Tuesday, 20 September 2011

Sterile preparation



Sterile Products
Type of dosage form of sterile products:
    1. Ophthalmic
    2. Injectable
    3. Powder for injection (Vial)

Gowning System:
In the manufacture of sterile drugs Gowning System is most important.
1) The gown must be sterilized and made of material which will not shed particles.
2) Everyone entering a clean or a sterile area must change gear garments and wear special garments which includes head, musk and footwear.
3) The number of people must be as low as possible and restricted to authorized people.


Environment Monitoring:
Environmental monitoring is one of the most important tasks in the sterile department. It is a regular check of view to take timely corrective measures for maintaining a favorable manufacturing environment, minimizing the risk of product contamination. It is also a part of validation exercise.
The environmental monitoring approach is also adopted to ensure that there is no significant risk of air borne cross-contamination.



Zonal Classification of Clean Room

Airborne particle limit  



 Aseptic Room Preparation:
The purpose of the aseptic technique is to prevent microorganisms from the environment.
To design of an aseptic room the following factors must be borne in mind:
1. Site
2. Size
3. Windows
4. Doors
5. Surfacing materials
6. Services
7. Corridors

The aseptic procedure comprises the following steps:
1) Sterilization of equipments
2) Sterilization of containers
3) Sterilization of gown.
4) Filling of the solution in the containers under aseptic conditions
5) Double door air lock system.
6) Pass box for materials.

Filling containers under aseptic conditions is the most critical step in the production cycle. This technique is filtration sterilization. HEPA (High Efficiency Particulate Air) filter is used. The most effective ones are claimed to retain 99.997% of the particles. Laminar Air flow cabinet is used under HEPA filter. Filling area is class-A zone whereas the background is class-B zone. The processing rooms must be supplied and flushed with air under controlled positive pressure.



Sterilization:
Sterile products can be classified in two classes:
  1. Products which can be sterilized in their final container.
  2. Products which must be processed under aseptic conditions since they cannot withstand the common methods of sterilization.
Most sterile preparations are aqueous solutions and the method of choice for sterilization is autoclave.

There are 5 types of sterilization:




CONTAINERS:
Containers for injectable preparations are made as far possible from the materials that-
>Are sufficiently transparent to permit visual inspections of the contents, except for implants.
>Do not adversely affect the quality of the preparations under the ordinary conditions of handling, shipment, storage, sale and use.
>Do not permit diffusion or across the walls of the container or yield foreign substances into the preparations. Injectable preparations may be supplied in glass ampules, vials or bottles or in other containers such as plastic bottles or bags etc.


The multiple dose containers may be used for intramuscular, subcutaneous or intracutaneous administration, but no multiple dose containers may contain a total volume of injection sufficient to permit the withdrawal of more than ten doses, unless otherwise stated in the individual monograph. The period of time between the withdrawal of the first and final dose should not be unduly prolonged.

CLOSURES
Vials or bottles with fitted with suitable closures a good seal, prevent the access of microorganisms and other contaminants and usually permit the withdrawal of a part of the whole of the contents of the container without removal of closures. The plastic of rubber materials of which the closure must be compatible with the preparation and be sufficiently firm and elastic to allow the passage of a needle with minimal shedding of particles and to ensure that the puncture is released when the needle is withdrawn.
  
AMPOULE:
Ampoules are the walled glass containers which after filling, are sealed by fusion of the glass. The contents are withdrawn of the glass. The contents are withdrawn after rupture of the glass for one time use.

VIALS:
Vials are thick glass container for dry powders injectable product in which suitable solvents are added to make solution or suspensions just before injections.

WATER FOR INJECTION:
The water which is used as solvent in parenteral product manufacturing is known as water for injections. This water should be highly purified and free from microorganism.


