面向丙烯/丙烷吸附分离的金属有机骨架材料的高通量计算筛选

丙烯、丙烷作为分子尺寸相近的共沸物,其分离一直是化工领域研究热点。金属有机骨架(MOFs)材料因其高度可调的孔道结构,在丙烯/丙烷分离应用上已展现出诱人潜能。本文基于Core MOF 2019数据库,采用巨正则蒙特卡洛基高通量计算筛选技术,获得了分离性优异的MOFs结构,发现其拥有适中的丙烯吸附量和较弱的丙烷吸附能力,且骨架孔径为3.70～4.10?、孔隙率中等(0.35～0.44),并揭示了孔道中心吸附位的选择性与丙烯/丙烷分离系数间关系。本研究阐明了高丙烯/丙烷分离性的骨架材料的结构和性能特征,为设计MOFs实现丙烯/丙烷的高效分离提供理论指导和数据支撑。     

丙烯对丙烷脱氢催化剂PtSnK/Al2O3炭沉积行为的影响

以含有不同比例丙烯的丙烷为原料进行丙烷脱氢反应,重点考察富丙烯条件下Pt基催化剂上的碳沉积行为。研究结果表明,原料中丙烯的存在加快了催化剂的积炭速率,缩短了积炭在载体上达到积炭平衡的时间,促进了活性相表面积炭的形成及积炭石墨化;同时原料中富含丙烯,使不饱和脂肪族化合物的生成量增加,从而促进了芳香性的碳、石墨化的碳的生成,但催化剂结构未遭到破坏。在丙烷脱氢过程中,当丙烯含量增加到1.5%时,出现活性相表面上的积炭“峰Ⅰ”,而“峰Ⅱ”向高温区移动。当烯烃含量增加3.0%时,峰Ⅰ和峰Ⅱ融合在一起,整个峰的面积明显增加,积炭量超过10.26%时,催化剂积炭石墨化程度越来越高。丙烯含量增加,加速了载体的容碳能力迅速饱和过程,同样的反应时间下,积炭量增加。     

氟对PtSnNaLa/ZSM-5催化剂丙烷脱氢反应性能的影响

在PtSnNaLa/ZSM-5催化剂中引入氟元素,制得用于丙烷脱氢反应的氟改性催化剂,利用X射线衍射(XRD)、NH₃吸脱附(NH₃-TPD)、红外(FT-IR) 、固体核磁(²⁷Al MAS NMR)和程序升温还原(H₂-TPR)等技术手段研究不同氟含量对催化剂的结构、表面酸性和丙烷脱氢反应性能的影响。 结果表明,氟能降低催化剂表面的弱酸强度,增强Pt与载体间的相互作用力,降低反应副产物的选择性,从而提高了产物丙烯的选择性,当氟的添加量为0.2%时,丙烯选择性可达到99.2%。 同时氟的加入易于载体骨架的脱铝,使得Sn组分的还原变得相对容易,但对催化剂结构没有明显的影响。     

Na对PtSn/ZSM-5催化丙烷脱氢反应性能的影响

以HZSM-5分子筛为载体, 利用分步浸渍法制得不同Na含量的PtSnNa/ZSM-5催化剂, 用于丙烷脱氢反应. 利用XRD、吡啶吸附红外光谱、NH3-TPD、氢化学吸附、TPR等手段, 研究了Na的添加对PtSn/ZSM-5催化剂物化性质的影响. 结果表明: Na的添加对PtSn/ZSM-5催化剂的反应性能影响明显. 适量Na的添加不仅降低了催化剂中的Brönsted酸中心和Lewis中强/强酸中心, 抑制了积碳的发生, 提高了催化反应的稳定性; 而且提高了催化剂表面的Pt金属裸露度, 增加了反应活性. 当Na含量为1.0%(w)时, 催化剂的丙烯选择性和收率达到最大, 反应30 h后, 丙烷转化率仍然保持很高(36.4%). 继续增加Na含量, 催化剂中的Lewis弱酸中心有所增加, 同时Sn组分易于被还原成Sn0, 丙烷裂解、氢解等副反应增加, 不利于脱氢反应的进行.     

