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Method for preparation of belite sulphoaluminate cement and co-production of sulfuric acid by reducing gypsum with sulfur gas

A Belite sulfoaluminate and teresulfoaluminate technology, which is applied in the field of building materials and chemical products, can solve the problems of high operating costs, difficulties in co-production of sulfuric acid "two conversions and two absorptions", comprehensive utilization rate of less than 40%, etc. question

Active Publication Date: 2020-08-25
上海三夫工程技术有限公司 +1
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AI Technical Summary

Problems solved by technology

At present, the annual output of desulfurized gypsum in my country is about 80 million tons, and the comprehensive utilization rate is about 83%; the annual output of phosphogypsum is about 80 million tons, and the comprehensive utilization rate is less than 40%; other by-product gypsum is about 25 million tons, and the comprehensive utilization rate is about 40%.
The purpose of the above-mentioned inventive method is to maximize the utilization of industrial by-product gypsum as calcium and sulfur raw materials, provide a good idea for the resource utilization of industrial by-product gypsum, and can get through in the process; but the above methods mostly use activated carbon or Solid coke or anthracite is used as a solid reducing agent, and gypsum, clay, high-quality bauxite, fly ash, iron slag, high-sulfur coal, etc. are calcined together to produce sulphoaluminate or belite sulphoaluminate cement clinker , carbon reduction generally has high investment energy consumption and high CO 2 Emissions, furnace gas SO 2 The concentration is low, the co-production of sulfuric acid is difficult for "two conversions and two absorptions", and the operation cost is high. There are problems in operation, environmental protection and economic cost.
[0010] There are also some patents or literature reports, using phosphogypsum or desulfurization gypsum or titanium gypsum and other industrial by-product gypsum and limestone together as the source of calcium and sulfur in cement ingredients, and other raw materials such as bauxite to configure the required cement raw materials. Calcination to produce sulphoaluminate cement clinker or belite sulphoaluminate cement clinker, these methods are a small part of the use of gypsum decomposition to replace a part of CaO in limestone, can not effectively use industrial waste gypsum on a large scale, calcination SO in flue gas 2 The concentration cannot reach the concentration requirements of conventional industrial production of sulfuric acid, and the SO 2 It also increases the burden of environmental protection

Method used

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  • Method for preparation of belite sulphoaluminate cement and co-production of sulfuric acid by reducing gypsum with sulfur gas
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  • Method for preparation of belite sulphoaluminate cement and co-production of sulfuric acid by reducing gypsum with sulfur gas

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Experimental program
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Effect test

preparation example Construction

[0084] F. Preparation of cement

[0085] From the cement clinker from the cooler in step E, add gypsum and composite materials, and then undergo subsequent grinding processing to obtain Belite sulfoaluminate cement products with different performance requirements.

Embodiment 1

[0088] process such as figure 2 As shown, dihydrate phosphogypsum, low-grade bauxite, and high-alumina fly ash are used as raw materials. The raw materials are dried and ground to >95%-80μm, and most of the fly ash produced by the combustion of fuel coal in the rotary kiln enters the In clinker, the chemical composition of raw material and raw meal is shown in Table 1.

[0089] Table 1 Chemical composition of raw materials and raw meal

[0090] project CaO SiO 2

Al 2 o 3

Fe 2 o 3

MgO P 2 o 5

Na 2 o

SO 3

LOSS total Phosphogypsum 32.56 4.76 0.97 0.39 0.31 1.05 0.30 43.63 15.98 99.95 Bauxite 2.25 24,20 53.51 2.45 0.07 0.00 0.13 0.20 17.98 99.73 fly ash 1.48 43.50 35.38 1.92 0.70 0.00 0.33 0.68 14.77 98.76 Raw material 27.34 10.86 8.18 0.69 0.33 0.87 0.29 36.30 15.96 100.00

[0091] The above raw materials of phosphogypsum dihydrate, low-grade bauxite, and ...

Embodiment 2

[0100] process such as image 3 As shown, dihydrate phosphogypsum and high-aluminum fly ash are used as raw materials. The raw materials are dried and ground to >95%-80μm. Most of the fly ash produced by the combustion of fuel coal in the rotary kiln enters the clinker. The raw materials and The chemical composition of the raw meal is shown in Table 4.

[0101] Table 4 Chemical Composition of Raw Materials and Raw Meals

[0102] project CaO SiO 2

al 2 o 3

Fe 2 o 3

MgO P 2 o 5

Na 2 o

SO 3

LOSS total Phosphogypsum 32.56 4.76 0.97 0.39 0.31 1.05 0.30 43.63 15.98 99.95 fly ash 1.48 43.50 35.38 1.92 0.70 0.00 0.33 0.68 14.77 99.73 Raw material 27.72 10.91 6.42 0.63 0.37 0.89 0.31 36.93 15.83 100.00

[0103] The above-mentioned phosphogypsum dihydrate and high-alumina fly ash raw materials are composed by weight: 84.2 parts of phosphogypsum dihydrate and 15.8 parts of high-a...

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Abstract

The invention relates to a method for the preparation of belite sulphoaluminate cement and the co-production of sulfuric acid by reducing gypsum with sulfur gas. According to the method, industrial byproduct gypsum is used as a main raw material; an alkalinity coefficient (C), an aluminum-sulfur ratio (P) and an aluminum-silicon ratio (N) are controlled according to the application requirements ofthe belite sulphoaluminate cement clinker; one or more of low-grade bauxite, coal ash, coal gangue, red mud, clay and iron slag are selected as ingredients, the gas sulfur is adopted as a reducing agent, so that the gypsum is promoted to be decomposed; and therefore, the belite sulphoaluminate cement is prepared, and meanwhile, high-concentration gas-phase SO2 flue gas is obtained and used for preparing sulfuric acid from follow-up flue gas. Compared with the prior art, the method can consume a large amount of industrial gypsum and save limestone and natural gypsum resources, meanwhile, can obtain high-quality belite sulphoaluminate cement and industrial sulfuric acid products; and the method has the advantages of simple process, high implementation performance of system control indexes,convenient operation and management, advanced process equipment, low device investment, low energy consumption, low operation cost and high automation degree.

Description

technical field [0001] The invention relates to building materials and chemical products, in particular to a method for producing belite sulfoaluminate cement by reducing raw material containing gypsum with sulfur gas to co-produce sulfuric acid. Background technique [0002] Sulphoaluminate cement has the advantages of low alkalinity, high early strength, micro-expansion, corrosion resistance and frost resistance, and is especially suitable for use in coastal and cold areas and emergency repair projects. Traditional sulphoaluminate cement is made of calcium sulphoaluminate by calcining limestone, bauxite and gypsum at high temperature (1200-1350°C). Dicalcium silicate (C 2 S) is the main mineral phase composition, and then mixed with a small amount of gypsum and ground to obtain sulphoaluminate cement products. Compared with ordinary Portland cement, due to the reduction in the amount of raw material limestone, the firing temperature is also 100-150°C lower than that of ...

Claims

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Application Information

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IPC IPC(8): C04B7/345C04B7/32C04B7/36C04B7/43C04B7/44C01B17/50C01B17/74
CPCC04B7/3453C04B7/323C04B7/36C04B7/434C04B7/44C01B17/508C01B17/506C01B17/74Y02P20/10Y02P20/129
Inventor 陈延信庞仁杰赵博张国兴韩丁张志远
Owner 上海三夫工程技术有限公司
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