Pharmaceutical drying Flashcards

1
Q

importance of drying

A

primary manufacturing
-water is capable of degrading many types of drug
-hydrolytic degredation is to be discouraged
-dry product is free flowing

secondary manufacturing
-wet granulation is commonly used to prepare formulations prior to tablet compaction
-stability, flow properties and compactability are all influenced by residual water content

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2
Q

Total moisture content

A

-total water content of a wet solid
-not all of this water can be easily removed
-easily removable water is sometimes reffered to as free moisture content or unbound water

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3
Q

equilibrium moisture content

A

-all solids will equilibrate with moisture present in air
-this water is called the eqilibrium moisture content
the absolute amount is dynamic as it changed with chamges in temperature and humidity
-each type of solid has its own inherent hygroscopicity.

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4
Q

karl-fischer potentiometric titration

A

measures the amount of water by the electrical conductivity of a redox titration - most accurate

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5
Q

dynamic vapour sorption

A

measures the weight change as a function of both temperature and humidity

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6
Q

thermogravimetric analysis

A

measures the weight change as a funciton of temperature

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7
Q

relative humidity (RH)

A

increased temperature will increase solubility
maximum solubility at a particular temperature
precipitation of the solute on cooling

-air at a given temperature will take up water vapour
-when no more vapour can be taken up the humidity is considered to be saturated

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8
Q

Relative humidity formula

A

RH % = (vapour pressure of water vapour in air/vapour pressure of water vapour in air at saturated temperature) X100

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9
Q

considerations prior to drying

A

-heat sensitivity of the material to be dried
-physical characteristics of the material
-requirment of aseptic conditions
-nature of the liquid to be removed
-scale of the operations
available sources of heat eg.electrial or steam

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10
Q

3 classification of drying methods

A

conduction, convecton, radiation

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11
Q

states of matter

A

latent heat is associated with all these phase changs
solid to liquid - melting
liquid to solid - freezing
solid to gas - sublimation
gas to liquid - cindensation
liquid to gas - evaporation

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12
Q

endothermic processes (+Q)

A

melting
sublimation
evaporation

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13
Q

exothermic procceses (-Q)

A

condensation
freezing

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14
Q

evaporation

A

change from liquid to vapour
-the pressure of a vapour in equlibirium is called the vapour pressure
-when the vapour pressure is equal to the external pressure, the liquid boils (boiling point)

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15
Q

conduction

A

vibration of atoms/molecules with no appreciable movement of molecules

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16
Q

convection

A

macroscopic movement of molecules and their associated heat energy

17
Q

radiation

A

absorption of electromagnetic rays resultiing in increase in temperature

18
Q

practical heat transfer

A

-conductioin is the most important heat transfer process in industrial pharmacy
-convection in industrial processes is normally of a forced nature rather than being natural

19
Q

sensible heat

A

-sensible heat is an appreciable rise in temperature
Q = mc(change in temp
Q - heat energy
c = specific heat capacity

20
Q

Latent heat

A

-heat evolved or absorpbed by unit mass when it changes phases without a change in temperature

21
Q

Latent heat formula

A

Q=mL

Q-heat energy
m-mass
L-heat absorbed/liberated in the change of phase of unit mass

22
Q

fluidised-bed drier

A

equipment used for pharmaceutical drying

23
Q

effect of air velocity on pressure drop
Describe all points on this graph

A

A - air velocity low / no disturbance on particles
B - frictional drag on particles is equal to force of gravity
C- rearrangement to offer least resistence / suspension
D - particle porosity produces small pressure drop

24
Q

Advantages of fluidised bed granulator

A

-Efficient heat and mass transfer
-drying occurs from the surface of individual particles
-temperature of fbd is uniform throughout
-some attrition of particles cause particle spherity
-short drying times

25
Q

disadvantages of fluidised bed drier

A

excessive attrition due to turbulent state
production of fines - must be filtered
generation of static electricity - explosion risk

26
Q

Spray drier

A

-solution is atomised by high pressure gradient through a nozzle
-the small spherical droplets are sprayed into a steam of hot air
-evaporation of the solvent is extremely fast due to the very high surface area of the droplets
- most of the heat used as latent heat and as a degree of evaporative cooling takes place - this keeps the particles from overheating
-each droplet dries an individual solid particle

27
Q

advantages of spray drying

A

-millions of small droplets give a massive surface area heat/mass transfer and hence fast evaporation of solvent
-the characteristic particle shape gives the product a high bul density - good flowability, fast dissolution
-uniform and controllable particle size
-labour costs are low - single operation

28
Q

disadvantages of spray drying

A

equipment is bulky
heat trasnfer from air is relatively inefficient

29
Q

applications of spray drying

A

-used for drying solutions and suspensions
-reasonably useful for thermolabile materials
-high outputs are possible
-capable of producing spherical particles suitable for dry powder inhalation products
-can be operated aseptically
-examples of materials that are spray dried: starch, lactose, calcium, citric acid