材料热力学习题集
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材料热力学习题1、阐述焓H 、内能U 、自由能F 以及吉布斯自由能G 之间的关系,并推导麦克斯韦方程之一:T P PST V )()(∂∂-=∂∂。
答: H=U+PV F=U-TS G=H-TS U=Q+W dU=δQ+δWdS=δQ/T, δW=-PdV dU=TdS-PdVdH=dU+PdV+VdP=TdS+VdP dG=VdP-SdTdG 是全微分,因此有:TP P TP ST V ,PT G T P G ,T V P G T P T G P ST G P T P G )()()()()()(2222∂∂-=∂∂∂∂∂=∂∂∂∂∂=∂∂∂∂=∂∂∂∂∂-=∂∂∂∂=∂∂∂因此有又而2、论述: 试绘出由吉布斯自由能—成分曲线建立匀晶相图的过程示意图,并加以说明。
(假设两固相具有相同的晶体结构)。
由吉布斯自由能曲线建立匀晶相图如上所示,在高温T 1时,对于所有成分,液相的自由能都是最低;在温度T 2时,α和L 两相的自由能曲线有公切线,切点成分为x1和x2,由温度T 2线和两个切点成分在相图上可以确定一个液相线点和一个固相线点。
根据不同温度下自由能成分曲线,可以确定多个液相线点和固相线点,这些点连接起来就成为了液相线和固相线。
在低温T 3,固相α的自由能总是比液相L 的低,因此意味着此时相图上进入了固相区间。
HPV UGTSTS FPV3、论述:通过吉布斯自由能成分曲线阐述脱溶分解中由母相析出第二相的过程。
第二相析出:从过饱和固溶体α中(x0)析出另一种结构的β相(xβ),母相的浓度变为xα. 即:α→β+ α1α→β+ α1 的相变驱动力ΔGm的计算为ΔGm=Gm(D)-Gm(C),即图b中的CD段。
图b中EF是指在母相中出现较大为xβ的成分起伏时,由母相α析出第二相的驱动力。
4、根据Boltzman方程S=kLnW,计算高熵合金FeCoNiCuCrAl和FeCoNiCuCrAlTi0.1(即FeCoNiCuCrAl各为1mol,Ti为0.1mol)的摩尔组态熵。
材料热力学与动力学(复习资料)一、 概念•热力学基本概念和基本定律1. 热0:一切互为热平衡的物体,具有相同的温度。
2. 热1: - 焓:恒压体系→吸收的热量=焓的增加→焓变等于等压热效应 - 变化的可能性→过程的方向;限度→平衡3. 热2:任何不受外界影响体系总是单向地趋向平衡状态→熵+自发过程+可逆过程→隔绝体系的熵值在平衡时为最大→熵增原理(隔离体系)→Gibbs 自由能:dG<0,自发进行(同T ,p : )4. 热3:- (H.W.Nernst ,1906): - (M .Plank ,1912):假定在绝对零度时,任何纯物质凝聚态的熵值为零S*(0K)=0 - (Lewis ,Gibson ,1920):对于过冷溶体或内部运动未达平衡的纯物质,即使在0K 时,其熵值也不等于零,而是存在所谓的“残余熵” - Final :在OK 时任何纯物质的完美晶体的熵值等于零• 单组元材料热力学1. 纯金属固态相变的体积效应- 除非特殊理由,所有纯金属加热固态相变都是由密排结构(fcc )向疏排结构(bcc )的转变→加热过程发生的相变要引起体积的膨胀→BCC 结构相在高温将变得比其他典型金属结构(如FCC 和HCP 结构)更稳定(除了Fe )- 热力学解释1→G :温度相同时,疏排结构的熵大于密排结构;疏排结构的焓大于密排结构→低温:H ;高温:TS - 热力学解释2→ Maxwell 方程: - α-Fe →γ-Fe :磁性转变自由能- Richard 规则:熔化熵-Trouton 规则:蒸发熵 (估算熔沸点)2. 晶体中平衡状态下的热空位- 实际金属晶体中空位随着温度升高浓度增加,大多数常用金属(Cu 、Al 、Pb 、W 、Ag …)在接近熔点时,其空位平衡浓度约为10-4;把高温时金属中存在的平衡空位通过淬火固定下来,形成过饱和空位状态,对金属中的许多物理过程(例如扩散、时效、回复、位错攀移等)产生重要影响3. 晶体的热容- Dulong-Petit :线性谐振动子+能量均分定律→适应于较高温度及室温附近,低温时与实验不符U Q W∆=-dH PV U d Q =+=)(δRd Q S Tδ=()d dH TdS G H d TS =--=00lim()lim()0p T T T GS T→→∂∆-=∆=∂()()V T T P V V S ∂∂=∂∂//()()()T T T V P V V S T V H ∂∂+∂∂=∂∂///RK mol J T H S mm m ≈⋅≈∆=∆/3.8/K mol J T H S b v v ⋅≈∆=∆/9.87/3V V VQ dU C RdT dT δ⎛⎫⎛⎫=== ⎪ ⎪⎝⎭⎝⎭-Einstein(固体振动热容理论):晶体总共吸收了n 个声子,被分配到3N 个谐振子中;不适用于极低温度,无法说明在极低温度时定容热容的实验值与绝对温度的3次方成比例。
材料热力学习题集液态铅在1个大气压下的热容量Cp(l)称为Cp(L)= 32.43-3.10×10-3TJ/(mol·k),固态铅的热容量Cp(s)为Cp(S)= 23.56+9.75×10-3TJ/(mol·k)。
众所周知,当液态铅的熔点(600 K)固化成固体时,液态铅释放4811.60 J/mol的热量,并计算了当液态铅过冷到590K并固化成固体时的焓变化。
液态铅固态铅600Kb恒温相变c温升590Ka初始状态相变d最终状态?H示意图实施例1-2众所周知,锡在505K(熔点)时的熔化热为7070.96焦耳/摩尔,厘泊(L) = 34.69-9.20×10-3TJ/(摩尔·K)厘泊(S) = 18.49+26.36×10-3TJ/(摩尔·K)用于计算锡过冷至495 K时自动凝固的比例505K恒温,放热b相变c最终状态吸收热上升温度吸收热相变放热495Ka初始状态1摩尔液体d x摩尔固体(1-x)摩尔液体?H图例1-3铅的熔点为600K,凝固热为4811.6 J/mol,计算了铅在600K 凝固时的熵值变化(在一个大气压下)。
例1-4已知在1个大气压下液态铅的比热为32.43-3.10×10-3tj/(mol·k)CP(s)= 23.56+9.75×10-3tj/(mol·k)液态铅在其熔点(600K)固化成固体时释放4811.6 J/mol的热量。
计算了液态铅过冷到590K凝固时(在一个大气压下)熵值的变化。
1液态铅固态铅恒温相变600Kbc冷却温升590Ka初始相变d最终状态计算?S示意图实施例2-1已知液态锌的Cp(l)为Cp(L)= 29.66+4.81×10-3TJ/(mol·k),固态锌的Cp(s)为Cp(S)= 22.13+11.05×10-3TJ/(mol·k),锌的熔点为692.6K,熔化热δH = 6589.8J/mol,自由能差δG(δ的实施例2-2使用第一章中的数据计算铅在590 K(过冷10 K)凝固时的自由能变化δg(590 K),并将其与简单近似计算的结果(铅在590K 凝固时δH =-4811.6J/mol)进行比较可以从第一章的计算中看出:当铅在590K凝固时,焓变化δH =-4722.56J/mol;熵变化δs =-8.0j/(Mol·k)例2-3已知γ-铁、δ-铁和液态铁的Cp为Cp(γ)= 7.70+19.50×10-3 TJ/Mol·kcp(d)= 43.93j/Mol·k(1674 ~ 1809k)Cp(L)= 41.84j/Mol·k(L)G亚稳态?相的理论熔点?第一阶段?1673年?L1809G?g?GLT/K?阶段225y = 246.65t-34.138 tlnt+9.75?10t 20-32y/100015y = 14861.57t = 1793.82k 105005001000t,k 1500200025003000| 286K时199例4-1,α-Sn β-Sn的δh = 2092j/mol,锡的= 118.7,πα-Sn = 5.75g/mL,ψ计算100个大气压下相变温度的变化值例4-2在95.5℃单斜硫菱形硫中,δV = 0.01395毫升/克,δH = 13.05焦耳/克,找出压力对相变温度的影响例4-3固体锌的蒸气压与温度的关系为:lgp(ATM)=-6850/T-0.755 gt+8.36液态锌的蒸气压与温度的关系为:lgp(ATM)=-6620/T-1.255 LGT+9.46q:1)液态锌在1个大气压下的沸点;2)三点温度;3)1 ATM沸点下的汽化热;4)三相点的熔化热;5)固体锌和液体锌之间的δCp 例4-4锌在610 K时的蒸气压为10 mmHg,镉的计算蒸气压也为10-5 mmHg杜林定律:当相似物质具有相同的蒸汽压时,T1/T2 =常数例4-5碳在1个大气压和25℃下以石墨为稳定相,并试图找出在25℃下将石墨转化为金刚石所需的压力实施例5-1实验测得的镉-镁的摩尔体积如下表所示Cd-镁合金-5实施例5-2已知三元溶液的摩尔体积为VM = 7x1+10 x2+12x 3-2x1x2+3x1x2x 3(cm3/mol)339解决方案:虚拟机∠X1 = x2 = x3 = 1/3 =869 X1 = 1-X2-X3,因为X1+X2+X3 = 1经过取代,我们可以得到:实施例5-3在1075℃下实验测得的氧在银中的溶解度如下表所示,我们可以找出:1)氧在银中的溶解度是否符合西沃特定律,我们可以找出溶解度常数;2)1075℃时空气中氧在银中的溶解度实施例5-4将0.567 g尿素(CON2H4)溶解在500 g水中,测量该水溶液的冰点为-0.0351℃,并计算尿素的分子量。
材料热⼒学练习题1、由5个粒⼦所组成的体系,其能级分别为0、ε、2ε及3ε,体系的总能量为3ε。
试分析5个粒⼦可能出现的分布⽅式;求出各种分布⽅式的微观状态数及总微观状态数。
2、有6个可别粒⼦,分布在4个不同的能级上(ε、2ε、3ε及4ε),总能量为10ε,各能级的简并度分别为2、2、2、1,计算各类分布的Ωj 及Ω总。
3、振动频率为ν的双原⼦分⼦的简谐振动服从量⼦化的能级规律。
有N 个分⼦组成玻⽿兹曼分布的体系。
求在温度T 时,最低能级上分⼦数的计算式。
4、⽓体N 2的转动惯量I =1.394?10-46kg ?m 2,计算300K 时的Z J 。
5、已知NO 分⼦的Θυ=2696K ,试求300K 时的Z υ。
ν~J υ7、计算300K 时,1molHI 振动时对内能和熵的贡献。
8、在298K 及101.3kPa 条件下,1molN 2的Z t 等于多少?9、在300K 时,计算CO 按转动能级的分布,并画出分⼦在转动能级间的分布曲线。
10、计算H 2及CO 在1000K 时按振动能级的分布,并画出分⼦在振动能间的分布曲线;再求出分⼦占基态振动能级的⼏率。
11、已知HCl 在基态时的平均核间距为1.264?10-10m ,振动波数ν~=2990m -1。
计算298K 时的Θm S 。
12、证明1mol 理想⽓体在101.3kPa 压⼒下Z t =bLM 3/2(T /K )5/2 (b 为常数)13、计算1molO 2在25?C 及101.3kPa 条件下的Θm G 、Θm S 及Θm H 。
设Θ0U 等于零。
14、已知300K 时⾦刚⽯的定容摩尔热容C V ,m =5.65J ?mol -1?K -1,求ΘE 及ν。
15.已知300K 时硼的定容摩尔热容C V ,m =10.46J ?mol -1?K -1,求(1) ΘD ;(2) 温度分别为30K 、50K 、100K 、700K 、1000K 时的C V ,m 值;(3) 作C V ,m 值? T 图形。
第一章一、选择题1. 下述说法中,哪一个是错误的?( )(A )系统放出的热量一定等于环境吸收的热量。
(B)系统温度的降低值一定等于环境温度的升高值。
(C )热力学平衡时系统温度与环境温度相等。
(D )若两物体分别与第三物体成热平衡,则此两物体的温度相同。
2.下列对可逆过程的描述何者不正确?( )(A )能使系统和环境完全复原的过程。
(B )在整个过程中系统内都无限接近于平衡态。
(C )过程进行无限缓慢,环境的温度、压力分别与系统的温度、压力相差甚微。
(D )一个带活塞储有一定量气体的气缸,设活塞无重量,控制内外压差无限小,缓慢膨胀到终态,再压缩使系统回到原始态。
3. 列宏观过程: (1)101325Pa 、273K 下冰融化为水;(2)气缸中活塞往复运动;(3)NaCl 溶解在水中;(4)水在101325Pa 、373K 下蒸发。
可看作可逆过程的是( )。
(A ) (1)(4) (B )(2)(3)(C )(1)(3)(D )(2)(4)4.一绝热容器中有一无摩擦、无质量的绝热活塞,两边各装入等量同温度同压力 的理想气体,左边有一电阻丝缓慢加热(如图),活塞慢慢向右移动。
今以左边气体为系统,其余为环境,则系统有( )(A )Q <0,W =0,ΔU <0(B )Q =0,W>0,ΔU >0(C )Q >0,W>0,ΔU >0(D )Q <0,W =0,ΔU >05上题若以两边气体为系统,其余为环境,则有( )(A )Q >0,W >0,ΔU <0(B )Q <0,W =0,ΔU >0(C )Q <0,W <0,ΔU =0(D )Q >0.W =0.ΔU >06.在一个密闭绝热的房间里放置一台电冰箱,将冰箱门打开,并接通电源使其工作,过一段时间之后,室内的平均气温将如何变化( )(A )升高(B )降低(C )不变(D )不能确定7.下述说法哪一种不正确?( )(A )一定量理想气体自由膨胀后,其ΔU =0。
安徽工业大学研究生材料热力学考试题
一、仔细阅读下列论述,判断正误,如果错误,请说明该论述违反了哪些热力学原理,并给出正确的论述。
(20分)
(1) 低压下不可能将石墨转变为金刚石。
(2) 在一炉10 吨的钢水(Fe-C 二元溶体)中加入12 克碳后,使钢水的吉布斯自由能的增加值即为Fe 的
化学位。
(3) 恒温恒压下,如果两相的吉布斯自由能相等,则两相彼此处于平衡状态。
(4) 纯金属中不存在空位时的吉布斯自由能最低。
(20分)
分)
三、(1)固态纯组元的G-T 曲线如下图所示,请判断哪条线正确,并解释原因。
(20
(2)A-B 二元系中,固相和液相的摩尔自由能-成分曲线如下图所示。
请在自由能-成分曲线上,图示出体系成分为X*处,固相纯A和液相纯B混合后的吉布斯自由能的变化量∆Gmix,并说明原因。
(20分)
四、试通过如图所示的A-B二元相图,判断A-B固溶体的性质、溶体组元间的相互作用能。
并请画出T1 温度下所存在的相的自由能-成分曲线。
(20分)。
