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Solvent or Aqueous Film Coating
By Suresh Pareek & Chetan Rajsharad
Tablet coating, which is known to pharmaceutical industry
for more than 200 years has undergone several changes during last 25 years owing
to the rapid development in pharmaceutical technology. As the industry is continuously
striving to provide modern medicines, the volumes required to be produced has
increased manifold. Due to the increased demand, the pressure on the industry
to manufacture pharmaceuticals like sugar coated tablets in large quantities
in short period of time, has increased. Hence, it became necessary to invest
efforts towards developing the tablet coating technology.
Research scientists in industry as well as academia have risen
to this challenge and developed the process of film coating. The coating equipment
available were meant for sugar coating; in order to adapt the process of film
coating, one had to change the solvent medium from water to organic solvents
as water being less volatile was causing problems in sufficient drying. Certainly
the use of organic solvents was much easier to use and provide good opportunity
to convert sugar coating, a time consuming and skilled operation, to a much
faster process of film coating.

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The latent heat of vaporisation of commonly used
solvents is as seen below
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Solvent
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Latent Heat (kj/kg)
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Methylene Chloride
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556
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Methanol
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1967
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Water
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2260
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Different solvents which were used (in some cases still being used) for different
application are (either alone or in combination) :
- Ethyl Alcohol
- Methyl Alcohol
- Isopropyl Alcohol
- Methylene Di chloride
- Acetone
- Chloroform
Such an effort to reinvent the tablet coating technology has not stopped just
by developing the process of film coating. As the consumption of organic solvents
increased alarmingly, the cost of these organic solvents increased. Moreover,
the people concerned with the protection of the environment, raised an objection
to high usage of toxic organic solvents. Hence, companies are attempting to
eliminate the usage of organic solvents completely due to:
The hazards associated with using both flammable and potentially toxic solvents.
Dealing with the environmental issues that are associated with organic solvents.
The organic solvents are expensive and are likely to become more expensive in
future.
The cost of insurance of the manufacturing facility is now very high if one
uses the organic solvents.
The best alternative to overcome these adverse situation is to revert back to
water as the solvent medium for tablet coating.
Scientists have observed several problem when converting this solvent system
from organic to aqueous :
- Increase in coating suspension preparation time
- Increase in coating time
- Negative impact on the drug stability; if water
is not effectively removed from coating
- Increased likelihood that the harsher coating condition
(working at elevated temperatures) may affect the drug release characteristics
(change in DT and dissolution profile)
The challenge is therefore, to develop suitable coating products and process
to effectively remove the water from the system and yet work under suitable
working conditions so as to maintain the product stability and the drug release
characteristics.
From the above figures, it is clear that water requires much higher amount of
energy for vaporistion. This energy for evaporation is a combination of Temperature
and Air CFM (volume). In aqueous or water-based system, process parameters and
set up of coating equipment play an important role. By the use of more efficient
coating products and by controlling the process parameters and coating equipment
set up, the whole system can be made efficient enough to make this conversion
from organic solvent to aqueous possible.
Another important factor is that the compressed air should be free from moisture;
air line should be fitted with suitable moisture trap and air filter or dehumidified
air can be used. Similarly, number of Baffles, Inlet air CFM, Exhaust CFM and
Pan RPM play an important role. It is necessary and advisable to use peristaltic
pump in case of conventional coating set up.
The example has been considered for 42 Conventional pan with 80 kg tablet
load of 200 mg each tablet totaling to a batch size of 4,00,000 Nos. The comparison
was done for solvent and aqueous system. Considering a theoretical weight gain
of three percent total film coating material required will be 2.4 kg (Sr.No.8
in the table) with a reconstitution level of five percent for organic system
the total solvent required will be (100-5) / 5 X 2.4 kg. Out of this 65 percent
will be MDC i.e. 29.6 kg and IPA will be 35 percent i.e. 16 kg. Taking an average
cost of Rs 70 per kg for IPA and Rs 48 for MDC the total cost of solvents works
out to Rs 2540 for 80 kg of tablets per batch. Assuming two batches are coated
per day i.e. 50 batches per month for 25 days working, total saving is the solvent
cost per month will be Rs1,27,000 totaling to Rs15.25 lakhs per annum. The saving
calculated above are based on the assumptions ment-ioned and may differ as per
actual conditions. There may be some changes required in the conventional coating
pan set up in the following:
- Drying Air Capacity Air Volume and heating
capacity to be increased
- Increase in number of Baffles
- Exhaust Air volume
- Peristaltic Pump
The cost for the above modifications will be approx. Rs 1.50 lakhs which is
recoverable in one month.
