氢氛还原法制备氧化铁/膨润土 复合材料及其表征研究

以膨润土和硝酸铁为原料,采用氢氛还原法制备Fe₃O₄/膨润土复合材料,并采用X射线衍射（XRD）、扫描电子显微镜（SEM）和电子能谱（EDS）做表征分析。通过实验得到最佳的工艺条件：n（OH^-）∶n（Fe³⁺）=1∶1、铁土比为10 mmol/g、还原温度为200 ℃、还原时间为30 min。制备的Fe₃O₄/膨润土具有良好的类Fenton催化性能、稳定性与磁分离性能。制备过程中铁元素化合物能够有效固载在膨润土上,并在氢气还原作用下转化为Fe3O4,所得Fe3O4/膨润土是结构分散、孔隙明显、物化形态优良的催化复合材料。     

H2S removal and regeneration properties of Zn–Al-based sorbents promoted with various promoters

In order to improve the poor regeneration properties of the ZnO–Al₂O₃ (ZA)sorbent with a high sulfur removing capacity and fast H₂S absorption rate, 5–10 wt.% of various additives such as iron (Fe₂O₃), cobalt (Co₃O₄), nickel (NiO) and cerium oxide (CeO₂) were added to the ZA sorbent. These sorbents were prepared by the co-precipitation method and their sulfur removing capacities and regeneration properties were measured in a fixed-bed reactor during multiple cycles at middle-temperature ranges between 480 and 580 °C. The sulfur removing capacities of these sorbents measured 0.17–0.20 g S/g sorbent, which corresponded to 80% of the theoretical value and the values were maintained to within 10 cycles. The poor regeneration property of the ZA sorbent, which needed a long time (600 min), was also improved by addition of these promoters. These sorbents were regenerated completely within 300 min. The additives such as Fe, Co and Ni formed their aluminates, which did not change into sulfide form during sulfidation. The additives/aluminates played an important role in transforming S in ZnS into SO₂. Cerium dioxide showed a similar role with such aluminates in the oxidation of sulfur. The catalytic roles of the promoters and the changes in the physical properties of sorbents, during multiple cyclic tests, are discussed.     

高温抗烧结吸附剂对SeO2捕集性能

使用气固瞬时反应装置在700~1100℃下对不同氧化物（氧化镁、氧化铁、氧化铝、氧化钙）的硒捕集性能进行研究,确定吸附产物性质。基于此选取相应的典型矿物及双组分抗烧结吸附剂改善硒高温吸附能力。结果表明：900℃前氧化钙捕集效果最好,但1100℃时其吸附量迅速降低到167.59μg/g;γ-氧化铝在高温下捕集效果较好,1100℃时吸附量可达415.04μg/g,这与其优异的孔隙结构有关。钙基矿物方解石因其具有一定的抗烧结能力和发达的孔隙结构,表现出更好的高温捕集能力,1100℃时吸附量可提高到1064.97μg/g。双组分吸附剂高温捕集能力展现出不同程度的提高。钙-铝基吸附剂高温捕集性能提高相对较小;而钙-硅基吸附剂在高温下效果远高于单组分吸附剂,与氧化钙相比,1100℃时可提高1787.21μg/g。     

Na2CO3基吸附剂颗粒制备及其脱碳性能

采用挤压-滚圆法制备Na₂CO₃基CO₂吸附剂微球颗粒,在自行设计的CO₂吸收系统中对制备的样品进行脱碳性能测试。结合相关表征测试,探明不同载体、不同负载量的Na₂CO₃基吸附剂的微观结构、脱碳性能以及机械性能的变化规律和内在原因。研究表明：不同载体的Na₂CO₃基吸附剂颗粒脱碳性能存在明显差异,其中氧化铝负载的吸附剂（Na₂CO₃/Al₂O₃）的脱碳性能最好,可达1.14mmol/g。铝酸钙水泥负载的吸附剂（Na₂CO₃/CA）机械性能较好,但其脱碳性能最差。结合吸附剂脱碳和机械性能的综合考量,Na₂CO₃/Al₂O₃是最为合适的CO₂吸附剂,并进一步研究不同Na₂CO₃负载量的影响。研究发现随着Na₂CO₃负载量的变化,吸附剂的微观结构、脱碳性能以及机械性能都存在明显的差异。虽然60%负载量的Na₂CO₃/Al₂O₃吸附剂颗粒的机械性能和脱碳效果较好,但其成球度较差,影响其实际应用。质量分数40%负载量的Na₂CO₃/Al₂O₃吸附剂颗粒具有良好的脱碳性能、机械性能以及成球度,CO₂脱除量为1.36mmol/g。总体而言,利用挤压-滚圆法制备的Na₂CO₃基吸附剂颗粒具有良好的流动特性、脱碳性能和机械性能,适用于电厂烟气中的CO₂脱除。     

