扬子地块周边C、P硅岩建造中硒的富集机理对比研究-以渔塘坝、紫阳富硒区为例

在自然界中存在一套由硅质岩、泥质岩／页岩或板岩、碳酸盐岩和粉砂岩组成的沉积建造，并以富含有机质和菌藻微生物等为特征，沉积厚度较大，岩石类型以硅岩为主，称之为“硅岩建造”。硅岩建造中的硅质岩不仅是许多重要矿种（如金、硒、铀、钒、磷、锰、铂族元素、重晶石和黄铁矿等）的赋存层和含矿岩系的重要岩类，而且由于它形成于特定的地球化学条件下，能够反映出某些沉积相带特殊的地质背景，另外，硅质岩本身就是一种生物岩，对探讨生物成岩、成矿作用有重要意义。所以对硅岩建造及其内硅质岩研究具有十分重要的理论意义和实用价值。因此，本论文选择扬子地块周边寒武系（南秦岭紫阳硒富集区）、二叠系（湖北恩施双河渔塘坝硒矿床）富硒硅岩建造为研究对象。通过岩石地球化学、同位素地球化学、矿物学以及流体包裹体等方法从含硒规律、岩石成因、沉积环境、成矿流体性质等方面，分别对对两个不同时代或不同层位的富硒硅岩建造开展了系统的地球化学对比研究；并从矿物学、包裹体成分及物理化学条件等方面对渔塘坝硒矿床的成因作了探讨。通过研究，取得了以下主要认识：1渔塘坝硒矿区和紫阳硒富集区富硒硅岩建造岩石以硅质岩为主，硅质岩中5102含量范围分别为64.2％-95.84％和63.62％-95.24％。同时包括部分碳质硅质岩丫碳质页岩 和碳、硅板岩及含腐泥层的石煤；渔塘坝硒矿床硅质岩中Se含量大于80ug/g的样品均采自下二叠统茅口组的硅质岩段内，紫阳下寒武统硒富集体中硅质岩中硒的含量最高（可达278ppm）。2微量元素研究表明，两地区富硒硅质岩中均含有较高的Cu，Ni、V、As、Sb、Cr，且U／Th＞1。在U-Th、Zr-Cr和P2O5-Y相关图以及Fe-Mn-（Cu+Co+Ni）三角图上，两研究区内硅质岩样品点均落于热水沉积区。渔塘坝硒矿区硅质岩的REE总量较低，平均为38.9×10-6，紫阳硒富集区硅质岩REE总量除个别较高（达110×10-6以上）外，总体也较低（12.0-37.6）×l0-6；另外，从稀土元素配分模式看，两地区硅质岩均有较明显的Ce负异常，且Eu从无明显Eu异常到出现正Eu异常。都反映出热水沉积硅质岩的特征。从si和O同位素组成来看，两个地区硅质岩的δ3051和δ18O值也总体位于热水成因硅质岩区域内。根据隧石一水的氧同位素分馏方程计算得知，两研究区硅质岩的形成温度分别为46℃-72℃和78.6℃-126.20℃。地球化学特征表明，两地区富硒硅质岩均来自热水沉积作用。另外，渔塘坝硒矿区硅质岩中Cr含量较高，且存在腕足类生物化石；紫阳硒富集区硅质岩中Ba及有机质含量较高，且存在叶琳生物标志化合物。结合两地区碳同位素组成特征（渔塘坝地区δ13c为正值，可能和上扬子区早、晚二叠世之间多期次喷发的火山活动，造成地球史上二叠纪生物大灭绝有关；紫阳地区δ13C为负值，说明碳同位素来源于沉积有机物质），暗示两地区硅质岩的成因可能与火山沉积作用有关，且在成岩过程中有部分生物的参与。3渔塘坝赋矿硅质岩硫同位素组成具有较高的负值，表明矿床形成于缺氧的海盆内：紫阳硒富集区形成黄铁矿的硫主要来自海水硫酸盐。4系统研究了渔塘坝硒矿区硒的矿物学，显示硒以自然硒、独立矿物、类质同像及有机吸附四种形式赋存于矿床中。废弃石煤堆中的自然硒矿物，是自然因素和人为活动共同干预的结果，并非石煤的缓慢自燃的结果。5对研究区成矿流体中包裹体均一温度、盐度和密度进行了系统研究，结果显示：两地区的流体包裹体以原生包裹体为主，数量较多且形态复杂；研究区（渔塘坝硒矿和紫阳硒富集区）成矿流体处于中一低温（ 190-250）℃和（120-155）℃条件。渔塘坝硒矿区石英和方解石包裹体内的流体盐度分别为（5.9-10.l）B％和（3.9-4.5）WB％，紫阳硒富集区流体盐度为（1.2-2.8）WB％，后者流体盐度明显低于前者。流体密度经计算分别为0.79-0.79／cm3和0.69-0.969／cm3。重点对渔塘坝硒矿区的石英和方解石包裹体进行了拉曼光谱成分测试，结果显示：包裹体成分以H2O和N2为主，含少量 CH4、C2H4、C2H6、C3H5、C4H6、C4H4和C6H6等成分，说明成矿溶液介质主要为具有还原性质的水溶液，其成矿条件具还原性的特点。6渔塘坝硒矿区成矿物理化学条件的研究表明，即富硒成矿流体为中低温（190-250）℃、压力平均为60Mpa。成矿早期02、eZ相对较低，乃较高，且fS2/fSe2＞l，有利于硫化物沉淀在成矿主阶段，随着硫化物的沉淀，fS2和fSe2相应增大，且fO2较高。高的fO2阻止了硒进入硫化物，而有利于硒化物的形成。 7系统研究了富硒硅岩建造的沉积环境和构造环境特征，认为渔塘坝硒矿床中富硒硅质岩主要形成于浅海滞留的盆地沉积环境，紫阳下寒武统硅质岩沉积环境属于深水滞留沉积环境；渔塘坝硒矿床主要形成于拉张的断陷盆地中，紫阳硒富集体则形成于拉张的裂谷环境。

