938 resultados para separazione gas PTMSP membrane grafene cattura CO2


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Increasing demand for energy and continuing increase in environmental as well as financial cost of use of fossil fuels drive the need for utilization of fuels from sustainable sources for power generation. Development of fuel-flexible combustion systems is vital in enabling the use of sustainable fuels. It is also important that these sustainable combustion systems meet the strict governmental emission legislations. Biogas is considered as one of the viable sustainable fuels that can be used to power modern gas turbines: However, the change in chemical, thermal and transport properties as well as change in Wobbe index due to the variation of the fuel constituents can have a significant effect on the performance of the combustor. It is known that the fuel properties have strong influence on the dynamic flame response; however there is a lack of detailed information regarding the effect of fuel compositions on the sensitivity of the flames subjected to flow perturbations. In this study, we describe an experimental effort investigating the response of premixed biogas-air turbulent flames with varying proportions of CH4 and CO2 to velocity perturbations. The flame was stabilized using a centrally placed conical bluff body. Acoustic perturbations were imposed to the flow using loud speakers. The flame dynamics and the local heat release rate of these acoustically excited biogas flames were studied using simultaneous measurements of OH and H2CO planar laser induced fluorescence. OH* chemiluminescence along with acoustic pressure measurements were also recorded to estimate the total flame heat release modulation and the velocity fluctuations. The measurements were carried out by keeping the theoretical laminar flame speed constant while varying the bulk velocity and the fuel composition. The results indicate that the flame sensitivity to perturbations increased with increased dilution of CH4 by CO2 at low amplitude forcing, while at high amplitude forcing conditions the magnitude of the flame response was independent of dilution.

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A technique is presented for measuring the exhaust gas recirculation (EGR) and residual gas fraction (RGF) using a fast UEGO based O2 measurement of the manifold or in-cylinder gases, and of the exhaust gases. The technique has some advantages over the more common CO2-based method. In the case of an RGF measurement, fuel interference must be eliminated and special fuelling arrangements are is required. It is shown how a UEGO-based measurement, though sensitive to reactive species in the exhaust (such as H 2), as a system reports EGR/ RGF rates faithfully. Preliminary tests showed that EGR and RGF measurements using the O2 approach agreed well with CO2-based measurements. Copyright © 2011 SAE International.

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The design, 3D FEM modelling and measurement results of a novel high temperature, low power SOI CMOS MEMS thermal conductivity gas sensor are presented here. The sensor consists of a circular membrane with an embedded tungsten micro-heater. The high sensing capability is based on the temperature sensitivity of the resistive heating element. The sensor was fabricated at a commercial foundry using a 1 μm process and measures only 1×1 mm 2. The circular membrane has a 600 μm diameter while the heating element has a 320 μm diameter. Measurement results show that for a constant power consumption of 75 mW the heater temperature was 562.4°C in air, 565.9°C in N2, 592.5°C for 1 % H2 in Ar and 599.5°C in Ar. © 2013 IEEE.

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Although studies on carbon burial in lake sediments have shown that lakes are disproportionately important carbon sinks, many studies on gaseous carbon exchange across the water-air interface have demonstrated that lakes are supersaturated with CO2 and CH4 causing a net release of CO2 and CH4 to the atmosphere. In order to more accurately estimate the net carbon source/sink function of lake ecosystems, a more comprehensive carbon budget is needed, especially for gaseous carbon exchange across the water-air interface. Using two methods, overall mass balance and gas exchange and carbon burial balance, we assessed the carbon source/sink function of Lake Donghu, a subtropical, eutrophic take, from April 2003 to March 2004. With the overall mass balance calculations, total carbon input was 14 905 t, total carbon output was 4950 1, and net carbon budget was +9955 t, suggesting that Lake Donghu was a great carbon sink. For the gas exchange and carbon burial balance, gaseous carbon (CO2 and CH4) emission across the water-air interface totaled 752 t while carbon burial in the lake sediment was 9477 t. The ratio of carbon emission into the atmosphere to carbon burial into the sediment was only 0.08. This low ratio indicates that Lake Donghu is a great carbon sink. Results showed good agreement between the two methods with both showing Lake Donghu to be a great carbon sink. This results from the high primary production of Lake Donghu, substantive allochthonous carbon inputs and intensive anthropogenic activity. Gaseous carbon emission accounted for about 15% of the total carbon output, indicating that the total output would be underestimated without including gaseous carbon exchange. (C) 2007 Elsevier Ltd. All rights reserved.

