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905-908
e , p1 0 < p2 The composition of vapour phase in0 equilibrium with the solution is determined by the partial pressures of the components If y1 and y2 are the mole fractions of the Fig
1
906-909
, p1 0 < p2 The composition of vapour phase in0 equilibrium with the solution is determined by the partial pressures of the components If y1 and y2 are the mole fractions of the Fig 1
1
907-910
equilibrium with the solution is determined by the partial pressures of the components If y1 and y2 are the mole fractions of the Fig 1 3: The plot of vapour pressure and mole fraction of an ideal solution at constant temperature
1
908-911
If y1 and y2 are the mole fractions of the Fig 1 3: The plot of vapour pressure and mole fraction of an ideal solution at constant temperature The dashed lines I and II represent the partial pressure of the components
1
909-912
1 3: The plot of vapour pressure and mole fraction of an ideal solution at constant temperature The dashed lines I and II represent the partial pressure of the components (It can be seen from the plot that p1 and p2 are directly proportional to x1 and x2, respectively)
1
910-913
3: The plot of vapour pressure and mole fraction of an ideal solution at constant temperature The dashed lines I and II represent the partial pressure of the components (It can be seen from the plot that p1 and p2 are directly proportional to x1 and x2, respectively) The total vapour pressure is given by line marked III in the figure
1
911-914
The dashed lines I and II represent the partial pressure of the components (It can be seen from the plot that p1 and p2 are directly proportional to x1 and x2, respectively) The total vapour pressure is given by line marked III in the figure Rationalised 2023-24 11 Solutions components 1 and 2 respectively in the vapour phase then, using Dalton’s law of partial pressures: p1 = y1 ptotal (1
1
912-915
(It can be seen from the plot that p1 and p2 are directly proportional to x1 and x2, respectively) The total vapour pressure is given by line marked III in the figure Rationalised 2023-24 11 Solutions components 1 and 2 respectively in the vapour phase then, using Dalton’s law of partial pressures: p1 = y1 ptotal (1 17) p2 = y2 ptotal (1
1
913-916
The total vapour pressure is given by line marked III in the figure Rationalised 2023-24 11 Solutions components 1 and 2 respectively in the vapour phase then, using Dalton’s law of partial pressures: p1 = y1 ptotal (1 17) p2 = y2 ptotal (1 18) In general pi = yi ptotal (1
1
914-917
Rationalised 2023-24 11 Solutions components 1 and 2 respectively in the vapour phase then, using Dalton’s law of partial pressures: p1 = y1 ptotal (1 17) p2 = y2 ptotal (1 18) In general pi = yi ptotal (1 19) Vapour pressure of chloroform (CHCl3) and dichloromethane (CH2Cl2) at 298 K are 200 mm Hg and 415 mm Hg respectively
1
915-918
17) p2 = y2 ptotal (1 18) In general pi = yi ptotal (1 19) Vapour pressure of chloroform (CHCl3) and dichloromethane (CH2Cl2) at 298 K are 200 mm Hg and 415 mm Hg respectively (i) Calculate the vapour pressure of the solution prepared by mixing 25
1
916-919
18) In general pi = yi ptotal (1 19) Vapour pressure of chloroform (CHCl3) and dichloromethane (CH2Cl2) at 298 K are 200 mm Hg and 415 mm Hg respectively (i) Calculate the vapour pressure of the solution prepared by mixing 25 5 g of CHCl3 and 40 g of CH2Cl2 at 298 K and, (ii) mole fractions of each component in vapour phase
1
917-920
19) Vapour pressure of chloroform (CHCl3) and dichloromethane (CH2Cl2) at 298 K are 200 mm Hg and 415 mm Hg respectively (i) Calculate the vapour pressure of the solution prepared by mixing 25 5 g of CHCl3 and 40 g of CH2Cl2 at 298 K and, (ii) mole fractions of each component in vapour phase (i) Molar mass of CH2Cl2 = 12 × 1 + 1 × 2 + 35
1
918-921
(i) Calculate the vapour pressure of the solution prepared by mixing 25 5 g of CHCl3 and 40 g of CH2Cl2 at 298 K and, (ii) mole fractions of each component in vapour phase (i) Molar mass of CH2Cl2 = 12 × 1 + 1 × 2 + 35 5 × 2 = 85 g mol–1 Molar mass of CHCl3 = 12 × 1 + 1 × 1 + 35
1
919-922