介孔CeNiO催化剂的合成及其丙烷氧化脱氢制丙烯反应性能

以十二烷基硫酸钠（SDS）和三嵌段共聚物P123为混合模板剂,尿素为沉淀剂,采用均匀沉淀法制备了具有介孔结构的NiO和CeNiO催化剂.考察了催化剂的丙烷氧化脱氧反应性能,并利用用N₂吸附-脱附、透射电镜（TEM）、X射线粉末衍射（XRD）和H₂程序升温还原（H₂-TPR）等技术对催化剂进行了表征.活性测试结果表明,在400-450℃范围内NiO和CeNiO催化剂有相似的催化性能,但后者表现出较高的低温（<400℃）催化活性.325℃反应时,纯NiO上丙烯收率仅为3.1%,而5CeNiO(n_Ce/n_Ni=5%)催化剂上丙烯收率高达12.2%.N₂吸附-脱附和TEM结果表明,制备的NiO和CeNiO催化剂均有较大的比表面积且具有虫孔状介孔结构.H₂-TPR结果表明,CeNiO催化剂中由于Ce的存在使得得一部分氧物种的可还原性能明显增强,这可能是该催化剂具有较高催化活性的重要原因.     

添加锡组分对Pt/ZSM-5催化剂丙烷脱氢反应性能的影响

丙烷脱氢制丙烯是优化利用炼厂气和油田伴生气资源的一条重要途径,这方面的研究已日益引起研究者的关注[1～5].对γ-Al2O3为载体的负载型铂催化剂丙烷脱氢催化性能已进行了深入的研究.通过引入特定的助剂,可以提高负载型铂催化剂低碳烷烃脱氢选择性和稳定性[6,7].与Ce、Zn、V、La、Cr、Fe、Zr、Mn等助剂比较,Sn助剂更有利于提高催化剂丙烷脱氢的反应稳定性[8].     

Cr对Pt-Sn/γ-Al2O3催化剂丙烷脱氢性能的影响

通过H2-TPR、O2-脉冲等表征手段,结合丙烷脱氢催化性能考察了助剂Cr对Pt-Sn/γ-Al2O3催化剂反应性能的影响。结果表明,添加少量Cr可显著改善Pt-Sn/γ-Al2O3催化剂的脱氢稳定性,可提高丙烯选择性,降低催化剂表面积炭量。这是由Cr和Pt-Sn之间存在的协同作用引起的,一方面,Pt促进了Cr的还原,生成了可提高丙烯选择性的+3价Cr;另一方面,Cr使Sn变得难于还原,在强还原气氛下保持了活性氧化态价态,进而改善了催化剂的脱氢稳定性。     

过渡金属修饰对Pt/M-DMSN催化剂丙烷脱氢性能的影响

以两步法制备了一系列过渡金属(M=Fe, Co, Ni, Cu, Zn)修饰的树枝状介孔二氧化硅纳米粒子(DMSN)负载铂(Pt/M-DMSN)催化剂, 并对该系列催化剂进行了丙烷催化脱氢性能评价. X射线衍射(XRD)、 透射电子显微镜(TEM)、 紫外-可见漫反射光谱(UV-Vis DRS)和氢气程序升温还原(H₂-TPR)表征结果表明, 不同过渡金属在DMSN载体表面分散状态不同,且与Pt的相互作用程度不同. 其中Zn-DMSN载体最有利于Pt的分散, 且反应后催化剂上积碳含量最低; Pt/Fe-DMSN催化剂中Pt与载体的相互作用力较强. 通过活性评价结果可知, Pt/Fe-DMSN催化剂表现出最优的丙烷催化脱氢性能, 丙烷初始转化率为44.2%, 反应6 h后丙烷转化率仍可达36.5%.     

