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Planar type multi-level material extra-kiln preheating decomposition device for rotary kiln

A rotary kiln, planar technology, applied in the field of multi-stage material kiln preheating and decomposition device for planar rotary kiln, can solve the problems of energy loss and waste, high filtration cost, difficult feeding, etc., to reduce materials and heat waste, improve calcination efficiency, and reduce installation costs

Pending Publication Date: 2018-11-06
青海奥雷德镁业有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the temperature of the flue gas at the kiln tail is as high as about 800°C, so it cannot directly enter the bag filter to be filtered and emptied.
In order to lower the temperature, a large amount of cold air is usually distributed through the air distributor to force the temperature to drop, which can cause a lot of energy loss and waste and increase the area of ​​the dust collector, and the filtration cost is very high
[0004] It is possible to stack multiple groups of preheating cyclone separators upwards to recycle heat, but in this way, the height of the overall equipment will be as high as ten meters or even higher, the installation cost is high, and the feed height is too high, resulting in Feeding is very difficult

Method used

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  • Planar type multi-level material extra-kiln preheating decomposition device for rotary kiln
  • Planar type multi-level material extra-kiln preheating decomposition device for rotary kiln
  • Planar type multi-level material extra-kiln preheating decomposition device for rotary kiln

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Such as figure 1 As shown, the multi-stage material preheating and decomposition device outside the kiln for the planar rotary kiln includes a rotary kiln 1, and the feed end of the rotary kiln 1 is connected to the air inlet on the upper part of the preheating cyclone separator 3 through the air induction pipe 1, The outlet at the bottom of the preheating cyclone one 3 is connected to the feed end of the rotary kiln 1 through the feeding pipe one 4, and one side of the preheating cyclone one 3 is provided with a preheating cyclone two 5 for preheating The discharge port at the bottom of the cyclone separator 2 5 is connected to the air induction pipe 1 2 through the feeding pipe 2 6, and the air inlet on the upper part of the preheating cyclone separator 2 5 is connected to the preheating cyclone separator 1 through the air induction pipe 2 7 3 The air outlet at the top, the feeding pipe 2 6 is provided with the feeding pump 1 8, the air outlet at the top of the prehea...

Embodiment 2

[0032] Such as figure 2As shown, the difference between this embodiment and Embodiment 1 is that a preheating cyclone three 16 is also arranged between the air outlet at the top of the preheating cyclone two 5 and the dust removal air duct 9, and the preheating cyclone three The device three 16 is located on one side of the preheating cyclone separator two 5, the outlet at the bottom of the preheating cyclone separator three 16 is connected to the draft pipe two 7 through the feeding pipe three 17, and the upper part of the preheating cyclone separator three 16 The air inlet is connected to the air outlet on the top of the preheating cyclone separator 25 through the air induction pipe 3 18, and the feeding pump 2 19 is arranged on the feeding pipe 3 17, and the air outlet on the top of the preheating cyclone separator 3 16 passes through the dust removal The air-introducing pipe 9 is connected to the dust collector 10, and the air-introducing pipe three 18 is provided with a ...

Embodiment 3

[0035] Such as image 3 As shown, the difference between this embodiment and Embodiment 2 is that a preheating cyclone separator 4 20 is also arranged between the air outlet at the top of the preheating cyclone separator 3 16 and the dust removal air duct 9, and the preheating cyclone separator 4 20 is arranged between the preheating cyclone separator Device 4 20 is positioned at one side of preheating cyclone separator 3 16, the outlet at the bottom of preheating cyclone separator 4 20 is connected to draft pipe 3 18 through feeding pipe 4 21, and the top of preheating cyclone separator 4 20 The air inlet is connected to the air outlet at the top of the preheating cyclone separator 3 16 through the air induction pipe 4 22, the feeding pipe 4 21 is provided with the feeding pump 3 23, and the air outlet at the top of the preheating cyclone separator 4 20 passes through the dust removal The air-introducing pipe 9 is connected to the dust collector 10, and the air-introducing pi...

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Abstract

The invention relates to a planar type multi-level material extra-kiln preheating decomposition device for a rotary kiln. The planar type multi-level material extra-kiln preheating decomposition device comprises a rotary kiln. The feeding end of the rotary kiln is connected to an air inlet in the upper portion of a first preheating cyclone separator through a first air guiding pipe. A dischargingopening in the bottom of the first preheating cyclone separator is connected to the feeding end of the rotary kiln through a first discharging pipe. A second preheating cyclone separator is arranged at one side of the first preheating cyclone separator. A discharging opening in the bottom of the second preheating cyclone separator is connected to the first air guiding pipe through a second discharging pipe. An air inlet in the upper portion of the second preheating cyclone separator is connected to an air outlet in the top of the first preheating cyclone separator through a second air guidingpipe. A first discharging pump is arranged on the second discharging pipe. An air outlet in the top of the second preheating cyclone separator is connected to a dust remover through a dust removal airguiding pipe. A feeding opening is formed in an air guiding pipe on the preheating cyclone separator at the terminal end. By means of the planar type multi-level material extra-kiln preheating decomposition device, calcination efficiency is improved; the energy is saved; waste of materials and heat is reduced; and the mounting cost is greatly lowered.

Description

technical field [0001] The invention relates to a multi-stage material kiln preheating and decomposition device for a planar rotary kiln, in particular to a magnesium oxide production and manufacturing device, including magnesium hydroxide, magnesite powder, hydromagnesite powder, magnesium carbonate, etc. Raw materials are calcined by this device to produce magnesium oxide products. Background technique [0002] Rotary kiln refers to rotary calcining kiln, which belongs to the category of building materials equipment. Rotary kiln can be divided into cement kiln, metallurgical chemical kiln and lime kiln according to different materials. Cement kilns are mainly used for calcining cement clinker, which can be divided into two categories: dry production cement kiln and wet production cement kiln. Metallurgical and chemical kilns are mainly used for magnetization roasting of lean iron ore in iron and steel plants in the metallurgical industry; oxidative roasting of chromium a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F27D13/00F27D17/00
CPCF27D13/00F27D17/004F27D17/008F27D2017/009
Inventor 刘士福
Owner 青海奥雷德镁业有限公司