合成工艺条件对A1－Ferron反应动力学特征及Al（Ⅲ）形态分布的影响

通过Al-Ferron络合比色动力学分析，对Al(Ⅲ)的形态进行了较为准确的划分和计算，考察了工艺条件对动力学参数和铝形态分布的影响．研究表明，铝的初始浓度、合成温度对Alh与Ferron的解离-络合反应的速率常数kb有一定的影响，而碱化度、合成时的搅拌强度和加碱速度对kb的影响不大；碱化度、铝的初始浓度对铝的形态分布影响很大，搅拌强度、合成温度和加碱速度对铝的形态分布也有一定的影响。     

调理脱水污泥的热解特性及动力学分析

利用TGA(Thermogravimetric analysis)热分析技术对污水处理厂原始污泥及调理脱水污泥进行了实验研究,获得了不同升温速率下污泥的TG(Thermogravimetric)和DTG失重曲线.实验发现,不同调理脱水污泥热解特性复杂,且热解动力学在不同转化率下对应的动力学反应也不同.并利用M-KAS(Kissinger-AkahiraSunose)模型和Discrete DAEM(Discrete distribute activation energy model)模型对不同调理污泥进行了动力学参数研究.结果表明,污泥的非等温热解过程包含3个失重阶段;升温速率影响污泥热解特征温度,随着升温速率的提高,失重曲线向高温区滑移.利用上述模型计算的动力学参数变化趋势表明所采用的Fenton及赤泥复合调理对污泥热解特性有很大影响,Fenton调理有助于污泥EPS(Extracellular polymeric substances)破坏,影响热解反应中的形核过程,进而影响热解动力学变化趋势;赤泥调理后,赤泥更容易与破坏的污泥细小颗粒结合,增加了污泥热解反应数量,影响整个污泥热解过程.从计算结果可以看出污泥热解由多步反应组成,整个热解过程动力学参数不断变化.     

利用响应面优化Klebsiella variicola对麻疯树籽饼粕佛波酯的固态发酵降解

为降解麻疯树籽饼粕中的毒性成分佛波酯,利用Klebsiella variicola进行固态发酵.采用单因素实验法研究了发酵温度、接种量、初始加水量、发酵时间对佛波酯降解率的影响.在此实验结果基础上,利用Design Expert8.0软件进行分析建立了发酵温度、接种量、初始加水量3个因素对佛波酯降解率影响的优化模型.该模型极显著(P0.001),拟合度良好.经实验证实,在发酵温度为37℃、接种量33%(V/m)、初始加水量为105%(V/m)条件下发酵48 h,佛波酯降解率可达到84.30%,另一种毒性物质curcin的降解率可达63.21%.研究表明,利用响应面优化K.variicola固态发酵麻疯树籽饼粕过程,既可提高佛波酯降解率,也可降解curcin,具有生产指导意义.     

合成工艺条件对Al-Ferron反应动力学特征及Al(Ⅲ)形态分布的影响

通过Al Ferron络合比色动力学分析 ,对Al(Ⅲ )的形态进行了较为准确的划分和计算 ,考察了工艺条件对动力学参数和铝形态分布的影响 .研究表明 ,铝的初始浓度、合成温度对Alb 与Ferron的解离 络合反应的速率常数kb 有一定的影响 ,而碱化度、合成时的搅拌强度和加碱速度对kb 的影响不大 ;碱化度、铝的初始浓度对铝的形态分布影响很大 ,搅拌强度、合成温度和加碱速度对铝的形态分布也有一定的影响 .     

