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.     

H2循环再生对烟气脱硫V2O5-CoO/AC催化-吸附剂的二次脱硫活性的影响

烟气脱硫后的V₂O₅-CoO/AC催化 吸附剂在H₂气氛下再生,并将再生尾气连续返回反应器,可以同时达到再生和资源化制备硫磺的目的。着重考察了不同情况下H₂循环再生后V₂O₅-CoO/AC的二次脱硫活性,结果表明,硫磺制备要求系统中的硫在固相和气相之间发生多次形态转变,再生后催化-吸附剂上的残余硫使二次脱硫活性有所下降。主要原因是催化-吸附剂上的残余硫占据了脱硫所需的微孔,增加了表面酸量。再生后的H₂吹扫可以将部分残余硫以H₂S的形式赶出,提高二次脱硫硫容。NH₃表面改性也可以降低表面酸量,提高二次脱硫硫容。     

Co-NH2-SBA-15的制备及其脱硫性能研究

采用水热合成法制备介孔分子筛SBA-15,用（CH₃COO）₂Co对其进行超声浸渍改性,并用硅烷偶联剂APTS将氨基引入SBA-15分子筛中,制备出Co-NH₂-SBA-15吸附剂,考察了常温条件下H₂S的吸附性能。通过SEM、XRD、FT-IR、BET、XPS等表征手段对吸附剂进行表征。结果表明,氨基与金属同时负载在分子筛表面,氨基与硅物质的量比为0.20,Co负载质量分数为8%的SBA-15吸附效果最好,当原料气H₂S体积分数为227 μL/L,温度25 ℃,气体流量75 mL/min时,穿透硫容和饱和硫容达0.151和0.190 mmol/g,且吸附剂可再生利用。SBA-15表面嫁接氨基并浸渍金属改性的手段不仅提高了吸附容量,同时提高了分子筛的稳定性。     

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。     

Ni含量对负载型NiO/ZnO-TiO2吸附剂结构及吸附脱硫性能的影响

以ZnO-TiO₂为载体,采用等体积浸渍法制备了不同Ni含量的NiO/ZnO-TiO₂汽油脱硫吸附剂。采用X射线衍射（XRD）、压汞、H₂程序升温还原（H₂-TPR）和H₂程序升温脱附（H₂-TPD）等手段对吸附剂进行了表征。同时,采用FCC轻汽油为原料,在固定床反应装置中对不同Ni含量的NiO/ZnO-TiO₂吸附剂进行脱硫性能评价,以考察Ni含量对该吸附剂脱硫性能的影响。结果表明,Ni含量适量增加对于吸附剂比表面积、内部孔道分布和颗粒强度影响较小,同时能够增加具有脱硫活性的Ni⁰物种,促进吸附剂脱硫活性。当吸附剂中Ni质量分数达到5.48%后,吸附剂的内部孔道分布改变,吸附剂的比表面积和颗粒强度明显降低,对吸附剂脱硫活性极为不利。当Ni质量分数为4.45%时,吸附剂具有最佳脱硫性能,能够将FCC轻汽油中3×10^-4的总硫含量降低至5×10^-6以下,并维持脱硫时间达152 h,穿透硫容达11.24%（112.4 mg S/g吸附剂）,且脱硫后FCC轻汽油烯烃含量变化较小。     

活性炭催化氧化脱除单质汞的研究

模拟煤气的气氛,在硫化氢（H₂S）和氧气（O₂）存在条件下,对活性炭催化氧化吸附单质汞（Hg⁰）的性能进行了研究。结果表明,H₂S和O₂存在条件下,活性炭对Hg⁰的吸附能力明显提高。在180min内,H₂S和O₂共存气氛下,脱汞效率约为78%;只有H₂S存在下,脱汞效率约为69%;没有H₂S和O₂气氛下活性炭脱汞效率快速下降为28%。随着吸附温度的升高,入口汞浓度的提高和吸附剂粒径的增大,活性炭的脱汞效率会随着下降。通过XRD表征表明,Hg⁰的吸附反应机理是Hg⁰在活性炭催化氧化下与H₂S形成硫化汞（HgS）,从而实现了Hg⁰的稳定化脱除。     

