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561.
《International Journal of Hydrogen Energy》2022,47(3):2050-2058
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562.
《International Journal of Hydrogen Energy》2019,44(7):3569-3579
N-decane decomposition with plasma to obtain prone detonation gaseous fuel is investigated by adopting fuel liquid film feeding mode at applied voltage of 10 kV and 15 kV, discharge frequency of 300–3000 Hz with interval 100 Hz. The result shows that the discharge parameters can regulate the composition and the concentration of the cracked products. When the composition of the product is unchanged, the concentration and proportion of the components can be increased as the discharge frequency becomes higher. The hydrogen concentration increases 3.4 times and 2.3 times respectively for the applied voltage of 15 kV and 10 kV as the discharge frequency is increased from 500 to 3000 Hz. However, the voltage has no effect on the proportion of the components, and increasing the voltage only increases the concentration of the species. For selectivity, raising the discharge frequency can greatly increase the species selectivity of hydrogen and acetylene that are most prone to detonate. The selectivities of hydrogen and acetylene are the highest at 15 kV and 3 kHz, reaching 18.40% and 4.22% respectively, and at this time, the selectivity of ethylene is the lowest, which is 60.4%. Besides, it is confirmed that high selectivity can be achieved at the lower specific energy input causing by low-voltage/high-frequency discharge. Through the analysis of the bond dissociation energy, there is a competitive relationship between the production of ethylene, ethane and pentane which all consume ethyl, and two possible pathways for the production of acetylene are put forward. 相似文献
563.
《International Journal of Hydrogen Energy》2019,44(16):8659-8668
Catalytic lanthanum ions (La3+), beneficial for fast dissociative adsorption of hydrogen on its surface, were chosen and introduced into SnO2 nanofibers with different atomic molar ratio to Sn (AMR: 0.5%, 1.0% and 3%) via electrospinning and calcination technique. The sensitivity of LaSnO2 metastable solid solution nanofibers (LSMSSNs) for H2 detection is 9.9 against 100 ppm H2 at 300 °C, which is 2.5 times and 1.6 times higher than that of SnO2 nanofibers and La2O3@SnO2 p-n heterojunction nanofibers (LSPNHNs), respectively. More importantly, LSMSSNs achieved both rapid response and recovery behavior of ∼ 1s, long range detectable linearity from 1000 to 25,000 p.m. against H2 and good selectivity towards ethanol, toluene, carbon monoxide and butane, which is very useful for the practical application. A plausible sensing mechanism based on p-type La3+ doping has been established and the relationship with La2O3@SnO2 p-n heterojunction has been investigated. This work provides a basis for understanding and optimizing the high sensitive metal oxide based gas sensors. 相似文献
564.
《International Journal of Hydrogen Energy》2020,45(23):12798-12814
We present a combined density functional theory (DFT) and microkinetic modeling study of synthesis gas conversion on Cu and Ca modified Mo6S8 catalysts to value-added products. Our results show that CO1 + H1 → HCO1 + (H) → H2CO1 + (H) → H3CO1 + (H) → CH3OH1 → CH3OH (g) is an optimal pathway on the Ca–Mo6S8 surface. With the combination of Energetic span model (ESM) and binding energy analysis, we conclude that Ca–Mo6S8 is a promising catalyst for formaldehyde and methanol from synthesis gas conversion. Meanwhile, the most energetically favorable outcome on the Cu–Mo6S8 surface is the production of ethanol. Microkinetics simulations are carried out on the basis of the first-principles data, which predict the synthesis gas conversion rate and the product distribution. This study demonstrates that introducing metal Cu or Ca into Mo6S8 will design high-performance catalysts with synergistic interactions for tuning selectivity. 相似文献
565.