Process Flow Chart:
(Sterile product manufacturing)




Process Flow Chart:
(Vial manufacturing)



Process Flow Chart:
(Ampoule manufacturing)


INFUSION:
According to the FDA Large volume parenterals means a terminally sterilized drug product packaged in a single dose container with a capacity of 100 mi or more and intended to be administered or used as man. It includes IV infusion, irrigating solution, peritoneal dialysis and blood collecting with anticoagulant. These solutions are usually administered by intravenous infusion to replenish body fluid or electrolytes or to provide nutrition. They are usually administered in volumes of 100 ml or1 L or more per day by slow IV infusion with or without a controlled rate infusion system.
Drug International intravenous fluid manufacturing plant may be regarded as one of the most technologically advanced plants in Bangladesh. In designing the whole process, special care has been taken by providing absolute sterile manufacturing condition. The prime feature of the process is that there is no human physical contact with the product at any given time. This has been ensured by way of a series of fully automated manufacturing procedure including robotics. The bottle pack aseptic system (Form-fill-seal or FFS) is a unique and innovative manufacturing technology. Plastic bottles are blow moulded, filled with the solution and seal under sterile condition, in a single working cycle where there is no environmental exposure or human contact during manufacturing. The IV fluids are presented in a scientifically designed bottle where there is an extra protective eurohead cap and a resealable rubber disk. The whole process is performed in a class 100 clean room. The air inside this room is cleaned up to 100 particles per cubic feet passing through HEPA (High Efficiency Particulate Air) filter. This ensures the highest standard of quality and purity in order to ensure the highest level of safety.






References:

1. The Theory and practice of Industrial Pharmacy, 
    (Leon. Lachman, H.A. Lieberman, J.L. Kanig)
2. Encyclopedia of Pharmaceutical Technology
    (James Swarbrick - Taylor and Francis)





Monday, 19 September 2011

Manufacturing Oral Liquid



 The oral use of liquid pharmaceuticals has generally been justified on the basis of ease of administration to those who have difficulty in swallowing solid dosage forms. A drug administed in solution is immediately available for absorption and in most case, is more rapidly and efficiently absorbed than the same amount of drug administered in a tablet or capsules.

Pharmaceutical dosage form has 3 type of oral liquid
1. Syrup
2. Suspension
3. Emulsion etc.
Syrup:
Syrups are oral preparations in which drugs are homogeneously distributed in a solution.
Suspension:
Suspensions are two phase heterogeneous systems in which solid particles are dispersed of suspended in liquid with the help of suspending agents.
Emulsion:
Emulsions are two phase systems in which two immiscible liquids are homogeneously distributed in a liquid with the help of emulsifying agent


Process Flow Chart:
(Oral liquid manufacturing)



  

WATER SUPPLY:
Demineralized water is supplied from water treatment plant. This water is then heated with steam at temperature of 1800 C. Then this hot water is used in the preparation of sucrose syrup which aids the solubility of ingredients and prevents microorganisms
Equipment used in oral liquid unit:

1. Syrup Vat
Anounts: 03
            Made in India
2. Pump
3. Homoginetor
4. Filter

DOCUMENTS:
1. Standard Operating Procedure (SOP)
2. Batch Manufacturing Record (BMR)
3. Batch Packaging Record (BPR)
4. Material Requisition Sheet (MRS)
4. In House specification
 

Pharmaceutical Capsules

Capsules are a solid dosage form enclosed in a hard shell or soft gelatin coating. When taken with water, the capsules' coating becomes slippery and easy to swallow.



i) Hard Gelatin Capsule


It is a solid dosage form in which medications are encapsulated in a two part empty hard gelatin capsule shell. The upper and small part is called ‘CAP’ and the remaining large part is called ‘BODY’. There are 8 different sizes of capsule shell(000,00,0,1,2,3,4,5) with different fill volume. Normally 0 and 2 sized shells are widely used. The shell of hard gelatin capsules basically consists of gelatin, plasticizers and water. Modern day shells may, in addition, consist of preservatives, colours, opacifying agents, flavours, sugars, acids, enteric materials etc. The gelatin is marketed in a large number of varieties and a specific quality and gelatin having specified gel strength, viscosity, iron content etc. should be selected for capsules. The variations in gelatin properties arise because of changes in molecular weights and methods followed in conversion into gelatin.
There are two filling process:
§  Pellet filling
§  Granules filling

Process:





Problems occurred during encapsulation:
  1. Blank shell
  2. Shell lock in channel
  3. Shell breaking
  4. Improper filling of shell
  5. Improper fitting of shell in dies if compressed air pressure is not adjusted properly.
  6. Improper or large size of pellets may cause blockage of nozzle. So shells are left empty.


