Process for manufacturing effervescent granules and tablets and high efficiency granulation tower for such process
The invention relates to a process for manufacturing effervescent tablets consisting in the steps of careful humidifying of the acid+base mixture, pre-drying and final drying and granulating.It has been found that these operations can be performed in a single apparatus, either integrally in fluid bed, or with vacuum-drying.
The present invention relates to an improved process for manufacturing effervescent mixtures and tablets containing in particular active principles for pharmaceutical use.
In this domain, positive progress has been made by the techniques described in French Pat. Nos. 71 12175 and 71 35069.
These techniques employ three stages of operation:
(1) Careful humidification of the sodium bicarbonate by a very small quantity of demineralized water, then addition of citric acid and possibly of glycocoll (binding agent), all this in a mixer of the kneader type, which starts off the reaction of the bicarbonate on the citric acid;
(2) pre-drying of the mixture in fluid bed obtained by blowing hot air, which interrupts the reaction;
(3) final drying, likewise in fluid bed, obtained by blowing hot air.
The two Patents mentioned above described with precision the details of the modus operandi for each of the three phases: duration, temperature of the air, humidity content, speed of the air jet, etc., and the man skilled in the art may usefully refer to them.
Although very interesting, this technique presents the drawback of necessitating the transfer of the filler, after step (1), from the mixer to the drier. Consequently, the effervescent reaction triggered off in the mixer cannot be mastered with total precision as its interruption, which occurs in step (2) in the drier, depends on the time for emptying and transferring the filler towards the drier, which time varies from one batch to the following.
This variation in time has a considerable repercussion on the quality of the grain at the end of granulation.
No solution to this problem of industrial working has been found since the invention of the technique, about twelve years ago, despite the obvious interest in solving it and the attempts which have been made to that end.
It has now been discovered, according to the invention, that all of the reactions and operations described hereinabove can be carried out in one and the same multi-function apparatus.
Taking into account the very high precision required in these operations in order to satisfy the very strict quality requirements laid down by the pharmaceutical industry (particularly concerning the homogeneity of the finished granule, and the interruption at a very precise degree of advance of the reaction initiated by the addition of solvent), this was not considered possible.
However, Applicant has achieved this result and, moreover, has also improved the quality of the granules.
BRIEF DESCRIPTION OF THE DRAWINGSThe invention will be more readily understood on reading the following description with reference to the accompanying drawings, in which:
FIG. 1 shows the apparatus, and in particular the granulator-drier, used for the tests referred to hereinbelow according to one variant embodiment of the invention.
The references in FIG. 1 have the following meanings:
A: hygrometric treatment of the air
B: dry incoming air
C: powder in suspension
D: humid outgoing air
1, 3 and 7: filters
2 and 8: turbines
4: heating element
5: heat regulating system
6: solvent spray
The operation of such an apparatus is obvious and is, moreover, generally known.
FIG. 2 schematically shows the arrangement of apparatus according to another variant of the invention in a production tower.
In FIG. 2, the references have the following meanings:
1. production tower
2. storage hoppers
3. automatic supply
4. mixing-granulation-drying apparatus
5. heat exchange hopper
6. band mixer
7. emptying
DESCRIPTIONAccording to a first variant of the invention (FIG. 1), a granulator-drier operating entirely in fluid bed is used.
Granulator-driers of the type which will be described hereinafter have been known for a long time.
However, it was not thought possible that the turbulence created in such apparatus by the blowing of air could suffice to suitably "imbricate" the particles of the starting reactive materials, which is essential in the technical sector in question, and it was thought, on the contrary, that only a "mechanical" stirring, i.e. of the type obtained by the blades in the mixers used in the prior known technique, could give a valid result. This is why no attempt has ever been made to use the granulator-driers, which are nonetheless well known.
It has now been unexpectedly discovered that these apparatus enable the particles of the starting material used in the technique in question to be correctly imbricated.
