ThinkPad X220 Tablet and X220i Tablet Hardware Maintenance Manual
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Transcript of Tablet
S. B. Thoke [M. pharm]
TABLET
WHAT IS TABLET …..?
DEFINITION
Tablets are solid preparations
consisting of one or more active ingredient
obtained by compressing uniform volumes of particles into
. various
shapes and sizes.
THE INGREDIENT CLASSIFICATION USED IS:
Fillers- Lactose, Starch, Dextrose, Mannitol, Sorbitol, Maltodextrin,
Sucrose, Cellulose etc.
Binders- acacia, gelatin, liquid glucose, sucrose syrup, starch paste,
methyl cellulose, CMC, PVP, EC, HPMC etc.
Disintegrates
Lubricants, Glidants, Anti-adherents
Wetting agents
Colors and flavors
Preservatives
LIST OF DISINTEGRANTS
DISINTEGRANTS CONC. IN GRANULES(%)
SPECIAL COMMENTS
Starch USP 5-20 Higher amount is required, poorly compressible
Starch 1500 5-15
Avicel®(PH 101, PH 102)
10-20 Lubricant properties and directly compressible
Cross-linked starchExplotab®
2-8 Sodium starch glycolate, superdisintegrant.
Crosscarmellose sodium AC-Di-Sol®
1-3 Direct compression
LUBRICANTS
In tablet manufacturing one faces the problem of flow of granules from the
hopper into the die cavity, sticking of material to the punches and die walls
and release free movement of the compressed tablets from the die cavity.
To overcome these difficulties
Lubricants- prevent adhesion of the tablet material to the surface of the
dies and punches, reduce interparticle friction, facilitate an easy ejection of
tablets from the die cavity and improves rate of flow of tablet granulation.
Eg. Talc, magnesium stearate, calcium stearate, stearic acid, hydrogenated
vegetable oil and PEG.
The quantity of lubricant significantly varies from 0.1 to 5%.
LIST OF LUBRICANTS
Lubricants Conc. Comments
Stearates(Magnesium Stearate, Calcium Stearate, Sodium stearate)
0.25 -1 Reduce tablet strength; prolong disintegration; widely used.
Talc 1 -2 Insoluble but not hydrophobic; moderately effective.
Glyceryl behapate (Compritol®888)
1 - 5 Both lubricant and binder;
GLIDANTS
Glidant-
Improves the flow characteristics of a powder mixture.
Always added in the dry state just prior to compression.
Eg. colloidal silicon dioxide (Cabosil®, Cabot®) and asbestos free talc etc.
They are used in concentration less than 1%.
Talc is also used and may serve the dual purpose of lubricant/glidant.
Glidants Range
Colloidal silica i.e. syloid, pyrogenic silica 0.25%
Hydrated sodium silioaluminate 0.75%
ANTIADHERENTS
Some material have strong adhesive properties towards the metal of
punches and dies or the tablet formulation containing excessive moisture
which has tendency to result in picking and sticking problem.
Antiadherent prevent sticking to punches and die walls.
Eg. Talc, magnesium stearate and corn starch etc.
Antiadherants Range Comments
Talc 1 – 5 Lubricant with excellent antiadherents properties
Cornstarch 3 –10 Lubricant with excellent antiadherents properties
Sodium lauryl sulfate <1 Antiadherents with water soluble lubricant
Colloidal silica 0.1 – 0.5 Does not give satisfactory results due to small surface area. Cab-O-Sil® and Syloid®
Stearates <1 Antiadherents with water insoluble lubricant
COLORS
Natural vegetable colors – limited availability & unstable
FD&C and D&C approved dyes are used.
Either added in dry granulation mix or in vehicle used for wet
granulation.
Lake dyes ( dyes absorbed on alumina or aluminium hydroxide) are used
in dry granulation.
Dyes tend to fade on standing and exposure to light leads to mottling.
Eg. FD&C approved lakes and dyes – lake sunset yellow, brilliant blue,
ferric oxide.
FLAVORS
Flavor's are usually limited to tablets intended to dissolve in the mouth.
