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