阅读说明：本技术 一种石膏制备生石灰过程中提炼二氧化硅的系统及方法 (System and method for refining silicon dioxide in process of preparing quicklime from gypsum ) 是由 张立强 王涛 周晓涵 李占尧 夏霄 成善杰 马春元 陈桂芳 于 2021-09-29 设计创作，主要内容包括：本发明公开了一种石膏制备生石灰过程中提炼二氧化硅的系统及方法,包括：依次连接的石膏预热器、还原煅烧炉和生石灰储仓,烟气换热器的烟气进口与还原煅烧炉的烟气出口连接；还原煅烧炉与还原气源连接,所述还原气源至少提供H-(2)和CO-(2)。石膏中的SiO-(2)与H-(2)在1000℃以上时发生反应生成气态SiO,SiO在1100℃以上时为气态,随高温烟气排出还原煅烧炉。当将含有H-(2)和CO-(2)的混合还原气与石膏混合还原煅烧时,既可以将石膏中的二氧化硅提炼出来,提高生石灰产品的纯度和反应活性,还可以促进CaSO-(4)定向分解为高活性CaO,进而得到高质量的生石灰产品。(The invention discloses a system and a method for refining silicon dioxide in a process of preparing quicklime from gypsum, wherein the method comprises the following steps: the flue gas inlet of the flue gas heat exchanger is connected with the flue gas outlet of the reduction calciner; the reduction calciner is connected with a reduction gas source, and the reduction gas source at least provides H 2 And CO 2 . SiO in gypsum 2 And H 2 The reaction is carried out at the temperature of more than 1000 ℃ to generate gaseous SiO, the SiO is gaseous at the temperature of more than 1100 ℃, and the gaseous SiO is discharged out of the reduction calciner along with high-temperature flue gas. When it will contain H 2 And CO 2 When the mixed reducing gas of (2) is mixed with gypsum for reduction and calcination, the dioxygen in the gypsum can be reducedSilicon is extracted to improve the purity and the reaction activity of the quicklime product and promote CaSO 4 The high-activity CaO is directionally decomposed, and then a high-quality quick lime product is obtained.)

1. The utility model provides a system for gypsum preparation quick lime in-process refines silica which characterized in that: the method comprises the following steps: the flue gas inlet of the flue gas heat exchanger is connected with the flue gas outlet of the reduction calciner;

the reduction calciner is connected with a reduction gas source, and the reduction gas source at least provides H₂And CO₂。

2. The system for refining silicon dioxide in the process of preparing quicklime from gypsum according to claim 1, is characterized in that: the flue gas outlet of the flue gas heat exchanger is connected with the gypsum preheater;

further, a flue gas outlet of the gypsum preheater is connected with the reduction calciner.

3. The system for refining silicon dioxide in the process of preparing quicklime from gypsum according to claim 1, is characterized in that: the device also comprises a silicon material storage bin, and the silicon material storage bin is connected with the solid phase outlet of the flue gas heat exchanger.

4. The system for refining silicon dioxide in the process of preparing quicklime from gypsum according to claim 3, is characterized in that: the quick lime slaker is connected with a quick lime storage bin, and the calcium silicate synthesizer is connected with a silicon material storage bin;

further, the calcium silicate synthesizer is connected with the reduction calciner.

5. The system for refining silicon dioxide in the process of preparing quicklime from gypsum according to claim 1, is characterized in that: the device also comprises a sulfur recovery device, and the sulfur recovery device is connected with a flue gas outlet of the flue gas heat exchanger.

6. A method for refining silicon dioxide in the process of preparing quicklime by gypsum is characterized by comprising the following steps: the method comprises the following steps:

and (3) carrying out reduction calcination on the preheated and dried gypsum and a reducing gas to prepare the quicklime, wherein the reducing gas comprises hydrogen and carbon dioxide.

7. The method for refining silicon dioxide in the process of preparing quicklime from gypsum according to claim 6, which is characterized in that: in the reducing gas, the volume fraction of hydrogen is 5-20%, and the volume fraction of carbon dioxide is 10-80%;

preferably, in the reducing gas, the volume fraction of the hydrogen is 8-18%, and the volume fraction of the carbon dioxide is 20-70%;

further, the reducing gas also comprises CH₄、C₂H₄、H₂S, natural gas and/or coal gas.

