Process for working up resh or shredder light fractions, with CaCO3
Assignee"Holderbank" Financiere Glarus AG
InventorAlfred Edlinger
Life of this patent
Estimating the term…
Abstract
In this process for working up RESH or shredder light fractions, the RESH or shredder light fractions are charged into a fluidized bed gasifier. Hot wind or combustion offgases having a temperature above 450° C. are blown into the fluidized bed through nozzles while forming a counterflow grinding space. CaCO3 is introduced into the fluidized bed and calcined in the grinding space to effect disintegration.
Claims22
A process for working up starting materials comprising a member selected from the group consisting of RESH and shredder light fractions, said process comprising:
- charging the starting materials into a fluidized bed gasifier having a fluidized bed;
- blowing at least one gas selected from the group consisting of hot air and combustion offgases having a temperature of above 450° C. through nozzles into the fluidized bed gasifier and thereby forming a counterflow grinding space;
- introducing CaCO3 into the fluidized bed gasifier;
- and
- calcining the CaCO3 in the counterflow grinding space to disintegrate the CaCO3 into disintegrated particles.
A process for working up starting materials comprising a member selected from the group consisting of RESH and shredder light fractions, the RESH and shredder light fractions containing iron, said process comprising:
- subjecting the starting materials to magnetic separation to provide the starting materials with a total iron content of less than 6% by weight, then charging the starting materials into a fluidized bed gasifier;
- blowing at least one gas selected from the group consisting of hot air and combustion offgases having a temperature of above 450° C. through nozzles into the fluidized bed gasifier and thereby forming a counterflow grinding space;
- introducing CaCO3 into the fluidized bed gasifier;
- and
- calcining the CaCO3 in the counterflow grinding space to disintegrate the CaCO3 into disintegrated particles.
A process for working up starting materials comprising a member selected from the group consisting of RESH and shredder light fractions, the starting materials containing iron and copper, said process comprising:
- charging the starting materials into a fluidized bed gasifier having a fluidized bed;
- blowing at least one gas selected from the group consisting of hot air and combustion offgases having a temperature of above 450° C. through nozzles into the fluidized bed gasifier and thereby forming a counterflow grinding space;
- introducing CaCO3 into the fluidized bed gasifier;
- calcining the CaCO3 in the counterflow grinding space to disintegrate the CaCO3 into disintegrated particles;
- drawing the disintegrated particles off from the counterflow grinding space of the fluidized bed gasifier and screening the disintegrated particles;
- melting the disintegrated particles to form a melt;
- providing a metal bath reactor containing a metal bath and reducing the melt above the metal bath;
- and
- drawing off from the metal bath reactor by liquation a copper-containing phase while retaining an iron-containing phase in the metal bath reactor.
A process for working up starting materials comprising a member selected from the group consisting of RESH and shredder light fractions, the starting materials containing iron and copper, said process comprising:
- charging the starting materials into a fluidized bed gasifier having a fluidized bed;
- blowing at least one gas selected from the group consisting of hot air and combustion offgases having a temperature of above 450° C. through nozzles into the fluidized bed gasifier and thereby forming a counterflow grinding space;
- introducing CaCO3 into the fluidized bed gasifier;
- calcining the CaCO3 in the counterflow grinding space to disintegrate the CaCO3 into disintegrated particles;
- providing a hot cyclone and drawing off the disintegrated particles from the fluidized bed gasifier, the disintegrated particles comprising coarse stock and fine stock;
- returning at least a portion of the coarse stock from the hot cyclone to the fluidized bed gasifier;
- discharging the fine stock from the hot cyclone and melting the discharged fine stock to produce a molten slag;
- providing a metal bath reactor containing a metal bath and reducing the molten slag above the metal bath;
- and
- drawing off from the metal bath reactor by liquation a copper-containing phase while retaining an iron-containing phase in the metal bath reactor.
Dependencies are inferred from the claim text.