离子热法合成沸石咪唑骨架材料及其溶解-结晶机理研究

基于沸石咪唑骨架材料在离子液体和低共熔溶剂中冷却结晶的析出方式,开发了一种离子热法合成沸石咪唑骨架材料的新途径,采用X射线衍射、扫描电镜、核磁共振光谱、红外光谱以及热重分析等方法对制备的产物进行了表征,研究了合成条件对产物结晶度、尺寸和形貌的影响,探讨了沸石咪唑骨架材料在离子热合成体系中的溶解-结晶析出机理.研究发现,冷却速率能够影响产物形貌,急速冷却时,sod(RCSR代码)型产物的形貌为球形,zni(RCSR代码)型产物为棒状或平板状;程序控制冷却时,sod型产物的形貌为多面体,zni型产物呈团簇状.     

Li4SiO4对CO2捕集性能的实验研究

以Li₂CO₃和SiO₂为原料,通过高温固相合成法合成了CO₂捕集剂Li₄SiO₄,并用X射线粉末衍射仪(XRD)、扫描电子显微镜(SEM)对所合成的材料在CO₂捕集前后的晶相变化以及微观结构进行了表征。通过热重分析仪(TGA)研究了Li₄SiO₄材料吸附CO₂的性能,并在小型热态实验台架上进行了CO₂热态捕集实验。实验结果表明,Li₄SiO₄对CO₂的捕集性能受Li₄SiO₄合成温度、CO₂的吸附温度以及气体中CO₂含量的影响,在700 ℃下制得的Li₄SiO₄具有最佳的CO₂吸附特性,最大吸附增量可达34%。Li₄SiO₄的吸附能力随着CO₂含量和吸附时间的增加而增加,当CO₂浓度分别为75%、67%、60%时,700 ℃ Li₄SiO₄对CO₂最大吸附量分别可达6.68 mmol/g、3.37 mmol/g、2.02 mmol/g (理论量8.33 mmol/g)。     

Efficient CO2 capture on low-cost silica gel modified by polyethyleneimine

In this work,a series of polyethyleneimine(PEI) functionalized commercial silica gel were prepared by wet impregnation method and used as CO 2 sorbent.The as-prepared sorbents were characterized by N 2 adsorption,FT-IR and SEM techniques.CO 2 capture was tested in a fixed bed reactor using a simulated flue gas containing 15.1% CO 2 in a temperature range of 25-100 C.The effects of sorption temperature and amine content on CO 2 uptake of the adsorbents were investigated.The silica gel with a 30 wt% PEI loading manifested the largest CO 2 uptake of 93.4 mg CO 2 /g adsorbent(equal to 311.3 mg CO 2 /g PEI) among the tested sorbents under the conditions of 15.1%(v/v) CO 2 in N 2 at 75 C and atmospheric pressure.Moreover,it was rather low-cost.In addition,the PEI-impregnated silica gel exhibited stable adsorption-desorption behavior during 5 consecutive test cycles.These results suggest that the PEI-impregnated silica gel is a promising and cost-effective sorbent for CO 2 capture from flue gas and other stationary sources with low CO 2 concentration.     

SO2对钙基CO2吸收剂循环煅烧/碳酸化反应的影响

在循环煅烧/碳酸化反应系统中,研究了SO₂对钙基吸收剂CaCO₃捕集CO₂的影响,获得了SO₂对钙基吸收剂碳酸化特性、煅烧特性以及循环稳定性的影响规律,并结合SEM分析结果,从循环煅烧/碳酸化反应角度,分析了可能存在的原因。结果表明,钙基吸收剂吸收CO₂的能力随着循环反应次数的增加逐渐发生衰减,在SO₂影响下,这种衰减会进一步加剧,且衰减程度随着SO₂浓度的增加而增大,经过十次循环后,碳酸化转化率分别为25.5%(0%SO₂)、16.9%(0.1%SO₂)和5.2%(0.2%SO₂)。造成这种衰减加剧的主要原因是反应产生较厚的硫酸化产物层,硫酸化产物层使颗粒表面孔隙发生堵塞,阻碍了CO₂在吸收剂内部的扩散,降低了碳酸化转化率。     