The problems of the first law1. a lead bullet is fired at a frigid surface. At what speed must it travel to melt on impact, if its initial temperature is 25℃ and heating of the rigid surface of the rigid surface is neglected? The melting point of lead is 327℃. The molar heat of fusion of the lead is 4.8kJ/mol. The molar heat capacity C P of lead may be taken as 29.3J/(mol K) (1.1)Solution: )/(5.112.20721]108.4)25327(3.29[2121)(2322s m V v n n WQ nMv mv W H T C n Q Q Q absorb melting p melt increase absorb ==⨯+-⨯===∆+∆=+=2. what is the average power production in watts of a person who burns 2500 kcal of food in a day? Estimate the average additional powder production of 75Kg man who is climbing a mountain at eh rate of 20 m/min (1.2)Solution )/(24560208.975)/(12160602410467000//)(104670001868.4102500sin 3S J t h mg P S J t Q t W P J Q gincrea Burning Burning =⨯⨯=∆==⨯⨯====⨯⨯=3 One cubic decimeter (1 dm 3) of water is broken into droplets having a diameter of one micrometer (1 um) at 20℃. (1.3)(a) what is the total area of the droplets?(b) Calculate the minimum work required to produce the droplets. Assume that the droplets arerest (have zero velocity)Water have a surface tension of 72.75 dyn/cm at 20℃ (NOTES: the term surface energy (ene/cm 2) is also used for surface tension dyn/cm)Solution)(25.218)106103(1075.72)(103)101(4)101(34)101(232523263631J S W m nS S Single total =⨯-⨯⨯⨯=∆=⨯=⨯⨯⨯⨯⨯⨯⨯⨯==-+----σππ4.Gaseous helium is to be used to quench a hot piece of metal. The helium is in storage in aninsulated tank with a volume of 50 L and a temperature of 25℃, the pressure is 10 atm. Assume that helium is an ideal gas.(a) when the valve is opened and the gas escapes into the quench chamber (pressure=1 atm), whatwill be the temperature of the first gas to hit the specimen?(b) As the helium flows, the pressure in the tank drops. What will be the temperature of thehelium entering the quench chamber when the pressure in the tank has fallen to 1 atm? (1.4)Solution: )(180118298)(1185.229810101325501010101325)5500(1)()(118)101(298)()(0334.0/00K T T T K RR nC W T b K T P PT T Adiabatic a p C R P=-=∆-==⨯⨯⨯⨯⨯⨯⨯-⨯==∆=⨯==--5 An evacuated (P=0), insulted tank is surrounded by a very large volume (assume infinite volume) of an ideal gas at a temperature T 0. The valve on the tank is opened and the surrounding gas is allowed to flow quickly into the tank until the pressure inside the tank is equals the pressure outside. Assume that no heat flow takes place. What is the final tempeture of the gas in the tank? The heat capacity of the gas, C p and C v each may be assumed to be constant over the temperature rang spanned by the experiment. You answer may be left in terms of C p and C vhint: one way to approach the problem is to define the system as the gas ends up in the tank. (1.5)solution 0/000/00)0()(T P P T T P PT T Adiabatic PPC R C R ≈-==6. Calculate the heat of reaction of methane with oxygen at 298K, assuming that the products of reaction are CO 2 and CH 4 (gas)[This heat of reaction is also called the low calorific power of methane] convert the answer into unites of Btu/1000 SCF of methane. SCF means standard cubic feet, taken at 298 and 1atmNOTE: this value is a good approximation for the low calorific powder of natural gas (1.6)DA TA:)()()(224g O H g CO g CH FOR80.5705.9489.17]/[0298---•∆mol g Kcal Hsolution)1000/(9.2610252103048.01101076.191)/(76.191)89.1780.57205.94()2(22333332982982224422SCF Btu mol g Kcal H H H H H OH CO O CH CH O H CO =⨯⨯⨯⨯⨯=•=∆+⨯---=∆-∆+∆-=∆+=+-7. Methane is delivered at 298 K to a glass factory, which operates a melting furnace at 1600 K. The fuel is mixed with a quantity of air, also at 298 K, which is 10% in excess of the amount theoretically needed for complete combustion (air is approximately 21% O 2 and 79% N 2) (1.7) (a) Assuming complete combustion, what is the composition of the flue gas (the gas followingcombustion)?(b) What is the temperature of the gas, assuming no heat loss?(c) The furnace processes 2000kg of glass hourly, and its heat losses to the surroundings average400000 kJ/h. calculate the fuel consumption at STP (in m 3/h) assuming that for gas H 1600-H 298=1200KJ/KG(d) A heat exchanger is installed to transfer some of the sensible heat of the flue gas to thecombustion air. Calculate the decrease in fuel consumption if the combustion air is heated to 800KDA TA STP means T=298K, P=1atm22224O N O H CO CH for 2.82.89.117.1316)/(C mol cal C P •Solution)(210448.1125.9100076.191298)/(25.9)]87.012.72(2.843.179.1171.87.13[01.0)(%87.0%%12.72%%43.17%2%%71.8)11.1(221791.1231%22)(0,,222222224K T T T C mol cal X C C b O N CO O H CO O H CO O CH a i i p p p =⨯⨯+=∆+=•=+⨯+⨯+⨯=======-⨯+⨯⨯+=+=+∑)/(1644)0224.011868.448.11)8001600(48.1125.9189570(102800000)/(189570)298800)](48.1187.8)48.1125.9[(100076.191)()/(87.848.11/]211002.22.816[)()/(3214)0224.011868.448.11)2981600(48.1125.9100076.191(102800000)/(280000040000020001200)(33min ,,,,298,,33min h m V mol g cal dTn C n C H H C mol cal X C C d h m V h KJ P C gConsu i i r p i i p p i i p r p g Consu =⨯⨯-⨯-⨯=•=-⨯-⨯-⨯=--∆=∆•=⨯⨯+===⨯⨯-⨯-⨯⨯==+⨯=⎰∑∑∑8.In an investigation of the thermodynamic properties of a-manganese, the following heat contents were determined:H 700-H 298=12113 J/(g atom) H 1000-H 298=22803 J/(g atom)Find a suitable equation for H T -H 298 and also for C P as a function of temperature in the form (a+bT) Assume that no structure transformation takes place in the given tempeture rang. (1.8)Solution )298(0055.0)298(62.35011.062.35011.062.3522803)2981000(2)2981000(12113)298700(2)298700(]2[2229822222982---=∆-=-===-+-=-+-+=+==∆⎰⎰T T H TC b a ba ba T baT bTdT a dT C H TP T P9.A fuel gas containing 40% CO, 10% CO 2, and the rest N 2 (by volume) is burnt completely with air in a furnace. The incoming and ongoing temperatures of the gases in the furnace are 773K and 1250K,respectively. Calculate (a) the maximum flame temperature and (b) heat supplied to the furnace per cu. ft of exhaust gas (1.9)molJ Hmol J H CO f CO f /393296/1104580,298,0,298,2-=∆-=∆)/(10184.403.29)/(1067.11010.492.19)/(1037.81020.935.44)/(1042.01097.345.283,253,253,253,222molK J T C molK J T T C molK J T T C molK J T T C N P O P CO P CO P -------⨯+=⨯-⨯+=⨯-⨯+=⨯-⨯+=Solution?0)499.0321.018.1()1067.01019.277.28(28.282831067.01038.477.289.0)1019.01058.528.33(2.0282838)()/(1019.01058.528.33722.0278.0)/(1067.01038.477.281.065.005.02.0)()/(282838110458393296%2.72%8.27%10%65%5%20)4/(1122298127332981523733253253298,,,,298,253,,,,,253,,,,,,,0,298,0,298,298,22222222222222==+--⨯+⨯++⨯=⨯-⨯++⨯⨯-⨯+-⨯=--∆=∆⨯-⨯+=+==⨯-⨯+=+++===-=∆-∆=∆========+-----------⎰⎰⎰∑∑⎰∑∑∑∑T T T T T T T dTT T dTT T dT n C n C n H H molK J T T C C n C C molK J T T C C C C n C C a mol J n H n H H N CO production O N CO CO reation then O N air mole need fuel mole when CO O CO T TT i i r p i i p p i i N P CO P i i p p r p O P N P CO P CO P i i p p r p i p f i r f idTT T Q dT T T Q b T T T T T T T dT T T dTT T dT n C n C n H H T TT i i r p i i p p i i 9.0)1019.01058.528.33(2.02828389.0)1019.01058.528.33(2.0282838)(0)499.0321.018.1()1067.01019.277.28(28.282831067.01038.477.289.0)1019.01058.528.33(2.0282838)(253125029812502982531250298125029829812125029815231250253253298,,,,298,⨯⨯-⨯++⨯-=⨯⨯-⨯++⨯-===+--⨯+⨯++⨯=⨯-⨯++⨯⨯-⨯+-⨯=--∆=∆-----------⎰⎰⎰⎰⎰∑∑⎰10. (a) for the reaction 2221CO O CO →+,what is the enthalpy of reaction (0H ∆) at 298 K ? (b) a fuel gas, with composition 50% CO, 50% N 2 is burned using the stoichiometric amount of air. What is the composition of the flue gas?