8. The method for refining silicon dioxide in the process of preparing quicklime from gypsum according to claim 6, which is characterized in that: the temperature of the gypsum after preheating and drying is 600-1000 ℃.

9. The method for refining silicon dioxide in the process of preparing quicklime from gypsum according to claim 6, which is characterized in that: the temperature of the reduction calcination is 1100-1200 ℃.

10. The method for refining silicon dioxide in the process of preparing quicklime from gypsum according to claim 6, which is characterized in that: the method also comprises the step of cooling the high-temperature flue gas generated by reduction and calcination to precipitate elemental silicon and silicon dioxide;

further, the temperature of the high-temperature flue gas after being cooled is lower than 1100 ℃.

Technical Field

The invention belongs to the technical field of solid waste resource utilization, and particularly relates to a system and a method for refining silicon dioxide in a process of preparing quicklime from gypsum.

Background

The statements herein merely provide background information related to the present disclosure and may not necessarily constitute prior art.

The quicklime is an inorganic material taking calcium oxide as a main component, and is widely applied to industries such as metallurgy, environmental protection, fine chemical industry, food and the like. The annual demand for quicklime in China is about 2.5 million tons, and the demand for high-quality, high-activity and high-calcium quicklime is about 1 million tons. In 2019, the yield of Chinese lime reaches 3 hundred million tons, which accounts for 70.75 percent of the total world yield. The traditional preparation method is that the calcium carbonate-rich material is calcined at 900-1100 ℃ by using blocky or powdery limestone, dolomite and other raw materials with high calcium carbonate content. The quicklime prepared by the method is in a block shape or a powder shape, and the active ingredient CaO in the quicklime has a poor pore structure and low activity. In addition, limestone and other natural resources are over-exploited, which causes serious damage to surface vegetation and ecological environment. And the process inevitably produces large amounts of CO₂And is not beneficial to carbon emission reduction in the lime industry.

Chinese gypsum resources are abundant, and the proven storage capacity is about 1000 hundred million tons. In addition, the quantity of industrial by-product gypsum in China is about 1.55 hundred million tons, wherein the yield of the phosphogypsum is about 0.55 hundred million tons, and the yield of the desulfurized gypsum is 1 hundred million tons. Its main components are CaSO₄·2H₂And O. The industrial byproduct gypsum has unstable property and low comprehensive utilization rate, and can cause secondary pollution to the environment after being stacked or buried for a long time. At present, it isThe utilization total amount of the byproduct gypsum in the ball industry is less, and 90 percent of the byproduct gypsum is low in low-end and low-added value utilization. The utilization rate of the phosphogypsum in the United states and Europe is generally lower than 10 percent, and most of the phosphogypsum is stockpiled. The current global phosphogypsum inventory is about 60 million tons, and the annual average new increment reaches 1.5 million tons. The utilization rate of the desulfurized gypsum is much larger than that of the phosphogypsum, the desulfurized gypsum is basically kept about 50 percent in Europe and China, and most of the desulfurized gypsum is used for basic building materials such as gypsum boards. Although the utilization rate of the phosphogypsum and the desulfurized gypsum in Japan reaches more than 90 percent (the Japan is seriously lack of natural gypsum sources), the usage amount is relatively small, and the phosphogypsum and the desulfurized gypsum are also in the low-end low-tech content fields of building materials and the like.

Furthermore, the inventors have found that the industrial by-product gypsum contains a certain amount of SiO₂Different gypsum SiO₂SiO of general industrial gypsum with different contents₂The content is 0.2-10%. SiO 2₂Stable property, not easy decomposition, and SiO in the process of preparing high-activity quicklime by using industrial by-product gypsum₂The content and activity of CaO in the final product can be influenced, thereby reducing the value of the quicklime product.

Disclosure of Invention

Aiming at the defects in the prior art, the invention aims to provide a system and a method for refining silicon dioxide in the process of preparing quicklime from gypsum.