Ca对PtSn／MgAl2O4结构及丙烷脱氢性能的影响

比较研究了Ｃａ改性的ＰｔＳｎ／ＭｇＡｌ２Ｏ４在氮气及水蒸汽稀稀释下的丙烷脱氢性能，并利用ＴＰＲ、Ｈ２－ＴＰＤ、ＸＰＳ及脉冲氢吸附对催化剂进行了表征，结果表明，ＰｔＳｎ／ＭｇＡｌ２Ｏ４中加入０．５％的Ｃａ，增加了催化剂的丙烷脱氢活性，抑制了积炭失活，过量Ｃａ的加入则促进了催化剂中Ｓｎ组分的还原，生成了零价锡并可能与Ｐｔ形成合金，从而导致催化剂失活。在水汽中反应哩，水蒸汽一方面可调变催化剂结构，增加其     

B修饰的ZrO2及其制备p H值对PtSn/B-ZrO2丙烷脱氢反应性能的影响（英文）

丙烯作为一种重要的石油化工基础原料,传统上是从石脑油蒸汽裂解或催化裂化过程中作为副产物生产的.随着原油的枯竭和页岩气开发技术的成熟,通过乙烷蒸汽裂解制备乙烯更具吸引力并已得到广泛的工业应用,但该路线乙烯选择性高,而副产物丙烯数量有限.为满足不断增加的丙烯需求量,利用油田气和页岩气中低附加值的丙烷为原料,将其直接脱氢制丙烯(PDH)具有重要的现实意义.目前已开发成功的PDH技术采用的催化剂主要为负载PtSn型催化剂和Cr基催化剂.其中,Pt基催化剂较Cr基催化剂更加环境友好,因此得到了更广泛的应用.由于Pt元素的昂贵和稀有,制备低Pt含量和良好性能的催化剂极具吸引力.UOP Oleflex工艺开发的最新一代催化剂DEH-16仅含有0.3 wt%Pt,相对于前一代催化剂Pt含量降低30%.然而,许多文献报道,随着Pt含量的降低,催化剂的稳定性很容易恶化,降低Pt含量并保持催化剂性能仍具有一定的挑战.研究表明,含有更多Lewis酸性位点和更少Bronsted酸位点的催化剂显示出较好的丙烷脱氢活性和丙烯选择性.此外,源自缺陷位或配位不饱和位的Lewis酸性位也可为负载的金属颗粒提供锚定位点.BASF对ZrO2作为载体的丙烷脱氢催化剂进行了广泛研究,但其催化剂尚未完全商业化.有文献报道,ZrO2负载的PtSn催化剂在脱氢反应中的稳定性较差.将元素硼(B)加入到ZrO2中可以极大地抑制Bronsted酸性而提高Lewis酸量和酸强度,因此我们推测含有适量配位不饱和Zr位点的ZrO2作为PtSn丙烷脱氢催化剂载体可能具有优异的性能.载体的合成pH值对催化剂PDH性能也会有影响.然而,目前还没有硼改性的ZrO2(B-ZrO2)合成pH值对PDH催化性能影响的研究.本文研究了B-ZrO2的合成pH值(9,10和11)对PtSn/B-ZrO2在丙烷脱氢反应中催化性能的影响.Py-IR结果表明各pH值下合成的B-ZrO2均只有Lewis酸,NH3-TPD结果则表明B-ZrO2的Lewis酸量和强度随合成pH值的增加而增加.XPS结果显示,载体对Pt和Sn电子性质的影响不容忽视.由于OSC与CO氧化活性之间没有线性关系,因此Pt和Sn之间的相互作用程度在CO氧化反应中可能起主要作用,并有如下递增趋势:PtSn/B-ZrO2-9相似文献   

A Self-Assembled Capsule for Propylene/Propane Separation

The development of energy-saving technology for the efficient separation of olefin and paraffin is highly important for the chemical industry. Herein, we report a self-assembled Fe₄L₆ capsule containing a hydrophobic cavity, which can be used to encapsulate and separate propylene/propane. The successful encapsulation of propylene and propane by the Fe₄L₆ cage in a water solution was documented by NMR spectroscopy. The binding constants K for the Fe₄L₆ cage toward propylene and propane were determined to be (5.0±0.1)×10³ M⁻¹ and (2.1±0.7)×10⁴ M⁻¹ in D₂O at 25 °C, respectively. Experiments and theoretical studies revealed that the cage exhibited multiple weak interactions with propylene and propane. The polymer-grade propylene (>99.5 %) can be obtained from a mixture of propylene and propane by using the Fe₄L₆ cage as a separation material in a U-shaped glass tube. This work provides a new strategy for the separation of olefin/paraffin.     

