Induced Crystallization of Polyelectrolyte-Surfactant Complexes at the Gas-Water Interface
物化词汇

一些物理化学专业英语词汇电泳electrophoresis 丁达尔效应Dyndall effect定容摩尔热容molar heat capacity under constant volume定容温度计Constant voIume thermometer定压摩尔热容molar heat capacity under constant pressure定压温度计constant pressure thermometer定域子系统localized particle system 动力学方程kinetic equations 动力学控制kinetics control 独立子系统independent particle system 对比摩尔体积reduced mole volume 对比体积reduced volume对比温度reduced temperature 对比压力reduced pressure对称数symmetry number 对行反应reversible reactions对应状态原理principle of corresponding state多方过程polytropic process多分子层吸附理论adsorption theory of multi-molecular layers二级反应second order reaction二级相变second order phase change 法拉第常数faraday constant 法拉第定律Faraday’s law 反电动势back E.M.F.反渗透reverse osmosis 反应分子数molecularity反应级数reaction orders 反应进度extent of reaction反应热heat of reaction 反应速率rate of reaction反应速率常数constant of reaction rate范德华常数van der Waals constant范德华方程van der Waals equation范德华力van der Waals force 范德华气体van der Waals gases范特霍夫方程van’t Hoff equation 范特霍夫规则van’t Hoff rule 范特霍夫渗透压公式van’t Hoff equation of osmotic pressure非基元反应non-elementary reactions 非体积功non-volume work 非依时计量学反应time independent stoichiometric reactions菲克扩散第一定律Fick’s first law of diffusion沸点boiling point 沸点升高elevation of boiling point费米-狄拉克统计Fermi-Dirac statistics分布distribution 分布数distribution numbers分解电压decomposition voltage 分配定律distribution law分散系统disperse system 分散相dispersion phase分体积partial volume 分体积定律partial volume law分压partial pressure 分压定律partial pressure law分子反应力学mechanics of molecular reactions分子间力intermolecular force 分子蒸馏molecular distillation封闭系统closed system 附加压力excess pressure弗罗因德利希吸附经验式Freundlich empirical formula of adsorption 负极negative pole负吸附negative adsorption 复合反应composite reaction盖·吕萨克定律Gay-Lussac law 盖斯定律Hess law甘汞电极calomel electrode 感胶离子序lyotropic series杠杆规则lever rule 高分子溶液macromolecular solution高会溶点upper consolute point 隔离法the isolation method格罗塞斯-德雷珀定律Grotthus-Draoer’s law隔离系统isolated system 根均方速率root-mean-square speed功work 功函work content共轭溶液conjugate solution 共沸温度azeotropic temperature构型熵configurational entropy 孤立系统isolated system固溶胶solid sol 固态混合物solid solution固相线solid phase line 光反应photoreaction光化学第二定律the second law of actinochemistry光化学第一定律the first law of actinochemistry光敏反应photosensitized reactions 光谱熵spectrum entropy 广度性质extensive property 广延量extensive quantity广延性质extensive property 规定熵stipulated entropy过饱和溶液oversaturated solution 过饱和蒸气oversaturated vapor 过程process 过渡状态理论transition state theory过冷水super-cooled water 过冷液体overcooled liquid过热液体overheated liquid 亥姆霍兹函数Helmholtz function亥姆霍兹函数判据Helmholtz function criterion亥姆霍兹自由能Helmholtz free energy 亥氏函数Helmholtz function 焓enthalpy 亨利常数Henry constant亨利定律Henry law 恒沸混合物constant boiling mixture恒容摩尔热容molar heat capacity at constant volume恒容热heat at constant volume 恒外压constant external pressure 恒压摩尔热容molar heat capacity at constant pressure恒压热heat at constant pressure 化学动力学chemical kinetics化学反应计量式stoichiometric equation of chemical reaction化学反应计量系数stoichiometric coefficient of chemical reaction化学反应进度extent of chemical reaction化学亲合势chemical affinity 化学热力学chemical thermodynamics 化学势chemical potential 化学势判据chemical potential criterion 化学吸附chemisorptions 环境environment环境熵变entropy change in environment挥发度volatility 混合熵entropy of mixing混合物mixture 活度activity活化控activation control 活化络合物理论activated complex theory 活化能activation energy 霍根-华森图Hougen-Watson Chart基态能级energy level at ground state基希霍夫公式Kirchhoff formula 基元反应elementary reactions积分溶解热integration heat of dissolution吉布斯-杜亥姆方程Gibbs-Duhem equation吉布斯-亥姆霍兹方程Gibbs-Helmhotz equation吉布斯函数Gibbs function 吉布斯函数判据Gibbs function criterion 吉布斯吸附公式Gibbs adsorption formula吉布斯自由能Gibbs free energy 吉氏函数Gibbs function极化电极电势polarization potential of electrode极化曲线polarization curves 极化作用polarization极限摩尔电导率limiting molar conductivity几率因子steric factor 计量式stoichiometric equation计量系数stoichiometric coefficient 价数规则rule of valence简并度degeneracy 键焓bond enthalpy胶冻broth jelly 胶核colloidal nucleus胶凝作用demulsification 胶束micelle 胶体colloid胶体分散系统dispersion system of colloid胶体化学collochemistry胶体粒子colloidal particles 胶团micelle 焦耳Joule焦耳-汤姆生实验Joule-Thomson experiment焦耳-汤姆生系数Joule-Thomson coefficient焦耳-汤姆生效应Joule-Thomson effect 焦耳定律Joule`s law接触电势contact potential 接触角contact angle节流过程throttling process 节流膨胀throttling expansion节流膨胀系数coefficient of throttling expansion结线tie line 结晶热heat of crystallization解离化学吸附dissociation chemical adsorption界面interfaces 界面张力surface tension浸湿immersion wetting 浸湿功immersion wetting work精馏rectify 聚(合)电解质polyelectrolyteBET公式BET formula DLVO理论DLVO theoryHLB法hydrophile-lipophile balance methodpVT性质pVT property ζ电势zeta potential阿伏加德罗常数Avogadro’number 阿伏加德罗定律Avogadro law阿累尼乌斯电离理论Arrhenius ionization theory阿累尼乌斯方程Arrhenius equation阿累尼乌斯活化能Arrhenius activation energy阿马格定律Amagat law 艾林方程Erying equation爱因斯坦光化当量定律Einstein’s law of photochemical equivalence 爱因斯坦-斯托克斯方程Einstein-Stokes equation安托万常数Antoine constant 安托万方程Antoine equation盎萨格电导理论Onsager’s theory of conductance半电池half cell 半衰期half time period饱和液体saturated liquids饱和蒸气压saturated vapor pressure饱和蒸气saturated vapor 饱和吸附量saturated extent of adsorption 爆炸界限explosion limits 比表面功specific surface work比表面吉布斯函数specific surface Gibbs function比浓粘度reduced viscosity 标准电动势standard electromotive force标准电极电势standard electrode potential标准摩尔反应焓standard molar reaction enthalpy标准摩尔反应吉布斯函数standard Gibbs function of molar reaction标准摩尔反应熵standard molar reaction entropy标准摩尔焓函数standard molar enthalpy function标准摩尔吉布斯自由能函数standard molar Gibbs free energy function 标准摩尔燃烧焓standard molar combustion enthalpy标准摩尔熵standard molar entropy标准摩尔生成焓standard molar formation enthalpy标准摩尔生成吉布斯函数standard molar formation Gibbs function标准平衡常数standard equilibrium constant标准氢电极standard hydrogen electrode 标准态standard state标准熵standard entropy 标准压力standard pressure标准状况standard condition 表观活化能apparent activation energy表观摩尔质量apparent molecular weight表观迁移数apparent transference number表面surfaces 表面过程控制surface process control表面活性剂surfactants 表面吸附量surface excess表面张力surface tension 表面质量作用定律surface mass action law 波义尔定律Boyle law 波义尔温度Boyle temperature波义尔点Boyle point 玻尔兹曼常数Boltzmann constant玻尔兹曼分布Boltzmann distribution 玻尔兹曼公式Boltzmann formula玻尔兹曼熵定理Boltzmann entropy theorem玻色-爱因斯坦统计Bose-Einstein statistics泊Poise 不可逆过程irreversible process不可逆过程热力学thermodynamics of irreversible processes不可逆相变化irreversible phase change布朗运动brownian movement 查理定律Charle’s law产率yield 敞开系统open system超电势over potential 沉降sedimentation沉降电势sedimentation potential 沉降平衡sedimentation equilibrium 粗分散系统thick disperse system 催化剂catalyst单分子层吸附理论mono molecule layer adsorption单分子反应unimolecular reaction触变thixotropy单链反应straight chain reactions 弹式量热计bomb calorimeter道尔顿定律Dalton law 道尔顿分压定律Dalton partial pressure law 德拜和法尔肯哈根效应Debye and Falkenhagen effect德拜立方公式Debye cubic formula等焓过程isenthalpic process德拜-休克尔极限公式Debye-Huckel’s limiting equation等焓线isenthalpic line 等几率定理theorem of equal probability等温等容位Helmholtz free energy 等温等压位Gibbs free energy等温方程equation at constant temperature 低共熔点eutectic point低共熔混合物eutectic mixture 低会溶点lower consolute point低熔冰盐合晶cryohydric第三定律熵third-law entropy第二类永动机perpetual machine of the second kind第一类永动机perpetual machine of the first kind缔合化学吸附association chemical adsorption 电池常数cell constant 电池电动势electromotive force of cells 电池反应cell reaction电导conductance 电导率conductivity电动势的温度系数temperature coefficient of electromotive force电动电势zeta potential 电功electric work电化学electrochemistry 电化学极化electrochemical polarization电极电势electrode potential 电极反应reactions on the electrode电极种类type of electrodes 电解池electrolytic cell电量计coulometer 电流效率current efficiency电迁移electro migration 电迁移率electromobility电渗electroosmosis 电渗析electrodialysis·聚沉coagulation 聚沉值coagulation value绝对反应速率理论absolute reaction rate theory绝对熵absolute entropy 绝对温标absolute temperature scale绝热过程adiabatic process 绝热量热计adiabatic calorimeter绝热指数adiabatic index 卡诺定理Carnot theorem卡诺循环Carnot cycle 开尔文公式Kelvin formula柯诺瓦洛夫-吉布斯定律Konovalov-Gibbs law科尔劳施离子独立运动定律Kohlrausch’s Law of Independent Migration of Ions可能的电解质potential electrolyte 可逆电池reversible cell可逆过程reversible process 可逆过程方程reversible process equation可逆体积功reversible volume work 可逆相变reversible phase change 控制步骤control step 库仑计coulometer扩散控制diffusion controlled雷利公式Rayleigh equation拉普拉斯方程Laplace’s equation 拉乌尔定律Raoult law兰格缪尔-欣谢尔伍德机理Langmuir-Hinshelwood mechanism兰格缪尔吸附等温式Langmuir adsorption isotherm formula冷冻系数coefficient of refrigeration 冷却曲线cooling curve离解热heat of dissociation 离解压力dissociation pressure离域子系统non-localized particle systems离子的标准摩尔生成焓standard molar formation of ion离子的电迁移率mobility of ions 离子的迁移数transport number of ions离子独立运动定律law of the independent migration of ions离子氛ionic atmosphere 离子强度ionic strength理想混合物perfect mixture 理想气体ideal gas接触电势contact potential 接触角contact angle节流过程throttling process 节流膨胀throttling expansion节流膨胀系数coefficient of throttling expansion结线tie line 结晶热heat of crystallization解离化学吸附dissociation chemical adsorption界面interfaces 界面张力surface tension浸湿immersion wetting 浸湿功immersion wetting work精馏rectify 聚(合)电解质polyelectrolyte聚沉coagulation 聚沉值coagulation value绝对反应速率理论absolute reaction rate theory绝对熵absolute entropy 绝对温标absolute temperature scale绝热过程adiabatic process 绝热量热计adiabatic calorimeter绝热指数adiabatic index 卡诺定理Carnot theorem卡诺循环Carnot cycle 开尔文公式Kelvin formula柯诺瓦洛夫-吉布斯定律Konovalov-Gibbs law科尔劳施离子独立运动定律Kohlrausch’s Law of Independent Migration of Ions可能的电解质potential electroly可逆电池reversible cell可逆过程reversible process 可逆过程方程reversible process equation 可逆体积功reversible volume work 可逆相变reversible phase change 克拉佩龙方程Clapeyron equation 克劳修斯不等式Clausius inequality 克劳修斯-克拉佩龙方程Clausius-Clapeyron equation控制步骤control step 库仑计coulometer扩散控制diffusion controlled 拉普拉斯方程Laplace’s equation 拉乌尔定律Raoult law雷利公式Rayleigh equation兰格缪尔-欣谢尔伍德机理Langmuir-Hinshelwood mechanism兰格缪尔吸附等温式Langmuir adsorption isotherm formula冷冻系数coefficient of refrigeration 冷却曲线cooling curve离解热heat of dissociation 离解压力dissociation pressure离域子系non-localized particle systems离子的电迁移率mobility of ions 离子的标准摩尔生成焓standard molar formation of ion离子的迁移数transport number of ions离子氛ionic atmosphere离子独立运动定律law of the independent migration of ions离子强度ionic strength 理想混合物perfect mixture理想气体ideal gas 理想气体的绝热指数adiabatic index of ideal gases 理想气体的微观模型micro-model of ideal gas理想气体反应的等温方程isothermal equation of ideal gaseous reactions理想气体绝热可逆过程方程adiabatic reversible process equation of