Abitibi-price, Inc.

Other

General Atomics, Inc.

3500764 Canada Inc.

Abitibi Consolidated Inc.

Philip Whiting

Kevin William Downey

Stanley L Koutz

Luke David Bond

David A Hazlebeck

Anthony Hassan Mehta

Charles Cheslay Mills

Arnold E Willoughby

Martin G Fairbank

Adele M Rhodes

Fraser McLellan

Hollis D MacEwen

Luke D Bond

Charles Chesley Mills

David Alan Hazlebeck

Charles C Mills

A method for oxidizing organic material in an aqueous stream containing one or more inorganic salts, inorganic salt precursors or mixtures thereof comprises oxidizing the organic material in a reactor at a temperature at least equal to the critical temperature of the aqueous stream so as to form a single homogeneous fluid phase and at a pressure sufficiently high to solubilize the inorganic salts in the single homogeneous phase.

Method for the critical water oxidation of organic compounds

A supercritical water oxidation reactor is alternately supplied with a feed stream and a flushing stream. The feed stream contains organic and inorganic materials. The organic materials are oxidized under supercritical conditions in the reactor and the inorganic materials precipitate out of solution under the same conditions. The flushing stream is a solution in which the inorganic material is soluble. More than one supercritical water oxidation reactor may be connected so that the feed stream is alternately supplied to each reactor. During the period when the feed stream is being supplied to a reactor the effluent from the reactor is cooled to a temperature at which inorganic precipitates are soluble and is then supplied as a flushing stream to one or more of the remaining connected supercritical water oxidation reactors.

Method and apparatus to remove inorganic scale from a supercritical

A supercritical water oxidation reactor is described having first and second reaction zones connected in series and through which an aqueous feed stream to be oxidized can be passed in either direction. A self-contained heat exchange fluid system allows supercritical and subcritical temperatures to be maintained in either reaction zone. When supercritical water oxidation is occuring in one reaction zone the effluent is being cooled to a subcritical temperature and used to flush the second reaction zone to remove inorganic scale.

Reversible flow supercritical reactor and method for operating same

Apparatus to remove inorganic scale from a supercritical water oxidation

A supercritical water oxidation reactor is described having first and second reaction zones connnected in series and through which an aqueous feed stream to be oxidized can be passed in either direction. A self-contained heat exchange fluid system allows supercritical and subcritical temperatures to be maintained in either reaction zone. When supercritical water oxidation is occuring in one reaction zone the effluent is being cooled to a subcritical temperature and used to flush the second reaction zone to remove inorganic scale.

A method for oxidizing organic material in an aqueous stream containing one or more inorganic salts, inorganic salt precursors or mixtures thereof, comprising oxidizing said organic material under supercritical conditions in the presence of an oxidant and a mobile surface of particles to which inorganic salts insoluble under the reaction conditions can adhere.

Supercritical water oxidation of organics using a mobile surface

Method to remove inorganic scale from a supercritical water oxidation

A process is provided for the bleaching of wood pulp with hydrogen or sodium peroxide. The process includes the steps of adding to a wood pulp a bleach liquor having an effective amount of hydrogen or sodium peroxide bleaching agent and, by weight of the diluted wood pulp, 0.5 to 6% sodium hydroxide, 0 to 5% sodium silicate, 0 to 1%, preferably 0.02 to 0.05%, magnesium sulphate, and a chelating agent in an amount sufficient to sequester heavy metal ions in the pulp, to produce a pulp consistency of 1 to 16% at a temperature in the range of the bleach liquor freezing point to 25.degree. C., uniformly mixing the bleach liquor with the wood pulp, and immediately thickening the diluted wood pulp to a consistency in the range of 20 to 70% for bleaching of the thickened wood pulp. The wood pulp can be subjected to a preliminary treatment by the addition of a chelating agent in an amount sufficient to sequester chelatable heavy metals including manganese at a pulp consistency of 1 to 10%, and dewatering said pulp to a consistency of 20 to 70% to remove the sequestered manganese to less than 10 ppm.

High consistency peroxide bleaching

Growing community of inventors

Milton, Canada

Philip Whiting