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Production process of active lime

A production process and a technology for active lime, applied in the field of active lime preparation, can solve the problems affecting the quality of low-carbon and high-active lime, the process of treating little sulfur element, and the difficulty in discharging gas, and achieve the advantages of promoting industrialization and reducing raw burning. and overburning phenomenon, the effect of accelerated decomposition

Active Publication Date: 2019-08-09
新兴永和河北能源科技股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When the limestone is calcined by the traditional process, due to the large particle size range of the limestone, the heat transfer rate of the lime is much lower than that of the limestone during the calcining process. As the outer lime layer becomes thicker, the inner limestone particles The heat transfer rate will become slower and slower, and the calcination time will be longer, and the long-term high temperature will make the surface of the limestone over-fired and "ceramized", and the CO generated during calcination will 2 The gas is difficult to discharge, the decarburization is not complete, and a raw burn is formed
This not only wastes energy, but also affects the quality of low-carbon high-activity lime
[0004] In addition, limestone contains a small amount of sulfur, usually in the form of CaSO 4 The form exists, while CaSO 4 The decomposition temperature of calcium carbonate is above 1200°C, and the decomposition process must be carried out completely at 1350-1400°C, which is much higher than the decomposition temperature of calcium carbonate, and because of its low content in limestone, there are few in the prior art. Process for treating sulfur in limestone

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] A kind of production technology of active lime, comprises the following steps:

[0035] (1) Limestone screening and pre-treatment: select limestone raw materials with an average diameter of 500 mm, clean and crush the limestone raw materials, and then screen to obtain limestone powder with an average diameter of 2 mm.

[0036] (2) Mixing: the limestone powder obtained in step (1) is uniformly mixed with 3% NaCl and 0.1% carbon with an average particle diameter of 2 μm to obtain a mixed limestone powder.

[0037] (3) Preheating: transport the mixed limestone powder obtained in step (2) to the preheater for preheating to 650°C for 20 minutes, and then transport the preheated mixed limestone powder to the first decompression chamber Reduced pressure to 0.3MPa.

[0038] (4) Calcination: The mixed limestone powder after decompression and preheating in step (3) is transferred to the sleeve lime kiln for calcination and heat preservation, and the gas consumption of the lower ...

Embodiment 2

[0043] A kind of production technology of activated lime, different from embodiment one is:

[0044] (1) In the step (1), the average diameter of the limestone raw material is 600 mm, and the average diameter of the limestone powder obtained after screening is 4 mm.

[0045] (2) The additive used in the step (2) is KCl, and the addition amount is 2.3%; the carbon average particle size is 1 μm, and the addition amount is 0.13%.

[0046] (3) In step (3), the preheating temperature is 750°C, and the preheating time is 13 minutes. The preheated mixed limestone powder is transported to the second decompression chamber for decompression to 0.7MPa, and then the second decompression chamber The mixed limestone powder in the bin is transported to the first decompression bin for decompression to 0.4MPa.

[0047] (4) In step (4), the gas consumption of the lower combustion chamber in the sleeve lime kiln is controlled to be 4 times the gas consumption of the upper combustion chamber; th...

Embodiment 3

[0052] A kind of production technology of activated lime, different from embodiment one is:

[0053] (1) In the step (1), the average diameter of the limestone raw material is 450 mm, and the average diameter of the limestone powder obtained after screening is 3 mm.

[0054] (2) The additive used in the step (2) is potassium oxalate, the addition amount is 2%; the carbon average particle size is 3 μm, the addition amount is 0.2%.

[0055] (3) In step (3), the preheating temperature is 680° C., and the preheating time is 10 minutes. The preheated mixed limestone powder is transported to the first decompression chamber for decompression to 0.5 MPa.

[0056] (4) In step (4), the gas consumption of the lower combustion chamber in the sleeve lime kiln is controlled to be 3 times the gas consumption of the upper combustion chamber; the excess air coefficient for the upper row of burners is 1.5. The calcination temperature is 900° C., and the calcination time is 4 minutes.

[0057]...

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PUM

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Abstract

The invention discloses a production process of active lime. The process comprises the following steps of (1) screening and pretreatment of limestone, (2) mixing, (3) preheating, (4) calcining, (5) cooling and (6) post-treatment. Firstly, an additive used in the production process reduces underfiring and overburning of the lime, increases the decomposition speed of CaCO3, shortens the calcining time, correspondingly reduces the energy consumption and is beneficial to industrial popularization. Furthermore, carbon is also added, decompression operation is adopted after preheating and before cooling separately, correspondingly the elements sulfur and carbon which remain in lime raw materials can be volatilized out more thoroughly, and the recombination of the elements with calcium oxide is avoided, so that the purity of the active lime is improved, and the activity degree of quicklime is further improved.

Description

technical field [0001] The invention relates to the technical field of active lime preparation, in particular to an active lime production process. Background technique [0002] Active lime is a kind of high-quality light burnt lime, which has fine grains (0.1-3μm), high porosity (50%), and large specific surface area (1.5-2.0m 2 / kg), small bulk density: (1.5~1.7g / cm 3 ), high activity (≥300ml), residual CO 2 Low content (≤2%) and other advantages. Activated lime is mainly used as a "slagging agent" for steelmaking, and is also widely used in environmental protection fields such as wet flue gas desulfurization and acidic industrial wastewater, as well as light calcium carbonate, calcium carbide, briquette binder, epichlorohydrin, Sintered alumina and other chemical production processes. [0003] Activated lime is made by calcining limestone to make calcium carbonate (CaCO 3 ) obtained by thermal decomposition. When the limestone is calcined by the traditional process,...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C04B2/10C04B2/02
CPCC04B2/104C04B2/02
Inventor 闫文海
Owner 新兴永和河北能源科技股份有限公司
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