$\frac{\mathrm{x}}{\mathrm{m}}=\mathrm{f}\left(\mathrm{T}\right) \mathrm{at} \mathrm{constant} \mathrm{P}$

  $\mathrm{p}=\mathrm{f}\left(\mathrm{T}\right) \mathrm{at} \mathrm{constant} \left(\mathrm{x}/\mathrm{m}\right)$

  $\frac{\mathrm{x}}{\mathrm{m}}=\mathrm{p}\times \mathrm{T}$

  $\frac{\mathrm{x}}{\mathrm{m}}=\mathrm{f}\left(\mathrm{p}\right) \mathrm{at} \mathrm{constant} \mathrm{T}$

  50 mL of 0.1 M AgNO₃ + 50 mL of 0.1 M KI

  50 mL of 1 M AgNO₃ + 50 mL of 0.5 M KI

  50 mL of 1 M AgNO₃ + 50 mL of 2 M KI

  50 mL of 2M AgNO₃ + 50 mL of 1.5 M KI

Sol particles move towards the anode.

Sol particles move towards the cathode of a sol.

Higher is the gold number, greater will be the protective power of a lyophilic colloid.

The dispersion medium moves towards the anode.

Directly proportional to the pressure.

Inversely proportional to the pressure.

Directly proportional to the square of the pressure.

Independent of pressure.

 $C{O}_2$             

 $N{H}_3$               

 ${\mathrm{Br}}_2$           

 $N_2$

 $\frac{x}{m}=k{p}^{0.3}$

 $\frac{x}{m}=k{p}^{2.5}$

 $\frac{x}{m}=k{p}^{-0.5}$

 $\frac{x}{m}=k{p}^{-1}$

  Forming an interfacial film between suspended particles and the medium

  Dissolving the suspended particles into the medium completely

  Coagulating the suspended particles from medium completely

  Converting the suspended particles into vapor completely

  11.2 L

  22.4 L

  7.46 L

  3.73 L

  ${\mathrm{CH}}_3 - {\left({\mathrm{CH}}_2\right)}_{14} - {{\mathrm{OSO}}_3}^{-} {\mathrm{K}}^{+}$

  ${\mathrm{CH}}_3 - {\left({\mathrm{CH}}_2\right)}_{10} - {\mathrm{COO}}^{-} {\mathrm{Na}}^{+}$

  ${\mathrm{CH}}_3 - {\left({\mathrm{CH}}_2\right)}_{11} - {{\mathrm{COO}}_3}^{-} {\mathrm{Na}}^{+}$

  ${\mathrm{CH}}_3 - {\left({\mathrm{CH}}_2\right)}_{15} - \stackrel{+}{\mathrm{N}}{\mathrm{H}}_3 {\mathrm{Br}}^{\mathrm{e}}$

  $\mathrm{NaCl} > {\mathrm{Al}}_2{\left({\mathrm{SO}}_4\right)}_3 > {\mathrm{Ba}}_3{\left({\mathrm{PO}}_4\right)}_2$

  ${\mathrm{Ba}}_3{\left({\mathrm{PO}}_4\right)}_2 > NaCl > {\mathrm{Al}}_2{\left({\mathrm{SO}}_4\right)}_3$

  ${\mathrm{Al}}_2{\left({\mathrm{SO}}_4\right)}_3 > {\mathrm{Ba}}_3{\left({\mathrm{PO}}_4\right)}_2 > NaCl$

  $\mathrm{NaCl} >{\mathrm{Ba}}_3{\left({\mathrm{PO}}_4\right)}_2 > {\mathrm{Al}}_2{\left({\mathrm{SO}}_4\right)}_3$

  25

  0.25

  2.5

  0.025

  High temperature; low pressure

  Low temperature; high pressure

  Low temperature; low pressure

  High temperature; high pressure

  ${\mathrm{NH}}_3, {\mathrm{CO}}_2, C{\mathrm{H}}_4, {\mathrm{H}}_2$

  ${\mathrm{CO}}_2, {\mathrm{NH}}_3, {\mathrm{H}}_2, C{\mathrm{H}}_4$

  ${\mathrm{H}}_2, C{\mathrm{H}}_4, {\mathrm{CO}}_2, {\mathrm{NH}}_3$

3.  $C{\mathrm{H}}_4, {\mathrm{NH}}_3, {\mathrm{CO}}_2, {\mathrm{H}}_2$

  36.5

  100

  200

  150

  $A{l}^{3+}<B{a}^{2+}<N{a}^{+}$

  $N{a}^{+}<B{a}^{2+}<A{l}^{3+}$

  $B{a}^{2+}<N{a}^{+}<A{l}^{3+}$

  $A{l}^{3+}<N{a}^{+}<B{a}^{2+}$

Temperature fluctuations within the liquid phase.

Attraction and repulsion between charges on the colloidal particles.

Impact of the molecules of the dispersion medium on the colloidal particles.

None of the above.

The extent of adsorption increases in physisorption.

The extent of adsorption decreases in physisorption.

No effect on adsorption.

Extent of adsorption first decreases then increases.

Solubility.

Stability of the colloidal particles.

Size of the colloidal particles.

Viscosity.

Berzelius

Kolbe

Wholer

Rutherford

coagulating the catalyst

getting adsorbed on the active centres on the surface of catalyst

chemical combination with any one of the reactants 

None of the above

Adsorption is spontaneous

Both enthalpy and entropy change of adsorption are negative

Adsorption on solid is reversible

Adsorption increases with an increase in temperature

Increases the activation energy

Decreases the energy barrier for the reaction

Decreases the collision diameter

Increases the temperature coefficient

the rate of dissociation of adsorbed molecules from the surface does not depend on the surface covered

the adsorption at a single site on the surface may involve multiple molecules at the same time

the mass of gas striking a given area of surface is proportional to the pressure of the gas

the mass of gas striking a given area of surface is independent of the pressure of the gas

Decrease in temperature

Increase in temperature

Decrease in pressure

Decrease in surface area

H increases

S increases

G increases

S decreases

Enzymes are specific biological catalyst that possess well defined active states

Enzymes are normally heterogeneous catalyst that are very specific in their action

Enzymes are specific biological catalysts that can not be poisoned

Enzymes are specific biological catalysts that can normally function at very high temperature (T$\simeq$1000K)

More easily liquefiable gases are adsorbed readily

Under high pressure it results into multimolecular layer on the adsorbent surface

Enthalpy of adsorption ($∆H_{adsorption}$) is low and positive

It occurs because of van der Waal's forces

Increases the average kinetic energy of the reacting molecules

Increases the activation energy

Alters the reaction path mechanism

Increases the frequency of collisions of the reacting species

Increases the equilibrium constant of the reaction

Changes the equilibrium conc. of reaction

Shortens the time to reach equilibrium

Supplies the energy of the reaction