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Freeze chamber

Figure 7. Configuration of the materials durability test system 1, Zymark robot arm 2, Mettler balance 3, blotting station 4, capping station 5, specimen rack 6, water bath 7, block oven 8, vacuum oven 9, freezing chamber 10, NDT station 11, automated micrometer, and 12, washing station. O, specimen holder. Figure 7. Configuration of the materials durability test system 1, Zymark robot arm 2, Mettler balance 3, blotting station 4, capping station 5, specimen rack 6, water bath 7, block oven 8, vacuum oven 9, freezing chamber 10, NDT station 11, automated micrometer, and 12, washing station. O, specimen holder.
Figure 2.7.1. shows the schema of a process for freezing pellets for freeze drying and Fig. 2.7.2 illustrates the details of the freezing chamber. Such installations are offered under the trade name Cryopel with throughputs between 10 and 250 kg/h. [Pg.132]

Preparation of Hydrazine Sulphate. Perform the experiment in a fume cupboard ). Preliminarily prepare a sodium hypochlorite solution. To do this, spill 100 g of ice (prepared from distilled water in the freezing chamber of a refrigerator) into a 300-ml flask and add a sodium hydroxide solution (dissolve 50 g of sodium hydroxide in 100 ml of water). Put the flask in a bath with ice. Pass chlorine during two hours into the cooled solution. When doing this, see that the temperature does not rise above 5 °C. [Pg.139]

Several design variations are possible for a direct freeze-separation process. The one reported utilizes the evaporation of water directly in an evacuated freeze chamber to form ice crystals and concentrated brine. Separation of ice from brine does not use any mechanical devices, such as centrifuges, but simply a counterflow wash column of ice being moved by applied hydraulic forces. [Pg.94]

When all the wells have been filled, reduce the temperature of the freezing chamber to -20 °C or place the block on dry ice or in a -80 °C freezer (see Note 10). [Pg.108]

As an alternative to nalgene freezing chambers, two styrofoam 15-ml Falcon tube holders may be sandwiched around tubes to provide insulation during slow freezing process. [Pg.176]

Ordinary freeze-drying is carried out in vacuum. Over the years, new developments showed that freeze-drying can be carried out at atmospheric pressure and as well as in a fluidized bed (e.g.. Refs. [102-104]). This has been extended to liquid protein, where protein is sprayed and frozen in a freezing chamber then transported to an FBD for drying... [Pg.178]

The proposed schematic flow diagram is shown in Figure 9.52. It basically consists of a drying or freezing chamber, an internal bag Alter, an internal fluidized bed, a liquid nitrogen cooler, a fan, nozzles, a pump, valves, pipes, etc. [Pg.223]

In freeze-drying, a solution is filled into vials, a special slotted stopper is partially inserted into the neck of the vial (Fig. 3), and trays of filled vials are transferred to the freeze-dryer. The solution is frozen by circulation of a fluid, such as silicone oil, at a temperature in the range of — 35 to about — 45°C through internal channels in the shelf assembly. When the product has solidified sufficiently, the pressure in the freeze-dry chamber is reduced to a pressure less that the vapor pressure of ice at the temperature of the product, and heat is applied to the... [Pg.398]

Mass transfer in freeze-drying refers to the transfer of water vapor from the sublimation front through open channels in the partially dried layer, created by prior sublimation of ice, through the headspace of the vial, past the lyostopper, through the chamber, to the condenser. [Pg.403]

S. L. Nail, The effect of chamber pressure on heat transfer in the freeze drying of parenteral solutions, J. Parenter. Drug Assoc., 34, 358-368 (1980). [Pg.417]

M. J. Pikal, S. Shah, M. L. Roy, and R. Putman, The secondary drying stage of freeze drying drying kinetics as a function of shelf temperature and chamber pressure, Int. J. Pharm., 60, 203-217 (1990). [Pg.417]

Figure 2 The rate of water loss and residual water content during freeze drying. Moxa-lactam disodium formulated with 12% mannitol in aqueous solution at 30% solids 10 mL tubing vials with a solution fill depth of 1 cm. The chamber pressure was 0.05 torr (6.6 Pa). (From Ref. 2.)... Figure 2 The rate of water loss and residual water content during freeze drying. Moxa-lactam disodium formulated with 12% mannitol in aqueous solution at 30% solids 10 mL tubing vials with a solution fill depth of 1 cm. The chamber pressure was 0.05 torr (6.6 Pa). (From Ref. 2.)...
Barriers to heat transfer produce corresponding temperature differences in a freeze-drying system, the actual temperature profile depending upon the rate of sublimation, the chamber pressure, and the container system as well as the characteristics of the freeze dryer employed. An experimental temperature profile is shown in Figure 5 for a system where vials were placed in an aluminum tray with a flat 5 mm thick bottom and a tray lid containing open channels for escape of water vapor. Here, heat transfer is determined by four barriers ... [Pg.628]


See other pages where Freeze chamber is mentioned: [Pg.234]    [Pg.175]    [Pg.179]    [Pg.909]    [Pg.555]    [Pg.169]    [Pg.909]    [Pg.91]    [Pg.357]    [Pg.184]    [Pg.124]    [Pg.895]    [Pg.306]    [Pg.234]    [Pg.175]    [Pg.179]    [Pg.909]    [Pg.555]    [Pg.169]    [Pg.909]    [Pg.91]    [Pg.357]    [Pg.184]    [Pg.124]    [Pg.895]    [Pg.306]    [Pg.62]    [Pg.428]    [Pg.247]    [Pg.24]    [Pg.207]    [Pg.234]    [Pg.266]    [Pg.41]    [Pg.72]    [Pg.190]    [Pg.182]    [Pg.399]    [Pg.403]    [Pg.404]    [Pg.404]    [Pg.622]    [Pg.624]    [Pg.625]    [Pg.630]    [Pg.634]   
See also in sourсe #XX -- [ Pg.265 ]

See also in sourсe #XX -- [ Pg.284 , Pg.286 ]




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