CN105664841A - Hydration-calcination modification method of high temperature CO2 adsorption material Li4SiO4 - Google Patents
Hydration-calcination modification method of high temperature CO2 adsorption material Li4SiO4 Download PDFInfo
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- 238000001354 calcination Methods 0.000 title claims abstract description 32
- 239000000463 material Substances 0.000 title claims abstract description 21
- 238000001179 sorption measurement Methods 0.000 title abstract description 19
- 238000002715 modification method Methods 0.000 title abstract description 5
- PAZHGORSDKKUPI-UHFFFAOYSA-N lithium metasilicate Chemical compound [Li+].[Li+].[O-][Si]([O-])=O PAZHGORSDKKUPI-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229910052912 lithium silicate Inorganic materials 0.000 claims abstract description 26
- 238000000034 method Methods 0.000 claims abstract description 22
- 239000000843 powder Substances 0.000 claims abstract description 16
- 238000010521 absorption reaction Methods 0.000 claims abstract description 14
- 230000036571 hydration Effects 0.000 claims abstract description 10
- 238000006703 hydration reaction Methods 0.000 claims abstract description 10
- 238000010532 solid phase synthesis reaction Methods 0.000 claims abstract description 10
- 230000004087 circulation Effects 0.000 claims abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- 238000003795 desorption Methods 0.000 claims description 4
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 claims description 3
- 229910052808 lithium carbonate Inorganic materials 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 235000012239 silicon dioxide Nutrition 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 2
- 229910052909 inorganic silicate Inorganic materials 0.000 claims 7
- 238000006243 chemical reaction Methods 0.000 claims 1
- 238000003837 high-temperature calcination Methods 0.000 claims 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 32
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 16
- 238000012986 modification Methods 0.000 abstract description 15
- 230000004048 modification Effects 0.000 abstract description 15
- 239000003463 adsorbent Substances 0.000 abstract description 9
- 239000002245 particle Substances 0.000 abstract description 8
- 239000001569 carbon dioxide Substances 0.000 abstract description 5
- 239000011148 porous material Substances 0.000 abstract description 2
- 230000002238 attenuated effect Effects 0.000 abstract 1
- 125000004122 cyclic group Chemical group 0.000 abstract 1
- 229910004283 SiO 4 Inorganic materials 0.000 description 7
- 230000000694 effects Effects 0.000 description 3
- 239000002803 fossil fuel Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000003980 solgel method Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 239000010431 corundum Substances 0.000 description 1
- 238000000635 electron micrograph Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000002336 sorption--desorption measurement Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
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- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
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Abstract
Description
技术领域technical field
本发明属于材料技术领域,具体涉及一种用于吸收高温二氧化碳的硅酸锂材料的改性制备方法,该材料可用于吸收化石燃料电厂、水泥窖等烟道中排放的二氧化碳。The invention belongs to the technical field of materials, and in particular relates to a modified preparation method of a lithium silicate material used for absorbing high-temperature carbon dioxide. The material can be used for absorbing carbon dioxide discharged from flues of fossil fuel power plants and cement pits.
背景技术Background technique
随着现代工业的迅猛发展,化石能源消耗量逐年递增,其利用过程中排放的大量CO2造成了严重的温室效应。化石燃料电厂是CO2的主要排放来源,且其高温炉中排放的CO2温度较高,高温烟气循环脱除方法可以避免CO2分离之前的降温处理,减少CO2捕集分离过程中的能量损失,实现节能减排的需求。因而合成高温下能够可逆吸收CO2的优良材料,对减少化石燃料电厂燃烧过程中CO2气体的排放,具有重要的理论意义和实际应用价值。硅酸锂材料被认为是用于高温吸附CO2的最好材料之一,它具有较高的吸收容量,在高温下具有良好的可循环性,为减少从高温炉中排放的CO2提供了新途径。With the rapid development of modern industry, the consumption of fossil energy is increasing year by year, and a large amount of CO 2 emitted during its utilization has caused a serious greenhouse effect. Fossil fuel power plants are the main source of CO 2 emissions, and the CO 2 emitted from the high-temperature furnace has a high temperature. The high-temperature flue gas circulation removal method can avoid the cooling treatment before CO 2 separation and reduce the CO 2 capture and separation process. Energy loss, the need to achieve energy saving and emission reduction. Therefore, the synthesis of excellent materials capable of reversibly absorbing CO 2 at high temperatures has important theoretical significance and practical application value for reducing CO 2 gas emissions in the combustion process of fossil fuel power plants. Lithium silicate material is considered to be one of the best materials for CO2 adsorption at high temperature, it has high absorption capacity, good recyclability at high temperature, and provides great potential for reducing CO2 emissions from high temperature furnaces new way.