文蛤养殖水体中重金属Cu的安全限量值研究

通过引入沉积物因子,构建海水-底泥-生物体体系,应用半静态双箱动力学模型在室内模拟了沉积物暴露条件下文蛤(Meretrix meretrix)对重金属Cu的生物富集实验。通过对富集与排出过程中文蛤体内重金属Cu的动态监测和监测结果的非线性拟合,得到了文蛤富集Cu的动力学参数:吸收速率常数k1为71.18、排出速率常数k2为0.03,生物富集系数(bioconcen-tration factors,BCF)平均值为4283.86。对模型的拟合优度检验结果显示,沉积物暴露条件下文蛤对重金属Cu的生物富集数据符合双箱模型。根据双箱动力学模型推算出来的文蛤养殖水体中Cu的安全限量值为0.017mg·L-1。实验结果表明,沉积物暴露条件下双箱动力学模型在一定条件下是可以应用于文蛤富集动力学研究的。通过对比室内模拟实验与实地调查所得BCF发现本研究得出的Cu的安全限量值略高于现有标准。     

高温堆肥中微生物的生长特征及动力学建模

对高温好氧堆肥中微生物的生长特征和动力学进行了研究，发现微生物的生长受温度影响很大，随温度变化呈波动性变化．同时，基于Logistic模型和Malthus模型，对微生物生长进行分析，得到了描述堆肥过程中的微生物生长动力学模型和模型参数．用实验数据与模型计算值进行验证比较，模型计算与实验结果拟合良好，模型正确地反映了高温好氧堆肥中微生物的生长过程及其动力学机制．图3表1参12     

改性竹炭颗粒对水溶液中孔雀绿的吸附动力学研究

用不同的酸碱溶液处理竹炭,研究改性竹炭颗粒对水溶液中孔雀绿的吸附效果,再对筛选出的竹炭颗粒进行吸附动力学试验,并用准二级动力学模型和颗粒扩散模型对试验数据进行拟合,在此基础上进一步探讨影响吸附过程的因素。试验结果表明,用0.5 mol.L-1NaOH溶液处理过的竹炭颗粒吸附效果最佳,最大吸附量可达9.96 mg.g-1。颗粒扩散模型能更好地描述吸附动力学过程。竹炭颗粒的质量增加会降低孔雀绿分子的扩散速率;孔雀绿溶液的初始浓度增加则提高孔雀绿分子的扩散速率;颗粒直径、搅拌速度以及溶液的初始pH值也会影响吸附过程。     

好氧颗粒污泥对水溶液中酸性淡黄2G的生物吸附

利用好氧颗粒污泥对酸性淡黄2G溶液进行吸附脱色研究,考察了pH值、吸附剂用量、初始酸性淡黄2G的浓度、温度以及NaCl浓度对吸附过程的影响.实验结果表明,吸附过程对溶液pH值具有很高的依赖性,其最佳pH值为2.0.Temkin等温线在整个实验染料浓度范围内能够很好地描述吸附过程.吸附动力学符合准二级动力学模型.内部扩散和边界层扩散都可能影响生物吸附速率.热力学分析表明,吸附过程是一个自发的放热过程.采用FTIR分析的结果进一步揭示了颗粒污泥上官能团(如胺基、羧基和羟基等)可能是染料生物吸附的活跃结合位点.这些结果表明,好氧颗粒污泥可以作为吸附剂以去除水中的酸性淡黄2G。     

硝基苯在江水中生物降解动力学模拟研究

以第二松花江哨口断面江水为微生物源,对硝基苯的生物降解动力学进行研究。结果表明,硝基苯在江水中的生物降解过程可由对数方程S=S_0+X_0(1—e~(μmt))描述;丙酮作标准液溶剂时,硝基苯的生物降解速率符合一级动力学方程;由此得到硝基苯生物降解动力学参数,即微生物最大比增长速率μm和一级速率常数K。硝基苯的初始浓度(53.5—535μg/L)对l'm没有明显的影响,温度、驯化条件对μm的影响显著,硝基芳烃、氯苯类化合物对硝基苯的降解有抑制作用。     

