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1.
在温和条件下,发展了一种以丁二醇-乙二胺体系新颖、高效地固定CO2的方法。在此方法中,CO2被快速激活并转化为一种固态的CO2储集材料(CO2SM),通过XPS、XRD、FTIR和13C NMR等技术表征证实为烷基碳酸胺。基于TGA结果,CO2SM的水溶液可以与Ca(OH)2和Ba(OH)2反应制备CaCO3和BaCO3微粒,还可用于循环吸收和解吸CO2的过程。此外,丁二醇-乙二胺水溶液在20℃下吸收CO2并在98.6℃下解吸CO2,没有明显的溶液损失。因此,丁二醇-乙二胺体系提供了一种绿色、高效、低成本的二氧化碳捕集利用方法。  相似文献   

2.
在室温下,将CeCl3溶液与CO2储存材料(CO2SM)混合、搅拌0.5 h制备了片状碳酸铈前驱体(CCPs),并在500℃下煅烧CCPs 4 h,制得平均尺寸为4.94 μm×0.92 μm,厚度为0.04~0.08 μm纳米结构片状CeO2晶体。在此过程中,CO2SM不但可以提供CO32-,还能起到分散剂和结构导向剂的作用。反应过程中,系统地研究了CO2SM用量、Ce3+浓度和搅拌时间3个因素对CCPs形态和大小的影响,得到最优制备条件:0.1 g CO2SM和50 mL 0.03 mol·L-1 Ce3+水溶液以1 000 r·min-1转速在室温下搅拌0.5 h。煅烧CCPs后,所制备的片状CeO2晶体在室温下CO2吸附量可达0.554 mmol·g-1。  相似文献   

3.
在常温常压下,由乙二胺(EDA)和乙二醇及其衍生物(EGs)组成的混合体系可捕集SO2并转化为一种SO2储集材料(SO2SM)。EDA+EGs体系呈现了强的捕集性能(0.364~0.662 gSO2·gabsorbent-1)。FTIR,XPS和XRD结果确证了SO2SM为一种烷基亚硫酸盐。以EG-SO2SM为原料制备具有多种形貌的BaSO3或BaSO4,在此过程中,EG-SO2SM不仅提供了原材料,而且可以释放EDA和EG用作表面活性剂,调控晶体的结晶化过程。  相似文献   

4.
在常温常压下,由乙二胺(EDA)和乙二醇及其衍生物(EGs)组成的混合体系可捕集SO2并转化为一种SO2储集材料(SO2SM)。EDA+EGs体系呈现了强的捕集性能(0.364~0.662 gSO2·gabsorbent-1)。FTIR,XPS和XRD结果确证了SO2SM为一种烷基亚硫酸盐。以EG-SO2SM为原料制备具有多种形貌的BaSO3或BaSO4,在此过程中,EG-SO2SM不仅提供了原材料,而且可以释放EDA和EG用作表面活性剂,调控晶体的结晶化过程。  相似文献   

5.
Li2ZrO3材料吸收CO2性能的进一步研究   总被引:8,自引:0,他引:8  
用不同结构的ZrO2合成了一系列在高温下吸收CO2的Li2ZrO3材料,并详细的研究了反应物质的物理和化学性质对生成物吸收CO2性能的影响。采用SEM、XRD以及TG分析法分别进行了材料结构及其吸收CO2性能的表征,并使用XPS法测定了材料表面的元素组成。实验结果表明,使用不同结构的ZrO2合成的Li2ZrO3,其吸收CO2的性能明显的不同。用ZrO2(t)(四方)合成的Li2ZrO3吸收CO2的速度快,在500 ℃下,20% CO2(80%空气)的气氛中保持3h,其吸收量可达25(±0.6)%(wt),而以ZrO2(m)(单斜)为原料制备的Li2ZrO3在上述吸收条件下重量仅增加9(±0.6)%(wt)。此外,实验结果还表明化学元素的掺杂对用ZrO2(m)合成的Li2ZrO3的CO2吸收速度及吸收容量影响较大。  相似文献   

6.
本文设计开发了一种以2,6-二甲酰基对甲苯酚为母体的新型荧光探针HMI,可用于高效识别EtOH-H2O (8/2, v/v, HEPES 10 mM, pH =7.4)体系中的CO32-。HMI在660 nm处显示发射带,加入CO32-后,在600 nm的等吸收点激发时,原来在660 nm处的荧光淬灭,而以540 nm为中心的新发射带荧光显着增加,为比率型荧光探针。HMI对CO32-表现出高选择性且具有较强的抗干扰能力。此外,荧光探针HMI对CO32-荧光响应的检测限较低,可达到3.938×10-6 M。更具有意义的是,HMI探针对CO32-的检测能够在实际水样中起到很好的应用,而且细胞成像研究表明,HMI可用于活体MCF-7细胞中CO32-的成像。  相似文献   