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Chemical-looping combustion (CLC) has the inherent property of separating the product CO2 from flue gases. Instead of air, it uses an oxygen carrier, usually in the form of a metal oxide, to provide oxygen for combustion. All techniques so far proposed for chemical looping with solid fuels involve initially the gasification of the solid fuel in order for the gaseous products to react with the oxygen carrier. Here, the rates of gasification of coal were compared when gasification was undertaken in a fluidised bed of either (i) an active Fe-based oxygen carrier used for chemical looping or (ii) inert sand. This enabled an examination of the ability of chemical looping materials to enhance the rate of gasification of solid fuels. Batch gasification and chemical-looping combustion experiments with a German lignite and its char are reported, using an electrically-heated fluidised bed reactor at temperatures from 1073 to 1223 K. The fluidising gas was CO2 in nitrogen. The kinetics of the gasification were found to be significantly faster in the presence of the oxygen carrier, especially at temperatures above 1123 K. A numerical model was developed to account for external and internal mass transfer and for the effect of the looping agent. The model also included the effects of the evolution of the pore structure at different conversions. The presence of Fe2O3 led to an increase in the rate of gasification because of the rapid oxidation of CO by the oxygen carrier to CO2. This resulted in the removal of CO and maintained a higher mole fraction of CO2 in the mixture of gas around the particle of char, i.e. within the mass transfer boundary layer surrounding the particle. This effect was most prominent at about 20% conversion when (i) the surface area for reaction was at its maximum and (ii) because of the accompanying increase in porosity and pore size, intraparticle resistance to gas mass transfer within the particle of char had fallen, compared with that in the initial particle. Excellent agreement was observed between the rates predicted by the numerical model and those observed experimentally. ©2013 Elsevier Ltd. All rights reserved.

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We investigated the synthesis of dimethyl ether (DME) from biomass synthesis gas using a kind of hybrid catalyst consisting of methanol and HZSM-5 zeolite in a fixed-bed reactor in a 100 ton/year pilot plant. The biomass synthesis gas was produced by oxygen-rich gasification of corn core in a two-stage fixed bed. The results showed that CO conversions reached 82.00% and 73.55%, the selectivities for DME were 73.95% and 69.73%, and the space-time yields were 124.28 kg m- 3 h- 1 and 203.80 kg m- 3 h- 1 when gas hourly space velocities were 650 h- 1 and 1200 h- 1, respectively. Deoxidation and tar removal from biomass synthesis gas was critical to the stable operation of the DME synthesis system. Using single-pass synthesis, the H2/CO ratio improved from 0.98-1.17 to 2.12-2.22. The yield of DME would be increased greatly if the exhaust was reused after removal of the CO2.

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In this paper, an interdigital electrode lipid film odour sensor (ILOS) is designed, fabricated and tested. It is made from a microfabricated chemiresistor coated with a synthetic multibilayer film. Nine odorants in gas phase at room temperature have been detected using the odour sensor. For most of the odorants, the relation between the response of the ILOS and odorant concentration obeys Stevens' power law, and there is a good correlation between the minimum odorant concentrations that give rise to a change of the sensor's conductance and human olfactory thresholds.

