side tank skin is provided with fixed support; Fixed support is provided with rotating shaft, and corresponding each opening is provided with and connects the coal flap in the rotating shaft.
The tank skin of said streaming tank is provided with pressure port, and pressure port is separately positioned between top, the fluidization regions bottom and air distribution plate of fluidization regions, between airduct inlet and the air distribution plate.
Compared with prior art; The beneficial effect of the utility model is: scheme is practical, technology accurately and reliably; Can obviously clearly observe the fluidisation situation of coal dust; Have easy to operate, data are accurate and characteristics such as visual, solved coal dust selection by winnowing basic data effectively and obtained problems such as difficulty.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Among the figure: 1-frequency converter 2-blower fan 3-airflow meter 4-air outlet 5-pressure port 6-streaming tank 7-fixed support 8-rotating shaft 9-connects the reverse leakproof rubber of coal flap 10-curtain 11-air distribution plate 12-airduct
Embodiment
Be described further below in conjunction with the embodiment of accompanying drawing the utility model:
Seeing Fig. 1, is the structural representation of the fluidizer of a kind of coal dust selection by winnowing experiment of the utility model usefulness, comprises streaming tank 6, air distribution plate 11 and airduct 12; Airduct 12 1 ends link to each other with streaming tank 6 bottoms, and air distribution plate 11 is located at airduct inlet top, streaming tank 6 bottom, and streaming tank 6 tops are provided with air outlet 4; Streaming tank stage casing, air distribution plate 11 top is a fluidization regions, and streaming tank 6 is transparent organic glass matter, and tank skin one side of fluidization regions evenly is provided with the opening more than three from top to bottom; Opening part is provided with reverse leakproof rubber curtain 10; The open side tank skin is provided with fixed support 7, and fixed support 7 is provided with rotating shaft 8, and corresponding each opening is provided with and connects coal flap 9 in the rotating shaft 8.
The tank skin of streaming tank 6 is provided with pressure port 5, and pressure port 5 is separately positioned between top, the fluidization regions bottom and air distribution plate of fluidization regions, between airduct inlet and the air distribution plate.
The utility model utilizes blower fan 2 in streaming tank 6, to blast air; Make coal dust be in stable fluidized state; Connect quality of pc and the coal particle size that coal flap 9 accesses through measurement, and pressure and air quantity numerical value obtains coal dust selection by winnowing basic data, the step of its realization is following:
1) coal dust is piled up in organic glass matter streaming tank 6 bottoms, and shakeouts with rake;
2) open blower fan 2,, regulate air quantity, and measure air quantity by airflow meter 3 through adjustment frequency converter 1;
3) air blast gets in the streaming tank 6 through air distribution plate 11 uniformly, and when airflow meter 3 arrived to a certain degree, coal dust will be blown up, and presents fluidized state;
4) when the coal dust in the streaming tank 6 is steady state (SS), the reading of record airflow meter 3 and pressure port 5, connecing coal flap 9 is axle with rotating shaft 8, gets into streaming tank 6 through reverse leakproof rubber curtain 10 fast, closes blower fan 2 simultaneously;
5) coal dust of fluidisation is fallen each respectively and is connect coal flap 9, and coal particle size is weighed, measured to the coal dust that connects on the coal flap 9 respectively, obtains the necessary data data of selection by winnowing experiment.

Claims (2)

1. the fluidizer of a coal dust selection by winnowing experiment usefulness comprises streaming tank, air distribution plate and airduct, and airduct one end links to each other with the streaming tank bottom; Air distribution plate is located at airduct inlet top, streaming tank bottom, and the streaming tank top is provided with air outlet, and streaming tank stage casing, air distribution plate top is a fluidization regions; It is characterized in that said streaming tank is an organic glass matter, tank skin one side of fluidization regions evenly is provided with the horizontal opening more than three from top to bottom; Opening part is provided with reverse leakproof rubber curtain; The open side tank skin is provided with fixed support, and fixed support is provided with rotating shaft, and corresponding each opening is provided with and connects the coal flap in the rotating shaft.
2. the fluidizer of a kind of coal dust selection by winnowing experiment usefulness according to claim 1; It is characterized in that; The tank skin of said streaming tank is provided with pressure port, and pressure port is separately positioned between top, the fluidization regions bottom and air distribution plate of fluidization regions, between airduct inlet and the air distribution plate.
CN2011205558961U 2011-12-27 2011-12-27 Fluidizing device for air separation experiment of pulverized coal Expired - Fee Related CN202453271U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011205558961U CN202453271U (en) 2011-12-27 2011-12-27 Fluidizing device for air separation experiment of pulverized coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011205558961U CN202453271U (en) 2011-12-27 2011-12-27 Fluidizing device for air separation experiment of pulverized coal

Publications (1)

Publication Number Publication Date
CN202453271U true CN202453271U (en) 2012-09-26

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011205558961U Expired - Fee Related CN202453271U (en) 2011-12-27 2011-12-27 Fluidizing device for air separation experiment of pulverized coal

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CN (1) CN202453271U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103743538A (en) * 2014-01-09 2014-04-23 煤炭科学研究总院 Air distributor test device for fluidized bed
CN105457889A (en) * 2015-12-09 2016-04-06 榆林学院 Device for sorting clean coal with different particle sizes

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103743538A (en) * 2014-01-09 2014-04-23 煤炭科学研究总院 Air distributor test device for fluidized bed
CN103743538B (en) * 2014-01-09 2019-10-18 煤炭科学技术研究院有限公司 A kind of fluidized bed air distribution plate experimental rig
CN105457889A (en) * 2015-12-09 2016-04-06 榆林学院 Device for sorting clean coal with different particle sizes
CN105457889B (en) * 2015-12-09 2017-11-21 榆林学院 A kind of device for sorting different grain size cleaned coal

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120926

Termination date: 20151227

EXPY Termination of patent right or utility model