No. of sale: 190521C
Starting date
ManufacturerMOVESA Year2010 ObservationsComplete plant for CO2 capture using carbonation and calcination technology. Composed of: Process equipment: Two main blower assemblies Two preheaters housing-tubes Four pneumatic control valves, two all/nothing pneumatic valves and a three-way valve for by-pass fumes compressed air system, Oara Solids Power Cleaning Electric Air Preheater for Starter Two self-supporting chimneys One combustor-carbonator reactor A four-cyclone combustor-calcinator reactor for solids separation Two lopp seal valves and two three-way solids divers One fuel hopper, mill, tamper, conveyor screws, weighing scales, rotary dosing valves and solid injection screws. Cooling equipment: Filling/emptying/hibernation tank Volatile condensate tank, where discharges the safety valve from the filling tank, Expansion tank, to absorb the dilations of the volume of the oil in cold and hot Three-way cooling valve Oil filling/emptying pump Of the circuit Centrifugal pumps with speed regulation Filters in the suction of air pumps Air cooler for heat evacuation Bottles with manoreductor for inertized with N2 deposit with heating resistors for start-up
The operation of calcination carbonation technology is based on the ease of co2 reaction with calcium oxide (CaO) to produce limestone powder (CaCO3). To start the process, this plant has two interconnected reactors, a carbonator and a calcinator, operating at atmospheric pressure and in a temperature range of 650 - 700oC and 850 - 950oC respectively. During the process, the CO2 (carbon dioxide) produced in the combustion of biomass within the carbonator reacts with the lime (CaO, calcium oxide) contributed to combustion by trapping the CO2 in the form of CaCO3 (calcium carbonate), so the smoke coming out of the reactor does not contain CO2. The process is completed with a second cycle that takes place in the calcinator. Here the CaCO3 obtained in the carbonator is introduced to transform it again, by means of heat input, into CaO that will enter the carbonator repeating the cycle.
ManufacturerMOVESA Year2010 ObservationsComplete plant for CO2 capture using carbonation and calcination technology. Composed of: Process equipment: Two main blower assemblies Two preheaters housing-tubes Four pneumatic control valves, two all/nothing pneumatic valves and a three-way valve for by-pass fumes compressed air system, Oara Solids Power Cleaning Electric Air Preheater for Starter Two self-supporting chimneys One combustor-carbonator reactor A four-cyclone combustor-calcinator reactor for solids separation Two lopp seal valves and two three-way solids divers One fuel hopper, mill, tamper, conveyor screws, weighing scales, rotary dosing valves and solid injection screws. Cooling equipment: Filling/emptying/hibernation tank Volatile condensate tank, where discharges the safety valve from the filling tank, Expansion tank, to absorb the dilations of the volume of the oil in cold and hot Three-way cooling valve Oil filling/emptying pump Of the circuit Centrifugal pumps with speed regulation Filters in the suction of air pumps Air cooler for heat evacuation Bottles with manoreductor for inertized with N2 deposit with heating resistors for start-up
The operation of calcination carbonation technology is based on the ease of co2 reaction with calcium oxide (CaO) to produce limestone powder (CaCO3). To start the process, this plant has two interconnected reactors, a carbonator and a calcinator, operating at atmospheric pressure and in a temperature range of 650 - 700oC and 850 - 950oC respectively. During the process, the CO2 (carbon dioxide) produced in the combustion of biomass within the carbonator reacts with the lime (CaO, calcium oxide) contributed to combustion by trapping the CO2 in the form of CaCO3 (calcium carbonate), so the smoke coming out of the reactor does not contain CO2. The process is completed with a second cycle that takes place in the calcinator. Here the CaCO3 obtained in the carbonator is introduced to transform it again, by means of heat input, into CaO that will enter the carbonator repeating the cycle.
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