《Advanced Powder Technology》2020,31(3):1274-1279
Zeolite-supported metal catalysts have been proven effective in many important catalytic reactions, such as hydrogenation, Fisher-Tropsch synthesis, automobile exhaust catalysis, selective catalytic reduction and many others. Despite the successful preparation of the catalyst through widely adopted methods, including ion exchange and impregnation, the metal dispersion over the zeolite is lack of control with high randomness. This renders the so-called “catalytic performance” an overall contribution from the metal sites located inside the zeolite micropores and those located on the external surface. This is exceptionally true for small to medium pore zeolites with typical free apertures of 0.3–0.6 nm (such as LTA and MFI). A more rational design of zeolite-supported metal catalysts is by encapsulating the metal nanoparticles or clusters within zeolite pores prior to the zeolite formation. Encapsulation of metals in zeolite prevents them from sintering and sulphur poisoning by cage confinement and molecular exclusion (via well-defined pore size and shape), respectively. This paper gives a new perspective on using metal clusters and nanoparticles as catalysts and the design of an effective zeolite-supported catalytic system. 相似文献
566.
《Advanced Powder Technology》2022,33(8):103665
Two novel Zn-MOFs constructed from 5-hydroxy-2-nitroisophthalic acid (H2DIPA) and 5-(4-carboxy-2-nitrophenoxy)-2-nitroisophthalic acid (H3BPPA), namely: {[Zn2(DIPA)2(bimp)5]·DMF·2H2O}n (Zn-MOF 1), {[Zn2(HBPPA)2(bibp)2]·2H2O}n (Zn-MOF 2) (bimp = 1,4-di(1H-imidazol-1-yl)butane, bibp = 4,4′-bis(imidazolyl) biphenyl), have been synthesized under solvothermal conditions and characterized by single crystal X-ray diffraction, elemental analysis, IR spectra, powder X-ray diffraction (PXRD) and thermogravimetric analysis (TG). The single-crystal X-ray diffraction analysis indicates that Zn-MOF 1 exhibits an uncommon 3-nodal framework with a (4·6·8)(4·63·82)(66) topology, whereas Zn-MOF 1 exhibits an uninodal 4-connected framework with a (44·62) topology. Moreover, both of the two Zn-MOFs exhibit exceptional dye adsorption capacities towards the organic dyes with high adsorption rates and excellent adsorption amounts. Particularly, Zn-MOF 1 can selectively adsorb the cationic dye malachite green (MG) whereas Zn-MOF 2 adsorb the anionic dye methyl orange (MO) when there exists another kind of dye in the system. The adsorption process can be illustrated by pseudo-second order kinetic and Langmuir isotherm, and the feasible adsorption mechanism could be the electrostatical interactions, hydrogen bonding between the MOFs and the dyes. Meanwhile, the two Zn-MOFs also show good photocatalytic degradation capabilities toward MB/MV dyes under UV irradiation, and the mechanism studies demonstrate that the main active species are ·OH radicals. Therefore, this functional MOF materials can be treated as a convenient and cost-efficient solution for the sewage handling and environmental protection. 相似文献
567.
利用原料一次加入进行间歇反应、抽真空连续吸收产品气体的实验方法,进行了硫酸-氯酸钠-氯化钠法制二氧化氯中ClO2/Cl2的选择性研究。实验结果表明:当采用较高的反应原料浓度、酸度和反应温度、NaCl/NaClO3的摩尔配比为1.1进行反应时,可获得产品气体中较高的ClO2/Cl2的选择性 相似文献
568.
徐靖凯;高倩;肖伟;张登华;张辉;张柳杰 《复合材料学报》2025,42(5):2683-2694
苯乙烯–丁二烯–苯乙烯嵌段共聚物(SBS)具有软硬段互相结合的独特结构,可通过挤压实现对气体分子的分离。本文以多孔α-Al2O3陶瓷管为载体,利用一系列x -SBS/四氢呋喃(THF)树脂溶液制备了相应的SMS-x 分离膜。FTIR、XRD、SEM等表征测试结果表明,SBS树脂与载体之间可较好结合,分离膜厚度均小于50 μm。气体测试表明,在0.05~0.3 MPa压力范围内,SMS-20分离膜对CH4/N2气体选择性(α )最优,在0.1 MPa时,α (CH4/N2) =3.81,CH4的摩尔通量为1.41×10−6 mol·m−2·s−1·Pa−1。在0.3 MPa,SMS-10的CH4摩尔通量最大,可达3.47×10−6 mol·m−2·s−1·Pa−1。此外,通过不同比例混合气体的测试验证了本文制备的分离膜同样可胜任相应的分离工作。本文制备的所有分离膜在0.1 MPa压差下可稳定分离气体长达7 d,具有良好的性能稳定性。因此,多孔α-Al2O3支撑型SBS分离膜可兼备优异的渗透通量及气体选择性,在煤层气CH4的富集方面提供有利选择。 相似文献
569.
