A kinetic and equilibrium studyof competitive adsorption b
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高一物理力学原理英语阅读理解25题1<背景文章>Newton's three laws of motion are fundamental principles in physics that have had a profound impact on our understanding of the physical world.The first law, also known as the law of inertia, states that an object at rest will stay at rest, and an object in motion will stay in motion with the same speed and in the same direction unless acted upon by an unbalanced force. For example, a book lying on a table will remain there until someone pushes or pulls it. This law was revolutionary as it challenged the then - existing ideas about motion. Newton discovered this law through his careful observations and experiments.The second law of motion is expressed as F = ma, where F is the net force acting on an object, m is the mass of the object, and a is the acceleration. This law explains how the force applied to an object is related to its mass and acceleration. In real - life applications, when you push a shopping cart, the harder you push (greater force), the faster it will accelerate, given that the mass of the cart remains the same.The third law states that for every action, there is an equal and opposite reaction. A classic example is when a rocket launches. The rocket expels gas downward (action), and in return, the gas exerts an equal andopposite force on the rocket, propelling it upward (reaction). Newton's discovery of these laws was a milestone in the history of science and has been used in various fields such as engineering, astronomy, and transportation.1. <问题1>A. According to Newton's first law, if an object is moving in a straight line at a constant speed, what will happen if no unbalanced force acts on it?A. It will gradually slow down.B. It will keep moving at the same speed and in the same direction.C. It will suddenly change direction.D. It will stop immediately.答案:B。
高三英语学术论文的阅读单选题40题1.The author's argument is cogent, but some critics find it controversial. The word "cogent" means _____.A.weakB.persuasiveC.confusingD.boring答案:B。
“cogent”的意思是“有说服力的”。
选项A“weak”表示“弱的”;选项C“confusing”表示“令人困惑的”;选项D“boring”表示“无聊的”。
在学术语境中,“cogent”常用来形容论证、观点等具有说服力。
2.The study presents a comprehensive analysis of the problem. The word "comprehensive" means _____.A.narrowB.partialC.thoroughD.superficial答案:C。
“comprehensive”的意思是“全面的、彻底的”。
选项A“narrow”表示“狭窄的”;选项B“partial”表示“部分的”;选项D“superficial”表示“表面的”。
在学术语境中,“comprehensive”常用来形容对某一问题的分析很全面。
3.The researcher's hypothesis is tenable. The word "tenable" means _____.A.impossibleB.doubtfulC.reasonableD.absurd答案:C。
“tenable”的意思是“站得住脚的、合理的”。
选项A“impossible”表示“不可能的”;选项B“doubtful”表示“可疑的”;选项D“absurd”表示“荒谬的”。
在学术语境中,“tenable”常用来形容假设、观点等合理。
equilibrium英文解释Equilibrium is a fundamental concept in physics, chemistry, economics, and other fields, referring to a state of balance or stability where opposing forces or influences are balanced, resulting in no net change or motion. In other words, it is a state where the system is at rest or in a constant state of motion, with no tendency to change.In physics, equilibrium is often described as the state where a system is in a state of dynamic balance, with all forces acting on it canceled out by opposing forces. This can be seen in mechanical systems, where objects are atrest or moving with constant velocity, or in thermodynamic systems, where the system is in a state of thermal balance, with no net heat flow.In chemistry, equilibrium is typically referred to as a state where a chemical reaction proceeds in both directions at the same rate, resulting in no net change in theconcentrations of the reactants and products. This state is known as chemical equilibrium, and it is described by the law of mass action, which states that the rate of a chemical reaction is proportional to the product of the concentrations of the reactants.In economics, equilibrium is often described as a state where the supply and demand for a particular good or service are balanced, resulting in a stable price. This state is known as market equilibrium, and it is described by the law of supply and demand, which states that the price of a good or service will adjust to balance the quantity supplied with the quantity demanded.In all these fields, equilibrium is an important concept because it represents a state of stability and predictability. When a system is in equilibrium, it is generally easier to understand and predict its behavior than when it is in a state of flux or change. Additionally, equilibrium states often correspond to optimal or most efficient conditions, making them important targets for engineering, economic policy, and other applications.However, it is important to note that equilibrium is not always a static or unchanging state. In many systems, equilibrium is a dynamic state, with small fluctuations or perturbations constantly occurring. These fluctuations can be caused by external influences, internal fluctuations in the system, or random events. In these cases, the system will continually adjust to maintain the balance orstability of the equilibrium state.Additionally, it is worth noting that achieving or maintaining an equilibrium state can often be challenging. In many cases, it requires careful control or management of the system, as well as an understanding of the interactions and dependencies within the system. For example, in economic systems, maintaining market equilibrium often requires government intervention or regulation to prevent market failures or excesses. In physical systems, achieving equilibrium may require precise control of external conditions or the manipulation of system parameters.In conclusion, equilibrium is a fundamental conceptthat describes a state of balance or stability in various fields. It represents a state where opposing forces or influences are balanced, resulting in no net change or motion. While equilibrium may be seen as a static or unchanging state in some cases, it is often a dynamic state that requires careful management and control to maintain. Understanding and manipulating equilibrium states iscrucial in many fields, including physics, chemistry, economics, and engineering, and has important applications in real-world scenarios.。
2022年考研考博-考博英语-西北大学考试全真模拟易错、难点剖析AB卷(带答案)一.综合题(共15题)1.单选题Tom wasn't happy about the delay, and ().问题1选项A.I was neitherB.I wasn't neitherC.neither was ID.either was I【答案】C【解析】句意:汤姆对耽搁很不高兴,我也是。
根据句意可知,前后表示同样的情况,肯定用So+助动词+主语,否定用Neither+ 助动词+主语,所以选项C正确。
2.单选题George Gallup, Jr ., the man who makes and()his reputation ()knowing what Americans think, has brought all his polling strategies together to identify and analyze what he calls future forces.问题1选项A.challenges...onB.stakes...onC.hazards...toD.bets...to【答案】B【解析】challenge…on在……方面挑战;stake…on把赌注押在……上面;hazard...to 对……有危险;bet不与to搭配。
句意:George Gallup,Jr .这个把自己的名誉押在知晓美国人想法上的人,将所有的投票策略集中到一起,以确定和分析他所说的未来力量。
选项B符合句意。
3.单选题In a world that aims to eliminate hunger and disparities in wealth, globe equilibrium is vital.问题1选项A.equityB.balanceC.inequalityD.discretion【答案】C【解析】根据句意可知,这里是消除贫富差距。
彭桓武留欧期间的科学贡献刘金岩【摘要】彭桓武,中国著名理论物理学家,"两弹一星"功勋奖章获得者.1938年至1947年,彭桓武先后在英国爱丁堡大学、爱尔兰都柏林研究院理论物理所学习工作.彭桓武回国后曾参与组织中华人民共和国核武器理论设计工作并注重培养理论物理人才.基于档案、书信以及手稿等资料,介绍彭桓武留欧期间与玻恩、薛定谔、海特勒等物理学家的交往.此外,尝试评述彭桓武早期在固体物理、介子理论和量子场论等方面的研究工作.从而,有助于理解彭桓武回国后在中国核武器理论设计和理论物理发展方面的贡献.%Huan-wu Peng ( 1915 ~2007 ) was a famous Chinese theoretical physicist. From 1938 to 1947 , he successively studied and worked in the University of Edinburgh and Dublin Institu-te for Advanced Studies in Ireland. After he came back China in 1947, Peng committed himself to the theoretical designs of nuclear weapons and cultivating young talents. Based on primary and other historical materials, this article makes a special inquiry into Peng's association with M. Born, E.Schr?dinger and W. H. Heitler. Moreover, it also attempts to make a preliminary comments on Peng's work on solid state physics, Meson theory and quantum field theory. All of the above men-tioned could be helpful to understand Peng's contributions to the theoretical design of nuclear weapon and theoretical physics' development in China.【期刊名称】《自然科学史研究》【年(卷),期】2018(037)001【总页数】17页(P87-103)【关键词】彭桓武;玻恩;薛定谔;介子理论;量子场论【作者】刘金岩【作者单位】中国科学院自然科学史研究所,北京 100190【正文语种】中文【中图分类】N092;K826.1彭桓武(1915~2007)是新中国核武器理论设计和理论物理研究的奠基者之一。