不同热解条件下制备的秸秆炭对铜离子的吸附动力学

研究了不同热解条件下制备的秸秆生物炭对铜离子的吸附动力学规律.以常见的玉米杆和番茄杆为原料,在限氧升温热解的条件下制备生物炭.研究不同热解温度(300、400、500、600、700℃)和不同热解时间(1、2、4、6、8 h)对秸秆生物炭吸附性能的影响,实验结果表明番茄杆样品T6004和玉米杆样品C6006分别获得对铜离子的最佳吸附效果,其去除率分别为98.40%和98.77%.通过批试验探明秸秆生物炭对Cu~(2+)的吸附动力学特征与机理,秸秆生物炭对Cu~(2+)的吸附动力学数据随时间的变化能很好地用准二级动力学方程进行拟合,说明生物炭对Cu~(2+)的吸附是一个复杂的过程,并不是简单的单层吸附.用颗粒内扩散模型进行拟合分析发现,热解时间和温度对秸秆生物炭的吸附边界层厚度均会产生不同程度的影响.此外,颗粒内扩散并非吸附过程的唯一控速步骤,表面吸附和液膜扩散共同控制吸附反应速率.     

鲜甘薯发酵生产燃料乙醇中的降粘工艺

鲜甘薯高浓度发酵生产燃料乙醇的瓶颈之一是醪液粘度高,容易堵塞管路,严重影响工业化生产和增加能源消耗,同时也会降低乙醇发酵效率.为解决此问题,进行了添加降粘酶系及其作用条件优化研究,结果如下:1)确定最适降粘酶系为四川禾本生物工程有限公司的纤维素酶,粘度由1.7×104mPa.s降到8.8×102mPa.s,并且降低了生产成本;2)确定降粘酶作用前高温处理条件:110℃,20 min;3)最适降粘酶对不同品种鲜甘薯高浓度发酵的降粘效果表明降粘酶对大部分品种鲜甘薯降粘效果较好,粘度均约为1.0×103mPa.s以下,最低粘度只有2.7×102mPa.s,粘度下降率均在95%以上;4)在确定最适降粘酶系和其作用前高温条件后,将其应用于工业化生产,加入降粘酶2 h后发酵醪液的粘度由1.8×105mPa.s下降到2.7×103mPa.s,发酵后终粘度仅为7.9×102mPa.s,发酵时间仅为23 h,乙醇浓度达到10.56%(V/V),进一步验证了该降粘酶系应用于工业化鲜甘薯燃料乙醇生产的实际意义.表8参19     

Equilibrium studies on the adsorption of acid dye into chitin

We report the adsorption isotherm of acid dye on the surface of chitin, a unique solid adsorbent. Adsorption process offers an attractive benefit for a dyeing house treatment. Influences of essential kinetic parameters such as adsorbent particle size, reaction temperature governing the dye adsorption have been investigated. Adsorptions isotherms of dye on chitin were developed and the equilibrium data fitted well to the Langmuir, Freundlich and Redlich Peterson isotherm model. At optimum conditions maximum dye adsorption capacity of chitin estimated with the Langmuir 44.0, 85.0, 104.3 mg/g and 85.0, 114.10, 113.62 mg/g adsorbent. The results showed that chelating polymer of chitin could be considered as potential adsorbents for acid dye removal from dilute solution.     

Aerobic granular sludge formation based on substrate availability: Effects of flow pattern and fermentation pretreatment

• Penetration depth and substrate characters affect AGS formation and performance. • The relationship between substrate gradient and particle size affects AGS stability. • The fermentation process is proposed as a pretreatment to improve AGS stability. The influences of flow patterns (mixed-flow and plug-flow) and fermentation pretreatment on aerobic granular sludge (AGS) formation with various substrate availability levels were investigated by running four identical laboratory-scale sequencing batch reactors (R1–R4), comparing two anaerobic feeding strategies and three kinds of substrates. R1 achieved faster granulation with a fast influent fill step followed by a modified anaerobic mixed-flow phase, but the AGS showed poorer stability with a cracked structure and a high suspended solids concentration in the effluent. The anaerobic plug-flow feeding mode (with influent fed slowly from the bottom) in R2 provided deeper penetration depth for the substance to reach the core of AGS and accordingly strengthen AGS stability. An acidogenic up-flow sludge bed reactor was introduced as a pretreatment to improve the AGS performance by enhancing glucose pre-fermentation (R4). AGS fed with mixed volatile fatty acids (VFA) after glucose fermentation showed similar performance compared with the reactor fed with acetate in the aspects of stability, structure, size distribution and nitrogen removal efficiency, and 74% similarity in the microbial community. For actual wastewater with low VFA concentrations, fermentation treatment was suggested as a promising pretreatment for stable AGS granulation and operation.     

