Photosynthetic bicarbonate utilization in Porphyra haitanensis (Bangiales, Rhodophyta)

The activities of carbonic anhydrase (CA) and photosynthesis of Porphyra haitanensis were investigated in order to see its photosynthetic utilization of inorganic carbon source. Both intra- and extra-cellular CA activities existed in the thallus. CA inhibitors, acetazolamide (AZ) and ethoxyzolamide (EZ), remarkably depressed the photosynthetic oxygen evolution in seawater of pH 8.2 and 10.0, and EZ showed stronger inhibition than AZ. The observed net photosynthetic rate In seawater of pH 8.2 was much higher than that of CO2 supply theoretically derived from spontaneous dehydration of HCO3-. P. haitanensis also showed a rather high pH compensation point (9.9). The results demonstrated that P. haitanensis could utilize bicarbonate as the external inorganic carbon source for photosynthesis. The bicarbonate utilization was closely associated with HCO3- dehydration catalyzed by extracellular CA activity. The inorganic carbon composition in seawater could well saturate the photosynthesis of P. haitanensis. The low K-m value and compensation points for inorganic carbon reflected the existence of CO2-concentrating mechanism in this alga.

内循环流化床生物质气化过程的神经网络模型

基于BP人工神经网络原理，利用MATLAB神经网络工具箱，以实验得到的57组气化实验数据作为样本，建立了一个以加料量和送风量为输入变量，以燃气热值、产气率、碳转化率和气化效率为输出变量，用于描述连续稳定气化过程的内循环流化床生物质气化模型。对模型的隐层节点数和训练周期改变对模拟结果的影响进行了分析，发现当隐层节点数为20，训练步骤为50步，模型的4个输出变量的模拟结果与实验结果相关系数均超过0．95；同时对该模型的预测能力进行了考察，模型预测结果与实验结果吻合良好，证明了该模型具有较强的泛化能力，为生物质内循环流化床气化系统的优化设计和自动控制提供新思路。

酸化油固定床酶法合成生物柴油研究

以固定化的假丝酵母酶为催化剂，在三段式固定床反应器内，醇油摩尔比为1：1，采用分级流加甲醇的方式，将高酸值的酸化油转化为生物柴油，探讨了酶量、溶剂量、水量、温度、反应液流速等与产物中甲酯含量的关系。正交实验结果表明，反应的最适条件为酶用量、溶剂量、水量分别为油重的15％、10％、10％，反应液流速为0.8g·min^-1，温度为45℃，在此条件下，产物中甲酯含量达到了90．18％。

生物质煤气废水氨氮脱除的研究

生物质煤气废水是一种新出现的高浓度氨氮有机废水。作者采用化学沉淀法去除该废水中的氨氮，研究了不同沉淀剂、pH、温度和搅拌时间对氨氮去除效果的影响。结果表明，MgCl2＋Na3PO4·12H2O明显优于其他沉淀剂组合。当n（Mg^2＋）：n（NH4^＋）：n（PO4^3-）=1：1：1、pH10．0、温度30℃、搅拌时间30min时，废水中的氨氮质量浓度从处理前的222mg/L降到17mg／L，去除率为92.3％。

生物质气化与废弃物焚烧联合发电的技术经济分析

介绍了生物质气化与废弃物焚烧联合发电技术项目，确定了该项目经济效益的评价指标，定量计算了项目的投资回收期、净现值和内部收益率。同时还对燃料费用、上网电价和固定资产变化引起的敏感性进行分析。结果表明，该联合发电技术的动态投资回收期为9.05a，净现值为2770万元，内部收益率为15.82％，三个经济指标均符合行业标准。从经济角度看是完全可行的。

Scale study of direct synthesis of dimethyl ether from biomass synthesis gas

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.

Kinetic Model Study on Enzymatic Hydrolysis of Cellulose Using Artificial Neural Networks

Enzymatic hydrolysis of cellulose was highly complex because of the unclear enzymatic mechanism and many factors that affect the heterogeneous system. Therefore, it is difficult to build a theoretical model to study cellulose hydrolysis by cellulase. Artificial neural network (ANN) was used to simulate and predict this enzymatic reaction and compared with the response surface model (RSM). The independent variables were cellulase amount X-1, substrate concentration X-2, and reaction time X-3, and the response variables were reducing sugar concentration Y-1 and transformation rate of the raw material Y-2. The experimental results showed that ANN was much more suitable for studying the kinetics of the enzymatic hydrolysis than RSM. During the simulation process, relative errors produced by the ANN model were apparently smaller than that by RSM except one and the central experimental points. During the prediction process, values produced by the ANN model were much closer to the experimental values than that produced by RSM. These showed that ANN is a persuasive tool that can be used for studying the kinetics of cellulose hydrolysis catalyzed by cellulase.

