有机胺功能化介孔固体吸附剂吸附分离CO2性能研究

针对当前固体胺CO₂吸附剂存在吸附容量小、循环稳定性差等问题,采用高比表面积、易嫁接胺的介孔SBA-15作为载体,研究分子筛模板剂脱除方法和有机胺改性方法对制备的固体吸附剂吸附性能的影响,并采用N₂物理吸附、X射线衍射、红外光谱、热失重分析等表征技术并对样品进行表征。实验结果表明,通过嫁接和浸渍能够合成出不同有机胺负载量的胺功能化吸附剂,其中混合胺嫁接法改性的APTES-SBA（U）-T60吸附剂其吸附容量最大,在75℃下的纯CO₂气氛中吸附量达到192.05 mg/g,优于溶剂萃取和煅烧法去除模板剂。此外,混合胺嫁接法制备的样品在多次的吸/脱附操作下,CO₂吸附稳定性良好,表明混合胺修饰的吸附剂具有很好的稳定性和再生性。     

分子筛SBA-15负载离子液体[P66614][Triz]脱除氢烷气中CO2

以高效吸收CO₂的离子液体（IL）[P₆₆₆₁₄][Triz]作为吸收剂,通过浸渍法负载到两种不同孔径的介孔分子筛SBA-15上,用于脱除生物氢烷气中CO₂,并利用N₂吸附仪、扫描电子显微镜（SEM）和高倍透射电子显微镜（HRTEM）对负载材料进行了表征分析。混合吸收剂SBA-15（4.3 nm）-50%[Triz]的吸收容量和吸收速率比SBA-15（6.6 nm）-50%[Triz]的分别提高了12.4%和95.1%,这是由于SBA-15（4.3 nm）的孔道长度更短,避免了填充在孔道内的[P₆₆₆₁₄][Triz]在反应过程中接触不到CO₂,从而比SBA-15（6.6 nm）-50%[Triz]有更多IL反应活性点参与反应。还研究了不同氢烷气速率下SBA-15（4.3 nm）-50%[Triz]对CO₂的吸收并与2种吸附动力学模型相拟合,结果表明SBA-15（4.3 nm）-50%[Triz]对CO₂的吸收更符合准二级吸附动力学模型,表明吸附过程受化学吸附机理的控制,验证了[P₆₆₆₁₄][Triz]是通过化学反应脱除CO₂。     

载银介孔SBA-15吸附剂的制备及其对脂肪酸甲酯的吸附研究

以介孔分子筛SBA-15作为载体,在3-氨基丙基三乙氧基硅烷(APTS)对SBA-15表面修饰的基础上负载银离子制备Ag⁺-APTS/SBA-15吸附剂,采用氮气吸附-脱附、X射线衍射(XRD)、傅里叶变换红外光谱(FT-IR)、透射电镜(TEM)、扫描电镜-能谱(SEM-EDS)对吸附剂进行表征,并将吸附剂应用于混合脂肪酸甲酯的分离以考察其吸附性能。氮气吸附-脱附、XRD和TEM分析结果可以看出,制备的吸附剂具有规则有序孔道结构;FT-IR数据显示,介孔SBA-15表面被APTS成功修饰;SEM-EDS结果表明,银离子成功负载到载体SBA-15上;对混合脂肪酸甲酯吸附研究表明,该吸附剂对不饱和脂肪酸甲酯(UFAMEs)吸附效果较好,且随着银离子负载量的增加以及UFAMEs双键数的增多,吸附效果增强;当银离子负载量为25%时,吸附剂对亚麻酸甲酯吸附率高达53.47%。     

有机胺功能化介孔固体吸附剂吸附分离CO_2性能研究

针对当前固体胺CO_2吸附剂存在吸附容量小、循环稳定性差等问题,采用高比表面积、易嫁接胺的介孔SBA-15作为载体,研究分子筛模板剂脱除方法和有机胺改性方法对制备的固体吸附剂吸附性能的影响,并采用N_2物理吸附、X射线衍射、红外光谱、热失重分析等表征技术并对样品进行表征。实验结果表明,通过嫁接和浸渍能够合成出不同有机胺负载量的胺功能化吸附剂,其中混合胺嫁接法改性的APTES-SBA(U)-T60吸附剂其吸附容量最大,在75℃下的纯CO_2气氛中吸附量达到192.05 mg/g,优于溶剂萃取和煅烧法去除模板剂。此外,混合胺嫁接法制备的样品在多次的吸/脱附操作下,CO_2吸附稳定性良好,表明混合胺修饰的吸附剂具有很好的稳定性和再生性。     