sat物理知识点总结SAT Physics is a subject test designed to assess students' knowledge and understanding of various physics concepts and principles. It covers a wide range of topics, including mechanics, electricity and magnetism, waves, optics, heat and thermodynamics, and modern physics. This knowledge summary will provide an overview of the key concepts and principles tested on the SAT Physics exam.MechanicsMechanics is the branch of physics that deals with the motion of objects and the forces that cause or influence that motion. It is a fundamental topic in physics and is tested extensively on the SAT Physics exam. Some of the key concepts and principles in mechanics include:1. Kinematics: Kinematics is the study of motion without considering the forces that cause it. It includes concepts such as displacement, velocity, acceleration, and equations of motion.2. Newton's laws of motion: Newton's laws of motion are fundamental principles that describe the behavior of objects in response to forces. They include the first law (inertia), the second law (F = ma), and the third law (action and reaction).3. Work, energy, and power: These concepts are related to the transfer and transformation of energy in mechanical systems. They include the work-energy theorem, kinetic and potential energy, and power.4. Linear momentum and collisions: Linear momentum is the product of an object's mass and velocity, and it is conserved in isolated systems. Collisions between objects involve the transfer of momentum and kinetic energy.5. Circular motion and gravitation: Circular motion is the motion of an object along a curved path, and it involves centripetal acceleration and centripetal force. Gravitation is the force of attraction between objects with mass, and it is described by the law of universal gravitation. Electricity and MagnetismElectricity and magnetism are closely related phenomena that are fundamental to many aspects of modern technology. The SAT Physics exam covers a range of topics related to electricity and magnetism, including:1. Electric fields and forces: Electric fields are regions of space around charged objects where electric forces are exerted on other charged objects. The strength and direction of the electric field can be calculated using Coulomb's law.2. Electric potential and capacitance: Electric potential is a measure of the potential energy per unit charge in an electric field. Capacitance is a measure of an object's ability to store electric charge.3. Electric circuits: Electric circuits are systems of conductors and components through which electric current can flow. They can be analyzed using principles such as Ohm's law and Kirchhoff's laws.4. Magnetic fields and forces: Magnetic fields are regions of space around magnets or current-carrying conductors where magnetic forces are exerted on other magnetic or current-carrying objects. The strength and direction of the magnetic field can be calculated using the right-hand rule.5. Electromagnetic induction: Electromagnetic induction is the process by which a changing magnetic field induces an electric current in a conductor. It is the principle behind generators and transformers.Waves and OpticsWaves and optics are important topics in physics that describe the behavior of light and other types of waves. The SAT Physics exam covers a range of topics related to waves and optics, including:1. Wave properties: Waves are disturbances that propagate through a medium or space, and they can be described in terms of properties such as wavelength, frequency, amplitude, and speed.2. Interference and diffraction: Interference is the interaction of two or more waves, leading to the reinforcement or cancellation of their amplitudes. Diffraction is the bending of waves around obstacles and through apertures.3. Ray optics: Ray optics describes the behavior of light as it interacts with lenses, mirrors, and other optical components. It can be used to understand phenomena such as reflection, refraction, and image formation.4. Wave optics: Wave optics describes the behavior of light as a wave, including phenomena such as interference, diffraction, and polarization.Heat and ThermodynamicsHeat and thermodynamics are important topics in physics that describe the behavior of thermal energy and the principles underlying processes such as heat transfer and thermodynamic cycles. The SAT Physics exam covers a range of topics related to heat and thermodynamics, including:1. Temperature and thermal equilibrium: Temperature is a measure of the average kinetic energy of the particles in a substance, and thermal equilibrium is the condition in which two objects have the same temperature.2. Heat transfer: Heat can be transferred between objects through conduction, convection, and radiation. These processes depend on factors such as temperature difference, material properties, and surface area.3. Laws of thermodynamics: The laws of thermodynamics describe the behavior of energy in thermodynamic systems, including principles such as conservation of energy, entropy, and the second law of thermodynamics.4. Ideal gases and the ideal gas law: Ideal gases are theoretical gases that obey the ideal gas law, which relates the pressure, volume, and temperature of a gas.Modern PhysicsModern physics is a branch of physics that deals with phenomena that cannot be explained by classical physics, including topics such as quantum mechanics and relativity. The SAT Physics exam covers a range of topics related to modern physics, including:1. Quantum mechanics: Quantum mechanics is the branch of physics that describes the behavior of matter and energy at the atomic and subatomic scales. It includes concepts such as quantization, wave-particle duality, and the uncertainty principle.2. Atomic and nuclear physics: Atomic and nuclear physics describe the behavior of atoms and atomic nuclei, including topics such as atomic structure, radioactivity, and nuclear reactions.3. Special relativity: Special relativity is a theory describing the behavior of objects moving at high speeds, including principles such as time dilation, length contraction, and the equivalence of mass and energy.4. Particle physics: Particle physics is the study of the fundamental particles and forces that make up the universe, including topics such as elementary particles, the standard model, and the properties of forces and interactions.In addition to these key topics, the SAT Physics exam also covers a range of practical skills related to experimental design, data analysis, and mathematical problem-solving. It is important for students to develop a strong understanding of the fundamental concepts and principles of physics, as well as the ability to apply this knowledge in various contexts. By mastering the key topics and skills tested on the SAT Physics exam, students can improve their performance and achieve success on the test.。
A Comprehensive Modeling Study of Hydrogen OxidationMARCUS´O CONAIRE,1HENRY J.CURRAN,2JOHN M.SIMMIE,1WILLIAM J.PITZ,3 CHARLES K.WESTBROOK31National University of Ireland,Galway,Ireland2Galway-Mayo Institute of Technology,Galway,Ireland3Lawrence Livermore National Laboratory,Livermore,CA94551Received19November2003;accepted28May2004DOI10.1002/kin.20036Published online in Wiley InterScience().ABSTRACT:A detailed kinetic mechanism has been developed to simulate the combustion ofH2/O2mixtures,over a wide range of temperatures,pressures,and equivalence ratios.Over theseries of experiments numerically investigated,the temperature ranged from298to2700K,thepressure from0.05to87atm,and the equivalence ratios from0.2to6.Ignition delay times,flame speeds,and species composition data provide for a stringent testof the chemical kinetic mechanism,all of which are simulated in the current study with varyingsuccess.A sensitivity analysis was carried out to determine which reactions were dominatingthe H2/O2system at particular conditions of pressure,temperature,and fuel/oxygen/diluentratios.Overall,good agreement was observed between the model and the wide range of exper-iments simulated.C 2004Wiley Periodicals,Inc.Int J Chem Kinet36:603–622,2004INTRODUCTIONThe prospect of a hydrogen-based economy has prompted increased interest in the use of hydrogen as a fuel given its high chemical energy per unit mass and cleanliness.It appears that most of the technologi-cal problems in using hydrogen in spark-ignited inter-nal combustion engines,including NO x emissions[1], have now been solved;vehicular on-board storage is probably the one remaining difficulty[2,3].There is also continued interest in developing a bet-ter understanding of the oxidation of hydrocarbon fu-Correspondence to:Henry J.Curran;e-mail:henry.curran@ nuigalway.ie.Contract grant sponsor:Higher Education Authority of Ireland.Contract grant number:PRTLI-II.c 2004Wiley Periodicals,Inc.els[4]over a wide range of operating conditions in order to increase efficiency and to reduce the emis-sion of pollutant species.All,or almost all petrochem-ical,fuels are hydrocarbons which burn to form carbon dioxide and water.Thus,the development of a detailed kinetic mechanism for hydrocarbon oxidation neces-sarily begins with a hydrogen/oxygen submechanism, followed by the addition of CO chemistry.In recent years,many kinetic studies of hydrogen oxidation have concentrated on a single set of experi-mental results obtained either in shock tubes,or inflow reactors or inflames;these have been simulated using a detailed kinetic mechanism.This procedure has been criticized recently by Smith[5]who asserts that uncer-tainty limits on individual reaction rate constants pro-duce a parameter space of possible mechanisms still too imprecise for accurate prediction of combustion properties such asflame speed or ignition delay,thus604´O CONAIRE ET AL.requiring additional system data.Smith adds that low pressure and counterflowflames,mixtures in shock tubes,andflow or well-stirred reactors are examples of such experimental environments.It is the aim of this study to apply a hydrogen kinetic mechanism to as broad a range of combustion environments as possible.There have been a very large number of measure-ments made on the reaction between hydrogen and oxy-gen.These includeflame speed measurements,burner-stabilizedflames in which species profiles are recorded, shock tube ignition delay times,and concentration pro-files inflow reactor studies.This study aims to simu-late these experiments using a detailed chemical kinetic mechanism which takes its origin from Mueller et al.