地幔去气与铀成矿的关系——以江西相山火山岩型铀矿为例

江西相山铀矿床，位于中生代赣一杭火山岩带相山火山塌陷盆地内，是中国目前发现的最大的火山岩型铀矿床，其独特的成矿环境及成矿机理为国内外地质界所瞩目。本论文主要运用岩石学、构造学寸流体包裹体地球化学、同位素地球化学、热力学方法，从相山铀矿床的成矿构造演化、成矿流体、岩石蚀变特征、成矿物质同位素组成特征以及热力学计算等方面对地慢去气特征、过程以及其与铀矿化的关系进行了详细的研究。本研究取得了以下主要认识：1、构造活动对成矿过程起到重要作用。区域深大断裂构造、慢源岩浆活动和碱交代蚀变作用，是相山铀矿田地（量去气作用产生的地慢流体参与成矿作用的有利条件和证据。2、热力学计算表明成矿期前成矿热液pH值为9．50，呈碱性；成矿期前，UO2（CO3）22-、UO2（Coa）44-两种形式迁移的U占总U的99.96％，即矿床中成矿期前的铀主要是以这两种形式迁移的。3、氦一氢同位素研究表明，相山铀矿床的成矿流体由富CO2和3He的慢源流体与贫CO2的大气成因流体混合而成。相山铀矿床成矿热液中的CO2总体属于慢源碳，主要是由地慢或分布在铀矿床中的漫源基性脉岩提供的，而且大部分是在地壳拉张作用期间由地慢去气作用产生而上升形成了成矿热液。4、相山铀矿田成矿期前的流体包裹体中气泡较大，气体含量较高，表明包裹体捕获时压力较大；成矿期和成矿后的包裹体中气泡较小，并存在大量的纯气相包体，通过激光拉曼分析测得的物相峰值极低，表明包体中所包含组分的含量极低。而且大量成矿期纯气相包体的发现也说明其是在去气过程中捕获的从成矿热液中释放出的气体。从成矿期前到成矿期后，CO2含量减小的变化。也说明了成矿作用中发生了减压去气过程。5、在铀成矿过程中，共发生了两次去气作用。第一次地慢去气作用产生并把C仇带入到成矿热液中，第二次成矿流体去气作用正好相反把CO2从成矿热液中带出。地慢去气作用产生富CO2+H2O的地慢流体运移到地壳浅部与大气降水混和，富含矿化剂的成矿溶液由此可以有效地从赋矿围岩（中酸性火山岩和盆地基底地层）中萃取出成矿所需的U。第一次地慢去气作用产生的富CO2+H2O的地慢流体为成矿提供了最充足的矿化剂（CO2），是成矿作用得以发生的最基本最重要的条件。