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。     

基于硫堇掺杂的聚乙烯醇薄膜的光波导传感器检测硫化氢气体

采用旋转甩涂法将硫堇掺杂的聚乙烯醇薄膜固定在K⁺交换玻璃光波导表面,研制出一种高灵敏硫化氢气体传感器。 传感膜与硫化氢(H₂S)气体作用时,薄膜颜色从紫色变为无色,从而降低薄膜对倏逝波的吸收,使传感器的输出光强度（信号）增强。 采用流动注射法对H₂S气体进行检测。 实验结果表明,H₂S传感器对浓度在0.14~56 mg/m3范围的H₂S气体具有良好的线性响应（r=0.99667）,检出限为0.11 mg/m³(S/N=3),相对标准偏差为4.0%,响应时间（t90）＜2 s。 该传感器具有灵敏度高、响应快、可逆性和重复性好等特点。     

Ni/MgO/Al2O3催化剂上以1-甲基萘为模型化合物高温焦炉煤气焦油的催化转化

采用共浸渍薄水铝石(AlOOH)方法制备了一系列Ni/MgO/Al₂O₃催化剂, 并采用N₂气吸附及Ｘ射线衍射等手段进行了表征. 选择1-甲基萘作为焦油模型化合物, 研究了该催化剂催化转化具有较低水蒸气/碳摩尔比(n_H2O/n_C) 的高温焦炉煤气(COG)中焦油催化反应性能. 考察了催化剂中MgO含量及反应条件等对催化剂性能的影响. 实验结果表明, 在775 ℃和n_H2O/n_C=0.7条件下, MgO改性的Ni/MgO/Al₂O₃催化剂对1-甲基萘催化转化为小分子气体反应具有较好的催化活性和稳定性; 热重分析表明, MgO的加入能显著提高催化剂的抗积炭能力. 在Ni/MgO/Al₂O₃催化剂上, 反应气中高浓度H₂S气体(0.25%, 体积分数)能够促进焦油催化转化为小分子气体, 这可能是由于H₂S在Ni表面的可逆吸附形成更适合于重整反应的活性位, 同时抑制了烷烃裂解吸附形成的碳在金属中的溶解、扩散并最终形成积炭过程.     

碱金属碳酸盐对褐煤程序升温热解过程中H2S和NH3生成的影响

以内蒙古锡盟褐煤为研究对象,通过HCl/HF洗脱煤中固有矿物质,采用机械混合法对原煤和脱矿物质煤分别负载3%的Li₂CO₃、Na₂CO₃和K₂CO₃,利用固定床程序升温热解-色谱分析法考察了煤中固有矿物质以及负载的碱金属碳酸盐对煤热解过程中H₂S和NH₃生成的影响。结果表明,煤中所固有矿物质对锡盟褐煤热解过程中H₂S和NH₃的生成和释放均有抑制作用,但对H₂S和NH₃生成的影响不同;矿物质的脱除不改变煤中有机结构及硫的存在形态,H₂S的释放温区没有发生改变,而HCN的二次反应是NH₃生成的主要来源之一,酸洗脱矿物质改变了煤中孔结构特性,从而影响不同温度段NH₃的释放。原煤及脱矿物质煤负载的碱金属碳酸盐对其热解过程中H₂S和NH₃的生成都有一定的影响,K₂CO₃除外, 负载到原煤的其他碱金属碳酸盐都抑制了H₂S的生成;Na₂CO₃除外,负载到脱矿物质煤的其他碱金属碳酸盐都促进了NH₃的生成。     

水热法制备NiS/Cd1-xZnxS及其高效光催化产氢性能

利用水热法制备 NiS 负载的 Cd1-xZnxS 光催化剂.结果表明：在0.35 mol?L-1 Na2SO3和0.25 mol?L-1 Na2S牺牲剂下,0.5%(摩尔分数, y) NiS/Cd0.3Zn0.7S (1840μmol?h-1)获得最好活性,是Cd0.3Zn0.7S (884μmol?h-1)的2.1倍,高于0.5%(质量分数, w) Pt (1390μmol?h-1)的产氢活性.测得其在λ=420 nm附近的表观量子效率为36.8%. X射线衍射(XRD)、紫外-可见漫反射光谱(UV-Vis DRS)、透射电子显微镜(TEM)以及X射线光电子能谱(XPS)的表征结果表明, NiS作为产氢活性位,转移光生电子,因此提高了光催化产氢活性.     

