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(4) NH4HS(s) is in equilibrium with arbitrary NH3(g) and H2S(g);

(5)Put I2 as solute in immiscible liquid H2O and CCl4, reaching distribution equilibrium(condensed system).

´ð°¸: (1)1,2,1;(2) 2,3,1;(3) 1,2,1; (4)2,2,2; (5)3,2,2

2.ÒÑÖªÒºÌå¼×±½(A)ºÍÒºÌå±½(B)ÔÚ90¡æʱµÄ±¥ºÍÕôÆøѹ·Ö±ðΪp?A?54.22kPaºÍ

?pB?136.12kPa.Á½Õß¿ÉÐγÉÀíÏëҺ̬»ìºÏÎï.½ñÓÐϵͳ×é³ÉΪxB,0?0.3µÄ¼×±½-±½

»ìºÏÎï5mol,ÔÚ90¡æϳÉÆø-ÒºÁ½Ïàƽºâ,ÈôÆøÏà×é³ÉΪyB?0.4556,Çó: (1)ƽºâʱҺÏà×é³ÉxB¼°ÏµÍ³µÄѹÁ¦p;

(2)ƽºâʱÆø-ÒºÁ½ÏàµÄÎïÖʵÄÁ¿n(l),n(g). At 90 ¡æ, toluene(A) and benzene(B) can form ideal liquid mixture. The saturated vapor pressure of them is 54.22kPa and 136.13kPa respectively, Now 5 mol mixture of them withxB,0?0.3,when g-l reaches equilibrium at 90¡æ,the the composition of the gas phase is yB?0.4556,please Calculate :

(1) how the composition of the liquid phasexB and total pressure of system p. (2) The amout of substance n(l),n(g) when g-l reach equilibrium

´ð°¸: (1)xB?0.2500,p?74.70kPa;(2)n?l??3.784mol,n?g??1.216mol 3. .ÒÑÖªÒºÌå¼×±½(A)ºÍÒºÌå±½(B)ÔÚ90¡æʱµÄ±¥ºÍÕôÆøѹ·Ö±ðΪp?A?54.22kPaºÍ

?pB?136.12kPa.Á½Õß¿ÉÐγÉÀíÏëҺ̬»ìºÏÎï.È¡200.0g¼×±½ºÍ200.0g±½ÖÃÓÚ´ø»îÈû

µÄµ¼ÈÈÈÝÆ÷ÖÐ,ʼ̬Ϊһ¶¨Ñ¹Á¦ÏÂ90¡æµÄҺ̬»ìºÏÎï.ÔÚºãÎÂ90¡æÏÂÖð½¥½µµÍѹÁ¦,ÎÊ: (1)ѹÁ¦½µµ½¶àÉÙʱ,¿ªÊ¼²úÉúÆøÏà,´ËÆøÏàµÄ×é³ÉÈçºÎ?

(2)ѹÁ¦½µµ½¶àÉÙʱ,ÒºÏ࿪ʼÏûʧ,×îºóÒ»µÎÒºÏàµÄ×é³ÉÈçºÎ?

(3)ѹÁ¦Îª92.00kPaʱ,ϵͳÄÚÆø-ÒºÁ½Ïàƽºâ,Á½ÏàµÄ×é³ÉÈçºÎ?Á½ÏàÎïÖʵÄÁ¿¸÷Ϊ¶àÉÙ? At 90 ¡æ, toluene(A) and benzene(B) can form ideal liquid mixture. The saturated vapor pressure of them is 54.22kPa and 136.13kPa respectively, If 200.0g C7H8 and 200.0g C6H6 was put into a thermal conducting container with a piston, keep the temperature of 90 ¡æand decrease the pressure gradually, Calculate :

(1)How much the pressure is,when the gas begins to product?And how the composition of

the gas phase is?

(2)How much the pressure is, when the liquid begins to disappear?And how the composition of the last drop of liquid is?

(3)If the pressure is 92kPa, how the gas-liquid composition in the system is?And how much the amount of substance both gas and liquid phase? ´ð°¸:

(1)p?98.54kPa,yB?0.7476;?2?p?80.40kPa,xB?0.3197;(3)n?l??3.022mol,n?g??1.709mol

4.ÒÑ֪ˮ-±½·ÓϵͳÔÚ30¡æÒº-Һƽºâʱ¹²éîÈÜÒºµÄ×é³Éw(±½·Ó)Ϊ:L1(±½·ÓÈÜÓÚË®),8.75%;L2(Ë®ÈÜÓÚ±½·Ó),69.9%. (1)ÔÚ30¡æ,100g±½·ÓºÍ200gË®ÐγɵÄϵͳ´ïÒº-Һƽºâʱ,Á½ÒºÏàµÄÖÊÁ¿¸÷Ϊ¶àÉÙ? (2)ÔÚÉÏÊöϵͳÖÐÈôÔÙ¼ÓÈë100g±½·Ó,ÓÖ´ïµ½Ïàƽºâʱ,Á½ÒºÏàµÄÖÊÁ¿¸÷Ϊ¶àÉÙ? Given that C6H5OH and H2O reaches liquid-liquid equilibrium at 30¡æ, the composition of the two conjugate solutions of this system are w(C6H5OH£¬L1)= 8.75%£¬w(C6H5OH£¬L2)= 69.9% respectively.

