面向氢能源、燃料电池和二氧化碳减排的制氢途径的选择

对氢气的多种制造途径加以探讨,也涉及到氢能的利用、燃料电池以及二氧化碳的减排。需要指出的是氢气并非能源,而只是能量的载体。 所以氢能的发展首先需要制造氢气。对于以化石燃料为基础的制氢过程,如煤的气化和天然气重整,需要开发更经济和环境友好的新过程,在这些新过程中要同时考虑二氧化碳的有效收集和利用问题。对于煤和生物质,在此提出了一种值得进一步深入研究的富一氧化碳气化制氢的概念。对于以氢为原料的质子交换膜燃料电池系统,必须严格控制制备的氢气中的一氧化碳和硫化氢;对于以烃类为原料的固体氧化物燃料电池,制备的合成气中的硫也需严格控制。然而,传统的脱硫方法并不适宜于这种用于燃料电池的极高深度的氢气和合成气的脱硫。氢能和燃料电池的发展是与控制二氧化碳排放紧密相关的。     

Methanol – die Basischemikalie

Today methanol is produced from synthesis gas derived from coal and natural gas. However carbon dioxide and hydrogen obtained from water electrolysis with renewable energy have the potential to play a leading role as fuel, energy raw material and chemical feedstock. As a liquid energy storage system it can be used to easily transport electric power conserved in chemical bonds with unparalleled efficiency. Homologisation making use of the Mobil zeolite processes (MTG, MTO, MTA) for instance, or via the methanol derived platform chemicals methyl formate and dimethyl ether, the majority of organic chemicals established in chemical industry is available. Through its diverse of applications methanol has the potential to substitute crude oil and natural gas as the leading feedstock for organic chemicals.     

煤和生物质共气化制备富氢气体的实验研究

在煤处理量为8kg/h的小型流化床反应器上,以富氧空气和水蒸气为气化介质,对煤和生物质共气化制取富氢燃气进行了实验研究。在850℃～1 050℃主要考察了空气当量比、水碳比、生物质比例和生物质种类对燃气组成和气体产率的影响。结果表明,对煤和稻草混合体系,稻草质量比为33%时,空气当量比增加,CO2含量显著增加,H2、CO和CH4含量减少,气体产率增加;水碳比增加,CO2和CH4含量增加,CO和H2含量减小,气体产率先增加后减小;生物质比例增加,CO2、H2和CH4含量增加,CO含量降低,气体产率先增加后减小,当生物质比例小于50%时,可以实现体系的稳定运行。对于三种不同的煤与生物质混合体系,煤与高粱秆共气化所得煤气中H2含量最高,气体产率的顺序为:煤/木屑煤/高粱秆煤/稻草煤。实验中H2在煤气中的体积分数最高可达37.25%,最大产率为0.54m3/kg。     

Performance of planar electrode-supported high-temperature solid oxide fuel cell using syngas

In China, coal is a dominant energy source. In order to ensure China’s energy security, coal should be used efficiently and cleanly. Integrated gasification fuel cell hybrid power generation system is a promising system for coal utilization. It combines clean coal gasification technology with high efficient fuel cell technology. In this work, the performance of solid oxide fuel cell using syngas as fuel was investigated, based on the commercial computational fluid dynamic software and the developed program used to analyze chemical, electrochemical, heat/mass transfer, current, and electric potential. The results show that the temperature difference is about 300 K in the cell under all calculation conditions. Along the cell length, hydrogen concentration rapidly reduces, and its decrement is larger than that of carbon monoxide. The variation of current density in electrolyte layer is relatively small along the direction of gas flow, but it is obvious along the direction vertical to gas flow.     

KOH对超临界水中褐煤连续制氢的影响

采用连续式超临界水反应装置,以20%的水煤浆为反应原料,考察了不同KOH/煤质量比、温度、压力对褐煤制氢过程的影响。实验结果表明,在水煤浆中添加KOH可以提高碳气化率及H2的体积分数和产率,在600℃、25 MPa、KOH/煤质量比为4.1%时,与未加KOH相比,气相产物收率由29.6%提高到49.5%,碳气化率由23.0%增大到31.5%;H2的产率由135.4 mL/(g daf coal)提高到239.1 mL/(g daf coal)。随着温度的升高,H2产率逐渐增大,650℃时达到287.8 mL/(g daf coal),是500℃时的5.4倍;高温、高压下,KOH对煤气化过程的催化作用更为明显。     

Comparative chemical analysis of commercial creosotes and solvent refined coal-II materials by high resolution gas chromatography

