Abstract:
Synthesis gas is produced by the partial oxidation of a feedstock comprising sulfur and ash-containing heavy liquid hydrocarbonaceous fuels, solid carbonaceous fuels, or mixtures thereof. An iron-containing additive is introduced into the reaction zone along with the feed to produce first and second liquid phase washing agents that collect and transport the vanadium-containing oxide laths and spinels and other ash components out of the reaction zone. A gaseous slag fludizing agent is also introduced into the top of the reaction zone so tha the gasifier is operated at a uniform temperature throughout under conditions that maximize the fluidity of the molten slag over the full opereating temperature range in the gasifier. Equilibrium oxygen and sulfur concentrations are provided in the gas phase in the reaction zone which provide specific partial pressures. By this method substantially all of the molten slag having a reduced viscosity and containing the nickel and vanadium-containing impurities from the feedstock are readily removed from the walls of the gas generator at a lower temperature. Simultaneously, in-situ desulfurization of the feedstock takes place in the gasifier so that the raw effluent product gas may leave the gasifier containing less than about 1.00 mole % of H.sub. 2 S and COS. In one embodiment, an additional supplemental gas e.g. free-oxygen, H.sub.2 S, COS, SO.sub.2, and mixtures thereof may be introduced into the gasifier so as to increase the carbon conversion without increasing the temperature in the reaction zone; or to prevent the formation of free-iron.
Abstract:
Synthesis gas is produced by the partial oxidation of a feedstock comprising a high silicon and sulfur-containing heavy liquid hydrocarbonaceous fuel and/or petroleum coke or tar sands having nickel and vanadium-containing ashes in admixture with a silicon and manganese-containing ash fusion temperature modifying agent in a vertical free-flow unobstructed reaction zone lined with a refractory which comprises in wt. %: silicon-containing material about 95 to 99.8, iron oxide about 0.1 to 1.0, Al.sub.2 O.sub.3 about 0.1 to 1.0, CaO about 0 to 0.4, and others about 0 to 1.2. In the reaction zone separate portions of said silicon and manganese-containing additive (i) combine with a portion of said Fe, Ni, and S to generate a first liquid phase washing agent which washes a portion of the high melting vanadium and oxide phases from the reaction zone, (ii) combine with a portion of said Ni, Ca, Si, Al, Mg and Na and/or K to generate a liquid oxide-silicate phase that fluxes and washes substantially all of the remaining vanadium and other ash components, and (iii) combine with a portion of the molten ash from the fuel and a minor portion of the refractory lining said reaction zone to increase the amount of said liquid oxide silicate phase and thereby enhance the removal of the vanadium from said reaction zone. By this method molten slag having a reduced viscosity and containing the nickel and vanadium-containing impurities from the feedstock and refractory components are readily removed from the gas generator.
Abstract:
A sulfur-containing heavy liquid hydrocarbonaceous fuel and/or solid carbonaceous fuel with nickel, vanadium, and silicon containing ashes is mixed with a copper and/or cobalt-containing material to provide a weight ratio of copper and/or cobalt to nickel in the range of about 0.2 to 10; and the weight ratio of copper and/or cobalt to silicon in said mixture is in the range of about 0.0001 to 0.04. The mixture is reacted by partial oxidation in a down-flowing free-flow unobstructed vertical reaction zone with refractory lined walls at a temperature in the range of about 1800.degree. F. to 2900.degree. F., an equilibrium oxygen concentration in the gas phase in the reaction zone with a partial pressure in the range of about 1.7.times.10.sup.-15 to 2.3.times.10.sup.-8 atmospheres; and an equilibrium sulfur concentration in the gas phase in the reaction zone with a partial pressure in the range of about 2.53.times.10.sup.-7 to 8.1.times.10.sup.-2 atmospheres. A raw effluent gas stream is produced comprising H.sub.2 +CO and containing entrained slag comprising the following phases: (i) Cu-Ni or Co-Ni alloy, (ii) copper silicate and/or cobalt silicate, (iii) a spinel phase, and (iv) about 0 to 5 wt. % of a fluid oxysulfide phase. Substantially no toxic Ni.sub.3 S.sub.2 is produced in the slag.
