CN110156075B - 一种用烧结烟气脱硫灰低温制备CaZrO3粉体的方法 - Google Patents
一种用烧结烟气脱硫灰低温制备CaZrO3粉体的方法 Download PDFInfo
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- 239000003546 flue gas Substances 0.000 title claims abstract description 31
- 239000000843 powder Substances 0.000 title claims abstract description 30
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 29
- 230000023556 desulfurization Effects 0.000 title claims abstract description 29
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 238000005245 sintering Methods 0.000 claims abstract description 24
- 229910002976 CaZrO3 Inorganic materials 0.000 claims abstract description 15
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 8
- -1 alkali metal salt Chemical class 0.000 claims abstract description 7
- 238000001354 calcination Methods 0.000 claims abstract description 7
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- 239000000203 mixture Substances 0.000 claims description 13
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical group [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 11
- 229910052593 corundum Inorganic materials 0.000 claims description 10
- 239000010431 corundum Substances 0.000 claims description 10
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 5
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 4
- 150000002500 ions Chemical class 0.000 claims description 4
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 claims description 4
- 239000011812 mixed powder Substances 0.000 claims description 4
- 150000001340 alkali metals Chemical class 0.000 claims description 3
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 3
- 239000007832 Na2SO4 Substances 0.000 claims description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 2
- INHCSSUBVCNVSK-UHFFFAOYSA-L lithium sulfate Inorganic materials [Li+].[Li+].[O-]S([O-])(=O)=O INHCSSUBVCNVSK-UHFFFAOYSA-L 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 229910052939 potassium sulfate Inorganic materials 0.000 claims description 2
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 claims description 2
- 238000004321 preservation Methods 0.000 claims description 2
- 239000011780 sodium chloride Substances 0.000 claims description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 24
- 230000015572 biosynthetic process Effects 0.000 abstract description 5