喀拉通克含矿岩体（Y2）的岩石学研究

从主元素化学来看，喀拉通克深成岩以低Ca、Al为特征，而火山岩（玄武岩类）以高Ca、Al为特征；在早期结晶矿物组合上，喀拉通克深成岩为橄榄石、斜方辉石和基性斜长石，而火山岩中斑晶以基性斜长石、背地里斜辉石为主，其次为橄榄石，没有见到斜方辉石斑晶，在Sr-Zr图和Nd-Zr图中二者具有较大差别。利用矿物温度计计算了橄榄石、辉石和斜长石的结晶温度。橄榄石是在稍高于1880℃下开始结晶的，二辉石共存时的温度为1100℃左右，基性斜长石的结晶温度也在1100℃左右，并定性讨论了二号岩体的水含量和氧逸度。比较详细地从定性和定量两方面探讨了岩体成岩压力范围，认为前人计算的7Kb过大。根据橄榄石和斜长石共存现象说明压力小于7Kb，单斜辉石中的铝含量进一步说明压力小于5Kb，最后半定量地利用角闪石地质压力计说明4Kb作为二号岩体的成岩压力是比较可信的。最后探讨了二号岩体所属系列和分异趋势。许多证据表明二号岩体属于钙碱系列岩体，比如结晶矿物类型和顺序等符合obsorn(1962)建立的造山带钙碱系列；在SiO2-K2O图和AFM图中皆落入钙碱系列；辉石的成分变化不具有富铁趋势；所有岩石都有一定量的角闪石；微量元素如Rb、K/Rb、Zr等以及稀土模式与岛弧钙碱岩浆相似。与世界著名钙碱系列岩体比较表明，它们共同的特征是产于造山带环境，岩石都有一定量的含水矿物存在，说明母岩浆富水对于钙碱系列的形成具有重要的作用。若将造岩矿物的成分变化范围投影到AFM图中，可以看出造成二号岩体如此钙碱系列演化线的原因在于岩石中橄榄石和辉石的富铁趋势很弱、岩石中含有较多的黑云母和角闪石以及随着分异进行结晶出越来越多的长石。二号岩体高Si、H2O，低Ca、Al的特征决定了二号岩体的矿物结晶顺序为橄榄石→斜方辉石→拉长石→单斜辉石→角闪石→黑云母，形成相应的岩相为橄榄苏长岩、苏长岩、辉长岩和闪长岩相。辉石的Mg~#值变化很窄，是由于二号岩体含水量较高，使辉石在高En值下停止结晶，而为含水矿物角闪石取代。以上通过对喀拉通克含矿岩体（Y2）的岩石学研究，可以得到如下结论：一、喀拉通克含矿岩体由橄榄苏长岩、苏长岩、辉长岩和闪长岩四个岩相组成。各个岩相是由同一母岩浆经分异形成的。岩体岩相的反环带结构说明岩体不可能是由均匀岩浆一次侵位就地分异形成，而是岩浆深部分异与构造活动结合的产物。二、喀拉通克含矿岩体的母岩浆是产于造山带的一种钙碱性岩浆，以高Si、H2O，低Ca、Al为特征，其母岩浆不z可能是科马提岩、洋中脊拉斑玄武岩、高铝玄武岩或碱性玄武岩浆中的任一种。三、喀拉通克含矿深成岩和该区火山岩在主元素、微量元素及矿物晶出顺序方面存在一定差异，这种差异不大可能是由结晶环境不同造成的，更可能的是两者起源于不同的母岩浆。四、从定性和定量两方面讨论了喀拉通克含矿岩体的成岩压力，从而将4Kb作为该岩体的成岩压力是比较可信的。五、从岩体分异趋势来看，喀拉通克含矿岩体属于钙碱系列岩体。造成钙碱系列分异趋势的主要原因在于岩石中橄榄石和辉石的富铁趋势很弱，岩石含有较多的黑云母和角闪石以及随着分异进行结晶出越来越多的长石。对于以上分异趋势的形成，岩浆富水起着较大的作用。富水一方面使辉石在高En值下停止结晶，以角闪石代替；另一方面使岩浆的氧逸度有所提高。

