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