In order to achieve the purpose, the invention is realized by the following technical scheme:

in a first aspect, the invention provides a system for refining silicon dioxide in a process of preparing quicklime from gypsum, which comprises: the flue gas inlet of the flue gas heat exchanger is connected with the flue gas outlet of the reduction calciner;

the reduction calciner is connected with a reduction gas source, and the reduction gas source at least provides H₂And CO₂。

SiO in gypsum in reduction calcining furnace₂And H₂The reaction is carried out at the temperature of more than 1000 ℃ to generate gaseous SiO, the SiO is gaseous at the temperature of more than 1100 ℃, and the gaseous SiO is discharged out of the reduction calciner along with high-temperature flue gas. When it will contain H₂And CO₂When the mixed reducing gas and the gypsum are mixed, reduced and calcined, the silicon dioxide in the gypsum can be extracted, the purity and the reaction activity of the quicklime product are improved, and the CaSO can be promoted₄The high-activity CaO is directionally decomposed, and then a high-quality quick lime product is obtained.

In some embodiments, the flue gas outlet of the flue gas heat exchanger is connected to a gypsum preheater. The gypsum is preheated by using the waste heat of the flue gas, so that the subsequent high-temperature reduction calcination is smoothly carried out.

Further, a flue gas outlet of the gypsum preheater is connected with the reduction calciner. For supplying carbon dioxide to the reduction calciner.

Furthermore, the device also comprises a silicon material storage bin, and the silicon material storage bin is connected with the solid phase outlet of the flue gas heat exchanger.

In the flue gas heat exchanger, when the temperature of high-temperature flue gas is reduced to below 1100 ℃, SiO is subjected to disproportionation reaction to generate solid simple substance silicon and silicon oxide, gas-solid separation is carried out through a high-temperature gas-solid separator, and the mixture of the simple substance silicon and the silicon oxide is separated from the high-temperature flue gas and stored in a silicon material storage bin.

Furthermore, the silicon-based silicon carbide ceramic material sintering device further comprises a quicklime slaker and a calcium silicate synthesizer which are connected with each other, wherein the quicklime slaker is connected with a quicklime storage bin, and the calcium silicate synthesizer is connected with a silicon material storage bin.

Further, the calcium silicate synthesizer is connected with the reduction calciner.

The slaked lime solution obtained by slaking the quicklime is conveyed to a calcium silicate synthesizer, and reacts with the mixture of the simple substance silicon and the silicon oxide in the silicon material storage bin in the calcium silicate synthesizer to prepare the calcium silicate, so that the silicon dioxide is extracted from the industrial byproduct gypsum, and the resource utilization of the silicon is realized. In addition, calcium silicate formation produces a certain amount of H₂The moiety H₂Can be conveyed to a reduction calciner to be recycled as reducing gas or fuel.

Further, the device also comprises a sulfur recovery device, and the sulfur recovery device is connected with a flue gas outlet of the flue gas heat exchanger. The method is used for recovering sulfur in the high-concentration sulfur dioxide in the flue gas.

In a second aspect, the invention provides a method for refining silicon dioxide in a process of preparing quicklime from gypsum, which comprises the following steps:

and (3) carrying out reduction calcination on the preheated and dried gypsum and a reducing gas to prepare the quicklime, wherein the reducing gas comprises hydrogen and carbon dioxide.

In some embodiments, the volume fraction of hydrogen in the reducing gas is 5-20% and the volume fraction of carbon dioxide is 10-80%.

Preferably, the volume fraction of hydrogen in the reducing gas is 8-18% and the volume fraction of carbon dioxide is 20-70%.

Further, the reducing gas also comprises CH₄、C₂H₄、H₂S, natural gas and/or coal gas.

In some embodiments, the temperature of the pre-heated dried gypsum is 600-.

In some embodiments, the temperature of the reduction calcination is 1100-1200 ℃.

In some embodiments, the method further comprises a step of cooling the high-temperature flue gas generated by the reduction calcination to precipitate the elemental silicon and the silicon dioxide.

Further, the temperature of the high-temperature flue gas after being cooled is lower than 1100 ℃.

The above one or more embodiments of the invention achieve the following advantageous effects:

the method for preparing the quicklime and the sulfur-containing product by reducing and decomposing the gypsum by using the hydrogen-containing reducing gas provides a brand new quicklime preparation process, and can reduce CO in the quicklime production process₂The discharge amount has important significance for carbon emission reduction and carbon neutralization.

The quicklime and the sulfur-containing products are prepared from the industrial byproduct gypsum, so that the problem that the industrial byproduct gypsum is difficult to treat is solved, the high-value recycling of industrial solid waste is realized, the added value of the process is higher, and the economy is better.

