Chemical equilibrium Polyprotic acid Removing products Acids Heat of vaporization Le Chatelier's Principle Bases Increasing pressure Increasing surface area Keq<1 Non-polar molecules pH>7 pH> Adding products Adding heat Neutralization ΔH>0 Kinetic Energy Heat of fusion Kw Catalyst Buffer solution Buff Universe Temperature Increasing temperature Activation energy 12 Increasing concentration ΔH<0 Lewis Model Joule Amphoteric Enthalpy 3.6 Arrhenius Model Weak base Collision Theory pH Bronsted- Lowry Model Endpoint Strong acid Endothermic reaction Reaction rate Weak acid pH<7 Exothermic reaction Strong base pOH Reversible reaction Indicator Chemical equilibrium Polyprotic acid Removing products Acids Heat of vaporization Le Chatelier's Principle Bases Increasing pressure Increasing surface area Keq<1 Non-polar molecules pH>7 pH> Adding products Adding heat Neutralization ΔH>0 Kinetic Energy Heat of fusion Kw Catalyst Buffer solution Buff Universe Temperature Increasing temperature Activation energy 12 Increasing concentration ΔH<0 Lewis Model Joule Amphoteric Enthalpy 3.6 Arrhenius Model Weak base Collision Theory pH Bronsted- Lowry Model Endpoint Strong acid Endothermic reaction Reaction rate Weak acid pH<7 Exothermic reaction Strong base pOH Reversible reaction Indicator
(Print)
Chemical equilibrium
Polyprotic acid
Removing products
Acids
Heat of vaporization
Le Chatelier's Principle
Bases
Increasing pressure
Increasing surface area
Keq<1
Non-polar molecules
pH>
Adding products
Adding heat
Neutralization
ΔH>0
Kinetic Energy
Heat of fusion
Kw
Catalyst
Buff
Universe
Temperature
Increasing temperature
Activation energy
12
Increasing concentration
ΔH<0
Lewis Model
Joule
Amphoteric
Enthalpy
3.6
Arrhenius Model
Weak base
Collision Theory
pH
Bronsted-Lowry Model
Endpoint
Strong acid
Endothermic reaction
Reaction rate
Weak acid
pH<7
Exothermic reaction
Strong base
pOH
Reversible reaction
Indicator