铁氧化物在流化床温度和CO气氛下的形态迁移及其对NO催化还原

利用小型固定床实验台实验研究了铁氧化物在典型流化床温度和CO还原性气氛下的形态迁移及其生成物对NO的催化还原作用,采用分级还原结合X射线衍射（XRD）表征分析,确定铁氧化物与CO和NO反应后生成物的价态及各种铁氧化物对NO的还原机制。结果表明,Fe₂O₃在实验条件下可依次被CO还原为Fe₃O₄、FeO和单质铁,反应过程中随着还原度的增加,还原速率逐级下降,从Fe₂O₃还原到Fe₃O₄的速率最高,FeO还原到Fe速率最低,在实验温度范围内,床温升高有利于提高Fe₂O₃到Fe₃O₄的还原速率和还原度。不同形态的铁氧化物对NO的催化还原特性不同,Fe₂O₃及其部分还原后生成的Fe₃O₄都不能直接与NO反应,Fe₂O₃对CO催化还原NO的效果很弱,而Fe₃O₄对CO还原NO的反应却有很强的催化作用,而进一步还原生成FeO与单质铁还可直接与NO反应。     

钙基碳载体造粒的捕集CO特性及力学性能

采用挤出滚圆法对钙基碳载体Ca（OH）₂进行造粒。在双固定床反应器上研究了黏结剂、支撑体和造孔剂对造粒后钙基碳载体循环捕集CO₂性能的影响,并提出采用多孔Al₂O₃球粉作为新型支撑体。结果表明,选择聚乙烯吡咯烷酮为颗粒黏结剂时最佳添加量为2%。高铝水泥和多孔Al₂O₃球粉均可作为支撑体造粒。多孔Al₂O₃球粉作为支撑体造粒后碳载体的循环捕集CO₂性能更高,其10次循环后CO₂吸收量为0.23g/g,是添加高铝水泥造粒碳载体的1.35倍。微晶纤维素作为造孔剂显著提高了造粒碳载体的循环捕集CO₂性能。多孔Al₂O₃球粉作为支撑体造粒后碳载体的抗压强度略高于高铝水泥作为支撑体。多孔Al₂O₃球粉造粒钙基碳载体拥有大量30~100nm孔隙,其比孔容高于高铝水泥造粒碳载体,这有利于CO₂捕集。     

Parametric study and effect of calcination and carbonation conditions on the CO2 capture performance of lithium orthosilicate sorbent

The world is currently facing the challenges of global warming and climate change. Numerous efforts have been taken to mitigate CO_2 emission, among which is the use of solid sorbents for CO_2 capture. In this work, Li_4SiO_4 was synthesised via a sol–gel method using lithium nitrate(LiNO_3) and tetraethylorthosilicate(Si C8 H20 O4) as precursors. A parametric study of Li:Si molar ratio(1-5), calcination temperature(600–800 °C) and calcination time(1–8 h) were conducted during sorbent synthesis. Calcination temperature(700–800 °C) and carbonation temperature(500–700 °C) during CO_2 sorption activity were also varied to confirm the optimum operating temperature. Sorbent with the highest CO_2 sorption capacity was finally introduced to several cyclic tests to study the durability of the sorbent through 10 cycles of CO_2 sorption–desorption test. The results showed that the calcination temperature of 800 °C and carbonation temperature of 700 °C were the best operating temperatures, with CO_2 sorption capacity of 7.95 mmol CO_2?(g sorbent)-1(93% of the theoretical yield). Throughout the ten cyclic processes, CO_2 sorption capacity of the sorbent had dropped approximately 16.2% from the first to the tenth cycle, which was a reasonable decline. Thus, it was concluded that Li_4SiO_4 is a potential CO_2 solid sorbent for high temperature CO_2 capture activity.     

