Encyclopedia of Glass Science, Technology, History, and Culture. Группа авторов

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the current IS‐machines, the loading speed of the gob is often so high that the finish is already formed at the gob‐loading step, which would make the settle‐blow unnecessary for the finish forming. This step is nonetheless maintained in the process to guarantee a constant heat transfer between the glass and the blank, from cycle to cycle, before counter‐blow. During settle‐blow, a vacuum can be applied through cavities in the molds to support the parison and finish forming. Some modern BB IS‐machines work without a funnel. They control the switch between settle‐blow and counter‐blow by a valve in the baffle to exhaust the compressed air that is used for settle‐blow.

      After settle‐blow, the baffle is quickly lifted, the funnel is removed, and the baffle settles again and closes the blank‐mold completely. A counter‐blow is applied from the down side through the formed finish, blowing the glass fully into the mold shape and forming the parison (Figure 3c).

(a–d) Schematic illustration of the blow & blow process, blank-side.

      After the parison has been formed, the baffle is removed (Figure 3d), the mold opens, and the parison is transferred via the invert mechanism to the blow‐side.

      After the container has been released by the blow‐mold, a take‐out grips it by its finish (Figure 4d) and places it over a dead‐plate through which air is blown from below to cool it further. Finally the container is transferred via a pusher onto a conveyor belt.

      3.3 Press & Blow Process

(a–d) Schematic illustration of forming the final container at the blow-side.

      3.4 Narrow‐Neck & Blow Process

(a–d) Schematic illustration of the press & blow process, blank-side.

      Restrictions in usage of the NNPB process are due to the plunger dimensions and finish openings and the corresponding cavities pressed into the parison. The parisons are usually shorter for NNPB than for BB if the same final container shape is to be produced (e.g. a 0.33 l beverage bottle). Another significant difference between NNPB and BB is that the required gob temperature is from around 20 to 50°C higher in NNPB because of difficult pressing conditions. This difference in consequence leads to different thermal requirements during the process in terms of mold‐cooling and reheat‐timing.

      Most forming processes take place at a viscosity of 102–104 Pa⋅s. Hence, for soda‐lime‐silica containers, the glass needs to be cooled from melting and fining at ca. 1500°C and a viscosity of 10 Pa⋅s down to ca. 1050°C and a viscosity of 103 Pa⋅s. This quite demanding task is accomplished in the forehearth. The forehearth is directly connected to the working‐end and ensures the required homogeneity of the glass while bringing it to the desired temperature and viscosity.

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