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