四乙烯五胺改性多孔二氧化硅制备及CO2吸附性能

以十六烷基三甲基溴化铵（CTAB）为模板剂，原硅酸乙酯（TEOS）为硅源，1,3,5-三异丙基苯（TPB）为扩孔剂，制备不同孔道结构的多孔二氧化硅纳米微球（PSNs），将四乙烯五胺（TEPA）通过物理浸渍法负载到PSNs上，合成TEPA-PSNs吸附剂。利用扫描电镜、透射电镜、红外光谱、N₂吸附-脱附循环实验和热重分析对材料的结构性能和热稳定性能进行表征，成功制备了具有不同孔道结构的胺基化多孔二氧化硅。对吸附剂材料进行CO₂吸脱附实验和动力学研究，结果表明：当TPB含量增多时，吸附剂材料吸附的CO₂量也随之增大，并且TEPA-PSNs-0.5在75℃时吸附量最大，达4.70mmol/g；一阶动力学模型能较好地预测该吸附剂的CO₂吸附过程；经过5次循环，其再生性能仍然高达94.34%。因此，合成的胺基化多孔二氧化硅具有高吸附量和良好稳定性，是用于二氧化碳捕集的潜在材料。     

拟薄水铝石负载PEI/AMP吸附CO2性能

用富含胺基的物质对多孔材料进行修饰可以得到高CO₂吸附量的吸附剂。采用浸渍法将聚乙烯亚胺(PEI)和2-氨基-2-甲基-1-丙醇(AMP)负载在拟薄水铝石上,考察了CO₂压力、胺类物质负载量等对吸附性能的影响。采用低温N₂吸附/脱附法(BET)、扫描电镜(SEM)、傅里叶变换红外线光谱分析仪(FTIR)等手段表征了吸附剂的结构特征及其物理性质,并使用重量法微天平实验装置对吸附剂的性能进行了评价。实验结果表明,当温度恒定为50℃,压力小于1 MPa时,负载PEI的吸附剂最高的CO₂吸附量为77.53 mg CO₂·(g吸附剂)^-1,最佳负载量为85%;压力大于1 MPa时,负载PEI的吸附剂最高的CO₂吸附量为123.79 mg CO₂·(g吸附剂)^-1,最佳负载量为10%。负载AMP的吸附剂最高的CO₂吸附量为128.01 mg CO₂·(g吸附剂)^-1,最佳负载量为85%。CO₂吸附稳定性实验表明,吸附剂对CO₂的吸附性能稳定。     

氨基功能化介孔硅吸附剂的制备及其对铬(Ⅲ)的吸附行为

采用3-氨丙基三甲氧基硅烷（APTMS）对SBA-15介孔硅进行改性,获得氨基功能化介孔硅吸附剂（NH₂-SBA-15）,从而赋予其螯合重金属离子的能力。利用XRD、SEM、TEM、EDX、TGA、BET和XPS等手段对吸附剂的表面形貌、孔道结构、元素分布和表面化学性质进行了表征。研究了NH₂-SBA-15吸附剂对水溶液中铬(Ⅲ)的吸附性能,分析了吸附动力学、吸附热力学和再生性能。结果表明,SBA-15吸附剂经过氨基功能化后,其原有的结晶结构没有明显变化,且对铬(Ⅲ)的吸附性能显著提高。NH₂-SBA-15对铬(Ⅲ)的吸附行为符合Langmuir等温吸附模型和拟二级吸附动力学方程。NH₂-SBA-15对铬(Ⅲ)的吸附过程主要依靠其表面—NH₂与铬(Ⅲ)的配位螯合作用,且为吸热过程。经过5次循环利用后,NH₂-SBA-15对铬(Ⅲ)的吸附率仍然保持在92%以上。该氨基功能化介孔硅吸附剂在吸附铬(Ⅲ)方面具有潜在的应用前景。     

甲醇对于PEI-SBA固态胺制备及其性能的影响

固态胺材料具有优异的二氧化碳(CO₂)选择吸附性能,是一类潜在的CO₂捕集材料。作为一种重要的固态胺材料,SBA-15负载聚乙烯亚胺(PEI-SBA-15)由于原材料较为廉价且性能优异受到了大量的关注。PEI-SBA-15的制备过程需要采用甲醇溶剂,而溶剂使用量对于其CO₂吸附性能的影响尚无系统研究。系统研究了溶剂使用量对SBA-15负载聚乙烯亚胺的CO₂吸附性能的影响。研究结果表明,可以同时实现提升CO₂吸附性能和CO₂/N₂选择性和大幅降低甲醇的使用量。对于降低PEI-SBA-15的制备成本以及提升制备过程环保性具有重要意义。     

