40results about "Horizontal gasifiers" patented technology

A method and process is described for producing negative carbon fuel. In its broadest form, a carbon-containing input is converted to combustible fuels, refinery feedstock, or chemicals and a carbonaceous solid concurrently in separate and substantially uncontaminated form. In an embodiment of the invention, biomass is converted via discrete increasing temperatures under pressure to blendable combustible fuels and a carbonaceous solid. The carbonaceous solid may be reacted to synthesis gas, sold as charcoal product, carbon credits, used for carbon offsets, or sequestered.

Combined microwave heating and plasma/electric arc heating is utilized in several processes and apparatus which involve co-production of pig iron and high quality syngas, biomass to liquid fuel production, coal to liquid fuel production, co-gasification of biomass and coal, municipal solid waste treatment, waste-to-energy (agriculture waste, ASR and PEF), EAF dust and BOF sludge treatment to recover zinc and iron, hazardous bottom ash vitrification, and bromine, chlorine and sulfur removal/recycling.

This invention provides a system and method for efficient reformulation of an initial gas with associated characteristics into an output gas with desired characteristic parameters, within a substantially sealed, contained, and controlled environment. The gas reformulating system uses a gas energizing field to disassociate the initial gas molecules and molecules of injected process additives of appropriate types and amounts, into their constituents that then recombine to form the output gas with the desired parameters. The gas reformulating system further comprises a control system that regulates the process and thereby enables the process to be optimized. The gas energizing field may be provided at least partly by hydrogen burners or plasma torches.

The invention discloses a multi-section spiral moving bed pyrolysis gasification device which comprises a dry-section reactor, a pyrolysis-section reactor and a gasification-section reactor. The dry-section reactor is used for drying materials, the pyrolysis-section reactor is used for pyrolyzing the materials, the gasification-section reactor is used for gasifying the materials, the dry-section reactor, the pyrolysis-section reactor and the gasification-section reactor are provided with feeding ports and discharging ports, the discharging port of the dry-section reactor is connected with thefeeding port of the pyrolysis-section reactor, and the discharging port of the pyrolysis-section reactor is connected with the feeding port of the gasification-section reactor. The device has the advantages that the standing time of the materials is controlled by adjusting the rotating speed of a motor, and matching amount of gasifying agents and the materials is manually and accurately controlledby combining the sectioned air supply speed of an air-distribution plate, so that physical and chemical properties of target products can be controlled.

The invention relates to a horizontal mobile grate gasifier, which comprises a furnace body with a grate and an air supply device. The air supply device consists of a primary air supply pipe and an upper-layer air supply pipe, the primary air supply pipe is connected with a plurality of air chambers and is arranged below the grate, the upper-layer air supply pipe is arranged on the two sidewalls of the furnace body and is communicated with the inner chamber of the furnace body, the rear part of the furnace body is provided with a flue gas channel, the rear end of the flue gas channel is connected with the combustor of a boiler, a flue gas circulating pipe which is connected with the rear part of the combustor communicates circulating flue gas and the upper-layer air supply pipe to form a mixed gas channel, the mixed gas channel and a steam pipe respectively extend into the air chamber and the cavity of the furnace body through a primary air Venturi pipe and a secondary air Venturi pipe; and mixed gas can flow to the front side of the combustor of the boiler through a gas mixing fan. The invention has the advantages of reducing Ringelman black and smoke emission, allowing the use of coal raw materials which are each to be coked, expanding the flexibility of the boiler use and the diversity of operating modes, and realizing the online real-time control and adjustment of parameters of steam output variables, grate operation and gasification dosage, thereby achieving the best operating conditions.

Process for manufacturing a hydrogen-containing synthesis gas from a natural gas feedstock, comprising the conversion of said natural gas into a raw product gas and purification of said product gas, the process having a heat input provided by combustion of a fuel; said process comprises a step of conversion of a carbonaceous feedstock, and at least a portion of said fuel is a gaseous fuel obtained by said step of conversion of said carbonaceous feedstock.

A two stage refuse gasification combustion system for processing refuse is disclosed. The system may contain features such as an advancer, a first and second gasifier, a gas regulator, and a post combustor. Additionally, methods for regulating gas and advancing refuse through a two stage refuse gasification combustion system are disclosed.

The present disclosure is generally directed to process of gasification of carbonaceous materials to produce synthesis gas or syngas. The present disclosure provides improved methods of gasification comprising adding a molecular oxygen- containing gas and optionally adding water into said gasifier. This disclosure is also directed to process of production of one or more alcohols from said syngas via fermentation or digestion in the presence of at least one microorganism.

In one aspect, a grate segment for a burner, comprises a substantially rigid body (30) having a dispersed array of cavities (38) filled with a refractory material. In another aspect, a solid fuel gasifier includes a housing (12) defining a gasifier chamber (14), and a solid fuel inlet (21), grate structure (22, 24) in the gasifier chamber. The grate structure includes base means, a plurality of agitator segments (32) positioned relative to the base means for reciprocating movement to agitate a fuel load in the gasifier, and means to support the base means and the agitator segments so that the latter reciprocate in a direction at a substantial inclination to both horizontal and vertical. In use of the gasifier a deep burden of fuel accumulates on the grate structure and the outward stroke of the reciprocation of the agitator elements is in the overall direction of flow of the fuel burden or generally oppositely thereto.

