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Experimental device and method used for research on particle flow characteristic in bubbling fluidized bed

A technology of bubbling fluidized bed and flow characteristics, applied in flow characteristics, measuring devices, instruments, etc., can solve problems such as the actual detection of wet particle motion characteristics in bubbling fluidized bed, and achieve the effect of ensuring accuracy

Inactive Publication Date: 2017-01-11
HARBIN INST OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] However, the practical detection of the motion characteristics of wet particles in a bubbling fluidized bed is a major challenge.

Method used

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  • Experimental device and method used for research on particle flow characteristic in bubbling fluidized bed
  • Experimental device and method used for research on particle flow characteristic in bubbling fluidized bed
  • Experimental device and method used for research on particle flow characteristic in bubbling fluidized bed

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Experimental program
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specific Embodiment approach 1

[0034] Specific implementation mode one: as figure 1 As shown, the experimental device provided in this embodiment for the study of the flow characteristics of wet particles in a bubbling fluidized bed consists of a PIV image processing system 1, a high-speed camera 2, a light source 3, a humidifier 4, a fixed bracket 5, and a bubbling fluidized bed. Bed 6, particles in the bed (dry particles or wet particles for experiments) 7, air distribution plate 8, air chamber 9, hot air flow meter 10, ventilation pipe 11, turbine flow meter 12, gas valve 13 and fan 14, among which:

[0035] The bubbling fluidized bed 6 is fixed on the fixed support 5;

[0036] The humidifier 4 is installed on the top of the bubbling fluidized bed 1;

[0037] The light source 3 is arranged at an angle of 45° obliquely above the bubbling fluidized bed 6;

[0038] The high-speed camera 2 is located at the front of the bubbling fluidized bed 1 and is connected to the PIV image processing system 1 to take ...

specific Embodiment approach 2

[0049] Specific implementation method two: Prepare enough spherical particles with an appropriate amount of diameter of 2.50mm, and evenly fill the particles at the bottom of the bubbling fluidized bed, turn on the high-speed camera, and take the bubbling fluidized bed into the lens, and adjust the The light source makes the picture captured by the camera clear enough to ensure the accuracy of post-image processing; turn on the fan, adjust the gas flow, and observe the indication of the turbine flowmeter at the same time, and read the gas flow at intervals after the indication is stable. Take the average value after the second reading; ensure that the fluidized bed is in a dry state during the fluidization process, when the flow is stable and the shooting time is long enough, first turn off the fan, and when the particles are completely still, turn off the high-speed camera; The results are imported into the post-processing computer to obtain results such as particle velocity d...

specific Embodiment approach 3

[0050] Specific implementation method three: Prepare enough spherical particles with an appropriate amount of diameter of 2.50 mm, calculate the volume of the required silicone oil according to the total volume of the particles and the required liquid amount of 0.55%, and mix the particle silicone oil evenly; fill the mixed particles evenly in the At the bottom of the bubbling fluidized bed, turn on the high-speed camera, take the bubbling fluidized bed into the lens, and adjust the light source at the same time, so that the picture captured by the camera is clear enough to ensure the accuracy of the post-image processing; turn on the fan, Adjust the gas flow while observing the reading of the turbine flowmeter. When the reading is stable, read the gas flow at intervals, and take the average value after multiple readings; add a certain amount to the particle system through the humidifier during the fluidization process. Silicone oil, to ensure that the volume fraction of silico...

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Abstract

The invention discloses an experimental device and method used for research on a particle flow characteristic in a bubbling fluidized bed. The experimental device is composed of a PIV image processing system, a high-speed camera, a light source, a humidifier, a fixing support, the bubbling fluidized bed, experimental dry particles or wet particles, a wind-distribution plate, a wind chamber, a hot wind flow meter, a ventilating pipeline, a turbine flower meter, a gas valve and a fan; the bubbling fluidized bed is fixed to the fixing support, the humidifier is installed at the top of the bubbling fluidized bed, the light source is arranged obliquely above the bubbling fluidized bed, the high-speed camera is located at the front of the bubbling fluidized bed and connected with the PIV image processing system, the wind chamber is located at the bottom of the bubbling fluidized bed and connected with the bubbling fluidized bed through wind-distribution plate, the hot wind flow meter is installed close to a wind chamber inlet of the bubbling fluidized bed, the fan is connected with the wind chamber through the ventilating pipeline, and the turbine flow meter and the gas valve are installed on the ventilating pipeline. The experimental device and method can carry out research on a dry particle system and the wet particle flow characteristic at the same time.

Description

technical field [0001] The invention relates to an experimental device and method capable of simultaneously conducting research on the flow characteristics of a dry particle system and a wet particle based on a bubbling fluidized bed. Background technique [0002] A fluidized bed where the velocity of the fluidizing gas in the bed exceeds the minimum fluidization velocity of the particles is referred to as a "bubbling fluidized bed". At this time, the particle system in the bed will no longer maintain a uniform and stable state, and the air bubbles generated at the bottom of the fluidized bed will pass through the dense phase region of solid particles to reach the surface of the bed. The bed is accompanied by the recurring process of bubble generation, movement, growth and rupture. During this period, the strong bubbling phenomenon makes the movement of particles more intense, and there are complex mixing, agglomeration and separation phenomena in the particle system. [00...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): G01N15/00G01N11/00
CPCG01N15/00G01N11/00
Inventor 何玉荣唐天琪任安星王天宇邰曈
Owner HARBIN INST OF TECH