It is therefore possible to carry out the three operational steps mentioned above in one and the same apparatus, with the following very important advantages both as regards the quality of the products and industrial profitability:
no emptying or transfer of the reaction mixture, therefore providing the possibility of interrupting the effervescent reaction in extremely precise manner; this in turn leads to the disappearance of the differences which might be noted from one batch to another in the prior known technique;
saving of time
the conventional mixers had to be placed under aspiration in order to avoid a rise in pressure due to the formation of CO.sub.2. In addition, they had to be regularly unclogged. These two factors caused considerable losses of powder, which are not found in the new process according to the invention (about 1%);
possibility of calculating parameters of and automating the granulator-driers used, which was very difficult, if not impossible, in the prior known technique.
The principle of wet granulation used makes it possible to obtain, from powders of defined calibre, an elaborate product whose granulometric characteristics are adapted for subsequent compression.
The process of granulation also enables mixtures of powders of homogeneous chemical composition to be obtained by using fluidization.
Granulation consists in a fixation by chemical bond of the particles of sodium bicarbonate and of citric acid. These chemical bonds are obtained by an addition of a defined quantity of demineralized water which provokes a partial effervescent reaction with the formation of mono-, di- or trisodium citrate. These molecules of sodium citrate are considered as bridges bonding the particles of sodium bicarbonate and the particles of citric acid and give the mixture the physical properties of compressibility.
The effervescent reaction triggered off by an outside addition of 1 to 6% by weight of aqueous solvent (water or wetting solution) will continue by itself as it is generative of water, and it will be interrupted by drying by means of hot dry air (60.degree.-70.degree. C.).
The .[.proces.]. .Iadd.process .Iaddend.of granulation-drying is applicable in particular to the production of an excipient type effervescent mixture on which the active principles and lubricants are added in a subsequent operation; by way of example, we shall cite the parameters defined for buffered effervescent aspirin, for which a wet-process granulation is effected on 3 compounds: sodium bicarbonate, citric acid and possibly glycocoll (binding agent).
It is also applicable to the production of an effervescent mixture containing one or more active principles. By way of example, we shall cite the parameters defined for a formula containing paracetamol.
According to a second variant, the invention enables a process of production employing a vacuum to be carried out in particularly .[.effective manner.]. .Iadd.efficient.Iaddend.. This technique makes it possible:
to eliminate the seperate wetting and drying phase
to shorten production time, thus improving productivity
to save energy without forgetting the lesser risk of chemical destabilization by a treatment from solvents.
A further original feature of the invention resides in the fact that the apparatus have been grouped together in a vertical production tower.
According to this second variant (FIG. 2), the process for producing effervescent granules intended for compression is characterized by the creation of a tower 1 in which the following operations are carried out:
1. The weighing of raw materials from storage hoppers 2,
2. the automatic supply (3) of all or part of these raw materials in the mixer-granulator-drier 4,
3. the mixing, granulation and drying of the effervescent granule in vacuo,
4. the cooling in a heat exchange hopper 5 by fluidization more compact than a drier employing fluidized air bed,
5. calibration by oscillating granulator and final mixing in a band mixer 6 for example of the Gondard type on scales for calculating the yield,
6. emptying (7) of this mixer into containers of the Flo-Bin type.
Operations 1 to 6 occur vertically downwardly, transfers taking place by gravity and being dustfree. The interest resides in the fact that the 3 operations of point 3 (mixing, granulation, drying) can be automated from the standpoint of monitoring of the process.
Similarly, operations 1 to 5 in their chronological sequence may be automated. Such automatization renders the process economical from the standpoint of manpower (about 1 t/hr. for 2 persons) by elimination of the interruptions between the operations.
The apparatus serving for mixing-granulation-drying is composed of a perfectly sealed tank, provided with a system of mechanical stirring for mixing the incorporated powders and equipped with lump-breaking cutters which divide the agglomerates formed by the solvent during wetting. This tank must also comprise:
a double wall allowing passage of a heat-exchanging fluid
a trap for admission and emptying of the raw materials
a vacuum-creating apparatus which enables a minimum pressure of 70 millibars to be obtained.
All the mechanical or physical elements intervening in the successive operations of granulation-drying are monitored by thermometric probe, by measurement of amperage and vacuum.
By way of example, an apparatus of the adapted DVT Lodige type is suitable. A further originality of the invention resides in the use of a heat exchange hopper for cooling the granules.
The following Examples illustrate the invention without, however, limiting the scope thereof. For the general modus operandi, reference will be made to the above-mentioned French Patents. Examples 1 to 4 relate to the first variant, and I and II to the second variant of the invention.
