Slagging-free type and multilevel differential temperature fluidized roasting system for crystallized aluminum salt and method thereof

A low-temperature roasting and aluminum salt technology is applied to the slagging-free, multi-stage differential temperature fluidized roasting system and field of crystalline aluminum salt, which can solve the problems of high material requirements, low reaction efficiency, poor continuous operation performance of equipment, etc. The effect of good system regulation and stability, high product purity and minimal energy consumption

Active Publication Date: 2012-06-20
BEIJING HANGHUA ENERGY SAVING ENVIRONMENTAL PROTECTION TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the use of rotary kilns as high-temperature roasting equipment for crystalline aluminum salts has the advantage of being easy to implement, but industrial devices such as rotary kilns have the following problems: thermal decomposition of crystalline aluminum salts at a low temperature of 200-300 °C needs to absorb a large amount of heat, and the rotary kiln can only The heat source is provided at the kiln head, which will inevitably lead to insufficient heat absorption or uneven heating of the crystalline aluminum salt in the low-temperature roasting section at the rear of the rotary kiln, resulting in low reaction efficiency
However, when the conventional aluminum hydroxide fluidized roasting system is used for the roasting and preheating of the crystalline aluminum salt, there are the following technical problems: ① The low-temperature drying of the crystalline aluminum salt needs to absorb a large amount of heat, so if the conventional multi-stage series cyclone is used to recover the waste heat As a preheating unit, due to the concentrated release of a large amount of crystal water, the heat supply is insufficient and untimely, and the material continues to be in a low-temperature state, which is prone to agglomeration and slagging, and the continuous operation performance of the equipment is poor.
②In the preheating unit, the corrosive gas released by the decomposition of crystalline aluminum salt (such as HCl, SO 3 ) is easy to condense and cause dew point corrosion, which brings serious corrosion problems to the equipment, and the material requirements are high
③Crystalline aluminum salt roasting has a large heat absorption and decomposes to produce a large amount of corrosive gas and water vapor. If a conventional single fluidized bed roaster is used to process crystallized aluminum salt in industrialization, the roaster is bulky and the amount of combustion material required for roasting is large , economically unfeasible

Method used

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  • Slagging-free type and multilevel differential temperature fluidized roasting system for crystallized aluminum salt and method thereof
  • Slagging-free type and multilevel differential temperature fluidized roasting system for crystallized aluminum salt and method thereof

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Embodiment 1

[0032] Such as figure 1 As shown, a slagging-free, multi-stage differential temperature fluidized roasting system for crystalline aluminum salts according to the present invention includes a low-temperature roasting system 32 for crystalline aluminum salts, a high-temperature alumina finished product roasting system 33, and a multi-stage fluidized cooling system for high-temperature alumina. And heat recovery system 34 and chimney 12;

[0033] The crystalline aluminum salt low-temperature roasting system 32 includes a low-temperature roasted fluidized bed body 3, the bottom of the low-temperature roasted fluidized bed body 3 is connected to a low-temperature roasted fluidized bed air chamber 30, and the lower part of the low-temperature roasted fluidized bed body 3 is also connected to the crystallization The aluminum salt silo and the feeding device 1 are fixedly connected, and the top outlet of the low-temperature roasting fluidized bed body 3 is fixedly connected to the upp...

Embodiment 2

[0056] The difference between this embodiment and Embodiment 1 is that if the roasted crystalline aluminum salt is crystalline aluminum hydroxide, the finished acid preheater 9, the acid gas absorption system 10, the first alkali washing tower 11 and the second alkali washing tower 11 in the system are cancelled. Alkali washing tower 15. The first bag filter 8 is a conventional temperature-resistant bag filter. The flue gas temperature after leaving the first bag filter 8 and the second bag filter 19 is 130-150°C. Other composition, connection mode are identical with embodiment 1.

[0057] The independent temperature control operation of each fractional bed in the present invention satisfies the requirement of a large amount of heat-absorbing characteristics in the low-temperature roasting stage of the crystalline aluminum salt, and solves the problem that the aluminum salt is easily slagged and agglomerated in the low-temperature roasting stage; at the same time, the roastin...

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Abstract

The invention provides a slagging-free type, low-energy consumption and multilevel differential temperature fluidized roasting system for crystallized aluminum salt and a method thereof. The system comprises a crystallized aluminum salt low-temperature roasting system, an aluminum oxide high-temperature finished product roasting system, a high-temperature aluminum oxide multilevel fluidized cooling and heat recovery system and a chimney. The method comprises the following steps of: reducing the outlet temperature of low-temperature roasting flue gas with large gas production rate by adopting a differential temperature multiple roasting method, so that sensible heat carried by the flue gas is greatly reduced; and carrying out reasonable cascade utilization on energy and converting fuel chemical energy inputted by a process system into effective heat of the system to a greatest extent. The slagging-free type and multilevel differential temperature fluidized roasting system has the remarkable advantages of strong adaptability to the content of attached water of the crystallized aluminum salt, good adjustment and stability, high product purity, low energy consumption, low investment, small floor area and the like.

Description

technical field [0001] The invention relates to a slagging-free, low energy consumption, multi-stage differential temperature fluidized roasting system and method for crystalline aluminum salts, in particular to a multi-stage, differential temperature roasting process for preparing industrial alumina by fluidized roasting crystalline aluminum salts systems and methods. The crystalline aluminum salt may include crystalline aluminum chloride hexahydrate, crystalline aluminum sulfate, aluminum hydroxide and the like. Background technique [0002] my country is the largest alumina producer in the world, but there is a serious shortage of high-grade bauxite in my country, which has seriously affected the rapid development of my country's alumina industry. my country is a big country with coal power, and a large amount of high-alumina fly ash (Al 2 o 3 ≥38wt%), according to statistics, the annual output of high-alumina fly ash is as high as 100 million tons, which is a very imp...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F7/30C01F7/32
CPCY02P20/129
Inventor 张楠钱永康陆志明姜振华王军李永胜侯凤云王会宁丁建亮罗剑
Owner BEIJING HANGHUA ENERGY SAVING ENVIRONMENTAL PROTECTION TECH CO LTD
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