ideal gases理想气体状态方程state equation of ideal gas 理想稀ideal dilute solution 理想液态混合物perfect liquid mixture 粒子particles粒子的配分函数partition function of particles连串反应consecutive reactions 链的传递物chain carrier链反应chain reactions 量热熵calorimetric entropy量子统计quantum statistics临界常数critical constant量子效率quantum yield 临界参数critical parameter临界点critical point 临界胶束浓度critical micelle concentration临界摩尔体积critical molar volume 临界温度critical temperature临界压力critical pressure 临界状态critical state零级反应zero order reaction 流动电势streaming potential流动功flow work 笼罩效应cage effect路易斯-兰德尔逸度规则Lewis-Randall rule of fugacity 露点dew point 露点线dew point line 麦克斯韦关系式Maxwell relations麦克斯韦速率分布Maxwell distribution of speeds麦克斯韦能量分布MaxwelIdistribution of energy毛细管凝结condensation in capillary毛细现象capillary phenomena 米凯利斯常数Michaelis constant 摩尔电导率molar conductivity 摩尔反应焓molar reaction enthalpy 摩尔混合熵mole entropy of mixing摩尔气体常数molar gas constant 摩尔热容molar heat capacity摩尔溶解焓mole dissolution enthalpy摩尔稀释焓mole dilution enthalpy内扩散控制internal diffusions control内能internal energy 内压力internal pressure能级energy levels 能级分布energy level distribution能量均分原理principle of the equipartition of energy能斯特方程Nernst equation 能斯特热定理Nernst heat theorem凝固点freezing point 凝固点降低lowering of freezing point凝固点曲线freezing point curve凝胶gelatin 凝聚态condensed state凝聚相condensed phase 浓差超电势concentration over-potential 浓差极化concentration polarization 浓差电池concentration cells 帕斯卡pascal 泡点bubble point泡点线bubble point line 配分函数partition function配分函数的析因子性质property that partition function to be expressed as a product of the separate partition functions for each kind of state 碰撞截面collision cross section碰撞数the number of collisions 偏摩尔量partial mole quantities平衡常数(理想气体反应)equilibrium constants for reactions of ideal gases平动配分函数partition function of translation平衡分布equilibrium distribution 平衡态equilibrium state平衡态近似法equilibrium state approximation平衡状态图equilibrium state diagram平均活度mean activity 平均活度系统mean activity coefficient平均摩尔热容mean molar heat capacity平均质量摩尔浓度mean mass molarity平均自由程mean free path 平行反应parallel reactionsLiveBandit破乳demulsification 铺展spreading普遍化范德华方程universal van der Waals equation其它功the other work 气化热heat of vaporization气溶胶aerosol 气体常数gas constant气体分子运动论kinetic theory of gases气体分子运动论的基本方程foundamental equation of kinetic theory of gases 气溶胶aerosol气相线vapor line 迁移数transport number潜热latent heat 强度量intensive quantity强度性质intensive property 亲液溶胶hydrophilic sol氢电极hydrogen electrodes 区域熔化zone melting热heat 热爆炸heat explosion热泵heat pump 热功当量mechanical equivalent of heat热函heat content 热化学thermochemistry热化学方程thermochemical equation 热机heat engine热机效率efficiency of heat engine 热力学thermodynamics热力学第二定律the second law of thermodynamics热力学第三定律the third law of thermodynamics热力学第一定律the first law of thermodynamics热力学基本方程fundamental equation of thermodynamics热力学几率thermodynamic probability热力学能thermodynamic energy热力学特性函数characteristic thermodynamic function热力学温标thermodynamic scale of temperature热力学温度thermodynamic temperature热熵thermal entropy 热效应heat effect熔点曲线melting point curve 熔化热heat of fusion溶胶colloidal sol 溶解焓dissolution enthalpy溶液solution 溶胀swelling乳化剂emulsifier 乳状液emulsion润湿wetting 润湿角wetting angle萨克尔-泰特洛德方程Sackur-Tetrode equation 三相点triple point 三相平衡线triple-phase line 熵entropy熵判据entropy criterion 熵增原理principle of entropy increase 渗透压osmotic pressure 渗析法dialytic process生成反应formation reaction 升华热heat of sublimation实际气体real gas 舒尔采-哈迪规则Schulze-Hardy rule松驰力relaxation force 松驰时间time of relaxation速度常数reaction rate constant 速率方程rate equations速率控制步骤rate determining step 塔费尔公式Tafel equation态-态反应state-state reactions 唐南平衡Donnan equilibrium淌度mobility 特鲁顿规则Trouton rule特性粘度intrinsic viscosity 体积功volume work统计权重statistical weight 统计热力学statistic thermodynamics 统计熵statistic entropy 途径path途径函数path function 外扩散控制external diffusion control完美晶体perfect crystalline 完全气体perfect gas微观状态microstate 微态microstate韦斯顿标准电池Weston standard battery 维恩效应Wien effect维里方程virial equation 无热溶液athermal solution维里系数virial coefficient 稳流过程steady flow process稳态近似法stationary state approximation无限稀溶液solutions in the limit of extreme dilution物理化学Physical Chemistry 物理吸附physisorptions吸附adsorption 吸附等量线adsorption isostere吸附等温线adsorption isotherm 吸附等压线adsorption isobar吸附剂adsorbent 吸附量extent of adsorption吸附热heat of adsorption 吸附质adsorbate析出电势evolution or deposition potential析因子性质property that partition function to be expressed as a product of the separate partition functions for each kind of state稀溶液的依数性colligative properties of dilute solutions稀释焓dilution enthalpy系统system 系统点system point系统的环境environment of system 相phase相变phase change 相变焓enthalpy of phase change相变化phase change 相变热heat of phase change相点phase point 相对挥发度relative volatility相对粘度relative viscosity 相律phase rule相平衡热容heat capacity in phase equilibrium 相图phase diagram相倚子系统system of dependent particles悬浮液suspension压缩因子compressibility factor循环过程cyclic process 压力商pressure quotient压缩因子图diagram of compressibility factor阳极anode亚稳状态metastable state 盐桥salt bridge盐析salting out杨氏方程Young’s equation 液体接界电势liquid junction potential 液相线liquid phase lines 一级反应first order reaction一级相变first order phase change逸度fugacity依时计量学反应time dependent stoichiometric reactions逸度系数coefficient of fugacity 阴极cathode荧光fluorescence 永动机perpetual motion machine永久气体Permanent gas 有效能available energy原电池primary cell 原盐效应salt effect增比粘度specific viscosity 憎液溶胶lyophobic sol沾湿adhesional wetting 沾湿功the work of adhesional wetting真溶液true solution 真实电解质real electrolyte真实气体real gas 真实迁移数true transference number振动配分函数partition function of vibration振动特征温度characteristic temperature of vibration蒸气压下降depression of vapor pressure 正常沸点normal point正吸附positive adsorption 支链反应branched chain reactions直链反应straight chain reactions 指前因子pre-exponential factor质量作用定律mass action law 制冷系数coefficient of refrigeration 中和热heat of neutralization 轴功shaft workLiveBandit转动配分函数partition function of rotation转动特征温度characteristic temperature of vibration转化率convert ratio 转化温度conversion temperature状态state 状态方程state equation状态分布state distribution 状态函数state function准静态过程quasi-static process 准一级反应pseudo first order reaction 自动催化作用auto-catalysis 自由度degree of freedom自由度数number of degree of freedom 自由焓free enthalpy自由能free energy 自由膨胀free expansion组分数component number 最低恒沸点lower azeotropic point最高恒沸点upper azeotropic point 最佳反应温optimal reaction temperature 最可几分布most probable distribution 最可几速率mostadikanghackneyed 陈腐的caustic 腐蚀性的erosion 腐蚀erode使腐蚀stale 陈腐的rot 腐烂rotten 腐烂的decay 腐败corrode 腐蚀decomposition 分解,腐烂rust 铁锈silica 硅土lime stone石灰石crystal 水晶gasoline 汽油methane 甲烷,沼气hydrocarbon 碳氢化合物petroleum 石油plastic 塑胶intermediary 媒介物catalysis 催化作用catalyst 催化剂adhesive 黏合剂scorch 使退色bleach 漂白,去色,漂白剂tint 染色,上色dye 染料chemistry 化学biochemistry 生物化学hydronic 液体循环加热的alchemy 炼金术,魔力artificial 人造的,假的,非原产地的ion 离子molecule 分子,些微solubility 溶度solution 解答溶液solvent 溶剂dissolve 溶解,解散element 元素impurity 杂质blend 混合compound 混合物substance 物质,实质particle 颗粒,微粒explosive 爆炸的,炸药blast 爆炸burning 燃烧的kindle 燃起sear 烧灼,烧焦ignite 使燃烧action 作用combination 化合,组合neutralize 中和polymerization 聚合functional 起作用的synthetic 综合的,合成的carbon 碳copper 铜lead 铅Mercury 水星nickel 镍platina 白金silver 银sodium 钠tin 锡,马口铁zinc 锌calcium 钙helium 氦silicon 硅ammonia 氨sulfur 硫磺iodine 碘nitrogen 氮oxygen 氧1.reagent 反应力反应物 4. molecule 分子摩尔5. electron 电子6. isotope 同位素核素7. polymer 聚合体 8. alloy 合金10. metalloid 非金属 11. derivative 衍生物12. alkali 碱金属 13. hydrate 水合物14. action 作用Catalysis are sometimes used to accelerate chemical action.15. adhesive 粘合剂胶粘的18. bleach 去色漂白Please soak shirts in bleach to remove the stains.19. blast 爆破 [例] The village was blast by enemy bombs.23. caustic 腐蚀性的 [例] Some chemicals are caustic by nature.24. combination 化合组合 [例] The safe combination of the two chemicals required a complicated chemical process./ This is a combination of two powerful ingredients.25. corrode 腐蚀 [例] The metal has corroded because of rust.26. crystal 结晶状的27. decay 腐败 [例] Sugar decays our teeth.29. erode 腐蚀 [例] The sea has eroded the cliff face over the years.30. explode 使爆炸 [例] The red balloon exploded when I popped it with a pin.31. explosive 爆炸的炸药 [例] Dynamite is highly explosive. / Politics can be explosive issue.33. ignite 使燃着 [例] A smoldering cigarette ignited the newspapers.37. neutralize 中和 [例] Alkalis neutralize acids. 38. nickel 镍41. polymerization 聚合42. scorch 使褪色 [例] Do not leave the iron on the delicate fabric or the heat will scorch it.52. rotten 腐烂的 [例] The rotten fruit smelled horrible.Bunsen burner 本生灯 product 反应产物flask 烧瓶 apparatus 设备 matrass 卵形瓶 litmus 石蕊PH indicator PH值指示剂,氢离子(浓度的)负指数指示剂litmus paper 石蕊试纸 graduate, graduated flask 量筒,量杯reagent 试剂 test tube 试管 burette 滴定管 retort 曲颈甑still 蒸馏釜 cupel 烤钵 crucible pot, melting pot 坩埚pipette 吸液管 filter滤管 stirring rod 搅拌棒。
水软化用诱导结晶

Water softening by induced crystallization in fluidized bedYuefang Chen ⁎,Rong Fan,Danfeng An,Yujie Cheng,Hazel TanSchool of Civil and Environment Engineering,Beijing Key Laboratory of Resource-oriented Treatment of Industrial Pollutants,University of Science and Technology Beijing,Beijing 100083,China.E-mail:yuefangchen@A R T I C L E I N F OA B S T R A C TArticle history:Received 15January 2016Revised 15June 2016Accepted 1August 2016Available online 27September 2016Fluidized bed and induced crystallization technology were combined to design a new type of induced crystallization fluidized bed reactor.The added particulate matter served as crystal nucleus to induce crystallization so that the insoluble material,which was in a saturated state,could precipitate on its surface.In this study,by filling the fluidized bed with quartz sand and by adjusting water pH,precipitation of calcium carbonate was induced on the surface of quartz sand,and the removal of water hardness was achieved.With a reactor influent flow of 60L/hr,a fixed-bed height of 0.5m,pH value of 9.5,quartz sand nuclear diameter of 0.2–0.4mm,and a reflux ratio of 60%,the effluent concentration of calcium hardness was reduced to 60mg/L and 86.6%removal efficiency was achieved.The resulting effluent reached the quality standard set for circulating cooling water.Majority of the material on the surface of quartz sand was calculated to be calcium carbonate based on energy spectrum analysis and moisture content was around 15.994%.With the low moisture content,dewatering treatment is no longer required and this results to cost savings on total water treatment process.