Li4SiO4吸附剂的制备方法主要包括高温固体合成法、溶胶-凝胶法以及沉淀法等。近年来,各国研究者结果表明减小颗粒尺寸、增大颗粒比表面积、提高材料活性,能有效提高Li4SiO4材料的吸附性能。尽管溶胶-凝胶法所合成的样品颗粒较细,相较于固相法而言,其制备成本高,合成时间长。The preparation methods of Li 4 SiO 4 adsorbent mainly include high temperature solid synthesis method, sol-gel method and precipitation method. In recent years, researchers from various countries have shown that reducing particle size, increasing particle specific surface area, and improving material activity can effectively improve the adsorption performance of Li 4 SiO 4 materials. Although the sample particles synthesized by the sol-gel method are finer, compared with the solid-phase method, its preparation cost is high and the synthesis time is long.
发明内容Contents of the invention
本发明的目的在于提供一种高温CO2吸附材料Li4SiO4的水合-煅烧改性方法,改性成本低廉且改性后对CO2的吸附效果好。The object of the present invention is to provide a hydration-calcination modification method of Li 4 SiO 4 , a high-temperature CO 2 adsorption material, which has low modification cost and good CO 2 adsorption effect after modification.
本发明的技术方案是:一种高温CO2吸附材料Li4SiO4的水合-煅烧法改性方法,对固相法合成硅酸锂粉末采用水合-煅烧方法进行改性,水合温度为80~100℃,煅烧温度为700℃~900℃,煅烧时间为2h~6h,所述吸附材料平均粒径小于50微米,吸收容量大于25%,经15次循环后吸收容量无明显衰减。The technical solution of the present invention is: a hydration-calcination method modification method for high - temperature CO2 adsorption material Li4SiO4 , the lithium silicate powder synthesized by solid-phase method is modified by hydration-calcination method, and the hydration temperature is 80~ 100°C, the calcination temperature is 700°C-900°C, the calcination time is 2h-6h, the average particle size of the adsorption material is less than 50 microns, the absorption capacity is greater than 25%, and the absorption capacity has no obvious attenuation after 15 cycles.
所述的固相法合成硅酸锂粉末的具体方法为:碳酸锂和二氧化硅混合均匀酒精研磨干燥后再高温煅烧得到硅酸锂粉末。The specific method for synthesizing lithium silicate powder by the solid-phase method is as follows: lithium carbonate and silicon dioxide are uniformly mixed, ground and dried with alcohol, and then calcined at high temperature to obtain lithium silicate powder.
所述的水合-煅烧方法具体为:将固相法合成硅酸锂粉末加入水中,水浴不断搅拌下反应充分后,烘干,再煅烧。The hydration-calcination method specifically includes: adding lithium silicate powder synthesized by solid-phase method into water, fully reacting under constant stirring in a water bath, drying, and then calcining.
水合过程中,保持水量不变。During hydration, keep the water volume constant.
所述的Li4SiO4高温CO2吸附剂的水合-煅烧法改性方法得到的Li4SiO4高温CO2吸附剂,对固相法合成硅酸锂采用水合-煅烧方法进行改性,水合温度为80~100℃,煅烧温度为700℃~900℃,煅烧时间为2h~6h,所述吸附剂平均粒径小于50微米,吸收容量大于25%,经15次循环吸附解吸循环后吸收容量无明显衰减。The Li 4 SiO 4 high-temperature CO 2 adsorbent obtained by the hydration-calcination method modification method of the Li 4 SiO 4 high-temperature CO 2 adsorbent is modified by the hydration-calcination method for the solid-phase synthesis of lithium silicate, and the hydration The temperature is 80-100°C, the calcination temperature is 700-900°C, and the calcination time is 2h-6h. The average particle size of the adsorbent is less than 50 microns, and the absorption capacity is greater than 25%. After 15 cycles of adsorption and desorption cycles, the absorption capacity No significant attenuation.
有益效果:Beneficial effect:
(1)吸附剂采用水合改性,方法简单,价格低廉。水合过程中需不断搅拌,且避免水分蒸发。(1) The adsorbent is modified by hydration, the method is simple and the price is low. Constant stirring is required during the hydration process, and water evaporation should be avoided.
(2)改性后的吸附剂孔隙结构更加丰富,具有较高的二氧化碳吸附速度和较大的吸附量。可以对水泥窑,玻璃厂等尾气烟道中排放的大量高温二氧化碳进行直接吸收。(2) The modified adsorbent has richer pore structure, higher carbon dioxide adsorption rate and larger adsorption capacity. It can directly absorb a large amount of high-temperature carbon dioxide emitted from the exhaust flue of cement kilns and glass factories.
(3)循环使用性能良好,经15次循环吸附/解吸循环后仍具有较好的吸附性能。(3) The recycling performance is good, and it still has good adsorption performance after 15 cycles of adsorption/desorption cycles.
附图说明Description of drawings
图1.实施例1中,改性前后硅酸锂样品吸附CO2热重曲线。Fig. 1. In embodiment 1, lithium silicate sample adsorption CO 2 thermogravimetric curves before and after modification.
图2.实施例1中,改性前后硅酸锂样品吸收/解吸循环性能。Figure 2. In Example 1, the absorption/desorption cycle performance of lithium silicate samples before and after modification.
图3.实施例1中,改性前后的硅酸锂样品电子显微图。Fig. 3. In embodiment 1, the electron micrograph of lithium silicate sample before and after modification.