5 g of CHCl3 and 40 g of CH2Cl2 at 298 K and, (ii) mole fractions of each component in vapour phase (i) Molar mass of CH2Cl2 = 12 × 1 + 1 × 2 + 35 5 × 2 = 85 g mol–1 Molar mass of CHCl3 = 12 × 1 + 1 × 1 + 35 5 × 3 = 119
1
920-923
(i) Molar mass of CH2Cl2 = 12 × 1 + 1 × 2 + 35 5 × 2 = 85 g mol–1 Molar mass of CHCl3 = 12 × 1 + 1 × 1 + 35 5 × 3 = 119 5 g mol-1 Moles of CH2Cl2 = 1 40 g 85 g mol = 0
1
921-924
5 × 2 = 85 g mol–1 Molar mass of CHCl3 = 12 × 1 + 1 × 1 + 35 5 × 3 = 119 5 g mol-1 Moles of CH2Cl2 = 1 40 g 85 g mol = 0 47 mol Moles of CHCl3 = 1 25
1
922-925
5 × 3 = 119 5 g mol-1 Moles of CH2Cl2 = 1 40 g 85 g mol = 0 47 mol Moles of CHCl3 = 1 25 5 g 119
1
923-926
5 g mol-1 Moles of CH2Cl2 = 1 40 g 85 g mol = 0 47 mol Moles of CHCl3 = 1 25 5 g 119 5 g mol = 0
1
924-927
47 mol Moles of CHCl3 = 1 25 5 g 119 5 g mol = 0 213 mol Total number of moles = 0
1
925-928
5 g 119 5 g mol = 0 213 mol Total number of moles = 0 47 + 0
1
926-929
5 g mol = 0 213 mol Total number of moles = 0 47 + 0 213 = 0
1
927-930
213 mol Total number of moles = 0 47 + 0 213 = 0 683 mol 2 xCH Cl2 = 0
1
928-931
47 + 0 213 = 0 683 mol 2 xCH Cl2 = 0 47 mol 0
1
929-932
213 = 0 683 mol 2 xCH Cl2 = 0 47 mol 0 683 mol = 0
1
930-933
683 mol 2 xCH Cl2 = 0 47 mol 0 683 mol = 0 688 xCHCl3 = 1
1
931-934
47 mol 0 683 mol = 0 688 xCHCl3 = 1 00 – 0
1
932-935
683 mol = 0 688 xCHCl3 = 1 00 – 0 688 = 0
1
933-936
688 xCHCl3 = 1 00 – 0 688 = 0 312 Using equation (2
1
934-937
00 – 0 688 = 0 312 Using equation (2 16), ptotal = p1 0 + (p2 0 – p1 0) x2 = 200 + (415 – 200) × 0
1
935-938
688 = 0 312 Using equation (2 16), ptotal = p1 0 + (p2 0 – p1 0) x2 = 200 + (415 – 200) × 0 688 = 200 + 147
1
936-939
312 Using equation (2 16), ptotal = p1 0 + (p2 0 – p1 0) x2 = 200 + (415 – 200) × 0 688 = 200 + 147 9 = 347
1
937-940
16), ptotal = p1 0 + (p2 0 – p1 0) x2 = 200 + (415 – 200) × 0 688 = 200 + 147 9 = 347 9 mm Hg (ii) Using the relation (2
1
938-941
688 = 200 + 147 9 = 347 9 mm Hg (ii) Using the relation (2 19), yi = pi/ptotal, we can calculate the mole fraction of the components in gas phase (yi)
1
939-942
9 = 347 9 mm Hg (ii) Using the relation (2 19), yi = pi/ptotal, we can calculate the mole fraction of the components in gas phase (yi) 2 pCH Cl2 = 0
1
940-943
9 mm Hg (ii) Using the relation (2 19), yi = pi/ptotal, we can calculate the mole fraction of the components in gas phase (yi) 2 pCH Cl2 = 0 688 × 415 mm Hg = 285
1
941-944
19), yi = pi/ptotal, we can calculate the mole fraction of the components in gas phase (yi) 2 pCH Cl2 = 0 688 × 415 mm Hg = 285 5 mm Hg pCHCl3 = 0
1
942-945
2 pCH Cl2 = 0 688 × 415 mm Hg = 285 5 mm Hg pCHCl3 = 0 312 × 200 mm Hg = 62
1
943-946
688 × 415 mm Hg = 285 5 mm Hg pCHCl3 = 0 312 × 200 mm Hg = 62 4 mm Hg 2 yCH Cl2 = 285
1
944-947
5 mm Hg pCHCl3 = 0 312 × 200 mm Hg = 62 4 mm Hg 2 yCH Cl2 = 285 5 mm Hg/347
1
945-948
312 × 200 mm Hg = 62 4 mm Hg 2 yCH Cl2 = 285 5 mm Hg/347 9 mm Hg = 0
1
946-949
4 mm Hg 2 yCH Cl2 = 285 5 mm Hg/347 9 mm Hg = 0 82 yCHCl3 = 62
1
947-950
5 mm Hg/347 9 mm Hg = 0 82 yCHCl3 = 62 4 mm Hg/347
1
948-951
9 mm Hg = 0 82 yCHCl3 = 62 4 mm Hg/347 9 mm Hg = 0
1
949-952
82 yCHCl3 = 62 4 mm Hg/347 9 mm Hg = 0 18 Note: Since, CH2Cl2 is a more volatile component than CHCl3, [ 2 p0CH Cl2 = 415 mm Hg and p0CHCl3 = 200 mm Hg] and the vapour phase is also richer in CH2Cl2 [ 2 yCH Cl2 = 0
1
950-953
4 mm Hg/347 9 mm Hg = 0 18 Note: Since, CH2Cl2 is a more volatile component than CHCl3, [ 2 p0CH Cl2 = 415 mm Hg and p0CHCl3 = 200 mm Hg] and the vapour phase is also richer in CH2Cl2 [ 2 yCH Cl2 = 0 82 and yCHCl3 = 0
1
951-954
9 mm Hg = 0 18 Note: Since, CH2Cl2 is a more volatile component than CHCl3, [ 2 p0CH Cl2 = 415 mm Hg and p0CHCl3 = 200 mm Hg] and the vapour phase is also richer in CH2Cl2 [ 2 yCH Cl2 = 0 82 and yCHCl3 = 0 18], it may thus be concluded that at equilibrium, vapour phase will be always rich in the component which is more volatile
1
952-955
18 Note: Since, CH2Cl2 is a more volatile component than CHCl3, [ 2 p0CH Cl2 = 415 mm Hg and p0CHCl3 = 200 mm Hg] and the vapour phase is also richer in CH2Cl2 [ 2 yCH Cl2 = 0 82 and yCHCl3 = 0 18], it may thus be concluded that at equilibrium, vapour phase will be always rich in the component which is more volatile Example 1
1
953-956
