Abstract: A system is provided with a segmented solid feed pump having a plurality of pump segments coupled together in series along a path. Each pump segment of the plurality of pump segments has opposite side walls disposed about a holding receptacle. The segmented solid feed pump also includes a first transport section disposed along a first portion of the path, wherein the first transport section includes a first inlet duct, a first outlet duct, and first opposite guides extending between the first inlet duct and the first outlet duct.

Abstract: A system is provided with a segmented solid feed pump having a plurality of pump segments coupled together in series along a path. Each pump segment of the plurality of pump segments has opposite side walls disposed about a holding receptacle. The segmented solid feed pump also includes a first transport section disposed along a first portion of the path, wherein the first transport section includes a first inlet duct, a first outlet duct, and first opposite guides extending between the first inlet duct and the first outlet duct.

Abstract: A system is provided with a segmented solid feed pump having a plurality of pump segments disposed along a closed-loop path. The plurality of pump segments are coupled together in series along the closed-loop path, and the plurality of pump segments move along the closed-loop path. Furthermore, each pump segment includes a holding receptacle.

Abstract: A system is provided with a segmented solid feed pump having a plurality of pump segments disposed along a closed-loop path. The plurality of pump segments are coupled together in series along the closed-loop path, and the plurality of pump segments move along the closed-loop path. Furthermore, each pump segment includes a holding receptacle.

Abstract: The invention is a thermocouple installation wherein the thermocouple measures the temperature in a gasification reactor. The thermocouple is installed through the wall of a gasification reactor such that the measuring element is behind a continuous layer of refractory hot face brick. The thermocouple assembly is mounted in a opening made through the gasifier wall, the insulating brick, and optionally a portion of the way through the hotface brick.

Abstract: An integrated liquefaction and gasification process converts bulk particulate halogen-containing waste plastic materials with minimal particle size reduction into a synthesis gas and a non-leachable, vitreous environmentally nontoxic slag. The process involves melting and cracking bulk particulate halogen-containing waste plastic material to form a lower boiling point, lower molecular weight halogen-containing oil composition which then undergoes partial oxidation in a quench gasifier to produce a synthesis gas. Any hazardous gases, liquids or solids that are produced can be purified into commercially valuable byproducts or recycled to the process, which does not release hazardous materials to the environment.

Abstract: Reactor for gasifying a carbonaceous fuel to produce a usable gas, and comprising an insulated outer shell. A reaction chamber within the shell receives a fuel mixture from an injection burner. The products or effluent of gasification include hot produced gases which are passed through a constricted throat to be cooled in a liquid bath. A dip tube, which guides the hot effluent into the bath, is provided with a stream of coolant from a quench ring. The latter is supported below the reaction chamber and is provided with a thermal barrier along its surface that is exposed to the hot produced gas. The barrier will reduce thermal stress in the quench ring and reduce drain of heat from the gasifier throat, thus avoiding premature chilling of the slag component.

Abstract: An assembly of a quench liquid distribution ring and dip-tube with or without a draft tube for use in a hot effluent gas quench cooling zone containing a pool of quench liquid in the bottom in combination with a vertical cylindrical free-flow refractory lined reaction zone of a partial oxidation gas generator. The hot effluent gas from the reaction zone passes through a bottom central discharge outlet and passage and then through a coaxial vertical dip-tube that extends down into a pool of quench liquid. A quench liquid distribution ring that includes an annular rectangular shaped bottom feed quench liquid distribution channel, surrounds the outside diameter of the dip-tube at its upstream end. A quench ring face and cover is provided that comprises a vertical cylindrical shaped leg portion and a top horizontal flat ring plate portion that extends perpendicularly outward from the upstream end of the leg portion.

