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Dokumentenidentifikation EP1485322 27.12.2007
EP-Veröffentlichungsnummer 0001485322
Titel VERFAHREN ZUR HERSTELLUNG EINES ZSM-5 KATALYSATORS
Anmelder Council of Scientific & Industrial Research, New Delhi, IN
Erfinder KULKARNI, Shivanand Janardan, Hyderabad 500 007 Andhra Pradesch, IN;
NAMA, Narendar, Hyderabad 500 007 Andhra Pradesch, IN;
PAVULURI, Srinivasu, Hyderabad 500 007 Andhra Pradesch, IN;
RAGHAVAN, Kondapuram Vijaja, Hyderabad 500 007 Andhra Pradesch, IN
Vertreter derzeit kein Vertreter bestellt
DE-Aktenzeichen 60223595
Vertragsstaaten AT, BE, CH, CY, DE, DK, ES, FI, FR, GB, GR, IE, IT, LI, LU, MC, NL, PT, SE, TR
Sprache des Dokument EN
EP-Anmeldetag 21.03.2002
EP-Aktenzeichen 027131663
WO-Anmeldetag 21.03.2002
PCT-Aktenzeichen PCT/IN02/00055
WO-Veröffentlichungsnummer 2003080510
WO-Veröffentlichungsdatum 02.10.2003
EP-Offenlegungsdatum 15.12.2004
EP date of grant 14.11.2007
Veröffentlichungstag im Patentblatt 27.12.2007
IPC-Hauptklasse C01B 39/38(2006.01)A, F, I, 20051017, B, H, EP
IPC-Nebenklasse C01B 39/40(2006.01)A, L, I, 20051017, B, H, EP   

Beschreibung[en]
Field of the invention

The present invention relates to an improved process for the preparation of crystalline ZSM-5 pentasil type of zeolite like ZSM-5 (Zeolite Socony Mobil-5), which are useful in acid catalyzed reactions.

Background of the invention

The synthesis of ZSM-5 is reported in US Patent 3702886 (1972 ). In the presently known processes ZSM-5 was synthesized from a mixture of alkali metal cation, especially sodium, tetra alkyl ammonium cation, aluminum source like sodium aluminate, silica source like sodium silicate and water in the pH range of 6.7 to 13.0, the autoclavation temperature of 120°- 200°C under autogeneous pressure. The ZSM-5 material showed characteristic X-ray diffraction pattern The ZSM-5 catalyst was initially prepared within eight days, typically at 150°C for six days. There are various attempts to reduce the time of the autoclavation from six days to two days by seeding gel method ( Microporous Materials 22, 626-627 (1998) . The attempts have been made to reduce the autoclavation time by using anionic promoters like H3PO4 (Nature, 381,298 (1996)) and by varying ratios of various precursors (Zeolites 12, 943 (1992)). Many other patents have been reported in the literature. These methods have some limitations and cannot be commercialized. The limitations are (1) X-ray crystalline purity, (2) crystalline phase purity (3) the promoter cation enters into tetrahedral position like the arsenate promoter leads to arsanate-silicalite with different catalytic properties. (4) The definite Si/A1 ratio in the gel and the product (5) product yield.

Objects of the invention

Accordingly it is an object of the invention to provide a process for the preparation of ZSM-5 catalyst which is commercially feasible.

It is another object of the invention, to provide a process for the preparation of ZSM-5 catalyst which shows high X-ray and crystalline phase purity and specific Si/Al ratios.

It is a further object of the invention to provide a process for the preparation of ZSM-5 catalyst which provides a high product yield in short autoclavation time.

Summary of the invention

The present invention relates to the improved synthesis of uniform porous, crystalline zeolitic material similar to ZSM-5 a member of pentasil family. ZSM-5 has a characteristic X-ray diffraction pattern The typical chemical composition of ZSM-5 may be represented as 3.25 Na2O: Al2O3: 30 SiO2: ∼958 H2O.

Accordingly the present invention provides an improved process for the preparation of ZSM-5 catalyst of the formula 3.25 Na2O. Al2O3.30SiO2.zH2O where z = 15-20 water molecules per unit cell, and XRD pattern as given in Table 1 below comprising autoclaving a mixture of a pre-prepared seeding gel comprising a mixture of a alkali metal cation, an alkali hydroxide, and a silica source in water, and further amounts of silica source and an aluminium source in the presence of an organic solvent near or above the super critical conditions of temperature and pressure for the said organic solvent.