In generally water soluble
Little acceptance in manufacturing due to poor stability.
Do not affect any physical characteristics of the tablet granulation.
Incorporated by spraying them on to the granules in the form of solutions
in some volatile organic solvent.
Also can be incorporated with lubricants
Proportion limited to 0.5 %
Excess quantity will interfere with free flow of granules
e.g. Raspberry, Pineapple, Peppermint, Blackcurrant, Orange, Mango,
Strawberry etc.
SWEETENERS
Use is primarily limited to tablets meant to dissolve in oral cavity
Mannitol – 72% as sweet as sucrose
Earlier saccharin was the only artificial sweetener used. It is 500 times
sweeter than sucrose but has a bitter aftertaste and also carcinogenic
properties.
Aspartame is the new sweetener- disadvantage is its instability in the
presence of moisture.
Three main manufacturing methods are used to prepare the running
powder:
1. Wet granulation
2. Direct compression
3. Dry granulation or slugging
Content uniformity
Uniform chemical composition.
Good mixing is essential, and segregation during the process
should be prevented.
WET GRANULATION
Wet granulation is a process of dry mixing, wet mixing, and particle size enlargement, and is a process of particle attachment (agglomeration).
It consists of six steps:
1. Dry mixing
2. Wet mixing
3. Milling of the wetted mass
4. Drying
5. Milling of the dried mass
6. Final blending
Wet Granulation
Mix powders
Add binder
Mill coarsely
Dry
Mill
Blend & lubricate
Compress or
fill into capsules
ADVANTAGES OF WET GRANULATION
Physical characteristics of the drug are usually not important.
The coalescing of particles locks in blend uniformity.
A wide variety of powder materials can be processed into a uniform
mix with improved flow.
Optimum fill density can be achieved by adjusting the process to create
the optimum final particle size distribution.
Compressibility and consolidation are improved via the choice of the
correct binder and the moisture content of the granules.
Dissolution is modified through hydrophilization to improve wetting
or, with the choice of more insoluble binders, to obtain a modified
release pattern.
Dust and segregation tendencies are reduced.
DISADVANTAGES OF WET GRANULATION
Large number of process steps; each step requires qualification,
cleaning, and cleaning validation.
Long process time, particularly for drying.
High labor and manufacturing costs.
Some material loss during processing.
Problems associated with heat and solvent sensitive drugs.
Capital requirements for extra building space and equipment.
Upon aging, dissolution from granules can be slowed after tableting.
Assay problems may occur for low dosage drugs due to incomplete
extraction if the active ingredient is complexed by the binder, or
adsorbed onto one of the other excipients.
Still no exact way to determine granulation endpoint (torque, power
consumption, etc.).
SINGLE-STEP FLUID BED WET GRANULATOR
Fluid-bed granulator
Binder solution spray
Warm air flow
DIRECT COMPRESSION
This is, a two-step process involving screening and/or milling and final
mixing.
An effective binder is needed and should have good compression and
consolidation properties as a dry additive, even at low concentrations
(< 30%) in the formulation.
Good adhesive properties in the dry form are a combination of a rough
and porous surface combined with a van der Waal's and/or a hydrophilic
bonding mechanism to attach the active ingredient(s) to the excipient.
This feature is needed to assure good mixing of drug and excipients and
to prevent segregation.
ADVANTAGES OF DIRECT COMPRESSION
Economy in labor, time, equipment, operational energy, and space.
Problems due to heat and moisture eliminated.
Greater physical stability provided; hardness and porosity changes
less with time when direct compression is broadly compared to wet
granulation systems.
Extraction of the drug from the dosage form is not inhibited during
the assay procedure (polymer binding).
Choice of ingredients allows the formulator to improve or retard
dissolution rate.
DISADVANTAGES OF DIRECT COMPRESSION
Critical nature of the raw materials; need for greater quality control in
purchasing to assure batch uniformity.
Difficulty obtaining dense hard tablets for high-dose drugs.
Non-homogenous distribution of low-dose drugs due to segregation after
blending (content uniformity).
Sensitivity of direct compression 'running' blends to over lubrication.