Abstract:
An aqueous dispersion of unreacted particulate petroleum coke substantially comprising carbon and containing a small amount of ash substantially comprising vanadium constituents and other materials from a process for the partial oxidation of petroleum coke to produce synthesis gas is mixed with C.sub.4 to C.sub.8 acyclic and/or cyclic alkanols and a frothing agent. After pH adjustment, if necessary, the mixture is subjected to aeration with or without mechanical agitation in a froth flotation zone. About 60 to 95 wt. % of the unconverted particulate petroleum coke (basis carbon) particles float in the froth layer that is formed. The remainder of the unconverted petroleum coke comprising coarser particles is suspended in a bottom aqueous dispersion on which the froth layer floats. In addition, selective separation of the vanadium constituents in the unconverted petroleum coke ash takes place. The vanadium content of the ash in the floated portion of unconverted petroleum coke is unexpectedly decreased about 40 to 80 weight percent. Simultaneously, the vanadium content of the ash in the unconverted petroleum coke suspended in the bottom layer of aqueous dispersion is unexpectedly increased about 20 to 60 weight percent. Water may be recovered from this aqueous dispersion and recycled to the gas quench cooling and scrubbing zones. At least portions of the unconverted particulate petroleum coke from the foam layer and the bottom layer are recycled to the partial oxidation gas generator and to a vanadium recovery zone, respectively. By the subject process, the vanadium content in the recycle stream of unconverted petroleum coke to the gas generator is reduced. The life of the refractory lining of the gas generator is thereby extended.
Abstract:
Synthesis gas is produced by the partial oxidation of a fuel feedstock comprising sulfur-containing petroleum coke and/or heavy liquid hydrocarbonaceous fuel and having a nickel and iron-containing ash in a free-flow refractory lined partial oxidation reaction zone. The production of toxic nickel subsulfide (Ni.sub.3 S.sub.2) in said slag is prevented, and there is a substantial reduction in the concentration of H.sub.2 S+COS in the raw product gas stream by introducing an iron-containing additive into the reaction zone along with the feed. The weight ratio of iron-containing additive to ash in the fuel feedstock is in the range of about 0.5 to 10.0. The weight ratio of iron to nickel in said mixture of iron-containing additive and fuel feedstock is greater than 0.33. The additive combines with at least a portion of the nickel and iron constituents and sulfur found in the feedstock to produce a very fluid sulfide phase of iron and nickel, and an Fe, Ni alloy phase. In another embodiment, a minor amount of a calcium compound is included with the iron-containing additive only at startup to reduce the softening temperature of the iron-containing addition agent. By this method, the molten slag produced is free from toxic Ni.sub.3 S.sub.2 and has a comparatively reduced viscosity. Further, the slag may be readily removed from the gas generator at a lower temperature and may be disposed of without contaminating the environment. Further, the life of the refractory lining is extended.
Abstract:
Synthesis gas is produced by the partial oxidation of a feedstock comprising petroleum coke and/or heavy liquid hydrocarbonaceous fuel containing sulfur and having an ash that contains nickel, vanadium and a comparatively high level of silicon. An iron and calcium-containing additive is introduced into the reaction zone along wth the feed. Separate portions of the additive (i) combine with a portion of the nickel, calcium and sulfur to generate a liquid phase washing agent that collects and transports out of the gas generator a portion of the vanadium-containing oxide laths and spinels and other ash components; and (ii) combine with a portion of the nickel, calcium and silicon to generate a liquid oxide-silicate phase that fluxes e.g. dissolves substantially all of the remaining portion of said vanadium-containing oxide laths and spinels and other ash components. In another embodiment, a minor amount of an additonal material selected from the group of elements consisting of magnesium, chromium, manganese, and mixtures thereof is included in the iron and calcium-containing additive. In still another embodiment, the iron and calcium-containing additive is uniformly dispersed in petroleum coke having a nickel and vanadium-containing ash. By this method two types of molten slag having reduced viscosities and containing the nickel and vanadium-containing impurities from the feedstock are readily removed from the gas generator at a lower temperature. Further, the life of the refractory lining is extended.
Abstract:
Mixtures of hydrogen and hydrocarbons may be separated by a membrane formed of a thin dense layer of platinum or palladium on the inside of a porous graphite tube.
Abstract:
Gases such as hydrogen/hydrocarbon may be separated by a separating membrane of a Group VIII noble metal on a deposit of non-noble Group VIII metal which is supported on a porous silver or a porous carbon body.
Abstract:
Mixture of gases such as hydrogen/carbon dioxide may be separated by use of membrane formed by reaction of an aluminum alkoxide with steam at high temperatures and pressures.
Abstract:
The present invention pertains to novel vanadium spinel materials and a method for their preparation. Each vanadium spinel material has a trivalent vanadium cation and is crystallized from a liquid having a composition that falls within a specific polygon shaped area in a ternary composition diagram of V.sub.2 O.sub.3 -FeO-SiO.sub.2 as shown in the drawing herein e.g., FIG. 1. The compositions may be used as a catalyst for oxidation reactions.
Abstract translation:本发明涉及新型钒尖晶石材料及其制备方法。 每个钒尖晶石材料具有三价钒阳离子,并且在V 2 O 3 -FeO-SiO 2的三元组成图中从具有落入特定多边形区域内的组成的液体中结晶,如图所示。 该组合物可用作氧化反应的催化剂。