US20010038819A1 - Process for the preparation of aluminum fluoride - Google Patents
Process for the preparation of aluminum fluoride Download PDFInfo
- Publication number
- US20010038819A1 US20010038819A1 US09/740,963 US74096300A US2001038819A1 US 20010038819 A1 US20010038819 A1 US 20010038819A1 US 74096300 A US74096300 A US 74096300A US 2001038819 A1 US2001038819 A1 US 2001038819A1
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- US
- United States
- Prior art keywords
- aluminum fluoride
- alumina
- fluorination
- alf
- preparing aluminum
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
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- KLZUFWVZNOTSEM-UHFFFAOYSA-K Aluminum fluoride Inorganic materials F[Al](F)F KLZUFWVZNOTSEM-UHFFFAOYSA-K 0.000 title claims abstract description 44
- IRPGOXJVTQTAAN-UHFFFAOYSA-N 2,2,3,3,3-pentafluoropropanal Chemical compound FC(F)(F)C(F)(F)C=O IRPGOXJVTQTAAN-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims description 14
- 238000002360 preparation method Methods 0.000 title description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 33
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000003682 fluorination reaction Methods 0.000 claims abstract description 23
- 239000011148 porous material Substances 0.000 claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 claims abstract description 13
- 229910052814 silicon oxide Inorganic materials 0.000 claims abstract description 4
- 239000000377 silicon dioxide Substances 0.000 claims description 13
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 4
- 229910052731 fluorine Inorganic materials 0.000 claims description 4
- 239000011737 fluorine Substances 0.000 claims description 4
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 3
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 16
- QPJSUIGXIBEQAC-UHFFFAOYSA-N n-(2,4-dichloro-5-propan-2-yloxyphenyl)acetamide Chemical compound CC(C)OC1=CC(NC(C)=O)=C(Cl)C=C1Cl QPJSUIGXIBEQAC-UHFFFAOYSA-N 0.000 description 14
- 241000640882 Condea Species 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000001354 calcination Methods 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002638 heterogeneous catalyst Substances 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- ZZBAGJPKGRJIJH-UHFFFAOYSA-N 7h-purine-2-carbaldehyde Chemical compound O=CC1=NC=C2NC=NC2=N1 ZZBAGJPKGRJIJH-UHFFFAOYSA-N 0.000 description 1
- 238000004438 BET method Methods 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- -1 aluminum halide Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000008246 gaseous mixture Substances 0.000 description 1
- 238000001033 granulometry Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 229910001055 inconels 600 Inorganic materials 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910003480 inorganic solid Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002815 nickel Chemical class 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 238000004876 x-ray fluorescence Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/48—Halides, with or without other cations besides aluminium
- C01F7/50—Fluorides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/06—Halogens; Compounds thereof
- B01J27/125—Halogens; Compounds thereof with scandium, yttrium, aluminium, gallium, indium or thallium
-
- B01J35/613—
-
- B01J35/615—
-
- B01J35/633—
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/22—Halogenating
- B01J37/26—Fluorinating
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/14—Pore volume
Definitions
- the present invention relates to a process for preparing aluminum fluoride and the so obtained aluminum fluoride.
- the invention relates to an improved process for preparing aluminum fluoride starting from the corresponding oxide.
- the aluminum fluoride (AlF 3 ) is an inorganic solid well known in the art of the preparation of heterogeneous catalysts. It is used both as such and as support for metal salts and shows catalytic activity due to its strong acidity according to Lewis and/or its thermal and chemical inertia. It is widely used, for instance, in the fluorination of chlorinated organic compounds to obtain the corresponding fluorinated compounds; in this case it is used also as a support of chromium, cobalt, nickel salts, etc. See for instance U.S. Pat. No. 4,967,023 and U.S. Pat. No. 5,008,475.
- a solid which must be used as heterogeneous catalyst both as such, and as a support for a catalytically active phase, has a surface area (SA) and a pore volume (vp) as higher as possible.
- SA surface area
- vp pore volume
- Typical examples of solid used to this purpose are the various kinds of alumina having surface areas of 200-300 m 2 /g and pore volumes around 0.5 cc/g.
