TG-MS与Py-GC相结合法研究惰性气氛下含硫模型化合物热解过程中硫的脱除及释放行为研究

采用热重-质谱法(TG-MS)和热解-气相色谱法(Py-MS)相结合的方法对模型化合物(十四硫醇、二丁基硫醚、苯硫醚、二甲基噻吩、苯并噻吩和二苯并噻吩等)在惰性气氛下硫的脱除及释放行为进行研究。惰性气氛下硫的脱除顺序为:十四硫醇>二丁基硫醚>二甲基噻吩>苯并噻吩>苯硫醚>二苯并噻吩,苯硫醚除外,该顺序与含硫官能团的热分解顺序一致。在热解过程中,所有模型化合物在质谱和气相色谱仪上均被检测到SO₂;除苯硫醚和二苯并噻吩外,其他模型化合物中均检测到了COS;而只在十四硫醇、二丁基硫醚和二甲基噻吩中检测到了H₂S。且热解气中SO₂含量要显著高于H₂S和COS。这是由于活性炭作载体时,惰性气氛下内部氢的含量显著小于内部氧的含量,所以大多数的含硫自由基易与内部氧结合以SO₂的形式逸出。对于苯硫醚、苯并噻吩和二苯并噻吩中没有检测到H₂S,是由于内部氢的不足,使得含硫自由基不能与内部氢结合,所以没有检测到H₂S逸出。     

哈密煤温和液化固体产物热解过程中硫的变迁规律

利用固定床反应器研究了哈密煤温和液化固体产物（MLS）在热解过程中含硫气体的释放规律以及不同形态硫的变迁规律，并分析了矿物质对硫变迁规律的影响。结果表明，在实验考察的条件范围内，MLS热解过程中大部分的硫残留在半焦中，仅有不到10%的硫迁移到焦油中或转化为含硫气体逸出。热解生成的含硫气体以H₂S为主，当热解温度为400℃时H₂S的逸出速率达到最大。通过改进方法测定了MLS及其热解半焦中各种形态硫的含量，发现MLS热解过程中以硫化物硫和有机硫的分解和转化为主。随着热解温度的升高，MLS中有机硫逐渐分解并以含硫气体的形式逸出；当热解温度低于600℃时，MLS中硫化物硫逐渐转化为含硫气体、有机硫和少量的黄铁矿硫；当热解温度高于600℃时，MLS中碱性矿物质吸收气相中的H₂S转化为硫化物硫，硫化物硫缓慢增加。醋酸酸洗可以保留MLS中大部分的硫化物硫，且酸洗后MLS热解生成的H₂S逸出速率增大，峰温向低温方向移动；当热解温度高于600℃时，有机硫和硫化物硫的脱硫反应速率降低，并且MLS中的碱性矿物质与H₂S反应生成金属硫化物，导致H₂S逸出速率明显降低。     

锂硫电池硫正极催化转换反应的研究进展

单质硫作为电池的正极材料,其电化学过程历经多个步骤,完全放电生成最终产物是一个2电子反应. 低阶多硫化锂的生成需克服一定的能垒,且由Li₂S₂得到一个电子还原生成Li₂S的反应是速控步骤. 硫正极的反应动力学是决定锂硫电池电化学性能,如比能量、比功率、低温性能等的关键因素. 提高速控步骤的反应动力学还能加速可溶性多硫化锂Li₂S₄向不溶性Li₂S₂和Li₂S的转化,有利于减缓或消除多硫化锂的“穿梭效应”. 近年,已有大量的过渡金属氧化物、硫化物、碳化物、氮化物、磷化物,单原子催化剂和氧化还原电子中继体等被应用于催化硫正极反应,提高了电极的电化学性能和循环稳定性. 但是,目前详细的催化反应机制尚不完全清晰. 本文重点综述了这些化合物在硫正极反应中的作用机制,总结了近年来的研究进展,并对硫正极催化转换反应的研究和发展进行了展望.     