稻壳白炭黑负载Fe2O3的气相芬顿反应NO预氧化

以稻壳为硅源,采用直接煅烧法制备白炭黑,以其为载体,采用共浸渍法制备Fe₂O₃/SiO₂催化剂;并采用同样方法以商用二氧化硅为载体制备Fe₂O₃/C-SiO₂催化剂,将二者用于催化H₂O₂预氧化NO的实验。探究不同工况（负载量、催化温度、H₂O₂汽化温度、H₂O₂流量和水汽浓度）对NO预氧化的影响,并对催化剂进行表征,分析其物理化学性质对催化性能的影响。结果表明,在负载量为50%、催化温度为140℃、H₂O₂汽化温度为120℃、H₂O₂流量为2.5mL/h时,达到最佳工况,NO氧化度能达到73%;在相同实验条件下Fe₂O₃/SiO₂催化剂的预氧化效果要比Fe₂O₃/C-SiO₂催化剂高20%左右。TPR结果表明载体可以降低活性组分的还原温度,减少活性组分的团聚;催化剂的晶相结构稳定,机械强度及热稳定性良好;ESR和XPS结果显示Fe₂O₃/SiO₂催化剂的催化性能优于Fe₂O₃/C-SiO₂催化剂,能够更好地催化分解H₂O₂产生·OH。     

Development of a novel nano-biosorbent for the removal of fluoride from water

The study was designed to investigate the use of two sorbents namely (i) Fe₃O₄ nanoparticles immobilized in sodiumalginate matrix (FNPSA) and (ii) Fe₃O₄ nanoparticles and saponified orange peel residue immobilized in sodium alginate matrix (FNPSOPR) as sorbents for fluoride removal from contaminated water. The synthesized nanoparticles were analyzed and characterized by dynamic light scattering, X-ray diffraction, vibrating sample magnetometry, and scanning electron microscopy with energy dispersive X-ray spectroscopy and Fourier transform-infrared spectrometry. The sorbentmatriceswere prepared in the formof beads and surface functionalized to enable enhanced sorption of fluoride ions. Batch sorption studieswere carried out and the sorption isotherm and reaction kinetics were analyzed. Both the sorbents followed Langmuir model of isotherm and fitted well with Pseudo first order reaction. The maximum sorption capacity exhibited by FNPSA and FNPSOPR was 58.24 mg·g^-1 and 80.33 mg·g^-1 respectively. Five sorption–desorption cycles exhibited 100%, 97.56%, 94.53%, 83.21%, and 76.53% of regeneration of FNPSOPR. Accordingly, it is demonstrated that FNSOPR could be used as a promising sorbent for easy and efficient removal of fluoride from contaminated water with good reusability. The current work suggests a simple and effective method to remove fluoride from contaminated water.     

Ethylene dimerization over NiSO4 supported on Fe2O3-promoted ZrO2 catalyst

The NiSO₄ supported on Fe₂O₃-promoted ZrO₂ catalysts were prepared by the impregnation method. Fe₂O₃-promoted ZrO₂ was prepared by the coprecipitation method using a mixed aqueous solution of zirconium oxychloride and iron nitrate solution followed by adding an aqueous ammonia solution. No diffraction line of nickel sulfate was observed up to 20 wt.%, indicating good dispersion of nickel sulfate on the surface of Fe₂O₃–ZrO₂. The addition of nickel sulfate (or Fe₂O₃) to ZrO₂ shifted the phase transition of ZrO₂ (from amorphous to tetragonal) to higher temperatures because of the interaction between nickel sulfate (or Fe₂O₃) and ZrO₂. 15-NiSO₄/5-Fe₂O₃–ZrO₂ containing 15 wt.% NiSO₄ and 5 mol% Fe₂O₃, and calcined at 500 °C exhibited a maximum catalytic activity for ethylene dimerization. NiSO₄/Fe₂O₃–ZrO₂ catalysts was very effective for ethylene dimerization even at room temperature, but Fe₂O₃–ZrO₂ without NiSO₄ did not exhibit any catalytic activity at all. The catalytic activities were correlated with the acidity of catalysts measured by the ammonia chemisorption method. The addition of Fe₂O₃ up to 5 mol% enhanced the acidity, surface area, thermal property, and catalytic activities of catalysts gradually, due to the interaction between Fe₂O₃ and ZrO₂ and due to consequent formation of Fe–O–Zr bond.     