Ultrafast Semi-Solid Processing of Highly Durable ZIF-8 Membranes for Propylene/Propane Separation

ZIF-8 membranes have emerged as the most promising candidate for propylene/propane (C₃H₆/C₃H₈) separation through its precise molecular sieving characteristics. The poor reproducibility and durability, and high cost, thus far hinder the scalable synthesis and industrial application of ZIF-8 membranes. Herein, we report a semi-solid process featuring ultrafast and high-yield synthesis, and outstanding scalability for reproducible fabrication of ZIF-8 membranes. The membranes show excellent C₃H₆/C₃H₈ separation performance in a wide temperature and pressure range, and remarkable stability over 6 months. The ZIF-8 membrane features dimethylacetamide entrapped ZIF-8 crystals retaining the same diffusion characteristics but offering enhanced adsorptive selectivity for C₃H₆/C₃H₈. The ZIF-8 membrane was prepared on a commercial flat-sheet ceramic substrate. A prototypical plate-and-frame membrane module with an effective membrane area of about 300 cm² was used for efficient C₃H₆/C₃H₈ separation.     

Mechanical Control of the Kinetic Propylene/Propane Separation by Zeolitic Imidazolate Framework‐8

One intriguing feature of many porous MOFs is their stimulus‐induced flexibility, which makes them unique compared to standard adsorbents. Here we propose an innovative concept to achieve an efficient kinetic separation of species with similar properties by the mechanical fine‐tuning of the pore architecture of the flexible zeolitic imidazolate framework ZIF‐8. This unprecedented approach was applied to one of the most challenging societally relevant separations: the separation of propylene and propane, which is of vital importance in the petrochemical industry. It was demonstrated that the application of an external pressure creates a gradual enhancement in the propylene/propane diffusion selectivity to more than one order of magnitude at 1 GPa pressure. A detailed analysis of the molecular simulations was further able to unravel the origin of this unusual behavior at the atomistic level.     

Uniformly Distributed Mixed Matrix Membranes via a Solution Processable Strategy for Propylene/Propane Separation

Aggregation of filler particles during the formation of mixed matrix membranes is difficult to avoid when filler loadings exceed a 10–15 wt %. Such agglomeration usually leads to poor membrane performance. In this work, using a ZIF-67 metal–organic framework (MOF) as filler along with surface modification of Ag₄tz₄ to improve processability and selective olefin adsorption, we demonstrate that highly loaded with a very low agglomeration degree membranes can be synthesized displaying unmatched separation selectivity (39) for C₃H₆/C₃H₈ mixtures and high permeability rates (99 Barrer), far surpassing previous reports in the literature. Through molecular dynamics simulation, the enhanced compatibility between ZIF-67 and polymer matrix with adding Ag₄tz₄ was proven and the tendency in gas permeability and C₃H₆ selectivity in the mixed matrix membranes (MMMs) were well explained. More importantly, the membrane showed a wide range of pressure and temperature resistance, together with remarkable long-term stability (>900 h). The modification method might help solve interface issues in MMMs and can be extended to the fabrication of other fillers to achieve high performance MMMs for gas separation.     

Effects of Olefins on the Thermal Decomposition of Propane Part IV. Influence of Propylene

On the basis of the thermal decomposition of mixtures of propylene and propane with molar ratios of 0.0–0.33 in the temperature range 779–812K, the influencing functions describing the inhibition by propylene of the decomposition of propane were determined. The rate-reducing effect is explained mainly by the reactions (in which ^.R = ^.H, ^.CH₃ and 2-?₃H₇) and also by the addition reactions It was established that the bulk of the allyl radicals formed participate in the chain step, but, due to their lower reactivity, they restore the decomposition chain more slowly than the original radicals do. From the characteristic change in the ratio υ/υ, the rate ratios of hydrogenabstraction reaction by radicals from propylene and propane could be determined. In these reactions there was no significant difference between the selectivities of the radicals. For an interpretation of the changes, the decomposition mechanism must be completed with the reaction Evaluation of the influencing curves revealed that the initiation reactions must be taken into account. By parameter estimation we have determined the rate ratios characterizing the above initiation reactions, the unimolecular decomposition of propane, hydrogen abstraction by radicals from propane and propylene, intermolecular isomerization of the 2-propyl radical via propane and propylene, and abstraction of propane hydrogens by the ethyl and methyl radicals; these are given in Tables II.     

