PROCESS FOR PREPARING A LARGE PORE MOLECULAR SIEVE

Abstract: The present invention relates to a process for the preparation of a large-pore molecular sieve, comprising crystallising the molecular sieve from a starting mixture at a pH in the range of from 3 to 8, and recovering a large-pore molecular sieve, the said starting mixture having a molar composition satisfying the following molar ratios: (0.01 - 2) R2/nO) : (0 - 1.5) M2/mO : (0 - 0.5) X2O3 : 1 YO2 : (5 - 1,000) H2O : (0.01 - 3) F<->, wherein n and m are the weighted average valences of R and M respectively, M is an alkali- or alkaline-earth metal, X is a trivalent metal and Y is a tetravalent element, wherein R comprises at least one main organic template Rm having the formula R1R2R3R4Q<+> wherein Q is nitrogen or phosphorus and wherein at least one and at most three of R1, R2, R3 and R4 is an aryl or alkyl group having 6 to 36 carbon atoms and each of the remainder of R1, R2, R3 and R4 is selected from hydrogen and an alkyl group having 1 to 5 carbon atoms. The invention further relates to a calcined large-pore molecular sieve and its use.

Description: PROCESS FOR PREPARING A LARGE PORE MOLECULAR SIEVE The present invention relates to a process for preparing a large pore molecular sieve. In particular, the present invention relates to a process for preparing a molecular sieve containing pores having diameters of at least 1.3 nm. Such molecular sieves are known in the art. International Application Publication No. WO 93/01884 (WO 93/01884) discloses a hydroprocessing catalyst containing a support material comprising an ultra-large pore crystalline material (molecular sieve) of high surface area and porosity. The crystalline material exhibits after calcination an X-ray diffraction pattern with at least one peak having a relative intensity of 100 at a d-spacing greater than 1.8 nm and having a benzene sorption capacity greater than 15 grams benzene per 100 grams of the material at 6.7 kPa and 25 β C. The crystalline material is typically prepared by crystallisation from a starting mixture at strong basic conditions, that is a pH in the range of from 9 to 14. In particular, if the starting mixture does not contain bivalent or pentavalent species it is stated that it is essential to maintain the pH within this range in three out of four synthesis procedures disclosed in WO 93/01884. The fourth synthesis procedure disclosed in WO 93/01884 should be carried out at a pH of less than 12. In this fourth procedure the same synthesis mixture is to be employed as disclosed with respect to the third synthesis procedure. The lower limit of the pH range which can be used in the fourth procedure is therefore about 9. Beck et al. (J. Am. Chem Soc. 1992, Vol. 114, pages 10834- 10843) discuss the influence of organic templates on the structure and properties of the crystalline material and propose two theoretical models for formation of the crystalline material. Monnier et al. (Science 1993, Vol. 261, pages 1299-1303) synthesized the crystalline materials at a range of experimental conditions and on the basis of the known experimental results developed a refined model of the formation process which could explain the then known experimental data and which could predict conditions needed for the synthesis of desired structures. According to this publication a pH of at least 9.5 seems essential in order to be able to directly synthesize the crystalline materials. According to Monnier et al. the crystal structure of a monoclinic, layered crystalline material produced in the initial stages of the synthesis process at a pH of at least 9.5 can be altered to a hexagonal crystalline material by a hydrothermal treatment at 373 K at a pH of 7 over 10 days. It has now been found possible to directly synthesize crystalline material, hereinafter called molecular sieves, as described in WO 93/01884 under acidic, neutral or weak basic conditions, by using starting mixtures containing a fluorine source. Accordingly, the present invention relates to a process for the preparation of a large-pore molecular sieve, comprising crystallising the molecular sieve from a starting mixture at a pH in the range of from 3 to 8, and recovering a large-pore molecular sieve, the said starting mixture having a molar composition satisfying the following molar ratio's: ( 0.01 - 2 ) 2 n°> : ( ° _ 1 - 5) M 2/m° : <° " °- 5 > x 2°3 : 1 γo 2 : (5 - 1000) H 2 0 : (0.01 - 3) F " , wherein n and m are the weighted average valences of R and M respectively, M is