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Reaction rate
View on Wikipedia| Reaction rate | |
|---|---|
Common symbols | ν |
| SI unit | mol⋅L−1⋅s−1 |
| In SI base units | mol⋅m−3⋅s−1 |
| Dimension | L−3⋅T−1⋅N |

The reaction rate or rate of reaction is the speed at which a chemical reaction takes place, defined as proportional to the increase in the concentration of a product per unit time and to the decrease in the concentration of a reactant per unit time.[1] Reaction rates can vary dramatically. For example, the oxidative rusting of iron under Earth's atmosphere is a slow reaction that can take many years, but the combustion of cellulose in a fire is a reaction that takes place in fractions of a second. For most reactions, the rate decreases as the reaction proceeds. A reaction's rate can be determined by measuring the changes in concentration over time.
Chemical kinetics is the part of physical chemistry that concerns how rates of chemical reactions are measured and predicted, and how reaction-rate data can be used to deduce probable reaction mechanisms.[2] The concepts of chemical kinetics are applied in many disciplines, such as chemical engineering,[3][4] enzymology and environmental engineering.[5][6][7]
Formal definition
[edit]Consider a typical balanced chemical reaction: The lowercase letters (a, b, p, and q) represent stoichiometric coefficients, while the capital letters represent the reactants (A and B) and the products (P and Q).
According to IUPAC's Gold Book definition[8] the reaction rate for a chemical reaction occurring in a closed system at constant volume, without a build-up of reaction intermediates, is defined as where [X] denotes the concentration of the substance X (= A, B, P or Q). The reaction rate thus defined has the units of mol/(L⋅s).
The rate of a reaction is always positive. A negative sign is present to indicate that the reactant concentration is decreasing. The IUPAC recommends[8] that the unit of time should always be the second. The rate of reaction differs from the rate of increase of concentration of a product P by a constant factor (the reciprocal of its stoichiometric number) and for a reactant A by minus the reciprocal of the stoichiometric number. The stoichiometric numbers are included so that the defined rate is independent of which reactant or product species is chosen for measurement.[9]: 349 For example, if a = 1 and b = 3, then B is consumed three times more rapidly than A, but is uniquely defined. An additional advantage of this definition is that for an elementary and irreversible reaction, is equal to the product of the probability of overcoming the transition state activation energy and the number of times per second the transition state is approached by reactant molecules. When so defined, for an elementary and irreversible reaction, is the rate of successful chemical reaction events leading to the product.
The above definition is only valid for a single reaction, in a closed system of constant volume. If water is added to a pot containing salty water, the concentration of salt decreases, although there is no chemical reaction.
For an open system, the full mass balance must be taken into account: where
- FA0 is the inflow rate of A in molecules per second;
- FA the outflow;
- is the instantaneous reaction rate of A (in number concentration rather than molar) in a given differential volume, integrated over the entire system volume V at a given moment.
When applied to the closed system at constant volume considered previously, this equation reduces to where the concentration [A] is related to the number of molecules NA by with (N0 denoting the Avogadro constant.
For a single reaction in a closed system of varying volume, the so-called rate of conversion can be used, in order to avoid handling concentrations. It is defined as the derivative of the extent of reaction with respect to time: where νi is the stoichiometric coefficient for substance i (equal to a, b, p, and q in the typical reaction above), V is the volume of reaction, and Ci is the concentration of substance i.
When side products or reaction intermediates are formed, the IUPAC recommends[8] the use of the terms the rate of increase of concentration and rate of the decrease of concentration for products and reactants respectively.
Reaction rates may also be defined on a basis that is not the volume of the reactor. When a catalyst is used, the reaction rate may be stated on a catalyst mass [mol/(g⋅s)] or surface area [mol/(m2⋅s)] basis. If the basis is a specific catalyst site that may be rigorously counted by a specified method, the rate is given in units of s−1 and is called a "turnover frequency".
Influencing factors
[edit]Factors that influence the reaction rate are the nature of the reaction, concentration, pressure, reaction order, temperature, solvent, electromagnetic radiation, catalyst, isotopes, surface area, stirring, and diffusion limit[10][11]. Some reactions are naturally faster than others. The number of reacting species, their physical state (the particles that form solids move much more slowly than those of gases or those in solution), the complexity of the reaction and other factors can greatly influence the rate of a reaction.
Reaction rate increases with concentration, as described by the rate law and explained by collision theory. As reactant concentration increases, the frequency of collision increases. The rate of gaseous reactions increases with pressure, which is, in fact, equivalent to an increase in the concentration of the gas. The reaction rate increases in the direction where there are fewer moles of gas and decreases in the reverse direction. For condensed-phase reactions, the pressure dependence is weak.
The order of the reaction controls how the reactant concentration (or pressure) affects the reaction rate.
