摘要:
The present invention relates to a technique for separating carbon dioxide from waste gas discharged from a blast furnace, sending the carbon dioxide to a regenerative chamber of a hot stove, and decomposing same by using heat energy stored in the hot stove regenerative chamber and heat of combustion of methane gas supplied from outside. Or, the present invention relates to a technique by which, when carbon dioxide and methane gas are sent to a hot stove regenerative chamber by the present invention, the carbon dioxide and the methane gas are decomposed into carbon monoxide and hydrogen gas by means of stored heat and heat of combustion, and when the decomposed carbon monoxide and hydrogen gas are re-sent to a blast furnace, same take on the role of a reducing gas for reducing iron ore.
摘要:
The invention relates to a method for generating syngas (5). Hydrocarbon (2) is thermally decomposed into hydrogen and carbon in a first reaction zone (Z1), and hydrogen produced in the process is conducted from the first reaction zone (Z1) to a second reaction zone (Z2) in order to react the hydrogen with carbon monoxide (4) in the second reaction zone so as to produce water and carbon monoxide. The invention is characterized in that the energy required for the thermal hydrocarbon decomposition in the first reaction zone (Z1) is supplied from the second reaction zone (Z2).
摘要:
Streams (11) of natural gas contaminated with significant amounts of carbon dioxide can be efficiently and economically processed to create Syngas (16). An available source (1) of flue gas that might otherwise be dispersed into the atmosphere in conjunction with such a CO2-laden natural gas stream (11) renders the process even more economical and efficient through the creation of multiple feedstreams (14, 27, 34) that are combined to deliver a composite near equal mixture of methane and CO2 to a plasma reactor (15) or the like that will generate Syngas. When coupled with a Fischer-Tropsch reactor (40), the overall process provides a particularly efficient and economical process for producing synthetic liquid hydrocarbons.
摘要:
A system and method for producing Syngas from the CO2 in a gaseous stream, such as an exhaust stream, from a power plant or industrial plant, like a cement kiln, is disclosed. A preferred embodiment includes providing the gaseous stream to pyrolysis reactor along with a carbon source such as coke. The CO2 and carbon are heated to about 1330° C. and at about one atmosphere with reactants such as steam such that a reaction takes place that produces Syngas, carbon dioxide (CO2) and hydrogen (H2). The Syngas is then cleaned and provided to a Fischer-Tropsch synthesis reactor to produce Ethanol or Bio-catalytic synthesis reactor.
摘要:
Method for the production of hydrogen from a fuel mixture substantially consisting of methane (CH 4 ) and carbon dioxide (CO 2 ) by means of a hydrogen production plant provided with carbonation reactor and calcination reactor, said method comprising the steps of: a) feeding said carbonation reactor with said fuel mixture; b) feeding said carbonation reactor with water vapor (gaseous H 2 O); c) feeding said carbonation reactor with calcium monoxide (CaO), said calcium monoxide (CaO) at least partially originating from said calcination reactor; d) production of hydrogen (H 2 ) and calcium carbonate (CaCO 3 ) from said carbonation reactor; e) feeding said calcination reactor, suitably heated, with said calcium carbonate (CaCO 3 ); f) production of calcium monoxide (CaO) and carbon dioxide (CO 2 ) from said calcination reactor, said calcium monoxide (CaO) and said carbon dioxide (CO 2 ) evolving by said calcium carbonate (CaCO 3 );
characterized in that during said controlled step of feeding said carbonation reactor with calcium monoxide (CaO), the ratio of the calcium monoxide (CaO) moles introduced in the carbonation reactor during step c) to the sum of the methane (CH 4 ) and carbon dioxide (CO 2 ) moles contained in said fuel mixture during the above-mentioned step a) is greater than 1.
摘要:
A method of gasifying organic materials (carbonaceous compounds) such as coal and fossil fuel and their mixtures including gasifying wastes into syngas, and an apparatus thereof. The apparatus is suitable to gasify carbonaceous wastes without secondary pollutants formed from oxidation. Further, the apparatus can be used in a system to drive a fuel cell.
摘要:
It is known that gaseous fuels can be reformed in several ways in order to produce a mixture of carbon monoxide and hydrogen or in order to produce hydrogen. According to the invention, a non-thermal plasma is produced in a region in which the densities of the gas constituents which are preferably excited in the plasma are below the densities of those which are less preferably excited, especially in order to convert a gaseous or liquid fuel by feeding an oxidant into a gas treatment stage, part of the oxidant being respectively supplied to the fuel flow in a plurality of gas treatment stages.
摘要:
The invention provides a burner array for a reduction reactor 100, wherein the burner array includes multiple burners 200 disposed on a wall 101 of the reduction reactor to allow an inner temperature in the reduction reactor 100 to reach above 1200°C, wherein the reduction reactor 100 has a reaction space formed therein, wherein each burner has a fuel feeding hole 210 and multiple oxygen feeding holes 220 formed therein, wherein each burner 200 has a head portion 201 thereof having an elongate combustion space 202 formed at one end thereof, the combustion space fluid-communicating with the reaction space of the reactor, wherein the elongate combustion space has a length such that oxygen supplied from the oxygen feeding holes thereto is completely consumed via oxidation or combustion with fuels supplied from the fuel feeding hole thereto only in the elongate combustion space upon igniting the burner, wherein non-combusted fuels and H 2 O molecules and/or CO 2 molecules generated via the oxidation reaction in the elongate combustion space are flowed into the reaction space of the reduction reactor, where only a reduction reaction of the H 2 O molecules and/or CO 2 molecules occur at the temperature above 1200°C using a radiation heat generated from the burner. Further, the invention provides a synthesis gas recycling system comprising: the burner array for the reduction reactor as defined above; a cooling and compressing module 400 configured to cool and compress the synthesis gas collected via a gas collection line 121 from the synthesis gas outlet 120; a storage tank 500 configured to receive and store the cooled and compressed gas from the cooling and compressing module 400, and to supply the stored gas to the burner array 200, thereby to allow synthesis gas recycling; and an oxygen generator 600 configured to generate oxygen and supply the oxygen to the oxygen feeding holes 220.