[6]in their study of hydrogen oxidation in aflow re-actor.Mueller and coworkers validated their mecha-nism using only theirflow reactor data over the tem-perature range850–1040K,at equivalence ratios of 0.3≤φ≤1.0,pressures of0.3to15.7atm and resi-dence times of0.004to1.5s.We have exercised their mechanism against shock-tube data,burner-stabilized flame experiments,andflame speed data and have made modifications to some of the kinetic parameters in or-der to achieve better overall agreement between mecha-nism simulations and this broader range of experimen-tal results.Previously,Marinov et al.[7]had also devel-oped a detailed H2/O2kinetic mechanism to simulate shock tube,flame speed,and burner-stabilizedflame experiments with good agreement between model and experiment but a large body of data sets have become available since then.Therefore,this study presents a new detailed chemical kinetic mechanism for hydro-gen oxidation but with increased attention paid to ex-periments conducted at high pressures since internal combustion engines operate at elevated pressures.Davis et al.[8]have recently presented a re-examination of a H2/CO combustion mechanism in which they simulated some of the experimental data included in this study.Their work was motivated by new kinetic parameters for the important reaction ˙H+O2+M=H˙O2+M and by new thermodynamic data for˙OH,and had the objective of optimizing their H2/CO model against experiment.IGNITION DELAYS IN SHOCK WAVESSchott and Kinsey[9]measured ignition delay times of two H2/O2/Ar fuel mixtures behind incident shock waves over a wide range of reactant densities in the temperature range1085–2700K and at1atm. Skinner and Ringrose[10]measured the ignition de-lays of an H2/O2/Ar mixture in the temperature range 965–1076K and at a reflected shock pressure of 5atm.Asaba et al.[11]performed experiments inthe temperature range1500–2700K,at reflected shockpressures of178–288Torr,at an equivalence ratio,φ,of0.5and with98%argon dilution.Fujimoto and Sujiki[12]measured ignition delay times of stoichiometricH2/O2/Ar fuel mixtures in the reflected shock pressurerange1.3–5atm and in the temperature range700–1300K.Hasegawa and Asaba[13]measured ignitiondelays in the temperature range920–1650K,at a re-flected shock pressure of5.5atm,withφ=0.25at94%argon dilution.Bhaskaran et al.[14]reported ignitiondelay times for a29.59%H2,14.79%O2,55.62%N2mixture in the temperature range1030–1330K and ata constant reflected shock pressure of2.5atm.More recently,Slack[15]studied stoichiometrichydrogen–air mixtures in a shock tube and measuredinduction times near the second explosion limit.Theexperiments were performed at a reflected shock pres-sure of2atm in the temperature range980–1176K.Cheng and Oppenheim[16]reported ignition delaytimes for a6.67%H2,3.33%O2,and90%Ar mixture inthe temperature range1012–1427K and at a reflectedshock pressure,P5 1.9atm.Koike[17]measured ignition delay times for two hydrogen/oxygen/argonfuel mixtures of incident shock pressure20Torr in thetemperature range1000–1040K.In a methane shock-tube study,Hidaka et al.[18]carried out some measurements of a H2/O2/Ar mix-ture at1250–1650K and at reflected shock pressuresof1.6–2.8bar.Petersen et al.[19]measured high-pressure(33–87atm)H2/O2/Ar reflected shock igni-tion delays at1189–1876K and at an equivalence ratioof1.0in every case for six mixtures.Petersen et al.[20]measured reflected ignition delay times in threehighly dilute H2/O2/Ar mixtures at temperatures of1010–1750K,equivalence ratio range1.0≤φ≤1.47and around atmospheric pressure.Finally,Wang et al.[21]carried out reflected shock measurements in vari-ous H2/air/steam mixtures at954–1332K and pressuresof3.36–16.63atm.Hydrogen concentration was15%of air throughout.FLAME MEASUREMENTSAtmospheric Flame Speed Measurements Very many hydrogen/airflame speed studies have been performed at atmospheric pressure,over various ranges of equivalence ratio.Koroll et al.[22]reported data in the equivalence ratio range0.15≤φ≤5.5, Iijima and Takeno[23]in the range0.5≤φ≤3.9,and Takahashi et al.[24]in the range1≤φ≤4.How-ever,these data did not account for the effects of flame stretch.A COMPREHENSIVE MODELING STUDY OF HYDROGEN OXIDATION 605The earliest stretch-corrected atmospheric hydro-gen/air flame speed experiments were performed by Wu and Law [25]in the range 0.6≤φ≤6.Since then,stretch-corrected flame speeds,all of which were per-formed at 1atm,have been reported at various equiva-lence ratio ranges:Egolfopoulos and Law [26](0.25≤φ≤1.5),Law [27](0.4≤φ≤1.5),Vagelopoulos et al.[28](0.3≤φ≤0.55),Dowdy et al.[29](0.3≤φ≤5),and Aung [30](0.3≤φ≤5)and Tse et al.[31](0.4≤φ≤4),Fig.1.The measurements of Takahashi et al.[24]are con-siderably faster than the rest of the data and 10%faster than the intermediate values of Tse et al.and Dowdy et al.at an equivalence ratio of 1.75.The slowest flame speeds are those of Aung et al.[30]that have a maxi-mum flame speed of 2.6m s −1at φ=1.65.The authors point to possible greater stretch effects than accounted for to explain the relative slowness of their data.The Koroll et al.values [22],on the other hand,are much faster than any other between 1.0≤φ≤2.5.The re-cent flame speed measurements of Dowdy et al.[29]and Tse et al.[31]probably are the most representa-tive of the entire data set;they have a maximum flame speed of 2.85m s −1at φ=1.75.Lamoureux et al.[32]very recently measured the speeds of freely propagating flames in a spherical bomb for five H 2/air mixtures using a diluent consisting of CO 2+He to mimic the effect of water vapor on flame speed.The mixtures were composed of as follows:x (40%He +60%CO 2)+(1−x )(H 2+air),wherexFigure 1Atmospheric H 2/O 2/air flame speeds versus equivalence ratio,T i =298K. Koroll et al.[22], +Iijima and Takeno [23], Takahashi et al.[24];stretch corrected: ×Wu and Law [25]×Egolfopoulos and Law [26],•Law [27],⊕Vagelopoulos et al.[28], Dowdy et al.[29],+Aung et al.[30],and Tse et al.[31].ranged from 0.0to 0.4,and with synthetic air of com-position O 2:N 2=20:80.High-Pressure Flame SpeedsIn addition to their atmospheric flame speed measure-ments,Tse et al.[31]also measured mass burning velocities for H 2/O 2/He mixtures in the equivalence ratio range 0.5≤φ≤3.5and between 1and 20atm at an initial temperature of 298K.It was reported that flames became increasingly unstable at elevated pres-sures.For this reason,true stretch-free flame speeds become more diffcult to measure.Experimentally,in the case of the 10–20atm data,the oxygen to fuel ratio was reduced to suppress diffusional-thermal instabil-ity and delay hydrodynamic ing helium as the diluent also helped minimize instability up to 20atm by reducing the Lewis number of the flame and retarding the formation of flame cells.Stretch-free flame speeds have only been available up to a few at-mospheres.The oxygen to helium ratio at 1to 5atm was 1:7(12%dilution)and at elevated pressures,this ratio was 1:11.5(8%dilution).Burner-Stabilized FlameIn their investigation of a rich 18.83%hydrogen,4.6%oxygen,and 76.57%nitrogen flame at atmospheric pressure,Dixon-Lewis and Sutton [33]measured the temperature pro file and the concentration pro files of the stable species in the flame,above and below the burner.Flame structure measurements had been car-ried out by Kohse-H ¨Oinghaus et al.[34]who measured˙Hand ˙OH radical concentrations versus distance in a H 2/O 2/Ar flame,at a pressure of 95mbar,in the equiva-lence ratio range 0.6≤φ≤1.4and in the temperature range 1100–1350K.Vandooren and Bian [35]investi-gated the structure of a rich H 2/O 2/Ar flame over a flat burner at a pressure of 35.5Torr and at an equivalenceratio of 1.91.They reported H 2,O 2,H 2O,˙H,˙O,and ˙OH species mole fractions versus distance above the burner.Flow ReactorsMueller et al.[6]measured H 2,O 2,and H 2O pro files over the temperature range 850to 1040K,at equiva-lence ratios of 0.3≤φ≤1.0in the pressure range from 0.3to 15.7atm and over a range of residence times of 0.004to 1.5s.Previously,Yetter et al.[36]reported atmospheric H 2,O 2,and H 2O pro files at 910K,and at an equivalence ratio of 0.3.606´O CONAIRE ET AL.Experiments SimulatedA representative selection of recent experimental work has been chosen to validate the H2–O2combustion mechanism.The chosen experiments were1.the ignition delay times measured by Schott andKinsey[9],Skinner and Ringrose[10],Fujimotoand Suzuki[12],Bhaskaran and Gupta[14],Slack[15],Cheng and Oppenheim[16],Petersenet al.[19],Hidaka et al.[18],Petersen et al.[20],and Wang et al.[21].Simulations of the dataof Asaba et al.[11],Hasegawa and Asaba[13],and Koike[17]were not attempted in this studybecause of a lack of sufficient information.2.theflame speed measurements of Dowdy et al.[29].Theseflame speeds not only span a widerange of equivalence ratio but are in agreementwith the more recent values of Tse et al.[31].Dowdy and coworkers also measured the tem-perature profiles,thus making their data moreamenable to simulation.3.the high-pressureflame speed measurements ofTse et al.[31].This data is the only set wherehydrogenflame speeds have been measured atpressures greater than5atm.4.the very lean H2/air and H2/air/CO2/Heflamespeed measurements of Lamoureux et al.