Process for manufacturing a material with a high specific surface area
11559781 · 2023-01-24
Assignee
Inventors
- Clément Sanchez (Bures-sur-Yvette, FR)
- Cédric Boissiere (Villebon sur Yvette, FR)
- Lionel Nicole (Brunoy, FR)
- Hiva Baradari (Paris, FR)
- Xavier Chaucherie (Versailles, FR)
- Bruno Gilardin (Verneuil sur Avre, FR)
Cpc classification
B01J20/3078
PERFORMING OPERATIONS; TRANSPORTING
B01J20/28004
PERFORMING OPERATIONS; TRANSPORTING
B01J20/28061
PERFORMING OPERATIONS; TRANSPORTING
B01J20/28064
PERFORMING OPERATIONS; TRANSPORTING
Y02W30/91
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B01J20/3064
PERFORMING OPERATIONS; TRANSPORTING
B01J20/28083
PERFORMING OPERATIONS; TRANSPORTING
B01J2220/4887
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J20/30
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A manufacturing process that includes spray-drying a liquid composition based on liquid residues derived from a chemical extraction of clinker to form a material with a high specific surface area. Also, a material based on clinker residues having a high specific surface area ranging from 200 m.sup.2.g.sup.−1 to 900 m.sup.2.g.sup.−1 and a mesopore size ranging from 2 nm to 50 nm. Further, the use of a material having a high specific surface area for the absorption of pollutants species.
Claims
1. A process for manufacturing a material with a BET specific surface area of at least 200 m.sup.2.g.sup.−1, and comprising mesopores having a size, determined by transmission electron microscopy, ranging from 2 nm to 50 nm, the process comprising a step of spraying of a liquid composition based on liquid residues derived from a chemical extraction of clinker wherein the liquid composition based on liquid residues derived from the chemical extraction of clinker comprises a structuring agent and a precursor, and, wherein the mole ratio between the structuring agent and the precursor ranges from 0.002 to 0.5.
2. The manufacturing process as claimed in claim 1, comprising a preliminary step of preparing said liquid composition.
3. The manufacturing process as claimed in claim 2, wherein the composition is prepared by mixing the liquid residues derived from a chemical extraction of clinker and the structuring agent.
4. The manufacturing process as claimed in claim 3, wherein the liquid residues derived from a chemical extraction of clinker are obtained by solid/liquid extraction of clinker.
5. The manufacturing process as claimed in claim 4, wherein the solid/liquid extraction is performed with an acidic and/or oxidizing solution.
6. The manufacturing process as claimed in claim 5, wherein the acidic and/or oxidizing solution is at least one of a hydrochloric acid (HCl), sulfuric acid (H.sub.2SO.sub.4), hydrofluoric acid (HF), sodium oxide (Na.sub.2O) or potassium oxide (K.sub.2O) solution.
7. The manufacturing process as claimed in claim 3, wherein the structuring agent is at least one of surfactants, polymers, cellulose-based compounds, and mineral salts.
8. The manufacturing process as claimed in claim 3, wherein the precursor is at least one of silicic acid, silicon alkoxides, silicate, colloidal silica, and silicon tetrachloride.
9. The manufacturing process as claimed in claim 3, comprising, after said spraying step, a step of removing the structuring agent.
10. The manufacturing process as claimed in claim 9, wherein the step of removing the structuring agent is a calcination step.
11. The manufacturing process as claimed in claim 10, wherein the calcination is performed at a temperature of from 400° C. to 600° C.
12. The manufacturing process as claimed in claim 10, wherein the calcination step is performed for a time of 1 hour to 3 hours.
13. The manufacturing process as claimed in claim 10, wherein it also comprises, after said calcination step, a step of washing and drying.