玉米套种堆作甘薯增产机理的研究

玉米套种“堆作甘薯”能充分利用光能，并降低土壤容重、增加孔隙度和提高三相比中的气相容积，同时使土壤热容量、导热率和热扩散率降低，昼夜温差增大，因此能明显提高甘薯的产量和品质。     

甘薯块根腐烂真菌的分离和鉴定

从腐烂甘薯块根中分离到4株丝状真菌,分别编号为SP-1、SP-2、SP-3和SP-4,它们都能在甘薯块根片上快速生长.将这4株真菌接种在PDA培养基上,观察其菌落形态和结构特征.提取4株菌的总DNA,利用真菌的18S rDNA通用引物进行扩增、克隆和测序,其18S rDNA序列的长度分别为1 810 bp、1 769 bp、1 768 bp和1 770 bp.将这些序列在GenBank中进行序列比对,获得的同源性较高的序列用于构建系统进化树.根据分子鉴定和形态观察的结果,SP-1菌株是匍枝根霉(Rhizopus stolonifer)SP-1,SP-2是尖镰孢(Fusarium oxysporum)SP-2,SP-3是康宁肉座菌(Hypocreakoningii)SP-3,SP-4是肉座菌属(Hypocrea),命名为Hypocrea sp.SP-4.     

青蒿毛状根分支生长的动力学模型

近年来，用m质粒转化药用植物诱导毛状根生产有用代谢产物的研究日益增多，转化产生的毛状根不仅生长迅速，分支多，而且遗传性和生理、生化特性稳定，具有较强的次生代谢合成能力，因此可望应用于大规模生产有用的次级代谢产物［‘－’］．青蒿毛状根可产生大量的次生代谢产物     

人居生活废弃物生物黑炭对水溶液中Cd2+的吸附研究

以人居生活废弃物生物黑炭为材料,探讨生物黑炭对Cd2+的吸附动力学及热力学特性,通过平衡吸附法研究吸附时间、Cd2+初始质量浓度、吸附剂投加量、溶液pH值以及黑炭粒径对Cd2+吸附率的影响.结果表明,吸附时间为2h时基本达到吸附平衡,准二级动力学方程能很好地描述生物黑炭对Cd2+的吸附过程.Langmuir模型能较好地描述生物黑炭对Cd2+的等温吸附过程,根据该模型模拟得到25℃条件下Cd2+最大吸附量为6.22mg·g-1.Cd2+去除率随生物黑炭投加量的增加而增大;生物黑炭对Cd2+吸附量随其粒径减小而增大;溶液初始pH值为4.0～7.5时,pH值变化对Cd2+吸附量的影响不显著.采用人居生活废弃物生物黑炭去除水溶液中Cd2+时,控制溶液Cd2+初始质量浓度30mg·L-1,粒径小于0.25 mm,投加水平8g·L-1,反应温度25℃,反应时间1～2h,Cd2+去除率可达80％.人居生活废弃物生物黑炭可以作为去除污染水体中Cd2+的吸附剂.     

Versuchsanlage zur energetischen Beurteilung von Substraten und Kofermentaten für Biogasanlagen

Goal, Scope and Background

Worldwide energy requirements are constantly increasing. Rising prices and the necessity to secure the future energy supply have led the decision-makers in politics and economy to focus on the more intensive use of their own resources. Before the background of possible climatic effects caused by the use of fossil energies, the use of renewable resources as primary energies, with its narrow C-circulation, have gained in importance, particularly in terms of economic aspects. The production of biogas is of specific interest here. It is a sensible ecological investment and a solid source of income for our agriculture.