7.
不同类型的CO32-替换羟基磷灰石固溶体晶体化学FT-IR研究   总被引:13,自引:0,他引:13  
利用FT-IR结合XRD对不同类型的CO32-替换磷灰石固溶体进行了晶体化学研究,结果表明:B型替换碳羟磷灰石(CHAP)的替换方式是[CO3·OH]四面体替换[PO4]四面体;A型替换CHAP的替换方式是[CO3]三角形配位体替换通道位置的OH-;AB混合型替换CHAP的FT-IR谱中非对称伸缩振动ν3分裂为ν3-1、ν3F、ν3-4,高斯函数法拟合表明ν3F峰是A型替换的ν3-2与B型替换的ν3-3的叠合。当WCO32-≦3.34%时,随CO32-含量增加,A型替换量增大,替换指数(SI)增大,且当WCO32-=3.34%时,SI达最大值,当3.34%CO32-≦7.52%时,随CO32-含量增加,SI减小,B型替换量增大,且当WCO32-=7.52%时总固溶量饱和。  相似文献   

8.
高温下硅酸锂吸收CO2的研究   总被引:3,自引:0,他引:3       下载免费PDF全文
以SiO2和Li2CO3为反应原料,采用高温固相法于不同温度下合成了一系列可在高温500~750 ℃之间直接吸收CO2的硅酸锂(Li4SiO4)材料。采用扫描电子显微镜(SEM)、X射线粉末衍射仪(XRD)分别观察和评价了合成材料的表面形貌与结构特征,用热重分析仪(TG)研究了硅酸锂材料吸收CO2的性能。实验结果表明,在750 ℃下煅烧6 h即可合成出吸收CO2性能良好的硅酸锂材料,在CO2气氛下,于700 ℃保持约15 min即可达到吸收平衡,其吸收量约达43%(wt)左右。与文献报道相比,材料的合成条件有所改善,材料吸收CO2的容量也有较大提高。  相似文献   

9.
介绍了由CO2+H2合成C2+烃的几种复合催化剂体系的研究进展,比较和评价了复合催化剂体系的活性和选择性及对C2+烃类生成的影响。着重于复合催化剂体系对C4+烃的生成及产物分布的影响并简述反应机理。  相似文献   

10.
时静雅  武培怡 《化学进展》2009,21(5):1023-1033
超临界CO2(scCO2)作为一种物理化学性质优良、具有高扩散速率及优良溶解性能的溶剂,在科学研究及工业生产中广受青睐。将scCO2应用于聚合物体系中,CO2 与聚合物间特殊的相互作用有利于CO2分子在聚合物中的吸附与扩散。同时通过CO2的吸附及其对聚合物的溶胀和塑化作用,聚合物所处微观化学环境以及整体结构性质会发生一定的变化。由于傅立叶变换红外光谱(FTIR)技术能够有效地考察化学环境变化对分子结构造成的影响,这一表征技术在超临界CO2作用体系中广为应用。本文主要选取了近年来利用FTIR技术考察scCO2作用于聚合物体系的一些实例,从CO2-聚合物相互作用机理,scCO2对聚合物或生物大分子的加工过程的影响两方面,阐述了利用红外光谱技术在scCO2作用体系中的应用以及前景。  相似文献   

11.
Dry potassium-based sorbents were prepared by impregnation with potassium carbonate on supports such as activated carbon (AC), TiO2, Al2O3, MgO, CaO, SiO2 and various zeolites. The CO2 capture capacity and regeneration property of various sorbents were measured in the presence of H2O in a fixed bed reactor, during multiple cycles at various temperature conditions (CO2 absorption at 50–100 °C and regeneration at 130–400 °C). The KAlI30, KCaI30, and KMgI30 sorbents formed new structures such as KAl(CO3)2(OH)2, K2Ca(CO3)2, K2Mg(CO3)2, and K2Mg(CO3)2·4(H2O), which did not completely convert to the original K2CO3 phase at temperatures below 200 °C, during the CO2 absorption process in the presence of 9 vol.% H2O. In the case of KACI30, KTiI30, and KZrI30, only a KHCO3 crystal structure was formed during CO2 absorption. The formation of active species, K2CO3·1.5H2O, by the pretreatment with water vapor and the formation of the KHCO3 crystal structure after CO2 absorption are important factors for absorption and regeneration, respectively, even at low temperatures (130–150 °C). In particular, the KTiI30 sorbent showed excellent characteristics with respect to CO2 absorption and regeneration in that it satisfies the requirements of a large amount of CO2 absorption (87 mg CO2/g sorbent) without the pretreatment with water vapor, unlike KACI30, and a fast and complete regeneration at a low temperature condition (1 atm, 150 °C). In addition, the higher total CO2 capture capacity of KMgI30 (178.6 mg CO2/g sorbent) than that of the theoretical value (95 mg CO2/g sorbent) was explained through the contribution of the absorption ability of MgO support. In this review, we introduce the CO2 capture capacities and regeneration properties of several potassium-based sorbents, the changes in the physical properties of the sorbents before/after CO2 absorption, and the role of water vapor and its effects on CO2 absorption.  相似文献   