- It is therefore an object of the present invention a process for preparing aluminum fluoride having an high surface area and high pore volume comprising the fluorination with gaseous HF of alumina having surface area of at least 150 m 2 /g and pore volume not lower than 0.3 cc/g, said alumina comprising from about 0.5 up to about 15% by weight of silicon oxide, preferably from 1 to 10% by weight, more preferably from 1.5 to 6% by weight.
- aluminum fluoride according to the present invention, it is meant the alumina fluorination product, having a fluorine content not lower than 90%, preferably not lower than 95%, of the stoichiometric.
- the AlF 3 obtained with the process of the invention maintains its characteristics of high surface area and of high pore volume also during its use in fluorination and therefore it does not require frequent regeneration processes.
- the AlF 3 obtainable with the process of the invention has been found to maintain a fraction of the surface area of the starting alumina which is also the double of that obtainable starting from alumina not containing silica. Likewise the maintained fraction of the pore volume results higher when alumina containing silica according to the present invention is used.
- the AlF 3 obtainable with the process of the invention has generally a surface area not lower than 25 m 2 /g, preferably not lower than 30 m 2 /g and a pore volume not lower than 0.20 cc/g, preferably 0.25 cc/g.
- the fluorination conditions of alumina containing silica are not particularly critical. One generally operates at a temperature comprised between about 250° C. and about 450° C., preferably higher than 300°-400° C. Indeed if one operates at temperatures lower than those indicated, the fluorination is too slow.
- the total pressure has no relevant effects and one generally operates at atmospheric pressure or slightly higher, generally of some atmospheres.
- HF diluted with a gas inert in the fluorination conditions for instance, air or nitrogen; the partial pressure of HF is generally comprised between 0.1 and 0.50.
- the alumina which is used according to the present invention contains less than 0.1% by weight (each) of undesirable contaminants in the final product AlF 3 such as: iron, sulphates, sodium.
- aluminas are in hydrated form, it is preferable to subject the aluminas to a calcination phase in air or nitrogen, at a temperature comprised between 300° C. and 400° C., before the fluorination step. This limits the development of water during the reaction, which is undesirable especially because it favours the equipment corrosion.
- aliminas containing silica are prepared with known methods in the art, for instance by spray-drying of suitable precursors.
- aluminas containing silica which are preferably used according to the present invention are for instance commercial products of Condea Chemie (Germany).
- Aluminas, aluminas containing silica and aluminum fluorides are characterized by techniques well known to the skilled in the art of the solid characterization: the surface area (SA) is measured by nitrogen adsorption according to the BET method; the pore volume is measured by mercury injection at high pressure; the crystalline phases by X ray diffraction; the constituent analyses are carried out by wet way according to known methods, or by X ray fluorescence by comparison with standards prepared on the same matrix by calibrated additions.
- SA surface area
- pore volume is measured by mercury injection at high pressure
- the crystalline phases by X ray diffraction
- the constituent analyses are carried out by wet way according to known methods, or by X ray fluorescence by comparison with standards prepared on the same matrix by calibrated additions.
- AlF 3 obtained according to the process of the present invention generally is mainly formed by gamma phase as described in FR 1,383,927.
- a sample of an alumina free from silica (commercial product CONDEA PURAL® SCC-10) is calcined in air flow at 360° C.; after the calcination it results to have:
- 370 g of this alumina are introduced in an Inconel 600® tubular reactor, having a 50 mm diameter, electrically heated and equipped with porous septum at the base, and fluorinated at 360° C. with an air/HF mixture for 30 hours at the temperature of 360° C.; at steady conditions the mixture composition is 0.85 mole/h of HF, 4 mole of air.
- the reactor is cooled under air flow and about 510 g of aluminum fluoride are discharged having the following characteristics:
- Vp 0.442 cm 3 /g
- DRX pseudo-bohemite
- Vp 0.26 cm 3 /g
- crytalline structure ⁇ -AlF 3 with a little of ⁇ -AlF 3 .
- DRX pseudo-bohemite
Abstract
Process for preparing aluminum fluoride having an high surface area and high pore volume comprising the fluorination with HF of alumina having surface area of at least 150 m2/g and pore volume not lower than 0.3 cc/g, said alumina comprising from about 0.5 up to about 15% by weight of silicon oxide.
Description
- The present invention relates to a process for preparing aluminum fluoride and the so obtained aluminum fluoride.
- In particular the invention relates to an improved process for preparing aluminum fluoride starting from the corresponding oxide.