CeO_2掺杂对CaO基吸收剂CO_2捕获性能的影响

以P123作为软模板剂,通过均相沉淀法制备了CeO_2掺杂的CaO基吸收剂,研究了CeO_2掺杂对CO_2捕获的影响。结果表明,CeO_2掺杂可促进表面氧物种的生成,从而促进CaO与CO_2的碳酸化反应。CaO-CeO_2的相互作用一方面促进了从Ca到表面氧物种的电子转移;另一方面,由于部分Ca离子对晶格中Ce离子的取代,晶格的电中性被打破,有利于CeO_2中晶格氧的逸出,以及氧空位和O~(2-)的生成。本实验制备的纯CaO吸收剂的碳酸化反应活化能为28.1 kJ/mol,而掺杂CeO_2后活化能显著降低,且当Ce/Ca(物质的量比)为0.25时达到最低值10.2 kJ/mol。另外,CeO_2的掺杂有利于CaO的分散,进而减缓CaO烧结。CeO_2掺杂的吸收剂在碳酸化/煅烧循环中表现出良好的CO_2捕获性能和循环稳定性。     

两个配位竞争策略制备的镁基金属有机骨架及其选择性CO2捕集

利用配位竞争策略制备了2个镁基金属有机骨架(MOFs)。在酸性条件下,镁离子与N,N-二甲基甲酰胺(DMF)热分解产生的甲酸原位反应得到三维甲酸镁 MOF：[Mg₃(HCO₂)₆]·DMF (1)。在相同条件下,当加入竞争配体 1,1′∶3′,1″-三联苯-3,3″,5,5″-四甲酸(H₄L)后,甲酸不再参与配位,得到新的三维镁基MOF：[Mg₂(L)(H₂O)₃]·2 H₂O·2CH₃CN·DMF (2)。单晶X射线分析表明,MOF 1具有[Mg₄@Mg2]四面体建筑块,它们形成dia拓扑网络并有一个孔径为0.44 nm的一维孔道。而MOF 2具有独特的[Mg₂]双核簇,与4-连接配体L^4-配位后,形成sra拓扑网络且沿a轴方向存在一个哑铃型孔道,长度为1.42 nm。气体吸附研究发现1具有微孔结构,其表面积为342 m²·g^-1,但2不能保持原有多孔特征。此外,1具有良好的水稳定性且在低压下展现快速吸收的Ⅰ型 CO₂吸附等温线,在 298 K和 2 000 kPa下吸附量达到样品重量的 14.5%。理想吸附溶液理论和吸附热计算表明 1具有良好的选择性CO₂/CH₄捕获能力。     

配位竞争策略制备的两个镁基金属有机骨架及其选择性CO2捕集

利用配位竞争策略制备了2个镁基金属有机骨架(MOFs)。在酸性条件下,镁离子与N,N-二甲基甲酰胺(DMF)热分解产生的甲酸原位反应得到三维甲酸镁MOF:[Mg₃(HCO₂)₆]·DMF(1)。在相同条件下,当加入竞争配体1,1′∶3′,1″-三联苯-3,3″,5,5″-四甲酸(H₄L)后,甲酸不再参与配位,得到新的三维镁基MOF:[Mg₂(L)(H₂O)₃]·2H₂O·2CH₃CN·DMF(2)。单晶X射线分析表明,MOF 1具有[Mg₄@Mg2]四面体建筑块,它们形成dia拓扑网络并有一个孔径为0.44 nm的一维孔道。而MOF 2具有独特的[Mg₂]双核簇,与4-连接配体L^4-配位后,形成sra拓扑网络且沿a轴方向存在一个哑铃型孔道,长度为1.42 nm。气体吸附研究发现1具有微孔结构,其表面积为342 m^2<...     

Separation of CO_2–N_2 using zeolite NaKA with high selectivity

The adsorption method based on solid adsorbents is one of feasible ways to capture and store CO_2. Using the ion exchange method, different zeolites Na KA varying in K+content were produced. The adsorption isotherms and kinetic uptakes were measured. The experimental results show that the optimal NaKA could adsorb significant quantities of CO_2 and little N_2. On the zeolite Na KA with 14.7 at.% K+, the adsorption capacity for pure CO_2 is over 3.10 mmol g~(-1) and the CO_2–N_2 selectivity is about 149 at ambient pressure and temperature. The kinetic CO_2–N_2 selectivity could also achieved 200 within 3 min according to the uptake data. To demonstrate the separation effectiveness, breakthrough curves of pure components and binary mixtures were investigated experimentally and theoretically in a fixed bed. It is found that the breakthrough points of CO_2 and N_2 are almost at the same time under the atmospheric pressure at 348 K with the raw gas composition CO_2/N_2(20:80, v/v). If the pressure has been increased higher than 0.1 MPa, CO_2 would break through the bed much slower than N_2. Therefore, the pressure may become the limiting factor for the separation performance of zeolites NaKA.     

