* * * INSIGHT * * * A General Discussion of the Steam Sterilization of Freeze-Dryers Ana Bacaoanu, Ph.D. Department of Chemical Engineering, “Gh. Asachi” Technical University of Iasi, Romania
Abstract An analysis of the heat transfer in the stationary large-scale dryers, during saturated steam sterilization, is realized. The inside surfaces temperature of dryers can be significantly different and time dependent. To ensure that all surface temperatures are equal or greater than 121 C, the steam temperature must be higher. Introduction The principal problem in the freeze-drying of pharmaceutical solution is to operate in sterile conditions. In the modern plants, the internal sterilization of equipment is usually made with pressured steam at 121 C. Sterilization is the process of the elimination (by removal or killing) of all microorganisms and the inactivation of viruses present in or on a product. It is an absolute condition and, in practice it is an ideal, which is approached in terms of achieving an acceptable probability of the absence of viable organisms. The practice has shown, however, that this theoretical goal cannot always be achieved, depending of the respective conditions. Consequently, one accepts today, above all for calculation of the required lethality of sterilization process, a contamination probability of 10-6 [1]. In other processes, such as disinfecting or preservation to prevent microbial spoilage, one is prepared to accept lower killing and inactivation rates. For sterilization process used in pharmaceutical and food industries we distinguish between processes employing: moist heat (steam) dry heat microbicidal gases (ethylene oxide, formaldehyde) ionizing radiation germ removal by filtration [2].
Processes employing saturated steam is the most reliable sterilization process, but their results are decisively affected by following factors: the type of microorganisms present and their functional state (vegetative forms or spores); the initial germ count and acceptable final concentration (probability of contamination of 10-6, i.e., sterility by definition, or a reduction in the germ count with a few isolated germs being tolerated in the end of product); the temperature at the coldest point and the treatment time at the lethal temperature. In the following discussion some aspects regarding the sterilization of dryers in the lyophilization process are addressed. Primarily the types of microorganisms found in the equipment govern the choice of the treatment temperatures. The vegetative forms are killed or inactivated in few minutes at 65-100 C; the fungal spores (conidiospores) are killed at 100-105 C; the Clostridium and Bacillus spores cause more severe difficulties and make it necessary to use higher treatment temperatures (121 C) [ 2]. As a rule sterilization of stationary of large-scale dryers, the sterilization is realized with the saturated steam at 121 C. The general procedure for thermal deactivation using condensing steam is: open steam points vent air build up pressure hold collapse steam in a controlled manner [3]. The temperature-time profile employed depends on the selected organism and its susceptibility to infection. Generally, thermal deactivation is designed for the inactivation of Bacillus Stearothermophilus. The entire system has to be brought to the sterilization temperature with special attention given to potential cold spots. The calculated sterilization time leads to desired effect, however, only if the lethal temperature (i.e., 121C) can be achieved at every point in the equipment being treated.
Analysis of the heat transfer processes during sterilization In the pharmaceutical industry one consider the start of sterilization process when a sensor in the drain line reaches 121 C. Is this always true? We are trying to find an answer to this question. To this end, the variations in the local heat transfer during sterilization process have been studied. The analysis of the heat transfer shows that the local conditions in the dryers are different and variable with time. In this situation, we are expecting that the surface temperature is not the same in every point, that is, the temperature in certain regions is lower than desired value (121 C), and the sterilization cannot be completed. The build up pressure and collapse steam takes place in an unsteady state. All local parameters vary with time. The hold stage can be considered as a quasi steady state. Inside of dryer, the heat transfer process during sterilization takes place by condensation of the steam. The condensation is an isothermal process, which supposes that a temperature difference between the wall temperature and steam temperature exists. |
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Heat transfer is linked to the fluid dynamic behavior, and because of the complexity of boundary layer behavior, we are dependent, for the most part, on the experimental data. The subject of convective heat transfer is much more empirical than that of heat conduction, and analytical solutions, for the most part, is limited to problems involving laminar flow. It is important to add that the convective heat transfer incorporates heat conduction in boundary layer. The dryers are insulated, but we cannot consider them an adiabatic system. Because of the temperature gradient, the heat is transferred by convection from steam to wall (a solid surface), then by conduction through metallic wall and insulation, and finally by convection and radiation to surrounding air. If this heat flux exists, then the temperature of the wall is lower than that of the steam. The difference ( Tsat - Tw ) is dependent upon the liquid film thickness. The heat transfer by condensation of vapor (steam) depends of the system (walls) geometry. On the vertical walls, the condensed liquid forms a continuous liquid film on the heat transfer surface. The condensed film thickness, (delta Greek letter) , increases with distance dawn the wall. Consequently, the wall temperature is lower in the regions where the thickness of the of the boundary layer is greater, because of the increase of thermal resistance. On the bottom of the dryers or on the inside horizontal surfaces one would have a liquid film draining under gravity forming a “pool” or stratified layer that flows along the surface. In these regions the thermal resistance is increased and a greater difference ( Tsat - Tw ) occurs, so that the wall temperature will be even lower. Very large dryers which are connected to steel structures for support have, at these points, substantial heat sinks which may need compensating steam to ensure that sterilization temperature is reached. The heat flux is transferred by steam condensation to the interior wall surface of the dryer, by conduction through the wall of the dryer and supports and by free convection and radiation to the surrounding air. The internal area of heat transfer is smaller than that external area, compared with the other regions of dryer. Consequently, the heat flux is greater in the regions of supports (the heat transfer is proportional with area). The internal heat flux, from steam to wall, has the same value as the external flux, from supports to air. It yields that the temperature difference will be larger, so that the wall temperature is lower in these regions, and the sterilization temperature is not reached. The shelves offer a big area of contact with steam, that is a big surface area for the heat transfer. The heat flux is proportional to this. The shelves are constructed from stainless steel having inside a serpentine path for the heat transfer fluid which supply the necessary refrigeration and the energy for sublimation of the ice and desorption of the water during the drying process [5]. During sterilization the shelves are exposed to convective heat transfer on the both surfaces, by the external steam flow. The heat transfer from steam to shelves occurs due to a temperature gradient perpendicular to surfaces that changes with time as heat is transferred into the shelves. The mean temperature of the shelves is different from that of the surface. If the shelves are heated at a uniform rate, then the temperature profile is parabolic. The heat transfer is symmetrical and no heat transfer passes across the centerline (symmetrical axe). The thermal equilibrium could be reached after a very long time, theoretical after an infinite time. In this situation even a very small difference temperature between wall and steam temperature will exist. The heat is transferred by convection from steam to the surfaces of shelves and by conduction inside of them (considering that the fluid is stagnant in the serpentine path). The heat flux is given by [4]:
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The warming of shelves involves conduction heat transfer in the transient state. This means that the temperature of body varies with both time and position of the points of body. The mathematical analysis is very complicated and well beyond the scope of this paper. Information about transient conduction in a thick slab subject to convection on one surface and insulated on the other, or subject to convection on both surfaces are given by G. H. Hewitt [4]. One can obtain the evolution of the temperature on the exterior surface and inside (center) of shelf with time. Two parameters should be calculated to this aim: One parameter is Biot number, which represents the ratio of convection to conduction [4]: |