(c) If the fuel gas and the air enter there burner at 298 K, what is the highest temperature theflame may attain (adiabatic flame temperature)? DA TA :standard heats of formation f H ∆ at 298 K (1.10))/(393000)/(1100002mol J CO mol J CO -=-=Heat capacities [J/(mol K)] to be used for this problem N 2=33, O 2=33, CO=34, CO 2=57 Solution)(21100)298)(39889.0(222.02830000)/(3975.03325.057)/(33111.034222.033666.033)(%,75%%,251.111002.22%%1.11%%,6.66%%,2.222.0/25.015.0%)()/(283000393000110000)(,0,,,,,,22220,298,0,298,0K T T dT C n H H K mol J X C C K mol J X C C C N CO product O N CO fuel b mol J n H n H H a P p p i P r i P r i P p i P p i P f i r f ==-⨯-⨯=-∆=∆•=⨯+⨯==•=⨯+⨯+⨯====-====+==+-=∆-∆=∆⎰∑∑∑∑11.a particular blast furnace gas has the following composition by (volume): N 2=60%, H 2=4, CO=12%, CO 2=24%(a) if the gas at 298K is burned with the stochiometric amount of dry air at 298 K, what is the composition of the flue gas? What is the adiabatic flame temperature? (b) repeat the calculation for 30% excess combustion air at 298K(C)what is the adiabatic flame temperature when the blast furnace gas is preheated to 700K (the dry air is at 298K)(d) suppose the combustion air is not dry ( has partial pressure of water 15 mm Hg and a total pressure of 760 mm Hg) how will the flame temperature be affected? DA TA(k J/mol) (1.11)2CO CO FOR513.393523.110)/(--∆mol kJ H f 2222,)(O N g O H CO CO FOR34505733]/[K mol J C P •Solution)(1052)(75438286370])295.03450(241604[026.0])335.03457(110523393513[079.0])([%8.66%%,8.6%%,6.2%%,8.15%%,9.72.0/83.110012%)()(1122)(82538313430])295.03450(241604[029.0])335.03457(110523393513[086.0])([%7.65%%,7.5%%,9.2%%,1.17%%,6.82.0/810012%2121)(,,,,,,,02222,,,,,,,0222222222K T K T T n C T T X C dT n C n C H x H N O H CO CO b K T K T T n C T T X C dT n C n C H x H N O H CO CO OH O H CO O CO a i i r P ii P i i r P i i p P i i i i r P ii P i i r P i i p P i i ===∆=∆-∆-⨯--+∆-⨯---=+--∆=∆=====⨯+====∆=∆-∆-⨯--+∆-⨯---=+--∆=∆=====+=→+→+∑∑∑⎰∑∑∑∑∑⎰∑∑)(1419),(11213842594034286.0)402(2.39714.0])295.03450(241604[029.0])335.03457(110523393513[086.0)3(K T K T T T T T H ===∆=∆⨯--∆⨯-∆-⨯--+∆-⨯---=∆12.A bath of molten copper is super cooled to 5℃ below its true melting point. Nucleation of solid copper then takes place, and the solidification proceeds under adiabatic conditions. What percentage of the bath solidifies?DA TA: Heat of fusion for copper is 3100 cal/mol at 1803℃(the melting point of copper) C P,L =7.5(cal/mol ℃), C P,S =5.41+(1.5*10-3T )(cal/mol ℃) (1.12) Solution)/(310355.75.0)17981803(105.1541.5310002231798,1798,17981803,18031798,1803,mol cal H H dT C dT C H L S SL L P S P L S =⨯-⨯-⨯+⨯+==+++-⎰⎰13.Cuprous oxide (Cu 2O) is being reduced by hydrogen in a furnace at 1000K, (a)write the chemical reaction for the reduced one mole of Cu 2O(b)how much heat is release or absorbed per mole reacted? Given the quantity of heat and state whether heat is evolved (exothermic reaction) or absorbed (endothermic reaction)DA TA: heat of formation of 1000K in cal/mol Cu 2O=-41900 H 2O=-59210 (1.13) solution)/(173104190059210222mol cal H OH Cu H O Cu =-=∆+=+,exothermic reaction14. (a) what is the enthalpy of pure, liquid aluminum at 1000K?(b) an electric resistance furnace is used to melt pure aluminum at the rate of 100kg/h. the furnace is fed with solid aluminum at 298K. The liquid aluminum leaves the furnace at 1000K. what is the minimum electric powder rating (kW) of furnace.DA TA : For aluminum : atomic weight=27g/mol, C p,s =26(J/molK), C p,L =29(J/molK), Melting point=932K, Heat of fusion=10700J/mol (1.14)Solution )(28.0)(7.2793600110002727184)/(2718410700)9321000(29)298932(261000932,932298,1000,kW W P mol J H dT C dT C H SLL P S P l ==⨯⨯==+-⨯+-⨯=++=⎰⎰15 A waste material (dross from the melting of aluminum) is found to contain 1 wt% metallic aluminum. The rest may be assumed to aluminum oxide. The aluminum is finely divided and dispersed in the aluminum oxide; that is the two material are thermally connected.If the waster material is stored at 298K. what is the maximum temperature to which it may rise if all the metallic aluminum is oxidized by air/ the entire mass may be assumed to rise to the same temperature. Data : atomic weight Al=27g/mol, O=16g/mol, C p,s,Al =26(J/molK), C p,s,Al2O3=104J/mol, heat formation of Al 2O 3=-1676000J/mol (1.15)Solution;)(600)(3021041029927275.116122711676000K T K T T ==∆∆⨯⨯++⨯⨯=⨯⨯16 Metals exhibit some interesting properties when they are rapidly solidified from the liquid state. An apparatus for the rapid solidification of copper is cooled by water. In the apparatus, liquid copper at its melting point (1356K) is sprayed on a cooling surface, where it solidified and cools to 400K. The copper is supplied to the apparatus at the rate of one kilogram per minute. Cooling water is available at 20℃, and is not allowed to raise above 80℃. What is the minimum flow rate of water in the apparatus, in cubic meters per minute?DA TA; for water: C p =4.184J/g k, Density=1g/cm 3; for copper: molecular weight=63.54g/mol C p =7cal/mol k, heat of fusion=3120 cal/mol (1.16)Solution:min)/(10573.2)2080(1min /min54.631000)]4001356(73120[min /33m V VQ Q Water Copper -⨯=-=⨯⨯-⨯+=17 water flowing through an insulated pipe at the rate of 5L/min is to be heated from 20℃ to 60℃ b an electrical resistance heater. Calculate the minimum power rating of the resistance heater in watts. Specify the system and basis for you calculation. DA TA; For water C p =4.184J/g k, Density=1g/cm 3 (1.17)Solution: )(139476010005)2060(184.4W W =⨯⨯-⨯=18 The heat of evaporation of water at 100℃ and 1 atm is 2261J/mol (a) what percentage of that energy is used as work done by the vapor?(b)if the density of water vapor at 100℃ and 1 atm is 0.597kg/m 3 what is the internal energy change for the evaporation of water? (1.18)Solution: )/(375971822613101%6.71822613101%)/(31010224.0273373101325mol J Q W U mol J V P =⨯+-=+=∆=⨯==⨯⨯=∆19 water is the minimum amount of steam (at 100℃ and 1 atm pressure) required to melt a kilogram of ice (at 0℃)? Use data for problem 1.20 (1.19) Solution )(125,3341000)10018.42261(g m m =⨯=⨯+20 in certain parts of the world pressurized water from beneath the surface of the earth is available as a source of thermal energy. To make steam, the geothermal water at 180℃is passed through a flash evaporator that operates at 1atm pressure. Two streams come out of the evaporator, liquid water and water vapor. How much water vapor is formed per kilogram of geothermal water? Is the process reversible? Assume that water is incompressible. The vapor pressure of water at 180℃is1.0021 Mpa( about 10 atm) Data: C P,L=4.18J/(g k), C P,v=2.00J/(g k), △H V=2261J/g, △H m=334 J/g (1.20)Solution:leirreversibgxxx)(138),1000(8018.4)8018.48022261(=-⨯⨯=⨯-⨯+。