Selective extraction of CO2 from simulated flue gas using polymeric ionic liquid sorbent coatings in solid-phase microextraction gas chromatography

The CO₂ selectivity of two polymeric task-specific ionic liquid sorbent coatings, poly(1-vinyl-3-hexylimidazolium) bis[(trifluoromethyl)sulfonyl]imide [poly(VHIM-NTf₂)] and poly(1-vinyl-3-hexylimidazolium) taurate [poly(VHIM-taurate)], was examined using solid-phase microextraction (SPME) for the determination of CO₂ in simulated flue gas. For comparison purposes, a commercial SPME fiber, Carboxen™-PDMS, was also studied. A study into the effect of humidity revealed that the poly(VHIM-taurate) fiber exhibited enhanced resistance to water, presumably due to the unique mechanism of CO₂ capture. The effect of temperature on the performance of the PIL-based and Carboxen fibers was examined by generating calibration curves under various temperatures. The sensitivity, linearity, and linear range of the three fibers were evaluated. The extraction of CH₄ and N₂ was performed and the selectivities of the PIL-based and Carboxen fibers were compared. The poly(VHIM-NTf₂) fiber was found to possess superior CO₂/CH₄ and CO₂/N₂ selectivities compared to the Carboxen fiber, despite the smaller film thicknesses of the PIL-based fibers. A scanning electron microscopy study suggests that the amine group of the poly(VHIM-taurate) is capable of selectively reacting with CO₂ but not CH₄ or N₂, resulting in a significant surface morphology change of the sorbent coating.     

湿磨法制备纳米Li_4SiO_4材料用于高温捕集CO_2

采用不同硅源、锂源以湿磨法结合高温焙烧制备了纳米Li_4SiO_4材料,利用X射线衍射(XRD)、扫描电子显微镜(SEM)和透射电子显微镜(TEM)表征了合成材料的结构和表面形貌,利用热重分析仪(TG)研究了Li_4SiO_4材料高温下的CO_2吸收性能和循环使用稳定性。结果表明,湿磨法制备的Li_4SiO_4材料在550℃、2.5×104Pa下,10min可达吸收平衡,平衡吸收量为27.9%(质量分数),经五次吸收-解吸后仍保持初始吸收性能,显示了良好的循环稳定性。将25%CO_2-25%N2-50%He混合气通过Li_4SiO_4材料床层,发现在550℃下,CO_2能被高效捕集,在相对湿度为10%的水汽存在下,Li_4SiO_4捕集CO_2的性能没有明显下降。     

氨基修饰的金属有机框架Cu_3(BTC)_2的制备及其CO_2吸附性能研究

首先制备了嫁接氨基的均苯三甲酸,同时以其为原料通过溶剂热法合成了金属有机框架材料Cu_3(NH_2BTC)_2,利用XRD、N_2吸附-脱附、热重、红外、原位红外分析等表征手段对吸附剂进行了表征,并通过固定床测量穿透曲线的方法研究其CO_2吸附性能。结果表明,氨基被成功引入Cu_3(BTC)_2骨架中。氨基修饰的Cu_3(BTC)_2对CO_2有着较高的吸附容量,在10 kPa,50℃的条件下CO_2吸附量为1.41 mmol/g,这源于材料对于CO_2同时存在着物理吸附和化学吸附。     

Removal of high concentration CO2 from natural gas at elevated pressure via absorption process in packed column

Carbon dioxide (CO2) removal is an essential step in natural gas (NG) processing to provide high quality gas stream products and minimize operational difficulties. This preliminary study aims to investigate the removal of CO2 at high concentration level from the mixture of CO2-NG gas stream at elevated pressure via absorption process. This is to explore the possibility of exploring high CO2 content natural gas reserves by treatment at offshore platform. A mixed amine solvent, Stonvent-II, was used for the absorption of approximately 75 vol% CO2 in CO2-NG stream at a pressure of 10 barg. The initial solvent temperature was varied in order to study the impact of initial temperature on the absorption performance. Preliminary study at temperatures of 35°C and 45°C indicates that Stonvent-II was able to perform almost 100% removal of CO2 under both conditions. However, the CO2 absorption effect took place faster when the initial liquid temperature was lower. This is because when the initial liquid temperature is high, the temperature increase in the packing bed caused by the reaction heat is high which impacts the efficiency of absorption negatively.     