脱硫石膏改性固体胺复合材料的制备及脱碳性能

将榴莲壳碳化制备生物炭（BC）,与硅钙渣混合作复合载体,在其表面浸渍负载五乙烯六胺（PEHA）,并加入含水分的脱硫石膏（FGDG）,得到胺功能化的含水CO₂固体吸附剂,与不含脱硫石膏的吸附剂相比吸附活性明显改善。通过FT-IR、TGA、SEM及N₂吸脱附等手段对吸附剂进行了表征,并在固定床反应器中考察了吸附剂脱硫石膏含量、吸附温度和CO₂浓度对吸附性能的影响。结果表明,脱硫石膏中水的存在改变了氨基与CO₂的相互作用机理。当脱硫石膏含量为30%、吸附温度为85℃时,CO₂最大吸附量为2.33 mmol/g。经12次循环再生后吸附量仅下降了4.2%,表现出良好的吸附稳定性。Clausius-Clapeyron方程计算的等量吸附热介于物理与化学吸附热之间,说明吸附过程中物理与化学作用同时进行。用多个动力学模型对实验数据进行拟合,pseudo-first-order与pseudo-second-order模型均不能准确拟合实验数据,而Avrami模型可较好地拟合整个吸附过程,进一步验证BC/SCS-PEHA-30% FGDG的CO₂吸附过程并非单纯的物理或化学吸附,而是两者同时发生。     

介孔SiO2吸附CO2的性能研究

以正硅酸乙酯（TEOS）为硅源,端氨基聚氧化丙烯醚（D2000）为模板剂,在水和乙醇的混合溶液中合成了蠕虫状介孔结构的介孔SiO₂（记为MSU-J）。采用物理浸渍的方法利用四乙烯五胺（TEPA）改性介孔MSU-J。采用红外、N₂吸附/脱附、元素分析表征改性介孔SiO₂。红外测试表明,经过物理浸渍可以将有机胺负载到介孔SiO₂上。N₂吸附/脱附试验表明,经过氨基修饰后,介孔SiO₂的介孔结构没有发生变化,但是介孔的孔容、孔径以及比表面积随着氨基浸渍量的增加而减小。在25℃和45℃,0.1 MPa下的纯CO₂吸附试验表明,氨基改性材料对CO₂吸附效果明显提高。当浸渍量为20%、吸附条件为25℃/0.1 MPa时,吸附量达到最大值138.6mg/g。当氨基含量继续增加时,吸附量反而降低。循环性试验表明,制备的吸附剂具有良好的循环性能,循环使用6次,材料的吸附量下降很少。     

Amine modified mesocellular siliceous foam (MCF) as a sorbent for CO2

Adsorption is considered a promising method for carbon capture. CO₂ adsorbents take a variety of forms - but one approach is to fill mesoporous substrates with a polymeric CO₂ selective sorbent. SBA-15 and mesocellular siliceous foam (MCF) are high pore volume, high surface area ordered mesoporous materials for which modification with amine should result in high capacity, highly selective adsorbents. SBA-15 and MCF were separately loaded with approximately one pore volume equivalent of linear polyethyleneimine (PEI) (M_w = 2500) or branched PEI (M_n = 1200). CO₂ adsorption/desorption isotherms under dry CO₂ were obtained at 75, 105 and 115 °C. The CO₂ adsorption/desorption kinetics were improved with temperature, though the CO₂ capacities generally decreased. The adsorption capacity for MCF loaded with branched PEI at 105 and 115 °C were 151 and 133 mg/g adsorbent, respectively (in 50% CO₂/Ar, 20 min adsorption time). These are significantly higher than the adsorption capacity observed for SBA-15 loaded with branched PEI under same conditions, which were 107 and 83 mg/g adsorbent, respectively. Thus the results indicate that, on a unit mass basis, amine modified MCF's are potentially better adsorbents than amine modified SBA-15 for CO₂ capture at modestly elevated temperature in a vacuum swing adsorption process.     