Limitations in color variations.
Need for assisted feed and precompression for some high-dose drugs.
Need for commensurate particle size or particle size distribution between
drug and excipients.
DRY GRANULATION
1. Mixing
2. Roller compaction
3. Milling
4. Screening
5. Final blending
Roller CompactorIt consists of five steps:
Compact
Size reduction ofcompacts intogranules
Powder to becompacted
Roller compactor"Chilsonator”
FINAL BLENDING
Final blending is usually done in a cone or V-type blender,
To obtain the final blend, it is necessary to consider the objectives of the
mixing steps:
1. To achieve drug content uniformity
2. To obtain uniformity of flow and bulk density
3. To effect distribution of lubricant, color, and surface active agents
4. To reduce or eliminate segregation
FINAL BLENDING
Mill
Blend & lubricate
Compress or
fill into capsules
EQUIPMENT'S USED FOR MIXING, BLENDING AND LUBRICATION
High share mixers
Tumbling mixers
Y-cone
Rotating cube
Double cone
Fluidized bed
Agitator mixers
Ribbon blender
TUMBLEBLENDERS
DRY MIXING EQUIPMENT'S
Sigma blade mixer Planetary mixer
Littleford Lodige mixers
GRANULATOR MIXER
Diosna mixer
RMG
EQUIPMENT'S USED IN SIEVING
COMPRESSION
Tableting procedure Filling Compression Ejection
Tablet compression machines Hopper for holding and feeding granulation to be compressed Dies that define the size and shape of the tablet Punches for compressing the granulation within the dies Cam tracks for guiding the movement of the punches Feeding mechanisms for moving granulation from the hopper into the
dies
SINGLE PUNCH MACHINE
The compression is applied by the upper punch
Stamping press
Upper andLower Collar
Collar locker
Common stages occurring during compression
Stage 1: Top punch is withdrawn from the die by the upper cam. Bottom punch is low in the die so powder falls in through the hole and fil ls the die
Stage 2: Bottom punch moves up to adjust the powderweight-it raises and expels some powder
Stage 3: Top punch is driven into the die by upper cam. Bottom punch is raised by lower cam. Both punch heads pass between heavy rollers to compress the powder
Stage 4: Top punch is withdraw by the upper cam. Lower punch is pushed up and expels the tablet. Tablet is removed from the die surface by surface plate
Stage 5: Return to stage 1
MULTI-STATION ROTARY PRESSES
The head of the tablet machine that holds the upper punches, dies
and lower punches in place rotates.
As the head rotates, the punches are guided up and down by fixed
cam tracks, which control the sequence of filling, compression and
ejection.
The portions of the head that hold the upper and lower punches are
called the upper and lower turrets.
The portion holding the dies is called the die table.
DIES & PUNCHES
Dies
Lower punchUpper punch
COMPRESSION CYCLE
Granules from hopper empty in the feed frame (A) containing several interconnected compartments.
These compartments spread the granulation over a wide area to provide time for the dies (B) to fill.
The pull down cam (C) guides the lower punches to the bottom, allowing the dies to overfill
The punches then pass over a weight-control cam (E), which reduces the fill in the dies to the desired amount
A swipe off blade (D) at the end of the feed frame removes the excess
granulation and directs it around the turret and back into the front of the
feed frame
The lower punches travel over the lower compression roll (F) while
simultaneously the upper punches ride beneath the upper compression
roll (G)
The upper punches enter a fixed distance into the dies, while the lower
punches are raised to squeeze and compact the granulation within the
dies
After the moment of compression, the upper punches are withdrawn as
they follow the upper punch raising cam (H)
The lower punches ride up the cam (I) which brings the tablets flush
with or slightly above the surface of the dies
The tablets strike a sweep off blade affixed to the front of the feed
frame (A) and slide down a chute into a receptacle
At the same time, the lower punches re-enter the pull down cam (C)
and the cycle is repeated
HIGH SPEED ROTARY MACHINE
MULTI ROTARY MACHINE
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If any question or further clarifications write to
Cell: +91 8275584727
Thanks
25-02-2013
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