- The aluminum fluoride (AlF3) is an inorganic solid well known in the art of the preparation of heterogeneous catalysts. It is used both as such and as support for metal salts and shows catalytic activity due to its strong acidity according to Lewis and/or its thermal and chemical inertia. It is widely used, for instance, in the fluorination of chlorinated organic compounds to obtain the corresponding fluorinated compounds; in this case it is used also as a support of chromium, cobalt, nickel salts, etc. See for instance U.S. Pat. No. 4,967,023 and U.S. Pat. No. 5,008,475.
- The preparation, in industrial scale, of aluminum fluoride is carried out by fluorination of the aluminum oxide (alumina) with anhydrous hydrofluoric acid (HF). Other methods are also known which however have substantially a laboratory application, such as the pyrolysis of hexafluoroaluminates; the treatment of alumina with chlorofluorinated organic compounds; the F/X exchange on an aluminum halide wherein X is equal to Cl, Br, et.
- In the case of alumina fluorination the amount of fluorine content depends on the reaction conditions and can be also much lower than the stoichiometric.
- The alumina fluorination with anhydrous HF to obtain AlF3 is well known in the art and is described for instance in FR 1,383,927, wherein the so obtained AlF3 is then used as such to catalyse the HF sum on acetylene.
- As it is well known to the skilled in the catalyst preparation, it is desirable that a solid which must be used as heterogeneous catalyst, both as such, and as a support for a catalytically active phase, has a surface area (SA) and a pore volume (vp) as higher as possible. Typical examples of solid used to this purpose are the various kinds of alumina having surface areas of 200-300 m2/g and pore volumes around 0.5 cc/g.
- However the alumina fluorination to obtain AlF3 drastically reduces said parameter values: the obtained AlF3 shows indeed low SA and low Vp. To try to increase these values it is well known to limit the fluorination well below the stoichiometric.
- This process of course cannot be applied to the fluorination catalysts, since the HF used as reactant would lead to completion the fluorination of the alumina, with consequent loss of surface area and of catalytic activity.
- In order to overcome this drawback, it has been suggested, see GB 1,000,485, to regenerate the alumina when it overfluorinated by steam treatment at high temperature. Such process is of course not very practical in industrial scale, especially for the great aggressiveness of the gaseous mixture of HF and water at high temperature which is thus produced. A further drawback is in that these kinds of catalyst require frequent regenerations and therefore the interruption of the production processes where they are used.
- It has been now surprisingly and unexpectedly found by the Applicant that it is possible to obtain AlF3 with high surface area and high pore volume, by fluorination of alumina with anhydrous HF by using the process described hereinafter.
- It is therefore an object of the present invention a process for preparing aluminum fluoride having an high surface area and high pore volume comprising the fluorination with gaseous HF of alumina having surface area of at least 150 m2/g and pore volume not lower than 0.3 cc/g, said alumina comprising from about 0.5 up to about 15% by weight of silicon oxide, preferably from 1 to 10% by weight, more preferably from 1.5 to 6% by weight.
- As aluminum fluoride, according to the present invention, it is meant the alumina fluorination product, having a fluorine content not lower than 90%, preferably not lower than 95%, of the stoichiometric.
- The AlF3 obtained with the process of the invention maintains its characteristics of high surface area and of high pore volume also during its use in fluorination and therefore it does not require frequent regeneration processes.
- The AlF3 obtainable with the process of the invention has been found to maintain a fraction of the surface area of the starting alumina which is also the double of that obtainable starting from alumina not containing silica. Likewise the maintained fraction of the pore volume results higher when alumina containing silica according to the present invention is used.
- The AlF3 obtainable with the process of the invention has generally a surface area not lower than 25 m2/g, preferably not lower than 30 m2/g and a pore volume not lower than 0.20 cc/g, preferably 0.25 cc/g.
- The fluorination conditions of alumina containing silica are not particularly critical. One generally operates at a temperature comprised between about 250° C. and about 450° C., preferably higher than 300°-400° C. Indeed if one operates at temperatures lower than those indicated, the fluorination is too slow.
- The total pressure has no relevant effects and one generally operates at atmospheric pressure or slightly higher, generally of some atmospheres.
- It is advantageous that the partial pressure of HF is low, especially at the beginning of the fluorination, to moderate the heat development which could locally increase the temperature over the above limits: indeed two highly exothermic phenomena contemporaneously occur: the reaction between HF and alumina with formation of AlF3 and water and the hydration of the unreacted HF from the latter.