Composite hollow fiber membranes for CO2 capture

Composite hollow fibers membranes were prepared by coating poly(phenylene oxide) (PPO) and polysulfone (PSf) hollow fibers with high molecular polyvinylamine (PVAm). Two procedures of coating hollow fibers outside and respective inside were investigated with respect to intrinsic PVAm solution properties and hollow fibers geometry and material.The influence of operating mode (sweep or vacuum) on the performances of membranes was investigated. Vacuum operating mode gave better results than using sweep because part of the sweep gas permeated into feed and induced an extra resistance to the most permeable gas the CO₂. The composite PVAm/PSf HF membranes having a 0.7–1.5 μm PVAm selective layer, showed CO₂/N₂ selectivity between 100 and 230. The selectivity was attributed to the CO₂ facilitated transport imposed by PVAm selective layer. The CO₂ permeance changed from 0.006 to 0.022 m³(STP)/(m² bar h) in direct correlation with CO₂ permeance and separation mechanism of the individual porous supports used for membrane fabrication. The multilayer PVAm/PPO membrane using as support PPO hollow fibers with a 40 nm PPO dense skin layer, surprisingly presented an increase in selectivity with the increase in CO₂ partial pressure. This trend was opposite to the facilitated transport characteristic behaviour of PVAm/porous PSf. This indicated that PVAm/PPO membrane represents a new membrane, with new properties and a hybrid mechanism, extremely stable at high pressure ratios. The CO₂/N₂ selectivity ranged between 20 and 500 and the CO₂ permeance from 0.11 to 2.3 m³(STP)/(m² bar h) depending on the operating conditions.For both PVAm/PSf and PVAm/PPO membranes, the CO₂ permeance was similar with the CO₂ permeance of uncoated hollow fiber supports, confirming that the CO₂ diffusion rate limiting step resides in the properties of the relatively thick support, not at the level of 1.2 μm thin and water swollen PVAm selective layer. A dynamic transfer of the CO₂ diffusion rate limiting step between PVAm top layer and PPO support was observed by changing the feed relative humidity (RH%). The CO₂ diffusion rate was controlled by the PPO support when using humid feed. At low feed humidity the 1.2 μm PVAm top layer becomes the CO₂ diffusion rate limiting step.     

Electrospun zeolitic imidazolate framework-8/poly(lactic acid) nanofibers for pipette-tip micro-solid phase extraction of carbamate insecticides from environmental samples

In the present study, electrospun zeolitic imidazolate framework-8/poly(lactic acid) nanofibers were successfully synthesized and characterized as a potential nanosorbent for the pipette-tip micro-solid phase extraction of chlorpropham, pirimicarb, carbaryl, and methiocarb carbamate insecticides from environmental water samples. The extraction procedure was followed by gas chromatography/mass spectrometry separation and determination of the target analytes. All the effective parameters of the extraction procedure were optimized through the one variable at-a-time method. Thanks to the very simple extraction procedure as well as the application of electrospun nanofibers with high surface area, the four analytes were efficiently extracted with as lowest extraction times as practicable. Under the optimal conditions, the calibration plots of the analytes were obtained within broad linear dynamic ranges of 0.5 – 150 ng mL^?1 for chlorpropham and pirimicarb plus 1.0 – 175 ng mL^?1 for carbaryl and methiocarb, respectively. Besides, limits of detection as low as 0.2 and 0.15 ng mL^?1 for chlorpropham and pirimicarb, respectively, as well as 0.5 ng mL^?1 for carbaryl and methiocarb indicate the favorable sensitivity of the analytical procedure. The applicability of the developed method was evaluated by quantitative determination of the target analytes in four different environmental water samples. Relative recoveries higher than 88.0% shows the acceptable accuracy of the method in the quantitative determination of the four carbamate insecticides.     

温和条件下CO2为原料电合成碳酸二甲酯

常温常压下, 研究了以CO₂和甲醇为原料电合成碳酸二甲酯的反应. 在四乙基溴化铵为支持电解质的乙腈溶液中, 通过恒电流电解得到了唯一的产物碳酸二甲酯. 为了优化电解条件, 分别考察了工作电极、电流密度、支持电解质、通电量以及电解前后加入甲醇顺序的不同等因素对该反应的影响. 以铜为工作电极, 石墨为对电极, 在17 mA•cm^－2的电流密度下恒电流电解, 当通过2 F•mol^－1的电量后, 碳酸二甲酯的产率可达74%, 大大高于文献报道值.     