In one embodiment of the invention, the alkali metal cation comprises sodium tetraalkyl ammonium cation.

In a further embodiment of the invention, the silica source comprises tetraethoxysilane.

In another embodiment of the invention, the aluminium source is sodium aluinate.

In one embodiment of the invention, the organic solvent used is selected from the group consisting of methanol, acetone, isopropanol, acetonitrile and ethanoL

In another embodiment of the invention, water is used as a co-solvent along with the organic solvent.

In a further embodiment of the invention, the autoclavation temperature is varied from 150 to 250°C, preferably under supercritical temperature of organic solvent.

In yet another embodiment of the invention, the autoclavation pressure is varied from 20 to 50 atm near to sub-critical and supercritical pressure of the organic solvent used.

In another embodiment of the invention, the Si/Al atomic ratio in the seeding gel is varied thereby controlling the Si/Al atomic ratio in the as synthesized ZSM-5.

In a preferred embodiment the Si/Al ratio can be varied in the range of 10 to 60. ZSM-5 is highly thermally stable. The organic template was removed by heating as-synthesized ZSM-5 at 550°C for 12-16 hours.

Detailed description of the invention

The seeding gel was used in the initial geL The seeding gel was typically prepared as follows: 0.6 g (0.01725 mole) of sodium hydroxide was dissolved in 71.028 ml (3.946 mole) of distilled water. 27.7M1 (0.02875 mole) of tetrapropylammonium hydroxide was added dropwise to NaOH solution with stirring. The mixture was stirred for 30 min. Then 27.5 ml (0.1322 mole) of tetraethoxysilane was added dropwise. The total mixture was stirred at 100°C for about 16 h. This mixture was used as seeding gel. The ZSM-5 was synthesized as follows: Sodium hydroxide of 0.88 g (o.22 mole) was dissolved in distilled water. Sodium aluminate of 1.05 g (0.0128 mole) and 196 ml (4.841 mole) of methanol as a solvent were added and the mixture was stirred for 30 min. Tetraethoxysilane of 41.9 ml (0.1882 mole) was added dropwise and stirred for an hour. Finally 15 g of the seeding gel was added and the mixture was stirred for 1 h. The initial pH of the mixture was 10.2-11.0. The total mixture was put into 600 ml Parr autoclave and stirred at 230°-250°C for 4-10 h. The solid product was filtered, washed with distilled water and dried at 100-110°C for 6 h.

The organic template was removed by calcining at 550°C for 12 h. The typical XRD pattern is given in Table 1. The ZSM-5 catalysts were synthesized with the autoclavation temperature 230-250°C and the autoclavation time 4, 6 and 10 h and the XRD patterns are given in Table 1, Table 2 and Table 3 respectively. The experimental conditions for the synthesis of ZSM-5 with various solvents and high pressure conditions are given in Table 4. The experimental conditions corresponding to the synthesis of ZSM-5 catalysts at various autoclavation temperatures are given in Table 5.

EXAMPLE 1:

This example 1 illustrates the synthesis of ZSM-5 using methanol and water as solvents. Sodium hydroxide of 0.88 g (0.22 mole), 1.05 g of sodium aluminate, 41.9 ml (0.1882 mole) of tetraethoxy silane, 196 ml (4.841 mole) of methanol and 15 g seeding gel as described earlier containing TPAOH were mixed thoroughly. The initial pH of mixture was ~10.2. The gel composition was as follows, (SiO2)29.4: (Al2O3)1: (Template)0.5: (H2O)260. The mixture was put in the Parr autoclave and heated at 242°C for 4 h. Then the solid material was filtered, washed thoroughly and dried at 100-110°C for 6 h. The organic template was removed by calcining at 550°C for ~12 h. The XRD pattern is as given in Table 1. The crystallinity was > 95%. The BET surface area was 361 m2.g-1.

EXAMPLE 2:

The synthesis of ZSM-5 was carried out as discussed in Example 1, except that methanol is replaced by acetone as a solvent. The autoclavation was carried out at 230°C and 47 atm autogeneous pressure for 10 h. The crystallinity was ~74% and the BET-N2-surface area was 364 m2.g-1. The XRD pattern of this catalyst is given in Table 6.