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沙棘广泛分布于亚欧大陆的温带地区和亚洲亚热带的高海拔地区。沙棘能适应多种生态环境,能耐受多种逆境(如干旱、低温、高温和盐害等)。在中国,沙棘常常被用作植被恢复中的先锋树种而大量栽培。本文以中国沙棘为试验材料,探索沙棘适应干旱机制,以及沙棘对干旱胁迫的适应机制是否存在种群间的差异,同时试图通过分析干旱胁迫下沙棘叶片蛋白质表达变化探索沙棘适应干旱胁迫的分子机理。 对三个分别来自低海拔湿润地区、低海拔干旱地区和高海拔湿润地区的中国沙棘种群进行干旱胁迫处理。干旱胁迫能提高根冠比,比叶面积,降低平均叶面积和总生物量,提高沙棘的抗氧化性酶活性、脯氨酸含量、脱落酸(ABA)含量、降低光合作用,提高长期用水效率。实验中的这两个低海拔种群比高海拔种群抵抗干旱的能力更强,不同的种群采用了不同的策略来耐受干旱胁迫和过氧化胁迫。 在2004 年度的实验中,干旱胁迫处理下,高海拔湿润种群(道孚种群)严重失水,生长也受到更大的抑制,非气孔因素在抑制光合作用方面占支配地位,抗坏血酸含量下降,ABA和脯氨酸含量增加幅度比九寨沟种群的要高,这可能是因为道孚种群严重失水而引起的;而低海拔湿润种群(九寨沟种群)的体内水分状况几乎不受干旱的影响,生长情况也较道孚种群要好。 在2005 年度的试验中,和高海拔湿润地区种群(道孚)相比较,低海拔干旱地区种群(定西)在叶片相对水含量、根冠比、抗氧化酶活性(过氧化氢酶、抗坏血酸过氧化物酶和谷胱甘肽过氧化物酶)、保护性物质(脯氨酸,脱落酸)含量等方面都要高,光能热耗散能力也更强,而且气体交换参数(气孔扩散阻力和胞间CO2浓度等)对干旱也更不敏感。 分析了干旱胁迫下沙棘叶片蛋白质表达的变化。共发现319 个蛋白质,有4 个蛋白在干旱胁迫下消失(Putative ABCtransporter ATP-binding protein 、Hypothetical proteinXP-515578,热激蛋白Hslu219 和一个没得到鉴定的蛋白),4 个只在干旱胁迫下出现(没命名的蛋白质产物,对甲基苯-丙酮酸双加氧酶,NTrX 和一个没得到鉴定的蛋白),46 个蛋白质的表达丰度变化显著,包括32 个干旱负调蛋白,14 个干旱正调蛋白(3 个Rubisco 的大亚基、J-type–co-chaperone Hsc20、putative protein DSM3645-2335、putative acyl-COA 脱氢酶、nesprin-2 和两个没有得到鉴定的蛋白质)。这些蛋白质参与了氮代谢调控、抗氧化行物质的合成、脂肪酸β-氧化、核骨架构造、[Fe-S]基团组装、物质跨膜运输、细胞分裂或作为分子伴侣和蛋白质酶起作用。putative ABC transporter ATP-binging protein、NtrX、nesprin-2 和Hslu 是本试验新发现的高等植物蛋白,我们主要从它们的保守结构域或在其他生物中的同源物来猜测它们的功能。实验结果为我们研究植物抗干旱机制提供了新线索和新视野。 Seabuckthorn (Hippophae rhamnoides L.) is widly distributed throughtout the temperatureresiogn of Europe and Asia and sub-tropical plateau zone of Asia. H. rhamnoides can adapatseveral different environments, and can tolerant several envioronmental stresses (e.g, lowtemperature, high temperature, drought and salty). It has been widely used in forest restoration asthe pioneer species in China. In present study, we applied H.rhamnoides subsp. Sinensis asexperimental materials to study its drought-tolerant mechanism, and expected to findpopulational difference in drought-tolerant mechanism that may exist among populations, and tryto get some insight in drought-tolerant mechanism of it at morecular level through analyzing thechange of leaf protein expression. Three populations from high altitude wet zone, low altitude wet zone and low altitude arid znoe,respectively, were applied in our experiment, and were subjected to drought. Drought increasedthe root/shoot ratio(RS), special leaf area, long-term water use efficinency, activity of antioxidantenzymes, proline content and abscisic acid (ABA) content, declined the net photosynthesis rate(A), average leaf area (ALA), total biomass (TB). Both two low altitude populations were moredrought-tolerant than the high altitude population, and different population applied differentstratedgies to tolerant oxidant stress and drought stress. The results of the exprement in 2004 showed that Daofu population was more drought-sensitivethan Jiuzhai population. Under drought conditions, leaf relative water content (RWC) greatlydecreased in Daofu population, but not in Jiuzhai population. The large loss of water in Daofupopulation resulted in a limitation on A mainly caused by non-stomatal factors, severer suppression in growth rate and a significant reduction in ascorbic acid (AsA) content, comparedwith Jiuzhai population. The greater increase in content of ABA and proline in Daofu populationmay be also induced by large loss in water, so that enable plants to cope with sever drought. In the exprement of 2005, drought significantly increased RS, activities of catalase (CAT),peroxidase (POD), glutathione peroxidase (GPX) and ascorbate peroxidase (APX), and alsosignificantly increased ABA and proline contents. On the other hand, compared with Daofupopulation, drought induced larger RS and activities of CAT, GPX and APX, and higher ABAcontent in Dingxi population, whereas gas exchange traits, e.g., stomatal limitation value (LS) andintercellular CO2 concentration (Ci), were less responsive to drought in Dingxi population thanthose in Daofu population. All these factors enable Dingxi population to tolerant drought betterthan Daofu population. The leaf protein profile of seabuchthorn subjected to drought was analyzed. Altogether 319proteins were detected in well-watered sample, four proteins disappeard by drought (putativeABCtransporter ATP-binding protein, hypothetical protein XP-515578, Hslu219and aunidentified protein), four only appeared under drought (a probable nitrogen regulation protein(NtrX), a 4-hydroxyphenylpyruvate dioxygenase , an unnamed protein product and an identified protein), 32 drought down-regulated proteins, and 14 drought up-regulated proteins (nine wereidentified: three large subunits of Rubisco, a hypothetical protein DSM3645-23351, a putativeacyl-COA dehydrogenase, a nesprin-2, a J-type-co-chaperone HSC20 and two unmatchedproteins). These proteins may involve in β-oxidation, cross-membrane transport, cell division,cytoskeleton stabilization, iron-sulfur cluster assembly, nitrogen metabolism regulation andantioxidant substance biosynthesis or function as molecular chaperone or protease. Four proteins(a putative ABC transporter ATP-binging protein, NtrX, nesprin-2, Hslu) were new found in highplants, and their functions were estimated from their conserved domain or their homologues inother organism. Our results provided new clue and new insight for us to study thedrought-tolerant mechanism in plants.