Investigation into the rheological properties of PES/NMP/nonsolvent membrane-forming systems

From the perspective of a polymer solution, the rheological properties of the popular polyethersulfone (PES)/N-methyl-2-pyrrolidone (NMP)/nonsolvent (NS) membrane-forming system were investigated thoroughly with a controlled stress rheometer (HAAKE RS75, Germany). The scope of the study included measurements of the controlled-stress flow curve, creep recovery, and dynamic oscillation. H2O, 1-butanol, ethylene glycol, and diethylene glycol were used as NS additives. The effects of the polymer concentration and the quality of the solvent mixture, as characterized by the approaching ratio, on the rheological behavior of the dopes were studied. Up to 38 wt % PES and extremely adjacent to the phase separation (i.e., the approaching ratio of the dope was 0.95), the viscous property dominated all the dopes, which behaved as Newtonian fluids. Moreover, all the membrane-forming dopes investigated were in the crossover regime in the semidilute region, in which the chains were overlapping but unentangled. (C) 2001 John Wiley & Sons, Inc.

NO reduction and CO oxidation over Cu/Ce/Mg/Al mixed oxide catalyst in FCC operation

Simultaneous NO reduction and CO oxidation in the presence of O-2,H2O and SO2 over Cu/Mg/AUO (Cu-cat), Ce/Mg/Al/O (Ce-cat) and Cu/Ce/Mg/Al/O (CuCe-cat) were studied. At low temperatures (<340 degreesC), the presence of O-2 or H2O enhanced the activity of CuCe-cat for NO and CO conversions, but significantly suppressed the activity of Cu-cat and Ce-cat, At high temperature (720 degreesC), the presence of O-2 or H2O had no adverse effect on the NO and CO conversions over these catalysts. The addition of SO2 to NO + CO + O-2 + H2O system had no effect on the, reaction of CO + O-2 over Cu-cat, but deactivated this catalyst for NO + CO and CO + H2O reactions; over Ce-cat, all of these reactions of NO + CO, CO + O-2 and CO + H2O were suppressed significantly; over CuCe-cat, NO + CO and CO + O-2 reactions were not affected while the reaction of CO + H2O was slightly inhibited. (C) 2002 Elsevier Science B.V. All rights reserved.

Adsorption and interaction of H2S/SO2 on TiO2

Adsorption and interaction of H2S/SO2 on titania as well as on alumina for comparison has been studied by temperature programmed desorption (TPD), infrared (IR) spectroscopy and temperature programmed electronic conductivity (TPEC) techniques. It was found that the adsorption of both H2S acid SO2 on TiO2 is much greater than on Al2O3. The electronic conductivity of TiO2 measured by TPEC varies significantly as adsorption and desorption takes place on TiO2, showing a strong interaction between TiO2 and adsorbates. At temperature above 200 degrees C, H2S or SO2 adsorbed on TiO2 can be converted into S, H2O and SO2 or SO3. While on the hydrogen treated TiO2, H2S is decomposed into S and H-2, SO2 into S. The active sites on TiO2 surface cannot be so strongly adsorbed by SO2 that it is much more resistant to the sulfation reaction. Unlike TiO2, Al2O3 only provides surface adsorption sites, which can be readily sulfated. The data obtained support one's understanding why TiO2 exhibits a better catalytic performance than that of Al2O3 as a Claus reaction catalyst. (C) 1999 Elsevier Science B.V. All rights reserved.

Formation and dissociation of protonated pyridine-methanol cluster ions at 355 and 266 nm

The multi-photon ionization process of the hydrogen-bond cluster of pyridine-methanol has been investigated using a conventional and reflectron time-of-flight mass spectrometer (RTOF-MS) at 355 and 266 nm laser wavelengths, respectively. The sequences of the protonated cluster ions (CH3OH)(n)H+ and (C5H5Nn)(CH3OH)(m)H+ (n = 1,2) were observed at both laser wavelengths, while the sequence of the cluster ions (CH3)OHn (H2O)H+ was observed only at 355 nm laser wavelength. The difference between the relative signal intensities of the protonated methanol cluster ions at different laser wavelengths is attributed to different photoionization mechanisms. Some nascent cluster ions in metastable states dissociated during free flight to the detector. The dissociation kinetics is also discussed. (C) 2000 Elsevier Science B.V.