[32].5.the burner-stabilizedflame profiles of Vandoorenand Brian[35]in which reactant and intermedi-ate species concentrations were measured as afunction of height above the burner surface.Alsoincluded are the species profiles of Dixon-Lewisand Sutton[33].6.the comprehensiveflow reactor data of Muelleret al.[6]along with a single data set from Yetteret al.[36].CHEMICAL KINETIC MODELINGThe chemical kinetic mechanism was developed and simulations performed using the HCT program[37]. Initially,ignition delay times measured by Slack[15], Fig.8,and Hidaka et al.[18],Fig.7,and theflow re-actor experiments of Mueller et al.[6],Fig.25,were simulated with very good agreement observed between experiment and model.The mechanism was then con-verted into Chemkin3.6[38]format and the simula-tions repeated in order to compare results from both codes,which were in very good agreement as expected. Thereafter,all other experiments including theflame speeds and the burner-stabilizedflame profiles were simulated using only the Chemkin applications.Thermodynamic and Transport Properties The H2/O2reaction mechanism consists of19reversible elementary reactions,Table I,togetherwith the thermochemical data,Table II.Reverse rateconstants were computed by microscopic reversibility.The thermochemical data for each species consideredin the mechanism are from the Chemkin thermody-namic database[51]with the exception of two:1. H f(H˙O2,298K)of3.0kcal mol−1,from Hillsand Howard[52]which is in good agreementwith the recent reappraisal by Ramond et al.[53]of3.2±0.5kcal mol−1.2. H f(˙OH,298K)of8.91kcal mol−1which isbased on recommendations by Ruscic et al.[54]and Herbon et al.[55].The Chemkin database of transport parameters wasused without modification.As in the study of Tseet al.[31],the kinetic parameters of helium were as-sumed equal to those of argon in order to simulateflame propagation where helium is the diluent.As Tseet al.noted,using the third-body efficiency of argon formonatomic helium is a useful starting estimate;ther-molecular reactions such as˙H+O2+M=H˙O2+M become significant at elevated pressures and so the un-certainties in these values can create considerable dif-ferences in theflame speeds.Mechanism FormulationThe kinetic mechanism referred to in this study as thisstudy or the revised mechanism has its origins in the CO/H2/O2reaction mechanism of Yetter et al.[56], which was updated later by Kim et al.[57]and is,for the most part,taken from the more recent work of Mueller et al.[6].We found it necessary to modify some of the kineticparameters of Mueller et al.in order to achieve an over-all improvement with all the experimental data sim-ulated here.This altered version of the mechanism,Table I,the revised mechanism,reproduces the se-lected experimental datasets more accurately than thatpublished by Mueller and coworkers.The entire data set has also been simulated using rel-evant portions from Leeds1.5[58],Konnov[59,60]andGRI-Mech3.0[61]which are all primarily methane ox-idation mechanisms.The reason for using both Konnovmechanisms is that the shock tube data presented inFigs.4–6was used to validate version0.3,while themore recent version0.5was used to simulate the re-maining data.A select set of experiments is repro-duced here using GRI-Mech,Leeds,and Konnov asA COMPREHENSIVE MODELING STUDY OF HYDROGEN OXIDATION607Table I Revised H2/O2Reaction Mechanism(units:cm3,mol,s,kcal,K)Reaction A n E a Ref.H2/O2chain reactions1˙H+O2=˙O+˙OH1.91×10140.0016.44[39]2˙O+H2=˙H+˙OH5.08×104 2.67 6.292[40]3˙OH+H2=˙H+H2O2.16×108 1.51 3.43[41]4˙O+H2O=˙OH+˙OH2.97×106 2.0213.4[42]H2/O2dissociation/recombination reactions5a H2+M=˙H+˙H+M4.57×1019−1.40105.1[43]6b˙O+˙O+M=O2+M6.17×1015−0.500.00[43]7c˙O+˙H+M=O˙H+M4.72×1018−1.000.00[43]8d,e˙H+˙OH+M=H2O+M4.50×1022−2.000.00[43]×2.0Formation and consumption of H˙O29f,g˙H+O2+M=H˙O2+M3.48×1016−0.41−1.12[44]˙H+O2=H˙O21.48×10120.600.00[45] 10H˙O2+˙H=H2+O21.66×10130.000.82[6]11H˙O2+˙H=˙OH+˙OH7.08×10130.000.30[6]12H˙O2+˙O=˙OH+O23.25×10130.000.00[46] 13H˙O2+˙OH=H2O+O22.89×10130.00−0.50[46]Formation and consumption of H2O214h H˙O2+H˙O2=H2O2+O24.2×10140.0011.98[47] H˙O2+H˙O2=H2O2+O21.3×10110.00−1.629[47] 15i,f H2O2+M=˙OH+O˙H+M1.27×10170.0045.5[48] H2O2=˙OH+O˙H2.95×10140.0048.4[49] 16H2O2+˙H=H2O+˙OH2.41×10130.00 3.97[43] 17H2O2+˙H=H2+H˙O26.03×10130.007.95[43]×1.25 18H2O2+˙O=˙OH+H˙O29.55×1006 2.00 3.97[43] 19h H2O2+˙OH=H2O+H˙O21.0×10120.000.00[50] H2O2+˙OH=H2O+H˙O25.8×10140.009.56[50]a Efficiency factors are H2O=12.0;H2=2.5.b Efficiency factors are H2O=12;H2=2.5;Ar=0.83;He=0.83.c Efficiency factors are H2O=12;H2=2.5;Ar=0.75;He=0.75.d Original pre-exponential A factor is multiplied by2here.e Efficiency factors are H2O=12;H2=0.73;Ar=0.38;He=0.38.f Troe parameters:reaction9,a=0.5,T∗∗∗=1.0×−30,T∗=1.0×10+30,T∗∗=1.0×10+100;reaction15,a=0.5,T∗∗∗=1.0×−30, T∗=1.0×10+30.g Efficiency factors are H2=1.3;H2O=14;Ar=0.67;He=0.67.h Reactions14and19are expressed as the sum of the two rate expressions.i Efficiency factors are H2O=12;H2=2.5;Ar=0.45;He=0.45;Table II H f(298.15K)kcal mol−1,S(300K)and C p(T)in cal mol−1K−1Specific heat capacity,C pSpecies H298KS300K300K400K500K800K1000K1500K f˙H52.09827.422 4.968 4.968 4.968 4.968 4.968 4.968˙O59.5638.500 5.232 5.139 5.080 5.016 4.999 4.982˙OH8.9143.933 6.947 6.9927.0367.1997.3417.827 H20.0031.256 6.902 6.960 6.9977.0707.2097.733 O20.0049.0507.0107.2207.4378.0688.3508.721 H2O−57.7745.1548.0008.2318.4469.2239.87511.258 H˙O2 3.0054.8098.3498.8869.46510.77211.38012.484 H2O2−32.5355.72410.41611.44612.34614.29415.21316.851 N20.0045.900 6.8207.1107.5207.7708.2808.620 Ar0.0037.000 4.900 4.900 4.900 4.900 4.900 4.900 He0.0030.120 4.970 4.970 4.970 4.970 4.970 4.970608´O CONAIRE ET AL.an indication of their performance but they have not been comprehensively tested.A comparison shows that these mechanisms are quite different,Table III;not only does the total num-ber of reactions differ but so do the rate constant expressions.Reaction KineticsIt will be clarified later why we made the modifications we did but for now let us look at those that have been made.One of the rate expressions that we modified was˙H+˙OH+M=H2O+M.Figure2illustrates a selection of experimental and review kinetic recommendations for this reaction from Tsang and Hampson[43],Gay and Pratt[62],Baulch et al.[63],Troe[64],Zellner et al.[65],and Bulewicz and Sugdan[66].Between1250and2000K,there is at least a100-fold range in reported experimental and review data.The revised rate constant,see Table I,is twice the recommendation of Tsang and Hampson. Most of the data for the reaction:H2O2+˙H= H2+H˙O2lies between700and1100K.The data plot-ted alongside our revised rate constant for this reac-tion,Fig.3,include the experimental data of Baldwin et al.[67]in addition to the review data of Baulch et al.[63],Tsang and Hampson[43],Lee and Hochgreb[68], Baldwin and Walker[69],and Gorse and V olman[70].In a recent study,Michael et al.[71]measured the rate constant of the reaction˙H+O2+M=H˙O2+M. The measured rate constants for the collision partners nitrogen and argon are in good agreement with our es-timates and so it was decided to adhere to the estimated rate constants and efficiencies.Simulating Experimental Conditions Senkin[72]or Aurora[73]compute the time evolution of a homogeneous reacting gas mixture in a closed sys-tem.This includes predicting the chemical behavior be-hind incident and reflected shock waves in a shock tubeTable III A comparison of the mechanisms testedListed Duplicate Actual Mechanism Reactions Reactions Reactions This study21419 Mueller et al.29427 GRI-Mech3.030627 Leeds1.523222 Konnov0.324223 Konnov0.529427Figure2˙H+˙OH+M=H2O+M.◦this study,⊗Tsang and Hampson[43](used by Mueller and coworkers),•Gay and Pratt[62], Baulch et al.[63], Troe[64], Zellner et al.[65], Bulewicz and Sugden[66], Baulch et al.[63].and species evolution in a laminarflow reactor.A limit-ing case,frequently applied when simulating reactions in shock waves and also used in this study,assumes a constant volume(density)boundary which we used to simulate reflected shock ignition delay times.The Shock code[74]was used to simulate ignition delay times behind incident shocks.We used the application Premix[75]to model time-independent,adiabatic freely propagating(expanding spherical)flame speeds in addition to speciesandFigure3H2O2+˙H=H˙O2+H2.◦this study,⊗Tsang and Hampson[43](used by Mueller and coworkers), Baulch et al.[63], Baldwin and Jackson[67], Lee and Hochgreb[68], Baldwin and Walker[69]and Gorse and V olman[70].A COMPREHENSIVE MODELING STUDY OF HYDROGEN OXIDATION 609intermediate concentration pro files in a burner-stabilized flame.In order to allow for changes in the structure of the flame with time,a re-gridding strat-egy is included which involves the computation of the optimum grid as part of the time-dependent solution.We used the standard Chemkin transport package,with thermal diffusion included and increased the number of grid-points until the flame speed converged.Mixture-averaged transport properties were employed.Some modeling workgroups such as Resources Research In-stitute,University of Leeds prefer to use the multi-component transport wrence Livermore Na-tional Laboratories use the mixture-averaged transport properties as we do.Shock TubeKonnov [59,60]used the experiments of Schott and Kinsey along with those of Skinner and Ringrose,to validate version 0.3of his mechanism at temperatures of 965–2700K.In both studies,ignition delays be-low 1200K correspond to the time of maximum [˙OH];above 1200K they correspond to the time at which [˙OH]=10−6mol dm −3.In addition,both studies plot-ted the experimental data as the concentration of molec-ular oxygen multiplied by the ignition delay time versus temperature.Figures 4–6depict both sets of experimen-tal results with Konnov ’s mechanism predictions in ad-dition to those of our current mechanism and those of Mueller et al.Both our predictions and those of Mueller et al.are identical except for Skinner et al.and are in overall good agreement with the experimental data.The ignition delay times,,measured by Hidaka and coworkers correspond to the tangent totheFigure 4×[O 2]versus 1/T Skinner and Ringrose [10]8%H 2+2%O 2+balance Ar,at 1atm.