L13- Crystallisation Flashcards
Crystallisation
Taking supersaturated material and forming solids/crystals
Saturated solution
Solution in thermodynamic equilibrium with solid phase at given temp
Supersaturated
Solution containing more dissolved solute than at equilibrium
Degree of supersaturation, Delta c
Delta c = c-c*
c = actual supersaturated concentration
c* = equilibrium concentration
Supersaturation ratio, S
S = c/c*
Relative supersaturation, phi
phi = delta c/c* = S-1
Crystallisation driving force
Supersaturation is the driving force for crystallisation;
fundamentally is the difference in chemical potential
Solubility-supersolubility diagram: width of metastable zone
delta c = (dc/dT)delta T
Solubility-supersolubility diagram: zones & factors affecting
Stable: no crystals readily form
Metastable: crystals do not form spontaneously but existing crystals would grown
Labile: crystals form since conc. above max show in supersolubility line
Depends on agitation, impurities and how got supersaturated
Solubility-supersolubility diagram: Moving from stable to labile (crystal growth)
Constant temp: saturate at metastable boundary, crystals form spontaneously at labile boundary
Cooling: saturate at metastable boundary, crystals form spontaneously at labile boundary
Nucleation
Creation of crystals within supersaturated liquor
Nucleation types
Primary: nucleation in absence of existing crystals
Homogeneous if only solute involved; heterogeneous when other substances involved or present
Secondary: nucleation in presence of existing crystals- nucleates more readily, i.e. lower supersaturation
Crystal growth kinetic stages
Diffusional stage: solute transported from bulk through solution boundary layer adjacent to crystal surface
Deposition stage: adsorbed solute deposited and integrated into crystal lattice
Overall mass deposition rate, RG
RG = KG(delta c^s) = [(6ap)/B](dr/dt) = [(6ap*u’)/B]
where particle mass, m = ap(d^3)
surface area, A = B*(d^2)
KG - overall crystal growth coefficient
s = constant between 1-2
u’ = mean linear velocity (dr/dt, m/s)
For spheres 6a/B = 1; octahedra 6a/B = 0.816
Crystal yield basis
estimated from conc. of initial solution and solubility at final temp, allowing for evaporation
Solvent (Water) balance
For solvent (usually water), the initial solvent present is equal to the sum of the final water in mother liquor + water of crystallisation within crystals and water evaporated
w1 = w2 + y[(R-1)/R] + w1E
w1, w2 = initial and final masses of solvent in liquor
y = yield of crystals
R = molecular mass of hydrate/anhydrous salt
E = mass of solvent evaporated/solvent in initial solution
Solute balance
w1c1 = w2c2 + y/R
w1, w2 = initial and final masses of solvent in liquor
y = yield of crystals
R = molecular mass of hydrate/anhydrous salt
Proof for crystal yield
Sub solvent balance (w2 =…) in solute balance:
w1c1 = c2{w1(1-E) - y[(R-1)/R]} + y/R
y = Rw1{[c1-c2(1-E)]/[1-c2(R-1)]}
Crystallisation processes & equipment
Reaction -> Evaporator -> Crystalliser -> Filter/centrifuge -> dryer
Cooling crystalliser: allow vessel to cool over time, surfaces provided for crystal growth
Economic for small batches, but uncontrolled crystal sizes,i.e. agitated/agitated w/ circulation through external HEx
Evaporating crystalliser: used when temp not decreased enough
Increases supersaturation, i.e. steam heated