Usually conducting a reaction at a higher temperature delivers more energy into the system and increases the reaction rate by causing more collisions between particles, as explained by collision theory. However, the main reason that temperature increases the rate of reaction is that more of the colliding particles will have the necessary activation energy resulting in more successful collisions (when bonds are formed between reactants). The influence of temperature is described by the Arrhenius equation. For example, coal burns in a fireplace in the presence of oxygen, but it does not when it is stored at room temperature. The reaction is spontaneous at low and high temperatures but at room temperature, its rate is so slow that it is negligible. The increase in temperature, as created by a match, allows the reaction to start and then it heats itself because it is exothermic. That is valid for many other fuels, such as methane, butane, and hydrogen.
Reaction rates can be independent of temperature (non-Arrhenius) or decrease with increasing temperature (anti-Arrhenius). Reactions without an activation barrier (for example, some radical reactions), tend to have anti-Arrhenius temperature dependence: the rate constant decreases with increasing temperature.
Many reactions take place in solution and the properties of the solvent affect the reaction rate. The ionic strength also has an effect on the reaction rate.
Electromagnetic radiation is a form of energy. As such, it may speed up the rate or even make a reaction spontaneous as it provides the particles of the reactants with more energy.[12] This energy is in one way or another stored in the reacting particles (it may break bonds, and promote molecules to electronically or vibrationally excited states...) creating intermediate species that react easily. As the intensity of light increases, the particles absorb more energy and hence the rate of reaction increases. For example, when methane reacts with chlorine in the dark, the reaction rate is slow. It can be sped up when the mixture is put under diffused light. In bright sunlight, the reaction is explosive.
The presence of a catalyst increases the reaction rate (in both the forward and reverse reactions) by providing an alternative pathway with a lower activation energy. For example, platinum catalyzes the combustion of hydrogen with oxygen at room temperature.
The kinetic isotope effect consists of a different reaction rate for the same molecule if it has different isotopes, usually hydrogen isotopes, because of the relative mass difference between hydrogen and deuterium. In reactions on surfaces, which take place, for example, during heterogeneous catalysis, the rate of reaction increases as the surface area does. That is because more particles of the solid are exposed and can be hit by reactant molecules.
Stirring can have a strong effect on the rate of reaction for heterogeneous reactions.
Some reactions are limited by diffusion. All the factors that affect a reaction rate, except for concentration and reaction order, are taken into account in the reaction rate coefficient (the coefficient in the rate equation of the reaction).
Rate equation
[edit]For a chemical reaction aA + bB → pP + qQ, the rate equation or rate law is a mathematical expression used in chemical kinetics to link the rate of a reaction to the concentration of each reactant. For a closed system at constant volume, this is often of the form
For reactions that go to completion (which implies very small kr), or if only the initial rate is analyzed (with initial vanishing product concentrations), this simplifies to the commonly quoted form
For gas phase reaction the rate equation is often alternatively expressed in terms of partial pressures.
In these equations k(T) is the reaction rate coefficient or rate constant, although it is not really a constant, because it includes all the parameters that affect reaction rate, except for time and concentration. Of all the parameters influencing reaction rates, temperature is normally the most important one and is accounted for by the Arrhenius equation.
The exponents n and m are called reaction orders and depend on the reaction mechanism. For an elementary (single-step) reaction, the order with respect to each reactant is equal to its stoichiometric coefficient. For complex (multistep) reactions, however, this is often not true and the rate equation is determined by the detailed mechanism, as illustrated below for the reaction of H2 and NO.
For elementary reactions or reaction steps, the order and stoichiometric coefficient are both equal to the molecularity or number of molecules participating. For a unimolecular reaction or step, the rate is proportional to the concentration of molecules of reactant, so the rate law is first order. For a bimolecular reaction or step, the number of collisions is proportional to the product of the two reactant concentrations, or second order. A termolecular step is predicted to be third order, but also very slow as simultaneous collisions of three molecules are rare.
By using the mass balance for the system in which the reaction occurs, an expression for the rate of change in concentration can be derived. For a closed system with constant volume, such an expression can look like
Example of a complex reaction: hydrogen and nitric oxide
[edit]For the reaction
the observed rate equation (or rate expression) is
As for many reactions, the experimental rate equation does not simply reflect the stoichiometric coefficients in the overall reaction: It is third order overall: first order in H2 and second order in NO, even though the stoichiometric coefficients of both reactants are equal to 2.[13]
In chemical kinetics, the overall reaction rate is often explained using a mechanism consisting of a number of elementary steps. Not all of these steps affect the rate of reaction; normally the slowest elementary step controls the reaction rate. For this example, a possible mechanism is
Reactions 1 and 3 are very rapid compared to the second, so the slow reaction 2 is the rate-determining step. This is a bimolecular elementary reaction whose rate is given by the second-order equation where k2 is the rate constant for the second step.
However N2O2 is an unstable intermediate whose concentration is determined by the fact that the first step is in equilibrium, so that where K1 is the equilibrium constant of the first step. Substitution of this equation in the previous equation leads to a rate equation expressed in terms of the original reactants
This agrees with the form of the observed rate equation if it is assumed that k = k2K1. In practice the rate equation is used to suggest possible mechanisms which predict a rate equation in agreement with experiment.
The second molecule of H2 does not appear in the rate equation because it reacts in the third step, which is a rapid step after the rate-determining step, so that it does not affect the overall reaction rate.