Desulfurization of commercial fuels by π-complexation: Monolayer CuCl/γ-Al2O3

Monolayer CuCl/γ-Al₂O₃ sorbent was studied for desulfurization of a commercial jet fuel (364.3 ppmw S) and a commercial diesel (140 ppmw S). The sorbent was prepared by means of spontaneous monolayer dispersion methods. Deep desulfurization (sulfur levels of <1 ppmw) was accomplished with this sorbent using a fixed-bed adsorber. The CuCl/γ-Al₂O₃ sorbent was capable of removing 6.4 and 11.2 mg of sulfur per gram for jet fuel at breakthrough (at <1 ppmw S) and saturation, respectively. The same sorbent was capable of removing 0.94 and 1.8 mg of sulfur per gram for BP diesel at breakthrough and saturation, respectively. The difference in sulfur capacities for jet fuel and diesel was apparently caused by the difference in concentrations of strongly binding compounds, such as nitrogen heterocycles, heavy (polynuclear) aromatics and fuel additives. In comparison with CuCl/γ-Al₂O₃, Cu(I)Y zeolite has higher sulfur capacities but is less stable and can be easily oxidized to Cu(II)Y by fuel additives (such as oxygenates) and moisture and consequently loses π-complexation ability. However, all these cuprous π-complexation sorbents selectively adsorb thiophenic compounds over aromatics and olefins (as predicted by the high separation factors), which resulted in the observed desulfurization capability. A feasibility study is shown for efficient regeneration of CuCl/γ-Al₂O₃ using ultrasound at ambient temperature. Possible problems associated with desulfurization using π-complexation sorbents for commercial fuels are discussed.     

化学链燃烧过程Fe2O3/Al2O3载氧体表面CH4反应：ReaxFF-MD模拟

借助ReaxFF-MD方法,对化学链燃烧过程Al₂O₃负载Fe₂O₃载氧体（Fe₂O₃/Al₂O₃）表面CH₄反应过程模拟,探究Al₂O₃惰性载体对Fe₂O₃-CH₄体系燃烧过程的调控机制。研究发现添加Al₂O₃惰性载体改变了化学链燃烧过程中Fe₂O₃载氧体反应性和Fe₂O₃/Al₂O₃-CH₄反应体系的热力学和动力学行为。主要是促进了Fe₂O₃载氧体表面CH₄氧化,并对CH₄反应过程、中间体、产物及其反应速率和放热量等均具有显著促进和调控作用。原因在于Al₂O₃惰性载体对Fe₂O₃活性相中晶格氧的活化作用促进了晶格氧的迁移-扩散-释放。添加惰性载体增强了Fe₂O₃载氧体在化学链燃烧过程晶格氧释放速率和释放量,有利于CH₄氧化燃烧向合成气的高效、清洁转化,强化了化学链燃烧过程,满足当前能源高效转化和碳减排目标。     

化学链燃烧过程Fe2O3/Al2O3载氧体表面CH4反应：ReaxFF-MD模拟

借助ReaxFF-MD方法,对化学链燃烧过程Al₂O₃负载Fe₂O₃载氧体（Fe₂O₃/Al₂O₃）表面CH₄反应过程模拟,探究Al₂O₃惰性载体对Fe₂O₃-CH₄体系燃烧过程的调控机制。研究发现添加Al₂O₃惰性载体改变了化学链燃烧过程中Fe₂O₃载氧体反应性和Fe₂O₃/Al₂O₃-CH₄反应体系的热力学和动力学行为。主要是促进了Fe₂O₃载氧体表面CH₄氧化,并对CH₄反应过程、中间体、产物及其反应速率和放热量等均具有显著促进和调控作用。原因在于Al₂O₃惰性载体对Fe₂O₃活性相中晶格氧的活化作用促进了晶格氧的迁移-扩散-释放。添加惰性载体增强了Fe₂O₃载氧体在化学链燃烧过程晶格氧释放速率和释放量,有利于CH₄氧化燃烧向合成气的高效、清洁转化,强化了化学链燃烧过程,满足当前能源高效转化和碳减排目标。     