Ni-Mo/Al_2O_3催化剂上硫转移反应的研究

制备了以γ-Al2O3为载体的Ni-Mo催化剂,并用于FCC汽油的加氢硫转移反应。对Ni-Mo/Al2O3催化剂上的硫转移反应机理进行了研究,考察了不同反应条件对硫转移反应的影响。实验结果表明,硫醇与烯烃的反应在催化剂表面的加氢活性位上进行,小分子的硫醇发生加氢脱硫,生成吸附态H2S,吸附态的H2S与烯烃反应,生成大分子硫醇和硫醚;另外小分子硫醇还可直接与烯烃发生反应,生成硫醚。提高反应温度、压力、氢油比或降低空速,均可提高催化剂的硫转移反应活性,轻质硫转化率得到明显提高,且单烯选择性还能维持在98%左右。     

TiO2光催化消除H2S的研究

在TiO₂上进行了气相H₂S光催化氧化消除的研究.氧对H₂S的光催化氧化消除过程是不可缺少的,对含量为560mg/m³的H₂S,当加入的氧气与原料气中H₂S的分子比为42:1,空速为28000h^-1时,去除率达到97%.在H₂S光催化氧化消除过程中,单质硫的产生可使TiO₂失活,经光照再生单质硫转化为SO₄^2-后,TiO₂活性恢复,而且SO₄^2-的生成对催化剂的中毒有抑制作用.     

H2S/H2硫化温度对MoP/SiO2催化剂硫醚化性能的影响

以负载磷酸钼为前驱体,采用程序升温还原法制备了MoP/SiO₂催化剂,以体积分数3%H₂S/H₂对其进行了硫化处理,利用XRD、CO化学吸附、NH₃-TPD、HRTEM-EDX、ICP-AES以及XPS等手段对催化剂进行了表征,研究了硫化温度对MoP/SiO₂催化剂结构和异戊二烯与正丁硫醇硫醚化性能的影响。结果表明,即使在400℃硫化处理也未改变MoP/SiO₂催化剂中MoP体相结构;随着硫化温度提高,催化剂表面酸量增加、金属位数量减少,降低了催化剂C-S键氢解及异戊二烯深度加氢活性,但同时也提高了催化剂烯烃聚合活性。经120℃硫化处理的MoP/SiO₂兼具较佳硫醚化及异戊二烯选择加氢性能。     

硫化氢对钴改性活性焦脱除煤气中汞的影响机理

采用等体积浸渍煅烧法制备钴改性活性焦(Co-AC),并采用BET、XRD等分析手段进行表征。 利用固定床吸附实验台,研究了模拟煤气(N₂、H₂、CO、H₂S)气氛下汞的吸附特性,重点关注H₂S对汞吸附的影响。 结果表明,5%负载量的Co-AC在120 ℃和H₂S作用下具有优异的脱汞能力,2 h内平均脱汞效率高达97.8%。 此外基于密度泛函理论,首先计算了H₂S、HS及S在Co₃O₄(110)表面的吸附能及键长,通过比较H—S键键长的变化得出H₂S会逐步解离成HS与S,然后将优化后的S-Co₃O₄(110)作为Hg的吸附基底,研究其吸附特性,得出Hg与S反应生成稳定的HgS,吸附能为-3.503 eV,证明了汞的吸附遵循Eley-Rideal机制。 Co-AC吸附剂在高温下脱汞性能受到极大的抑制,因为随吸附温度升高,表面活性硫的减少及硫和汞的反应平衡常数下降显著,导致汞的脱除能力下降。 本文采用了实验加模拟的手段,探明了H₂S存在时Hg⁰在钴基吸附剂表面的反应机理,为协同脱除煤气中的H₂S和Hg⁰提供了理论指导。     

LaCoO3对H2S选择氧化性能的影响

使用溶胶-凝胶法制备了LaCoO₃催化剂,采用XRD、BET和XPS等方式对催化剂进行了表征,考察了该催化剂制备过程中煅烧温度、表面活性剂PEG-6000和PEG-20000含量对其H₂S选择氧化制硫磺反应催化活性的影响。结果表明,表面活性剂PEG-6000及PEG-20000的添加能明显提高LaCoO₃的催化活性。0.02 mol La（NO₃）₃+0.02mol Co（NO₃）₂溶液中添加0.30 g PEG-20000、煅烧温度为650℃时所制备的LaCoO₃催化活性最好;在最佳反应温度260℃下,H₂S的转化率达到96.10%,硫选择性为93.77%。     