- 238000003786 synthesis reaction Methods 0.000 abstract description 4
- 238000010532 solid phase synthesis reaction Methods 0.000 abstract description 3
- 239000002910 solid waste Substances 0.000 abstract description 3
- 239000007769 metal material Substances 0.000 abstract description 2
- 239000002956 ash Substances 0.000 description 20
- 239000000047 product Substances 0.000 description 20
- 238000006243 chemical reaction Methods 0.000 description 10
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 239000002994 raw material Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 6
- 238000005406 washing Methods 0.000 description 4
- 230000007547 defect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
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- 239000002245 particle Substances 0.000 description 3
- 238000002441 X-ray diffraction Methods 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L calcium carbonate Substances [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910014813 CaC2 Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
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- 238000005260 corrosion Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000000713 high-energy ball milling Methods 0.000 description 1
- 238000003837 high-temperature calcination Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
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- 238000012986 modification Methods 0.000 description 1
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Abstract
本发明提供一种用烧结烟气脱硫灰低温制备CaZrO3粉体的方法,属于工业固废综合利用与无机非金属材料制备技术领域。本发明具体包括如下步骤:将烧结烟气脱硫灰、ZrO2和含有碳酸盐在内的碱金属盐粉体混合加热至850℃以上煅烧,所得产物用水浸泡,经过滤、清洗、干燥后即得到CaZrO3粉体。本发明以廉价的烧结烟气脱硫灰为Ca源,合成温度较传统固相法有显著降低,且所得产品粒径较小。该发明方法工艺简单、成本低,可实现烧结烟气脱硫灰的高附加值利用,具有显著的社会经济效益。
Description
技术领域
本发明属于工业固废综合利用与无机非金属材料制备技术领域,具体涉及一种用烧结烟气脱硫灰低温制备CaZrO3粉体的方法,
背景技术
烧结烟气脱硫技术的成熟与发展,有效解决了烟气污染问题,但随之产生了大量的脱硫灰,造成了新的固废污染。目前,脱硫灰处理技术还不够成熟,大多只能堆存处理,不仅占用了大量宝贵的土地资源,还可能会对环境造成二次污染。现有脱硫灰的开发利用主要集中在水泥、墙体填充材料、土壤改性等方面,产品附加值相对较低。
钙钛矿型CaZrO3的熔点高达2345℃,其热膨胀系数小、机械强度高、化学性能稳定好,并且具有良好的高温质子导电性、抗水化性能、优良的抗热震性、较高的荷重软化温度、优异的抗硅酸盐水泥熟料的侵蚀等性能,是一种应用前景广泛的高温结构材料和高温功能材料。目前,CaZrO3粉体的制备方法主要有以下三种:(1)高温固相法:以含Ca物质(CaCO3、Ca(OH)2、CaC2O4等)与 ZrO2的混合粉体为原料进行高温煅烧;该法工艺简单,原料来源广泛,生产量大,后续处理问题小,但存在烧结温度高(≥1500℃)、产物均匀性差和活性度低等缺点。(2)机械力化学法:以CaO与ZrO2的混合粉体为原料,经高能球磨过程中产生的机械力给予反应物能量,促使化学反应发生;该法工艺简单,但存在反应产物纯度过低、反应不完全、反应时间长、产率低等缺点。(3)液相法:包括共沉淀法、水热法、溶胶凝胶法等;所制备的CaZrO3粉体纯度高、粒径小,但原料成本高且工艺复杂,最终还需要高温煅烧处理。从以上分析可知,寻求一种工艺、成本、性能兼顾的制备方法对于拓展CaZrO3材料的应用范围具有非常重要的意义。
