Process for manufacturing highly porous slaked lime and product thereby obtained
US-10669199-B2 · Jun 2, 2020 · US
US10934210B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10934210-B2 |
| Application number | US-201716309783-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 23, 2017 |
| Priority date | Jun 24, 2016 |
| Publication date | Mar 2, 2021 |
| Grant date | Mar 2, 2021 |
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The present invention relates to a method for producing a highly porous fine powdery slaked lime composition, comprising a fluidification step for forming said highly porous fine powdery slaked lime composition having an Alpine fluidity greater than 50% and which is carried out in a dryer/grinder chosen from the group consisting of a pin-type dryer/grinder, a cage-type dryer/grinder, an instantaneous dryer/disagglomerator and a combination of these until the powdery slaked lime composition has a non-solid residual-phase content of less than or equal to 3.5% by weight and greater than or equal to 0.3% by weight, as well as the product obtained therefrom.
Opening claim text (preview).
The invention claimed is: 1. Method for producing a highly porous fine powdery slaked lime composition, comprising the steps consisting of: introducing quicklime into a feeding zone of a hydrator, introducing water into the feeding zone of the hydrator; slaking said quicklime in a slaking zone of the hydrator by means of a quantity of water that is sufficient to obtain a slaked lime having a non-solid residual-phase content of between 15% and 55% by weight; drying and grinding said slaked lime in order to form the powdery slaked lime composition, characterised in that said drying and grinding steps are performed simultaneously and are a single step of fluidification of the slaked lime in order to form said fine and highly porous fine powdery slaked lime composition having an Alpine fluidity greater than 50%, the Alpine fluidity AF being defined by the equation AF = m i - m R 90 ( T 15 ; P 100 ) m i - m R 90 ( T 120 ; P 150 ) · 100 where: m 1 is the is the initial mass of 50 g of powder distributed over a 90 μm sieve; m R90(T15; P100) is the mass of residues of material on the sieve after 15 seconds with a negative pressure at 100 mm of manometric liquid of density 0.88; m R90(T120; P150) is the mass of residues of material on the sieve after 15 seconds with a negative pressure at 100 mm of manometric liquid of density 0.88 and after 120 seconds with a negative pressure at 150 mm of manometric liquid of density 0.88; said drying and grinding steps being carried out in a drier/grinder selected from the group consisting of a pin-type dryer/grinder, a cage-type dryer/grinder, an instantaneous dryer/disagglomerator and a combination of these until the highly porous fine powdery slaked lime composition has a residual non-solid phase content, measured by a loss-on-ignition test at 180° C., less than or equal to 3.5% by weight and greater than or equal to 0.3% by weight with respect to the total weight of the powdery slaked lime composition; and characterised in that the drying/grinding steps are performed until the powdery slaked lime composition has a first fraction of particles having a size less than 32 μm and a second fraction of particles having a size greater than 32 μm, provided that the second fraction is less than or equal to 50% by weight with respect to the total weight of the powdery slaked lime composition. 2. Method according to claim 1 , characterised in that it further comprises, before, during and/or after the step of slaking the lime and/or before, during and/or after the drying and grinding steps, a step consisting of adding an additive to the quicklime, the slaking water and/or the slaked lime. 3. Method according to claim 1 , characterised in that the drying/grinding steps are performed until the powdery slaked lime composition has a mean particular size d 50 of less than or equal to 10 μm. 4. Method according to claim 1 , in which the hot air is supplied during the drying/grinding step, at a temperature between 250° C. and 500° C. 5. Method according to claim 1 , in which the drying/grinding step has a duration of between a few seconds and a few minutes.
Oxides or hydroxides (production of lime C04B2/00) · CPC title
Slaking {(simultaneous dehydrating of gypsum and slaking of lime C04B11/022)} · CPC title
Hydroxides · CPC title
Surface area, e.g. BET-specific surface · CPC title
Powder free flowing behaviour · CPC title
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