“材料热力学”补充习题参考答案教材各章习题参考答案 (魏)3.2 ΔG = -108.9 J/mol; ΔS = -21.42 J/(mol.K) 3.6 (a )22.09/(.)S J mol K ?=;(b) At 0?C, ?G =0;(c) ?H = 5841.9 J;(d) ?S =21.39J /(mol.K),?G = 109.38 J/mol4.1 (a ) 2898.28J/mol; ( b ) No; ( c ) 345 J/mol; ( d ) 14939 atm; ( e )4921 J/mol 4.2 ( a ) 272.8K; ( b ) Pa P 610345?≈? ; ( c ) 249.46K4.3 1202K4.4 P=5.73?10-6 atm 4.5 0.16P 4.708.10430685ln +-=TP4.8 ( a ) 1180K; ( b ) 695.3K; ( c ) 114.4kJ/mol; ( d ) 7123 J/mol; ( e )4.2J/mol4.9 In the initial state: 4.06 mol %; in the final state:5.3 mol% 4.10 ( a )348 kJ; ( b ) 2.3×10-3Pa ;( c ) “ solution not possible ”; (d ) “solution not possible ”5.1atmp H 0005.0=5.2、atmp o 1221007.1-?=If the error in enthalpy is 500cal, the uncertainty in the pressure calculated is 28.6%, and if the error in enthalpy is -500cal, the uncertainty is -22.1%5.3、(a) T =462K; (b) T = 420K 5.4 (a)atmP O 2621014.1-?=, (b) P O2 =2.28?10-10 atm., (c) The equilibriumoxygen pressure remains the same when the total pressure increases, which means a higher purity level of N 2 .5.5 (a) 略; (b) Pa atm P H 8.181013056.1800019.0)('2=?==; (c) 21.5L Ar is needed to be bubbled into the melt.5.6(a )0.880.900.920.940.960.981.00 1.02 1.04 1.06 1.087.27.47.67.88.08.28.48.6l n K a1/T , 10-31/K=-=?ooG kJ H1000;50- 66.6kJ(b) Ja = 3 < Ka, the reaction will proceed from left to right, and theatmosphere will not oxidize Ni. 5.7 略5.8. (a) P SiO = 8.1?10-8 (atm) (b) ?H o = 639500J; ?So =334.9J/K(c ) PO2 =10-30 atm 5.9 5.10.JH o72250=?,the reaction is an endothermic one.5.11. (a),166528J Ho=?the reaction is an endothermic one.;(b) At 1168K, the equilibrium pressure of CO2 equals one atmosphere. 5.12 (a) 略, (b) MgCO P P =; (c) T = 2037 K5.13 (a) 略; (b) 13109.2?=K ; (c) ppm 186.05.14 (a) 略; (b) kJ H 52.267=?; (c) K T 1592=5.15 (a) )(106.13atm -?≈; (b) )(1028.210)(2atm P g O H -?=5.16 (a)97.9=K ; (b) atm x 14.4=; (c) if the temperature is increased,the fraction of water reacted will increase since the equilibria constant increases with increasing temperature.6.2 (a )1.287V;(b) When the water impure, the voltage will go higher; (c)1.219V 6.4 (a) 145.3kJ;(b) The maximum work that could be derived is 702.36kJ; (c) In this case, the maximum work that could be derived is 696.56kJ.)(106.08)(atm Pg u -?=6.5 (a) -6252J/mol; (b) 370.0)(=II Cda ; (c) )(42.3mmHg P Cd =;6.67.87?10-4 V 6.7 (a))(22g Cl Mg MgCl+=(b)Pa P Cl 21'1086.82-?=;(c) 2.485V6.8 (a) PaP O 11'2105.5-?=;(b) Anode: e Ni Ni 2+→Cathode: -→+2222/1Oe O ;(c) 0.757V; (d) 0.261V6.10 (a) )(509.3V E o=;(b) 0.074kJ;(c) 4.1?106J;(d) Y es. In this case, the open circuit voltage is 3.648V;(e) In this case, to keep the temperature constant, 3.92?106J heatshould be removed from the battery per hour. 6.11(a)TGCOAl C O Al o26.3211008.12/322/36232-?=+=+Δ(b) The minimum voltage at which the electrolysis may be carriedout at 1250K is 1.172V .7.1 0.117 atm 7.5 ( a ) ,82.52.52.5BA BA BB T PV V V x x x x x ??=+=-- ?,102.5 2.5 2.5A B A A B A T PV V V x x x x x ??=+=-- ?( b) B A Mx x V5.2=7.72)1(736.0ln Sn Snx --=γ7.8 The maximum solubility of MgF2 in liquid MgCl at 900?Cis 19mol% .7.9 ( a ) 1121K; ( b ) 1. 8 cal/K 9.69.8 Solution:(a) 90 mol%B is the composition of the first solid to form;10 mol % is the composition of the last liquid drop.(b) solid (60 mol%B is the composition) is about 77% ; liquid(15 mol%B is the composition) is 23%9.9 (a) 2900℃, α(12%) (b) 2300℃, liq(95%) (c) 8.2%α(compositionis 24% )+91.8%β(85%)补充习题参考答案(魏)1.ΔS m =19.1J/mol.K, ΔG m = -5740 J/mol, ΔF m = -5740 J/molIsothermally expan ds to a vacuum: w = 0, ΔH m =0 , ΔU m =0,ΔS m =19.1J/mol.K, ΔG m = -5740 J/mol, ΔF m = -5740 J/mol2. 3.68 × 10-3 atm3、x x Br H C Cl H C 406.0;594.05556==Pa p Pa p Br H C Cl H C 26838;744445556==4.5、JGJ GJ G a a exmix idmix mix B A R B R A 5302)5(;6912)4(;1610)3(;788.1;62.1)2(;894.0;81.0)1()()(=?-=?-=?====γγ6. a endothermic one; b. Y es; c JJ EMn EFe 704;1584==μμd;/9363mol J G m mix -=?ePap Pa p Fe Mn 4;1198==S n P b4578-=ω;418.0=Sn a8. a) Mg boils and which makes oS ?more negative, so the slope changes for larger; b) Firstly, we should avoid using metallic material for this purpose since the melting points of metals are mostly too low. Ceramic materials, usually composed of oxides and having high melting points can be chosenThe material should not be reduced by pure silicon at 1600oC. By examing Ellingham diagram, crucibles (坩埚) made of Al 2O 3 .c ) -890kJ /molO2;d ) -170kJ /molFeO; e) -30kJ; f) Pa2110-;g)721063.0/?=pco p COPure Substance as Standard Statepq(b )I 、II 、IIIIII:AA x RT T p RT T T ln )(ln)()(**+=+=μμμk A9、① 650oC ,1220 oC and 1520 oC ; ② 1480 oC ;③ When the temperature is equal to or higher that 710 oC ;④ 2/100molO kJ G o-=?⑤ 900 oC; ⑥,102/112,1010'25'2=?=-=?=--G Pa PmolO kJ G Pa P O O ,Pap e O 10')(210-=⑦ 510-=K;⑧ 1220oC10、a) -489120+197.06TlnT J/mol; b) 2.89×10-54 ; c)JG 749429=?; Ni is stable under thiscondition, and NiO is not stable; d)p e o 58')(21046.3?= e) fromthe calculation, we found that at 1000oC,Pap e o 58')(21046.3?=. Soat 1000oC, when the oxygen pressure is less than 3.46×1058Pa, Ni is stable and can not be oxidized, and NiO will be reduced to Ni under this condition. 11. a)molkJ G o/2.23=?; b)43.42=eCO CO p p . This is theminimum CO/CO2 ratio required to reduce pure FeO to Fe at 1600oC. c)2.142=eCO CO p p . This is the minimum CO/CO2ratio required to reduce FeO in a slag( 炉渣) to Fe in a metallic iron melt under the given conditions at 1600oC.12.%10?-Ar .3 15 % 100 ) 10。
新型材料设计及其热力学与动力学The excess Gibbs energies of bcc solid solution of (Fe,Cr) and fee solid solution of (Fe,Cr) is represe nted by the follow ing expressi ons:exG (bcc)/J = x cr X Fe (25104 —11.7152 T);G ex(fcc)/J = X cr X Fe (13108 —31.823 T+ 2.748 T log e T)For the bcc phase, please do the follow ing calculatio ns using one calculator.(a) Calculate the partial Gibbs energy expressions for Fe and Cr(b) Plot the integral and partial Gibbs energies as a function of composition at 873 K(c) Plot the activities (a cr and a Fe) as a function of composition at 873K(d) What are the Henry 'law constants for Fe and Cr?For the fcc phase, please do the calculati ons (a) to (b) by using your own code翻译:BCC (Fe , Cr )固溶体的过剩吉布斯自由能和fcc固溶体(Fe, Cr )的吉布斯自由能表达式如下:exG (bcc)/J = X cr X Fe (25104 —11.7152 T);G ex(fcc)/J = X cr X Fe (13108 —31.823 T + 2.748 T ln T) G ex/J对于体心立方相,请使用计算器做下面的计算。
《材料热力学》复习思考题解答3. 在1560℃时,C 在液态铁中的活度系数和偏摩尔超额焓由下列式表示: 2l n 0.37711.7c C C X X γ=-++25.415.017.25E C C C H X X =++(K Cal) 其标准态为纯石墨,计算1560℃时液相与石墨平衡的相线的斜率。
解:以石墨为标准态时,C 在液态铁中的化学位为:l n (1)LC CC R T a μμ=+ 石墨 当液相与石墨平衡时,L C Cμμ=石墨。
即ln 0C α=。
又ln ln ln C C C X αγ=+ln ln 0(2)C C X γ∴+=由(2)式得:平衡时0.2067C X =两边取微分得:(ln )(ln )1[](1/)[]0(1/)C C C X T C C C C d T dX dX T X X γγ∂∂++=∂∂ (ln )[](1/)ln ln 1(1/)[()]1()CC X EC C C C C T C TC C CdX H X T d T R X X X X γγγ∂-∂∴==⋅∂∂-++∂∂2(5.415.017.25) 4.1810000.20678.311(723.4)278.6C C CC X X X X ++⨯⨯=-⋅++=- 2C dX T dT=-CdX 又d(1/T)5221278.68.310(1560273)C dX dT T -∴=-==⨯+C dX d(1/T) 1()K - 4. 在1000K 时,A-B 二元溶液中,当0.01B X =时,0.1B a =。
在盛有大量A 的量热计中加入少量的B 组元时,测得吸热7000Cal/mol ,假定2ln ln B A B X γγ=。
求1500K 时,当0.02B X =时,B 组元的活度。
解:在1000K 时,当0.01B X =时,0.1B a =0.1100.01B γ∴== 又022ln ln10ln 2.3490.99B B A X γγ=== 又ln [](1/)ii P H R T γ∂∆=∂15001500010001000l n (1/)BBH d d T Rγ∆∴=⎰⎰1500100011[ln ][ln ]()15001000B B B H R γγ∆∴=+-7000 4.18112.349()8.31150010001.175⨯=+-= 202l n (l n )0.981.175B A B X γγ∴==⨯ 1.128= l n 3.09B γ∴= 3.090.020.0B B B a X γ==⨯=7. 若A-B 二元合金系在液、固态两组元均能无限互溶,且均为理想溶液。
