Abstract:
A flexible, multi-layer filter for separating solid and liquid wastes. In a preferred embodiment, the filter includes first, second, third, and fourth layers, interconnected by appropriately spaced connectors. The first layer comprises sub-layers of parallel strands, wherein the strands in one sub-layer cross and overlap the strands in the other sub-layer to form a netting. The second layer comprises a fibrous mat, and the third layer comprises a netting like that of the first layer. The fourth layer includes a porous filter cloth. The third layer may be cut to form end and side tabs for retaining the filter inside a conventional waste container. After a semi-solid mixture of waste is poured, dumped, or otherwise placed into the waste container, liquid waste passes through the filter layers under the force of gravity. The liquid waste is channelled through the first layer along the bottom of the waste container. The liquid waste may be discharged from the container by opening a drain, or by slightly-opening a gate in the waste container. The invention is especially effective for extracting liquid waste from semi-solid materials, such as catalysts produced in petroleum refining, industrial process sludges, slurries, sewage matter, and materials collected in storm drains such as grit, rocks, leaves, silt, and dirt.
Abstract:
A portable liquid-solid separator for handling sludge in bulk with an upright vessel having a bed with a drain and surrounding sides. A grate overlays the interior of the vessel, bed and sides. A filter overlays the grate, extending up the sides and overlapping the side grate. The separator is filled with a sludge which is then separated by gravity filtration and the wicking action of the filter. Liquid is drained out the bottom of the vessel and the solids are transported within the vessel. In a preferred embodiment, the vessel is a bath tub style trailer with dumping capabilities.
Abstract:
A method of spreading a pulp for the purpose of drying it naturally, the pulp having a solid fraction which has a d.sub.80 of less than 100 microns. This method comprises the following steps:(a) adjusting the level of solids of the pulp to between 2 and 25%;(b) adding a flocculating agent to the pulp and mixing it with same, the amount of said flocculating agent being between two-thirds of 98% of the optimum required fo the flocculation of said pulp; and(c) spreading the mixture of pulp and flocculating agent, in the open air, in a bed the sides of which are permeable, and the bottom of which has a slope of less than 5 meters per 1000 meters, said spreading taking place 1 to 20 minutes after the adding are mixing of the flocculating agent.
Abstract:
A saturated layer stormwater filtering system with down-flow layered multimedia filters is disclosed. The filtering system may include an upflow pretreatment chamber and a subsequent filtration chamber. It also includes a snorkel pipe as an adjustable head control or internal baffles. The system incorporates gravity powered partially saturated stormwater media filters to harness the potential energy of stormwater from downspouts and pumped flows from stormwater catchments to drive the polluted stormwater in a hydraulically controlled fashion by gravity through a series of filter media layers.
Abstract:
PCT No. PCT/SE94/00020 Sec. 371 Date Aug. 14, 1995 Sec. 102(e) Date Aug. 14, 1995 PCT Filed Jan. 14, 1994 PCT Pub. No. WO94/19533 PCT Pub. Date Sep. 1, 1994The present invention relates to a straining device in association with the displacement of liquid through a pulp bed preferably in connection with the withdrawal of cooking liquid in a continuous digester (1) for producing chemical pulp, which straining device (2) is preferably rectangular and comprises a number of strainer-bars (3), arranged in parallel, which have been fixed to at least two rod elements (4, 5), which are placed transversely in relation to the lengthwise extension of the bar-strainers, the said rod elements (4, 5) being made of metal, preferably stainless steel, and having a strength value RP 0.2 at 100 DEG C. which exceeds 200 MPA, preferably 300 MPA, and more preferably 350 MPA, and the width of the said rod element (4) being less than 800 mm, preferably 650 mm, and more preferably 550 mm, so that the straining device becomes self-supporting.