 EQUIPMENTS:
1. Automatic Capsule Filling machine
Capacity: 65000 capsule/hour
Made in China

2. SEJONG
Model: SF-30
Capacity: 40000capsule/hour

3. Semi automatic capsule filling machine
Model: SCORPIO
Capacity: 7500cap/hr


Process of Gelatin Capsule Manufacture:
 





ii) Soft Gelatin Capsule

A softgel (or a soft gelatin capsule) is a solid capsule (outer shell) surrounding a liquid or semi-solid center (inner fill). An active ingredient can be incorporated into the outer shell, the inner fill, or both. These capsules are available in a variety of shapes, the common shapes being spherical, oblong and elliptical. Size wise also the range is bigger and capsules of capacities ranging from 0.1 ml to 30 ml are used. The composition of soft gelatin capsule shells is similar to the hard gelatin capsules except that a larger proportion of plasticizer is incorporated to make them soft and elastic.

Composition shell
The outer shell is composed of a gelatin or potato starch matrix. Gelatin matrix consists of gelatin, plasticizer, solvent and optional ingredients such as flavors and colorants.

Gelatin - Bovine, porcine, or piscine (fish) origin. Comes in a variety of bloom strengths, the higher the bloom strength, the more resilient the gel. Most oil based fills are encapsulated using a bloom strength of 150. When polyethylene (PEG) based fills are used, a higher bloom strength is generally used.

The limitations of bovine (i.e. bovine-related diseases) and porcine (i.e. not kosher) gelatin may be overcome by piscine (fish) gelatin.
Plasticizer - Glycerin and Sorbitol Special are the two most common plasticizers. Glycerin is generally used with oil based fills. Sorbitol Special is used with PEG based fills. Sorbitol is not soluble in PEG and therefore will not leach out of the shell into the PEG base fill like Glycerin would. Sorbitol Special is formulated to inhibit sorbitol from crystallizing out in the gelatin shell. Do not substitute Sorbitol for Sorbitol Special.
Solvent   -Water
Optional Ingredients   -Colors
                                 -Flavors



Incompatibility
Avoid aldehydes which can lead to cross linking (pellicle formation) of the gelatin, and poor dissolution of the gelatin capsule in water. This may be overcome by adding enzymes to the dissolution media, (see FDA Guidelines)

Drugs sensitive to water can degrade (e.g. ranitidine) or undergo polymorphic conversion (e.g. terazosin). 
Compounds (especially those of high water solubility) can migrate from the fill into the shell or get trapped in a hydrophobic matrix resulting in poor dissolution and loss of bioavailability. 
Soft Gelatin Encapsulation Processes and Equipment 
Rotary Die process
Two ribbons of gelatin are fed continuously into a rotating die assembly and are simultaneously formed into the two halves of a capsule. The ribbons converge adjacent to a fill injector. The fill injector is actuated by a pump which measures and dispenses the appropriate volume of fill material into the capsules. The filled capsules are subsequently sealed as the die assembly rotates. This process permits accurate and reproducible fill uniformity.
Pump heads are available for fill weights as low as 100 mg. For oral dosage forms, the fill weight ranges from 100 mg up to about 1 gram.    
The following should be monitored/controlled:
1. Gelatin temperature
2. Fill temperature
3. Ribbon thickness
4. Seal or seam width
5. Fill quantity
Following encapsulation, the capsules undergo drying in a tumble drying tunnel with an elevated temperature and a large volume of forced air. From the drying tunnel, the capsules are transferred onto trays and placed into a low humidity drying room. Drying is a dynamic process, and the goal is to have the gelatin shell return to its equilibrium moisture content in the range of 6 - 8%.Oil fills dry faster than PEG fills, and typically reach a shell moisture content of 6 to 8% within 24 hours.   


MANUFACTURING PROCESS:
Soft gelatin capsules are generally manufactured by the plate or the rotary die process.

In the plate process a sheet of soft gelatin is placed on a plate having a number of dies and the sheet is drawn into the dies by application of vacuum. The material is then filled in and another sheet of gelatin overlaid. Then a die press descends which seals and cuts out the capsules. This process can, at best, be considered to be semi-automatic.

The rotary die machines, of which several versions are now in the market, operate on a continuous basis and are suitable for large scale manufacture. In rotary machine two continuous gelatin sheets are produced on two rotating drums and are conveyed to two cylinders with matching dies rotating in the same direction. As the gelatin sheets come between the dies the material to be filled is injected through a metering device causing the sheet to swell up and form capsules. Simultaneously the pressure exerted by converging di8es seal and cuts out the capsules. The finished capsules, which fall on a conveyor belt, are carried through rapid dryers, where a greater part of the moisture goes off. The remaining moisture is removed by passing capsules through drying channels into which air is passed under pressure. Most of the early machines could fill liquid preparations only. Recently Accogel or Stern machines capable of filling powders as well have been marketed by Lederle Laboratories.


