M.c. Gill Corporation

John Zink Company, LLC

Koch Engineering Company, Inc.

Other

Mcgill Environmental Systems, Inc.

Eugene C McGill

Robert L Rawlings

Robert D Reed

Ronald D Bell

William C Gibson

James C McGill

Lee R Massey

David W Schmitt

Gerald W Scott

Kevin W McQuigg

John W Schindeler, Jr

Bob R Cartwright

Disposal of land filled-produced leachate, gas and condensate, comprising combusting a first portion of a land filled-produced gas to produce hot flue gas, contacting the landfill-produced leachate and condensate with a portion of the hot flue gas to vaporize all of the leachate and condensate liquids to form a composite gas stream, and combusting the composite gas stream to convert any noxious components remaining therein to non-polluting compounds. Further, solids entrained in the composite gas stream can be separated from the composite gas stream. Following combustion of the composite gas stream, only non-polluting compounds are discharged to the atmosphere.

Landfill leachate, gas and condensate disposal system

A multiple purpose burner process and apparatus in which a burner assembly having a burner member defining a burner throat bore extending therethrough and forming an ignition zone and at least one mixing zone in the burner throat bore, the total combustion air passing through the burner throat bore. A minor portion of fuel gas as ignition fuel produces a continuous ignition flame in the ignition zone, and plural meter channels extending through the burner member communicate with the mixing zone to pass an admixture of a diluent gas with the remainder portion of the fuel, as a primary fuel stream, to the mixing zone for forming with the remaining combustion air a primary fuel/diluent/combustion air mixture, and the primary fuel/diluent/combustion air mixture is ignited by the ignition flame in the mixing zone. Diluents can be internally recirculating flue gas or can be from an external source, and the flame envelope achieved by the burner assembly can be variously shaped for an industrial combustion application as required.

Multiple purpose burner process and apparatus

A process for disposing of a waste chemical stream containing materials which can produce objectionable combustion products, such as NO.sub.x, free bromine, carbon, particulates or ash, the process comprising the steps of passing the waste chemical stream to an oxidizing first zone where burning occurs in stoichiometric oxygen excess above about 2000.degree. F.; then to a reducing second zone where reaction occurs in stoichiometric reduction at a temperature of above about 2000.degree. F.; and then to an oxidizing third zone to oxidize the combustibles at temperatures of between about 1400.degree. F. and 2000.degree. F. The process provides high efficiency destruction of waste compounds, whether solid, liquid or gaseous, in a substantially NO.sub.x free manner. In the case of brominated compounds, the process generates HBr which is readily scrubbed.

Three stage combustion apparatus

A process for the thermal destruction of waste materials of unknown volatility disposed within a container, the process comprising the steps of (a) placing the open container in a combustion chamber of a pyrolysis furnace; (b) providing the pyrolysis furnace with a reducing atmosphere and raising the temperature in the pyrolysis furnace to remove volatile components of the material until a preselected temperature is reached; (c) maintaining the temperature in the pyrolysis furnace while controllably adding air until all the combustible materials are pyrolyzed; (d) continuing to add air during a final oxidation period to achieve combustion of all nonvolatile combustible materials; and (e) processing all volatilized materials in a secondary combustor fluidly communicating with the pyrolysis furnace.

Thermal destruction system for toxic substances

An improved smoke suppressant apparatus for flare gas combination comprising a flare housing and a liner cylinder member coaxially disposed therewithin, an annular orifice channel formed between the liner cylinder and the flare housing. A first flare conduit is in fluid communication with the orifice channel and a first flare gas portion passing through the flare conduit is discharged from the orifice channel at the upper end of the flare housing as a perimeter zone discharge configured as a relatively thin cylindrical layer of flare gas. A second flare conduit may be provided in fluid communication with the inner core of the liner cylinder to discharge a second flare gas portion therethrough as an inner zone discharge, and a liquid seal is provided to permit flare gas to pass via the second flare conduit only when the pressure of the inlet flare gas exceeds a predetermined value. A fluid injected assembly is disposed within the upper end portion of the liner cylinder member for discharging a pressurized fluid into the perimeter zone discharge. A second fluid injector assembly may also be disposed around the upper end portion of the flare housing for discharging a pressurized fluid into the perimeter zone discharge.

Smoke suppressant apparatus for flare gas combustion

An improved purging process in which purge gas is flowed through a flare system at a sufficient flow rate to minimize or at least acceptably control the rate of back flow of air migration into the exit port of the system. The flow of purge gas is periodically terminated (or reduced) for a predetermined interval of time during which air begins to migrate into the flare system. During this purge gas cessation interval, the flow rate of the flare gas is sensed, and depending upon predetermined flow rate ranges for the flare gas, the purge gas cessation is continued during the cessation interval or a partial purge gas flow is commenced to assure that the total gas flow rate in the system is maintained above a predetermined flow rate. In any event, once the cessation interval of time has lapsed, the full purge gas flow is re-established to assure that air migration is cleared from the system.

Purging process

An improved purging process in which purge gas is flowed through a flare system at a sufficient flow rate to minimize or at least acceptably control the rate of back flow of air migration into the exit port of the system. The purge gas is periodically terminated for a predetermined interval of time during which air begins to migrate into the flare system. Before this admittance of air can result in a hazardous condition within the system, the purge gas flow is re-established to sweep the air back out of the system.