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A transverse field gas ionization chamber as Delta E detector at the Radioactive Ion Beam Line in Lanzhou (RIBLL) is described. A high detection efficiency and long plateau are achieved with the mixed gas Ar(80%)+CO2(20%). The energy resolution is 3.25% for 4.94MeV alpha particle. This ionization chamber has been tested in the experiment with 50MeV/u Ni-58 bombarding Ta at RIBLL. All the fragments can be identified clearly by the ionization chamber.

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The preparation of light alkenes by the gas phase oxidative cracking (GOC) or catalytic oxidative cracking (COC) of model high hydrocarbons ( hexane, cyclohexane, isooctane and decane in the GOC process and hexane in the COC process) was investigated in this paper. The selection for the feed in the GOC process was flexible. Excellent conversion of hydrocarbons ( over 85%) and high yield of light alkenes ( about 50%) were obtained in the GOC of various hydrocarbons including cyclohexane at 750 degreesC. In the GOC process, the utilization ratio of the carbon resources was high; CO dominated the produced COX (the selectivity to CO2 was always below 1%); and the total selectivity to light alkenes and CO was near or over 70%. In the COC of hexane over three typical catalysts (HZSM-5, 10% La2O3/HZSM-5 and 0.25% Li/MgO), the selectivity to COX was hard to decrease and the conversion of hexane and yield of light alkenes could not compete with those in the GOC process. With the addition of H-2 in the feed, the selectivity to COX was reduced below 5% over 0.1% Pt/HZSM-5 or 0.1% Pt/MgAl2O4 catalyst. The latter catalyst was superior to the former catalyst due to its perfect performance at high temperature, and with the latter, excellent selectivity to light alkenes ( 70%) and the conversion of hexane (92%) were achieved at 850 degreesC ( a yield of light alkenes of 64%, correspondingly).

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NaA zeolite membrane was successfully synthesized on a ceramic hollow fiber with an outer diameter of 400 mum, a thickness of 100 mum and an average pore radius of 0.1 mum. The as-synthesized membranes were characterized by XRD, SEM as well as gas permeation. A continuous C NaA zeolite membrane formed after a three-stage synthesis. The membrane thickness was similar to5 mum. Gas permeation data indicated that a relatively high quality NaA zeolite membrane formed on the ceramic hollow fiber support. (C) 2003 Elsevier B.V. All rights reserved.