The problems of the first law1. a lead bullet is fired at a frigid surface. At what speed must it travel to melt on impact, if its initial temperature is 25℃ and heating of the rigid surface of the rigid surface is neglected? The melting point of lead is 327℃. The molar heat of fusion of the lead is 4.8kJ/mol. The molar heat capacity C P of lead may be taken as 29.3J/(mol K) (1.1)Solution: )/(5.112.20721]108.4)25327(3.29[2121)(2322s m V v n n WQ nMv mv W H T C n Q Q Q absorb melting p melt increase absorb ==⨯+-⨯===∆+∆=+=2. what is the average power production in watts of a person who burns 2500 kcal of food in a day? Estimate the average additional powder production of 75Kg man who is climbing a mountain at eh rate of 20 m/min (1.2)Solution )/(24560208.975)/(12160602410467000//)(104670001868.4102500sin 3S J t h mg P S J t Q t W P J Q gincrea Burning Burning =⨯⨯=∆==⨯⨯====⨯⨯=3 One cubic decimeter (1 dm 3) of water is broken into droplets having a diameter of onemicrometer (1 um) at 20℃. (1.3)(a) what is the total area of the droplets?(b) Calculate the minimum work required to produce the droplets. Assume that the dropletsare rest (have zero velocity)Water have a surface tension of 72.75 dyn/cm at 20℃ (NOTES: the term surface energy (ene/cm 2) is also used for surface tension dyn/cm)Solution)(25.218)106103(1075.72)(103)101(4)101(34)101(232523263631J S W m nS S Single total =⨯-⨯⨯⨯=∆=⨯=⨯⨯⨯⨯⨯⨯⨯⨯==-+----σππ4.Gaseous helium is to be used to quench a hot piece of metal. The helium is in storage in an insulated tank with a volume of 50 L and a temperature of 25℃, the pressure is 10 atm. Assume that helium is an ideal gas.(a) when the valve is opened and the gas escapes into the quench chamber (pressure=1 atm),what will be the temperature of the first gas to hit the specimen?(b) As the helium flows, the pressure in the tank drops. What will be the temperature of thehelium entering the quench chamber when the pressure in the tank has fallen to 1 atm? (1.4)Solution: )(180118298)(1185.229810101325501010101325)5500(1)()(118)101(298)()(0334.0/00K T T T K RR nC W T b K T P PT T Adiabatic a p C R P=-=∆-==⨯⨯⨯⨯⨯⨯⨯-⨯==∆=⨯==--5 An evacuated (P=0), insulted tank is surrounded by a very large volume (assume infinite volume) of an ideal gas at a temperature T 0. The valve on the tank is opened and the surrounding gas is allowed to flow quickly into the tank until the pressure inside the tank is equals the pressure outside. Assume that no heat flow takes place. What is the final tempeture of the gas in the tank? The heat capacity of the gas, C p and C v each may be assumed to be constant over the temperature rang spanned by the experiment. You answer may be left in terms of C p and C vhint: one way to approach the problem is to define the system as the gas ends up in the tank. (1.5)solution 0/000/00)()(T P P T T P PT T Adiabatic PPC R C R ≈-==6. Calculate the heat of reaction of methane with oxygen at 298K, assuming that the products of reaction are CO 2 and CH 4 (gas)[This heat of reaction is also called the low calorific power of methane] convert the answer into unites of Btu/1000 SCF of methane. SCF means standard cubic feet, taken at 298 and 1atmNOTE: this value is a good approximation for the low calorific powder of natural gas (1.6)DA TA:)()()(224g O H g CO g CH FOR80.5705.9489.17]/[0298---∙∆mol g Kcal Hsolution)1000/(9.2610252103048.01101076.191)/(76.191)89.1780.57205.94()2(22333332982982224422SCF Btu mol g Kcal H H H H H OH CO O CH CH O H CO =⨯⨯⨯⨯⨯=∙=∆+⨯---=∆-∆+∆-=∆+=+-7. Methane is delivered at 298 K to a glass factory, which operates a melting furnace at 1600 K. The fuel is mixed with a quantity of air, also at 298 K, which is 10% in excess of the amount theoretically needed for complete combustion (air is approximately 21% O 2 and 79% N 2) (1.7)(a) Assuming complete combustion, what is the composition of the flue gas (the gasfollowing combustion)?(b) What is the temperature of the gas, assuming no heat loss?(c) The furnace processes 2000kg of glass hourly, and its heat losses to the surroundingsaverage 400000 kJ/h. calculate the fuel consumption at STP (in m 3/h) assuming that for gas H 1600-H 298=1200KJ/KG(d) A heat exchanger is installed to transfer some of the sensible heat of the flue gas to thecombustion air. Calculate the decrease in fuel consumption if the combustion air is heated to 800KDA TA STP means T=298K, P=1atm22224O N O H CO CH for 2.82.89.117.1316)/(C mol cal C P ∙Solution)(210448.1125.9100076.191298)/(25.9)]87.012.72(2.843.179.1171.87.13[01.0)(%87.0%%12.72%%43.17%2%%71.8)11.1(221791.1231%22)(0,,222222224K T T T C mol cal X C C b O N CO O H CO O H CO O CH a i i p p p =⨯⨯+=∆+=∙=+⨯+⨯+⨯=======-⨯+⨯⨯+=+=+∑)/(1644)0224.011868.448.11)8001600(48.1125.9189570(102800000)/(189570)298800)](48.1187.8)48.1125.9[(100076.191)()/(87.848.11/]211002.22.816[)()/(3214)0224.011868.448.11)2981600(48.1125.9100076.191(102800000)/(280000040000020001200)(33min ,,,,298,,33min h m V mol g cal dTn C n C H H C mol cal X C C d h m V h KJ P C gConsu i i r p i i p p i i p r p g Consu =⨯⨯-⨯-⨯=∙=-⨯-⨯-⨯=--∆=∆∙=⨯⨯+===⨯⨯-⨯-⨯⨯==+⨯=⎰∑∑∑8.In an investigation of the thermodynamic properties of a-manganese, the following heat contents were determined: H 700-H 298=12113 J/(g atom) H 1000-H 298=22803 J/(g atom)Find a suitable equation for H T -H 298 and also for C P as a function of temperature in the form (a+bT) Assume that no structure transformation takes place in the given tempeture rang. (1.8)Solution )298(0055.0)298(62.35011.062.35011.062.3522803)2981000(2)2981000(12113)298700(2)298700(]2[2229822222982---=∆-=-===-+-=-+-+=+==∆⎰⎰T T H TC b a ba ba T baT bTdT a dT C H TP T P9.A fuel gas containing 40% CO, 10% CO 2, and the rest N 2 (by volume) is burnt completely with air in a furnace. The incoming and ongoing temperatures of the gases in the furnace are 773K and 1250K,respectively. Calculate (a) the maximum flame temperature and (b) heat supplied to the furnace per cu. ft of exhaust gas (1.9)molJ Hmol J H CO f CO f /393296/1104580,298,0,298,2-=∆-=∆)/(10184.403.29)/(1067.11010.492.19)/(1037.81020.935.44)/(1042.01097.345.283,253,253,253,222molK J T C molK J T T C molK J T T C molK J T T C N P O P CO P CO P -------⨯+=⨯-⨯+=⨯-⨯+=⨯-⨯+=Solution?0)499.0321.018.1()1067.01019.277.28(28.282831067.01038.477.289.0)1019.01058.528.33(2.0282838)()/(1019.01058.528.33722.0278.0)/(1067.01038.477.281.065.005.02.0)()/(282838110458393296%2.72%8.27%10%65%5%20)4/(1122298127332981523733253253298,,,,298,253,,,,,253,,,,,,,0,298,0,298,298,22222222222222==+--⨯+⨯++⨯=⨯-⨯++⨯⨯-⨯+-⨯=--∆=∆⨯-⨯+=+==⨯-⨯+=+++===-=∆-∆=∆========+-----------⎰⎰⎰∑∑⎰∑∑∑∑T T T T T T T dT T T dTT T dT n C n C n H H molK J T T C C n C C molK J T T C C C C n C C a mol J n Hn H H N CO production O N CO CO reation then O N air mole need fuel mole when CO O CO T TT i i r p i i p p i i N P CO P i i p p r p O P N P CO P CO P i i p p r p i pf i rf idTT T Q dT T T Q b T T T T T T T dT T T dTT T dT n C n C n H H T TT i i r p i i p p i i 9.0)1019.01058.528.33(2.02828389.0)1019.01058.528.33(2.0282838)(0)499.0321.018.1()1067.01019.277.28(28.282831067.01038.477.289.0)1019.01058.528.33(2.0282838)(253125029812502982531250298125029829812125029815231250253253298,,,,298,⨯⨯-⨯++⨯-=⨯⨯-⨯++⨯-===+--⨯+⨯++⨯=⨯-⨯++⨯⨯-⨯+-⨯=--∆=∆-----------⎰⎰⎰⎰⎰∑∑⎰10. (a) for the reaction 2221CO O CO →+,what is the enthalpy of reaction (0H ∆) at 298 K ?