- To moderate these exothermic effects it is sufficient to use HF diluted with a gas inert in the fluorination conditions, for instance, air or nitrogen; the partial pressure of HF is generally comprised between 0.1 and 0.50.
- A better control of the temperature is possible also by carrying out the reaction in fluidized bed and this is the preferred way to carry out the fluorination. In this case the aluminas to be fluorinated have a granulometry compatible with the use of fluidized beds.
- In general the alumina which is used according to the present invention contains less than 0.1% by weight (each) of undesirable contaminants in the final product AlF3 such as: iron, sulphates, sodium.
- If aluminas are in hydrated form, it is preferable to subject the aluminas to a calcination phase in air or nitrogen, at a temperature comprised between 300° C. and 400° C., before the fluorination step. This limits the development of water during the reaction, which is undesirable especially because it favours the equipment corrosion.
- The aliminas containing silica are prepared with known methods in the art, for instance by spray-drying of suitable precursors.
- The aluminas containing silica which are preferably used according to the present invention are for instance commercial products of Condea Chemie (Germany).
- Aluminas, aluminas containing silica and aluminum fluorides are characterized by techniques well known to the skilled in the art of the solid characterization: the surface area (SA) is measured by nitrogen adsorption according to the BET method; the pore volume is measured by mercury injection at high pressure; the crystalline phases by X ray diffraction; the constituent analyses are carried out by wet way according to known methods, or by X ray fluorescence by comparison with standards prepared on the same matrix by calibrated additions.
- AlF3 obtained according to the process of the present invention generally is mainly formed by gamma phase as described in FR 1,383,927.
- Some examples are reported for illustrative purposes, the variations which can be introduced without deviating from the scope of the invention are easily accessible to the skilled in the art.
- Use of an alumina free from silica
- A sample of an alumina free from silica (commercial product CONDEA PURAL® SCC-10) is calcined in air flow at 360° C.; after the calcination it results to have:
- SA=275 m2/g
- Vp=0.402 cm3/g
- Z crystalline structure: pseudo-bohemite.
- 370 g of this alumina are introduced in an Inconel 600® tubular reactor, having a 50 mm diameter, electrically heated and equipped with porous septum at the base, and fluorinated at 360° C. with an air/HF mixture for 30 hours at the temperature of 360° C.; at steady conditions the mixture composition is 0.85 mole/h of HF, 4 mole of air.
- The reactor is cooled under air flow and about 510 g of aluminum fluoride are discharged having the following characteristics:
- SA=19.8 m2/g
- Vp=0.19 cm3/g
- crystalline structure: γ-AlF3
- Use of an alumina CONDEA SIRAL® 1.5 containing 1.5% of silica
- An alumina containing 1.5% of silica (% by weight of the anhydrous product) is calcined and characterized as described in the preceding Example. It results to have:
- SA=305 m2/g
- Vp=0.442 cm3/g
- DRX: pseudo-bohemite.
- 370 g of this alumina are fluorinated as described in the preceding Example: about 510 g of AlF3 are obtained with the following characteristics:
- SA=34.5 m2/g
- Vp=0.26 cm3/g
- crytalline structure: γ-AlF3 with a little of α-AlF3.
- Use of an alumina CONDEA SIRAL® 5 containing 5.4% of silica
- After calcination the alumina results to have:
- SA=295 m2/g
- Vp=0.499 cm3/g
- DRX: pseudo-bohemite.
- 370 g of this alumina are fluorinated as described in the preceding Example: about 530 g of AlF3 are obtained with the following characteristics:
- SA=43.0 m2/g
- Vp=0.35 cm3/g
- crystalline structure: γ-ALF3 with a little of α- and β-AlF3. It is evident in Examples 2 and 3, the increase of SA and Vp with respect to the comparative Example, although the starting aluminas differed not very much from each other in the chemical-physical characteristics.
- From the comparison of the Examples it can be noted that both the surface area and the pore volume of the obtained AlF3 are always higher when an alumina containing silica according to the present invention is used.
Claims (10)
1. A process for preparing aluminum fluoride having an high surface area and high pore volume comprising the fluorination with HF in gas phase of alumina having a surface area of at least 150 m2/g and pore volume not lower than 0.3 cc/g, said alumina comprising from about 0.5 up to about 15% by weight of silicon oxide.