The chemical composition of a commercially available creosote was compared to a direct coal liquefaction product, i.e., solvent refined coal-II fuel oil blend (SRC-II FOB) using high resolution gas chromatography (HRGC). In addition, hydrogenated products of these materials were studied. Samples were fractionated by chemical class on neutral alumina. Those fractions previously shown to be the most mutagenic and tumorigenic in laboratory bioassays of coal-derived materials were analyzed and compared by HRGC and gas chromatography/mass spectrometry (GC/MS). Individual components were tentatively identified and quantitated. Although similar chemical components were present in the creosote and SRC-II FOB fractions studied, the creosotes had higher concentrations of heavy molecular weight materials and a lower ratio of alkylated to parent polycyclic aromatic compounds than the coal liquefaction products. The creosote samples also had a significantly higher concentration of components which eluted in the polycyclic aromatic hydrocarbon (PAH) chemical class fraction. Amino-substituted PAH were present in both nonhydrogenated coal liquid and creosote materials. The creosote and SRC-II FOB crudes and nitrogen-containing polycyclic aromatic compound (NPAC) chemical class fractions expressed similar microbial mutagenicity. Based on chemical analysis data, the predicted tumorigenic potency of the creosote in laboratory bioassay systems would be equivalent to or greater than the SRC-II FOB.     

Specific characteristics of molten carbonate fuel cell in realization of electrochemical coal oxidation

The test object was a fuel cell with free molten carbonate electrolyte providing realization of direct electrochemical oxidation of solid hydrocarbons. This study involved the effect of the fuel type and dispersion as well as cathode reagent gas mixture composition to the fuel cell functional parameters. The used fuels were dispersed and monolithic graphite, anthracite, and jet coal specimens. The effect of oxygen/carbon dioxide ratio on the mixture fed to cathode to the open circuit cell voltage and achieved current density levels was studied with respect to interrelation of the processes taking place in the cathode and anode units of the fuel cell. A correlation was noted between the specific fuel cell characteristics and hydrogen content in the fuel material. The highest level of current density and specific power was recorded for jet coal characterized with high hydrogen content. The different characteristics of monolithic and dispersed fuel specimens were accounted for by the effect of losses at contacts between particles. Achievement of high current density and specific power was demonstrated by using dispersed coal fuel.     

钙钛矿材料在固体氧化物燃料电池燃料重整中的应用

固体氧化物燃料电池（solid oxide fuel cell,SOFC）是通过电化学反应将化石燃料（煤、石油和天然气等）、生物质燃料或其它碳氢燃料中的化学能直接转换为电能的发电装置,能量转换效率更高、污染更低,被公认为21世纪高效绿色能源技术. 但直接以碳氢化合物为燃料时,镍基阳极中容易产生积碳,从而失去电化学催化活性. 在阳极外侧进行一次燃料的预重整是一种行之有效的解决办法,其中高效稳定的重整催化剂至关重要. 本文将结合本课题组的研究进展对钙钛矿催化剂在燃料重整中的应用进行概述,并提出自己相应的观点和展望.     

压力对塔里木原油四组分热解性能的影响

压力对深层油藏原油热化学过程的影响尚存在较大争议,为研究其在油藏原油热解成气过程中的作用机理,我们在450℃、5~40 MPa压力下对塔里木原油四组分(饱和分、芳香分、胶质和沥青质)进行了封闭体系的热解实验,通过气相色谱(GC)和气相色谱/质谱(GC/MS)分别对原油四组分热解反应的气体产物及饱和分热解过程的液态产物进行了分析。结果表明,在450℃、24 h及不同压力下,沥青质热解产气率高于胶质、芳香分和饱和分;四组分的气相热解产物中,C1的产率明显高于C2~C5组分。增大压力抑制沥青质、胶质及芳香分的热解产气过程而促进饱和分的热解产气过程。随压力的增大,饱和分热解的液态产物的主峰组分碳数先减小,再增大。压力低于20 MPa时,饱和分热解过程中以裂解反应为主;高于30 MPa时,增大压力有利于缩合反应。研究结果可为认识深层油藏原油的稳定程度及天然气的成因提供一定的理论参考。     

中国部分煤种二氯甲烷萃取液中极性和烃类有机物分布特性研究

利用高分辨气相色谱－低分辨质谱联用仪（HRGC／LRMS）检测原煤二氯甲烷萃取液中极性有机物和烃类有机物（脂肪烃和芳香烃）的浓度分布，研究了萃取液中这两类有机物和煤种、煤种成分（固定碳、挥发分、灰分、水分）之间的联系。研究发现萃取液中的有机物浓度和固定碳、挥发分关系密切；极性有机物分布较集中，主要为酯类和醇类；芳香烃以菲、二苯并蒽和苯并Bai为主，烟煤和贫煤多环芳烃含量和毒性当量（TEQ）相对较高，并发现煤的碳化程度越高，芳香化程度越大。本文的结果为将来进一步研究燃煤过程中有机污染物形成机理提供依据。     

The potential of proton exchange membrane–based electrolysis technology

Hydrogen is an important chemical feedstock for many industrial applications, and today, more than 95% of this feedstock is generated from fossil fuel sources such as reforming of natural gas. In addition, the production of hydrogen from fossil fuels represents most carbon dioxide emissions from large chemical processes such as ammonia generation. Renewable sources of hydrogen such as hydrogen from water electrolysis need to be driven to similar production costs as methane reforming to address global greenhouse gas emission concerns. Water electrolysis has begun to show scalability to relevant capacities to address this need, but materials and manufacturing advancements need to be made to meet the cost targets. This article describes specific needs for one pathway based on proton exchange membrane electrolysis technology.     