(1) At 30¡æ,t he system formed by 100g C6H5OH and 200g H2O reaches liquid-liquid equilibrium ,please calculate the mass of the two liquid phase.

(2) If 100g C6H5OH was added into the above system ,when the system reaches

liquid-liquid equilibrium again, please calculate the mass of the two liquid phase. ´ð°¸: (1)m?L1??179.6g,m?L2??120.4g;?2?m?L1??130.2g,m?L2??269.8g 6.ÀûÓÃÏÂÁÐÊý¾Ý,´ÖÂÔµØÃè»æ³öMg-Cu¶þ×é·ÖÄý¾ÛϵͳÏàͼ,²¢±ê³ö¸÷ÇøµÄÎȶ¨Ïà.ÒÑÖªMgºÍCuµÄÈÛµã·Ö±ðΪ648¡æ,1085¡æ.Á½Õß¿ÉÐγÉÁ½ÖÖÎȶ¨»¯ºÏÎï,Mg2Cu,MgCu2,ÆäÈÛµãÒÀ´ÎΪ580¡æ,800¡æ.Á½ÖÖ½ðÊôÓëÁ½ÖÖ»¯ºÏÎïËÄÕßÖ®¼äÐγÉÈýÖֵ͹²ÈÛ»ìºÏÎï.µÍ¹²ÈÛ»¯ºÏÎïµÄ×é³É¼°ÈÛµã¶ÔӦΪ:35%,380¡æ;66%,560¡æ;90.6%,680¡æ.

Using the data below, a rough describe Mg-Cu two component condensing system phase diagram and point out the stable phase of every region. Given Melting point of Mg and Cu is 648¡æ and 1085¡æ respectively.They can form of two stable compounds Mg2Cu and MgCu2 whose melting point are 580¡æ,800¡æ respectively. Two metal and two compounds can form three kinds of eutectic mixture.Composition of eutectic mixture w(Cu) and eutectic point corresponding are: 35%,380¡æ;66%,560¡æ;90.6%,680¡æ. 7.AºÍB¹Ì̬ʱÍêÈ«²»»¥ÈÜ£¬102325PaʱA(s)µÄÈÛµãΪ30¡æ£¬B(s)µÄÈÛµãΪ50¡æ£¬AºÍBÔÚ10¡æ¾ßÓÐ×îµÍ¹²È۵㣬Æä×é³ÉΪxB,E=0.4£¬ÉèAºÍBÏ໥Èܽâ¶È¾ùΪֱÏß¡£

(1)»­³ö¸ÃϵͳµÄÈÛµã-×é³Éͼ(t-xBͼ)£»

(2)½ñÓÉ2molAºÍ8molB×é³Éһϵͳ£¬¸ù¾Ý»­³öµÄt-xBͼ£¬Áбí»Ø´ðϵͳÔÚ5¡æ£¬ 30¡æ£¬50¡æʱµÄÏàÊý¡¢ÏàµÄ¾Û¼¯Ì¬¼°³É·Ö¡¢¸÷ÏàµÄÎïÖʵÄÁ¿¡¢ÏµÍ³ËùÔÚÏàÇøµÄÌõ¼þ×ÔÓɶȡ£ A and B are immiscible in solid phase, at p=101325Pa, the melting point of A and B are30?C and 50?C respectively. A and B has the lowest cocrystalline point at 10¡æ, its component is xB,E=0.4,supposing the dissolving line is straight line.

(1)Draw melting point-composition diagram (t-xB)of this system.

(2)Now the system formed by 2mol A and 8mol B , according to (t-xB)Phase diagram, list table and write P , state of aggregation(g, l or s) and ingredient of phase, amount of the phases and f ¡¯ of regions when the system temperature is 5¡æ£¬ 30¡æ£¬50¡æ respectivly . ´ð°¸: (2) ϵͳµÄζÈ/¡æ 5 30 50 ÏàÊý 2 2 1 ÏàµÄ¾Û¼¯Ì¬¼°³É·Ö S(A)+ S(B) l(A+B)+ S(B) l(A+B) ¸÷ÏàµÄÁ¿ nA=2mol nB=8mol nl=6.67mol nB=3.33mol nl=10mol ϵͳËùÔÚÏàÇøµÄF¡¯ 1 1 2 8. AºÍBÔÚҺ̬²¿·Ö»¥ÈÜ£¬AºÍBÔÚ100kPaϵķеã·Ö±ðΪ100? CºÍ120?C£¬¸Ã¶þ×é·ÖµÄÆø¡¢ÒºÆ½ºâÏàͼÈçͼËùʾ£¬ÇÒÖªC£¬E£¬DÈý¸öÏàµãµÄ×é³É·Ö±ðΪxB,C = 0.05, yB,E = 0.60£¬ xB,D = 0.97