©2016The Research Center for Eco-Environmental Sciences,Chinese Academy of Sciences.Published by Elsevier B.V.Keywords:Fluidized bedInduced crystallization HardnessSoftening capability Quartz sandIntroductionWater hardness can be attributed to the presence of certain ions in water which can easily form undissolved salts (Teixeira et al.,2012).Some of the common ions include calcium ions,magnesium ions,ferrous ions,manganese ions and aluminum ions.Treatment processes often include the removal of these ions due to certain water quality requirements (Apell and Boyer,2010).In industries,circulating water used for cooling comprises the largest percentage in water utilization.Strict require-ments exist even for circulating water as the quality of the water may also affect the overall industrial process used.An example of a situation that is brought about by uncontrolled cooling water quality is the formation of salt crusts on the surface of heat exchangers.Various dissolved scaling salts may exist in cooling water.If these salt ions are not removed,certain physical and chemical conditions in the system may cause an increase in the concentration beyond saturation point,resulting in crystallization of various salt ions (Esfahani and Yoo,2014).These ions adhere to the surface of heat exchangers and other equipment,forming salt crusts and requiring maintenance.Salt crusts include calcium carbonate,calcium sulfate and calcium metasilicate and so on,of which,calcium carbonate is the most common and hazardous for water systems.Nowadays,there are various methods used to prevent calcium carbonate scale formation,such as softening through heating,seeding,ion exchange,nanofiltration,and electro-deionization (Omar et al.,2010).In the field of water softening treatment,lime soda softening process is the most common one in application.This is due to the numerous advantages of the process,such as,extensive sources of lime,easy disposal of solid waste,no pollution to the natural water bodies,and a big decrease of organic matter,silicate and ironJ O U R N A L O F E N V I R O N M E N T A L S C I E N C E S 50(2016)109–116⁎Correspondingauthor./10.1016/j.jes.2016.08.0141001-0742/©2016The Research Center for Eco-Environmental Sciences,Chinese Academy of Sciences.Published by ElsevierB.V.A v a i l a b l e o n l i n e a t w w w.s c i e n c e d i r e c t.c o mScienceDirectw w w.e l s e v i e r.c o m /l o c a t e /j e sin effluent.However,there are disadvantages when using the traditional lime softening method due to the generation of high-moisture sludge which is also hard to sediment. Generation of such sludge is undesirable as it means additional dewatering treatments not to mention that dealing with dewatered sludge has already been an urgent problem for national governments for a long time now(Indarawis and Boyer,2013;Chehayeb et al.,2014).Therefore,a new kind of treatment method is required to remove water hardness and at the same time,minimize the generation of sludge.Segev et al.(2013)modeled a fluidized bed system maintaining a high alkaline environment.With this,calcium ion in solution was induced to precipitate as calcium carbonate.Then,carbon dioxide was utilized to strip calcium carbonate from the system, thereby reducing water hardness.Currently,for precipitation from solution,evidences have shown that precipitation occurs more when certain amount of tiny particles already exist or form in the solution(Da Silva et al.,2014).Nowadays,the method of fluidized induced crystallization/precipitation is being used.This method combines the technology of fluid-bed and induced crystallization precipitation technology.The process operation just utilizes fluidized bed which has a certain number of induced crystal nuclei,and then,the precipitant which could form insoluble matters with ions is added,having an effect of purifying water(Comstock and Boyer,2014).Kim van Schagen et al.paved small pellets on fluidized bed,and used the advantage of these pellets to enhance the water softening capability by fluidized bed. Moreover,evidences showed that it was possible to keep the reactor at desired operational parameters(pellet size and bed height)under varying operational conditions in a simulation experiment.In this way,the cost of pellet softening is reduced and the situation of irregularities could be prevented.However, the potential cost limited further development of this technique because of the addition of the induced crystal nucleus(van Schagen et al.,2008;Segev et al.,2011).Quartz sand is a kind of silicate mineral which is hard, wear-proof and has stable chemical properties.Furthermore, it is an irreplaceably important raw material of fireproofing, glass-making and building industries because of the abundant sources and low cost.Taking some quartz sand with specific proportion and particle size into wastewater and keeping it in fluidized state by adjusting the rate of inflow,quartz sand could serve as a crystal nucleus to induce precipitation of insoluble matters on the surface.This shows that it has properties of good settling ability,high solid content,and good sludge dewatering ability.The precipitate could also be used as building pared with traditional methods,the method of crystal quartz sand was easy to conduct and had a small floor coverage,which could reduce capital expenditure and running cost(Du et al.,2011).In this study,quartz sand was utilized as induced crystal nucleus,and the research combined the technology of fluid-bed and induced crystallization precipitation to explore water softening process.1.Materials and methodsThis study was aimed to solve the problem of water hardness of the secondary effluent from Guodian Longshan Sewage Treatment Station.A laboratory-scale process was established to optimize various parameters of fluidized induced crystallization/ precipitation at metastable region.Factors affecting calcium carbonate removal were also studied to determine the best runtime conditions to achieve good effluent quality as required by government standards.The test device and the experimental flowchart are shown in Fig.1.The reactor is a 5.5L cylindrical transparent Plexiglas with a total height of2400mm including the conical bottom, the cylindrical body and the water outlet.The column was connected using screws and nuts and a rubber gasket was added to prevent water leakage.Size200mesh filters were placed at the top and bottom of the cylindrical column to serve as the support for the quartz sand bed layer.The lower part of the column is the fluidized bed and has a height of2m and a diameter of5cm.The upper part of the column is used for the water,having a height of20cm and an inner diameter of10cm.The water inlet and dosing point inlet are located at the bottom of the reactor.Water and softening agents enter the column in a tangential direction.The water inlet pipe is8cm.Located30cm with increments of10cm from the bottom are10sampling ports.A100mesh screen was installed near the outlet of the sampling port in order to prevent outflow of quartz sand.To start the process,the column was filled with washed quartz sand.After loading the sand into the reactor,water was pumped into the reactor from the bottom,bringing the quartz sand to a fluidized state.Flow meters were installed to control the influent flow.Once the fluidized state stabilized, sodium carbonate solution was added into the reactor to serve as the precipitant,with quartz sand as the induced nucleus. This resulted in the formation of calcium carbonate precipi-tate on the surface of quartz sand,achieving the purpose of removing calcium ions.Treated water flowed out from the upper part of the column.In order to identify the optimum operating conditions, experiments were done with controlled variables while varying others.The experiments were performed at a room temperature of25°C,using water solution with calcium ion concentration of450mg/L.The concentration used in the research was chosen by taking the average value of the concentration of calcium ions in actual water samples obtained from the plant.Dynamic experiments were con-ducted to determine the effects of pH conditions,fixed-bed height,particle size,flow rate,and reflux ratio on the removal efficiency.1.1.Wastewater samplesThis study focused on the optimal conditions for the removal of calcium ions from wastewater.Actual water samples from the sewage treatment plant had high calcium ion concentra-tions(ranging from449to456mg CaCO3/L).In order to simulate the conditions of the actual wastewater,an equally high concentration of450mg CaCO3/L was used during the experimental phases to test the effects of pH conditions, fixed-bed height,particle size,flow rate,and reflux ratio on the removal rates.Removal of water hardness is greatly affected by the pH of the water system and the saturation pH.Because crystallization110J O U R N A L O F E N V I R O N M E N T A L S C I E N C E S50(2016)109–116is highly dependent on the saturation index,which in turn,is greatly affected by the pH,the best pH conditions were determined first.By varying the pH conditions and keeping the other parameters constant,the effects of pH on calcium ion removal was determined.After which,the effects of other parameters were studied.1.2.Analytical methodsAt the end of the experiments,quartz sand samples were obtained for analysis.First,the quartz sand carrier was removed and placed inside an oven to be dried at 105°C for 3hr.After drying,the weight was obtained and moisture content was calculated by subtracting the dry weight from the total weight before drying.Samples were then analyzed using Scanning Electron Microscope and Energy Dispersive Spec-trometer SEM-EDS (Model:SSX-550)with a magnification of ×450.The energy spectrum image of the sediment was also obtained and was determined using elemental analysis.At the end of the experiment,after drying the samples,the quartz sand samples were placed in a beaker.Deionized water and 0.1mol/L hydrochloric acid were added and the solution was poured into a 1-L volumetric flask.The beaker was washed repeatedly with deionized water to ensure that no residue remained in the beaker.After filling the volumet-ric flask,an electromagnetic mixer was used to mix the solution in the flask.After which,the concentration of the calcium ion in the digestive juice was ing Eq.