Abstract: An uncoated paperboard for packages composed of one or more layers with a top layer of bleached kraft pulp having a gloss value of 15-50% measured according to Tappi T480, a minimal gloss variation (a coefficient of variation in the wavelength regions 3-30 mm of less than 5%), and a surface roughness (PPS-10) of 2-5 ?mm measured according to ISO 8791-4, wherein the paperboard has a density in the range of 700 to 850 kg/m3 and is hydrophobic from a sizing agent treatment of each layer, is described. A package comprising the paperboard is suitable for co-sterilization of the package and its contents.

Abstract: An uncoated paperboard for packages composed of one or more layers with a top layer of bleached kraft pulp having a gloss value of 15-50% measured according to Tappi T480, a minimal gloss variation (a coefficient of variation in the wavelength regions 3-30 mm of less than 5%), and a surface roughness (PPS-10) of 2-5 mm measured according to ISO 8791-4, wherein the paperboard has a density in the range of 700 to 850 kg/m3 and is hydrophobic from a sizing agent treatment of each layer, is described. A package comprising the paperboard is suitable for co-sterilization of the package and its contents.

Abstract: It is possible to filter a suspension or emulsion in a filter bed of particulate filter medium by allowing the suspension to flow upwards through the filter bed simultaneously as the medium flows downwards through a filtering tank wherein filtration takes place. Filtration thus takes place during counterflow between suspension and filter medium. The supply of suspension takes place in the lower part of the filter bed and the filtered liquid phase is taken away from a zone above the filter bed. The polluted filter medium close to the bottom of the filter tank is taken out for conveyance to a washing apparatus above the filter bed and after washing is returned to the upper side of the filter bed. For providing a filter which has a considerably lower construction height for a given and unchanged volume of the filter medium, the washing apparatus is lowered so that its lower part is at a level below the upper surface of the filter bed.

Abstract: In the particular embodiment of the invention described in the specification, a plate pack for an inclined plate separator has plate support members forming the side walls of the separator in which the separation plates are received in grooves formed by converging tongues. The support members are releasably joined together edge to edge by a bead projecting from one edge of the support member and a groove formed in the adjacent edge of the next supporting member.

Abstract: The representative web presses disclosed in the specification include a press drum and a pair of webs to convey a suspension partly around the press drum and two pressure belt means for applying substantially constant pressure against the outer web in the direction radial to the drum along pressure paths which are spaced so as to be substantially symmetrical with respect to the press drum.

Abstract: Arrays of baffles are disposed in apparatus for distributing a composite liquid to the separation passages of a multi-plate laminar separation apparatus to decelerate the influent composite liquid and repeatedly deflect its direction of flow such that it is uniformly distributed to the separation passages in the apparatus.

Abstract: In the embodiments of the web press disclosed in the specification, a pair of webs carries suspension material partly about a series of press drums of decreasing diameter in a first pressing section. One of the webs carrying the suspension material passes to a second press section where a further web replaces the other of the pair of webs to provide the inner web in a path around a press drum. Increased pressure is applied by a pressure belt to the webs as they pass around the press drum in the second pressing section.