Description
EXAMPLES
Example 1
Production of the Liquid Residues Derived from a Chemical Extraction of Clinker
(1) The clinker leachate is obtained from 1 kg of dried and ground clinker screened to less than 100 μm, to which are added, in a fume cupboard, 1.18 kg of hydrochloric acid at 37% by mass, portionwise so as to limit the exothermic reaction.
(2) Once the hydrochloric acid addition is complete (the change from a pasty state to a liquid state is very rapid; on obtaining the liquid state the exothermic reaction stops), 2 kg of mains water are added with stirring for 10 minutes. This addition makes it possible notably to make the preparation filterable. The mixture is then filtered through a funnel with filter paper of 10 μm porosity.
Example 2
Manufacture a Material with a High Specific Surface Area
(3) Several mesostructured materials with a high specific surface area were manufactured according to the process of the invention from liquid residues derived from a chemical extraction of clinker and by varying the nature of the structuring agent(s) and of the precursor and the amount of structuring agent(s).
(4) For each of the manufactures, the spraying is performed with a Büchi® B-290 spray-dryer and the particles have a diameter of between 0.5 and 10 μm (diameter determined by scanning electron microscopy). a) Mesostructured material with a micron-sized high specific surface area based on leachate from the washing of clinker, TEOS and Brij® 58 (molar composition: 1 leachate dry extract: 1 TEOS: 0.12 Brij® 58).
(5) The following compounds are added in order and with magnetic stirring (500 revolutions.Math.min.sup.−1) to a 500 mL beaker: 25 mL of leachate from the washing of clinker with HCl (37% by mass), 200 mL of osmosed water and 20.49 g of Brij® 58.
(6) The solution is then stirred at 60° C. until the Brij® 58 has fully dissolved. After dissolution of the surfactant and cooling of the solution to 25° C., 31.62 g of tetraethoxysilane (TEOS) are added to the solution dropwise using a Pasteur pipette.
(7) The solution is then stirred at 25° C. for 1 to 2 hours until a clear solution is obtained.
(8) The solution is then sprayed as micrometer-sized droplets in a stream of hot gas (air) using a mono-nozzle with an aperture diameter of 0.7 mm.
(9) The circulation flow rate of the solution was set at 0.36 L.Math.h.sup.−1. The flow rate of compressed air for the spraying was set at 670 L.Math.h.sup.−1. The circulation of air for the suction of the sprayed droplets was set at 34 m.sup.3/h. The nominal sprayer inlet temperature was set at 170-180° C. so that the outlet temperature observed was about 90° C.
(10) The particles thus synthesized and recovered in the recovery tank are then hermetically stored in a polypropylene flask at room temperature, to be subsequently calcined at 450° C. in an oven (ramp of 3° C./min and steady stage of 2 hours at 450° C.).
(11) The material obtained is in powder form and has a BET specific surface area of 505 m.sup.2/g. b) Mesostructured material with a micron-sized high specific surface area based on leachate from the washing of clinker, TEOS and Brij® 58 (molar composition: 1 leachate dry extract: 1 TEOS: 0.20 Brij® 58).
(12) The following compounds are added in order and with magnetic stirring (500 revolutions.Math.min.sup.−1) to a 500 mL beaker: 25 mL of leachate from the washing of clinker with HCl (37% by mass), 200 mL of osmosed water and 34.15 g of Brij® 58.
(13) The solution is then stirred at 60° C. until the Brij® 58 has fully dissolved. After dissolution of the surfactant and cooling of the solution to 25° C., 31.62 g of tetraethoxysilane (TEOS) are added to the solution dropwise using a Pasteur pipette.
(14) The solution is then stirred at 25° C. for 1 to 2 hours until a clear solution is obtained.
(15) The solution is then sprayed as micrometer-sized droplets in a stream of hot gas (air) using a mono-nozzle with an aperture diameter of 0.7 mm.