催化剂对东都风化煤硝酸氧解及其产物特性的影响

对东都风化煤进行硝酸氧解,利用元素分析与红外光谱分析研究产物硝基腐植酸（NHA）的结构和性质,讨论硝酸氧解中催化剂对硝基腐植酸的产率、元素组成和官能团的影响。结果表明,浓硫酸、过氧化氢、碳纳米管负载过渡金属和固体酸催化剂都能显著提高煤氧解NHA的产率,产物C、H的质量分数和H/C原子比降低,氮的质量分数增加,E4/E6增加。固体酸与浓硫酸对提高产物氮的质量分数更明显,镀镍碳纳米管（CNTs）负载三氧化二铁、碳纳米管负载镍和浓硫酸作为催化剂得到腐植酸分子更小。催化剂存在下产物活性官能团增加更多,不同催化剂对产物有不同的影响。     

Hydrocarbon/hydrogen mixed gas permeation in poly(1-trimethylsilyl-1-propyne) (PTMSP), poly(1-phenyl-1-propyne) (PPP), and PTMSP/PPP blends

The gas permeation properties of poly(1-trimethylsilyl-1-propyne) (PTMSP), poly(1-phenyl-1-propyne) (PPP), and blends of PTMSP and PPP have been determined with hydrocarbon/hydrogen mixtures. For a glassy polymer, PTMSP has unusual gas permeation properties which result from its very high free volume. Transport in PPP is similar to that observed in conventional, low-free-volume glassy polymers. In experiments with n-butane/hydrogen gas mixtures, PTMSP and PTMSP/PPP blend membranes were more permeable to n-butane than to hydrogen. PPP, on the other hand, was more permeable to hydrogen than to n-butane. As the PTMSP composition in the blend increased from 0 to 100%, n-butane permeability increased by a factor of 2600, and n-butane/hydrogen selectivity increased from 0.4 to 24. Thus, both hydrocarbon permeability and hydrocarbon/hydrogen selectivity increase with the PTMSP content in the blend. The selectivities measured with gas mixtures were markedly higher than selectivities calculated from the corresponding ratio of pure gas permeabilities. The difference between mixed gas and pure gas selectivity becomes more pronounced as the PTMSP content in the blend increases. The mixed gas selectivities are higher than pure gas selectivities because the hydrogen permeability in the mixture is much lower than the pure hydrogen permeability. For example, the hydrogen permeability in PTMSP decreased by a factor of 20 as the relative propane pressure (p/p_sat) in propane/hydrogen mixtures increased from 0 to 0.8. This marked reduction in permanent gas permeability in the presence of a more condensable hydrocarbon component is reminiscent of blocking of permanent gas transport in microporous materials by preferential sorption of the condensable component in the pores. The permeability of PTMSP to a five-component hydrocarbon/hydrogen mixture, similar to that found in refinery waste gas, was determined and compared with published permeation results for a 6-Å microporous carbon membrane. PTMSP exhibited lower selectivities than those of the carbon membrane, but permeability coefficients in PTMSP were nearly three orders of magnitude higher. © 1996 John Wiley & Sons, Inc.     

Hydrocarbon type analysis by thin-layer chromatography with flame-ionization detection: vacuum gas oils, heavy feeds, and hydroprocessed products

Thin-layer chromatography with flame-ionization detection (TLC-FID) provides quantitative hydrocarbon type data as well as distribution of aromatics by ring number. This method has been applied to obtain amounts of saturates, aromatics, and polars in heavy oil distillates such as light vacuum gas oils and heavy vacuum gas oils derived from different crude sources. TLC-FID chromatograms and resultant quantitative hydrocarbon type data show that these distillates vary markedly in aromatic contents and aromatic ring types. Similar observations are made with several fluid catalytic cracking feeds. Effects of process parameters such as operating pressure and temperature on hydroconversion of aromatics and polars from a heavy oil are assessed by TLC-FID. It has been demonstrated that there is a preferential reduction of higher polycyclic aromatic hydrocarbons and polars with an increase of both hydrogen partial pressure and reactor temperature.     