Temperature dependence
[edit]Each reaction rate coefficient k has a temperature dependency, which is usually given by the Arrhenius equation: where
- A, is the pre-exponential factor, or frequency factor,
- exp is the exponential function,
- Ea is the activation energy,
- R is the gas constant.
Since at temperature T the molecules have energies given by a Boltzmann distribution, one can expect the number of collisions with energy greater than Ea to be proportional to .
The values for A and Ea are dependent on the reaction. There are also more complex equations possible, which describe the temperature dependence of other rate constants that do not follow this pattern.
Temperature is a measure of the average kinetic energy of the reactants. As temperature increases, the kinetic energy of the reactants increases. That is, the particles move faster, which allows more collisions to take place and at a greater speed, so the chance of reactants forming into products increases, which in turn results in the rate of reaction increasing. As a rule of thumb, a rise of ten degrees Celsius results in approximately twice the reaction rate constant.[14]
The minimum kinetic energy required for a reaction to occur is called the activation energy and is denoted by Ea or ΔG‡. The transition state or activated complex shown on the diagram is the energy barrier that must be overcome when changing reactants into products. The molecules with an energy greater than this barrier have enough energy to react.
For a successful collision to take place, the collision geometry must be right, meaning the reactant molecules must face the right way, so the activated complex can be formed.
A chemical reaction takes place only when the reacting particles collide. However, not all collisions are effective in causing the reaction. Products are formed only when the colliding particles possess a certain minimum energy called threshold energy. For a given reaction, the ratio of its rate constant at a higher temperature to its rate constant at a lower temperature is known as its temperature coefficient (Q). Q10 is commonly used as the ratio of rate constants that are 10 °C apart and is usually on the order of 2.
Pressure dependence
[edit]The pressure dependence of the rate constant for condensed-phase reactions (that is, when reactants and products are solids or liquid) is usually sufficiently weak in the range of pressures normally encountered in industry that it is neglected in practice.
The pressure dependence of the rate constant is associated with the activation volume. For the reaction proceeding through an activation-state complex, the activation volume ΔV ‡ is where V denotes the partial molar volume of a species, and ‡ (a double dagger) indicates the activation-state complex.
For the above reaction, one can expect the change of the reaction rate constant (based either on mole fraction or on molar concentration) with pressure at constant temperature to be[9]: 390 In practice, the matter can be complicated because the partial molar volumes and the activation volume can themselves depend on pressure.
Reactions can increase or decrease their rates with pressure, depending on the value of ΔV ‡. As an example of the possible magnitude of the pressure effect, some organic reactions were shown to double the reaction rate when the pressure was increased from atmospheric (0.1 MPa) to 50 MPa (which gives ΔV ‡ = −0.025 L/mol).[15]
See also
[edit]Notes
[edit]- ^ McMurry, John; Fay, Robert C.; Robinson, Jill K. (31 December 2014). Chemistry (Seventh ed.). Boston. p. 492. ISBN 978-0-321-94317-0. OCLC 889577526.
{{cite book}}: CS1 maint: location missing publisher (link) - ^ Petrucci, Ralph H.; Herring, F. Geoffrey; Madura, Jeffry D.; Bissonnette, Carey (4 February 2016). General chemistry: principles and modern applications (Eleventh ed.). Toronto. p. 923. ISBN 978-0-13-293128-1. OCLC 951078429.
{{cite book}}: CS1 maint: location missing publisher (link) - ^ Silva, Camylla K. S.; Baston, Eduardo P.; Melgar, Lisbeth Z.; Bellido, Jorge D. A. (2019-10-01). "Ni/Al2O3-La2O3 catalysts synthesized by a one-step polymerization method applied to the dry reforming of methane: effect of precursor structures of nickel, perovskite and spinel". Reaction Kinetics, Mechanisms and Catalysis. 128 (1): 251–269. doi:10.1007/s11144-019-01644-3. ISSN 1878-5204. S2CID 199407594.
- ^ Elizalde, Ignacio; Mederos, Fabián S.; del Carmen Monterrubio, Ma.; Casillas, Ninfa; Díaz, Hugo; Trejo, Fernando (2019-02-01). "Mathematical modeling and simulation of an industrial adiabatic trickle-bed reactor for upgrading heavy crude oil by hydrotreatment process". Reaction Kinetics, Mechanisms and Catalysis. 126 (1): 31–48. doi:10.1007/s11144-018-1489-7. ISSN 1878-5204. S2CID 105735334.
- ^ Liu, Jiaqi; Shen, Meiqing; Li, Chenxu; Wang, Jianqiang; Wang, Jun (2019-10-01). "Enhanced hydrothermal stability of a manganese metavanadate catalyst based on WO3–TiO2 for the selective catalytic reduction of NOx with NH3". Reaction Kinetics, Mechanisms and Catalysis. 128 (1): 175–191. doi:10.1007/s11144-019-01624-7. ISSN 1878-5204. S2CID 199078451.
