A well dispersed colloidal suspension consists of individual, separated particles and is stabilized by repulsive inter-particle forces. When the repulsive forces weaken or become attractive through the addition of a coagulant, particles start to aggregate. Initially, particle doublets A2 will form from singlets A1 according to the scheme \ce{A1 + A1 -> A2} In the early stage of the aggregation process, the suspension mainly contains individual particles. The rate of this phenomenon is characterized by the aggregation rate coefficient . Since doublet formation is a
second order rate process, the units of this coefficients are m3s−1 since particle concentrations are expressed as
particle number per unit volume (m−3). Since absolute aggregation rates are difficult to measure, one often refers to the
dimensionless stability ratio , defined as W = \frac{k_\text{fast}}{k} where is the aggregation rate coefficient in the fast regime, and the coefficient at the conditions of interest. The stability ratio is close to unity in the fast regime, increases in the slow regime, and becomes very large when the suspension is stable. Often, colloidal particles are suspended in water. In this case, they accumulate a
surface charge and an
electrical double layer forms around each particle. The overlap between the diffuse layers of two approaching particles results in a repulsive
double layer interaction potential, which leads to particle stabilization. When salt is added to the suspension, the electrical double layer repulsion is screened, and
van der Waals attraction become dominant and induce fast aggregation. The figure on the right shows the typical dependence of the stability ratio versus the electrolyte concentration, whereby the regimes of slow and fast aggregation are indicated. The table below summarizes the critical coagulation concentration (CCC) ranges for different net charge of the counter
ion. The charge is expressed in units of
elementary charge. This dependence reflects the Schulze–Hardy rule, which states that the CCC varies as the inverse sixth power of the counter ion charge. The CCC also depends on the type of ion somewhat, even if they carry the same charge. This dependence may reflect different particle properties or different ion affinities to the particle surface. Since particles are frequently negatively charged, multivalent metal cations thus represent highly effective coagulants. Adsorption of oppositely charged species (e.g., protons, specifically adsorbing ions,
surfactants, or
polyelectrolytes) may destabilize a particle suspension by charge neutralization or stabilize it by buildup of charge, leading to a fast aggregation near the charge neutralization point, and slow aggregation away from it. Quantitative interpretation of colloidal stability was first formulated within the
DLVO theory. This theory confirms the existence slow and fast aggregation regimes, even though in the slow regime the dependence on the salt concentration is often predicted to be much stronger than observed experimentally. The Schulze–Hardy rule can be derived from DLVO theory as well. Other mechanisms of colloid stabilization are equally possible, particularly, involving polymers. Adsorbed or grafted polymers may form a protective layer around the particles, induce steric repulsive forces, and lead to steric stabilization at it is the case with
polycarboxylate ether (PCE), the last generation of chemically tailored
superplasticizer specifically designed to increase the workability of
concrete while reducing its water content to improve its properties and durability. When polymers chains adsorb to particles loosely, a polymer chain may bridge two particles, and induce bridging forces. This situation is referred to as bridging flocculation. When particle aggregation is solely driven by diffusion, one refers to
perikinetic aggregation. Aggregation can be enhanced through
shear stress (e.g., stirring). The latter case is called
orthokinetic aggregation. ==Later stages==