On the acid-base stability of Keggin Al-13 and Al-30 polymers in polyaluminum coagulants

The acid-base stabilities of Al-13 and Al-30 in polyaluminum coagulants during aging and after dosing into water were studied systematically using batch and flow-through acid-base titration experiments. The acid decomposition rates of both Al-13 and Al-30 increase rapidly with the decrease in solution pH. The acid decompositions of Al-13 and Al-30 with respect to H+ concentration are composed of two parallel first-order and second-order reactions, and the reaction orders are 1.169 and 1.005, respectively. The acid decomposition rates of Al-13 and Al-30 increase slightly when the temperature increases from 20 to ca. 35 A degrees C, but decrease when the temperature increases further. Al-30 is more stable than Al-13 in acidic solution, and the stability difference increases as the pH decreases. Al-30 is more possible to become the dominant species in polyaluminum coagulants than Al-13. The acid catalyzed decomposition and followed by recrystallization to form bayerite is one of the main processes that are responsible for the decrease of Al-13 and Al-30 in polyaluminum coagulants during storage. The deprotonation and polymerization of Al-13 and Al-30 depend on solution pH. The hydrolysis products are positively charged, and consist mainly of repeated Al-13 and Al-30 units rather than amorphous Al(OH)(3) precipitates. Al-30 is less stable than Al-13 upon alkaline hydrolysis. Al-13 is stable at pH < 5.9, while Al-30 lose one proton at the pH 4.6-5.75. Al-13 and Al-30 lose respective 5 and 10 protons and form [Al-13] (n) and [Al-30] (n) clusters within the pH region of 5.9-6.25 and 5.75-6.65, respectively. This indicates that Al-30 is easier to aggregate than Al-13 at the acidic side, but [Al-13] (n) is much easier to convert to Alsol-gel than [Al-30] (n) . Al-30 possesses better characteristics than Al-13 when used as coagulant because the hydrolysis products of Al-30 possess higher charges than that of Al-13, and [Al-30] (n) clusters exist within a wider pH range.

Synthesis of biodiesel from waste cooking oil using immobilized lipase in fixed bed reactor

Waste cooking oil (WCO) is the residue from the kitchen, restaurants, food factories and even human and animal waste which not only harm people's health but also causes environmental pollution. The production of biodiesel from waste cooking oil to partially substitute petroleum diesel is one of the measures for solving the twin problems of environment pollution and energy shortage. In this project, synthesis of biodiesel was catalyzed by immobilized Candida lipase in a three-step fixed bed reactor. The reaction solution was a mixture of WCO, water, methanol and solvent (hexane). The main product was biodiesel consisted of fatty acid methyl ester (FAME), of which methyl oleate was the main component. Effects of lipase, solvent, water, and temperature and flow of the reaction mixture on the synthesis of biodiesel were analyzed. The results indicate that a 91.08% of FAME can be achieved in the end product under optimal conditions. Most of the chemical and physical characters of the biodiesel were superior to the standards for 0(#)diesel (GB/T 19147) and biodiesel (DIN V51606 and ASTM D-6751).

The design and operation of a new clapboard-type internal circulating fluidized-bed gasifier

The design and operation of a new clapboard-type internal circulating fluidized-bed gasifier is proposed in this article. By arranging the clapboard in the bed, the gasifier is thus divided into two regions, which are characterized by different fluidization velocities. The bed structure is designed so that it can guide the circulating flow passing through the two regions, and therefore the feedstock particles entrained in the flow experience longer residence time. The experimental results based on the present new design, operating in the temperature range of 790 degrees C-850 degrees C, indicate that the gas yield is from 1.6-1.9 Nm(3)/kg feedstock, the gas enthalpies are 5,345 kJ/Nm(3) for wood chip and 4,875 kJ/m(3) for rice husk, and a gasification efficiency up to 75% can be obtained.

A study on the economic efficiency of hydrogen production from biomass residues in China

As part of Pilot Project of KIP of CAS, a feasibility study of hydrogen production system using biomass residues is conducted. This study is based on a process of oxygen-rich air gasification of biomass in a downdraft gasifier plus CO-shift. The capacity of this system is 6.4 t biomass/d. Applying this system, it is expected that an annual production of 480 billion N m(3) H-2 will be generated for domestic supply in China. The capital cost of the plant used in this study is 1328$/(N m(3)/h) H-2 out, and product supply cost is 0.15$/N m(3) H-2. The cost sensitivity analysis on this system tells that electricity and catalyst cost are the two most important factors to influence hydrogen production cost.

Novel biodiesel production technology from soybean soapstock

This paper describes an attractive method to make biodiesel from soybean soapstock (SS). A novel recovery technology of acid oil (AO) from SS has been developed with only sulfuric acid solution under the ambient temperature (25 +/- 2 degrees C). After drying, AO contained 50.0% FFA, 15.5% TAG 6.9% DAG 3.1% MAG 0.8% water and other inert materials. The recovery yield of AO was about 97% (w/w) based on the total fatty acids of the SS. The acid oil could be directly converted into biodiesel at 95 degrees C in a pressurized reactor within 5 hours. Optimal esterification conditions were determined to be a weight ratio of 1 : 1.5 : 0.1 of AO/methanol/sulfuric acid. Higher reaction temperature helps to shorten the reaction time and requires less catalyst and methanol. Ester content of the biodiesel derived from AO through one-step acid catalyzed reaction is around 92%. After distillation, the purity of the biodiesel produced from AO is 97.6% which meets the Biodiesel Specification of Korea. The yield of purified biodiesel was 94% (w/w) based on the total fatty acids of the soapstock.