发明内容
为克服现有技术的不足,本发明要解决的技术问题是提供一种用烧结烟气脱硫灰低温制备CaZrO3粉体的方法,以期原料成本低廉、制备工艺简单且制备温度较现有技术显著降低。
为解决上述技术问题,本发明是通过以下技术方案予以实现的。
本发明一种用烧结烟气脱硫灰低温制备CaZrO3粉体的方法,具体包括如下步骤:
(1)将烧结烟气脱硫灰、ZrO2和碱金属盐粉体混合;
所述烧结烟气脱硫灰中Ca元素和ZrO2的摩尔比为1:1;所述碱金属盐为 Na2CO3、K2CO3、Li2 CO3、NaCl、KCl、LiCl、Na2SO4、K2SO4、Li2SO4中的一种或多种,且至少含有一种碳酸盐,碱金属盐中CO3 2-离子和烧结烟气脱硫灰中S 元素的摩尔比为1~3:1。
(2)将步骤(1)得到的混合粉体放入刚玉坩埚中,加热煅烧后自然冷却;
所述煅烧温度为850℃以上,保温时间为1~5h。
(4)将步骤(2)得到的混合物放入水中浸泡1~3h,经过滤、清洗、干燥后即得到CaZrO3粉体。
作为一种优化,所述碱金属盐为Na2CO3。
本发明所用主要原料为半干法烧结烟气脱硫灰,主要结晶性物质为 CaSO3.0.5H2O和CaCO3,其典型成分见表1。该脱硫灰中的Ca元素的含量高达 42.36wt.%,可为CaZrO3的合成提供Ca源。此外,该脱硫灰中还含有丰富的SO3 2-或SO4 2-、Cl-、K+和Na+等。
表1烧结烟气脱硫灰的主要化学成分(wt.%)
本发明的主要反应过程及原理如下:
(1)加入的碱金属盐中的CO3 2-离子在加热过程中将烧结烟气脱硫灰中的 CaSO3转换成CaCO3,并将SO3 2-氧化成SO4 2-;
(2)上述反应生成的CaCO3,以及烧结烟气脱硫灰中原来含有的CaCO3、 CaO、Ca(OH)2等与ZrO2反应生成CaZrO3;
(3)原料中或反应产生的SO4 2-、Cl-、K+、Na+、Ca2+等离子在煅烧过程中促进低熔点物质的形成,为反应提供了一个液相环境,促进反应物质的扩散与反应,有效降低合成温度并抑制产物颗粒的晶粒长大。
与现有技术相比,本发明具有以下技术效果:
(1)以烧结烟气脱硫灰为Ca源,原料成本低廉。
(2)充分利用了烧结烟气脱硫灰中大量的SO3 2-、SO4 2-、Cl-、K+、Na+、Ca2+等离子在煅烧过程中能促进生成液相物质的特性,可使CaZrO3的合成温度从传统固相法的1500℃降至850-1050℃,并且产物颗粒尺寸细小,而这些离子最后可通过简单的水洗方式去除。
(3)该法工艺简单、成本低,可实现烧结烟气脱硫灰的高附加值利用,具有显著的社会经济效益。
附图说明
图1为实施例1制得的CaZrO3粉体的X射线衍射(XRD)图谱。
图2为实施例1制得的CaZrO3粉体的扫描电子显微镜(SEM)照片。
具体实施方式
为了进一步了解本发明的技术内容,以下结合附图和实施例详述本发明,但本发明不局限于下述实施例。
实施例1
将1.000g烧结烟气脱硫灰,1.302g ZrO2及1.119g Na2CO3粉体混合均匀后放入刚玉坩埚中,加热至850℃,保温5h后自然冷却,然后将产物放入中浸泡2h,过滤,分别用水和乙醇清洗多次,干燥即得到CaZrO3粉体。
图1为本实施例所制备CaZrO3粉体的XRD图谱,可以看出,本实施例所制备的粉体为结晶CaZrO3,基本无其它杂质相。图2为本实施例所制备CaZrO3粉体的SEM照片,可以看出,该粉体的粒径为100~200nm。
实施例2
将1.000g烧结烟气脱硫灰,1.302g ZrO2及1.459g K2CO3粉体混合均匀后放入刚玉坩埚中,加热至900℃,保温3h后自然冷却,然后将产物放入中浸泡2h,过滤,分别用水和乙醇清洗多次,干燥即得到CaZrO3粉体。
实施例3
将1.000g烧结烟气脱硫灰,1.302g ZrO2及2.506g Na2CO3粉体混合均匀后放入刚玉坩埚中,加热至950℃,保温2h后自然冷却,然后将产物放入中浸泡2h,过滤,分别用水和乙醇清洗多次,干燥即得到CaZrO3粉体。
实施例4
将1.000g烧结烟气脱硫灰、1.302g ZrO2、0.425g Na2CO3及0.466g KCl粉体混合均匀后放入刚玉坩埚中,加热至1050℃,保温1h后自然冷却,然后将产物放入中浸泡3h,过滤,分别用水和乙醇清洗多次,干燥即得到CaZrO3粉体。
Claims (2)
1.一种用烧结烟气脱硫灰低温制备CaZrO3粉体的方法,其特征在于包括如下步骤:
(1)将烧结烟气脱硫灰、ZrO2和碱金属盐粉体混合;
所述烧结烟气脱硫灰中Ca元素和ZrO2的摩尔比为1:1;所述碱金属盐为Na2CO3、K2CO3、Li2 CO3、NaCl、KCl、LiCl、Na2SO4、K2SO4、Li2SO4中的一种或多种,且至少含有一种碳酸盐,碱金属盐中CO3 2-离子和烧结烟气脱硫灰中S元素的摩尔比为1~3:1;
(2)将步骤(1)得到的混合粉体放入刚玉坩埚中,加热煅烧后自然冷却;
所述煅烧温度为850℃以上,保温时间为1~5h;
(3)将步骤(2)得到的混合物放入水中浸泡1~3h,经过滤、清洗、干燥后即得到CaZrO3粉体。
2.如权利要求1所述的一种用烧结烟气脱硫灰低温制备CaZrO3粉体的方法,其特征在于,所述碱金属盐为Na2CO3。
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