(16) The circulation flow rate of the solution was set at 0.36 L.Math.h.sup.−1. The flow rate of compressed air for the spraying was set at 670 L.Math.h.sup.−1. The circulation of air for the suction of the sprayed droplets was set at 34 m.sup.3/h. The nominal sprayer inlet temperature was set at 170-180° C. so that the outlet temperature observed was about 90° C. The particles thus synthesized and recovered in the recovery tank are then hermetically stored in a polypropylene flask at room temperature, to be subsequently calcined at 450° C. in an oven (ramp of 3° C./min and steady stage of 2 hours at 450° C.).
(17) The material obtained is in powder form and has a BET specific surface area of 410 m.sup.2/g. c) Mesostructured material with a micron-sized high specific surface area based on leachate from the washing of clinker, TEOS, MTEOS and Brij® 58 (molar composition: 1 leachate dry extract: 0.95 TEOS: 0.05 MTEOS: 0.12 Brij® 58).
(18) The following compounds are added in order and with magnetic stirring (500 revolutions.Math.min.sup.−1) to a 500 mL beaker: 40 mL of leachate from the washing of clinker with HCl (37% by mass), 100 mL of osmosed water and 24.14 g of Brij® 58.
(19) The solution is then stirred at 60° C. until the Brij® 58 has fully dissolved. After dissolution of the surfactant and cooling of the solution to 25° C., 29.99 g of tetraethoxysilane (TEOS) and 0.64 g of methyltriethoxysilane (MTEOS) are added to the solution dropwise using a Pasteur pipette.
(20) The solution is then stirred at 25° C. for 1 to 2 hours until a clear solution is obtained. The solution is then sprayed as micrometer-sized droplets in a stream of hot gas (air) using a mono-nozzle with an aperture diameter of 0.7 mm.
(21) The circulation flow rate of the solution was set at 0.36 L.Math.h.sup.−1. The flow rate of compressed air for the spraying was set at 670 L.Math.h.sup.−1. The circulation of air for the suction of the sprayed droplets was set at 34 m.sup.3/h.
(22) The nominal sprayer inlet temperature was set at 170-180° C. so that the outlet temperature observed was about 90° C.
(23) The particles thus synthesized and recovered in the recovery tank are then hermetically stored in a polypropylene flask at room temperature, to be subsequently calcined at 350° C. in an oven (ramp of 3° C./min and steady stage of 2 hours at 350° C.).
(24) The material obtained is in powder form and has a BET specific surface area of 440 m.sup.2/g. d) Mesostructured material with a micron-sized high specific surface area based on leachate from the washing of clinker, SiCl.sub.4 produced and Brij® 58 (molar composition: 1 leachate dry extract: 1 SiCl.sub.4: 0.12 Brij® 58).
(25) The following compounds are added in order and with magnetic stirring (500 revolutions.Math.min.sup.−1) to a 300 mL beaker: 12.5 mL of leachate from the washing of clinker with HCl (37% by mass), 100 mL of osmosed water and 10.24 g of Brij® 58.
(26) The solution is then stirred at 60° C. until the Brij® 58 has fully dissolved.
(27) In a second 500 mL beaker, 12.9 g of SiCl.sub.4 stored at 4° C. are added dropwise to 22.15 mL of absolute ethanol stored at 4° C. Since the reaction is exothermic and highly reactive, this mixing takes place in an ice bath with vigorous stirring (1000 revolutions.Math.min.sup.−1).
(28) After dissolution of the surfactant and cooling of the leachate/Brij 58 solution to 25° C., this solution is added to the SiCl.sub.4/ethanol solution dropwise using a Pasteur pipette and with vigorous stirring (1000-1200 revolutions.Math.min.sup.−1).
(29) The solution obtained is then stirred at 25° C. for 1 to 2 hours until a clear solution is obtained, and is then sprayed as micrometer-sized droplets in a stream of hot gas (air) using a mono-nozzle with an aperture diameter of 0.7 mm.