基于铁基载氧体的无烟煤化学链燃烧过程中硫分布特性

在间歇式固定床反应器上,基于Fe₂O₃/Al₂O₃载氧体,研究了还原阶段反应温度和Fe₂O₃负载量对无烟煤化学链燃烧产物及S元素分布的影响。研究结果表明,含碳气体释放量随反应温度升高而增加,随Fe₂O₃负载量先增加后减少。产物中CO₂比例随反应温度升高先增加后减少,在850℃时达到最高（37.6%）。在实验条件下,未检测到SO₂生成。反应2 h时,载氧体中S元素的富集程度随温度和Fe₂O₃负载量升高而增加;5.5 h时,载氧体中S元素分布比例随温度升高而显著降低。利用SEM分析了载氧体表面微观形态结构。分析表明,Fe₂O₃负载量大于40%会导致载氧体轻微烧结。     

氧化铁/石墨烯原位复合物对铬酸钾吸附性能研究

采用共沉淀法制备Fe_3O_4磁性纳米颗粒以及通过原位生长法制备Fe_3O_4与氧化石墨烯的复合物,并加入十六烷基三甲基溴化铵形成共价键交联反应化合物。采用X射线衍射仪和透射电子显微镜表征样品的形貌与尺寸,并以铬酸钾为吸附对象,研究吸附温度、吸附时间和溶液p H值对Fe_3O_4吸附性能的影响。结果表明,椭圆形颗粒的Fe_3O_4尺寸约(10~15)nm,与氧化石墨烯复合后,分散性明显提高;在室温和p H=3.5条件下,以Fe_3O_4与氧化石墨烯的质量比2∶1复合物作为吸附剂对铬酸钾的吸附效果达到最佳,每克的吸附容量可达251 mg;复合物经过磁分离、反复吸附循环实验6次后,对铬酸钾的吸附率仅下降10个百分点。     

Efficient MgO-doped CaO sorbent pellets for high temperature CO2 capture

Novel MgO-doped CaO sorbent pellets were prepared by gel-casting and wet impregnation. The effect of Na⁺ and MgO on the structure and CO₂ adsorption performance of CaO sorbent pellets was elucidated. MgO-doped CaO sorbent pellets with the diameter range of 0.5-1.5 mm exhibited an excellent capacity for CO₂ adsorption and adsorption rate due to the homogeneous dispersion of MgO in the sorbent pellets and its effects on the physical structure of sorbents. The results show that MgO can effectively inhibit the sintering of CaO and retain the adsorption capacity of sorbents during multiple adsorption-desorption cycles. The presence of mesopores and macropores resulted in appreciable change of volume from CaO (16.7 cm³∙mol⁻¹) to CaCO₃ (36.9 cm³∙mol⁻¹) over repeated operation cycles. Ca2Mg1 sorbent pellets exhibited favorable CO₂ capture capacity (9.49 mmol∙g⁻¹), average adsorption rate (0.32 mmol∙g⁻¹∙min⁻¹) and conversion rate of CaO (74.83%) after 30 cycles.     

HYDROTHERMAL REACTION OF FLY ASH/HYDRATED LIME: CHARACTERIZATION OF THE REACTION PRODUCTS

Class F coal fly ash was slurried with hydrated lime at 90°C in 1/3, 5/3, 9/3, and 15/3 weight ratios and for 3, 5, 7, and 9 hours of hydration, in a process to prepare sorbents for SO₂ removal. The amounts of aluminum, silicon, and calcium in the product of the pozzolanic reaction were determined in order to study the evolution of product composition with the initial raw materials ratio and hydration time and to relate this composition to the desulfurization capability of the material. Al, Si, and Ca were present in the solid product for any raw materials ratio and hydration time, showing that calcium silicates, calcium aluminates, and/or calcium aluminum silicates were obtained simultaneously. The products formed show a nearly constant molar ratio of Al₂O₃/SiO₂ independent of the experimental conditions tested and similar to the Al₂O₃/SiO₂ ratio in the fly ash. The SiO₂/CaO molar ratio in the products decreased as the initial fly ash/Ca(OH)₂ ratio decreased, being approximately constant for each ratio with respect to hydration time after 5 hours of hydration. The maximum moles of CaO, SiO₂, and Al₂O₃ per gram of sorbent in the reaction product were found for any hydration time for the 5/3 sorbents, meaning that at this initial ratio the pozzolanic reaction takes place at the highest rate. The capacity of the sorbent for SO₂ removal depends not only on the amount of products produced by the pozzolanic reaction but also on the specific surface area of the sorbent.     