Abstract: Process for the production of gaseous mixtures comprising H.sub.2 +CO e.g. synthesis gas, reducing gas, or fuel gas by the partial oxidation of a vanadium-containing liquid hydrocarbonaceous fuel, solid carbonaceous fuel, or mixtures thereof in a free-flow vertical refractory lined gas generator. The feed mixture to the gas generator comprises (i) a vanadium-containing fuel; (ii) supplemental copper-containing additive; and (iii) at least a portion of the remainder of the copper-containing slag after separation of an enriched vanadium-containing coarse slag fraction. Materials (ii) and (iii) combine in the partial oxidation reaction zone with at least a portion of the nickel and iron constituents and the sulfur found in the feedstock to produce a liquid phase washing agent that collect and transports at least a portion of the vanadium-containing oxide laths and spinels and other ash components out of the reaction zone as molten vanadium-containing slag.

Abstract: Process for the production of gaseous mixtures comprising H.sub.2 +CO e.g. synthesis gas, reducing gas, or fuel gas by the partial oxidation of a vanadium-containing liquid hydrocarbonaceous fuel, solid carbonaceous fuel, or mixtures thereof in a free-flow vertical refractory lined gas generator. The feed mixture to the gas generator comprises (i) a vanadium-containing fuel; (ii) supplemental iron-containing ash fusion temperature reducing agent; and (iii) at least a portion of the remainder of the iron-containing slag after separation of an enriched vanadium-containing coarse slag fraction. The coarse slag fraction has a decreased Fe/V weight ratio and is formed by depositing a portion of the slag entrained in the hot raw effluent gas stream from the partial oxidation reaction zone on the walls of a slag separation chamber located between the bottom discharge outlet in the reaction zone and the effluent gas quench tank located at the bottom of the gas generator.

Abstract: A partial oxidation process for the production of a stream of mixed gases comprising H.sub.2 and CO. An aqueous particulate solid carbonaceous fuel slurry feedstream is preheated by indirect heat exchange with a process-derived stream of skimmed gases substantially comprising H.sub.2 O. The aqueous carrier of the slurry is vaporized by introducing superheated steam directly into the slurry pipeline. A suspension of particulate solid carbonaceous fuel entrained in a gaseous mixture substantially comprising steam e.g. about 90 to 99.9 wt. % H.sub.2 O and about 0.1 to 10 wt. % of a CO.sub.2 -containing gas mixture is produced. The suspension of solid fuel in the gaseous mixture is then separated in a skimming operation into an overhead gas stream substantially comprising steam, as previously described, and a bottom stream comprising particulate solid carbonaceous fuel with the remainder of said gaseous mixture.

Abstract: In a means for supporting an elongated heavy thermocouple assembly the weight of the assembly is carried by a rigid support at an intermediate point along its length instead of by a long lever arm exerting a substantial torque at the point of attachment to the reactor vessel shell as in the conventional design.

Abstract: A feeder for finely divided solids from atmospheric pressure into a high pressure atmosphere. It has a chute to hold the solids at atmospheric pressure, and a valve with seals to deliver the solids into a loading chamber. There is an arrangement for pressurizing the loading chamber, and the chamber is oriented so that the solids will discharge through another valve by gravity flow into the high pressure atmosphere after pressurization of the chamber. There is also an arrangement for displacing the high pressure atmosphere from the chamber after discharge of the solids and before the next delivery of another charge from the chute.

Abstract: A method is provided for turning down or up the output of raw product gas from a partial oxidation gas generator while maintaining in an acceptable range the efficiency of the gas generation, or conversion of the fuel to gas, and the quality of the gas produced. In the process, the flow rates for the separate feedstreams to the burner comprising fuel optionally in admixture with a temperature moderator, at least one stream of free-oxygen containing gas optionally in admixture with a temperature moderator, and with or without a separate feedstream of temperature moderator are adjusted down or up a predetermined amount to obtain a specified output of raw product gas while maintaining substantially constant in the reaction zone the levels of O/C atomic ratio and the temperature moderator/fuel weight ratio.

Abstract: Gold electroplating solutions, particularly useful for plating onto nickel-iron substrates, are prepared utilizing electrolytes of relatively low conductivity, such as boric acid, alkali metal and ammonium acetates, nitrates, sulfates and orthophosphates. The gold is plated onto substrates using a current density ranging from about 1 to about 2000 amperes/square foot at a temperature of about 20.degree. to about 90.degree. C.