——this study ,–-–-Mueller et al.,···Konnov 0.1–0.3,[59].Figure 5×[O 2]versus 1/T Schott and Kinsey [9]1%H 2+2%O 2+balance Ar,at 1atm.——this study and Mueller et al.,···Konnov 0.1–0.3,[59].maximum rate of increase in water concentration,(d[H 2O]/d t )max =,and were thus calculated in our simulations with very good agreement between our model (the Mueller mechanism gives identical results)and experiment,Fig.7.Slack [15]measured ignition delay times in stoi-chiometric hydrogen/air mixtures at a re flected shock pressure of two atmospheres.The revised mecha-nism performed very well over the entire tempera-ture range in simulating the experimental data,Fig.8.The Mueller et al.mechanism,on the other hand,pre-dicts slower ignition times,particularly at temperatures below 1025K.Figure 6×[O 2]versus 1/T Schott and Kinsey [9]4%H 2+2%O 2+balance Ar,at 1atm.——this study and Mueller et al.,···Konnov 0.1–0.3,[59].610´OCONAIRE ETAL.Figure 7Ignition delay measurements 1.0%H 2+1.0%O 2,balance Ar,at 3bar;Hidaka et al.[18] ;model predictions ——this study and Mueller et al.,---Leeds 1.5,···GRI-Mech 3.0,–--Konnov 0.5.The mechanism is in good agreement with theignition delays of Fujimoto and Suzuki [12],partic-ularly between 900and 1100K,Fig.9,although the mechanism is too slow at temperatures below 950K.The results of Petersen et al.[19]along with model predictions are shown in Fig.10.Three sets of data from the same study,in the pressure range 33–64atm and in the temperature range 1650–1930K,have also been simulated with good agreement,but are not shown here.The ignition delays were measured as the tangent of the pressure pro file versus time.Figure 11illustratesFigure 8Ignition delay times of stoichiometric H 2/air,at 2atm,from Slack [15]: ;model predictions ——this study ,–-–-Mueller et al.and Mueller et al.with ⑀(H 2)=1.3for˙H+O 2+M =H ˙O 2+M,---Leeds 1.5,···GRI-Mech 3.0and Konnov0.5.Figure 9Ignition delay times for stoichiometric H 2/air,from Fujimoto and Suzuki [12]: light emission,◦pressure;——this study ,---Mueller et al.the difference between the ignition delay time mea-sured from the onset of temperature rise and the ignition time measured by the tangent of the pressure pro file.The more recent atmospheric shock tube measurements of Petersen et al.[20],Figs.11and 12,are also re-produced with reasonable success by our mechanism although the experiments shown in Fig.12are con-siderably faster than those predicted by this study and Mueller et al.For this set of data,the ignition delay time could not be determined from the simulated pressure or temperature pro files at high temperatures,simply because the pressure and temperature did not give an unambiguous ignition delay time as the mixtureswereFigure 10Ignition delay times for stoichiometric H 2/O 2/Ar [19]; 0.5%H 2+0.25%O 2,64–87atm;•2.0%H 2+1.0%O 2,33atm; 0.1%H 2+0.05%O 2,64atm;model predictions:——this study and Mueller et al.,–-,---Leeds 0.5,···GRI-Mech 3.0,–--Konnov 0.5.A COMPREHENSIVE MODELING STUDY OF HYDROGEN OXIDATION611Figure 11Ignition delay times [20]: 1.03%H 2+0.5%O 2,balance Ar,at 1atm;model predictions ——based on pressure-rise,---based on temperature-rise.very dilute;so,the ignition delay time was re-de fined,in this case only,as the time corresponding to a maxi-mum in the product of the concentrations of ˙OHand ˙O,that is [˙O]×[˙OH].Two additional sets of data from thatstudy,in the temperature range 1100–1520K and at 1atm were simulated with good agreement but are not shown here.The measurements of Cheng et al.[16]and Bhaskaran et al.[14]are replicated well in this study ,Figs.13and 14.The experiments of Wang et al.[21]are well reproduced although only one data set is shown here,Fig.15.The only signi ficant discrepancies arise for the 0%and 15%steam mixtures,where the mea-sured ignition delay times are a lot faster thanthoseFigure 12Ignition delay measurements [20]: 1.03%H 2+0.5%O 2,balance Ar,at 1atm;model predictions ——this study and Mueller etal.Figure 13Ignition delay times from Cheng and Oppenheim [16]: 6.67%H 2+3.33%O 2,balance Ar,at 1.9atm;model predictions ——this study ,–-–-Mueller et al.,---Leeds 0.5,···GRI-Mech 3.0,–--Konnov 0.5.predicted by the models below 1010and 1090K,respectively.Rotational relaxation of N 2was not taken into consideration.Given that atomic species substantially decrease the vibrational relaxation rate [76,77],this is probably a reasonable assumption for Figs.8,14,and 15.The improved predictions are a result of choosing athird-body ef ficiency of 1.3for H 2in the reaction ˙H+O 2+M =H ˙O2+M,whereas Mueller et al.adopted a value of 2.5.This has resulted in the improvements seen in the simulation of the ignition delays of Slack,Fig.8,and those of Fujimoto et al.,Fig.9.Figure 14Ignition delay measurements from Bhaskaran et al.[14]: 22.59%H 2+14.79%O 2,balance N 2,at 2.5atm;model predictions ——this study ,–-–-Mueller et al.,---Leeds 0.5,···GRI-Mech 3.0,–--Konnov 0.5.。
关于冰块实验的作文英语Title: The Ice Cube Experiment: Unveiling the Secrets of Science。
Introduction:Science, with its endless mysteries and intriguing phenomena, often beckons us to explore and unravel its secrets. Among the many fascinating experiments that captivate both young minds and seasoned scientists alike is the timeless ice cube experiment. This experiment, seemingly simple yet profoundly insightful, unveils the principles of physics, chemistry, and thermodynamics. In this essay, we delve into the intricacies of the ice cube experiment, exploring its underlying principles, applications, and significance in scientific inquiry.Understanding the Experiment:At its core, the ice cube experiment involves observingthe process of ice melting in various environmental conditions. It serves as a practical demonstration of concepts such as heat transfer, phase transitions, and equilibrium. By subjecting ice cubes to different temperatures, pressures, and mediums, researchers can investigate the factors influencing the rate of melting and the final equilibrium state.Key Concepts:1. Heat Transfer: Heat transfer plays a central role in the ice cube experiment. When an ice cube is exposed to a warmer environment, such as room temperature air or water, heat energy flows from the surroundings to the ice cube. This influx of heat causes the ice cube to absorb thermal energy, leading to a rise in temperature and ultimately melting.2. Phase Transitions: The transition of water from a solid (ice) to a liquid state exemplifies a phase transition. As heat is absorbed by the ice cube, thekinetic energy of its molecules increases, eventuallysurpassing the threshold for maintaining a solid structure. Consequently, the bonds holding the water molecules in a rigid lattice break, resulting in the formation of liquid water.3. Equilibrium: Throughout the melting process, the system strives to reach equilibrium, where the rate of ice melting equals the rate of heat absorption. At equilibrium, the temperature remains constant, and the ice-water mixture coexists in a delicate balance. Understanding the concept of equilibrium is crucial for interpreting experimental results and predicting the behavior of complex systems.Experimental Variations:The versatility of the ice cube experiment allows for a myriad of variations, each offering unique insights into physical phenomena. Some common variations include:1. Temperature Variation: Altering the temperature of the surroundings can significantly impact the rate of ice melting. By placing ice cubes in environments of differenttemperatures, researchers can observe how heat transfer influences the melting process.2. Pressure Variation: Pressure also affects the melting point of ice, albeit to a lesser extent than temperature. High-pressure environments, such as those found deep underwater or in pressurized containers, can lower the melting point of ice, causing it to melt more rapidly.3. Medium Variation: The medium surrounding the ice cube, whether air, water, or another substance, can influence the rate of melting. For instance, ice melts more slowly in cold water than in warm water due to differences in thermal conductivity.Significance and Applications:Beyond its educational value, the ice cube experiment has practical applications in various fields:1. Climate Science: Studying the melting behavior ofice cubes provides insights into the processes driving glacial melting and sea-level rise, crucial considerations in climate change research.2. Engineering: Understanding heat transfer and phase transitions is essential for designing efficient cooling systems, refrigeration units, and thermal insulation materials.3. Food Science: Food preservation techniques oftenrely on controlling temperature and phase transitions to extend the shelf life of perishable goods.Conclusion:In conclusion, the ice cube experiment serves as a gateway to understanding fundamental principles of physics and chemistry. Its simplicity belies the depth of knowledge it offers, making it a timeless educational tool and a cornerstone of scientific inquiry. By unraveling the mysteries hidden within the humble ice cube, we gain valuable insights into the workings of the natural worldand pave the way for technological advancements that benefit society as a whole.。