- ^ Li, Xiaoliang; Feng, Jiangjiang; Xu, Zhigang; Wang, Junqiang; Wang, Yujie; Zhao, Wei (2019-10-01). "Cerium modification for improving the performance of Cu-SSZ-13 in selective catalytic reduction of NO by NH3". Reaction Kinetics, Mechanisms and Catalysis. 128 (1): 163–174. doi:10.1007/s11144-019-01621-w. ISSN 1878-5204. S2CID 189874787.
- ^ Vedyagin, Aleksey A.; Stoyanovskii, Vladimir O.; Kenzhin, Roman M.; Slavinskaya, Elena M.; Plyusnin, Pavel E.; Shubin, Yury V. (2019-06-01). "Purification of gasoline exhaust gases using bimetallic Pd–Rh/δ-Al2O3 catalysts". Reaction Kinetics, Mechanisms and Catalysis. 127 (1): 137–148. doi:10.1007/s11144-019-01573-1. ISSN 1878-5204. S2CID 145994544.
- ^ a b c IUPAC, Compendium of Chemical Terminology, 5th ed. (the "Gold Book") (2025). Online version: (2006–) "Rate of reaction". doi:10.1351/goldbook.R05156.
- ^ a b Laidler, K. J.; Meiser, J. H. (1982). Physical Chemistry. Benjamin/Cummings. ISBN 0-8053-5682-7.
- ^ "Factors Affecting Rates of Reaction". Student Academic Success. Retrieved 2025-09-17.
- ^ "14.1: Factors that Affect Reaction Rates". Chemistry LibreTexts. 2015-02-06. Retrieved 2025-09-17.
- ^ Onuchukwu, A. I.; Mshelia, P. B. (1985-09-01). "The production of oxygen gas: A student catalysis experiment". Journal of Chemical Education. 62 (9): 809. doi:10.1021/ed062p809. Retrieved 2025-09-17.
- ^ Laidler, K. J. (1987). Chemical Kinetics (3rd ed.). Harper & Row. p. 277. ISBN 0060438622.
- ^ Connors, Kenneth (1990). Chemical Kinetics: The Study of Reaction Rates in Solution. VCH Publishers. p. 14. ISBN 978-0-471-72020-1.
- ^ Isaacs, Neil S. (1995). "Section 2.8.3". Physical Organic Chemistry (2nd ed.). Harlow: Addison Wesley Longman. ISBN 9780582218635.
External links
[edit]Reaction rate
View on GrokipediaFundamentals
Definition
In chemical kinetics, the reaction rate is defined as the change in the concentration of a reactant or product over a specified period of time.[2] This measure quantifies how quickly a chemical reaction proceeds, typically expressed as the speed at which reactants are consumed or products are formed during the transformation. The concept of reaction rate was first quantitatively studied in 1850 by Ludwig Wilhelmy, who investigated the acid-catalyzed inversion of sucrose using polarimetry to track concentration changes over time.[11] Wilhelmy's work established that the rate depends on the concentrations of sucrose and acid, marking the foundational quantitative approach to kinetics.[12] Reaction rates can be described as either average or instantaneous. The average rate represents the overall change in concentration divided by the time interval, calculated as , providing a broad measure over a finite period. In contrast, the instantaneous rate is the rate at a specific moment, conceptualized as the derivative of concentration with respect to time, which captures the reaction's speed precisely at that point.[2] For a general reaction , the rate is expressed accounting for stoichiometric coefficients: The negative sign applies to reactants to indicate decreasing concentration, while the positive sign applies to products. This formulation ensures the rate is consistent across all species involved, proportional to their stoichiometric ratios.Units and Measurement
The standard unit for reaction rate in the SI system is moles per liter per second, denoted as M/s or mol dm⁻³ s⁻¹, which quantifies the change in concentration of a species per unit time.[13][14] Reaction rates are typically measured by monitoring the change in concentration of reactants or products over time, often through techniques such as spectroscopy to detect absorbance variations or titration to quantify species amounts.[15][16] To account for the stoichiometry of the reaction, the rate is defined independently of the specific species; for a general reaction where a reactant A or product P has stoichiometric coefficient ν, the rate is expressed as for products or equivalently for reactants , ensuring consistency across the reaction equation.[17] Rates are frequently reported as initial rates, taken at the start of the reaction when concentrations are well-defined and the rate is approximately constant, which simplifies the determination of rate laws without interference from subsequent concentration variations.[18][19]Rate Laws
General Form
The general form of a rate law for a simple reaction involving reactants A and B is expressed as where is the rate constant, and and are the reaction orders with respect to A and B, respectively.[20] This empirical equation relates the reaction rate to the concentrations of the reactants raised to powers that reflect their influence on the rate.[20] Rate laws are determined experimentally through methods such as measuring initial rates at varying concentrations, rather than being derived directly from the balanced chemical equation or stoichiometry.[21] For a general reaction products, the rate can be defined in terms of the disappearance of reactants or the appearance of products, ensuring consistency: .[22] This distinction accounts for the stoichiometric coefficients and the directional change in concentration (negative for reactants, positive for products).[22] Special cases of the general rate law arise based on the values of and , corresponding to zero-order, first-order, and second-order kinetics. In zero-order kinetics, where and , the rate is independent of reactant concentrations (), as seen in certain catalytic reactions like the hydrogenation of ethylene on a metal surface.[21] First-order kinetics occurs when the overall order is 1 (e.g., , ; ), typical for unimolecular reactions such as the decomposition of dinitrogen pentoxide ().[21] Second-order kinetics features an overall order of 2 (e.g., , ; ), exemplified by the reaction between nitrogen monoxide and oxygen ().[21] The units of vary with the overall reaction order to ensure dimensional consistency in the rate law.[20]Reaction Order