Method for producing quicklime by reducing and decomposing gypsum by using hydrogen-containing reducing agent to cooperate with SiO in gypsum₂Refining and reducing the impurity SiO in the quicklime product₂Content of (A) to (B)The content of the active ingredient CaO is high, so that the CaO content is more than or equal to 90 percent, and the grade of the high-class product in the quicklime product is achieved.

Part of SiO in gypsum₂Reacting with active calcium oxide at high temperature to generate calcium silicate, reducing the reactivity of quicklime product, and preparing SiO with the quicklime₂The calcium silicate is reduced to a great extent by extraction, and the reactivity of the quicklime product is improved.

Reducing gypsum to prepare quicklime and simultaneously reducing impurity SiO in the quicklime₂And (3) refining and obtaining a calcium silicate product through alkaline washing, wherein the calcium silicate product can be used as a raw material for firing cement clinker, and the recovery and utilization of silicon resources in industrial byproduct gypsum are realized.

The process not only provides a sustainable pollution-free treatment mode for the industrial byproduct gypsum which is difficult to treat at present, but also realizes the resource utilization of the gypsum to produce high-quality quicklime, sulfur-containing byproducts and calcium silicate. The preparation of the quicklime is realized by utilizing industrial solid wastes, the exploitation of limestone is reduced, and the ecological environment is protected. The sulfur-containing byproduct can relieve the current situation of shortage of sulfur resources in China and reduce the external dependence of the sulfur resources. The calcium silicate is used as a preparation raw material and an additive of the cement clinker, and also has good utilization value. In addition, the method for preparing the quicklime by reducing and decomposing the industrial byproduct gypsum by using the hydrogen-containing reducing gas can effectively reduce CO in the quicklime production process₂The emission amount has great significance for carbon emission reduction and carbon neutralization in the industrial process.

Drawings

The accompanying drawings, which are incorporated in and constitute a part of this specification, are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate exemplary embodiments of the invention and together with the description serve to explain the invention and not to limit the invention.

Fig. 1 is a schematic view of the overall structure of a system for refining silica in a process of manufacturing quicklime from gypsum according to one or more embodiments of the present invention.

The system comprises a gypsum preheater 1, a reduction calciner 2, a quick lime storage bin 3, a quick lime slaker 4, a flue gas heat exchanger 5, a silicon material storage bin 6, a calcium silicate synthesizer 7, a calcium silicate storage bin 8, a sulfur recovery device 9 and a flue gas purification device 10.

Detailed Description

It is to be understood that the following detailed description is exemplary and is intended to provide further explanation of the invention as claimed. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs.

The invention is further described with reference to the following figures and specific examples.

The research shows that the effective components of various plasters are CaSO₄，CaSO₄Can react with H within the temperature range of 700-1200 DEG C₂The reaction takes place to yield CaO and CaS, as shown in equations (1) and (2). By adding a certain proportion (10-80%) of CO₂Thereafter, CaSO may be added₄The calcium oxide is directionally decomposed into high-activity CaO, thereby realizing the conversion of the gypsum to the quicklime. SiO 2₂Can react with coke at more than 1900 ℃, but reacts with H₂Can react to generate SiO and H at the temperature of over 1000 DEG C₂O, as shown in equation (3). Wherein SiO is gaseous above 1100 deg.C and has stable properties. When the temperature is reduced to below 1100 ℃, disproportionation reaction of SiO occurs to generate simple substance silicon and silicon dioxide. Elemental silicon and silica can be reacted with alkali to produce silicates, where water is added to the quicklime to produce calcium silicate, as shown in equations (4) and (5). The calcium silicate can be used as a raw material for preparing cement clinker, and H can be generated while the simple substance silicon reacts with alkali to generate silicate₂The hydrogen can be returned to the process of preparing the quicklime by reducing and decomposing the gypsum to be used as a reducing agent or fuel.

CaSO₄+CO/H₂→CaO+CO₂/H₂O+SO₂ (1)

CaSO₄+4CO/H₂→CaS+4CO₂/H₂O (2)

SiO₂+H₂→SiO+H₂O (3)

Si+CaO+2H₂O→CaSiO₃+2H₂ (4)

SiO₂+CaO+H₂O→CaSiO₃+H₂O (5)

CaSO as main ingredient of gypsum (natural gypsum or industrial by-product gypsum)₄In addition, according to the different types of the gypsum, 0.2 to 10 percent of SiO is contained₂. After reduction and calcination by hydrogen-containing reducing gas, by precisely controlling the reaction conditions, CaSO₄The decomposition rate and CaO yield of (2) are close to 100%. The content of CaO in the product quicklime is higher than 90 percent, and the product reaches the high-class product standard of the quicklime product standard.

