Abstract:
A process of dissolving solid waste material in packed beds comprises the addition to the packed bed of a solvent for the solid waste and a material which releases a gas on contact with the solvent which forms channels in the packed bed allowing more rapid access of the solvent to the bed.
Abstract:
The process for separating off rare metal catalysts used in the preparation of ether-carboxylic acids by catalytic oxidation with a suspended catalyst comprises carrying out a crossflow filtration and pretreating the filter elements used with a medium which is not solid under the treatment conditions and is composed of one or more carboxylic acids.
Abstract:
A system for filtering solid-containing plating waste comprises a reusable filter media belt that travels in a continuous loop between a filter tray, where filtration takes place, and a multi-compartmented cleaning tank where the belt is cleaned for reuse. Each compartment in the tank is substantially closed at its lower end, and open at its upper end. The belt travels in and out of each of the tank compartments in sequence, being subjected to a liquid cleaning treatment in each by contacting sprays and/or bath immersion before being returned to the filter tray for reuse. A wringer is provided at the top of each compartment through which the belt passes before proceeding to the next compartment in order to isolate the treatment liquids from each other.
Abstract:
There is provided an improvement in a waste effluent filter of the type including a tank, a generally flat fine mesh screen over the lower portion of the tank to define an underdrain cavity below the screen and a filter bed of particulate material having an upper surface and a lower general surface adjacent the underdrain cavity. The particle size of the particulate material being greater than the size of the apertures in the fine mesh screen. The filter improvement includes a jet creating grid for creating a plurality of upwardly directed hydraulic jets evenly distributed throughout the filter bed during the filtering of the effluent through the bed wherein the jet creating grid includes a plurality of nozzles in the bed itself substantially below the upper surface of the bed and above the fine mesh screen a selected distance to retain the lower layer of the bed undisturbed. As a further improvement a plurality of horizontal liquid jets are created as a network over the upper surface of the sand bed to scour the media surface during filtering. A further improvement in the filter is the creation of a plurality of hydraulic cleaning jets usable during backwashing along with a vertical flushing action through the screen from the underdrain cavity. Yet a further improvement in the filter is the provision of a chemical cleaning feature utilizing two separate and distinct chemicals injected into the bed for cleaning the filter bed. Preferably, the chemical injection uses the two sets of vertically displaced jets.
Abstract:
This application is directed to the regeneration of fixed bed granular media filters used for the clarification of liquids, after said filters have become unsuitable or inefficient due to the occlusion of oily substances. One such regeneration method comprises the steps of: backwashing the filter, draining the filter, contacting the filter with an aqueous alkali solution composed of sodium hydroxide dissolved in demineralized water, said solution having a pH value of about 10.5 or greater, at a temperature ranging from about ambient to about 200.degree. F, for a time sufficient to regenerate the filter, and backwashing the filter. Generally, the alkali solution comprises about 0.1 to about 50 weight percent aqueous sodium hydroxide and the contacting is conducted for a period of about 0.1 to about 10 hours.
Abstract:
A process is described for recovering calcium hypochlorite values from the filter media employed in the filtration of calcium hypochlorite slurries. Deposits of Ca(OCl).sub.2 along with insoluble materials adhering to the filter media are washed with an aqueous solution of calcium hypochlorite to form a slurry of calcium hypochlorite solids. Water is used to wash the filter media to dissolve any remaining Ca(OCl).sub.2 and form a solution of calcium hypochlorite. The slurry and solution are then admixed to provide a solution of calcium hypochlorite whose concentration is controlled within the range of from about 45 to about 215 grams per liter of Ca(OCl).sub.2. This solution is employed in the production of calcium hypochlorite and is recycled to the washing step.
Abstract:
Filtering solids from waste water liquids and cleaning, degreasing and restoring the filtering media through the use of cleaning compounds forced up through the filtering substances.
Abstract:
1,013,069. Filters for liquids; ion-exchange. INTERNATIONAL ANALYZER S.A. April 26, 1962 [May 29, 1961], No. 16010/62. Headings B1D and B1J. During upflow of liquid to be filtered or treated, or of regenerating liquid, the free space 7, Fig. 1, above the bed 2, is eliminated by introduction of a fluid at 8, Fig. 2, to the region 5 between the outer cylindrical wall 1 and a resilient cylindrical wall 6, to prevent channelling of the bed. During upflow rinsing, the free space may be partially eliminated by the same means. A cylindrical resilient wall may be arranged within the bed along the axis to provide a central expandible region, Fig. 3 (not shown). The pervious wall 4 above the bed may be replaced by a layer of coarse granules of lower specific gravity than the bed, Fig. 5 (not shown).