EXAMPLE 3:

The synthesis of ZSM-5 was carried out as discussed in Example 1 except that methanol was replaced by isopropanol as a solvent. The autoclavation was carried out at 230°C and 48 atm autogeneous pressure for 10 h. The crystallinity was ~ 71% and the N2 BET surface area was 346 m2.g-1. The XRD pattern of this catalyst is given in Table 7.

EXAMPLE 4:

The synthesis of ZSM-5 was carried out as discussed in Example 1 except that methanol was replaced by ethanol as a solvent. The autoclavation was carried out at 233°C and 50 atm autogeneous pressure for 10 h. The crystallinity was ~53% and BET surface area using nitrogen was 343 m2.g-1.The XRD pattern of this catalyst is given in Table 8.

EXAMPLE 5: COMPARATIVE:

The synthesis of ZSM-5 was carried out as discussed in Example 1 except that methanol was replaced by water as the only solvent. The autoclavation was carried out at 260°C and 47 atm autogeneous pressure for 10 h. The crystallinity of the zeolite was ~83% and BET surface area using nitrogen was 379 m2 g-1. The XRD pattern of this ZSM-5 catalyst is given in Table 9.

EXAMPLE 6:

The synthesis of ZSM-5 was carried out as discussed in Example 1 except that the autoclavation was carried out at 200°C and 39 atm autogeneous pressure for 4 h, The crystallinity of the zeolite was ~94% and BET surface area using nitrogen was 358 m2.g-1. The XRD pattern of this ZSM-5 catalyst is given in Table 10. Table 1: XRD pattern of ZSM-5 catalyst (solvent=CH<sub>3</sub>OH, autoclavation time=4h) d, Interplane spacing Intensity ratio 11.290 51.9 10.090 34.0 7.500 7.0 6.763 5.1 6.397 10.3 6.042 12.1 5.746 6.1 5.594 6.9 5.020 5.2 4.633 6.9 4.277 9.5 4.022 7.3 3.854 100.0 3..741 39.4 3.658 23.5 3.453 9.3 3.356 10.6 3.060 8.4 2.993 13.5 2.742 5.6 2.687 6.1 2.687 7.4 2.492 8.8 2.408 5.6
Table 2: XRD pattern of ZSM-5 (solvent= methanol, autoclavation time= 6 h) d, Interplaner spacing Intensity ratio 23.47 15.1 19.25 18.3 13.76 14.3 11.30 58.3 10.08 46.5 9.05 9.0 7.49 11.6 7.13 11.1 6.74 11.3 6.41 20.6 6.03 20.1 5.60 42.2 5.38 11.3 5.02 12.0 4.62 14.9 4.27 43.8 4.0 17.5 3.85 100.0 3.74 84.5 3.66 66.2 3.43 43.5 3.35 31.8 3.15 5.5 3.06 10.0 2.98 12.8 2.92 8.3 2.79 4.6 2.68 7.3 2.60 4.5 2.50 6.2 2.46 7.3 2.4 10.1
Table 3: XRD pattern of ZSM-5 (solvent= methanol, autoclavation time= 10 h) d, Interplaner spacing Intensity ratio 13.99 1.3 11.53 84.2 10.29 44.8 7.589 6.8 6.828 7.3 6.479 13.7 6.102 20.2 5.807 7.8 5.668 7.9 5.457 6.7 5.065 9.6 4.678 5.4 4.423 7.0 4.309 10.8 4.079 7.1 3.890 100.0 3.775 55.4 3.683 30.3 3.471 15.0 3.166 10.1 3.076 11.5 3.007 20.3 2.756 8.2 2.622 9.5 2.418 7.0 2.338 6.3

The experimental conditions for the synthesis of ZSM-5 are given the Table 4. Table 4: Synthesis of ZSM-5 with various solvents and under high pressure conditions. Entry Solvent Gel Composition Autoclavation Temperature (°C) Autogeneous Pressure (atm) Time (h) Initial pH Final pH Surface area (m2.g-1) % Crystallinity (Si/Al) atomic zeolite 1 Methanol R. (CH3OH)756 242 50 4 10.2 11.6 361 95.0 27.25 242 49 6 10.2 11.6 351 83.0 -- 242 50 10 10.1 11.8 387 92.0 -- 2 Acetone R. (CH3COCH3)417 230 47 10 10.2 11.3 364 74.0 17.10 3 Isopropanol R. ((CH3)2CHOH)400 230 48 10 10.3 11.4 346 71.0 17.63 4 Ethanol R. (CH3CH2OH)525 233 50 10 10.3 11.6 343 53.0 17.63 5 Acetonitrile R. (CH3CN)586 265 50 10 10.0 11.2 333 -- 16.43 6 Water R (H2O)1701 260 47 10 10.4 11.6 379 83.0 13.85 R = (SiO2)29.4, (Al2O3)1, (Templ)0.5. (H2O)260

