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A dynamic calciner for powder with double outlets

A dynamic calcination and double discharge technology, applied in the field of calcination furnace, can solve the problems of high energy consumption, reduction of carbon dioxide concentration, increase of exhaust volume, etc., and achieve the effects of avoiding material accumulation at the bottom of the furnace, increasing the contact area, and fully burning

Inactive Publication Date: 2018-01-30
SICHUAN HAIYA POWDER TECH CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] 1. Since the calcination furnace has a certain height, it takes a lot of energy to transport a large amount of materials from the bottom of the furnace to the top of the furnace;
[0004] 2. Since a large amount of carrier air needs to be added to transport a large amount of materials from the lower part of the calciner to the upper part, the total exhaust volume of the entire calciner will increase a lot, thus increasing the energy consumption of the calciner;
[0005] 3. Due to the particle size and humidity of the calcined material, it will cause the bottom of the calcined furnace to accumulate material easily;
However, the increase in the total exhaust volume of the calciner will reduce the concentration of carbon dioxide in the tail gas, and this industry cannot use the traditional boiling calciner or swirling flow dynamic calciner for calcining

Method used

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  • A dynamic calciner for powder with double outlets

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Embodiment Construction

[0017] The present invention will be further described below in conjunction with accompanying drawing, protection scope of the present invention is not limited to the following:

[0018] Such as figure 1 As shown, a dynamic calciner for powder with double discharges, which includes a calciner main body 1, a raw material heater 2, a heater A3, a vacuum cleaner A6, a star discharge valve A7, a cyclone separator A9, and a star discharge valve B8, air-air heat exchanger A10, air cooler A11, heater B12, air-air heat exchanger B19, air cooler B20, cyclone separator B14, star discharge valve C15, vacuum cleaner B18, star discharge valve D16 and Tail exhaust fan 17, heat exchanger A10, cyclone separator A9 and vacuum cleaner A6 are connected in series in sequence, heat exchanger B19, cyclone separator B14 and vacuum cleaner B18 are connected in series in sequence, and gas-gas heat exchanger B19 is connected above the calciner main body 1, In this embodiment, the air cooler A11 is arr...

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PUM

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Abstract

The invention discloses a dual-discharge powder dynamic calcining furnace, which comprises a calcining furnace main body (1), a raw material heater (2), a heater A (3), a vacuum cleaner A (6) and a star discharge valve A (7), cyclone separator A (9), star discharge valve B (8), heat exchanger A (10), air cooler A (11), heater B (12), heat exchanger B (19) ), air cooler B (20), cyclone separator B (14), star discharge valve C (15), vacuum cleaner B (18), star discharge valve D (16) and tail exhaust fan (17) , the heat exchanger A (10), the cyclone separator A (9) and the vacuum cleaner A (6) are connected in series in sequence, and the heat exchanger B (19), the cyclone separator B (14) and the vacuum cleaner B (18) are connected in series in sequence. The beneficial effects of the invention are as follows: the device has the advantages of small air extraction, reducing the heat carried by the exhaust gas, less material accumulation at the bottom, recovering part of the waste heat to save energy, and preventing material accumulation in the calciner.

Description

technical field [0001] The invention relates to a calciner, in particular to a dynamic calciner for powder with double discharges. Background technique [0002] The powder raw materials to be calcined in the fluidized calciner and swirling flow dynamic calciner under the existing technical conditions are all fed from the lower part of the calciner, and the calcined finished product is drawn out from the upper part of the calciner through the tail-mounted induced draft fan. This calcination method has the following disadvantages: [0003] 1. Since the calcination furnace has a certain height, it takes a lot of energy to transport a large amount of materials from the bottom of the furnace to the top of the furnace; [0004] 2. Since a large amount of carrier air needs to be added to transport a large amount of materials from the lower part of the calciner to the upper part, the total exhaust volume of the entire calciner will increase a lot, thus increasing the energy consump...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F27B15/08F27B15/09
Inventor 周安虎
Owner SICHUAN HAIYA POWDER TECH CO LTD
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