(1),the amount of calcium carbonate on the surface of the carrier was calculated.W CaCO 3¼C Ca 2þÂ1L ÂW T Wð1Þwhere,W CaCO3(mg)is the weight of the calcium carbonate on the carrier,C Ca2+(mg/L)is the calcium ion concentration indigestive juice,W T (g)is the total carrier weight,and W (g)is the weight of carrier for digestive reaction.2.Results and discussion2.1.Effect of pH valueDepending on the pH of the system,calcium ions can exist in different forms:CaCO 3at higher pH (usually close to 10.3)and H 2CO 3at pH lower than 6.3.Calculation of the saturation index could gauge whether calcium carbonate can be precipitated or dissolved.If the saturation pH of CaCO 3is less than the actual pH,the water is considered scale forming and calcium carbonate is deposited.The saturation index increases when actual pH is increased.This may explain why past researches using crystal-lization in fluidized bed reactors were conductedatFig.1–(a)Fluidized bed reactor,(b)experimentalflowchart.Fig.2–Removal of calcium ion at different pH.111J O U R N A L O F E N V I R O N M E N T A L S C I E N C E S 50(2016)109–116environments with high pH,usually above9.0but lower than11. In this part of the study,the pH values were changed while the following conditions remained constant:the rate of inflow was 60L/hr,the size of induced crystal nucleus was0.2–0.4mm,and the fixed-bed height was0.5m.Fig.2shows the influence of calcium ion removal at various pH levels.It displayed that the effluent calcium ion concentration decreased with time and stability was achieved after a certain performance period.It can also be seen in the graph that calcium ion concentration in effluent became lower when pH level was higher.This is because carbonate ion would became more stable and the amount also increased when the system had a higher pH level.On the contrary,when the pH level decreases,carbonate ion would decrease before finally disappearing.Further study found that the removal rate of calcium ion decreased when calcium ion concentration in the effluent was stable and the pH level was higher than9.5.The reason was that the pH level increases with increasing concentrations of sodium hydroxide.This causes a sharp increase in the partial degree of supersaturation which induces crystallization of calcium carbonate by spontaneousnucleation and results to a decrease in the heterogeneous nucleation efficiency(Li et al.,2005;Burggraeve et al.,2013).Furthermore,when the pH value of water sample was around10,Mg2+would also react with carbonate ion to produce magnesium hydroxide precipitation,as shown in Fig.3.Since the solubility product constant of magnesium hydroxide is much lower than the solubility product constant of calcium carbonate,this signifies that it is easier for magnesium hydroxide to form precipitates.The formation of this kind of precipitate means the consumption of hydroxide ion,thus reducing the amount of carbonate ion.This,in turn,has an effect on the bonding between calcium and carbonate ion,and eventually,on the removal rate of calcium ion(Zhani,2013).2.2.Effect of the height of fixed-bedFig.4shows the part of the study focused on the influence of the height of the fixed-bed.The constant parameters were as follow:size of induced crystal nucleus was0.2–0.4mm,the pH value was around9.5,and the inflow was60L/hr.As time passed,calcium ion concentration in effluent declined,and this tendency was consistent at various heights of fixed-bed. The lowest calcium ion concentration in effluent was found when the height of fixed-bed was0.5m.Since the surface area of the carriers is proportional to the fixed-bed height,there was an increase in the contact time and area between water sample and sand.This made it feasible for calcium carbonate to adhere to the carriers,enhancing the removal rate(Ping et al.,2013).However,the study found that there was too much pressure when the height of fixed-bed was at0.6m or higher,which made the degree of fluidization become smaller.Thus,the optimal height of fixed-bed was0.5m.2.3.Effect of the induced crystal nucleus sizesFig.5shows the effect of different sizes of crystal nuclei.In this part of the experiment,the rate of inflow was maintained at 60L/h and the compacted height of fixed-bed was0.5m.For the size of sand spheres,the surface area was0.02–0.05m2/g of beads.The size of the induced quartz crystalnuclei Fig.3–Removal of Mg2+at different pHvalues.Fig.4–Removal of Ca2+at different heights offixed-bed.Fig.5–Removal of at different particle sizes of the crystalnucleus.112J O U R N A L O F E N V I R O N M E N T A L S C I E N C E S50(2016)109–116were varied and the following sizes were used:0.2–0.4mm,0.6–0.8mm,1–1.5mm.Based on the results of the experiments,it can be seen that at longer run times,there is a decrease in the effluent calcium concentration before reaching stability.It is seen in the graph that the effluent calcium ion concentration was lowest when the size of the induced quartz crystal nucleus was0.2–0.4mm. Because the surface area is bigger when the size of induced quartz crystal nucleus is smaller,the chances of contact between supersaturated calcium carbonate and induced quartz crystal nucleus increases.As such,a smaller crystal nucleus is preferred for crystallization of calcium carbonate from water sample and also,for higher treatment efficiency(Li et al.,2012). However,it must also be taken into account that the size of the particle must be small enough for larger contact area but big enough to not be carried away with the effluent.Otherwise,this would bring down the removal efficiency despite having a bigger surface area(Wang et al.,2013).In this study,the size of 0.2–0.4mm was optimal.2.4.Effect of the flow rateIn Fig.6,the influence of inflow rate was studied by changing inflow rates while maintaining the same values for other parameters.With ongoing run time,calcium ion concentra-tion decreased,a common behavior at various inflow rates. The effluent containing the lowest calcium ion concentration (180.8mg/L)and highest removal rate was obtained at an inflow rate of60L/hr.Theoretically,the removal rate is better at a lower inflow rate because there is an increased contact time between water sample and induced crystal nucleus (Zamankhan,2012).However,based on the study and as shown in Fig.6,the largest removal rate was not at the40L/hr inflow rate.Since the fluidized crystal nucleus could not match the minimum fluidization velocity required,it could not achieve the state of fluidization,only having contact with the sand(Aldaco et al.,2007a).In this state,contact efficiency decreased and removal rate was affected.2.5.Effect of reflux ratioAs it is easier for supersaturated ions to precipitate out on the surface of crystal nuclei,it seemed significant to utilize treated crystal nucleus to deal with water sample.With ongoing run time,the induced crystal nucleus would expand in fluidized bed,filling up the space and consequently, influencing the treatment process.In this study,the size of induced crystal nucleus was 0.2–0.4mm,the pH value was around9.5,and the inflow was 60L/h.The influence of different reflux ratios on the flow of effluent was studied.From Fig.7,with ongoing run time, calcium ion concentration in effluent declined at various reflux ratios.When the reflux ratio increased,the treated crystal nucleus induced precipitation of supersaturated ions while lowering the pH of the system(Günther et al.,2013). The curve of reflux ratio of0%indicated an increase in the removal rate of calcium ion from a slower rate at initial stage. While it is hard for supersaturated ions to dissolve out on the smooth surface of the induced crystal nucleus,longerrun Fig.6–Removal of Ca2+at different flowrates.Fig.7–Removal of Ca2+at different refluxratios.Fig.8–The flow of effluent at different reflux ratios.113 J O U R N A L O F E N V I R O N M E N T A L S C I E N C E S50(2016)109–116time will increase the number of particles.As the surface becomes rougher,it becomes easier for the supersaturated ions to precipitate out (Hickenbottom and Cath,2014).Thus,theoretically,the higher the reflux ratio,the better the treatment effect.On the other hand,Fig.8shows the variation of effluent flow at different reflux ratios.At longer run time,the effluent flow declined at various reflux ratios,and the degree of decline became larger when the reflux ratio turned higher.A higher reflux ratio could mean more crystallization occurrence in fluidized bed when the reactor is in operation (Chmelar et al.,2013).It can be seen that the flow of effluent decreased by half when the reflux ratio was higher than 80%.In contrast,the 0%–60%reflux ratio had an acceptable range,accounting for less than or approximately 10%loss in effluent flow rate.Thus,combining with the results from other conditions,this study chose the reflux ratio of 60%as optimal level.2.6.Identification and analysis of crystal nucleus 2.6.1.Moisture content of crystal nucleusAfter a complete process of treating water sample in fluidized bed,this study attained a certain amount of induced crystal nuclei,all of which were obtained at optimum conditions.In order to ensure reliability in testing,five portions of induced crystal nucleus were weighted before and after three hours ofdrying in the drying oven at 105°C,as shown in Fig.9.The study found that the average moisture content of induced crystal nucleus was 15.99%.This value displayed a very low moisture level from crystallization fluidized bed reactor when compared with the sludge from mechanical accelerated clarifier (Plappally and Lienhard,2012).Therefore,the use of crystallization fluidized bed reactor could reduce the volume of discharged sludge and save the cost of sludge dewatering for water softening process.Thus,it is feasible to utilize fluidized crystallization technology.2.6.2.Surface topography of crystal shapeThe SEM images of quartz sand particles before and after the fluid-bed processing are shown in Fig.10.As shown in Fig.10a,unused crystalline precipitates had no sediment and crystallization;in Fig.10b,c,some obvious crystal substances were brought out on the surface of quartz sand particles,becoming rougher as the water traveled upward.A layer of calcium carbonate crystals were found on the surface (Grumiaux et al.,2012).Deposition and growth of crystal