PERGAMON Carbon 39(2001)25–37A kinetic and equilibrium study of competitive adsorptionbetween atrazine and Congo red dye on activated carbon:theimportance of pore size distributiona ,b*Costas Pelekani ,Vernon L.Snoeyink aAustralian Water Quality Center ,Private Mail Bag 3,Salisbury ,SA 5108Australia b Department of Civil and Environmental Engineering ,University of Illinois ,205North Mathews Avenue ,Urbana ,IL 61801,USAReceived 15August 1999;accepted 20February 2000AbstractA series of phenolic resin-based microporous activated carbon fibers (ACF)with different micropore size distributions were used to assess the role of pore size distribution (PSD)in the mechanism of competitive adsorption between the organic micropollutant,atrazine,and a compound larger in size,Congo red dye (CR).Batch kinetic and equilibrium experiments with the CR/atrazine system consisted of single-solute,simultaneous adsorption,CR preloading followed by atrazine contact,and atrazine preloading followed by CR contact.Based on the previous pore characterization studies and the PSD,two types of pore structures were proposed:telescopic pores and branched pores.With the telescopic pore structure,evidence is presented to support a transition from surface pore blockage to pore constriction (without loss of atrazine capacity)to direct competition for adsorption sites,with increasing average micropore size.With the branched pore structure (micropores branching off from mesopores),direct competition for adsorption sites in a fraction of the large micropores and pore constriction and pore blockage of smaller micropores were found to be important.The kinetics of adsorption was found to be important in determining the impact of simultaneous adsorption,while CR surface coverage and preloading time were the key factors controlling the impact of preloading on atrazine adsorption.©2000Elsevier Science Ltd.All rights reserved.Keywords :A.Activated carbon;Carbon fibers;C.Adsorption;D.Microporosity1.Introductionremoval of synthetic organic chemicals including pes-ticides,herbicides and industrial waste products;taste and An understanding of activated carbon adsorption pro-odor compounds which are derived from algal metabolites cesses requires knowledge of adsorbate–adsorbent prop-and bacteria;and algal toxins.erties,including their respective solution chemistries andOf the important factors that influence the removal of pore size distribution.This knowledge is invaluable intrace compounds in the presence of NOM,the role of pore selecting a carbon adsorbent for a particular treatmentsize distribution in relation to the size of the contaminant application,and applying it in an effective manner.Inmolecule and the molecular size distribution of NOM has drinking water treatment,some applications of activatednot been extensively ing conventional activated carbon include:the control of disinfection by-productcarbons,Newcombe et al.[1]found that low molecular precursors (DBP)which are present as part of the naturalweight NOM fractions consistently had a more deleterious organic matter (NOM)mixture present in all waters;theimpact on adsorption of the taste and odor compound,2-methylisoborneol (MIB),than the larger NOM fractions.They proposed that direct competition between MIB and NOM compounds of similar size dominated,with minimal *Corresponding author.Tel.:161-882-590-369;fax:161-pore blockage by the larger NOM components.Pelekani 882-590-228.and Snoeyink [2]used an activated carbon fiber (ACF)E -mail address :con.pelekani@.au (C.Pelekani).containing only primary micropores (pore width less than 0008-6223/01/$–see front matter ©2000Elsevier Science Ltd.All rights reserved.PII:S0008-6223(00)00078-626C.Pelekani,V.L.Snoeyink/Carbon39(2001)25–37˚8A)to assess the role of pore size in the mechanism of Therefore,for short contact times(e.g.7days)adsorption competition between atrazine and groundwater NOM.It in these pores was essentially irreversible.In larger was shown that the NOM could not adsorb in the primary secondary micropores,this phenomenon was not observed micropores and competed by surface pore blockage.In-and displacement of preloaded atrazine by methylene blue creasing the volume of secondary micropores(pore width was a relatively fast process.˚8–20A)resulted in a large improvement in atrazine In this study,using the same microporous ACFs,the adsorption capacity,and a shift to direct competition for impact of increasing the size of the competing compound adsorption sites in these larger micropores.on the competitive adsorption mechanism in different size Sakoda et al.[3]assessed the feasibility of using ACFs pores was evaluated by a series of batch kinetic and in columnfiltration mode to remove trihalomethanes,equilibrium experiments.Specifically,Congo red(CR),an including chloroform(CHCl),from drinking water con-anionic dye with a molecular weight of651(cf.284for 3taining NOM.One ACF with micropores of width less methylene blue),was used.CR is much larger than ˚than14A,and another ACF containing both micropores methylene blue,and is possibly more representative of the ˚and mesopores(,60A)were used.With the strictly molecular size of small NOM molecules present in drink-microporous ACF,a15%reduction in CHCl capacity was ing water supplies.3obtained,with respect to CHCl adsorption in organic-free3water.However,with the mesoporous ACF,the relativedecrease was70%.It was proposed that NOM adsorbed in 2.Experimentalthe mesoporous ACF not only reduced the number ofadsorption sites for CHCl,but also blocked their passage 2.1.Materials3into smaller micropores.The authors provided no in-formation about the molecular size distribution of the anic-free waterNOM present in the drinking water and the relative Deionized-distilled water(DDW)with a dissolved or-adsorption capacities of the two ACFs for NOM.ganic carbon concentration of less than0.2mg/l was used In developing a conceptual model of competitive ad-to prepare all solutions.sorption between small organic contaminants and othercompounds,based on pore size,the molecular size hetero- 2.1.2.Adsorbatesgeneity of NOM can make it difficult to ascertain the The target micropollutant was atrazine,a selective pre-specific impacts of molecules of different size in pores of emergent herbicide that is widely used in North America varying size.This can be overcome using molecular and Europe.Congo red(CR),an anionic dye,much larger probes,compounds of known size and shape in competi-in size than atrazine was selected as the competing tive adsorption studies.adsorbate.The structural formulae of atrazine and CR are14Pelekani and Snoeyink[4]usedfive ACF adsorbents shown in Fig.1.C-labeled atrazine(Novartis,Green-with different micropore size distributions to assess the sboro,NC)was utilized due to ease of analysis and the impact of pore size on the competition mechanism between small sample volumes required.CR was received97% the target organic micropollutant,atrazine,and methylene pure(Aldrich,Milwaukee,WI).Table1compares selected blue dye,a compound of similar size.It was shown that chemical properties of CR and atrazine.Molecular dimen-these compounds directly competed for adsorption sites in sion data were obtained using ChemSketch3.5(Advanced the accessible micropore region.When only primary Chemistry Development,Toronto,Canada).micropores were present,overlapping pore wall potentialsin these small pores resulted in strong binding of atrazine, 2.1.3.Activated carbonfiber adsorbents(ACF)with subsequent desorption being a very slow process.Four microporous phenolic resin-based ACFs withFig.1.Molecular structures of atrazine(left)and Congo red dye(right).C .Pelekani ,V .L .Snoeyink /Carbon 39(2001)25–3727Table 1was chosen to ensure equilibration at the low relative 25Selected chemical properties of Congo red dye and atrazinepartial pressures (,10)which is critical for the analysis of the micropore region [6].The isotherm data were used Property Atrazine CRto calculate the BET surface area,micropore volume and aMolecular weight (g/mol)215.68650.73pore size distributions of the ACFs.3Molar volume (cm /mol)169.8422.9˚Width (A)9.626.2˚Depth (A)8.47.42.2.4.Adsorption isotherms ˚Thickness (A)|3 4.3Adsorption isotherms were performed at pH 7.0using a Does not include associated sodium ions.the bottle-point technique [7].Due to the acid–base character of the CR dye,all solutions were buffered with 1mM phosphate buffer.At pH 7.0,CR was completely ionized (red color).The p K of CR is |5.5.In the a increasing degrees of activation,designated ACF-10,ACF-simultaneous adsorption experiments,the CR concentra-15,ACF-20and ACF-25were used (Nippon Kynol,tion used was |8m M (5.2mg/l).The atrazine con-Japan).They were received as twilled-weave fabrics.Acentration was |50m g/l (0.23m M).Samples for analysis mesoporous ACF was produced by further activating ACF-were taken after 7days