A process for producing sintered bricks with ultra-high content of fly ash

A technology for fly ash and sintered bricks, which is applied in the technological field of producing sintered bricks with ultra-high content of fly ash, can solve the problems of product strength influence, large drying shrinkage, easy deformation of wet blanks, etc. risk, solve corrosion resistance problems, improve the effectiveness of dry contact surfaces

Active Publication Date: 2016-05-04
西安瑞泰机械设备制造有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When using shale powder with this particle size, the amount of fly ash is generally controlled below 25wt%, otherwise it will be difficult to achieve a satisfactory product pass rate and the product strength will be affected. At the same time, due to the low amount of fly ash, the roasting process must More high-quality coal is artificially cast outside, and energy consumption is high
However, when a higher amount of fly ash is used, the wet body of fly ash sintered brick has low strength, large drying shrinkage, and large residual moisture. As a result, under the traditional process conditions, the wet body is easily deformed, cracked, and the strength is low. rate is not high
And under the traditional production conditions, when the fly ash with high sulfur content from the power plant is used, the corrosion damage to the roof of the sintering kiln is great, and the maintenance and maintenance costs of the kiln body are high, which is not suitable for long-term large-scale industrial production

Method used

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  • A process for producing sintered bricks with ultra-high content of fly ash

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Prepare materials by weight:

[0026] Material name parts by weight

[0027] 62 parts of fly ash

[0028] Hard Shale 38 parts

[0029] The hard shale is sent to the hammer crusher for crushing, and then sent to the pendulum mill for further refining treatment. The particle size of the shale powder after refining treatment is below 2mm, and the particles below 1mm account for 82wt% , Particles below 0.25mm accounted for 35wt%. Feed the fly ash and finely ground shale powder into the rod mixer for mixing; after mixing evenly, send them into the first double-shaft mixer, add room temperature water for stirring; after stirring evenly , into the second twin-shaft mixer, based on the total weight of the fly ash and the refined shale powder, add 15wt% of 90-degree hot water for stirring.

[0030] Afterwards, the stirred material is sent to the aging warehouse for aging for more than 72 hours. The aged material is extruded through a two-stage vacuum brick extrusion machine...

Embodiment 2

[0034] Prepare materials by weight:

[0035] Material name parts by weight

[0036] 65 parts of fly ash

[0037] Hard Shale 35 parts

[0038] The hard shale is sent to the hammer crusher for crushing, and then sent to the pendulum mill for further refinement. The particle size of the shale powder after refinement is below 1.8mm, and the particles below 1.5mm account for 85wt%, particles below 0.25mm accounted for 40wt%. Send the fly ash and ground shale powder into the rod mixer for mixing; after mixing evenly, send them into the first double-shaft mixer, add room temperature water for stirring; after stirring evenly, send them into In the second twin-shaft mixer, based on the total weight of the fly ash and the refined shale powder, 18% of water or steam is added for stirring.

[0039] Afterwards, the stirred material is sent to the aging warehouse for aging for more than 72 hours. The aged material is extruded through a two-stage vacuum brick extrusion machine, the extr...

Embodiment 3

[0043] Prepare materials by weight:

[0044] Material name parts by weight

[0045] 70 parts of fly ash

[0046] 30 parts of clay

[0047] The rest of the production process is the same as in Example 1, the difference is only that the clay is crushed by using a high-speed finely crushed pair of rollers, and the firing temperature is set at 1080°C

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Abstract

The invention provides a high efficiency and energy saving fly ash sintered brick making method. The optimization of granularity graduation of shale powder and the introduction of a single layer drying process capable of realizing large-scale continuous production solve the problems of low strength and easy deformation of green bricks in the drying process of ultrahigh-content fly ash sintered bricks, and multi-time mixing, forced mixing, heat insulation time prolongation processes further improve the product stability, so the large-scale industrial production of ultrahigh-content fly ash sintered bricks is successfully realized, the sintered bricks obtained in the invention has high yield, excellent strength and reduced weight, and energy consumed by sintering is effectively reduced. The selection of a kiln top and a hanging structure made of a sintered refractory material improves the acid corrosion resistance of a kiln body, can effectively adapt to the production of high--sulfur high-carbon fly ash sintered bricks, solves the problem of difficult utilization of fly ash from a circulating fluidized bed power plant, and improves the resource utilization rate.

Description

technical field [0001] The invention relates to a production process of sintered bricks for construction, in particular to a process for producing sintered bricks with ultra-high content of fly ash. Background technique [0002] For a long time, the leading product of my country's brick and tile industry has been solid clay bricks. The preparation of clay bricks has problems such as damaging the environment and high coal consumption. However, the annual discharge of fly ash produced by thermal power plants is high, and the accumulation covers an area of ​​more than 1 million mu, causing serious pollution. The use of fly ash and other wastes to make building bricks is the main direction of developing new wall materials for energy saving, land saving, waste utilization, heat preservation and heat insulation. At the same time, as a resource-saving unit, the circulating fluidized bed unit can effectively use energy with low calorific value. used waste. How to use high dosage ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C04B30/00C04B18/08
CPCY02W30/91
Inventor 赵逸川
Owner 西安瑞泰机械设备制造有限公司
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