82 and yCHCl3 = 0 18], it may thus be concluded that at equilibrium, vapour phase will be always rich in the component which is more volatile Example 1 5 Example 1
1
954-957
18], it may thus be concluded that at equilibrium, vapour phase will be always rich in the component which is more volatile Example 1 5 Example 1 5 Example 1
1
955-958
Example 1 5 Example 1 5 Example 1 5 Example 1
1
956-959
5 Example 1 5 Example 1 5 Example 1 5 Example 1
1
957-960
5 Example 1 5 Example 1 5 Example 1 5 Solution Solution Solution Solution Solution Rationalised 2023-24 12 Chemistry According to Raoult’s law, the vapour pressure of a volatile component in a given solution is given by pi = xi pi 0
1
958-961
5 Example 1 5 Example 1 5 Solution Solution Solution Solution Solution Rationalised 2023-24 12 Chemistry According to Raoult’s law, the vapour pressure of a volatile component in a given solution is given by pi = xi pi 0 In the solution of a gas in a liquid, one of the components is so volatile that it exists as a gas and we have already seen that its solubility is given by Henry’s law which states that p = KH x
1
959-962
5 Example 1 5 Solution Solution Solution Solution Solution Rationalised 2023-24 12 Chemistry According to Raoult’s law, the vapour pressure of a volatile component in a given solution is given by pi = xi pi 0 In the solution of a gas in a liquid, one of the components is so volatile that it exists as a gas and we have already seen that its solubility is given by Henry’s law which states that p = KH x If we compare the equations for Raoult’s law and Henry’s law, it can be seen that the partial pressure of the volatile component or gas is directly proportional to its mole fraction in solution
1
960-963
5 Solution Solution Solution Solution Solution Rationalised 2023-24 12 Chemistry According to Raoult’s law, the vapour pressure of a volatile component in a given solution is given by pi = xi pi 0 In the solution of a gas in a liquid, one of the components is so volatile that it exists as a gas and we have already seen that its solubility is given by Henry’s law which states that p = KH x If we compare the equations for Raoult’s law and Henry’s law, it can be seen that the partial pressure of the volatile component or gas is directly proportional to its mole fraction in solution Only the proportionality constant KH differs from p1 0
1
961-964
In the solution of a gas in a liquid, one of the components is so volatile that it exists as a gas and we have already seen that its solubility is given by Henry’s law which states that p = KH x If we compare the equations for Raoult’s law and Henry’s law, it can be seen that the partial pressure of the volatile component or gas is directly proportional to its mole fraction in solution Only the proportionality constant KH differs from p1 0 Thus, Raoult’s law becomes a special case of Henry’s law in which KH becomes equal to p1 0
1
962-965
If we compare the equations for Raoult’s law and Henry’s law, it can be seen that the partial pressure of the volatile component or gas is directly proportional to its mole fraction in solution Only the proportionality constant KH differs from p1 0 Thus, Raoult’s law becomes a special case of Henry’s law in which KH becomes equal to p1 0 Another important class of solutions consists of solids dissolved in liquid, for example, sodium chloride, glucose, urea and cane sugar in water and iodine and sulphur dissolved in carbon disulphide
1
963-966
Only the proportionality constant KH differs from p1 0 Thus, Raoult’s law becomes a special case of Henry’s law in which KH becomes equal to p1 0 Another important class of solutions consists of solids dissolved in liquid, for example, sodium chloride, glucose, urea and cane sugar in water and iodine and sulphur dissolved in carbon disulphide Some physical properties of these solutions are quite different from those of pure solvents
1
964-967
Thus, Raoult’s law becomes a special case of Henry’s law in which KH becomes equal to p1 0 Another important class of solutions consists of solids dissolved in liquid, for example, sodium chloride, glucose, urea and cane sugar in water and iodine and sulphur dissolved in carbon disulphide Some physical properties of these solutions are quite different from those of pure solvents For example, vapour pressure