(1)ÊÔ½«Í¼Öи÷ÏàÇø¼°CEDÏßËù´ú±íµÄÏàÇøµÄÏàÊý¡¢¾Û¼¯Ì¬¼°³É·Ö£¨¾Û¼¯Ì¬ÓÃg£¬l¼°s±íʾÆø¡¢Òº¼°¹Ì£»³É·ÖÓÃA£¬B»òA+B±íʾ£©¡¢Ìõ¼þ×ÔÓɶÈf ¡¯Áгɱí¸ñ£»

(2)ÊÔ¼ÆËã3mol BÓë7mol AµÄ»ìºÏÎÔÚ100kPa£¬80?C´ï³ÉƽºâʱÆø¡¢ÒºÁ½Ïà¸÷ÏàµÄÎïÖʵÄÁ¿¸÷Ϊ¶àÉÙĦ¶û£¿

A and B are partially miscible in liquid phase,

at p=100kPa, the boiling point are100?C and 120?C respectively. In the gas-liquid

equilibrium phase diagram, the composition of phase point C, E and D are xB,C = 0.05, yB,E = 0.60 and xB,D = 0.97 respectively.

(1) list table and write P , state of aggregation(g, l or s) and ingredient(A, B or A+B) of phase and f ¡¯ of all regions and CED line.

(2) mixture formed by 3mol B and 7mol A reaches gas-liquid equilibrium at 100kPa£¬80?C . Please calculate n(l) and n(g). ´ð°¸: n (g) = 5.7 mol n ( l ) = 4.3 mol

9.ÈçͼËùʾ£¬ÔÚ101.325 kPa Ï£¬A£¬B ¶þ×é·ÖҺ̬ÍêÈ«»¥ÈÜ£¬¹Ì̬ÍêÈ«²»»¥ÈÜ£¬ÆäµÍ¹²ÈÛ»ìºÏÎïwB= 0.60 ½ñÓÐ180 g£¬wB= 0.40 µÄÈÜÒº£¬ÊԻشð£º

£¨1£©Àäȴʱ£¬×î¶à¿ÉµÃ¶àÉÙ¿Ë´¿A(s)£¿

£¨2£©ÔÚÈýÏàƽºâʱ£¬ÈôµÍ¹²ÈÛ»ìºÏÒºµÄÖÊÁ¿Îª60 g ,ÓëÆäƽºâµÄ¹ÌÌåA¼°B¸÷Ϊ¶àÉÙ¿Ë£¿

As shown in the diagram, A and B are miscible in liquid phase and immiscible in solid phase at p=101.325kPa, the lowest cocrystalline component is wB=

0.60, Now 180g solution with wB= 0.40.Calculate:

(1)How much pure A(s) we can get when the solution was cooled.

(2) the amount of A and B when the system reaches triple phase equilibrium and the mass of the lowest cocrystalline solution is 60g.

´ð°¸: (1) µÃµ½60g´¿A(s);(2) ÈôµÍ¹²ÈÛ»ìºÏÎïµÄÖÊÁ¿Îª60gʱ£¬ÓëÆäƽºâµÄ¹Ì

ÌåAΪ84g ¹ÌÌåBΪ36g

10. ͼΪA£¬B¶þ×é·ÖÄý¾ÛϵͳƽºâÏàͼ¡£tA*£¬tB* ·Ö±ðΪA£¬B µÄÈ۵㡣

£¨1£©Çë¸ù¾ÝËù¸øÏàͼÁбíÌîдI ÖÁ VI ¸÷ÏàÇøµÄÏàÊý¡¢ÏàµÄ¾Û¼¯Ì¬¼°³É·Ö¡¢Ìõ¼þ×ÔÓɶÈÊý£»

£¨2£©ÏµÍ³µãa0 ½µÎ¾­¹ýa1£¬a2£¬a3£¬a4£¬Ð´³öÔÚa1£¬a2£¬a3 ºÍa4µãϵͳÏà̬·¢ÉúµÄ±ä»¯²¢»­³ö²»ÀäÇúÏß¡£

It¡¯s the phase diagram of A and B. tA*£¬tB* is the melting point of A and B respectively.

(1) According to the phase diagram, list table and write P , state of aggregation(g, l or s) and ingredient(A, B or A+B) of phase and f ¡¯ of regions from I to VI.

(2) The system point pass through a1£¬a2£¬a3£¬a4 when cooling, write out the system phase state changes at point a1£¬a2£¬a3,a4 and draw the cooling curve.

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