Rotary Die Encapsulating Machine for Soft Gelatin Capsule:






Process flow chart:
(Soft gelatin capsule manufacturing)












References:

1. Handbook of Pharmaceutical Granulation Technology
    (Dilip M. Parikh)
2. Encyclopedia of Pharmaceutical Technology
    (James Swarbrick - Taylor and Francis)
3. The Theory and practice of Industrial Pharmacy, 
    (Leon. Lachman, H.A. Lieberman, J.L. Kanig)
4. sunkingpm.com
5. hl-jn.com




Dry Syrups


Dry syrups which are also known as powder for suspension are dosage forms that contain the medication in powder form. This solid powder should be reconstituted by dissolving or suspending in water before administration. Dry syrup is usually suitable for children and elderly patients because of easy administration. Many antibiotics which are not stable in liquid media for long period can easily supply in this dry form. They are to be reformulated by mixing with certain amount of boiled water and should be use up within certain periods of times which is normally 5 days. The processing steps are also reduced for dry syrup compared to other oral liquids and subsequently reduced cost.

Dry syrup manufacturing
 Before manufacturing dry syrup first following work are done

 


ENVIRONMENT OF DRY SYRUP UNIT:
Temperature: 210 C
Humidity: 35-40 %

Dry syrup manufacturing process flow chart:
 


 
EQUIPMENT USED IN DRY SYRUP UNIT:
1.      Drum  mixer:
Purpose: Proper mixing in small scale
Capacity: Approximately 60 kg
Source: China

2.      Three dimensional motion mixer;
Purpose: Uniform mixing in large scale
Capacity: 400Lit
Quantity: 01
Model: SYH-400
Source: China

3.      Automatic Powder filling machine;
Purpose: Filling of prepared dry syrup into the bottle
Quantity: 02
Model: 521
Source: Bangladesh

4.      Powder filling machine
SAVPAK
Model: 3221
Capacity: 12 bottle/min
Amounts: 02
Manufacturer: Thai Sek Son Co. Ltd, Thailand

5.      Auto labeling machine
Videojet
Model-435
Amounts: 01
Capacity: 60 bottle/min (60ml syrup)
Mechanical sieve, India

6.      Auto cartoning machine
Model: ZHJ-80
Capacity: 60 bottle/min (60ml syrup) and 100ml
Amount: 02
Manufacturer: Zhejiang Hualian Pharmaceutical Machinery Co. China.

Pharmaceutical Mixing


Process that results in randomization of dissimilar particles within a system. Mixing is one of the most common pharmaceutical operations. It is difficult to find a pharmaceutical product in which mixing is not done at one stage or the other during its manufacturing. The terms "mixing" and "blending" are often used interchangeably, but technically they are slightly different. Blending is a process of combining materials, but blending is a relatively gentle process compared to mixing. In terms of the phase of material, blending is the process of solid-solid mixing or mixing of bulk solids with small quantity of liquid. The terminology mixing is more closely associated with liquid-liquid, gas-liquid, and viscous materials.

Importance of Mixing Technology
Mixing is a critical process because the quality of the final product and its attributes are derived by the quality of the mix. Improper mixing results in a non-homogenous product that lacks consistency with respect to desired attributes like chemical composition, color, texture, flavor, reactivity, and particle size.

The wide variety and ever increasing complexity of mixing processes encountered in industrial applications requires careful selection, design, and scale up to ensure effective and efficient mixing. Improved mixing efficiency leads to shorter batch cycle times and operational costs. Today's competitive production lines necessitate robust equipment that are capable of fast blend times, lower power consumption, equipment flexibility, ease of cleaning, and a gamut of customized features. In addition to blending components, many modern mixers are designed to combine different process steps in a single equipment, e.g. coating, granulation, heat transfer, drying, etc.


I. Liquid mixing or Wet mixing:
Wet mixing may be divided into following two subgroups:

1. Mixing of liquids and liquids
a) Mixing of two miscible liquids
b) Mixing of two immiscible liquids
2. Mixing of liquids and solids
a) Mixing of liquids and soluble solids
b) Mixing of liquids and insoluble solids

1. (a) Mixing of two miscible liquids (homogeneous mixtures e.g. solutions) – mixing of two miscible liquids is quite easy and occur by diffusion. Such type of mixing does not create any problem. Simple shaking or stirring is enough but if the liquids are not readily miscible or if they have very different viscosities then electric stirrer may be used.