(b) a fuel gas, with composition 50% CO, 50% N 2 is burned using the stoichiometric amount of air. What is the composition of the flue gas?(c) If the fuel gas and the air enter there burner at 298 K, what is the highest temperaturethe flame may attain (adiabatic flame temperature)? DA TA :standard heats of formation f H ∆ at 298 K (1.10))/(393000)/(1100002mol J CO mol J CO -=-=Heat capacities [J/(mol K)] to be used for this problem N 2=33, O 2=33, CO=34, CO 2=57 Solution)(21100)298)(39889.0(222.02830000)/(3975.03325.057)/(33111.034222.033666.033)(%,75%%,251.111002.22%%1.11%%,6.66%%,2.222.0/25.015.0%)()/(283000393000110000)(,0,,,,,,22220,298,0,298,0K T T dT C n H H K mol J X C C K mol J X C C C N CO product O N CO fuel b mol J n H n H H a P p p i P r i P r i P p i P p i P f i r f ==-⨯-⨯=-∆=∆∙=⨯+⨯==∙=⨯+⨯+⨯====-====+==+-=∆-∆=∆⎰∑∑∑∑11.a particular blast furnace gas has the following composition by (volume): N 2=60%, H 2=4, CO=12%, CO 2=24%(a) if the gas at 298K is burned with the stochiometric amount of dry air at 298 K, what is the composition of the flue gas? What is the adiabatic flame temperature? (b) repeat the calculation for 30% excess combustion air at 298K(C)what is the adiabatic flame temperature when the blast furnace gas is preheated to 700K (the dry air is at 298K)(d) suppose the combustion air is not dry ( has partial pressure of water 15 mm Hg and a total pressure of 760 mm Hg) how will the flame temperature be affected? DA TA(k J/mol) (1.11)2CO CO FOR513.393523.110)/(--∆m o lkJ H f 2222,)(O N g O H CO CO FOR34505733]/[K mol J C P ∙Solution)(1052)(75438286370])295.03450(241604[026.0])335.03457(110523393513[079.0])([%8.66%%,8.6%%,6.2%%,8.15%%,9.72.0/83.110012%)()(1122)(82538313430])295.03450(241604[029.0])335.03457(110523393513[086.0])([%7.65%%,7.5%%,9.2%%,1.17%%,6.82.0/810012%2121)(,,,,,,,02222,,,,,,,0222222222K T K T T n C T T X C dT n C n C H x H N O H CO CO b K T K T T n C T T X C dT n C n C H x H N O H CO CO OH O H CO O CO a i i r P ii P i i r P i i p P i i i i r P ii P i i r P i i p P i i ===∆=∆-∆-⨯--+∆-⨯---=+--∆=∆=====⨯+====∆=∆-∆-⨯--+∆-⨯---=+--∆=∆=====+=→+→+∑∑∑⎰∑∑∑∑∑⎰∑∑)(1419),(11213842594034286.0)402(2.39714.0])295.03450(241604[029.0])335.03457(110523393513[086.0)3(K T K T T T T T H ===∆=∆⨯--∆⨯-∆-⨯--+∆-⨯---=∆12.A bath of molten copper is super cooled to 5℃ below its true melting point. Nucleation of solid copper then takes place, and the solidification proceeds under adiabatic conditions. What percentage of the bath solidifies?DATA: Heat of fusion for copper is 3100 cal/mol at 1803℃(the melting point of copper) C P,L =7.5(cal/mol ℃), C P,S =5.41+(1.5*10-3T )(cal/mol ℃) (1.12) Solution)/(310355.75.0)17981803(105.1541.5310002231798,1798,17981803,18031798,1803,mol cal H H dT C dT C HL S SL L P S P LS =⨯-⨯-⨯+⨯+==+++-⎰⎰13.Cuprous oxide (Cu 2O) is being reduced by hydrogen in a furnace at 1000K, (a)write the chemical reaction for the reduced one mole of Cu 2O(b)how much heat is release or absorbed per mole reacted? Given the quantity of heat and state whether heat is evolved (exothermic reaction) or absorbed (endothermic reaction) DATA: heat of formation of 1000K in cal/mol Cu 2O=-41900 H 2O=-59210 (1.13) solution)/(173104190059210222mol cal H OH Cu H O Cu =-=∆+=+,exothermic reaction14. (a) what is the enthalpy of pure, liquid aluminum at 1000K?(b) an electric resistance furnace is used to melt pure aluminum at the rate of 100kg/h. the furnace is fed with solid aluminum at 298K. The liquid aluminum leaves the furnace at 1000K. what is the minimum electric powder rating (kW) of furnace.DATA : For aluminum : atomic weight=27g/mol, C p,s =26(J/molK), C p,L =29(J/molK), Melting point=932K, Heat of fusion=10700J/mol (1.14)Solution )(28.0)(7.2793600110002727184)/(2718410700)9321000(29)298932(261000932,932298,1000,kW W P mol J H dT C dT C H SLL P S P l ==⨯⨯==+-⨯+-⨯=++=⎰⎰15 A waste material (dross from the melting of aluminum) is found to contain 1 wt% metallic aluminum. The rest may be assumed to aluminum oxide. The aluminum is finely divided and dispersed in the aluminum oxide; that is the two material are thermally connected.If the waster material is stored at 298K. what is the maximum temperature to which it may rise if all the metallic aluminum is oxidized by air/ the entire mass may be assumed to rise to the same temperature. Data : atomic weight Al=27g/mol, O=16g/mol, C p,s,Al =26(J/molK), C p,s,Al2O3=104J/mol, heat formation of Al 2O 3=-1676000J/mol(1.15)Solution;)(600)(3021041029927275.116122711676000K T K T T ==∆∆⨯⨯++⨯⨯=⨯⨯16 Metals exhibit some interesting properties when they are rapidly solidified from the liquid state. An apparatus for the rapid solidification of copper is cooled by water. In the apparatus, liquid copper at its melting point (1356K) is sprayed on a cooling surface, where it solidified and cools to 400K. The copper is supplied to the apparatus at the rate of one kilogram per minute. Cooling water is available at 20℃, and is not allowed to raise above 80℃. What is the minimum flow rate of water in the apparatus, in cubic meters per minute? DATA; for water: C p =4.184J/g k, Density=1g/cm 3; for copper: molecular weight=63.54g/mol C p =7cal/mol k, heat of fusion=3120 cal/mol (1.16)Solution:min)/(10573.2)2080(1min /min54.631000)]4001356(73120[min /33m V VQ Q Water Copper -⨯=-=⨯⨯-⨯+=17 water flowing through an insulated pipe at the rate of 5L/min is to be heated from 20℃ to 60℃ b an electrical resistance heater. Calculate the minimum power rating of the resistance heater in watts. Specify the system and basis for you calculation. DATA; For water C p =4.184J/g k, Density=1g/cm 3 (1.17) Solution: )(139476010005)2060(184.4W W =⨯⨯-⨯=18 The heat of evaporation of water at 100℃ and 1 atm is 2261J/mol (a) what percentage of that energy is used as work done by the vapor?