摘要:
A process for using a facility having a first reactor (1) for reducing oxide in which enter a fuel material E1) and metal oxide for providing a reaction of combustion of the fuel material (E1), the first reactor (1) being connected to a second reactor (4) for oxidizing oxide, where the process includes additional oxygen (O) in a gaseous form being injected into the first reactor (1) for reducing oxide and in that the additional oxygen (O) quantity is comprised between 10 and 30% relatively to stoichiometric oxygen for full fuel material (E1) combustion.
摘要:
The invention concerns a process for using a facility in which circulates at least one oxide which is reduced and then oxidized in each of both reactors (1, 4) and including a reactor (1) for reducing oxide in which enter a grounded solid fuel material (E1) and oxide (E2), a lower efficiency separation device (2) receiving entrained solids from the reactor (1) for reducing oxide the upper stream of the solids of the lower efficiency separation device (2) being circulated into a higher efficiency separation device (6), in order to separate the solids from the gases and to re-introduce the solids into the reactor (1) for reducing oxides, a carbon separator (3) installed at the outlet of the lower efficiency separation device (2) in order to send the carbonaceous particles into the reactor (1) for reducing oxide and the oxide into a reactor (4) for oxidizing oxide and a separation device (5) receiving entrained solids from the reactor (4) for oxidizing oxide. According to the invention, the average particle diameter of the entering solid fuel material (E1) is controlled to be at least twice smaller than the average particle diameter of the entering oxide (E2).
摘要:
The invention is related to a system (1) for converting fuel material comprising: a first reactor (2) in which a fuel material reacts with an oxide material for producing reaction products including fuel particles, ash and oxide particles, a second reactor (3) for oxidizing the oxide particles produced in the first reactor (2), a carbon separator (4) that receives fuel particles, ash and oxide particles produced in the first reactor (2) and suitable for separating the oxide particles and ash from the fuel particles, the carbon separator (4) comprising an outlet path (4c) for the oxide particles and ash exhaust, characterized in that said outlet path (4c) of the carbon separator (4) is connected to an ash separator (10) for separating the ash from the oxide particles.
摘要:
A hot solids process selectively operable for purposes of generating at least one predetermined output based on what the specific nature of the primary purpose of the hot solids process is for which the at least one predetermined output that is selected from a multiplicity of predetermined outputs, such as H2 and CO2, is being produced, and wherein such primary purpose of the hot solids process is designed to be pre-selected from a group of primary purposes of the hot solids process that includes at least two of the generation of H2 for electric power purposes, the generation of SynGas for electric power production as well as for other industrial uses, the production of steam for electric power generation as well as for other uses, the production of process heat, the production of CO2 for agricultural purposes, and the generation of a feedstock such as H2 for use for the production of liquid hydrocarbons.
摘要:
The invention is related to a system (1) for converting fuel material comprising: a first reactor (2) in which a fuel material reacts with an oxide material for producing reaction products including fuel particles, ash and oxide particles, a second reactor (3) for oxidizing the oxide particles produced in the first reactor (2), a carbon separator (4) that receives fuel particles, ash and oxide particles produced in the first reactor (2) and suitable for separating the oxide particles and ash from the fuel particles, the carbon separator (4) comprising an outlet path (4c) for the oxide particles and ash exhaust, characterized in that said outlet path (4c) of the carbon separator (4) is connected to an ash separator (10) for separating the ash from the oxide particles.