In chemical kinetics, the order of a reaction with respect to a particular reactant is the exponent of its concentration term in the rate law, which empirically describes how the reaction rate depends on that concentration. The overall order of a reaction is the sum of the orders with respect to each reactant, providing a measure of the total concentration dependence of the rate.[18] For instance, if the rate law is rate = k [A]^m [B]^n, the overall order is m + n, where m and n are typically determined experimentally rather than from stoichiometry.[2] Determining the reaction order requires careful experimental design to isolate the effects of individual reactant concentrations. The method of initial rates is a primary technique, involving a series of experiments where the initial concentration of one reactant is systematically varied while holding all others constant, and the initial reaction rate is measured in each case. By comparing how the rate changes with concentration—for example, if doubling the concentration doubles the rate, the order is 1—the exponent for that reactant is established.[23] This approach assumes that the initial rates reflect the rate law without significant interference from product buildup or side reactions.[3] When independent variation of concentrations is challenging, such as in reactions with interdependent species, the isolation method is employed. In this technique, all reactants except one are present in large excess, rendering their concentrations effectively constant throughout the reaction; the order with respect to the limiting reactant can then be determined by treating the process as a pseudo-order reaction dependent only on that species.[24] This method simplifies complex systems and allows sequential determination of orders for each component.[25] Reaction orders provide insight into kinetic behavior through characteristic properties like half-life, the time required for reactant concentration to halve. For a first-order reaction, where the overall order is 1, the half-life remains constant and independent of the initial concentration, reflecting an exponential decay process.[26] In a second-order reaction, with an overall order of 2, the half-life is inversely proportional to the initial concentration, meaning higher starting concentrations lead to shorter half-lives due to increased collision frequency.[27] Orders are not always integers; fractional values, such as 1/2 or 3/2, arise in many reactions and signal underlying complexity. These non-integer orders typically indicate that the reaction does not proceed via a single elementary step but involves a more intricate mechanism, often with intermediates or steady-state approximations influencing the observed rate.[28] Such cases underscore the empirical nature of rate laws and the need for mechanistic studies to interpret them fully.[2]Complex Reactions
In complex reactions, which are non-elementary and proceed through multiple stepwise processes rather than a single collision, the overall reaction rate is governed by the slowest elementary step, known as the rate-determining step (RDS). The RDS limits the rate at which the entire reaction can occur, as subsequent steps depend on the concentration of species produced up to that point; prior steps are typically fast equilibria or rapid processes that do not bottleneck the reaction. The rate law for the overall reaction is thus derived directly from the stoichiometry and rate constant of the RDS, incorporating concentrations of reactants or intermediates involved in that step.[29] A classic example is the reaction between nitric oxide and hydrogen:with an experimentally observed rate law of
This third-order rate law does not match the 1:1 stoichiometric ratio of H₂ to NO in the balanced equation. The proposed mechanism involves an intermediate:
- (fast equilibrium, with equilibrium constant )
- (slow, RDS)
Influencing Factors
Concentration Effects
The concentration of reactants is a primary determinant of reaction rate, as articulated in the law of mass action formulated by Cato Maximilian Guldberg and Peter Waage in their 1864 publication Studier i affiniteten and expanded in 1867.[32] This principle states that the rate of a chemical reaction is directly proportional to the product of the concentrations of the reacting substances, each raised to a power corresponding to the reaction's stoichiometric coefficients or empirical orders.[32] In the general rate law , where is the rate constant and and are the orders with respect to reactants A and B, increasing the concentration of a reactant typically accelerates the reaction when the order is positive, due to more frequent molecular collisions.[33] The impact of concentration changes varies with the reaction order. For a first-order reaction, such as the decomposition of hydrogen peroxide (), the rate is ; doubling the concentration of doubles the rate, as the order is 1.[33] In contrast, for a second-order reaction, like the reaction between nitric oxide and oxygen (), the rate is ; doubling the concentration of NO (while holding [O_2] constant) quadruples the rate, reflecting the squared dependence.[33] These effects underscore how concentration scales the reaction velocity nonlinearly for orders greater than 1, enhancing efficiency in processes like industrial catalysis where reactant levels are optimized. Inverse effects occur in reactions involving inhibitors or autocatalytic mechanisms, where increasing the concentration of certain species can decrease the overall rate, resulting in negative orders. In substrate inhibition, common in enzymatic reactions, high substrate concentrations bind to the enzyme-substrate complex to form an inactive state, yielding a rate law such as , where the term introduces negative order behavior with respect to substrate [S] at high levels; for example, in alcohol dehydrogenase, excess ethanol inhibits the enzyme, slowing ethanol oxidation.[34] Autocatalysis, where a product accelerates the reaction, typically exhibits positive order dependence on the product in the catalytic step.[35]Temperature Effects