2. Process for preparing aluminum fluoride according to , wherein the amount of silicon oxide is comprised between 1 and 10% by weight.
claim 1
3. Process for preparing aluminum fluoride according to claims 1 and 2, wherein the aluminum fluoride has a fluorine content not lower than 90%.
4. Process for preparing aluminum fluoride according to , wherein the fluorine content is not lower than 95%.
claim 3
5. Process for preparing aluminum fluoride according to claims from 1 to 4, wherein the fluorination of the alumina containing silica is carried out at a temperature between about 250° C. and about 450° C., preferably higher than 300°-400°C.
6. Process for preparing aluminum fluoride according to claims from 1 to 5, wherein the partial pressure of HF is comprised between 0.1 and 0.5.
7. Process for preparing aluminum fluoride according to , wherein HF diluted with a gas inert under fluorination conditions, preferably air or nitrogen, is used.
claim 6
8. Process for preparing aluminum fluoride according to claims from 1 to 7, wherein the fluorination reaction is carried out in fluidized bed.
9. Aluminum fluoride obtainable with the process according to claims from 1 to 8, wherein AlF3 has generally a surface area not lower than 25 m2/g, preferably not lower than 30 m2/g and a pore volume not lower than 0.20 cc/g, preferably 0.25 cc/g.
10. Aluminum fluoride according to , wherein AlF3 is mainly formed by the gamma phase.
claim 9
Priority Applications (1)
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US09/740,963 US20010038819A1 (en) | 1997-05-22 | 2000-12-21 | Process for the preparation of aluminum fluoride |
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ITMI97A001195 | 1997-05-22 | ||
IT97MI001195A IT1291758B1 (en) | 1997-05-22 | 1997-05-22 | PROCESS FOR THE PREPARATION OF ALUMINUM FLUORIDE |
US09/081,294 US6187280B1 (en) | 1997-05-22 | 1998-05-20 | Process for the preparation of aluminum fluoride |
US09/740,963 US20010038819A1 (en) | 1997-05-22 | 2000-12-21 | Process for the preparation of aluminum fluoride |
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US09/081,294 Division US6187280B1 (en) | 1997-05-22 | 1998-05-20 | Process for the preparation of aluminum fluoride |
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US09/740,963 Abandoned US20010038819A1 (en) | 1997-05-22 | 2000-12-21 | Process for the preparation of aluminum fluoride |
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US (2) | US6187280B1 (en) |
EP (1) | EP0879790B1 (en) |
JP (1) | JP4324257B2 (en) |
DE (1) | DE69832325D1 (en) |
IT (1) | IT1291758B1 (en) |
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IT1303073B1 (en) * | 1998-05-07 | 2000-10-23 | Ausimont Spa | PROCESS FOR THE PREPARATION OF ALUMINUM FLUORIDE |
IT1307755B1 (en) | 1999-02-05 | 2001-11-19 | Ausimont Spa | DIMERIZATION PROCESS OF (CFC-113A). |
ITMI20010287A1 (en) | 2001-02-13 | 2002-08-13 | Ausimont Spa | PROCEDURE FOR OBTAINING CFC 113A FROM CFC 113 |
US7316838B2 (en) * | 2001-02-15 | 2008-01-08 | Integral Technologies, Inc. | Low cost electrically conductive carpeting manufactured from conductive loaded resin-based materials |
US7485598B2 (en) * | 2006-06-21 | 2009-02-03 | Arkema Inc. | High pressure catalyst activation method and catalyst produced thereby |
AU2003294000A1 (en) * | 2003-01-03 | 2004-07-29 | Solvay Solexis S.P.A. | Aluminium fluoride |
EP1502906A1 (en) * | 2003-07-31 | 2005-02-02 | Solvay Solexis S.p.A. | Process for activation of AIF3 based catalysts and process for isomerising hydrochlorofluorocarbons |