PREPARATION OF PEROVSKITE 0.75Pb(Ni1/3Nb2/3)O3-0.25PbTiO3 CERAMICS USING SEMICHEMICAL METHODS AND RELATED REACTION MECHANISMS

This article discusses a mechanism for preparing perovskite powders, 0.75Pb(Ni_1/3Nb_2/3)O₃-0.25PbTiO₃ (PNN-PT), using a semichemical method (SCM).Precursors were prepared by adding aqueous Ni(Ac)₂ solutions to an alcohol slurry of PbO, Nb₂O₅, and TiO₂. The TG-DTG and DSC analysis of the precursors and XRD analysis of the powders at different thermal treatment temperatures showed that the reaction mechanisms in this method differ from those in the conventional mixed-oxide method. The aqueous Ni(Ac)₂ solution reacted with PbO to form Pb(Ac)₂ · Pb(OH)₂ · H₂O and Ni(OH)₂, which decomposed to form nascent PbO and NiO, thereby improving the reactivity and distribution of PbO and NiO. Pb₃Nb₂O₈ and NiNb₂O₆ formed and were easily converted into the perovskite phase during the thermal treatment process. At a thermal treatment temperature of 850°C, the content of the perovskite phase reached 98%. Pyrochlore-free PNN-PT ceramic was obtained after 2 h of sintering at 1100°C, and its dielectric properties were found to be excellent at temperatures ranging between -55 and 120°C.     

纳米四氧化三铁的制备及表面修饰研究

采用化学共沉淀法制备了纳米四氧化三铁,并利用IR和XRD对其进行了表征。利用γ-氨基丙基三乙氧基硅烷（KH-550）对四氧化三铁表面进行预处理,考察了水解时间、pH等因素对KH-550水解电导率的影响,讨论了Fe_3O_4与KH-550配比、反应温度和反应时间等因素对Fe_3O_4表面羟基数的影响。以丙烯酰胺为功能单体,过硫酸铵为引发剂,对偶联后的四氧化三铁进行接枝共聚,制备了Fe_3O_4/KH-550/PAM磁性高分子复合物,并用IR对磁性高分子复合物的结构进行了表征。     

Piezoelectric properties of Pb(Mn1/3Nb2/3)O3–PbZrO3–PbTiO3 ceramics with sintering aid of 2CaO–Fe2O3 compound

Since the electromechanical devices move towards enhanced power density, high mechanical quality factor (Q_m) and electromechanical coupling factor (k_p) are commonly needed for the high powered piezoelectric transformer with Q_m≥2000 and k_p=0.60. Although Pb(Mn_1/3Nb_2/3)O₃–PbZrO₃–PbTiO₃ (PMnN–PZ–PT) ceramic system has potential for piezoelectric transformer application, further improvements of Q_m and k_p are needed. Addition of 2CaO–Fe₂O₃ has been proved to have many beneficial effects on Pb(Zr,Ti)O₃ ceramics. Therefore, 2CaO–Fe₂O₃ is used as additive in order to improve the piezoelectric properties in this study. The piezoelectric properties, density and microstructures of 0.07Pb(Mn_1/3Nb_2/3)O₃–0.468PbZrO₃–0.462PbTiO₃ (PMnN–PZ–PT) piezoelectric ceramics with 2CaO–Fe₂O₃ additive sintered at 1100 and 1250 °C have been studied. When sintering temperature is 1250 °C, Q_m has the maximum 2150 with 0.3 wt.% 2CaO–Fe₂O₃ addition. The k_p more than 0.6 is observed for samples sintered at 1100 °C. The addition of 2CaO–Fe₂O₃ can significantly enhance the densification of PMnN–PZ–PT ceramics when the sintering temperature is 1250 °C. The grain growth occurred with the amount of 2CaO–Fe₂O₃ at both sintering temperatures.