CaO对Cu-ZnO-ZrO_2催化CO_2加H_2合成甲醇性能影响

用CaO作为改性助剂,采用并流共沉淀法制备了CuO∶ZnO∶ZrO_2为5∶4∶1(物质的量比),CaO添加量为0、1%、2%、4%、8%、16%(摩尔分数)的六组催化剂。用X射线衍射(XRD)、微商热重(TG-DTG)、傅里叶红外(FT-IR)、N2吸附脱附(BET)、X射线光电子能谱(XPS)、氢气程序升温还原(H_2-TPR)、CO_2程序升温脱附(CO_2-TPD)、NH_3程序升温脱附(NH_3-TPD)对催化剂进行了表征。用自制固定床评价了催化剂活性。结果表明,添加CaO后,催化剂路易斯酸性和表面碱性增强;催化剂母体中高温碳酸盐含量增加,热稳定性增强,CuO颗粒粒径变小,Cu-Zn协同作用增强,Cu比表面积增大,分散性变好。催化剂活性受到表面酸碱性、铜比表面积、Cu-Zn协同作用和铜分散性共同影响。当CaO为2%时,铜比表面积为79.3 m2/g、铜分散度为34.8%、CO_2转化率为24.55%、甲醇选择性为19.01%、甲醇收率为0.044 g/(gcat·h),催化剂活性最好。过量CaO占据催化剂孔道和覆盖表面活性位,使催化剂路易斯酸性和表面碱性过强,CuO与H_2有效接触减少,CO_2难以脱附,催化活性下降。因此,适量CaO(2%)添加可促进CO_2加氢反应合成甲醇。     

A parametric study of CO2/N2 gas separation membrane processes for post-combustion capture

Capture of CO₂ from flue gases produced by the combustion of fossil fuels and biomass in air is referred to as post-combustion capture. Chemisorbent processes are considered to be the most feasible method and are already at an advanced stage of development, but gas separation membranes are attracting more and more attention as a possible alternative. This paper describes a detailed parametric study of mass and energy balances for a simulated single membrane process. Typical operating conditions (CO₂ concentration in the flue gas, pressure and temperature, etc.) together with the influence of the membrane quality (permeability, selectivity) and membrane area on membrane performance (CO₂ separation degree and CO₂ purity) are simulated over a wide range of parameters.     

Fe/Al-SiO_2复合金属氧化物用于燃煤烟气中汞的脱除

采用不同方法制备了Fe/Al-SiO_2复合金属氧化物以模拟赤泥成分,模拟烟气条件下考察其脱汞性能。结果表明,采用溶胶-凝胶法得到的复合金属氧化物在300-450℃具有优异的脱汞性能,其中,在350℃、3 h内平均脱汞率可达到94.8%。Fe_2O_3为Hg~0的氧化提供了晶格氧和化学吸附氧;SiO_2形成的硅溶胶则有利于活性组分Fe_2O_3的分散,增强了Hg~0与活性位的接触。基本模拟烟气中存在微量HCl和NO时,Hg~0脱除率接近100%;当烟气中存在0.2 mL/min、0.4 mL/min的SO_2时,吸附剂的平均脱汞率分别降至90.7%、53.4%,这主要是由于SO_2与Fe_2O_3反应生成Fe_2(SO_4)_3,导致了Fe_2O_3的失活并抑制汞的脱除。     

Cu-ZnO-CeO2催化剂组成对CO2加H2合成甲醇性能的影响

采用并流沉淀法分别制备了CuO-CeO₂（物质的量比为5：1）、CuO-ZnO（物质的量比为5：4）、CuO-ZnO-CeO₂（物质的量比为5：4：1）三组目标催化剂,通过X射线衍射（XRD）、氢气升温还原（H₂-TPR）、CO₂程序升温脱附（CO₂-TPD）、氮气吸附-脱附、X射线光电子能谱（XPS）、N₂O滴定表征技术对催化剂的物化性能进行了测试,并在高温高压微催化反应器中对催化剂进行活性评价。研究了CuO-ZnO-CeO₂组成对CO₂加氢合成甲醇的影响。结果表明,与二组分催化剂相比较,三组分CuO-ZnO-CeO₂催化剂物化性能及催化活性发生了很大变化,催化剂表面碱性位增强,热稳定性增强,CuO颗粒粒径变小,铜分散度以及氧空位浓度提高,最终催化活性显著提高。其中,CuO-ZnO-CeO₂催化剂中,CuO颗粒粒径为8.2nm,铜的比表面积为68.4m²/g,铜分散度为7.19%,甲醇的选择性和收率分别为48.6%和0.057mmol/（g·min）,催化剂活性较好。