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Combined fluidized bed type gas-solid heat exchange device utilizing waste heat of furnace slag

A heat exchange device and composite flow technology, applied in fluidized bed heat exchangers, indirect heat exchangers, heat exchanger types, etc., can solve the problems of inability to recover slag heat, high additional energy consumption, large water resources, etc. , to extend the residence heat exchange time, ensure the cooling effect, and improve the adaptability.

Active Publication Date: 2016-05-11
CHONGQING UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the water quenching method has obvious defects: it consumes a lot of water resources; it cannot recover the heat of slag; it pollutes the environment; after water quenching, the slag particles need to be dried, and the additional energy consumption is high.

Method used

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  • Combined fluidized bed type gas-solid heat exchange device utilizing waste heat of furnace slag
  • Combined fluidized bed type gas-solid heat exchange device utilizing waste heat of furnace slag
  • Combined fluidized bed type gas-solid heat exchange device utilizing waste heat of furnace slag

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Embodiment Construction

[0015] The following is attached with the manual Figure 1 to Figure 4 The device of the present invention is described in detail.

[0016] A composite fluidized bed gas-solid heat exchange device utilizing waste heat from slag, including a gas-solid heat exchange body 5, the gas-solid heat exchange body 5 includes a front panel 5-2, a rear panel 5-1, a left panel 5-3, and a right panel 5-4, the top plate 5-5 and the bottom plate 5-6; the top of the gas-solid heat exchange main body 5 is provided with an air outlet 6; the gas-solid heat exchange main body 5 is arranged in a direction parallel to the left panel 5-3 and the right panel 5-4 There are two partition walls 3, both of which are connected to the front panel and rear panel of the gas-solid heat exchange body 5, and divide the internal chamber of the gas-solid heat exchange body 5 into the left bubbling bed chamber 4-1, the spray The bed compartment 2 and the right bubbling bed compartment 4-2, the left and right bubbl...

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Abstract

The invention discloses a combined fluidized bed type gas-solid heat exchange device utilizing waste heat of furnace slag. The device comprises a gas-solid heat exchange body, and an air outlet is arranged at the top of the gas-solid heat exchange body. The device is characterized in that two partition walls are arranged in the gas-solid heat exchange body, connect a front faceplate with a rear faceplate of the same and divide a cabin inside the gas-solid heat exchange body into a left bubbling bed cabin, a spouted bed cabin and a right bubbling bed cabin, the left and right bubbling bed cabins are symmetrically arranged on two sides of the spouted bed cabin, the upper portions and the lower portions of the three cabins are communicated respectively, an independent air chamber is arranged at the bottom of each cabin, a dense-hole-type air distribution plate is arranged above the air chamber in the spouted bed cabin, a left air-cap-type air distribution plate and a right air-cap-type air distribution plate are arranged at the tops of the air chambers in the left and right bubbling bed cabins respectively, and the left air-cap-type air distribution plate is connected with the dense-hole-type air distribution plate through a second dense-hole-type air distribution plate and a first orthostomous section. The combined fluidized bed type gas-solid heat exchange device has good gas-solid heat exchange effect and can be widely applied in the field of steel and iron and power.

Description

technical field [0001] The invention relates to the technical field of blast furnace slag heat exchange, in particular to a compound fluidized bed type gas-solid heat exchange device utilizing waste heat of slag. Background technique [0002] The iron and steel industry is a pillar industry for the development of my country's national economy. Over the past few decades, steel production technology and scale have developed rapidly. In 2013, global steel production reached 1.527 billion tons, and China's steel production was about 779 million tons, accounting for nearly half of global steel production. The total energy consumption of the iron and steel industry accounts for about 16% of the total industrial energy consumption of the country. Calculated by the energy input of 1.757GJ per ton of steel production, a total of 417 million standard coal is consumed, and 1.9 tons of carbon dioxide emissions per ton of steel are calculated, a total of 13.21 billion tons of carbon dio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C21B3/08F28D13/00
CPCC21B3/08F28D13/00
Inventor 王宏李华朱恂丁玉栋付乾黄云张亮廖强李俊陈蓉
Owner CHONGQING UNIV
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