1.(b) Mixing of two immiscible liquids (heterogenous mixtures e.g. emulsions) – two immiscible liquids are mixed to effect transfer of a dissolved substance from one liquid to another loquid. When two immiscible liquids are mixed together in the presence of an emulsifying agent an emulsion is produced. For the production of a stable emulsion, the mixing must be very efficient.

2. (a) Mixing of liquids and soluble solids (homogeneous mixtures e.g. solutions)- in this case soluble solids are dissolved in a suitable liquid by means of stirring. It is a physical change, a soluble solid is converted to a solution.

2.(b) Mixing of liquids and insoluble solids (heterogeneous mixtures e.g. suspensions) – when insoluble solids are mixed with a liquid a suspension is produced which is an unstable system.

II Solid-Solid Mixing or Dry Mixing:
Dry mixing is a process in which two or more than two solid substances are intermingled in a mixer by continuous movement of the particles. Mainly, the object of mixing operation is to produce a bulk mixture which when divided into different doses, every unit of dose must contain the correct proportion of each ingredient. The degree of mixing will increase with the length of time for which mixing is done.



References:
 1. Wikipedia
2. The Theory and practice of Industrial Pharmacy,

    (Leon. Lachman, H.A. Lieberman, J.L. Kanig)

The Concept of Pharmaceutical Preformulation


Almost all drugs are marketed as tablets, capsules or both. Prior to the development of these  major dosage forms, it is essential that pertain fundamental physical and chemical properties of the drug molecule and other divided properties of the drug powder are determined. This information decides many of the subsequent events and approaches in formation development. This first learning phase is known as preformulation.

Definition:-
Preformulation involves the application of biopharmaceutical principles to the physicochemical parameters of drug substance are characterized with the goal of designing optimum drug delivery system.
Before beginning the formal preformulation programs the preformulation scientist must consider the following factors:-
- The amount of drug available.
- The physicochemical properties of the drug already known.
- Therapeutic category and anticipated dose of compound.
- The nature of information, a formulation should have or would like to have.


UV Spectroscopy:-
The first requirement of any preformulation study is the development of a simple analytical method for quantitative estimation in subsequent steps. Most of drugs have aromatic rings and/or double bonds as part of their structure and absorb light in UV range, UV spectroscopy being a fairly accurate and simple method is a performed estimation technique at early preformulation stages. The absorption Co-efficient of the drug can be determined by the formula:-

 E =    AF / X 

Where,      A = Asborbance, F= dilution factor , X = weight of drug (mg)

It is now possible to determine connectration of drug in any solution by measuring absorbance.

C =      AF / E mg/ ml

 Characterization of drug molecules is very important step at the preformulation phase of product development. Following studies are conducted as basic preformulation studies, special studies are conducted depending on the type of dosage form and the type of drug molecules.
 1)         Solubility determination
 2)         pKa determination
 3)         Partition co-efficient
 4)         Crystal properties and polymorphism
 5)         Practical size, shape and surface area.
 6)         Chemical stability profile.

1.      Solubility Determination:-
 The solubility of drug is an important physicochemical property because it effects the bioavailabilty of the drug, the rate of drug resale into dissolution medium and consequently, the therapeutic efficiency of the pharmaceutical product.

The solubility of the molecules in various solvents is determined as a first step. This information is valuable is developing a formulation. Solubility is usually determined in variety of commonly used solvents and some oils if the molecules is lipophillic.  
The solubility of material is usually determined by the equilibrium solubility method, which employs a saturated solution of the material, obtained by stirring an excess of material in the solvent for a prolonged until equilibrium achieved.
Common solvents used for solubility determination are:-
Water, Polyethylene Glycols, Propylene Glycol, Glycerin, Sorbitol, Ethyl Alcohol, Methanol, Benzyl, Alcohol, Isopropyl Alcohol, Tweens, Polysorbates, Castor Oil, Peanut Oil, Sesame Oil, Buffer at various pHs
Aqueous Solubility:-
The availability of a drag is always limited and the preformulation scientist may only have 50 mg. Solubility dictates the ease with which formulation for oral gavages and intravenous injection studies in animals are obtained the pKa allives the informed of pH to maintain solubility and to choose salts required to achieve good bioavailability from the solid state and improve stability and powder properties.