Lewis酸引发的LLDPE/PS共混体系的原位反应增容及其结构与性能研究

本文以单组分和双组分Lewis酸为催化剂，采用反应加工的方法，制备了原位反应增容的线性低密度聚乙烯/聚苯乙烯共混物（LLDPE/PS），并对原位反应增容的机理、增容体系的结构性能以及Lewis酸对共混组分的降解作用进行了系统研究。 以FTIR和NMR为手段、二甲苯为模拟化合物，确认LLDPE/PS共混体系在Lewis酸为催化剂作用下发生了LLDPE与PS的接枝反应，LLDPE接枝在PS苯环的对位上。形成的原位接枝共聚物对体系起增容作用。 使用溶剂抽提、SEM、DMA、流变和DSC等手段对以单组分Lewis酸AlCl3 为催化剂的LLDPE/PS共混物的结构性能进行了研究。从溶剂抽提前后的重量比计算了接枝物的含量。催化剂用量较低时体系中的接枝物含量随AlCl3的增加而提高，随着AlCl3进一步增加，接枝物含量不会增加反而下降，发现AlCl3导致均聚物的降解。研究结果表明，共混体系中加入适量的AlCl3催化剂后，分散相尺寸减小，分布均匀，储能模量增加，低频区的复数黏度升高。但AlCl3用量过高时使共混物的分散相尺寸增加，分布均匀度下降，储能模量和复数黏度降低。以GPC为手段研究了单组分 Lewis酸AlCl3对共混组分的降解作用，发现对PS的降解作用显著。 由于单组分Lewis酸催化剂会导致共混组分降解，使共混体系的物理机械性能变劣，为此，我们在LLDPE/PS共混物中引入了双组分Lewis酸催化剂（Me3SiCl、InCl3•4H2O）。结果表明双组分Lewis酸催化剂不但能够催化LLDPE和PS的原位接枝反应，获得高性能的LLDPE/PS合金材料，而且不会引发共混组分PS的降解。在催化剂用量固定时，采用双组分催化剂时共混物的拉伸强度随着LLDPE含量的增加几乎保持不变，但冲击强度有十分明显的提高。对比了加入催化剂前后共混物形貌的变化，增容后的共混物中分散相粒子尺寸显著降低，证明了双Lewis酸良好的催化性能。 对以双Lewis酸为催化剂的共混物的流变行为和结晶行为进行了研究。随着催化剂的加入，两相之间的相互作用增强，因此共混物的复数黏度，储能模量和损耗模量都有不同程度的提高。增容后的LLDPE相区变小，因而在冷却过程中出现不同程度的分步结晶现象。 对单组分和双组分Lewis酸催化剂原位反应增容LLDPE/PS共混体系的机理进行了探讨。机理为Friedel-Crafts烷基化反应。在采用单组分Lewis酸催化剂时， AlCl3与体系中含有的微量水等杂质发生反应，形成一个复合物，然后进一步与聚乙烯中的不饱和的双键发生反应形成碳正离子，并攻击LLDPE分子链从而形成大分子的碳正离子LLDPE+，而这些LLDPE+则通过电子的重排而发生剪切断裂。在催化剂的存在下，这些断裂的LLDPE片断取代PS中的苯环上的质子而发生接枝反应，从而形成LLDPE-g-PS共聚物。采用双组分Lewis酸催化剂时，首先发生双Lewis酸的耦合；耦合后的Lewis酸与水等杂质反应生成复合物，然后与非饱和的LLDPE分子反应生成初级碳正离子；初级碳正离子进攻LLDPE主链，生成较大的碳正离子；LLDPE+碳正离子取代PS苯环对位的质子而生成接枝共聚物。

一价铜催化Ullmann 反应合成联苯醚和芳基烷基醚的研究

联苯醚和芳基烷基醚类化合物是天然产物和聚合物材料中的重要的片段结构，研究其合成具有重要意义。近年来，过渡金属催化形成碳-氧键已成为制备联苯醚和芳基烷基醚类化合物的重要方法。钯体系虽然成功，但由于其属于贵金属，价格昂贵，而且反应所必须的有机膦配体，毒性较大，对环境危害较大，所以其应用受到了限制。 本论文通过利用空气稳定的Cu(bpy)2BF4 配合物，使得苯酚和烷基醇有效地进行偶合得到联苯醚产物。该方法可以在不使用昂贵弱碱Cs2CO3 的情况下，取得很好的产率，并且在较低的催化剂载入量的情况下，可以很好地适应各种官能团取代的底物。 本论文通过配体的扫描筛选，使得溴代苯和烷基醇的偶合反应得到了发展。更重要的是，使用该体系时分子间和分子内的碳-氧键都可以形成。通过该方法合成了一系列苯并环醚类化合物，这也是一价铜体系催化制备该类化合物的首次报道。