The temperature of a reaction mixture profoundly influences the reaction rate, primarily through its effect on the rate constant , which governs the overall speed of the chemical transformation. As temperature rises, the kinetic energy of reactant molecules increases, leading to more frequent and energetic collisions, thereby enhancing the probability of successful bond breaking and forming. This relationship is exponential, meaning even modest temperature increases can dramatically accelerate reactions, a principle central to fields like industrial catalysis and biochemistry.[36] The quantitative description of this temperature dependence is provided by the Arrhenius equation, empirically derived by Svante Arrhenius in 1889 from studies on the acid-catalyzed inversion of sucrose. The equation is expressed as: where is the rate constant, is the pre-exponential factor representing the frequency of collisions and their orientation, is the activation energy, is the gas constant (8.314 J/mol·K), and is the absolute temperature in Kelvin. Arrhenius fitted this form to experimental data, showing that plotting versus yields a straight line with slope , allowing determination of activation parameters.[37][38] Activation energy represents the minimum energy barrier that reactant molecules must overcome for a collision to result in products, often visualized as the height of a potential energy hump in the reaction coordinate diagram. Molecules with energy below undergo ineffective collisions, while those exceeding it can form transient bonds leading to reaction. The exponential term thus quantifies the fraction of molecules possessing sufficient energy at a given temperature, decreasing sharply as increases or temperature drops. For typical reactions, ranges from 20 to 100 kJ/mol, emphasizing its role as the key determinant of thermal sensitivity.[39][38] A practical guideline, observed for many reactions near room temperature (around 298 K), is that the rate approximately doubles for every 10°C increase, corresponding to an of about 50 kJ/mol in the Arrhenius framework. This rule of thumb arises from differentiating the Arrhenius equation, yielding , and substituting typical values. It underscores why processes like food spoilage or enzyme activity accelerate in warmer conditions but must be applied cautiously, as it varies with .[40] Transition state theory, developed in the 1930s by Henry Eyring and others, provides a theoretical foundation for the Arrhenius parameters by positing that reactants form a high-energy activated complex or transition state at the peak of the energy barrier before decomposing into products. This short-lived species, with partial bonds, exists in equilibrium with reactants, and the rate is proportional to its concentration, modulated by a transmission coefficient accounting for quantum effects. The theory refines as related to the entropy of activation and predicts from the enthalpy barrier, offering deeper insight into reaction mechanisms beyond empirical fits.[41]Pressure and Other Effects
In gaseous reactions, pressure influences the reaction rate primarily by altering the concentration of reactant molecules. According to the ideal gas law, at constant temperature, the concentration of a gas is directly proportional to its partial pressure (), so for a reaction of overall order , the rate is proportional to , where is the total pressure assuming ideal behavior and equal partial pressures. This effect arises because higher pressure compresses gas molecules into a smaller volume, increasing collision frequency without changing the temperature. For example, in the synthesis of ammonia from nitrogen and hydrogen, elevated pressures significantly accelerate the forward rate by increasing the concentrations of gaseous reactants, and also shift the equilibrium toward products due to the decrease in moles of gas.[42] Catalysts accelerate reaction rates by providing an alternative pathway with a lower activation energy, thereby increasing the fraction of collisions that are effective, while remaining unchanged at the end of the reaction. They do not alter the thermodynamics of the reaction but can dramatically enhance kinetics; for instance, the enzyme catalase decomposes hydrogen peroxide into water and oxygen at rates up to times faster than the uncatalyzed process. Catalysts are classified as homogeneous if they exist in the same phase as the reactants, such as dissolved acids catalyzing ester hydrolysis, or heterogeneous if in a different phase, like solid platinum catalyzing the oxidation of sulfur dioxide in contact processes.[43][44][45] The physical state of reactants and the solvent environment also impact reaction rates beyond simple concentration changes. In heterogeneous reactions involving solids, such as the combustion of powdered magnesium versus a lump, increasing the surface area exposes more reactant sites for collisions, thereby elevating the rate proportionally to the available interfacial area. A common example is the reaction of calcium carbonate (CaCO₃) with hydrochloric acid (HCl) to produce carbon dioxide gas. Using the same mass of calcium carbonate (e.g., 5 g) in different particle sizes (large marble chips versus fine powder) with excess HCl (e.g., 50 cm³ of 2 mol/dm³), the rate is measured by collecting the volume of CO₂ produced over time using a gas syringe. The fine powder results in a faster initial rate, shown by a steeper gradient in the volume versus time graph, due to its greater surface area available for reaction. To ensure reliable results, experiments should maintain constant temperature, use the same apparatus and acid concentration/volume, avoid gas leaks, use excess acid, and perform repeats for averaging. Solvent effects arise from interactions like polarity, where polar protic solvents (e.g., water) can stabilize charged transition states in nucleophilic substitutions, accelerating rates for ionic mechanisms, while nonpolar solvents may slow them by providing less stabilization. Viscosity in solvents generally impedes diffusion-controlled rates by reducing molecular mobility.[46]/Unit_5:_Kinetics_and_Equilibria/Chapter_13:_Chemical_Kinetics/Chapter_13.1:_Factors_that_Affect_Reaction_Rates) Light or radiation plays a key role in photochemical reactions, where absorbed photons excite molecules to higher energy states, initiating bond breaking or rearrangement that would otherwise require thermal activation. The rate is typically proportional to the intensity of the incident light and the quantum yield, as governed by the Grotthuss-Draper law, which states that only absorbed light triggers the reaction; for example, in the photodissociation of ozone, ultraviolet radiation directly determines the atmospheric destruction rate.[47]Applications and Determination