An improved flare gas combustion apparatus comprising a plurality of linear burners connected to plural flare gas conduits, each burner having an elongate tubular member with a plurality of aligned apertures and one of the flare gas conduits connected in fluid communication with the tubular members. A first flare gas conduit is maintained open during operation and the remaining flare gas conduits are selectively and sequentially opened in response to flow indicating devices disposed in a connected flare gas header so that the continuously open flare gas conduit is joined in sequence by the other flare gas conduits as predetermined flow rate values are reached in the flare gas header. For safety purposes a pressure indicating device disposed in the flare gas header is provided to simultaneously open all of the flare gas conduits for flare gas discharge to all of the linear burners when the pressure in the flare gas header reaches a predetermined value.

Linear combustion apparatus for atmospheric burning of flare gases

A flare gas combustion apparatus comprising a flare housing and a liner cylinder member coaxially disposed therewithin, an annular orifice channel formed between the liner cylinder and the flare housing. A first flare conduit is in fluid communication with the orifice channel and a first flare gas portion passing through the flare conduit is discharged from the orifice channel at the upper end of the flare housing as a perimeter zone discharge configured as a relatively thin cylindrical layer of flare gas. A second flare conduit may be provided in fluid communication with the inner core of the liner cylinder to discharge a second flare gas portion therethrough as an inner zone discharge, and a liquid seal is provided to permit flare gas to pass via the second flare conduit only when the pressure of the inlet flare gas exceeds a predetermined value.

Flare gas combustion apparatus

An improved process for disposal of chemically bound nitrogen in industrial waste streams is provided wherein a effluent stream containing chemically bound nitrogen, such as ammonia stream, is contacted with an effective amount of oxygen containing gas and a stoichiometric excess of a hydrocarbon, based on the total amount of available oxygen, at a temperature greater than about 2000.degree. F. or less than 3000.degree. F., to provide a combustion effluent. The combustion effluent is thereafter contacted with an effective amount of a gaseous stream containing less oxygen than that which supports flame propagation at a temperature in the range of from about 1600.degree. F. to about 1800.degree. F., to substantially oxidize all combustibles present in the combustion effluent and provide an oxidation effluent substantially free of oxides of nitrogen (NO.sub.x) and combustibles. The oxidation effluent may be cooled in heat exchange equipment to recover energy, recycled to support the combustion and/or the oxidation of the combustibles, or vented to the atmosphere.

Process of conversion for disposal of chemically bound nitrogen in

An improved process for reducing the concentration of oxides of nitrogen (NO.sub.x) in a waste stream is provided wherein an effluent stream containing oxides of nitrogen (NO.sub.x) is burned at a temperature greater than about 2000.degree. F. and less than about 3000.degree. F. with an effective amount of an oxygen containing gas and a stoichiometric excess of a hydrocarbon, based on the total amount of available oxygen, to provide a combustion effluent. The combustion effluent is thereafter contacted, at a temperature in the range of from about 1600.degree. F. to about 1800.degree. F., with an effective amount of a gaseous stream containing less than 21 volume percent oxygen to substantially oxidize all combustibles present in the combustion effluent and provide an oxidation effluent substantially free of oxides or nitrogen (NO.sub.x) and combustibles. The oxidation efluent may be cooled in heat exchange equipment to recover energy, recycled to support the combustion and/or the oxidation of the combustibles, or vented to the atmosphere.

Process for reduction of oxides of nitrogen

An improved, self-supporting incinerator having a combustion chamber for burning sulfur containing compounds therein and adapted to eliminate plume formation resulting from the combustion of such compounds. The incinerator includes a vertically disposed housing and a vertically disposed elongated stack concentrically disposed in the housing such that a portion of the stack extends a distance from the housing. The portion of the stack extending above the housing is further provided with an expandable shield formed of a plurality of members, the expandable shield adapted to expand independently to the expansion of the stack.

Self-supporting incinerator and expandable shield therefor

A method and apparatus for burning fuels with air, with reduced production of NOx, involves the premixing of water vapor with the fuel prior to the burning operation. Because of the low retention of water vapor at low temperatures, means are provided for preheating the fuel and spraying water into the fuel so that water vapor will be taken up by the heated fuel in sufficient quantity to provide the desired results. Various embodiments of apparatus are illustrated.

Fuel-water vapor premix for low NOx burning

A method and apparatus of combusting an acid gas (H.sub.2 S) stream and a second stream containing an organic sulfur compound which may be contaminated with ammonia, and/or hydrocarbons, either liquid or gaseous, to create SO.sub.2 and H.sub.2 S for ultimate recovery of sulfur.

Process and apparatus for burning hydrogen sulfide and other combustible

This invention describes a furnace system for the reduction of nitrogen oxide containing gases which utilizes a two-chambered refractory lined furnace. Fuel gas and stoichiometric air is introduced into the first chamber to provide an ambient temperature sufficient for the reaction of steam and hydrocarbon gases which are introduced into the first chamber to provide a reducing atmosphere. The nitrogen oxide (NO.sub.x) containing gases are also introduced into the first chamber where the NO.sub.x is reduced. The gases then pass into the second chamber where they are rapidly cooled to a temperature below that at which there is thermo-regeneration of nitrogen oxides. Additional air is supplied to the second chamber for the combustion of combustible gases remaining therein after reduction, care being taken that the temperature never rises above the temperature at which there is substantial regeneration of nitrogen oxides.

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Skiatook, OK, United States of America

Eugene C McGill