1
965-968
Another important class of solutions consists of solids dissolved in liquid, for example, sodium chloride, glucose, urea and cane sugar in water and iodine and sulphur dissolved in carbon disulphide Some physical properties of these solutions are quite different from those of pure solvents For example, vapour pressure Liquids at a given temperature vapourise and under equilibrium conditions the pressure exerted by the vapours of the liquid over the liquid phase is called vapour pressure [Fig
1
966-969
Some physical properties of these solutions are quite different from those of pure solvents For example, vapour pressure Liquids at a given temperature vapourise and under equilibrium conditions the pressure exerted by the vapours of the liquid over the liquid phase is called vapour pressure [Fig 1
1
967-970
For example, vapour pressure Liquids at a given temperature vapourise and under equilibrium conditions the pressure exerted by the vapours of the liquid over the liquid phase is called vapour pressure [Fig 1 4 (a)]
1
968-971
Liquids at a given temperature vapourise and under equilibrium conditions the pressure exerted by the vapours of the liquid over the liquid phase is called vapour pressure [Fig 1 4 (a)] In a pure liquid the entire surface is occupied by the molecules of the liquid
1
969-972
1 4 (a)] In a pure liquid the entire surface is occupied by the molecules of the liquid If a non-volatile solute is added to a solvent to give a solution [Fig
1
970-973
4 (a)] In a pure liquid the entire surface is occupied by the molecules of the liquid If a non-volatile solute is added to a solvent to give a solution [Fig 1
1
971-974
In a pure liquid the entire surface is occupied by the molecules of the liquid If a non-volatile solute is added to a solvent to give a solution [Fig 1 4
1
972-975
If a non-volatile solute is added to a solvent to give a solution [Fig 1 4 (b)], the vapour pressure of the solution is solely from the solvent alone
1
973-976
1 4 (b)], the vapour pressure of the solution is solely from the solvent alone This vapour pressure of the solution at a given temperature is found to be lower than the vapour pressure of the pure solvent at the same temperature
1
974-977
4 (b)], the vapour pressure of the solution is solely from the solvent alone This vapour pressure of the solution at a given temperature is found to be lower than the vapour pressure of the pure solvent at the same temperature In the solution, the surface has both solute and solvent molecules; thereby the fraction of the surface covered by the solvent molecules gets reduced
1
975-978
(b)], the vapour pressure of the solution is solely from the solvent alone This vapour pressure of the solution at a given temperature is found to be lower than the vapour pressure of the pure solvent at the same temperature In the solution, the surface has both solute and solvent molecules; thereby the fraction of the surface covered by the solvent molecules gets reduced Consequently, the number of solvent molecules escaping from the surface is correspondingly reduced, thus, the vapour pressure is also reduced
1
976-979
This vapour pressure of the solution at a given temperature is found to be lower than the vapour pressure of the pure solvent at the same temperature In the solution, the surface has both solute and solvent molecules; thereby the fraction of the surface covered by the solvent molecules gets reduced Consequently, the number of solvent molecules escaping from the surface is correspondingly reduced, thus, the vapour pressure is also reduced The decrease in the vapour pressure of solvent depends on the quantity of non-volatile solute present in the solution, irrespective of its nature
1
977-980
In the solution, the surface has both solute and solvent molecules; thereby the fraction of the surface covered by the solvent molecules gets reduced Consequently, the number of solvent molecules escaping from the surface is correspondingly reduced, thus, the vapour pressure is also reduced The decrease in the vapour pressure of solvent depends on the quantity of non-volatile solute present in the solution, irrespective of its nature For example, decrease in the vapour pressure of water by adding 1