用于检测多硫化氢和亚硝酰氢的小分子荧光探针

多硫化氢（H₂S_n）和亚硝酰氢（HNO）在一系列生理病理过程中起着重要的作用,包括调节细胞内氧化还原信号传递过程、增强心肌的收缩能力、抑制血小板聚集等。H₂S_n可以通过硫化氢（H₂S）与活性氧物种反应得到。一氧化氮（NO）和HNO可以在超氧化物歧化酶（SOD）作用下相互转化,H₂S和NO反应可以生成H₂S_n和HNO,调控酶的活性以及蛋白与蛋白之间的相互作用,从而影响蛋白质的生理功能。因此,实时检测生物体内H₂S_n和HNO的浓度具有十分重要的生物医学意义。在各种生物检测技术中,荧光探针具有选择性好,灵敏度高,可以实时原位检测,对样品损伤小等优点,受到了广泛关注。本文将按照探针响应基团的反应类型,将近几年用于定性定量检测H₂S_n和HNO荧光探针进行分类和总结,重点概述探针的设计理念、响应机制和生物应用,并对探针的应用前景进行了展望。同时,本文也关注了硫化氢和其他硫烷硫类物种荧光检测的近期进展。     

二价钌催化的金属卡宾经由的硫叶立德[2,3]-σ重排反应研究

报道烯(炔)基硫醚与α-重氮羰基化合物, 在[RuCl₂(p-cymene)]₂催化下, 经由金属卡宾发生硫叶立德[2,3]-σ重排反应(Doyle-Kirmse反应). 在Ru(II)作用下, α-重氮羰基化合物与烯丙基硫醚的反应以较好收率生成相应的[2,3]-σ重排产物高烯丙基硫醚. 同样条件下与炔丙基硫醚的反应则生成[2,3]-σ重排产物联烯和呋喃衍生物, 后者是联烯进一步在Ru(II)作用下重排的产物.     

Hydrodeoxygenation of benzofuran over sulfided and reduced Ni–Mo/γ-Al2O3 catalysts: Effect of H2S

Effect of H₂S on the catalytic performance of the reduced and sulfided Ni–Mo/Al₂O₃ catalysts in hydrodeoxygenation of benzofuran is studied. The steady-state reaction experiments showed a decrease in activity for both reduced and sulfided catalysts when H₂S was introduced into the feed. The reaction conversion of benzofuran over the reduced catalyst still remained superior to that of the sulfided catalyst in the presence of H₂S, however, at high reaction temperatures, the product distribution over the pre-reduced catalyst is similar to the sulfided catalyst. The studies with temperature-programmed desorption (TPD), temperature-programmed reaction (TPRxn) and X-ray photoelectron spectroscopy (XPS) techniques showed a partial sulfidation of the reduced catalysts when exposed to H₂S under reaction conditions, however, the catalyst does not go through a complete conversion to a molybdenum sulfide phase. Instead oxygen–sulfur exchange on the surface leaves behind oxisulfide species, with catalytic activity closely resembling that of the reduced catalysts. The effect of H₂S on the reaction performance is mainly coming from the competitive adsorption between H₂S and benzofuran and the formation of SH groups with decomposition of H₂S at high temperatures.     

硫化氢对活性炭脱除单质汞的影响

H₂S是煤气中的含硫成分,活性炭能否催化氧化煤气中的H₂S形成活性硫,以促进H₂S和Hg⁰的协同脱除是值得研究的。 本文首先通过程序升温脱附和热力学分析了低温情况下H₂S对活性炭脱除Hg⁰的影响。 在较低吸附温度130 ℃下,H₂S不仅不能作为硫源,还使活性炭对Hg⁰的吸附显著减弱,这主要是由于H₂S对活性炭表面的吸附氧的消耗以及H₂S对含氧官能团的氧的取代反应造成的。 在此基础上,进一步研究了高温下H₂S对活性炭的影响,高温也不能使活性炭有效渗入单质硫。 所以无论低温还是高温情况下,利用H₂S作为硫源使Hg⁰以HgS的形式脱除并不是活性炭脱汞的可行手段。 本文揭示了较宽的温度范围内H₂S对单纯的活性炭脱除Hg⁰的影响机理,能为用于煤气脱汞的活性炭的设计以及作为负载时机理研究提供支持作用。     

加压热解气氛对碳酸钾催化煤热解过程中硫迁移的影响

在加压热解装置上,考察了碳酸钾及热解气氛对煤热解过程中硫分布及其形态的影响。结果表明,碳酸钾通过捕获H_2S增加了半焦硫含量,同时可将煤焦表面活化,导致煤中有机质与黄铁矿分解产生的活泼硫结合形成新的有机硫。氢气能促进煤中硫的脱除,但是碳酸钾存在下热解释放的硫一部分以K_2S的形式固定于半焦中。水蒸气可显著促进煤中黄铁矿的分解,同时可与煤焦中的K_2S反应,降低半焦中的硫含量。两段床催化气化炉中,碳酸钾催化剂经热解后不影响其对煤焦的催化性能。     