An integrated air-POM syngas/dimethyl ether process from natural gas

A Cu-Zn-Al methanol catalyst combined with HZSM-5 was used for dimethyl ether (DME) synthesis from a syngas containing nitrogen, which was produced by air-partial oxidation of methane (air-POM). Air-POM occurred at 850 degreesC, 0.8 MPa, CH4/air/H2O/CO2 ratio of 1/2.4/0.8/0.4 over a Ni-based catalyst modified by magnesia and lanthanum oxide with 96% CH4 conversion and constantly gave syngas with a H-2/CO ratio of 2/1 during a period of 450 h. The obtained N-2-containing syngas was used directly for DME synthesis. About 90% CO per-pass conversion, 78% DME selectivity and 70% DME yield could be achieved during 450 h stability testing under the pressure of 5.0 MPa. the temperature of 240 degreesC and the space velocity of 1000 h(-1). (C) 2002 Elsevier Science B. V. All rights reserved.

A remarkable synergic effect of water-soluble bimetallic catalyst in the hydrogenation of aromatic nitrocompounds

Hydrogenation of nitrobenzene can be catalyzed by the water-soluble catalyst PdCl2(TPPTS)(2) (TPPTS = tris(m-sulfonatophenyl)phosphine trisodium salt) under normal pressure at 65 degrees C in H2O/toluene biphasic solvent system. The exhibits higher catalytic activity and selectivity for the hydrogenation of aromatic nitrocompounds, compared with PdCl2(TPPTS)(2) or H2PtCl6 alone. The transmission electron micrographs demonstrate that the monometallic catalyst is composed of ultrafine palladium particles of almost uniform size while the particles of bimetallic catalyst are more widely distributed in size than those of the monometallic ones. (C) 1999 Elsevier Science B.V. All rights reserved.

Isospecific polymerization of styrene with modified ziegler-type catalysts

Effects of various kinds of additives as well as aging of the catalyst on the polymerization of styrene catalyzed by TiCl4/MgCl2-AlEt3 system have been studied. Experiments show that in toluene the isotacticity of polystyrene can be up to 83% for aged catalyst, whereas when the catalyst is not aged. non-stereospecific polymer is the main product. When PCl3 is used as an additive, the catalyst system gives high activity and isotacticity. The use of a mixture of AlEt3/H2O (1: 1 mole ratio) as a cocatalyst is also efficient. The catalyst [TiCl4-PCl3/MgCl2-AlEt3/H2O] displays high activity and product isotacticity (94%) with an average molecular weight up to 2 X 10(-6). When Co(acac)(3) is added to to [TiCl4/MgCl2-AlEt3] catalyst after it was aged, the isotacticity can be up to 97%. (C) 2001 Elsevier Science Ltd. All rights reserved.

Modeling of a compact plate-fin reformer for methanol steam reforming in fuel cell systems

The characteristics of a compact plate-fin reformer (PFR) which integrates endothermic and exothermic reactions into one unit have been investigated by experiment as well as by numerical simulation. One reforming chamber was integrated with two vaporization chambers and two combustion chambers to constitute a single unit of PFR. In the PFR, which is based on a plate-fin beat exchanger, catalytic combustion of the reforming gas is used to simulate the fuel cell anode off gas (AOG) which supplies the necessary heat for the methanol steam reforming. Temperature distributions in all chambers and composition distribution in reforming chamber have been studied, and the effect of the ratio of H2O/CH3OH on the performance of the PFR has also been investigated. A model of the PFR was derived using a three-dimensional numerical model for a cross-current flow arrangement. Theoretical predictions of the temperature distributions in the PFR were in good agreement with experimental values. In addition, the numerical model was able to accurately predict the methanol conversion and the reformate composition in reforming chamber. © 2005 Elsevier B.V. All rights reserved.