The autoclavation temperature and corresponding pressure was varied and given in Table 5. Table 5: Synthesis of ZSM-5<sup>a</sup>: Effect of Temperature Entry Autoclavation Temperature (°C) Autogeneous Pressure (atm) Gel Composition Time (h) Initial pH Final pH Surface area (m2.g-1) % Crystallinity 1. 242 50 R. (CH3OH)756 4 10.2 11.6 361 95.0 2. 200 39 " 4 10.1 11.2 358 94.0 3. 180 34 " 4 9.9 11.0 342 95.0 4. 150 27 " 4 9.8 11.1 347 61.0 a: Methanol used as a solvent

R= (SiO2)29.4. (Al2O3)1. (Templ)0.5. (H2O)260
Table 6: XRD pattern of ZSM-5 (solvent= acetone, autoclavation time =10 h) d, Interplaner spacing Intensity ratio 11.18 51.9 10.01 39.3 7.423 8.6 6.390 16.9 6.011 15.4 5.571 15.1 5.365 11.6 4.596 9.2 4.264 29.0 4.039 21.9 3.852 100.0 3.728 64.9 3.649 27.5 3.346 68.7 3.051 13.9 2.982 17.6 2.848 13.2 2.748 9.2 2.489 4.7 2.398 16.0
Table 7: XRD pattern of ZSM-5 (solvent= isopropanol, autoclavation time= 10 h) d, Interplaner spacing Intensity ratio 28.12 9.3 22.59 6.9 17.96 5.8 13.66 5.4 11.06 63.3 9.869 37.7 8.812 6.7 7.414 6.4 6.666 5.6 6.325 5.2 5.946 12.8 5.675 11.3 5.557 7.4 5.334 5.7 4.978 11.7 4.591 8.7 4.352 7.4 4.240 33.2 4.022 12.2 3.830 100.0 3.714 50.2 3.630 25.5 3.468 7.4 3.424 9.7 3.332 72.4 3.321 6.1 3.126 4.3 3.044 11.2 2.971 14.6 2.863 6.9 2.729 5.2 2.669 5.1 2.568 5.6 2.453 11.6 2.276 9.3
Table 8: XRD pattern of ZSM-5 catalyst (solvent= ethanol, autoclavation time= 10 h) d, Interplaner spacing Intensity ratio 11.12 49.4 9.936 37.8 6.369 16.5 5.991 17.8 5.616 15.8 4.999 9.9 4.592 11.2 4.253 44.2 4.035 98.2 3.836 100.0 3.723 55.2 3.630 25.3 3.454 9.3 3.341 65.1 3.138 16.9 3.049 15.2 2.978 26.2 2.848 17.8 2.742 11.4 2.478 18.5
Table 9: XRD pattern of ZSM-5 catalyst (solvent= water, autoclavation time= 10 h) d, Interplaner spacing Intensity ratio 11.48 73.1 10.26 55.6 9.186 6.9 7.605 6.3 6.805 7.2 6.476 11.7 6.074 14.7 5.657 14.9 5.425 8.8 5.055 9.1 4.658 9.3 4.307 12.5 4.042 7.6 3.883 100.0 3.762 50.6 3.683 28.3 3.480 10.7 3.362 16.7 3.075 16.4 3.002 15.5 2.877 7.6 2.757 8.2 2.506 9.6 2.418 7.7 2.300 5.8 2.016 13.1 1.917 6.4 1.817 7.0
Table 10: XRD pattern of ZSM-5 catalyst (solvent= methanol, autoclavation temperature= 200°C) d, Interplaner spacing Intensity ratio 32.51 4.9 21.67 5.2 16.15 5.1 11.52 66.0 10.31 43.4 9.209 4.9 7.605 10.5 7.234 9.6 6.862 8.2 6.495 8.3 6.097 20.0 5.815 8.2 5.656 17.8 4.668 7.9 4.413 7.2 4.318 9.3 4.055 6.8 3.880 100.0 3.793 28.3 3.756 55.5 3.689 33.4 3.467 8.5 3.339 8.2 3.000 9.7 3.005 12.1 2.629 9.6


