Ppg Industries, Inc.

Basf Corporation

David A Longhini

Chin Li

Harlan B Johnson

Thomas G Krivak

Bhima R Vijayendran

Bhima R Vijayendrar

Describes flotation deinking of secondary fiber using a froth moderating agent, a composition of the froth moderating agent with flotation deinking chemicals, and reducing the amount of stickies in separated seconday fiber. The froth moderating agent is selected from the group consisting of:

Froth moderating agent for controlling froth and reducing stickies in

Describes flotation deinking of secondary fiber using a froth moderating agent, a composition of the froth moderating agent with flotation deinking chemicals, and reducing the amount of stickies in separated secondary fiber. The froth moderating agent is selected from the group consisting of:

Method for controlling froth and reducing stickies in the flotation

Describes a composition for use in flotation deinking of secondary fiber containing electrostatic ink and/or stickies and optionally conventional impact ink. The composition consists essentially of displector deinking chemicals having an HLB value greater than 10 and non-ionic surfactant deinking additives such as (i) capped aliphatic and alicyclic alkoxylates, e.g., chloride capped C.sub.5 -C.sub.20 alkyl ethoxylates, (ii) alkyl phenol ethoxylates, e.g., octyl phenol ethoxylates, and (iii) a combination of (i) and (ii). Also described is a method for using the composition in a deinking process that includes a flotation step.

Deinking electrostatic waste paper

Precipitated amorphous silica useful for manufacturing microporous battery separators is prepared by establishing an aqueous solution of alkali metal silicate having an alkali metal oxide concentration of (a) from 2.1-2.6 grams per liter and a temperature of from about 179.degree. F. to 186.degree. F., or (b) from 5.6 to 7.2 grams per liter and a temperature of from 190.degree. to 198.degree. F.; adding from (a) 14.5 to 19 times or (b) 2 to 5 times respectively the amount of alkali metal silicate initially present in the initial aqueous solution simultaneously with acidifying agent, e.g., sulfuric acid, to the initial aqueous solution while maintaining the initial alkali metal oxide concentration therein substantially constant; reducing the pH of the resulting slurry to from 8 to 9; ageing the slurry at precipitation temperatures for from 15 to 90 minutes; reducing the pH of the aged slurry to from 3.8 to 4.7 and then recovering, e.g., separating, the silica from its entraining slurry, washing the recovered silica, and drying the washed precipitated silica. Optionally, the recovered and dried silica is milled after drying to produce a product having a median agglomerate particle size of from 6 to 15 micrometers.

Preparation of amorphous, precipitated silica and siliceous

1,2-Dichloroethane is pyrolyzed in a pyrolysis furnace to produce a stream comprising vinyl chloride and 1,2-dichloroethane. The stream is removed from the furnace and introduced to essentially unheated conduit means to establish a stream flowing in the conduit means. Pyrolysis promoter is introduced to the stream in the conduit means and sensible heat of the stream is utilized in the conduit means to pyrolyze further amounts of 1,2-dichloroethane and to increase the yield of vinyl chloride.

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Pittsburgh, PA, United States of America

David A Longhini