Process for Manufacturing Highly Porous Slaked Lime and Product Thereby Obtained

Patent metadata

Field	Value
Publication number	US-2018155240-A1
Application number	US-201615578581-A
Country	US
Kind code	A1
Filing date	Aug 12, 2016
Priority date	Aug 14, 2015
Publication date	Jun 7, 2018
Grant date	—

Abstract

Process for manufacturing highly porous slake lime comprising a feeding step of quicklime, a feeding step of water in a feeding zone of a hydrator, a slaking step of said quicklime in a slaking zone of said hydrator and a maturation step in a maturation zone of said hydrator to form slaked lime.

First claim

1 . Process for manufacturing highly porous slaked lime comprising a feeding step of quicklime, a feeding step of water in a feeding zone of a hydrator, a slaking step of said quicklime in a slaking zone of said hydrator and a maturation step in a maturation zone of said hydrator to form slaked lime, characterized in that said feeding step of quicklime and said feeding step of water are performed so as to obtain a water/quicklime ratio comprised between 0.8 and 1.3 by weight, preferably between 0.9 and 1.2 and more preferably close to 1, the process further comprising a step of removing vapor generated during said slaking step, said step of removing vapor being performed substantially along said slaking zone to form a raw highly porous slaked lime being a high specific surface area and high pore volume slaked lime.

2 . Process for manufacturing highly porous slaked lime according to claim 1 , further comprising a drying step of said raw slaked lime to form a dried powdery high specific surface area and high pore volume slaked lime.

3 . Process for manufacturing highly porous slaked lime according to claim 1 , wherein said slaking step of said quicklime is performed into a single stage hydrator.

4 . Process for manufacturing highly porous slaked lime according to claim 1 , wherein said step of removing vapor is performed through a fabric filter.

5 . Process for manufacturing highly porous slaked lime according to claim 1 , wherein said step of removing vapor is performed along the entire length of the hydrator.

6 . Process for manufacturing highly porous slaked lime according to claim 1 , wherein the feeding step of quicklime is made by a weighing device, said weighing device comprising a conveyor belt, said conveyor belt allowing quicklime to fall into the hydrator.

7 . Process for manufacturing highly porous slaked lime according to claim 6 , wherein the feeding of water is carried out at a single point at the entry of the hydrator, onto the falling quicklime.

8 . Process for manufacturing highly porous slaked lime according to claim 1 , wherein said quicklime presents a reactivity towards water t 60 , measured according to the European standard EN 459-2, equal to or greater than 15 seconds and equal to or lower than 10 minutes.

9 . Process for manufacturing highly porous slaked lime according to claim 1 , wherein said quicklime presents a particle size d 98 comprised between 90 μm and 10 mm.

10 . Process for manufacturing highly porous slaked lime according to claim 1 , wherein said water presents a temperature equal to or lower than 60° C.

11 . Process for manufacturing highly porous slaked lime according to claim 1 , wherein during said slaking step, lime is mixed and lifted by a shaft equipped with mixing paddles.

12 . Process for manufacturing highly porous slaked lime according to, wherein the temperature in the hydrator is kept below 100° C.

13 . Process for manufacturing highly porous slaked lime according to claim 11 , wherein the manufacturing process of highly porous slaked lime is controlled by measuring the moisture of the raw slaked lime or the motor intensity of the shaft equipped with mixing paddles.

14 . Process for manufacturing highly porous slaked lime according to claim 1 , wherein the moisture content of the raw slaked lime is ranking between 15 and 30 weight % with respect to the weight of said raw slaked lime.

15 . Process for manufacturing highly porous slaked lime according to claim 1 , wherein the feeding step of water is a feeding step of water comprising additives, said additives including di-ethylene glycol or an alkali metal compound selected from the group consisting of alkali metal hydroxides, carbonates, hydrogencarbonates, and mixtures thereof.

16 . A lime composition obtained by the process according to claim 1 , presenting a reproducible partial BJH pore volume composed by the pores with a diameter ranking from 100 Angstroms to 300 Angstroms, higher or equal to 0.07 cm 3 /g and typically lower than 0.15 cm 3 /g.

Assignees

• Lhoist Rech Et Developpement Sa

Inventors

• Chini Stephan
• Lorgouilloux Marion
• Nyssen Olivier
• Francoisse Olivier

Classifications

• C04B2/06

  with addition of substances, e.g. hydrophobic agents {; Slaking in the presence of other compounds} · CPC title

• C04B2/08

  Devices therefor · CPC title

• C04B2/04 Primary

  Slaking {(simultaneous dehydrating of gypsum and slaking of lime C04B11/022)} · CPC title

• B01J20/041

  Oxides or hydroxides · CPC title

• C01F11/02 Primary

  Oxides or hydroxides (production of lime C04B2/00) · CPC title