Photoabsorption spectra of H2S, CH3SH and SO2 near the sulfur K edge

Photoabsorption spectra of the isolated sulfur containing molecules H₂S, CH₃SH and SO₂ are measured at high resolution near the sulfur K edge, using synchrotron radiation. Resonances are observed in the discrete and continuum parts of the spectra. The most intense resonances are shown to result from virtual orbital effects on the basis of comparisons with the L edge photoabsorption spectra (H₂S, SO₂), the equivalent core model (SO₂) and low-energy electron scattering measurements (H₂S, SO₂).     

基于密度泛函理论下H2S在单原子催化剂V/Ti2CO2上的分解机理研究

In-depth understanding of the mechanisms of hydrogen sulfide (H₂S) adsorption on catalysts during desulfurization from industrial waste gas streams is important for developing effective catalysts to be used in the decomposition of H₂S. In this work, the dissociation behavior of H₂S adsorbed on a single-atom catalyst (Ti or V-decorated Ti₂CO₂ surface) was investigated by performing density functional theory (DFT) calculations. The corresponding diffusion behavior revealed that Ti or V atoms could be dispersed on the Ti₂CO₂ monolayer, without aggregation in the form of single atoms. In addition, analyses of the partial density of states (PDOS), Hirshfeld charges, and electron density difference indicated that the decorated Ti or V atoms led to charge redistribution on the Ti₂CO₂ surface and significantly improved the interaction between the H₂S gas molecules and Ti₂CO₂, thereby enhancing the catalytic activity of V/Ti₂CO₂. In order to gain a deeper understanding of the mechanism of H₂S decomposition (H₂S → HS* + H* → H₂ + S*), a comparative analysis of the results for the decomposition of H₂S on the Ti/Ti₂CO₂ and V/Ti₂CO₂ surfaces was carried out. The catalytic dissociation behavior of H₂S is explained as follows: once H₂S is adsorbed on the V/Ti₂CO₂ or Ti/Ti₂CO₂ surface, it spontaneously dissociates into HS*/H* without any energy barrier on the catalyst surface. Subsequently, the V atoms would not only promote the cleavage of the H-S bond, but also play a major role in the formation of S atoms. Moreover, the rate-limiting step for the entire process proceeded on the Ti/Ti₂CO₂ surface with an energy barrier of 0.86 eV, while that for V/Ti₂CO₂ was 0.28 eV, indicating that the H₂S molecules easily dissociated into S and H₂ on the V/Ti₂CO₂ surface at room temperature. The reaction time for H₂S decomposition on the V/Ti₂CO₂ surface at 500 K was 65.79 ns, which was almost two orders of magnitude higher than that at room temperature. Thus, the decomposition of H₂S on the V-doped Ti₂CO₂ surface is associated very fast kinetics. Furthermore, the S atoms can form elemental sulfur with aggregation on the V/Ti₂CO₂ surface to promote recycling reactions. Compared with previously reported catalytic systems, the single-atom catalyst (SAC) V/Ti₂CO₂ catalyst has greater application prospects in terms of sustainable economy or removal efficiency for H₂S treatment. Our results suggest that V-doped Ti₂CO₂ is an excellent candidate for a highly effective non-noble metal catalyst applicable to H₂S decomposition.      

Radiation induced scavenging of NOx, SO2, H2S from exhaust gases

The theoretical model of exhaust gases radiation induced oxidation was developed. NO, SO₂ and H₂S concentrations curves vs dose calculated by use of this model for mixtures containing N₂ (80.5%), O₂ (11%), H₂O (8.4%), NO (100–600 ppm), SO₂ (150–500 ppm) and H₂S (300–1000 ppm) have been obtained. It has been shown that NO and SO₂ conversion reactions with acids formation go simultaneously with oxidizing reaction of H₂S giving SO₂ as an intermediate substance. These processes were evaluated for different initial concentrations of NO, SO₂ and H₂S. Data established by our simulation calculations show that the electron beam process can be judged as a promising technology for simultaneous removal of SO₂, NO and H₂S from exhaust gases.