Anspruch[de]
Verfahren zur Herstellung eines ZSM-5 Katalysators mit der Formel 3,25 Na2O·Al2O3·30SiO2·zH2O, in welcher z = 15-20 Wassermoleküle pro Einheitszelle darstellen, wobei das Verfahren eine Autoklavbehandlung einer Mischung aus einem vorher zubereiteten Keimgel aufweist, welch letzteres eine Mischung umfasst aus einem Alkalimetallkation, einem Alkalihydroxid, und einer Kieselerdequelle in Wasser, und weiteren Mengen an Kieselsäurequelle und an Aluminiumquelle in Anwesenheit eines organischen Lösungsmittels in der Nähe oder oberhalb der superkritischen Bedingungen von Temperatur und Druck für das organische Lösungsmittel. Verfahren gemäß Anspruch 1, bei welchem der ZSM-5 Katalysator ein XRD Muster aufweist, welches in der nachfolgenden Tabelle dargelegt wird: D, Netzebenenabstände Intensitätsverhältnis 11,290 51,9 10,090 34,0 7,500 7,0 6,763 5,1 6,397 10,3 6,042 12,1 5,746 6,1 5,594 6,9 5,020 5,2 4,633 6,9 4,277 9,5 4,022 7,3 3,854 100,0 3,741 39,4 3,658 23,5 3,453 9,3 3,356 10,6 3,060 8,4 2,993 13,5 2,742 5,6 2,687 6,1 2,687 7,4 2,492 8,8 2,408 5,6
Verfahren gemäß Anspruch 1, bei welchem das Alkalimetallkation ein Natriumtetraalkylammoniumkation aufweist. Verfahren gemäß Anspruch 1, bei welchem die Kieselerdequelle ein Tetraethoxysilan aufweist. Verfahren gemäß Anspruch 1, bei welchem die Aluminiumquelle ein Natriumaluminat aufweist. Verfahren gemäß Anspruch 1, bei welchem das verwendete organische Lösungsmittel ausgewählt wird aus der Gruppe bestehend aus Methanol, Aceton, Isopropanol, Acetonitril und Ethanol. Verfahren gemäß Anspruch 1, bei welchem Wasser zusammen mit dem organischen Lösungsmittel als ein Co-Lösungsmittel verwendet wird. Verfahren gemäß Anspruch 1, bei welchem die Temperatur der Autoklavbehandlung von 150 bis 250 °C variiert, vorzugsweise unterhalb der superkritischen Temperatur eines organischen Lösungsmittels. Verfahren gemäß Anspruch 1, bei welchem der Druck der Autoklavbehandlung von 20 bis 50 atm (2,03 bis 5,07 MPa) variiert. Verfahren gemäß Anspruch 1, bei welchem das Si/Al Atomverhältnis in dem Keimgel variiert wird, wodurch das Si/A1 Atomverhältnis gesteuert wird in dem ZSM-5, so wie es synthetisiert worden ist. Verfahren gemäß Anspruch 1, bei welchem das Si/Al Atomverhältnis in dem Keimgel in dem Bereich von 10 bis 60 variiert wird. Verfahren gemäß Anspruch 1, bei welchem die organische Matrix entfernt wird durch ein Erhitzen des ZSM-5, so wie es synthetisiert worden ist, bei 550 °C während einer Zeitdauer von 12-16 Stunden.
Anspruch[en]
A process for the preparation of ZSM-5 catalyst of the formula 3.25 Na20. Al2O3.3OSiO2.zH2O where z = 15-20 water molecules per unit cell comprising autoclaving a mixture of a pre-prepared seeding gel comprising a mixture of an alkali metal cation, an alkali hydroxide, and a silica source in water, and further amounts of silica source and an aluminium source in the presence of an organic solvent near or above the super critical conditions of temperature and pressure for the said organic solvent. A process as claimed in claim 1 wherein the ZSM - 5 catalyst has an XRD pattern given in the table below: D, Interplaner spacing Intensity ratio 11.290 51.9 10.090 34.0 7.500 7.0 6.763 5.1 6.397 10.3 6.042 12.1 5.746 6.1 5.594 6.9 5.020 5.2 4.633 6.9 4.277 9.5 4.022 7.3 3.854 100.0 3.741 39.4 3.658 23.5 3.453 9.3 3.356 10.6 3.060 8.4 2.993 13.5 2.742 5.6 2.687 6.1 2.687 7.4 2.492 8.8 2.408 5.6