12.
La2(CO3)3 nanowires were prepared in the nonionic surfactant microemulsion(Triton X-100/cyclohexane/water)system. Transmission electron microscopy (TEM) and selected area electronic diffraction (SAED) were used to characterize the shape and size of the products. The results showed that the pH value and concentration of mother solution, temperature and aging time all could affect the morphology and size of the La2(CO3)3 nanowires. The lengths of the nanowires were more than 10 μm and the diameters were in the range of 30~200 nm.  相似文献   

13.
Pressureless sintering of CaCO3 was carried out, with Li2CO3 (from 0.5 to 8 wt%) as an additive, under different pressures of CO2. Densification occurs between 600 and 700°C. Sintering above the eutectic temperature (T>662°C) leads to the decomposition of calcium carbonate and the materials become expanded. At 620° under 1 kPa of CO2, a relative density of 96% is reached. Li2CO3 enhances the densification process and grain growth of calcium carbonate. CO2 pressure slows down densification and grain growth kinetics. These results are explained by the influence of carbonate and calcium ion vacancies on the sintering mechanisms. This revised version was published online in August 2006 with corrections to the Cover Date.  相似文献   

14.
Adsorption isotherms of carbon dioxide (CO2), methane (CH4), and nitrogen (N2) on Hβand sodium exchanged β-zeolite (Naβ) were volumetrically measured at 273 and 303 K. The results show that all isotherms were of Brunauer type I and well correlated with Langmuir-Freundlich model. After sodium ions exchange, the adsorption amounts of three adsorbates increased, while the increase magnitude of CO2 adsorption capacity was much higher than that of CH4 and N2. The selectivities of CO2 over CH4 and CO2 over N2 enhanced after sodium exchange. Also, the initial heat of adsorption data implied a stronger interaction of CO2 molecules with Na+ ions in Naβ . These results can be attributed to the larger electrostatic interaction of CO2 with extraframework cations in zeolites. However, Naβ showed a decrease in the selectivity of CH4 over N2, which can be ascribed to the moderate affinity of N2 with Naβ. The variation of isosteric heats of adsorption as a function of loading indicates that the adsorption of CO2 in Naβ presents an energetically heterogeneous profile. On the contrary, the adsorption of CH4 was found to be essentially homogeneous, which suggests the dispersion interaction between CH4 and lattice oxygen atoms, and such interaction does not depend on the exchangeable cations of zeolite.  相似文献   

15.
Carbon from fossil CO2 emissions, without a significant presence of 14C, causes dilution of 14C in the carbon isotopic mixture (Suess effect). Reported 14C activities are usually connected to radiocarbon amount in the carbon isotopic mixture. Our paper is aimed on estimation of 14C/14CO2 amount in the atmosphere (and its trend), utilizing calculation of a 14C activity concentration. A parameter connected only with a 14C quantity in the volume or mass unit of air is not influenced by a fossil carbon amount. Such a “robust” parameter can be influenced only by processes connected with 14C emissions/depositions.  相似文献   

16.
以γ-Al2O3为载体,采用等体积浸渍法,制备了不同K2CO3含量的Ni-Cu-Mn-K/Al2O3水煤气变换催化剂,采用低温N2吸附、XRD、TPD和TPR,考察了K2CO3含量对催化剂结构和性能的影响。结果表明:K2CO3的加入使催化剂的还原温度有所提高,适量的K2CO3能增加活性组分的电子密度,从而增强其给电子活化CO的能力,提高催化剂的活性。但过量的K2CO3使得催化剂比表面积和孔容降低,且导致催化剂对CO吸附过强,催化活性降低。当Ni-Cu-Mn-K/γ-Al2O3催化剂中K2CO3的添加量为7.5%时,且催化剂经530 ℃耐热15 h后,在350 ℃时水煤气变换反应中CO转化率达62.29%。  相似文献   

17.
The rapid growth of CO2 emissions in the atmosphere has attracted great attention due to the influence of the greenhouse effect. Aerogels’ application for capturing CO2 is quite promising owing to their numerous advantages, such as high porosity (~95%); these are predominantly mesoporous (20–50 nm) materials with very high surface area (>800 m2∙g−1). To increase the CO2 level of aerogels’ uptake capacity and selectivity, active materials have been investigated, such as potassium carbonate, K2CO3, amines, and ionic-liquid amino-acid moieties loaded onto the surface of aerogels. The flexibility of the composition and surface chemistry of aerogels can be modified intentionally—indeed, manipulated—for CO2 capture. Up to now, most research has focused mainly on the synthesis of amine-modified silica aerogels and the evaluation of their CO2-sorption properties. However, there is no comprehensive study focusing on the effect of different types of aerogels and modification groups on the adsorption of CO2. In this review, we present, in broad terms, the use of different precursors, as well as modification of synthesis parameters. The present review aims to consider which kind of precursors and modification groups can serve as potentially attractive molecular-design characteristics in promising materials for capturing CO2.  相似文献   

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