Intensic  Solubility (Co) :-
An increase in solubility in acid compared to aqueous solubility suggests a weak base and an increase in alkali, a weak acid. An increase in acidic and alkaline solubility suggests either impotence or zuitter ion behaviour. In this case there will be two pKa’s, one acidic & one basic. When the pavrity of the drug sample can be assured the solubility obtained in acid for a weak acid or albali for a weak base can be assured to be the instensic solubility (Co.) i.e. the fundamental solubility when completely unionized. The solubility should ideally be measured at two temperatures.

 1)4C to ensure physical stability and entered short term storage and chemical stability unit more definitive data are available. The minimum density of water occurs at 4C. This leads to a minimum aqueous solubility.
 2)37C to support biopharmaceutral evaluation.    



2.      pKa Determination:-
Determination of the dissociation content for a drug capable of ionization within a ph rang of 1 to 10 is important since solubility and consequently absorption, cab be altered by orders of magnitude with changing pH. The Henderson – Hasseslebach equation provides an estimate of the ionized and un-ionized durg concentration at a particular pH.

 For acidic compounds
 pH = pKa + log  (un-ionized drug]) / [ionized drug])

3.      Partition Co-efficient :-
Partition Coefficient (oil/ water) is a measure of a drug’s lipophilicity and an indication of its ability to cross cell membranes. It is defined as the ratio of unionized drug distributed between the organic and aqueous phases at equilibrium.

P o/w = (C oil / C water) equilibrium.

For series of compounds, the partition coefficient can provide an empiric handle in screening for some biologic properties. For drug delivery, the lipophilic/ hydrophilic balance has been shown to be a contributing factor for the rate and extent of drug absorption. Although partition coefficient data alone does not provide understanding of in vivo absorption, it does provide a means of characterizing the lipophilic/ hydrophilic nature of the drug.

Since biological membranes are lipoidal in nature. The rate of drug transfer for passively absorbed drugs is directly related to the lipophilicity of the molecule. The partition coefficient is commonly determined using an oil phase of octanol or chloroform and water.

Drugs having values if P much greater than 1 are classified as lipophilic, whereas those with partition coefficient much less than 1 are indicative of a hydrophilic drug.

Although it appears that the partition coefficient may be the best predictor of absorption rate, the effect id dissolution rate, pKa and solubility on absorption must not be neglected.

Dissolution:-
The dissolution rate of the drug is only important where it is the rate limiting step in the absorption process. Kaplan suggested that provided the solubility of a drug exceded to mg/ ml at pH, 7 no bioavailability or distinction related problems were to be expected. Below / mg/ ml such problems were quite possible and salt formation could improve absorption and solubility by controlling the pH of the microenvironment, independently of the drug and dosage forms position within the GI ireat.

Intrinsic Dissolution Rate:-
When dissolution is controlled solely by diffusion the rate of diffusion is directly proportional to the saturated concentration of the drug in solution under these conditions the rate constant K1 is defined by

 K1 = 0.62 D2/3 v 1/6 w1/2

Where, V is the kinemative viscosity, W is the anguter velocity of a rotating disc of drug.


Common Ion Effect:-
A common ion significantly reduces, the solubility of a slightly soluble electrolyte. The ‘selling out’ results from the removal of water molecules as solvent owing to the completing hydration of other ions. The reverse process ‘salting in’ qries with large anions e.g. benzoate, salivate which open the water structure. These hydro topics increase the solubility of properly water soluble compounds such as diazepam.

Melting Point:- 
The melting point of a drug can be measured using three techniques:-
1) Capillary Melting
2) Hot Stage Microcopy
3) Differential scanning calorinetry or thermal Anaylysis.



Capillary Melting:-
Capillary melting gives information about the melting range but it is different to assign an accurate melting point.

Hot Stage Microcopy:-
 This the issued observation of melting under a microscope equipped with a heated and lagged sample stage. The heating rate is controllable and upto three transitions can e registered.  

Differential Scanning  Calorimeltry and thermal analysis:-
Differential thermal analysis (DTA) measures the temperature difference between the sample and a reference as a function of temperature or time when heating at a constant rate differential scanning calorinetry (DSC) is similar to DTA except that the instrument measures the amount of energy required to keep the sample at the same temperature as the reference i.e. it measures the enthalpy of transition.

