Abstract: A method and apparatus for reducing the concentration of haloorganic compounds in water-contaminated with haloorganic compounds is disclosed. The haloorganic compounds are extracted from the water and concentrated into certain water immiscible alkane hydrocarbon solvent. The solvent is separated from the water, is regenerated by ultraviolet radiation to degrade the haloorganics, and is recirculated to contact additional contaminated water. After extraction the water separated from the solvent may be subjected to conventional drinking water treatment, or passed to groundwater.

Abstract: The invention provides a process for the preparation of 4-fluorophenols of formula ##STR1## wherein n is 0 to 3, each R independently represents a halogen atom or an alkyl, alkoxy, cyano or optionally substituted amino group and Z represents a hydrogen or halogen atom or a cyano group characterized by reacting a fluorohalocyclohexadienone of formula ##STR2## wherein X represents a halogen atom, with a compound of formula A-Z, wherein Z is as defined above and A represents a hydrogen or alkali metal atom, provided that when both A and Z are hydrogen, the reaction is carried out in the additional presence of a Group VIII metal hydrogenation catalyst, and 4-fluorophenols of formula I per se wherein Z is a CN group.

Abstract: A system employing wind-driven venting for reducing the volatile organics content of soil contaminated by leakage or accidental spill of volatile organics such as petroleum hydrocarbons is disclosed.

Abstract: Burner (1) for a gaseous fuel comprising a distributing zone (2) surrounded by an outer wall (4) of a porous medium, an air supply tube (9) debouching in the distributing zone (2), a fuel supply tube (12), and a mixing head (13) arranged in the air supply tube (9), which mixing head (13) comprises a box (15) in which the fuel supply tube (12) debouches and open-ended mixing tubes (23 and 24), which extend through the box (15), wherein the part of the wall of a mixing tube (24 or 25) located in the box (15) is provided with openings (29).

Abstract: In a process for carrying out a chemical equilibrium reaction by introducing gaseous starting compounds in a reaction zone containing a fixed bed of coarse catalyst particles having interstices between them, fine particles adsorbing substantially all of the product compounds are passed downwardly through the interstices and subsequently withdrawn from the reaction zone.

Abstract: A process for the production of epichlorohydrin is disclosed which comprises reacting allyl chloride, chlorine and water to form an intermediate, then rapid conversion and separation of epichlorohydrin product; the epichlorohydrin-depleted reaction mixture is cooled and subjected to electrodialysis then reverse osmosis to concentrate and remove deleterious by-products, and at least a substantial portion of the resultant permeate is recycled to the reaction zone, thereby enabling reduced operating costs and/or improved yield.

Abstract: A continuous process for the production of dichlorohydrin by the reaction of allyl chloride, water and chlorine having substantially lower energy requirements than conventional processes, wherein the reaction mixture is subjected to reverse osmosis to concentrate the dichlorohydrin and to provide a permeate stream substantially free of dichlorohydrin, which permeate stream is recycled to the reaction.

Abstract: The level of impurities such as glycerol-based acetals and/or ketals in glycerine, particularly glycerol-dimethylketal, is reduced by extraction of the glycerine with supercritical or near critical carbon dioxide.

Abstract: A continuous process for the production of dichlorohydrin by the reaction of chlorine, water and allyl chloride, having reduced water consumption wherein the dichlorohydrin formed is extracted into an inert organic solvent and the remaining aqueous reaction product is subjected to reverse osmosis, and at least a portion of the resulting permeate is recycled to the reaction.

Abstract: Process for the co-production of carboxylic acids of the general formula R.sup.1 --COOH and R.sup.2 --COOH and carboxylic acid esters of the general formula R.sup.1 --COOCH.sub.2 R.sup.2 and R.sup.2 --COOCH.sub.2 R.sup.1 from carboxylic acid esters of the general formula R.sup.1 --COOR.sup.2 and/or ethers of the general formula R.sup.3 OR.sup.4 (R.sup.1, R.sup.2, R.sup.3, R.sup.4 representing (substituted) alkyl or (substituted) aryl, alkaryl or aralkyl, R.sup.1 also representing H), carbon monoxide and hydrogen at elevated temperature and pressure in the presence of a ruthenium compound, a further Group VIII metal compound, and a compound R.sup.5 Hal or R.sup.5 COHal where R.sup.5 has one of the meanings given for R.sup.2 and Hal is iodine or bromine, the reaction mixture being substantially free from other transistion metal or Group II metal iodides or bromides, and containing a trivalent nitrogen compound containing a group ##STR1## (X=O or S), such as an amide, a carbamate, a urea or a derivative thereof.