High‐Flux Zeolitic Imidazolate Framework Membranes for Propylene/Propane Separation by Postsynthetic Linker Exchange

While zeolitic imidazolate framework, ZIF‐8, membranes show impressive propylene/propane separation, their throughput needs to be greatly improved for practical applications. A method is described that drastically reduces the effective thickness of ZIF‐8 membranes, thereby substantially improving their propylene permeance (that is, flux). The new strategy is based on a controlled single‐crystal to single‐crystal linker exchange of 2‐methylimidazole in ZIF‐8 membrane grains with 2‐imidazolecarboxaldehyde (ZIF‐90 linker), thereby enlarging the effective aperture size of ZIF‐8. The linker‐exchanged ZIF‐8 membranes showed a drastic increase in propylene permeance by about four times, with a negligible loss in propylene/propane separation factor when compared to as‐prepared membranes. The linker‐exchange effect depends on the membrane synthesis method.     

分离丙烯/丙烷的超薄聚电解质中空纤维复合膜的制备

以含二氮杂萘联苯结构的聚芳醚砜酮PPESK(Tg为263~305℃)为膜材料,以干-湿纺丝技术制备基膜,外涂法涂覆聚电解质(聚乙烯基吡咯烷酮PVP)并络合Ag 离子,制备了超薄皮层中空纤维复合膜,皮层厚度约为1μm。研究了复合膜聚电解质涂层PVP质量分数、Ag 含量、气体压力差、测试温度和不同过渡金属离子等对复合膜丙烯/丙烷分离性能的影响。结果表明,在压力为200kPa、温度为23℃下,当PVP质量分数为10%、n(Ag )∶n(CO)=1∶1的条件下,复合膜对丙烯渗透率可达16.32GPU,分离系数为4.79。     

Cr/NaZSM-5催化剂上CO2氧化丙烷脱氢反应

以亚微米级NaZSM-5为载体合成了一系列负载型Cr催化剂, 采用氮气吸附、 XRD、 UV-Vis和H2-TPR对Cr/NaZSM-5催化剂的结构和织构性质进行了表征, 并评价了催化剂在CO2气氛下的丙烷脱氢性能. 硅铝摩尔比为60, Cr质量分数为3%的催化剂具有最高的反应活性, 于550 ℃反应10 min和8 h后的丙烷转化率分别为48.3%和30.1%, 丙烯选择性则分别为86.0%和91.8%. 催化剂中的Cr6+含量和反应初活性具有良好的对应关系, 表明高Cr6+含量对催化剂表现出高的丙烷脱氢活性是至关重要的. CO2气氛下的丙烯产率明显比氮气气氛下的高, 这是由于CO2气氛下催化剂表面有较多量的Cr6+, 并且CO2可通过逆水煤气变换反应除去脱氢反应生成的氢.     

SBA-15负载高分散纳米NiO的丙烷氧化脱氢制丙烯催化性能

采用浸渍法通过改变焙烧气氛制备了系列NiO/SBA-15 (w_NiO=20%)催化剂, 并考察了催化剂的丙烷氧化脱氢(ODHP)反应性能. 实验结果表明, 与在静止和流动空气中焙烧的催化剂相比, 在1%NO/He (V_NO/V_He=1:99)气氛中焙烧的NiO/SBA-15-NO具有优异的低温丙烷氧化脱氢制丙烯性能, 在350 ℃时, 丙烷的转化率和丙烯收率分别约达29%和13%. 反应温度升至450 ℃时, 丙烯的选择性仍保持在45%左右. X射线粉末衍射(XRD)和透射电镜(TEM)测试结果表明, 1%NO/He气氛可有效抑制焙烧过程中NiO纳米颗粒的团聚, 使NiO物种高分散于SBA-15 的孔道中. H₂-程序升温还原(H₂-TPR)和O₂-程序升温脱附(O₂-TPD)测试结果表明, 随着NiO在SBA-15上分散度的提高, 催化剂的抗还原性增强, ODHP活性氧物种O-的含量增加, 进而使1%NO/He气氛中焙烧的NiO/SBA-15-NO在较宽的温度范围内(350-450 ℃)均具有良好的丙烯选择性, 并显著提高了催化剂的低温活性.