A treatment method and apparatus is provided to effectively use a combustible waste such as waste plastic, waste tires, rice husk, wood shavings, PKS, RDF and sludge while maintaining stable operation; to improve the combustion efficiency of a fossil fuel such as coal and coke; and furthermore to reduce the NOx concentration in a cement kiln exhaust gas. An apparatus 1 for treating a combustible, the apparatus comprising: a mixer 3 for mixing a combustible C with a preheated raw material R2, which has a temperature of 600° C. or higher and 900° C. or lower and which is drawn from a preheater cyclone of a cement burning device 10, to gasify the combustible; and a feeder 5 for feeding the gasified combustible and the preheated raw material (mixed raw material M) to a region from an inlet end 13a of the cement burning device to a calciner 12. When the combustible and the preheated raw material are mixed, moisture may be added to cause water gas shift reaction, and the resultant water gas and the preheated raw material may be introduced to the region from the inlet end of the cement burning device to the calciner.

This invention relates generally to high temperature burners such as a solid fuel burner of the type commonly referred to as a gasifier or gasifier combustor. The invention includes a refractory wall structure having an array of tubular members. Refractory material is arranged about the tubular members so that the tubular members protrude from a wall defined by the refractory material by a distance smaller than the diameter of the tubular members.

The invention discloses a biomass horizontal pyrolysis gasifier. The structure of the biomass horizontal pyrolysis gasifier comprises a furnace body (1), a feed inlet (8), a gas nozzle (9), an air inlet (5) and an ash discharge opening (7). The feed inlet is arranged at the rear end of the furnace body. The furnace body (1) is a sandwich structure, wherein an inner cavity of the sandwich structure is a gasifying chamber (11), and the middle part of the sandwich structure is an air inlet chamber (12). The feed inlet (8) and the gas nozzle (9) are communicated with the gasifying chamber. The air inlet (5) is communicated with the air inlet chamber (12). The bottom of the furnace body is provided with a feed delivery mechanism (4). The gasifying chamber (11) and the air inlet chamber (12) are communicated with each other at the position of the feed delivery mechanism. According to the biomass horizontal pyrolysis gasifier, by introducing cold air into the air inlet of the sandwich structure, the furnace wall and a reciprocating grate are cooled, and heat-absorbed hot air also can flow upwards from the bottom of a feed layer through the reciprocating grate. By an up-to-bottom counter-burning mode, the feed layer will not be overlapped or mixed during operation of the reciprocating grate, multiple tower-type feed layers are formed to undergo continuous pyrogasification, and safe and stable operation can be carried out on the grate.

The invention discloses a horizontal coal gas gasifier and a gasification method thereof, and relates to the field of clean coal gasification. According to the horizontal gas gasifier and the gasification method thereof, the horizontal gasifier comprises a gasification reaction chamber, a gas-slag separation section and a slag pool which are sequentially arranged from top to bottom, burner channels are symmetrically arranged on the two sides of the gasification reaction chamber, pulverized coal is introduced into the burner channels for incomplete combustion, and high-temperature coal gas and slag generated by gasification reaction enter the gas-slag separation section from a slag discharging opening; a membrane type water cooling wall is vertically arranged in the middle of the gas-slag separation section, low-temperature coal gas enters the gas-slag separation section from a chilling ring arranged on the upper portion of the membrane type water cooling wall, the temperature of the high-temperature coal gas is reduced to be below the ash melting point of slag, the slag is solidified into solid slag, the coal gas and the solid slag are subjected to gas-slag separation at the bottom, the slag falls into the slag pool, coal gas enters a subsequent system from the coal gas outlet in the upper portion, the horizontally-arranged gasification reaction chamber and the membrane type water cooling wall are adopted to play a baffling role, and then the overall height of the gasifier is greatly reduced.

The present invention is directed to an apparatus for domestic hot water and electricity production by the use of a natural organic fuel, the apparatus comprising a separated chambers pyrolysis furnace comprising: a) a pyrolysis chamber wherein the fuel is heated, substantially in the absence of oxygen at a temperature capable of causing pyrolysis of fuel; b) a combustion chamber of the pyrolyzed fuel, wherein the pyrolyzed fuel is burned in the presence of an air flux. The invention is also directed to an apparatus for the production of domestic hot water and electricity, which apparatus comprises: the above defined furnace; b) a heat exchanger connected to the exit of the exhausted gas, wherein domestic water is heated; c) a power generator connected with the exit of syngas, wherein syngas produced in the pyrolysis chamber is used as a fuel.

A gasification system for the partial oxidation of a carbonaceous feedstock to at least provide a synthesis gas, comprising: a reactor chamber for receiving and partially oxidizing the carbonaceous feedstock, the reactor chamber having a reactor chamber floor; a quench chamber below the floor of the reactor chamber for holding a bath of liquid coolant; an intermediate section at said reactor chamber floor, the intermediate section having a reactor outlet opening through which the reactor chamber communicates with the quench chamber to conduct the synthesis gas from the reactor chamber into the bath of the quench chamber; at least one layer of refractory bricks arranged on and supported by the reactor chamber floor, the lower end section of the refractory bricks enclosing the reactor outlet opening and defining the inner diameter thereof; and a dip tube extending from the reactor outlet opening to the bath of the quench chamber, the dip tube having a widened top section.