As shown in figure 1, SiO is extracted in the process of preparing quicklime from gypsum₂The system comprises a gypsum preheater 1, a reduction calciner 2 and a quicklime storage bin 3 which are connected in sequence, wherein a flue gas inlet of a flue gas heat exchanger 5 is connected with a flue gas outlet of the reduction calciner 2; the reduction calciner 2 is connected with a reduction gas source.

The flue gas outlet of the flue gas heat exchanger 5 is connected with the gypsum preheater 1, the flue gas outlet of the gypsum preheater 1 is connected with the reduction calciner 2, the silicon material storage bin 6 is connected with the solid phase outlet of the flue gas heat exchanger 5, the quick lime slaker 4 is connected with the quick lime storage bin 3, the calcium silicate synthesizer 7 is connected with the silicon material storage bin 8, the calcium silicate synthesizer 8 is connected with the reduction calciner 2, and the sulfur recovery device 9 is connected with the flue gas outlet of the flue gas heat exchanger 5.

The gypsum preheater 1 can be a multi-stage cyclone separator, a shell-and-tube heat exchanger, a plate-and-shell heat exchanger, a plate-and-tube heat exchanger and other gas-solid heat exchangers in various forms.

The sulfur recovery device 9 can be a device for preparing concentrated sulfuric acid from sulfur-containing flue gas, a device for preparing dilute sulfuric acid from sulfur-containing flue gas, and a device for preparing liquid SO from sulfur-containing flue gas₂The device and the device for preparing sulfur by using sulfur-containing flue gas and other various sulfur-containing byproduct recovery devices.

The calcium silicate synthesizer 7 can be in various forms such as a moving bed, a rotary kiln, a fixed bed, a turbulent bed, a bubbling bed, a micro fluidized bed, a spouted bed and the like.

The used feeder can be a screw feeder, an air-locking feeder and other various feeding forms.

A high-temperature gas-solid separator can be arranged between the flue gas heat exchanger and the silicon material storage bin, and can be a high-temperature cyclone separator, a high-temperature axial flow separator and other separators in various forms.

The flue gas purification device 10 can be a wet flue gas desulfurization system, a semi-dry flue gas desulfurization system, a dry flue gas desulfurization system, an active coke, a molecular sieve and other flue gas purification devices;

the reduction calciner 2 can be in various forms such as a moving bed, a rotary kiln, a fixed bed, a turbulent bed, a bubbling bed, a micro-fluidized bed, a spouted bed and the like.

The flue gas heat exchanger can be a heat exchanger in various forms such as a multi-stage cyclone separator, a shell-and-tube heat exchanger, a plate-and-shell heat exchanger, a plate heat exchanger and the like, and also comprises a heat exchanger made of various materials such as stainless steel, silicon carbide and the like.

The gas conveying process is provided with conveying power by an induced draft fan or a blower.

Example 1

The process method specifically comprises the following steps:

the gypsum is stored in a gypsum storage bin, the feeding amount is accurately controlled by a feeding machine and is conveyed to a gypsum preheater for preheating and drying, and a high-temperature heat source is from the heated circulating flue gas; the preheated and dried gypsum is at the temperature of 900-950 ℃, firstly enters a reduction calciner, the reaction temperature of 1100-1150 ℃ and the volume ratio of hydrogen-containing reduction gas to circulating flue gas are controlled in the reduction calciner, so that the volume fraction of hydrogen in the gas is 30-35 percent, the volume fraction of carbon dioxide is 30-40 percent, and the relatively high temperature and low reduction potential can be obtainedUnder reaction conditions such that CaSO₄And decomposing the calcium oxide into CaO completely to obtain high-purity quicklime.