氢气存在下一氧化碳偶联反应的化学和性能

实验研究了在氢气存在下，一氧化碳与亚硝酸乙酯偶联合成草酸二乙酸反应体系在典型操作条件下的化学反应和反应性能，结果表明氢气只与反应体系中的亚硝酸乙酯反应生成乙醇。由于氢气与一氧化碳在催化剂表面竞争吸附，并且氢的存在打破了生成草酸二乙酯所必需的正常的氧化还原过程：Pd^0→Pd^2 →Pd^0，因此氢的引入使一氧化碳转化率及草酸二乙酯选择性下降。此外，化学吸附测试结果表明氢气和一氧化碳是在催化剂表面同一活性中心上吸附。     

Effects of hydrocarbon quenching in gas chromatography when using the flame photometric detector

Summary The long time retardation of the main hydrocarbon peak in the chimney of the flame photometric detector greatly reduces the responses of later-eluting sulfur compounds. In the absence of hydrocarbons in the flame, the slope (s) of the log I vs. log [S] plot (where I is the sulfur response and [S] is the sulfur concentration in the sample) is of the highest value and is constant for all experimental conditions tested. Flame hydrocarbons cause the s value to decrease, and this is dependent on the oxygen to hydrogen ratio in the flame (O/H) and, under certain conditions, also on the sulfur to carbon ratio (S/C) of the sample. The abnormalities observed in the determination of methyl thiol in natural gas are explained on the basis of the present study.     

CaO对褐煤在超临界水中制取富氢气体的影响

以褐煤在超临界水中制取富氢气体为目的,利用小型高压间歇反应装置,在Ca/C 摩尔比为0～0.60、温度450℃～680℃、压力23MPa～38MPa和停留1min～30min下,考察了小龙潭褐煤的反应特性。研究表明,CaO不仅可以固定气相中的CO2,提高H2的体积分数,而且可以提高碳转化率和气体产率。600℃、28MPa,Ca/C摩尔比为0.42时,气相产物中的CO2趋于完全固定,H2产率比无添加剂时提高2.5倍,H2体积分数为48％,其余为CH4和烃类气体。升高反应温度使CaO的催化作用更为显著, 碳转化率和气体产率（H2、CH4、烃类气体）随着反应温度的升高而逐渐增加,液相收率减少。增大反应压力可以促使煤转化率和气体产率升高,停留时间对反应的影响相对较小。以900℃热解焦为反应原料进行了气化实验,结果表明,在600℃和650℃反应5min后,碳转化率分别为8.6％和12.5％,CaO对气化反应和甲烷化反应起不同程度的催化作用。     

Characterization of liquid products of automobile tire pyrolysis

The liquid product of automobile tire pyrolysis and its fractions were studied. The amount of the liquid hydrocarbon fraction is 40–45% of the total weight of pyrolysis products. The hydrocarbon fraction is similar in its characteristics to low-sulfur heavy crude oil. Fractionation of the hydrocarbon fuel was performed. The maximal yield of the light distillation fraction is 39% (temperature interval 180–340°C). The extent to which the characteristics of the light fraction obtained meet the regulations was evaluated. The light fraction of hydrocarbon fuel produced by pyrolysis is recommended for use as a component of diesel motor fuel after additional purification.     

生物质流化床富氧气化的实验研究

在常压流化床装置上进行了生物质在富氧条件下定向气化的实验研究。实验主要考察了氧的当量比和氧体积分数对气化气组成、碳转化率和气体热值的影响。当量比值是与温度紧密联系的一个量，本实验主要通过调节进料量来改变它的值，随着当量比的变化（0.21～0.29），燃气成分也会改变，其中变化最大的是H2、CO。H2体积分数显著增加，CO和CH4体积分数有降低的趋势，使燃气热值降低；氧体积分数是富氧气化过程中较重要的参数，在实验研究的范围内，发现增大氧气体积分数可以提高H2体积分数及有利于调节H2/CO(体积分数)的比值。当氧气体积分数从21％提高到45％，H2体积分数从20％增加到27.7％，H2/CO(体积分数)从0.38增加到0.75，比较接近合成液体燃料的气体比值。     

Natural gas and biofuel as feedstock for hydrogen production on Ni catalysts

In this article,the aptitude of natural gas as feedstock in steam reforming process for hydrogen production is compared with that of different liquid fuels (pure compounds and commercial fuels),with the aim to investigate the potentialities of biofuels to overcome the CO2 emission problems deriving from fossil fuel processing.The performances of a nickel based catalyst (commercially used in steam reforming of natural gas) were evaluated in terms of feed conversion and yield to the different products as function of temperature,space velocity and water/fuel ratio.Furthermore,a preliminary evaluation of catalyst durability was effected by monitoring yield to H2 versus time on stream and measuring coke formation at the end of experimental tests.High yields to hydrogen were obtained with ail fuels investigated,whereas the deactivation phenomena,which are correlated to carbon deposition on the catalyst,were observed with all tested fuels,except for methane and biofuel.