and 30days contact time.In the 25in a bench-scale tubular reactor furnace (Lindberg;CR preloading experiments,the adsorbents were exposed Model 54232).A 60:40steam:nitrogen gas mixture wasto CR for 7days,filtered and contacted with single-solute used (1l/min at 1atm and 23C),with a furnace tempera-atrazine.Atrazine samples were taken after an additional 7ture of 8508C.One-gram samples of ACF-25were exposeddays and 30days of contact time.Additional preloading for at least 8h,resulting in a yield of only 4–6%.tests were performed with MESO ACF (see Section 3.7).Preliminary experiments showed that very high burnoffsIn the atrazine preloading experiments,the adsorbents were required to produce significant mesoporosity.Thiswere loaded with single-solute atrazine using an initial adsorbent was designated MESO.The carbons were driedconcentration of 400–500m g/l.After 7days of contact,at 1058C and stored in a desiccator to minimize moisturethe bottles were sampled and the atrazine-loaded ACF-10contact.In all experiments,the ACFs were cut into smallsamples were filtered and contacted with single-solute CR pieces,except for MESO ACF,which was extremelysolution (8m M)for an additional 7days.friable and rapidly broke into short fiber lengths duringcontact.2.2.5.Batch kinetic tests 2.2.MethodsA jar test apparatus (Six Paddle Stirrer Model 7790-400,Phipps &Bird,Richmond,V A)and modified square jars 22.2.1.Atrazine analysis(B-KER ,Phipps &Bird)were used to assess the short 14C-Atrazine was quantified by liquid scintillation [5].term adsorption kinetics (3days)of atrazine for various This was achieved by mixing 2.5-ml aliquots of 0.22m mcompetitive adsorption modes.A liquid volume of 2l was filtered sample with 18ml of scintillation cocktail (Ecos-used for all tests.The ACFs were soaked overnight in 10cint,National Diagnostics,Manville,NJ),and measuringml of DDW,to ensure complete wetting.In the preloading the resulting fluorescence in a liquid scintillation countertests,the carbon was filtered after the initial loading step (Tri-Carb Model 1600CA,Packard Instrument,Downersprior to contact with the adsorbate of interest.Grove,IL).The specific activity (38.7–56.3m Ci/mg)of14the C-atrazine yielded a detection limit of |0.05m g/lwithout sample pre-concentration.3.Results and discussion 2.2.2.Congo red (CR )analysis3.1.Physical adsorbent characterization CR was analyzed using a Beckman DU 7500diodearray spectrophotometer (Beckman Instruments,Fullerton,Table 2summarizes the micropore size,pore volume CA),with detection at 497nm.The detection limit wasand surface area data.As the level of activation increases,|0.5m M.there is an increase in the BET surface area,micropore volume and average pore size.The pore size distributions 2.2.3.Characterization of ACF physical properties(PSDs)were calculated using the 3-D discrete PSD model A Coulter Omnisorp 100(Hialeah,FL)was used for thedeveloped by Sun et al.[8],and are shown in Fig.2.volumetric measurement of the nitrogen adsorption iso-ACF-10contains mainly primary micropores,with a pore therms at 77K.The ACFs were outgassed at 2008C under˚size range of 6–9A.ACF-15,ACF-20and ACF-25are vacuum for 36h prior to analysis.The nitrogen adsorption˚experiments were performed in static mode using a massshifted to larger pore sizes (7–9A),with ACF-25having a ˚flow controller programmed to provide a fixed dose ofsmall volume of micropores in the 14–20A range.MESO nitrogen to the sample container.This mode of operation ACF has a bimodal PSD with a large volume of micro-28C .Pelekani ,V .L .Snoeyink /Carbon 39(2001)25–37Table 2Physical properties of ACFsPropertyACF-10ACF-15ACF-20ACF-25MESO 2BET surface area (m /g)87715181615191829993aMicropore volume (cm /g)0.3070.6310.6860.884 1.4743aTotal pore volume (cm /g)0.3070.6310.6860.893 2.127aFraction microporosity (%)1001001009969.32bMesopore area (m /g)16.224.929.548.4414a ˚Average micropore width (A)7.17.87.88.910.6a ˚Average pore width (A)7.17.87.89.718.6a Using 3-D PSD model.0.950.4292d V (P /P )24.6164ads o b 2]]]]]]]]Applying BJH model:t 5[15]S (m /g)5E .MESO P t S D ]0.400.03402log S D P oFig.2.3-D model PSDs for the ACFs.˚pores in the 8–10A range,and a significant volume of pore tree structure exists,with small micropores branching ˚pores in the 14–54Arange.The degree of microporosity off from large micropores or mesopores.A comparison of is almost 100%for ACF-10→ACF-25,decreasing to 69%these pore structures is shown in Fig.3.Kawabuchi et al.for MESO ACF,which has a large mesopore volume.[10]also proposed this transition in the pore structure of Daley et al.[9]showed,via scanning tunneling micro-ACFs with increasing activation,via chemical vapor scopy experiments,the telescopic pore structure of ACF-deposition experiments.It should be pointed out that the 10,ACF-15,ACF-20and ACF-25.They also found thatproposed structures are only snapshots within the bulk within the bulk fiber the pores formed an interconnectedfibers.The adsorbents still possess an interconnected pore network.This is consistent with the narrow pore sizenetwork,otherwise the large pore volumes attainable with distributions of these materials.In contrast,a different poreactivated carbons could not exist.structure is proposed for MESO ACF due to the bimodalnature of its PSD.Rather than telescopic pores,a branched 3.2.Single -solute Congo red adsorptionFig.4illustrates the 7-day single-solute CR adsorptionisotherms.As the average pore size,total microporevolume and total mesopore surface area increase,there is aconsistent increase in CR adsorption capacity.ACF-10hada very low CR capacity (2m mol/g)while MESO ACFshowed extremely high capacity (|800m mol/g).ACF-15,ACF-20and ACF-25showed intermediate adsorptioncapacities of 30,50and 220m mol/g,respectively.The3maximum CR loadings (m mol/g)were converted to cm /g3using a molar volume of 422.9cm /mol for the CRFig.3.Proposed pore structures.molecule (from Table 1),and plotted against pore volumeC.Pelekani,V.L.Snoeyink/Carbon39(2001)25–3729Fig.4.Single-solute CR isotherms for ACFs at pH7.0.in different size ranges to determine which region gave the width possibly being the limiting factor since it will result best correlation.An excellent correlation was obtained in steric hindrance inside the narrow micropores.The˚when pore volume in the8.5–9.5A range was considered experimental results show that part of the CR molecule can (Fig.5).This is not to say that CR did not adsorb in larger adsorb in small secondary micropores.These studies by pores.Apparently,the concentration of CR used was not Krupa and Cannon,and Kasaoka et ed very high CR sufficient tofill the larger micropores and mesopores of concentrations:200mg/l and2000mg/l,respectively. MESO ACF.Although not measured,surface chemistry These values are10–100times higher than those used in may play a role in CR adsorption,particularly since the this study.In addition,a short contact time of3days was anionic form of the dye was used in adsorption experi-used.These experimental conditions place emphasis on ments.Krupa and Cannon[11]found that CR adsorption adsorption in the larger pores,instead of focusing on the on activated carbon at pH8–10was strongly correlated small micropores.˚with adsorption in pore sizes from14–475A,confirmingthat CR can adsorb in large micropores and mesopores.In 3.3.Single-solute atrazine adsorptionanother study,Kasaoka et al.[12]determined that the˚critical adsorption pore size for CR was22.6A.If the The Freundlich adsorption parameters for the7-day ˚lower limit of14A is strictly true,then ACF-10,ACF-15single-solute atrazine isotherms are summarized in Table and ACF-20should yield no CR adsorption,which clearly 3.The data are valid for residual concentrations less than is not the case.The depth and width of the ionized CR100m g/l.It was found that atrazine adsorption correlated ˚˚˚molecule are7.4A and26.2A,respectively(Table1).The well with pore volume in pores larger than7.5A at high critical adsorption pore dimension is expected to be a(.1000m g/l)residual concentrations[4].At low solution contribution of both of these dimensions,with the large concentrations,the volume of small micropores and pos-Fig.5.Correlating CR adsorption with ACF pore size.30C.Pelekani,V.L.Snoeyink/Carbon39(2001)25–37Table3higher than CR.The degree of direct site competition Freundlich parameters for atrazine adsorption on ACFs between methylene blue and atrazine would be much1/n greater than that between CR and atrazine.The larger CR ACF K(mg/g)(l/m g)1/nmolecules adsorb on the outer surface of thefiber,and in 10 3.90.15the large micropores and mesopores(if any)that are very 1522.3 1.02near thefiber surface.This results in pore blockage and a 2022.70.97reduction in size(constriction)of the larger pores.Rela-2513.20.63tively few molecules of CR can thus prevent the adsorption MESO 6.70.66of many atrazine molecules.The similar results for thesimultaneous adsorption and CR preloading experimentssupport the concept of pore blockage at thefiber surface. sibly surface chemistry influenced atrazine adsorption,Surface pore blockage is a relatively fast process compared leading to lower capacities for ACF-25and MESO ACF to diffusion within micropores because of the short dis-than ACF-15and ACF-20.Atrazine adsorption capacity tance the CR molecule must travel.Although the atrazine was much higher than CR capacity on all ACFs,consistent