SiO in gypsum in reduction calcining furnace₂And H₂Reacting at a temperature of over 1000 ℃ to generate gaseous SiO, discharging the SiO at a temperature of over 1100 ℃ out of the reduction calciner along with high-temperature flue gas, feeding the high-temperature flue gas discharged from the reduction calciner into a high-temperature gas-solid separator, and passing quicklime through the high-temperature gas-solid separatorThe high-temperature gas-solid separator is separated, cooled and stored in a quicklime storage bin. The high-temperature flue gas discharged by the high-temperature gas-solid separator firstly enters a flue gas heat exchanger at the temperature of about 1100-1200 ℃ to preheat the circulating flue gas. The cooled high-temperature flue gas enters a high-temperature gas-solid separator at the temperature of about 600-700 ℃. In the flue gas heat exchanger, when the temperature of high-temperature flue gas is reduced to below 1100 ℃, SiO is subjected to disproportionation reaction to generate solid simple substance silicon and silicon oxide, gas-solid separation is carried out through a high-temperature gas-solid separator, and the mixture of the simple substance silicon and the silicon oxide is separated from the high-temperature flue gas and stored in a silicon material storage bin.

The high-temperature flue gas from the high-temperature gas-solid separator contains high-concentration SO₂Producing sulfur, sulfuric acid and liquid SO according to the requirement by a sulfur recovery device₂Thereby realizing the recovery of sulfur resources from the industrial byproduct gypsum.

And (3) circulating a part of the high-temperature flue gas recovered by sulfur back to the flue gas heat exchanger, preheating to 800-. And the other part of the high-temperature flue gas after sulfur recovery is purified by a flue gas purification device and then is emptied.

The quicklime stored in the quicklime storage bin can be directly utilized as a high-value product, and the calcium resource recovery from the industrial byproduct gypsum is realized. Or partially feeding into quicklime slaker to react with water to prepare slaked lime solution (Ca (OH)₂Solution), the slaked lime solution is conveyed to a calcium silicate synthesizer, the slaked lime solution reacts with the mixture of the simple substance silicon and the silicon oxide in the silicon material storage bin in the calcium silicate synthesizer to prepare calcium silicate, the obtained calcium silicate is stored in the calcium silicate storage bin, and thus the purpose of extracting SiO from industrial byproduct gypsum is realized₂And realizes the resource utilization of silicon. A certain amount of H is generated in the formation process of calcium silicate₂The moiety H₂Can be conveyed to a reduction calciner to be recycled as reducing gas or fuel.

The gypsum has the grain diameter of 60 mu m-3mm and the water content of 5-20 percent and can be calcium sulfate products such as wet desulphurization gypsum, semi-dry desulphurization ash, phosphogypsum, natural gypsum, titanium gypsum, fluorgypsum and the like.

The parameters of the high-temperature flue gas are as follows: SO (SO)₂％＝2-10％，CO％＝2-20％，H₂2-20% of SiO 2-20%, 1100-1200 deg.C of temp., and SO as main component₂、CO、N₂、H₂、SiO、CO₂And H₂O, and the like.

Hydrogen-containing reducing gas, main component H₂、CH₄、C₂H₄、H₂The contents of S, natural gas, coal gas and the like can be the combination of a plurality of or all the components according to the difference of the reducing gas sources.

Circulating flue gas with main component N₂、CO、H₂、H₂O、CO₂Etc. CO₂％＝5％-80％，H₂O％＝5％-50％。

The CaO content in the quicklime CaO-1 prepared by using the industrial byproduct gypsum is more than 90 percent, and the grade of a high-class product in the quicklime product standard is reached.

Example 2

The differences from example 1 are:

the temperature of the preheated and dried gypsum is 700-750 ℃, the gypsum firstly enters a reduction calcining furnace, the reaction temperature is 1150-1200 ℃ and the ratio of hydrogen-containing reduction gas to the amount of circulating flue gas in the reduction calcining furnace are controlled, so that the volume fraction of hydrogen in the gas is 20-25%, and the volume fraction of carbon dioxide is 50-60%.

The CaO content of the quicklime CaO-2 prepared by using the industrial byproduct gypsum is more than 90 percent, and the grade of a high-class product in the quicklime product standard is reached. Further, the data on the porosities of the quicklime prepared in example 1 and example 2 are shown in table 1.

Comparative example

The lump limestone is calcined at 1000 ℃ for 2 hours to prepare CaO-3, and the porosity related data is shown in Table 1.

In Table 1, BET is the specific surface area, Volume is the void Volume, and Average Pore Size is the Average Pore Size, and it can be seen that the quicklime prepared in examples 1 and 2 has a better Pore structure.

TABLE 1

The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.