Experimental Methods
Experimental methods for determining reaction rates typically involve monitoring changes in concentration, physical properties, or other observables over time under controlled conditions, such as constant temperature and initial concentrations. These techniques allow chemists to quantify the rate of a reaction and derive its rate law by systematically varying experimental parameters. Common approaches focus on either initial reaction phases or specific monitoring methods suited to the reaction type, ensuring accurate data collection without interference from subsequent steps in complex mechanisms.[48] The initial rates method is a fundamental technique for establishing rate laws, where the reaction rate is measured at the very beginning of the process—when product concentrations are negligible and reverse reactions are minimal—by determining the initial slope of concentration versus time plots. To find the reaction order with respect to each reactant, experiments are conducted with varying initial concentrations of one species while keeping others constant, allowing the rate dependence on that species to be isolated. This method requires rapid measurement capabilities relative to the reaction timescale and is particularly useful for reactions where the full time course might be complicated by side reactions or equilibria. For instance, in the iodination of acetone, initial rates are measured by titrating unreacted iodine at short times after mixing.[49][23] Several laboratory techniques are employed to track concentration changes during initial rate experiments, selected based on the reaction's observable properties. Spectrophotometry monitors color changes by measuring absorbance of light, applying Beer's law to relate optical density to species concentration; it uses a spectrophotometer or colorimeter with a fixed-path observation cell and is ideal for reactions involving colored reactants or products, such as the oxidation of iodide by persulfate. Conductometry detects variations in electrical conductivity arising from ionic species, employing an AC bridge circuit to measure conductance without electrolysis; this is suitable for reactions producing or consuming ions, like acid-base neutralizations. For gas-evolving reactions, such as the decomposition of hydrogen peroxide, a gas syringe or pressure sensor records volume or pressure changes over time, converting these to concentration via the ideal gas law if needed. These methods provide real-time data with high precision, often automated for reproducibility.[48][50] To determine reaction orders, especially in multi-reactant systems, the isolation method pseudo-orders the reaction by using a large excess of all but one reactant, keeping the excess concentrations effectively constant and simplifying the rate law to first-order in the isolated species. The order is then found by analyzing the pseudo-first-order rate constant's dependence on the isolated reactant's concentration across multiple runs. Complementing this, half-life measurements assess order by tracking the time required for the concentration of a reactant to halve; for first-order reactions, this half-life is independent of initial concentration, whereas it increases with initial concentration for second-order processes, allowing graphical analysis of log(t_{1/2}) versus log(initial concentration) to yield the order as the negative slope plus one. These approaches relate directly to reaction order concepts by providing empirical verification of kinetic behavior.[24][51][52] For fast reactions occurring on millisecond or shorter timescales, where conventional mixing is too slow, modern techniques developed after the 1950s enable precise studies. The stopped-flow method, pioneered in the early 1950s by Britton Chance and refined by Quentin Gibson, rapidly mixes reactants using high-pressure syringes that drive solutions into an observation cell, stopping the flow abruptly to initiate timing; absorbance or fluorescence is then monitored with dead times as low as 1 ms, conserving sample volumes and suiting solution-phase kinetics like enzyme mechanisms. Flash photolysis, introduced in 1949 by Ronald G. W. Norrish and George Porter—who shared the 1967 Nobel Prize in Chemistry with Manfred Eigen for fast reaction studies—uses a brief, intense light pulse to photodissociate a precursor, generating reactive intermediates like radicals, whose subsequent kinetics are probed spectroscopically with resolutions down to femtoseconds using lasers. These innovations extended kinetic measurements from seconds to ultrashort regimes, revolutionizing studies of transient species in photochemistry and biochemistry.[53][54][55][56]Integrated Rate Laws