nucleus would develop after the solution obtains a state of saturation,or supersaturation.Then,once the crystal nucleus is formed,it is easier for supersaturated ions to precipitate out on rough surfaces.This shows that the reaction rate would increase with time.Calcium ion concentration would de-crease slowly until it reaches stability (Aldaco et al.,2007b ).Thus,this research displayed that the rate of crystallization of calcium carbonate would increase after an initial layer of calcium carbonate crystal is formed (Aldaco et al.,2007c ).Energy spectrum analysis showed the spectral image and the analysis of the elements.Fig.11and Table 1display the analysis of the sediment on the surface of quartz sand.Based on the mole ratio,the sediment obtained may be calcium carbonate,magnesium hydroxide,or carbonate silicon.Because the quality proportion of magnesium ion and silicon was very low,it was concluded that the main substance was CaCO 3,since the mole ratio of Ca,C and O was 1:1:3(Hermosillo et al.,2012).3.Conclusions(1)Optimal conditions for the removal of water hardnesswere found to be at an environment with pH 9.5,a reflux ratio of 60%,and an inflow rate of 60L/hr.Optimum height of the fixed-bed was 0.5m and the size of induced crystal nucleus was 0.2–0.4mm.Addition of induced crystal nucleus had a positive effect on thefluidizedFig.9–Moisture content of quartzsand.Fig.10–(a)SEM of unused crystalline precipitates,(b)crystalline precipitates at the center of the fluidized bed,(c)crystalline precipitates at the bottom of the fluidized bed.114J O U R N A L O F E N V I R O N M E N T A L S C I E N C E S 50(2016)109–116crystallization and is an advantage when reducing hard-ness in water.Concentration of calcium ion in CaCO 3form in the effluent was reduced to 60mg/L,a removal rate of 86.6%in this study.This calcium hardness index reached the standard set for circulating cooling water.(2)In the study,the removal rate of calcium ion was low atthe initial stage.As time passed,crystallization of calcium carbonate was observed on the surface of quartz sand and gradual increase in removal rate followed.This showed that water softening is possible after a period of time.(3)Energy spectrum 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LTPS低温多晶硅技术浅析

LTPS低温多晶硅技术浅析一、LTPS简介低温多晶硅(Low Temperature Poly-silicon;LTPS,以下以LTPS代称)是平板显示器领域中的又一新技术。
继非晶硅(Amorphous-Silicon,以下以a-Si代称)之后的下一代技术。
Polysilicon (多晶硅) 是一种约为0.1至数个um大小、以硅为基底的材料,由许多硅粒子组合而成。
在半导体制造产业中,多晶硅通常经由LPCVD(Low Pressure Chemical Vapor Deposition)处理后,再以高于900C的退火程序,此方法即为SPC (Solid Phase Crystallization) 。
然而此种方法却不适合用于平面显示器制造产业,因为玻璃的最高承受溫度只有650℃。
因此,LTPS技术即是特別应用在平面显示器的制造上。
传统的非晶硅材料(a-Si)的电子迁移率只有0.5 cm2/V‧S,而低温多晶硅材料(LTPS)的电子迁移率可达50~200 cm2/V‧S,因此与传统的非晶硅薄膜电晶体液晶显示器(a-Si TFT-LCD)相比,低溫多晶硅TFT-LCD具有更高解析度、反应速度快、亮度高(开口率aperture ratio高)等优点,同时可以将周边驱动电路同时制作在玻璃基板上,达到在玻璃上集成系统(SOG)的目标,所以能够节省空间和成本此外,LTPS技术又是发展主动式有机电致发光(AM-OLED)的技术平台,因此LTPS技术的发展受到了广泛的重视。
二、非晶硅(a-Si)与低温多晶硅(LTPS)的区别一般情况下低温多晶硅的制程温度应低于摄氏600℃,尤其对LTPS区别于a-Si制造的制造程序“激光退火”(laser anneal)要求更是如此。
与a-Si相比,LTPS的电子移动速度要比a-Si 快100倍,这个特点可以解释两个问题:首先,每个LTPS PANEL 都比a-Si PANEL反应速度快;其次,LTPS PANEL 外观尺寸都比a-Si PANEL小。
有机化学英语专业词汇

表面张力 surface tension
表面质量作用定律 surface mass action
law 波义尔定律 波义尔温度
Boyle law Boyle temperature
波义尔点 Boyle point 玻尔兹曼常数 Boltzmann constant
玻尔兹曼分布 Boltzmann distribution 玻尔兹曼公式 Boltzmann formula
coefficient of electromotive force 电动电势 zeta potential 电功 electric work 电化学 electrochemistry 电化学极化 electrochemical polarization 电极电势 electrode potential 电极反应 reactions on the electrode 电极种类 type of electrodes 电解池 electrolytic cell 电量计 coulometer 电流效率 current efficiency 电迁移 electro migration 电迁移率 electromobility 电渗 electroosmosis 电渗析 electrodialysis 电泳 electrophoresis
nucleophilic reaction 亲核反应
物理化学英语词汇
19203137 发表于: 2008-5-08 22:31 来源: 化 学吧 - 化学论坛 - 学术论坛
BET 公式 BET formula
DLVO 理论 DLVO theory HLB 法 hydrophile-lipophile balance
有机化学英语专业词汇 organic compounds 有机化合物
化工专业英语词汇

化工专业英语词汇reaction kinetics 反应动力学reactant 反应物purify 精制提纯recycle 循环回收uncon verted reacta n未转化的反应物chemical reactor transfer of heat, evaporation, crystallization 结晶drying 干燥scree ning筛选,浮选chemical reacti on 化学反应cracking of petroleum 石油裂解catalyst催化剂,reacti on zone 反应区con servati on of mass and en erg能量与质量守衡定律technical advance 技术进步efficiency improvement 效率提高reaction 反应separation 分离heat exchange 热交换reactive distillation 反应精馏capital expenditure 基建投资setup 装置capital outlay 费用,成本,基建投资yield 产率,收率reaction byproduct 反应副产物equilibrium constant 平衡常数waste 废物feedstock 进料,原料product 产物,产品perce nt conv ersi on百分比转化率ether 乙醚gasoli ne 汽油oxygenate content 氧含量catalyst 催化剂reactant 反应物inert 惰性物,不参加反应的物质reactive distillation 反应精馏energy saving 节约能量en ergy efficie ncy 能量效率heat-se nsitive material 热敏性物质pharmaceutical 希9药foodstuff 食品gas diffusivity气体扩散性,气体扩散系数gas adsorption 吸收;absorption:吸附specialty chemical特殊化学品,特种化学品batch间歇的;continuous:连续的micro-reactor微型反应器hydroge n and metha ne oxidati on氢气和甲烷氧化反应ethyle ne epoxidati on乙烯环氧化反应phosgene synthesis光气合成. commercial proportions 商业规模replication 复制sen sor传感器,探头separati on of solids 固体分离suspension 悬浮液porous medium多孔介质filtratio n 过滤medium介质filter 过滤器trap收集,捕集Buch nerfunnel 布氏漏斗Vacuum真空coni cal funnel 锥形漏斗filter paper 滤纟氏area面积filter cake 滤饼factor 因数,因子,系数,比例viscosity 黏度den sity 密度corrosive property 腐蚀性particle size 颗粒尺寸shape形状size distributi on 粒度分布pack ing characteristics 填充性质concen trati on 浓度filtrate 滤液feed liquor 进料液pretreatme nt 预处理late nt heat 潜热resista nee阻力surface layer 表面层filteri ng medium 过滤介质drop in pressure 压降filteri ng surface 过滤表面filter cake 滤饼cake filtratio n 饼层过滤deep bed filtrati on 深层过滤depth深度law定律net flow净流量con ducti on 传导convection 对流radiati on 辐射temperature gradie nt 温度梯度metallic solid 金属固体thermal con ducti on 热传导motio n of unbound electro ns 自由电子的运动electrical conductivity 导电性thermal conductivity 导热性poor con ductor of electricity 不良导电体tran sport of mome ntum 动量传递the random moti on of molecules 分子无规贝U运动brick wall 墙壁furnace火炉,燃烧器metal wall of a tube 金属管壁macroscopic particle 宏观的粒子control volume 控制体enthalpy 焓macroscopic phe nomenon 宏观现象forces of friction 摩擦力fluid mecha nics 流体力学flux (通量,流通量)of enthalpy焓通量eddy尾流,涡流turbulent flow 湍流n atural a nd forced con vecti on自然对流和强制对流buoya ncy force 浮力temperature gradie nt 温度梯度electromag netic wave 电磁波fused quartz熔化的石英reflect 反射,inflection:折射matte无光泽的,无光的temperature level 温度高低in ter-phase mass tran sfer界相际间质量传递rate of diffusi on 扩散速率acet one 丙酮dissolve 溶解ammon ia 氨ammoni a-air mixture 氨气-水混合物physical process 物理过程oxides of n itroge n 氮氧化物n itric acid 硝酸carb on dioxide 二氧化碳sodium hydroxide 氢氧化钠actualrate of absorpti on 实际吸收速率two-film theory 双膜理论concen trati on differe nee 浓度差in the vicinity of 在…附近,靠近.., 大约…,在…左右molecular diffusi on 分子扩散laminar sub-layer 层流底层resista nee 阻力,阻止boun dary layer 边界层Fick ' s Law 费克定律is proporti onal to 与…成比例concen trati on gradie nt 浓度梯度plate tower 板式塔in stallati on 装置feed进料bottom底部,塔底solve nt 溶剂top顶部,塔顶partial vaporizati on 咅E分汽化boili ng point 沸点equimolecular coun ter-diffusi on 等分子反向扩散ideal system 理想系统ratio of A to B A 与B 的比值with the result that :由于的缘故,鉴于的结果tray 塔板packed tower 填料塔bubble-cap tower 泡罩塔spray chamber 喷淋室maintenance expense 维修费foun dati on 基础tower shell 塔体pack ing material 填料pump 泵blower风机accessory heater 附属加热器cooler 冷去卩器heat excha nger 换热器solve nt-recovery system 溶剂回收系统operati ng cost 操作费用power动力circulati ng gas 循环气labor 劳动力steam蒸汽regen erate 再生cooli ng water 冷去卩水solve nt make-up 补充溶剂optimum最优的unabsorbed component 未吸收组分purity纯度volatility 挥发性vapor pressure蒸汽压liquid mixture液体混合物condense凝缩,冷凝bin ary distillatio n 双组分精馏multi-component distillation 多组分精馏stage-type distillation column 级板式精馏塔mount安装,固定conduit导流管), dow ncomej降液管gravity 重力weir溢流堰vapor-liquid contacting device 汽液接触装置valve tray浮阀塔板reboiler再沸器vaporization 汽化con de nsate冷凝液,凝缩液overhead vapor塔顶汽体condenser冷凝器i feed tray进料板base塔底,基础bottoms product 塔底产品conden sati on 冷凝stripping section汽提段,提馏段distillate sectio n 精馏段total condense全凝器distillate product塔顶馏出产品reflux回流thermodynamic equilibrium 热力学平衡solution 溶液fractional crystallizatio n 分步结晶solubility ,溶解度,溶解性soluble可溶解的solve nt 溶剂employ采纳,利用miscible可混合的,可溶的,可搅拌的mecha ni cal separati on 机械分离)liquid-liquid extract ion 液液萃取aromatic 芳香烃的paraffi n 石蜡,链烷烃lubricat ing oil _ 润滑油decompose分解,离解,还原,腐烂pen icilli n 青霉素streptomyci n (链霉素)precipitati on 沉淀,沉析ethyl alcohol 乙醇)extract 萃取液heat requireme nt 热负荷solute溶质extract phase 萃取相baffle-plate 折流挡板,缓冲挡板settli ng tank 沉降槽centrifuge 离心.离心机,离心分离emulsify ing age nt 孚L化剂den sity differe nee 密度差raffin ate 萃余液extract 萃取液dryi ng of Solids 固体干燥process material 过程物料(相对最终产品而言的)organic有机的,有机物的benzene 苯humidity 湿度moisture content 湿含量drying rate 干燥速率critical moisture content 临界湿湿含量falli ng-rate 降速con cave (凸的,凸面)or convex (凹的,凹面)approximate to :接近,趋近straight line :直线con sta nt-rate drying period 恒速干燥阶段convection drying 对流干燥drying gas 干燥气体falli ng-rate period 降速干燥阶段mean value平均值vacuum drying真空干燥discolor 变色,脱色sublime 升华freeze dryi ng 冷冻干燥adiabatic 绝热的,不传热的pressure gradie ntperpe ndicular to :与——垂直coun ter-curre nt 逆流per unit area 单位面积water-cooli ng tower 水冷塔sen sible heat (sen sible heat : 显热)water droplet 水珠,水滴qua ntitative relati on 定量关系thermal diffusi on 热扩散at right an gles to 与…成直角,与…垂直by virtue of 由于,根据,凭借于molecular tran sfer 分子传递balanee抵消,平衡drag forces 曳力a function of …的函数of the same order 具有同一数量级eddy diffusio n 涡流扩散is almost inv ersely proporti onal to 几乎与…成反比Reyno Ids nu mber 雷诺准数fully developed turbule nt flow 充分发展湍流coefficie nt 系数In prin ciple 从原理而言exothermic (放热的,endothermic 吸热的,adiabatic 绝热的)triple bond 三健,三价n itroge n oxides 氮氧化物compo und化合物conv ersi on 转化,转化率protein 蛋白质compress 压缩reacti on yield 反应产率reacti on speed 反应速度one-pass (单程)reactoren ergy in put 能量输入maximum最大的n ear toequilibrium 接近平衡output产出,输出,产量fertilizer 化肥urea尿素ammonium nitrate 硝酸铵ammon ium phosphate 磷酸铵ammonium sulfate 硫酸铵diammonium hydrogen phosphate 磷酸二氢铵ash纯碱pyridi ne 砒啶polymers聚合物nylon尼龙acrylics 丙烯酸树脂via经,由,通过,借助于hydrogen cyanide 氰化氢n itric acid 硝酸bulk explosive 集装炸药crude oil 原油n atural gas 天然气bitume n 沥青fossil fuel化石燃料seepage渗出物asphalt 沥青oil drilling 采油gasoli ne 汽油paint 涂料plastic 塑料syn thetic rubber 合成橡胶fiber纤维soap月肥皂clea nsing age n清洗剂wax石蜡explosive 炸药oil shale油页岩deposit沉积物aquatic pla nt水生植物sedime ntary rock 沉积岩san dst one砂岩siltst one 泥岩tar sand沥青石cha in-shaped 链状的metha ne 甲烷paraffin石蜡,烷烃rin g-shaped (环状的)hydrocarb onn aphthe ne环烷烃naphtha石脑油tarry柏油的,焦油的,焦油状的asphalte ne沥青油impurity 杂质pollutant污染物combusti