(b)if the density of water vapor at 100℃ and 1 atm is 0.597kg/m 3 what is the internal energy change for the evaporation of water? (1.18)Solution: )/(375971822613101%6.71822613101%)/(31010224.0273373101325mol J Q W U mol J V P =⨯+-=+=∆=⨯==⨯⨯=∆19 water is the minimum amount of steam (at 100℃ and 1 atm pressure) required to melt a kilogram of ice (at 0℃)? Use data for problem 1.20 (1.19) Solution )(125,3341000)10018.42261(g m m =⨯=⨯+20 in certain parts of the world pressurized water from beneath the surface of the earth is available as a source of thermal energy. To make steam, the geothermal water at 180℃ is passed through a flash evaporator that operates at 1atm pressure. Two streams come out of the evaporator, liquid water and water vapor. How much water vapor is formed per kilogram of geothermal water? Is the process reversible? Assume that water is incompressible. The vapor pressure of water at 180℃ is 1.0021 Mpa( about 10 atm) Data: C P,L =4.18J/(g k), C P,v =2.00J/(g k), △H V =2261J/g, △H m =334 J/g (1.20) Solution:leirreversib g x x x )(138),1000(8018.4)8018.48022261(=-⨯⨯=⨯-⨯+The problems of the second law1 The solar energy flux is about 4J cm 2/min. in no focusing collector the surface temperature can reach a value of about 900℃. If we operate a heat engine using the collector as the heat source and a low temperature reservoir at 25℃, calculate the area of collector needed if the heat engine is to produce 1 horse power. Assume the engine operates at maximum efficiency. (2.1)Solution )(664.0)(74660104273900)25900(24m S W tWP StQ T T T W H H L H ===⨯⨯+-=-=2 A refrigerator is operated by 0.25 hp motor. If the interior of the box is to be maintained at -20℃ ganister a maximum exterior temperature of 35℃, what the maximum heat leak (in watts) into the box that can be tolerated if the motor runs continuously? Assume the coefficient of performance is 75% of the value for a reversible engine. (2.2)Solution:)(114474625.02035202733475.0%75W P P T T T P Q T T T W L LLLH HHLH =⨯⨯+-⨯=-=-=3 suppose an electrical motor supplies the work to operate a Carnot refrigerator. The interior of the refrigerator is at 0℃. Liquid water is taken in at 0℃ and converted to ice at 0℃. To convert 1 g of ice to 1 g liquid. △H=334J/g is required. If the temperature outside the box is 20℃, what mass of ice can be produced in one minute by a 0.25 hp motor runningcontinuously? Assume that the refrigerator is perfectly insulated and that the efficiencies involved have their largest possible value. (2.3)Solution: )(4576033474625.020273g m M m P P T T T P L LLLH ===⨯⨯=-=4 under 1 atm pressure, helium boils at 4.126K. The heat of vaporization is 84 J/mol what size motor (in hp) is needed to run a refrigerator that must condense 2 mol of gaseous helium at 4.126k to liquid at the same temperature in one minute? Assume that the ambient temperature is 300K and that the coefficient of performance of the refrigerator is 50% of the maximum possible. (2.4)Solution: )(52.0)(393'60284216.4216.4300'5.0%50hp W P P T T T P P Q T T T W L L L H LLLH ==⨯⨯-=-==-= 5 if a fossil fuel power plant operating between 540 and 50℃ provides the electrical powerto run a heat pump that works between 25 and 5℃, what is the amount of heat pumped into the house per unit amount of heat extracted from the power plant boiler. (a) assume that the efficiencies are equal to the theoretical maximum values(b) assume the power plant efficiency is 70% of maximum and that coefficient ofperformance of the heat pump is 10% of maximum(c) if a furnace can use 80% of the energy in fossil foe to heat the house would it be moreeconomical in terms of overall fissile fuel consumption to use a heat pump or a furnace ? do the calculations for cases a and b (2.5)solution:1,2,2,1,212,2,2,2,21,1,1,1,198.82527352527354050540)(H H H H H H L H H H L H P P P P P P P T T T P P T T T P a =+-=+-=-=-=.,)(6286.0)(1,2,not is b ok is a c P P b H H =6 calculate △U and △S when 0.5 mole of liquid water at 273 K is mixed with 0.5 mol of liquid water at 373 K and the system is allowed to reach equilibrium in an adiabaticenclosure. Assume that C p is 77J /(mol K) from 273K to 373K (2.6) Solution:)/(933.0)273323ln(5.0)373323ln(5.0)ln()ln()(02211K J C C T T C n T T C n S J U P P E P E P =+=+=∆=∆ 7 A modern coal burning power plant operates with a steam out let from the boiler at 540℃and a condensate temperature of 30℃.(a) what is the maximum electrical work that can be produced by the plant per joule of heatprovided to the boiler?(b) How many metric tons (1000kg) of coal per hour is required if the plant out put is to be500MW (megawatts). Assume the maximum efficiency for the plant. The heat of combustion of coal is 29.0 MJ/k g(c) Electricity is used to heat a home at 25℃ when the out door temperature is 10℃ bypassing a current through resistors. What is the maximum amount of heat that can be added to the home per kilowatt-hour of electrical energy supplied? (2.7)Solution:)(3.69)(6937136005000.29)()(89.013054030540)(ton kg m T T T mb J Q T T T W a LH LH H L H ==⨯=-=+-=-=)(9.191102525273)(J Q Q T T T W c H HHLH =-+=-=8 an electrical resistor is immersed in water at the boiling temperature of water (100℃) the electrical energy input into the resistor is at the rate of one kilowatt(a) calculate the rate of evaporation of the water in grams per second if the water containeris insulated that is no heat is allowed to flow to or from the water except for that provided by the resistor(b) at what rate could water could be evaporated if electrical energy were supplied at therate of 1 kw to a heat pump operating between 25 and 100℃data for water enthalpy of evaporation is 40000 J/mol at 100℃; molecular weight is 18g/mol; density is 1g/cm 3 (2.8)solution:)(23.2,2510027310010004000018)()(45.0,10004000018)(g m m b g m ma =-+===9 some aluminum parts are being quenched (cooled rapidly ) from 480℃ to -20℃ byimmersing them in a brine , which is maintained at -20℃ by a refrigerator. The aluminum is being fed into the brine at a rate of one kilogram per minute. The refrigerator operates in an environment at 30℃; that is the refrigerator may reject heat at 30℃. what is them minuspower rating in kilowatts, of motor required to operate the refrigerator? Data for aluminum heat capacity is 28J/mol K; Molecular weight 27g/mol (2.9)Solution:)(5.102)(102474202732030)20480(28271000kW W P P T T T P P L L L L H W L ==---=-=--⨯=10 an electric power generating plant has a rated output of 100MW. The boiler of the plantoperates at 300℃. The condenser operates at 40℃(a) at what rate (joules per hour) must heat be supplied to the boiler?(b) The condenser is cooled by water, which may under go a temperature rise of no morethan 10℃. What volume of cooling water in cubic meters per hour, is require to operate the plant?