Abstract: The invention provides a process for the preparation of 4,4-disubstituted cyclohexadienones of which at least one of the substituents is fluorine, which comprises reacting a compound of formula ##STR1## wheren X represents a hydrogen or halogen atom or an alkyl group, each R independently represents a halogen atom or an alkyl, alkoxy, or cyano or optionally substituted amino group, Z represents a hydrogen atom or an alkyl, acyl or aryloxycarbonyl group, and n is 0 to 4, with hydrogen fluoride and a Pb(IV) compound, in the presence of a compound which acts as a base towards HF.

Abstract: A continuous process for the production of dichlorohydrin by the reaction of allyl chloride, water and chlorine enabling several options for improving yields, lowering operating costs and having reduced effluent treating requirements which multi-stage reaction zone process employs electrodialysis and post reaction reverse osmosis, with integrated recycled streams therebetween.

Abstract: A continuous process for the production of dichlorohydrin by the reaction of allyl chloride, water and chlorine in a reaction zone comprising a first reaction stage, a final reaction stage and optionally at least one intermediate reaction stage, where the reaction mixture from at least one reaction stage is electrodialyzed in at least one electrodialysis zone to remove ions formed during the reaction, whereas at least a portion of the reaction product from said final reaction stage is passed to the concentrate inlet of said at least one electrodialysis zone, and withdrawing an ion-containing reaction product concentrate stream from said electrodialysis zone, whereby any dichlorohydrin which passes into the concentrate stream in said at least one electrodialysis zone may be recovered.

Abstract: A process for the multi-stage condensation of an overhead fraction is disclosed. The process facilitates optimal response to changes in distillation column controls wherein column top reflux condensation is preferentially returned to said distillation column, but auxiliary surge capacity is obtained by connection to a first accumulator section of an accumulating zone, which surge capacity is supplemented by one-way flow of liquid from a cooler, second section in said accumulation zone.

Abstract: Process for the co-production of carboxylic acids of the general formula R.sup.1 --COOH and R.sup.2 --COOH and carboxylic acid esters of the general formula R.sup.1 --COOCH.sub.2 R.sup.2 and R.sup.2 --COOCH.sub.2 R.sup.1 from carboxylic acid esters of the general formula R.sup.1 --COOR.sup.2 and/or ethers of the general formula R.sup.3 OR.sup.4 (R.sup.1, R.sup.2, R.sup.3, R.sup.4 representing (substituted) alkyl or (substituted) aryl, alkaryl or aralkyl, R.sup.1 also representing H), carbon monoxide and hydrogen at elevated temperature and pressure in the presence of a ruthenium compound, a further Group VIII metal compound, a phosphine oxide and a compound R.sup.5 Hal or R.sup.5 COHal where R.sup.5 has one of the meanings given for R.sup.2 and Hal is iodine or bromine, the reaction mixture being substantially free from other transition metal or Group II metal iodides or bromides, and containing a tertiary phosphine oxide.

Abstract: A continuous process for the production of dichlorohydrin by the reaction of allyl chloride, water and chlorine in a reaction zone comprising a plurality of reaction stages, wherein the aqueous reaction product from each stage, except the final stage is electrodialyzed and the diluate is passed to a subsequent reaction stage.

Abstract: In a multistage reaction system for the preparation of dichlorohydrin by the reaction of allyl chloride, water and chlorine and where the hydrochloric acid by-product is removed by electrodialysis, increased efficiency for acid removal by electrodialysis results from at least partial neutralization of the acid in the electrodialysis concentrate receiving stream, enabling the use of smaller electrodialysis membrane area and or lower energy consumption.

Abstract: A continuous process for the production of dichlorohydrin by the reaction of chlorine, water and allyl chloride, having reduced water consumption wherein the dichlorohydrin formed is extracted into an inert organic solvent and the remaining aqueous reaction product is electrodialyzed, and at least a portion of the resulting diluate is recycled to the reaction.

Abstract: A distillation method and apparatus which comprises (a) a distillation zone adapted for the countercurrent contact of liquid and vapor, (b) a reboiler feed liquid compartment (c) means for directing distillation zone liquid into the reboiler liquid feed compartment, (d) a thermosyphon reboiler for partial vaporization of liquid thereto to produce reboiled vapor and liquid flows, (e) a conduit for the flow of liquid from the reboiler liquid feed compartment to the reboiler, (f) a reboiler return liquid compartment, (g) a conduit for the flow of reboiled liquid from the reboiler to the reboiler return compartment, (h) a conduit for the flow of reboiled vapor from the reboiler to the distillation zone, (i) means for communication of liquid by gravity flow between the reboiler feed compartment and the reboiler return compartment to provide substantially equal liquid levels in the two reservoirs, (j) a distillation zone liquid product compartment, (k) means for overflow of liquid from the reboiler return compartme

Abstract: A process for the preparation of alpha-haloalkylesters, wherein an acylhalide having the general formula ##STR1## in which R.sup.1 represents a substituted or unsubstituted hydrocarbyl group and Hal represents chlorine or bromine is contacted with hydrogen at elevated temperature and pressure in the presence of a catalytic system comprising at least one Group VIII element.