Material and Methods

The operator uses a complex biological system in a plant with high investment costs. An economic operation is only possible if the process parameters are optimized and the properties of the substrates and the co-ferments are known. For the important determination of the blogas potential, we present an efficient and robust system, which is easy to handle and low cost, that has been developed by the LHL and LLH at the Eichhof. This procedure enables one to make statements on the implementation dynamics and is also suited to judge the fermentation process depending on the size of particles, as the co-ferments are used in a practice-oriented consistency.

Results

With the described fermentation apparatus you can not only assess the potential development of biogas and methane, but also the process of fermentation. The sum-graphs determined allow one to make conclusions on the implementation dynamics and, thus, on the optimization of the process. The advanced equipment makes it possible to determine the process of fermentation and the gas yield under different retention times and digester loads. The determination of the potential of the biogas and also the evaluation of the continuous fermentation are related to a specific correction factor won from the standard.

Discussion

A prerequisite for economic process management is the knowledge of the attainable gas yield and the fermentation process of substrates and co-ferments. A precise calibration is the quality basis for the results achieved with this method, as is the case with other fermentation tests as well. For the tests, a highly homogeneous substrate, which guarantees a continuous biological activity in the digesters, ought to be used. The possibility of determining optimum retention times and digester loads with this equipment makes costly tests with a full scale reactor unnecessary.

Conclusions

All tests run demonstrated that the fermentation apparatus originally developed to determine the biogas yield is absolutely suited to also assess the impact of different digester loads and retention times.

Recommendations

The problem of the suitability and the potential of different materials, the optimum reactor performance and the combination of different processes of energy generation from renewable but also conventional resources will increaseingly become the focus of laboratory tests. The following subjects have to be taken into account:

- Testing different materials on their suitability

- Evaluation security of common and new co-ferments

- Guidelines for mixtures to optimize reactor performance

- Mixtures of different substrates and co-ferments available to a particular operator (also with the help of simulation models)

- Processing changing quantity proportions of plants won from a rotation of crops altered for energy generation

- Other parameters like pre-fermentation, particle size and fer mentation supplements.

Perspective

These tests with a high practical relevance are supposed to contribute to a reliable method of producing biogas, in order to optimize the yield of gas production, but also to find a calibration of less costly procedures like those involving Near Infrared Spectroscopy (NIRS).     

人居生活废弃物生物黑炭对水溶液中Cd^2＋的吸附研究

以人居生活废弃物生物黑炭为材料,探讨生物黑炭对Cd^2＋的吸附动力学及热力学特性,通过平衡吸附法研究吸附时间、Cd^2＋初始质量浓度、吸附剂投加量、溶液pH值以及黑炭粒径对Cd^2＋吸附率的影响。结果表明,吸附时间为2h时基本达到吸附平衡,准二级动力学方程能很好地描述生物黑炭对Cd^2＋的吸附过程。Langmuir模型能较好地描述生物黑炭对Cd^2＋的等温吸附过程,根据该模型模拟得到25℃条件下Cd^2＋最大吸附量为6．22 mg·g^-1 Cd^2＋去除率随生物黑炭投加量的增加而增大;生物黑炭对Cd^2＋吸附量随其粒径减小而增大;溶液初始pH值为4．0-7．5时,pH值变化对Cd2’吸附量的影响不显著。采用人居生活废弃物生物黑炭去除水溶液中Cd^2＋时,控制溶液Cd^2＋初始质量浓度30mg·L^-1,粒径小于0．25mm,投加水平8g·L^-1,反应温度25℃,反应时间1-2h,Cd^2＋去除率可达80％。人居生活废弃物生物黑炭可以作为去除污染水体中Cd^2＋的吸附剂。     

Economical pollution control in warm climates by contact stabilization wastewater treatment

Water pollution abatement with economical solutions, for wastewater treatment plants design and operation, is a crucial problem, especially for economically developing countries. The purpose of this study is the evaluation of the contact stabilization process to achieve economical secondary treatment as well as partial nitrification under favorable temperature conditions. The examined variables are easily definable parameters of practical importance for any wastewater treatment plant. Based on full scale plants data, correlations between design or operation variables and plant performance or effluent quality are reported.