1
978-981
Consequently, the number of solvent molecules escaping from the surface is correspondingly reduced, thus, the vapour pressure is also reduced The decrease in the vapour pressure of solvent depends on the quantity of non-volatile solute present in the solution, irrespective of its nature For example, decrease in the vapour pressure of water by adding 1 0 mol of sucrose to one kg of water is nearly similar to that produced by adding 1
1
979-982
The decrease in the vapour pressure of solvent depends on the quantity of non-volatile solute present in the solution, irrespective of its nature For example, decrease in the vapour pressure of water by adding 1 0 mol of sucrose to one kg of water is nearly similar to that produced by adding 1 0 mol of urea to the same quantity of water at the same temperature
1
980-983
For example, decrease in the vapour pressure of water by adding 1 0 mol of sucrose to one kg of water is nearly similar to that produced by adding 1 0 mol of urea to the same quantity of water at the same temperature Raoult’s law in its general form can be stated as, for any solution the partial vapour pressure of each volatile component in the solution is directly proportional to its mole fraction
1
981-984
0 mol of sucrose to one kg of water is nearly similar to that produced by adding 1 0 mol of urea to the same quantity of water at the same temperature Raoult’s law in its general form can be stated as, for any solution the partial vapour pressure of each volatile component in the solution is directly proportional to its mole fraction In a binary solution, let us denote the solvent by 1 and solute by 2
1
982-985
0 mol of urea to the same quantity of water at the same temperature Raoult’s law in its general form can be stated as, for any solution the partial vapour pressure of each volatile component in the solution is directly proportional to its mole fraction In a binary solution, let us denote the solvent by 1 and solute by 2 When the solute is non-volatile, only the solvent molecules are present in vapour phase and contribute to vapour pressure
1
983-986
Raoult’s law in its general form can be stated as, for any solution the partial vapour pressure of each volatile component in the solution is directly proportional to its mole fraction In a binary solution, let us denote the solvent by 1 and solute by 2 When the solute is non-volatile, only the solvent molecules are present in vapour phase and contribute to vapour pressure Let p1 be 1
1
984-987
In a binary solution, let us denote the solvent by 1 and solute by 2 When the solute is non-volatile, only the solvent molecules are present in vapour phase and contribute to vapour pressure Let p1 be 1 4
1
985-988
When the solute is non-volatile, only the solvent molecules are present in vapour phase and contribute to vapour pressure Let p1 be 1 4 2 Raoult’s Law as a special case of Henry’s Law 1
1
986-989
Let p1 be 1 4 2 Raoult’s Law as a special case of Henry’s Law 1 4
1
987-990
4 2 Raoult’s Law as a special case of Henry’s Law 1 4 3 Vapour Pressure of Solutions of Solids in Liquids Fig
1
988-991
2 Raoult’s Law as a special case of Henry’s Law 1 4 3 Vapour Pressure of Solutions of Solids in Liquids Fig 1
1
989-992
4 3 Vapour Pressure of Solutions of Solids in Liquids Fig 1 4: Decrease in the vapour pressure of the solvent on account of the presence of solute in the solvent (a) evaporation of the molecules of the solvent from its surface is denoted by , (b) in a solution, solute particles have been denoted by and they also occupy part of the surface area
1
990-993
3 Vapour Pressure of Solutions of Solids in Liquids Fig 1 4: Decrease in the vapour pressure of the solvent on account of the presence of solute in the solvent (a) evaporation of the molecules of the solvent from its surface is denoted by , (b) in a solution, solute particles have been denoted by and they also occupy part of the surface area Rationalised 2023-24 13 Solutions the vapour pressure of the solvent, x1 be its mole fraction, pi 0 be its vapour pressure in the pure state
1
991-994