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Using a dry/wet spinning process, asymmetric cellulose hollow fiber membranes (CHFM) were prepared from a dope composed of cellulose/N-methylmorpholine-N-oxide/water. The formation mechanism for the finger-like macrovoids at the inner portion of as-spun fibers was explained. Naturally drying and three solvent exchange drying methods were tried to investigate their influence on morphology and properties of CHFM. It was found that the ethanol-hexane exchange drying was an appropriate method to minimize morphology change of the as-spun CHFM, whereas the naturally drying caused the greatest shrinkage of the fibers that made the porous membrane become dense. The result, CHFM from ethanol-hexane exchange drying performed the highest gas permeation rate but gas permeation of the naturally dried membrane could not be detectable. The resultant CHFM from the ethanol-hexane exchange drying also showed acceptable, mechanical properties, thus it was proposed to be an appropriate method for gas separation purpose. The experimental results supported the proposed drying mechanism of CHFM. The free water would evaporate or be replaced by a solvent that subsequently would evaporate but the bonded water would remain in the membrane. What dominated the changes of membrane morphology during drying should be. the molecular affinities of cellulose-water, water-solvent and solvent-solvent. (C) 2004 Elsevier B.V. All rights reserved.

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A high quality pure hydroxy-sodalite zeolite membrane was successfully synthesized on an alpha-Al2O3 support by a novel microwave-assisted hydrothermal synthesis (MARS) method. Influence of synthesis conditions, such as synthesis time, synthesis procedure, etc., on the formation of hydroxy-sodalite zeolite membrane by MAHS method was studied by X-ray diffraction (XRD), scanning electron microscopy (SEM) and gas permeation measurements. The synthesis of hydroxy-sodalite zeolite membrane by MAHS method only needed 45 min and synthesis was more than 8 times faster than by the conventional hydrothermal synthesis (CHS) method. A pure hydroxy-sodalite zeolite membrane was easily synthesized by MAHS method, while a zeolite membrane, which consisted of NaX zeolite, NaA zeolite and hydroxy-sodalite zeolite, was usually synthesized by CHS method. The effect of preparation procedures had a dramatic impact on the formation of hydroxy-sodalite zeolite membrane and a single-stage synthesis procedure produced a pure hydroxy-sodalite zeolite membrane. The pure hydroxy-sodalite zeolite membrane synthesized by MARS method was found to be well inter-grown and the thickness of the membrane was 6-7 mum. Gas permeation results showed that the hydrogen/n-butane permselectivity of the hydroxy-sodalite zeolite membrane was larger than 1000. (C) 2004 Elsevier Inc. All rights reserved.

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A palladium membrane has been prepared by electroless plating on the surface of a porous stainless steel tube. Since the large surface pores of the tube are obstacle for preparation of a defect-free palladium film on the surface, zirconium oxide particles were deposited inside the pores. The mean thickness of the resulting Pd membrane on the modified tube was ca. 10 mum. It is suggested that the permeability of hydrogen is partly governed by gas diffusion in the pores. (C) 2004 Elsevier B.V. All rights reserved.

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A new process has been suggested for converting natural gas to ethylene by combining oxidative coupling of methane with ethane dehydrogenation to provide an efficient method for the utilization of thermicity and CO2. From their thermodynamics, it is clear that the exothermicity from CH4 oxidative coupling reaction (DeltaH(800degreesC) = -174.3 kJ mol(-1)) can support C2H6 dehydrogenation by CO2 (DeltaH(800degreesC) = + 180.2 kJ mol(-1)). Meanwhile, the two reactions can be conducted under the same reaction conditions, such as the reaction temperature and reaction pressure as well as space velocity. In addition, the CO2 yielded from CH4 oxidative coupling reaction can be directly used for C2H6 dehydrogenation. Two kinds of catalyst are developed for this combined process with an achievement, from which C2H4 content in tail gas can reach attractively 16.4%, which can be used directly to produce ethylbenzene by the alkylation of benzene. (C) 2002 Elsevier Science Ltd. All rights reserved.