A process as claimed in claim 1 wherein the alkali metal cation comprises sodium tetraalkyl ammonium cation. A process as claimed in claim 1 wherein the silica source comprises tetraethoxysilane. A process as claimed in claim 1 wherein the aluminium source comprises sodium aluminate. A process as claimed in claim 1 wherein the organic solvent used is selected from the group consisting of methanol, acetone, isopropanol, acetonitrile and ethanol. A process as claimed in claim 1 wherein water is used as a co-solvent along with the organic solvent. A process as claimed in claim 1 wherein the autoclavation temperature is varied from 150 to 250°C, preferably under supercritical temperature of organic solvent. A process as claimed in claim 1 wherein the autoclavation pressure is varied from 20 to 50 atm (2.03 to 5.07 MPa). A process as claimed in claim 1 wherein the Si/A1 atomic ratio in the seeding gel is varied thereby controlling the Si/Al atomic ratio in the as synthesized ZSM-5. A process as claimed in claim 1 wherein the Si/Al atomic ratio in the seeding gel is varied in the range of 10 to 60. A process as claimed in claim 1 wherein the organic template is removed by heating as-synthesized ZSM-5 at 550°C for 12-16 hours.
Anspruch[fr]
Procédé pour la préparation du catalyseur ZSM-5 de la formule 3,25Na2O·Al2O3·30SiO2·zH2O où z = 15-20 molécules d'eau par cellule élémentaire comprenant le passage à l'autoclave d'un mélange d'un gel d'ensemencement pré-préparé comprenant un mélange d'un cation de métal alcalin, d'un hydroxyde alcalin et d'une source de silice dans de l'eau, et d'autres quantités de source de silice et d'une source d'aluminium en présence d'un solvant organique près ou au-dessus des conditions supercritiques de température et de pression pour ledit solvant organique. Procédé suivant la revendication 1, dans lequel le catalyseur ZSM-5 possède un diagramme XRD donné dans le tableau ci-dessous: D, espacement interplanaire Rapport d'intensité 11,290 51,9 10,090 34,0 7,500 7,0 6,763 5,1 6,397 10,3 6,042 12,1 5,746 6,1 5,594 6,9 5,020 5,2 4,633 6,9 4,277 9,5 4,022 7,3 3,854 100,0 3,741 39,4 3,658 23,5 3,453 9,3 3,356 10,6 3,060 8,4 2,993 13,5 2,742 5,6 2,687 6,1 2,687 7,4 2,492 8,8 2,408 5,6
Procédé suivant la revendication 1, dans lequel le cation de métal alcalin comprend un cation de tétraalkylammonium de sodium. Procédé suivant la revendication 1, dans lequel la source de silice comprend un tétraéthoxysilane. Procédé suivant la revendication 1, dans lequel la source d'aluminium comprend un aluminate de sodium. Procédé suivant la revendication 1, dans lequel le solvant organique utilisé est choisi dans le groupe constitué de méthanol, d'acétone, d'isopropanol, d'acétonitrile et d'éthanol. Procédé suivant la revendication 1, dans lequel l'eau est utilisée comme un co-solvant accompagné du solvant organique. Procédé suivant la revendication 1, dans lequel la température du passage à l'autoclave est variée de 150 à 250°C, de préférence en dessous de la température supercritique du solvant organique. Procédé suivant la revendication 1, dans lequel la pression du passage à l'autoclave est variée de 20 à 50 atm (de 2,03 à 5,07 MPa). Procédé suivant la revendication 1, dans lequel le rapport atomique de Si/Al dans le gel d'ensemencement est varié, régulant ainsi le rapport atomique de Si/Al dans ZSM-5 tel que synthétisé. Procédé suivant la revendication 1, dans lequel le rapport atomique de Si/Al dans le gel d'ensemencement est varié dans l'intervalle de 10 à 60. Procédé suivant la revendication 1, dans lequel la matrice organique est retirée en chauffant ZSM-5 tel que synthétisé à 550°C pendant 12-16 heures.






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