on 燃烧capillarity毛细现象,毛细管力viscous resista nee占性阻力barrel桶(国际原油计量单位) tan ker油轮kerose ne 煤油heavy gas oil重瓦斯油reforming 重整crack ing 裂化octane nu mber of gasoli ne汽油辛烷值branched-chain (带支链的)materials scie nee 材料科学mechanical, thermal, chemical, electric, magnetic, and optical behavior. (机械性能、热学性能、化学性能、电学性能、磁性能、光学性能)Amalgam汞齐,水银;混合物,交叉solid state physics 固体物理学metallurgy 冶金学,冶金术magnet磁铁,有吸引力的人或物in sulati on 绝缘catalytic crack ing 催化裂化structural steels 结构钢computer microchip 计算机芯片Aerospace 航空Telecom mun icatio n 电信in formatio n process ing 信息处理nu clear power 核能en ergy conv ersi on 能量转化in ternal structure 内部结构defect structure 结构缺陷crystal flaw 晶体瑕疵vaca nt atomic site 原子空位dislocati on 错位precipitate 沉淀物semic on ductor 半导体mecha ni cal disturba nee 机械扰动ductility 延展性brittle ness 脆性spinning electr ons 旋转电子amorphous非定型的,非晶型的,非结晶的,玻璃状的;无一定目的的,乱七八糟chemical process safety 化工过程安全exotic chemistry 奇异化学hydrodynamic model 水力学模型two-phase flow 两相流dispers ion model 分散模型toxic 有毒的release释放,排放probability of failure 失效概率accide nt preve nti on 事故预防hard hat 安全帽safety shoe 防护鞋rules and regulati ons 规章制度loss preve nti on 损失预防hazard ide ntificati on 危害辩识,tech ni cal evaluati on 技术评估safety man ageme nt support 安全管理基础知识safety experie nee 安全经验tech ni cal compete nce 技术能力safety kno wledge 安全知识desig n engin eer 设计师cost engin eer 造价师process engin eeri ng 过程工程pla nt layout 工厂布局gen eral service facilities 公用工程pla nt locati on 工厂选址close teamwork 紧密的团队协作specialized group 专业组storage 仓库waste disposal 废物处理terminology 术语,词汇accountant 会计师,会计,出纟内fin al-proposal 决议tan gible return 有形回报Empirical model 经验模型process control (过程控制)first-principles基本原理,基本规则regression model 回归模型. operating condition 操作条件nonlinear-equation-solving technique 非线性方程求解技术process-simulation software packages 过程模拟软件包least-squares-regressi on 最小二乘法statistical technique 统计技术intensity强度,程度phenomenological model 现象模型model identification 模式识另Uneural network 神经网络a priori :先验的,既定的,不根据经验的,由原因推出结果的,演绎的,直觉的process data historia n:过程数据历史编撰师qualitative 定性的quantitative precision 定量的精确high-fidelity 高保真的computati on ally inten sive 计算量大的mathematical expressi on steady-state model 稳态模型bioe ngin eeri ng 生物工程artificial 人工的heari ng aid 助听器artificial limb 假肢supportive or substitute orga n 辅助或替代器官biosy nthesis 生物合成life scie ntist 生命科学家agricultural engin eer 农艺师ferme ntatio n 发酵civil engin eer 土木工程师san itati on 卫生physiologists 生理学criteria 扌旨标human medicine 人体医学medical electr onics 医疗电子medical in strume ntatio n 医疗器械blood-flow dyn amics 血液流动动力学prosthetics 假肢器官学biomechanics生物力学surge on外科医生replaceme nt orga n 器官移植physiologist 生理学家cou nterpart 对应物,配对物psychology 心理学self-taught 自学barrier 障碍物medical engin eeri ng 医学工程,医疗工程health care 保健diag no stic applicati on of computers 计算机诊断agricultural engin eeri ng 农业工程biological producti on 生物制品生产bion ics (仿生学)huma n-factors engin eeri ng 人类与环境工程en vir onmen tal health engin eeri ng 环境健康工程en viro nmen tally benign processi ng 环境友好加工commodity or specialty 通用商品或特殊化学品styre ne苯乙烯ibuprofe n异丁苯丙酸the Chemical Manu facturers Association化工生产协会as a whole整体而言emission释放物,排放物voluntary自愿的,无偿的,义务的;有意的,随意的;民办的in the abse nee of 无---存在deactivate 失活bulk chemical大宗化工产品Fine chemical 精纟田化工Pharmaceutical 制药segme nt段,片,区间,部门,部分;弓形,圆缺;分割,切断tonn age吨位,吨数,吨产量inorganic salt 无机盐hydroquinone 对苯二酚dem on strate论证,证明,证实;说明,表明,显示forefro nt最前线,最前沿Lewis acid不可再生的路易斯酸an hydrous无水的phaseout消肖除HF alkylation氰氟酸烷基化catalytic oxidation 催化氧化gover nmen tal regulatio n 政府规定pharmaceutical in termediate药物中间体stereoselective立体选择性的ket one 酮fun cti onal group 官能团detrimental 有害的chlorofluorocarb on二氯二氟化碳,氟里昂carb on tetrachloride 四氯化碳straightforward 简单明了的coordi nati ng liga nd配合体,向心配合体kilogram 千克thermal stability 热稳定性devastate破坏,蹂躏outline描绘,勾勒membra ne tech no logy 膜技术product ion line 生产线dairy 牛奶water purificati on 水净化lifetime 寿命membra ne module膜组件durability 耐久性,寿命,使用期限,强度chemical additive 添加剂en d-of-pipe soluti on 最终方案closed system 圭寸闭系统substitute 取代,替代techni cal challe nge 技术挑战,技术困难wastewater treatme nt 污水处理fouli ng污垢,发泡surface treatme nt 表面处理applied Chemistry 应用化学nomen clature of chemical compo und 化学化合物的命名法descriptive 描述性的prefix 前缀alkane烷烃family 族carb on skelet on 碳骨架chain 链Latin or Greek stem 拉丁或者希腊词根suffix后缀con stitute 取代物,取代基homologous series 同系物branched chain 支链烷烃pare nt 母链,主链derivative 衍生物substitue nt 取代基locant 位次,位标replicat ing prefix 重复前缀词Gas and Liquid Chromatography 气相色谱与液相色谱an alytical chemistry 分析化学moving gas stream 移动的气流heats of solutio n and vaporizati on 溶解热和汽化热activity coefficie nt 活度系数counteract 抵消milliliter 毫升esse ntial oil 香精油test mixture 测试混合物sample样品helium 氦argon 氩carrier 载体injectio n 注射stati onary nonv olatile phase 静止的不挥发相detector检测器fraction collector 馏分收集器colu mnar liquid chromatography 柱状液相色谱仪rete nti on volume 保留体积rete nti on times 保留时间high-performa nee 高性能mobile phase 移动相high-efficie ncy 高效的analyte分析物pla ne chromatography 薄层色谱capillary actio n 毛细管作用assay分析化验fluoresce nee 荧光色,荧光retardati on factor 保留因子,延迟因子。
化学专业英语试卷B答案

化学专业英语试卷B答案文档编制序号:[KKIDT-LLE0828-LLETD298-POI08]2013—2014学年度第一学期应用化学专业《专业英语》课程试卷(A)注意事项:1. 考生务必将自己姓名、学号、专业名称写在指定位置;2. 密封线和装订线内不准答题。
一、词汇填空(写出下列每个词汇对应的英汉单词)(共20小题,每空1分,共20分)1、分子( molecule )2、物理性质( physical property)3、硬度( hardness )4、电解质( electrolyte )5、熔点( melting point )6、沸点( boiling point )7、离子键( ionic bond or electrovalent bond )8、晶体( crystal )9、硅( silicon )10、钾( potassium )11、溶解度( solubility )12、构型( configuration )13、挥发性 ( volitility)14、正电荷( positive charge )15、phosphorus(磷)16、alcohol (乙醇)17、acetone (丙酮)18、base (碱)19、acid (酸)20、ether (乙醚)二、给下列无机化合物的英语名称(共10小题, 每小题2分,共20分)1、NaCN Sodium cyanide2、Ba(OH)2 Barium hydroxide3、KMnO4 Potassium permanganate4、H2SO4 Sulfuric acid5、ZnSO4 zinc sulfate or zinc sulphate6、FeS Iron (II) sulfide or Ferrous sulfide7、H3PO4 phosphoric acid8、H2SO3 Sulfurous acid9、HClO4 Perchloric acid10、FeCl3 iron (III) chloride or ferric chloride二、给下列有机化合物的英语名称(共5小题, 每小题4分,共20分)1.甲乙醚 ethyl methyl ether2.对甲基苯酚 4-methyl phenol3.苯乙烯 styrene4.CH3CH=C(CH2CH3) CH2 OH 2-ethyl-2-buten-1-ol5.(CH3)3CCH2CH2OH 4,4-dimethyl-1-butanol or 4,4-dimethyl butanol三、英译汉(共10小题, 每小题4分,共40分)1、Carbon-sodium and carbon-potassium bonds are largely ionic in character;carbon-lead, carbon-tin, carbon-thallium and carbon-mercury bonds are essentially covalent.碳-钠键和碳-钾键有较大的离子性,碳-铅键,碳-锡键,碳-铊键和碳-汞键基本上属于共价键。
反溶剂诱导结晶法英文

反溶剂诱导结晶法英文Antisolvent-Induced Crystallization: A Comprehensive Overview.Introduction:Antisolvent-induced crystallization (AIC) is a versatile technique widely employed in the pharmaceutical, chemical, and food industries to produce crystalline materials with tailored properties. This method involves introducing an antisolvent into a supersaturated solution of the target compound, triggering the nucleation and growth of crystals. AIC offers numerous advantages over other crystallization techniques, including enhanced control over crystal size, shape, and purity.Mechanism of AIC:The antisolvent, typically a non-solvent or a solvent with low solubility for the target compound, plays acrucial role in the AIC process. When added to a supersaturated solution, the antisolvent reduces the solubility of the solute, leading to the formation of a metastable zone. Within this zone, small crystal nuclei form and begin to grow. The antisolvent concentration, temperature, and solution composition influence the nucleation and growth kinetics, ultimately determining the characteristics of the final crystals.Advantages of AIC:AIC offers several advantages over conventional crystallization methods, including:Control over Crystal Morphology: AIC allows for the manipulation of crystal size, shape, and surface structure by varying process parameters such as antisolvent type, concentration, and temperature.Enhanced Purity: The antisolvent acts as a washing agent, removing impurities from the growing crystals and improving their purity.Scalability: AIC is a scalable process suitable for both small-scale laboratory experiments and large-scale industrial production.Energy Efficiency: Compared to other crystallization techniques, AIC often requires lower energy input due to reduced evaporation and milder operating conditions.Applications of AIC:AIC finds applications in a wide range of industries, including:Pharmaceuticals:Production of active pharmaceutical ingredients (APIs) with controlled bioavailability and dissolution rates.Development of drug delivery systems with specific release profiles.Chemicals:Synthesis of fine chemicals and specialty materials.Crystallization of inorganic compounds for electronic and optical applications.Food:Production of food additives and flavors.Crystallization of sugars and sweeteners.Process Parameters:The success of AIC depends on the careful optimization of several process parameters, including:Antisolvent Selection: The choice of antisolvent is crucial and depends on its solubility characteristics, miscibility with the solvent, and ability to promote nucleation.Antisolvent Concentration: The concentration of the antisolvent determines the degree of supersaturation andthe nucleation rate.Temperature: Temperature plays a significant role in crystal growth and morphology. Lower temperatures generally favor smaller crystal sizes.Mixing: Efficient mixing is essential for uniform distribution of the antisolvent and to preventagglomeration of crystals.Crystal Seeding: Seeding with pre-formed crystals can control nucleation and promote the growth of specificcrystal faces.Equipment for AIC:AIC can be carried out using various types of equipment, such as:Batch Crystallizers: Simple vessels where the antisolvent is added to a supersaturated solution.Continuous Crystallizers: Allow for continuous operation and better control over crystal growth.Fluidized Bed Crystallizers: Suspend crystals in a fluidized bed, facilitating efficient mass transfer and crystal growth.Challenges and Considerations:Despite its versatility, AIC also faces some challenges:Crystal Agglomeration: High supersaturation or insufficient mixing can lead to agglomeration, resulting in non-uniform crystal properties.Nucleation Control: Controlling the nucleation rate is crucial to obtain the desired crystal size and distribution.Solvent Selection: The choice of solvent andantisolvent combination must consider their solubility and stability under process conditions.Conclusion:Antisolvent-induced crystallization is a powerful technique that offers significant advantages for the production of crystalline materials with tailored properties. Its versatility, scalability, and ability to control crystal morphology and purity make AIC a valuable tool for various industries, including pharmaceuticals, chemicals, and food. Continued research and development in AIC aim to further optimize the process and expand its applications.。
