Class 12th
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New answer posted
11 months agoContributor-Level 10
4.34 t1/2 = 3.00 hours
We know, t1/2 = 0.693/k
? k = 0.693/3 k = 0.231 hrs-1
We know, time
Where, k- rate constant
[R]° -Initial concentration
[R]-Concentration at time 't'
Thus, substituting the values,
log ( [R]0/ [R]) = 0.8
log ( [R]/ [R]0) = -0.8
[R]/ [R]0 = 0.158
Hence, 0.158 fraction of sucrose remains.
New answer posted
11 months agoContributor-Level 10
4.33 Given,
k = 2.0 * 10–2s-1
time t = 100s
Concentration [A0] = 1.0 mol L-1
We know,
On substituting the values, Log (1/ [A]) = 2.303/2
Log [A] = -2.303/2 [A] = 0.135 mol L–1
New answer posted
11 months agoContributor-Level 10
4.32 Given,
k = 2.418 * 10-5 s-1
T = 546 K
Ea = 179.9 kJ mol-1 = 179.9 * 103J mol-1
The Arrhenius equation is given by k = Ae-Ea/RT Taking natural log on both sides,
Ln k = ln A- (Ea/RT) Substituting the values,
ln (2.418 * 10-5 ) = ln A-179.9/ (8.314 * 546)
ln A = 12.5917
A = 3.9 * 1012 s-1 (approximately)
New answer posted
11 months agoContributor-Level 10
4.31 To convert the temperature in °C to °K we add 273 K.

The graph is given as:
The Arrhenius equation is given by k = Ae-Ea/RT
Where, k- Rate constant
A- Constant
Ea-Activation Energy
R- Gas constant
T-Temperature
Taking natural log on both sides,
ln k = ln A- (Ea/RT). equation 1
By plotting a graph, ln K Vs 1/T, we get y-intercept as ln A and Slope is –Ea/R.
Slope = (y2-y1)/ (x2-x1)
By substituting the values, slope = -12.301
? –Ea/R = -12.301
But, R = 8.314 JK-1mol-1
? aE= 8.314 JK-1mol-1 * 12.301 K
? aE= 102.27 kJ mol-1
Substituting the values in equation 1 for data at T = 273K

(? At T = 273K, ln k =-7.147)
On solving, we get ln A = 37.
New answer posted
11 months agoContributor-Level 10
4.30 When t = 0, the total partial pressure is P0 = 0.5 atm

When time t = t, the total partial pressure is Pt = P0 + p
P0-p = Pt-2p, but by the above equation, we know p = Pt-P0
Hence, P0-p = Pt-2 (Pt-P0)
Thus, P0-p = 2P0 – Pt
We know that time
t= 2.303/K log R0 / R
Where, k- rate constant
[R]° -Initial concentration of reactant [R]-Concentration of reactant at time 't'
Here concentration can be replaced by the corresponding partial pressures.
Hence, the equation becomes,
t= 2.303/K log P0 / P0 - P
t= 2.303/K log P0 / 2P0 - Pt
? equation 1
At time t = 100 s, Pt = 0.6 atm and P0 = 0.5 atm,
Substituting in equation 1,
100 = 2.303/k log 0.5 /
New question posted
11 months agoNew answer posted
11 months agoContributor-Level 10
4.29 When t = 0, the total partial pressure is P0 = 35.0 mm of Hg

When time t = t, the total partial pressure is Pt = P0 + p
P0-p = Pt-2p, but by the above equation, we know p = Pt-P0 Hence, P0-p = Pt-2 ( Pt-P0)
Thus, P0-p = 2P0 – Pt
We know that time
t= 2.303/K log R0 / R
Where, k- rate constant
[R]° -Initial concentration of reactant
[R]-Concentration of reactant at time 't'
Here concentration can be replaced by the corresponding partial pressures.
Hence, the equation becomes,
t= 2.303/K log P0 / P0 - P
t= 2.303/K log P0 / 2P0 - Pt
? equation 1
At time t = 360 s, Pt = 54 mm of Hg and P0 = 30 mm of Hg, Substituting in equation 1,
360 = 2
New answer posted
11 months agoContributor-Level 10
A binary operation * on {a, b} is a function from {a, b} * {a, b} → {a, b}
i.e., * is a function from { (a, a), (a, b), (b, a), (b, b)} → {a, b}.
Hence, the total number of binary operations on the set {a, b} is 24 i.e., 16.
The correct answer is B.
New answer posted
11 months agoContributor-Level 10
It is given that,
is defined as
Also, is defined as , where [x] is the greatest integer less than or equal to x.
Now, let
Then, we have:
if and if
Thus, when , we have
Hence, fog and gof do not coincide in (0, 1).
Therefore, option (B) is correct.
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