an alkali- or alkaline earth metal, X is a trivalent metal and Y is a tetravalent element, wherein R comprises at least one main organic template R^ having the formula R^ 2R3R4Q + wherein Q is nitrogen or phosphorus and wherein at least one and at most three of lf R 2 , 3 and R is an aryl or alkyl group having 6 to 36 carbon atoms and each of the remainder of R j _, R 2 , R3 and 4 is selected from hydrogen and an alkyl group having 1 to 5 carbon atoms. The compound from which the above ammonium or phosphonium ion is derived may be, for example, the hydroxide, halide, silicate or mixtures thereof. It will be appreciated that in the starting mixture electroneutrality is preserved. Accordingly, both R / n O and M 2 / n O as well as any other ingredient of the starting mixture may be present in the starting mixture in an ionic form. A disadvantage of the preparation methods under strong basic conditions is that the starting mixture does not contain sufficient H + to act as counter-ion for A10 2 ~ in the molecular sieve crystal lattice. Thus, the starting mixture normally contains alkali- or alkaline earth metal compounds to act as counter-ion. Alkali- or alkaline earth metal compounds-containing molecular sieves are usually not desired as such molecular sieves are hardly acidic, if at all. Thus, normally the alkali- or alkaline earth metal compounds-containing molecular sieves are first calcined or extracted to remove organic template(s), then ion-exchanged with an aqueous ammonium solution to remove alkali- or alkaline earth metal compounds from ion-exchange sites of the molecular sieve, and finally calcined to convert NH 4 + in ion-exchange sites to H + , whilst producing NH3 containing gas. It is known in zeolite synthesis to synthesise zeolitic materials in the presence of NH 4 + rather than alkali- or alkaline earth metals. However, at the high pH employed in the experiments described in WO 93/01884, NH 4 + is unstable and converts to NH3. Accordingly, at such high pH NH 4 + cannot normally be used instead of alkali- and/or alkaline earth metal compounds. In theory it is feasible to synthesize crystalline materials at high pH in the absence of any added counter-ion apart from ionic forms of the organic template(s). However, at strong basic conditions this requires excessive amounts of expensive organic template(s) . It would be particularly desirable if large-pore molecular sieves could be produced from a starting mixture containing substantially no, preferably no, alkali- or alkaline earth metal compound(s) . It has now been found possible to synthesize the crystalline material of the present invention in the absence of alkali- or alkaline-earth metal compounds, and in the presence of fluorine, in accordance with the process of the present invention. Accordingly, in a preferred embodiment the present invention relates to a process for preparing a large-pore molecular sieve comprising crystallising the molecular sieve from a starting mixture having a molar composition satisfying the following molar ratio's: (0.01 - 2) R 2 / n O : (0 - 0.5) X 2 0 3 : 1 Y0 2 : (5 - 1000) H 2 0 : (0.01 - 3) F ~ . More preferably the starting mixture has a molar composition satisfying the following molar ratio's: (0.02 - 1) R 2 / n O : (0.0001 - 0.5) X 2 0 3 : 1 Y0 2 : (10 - 900) H 2 0 : (0.05 - 2.5) F " . Preferably, R comprises an additional organic template R a in the form of an ammonium or phosphonium ion of the above formula (R 1 R 2 3 4 Q + ) but wherein each R j _, R 2 , R 3 and R 4 is selected from hydrogen and an alkyl group having 1 to 5 carbon atoms, and wherein 2 alkyl groups can be interconnected to form a cyclic compound. The compound from which the additional organic template ion is derived may be, for example, the hydroxide, halide, silicate or mixtures thereof. The molar ratio additional organic template R a / main organic template R JJ . may typically range from 0.01 to 100. The total of organic template R being used in the starting mixture should however remain within the ranges described herein. Preferably, the R 2 / n 0/(Y0 2 + X 2 0 3 ) molar ratio in the starting mixture is at least 0.1 if R comprises both R j -. and R a . In order to vary the pore size of the molecular sieve, the starting mixture may comprise an auxiliary organic compound R c in addition to the organic templates R, that is R jj . + R a , described hereinabove. Typically, this organic compound is selected from the group of aromatic hydrocarbons and amines having 5 to 20 carbon atoms and