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A kind of method for preparing Belite sulfoaluminate cement co-producing sulfuric acid

A belite sulfoaluminate and special sulfoaluminate technology, applied in the field of building materials and chemical products, can solve the problem of high operating cost, inability to effectively utilize industrial waste slag gypsum on a large scale, and no co-production process of sulfuric acid has been found. technical or methodological issues to achieve the effect of saving resources

Active Publication Date: 2022-07-15
上海三夫工程技术有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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 invention method is to maximize the utilization of industrial by-product gypsum as calcium and sulfur raw materials, which provides a good idea for the resource utilization of industrial by-product gypsum, and can get through in the process; but most of the above methods 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.
[0011] 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. Sintering 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, and cannot effectively utilize industrial waste gypsum on a large scale, calcining 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
[0012] Existing documents and patents have been searched, and there are reports on the method of using sulfur or sulfur gas to reduce gypsum to produce calcium oxide or Portland cement. No information has been found on the use of sulfur gas and high-sulfur bauxite to reduce gypsum to produce Bailey. A report on the process technology or method of co-production of sulfuric acid with sulfoaluminate cement

Method used

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  • A kind of method for preparing Belite sulfoaluminate cement co-producing sulfuric acid
  • A kind of method for preparing Belite sulfoaluminate cement co-producing sulfuric acid
  • A kind of method for preparing Belite sulfoaluminate cement co-producing sulfuric acid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0076] Process such as figure 2 As shown in the figure, phosphogypsum, high-sulfur bauxite and fly ash are used as raw materials, and the raw materials are dried and pulverized to > 95%-80 μm. The chemical composition of raw materials and raw meal is shown in Table 1.

[0077] Table 1 Chemical composition of raw materials and raw meal

[0078] 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 High sulfur bauxite 2.42 22.55 52.93 7.45 0.09 0.00 0.21 6.25 7.52 99.42 fly ash 1.48 43.50 35.38 1.92 0.70 0.00 0.33 0.68 14.77 98.76 Raw material 27.31 9.47 8.65 1.19 0.32 0.87 0.29 36.68 15.10 100.00

[0079] The above-mentioned phosphogypsum dihydrate, high-sulfur bauxite, and fly ash raw materials are composed by weight: 82.7 parts of phosphogypsum dihydrate, 9.6 parts of ...

Embodiment 2

[0088] Process such as image 3 As shown, using dihydrate phosphogypsum and high-sulfur and low-grade bauxite as raw materials, the raw materials are dried and pulverized to > 95%-80 μm, and most of the fly ash produced by the combustion of fuel coal in the rotary kiln enters the clinker. The chemical composition of raw materials and raw meal is shown in Table 4.

[0089] Table 4 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 High sulfur bauxite 2.42 20.35 44.18 12.86 0.09 0.00 0.21 11.37 7.82 99.30 Raw material 26.58 7.89 9.63 2.89 0.27 0.84 0.28 37.24 14.37 100.00

[0091] The above-mentioned phosphogypsum dihydrate and high-sulfur and low-grade bauxite raw materials are composed by weight as follows: 80.0 parts of ph...

Embodiment 3

[0099] Process such as Figure 4 As shown, using desulfurized gypsum, high-sulfur and high-iron bauxite, and fly ash as raw materials, the raw materials are dried and pulverized to > 95%-80 μm, and most of the fly ash produced by the combustion of the fuel coal in the rotary kiln enters the clinker , and its chemical composition is shown in Table 7.

[0100] Table 7 Chemical composition of raw materials and raw meal

[0101] project CaO SiO 2

Al 2 O 3

Fe 2 O 3

MgO TiO 2

Na 2 O

SO 3

LOSS total Desulfurized gypsum 34.35 1.56 1.78 1.15 2.24 0.12 0.15 41.56 17.06 99.97 High sulfur bauxite 2.42 20.35 44.18 12.86 0.09 0.65 0.21 11.37 7.82 99.95 fly ash 1.48 43.50 35.38 1.92 0.70 1.18 0.33 0.68 14.77 99.94 Raw material 27.16 8.00 10.37 2.69 1.82 0.29 0.18 33.81 15.69 100.00

[0102] The above-mentioned dihydrate desulfurization gypsum, high-sulfur and low-grade b...

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Abstract

The invention relates to a method for preparing Belitt sulfoaluminate cement co-producing sulfuric acid. Gas sulfur and high-sulfur bauxite are used as reducing agents to synergistically reduce and dehydrate gypsum to prepare Belitt sulfoaluminate cement. Obtain high concentrations of gas-phase SO 2 The flue gas is used for the subsequent co-production of flue gas to produce sulfuric acid. Compared with the prior art, the present invention can not only obtain a high decomposition rate of gypsum in the cement raw meal, completely use the CaO decomposed by gypsum to replace the CaO in the limestone, but also can use the calcium oxide which is difficult to be directly affected by alumina, refractory, building materials and cement industries at present. The high-sulfur bauxite used is used as raw material, in which Al 2 O 3 As an aluminum raw material in cement, iron sulfide is used as an auxiliary reducing agent for iron raw material and gypsum decomposition, and by further supplementing the reducing agent sulfur gas, the decomposition reaction of gypsum can be carried out quickly and efficiently, and a high concentration of gas-phase SO can be obtained. 2 The flue gas provides the best process conditions for the subsequent co-production of sulfuric acid.

Description

technical field [0001] The invention relates to building materials and chemical products, in particular to a method for co-producing sulfuric acid by co-reducing gypsum-containing raw meal with sulfur gas and high-sulfur bauxite to prepare Belite sulfoaluminate cement. Background technique [0002] Sulfoaluminate cement has the advantages of low alkalinity, high early strength, micro-expansion, good corrosion resistance and frost resistance, and is especially suitable for coastal and cold areas and emergency repair projects. Traditional sulfoaluminate cement is made of calcium sulfoaluminate by sintering at high temperature (1200-1350 ℃) using limestone, bauxite and gypsum as raw materials. Dicalcium Silicate (C 2 S) is the main mineral phase composition, and then a small amount of gypsum is added and ground to obtain a sulfoaluminate cement product. Compared with ordinary Portland cement, due to the reduction in the amount of raw limestone and the sintering temperature o...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C04B7/32C04B7/44C01B17/50C01B17/74
CPCC04B7/32C04B7/44C04B7/4407C01B17/508C01B17/74Y02P20/10Y02P20/129
Inventor 庞仁杰赵博张国兴陈延信韩丁张志远
Owner 上海三夫工程技术有限公司
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