(30) The circulation flow rate of the solution was set at 0.36 L.Math.h.sup.−1. The flow rate of compressed air for the spraying was set at 670 L.Math.h.sup.−1. The circulation of air for the suction of the sprayed droplets was set at 34 m.sup.3/h. The nominal sprayer inlet temperature was set at 170-180° C. so that the outlet temperature observed was about 90° C.
(31) The particles thus synthesized and recovered in the recovery tank are then hermetically stored in a polypropylene flask at room temperature, to be subsequently calcined at 450° C. in an oven (ramp of 3° C./min and steady stage of 2 hours at 450° C.). The material obtained is in powder form and has a BET specific surface area of 560 m.sup.2/g. e) Mesostructured material with a micron-sized high specific surface area based on leachate from the washing of clinker, SiCl.sub.4, MTEOS and Brij® 58 (molar composition: 1 leachate dry extract: 0.95 SiCl.sub.4: 0.05 MTEOS: 0.12 Brij® 58).
(32) The following compounds are added in order and with magnetic stirring (500 revolutions.Math.min.sup.−1) to a 200 mL beaker: 12.5 mL of leachate from the washing of clinker with HCl (37% by mass), 100 mL of osmosed water and 10.24 g of Brij® 58.
(33) The solution is then stirred at 60° C. until the Brij® 58 has fully dissolved.
(34) In a second 500 mL beaker, 12.27 g of SiCl.sub.4 stored at 4° C. are added dropwise (Pasteur pipette) to 21.04 mL of absolute ethanol stored at 4° C. Since the reaction is exothermic and highly reactive, this mixing takes place in an ice bath with vigorous stirring (1000 revolutions.Math.min.sup.−1). The 0.51 g of methyltriethoxysilane (MTEOS) is added dropwise (Pasteur pipette) to the SiCl.sub.4/ethanol solution.
(35) After dissolution of the surfactant and cooling of the leachate/Brij® 58 solution to 25° C., this solution is added to the SiCl.sub.4/ethanol/MTEOS solution dropwise using a Pasteur pipette and with vigorous stirring (1000-1200 revolutions.Math.min.sup.−1).
(36) The solution obtained is then stirred at 25° C. for 1 to 2 hours until a clear solution is obtained. The solution is then sprayed as micrometer-sized droplets in a stream of hot gas (air) using a mono-nozzle with an aperture diameter of 0.7 mm. The circulation flow rate of the solution was set at 0.36 L.Math.h.sup.−1. The flow rate of compressed air for the spraying was set at 670 L.Math.h.sup.−1. The circulation of air for the suction of the sprayed droplets was set at 34 m.sup.3/h. The nominal sprayer inlet temperature was set at 170-180° C. so that the outlet temperature observed was about 90° C.
(37) The particles thus synthesized and recovered in the recovery tank are then hermetically stored in a polypropylene flask at room temperature, to be subsequently calcined at 350° C. in an oven (ramp of 3° C./min and steady stage of 2 hours at 350° C.). The material obtained is in powder form and has a BET specific surface area of 620 m.sup.2/g. f) Mesostructured material with a micron-sized high specific surface area based on leachate from the washing of clinker, SiCl.sub.4, MTEOS and Brij® 58 (molar composition: 1 leachate dry extract: 0.85 SiCl.sub.4: 0.15 MTEOS: 0.12 Brij® 58).
(38) The following compounds are added in order and with magnetic stirring (500 revolutions.Math.min.sup.−1) to a 200 mL beaker: 12.5 mL of leachate from the washing of clinker with HCl (37% by mass), 100 mL of osmosed water and 10.24 g of Brij® 58. The solution is then stirred at 60° C. until the Brij® 58 has fully dissolved.
(39) In a second 500 mL beaker, 11.63 g of SiCl.sub.4 stored at 4° C. are added dropwise (Pasteur pipette) to 20.26 mL of absolute ethanol stored at 4° C. Since the reaction is exothermic and highly reactive, this mixing takes place in an ice bath with vigorous stirring (1000 revolutions.Math.min.sup.−1). The 1.03 g of methyltriethoxysilane (MTEOS) are added dropwise (Pasteur pipette) to the SiCl.sub.4/ethanol solution.