1 4: Decrease in the vapour pressure of the solvent on account of the presence of solute in the solvent (a) evaporation of the molecules of the solvent from its surface is denoted by , (b) in a solution, solute particles have been denoted by and they also occupy part of the surface area Rationalised 2023-24 13 Solutions the vapour pressure of the solvent, x1 be its mole fraction, pi 0 be its vapour pressure in the pure state Then according to Raoult’s law p1 µ x1 and p1 = x1 p10 (1
1
992-995
4: Decrease in the vapour pressure of the solvent on account of the presence of solute in the solvent (a) evaporation of the molecules of the solvent from its surface is denoted by , (b) in a solution, solute particles have been denoted by and they also occupy part of the surface area Rationalised 2023-24 13 Solutions the vapour pressure of the solvent, x1 be its mole fraction, pi 0 be its vapour pressure in the pure state Then according to Raoult’s law p1 µ x1 and p1 = x1 p10 (1 20) The proportionality constant is equal to the vapour pressure of pure solvent, 0 1 p
1
993-996
Rationalised 2023-24 13 Solutions the vapour pressure of the solvent, x1 be its mole fraction, pi 0 be its vapour pressure in the pure state Then according to Raoult’s law p1 µ x1 and p1 = x1 p10 (1 20) The proportionality constant is equal to the vapour pressure of pure solvent, 0 1 p A plot between the vapour pressure and the mole fraction of the solvent is linear (Fig
1
994-997
Then according to Raoult’s law p1 µ x1 and p1 = x1 p10 (1 20) The proportionality constant is equal to the vapour pressure of pure solvent, 0 1 p A plot between the vapour pressure and the mole fraction of the solvent is linear (Fig 1
1
995-998
20) The proportionality constant is equal to the vapour pressure of pure solvent, 0 1 p A plot between the vapour pressure and the mole fraction of the solvent is linear (Fig 1 5)
1
996-999
A plot between the vapour pressure and the mole fraction of the solvent is linear (Fig 1 5) Liquid-liquid solutions can be classified into ideal and non-ideal solutions on the basis of Raoult’s law
1
997-1000
1 5) Liquid-liquid solutions can be classified into ideal and non-ideal solutions on the basis of Raoult’s law The solutions which obey Raoult’s law over the entire range of concentration are known as ideal solutions
1
998-1001
5) Liquid-liquid solutions can be classified into ideal and non-ideal solutions on the basis of Raoult’s law The solutions which obey Raoult’s law over the entire range of concentration are known as ideal solutions The ideal solutions have two other important properties
1
999-1002
Liquid-liquid solutions can be classified into ideal and non-ideal solutions on the basis of Raoult’s law The solutions which obey Raoult’s law over the entire range of concentration are known as ideal solutions The ideal solutions have two other important properties The enthalpy of mixing of the pure components to form the solution is zero and the volume of mixing is also zero, i
1
1000-1003
The solutions which obey Raoult’s law over the entire range of concentration are known as ideal solutions The ideal solutions have two other important properties The enthalpy of mixing of the pure components to form the solution is zero and the volume of mixing is also zero, i e
1
1001-1004
The ideal solutions have two other important properties The enthalpy of mixing of the pure components to form the solution is zero and the volume of mixing is also zero, i e , DmixH = 0, DmixV = 0 (1
1
1002-1005
The enthalpy of mixing of the pure components to form the solution is zero and the volume of mixing is also zero, i e , DmixH = 0, DmixV = 0 (1 21) It means that no heat is absorbed or evolved when the components are mixed
1
1003-1006
e , DmixH = 0, DmixV = 0 (1 21) It means that no heat is absorbed or evolved when the components are mixed Also, the volume of solution would be equal to the sum of volumes of the two components
1
1004-1007
, DmixH = 0, DmixV = 0 (1 21) It means that no heat is absorbed or evolved when the components are mixed Also, the volume of solution would be equal to the sum of volumes of the two components At molecular level, ideal behaviour of the solutions can be explained by considering two components A and B