Removal of carbonyl sulfide from CO2 stream using AgNO3-modified NaZSM-5

Removal of carbonyl sulfide (COS) from CO₂ stream is significant for the production and utilization of food grade CO₂. This study investigates the adsorption performance of Ag/NaZSM-5 as adsorbent prepared by incipient wetness impregnation for the removal of COS from a CO₂ stream in a fixed-bed adsorption apparatus. Effects of various conditions on the preparation of adsorbent, adsorption and desorption were intensively examined. The results revealed that COS can be removed to below 1×10^?9 from a CO₂ stream (1000 ppm COS/CO₂) using Ag/NaZSM-5 (10 wt% AgNO₃) with an adsorption capacity of 12.86 mg-g^?1. The adsorbent can be fully regenerated using hot air at 450 °C. The adsorption ability remained stable even after eight cycles of regeneration.     

Highly effective water adsorbents based on aluminum oxide

A method of preparation of a stable, high performance water adsorbent with the phase composition η-Al₂O₃ + γ-Al₂O₃ + χ-Al₂O₃ from thermally activated hydrargillite has been developed. The synthesis procedure does not involve a reprecipitation stage. The resulting adsorbent has a high specific surface area (400 m²/g) and a mean pore diameter of 3.5 nm or below. The static capacity of the adsorbent reaches 24.2 g H₂O per 100 g of sorbent, and its dynamic capacity is 8.2 g H₂O per 100 g of sorbent. Service life tests showed the stability of the adsorbent in multiple sorption-desorption cycles. The minimum dew point in drying is ?58.8°C.     

Ho(NO3)3(C2H5O2N)4·H2O的低温热容和热力学函数

合成了稀土(钬, Ho)-氨基酸(甘氨酸, C₂H₅O₂N)二元配合物Ho(NO₃)₃(C₂H₅O₂N)₄·H₂O, 并且通过化学分析、元素分析和红外(IR)光谱对配合物进行了表征. 用高精度全自动绝热量热仪, 测定了该配合物在80-390 K温度区间的定压摩尔热容(C_p,m). 利用实验测定的热容数据, 采用最小二乘法, 将热容曲线上热容峰以外的两段平滑区的摩尔热容对折合温度进行拟合, 建立了热容随折合温度变化的多项式方程. 根据热容与焓、熵的热力学关系,计算出了配合物在80-390 K温度区间内,每隔5 K,相对于298.15 K的摩尔热力学函数(H_T,m-H_298.15,m)和(S_T,m-S_298.15,m). 通过热容曲线分析, 计算出了350 K附近转变过程的焓变(Δ_trsH_m)和熵变(Δ_trsS_m). 用差示扫描量热法(DSC)测定了配合物的热稳定性.     

The Reactions of H Atoms with H2S and COS

The kinetics of the reactions of H atoms with H₂S and with COS were measured at 298deg;K in a flow system using mass-spectrometric detection. The rate constants were found to be 3.8 × 10^?13 and 2.2 × 10^?14 cm₃ part^?1 sec^?1, respectively, with an estimated accuracy of 25%. At high flow rates of H₂S, 0.5 molecules of H₂S are consumed per H atom originally present. At all flow rates of COS, H₂S is a major product, CO production equals COS consumption, and 0.5 molecules of COS are consumed per H atom. The results are consistent with the reaction HS + HS → H₂S + S being the dominant process for thiyl radicals, and evidence is presented to indicate that its reaction rate is close to collisional frequency.     

Nonisothermal Kinetics of Dehydration Process of [Sm（m-CIBA）3phen]2·2H2O and [Sm（p-CIBA）3phen]2·2H2O

Compounds [Sm（m-CIBA）3phen]2.2H20 and [Sm（p-CIBA）3phen]2·2H20（m-CIBA=m-chlorobenzoate, pClBA=p-chlorobenzoate, phen=l,10-phenanthroline） were prepared. The dehydration processes and kinetics of these compounds were studied from the analysis of the DSC curves using a method of processing the data of thermal analysis kinetics. The Arrhenius equation for the dehydration process can be expressed as lnk=-38.65-243.90×l0^3/RT for [Sm（m-CIBA）3phen]2·2H2O, and lnk=38.70-172.22×103/RT for [Sm（p-CIBA）3phen]2·2H2O. The values of △H^1, △G^1, and △S^1 of dehydration reaction for the title comnonnds are determined respectively.     