halogen- and C^ - C^ alkyl-substituted derivatives thereof; or cyclic and polycyclic aliphatic hydrocarbons and amines of 5 to 20 carbon atoms and halogen- and C^ - C^ 4 alkyl-substituted derivatives thereof; or straight and branched chain aliphatic hydrocarbons and amines having 3 to 16 carbon atoms and hydroxyl or halogen-substituted derivatives thereof. In the auxiliary organic compounds the halogen derivative is preferably a bromine, fluorine or chlorine derivative. The molar ratio auxiliary organic compound R c / ( j -, + R a ) may range from 0.02 to 100, preferably from 0.05 to 35. It is to be understood that for the purposes of this specification the auxiliary organic compound R c is not comprised within the term "organic template(s) ", "R" or "R 2 / n O" as used herein. If present in a starting mixture, the molar ratio R c /Y0 2 typically ranges from 0.05 to 20, preferably from 0.1 to 10. Typically, the synthesis is carried out at a crystallisation time in the range of from 2 to 336 hours, preferably at a crystallisation time in the range of from 12 to 240 hours, more preferably in the range of from 24 to 120 hours. Typically a reaction temperature is employed in the range of from 60 to 250 β C, preferably in the range of from 90 to 200 β C. Preferably, the synthesis is carried out at a pH in the range of from 3 to 7.5, more preferably in the range of from 4 to 7. X is preferably chosen from Ga, Fe, B and/or Al, more preferably Al. Examples of suitable sources of X include any oxides, hydroxides, sulphates, alkoxides and/or halides of X. Y is preferably chosen from Ti, Zr and/or Si, more preferably Si. Examples of suitable sources of Y include any oxides, alkoxides and/or halides of Y as well as quaternary ammonium compounds such as tetramethylammonium silicate, and tetraethylorthosilicate. Typically, any source of fluorine ions in the starting mixture can be used in the process of the present invention. Particularly suitable sources include HF and NH 4 F. For reasons of safety NH F is preferably used. It is to be understood that the amount of NH + in the starting mixture is not critical and is in fact determined by the amount of ammonium salts used in preparation of the starting mixture. NH 4 + may even be absent from the starting mixture as in the synthesis according to the present invention ionic forms of the organic template(s) used and any auxiliary organic compound may act as counter-ion in the crystal lattice of the crystalline molecular sieve. The organic template(s) and any auxiliary organic compound(s) may be removed from the large-pore crystalline molecular sieve according to the present invention by calcining the molecular sieve at a temperature in the range of from 350 to 600 °C for 1 to 24 hours. Alternatively, R, that is the organic template(s) P^. and optionally R a , and any R c , that is the auxiliary organic compound(s), may be removed from the large-pore crystalline molecular sieve according to the present invention by contacting the molecular sieve with a polar solvent capable of extracting R and any R c from the molecular sieve. A suitable method has been disclosed in United States patent specification No. 5 143 879. In yet another aspect the present invention relates to a large- pore crystalline molecular sieve having in its calcined state an X- ray diffraction pattern with at least one peak at a d-spacing of at least 1.8 nm, a benzene sorption capacity of more than 15 grams benzene per 100 grams of the crystalline molecular sieve at 6.7 kPa and 25 °C, and a chemical composition which can be expressed as follows: 0 - 0.5 M 2 / n 0 : 0 - 0.5 X 2 0 3 : 1 Y0 2 : 0 - 6 H 2 0 : 0.001 - 2 F. Ways to determine the benzene sorption capacity are known to those skilled in the art. Suitable techniques have been described in WO 93/01884. Preferably, the crystalline molecular sieve has the following chemical composition: 0.001 - 0.5 X 2 0 3 : 1 Y0 : 0 - 6 H 2 0 : 0.001 - 2 F. In a most preferred embodiment X is Al and Y is Si. Typically, in the X-ray diffraction pattern of the crystalline molecular sieve, the relative intensity of the strongest peak at a d-spacing of at least 1.8 nm is 100. Preferably, the X-ray diffraction pattern exhibits no peaks at d-spacings less than 1.0 nm having a relative intensity of more than 20 %, more preferably more than 10 %, of the strongest peak. Preferably, the calcined crystalline molecular sieve has an X- ray diffraction pattern in which a d-spacing of at least 1.8 nm can be indexed as Ways to index d-spacings