电化学书籍

学标准电极电位数据手册 《Surface scie nee studies of model fue cell electrocatalysts 》 《标准电极电势》 《Fuel Cells - Green Power 》Handbook of Batteries 燃料电池 《Fuel cell systemsexpla ined 》 《Electrochemistry in light water reactors 》 《Build your own Fuel Cells 》Fuel cell Handbook 第 7 版《经典专著 化学电源》《Battery Separators 〉电池用铝合金阳极材料研Fuel_Cell_Electronics_Packaging EIS 在电池研发中的应用 化学与能源 一本燃料电池的书籍----教你制做燃料电 池碳材料电化学电容器综述 微生物燃料电池 第一本书(Logan , 2008)研究表征和评价化学电源的传统电化学技术Fuel Cell Tech no logy PEM Fuel《电化学测试技术》 《Impeda nee Spectroscopy, Theory Experime ntand Applications 》 《Techniques and Mechanisms in Electrochemistry) 《实验电化学》 《电化学阻抗谱导论》 标准电极电位数据手册 电 化学阻抗谱-浙江大字-张鉴清 《Electrochemistry principles, methods, and applications 》《交流阻抗综述》电导率的测定资料专著实验电化学原理及应用 08年新书,Electrochemical Impedanee Spectroscopy 《标准电极电势》electrochemical instruments introduction电极 的维护和保养 极化曲线的原理及应用 天津大学电化学测试方法 PPT Basics of Electrochemical Impeda nee Spectroscopy Ag/AgCl 软件极化曲线拟合软件 循环伏安法模拟软件 电化学测定方法.腾岛.昭.等著.陈震等译 voltammetry and polarography (PPT form) 电化学仪器(美国)其他 电池 究的新进展专著Cells modeling solid oxide fuel cell动力电池论坛参比电极的制备zview 阻抗使用说明(含交流阻抗)不同型号CHI工作站官方资料电化学阻抗谱EIS简介.电化学暂态研究技l.ppt电化学测试技术电化学阻抗谱导论电化学拉曼《金属腐蚀与防护》《腐蚀电化学》赵世伟标准电极电位数据手册金《Electrochemistry prin ciples, methods, and applicati onS〉《Corrosi on 属Dictio nary》《Chemical Processes on Solid Surface》电导率的测腐定资料《标准电极电势》仪器分析录像片[14]电化学系统金属电化学保护参比电极阴极保护简明手册(德一贝克曼)金属腐蚀学原理(高校用书)腐蚀电化学蚀分析实验金属腐蚀电化学测试技术简介Ag/AgCI参比电极的制备电极的维护和保养材料选择不当造成的腐蚀破坏案例ASTMG5-94(1999)e1作静电位标记和动电位阳与极极化测量的基准测试方法厦门大学金属防腐课件腐蚀电化学分析腐蚀与防护全书--热喷涂腐蚀与防护全书--肖纪美--腐蚀总论——材料的腐蚀及其控制方法腐蚀防与防护全书--周静好--防锈技术腐蚀与防护全书--自然环境的腐蚀与防护腐蚀与防护全书--工业冷却水系统中金属的腐蚀与防护腐蚀与防护全书--肖纪美--应力作用护下的金属腐蚀.pdf腐蚀与防护全书--腐蚀试验的统计分析方法--曹楚南腐蚀与防护全书-腐蚀电化学研究方法腐蚀与防护全书--曹楚南--腐蚀电化学腐蚀与防护全书-不锈钢(王正樵编著化学工业出版社1991年版)NACE standard RP0775-05 NACE 阴极保护培训课程教案金属腐蚀电化学热力学一一电位一PH图及其应用。
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a r X i v :c o n d -m a t /0401194v 1 [c o n d -m a t .s o f t ] 12 J a n 2004Induced Crystallization of Polyelectrolyte-Surfactant Complexes at the Gas-WaterInterfaceD.Vaknin 1,S.Dahlke 1,A.Travesset 1,G.Nizri 2,and S.Magdassi 21Ames Laboratory and Department of Physics and Astronomy Iowa State University,Ames,Iowa 500112Institute of Applied Chemistry,Hebrew University of Jerusalem,Jerusalem,Israel 91904(Dated:February 2,2008)Synchrotron-X-ray and surface tension studies of a strong polyelectrolyte (PE)in the semi-dilute regime (∼0.1M monomer-charges)with varying surfactant concentrations show that minute surfac-tant concentrations induce the formation of a PE-surfactant complex at the gas/solution interface.X-ray reflectivity and grazing angle X-ray diffraction (GIXD)provide detailed information of the top most layer,where it is found that the surfactant forms a two-dimensional liquid-like monolayer,with a noticeable disruption of the structure of water at the interface.With the addition of salt (NaCl)columnar-crystals with distorted-hexagonal symmetry are formed.PACS numbers:82.70.Uv,82.35.Rs,81.07.NbThere has been a growing interest in the phase-behavior,aggregation and precipitation of polymer-surfactant mixtures,in particular of ionic surfactants and oppositely charged flexible polyelectrolytes (PEs)[1,2,3,4,5,6],or semi-flexible PEs such as DNA[7]or actin[8].In addition to the fundamental interest in the principles governing phase-behavior,aggregation and precipitation of polymer-surfactant mixtures,understanding the be-havior of these complex systems is crucial for technologi-cal applications concerning detergents,paints,cosmetics,and in DNA transfection (i.e.,the incorporation of exoge-nous DNA into a cell)[9,10,11]and others.Some important aspects regarding the formation of flexible polyelectrolyte-surfactant complexes present ex-citing challenges,both experimentally and theoretically.The role played by the interface in the growth and nu-cleation of these complexes,for example,is to a large extent unknown,although neutron and X-ray reflectivity studies provided invaluable insight into the density pro-file across the interface of the PE/surfactant solutions[12,13,14,15].The role salt concentration has on aggre-gation and precipitation of PE-and PE-surfactant so-lutions is to a large extent an open problem[6].There are recent suggestion that at high salt concentrations,macromolecules may be over-screened by counterions,ef-fectively reversing their charge[16,17,18],and that same-charge macromolecules may attract each other in several density-regimes[19].Previous studies on surfactant-polyelectrolyte com-plexes have focused on bulk properties and the self-assembly as driven by surfactant concentration.The present study focuses on interfacial behavior,in partic-ular on the role played by the gas-water interface in the precipitation process,and how the self-assembly may be controlled by the weakening of the electrostatic inter-actions (salt concentration).Herein,we report surface sensitive synchrotron X-ray diffraction studies,both re-flectivity and diffraction at grazing angle of incidence (GIXD),on a model system consisting of sodium dodecyl sulfate (SDS)and Poly-diallyldimethylammonium chlo-ride (PDAC)(molecules are shown in Fig.1).SodiumFIG.1:Chemical structure of Sodium dodecyl sulfate (SDS)and Poly-diallyldimethylammonium chloride,(PDAC),used in this study.Surface tension as a function of SDS concentra-tion in water and,0.1M NaCl and 2%PDAC both at 0.1M salt and without salt.dodecyl sulfate (SDS)(C12H27O4SNa;MW =290288.4)and Poly-diallyldimethylammonium chloride,(PDAC)(MW =100,000-200,000;see Fig.1)[C8H16NCl]n;n=685-1370;obtained from Sigma (Materials have cat-alog numbers L-4509and 40,901-4in the 2002Sigma-Aldrich catalog;shown in Fig.1).PDAC at 2%(by weight;concentration of PE charges was 0.137M)in pure water (Milli-Q apparatus Millipore Corp.,or Bedford,MA;resistivity,18.2MΩcm)and in 0.1M NaCl was used in all experiments.After stirring for 10-20minutes,so-lutions were poured into a temperature-controlled Teflon Langmuir trough which was maintained at 19o C and en-closed in a gas tight aluminum container,where surface-tension was measured with a microbalance using a Wil-helmy filter-paper-plate.The surface tension of the var-ious solutions was measured as a function of time after pouring into the trough,or after compression or decom-2pression of the surface with the Langmuir barrier,and the equilibrium value was averaged after a 30-60min relax-ation (in all cases,the time dependent pressure showed an exponential behavior,exp −t/τ;τ≈2−5min.).Surface sensitive X-ray diffraction studies of the struc-ture of free gas/solution interface were conducted on the Ames Laboratory Liquid Surface Diffractometer at the AdvancedPhoton Source (APS),beam-line 6ID-B (de-scribed elsewhere[21].The highly monochromatic beam (8keV and 16.2keV;λ=0.765334˚A and λ=1.5498˚A ),selected by a downstream Si double crystal monochro-mator,is deflected onto the liquid surface to a desired angle of incidence with respect to the liquid surface by a second monochromator [Ge(111)and Ge(220)crystals at 8.0and 16.2keV respectively]located on the diffrac-tometer.Specular X-ray reflectivity experiments yield the electron density (ED)profile across the interface,and can be related to molecular arrangements in the film.The ED profile across the interface is extracted by refining a slab-model that best fit the measured re-flectivity by non-linear least-squares method.The re-flectivity from the slab model at a momentum transferQ z ,is calculated by R (Q z )=R 0(Q z )e −(Q z σ)2where,R 0(Q z )is the reflectivity from step-like functions calcu-lated by the recursive dynamical method,and σis an ef-fective surface roughness,accounting for the smearing of all interfaces due to thermal capillary waves and surface inhomogeneities[21,22].The GIXD measurements are conducted with an evanescent incident beam that grazes the surface an angle slightly below the critical-angle for total-reflection from the surface,yielding the in-plane or-dering within the penetration depth of the X-ray beam.FIG.2:A)Reflectivity normalized to R F (R F is the reflec-tivity from ideally flat water interface)for (a )10−4M SDS in water (b )10−4M SDS 0.1M NaCl (c )2%wt PDAC in pure wa-ter (d )10−4MSDS in 2%wt PDAC solution (e )10−4MSDS 2%wt PDAC after the addition of 0.1M NaCl.B)Electron density profiles used to generate the fitted reflectivity (solid lines in A),the step-like functions (box-model)are generated assuming no surface roughness (σ=0).Surface tension versus SDS concentration in salt so-lution (0.1M NaCl)and in pure water for comparison are shown in Fig.1,and similarly for 2%wt PDAC so-lutions in pure water and in 0.1M NaCl solution.The reduction in surface tension indicates the adsorption of surfactants at the surface,as inferred from the Gibbs absorption equation[11].The onset for the reduction in surface tension at 0.1M NaCl occurs at SDS concentra-tions that are two orders of magnitude lower than those of SDS in pure water[28].Likewise,in the presence of the polyelectrolyte,Figure 1shows that the lowering of surface tension occurs at even lower SDS concentra-tions,suggestive of the formation of highly hydrophobic surfactant-polyelectrolyte complexes[10,20].Within ex-perimental error,our measurements in Fig.1show that surface-tension as function of SDS concentration with 2%wt PDAC is not affected by the addition of simple salt (NaCl 0.1M)to water.The lowering of surface tension by SDS to about 33mN/m suggests that the main con-stituents of the top-most layer are similar with and with-out NaCl.X-ray reflectivity and GIXD studies of PDAC-solutions surfaces were conducted at various SDS concentrations (with and without 0.1M NaCl).Figure 2shows a se-quence of normalized reflectivities,R/R F (where R F is the calculated reflectivity of an ideally flat water inter-face)for a typical SDS concentration,(10−4M)in pure water and in PDAC solutions,and after adding 0.1M NaCl to the same solutions.At SDS concentrations greater than 10−4M (in pure water),the reflectivity [Fig.2(A)]is similar to that of a pure water surface,although with a surface roughness σ=3.5˚A ,significantly larger than that measured for a water surface under similar con-ditions and with the same instrumental setup (σW =2.4˚A ).The enhanced surface roughness is evidence for the presence of a dilute inhomogeneous SDS-film in a gas phase at the air/water interface.The addition of NaCl to the SDS solution modifies the reflectivity,and gives rise to a minimum due to the formation of a more homo-geneous film,at Q z ≈0.53˚A −1.The detailed analysis in terms of a two-box model[22],yields the ED profile shown in Fig.2(B)with a total film-thickness d total =12˚A compared to the estimated stretched SDS molecule d st =19.3˚A .This implies an average molecular tilt-angle,t =51.5degrees with respect to the surface normal [t =acos(d total /d st )].Additional,reflectivity studies as a function of SDS concentrations (with and without NaCl)show systematic increase of total film-thickness,up to ≈18˚A ,with the increase of SDS concentration[24].Assum-ing an average SDS molecular-area A ,the number of elec-trons per SDS molecule (including adsorbed molecules -H 2O or ions)N ref is given by,N ref =N SDS +N other =Aρ(z )dz ,(1)where N SDS =148electrons and N other is the number ofelectrons due to integrated water molecules or ions that are inseparable from the top most ing Eq.