Abstract: The invention relates to injecting ozone through at least one injecting means operating with a pressure drop of at least about 35 psi into a pressurized stream of aqueous solution, allowing the ozone injected stream to travel or flow at a velocity of at least about 7 feet per second for a distance sufficient to dissolve at least about 70% of the ozone injected and mixing the resulting ozonated stream with an aqueous stream solution to be ozonated.

Abstract: Polyvinylaminals, optionally as the formed copolymer with polyvinylhemiaminals and polyvinylacetals are useful as separating agents and are provided by reacting a poly(vinylamine) or a copolymer containing vinyl alcohol and vinylamine units with a monoaldehyde. The aldehyde, such as butyraldehyde, can be introduced into the polymer aminalization as a liquid or gas, generally in a proportion of about 0.02 to 0.5 mol per mol of alcohol and amine units in the polymer chain. These polymers, especially as the cationic salt, perform very well in the flocculation, settling, clarification and dewatering of wastewater.

Abstract: Coal fines and suspended insoluble metals are flocculated from coal mine drainage waters by adding a polymeric tannin-amine compound.

Abstract: A device for precipitating polymers from a liquid by at least one precipitant fluid includes a feed line, a nozzle plate having at least one outlet orifice for a polymer containing fluid with the outlet orifice communicating with the feed line, at least one nozzle for at least one precipitant fluid, the axis of which is arranged approximately perpendicularly to the axis of the outlet orifice, a precipitation chamber positioned on the side of the nozzle plate wherein at least one nozzle for at least one precipitant fluid is located, a discharge line for discharging a mixture which contains the precipitated polymer and a degassing chamber which is connected to the discharge line.

Abstract: A process is disclosed for treating an aqueous waste stream containing a photoresist waste component. Under this process the pH of the waste stream is adjusted in a range from about 4.0 to about 6.0 and an additive is added to the waste stream in a concentration effective to separate a precipitant from the waste solution in the form of a non-sticky residue. The additive is selected from the group consisting of FeCl.sub.3, CuCl.sub.2, NH.sub.4 Cl, AlCl.sub.3, and combinations thereof.

Abstract: A method for oxidizing organic and/or heavy metal contaminants in wastewaters, sludges, or soils containing such contaminants by contacting the wastewaters, sludges, or soils with soybean peroxidase and a peroxide.

Abstract: Metal complexes and especially nickel EDTA is decomposed by adding an oxidizing agent to an aqueous solution containing metal complexes to define an oxidizable aqueous solution. The oxidizable aqueous solution is then exposed to a source of ultraviolet radiation in the range of from 185-300 nanometers for a period of time sufficient to destroy the complex portion of the metal complex. The remaining metal is recovered.

Abstract: Oil spills on natural bodies of water are treated with amine-substituted water swelling clays. The organoclays are added to oil spills in an amount which herds oil into islands of oil separated by surfaces of water containing no oil. The clays can also be added to oil spills in an amount which produces quasisolid, buoyant organoclay/oil flocculate clumps which float in the water and which are amenable to collection from the surface of the water.

Abstract: A process and apparatus is provided for removing color from a wastewater stream. The process includes directing the wastewater stream through at least one UV reactor and simultaneously injecting a hydrogen peroxide charge into the wastewater stream exactly at the UV irradiation zone of the reactor. The apparatus of the subject invention includes a UV reactor having a smooth flow channel for wastewater and a zone for exposing the wastewater to UV irradiation. The reactor further includes tubing for directing hydrogen peroxide into the reactor exactly at the UV irradiation zone, such that the hydrogen peroxide is introduced simultaneously to the wastewater stream and the UV irradiation zone.

Abstract: The present invention describes a novel method and apparatus for treating and/or disinfecting water and/or wastewater wherein the contact vessel is sealed and under greater than atmospheric pressure having a detention time of no more than 5 minutes.

Abstract: A method for efficiently thickening and dewatering a slurry sludge in a short period of time without the necessity of a vast site, which comprises the steps of: stirring a slurry sludge added with a coagulant in a stirring tank to convert the slurry sludge into a floc; supplying the floc and a superantant liquid, which are produced in the stirring tank, onto an inlet side of an inclined endless travelling filter cloth of an endless travelling filter cloth type dewatering unit, which comprises a dewatering tank and the above-mentioned inclined endless travelling filter cloth arranged in the dewatering tank; continuously travelling the thus supplied floc, on the endless travelling filter cloth, toward an exit side thereof; thickening the floc on a portion of the endless travelling filter cloth, which portion is located in the supernatant liquid in the dewatering tank, and dewatering the thus thickened floc on a portion of the endless travelling filter cloth, which portion is located above the surface of the sup

Abstract: A fuel filter for a motor vehicle includes a housing made of a base Nylon 12 material to which are added stainless steel fibers to render the housing electrically conductive while retaining moldability. The electrically conductive housing permits charges generated by the fuel passing through the filtering media to be dissipated to the vehicle body, thereby preventing erosion of the housing and subsequent leaks.