Integrated rate laws are derived by integrating the differential rate laws with respect to time, providing explicit expressions for the concentration of a reactant as a function of time, which allows for the prediction of how concentrations evolve during a reaction. These laws are particularly useful for analyzing experimental data where concentrations are measured over time, enabling the determination of reaction order through linear plotting methods. Unlike differential rate laws, which describe instantaneous rates, integrated forms facilitate calculations of half-lives and long-term behavior without requiring differential calculus in application.[57][58] For a zero-order reaction, where the rate is independent of reactant concentration, the integrated rate law is obtained by integrating the differential form -d[A]/dt = k from initial concentration [A]_0 at t=0 to [A] at time t. This yields [A] = [A]0 - kt, indicating a linear decrease in concentration with time. The half-life for a zero-order reaction, the time required for the concentration to halve, is t{1/2} = [A]_0 / (2k), which depends on the initial concentration and thus increases with higher starting amounts.[59][60] In a first-order reaction, the rate is proportional to the concentration of one reactant, leading to the differential equation -d[A]/dt = k[A]. Integration gives the logarithmic form \ln[A] = -kt + \ln[A]_0, or equivalently [A] = [A]0 e^{-kt}, showing exponential decay. The half-life is independent of initial concentration, calculated as t{1/2} = \ln 2 / k ≈ 0.693 / k, a constant value that simplifies predictions for processes like radioactive decay. To identify first-order kinetics, a plot of \ln[A] versus t yields a straight line with slope -k; deviations indicate other orders. This form is widely applied in pharmacokinetics, where drug elimination often follows first-order kinetics, allowing estimation of plasma concentration over time using [C] = [C]_0 e^{-kt}, with k related to clearance.[57][61][62] For second-order reactions, involving either two molecules of the same reactant or two different reactants, the differential rate law is -d[A]/dt = k[A]^2 (for the unimolecular case). Integration results in the reciprocal form 1/[A] = kt + 1/[A]0, where concentration decreases hyperbolically with time. The half-life is t{1/2} = 1 / (k [A]_0), which inversely depends on initial concentration, meaning reactions starting at lower concentrations take longer to halve. Confirmation of second-order behavior comes from a linear plot of 1/[A] versus t, with slope equal to k.[59][60]Practical Examples
Radioactive decay serves as a classic example of a first-order reaction process, where the rate of decay is directly proportional to the number of undecayed nuclei present. The decay rate is expressed by the equationwhere is the decay constant specific to the isotope and is the number of radioactive atoms.[63] This first-order dependence results in a constant half-life, , which remains independent of the initial amount of material and allows predictable modeling of decay over time.[64] For instance, carbon-14 dating relies on this kinetics to estimate the age of organic artifacts, as the decay rate provides a reliable clock.[63] Enzyme kinetics in biological systems demonstrate a more complex rate behavior through the Michaelis-Menten model, which accounts for substrate binding to the enzyme. The initial reaction velocity is given by
where is the maximum achievable rate when the enzyme is fully saturated, is the substrate concentration, and represents the substrate concentration at which .[65] This equation captures the saturation kinetics observed in enzymatic reactions, where rate increases hyperbolically with at low concentrations but plateaus at high due to limited enzyme active sites.[65] Such behavior is crucial for metabolic pathways, enabling efficient regulation of reaction rates in cells. The industrial synthesis of ammonia via the Haber-Bosch process highlights how reaction rates are optimized by manipulating temperature and pressure in equilibrium systems. The reaction exhibits a rate that increases with temperature due to higher kinetic energy of reactants, but excessive heat shifts the equilibrium unfavorably toward reactants per Le Chatelier's principle.[66] Elevated pressures, typically 150–300 atm, accelerate the forward rate by increasing reactant concentrations and favoring product formation, while catalysts like iron promote the surface-mediated reaction.[66] Operating conditions around 400–500°C balance these effects to achieve industrially viable rates, producing approximately 180 million metric tons of ammonia annually as of 2023 for fertilizers and chemicals.[67] Atmospheric reactions, such as ozone depletion, illustrate the dramatic impact of catalytic species on reaction rates in the stratosphere. Chlorine radicals (Cl•), released from chlorofluorocarbons (CFCs), act as highly efficient catalysts in chain reactions that destroy ozone () molecules.[68] Each Cl• can initiate cycles leading to the net decomposition of up to 100,000 molecules before termination, vastly accelerating the depletion rate compared to uncatalyzed processes.[69] This catalytic enhancement, peaking in polar regions during spring, has contributed to the Antarctic ozone hole, underscoring the environmental consequences of altered reaction kinetics.[68] A practical laboratory example demonstrating the effect of particle size (and thus surface area) on reaction rate is the heterogeneous reaction between calcium carbonate () and hydrochloric acid (): The rate is monitored by measuring the volume of carbon dioxide gas produced using a gas collection method. A reliable procedure uses the same mass (e.g., 5 g) of calcium carbonate in different particle sizes (large marble chips versus fine powder) to vary only the surface area. Excess (e.g., 50 cm³ of 2 mol/dm³) is placed in a conical flask connected to a gas syringe. The acid is added to the calcium carbonate, the flask is sealed, a timer is started, and the volume of is recorded at regular intervals (e.g., every 10 s) until the reaction completes. The experiment is repeated three times for each particle size, with results averaged for reliability. Graphs of volume of versus time are plotted, and the initial reaction rate is determined from the gradient of the initial linear portion of the curve. Smaller particles produce steeper initial gradients, indicating faster rates due to greater surface area available for reaction. Validity is ensured by maintaining constant temperature (using a water bath if needed), using the same acid concentration, volume, and apparatus for all trials, preventing gas leaks, and employing excess acid so the reaction rate depends only on the calcium carbonate surface area. Comparing initial rates avoids complications from changing reactant concentrations as the reaction progresses.[70]