EP2172441A1 (en) | 2008-10-02 | 2010-04-07 | Solvay Fluor GmbH | Process for the manufacture of hydrochlorofluorocarbons using trifluoromethane as fluorinating agent |
BRPI1008131A2 (en) * | 2009-02-27 | 2016-03-08 | Applied Nanostructured Sols | "low temperature carbon nanotube growth using gas preheat method". |
CN106277004A (en) * | 2015-06-23 | 2017-01-04 | 中南大学 | The preparation method of two kinds of high catalytic activity aluminium fluoride and the application in perfluor halogenated hydrocarbons synthesizes |
CN112042018B (en) * | 2018-03-27 | 2023-11-07 | 本田技研工业株式会社 | Negative electrode active material for fluoride ion secondary battery, negative electrode using same, fluoride ion secondary battery, and method for producing same |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1209223A (en) * | 1958-07-03 | 1960-02-29 | Pechiney | Process for recovering hydrofluoric gas by alumina |
GB1000485A (en) | 1962-02-07 | 1965-08-04 | Sicedison Spa | Improvements in or relating to the fluorination of halo-olefines |
GB1026131A (en) * | 1962-02-16 | 1966-04-14 | Imp Smelting Corp Ltd | Improvements in or relating to the production of aluminium fluoride |
DE1224732B (en) | 1962-11-08 | 1966-09-15 | Du Pont | Process for the production of vinyl fluoride and 1,1-difluoroethane |
US3473887A (en) * | 1968-02-21 | 1969-10-21 | Allied Chem | Aluminum fluoride production |
JPS4823797B1 (en) * | 1968-08-14 | 1973-07-16 | ||
NL7100858A (en) * | 1970-01-27 | 1971-07-29 | ||
GB1290749A (en) * | 1970-05-04 | 1972-09-27 | ||
JPS5033992B1 (en) * | 1970-12-23 | 1975-11-05 | ||
DE2106306C3 (en) * | 1971-02-10 | 1974-12-19 | Metallgesellschaft Ag, 6000 Frankfurt | Process for the production of aluminum fluoride |
US4275046A (en) * | 1978-01-16 | 1981-06-23 | Exxon Research & Engineering Co. | Preparation of high surface area metal fluorides and metal oxyfluorides, especially aluminum fluoride extrudates |
FR2590251B1 (en) * | 1985-11-15 | 1988-10-14 | Atochem | PROCESS FOR THE SYNTHESIS OF CHLOROPENTAFLUOROETHANE FROM DICHLOROTETRAFLUOROETHANE AND FLUORHYDRIC ACID |
IT1202652B (en) | 1987-03-09 | 1989-02-09 | Ausimont Spa | PROCESS FOR THE PREPARATION OF 1,1,1-TRIFLUORO-2,2-DICHLOROETHANE BY HYDROFLUORATION IN THE PRESENCE OF CATALYSTS |
US4754084A (en) * | 1987-04-01 | 1988-06-28 | E. I. Du Pont De Nemours And Company | Preparation of substituted fluorobenzenes |
US5008475A (en) | 1987-07-07 | 1991-04-16 | E. I. Du Pont De Nemours And Company | Gas-phase fluorination process |
JPH02116618A (en) * | 1988-10-26 | 1990-05-01 | Central Glass Co Ltd | Production of aluminum fluoride |
CN1041804C (en) * | 1995-09-13 | 1999-01-27 | 西安近代化学研究所 | Catalyst for fluoreation of halogenated hydrocarbon |
-
1997
- 1997-05-22 IT IT97MI001195A patent/IT1291758B1/en active IP Right Grant
-
1998
- 1998-05-14 EP EP98108740A patent/EP0879790B1/en not_active Expired - Lifetime
- 1998-05-14 DE DE69832325T patent/DE69832325D1/en not_active Expired - Lifetime
- 1998-05-20 JP JP13835098A patent/JP4324257B2/en not_active Expired - Fee Related
- 1998-05-20 US US09/081,294 patent/US6187280B1/en not_active Expired - Fee Related
-
2000
- 2000-12-21 US US09/740,963 patent/US20010038819A1/en not_active Abandoned
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ITMI971195A1 (en) | 1998-11-22 |
EP0879790A1 (en) | 1998-11-25 |
JPH1111940A (en) | 1999-01-19 |
DE69832325D1 (en) | 2005-12-22 |
JP4324257B2 (en) | 2009-09-02 |
EP0879790B1 (en) | 2005-11-16 |
US6187280B1 (en) | 2001-02-13 |
ITMI971195A0 (en) | 1997-05-22 |
IT1291758B1 (en) | 1999-01-21 |
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