(c) The boiler tempeture is to be raised to 540℃,but the condensed temperature and electricoutput will remain the same. Will the cooling water requirement be increased, decreased, or remain the same?Data heat capacity 4.184, density 1g/cm 3 (2.10)Solution: )(109.7)(102.21040300273300)(1188J t P Q W P T T T P a H H L H H H ⨯==⨯=-+=-=)(1003.1184.41010)(103.4)(34611m V Q V J Q b L L ⨯==⨯⨯⨯⨯=noW P T T T P c L H H H )(10626.11040540273540)(88⨯=-+=-=11 (a) Heat engines convert heat that is available at different temperature to work. Theyhave been several proposals to generate electricity y using a heat engine that operate on the temperature differences available at different depths in the oceans. Assume that surface water is at 20℃, that water at a great depth is at 4℃, and that both may be considered to be infinite in extent. How many joules of electrical energy may be generated for each joule of energy absorbed from surface water? (b) the hydroelectric generation of electricity use the drop height of water as the energy source. in a particular region the level of river drops from 100m above sea level to 70m above the sea level . what fraction of the potential energy change between those two levels may be converted into electrical energy? how much electrical energy ,in kilowatt-hours, may be generated per cubic meter of water that undergoes such a drop? (2.11)Solution:)/(1006.136001000)()(055.0127320420)(6h kW hmg P b J Q T T T W a H H L H ⨯=⨯∆==+-=-=12 a sports facility has both an ice rink and a swimming pool. to keep the ice frozen during the summer requires the removal form the rink of 105 KJ of thermal energy per hour. It has been suggested that this task be performed by a thermodynamic machine, which would be use the swimming pool as the high temperature reservoir. The ice in the rink is to be maintain at a temperature of –15℃, and the swimming pool operates at 20℃, (a) what is the theoretical minimum power, in kilowatts, required to run the machine? (b) how much heat , in joule per hour , would be supplied t the pool by this machine? (2.12)Solution:)(1014.1101527320273)()(77.33600/10152731520)(555kJ Q b kW P T T T P a H L L L H ⨯=-+==-+=-=13solution:)/(81.6810ln 314.877.45277.6282.4)/(152940)()/(67.4977.45277.6282.4)()/(152940)(22)(2molK cal S mol cal H d molK cal S c mol cal H b AlNN Al a -=+-⨯-⨯=∆=∆-=-⨯-⨯=∆=∆=+14solution:)/(2257412000)27340273ln 184.4273336263273ln1.2()(40,010,K J dT T C T H dT T C m S WATER P m mICE P =+++=+∆+=∆⎰⎰- 15)(70428)(2896100077773002J W J Q T T T W L L L H ==-=-=16)(4.3719))2.4300(314.85.13.83(3002.4300)(7.58663.832.42.4300J Q T T T W J Q T T T W H H L H L L L H =-⨯+-=-==-=-=17yesd Q c K J PPnR S b J pdV n W Q OU T a )(0)()/(1.1910ln 314.81ln )()(570410ln 298314.810)(0==⨯⨯==∆=⨯⨯=-=-==∆=∆⎰18)(122233527302033560500g m m m T T T L L H =-=-=⨯教材各章习题参考答案 (魏)3.2 ΔG = -108.9 J/mol; ΔS = -21.42 J/(mol.K)3.6 (a ) 22.09/(.)S J mol K ∆=;(b) At 0︒C, ∆G =0; (c) ∆H = 5841.9 J;(d) ∆S =21.39J /(mol.K),∆G = 109.38 J/mol4.1 (a ) 2898.28J/mol; ( b ) No; ( c ) 345 J/mol; ( d ) 14939 atm; ( e )4921 J/mol4.2 ( a ) 272.8K; ( b ) Pa P 610345⨯≈∆ ; ( c ) 249.46K 4.3 1202K4.4 P=5.73⨯10-6 atm 4.5 0.16P4.7 08.10430685ln +-=TP 4.8 ( a ) 1180K; ( b ) 695.3K; ( c ) 114.4kJ/mol; ( d ) 7123 J/mol; ( e )4.2J/mol4.9 In the initial state: 4.06 mol %; in the final state:5.3 mol% 4.10 ( a )348 kJ; ( b ) 2.3×10-3Pa ;( c ) “ solution not possible ”; (d ) “solution not possible ”5.1 atm p H 0005.0= 5.2、atmp o 1221007.1-⨯=If the error in enthalpy is 500cal, the uncertainty in the pressure calculated is 28.6%, and if the error in enthalpy is -500cal, the uncertainty is -22.1%5.3、(a) T =462K; (b) T = 420K5.4 (a) atm P O 2621014.1-⨯=, (b) P O2 =2.28⨯10-10 atm., (c) The equilibriumoxygen pressure remains the same when the total pressure increases, which means a higher purity level of N 2 .5.5 (a) 略; (b) Pa atm P H 8.181013056.1800019.0)('2=⨯==; (c) 21.5L Ar isneeded to be bubbled into the melt.5.6(a )l n K a1/T, 10-31/K=∆-=∆o o G kJ H 1000;50- 66.6kJ(b) Ja = 3 < Ka, the reaction will proceed from left to right, and theatmosphere will not oxidize Ni. 5.7 略5.8. (a) P SiO = 8.1⨯10-8 (atm) (b) ∆H o = 639500J; ∆So =334.9J/K (c ) PO2 =10-30 atm 5.9 5.10.J H o72250=∆,the reaction is an endothermic one.5.11. (a),166528J H o =∆ the reaction is an endothermic one.; (b) At 1168K, the equilibrium pressure of CO2 equals one atmosphere.)(106.08)(atm Pg u -⨯=5.12 (a) 略 , (b) Mg CO P P =; (c) T = 2037 K 5.13 (a) 略; (b) 13109.2⨯=K ; (c) ppm 186.0 5.14 (a) 略; (b) kJ H 52.267=∆; (c) K T 1592= 5.15 (a) )(106.13atm -⨯≈; (b) )(1028.210)(2atm P g O H -⨯=5.16 (a) 97.9=K ; (b) atm x 14.4=; (c) if the temperature is increased, the fraction of water reacted will increase since the equilibria constant increases with increasing temperature.6.2 (a )1.287V;(b) When the water impure, the voltage will go higher; (c) 1.219V 6.4 (a) 145.3kJ;(b) The maximum work that could be derived is 702.36kJ; (c) In this case, the maximum work that could be derived is696.56kJ.6.5 (a) -6252J/mol; (b) 370.0)(=II Cd a ; (c) )(42.3mmHg P Cd =; 6.67.87⨯10-4 V 6.7 (a))(22g Cl Mg MgCl +=(b) Pa P Cl 21'1086.82-⨯=;(c) 2.485V6.8 (a) Pa P O 11'2105.5-⨯=;(b) Anode: e Ni Ni 2+→Cathode: -→+2222/1O e O ;(c) 0.757V; (d) 0.261V6.10 (a) )(509.3V E o=;(b) 0.074kJ;(c) 4.1⨯106J;(d) Yes. In this case, the open circuit voltage is 3.648V;(e) In this case, to keep the temperature constant, 3.92⨯106J heatshould be removed from the battery per hour. 6.11(a) TG CO Al C O Al o 26.3211008.12/322/36232-⨯=+=+Δ(b) The minimum voltage at which the electrolysis may be carriedout at 1250K is 1.172V .7.1 0.117 atm 7.5 ( a ) ,82.5 2.5 2.5B A BA BB T PV V V x x x x x ⎛⎫∂=+=--⎪∂⎝⎭ ,102.5 2.5 2.5A B A A B A T PV V V x x x x x ⎛⎫∂=+=-- ⎪∂⎝⎭( b) B A M x x V 5.2=7.7 2)1(736.0ln Sn Sn x --=γ7.8 The maximum solubility of MgF2 in liquid MgCl at 900︒C is 19。
材料热力学习题
1熟悉的条件、表达式及意义()。
2. 熟悉配分函数的条件、表达式及意义()。
3.三大分布是什么?,表达式?
4、热力学函数的微分表达式;热力学意义定律,第二定律;
5、固溶体中配置熵的计算;高分子模型中配置熵的计算;
6、分析铁基马氏体与有色金属中马氏体相变时的动力与阻力。
7、交互作用参数意义,各参数变化对其影响;
8、正规熔体及热函数表达式
9、在定压热容C p的经验表达式中,,试导出这时的焓(H)、熵(S)和Gibbs自由能(G)的表达式。
10、利用讨论偏析引起的自由能的变化。
复习题(材料热力学)1、体系与环境之间的关系?体系分为几种类型?其划分依据是什么?2、状态变数与状态函数?状态函数的特点是什么?3、分别阐述热力学第一定律、第二定律和第三定律?4、推导可逆过程体积功的表达式?5、设有64×10-3 kg氧气,在25℃下极缓慢地膨胀,使其体积由0.05 m3变为0.1 m3。
计算该过程气体所做的体积功。
6、设有10 mol氢气,在25 ℃下可逆压缩,使其压力增大3倍。
计算该过程气体所做的体积功。
7、推导焓的表达式?并解释其物理意义?8、在1大气压下,1 mol的水从25℃加热至150 ℃,计算该过程中的Q,W以及△U和△H。
9、推导基尔霍夫定律,并说明反应热与比热容变△Cp之间的关系。
10、熵的定义及其统计意义是什么?11、熵变计算:A.1 mol理想气体,在恒温T下体积增大10倍,求其熵变(1)设为可逆过程;(2) 设向真空膨胀。
B. 铅的熔点为600 K,凝固热为4811.6 J/mol,求铅在600 K凝固时熵值的变化(1 atm)C. 求液体铅过冷至590 K凝固时熵值的变化(1 atm)。
12、简述Richard和Trouton规则13、自由能和自由焓的表达式分别是什么?14、简述最小自由能原理?15、推导热力学基本关系式:VP S T U d d d -=PV S T H d d d +=VP T S F d d d --=P V T S G d d d +-=⎛⎛⎛⎛⎛⎛⎛⎛P V U T S U S V =-,⎪⎭⎫ ⎝∂∂=⎪⎭⎫ ⎝∂∂V P H T S H S P =,⎪⎭⎫ ⎝∂∂=⎪⎭⎫ ⎝∂∂P V F S T F T V -⎪⎭⎫ ⎝∂∂-=⎪⎭⎫ ⎝∂∂=,V P G S T G T P =,⎪⎭⎫ ⎝∂∂-=⎪⎭⎫ ⎝∂∂16、 什么是饱和蒸汽压?蒸汽压与体系自由能之间关系的表达式是什么? 17、 推导Gibbs-Helmholtz 方程,并简述相变自由能与温度关系的计算过程。
2009-2010 年 秋 季学期研究生课程考试试题考 试 科 目:材料热力学与动力学 学生所在院(系):材料学院、航天学院学生所在学科:材料学、材料加工工程 (* 题签与答题纸一起上交)一、仔细阅读下列论述,判断正误,如果错误,请说明该论述违反了哪些热力学原理,并给出正确的论述。
(16分)(1) 纯金属中不存在空位时的吉布斯自由能最低。
(2) 可采用公切线法则确定晶界偏析(晶界相成分)。
(3) 材料变形过程的热力学流是扩散通量。
(4) 低压下不可能将石墨转变为金刚石。
二、(1)固态纯组元的G-T 曲线如下图所示,请判断哪条线正确,并解释原因。
(6分)(2)A-B 二元系中,固相和液相的摩尔自由能-成分曲线如下图所示。
请在自由能-成分曲线上,图示出体系成分为X*处,固相纯A 和液相纯B 混合后的吉布斯自由能的变化量∆G mix ,并说明原因。
(6分) (此题请直接答在题签上)三、简答题:(1) 请说明化学位和活度的物理意义。
(6分)(2) 简述Calphad 的三要素及其主要功能。
(6分)(3) 请解释Onsager 倒易关系、最小熵产生原理。
(6分)四、某些在平衡条件下固态互不混溶的二元系(I AB >0),通过高能球磨或高压扭转等剧烈塑性形变(应变量非常大)实现纳米化后,可发现两个组元的相互固溶度会显著提高。
试从热力学的角度解释该现象。
(8分)学院学号 姓名五、15克金和25克银混合后形成单相理想固溶体,问(1)金和银的摩尔分数各是多少?(2)固溶体总的混合熵是多少?(3)500o C 时,摩尔自由能变化为多少?(4)令纯金和纯银的自由能为零,那么500o C 时金和银的化学势各为多少?(5)在500o C 加入一个金原子,固溶体的自由能变化为多少?已知:金的原子量为197,银的原子量为108,气体常数R 为8.314J·mol -1·K -1. (15分)六、试通过如图所示的A-B 二元相图,判断A-B 固溶体的性质、溶体组元间的相互作用能。