(40) After dissolution of the surfactant and cooling of the leachate/Brij® 58 solution to 25° C., this solution is added to the SiCl.sub.4/ethanol/MTEOS solution dropwise using a Pasteur pipette and with vigorous stirring (1000-1200 revolutions.Math.min.sup.−1).
(41) The solution obtained is then stirred at 25° C. for 1 to 2 hours until a clear solution is obtained. The solution is then sprayed as micrometer-sized droplets in a stream of hot gas (air) using a mono-nozzle with an aperture diameter of 0.7 mm. The circulation flow rate of the solution was set at 0.36 L.Math.h.sup.−1. The flow rate of compressed air for the spraying was set at 670 L.Math.h.sup.−1. The circulation of air for the suction of the sprayed droplets was set at 34 m.sup.3/h. The nominal sprayer inlet temperature was set at 170-180° C. so that the outlet temperature observed was about 90° C.
(42) The particles thus synthesized and recovered in the recovery tank are then hermetically stored in a polypropylene flask at room temperature, to be subsequently calcined at 350° C. in an oven (ramp of 3° C./min and steady stage of 2 hours at 350° C.). The material obtained is in powder form and has a BET specific surface area of 625 m.sup.2/g. g) Mesostructured material with a micron-sized high specific surface area based on leachate from the washing of clinker, SiCl.sub.4, PTEOS and Brij® 58 (molar composition: 1 leachate dry extract: 0.95 SiCl.sub.4: 0.05 PTEOS: 0.12 Brij® 58).
(43) The following compounds are added in order and with magnetic stirring (500 revolutions.Math.min.sup.−1) to a 200 mL beaker: 12.5 mL of leachate from the washing of clinker with HCl (37% by mass), 100 mL of osmosed water and 10.24 g of Brij® 58. The solution is then stirred at 60° C. until the Brij® 58 has fully dissolved.
(44) In a second 500 mL beaker, 12.27 g of SiCl.sub.4 stored at 4° C. are added dropwise (Pasteur pipette) to 21.04 mL of absolute ethanol stored at 4° C. Since the reaction is exothermic and highly reactive, this mixing takes place in an ice bath with vigorous stirring (1000 revolutions.Math.min.sup.−1). The 0.91 g of phenyltriethoxysilane (PTEOS) is added dropwise (Pasteur pipette) to the SiCl.sub.4/ethanol solution.
(45) After dissolution of the surfactant and cooling of the leachate/Brij® 58 solution to 25° C., this solution is added to the SiCl.sub.4/ethanol/PTEOS solution dropwise using a Pasteur pipette and with vigorous stirring (1000-1200 revolutions.Math.min.sup.−1).
(46) The solution obtained is then stirred at 25° C. for 1 to 2 hours until a clear solution is obtained. The solution is then sprayed as micrometer-sized droplets in a stream of hot gas (air) using a mono-nozzle with an aperture diameter of 0.7 mm. The circulation flow rate of the solution was set at 0.36 L.Math.h.sup.−1. The flow rate of compressed air for the spraying was set at 670 L.Math.h.sup.−1. The circulation of air for the suction of the sprayed droplets was set at 34 m.sup.3/h. The nominal sprayer inlet temperature was set at 170-180° C. so that the outlet temperature observed was about 90° C.
(47) The particles thus synthesized and recovered in the recovery tank are then hermetically stored in a polypropylene flask at room temperature, to be subsequently calcined at 350° C. in an oven (ramp of 3° C./min and steady stage of 2 hours at 350° C.). The material obtained is in powder form and has a BET specific surface area of 695 m.sup.2/g. h) Mesostructured material with a micron-sized high specific surface area based on leachate from the washing of clinker, SiCl.sub.4, APTES and Brij® 58 (molar composition: 1 leachate dry extract: 0.95 SiCl.sub.4: 0.05 APTES: 0.12 Brij® 58).