EXAMPLE 1reactive principle: aspirin
effervescent mixture:
sodium bicarbonate
citric acid
glycocoll (optional)
for 255.22 kg of powder.
Operation 1: PremixIncorporate successively the sodium bicarbonate, the citric acid and the glycocoll; switch on the turbine of the granulator at an output allowing fluidization of the powders.
Air temperature: 64.degree. C.
Operation 2: SprayingSolvent=demineralized water
The solvent is always sprayed on the powders in suspension in air, which makes it possible to increase the exchange surface between the base particles and the acid particles; at this stage of operation, the output and spray time must be monitored.
Operation 3: DryingThe rate of flow of air is to be monitored so as to avoid too great a turbulence of the powders in the cavity of the apparatus, which would render the particles fragile.
Temperature of incoming air: 64.degree. C.
EXAMPLE 2Granulation on granulator-drier of an effervescent mixture containing a plurality of active principles.
______________________________________
Formula of granulation
______________________________________
Paracetamol 28 kg
Monosodium carbonate 100 kg
Monopotassium carbonate 3.740 kg
Sorbitol 25.500 kg
Anhydrous citric acid 73.000 kg
Ascorbic acid 17.000 kg
TOTAL 247.24 kg
______________________________________
Operation 1: Premix
Operation is carried out as in Example 1.
Air temperature: 64.degree. C.
Operation 2: SprayingNature of the solvent: solvent of manoxol in water
Operation is carried out as in Example 1.
Operation 3: DryingTemperature of air: 64.degree. C.
Operation is carried out as in Example 1.
For the following two Examples, operation is carried out as in Examples 1 and 2, from the formulations hereinbelow:
______________________________________
Disodium sulfate 20.200 kg
Sodium bromide 7.100 kg
Disodium phosphate
13.800 kg
Monosodium carbonate
101.000 kg
Anhydrous citric acid
89.000 kg
______________________________________
Nature of the solvent: aqueous solution by doxylamine succinate
______________________________________
Monosodium carbonate
108.000 kg
Anhydrous citric acid
14.500 kg
Betaine citrate 142.000 kg
______________________________________
Nature of the solvent: demineralized water.
Example I--Example of granulationFormulation
paracetamol
vitamin C
sodium bicarbonate
citric acid
potassium bicarbonate
sorbitol.
The tests were carried out on a mixture of the 58 kg of powders.
Operation 1: PremixThe different raw materials mentioned above are successively incorporated in the mixer 4 without taking into account any physical incompatibilities existing therebetween. The premix is effected in 3 minutes. During this period of time, the temperature of the powder is raised by introducing a heat-exchange liquid in the double jacket of the mixer.
Operation 2: Incorporation of the solvent in the mixer
The solvent is a mixture of water/sodium dioctylsulfosuccinate.
Wetting by spraying, or aspiration of the solvent under .[.partical.]. .Iadd.partial .Iaddend.vacuum.
Concentration of the solvent: 0.64% with respect to the weight of the powder.
Operation 3: GranulationGranulation is effected under atmospheric pressure for 5 minutes.
Operation 4: DryingThis is obtained by reducing the atmospheric pressure to 70 millibars; at that pressure, the boiling point of the solvent is attained. Drying continues by raising the temperature.
This operation lasts about 37 minutes, stoppage of drying being triggered off by monitoring the residual humidity of the powder.
The advantages of this technique are as follows:
obtaining of a granule of better quality, in particular one which is more homogeneous,
use of sufficiently low thermal zones, for the thermolabile active products not to be destabilized,
complete automation possible,
the addition of heat necessary for evaporation of the solvent is very little.
Example II--Example of mixing by direct compression
Formulation:
Calcium carbasalate
Lysine carbamate
Citric acid
Aroma
PEG (polyethylene glycol)
Ammonium saccharinate
Description of manufacture(1) The calcium carbasalate will be stored in one of hoppers 2. It will then be pre-weighed at 3 and incorporated in the mixer-granulator-drier 4.
In this variant of the invention, the automation of the tower makes it possible to eliminate the functions of mixing and granulation and to conserve only the drying function of apparatus 4.
