Powder multistage suspension preheating kiln outside calcium oxide calcining method

A technology of suspension preheating and decomposition outside the kiln, applied in chemical instruments and methods, calcination, preheating costs, etc., can solve the problems of increasing environmental protection desulfurization, poor combustion effect, long calcination and decomposition time, etc. The effect of decomposing quickly and fully and reducing unit consumption

Active Publication Date: 2019-11-26
GUANGXI SIWEI MATERIALS TECH CO LTD
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  • Summary
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AI Technical Summary

Problems solved by technology

[0003] The vertical kiln is for calcination of large limestone with a particle size of 100mm-300mm. During the calcination process, it needs to be matched with suitable fuel, and it enters the kiln simultaneously for combustion. In this process, large limestone is required to achieve the effect of ventilation and combustion. Slow burning speed, low efficiency, high energy consumption, low output, poor quality, and need to increase environmental protection desulfurization and denitrification equipment, resulting in high production costs
[0004] The single-stage preheating rotary kiln is for calcination of limestone with a particle size of 40mm-80mm. The material slowly enters the kiln head of the rotary kiln and injects fuel for combustion. The waste heat generated during the combustion process of the rotary kiln enters the single-stage preheater at the kiln tail. Inside, the material has a certain preheating effect, but it absorbs heat slowly, and the material particles are relatively large, resulting in relatively poor combustion effect, relatively long calcination and decomposition time, poor ventilation effect, etc., low output, high energy consumption, poor quality, and It is also necessary to increase environmental protection desulfurization and denitrification equipment
[0005] These two traditional processes are to calcinate block limestones of different sizes into block lime at high temperature, and then undergo grinding, hydration and other processes, and further process them into lime powder, lime paste (slaked lime) and other materials. Traditional processing methods Low production capacity, the current single machine production capacity is 100 to 800 tons / day, and the energy consumption is high, the energy consumption is 3350kJ / kg (200 kg standard coal), and the power consumption is 50 degrees

Method used

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  • Powder multistage suspension preheating kiln outside calcium oxide calcining method
  • Powder multistage suspension preheating kiln outside calcium oxide calcining method

Examples

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Embodiment 1

[0035] Such as figure 1 As shown, the processing system used in the method for decomposing and calcining calcium oxide outside the powder multi-stage suspension preheating kiln described in this embodiment includes six-stage hot flue gas cyclone C1-C6, decomposition furnace 4, rotary kiln 6 and cooler 7. The rotary kiln 6 is provided with a fuel injection port, and a tertiary hot air pipe 5 is provided between the fuel injection port of the rotary kiln 6 and the calciner 4. The smoke chamber of the rotary kiln 6 is connected with the calciner 4 and the hot air duct 3. The outlet of the outlet is connected with cooler 7.

[0036]The six-stage hot flue gas cyclones C1-C6 are sequentially connected in series on the hot air duct 3 that conveys the hot flue gas upwards. An exhaust fan 2 is installed at the end of the hot air duct 3, and the hot flue gas cyclone at the top is the first-stage hot air duct. The flue gas cyclone C1, the blanking outlet of the first stage hot flue gas...

Embodiment 2

[0049] In this embodiment, the processing system described in Example 1 is used to prepare calcium oxide, and the production capacity is 2250 tons / day. The size of the hot flue gas cyclones at all levels is: the diameter of cyclone C1 is 5.67m, and the height is 5.35m; the diameter of cyclone C2 Cyclone C3 is 6.58m in diameter and 5.83m in height; cyclone C3 has a diameter of 6.96m and a height of 6.93m; cyclone C4 has a diameter of 7.15m and a height of 5.58m; cyclone C5 has a diameter of 7.86m and a height of 5.91m; C6 has a diameter of 7.93m and a height of 5.98m. The calciner has a diameter of 6.8m and a height of 13.5m; the size of the rotary kiln is Φ4.2×60m, and the kiln speed is 3.5 rpm.

[0050] The specific method is: crush the limestone and grind it into powder raw meal with a particle size of less than 70 mesh, and put 180 tons of raw meal per hour into the first-stage hot flue gas cyclone C1 and the second-stage hot flue gas through the elevator. After suspension ...

Embodiment 3

[0052] The present embodiment adopts the processing system identical with embodiment 2 to prepare calcium oxide, and concrete method is:

[0053]The limestone is crushed and ground into powder raw meal with a particle size of less than 70 mesh, and the raw meal is put into the first-stage hot smoke cyclone C1 and the second-stage hot smoke cyclone C2 through the hoist at a rate of 195 tons per hour. After suspending and preheating in the connecting pipe between them, it enters the first-stage hot gas cyclone C1. After suspending and preheating, the material enters the hot air passage between the second-stage hot-flue gas cyclone C2 and the third-stage hot-flue gas cyclone C3. Suspension preheating, the material is brought into the second-stage hot smoke cyclone C2 by the hot air flow to collect and preheat. At this time, the temperature of the second-stage hot smoke cyclone C2 is controlled at 400°C (T2), and under the control of the exhaust fan, the negative pressure is 4Pa k...

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Abstract

The invention discloses a powder multistage suspension preheating kiln outside calcium oxide calcining method. The powder multistage suspension preheating kiln outside calcium oxide calcining method comprises following steps: 1, limestone powder is introduced into a multistage suspension preheating kiln for preheating to 800 to 900 DEG C; 2, the pre-heated material is introduced into a decomposition furnace, and calcining is carried out for 25 to 35s at 900 to 1100 DEG C; 3, the calcined material is conveyed back into a rotary kiln, and is subjected to calcining for 25 to 35min at 1100 to 1300DEG C, and is cooled to obtain calcium oxide. According to the method, the step in the prior art that block limestone is subjected to direct calcining is changed into the above steps that limestone is crushed into powder, and suspension preheating, decomposition furnace calcining decomposition, and rotary kiln calcining slaking are adopted to prepare powdery calcium oxide, the single line production capacity is 5 to 10 times higher than that of the conventional method, and energy saving and environment protection are realized.

Description

technical field [0001] The invention relates to a calcining method for calcium oxide, in particular to a method for decomposing and calcining calcium oxide outside a powder multistage suspension preheating kiln. Background technique [0002] There are mainly two methods for producing calcium oxide (lime) at present. The first method is to use a vertical kiln to fire, and the second method is to use a single-stage preheating rotary kiln to fire. [0003] The vertical kiln is for calcination of large limestone with a particle size of 100mm-300mm. During the calcination process, it needs to be matched with suitable fuel, and it enters the kiln simultaneously for combustion. In this process, large limestone is required to achieve the effect of ventilation and combustion. The combustion speed is slow, the efficiency is low, the energy consumption is high, the output is low, the quality is poor, and it is necessary to increase environmental protection desulfurization and denitrifi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C04B2/10
CPCC04B2/10B01J3/006B01J6/001B01J6/004B01J8/14B01J8/386C01F11/06C01P2006/80F27B15/003F27B15/08F27B15/09F27B15/10F27D13/00F27D15/02F27D2013/007Y02P20/10B01J6/002C01P2004/60
Inventor 庄严庄里程庄前程
Owner GUANGXI SIWEI MATERIALS TECH CO LTD
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