Promoted adsorption of CO2 on amine‐impregnated adsorbents by functionalized ionic liquids

Amine‐impregnated adsorbents are promising alternatives to aqueous amines for CO₂ capture. However, the diffusion‐controlled CO₂ adsorption process is a significant issue associated with them, resulting in the insufficient utilization of amine groups. Herein, we propose the use of functionalized ionic liquids 1‐ethyl‐3‐methylimidazolium acetate ([emim][Ac]) with chemical reactivity to CO₂ and low viscosity as the additive to amine‐impregnated adsorbents. The key is that [emim][Ac] does not show drastic increase in viscosity after reacting with CO₂. Taking the polyethyleneimine (PEI)‐impregnated SBA‐15 as a model system, it is found that the CO₂ capacities of PEI/SBA‐15 composites are improved by 86%, and the active site efficiencies are improved by 270%, after the addition of [emim][Ac]. The addition of [emim][Ac] to PEI/SBA‐15 composites also helps improve the CO₂ adsorption rate and recycling stability of composites. Therefore, [emim][Ac] offers the opportunity to fabricate amine‐impregnated adsorbents with simultaneously improved CO₂ capacities, adsorption kinetics, and recycling stability. © 2018 American Institute of Chemical Engineers AIChE J, 64: 3671–3680, 2018     

CO2 adsorption performance of polyethyleneimine-modified ion-exchange resin

A series of solid amine adsorbents were prepared by the template method with ion-exchange resin (D001) as the carrier and polyethyleneimine (PEI) as the modifier. The absorbents were characterized by energy disperse spectroscopy (EDS), scanning electron microscope (SEM), N₂ adsorption–desorption, Fourier transform infrared spectroscopy (FTIR) and thermogravimetric analysis (TGA) techniques. The effects of PEI loading, adsorption temperature and influent velocities on CO₂ adsorption capacity in a fixed-bed reactor were investigated. The results show that the solid amine adsorbent prepared by the template method had a better PEI dispersion, stability and CO₂ adsorption capacity. The maximum CO₂ adsorption capacity was 3.98 mmol·g^?1 when PEI loading was 30%, the adsorption temperature was 65°C and the influent velocity was 40 mL·min^?1. The CO₂ adsorption capacity decreased only by 9.50% after 10 cycles of adsorption–desorption tests. The study of kinetics indicates that both chemical adsorption and physical adsorption occurred in the CO₂ adsorption process. The CO₂ adsorption process included fast breakthrough adsorption and gradually approaching equilibrium stage. The particle internal diffusion process was the control step for CO₂ adsorption.     

Carbon dioxide capture under postcombustion conditions using amine-functionalized SBA-15: Kinetics and multicyclic performance

ABSTRACT

In this work, ordered mesoporous SBA-15 was synthesized and functionalized by polyethyleneimine (PEI). The morphological properties were characterized by N₂ adsorption/desorption, field–emission scanning electron microscopy (FE-SEM), high–resolution transmission electron microscopy (HR-TEM) and Fourier transform infrared (FTIR) spectroscopy methods. The carbon dioxide (CO₂) uptake on the sorbents, kinetics of CO₂ adsorption/desorption and long-term multicycle stability of PEI-impregnated sorbent were measured. An optimal amine loading of 50 wt.% showed a CO₂ adsorption capacity ~3.09 mmol g^?1 using 10% pre-humidified CO₂ at 75°C. The presence of moisture in flue gas showed a promoting effect in CO₂ sorption capacity. The temperature swing adsorption/desorption cycles showed excellent multicycle stability over 60 cycles during 65 h of operations under humid CO₂.     

Mesoporous Silica Sorbents Impregnated with Blends of Tetraethylenepentamine and Alkanolamine for CO2 Separation

Mesocellular silica foam (MSU-F) supports were functionalized via wet impregnation with various amine and alcohol compounds for use as high-capacity adsorbents for CO₂ separation. The effect of the amino, hydroxyl, and ether functional groups in the impregnating mixture on the CO₂ adsorption capacity was investigated. Chemical adsorption was controlled by the composition of the compounds, and the blending effect on the adsorption performance was dependent on the temperature. MSU-F (30 wt.%) impregnated with a mixture of tetraethylenepentamine (40 wt.%) and aminoethylethanolamine (30 wt.%) showed a high adsorption capacity of 5.4 mmol/g at 333 K for 15 kPa CO₂.     