(1),and the ED profiles,the lower limit for the SDS molecu-FIG.3:A)In-plane diffraction(GIXD)scans of pure wa-ter,and2%wt PDAC2x10−5M SDS and0.1M NaCl as indi-cated and the difference between the two scans.B)Similar differences between solutions of2%wt PDAC a)0M SDS b) 2x10−5M SDS c)2x10−4M SDS.The disruption of the struc-ture of water at the interface is apparent.lar area(i.e.,N other=0),to be A min≈35.6˚A2,whereas assuming two bound water molecules per SDS molecule yields A≈40.4˚A2,inagreement with values extractedfrom surface tension isotherms[23].The two-box model shown in Fig.2(B)reflects the molecular ED,with a elec-tron rich sulfate head-group compared to the low density hydrocarbon chains.The ED of the slab associated withthe hydrocarbon chains(0.27e/˚A3)is much lower than that of closely-packed hydrocarbon chains≈0.34˚A3inalkanes,for instance,indicating that the SDS molecules are not closely packed,most likely in a2D liquid-likestate.The reflectivity from a2%PDAC in water(with no SDS)is shown in Fig.2to demonstrate that the effectof the PE on the surface even at this high concentration is negligible showing a small step of lower density at theinterface.The addition of SDS to the2%PDAC solutionbrings the minimum in R/R F to Q z≈0.38˚A−1,demon-strating thefilm is thicker(d total=22.46˚A)and moreorganized than that of SDS in water or in salt solution. The thickness of the slab associated with the head-groupregion(d head≈11˚A)is evidence that thefilm consists of PDAC-SDS complex at the interface.The thickness andthe ED of the two slabs at the air interface,associated with the hydrocarbon tails that are not loosely packed as in a liquid state.The most dramatic effect in the reflec-tivity is observed with the addition of salt to the PDAC-SDS solution,where Bragg reflections are superimposed on the reflectivity at Q I z≈0.165˚A−1and at Q II z≈0.345˚A−1.These two peaks,as will be shown below are the first and second order Bragg reflections from hexagonal structure that is normal to the scattering plane(in reflec-tivity configuration).Similar neutron reflectivity studies of the dilute PDAC solutions with SDS and NaCl are consistent with the presentfindings[15].The picture of a liquid-likefilm with disordered SDSat the gas-water interface is corroborated by our GIXD studies.Figure3(A)shows the diffraction patterns of pure water surface[25],and that of the PDAC-SDS FIG.4:A)A scan along Q x of(10)peak at Q z=0.098˚A−1.B)A rod scan along the same peak(logarithmic scale)also revealing the(11)peak.C)The observed peaks in the Q x,Q z plane D)A schematic illustration of the suggested model structure with the unit oblique cell.The long axes of cylindri-cal micelles are parallel to the liquid surface with each layer separated by the polymer.(2×10−4M).The difference between the two patterns is shown in Fig.3at two SDS concentrations.The broad peak in the diffraction at Q r=1.34˚A−1of an average4.69˚A d-spacing is due to scattering from2D-liquid hydrocarbon chains(compared to typical d-spacing for hexagonally ordered hydrocarbon chains is 4.2˚A). The linewidth of the peak,∆Q=0.31˚A−1with average correlation-lengthξ≈20˚A,is further evidence for the 2D disordered chains[26].At small angles,the GIXD reveals several discrete Bragg reflections,evidence of a diffraction pattern from crystals that are highly oriented with respect to the water surface.In fact,these reflections are found to be related to those observed in the reflectivity.As shown in Fig. 4,these peaks are sharp characteristic of3D ordering, with no rod-like scattering typical of quasi-2D system. The positions of the peaks observed and their layout as shown in Fig.4(C)are consistent with a slightly distorted hexagonal structure,as depicted in Fig.4(D)with a= 40.3±0.5˚A,b=44.6±0.6˚A,andγ=121±1deg. The peaks observed are similar although not the same as those observed by Chu and co-workers[1,2]in small angle X-ray scattering experiments from related systems. Based on the anisotropy observed,we propose a simple structure of stacked cylindrical micelles,with their long axis parallel to the water-surface,where each layer is sep-arated by a layer of the PEs,as depicted in Fig.4,form-ing a2D polycrystalline system with preferred orienta-tion with respect to the surface.The distorted hexagonal diffraction pattern shows the growth is anisotropic,and implies the interface plays an important role in initiating complexation(aggregation)processes.Another impor-tant result is the effect the addition of salt(NaCl)has onFIG.5:A)Schematic pathways of complexation and sub-sequent crystallization A)Negligible surfactant concentrationthe PE is repelled from the interface.B)Below the CACa PE surfactant is formed at the interface.C)Beyond theCAC micellization occurs D)The addition of salt transformsmicelles to cylindrical shape and crystallizes them.promoting PE/surfactant crystallization.Our heuristicinterpretation of the aggregation and subsequent crys-tallization is depicted in Fig5.The PE,with no sur-factants or salt added,is highly soluble in water and isrepelled from the air/water interface due to the discon-tinuity in dielectric constant[27].Minute increase in sur-factant concentration lowers surface tension(see Fig.1)and initiates the micellization.We argue that micelle-formation is initiated at the interface as the ideal linearbulk-separation among surfactants is≈250˚A(surfac-tant concentrations(≈10−4M).The addition of NaCl tothe PE/surfactant solution screens electrostatic interac-tions,leading to cylindrical-micelles[28].Absorption ofPE to micelles is then expected to be enhanced by themechanism of counterion release[29],and we speculatethat micelles will then self-attract by a similar correla-tion mechanism as has been recently observed in multi-valent ions[30],eventually condensing into an hexagonal(columnar)crystal,and thus growing crystals from theinterface.In summary,we have shown the fundamental roleplayed by the interface in nucleating PE surfactant com-plexes,and how crystallization may be induced by saltconcentration at tiny surfactant concentrations.Ourstudy also shows the capabilities available by X-ray scat-tering techniques.We wish to thank M.Muthukumar and D.S.Robinsonfor helpful discussions.The MUCAT sector at the APSis supported by the U.S.DOE Basic Energy Sciences,Of-fice of Science,through Ames Laboratory under contractno.W-7405-Eng-82.Measurements were supported bythe U.S.DOE,Basic Energy Sciences,Office of Science,under contract no.W-31-109-Eng-38.[1]B.Chu,et al.,Macromolecules28,8447(1995).[2]F.Yeh,et al.,J.Am.Chem.Soc.118,6615(1996).[3]P.Hanson,,Langmuir14,4059(1998).[4]K.Kogej,et al.,Langmuir173175(2001).[5]P.Hanson,Langmuir17,4167(2001).[6]M.J.Leonard,and H.H.Strey,Macromolecules36,9549(2003).[7]I.Koltover,et al.,Science281,78(1998),and Strey etal.,Curr.Op.Struc.Bio.8,309(1998).[8]G.C.L.Wong and et al.,Science288,2035(2000).[9]M.J.Rosen,Surfactants and Interfacial Phenomena;Wi-ley Sons,New York,(1978).[10]E.D.Goddard,and K.P.Ananthapadmanabham Edi-tors;Interactions of Surfactants with Polymers and Pro-teins,CRC Press,Boca Raton,(1993).[11]P.C.Hiemenz and R.Rajagopalan,Principles of colloidand surface chemistry,Marcel Dekker Inc.,New York,(1997).[12]C.Stubenrauch,et al.,Langmuir16,3206(2000).[13]J.R.Lu,et al.,J.Colloid and Interface Sci.174,441(1995).[14]H.Yim,et al.,Macromolecules33,6126(2000).[15]E.Staples,et al.,Langmuir(2002).[16]J.F.Joanny,Eur.Phys.J.B9,117(1999).[17]T.T.Nguyen,A.Yu.Grosberg,and B.I.Shklovskii,J.Chem.Phys.113,1110(2000).[18]A.D.Dobrynin, A.Deshkovski,and M.Rubinstein,Macromolecules34,3421(2001.[19]W.M.Gelbart,R.F.Bruinsma,P.A.Pincus,V.A.Parsegian,Physics Today53,38(2000).[20]T.Wallin,and P.Linse,Langmuir14,2940(1998);C.Von Ferber and H.Lowen,J.Phys.Chem.118,10774(2003).[21]D.Vaknin,in Methods in Materials Research,edited byE.N.Kaufmann,et al.,p.10d.2.1(Wiley,New York,2001).[22]J.Als-Nielsen,and K.Kjaer,Proc.NATO ASI Ser.B,211(1989).[23]A.J.Prosser,and E.I.Franses,Collo.Surf.A178,1(2001).[24]D.Vaknin(unpublished results).[25]For bulk water thefirst peak in the structure factor isobserved at Q r 2.0˚A−1compared to the1.96˚A−1for water surface.The penetration depth of the incidentevanescent X-ray is smaller than100˚A),thereby probingthe top most water layers with some contribution frombulk liquid.The shift in the position of thefirst peakindicates a slightly larger O-O d-spacing at the interface.[26]Thefirst and strongest peak,in the structure factor of liq-uid alkanes is found at the1.3-1.4˚A−1;see Habenschuss,A.;Narten,A.H.J.Chem.Phys.92,5692(1990).[27]W.K.H.Panofsky,and M.Philipis,Classical Electricityand Magnetism,Addison-Wesley,Reading,MA(1972).[28]C.Tanford,The hydrophobic effect:Formation of mi-celles and biological membranes John Wiley and Sons,(1980).[29]R.Bruinsma,Eur.Phys.J.B4,75(1998).[30]Angelini et Al.,PNAS100,8634(2003).[31]J.Israelachvili,Intermolecular and surface forces,Aca-demic Press,London,(2000).。