4.      Crystal Properties and Polymorphism:-
Many drug substance can exit in more than one crystalline from with different space lattice arrangements. This property is known as polymorphism. Polymorphs generally have diffrent melting points, x-ray diffraction patterns and  solubility even though they are  chemically identical.
Differences in the dissolution rates and solubilities of different polymorphic forms of a given drug are very commonly observed. When the absorption of a drug is dissolution rate limited, a more soluble and faster-dissolving from may be utilized to improve the rate and extent of bioavailability.

For drugs pane to degradation in the solid state, physical form of the drug influences degradation. Selection of a polymorph that is chemically more stable is a solution in many cases. Different polymorph also lead to different morphology, tensile strength and density of power bed which all contribute of compression characteristics of materials. Some investigation of polymorphism and crystal habit of a drug substance as it relates to pharmaceutical processing is desirable during its Preformulation evaluation especially when the active ingredient is expected to constitute the bulk of the tablet mass. Although a drug substance may exist in two or more polymorphic forms, only one form is theromdynamically stable at a given temperature and pressure. The other forms would convert to the stable form with time. In general, the stable polymorph exhibits the highest melting point, the lowest solubility, and the maximum chemical stability. Various techniques are available for the investigation of the solid state. These include microscopy (including hot stage microcopy), infrared spectrophotometry, single-crystal x-ray and x-ray power diffraction, thermal analysis, and dilalometry.

5.      Particle Size, Shape and Surface Area:-
Bulk flow, formulation homogeneity, and surface-area controlled processes such as dissolution and Surface morphology of the drug particles. In general, each new drug candidate should be tested during Preformulation with the smallest particle size as is practical to facilitate preparation of homogeneous samples and maximize the drug’ s surface area for interactions.

Various chemical and physical properties of drug substances are affected by their particle size distribution and shapes. The effect is not only on the physical properties of solid drugs but also, in some instances, on their biopharmaceutical behavior. It is generally recognized that poorly soluble drugs showing a dissolution- rate limiting step in the absorption process will be more readily bio available when administered in a finely subdivided state rather than as a coarse material.

 In case of tablets, size and shape influence the flow and the mixing efficiency of powders and granules. Size can also be a factor in stability: fine materials are relatively more open to attack from atmospheric oxygen, the humidity, and interacting axcipients than are coarse materials.
- Determination of particle size
-Determination of surface area

Particle size Determination:-
Though microscopy is the simplest technique of estimating size ranges and shapes, it is to slow for quantitative determination the material is best observed as a suspension in non dissolving fluid. Saving is less useful technique at preformulation storage due to lack of bulk material. Andreason  pipette is based on the rate difference of sedimentation of different particles, but techniques like this are seldom used due to their tedious nature instruments based on light scattering, (Royco), light blockage (HIAC) and blockage of electrical conductivity path (coulter counter) are available.

Surface Area Determination:-
Surface area is most commonly determined based on brunaver emette teller (BET) theory of adsorption. Most substances adsorb a mono molecular layer of gas under certain conditions of partial pressure of gas and temperature. Knowing the monolayer capacity of adsorbent and the area of absorbale molecule, the surface area can be calculated the adsorption process is carried out with nitrogen at-195 degree Celsius at a partial pressure attainable when nitrogen is in a 30% temperature with an inert gas (helium). The adsorption takes place by virtue of vander wall’s forces.

Power Flow Properties:-
When limited amounts of drugs are available Power flow properties can be evaluated by measurements of bulk density and angle of repose. Changes in particles size, and shape are generally very important an increase in crystal size or a more uniform shape will lead to a small angle or rpose  and a smaller Carr’s index. 

Bulk Density:-
Knowledge of absolute and bulk density of the drug substance is Very useful in Having some idea as to the size of final dosage form the density of solids also of affects their flow Properties Carr’s compressibility index can be used to predict the flow properties based on density measurement.
 


 A similar index has been defined by Hausner: 
 
Angle of repose:-
The maximum angle which is formed b/w the surface of a pile of powder and horizontal surface is called the angle of repose.

Relationship between flow, angle of repose, Carr’s index fee power flow



6.      Chemical stability profile:-
Preformulation stability studies are usually the first quantitative  assessment of chemical stability of a new drug. These studies include both solution and solid state experiments under condition typical for the handing, formulation, storage, and administration of a drug candidate as well as stability in presence of other recipients.