Promoting the CO2 adsorption in the amine-containing SBA-15 by hydroxyl group

Novel CO₂ capturer with a high efficiency is fabricated through dispersing the amine mixture of tetraethylenepentamine (TEPA) and diethanolamine (DEA) or glycerol within the as-synthesized mesoporous silica SBA-15, and the resulting sample is characterized by low angle X-ray diffraction and N₂ adsorption to evaluate the distribution of the guest. The influence of hydroxyl group on the CO₂ adsorption capacity of the composite is investigated by using CO₂-TPD and TG–MS techniques. The hydroxyl group of the P123 ((EO)₂₀(PO)₇₀(EO)₂₀, template preserved in as-synthesized SBA-15) and the guest could promote the capture of CO₂ by the amine through changing the interaction mechanism. In addition, the presence of hydroxyl group promotes the formation of the intermediate between CO₂ and the amine with a lower thermal stability hence the CO₂ trapped by the composite is easier to be desorbed and thus the regeneration of adsorbent is facilitated. Therefore, using this mixed amine (TEPA and DEA) modified as-synthesized SBA-15 as CO₂ capturer not only saves the energy for removal of template, but also cut down the cost in the preparation and regeneration of CO₂ capturer, which is critical in CO₂ separation and capture.     

Carbon Di-Oxide Removal with Mesoporous Adsorbents in a Single Column Pressure Swing Adsorber

Abstract

A five-step PSA cycle was studied for CO₂ separation from CO₂-N₂ gas mixture in a single column at elevated temperatures using Poly-ethyleneimine (PEI) impregnated mesoporous silica SBA-15 as adsorbent. The PSA cycle study included a strong adsorptive rinse step in which the strongly adsorbed component, i.e., CO₂ was used for rinsing the adsorbent bed in order to increase the purity of CO₂ product. The study indicates that the adsorbent is regenerable under typical PSA conditions. The productivity of the adsorbent studied for CO₂ separation was found to be comparable with commercial zeolite adsorbents as reported in literature.     

Mixed-amine Modified SBA-15 as Novel Adsorbent of CO2 Separation for Biogas Upgrading

A novel adsorbent of CO₂ from biogas was prepared by synthesizing and modifying the mesoporous molecular silica of SBA-15 with methyl-diethyl-amine (MDEA) and piperazine (PZ). The adsorbent showed good performance in separating CO₂ from biogas. The loaded amines did not change the ordered structure of SBA-15, but enhanced its adsorption of CO₂. The adsorbents were characterized by X-ray powder diffraction (XRD) and N₂ adsorption/desorption. With the increase in MDEA loading, the surface area, pore size, and pore volume of the MDEA-loaded SBA-15 decreased. The modification of amines enlarged the difference between the equilibrium adsorption of CO₂ and CH₄. Quantitatively evaluated on the basis of the breakthrough curves, the separation factors between CO₂ and CH₄, was increased more than seven fold due to the MDEA modification. With mixed-amine (MDEA + PZ) modification, the separation factors between CO₂ and CH₄ was further improved. In addition, not only the adsorbent was regenerable by purging with the purified gas, but also the adsorption performance is stable in adsorption cycles. Effect of moisture on adsorption of CO₂ is investigated and the results show the increase in the adsorption performance.     

Synthesis of chloropropylamine grafted mesoporous MCM-41, MCM-48 and SBA-15 from rice husk ash: their application to CO<Subscript>2</Subscript> chemisorption

Mesoporous siliceous MCM-41, MCM-48 and SBA-15 were synthesized using Rice Husk Ash (RHA) as the silica source. Their defective –OH sites were then grafted with 3-chloropropyl amine hydrochloride (3-CPA) and characterized by X-ray powder diffraction (XRD), Fourier transform infrared spectroscopy (FT-IR), and BET techniques. Those results portrayed their resemblance with that synthesized from conventional silica sources. 3-CPA grafted mesoporous silicas were tested for CO₂ chemisorption over fixed bed reactor at different temperatures. The maximum adsorption of 1.7 mmol/g of CO₂ was observed on 3-CPA grafted SBA-15 (SBA-15/CPA) at 25°C. The chemisorbed CO₂ on amine grafted mesoporous silica was stabilized by weak hydrogen bonds formed during the nucleophilic attack between lone pair of electrons in amine groups and quadrupolar CO₂ with more degree of positive charge to form carbamates. The rapid steep slope which arises due to CO₂ adsorption illustrated a minimal mass transfer effect and extreme fast kinetics. Performance tests such as reproducibility, stability and selectivity towards CO₂ adsorption were also carried out over 3-CPA grafted mesoporous silica and the results were in line with that of well established CO₂ sorbent.