Pei Xue Meng Zheng Longwei Wang Liyuan Cao Liang Zhao Jinsen Gao Chunming Xu 《中国化学工程学报》2021,39(11):68-78
Competition of hydrocarbon compounds with sulfides in gasoline has caused a not very high selectivity of sulfides in adsorption desulfurization so far, resulting in a reduction of catalyst lifetime as well as more sulfur oxide emissions. Tostudy the whole competitive process changing with the increase of the loading, the dynamic competition adsorption mechanism of cyclohexene and thiophene in siliceous faujasite (FAU) zeolite was analyzed by the Monte Carlo simulation. The results showed that with the increase of the loading, thiophene and cyclohexene had different performances before and after the inflection point of 40 molecule/UC. The adsorbates weredistributed ideally at optimal sites during the stage that occurredbefore the inflection point, which is called the \"optimal-displacement adsorption\" stage. When approachingthe inflection point, the competition became apparent and the displacement appeared accordingly, some thiophene molecules at S sites (refers to the sites inside the supercages) were displaced by cyclohexene. After the inflection point, the concentration of adsorbates at W sites (refers to the 12-membered ring connecting the supercages) was significantly reduced, whereas the adsorbates at S sites got more concentrated. The stage some cyclohexene molecules displaced by thiophene and inserted into the center of the supercage can be named as the \"insertion-displacement adsorption\" stage, and both the adsorption behavior and the competitive relationship became localized when the adsorption amount became saturated. This shift in the competitive adsorption mechanism was due to the sharp increase of interaction energy between the adsorbates. Besides, the increase in temperature and ratio of Si/Al will allow the adsorbates, especially thiophene molecules to occupy more adsorption sites, and it is beneficial to improve the desulfurization selectivity. 相似文献
570.
Cuiting Yang Bowen Wu Zewei Liu Guang Miao Qibin Xia Zhong Li Michael J. Janik Guoqing Li Jing Xiao 《中国化学工程学报》2022,42(2):25-34
Ultra-deep desulfurization of transformer oil is of great demand among power industry. In this work, the effective and deep removal of various types of organosulfurs, including mercaptan, sulfide and disulfide via catalytic adsorptive desulfurization (CADS) using bifunctional Ti-based adsorbent is reported. Compared to adsorptive desulfurization (ADS), dramatically improvement of the organosulfur uptakes were achieved under CADS process. The equilibrium adsorption capacity at 5 μg·g-1 S reached up to 15.7, 33.4, 11.6 and 11.9 mg·g-1 for propyl mercaptan(n-PM), dimethyl sulfide(DMS), di-t-butyl disulfide (DTBDS) and dibenzyl disulfide (DBDS), which was 262, 477, 97 and 128 times to that of ADS process, respectively, and was the highest among the reported desulfurization adsorbents. Moreover, it achieved superior breakthrough capacity of 2050, 530 and 210 ml F·(g A)-1 at the breakthrough S concentration of 1 μg·g-1 of the commercial transformer oil S containing 10, 50 and 150 μg·g-1, respectively. The effectiveness of CADS is associated to the transformation of sulfur species to higher polar sulfonic species with the assistance of mild oxidant, which can be readily captured by silanol groups on SiO2 through H-bonding interaction. The excellent recyclability of the adsorbent can be realized through solvent washing or oxidative air treatment. This work provides an effective and economic approach for the elimination of trace amount of mercaptan, sulfide and disulfide from transformer oil. 相似文献