 Factor effecting chemical stability critical in rational dosage form design include temperature, pH and dosage form diluents. The method of sterilization of potential product will be largely dependent on the temperature stability of the drug. Drugs having decreased stability at elevated temperatures cannot be sterilized by autoclaving but must be sterilized by another means, e.g., filtration. The effect of pH on drug stability is important in the development of both oral administration must be protected from the highly acidic environment of the stomach. Buffer selection for potential dosage forms will be largely based on the stability characteristic of the drug.
- Solid state stability
- Solution phase stability
- Compatibility studies: stability in the Presence of excipients
- Typical stability protocol for anew Chemical Entity

Solid state stability:-
Chemical instability normally results from either of the following reaction; hydrolysis, oxidation, photolysis and pyrolysis, Chemical structure of the drug is the determination of drug to either of these attacks. Esters and lactase and to lesser extent, amides are to prone to solvolysis. Instauration or electron rich centre in the structure make the molecule vulnerable for free radical mediated or photo-catalysed oxidation. physical properties of drugs. Amorphous materials are less stable than their crystalline forms. Denser materials are more stable to ambient stress.

Elevated temperature studies:-
The elevated temperatures commonly used are 40, 50, and 60 degree centigrade with ambient humidity. The samples stored at highest temperature are observed weekly for physical and chemical changes and compared to an appropriate control . If a substantial change is seen, samples stored at lower temperature are examined. If no changesisseen after 30 days at 60 degree centigrade, the stability prognosis is excellent.

Stability under high humidity conditions:-
Solid drug samples can be exposed to different relative humidity conditions by keeping them in laboratory desiccators containing saturated solutions of various salts. The closed desiccators in turn are kept in oven to provide constant temperature. The preformulation data of this nature are useful in determining if the material should be protected and stored in controlled low humidity environment or if non aqueous solvent be used during formulation.

Photolytic stability:-
Many drugs fade or dorpen on exposure light. Though the extent of degradations small and limited to the exposed surface area, it presentsanaesthetic problem. Exposure of drug 400 and 900 foot-candles of illumination for 4 and 2 week periods respectively is adequate to provide some idea of photosensitivity. Resulting data may be useful in determining if an amber colored container is required or if color masking bye should be used in the formulation.

Stability to Oxidation:-
Drug’s sensitivity to oxidation can be examined by exposing it to atmosphere of high oxygen tension. Usually a 40% oxygen atmosphere allows for rapid evaluation. A shallow layer of drug exposed to a sufficient headspace volume ensures that the system is not oxygen limited. Samples are kept in desiccators equipped with three-way stop cocks, which are alternatively evacuated and flooded with desired atmosphere. The process is repeated 3 or 4 times to ensure 100% desired atmosphere. Results may be useful in predicting if an antioxidant is required in the formulation or if the final product should be packaged under inert atmospheric conditions.

Compatibility studies:-
The knowledge of drug excipients interaction is useful for the formulation to select appropriate excipients. The described preformulation screening of drug excipients interaction requires only 5mg of drug in a 50% mixture with the excipients to maximize the likelihood of obscuring an interaction. Mixtures should be examined under nitrogen to ultimate oxidation and paralytic effect at a standard heating rate on DSC, over a temperature range, which will encompass any thermal changes due to both the drug and appearance or disappearance one or more peaks in themogrames of drug excipient mixtures are considered of indication of interaction.

Solution phase stability:
As compared with the dry form, the degradation is much rapid in solution form. It is important ascertain that the drug doesn’t degrade when exposed to GI fluid. The pH based stability study, using different stimulator GI condition can be designed. A poor solution stability of drug may urge the formulator to choose a less soluble salt form, provided the bioavailability is not compromised

Absorption behavior:
It is essential to test the in vivo behavior of the new drug for successful formulation of a dosage from good bioavailability. Partial in vivo and in vitro test are designed to study pharmacokinetic profile of the drug.









References:
1. Pharmaceutical Preformulation
    (Wei-Qin (Tony) Tong, Ph.D.)
2. The Theory and practice of Industrial Pharmacy, 
    (Leon. Lachman, H.A. Lieberman, J.L. Kanig)
3. Modern Pharmaceutics
    (G. Banker and C.T. Rhodes)
4. Preformulation and Formulation
    M. Gibson, Pharmaceutical