Catalytic steam reforming of ethanol to produce hydrogen and acetone

Steam reforming of ethanol over CuO/CeO2 was studied. Acetaldehyde and hydrogen were mainly produced at 260degreesC. At 380degreesC, acetone was the main product, and 2 mol of hydrogen was produced from 1 mol of ethanol. The formation of hydrogen accompanied by the production of acetone was considered to proceed through the following, consecutive reactions: dehydrogenation of ethanol to acetaldehyde. aldol condensation of the acetaldehyde, and the reaction of the aldol with the lattice oxygen [O(s)] on the catalyst to form a surface intermediate, followed by its dehydrogenation and decarboxylation. The overall reaction was expressed by2C(2)H(5)OH + H2O --> CH3COCH3 + CO2 + 4H(2). Ceria played an important role as an oxygen supplier. The addition of MgO to CuO/CeO2 resulted in the production of hydrogen at lower temperatures by accelerating aldol condensation. (C) 2004 Elsevier B.V. All rights reserved.

Methanol steam reforming in a compact plate-fin reformer for fuel-cell systems

A compact plate-fin reformer (PFR) consisting of closely spaced plate-fins, in which endothermic and exothermic reactions take place in alternate chambers, has been studied. In the PFR, which was based on a plate-fin heat exchanger, catalytic combustion of the reforming gas, as a simulation of the fuel cell anode off gas (AOG), supplied the necessary heat for the reforming reaction. One reforming chamber, which was for hydrogen production, was integrated with two vaporization chambers and two combustion chambers to constitute a single unit of PFR. The PFR is very compact, easy to be placed and scaled up. The effect of the ratio of H2O/CH3OH on the performance of the PFR has been investigated, and temperature distributions in different chambers were studied. Besides, the stationary behavior of the PFR was also investigated. Heat transfer of the reformer was enhanced by internal plate-fins as well as by external catalytic combustion, which offer both high methanol conversion ratio and low CO concentration. In addition, the fully integrated reformer exhibited good test stability. Based on the PFR, a scale-up reformer was designed and operated continuously for 1000 h, with high methanol conversion ratio and low CO concentration. (c) 2004 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.

Autothermal reforming of n-octane on Ru-based catalysts

In an attempt to effectively integrate catalytic partial oxidation (CPO) and steam reforming (SR) reactions on the same catalyst, autothermal reforming (ATR) of n-octane was addressed based on thermodynamic analysis and carried out on a non-pyrophoric catalyst 0.3 wt.% Ru/K2O-CeO2/gamma-Al2O3. The ATR of n-octane was more efficient at the molar ratio Of O-2/C 0.35-0.45 and H2O/C 1.6-2.2 (independent parameters), respectively, and reforming temperature of 750-800 degrees C (dependent parameter). Among the sophisticated reaction network, the main reaction thread was deducted as: long-chain hydrocarbon -> CH4, short-chain hydrocarbon -> CO2, CO and H-2 formation by steam reforming, although the parallel CPO, decomposition and reverse water gas shift reaction took place on the same catalyst. Low temperature and high steam partial pressure had more positive effect on CH4 SR to produce CO2 other than CO. This was verified by the tendency of the outlet reformate to the equilibrium at different operation conditions. Furthermore, the loss of active components and the formation of stable but less active components in the catalyst in the harsh ATR atmosphere firstly make the CO inhibition capability suffer, then eventually aggravated the ATR performance, which was verified by the characterizations of X-ray fluorescence, BET specific surface areas and temperature programmed reduction. (c) 2005 Elsevier B.V. All rights reserved.

Combined single-pass conversion of methane via oxidative coupling and dehydro-aromatization

A single-pass process with the combination of oxidative coupling (OCM) and dehydro-aromatization (MDA) for the direct conversion of methane is carried out. With the assistance of the OCM reaction over the SrO-La2O3/CaO catalyst loaded on top of the catalyst bed, the duration of the dehydro-aromatization reaction catalyzed by a 6Mo/HMCM-49 catalyst shows a significant improvement, and. the initial deactivation rate constant of the overall process revealed about 1.5 x 10(-6) s(-1). Up to 72 h on stream, the yield of aromatics was still maintained at 5.0% with a methane conversion of 9.6%, which is obviously higher than that reported for the conventional MDA process with single catalyst. Upon the TPR results, this wonderful enhancement would be attributed to an in-situ formation of CO2 and H2O through the OCM reaction, which serves as a scavenger for actively removing the coke formed during the MDA reaction via a reverse Boudouard reaction and the water gas reaction as well.