A continuous flow instrument with flow regulation and automatic sensitivity range adaptation for the determination of atmospheric H2S

A set-up for continuous measurements of atmospheric H₂S concentrations in the range between 0.138 g/m³ and 17.5 g/m³ is described. All flows are regulated by flow sensors which are connected to the respective pump by a feed back circuit. The instrument is working in two sensitivity ranges. One is provided for low H₂S concentrations (lower than 1.75 g/m³) and the other for higher levels (higher than 1.75 g/m³). During continuous measurements the set-up enables an automatic adaptation of one of the sensitivity ranges to ambient H₂S concentrations. The critical step of absorption of gaseous H₂S into the liquid phase of the continuous flow system could be stabilised by the development of a new fluid level control system. After numerous test measurements under laboratory conditions the instrument was tested for the first time in June 1993 during field measurements in the tropics. These measurements took place in the environment of natural and industrial sources of H₂S in the vicinity of Salvador da Bahia in Brazil. Data are presented which prove the ability of the instrument.Dedicated to Professor D. Dieter Klockow on the occasion of his 60th birthday     

Eu(C10H9N2O4)(C10H8N2O4)(H2O)3]•0.5bipy•3H2O配合物的合成、晶体结构及荧光性质

在水-乙醇混合体系中, 以2-羰基丙酸水杨酰腙(C₁₀H₁₀N₂O₄)、2,2-联吡啶(C₁₀H₈N₂, 简写bipy)与Eu(NO₃)₃•4H₂O反应, 首次培养出黄色单晶[Eu(C₁₀H₉N₂O₄)(C₁₀H₈N₂O₄)(H₂O)₃]•0.5bipy•3H₂O. 该晶体属三斜晶系, 空间群为P-1, 晶胞参数a＝0.93392(16) nm, b＝1.3100(2) nm, c＝1.3895(2) nm, α＝97.205(3)°, β＝105.411(2)°, γ＝106.364(2)°, V＝15.35(2) nm³, Z＝2, μ＝2.118 mm^－1, D_c＝1.686 Mg/m³, F(000)＝786, R＝0.0116, wR＝0.0507, GOF＝0.995. 晶体测试结果表明, 该单晶结构为铕的9配位配合物, 两个2-羰基丙酸水杨酰腙分别以负一价和负二价酮式和三个水分子同时参与配位; 每个2-羰基丙酸水杨酰腙中的羧基氧、酰胺基中的羰基氧和C＝N中的氮与Eu^3＋配位, 形成两个共边的稳定五元环, 另三个配位原子则分别来自三个水分子中的氧原子, 该配合物在空间呈扭曲的单帽四方反棱柱, 而在不对称单位中还有游离的一个2,2-联吡啶分子和三个水分子, 这些游离分子与配位分子之间存在大量分子内和分子间氢键, 整个分子在空间呈三维网状结构. 发光性能测试表明该配合物具有很好的荧光性质.     

Use of Dithiasuccinoyl-Caged Amines Enables COS/H2S Release Lacking Electrophilic Byproducts

The enzymatic conversion of carbonyl sulfide (COS) to hydrogen sulfide (H₂S) by carbonic anhydrase has been used to develop self-immolating thiocarbamates as COS-based H₂S donors to further elucidate the impact of reactive sulfur species in biology. The high modularity of this approach has provided a library of COS-based H₂S donors that can be activated by specific stimuli. A common limitation, however, is that many such donors result in the formation of an electrophilic quinone methide byproduct during donor activation. As a mild alternative, we demonstrate here that dithiasuccinoyl groups can function as COS/H₂S donor motifs, and that these groups release two equivalents of COS/H₂S and uncage an amine payload under physiologically relevant conditions. Additionally, we demonstrate that COS/H₂S release from this donor motif can be altered by electronic modulation and alkyl substitution. These insights are further supported by DFT investigations, which reveal that aryl and alkyl thiocarbamates release COS with significantly different activation energies.