preload experiment followed by CR contact was not with its smaller size and ability to access correspondingly performed with ACF-10,Pelekani and Snoeyink[4] smaller micropores.showed that methylene blue was not able to displace any Three competitive adsorption modes were used to significant quantity of atrazine after7days,because the elucidate the mechanism of competition,including:strong adsorption potentials in small micropores resulted invery slow desorption.With a much larger molecule,suchas CR,which cannot access the same micropores,negli-•simultaneous adsorption of atrazine and CR;gible displacement of atrazine is expected after even long •adsorption of CR followed by atrazine contact(CRcontact times.preloading);Figs.7and8show an increase in atrazine adsorption at •adsorption of atrazine followed sequentially by DDW30days,for both the simultaneous adsorption and CR and CR contact(atrazine preloading).preload experiments.However,the data are still wellbelow the single-solute isotherm;this indicates that CR has petitive adsorption experiments on ACF-10both a kinetic effect and an equilibrium effect.Thecapacity reduction is due to complete pore blockage of a Fig.6compares the effect of simultaneous adsorption fraction of the pores,whereas the reduction in the rate of and CR preloading on atrazine capacity on ACF-10,which atrazine adsorption is likely due to hindered diffusion contained the smallest micropores.From the single-solute because of a reduction in pore size.An important observa-experiments the adsorption capacity for atrazine was25tion is that the30-day CR preload capacity is higher than times greater than for CR,indicative of the smaller size of the30-day simultaneous adsorption capacity.The reason the atrazine molecule.Both modes of contact reduced for this behavior is that in the CR preload experiment,the atrazine capacity by more than one order of magnitude.preloaded carbon was contacted with single-solute at-Pelekani and Snoeyink[4]showed a similar reduction in razine,and thus desorption of pore-blocking molecules capacity using a smaller competing adsorbate,methylene occurred that was not observed in the simultaneous ad-blue,even though it had a single-solute capacity30times sorption experiment.Fig.6.Effect of simultaneous adsorption and CR preloading on atrazine adsorption capacity on ACF-10(7days contact).C.Pelekani,V.L.Snoeyink/Carbon39(2001)25–3731Fig.7.Effect of contact time on atrazine adsorption on ACF-10under simultaneous adsorption conditions.Fig.8.Effect of contact time on atrazine adsorption on ACF-10under CR preload conditions.petitive adsorption on ACF-15and ACF-20For carbon doses greater than3mg/l,the7-day competi-tive adsorption data lie essentially on the single-solute Fig.9shows the effect of simultaneous adsorption and isotherm line,indicating no competitive effect due to the CR preloading on atrazine adsorption capacity with ACF-presence of CR.At lower carbon doses,a significant 15.The initial CR concentration was8m M(5.2mg/l)and kinetic effect was observed at7days(data point at23 the initial atrazine concentration was50m g/l(0.23m M).m g/l),which shifted to8m g/l at30days.Two-day batchFig.9.Effect of contact time on atrazine capacity for simultaneous CR/atrazine adsorption on ACF-15.C.Pelekani,V.L.Snoeyink/Carbon39(2001)25–3733Fig.12.Atrazine preload(ACF-15)followed by7days of contact with8m M CR.confirming micropore constriction without pore blockage.sorption,while preloading with CR yielded a larger Batch kinetic tests showed much faster adsorption of impact,with a30%reduction in atrazine capacity(evalu-atrazine than with ACF-15,indicating the presence of ated at1m g/l).The30-day simultaneous adsorption data some larger micropores to facilitate transport into the small were the same as the7-day data,contrary to the results micropores.Although the presence of CR reduced the obtained with ACF-10,ACF-15and ACF-20.This be-atrazine uptake rate,the impact was less than with ACF-havior is consistent with the presence of a significant˚15,and the single-solute capacity was attained after48h.volume of larger secondary micropores in the14–20A Preloading with CR reduced the rate of adsorption for low range in ACF-25,in which the larger CR molecules carbon doses(,2mg/l)at7days.However,unlike preferentially adsorb(even though it has been shown that it ACF-15,the data shifted to the single-solute isotherm at30can adsorb in smaller pores),without restricting access of days,indicating no loss in atrazine capacity and thus the atrazine to the small micropores.Batch kinetic tests(Fig. absence of pore blockage.This confirms the presence of14)showed that the atrazine uptake rate in the presence of slightly larger micropores,where CR will adsorb and result8m M CR was the same as in DDW,providing evidence for in pore constriction without pore blockage,even at high the absence of micropore constriction with ACF-25.This surface coverage.Preloading with atrazine followed by is an important result because the CR adsorption capacity single-solute CR contact showed very similar results to on ACF-25was seven times andfive times greater than for ACF-15,indicating that CR could not displace pre-ad-ACF-15and ACF-20,respectively.This is associated with sorbed atrazine.the increase in pore volume in secondary micropores.In comparison with ACF-10,which showed a significant petitive adsorption on ACF-25competitive effect associated with surface pore blockage,the competitive effect has been substantially reduced and The7-day simultaneous adsorption and CR preload pore blockage minimized by shifting the pore size dis-adsorption isotherms are shown in Fig.13.Simultaneous tribution to larger sizes(e.g.ACF-25).This highlights the adsorption resulted in a small reduction in atrazine ad-importance of having a wide distribution of micropores toFig.13.Adsorption isotherms for atrazine on ACF-25.34C.Pelekani,V.L.Snoeyink/Carbon39(2001)25–37Fig.14.Effect of CR on atrazine adsorption kinetics on ACF-25under simultaneous adsorption conditions.reduce competitive adsorption effects with small organic adsorption sites is therefore less important and poreblockage must be predominant.However,this is not compounds.consistent with the mechanisms established with ACF-10, Table4summarizes the results of an atrazine preloadACF-15and ACF-20.The pore size distribution of ACF-experiment with ACF-25followed by contact with single-25in Fig.2indicates a small volume of micropores in the solute CR solution.The amount of atrazine displaced was˚related to the surface coverage of atrazine,with more14–20A range,with the absence of micropores of size˚atrazine being displaced at high coverage(e.g.2.3%at9–14A.This is a strong indication that a small fraction of 1458m mol/g).At low surface coverage,atrazine pref-the telescopic pores was converted to a branched pore˚erentially adsorbs in small micropores that cannot be structure with the smaller micropores(7–9A)branching accessed by CR,so atrazine displacement is low.At high off from the larger micropores.With this structure,some coverage,atrazinefills both the small and large micro-CR molecules could effectively block pores leading off pores.CR is able to effectively compete with atrazine from the larger micropores.This mechanism would be adsorbed in the larger micropores,resulting in an increase consistent with the uniform reduction in atrazine adsorp-in the level of displacement at high loadings.In the tion capacity that is observed over a wide concentration competitive adsorption experiments,most of the data lie in range.Direct competition for adsorption sites would only the1–10mg/g loading range(4.6–46m mol/g),which is become important at higher loadings.much less than the lowest loading tested in the atrazine The small reduction in capacity observed in the simulta-preload test(168m mol/g).This is important because neous adsorption isotherm is probably also due to a pore Table4would indicate that negligible displacement of blocking effect.The impact is less because the small atrazine should occur if all the atrazine is adsorbed in atrazine molecules diffuse much faster into the micropore micropores too small for CR to access.region than the larger CR molecules,so more atrazine is Carter et al.[13]proposed that the slope of an isotherm able to penetrate into the primary adsorption space before (adsorbent preloaded with the competing species)provided some of the micropores are completely blocked.The30% information about adsorption site heterogeneity for the reduction in atrazine capacity(relative to single-solute) target compound.Fig.13shows that preloading with CR under CR preloading conditions was not observed with did not alter the site heterogeneity for atrazine adsorption;ACF-15and ACF-20.It is possible to explain this result the slope is identical to the single-solute isotherm.This is using the transition in pore structure.Preloading with CR consistent with CR not being able to access the smallest would allow these molecules to block the entrances to micropores due to steric hindrance.Direct competition for small micropores branching off from larger pores.Table4Summary of ACF-25atrazine preload(CR contact)experimental resultsCarbon Atrazine Atrazine CR removed Atrazine dose loading displaced by from solution displacement (mg/l)(m mol/g)CR(m M)(m M)by CR(%) 0.911457.90.2980.61 2.282.2228.980.0368 1.99 1.466.29161.550.00313 4.10.088。