The coating process parameters have been considered for the same batch size
as in the example in Table 1. Because of the difference in reconstitution level
of organic (five percent ) and Aqueous Instacoat Aqua III (15 percent) the total
film coating solution is 48 kg for solvent system and 16 kg for aqueous system.
With a spray rate of 300 gm per minute for solvent system as compared to 120
gms for aqueous system time taken for aqueous system is 133 minutes as against
160 minutes for solvent based system thus there is a time saving of about 27
minutes per batch-16 percent.
These enable the users to successfully migrate from solvent
to aqueous system, technical experts from Ideal Cures are in a position to offer
services for taking commercial batches as well as for providing the technical
training to the production staff.
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Let us also look at the Coating Parameters for both
Solvent & Aqueous coating as mentioned in the Table 2
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PARAMETERS
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CONVENTIONAL COATER
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CONVENTIONAL COATER
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| COATING EQUIPMENT |
PAN 42" |
PAN 42" |
| Tablet Charge ( kg ) |
80 |
80 |
| Solvent System |
Organic |
Aqueous |
| Pan Speed(rpm) |
8-10 |
8-10 |
| Baffles |
3 |
6 |
| Tablet bed temperature(șC) |
35-40 |
37-40 |
| Spray nozzle(mm) |
1.5 |
1.5 |
| Number Of Spray Guns |
1 |
1 |
| Atomising air pressure(bar) |
2.5-3.5 |
2.5-3 |
| Spray procedure |
Continuous |
Continuous |
| Drying air volume(cfm) |
500-600 |
800-900 |
| Inlet air temperature |
60-65 |
70-75 |
| Weight gain(%) on Tablet |
2.5 |
2.5 |
| Process Loss |
0.5 |
0.5 |
| Total Material Required% |
3% |
3% |
| Total Material Required Kgs |
2.4 |
2.4 |
| Solid Contents(%) |
5 |
15 |
| Total Solvents Required kgs |
45.6 |
13.6 |
| Total Solution in Gms |
48000 |
16000 |
| Spray rate(g/min) |
300 |
120 |
| Total time taken in Minutes |
160 |
133 |
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The following table gives the comparison in saving
of cost of Solvent vs Aqueous coating.
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COMPARITIVE COST SOLVENT VS. AQUEOUS SYSTEM IN CONVENTIONAL
COATING PAN
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SOLVENT BASED SYSTEM
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INSTACOAT AQUA III
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| COATING PAN SIZE |
Inch |
42" |
42" |
| Total Weight of the Tablets |
Kgs |
80 |
80 |
| Weight of each tablet |
mg |
200 |
200 |
| Batch Size - No of Tablets |
Nos |
400000 |
400000 |
| Average weight gain After Coating |
% |
2.5 |
2.5 |
| Spray Loss during coating Process |
20% |
0.5 |
0.5 |
| Total INSTACOAT required in |
% |
3 |
3 |
| INSTACOAT Required including spray loss |
Kgs |
2.4 |
2.4 |
| RECONSTITUTION LEVEL (SOLID CONTENTS) |
% |
5 |
15 |
| Total Quantity of Organic Solvents required |
Kgs |
45.6 |
13.6 |
| Water |
0 |
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13.6 |
| IPA |
kgs |
16 |
0 |
| MDC |
Kgs |
30 |
0 |
| Cost of Solvent |
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| Water |
Rs. |
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| IPA @ Rs 70 per Kg |
Rs. |
1117 |
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| MDC @ Rs. 48 per Kg |
Rs. |
1423 |
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| TOTAL COST of Solvent for 80 kg. Tablets |
Rs. |
2540 |
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| Total No of Batches per Month |
Nos |
50.00 |
50.00 |
| Total Savings of Solvent per Month |
Rs |
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127000 |
| Total Savings of solvents per Year |
Rs |
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1524000 |
E-mail: srp19@vsnl.com
Fax: 022-56764495
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