Abstract: Biocide treatment of the water system of a papermaking process comprising the steps of encapsulating the biocide as the core of the capsule in a water suspension, in which the shell is degradable at high water dilution, and introducing the microcapsules into the water stream to undergo dilution release.

Abstract: A process for the flocculation, precipitation, agglomeration or coagulation of substances or microorganisms present in a liquid in a dissolved, colloidally dissolved, suspended or emulsified state and a device for carrying out the process. The respective liquid is exposed to one or several fields of stationary ultrasonic waves, the ultrasonic frequency f being higher than one seventh of a cutoff frequency fo which depends on the kinematic viscosity of the liquid and the effective radius of the particles present in the liquid.The device includes an ultrasonic treatment tank which receives the liquid to be purified and is provided with an ultrasonic transducer radiating the ultrasonic waves to an opposing reflecting surface.

Abstract: Disclosed herein is a process for separation and analysis of free and bound hydrophobic components in whole blood. In this process, whole blood is passed through an internal surface reverse phase material having particles large enough to allow blood cells to pass through. These particles have hydrophobic pores that are small enough to prevent penetration by proteinaceous substances and large enough to allow penetration by free hydrophobic components. Thus, free hydrophobic components are retained by the internal pore surfaces. A non-denaturing solvent is used to wash the whole blood through the material, and a hydrophobic or organic solvent may be separately used to wash the hydrophobic components from the material. This process may be combined with qualitative, quantitative, and selective detection techniques, such as radiolabelling.

Abstract: A water soluble ethylene dichloride ammonia polymer having a molecular weight of from 500 to 10,000 which contains from 5 to 50 mole % of dithiocarbamate salt groups. Also, disclosed is the use of these polymers in removing heavy metals from water.

Abstract: A system and method are disclosed for desalinating sea water. The system includes an energy source such as a laser 13, and a container 19 (partly or wholly transparent) for holding the sea water, the sea water having sodium and chlorine ions and a solvent (H.sub.2 O) with a predetermined dielectric value. The system applies a predetermined amount of energy, in the form of a laser beam 35 through the transparent container 19, to the seawater substantially at a resonance frequency of the solvent, for reducing the dielectric value of the solvent and vibrating the ions, permitting them to combine and precipitate out of the seawater, thereby desalinating the seawater. To increase the effect of the beam 35, the system includes a pair of mirrors 15,17 for reflecting the beam back and forth through the sea water.

Abstract: A process for removing cyanide anions from waste waters using halogen-free ferric salts is disclosed. The process is particularly effective when treatment of cyanide waste waters is done by adding ferric sulfate while adjusting pH of the waste waters with a halogen-free acid, such as sulfuric acid, to a pH ranging from about 3.0 to 5.0.The ferric ferricyanides formed are agglomerated and flocculated using synthetic polymers along with whatever other dispersed or suspended solids may be present in the waste waters, and this dense sludge is separated in a clarifier. Cyanide removal is at least 80%, relative to initial cyanide concentrations, and preferably 90% removal or higher.Cyanide wastes from coke oven off gas scrubbing waters are particularly waste waters amenable to this treatment.

Abstract: Glutaraldehyde is effective in controlling Zebra mussels found in industrial process waters.

Abstract: A process for removing at least a portion of any iron, copper, nickel and chromium ions that are chelated by a alkylenepolyamine polyacetic acid or salt in an aqueous liquid waste. The process comprises the steps of (a) adjusting the pH of the liquid to above about 10; (b) adding sufficient sodium sulfide to react with at least a portion of the copper ions; (c) separating precipitated iron and copper compounds; (d) adding nitric acid to adjust the pH to the range of about 6 to 8; (e) adding sufficient sodium nitrite to the liquid to react with at least a portion of the nickel and chromium present; (f) heating the liquid to above about 575.degree. F. for at least about 15 minutes to facilitate precipitation of nickel and chromium; and (g) separating precipitated solids to leave a non-hazardous filtrate.