(48) The following compounds are added in order and with magnetic stirring (500 revolutions.Math.min.sup.−1) to a 200 mL beaker: 12.5 mL of leachate from the washing of clinker with HCl (37% by mass), 100 mL of osmosed water and 10.25 g of Brij® 58. The solution is then stirred at 60° C. until the Brij® 58 has fully dissolved.
(49) In a second 500 mL beaker, 12.27 g of SiCl.sub.4 stored at 4° C. are added dropwise (Pasteur pipette) to 21.04 mL of absolute ethanol stored at 4° C. Since the reaction is exothermic and highly reactive, this mixing takes place in an ice bath with vigorous stirring (1000 revolutions.Math.min.sup.−1). The 0.84 g of aminopropyltriethoxysilane (APTES) is added dropwise (Pasteur pipette) to the SiCl.sub.4/ethanol solution. After dissolution of the surfactant and cooling of the leachate/Brij® 58 solution to 25° C., this solution is added to the SiCl.sub.4/ethanol/APTES solution dropwise using a Pasteur pipette and with vigorous stirring (1000-1200 revolutions.Math.min.sup.−1).
(50) The solution obtained is then stirred at 25° C. for 1 to 2 hours until a clear solution is obtained. The solution is then sprayed as micrometer-sized droplets in a stream of hot gas (air) using a mono-nozzle with an aperture diameter of 0.7 mm. The circulation flow rate of the solution was set at 0.36 L.Math.h.sup.−1. The flow rate of compressed air for the spraying was set at 670 L.Math.h.sup.−1. The circulation of air for the suction of the sprayed droplets was set at 34 m.sup.3/h. The nominal sprayer inlet temperature was set at 170-180° C. so that the outlet temperature observed was about 90° C.
(51) The particles thus synthesized and recovered in the recovery tank are then hermetically stored in a polypropylene flask at room temperature, to be subsequently calcined at 350° C. in an oven (ramp of 3° C./min and steady stage of 2 hours at 350° C.). The material obtained is in powder form and has a BET specific surface area of 410 m.sup.2/g. i) Mesostructured material with a micron-sized high specific surface area based on leachate from the washing of clinker, TEOS and CTAB (molar composition: 1 leachate dry extract: 1 TEOS: 0.28 CTAB).
(52) The following compounds are added in order and with magnetic stirring (500 revolutions.Math.min.sup.−1) to a 500 mL beaker: 25 mL of leachate from the washing of clinker with HCl (37% by mass), 200 mL of osmosed water and 15.49 g of CTAB. The solution is then stirred until the CTAB has fully dissolved.
(53) After dissolution of the surfactant, 31.62 g of tetraethoxysilane (TEOS) are added to the solution dropwise using a Pasteur pipette. The solution is then stirred at 25° C. for 1 to 2 hours until a clear solution is obtained.
(54) The solution is then sprayed as micrometer-sized droplets in a stream of hot gas (air) using a mono-nozzle with an aperture diameter of 0.7 mm. The circulation flow rate of the solution was set at 0.36 L.Math.h.sup.−1. The flow rate of compressed air for the spraying was set at 670 L.Math.h.sup.−1. The circulation of air for the suction of the sprayed droplets was set at 34 m.sup.3/h. The nominal sprayer inlet temperature was set at 170-180° C. so that the outlet temperature observed was about 90° C.
(55) The particles thus synthesized and recovered in the recovery tank are then hermetically stored in a polypropylene flask at room temperature, to be subsequently calcined at 450° C. in an oven (ramp of 3° C./min and steady stage of 2 hours at 450° C.). The material obtained is in powder form and has a BET specific surface area of 485 m.sup.2/g.