(2) After drying, the calcium carbasalate is sent into cooler 5 in order to return the product to its initial temperature.
(3) Calibration is effected, either by simple passage over a grid, or by crushing, the choice being made as a function of the nature of the products delivered.
(4) Emptying into a band mixer 6 in which the product is exactly weighed.
The four operations mentioned above are then repeated for the lysine carbamate and the citric acid.
After reception of these three constituents in the mixer, the auxiliary constituents: aroma, PEG and ammonium saccharinate, are added into the band mixer.
The running of the mixer and its working principle guarantee the required quality of the active principle of this formula from the standpoint of homogeneity.
Claims
- effervescent mixture:
- sodium bicarbonate
- citric acid
- paracetamol
- monosodium carbonate
- monopotassium carbonate
- sorbitol
- anhydrous citric acid
- ascorbic acid
- mixing means
- means for introducing the solvent
- means for regulating the temperature
- means for creating a vacuum,
- paracetamol
- vitamin C
- sodium bicarbonate
- citric acid
- potassium bicarbonate
- sorbitol..]..[.9. A process as claimed in claim 5 wherein the raw materials in powdered form are as follows:
- calcium carbasalate
- 1ysine carbamate
citric acid..]..Iadd.10. A process for the manufacture of effervescent tablets from a plurality of powdered raw materials, with the avoidance of external contamination, said process comprising the steps of:
- (a) storing said powdered raw materials in storage hoppers;
- (b) transferring said raw materials downwardly by gravity to a granulator-vacuum-dryer device, introducing into said granulator-vacuum dryer device a granulation agent in an amount effective to wet form wet granules and drying under vacuum said wet granules therein to obtain dried granules;
- (c) evacuating the dried granules by gravity from said granulator-vacuum dryer, transferring them downwardly by gravity to a cooler and cooling said dried granules to a temperature at which destabilization is impeded; and
- (d) transferring said dried and cooled granules downwardly by gravity to a storage container;
- said process being carried out in an enclosed vertically arranged apparatus
array..Iaddend..Iadd.11. The process of claim 10, wherein the raw materials are individually subjected to said steps (a), (b) and (c), then mixed together and subjected to direct compression..Iaddend..Iadd.12. The process of claim 10, wherein the raw materials are pre-mixed within said granulator-vacuum-dryer device..Iaddend..Iadd.13. The process of claim 10, wherein said granulation agent is a solvent selected from the group consisting of demineralized water an aqueous wetting solutions..Iaddend..Iadd.14. The process of claim 10, wherein said granulation agent is a solution of dioctylsulfosuccinate in water..Iaddend.
.Iadd. The process of claim 10, wherein after drying and cooling, the dried and cooled raw materials are transferred by gravity to a calibration device..Iaddend..Iadd.16. The process of claim 15, wherein after calibration, said dried, cooled and calibrated raw materials are transferred by gravity to a band mixer..Iaddend..Iadd.17. The process according to claim 10, wherein the raw materials are weighed before any treatment..Iaddend..Iadd.18. The process of claim 10, wherein said dryer has a jacket for a heat exchange fluid and during said drying step (b), said raw materials are subjected to mechanical stirring with lump-breaking cutters, a vacuum is created and a granulation agent introduced by aspiration, the temperature being regulated by circulating a heat-exchange fluid in said jacket..Iaddend..Iadd.19. The process of claim 10, wherein the raw materials comprise:
- effervescent mixture:
- sodium bicarbonate
- citric acid
- paracetamol
- monosodium carbonate
- monopotassium carbonate
- sorbitol
- anhydrous citric acid
- ascorbic acid
water..Iaddend..Iadd.22. The process of claim 10, wherein the raw materials in powder form are as follows:
- calcium carbasalate
- 1ysine carbamate
- citric acid.Iaddend..Iadd.23. The process of claim 10, wherein the raw materials are as follows:
- calcium carbasalate
- 1ysine carbamate
- citric acid
- aroma
- PEG (polyethyleneglycol)
ammonium saccharinate..Iaddend..Iadd.24. A process for the manufacture of effervescent tablets from a plurality of powered raw materials, with the avoidance of external contamination, said process comprising the steps of:
- (a) storing said powdered raw materials in storage hoppers;
- (b) transferring said raw materials downwardly by gravity to a mixer-granulator-dryer device, mixing said raw materials, introducing into said mixer-granulator-dryer device a granulation agent, mixing the raw materials and the granulation agent under substantially atmospheric pressure for a period of time sufficient to achieve formation of wet granules and drying under vacuum said wet granules in said mixer-granulator-dryer device to obtain dried granules;
- (c) evacuating the dried granules by gravity from said granulator-vacuum dryer, transferring them downwardly by gravity to a cooler and cooling said dried granules to a temperature at which destabilization is impeded; and
- (d) transferring said dried and cooled granules downwardly by gravity to a storage container;
- said process being carried out in an enclosed vertically arranged apparatus
array..Iaddend..Iadd.25. The process of claim 24, wherein the granulation agent is introduced by spraying or by aspiration under partial vacuum..Iaddend..Iadd.26. The process of claim 24, wherein there is introduced one to six weight percent of granulation agent..Iaddend..Iadd.27. The process of claim 24, which is automated..Iaddend.