具体实施方式detailed description
实施例1Example 1
将摩尔比为2:1的碳酸锂和二氧化硅混合均匀,加入适量酒精研磨混合,然后进行干燥。在800℃下将混合后粉末放入马弗炉中进行煅烧4小时得到硅酸锂粉末。将制得的硅酸锂粉末(1-2g)放入500ml盛满水的烧杯中,而后将烧杯置于80℃的水浴锅中不断搅拌,8h后取出,于105℃下烘干。将烘干后的粉状物再次放入马弗炉中,800℃下煅烧4h,得到硅酸锂粉末。Mix lithium carbonate and silicon dioxide with a molar ratio of 2:1 evenly, add an appropriate amount of alcohol to grind and mix, and then dry. The mixed powder was put into a muffle furnace for calcination at 800° C. for 4 hours to obtain lithium silicate powder. Put the prepared lithium silicate powder (1-2g) into a 500ml beaker filled with water, then place the beaker in a water bath at 80°C and stir continuously, take it out after 8 hours, and dry it at 105°C. The dried powder was put into the muffle furnace again, and calcined at 800° C. for 4 hours to obtain lithium silicate powder.
将改性前后的硅酸锂粉末放入热重分析仪,在99.999%N2气氛中,以10K/min的升温速率升温至680℃,而后切换至99.999%CO2气氛中,在680℃下恒温2h进行CO2吸收反应,所得热重曲线如附图1所示,改性前后的硅酸锂样品最大吸附量分别为23.8%、30.3%。Put the lithium silicate powder before and after modification into the thermogravimetric analyzer, in the 99.999% N2 atmosphere, raise the temperature to 680°C at a rate of 10K/min, and then switch to the 99.999% CO2 atmosphere, at 680°C The CO2 absorption reaction was carried out at a constant temperature for 2 hours, and the obtained thermogravimetric curve is shown in Figure 1. The maximum adsorption capacity of the lithium silicate samples before and after modification was 23.8% and 30.3%, respectively.
将改性前后的硅酸锂粉末在双温区管式炉中,进行多次循环吸附测试,测试方法如下:吸收和解吸循环试验过程中,分别通入CO2和N2,流量均为1.0L/min,所对应炉膛温度分为设定为680℃、800℃。测试过程中将样品称重并均匀铺在刚玉方舟内形成薄层,在680℃碳酸化炉内反应30min后,称重,然后进入煅烧炉内煅烧10min,如此反复进行试验。经过15次循环,CO2的吸收量如图2所示。改性后W-Li4SiO4、改性前S-Li4SiO4样品吸收率分别维持在27%、11%左右,样品中的吸收容量没有出现明显衰减。The lithium silicate powder before and after modification was tested in a dual-temperature zone tube furnace for multiple cycle adsorption tests. The test method was as follows: during the cycle test of absorption and desorption, CO 2 and N 2 were introduced respectively, and the flow rate was 1.0 L/min, the corresponding furnace temperature is divided into 680°C and 800°C. During the test, the samples were weighed and evenly spread in the corundum ark to form a thin layer. After reacting in the carbonation furnace at 680°C for 30 minutes, weighed, and then entered the calciner for 10 minutes of calcination, and the test was repeated in this way. After 15 cycles, the CO2 uptake is shown in Fig. 2. The absorption rates of W-Li 4 SiO 4 after modification and S-Li 4 SiO 4 before modification were maintained at about 27% and 11%, respectively, and the absorption capacity of the samples did not decay significantly.
采用扫描电子显微镜,对改性前后的硅酸锂粉末进行观察,如附图3所示,其中(a)为改性前(b)为改性后SEM图,由图可见采用水合-煅烧改性后,颗粒的平均粒径由原来的200μm减小到50μm。Using a scanning electron microscope, the lithium silicate powder before and after modification is observed, as shown in Figure 3, wherein (a) is before modification and (b) is the SEM image after modification. It can be seen from the figure that hydration-calcination modification After curing, the average particle size of the particles is reduced from 200 μm to 50 μm.
实施例2Example 2
参考实例1进行水合-煅烧制备硅酸锂吸附剂,并在相同条件下进行CO2吸附测试,所不同的是,水合温度为100℃,水合时间为4h,得到CO2吸收容量为29.7%。Reference Example 1 was hydrated and calcined to prepare a lithium silicate adsorbent, and the CO2 adsorption test was carried out under the same conditions, except that the hydration temperature was 100°C and the hydration time was 4h, and the CO2 absorption capacity was 29.7%.
实施例3Example 3
参考实例1进行水合-煅烧制备硅酸锂吸附剂,并在相同条件下进行CO2吸附测试,所不同的是,煅烧时间为2h、6h,得到CO2吸收容量为32.3%、25.5%。Reference Example 1 was hydrated-calcined to prepare a lithium silicate adsorbent, and the CO2 adsorption test was carried out under the same conditions. The difference was that the calcination time was 2h and 6h, and the CO2 absorption capacity was 32.3% and 25.5%.
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