.Iadd. A vertically disposed apparatus array for the manufacture of effervescent tablets, said apparatus array constituting a tower and comprising in vertically descending order:
- (a) storage hopper means positioned near the top of said tower for the storage of raw materials;
- (b) granulation and vacuum drying means including means for introducing a granulation agent to wet form wet granules and means for eliminating humidity from said wet granules to obtain dried granules;
- (c) cooling means for lowering the temperature of said dried granules, and
- (d) at least one storage container for dried and cooled granules:
- said apparatus comprising also means for feeding material by gravity from said storage hopper means to said granulation-vacuum drying means, means for evacuating said dried granules by gravity from said granulation-vacuum-drying means and feeding them by gravity to said cooling means, and means for transferring granules by gravity from said cooling means to said storage container or containers..Iaddend.
.Iadd. The apparatus of claim 28, further comprising calibrating means for calibrating the materials after they leave said cooler..Iaddend..Iadd.30. The apparatus of claim 29, further comprising a band mixer for mixing the materials after they leave said calibrating means..Iaddend..Iadd.31. The apparatus of claim 30, further comprising weighing means for weighing said raw materials before any treatment..Iaddend..Iadd.32. The apparatus of claim 29, wherein said drying device comprises mixing means comprising a system of mechanical stirring with lump-breaking cutters, means for introducing a granulation agent by creation of a vacuum or a spraying system supplied by a pump, means for regulating the temperature comprising a double jacket for circulating heat-exchange fluid, and vacuum means for creating vacuum..Iaddend..Iadd.33. A vertically disposed apparatus array for the manufacture of effervescent tablets, said apparatus array constituting a tower and comprising in vertically descending order:
- (a) storage hopper means positioned near the top of said tower for the storage of raw materials;
- (b) a mixer-granulator-dryer device having mixing means, means for introducing a granulation agent, means for subjecting said mixer-granulator-dryer device to substantially atmospheric pressure at least during granulation and means for eliminating humidity from said wet granules material under vacuum to obtain dried granules;
- (c) cooling means for lowering the temperature of the dried granules, and
- (d) at least one storage container for dried and cooled granules;
- said apparatus comprising also means for feeding material by gravity from said storage hopper means to said mixer-granulator-dryer device, means for evacuating said dried granules by gravity from said mixer-granulator-dryer device and feeding them by gravity to said cooling means, and means for transferring said granules by gravity from said cooling means to said
storage container or containers..Iaddend..Iadd.34. The apparatus array of claim 33, wherein said mixing means comprise mechanical stirring means with lump-breaking cutters, said means for introducing a granulation agent comprises means for creating a vacuum or spraying system means supplied by a pump; and said mixer-granulator-dryer device includes means for regulating the temperature comprising a double jacket for circulating heat-exchange fluid, and vacuum means for creating vacuum..Iaddend.
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Type: Grant
Filed: Jul 10, 1987
Date of Patent: Oct 10, 1989
Inventor: Jean Bru (Paris 75016)
Primary Examiner: Richard D. Lovering
Law Firm: Ostrolenk, Faber, Gerb & Soffen
Application Number: 7/71,991
International Classification: A61L 904; B01F 312; C06D 510; F26B 1712;