in X-ray diffraction patterns are known to those skilled in the art. A suitable method is described in WO 93/01884. Preferably, the crystalline molecular sieve has a hexagonal arrangement of uniformly-sized pores having diameters of at least 1.3 nm, as defined in WO 93/01884 and WO 91/11390. In another aspect, the present invention relates to the use of a crystalline molecular sieve according to the present invention as described hereinbefore, as a catalyst, catalyst carrier, adsorbent or as component in a washing composition. Preferably the crystalline molecular sieve is used in its R-free form. It is to be understood that the crystalline molecular sieve may be composited with a matrix material for example when used as catalyst or catalyst carrier for certain applications. Examples of suitable matrix materials have been described in WO 93/01884. Further, it will be appreciated that when the crystalline molecular sieve is used as catalyst or catalyst carrier, the finished catalyst may comprise (catalytically active) metals, such as those from Group V II or VIB from the Periodic Table of the Elements. In a preferred embodiment, the crystalline molecular sieve in combination with a metal having hydrogenation/- dehydrogenation activity, is used as a hydroprocessing catalyst for hydroprocessing of mineral or synthetic oil feedstocks. The term hydroprocessing as used herein includes hydrocracking, hydrotreating, hydrofinishing, hydroisomerisation, hydro- desulphurisation, and hydrodenitrogenation. In a particular preferred embodiment, the crystalline molecular sieve is used in a hydrocracking and/or hydroisomerisation process to produce lubricating base oils from flashed distillates and/or waxy feedstocks, such as slack wax. The invention will now be illustrated further with reference to the following Examples. The Examples are given for illustrative purposes only and should not be construed as in any way limiting the invention to a scope which is narrower than the present claims. Examples Example I; A synthesis mixture was prepared by admixing colloidal acid-stabilised silica commercially available from Nalco, water, aqueous NH 4 F solution, and as organic templates cetyltrimethyl- ammoniumchloride (CTMACl) and trimethylammoniumchloride (TMACl) . The synthesis mixture had the following molar composition: 15 Si0 2 / 3.0 TMACl/ 5.0 CTMACl/ 500 H 2 0/ 6.0 NH F The synthesis mixture had a pH of 7. The mixture was heated for 24 hours to 107 β C in a teflon-lined autoclave under autogeneous pressure. After washing and filtering a crystalline material was obtained having a X-ray diffraction pattern in which the largest d- spacing amounted to 5.4 nm. Example II: The as-synthesised crystalline molecular sieve obtained in the experiment described in Example I was subjected to a calcination treatment in air at 540 β C for 10 hours The calcined crystalline material had an X-ray diffraction pattern in which the largest d-spacing amounted to 4.9 nm. Example III: The experiment described in Example I was repeated, but dodecyltrimethylammoniumbromide (DTMABr) was used instead of cetyltrimethylammoniumchloride, in the same molar amount. After washing and filtering a crystalline material was obtained having a X-ray diffraction pattern in which the largest d-spacing amounted to 4.3 nm. Example IV: A synthesis mixture was prepared by admixing colloidal acid-stabilised silica commercially available from Nalco, water, aqueous NH 4 F solution, and as organic templates cetyltrimethyl- ammoniumbromide (CTMABr) and trimethylammoniumchloride (TMACl) . The synthesis mixture had the following molar composition: 8.1 Si0 2 / 1.5 TMACl/ 4.0 CTMABr/ 500 H 2 0/ 1.1 NH 4 F The mixture was heated for 100 hours at 108 β C in a teflon-lined autoclave under autogeneous pressure. After washing and filtering a crystalline material was obtained having a X-ray diffraction pattern in which the largest d-spacing amounted to 5.7 nm. Example V: A synthesis mixture was prepared by admixing colloidal acid-stabilised silica commercially available from Nalco, water, aqueous NH 4 F solution, cetyltrimethylammoniumbromide (CTMABr) , trimethylammoniumchloride (TMACl) and aluminiumchloride (A1C1 3 .6H 2 0) . The synthesis mixture had the following molar composition: 15.0 Si0 2 / 0.75 A10 2 ~ / 3.0 TMACl/ 5.0 CTMABr/ 500 H 2 0/ 6.0 NH 4 F The mixture was heated for 24 hours at 106 β C in a teflon-lined autoclave under autogeneous pressure. After washing and filtering a crystalline material was obtained having a X-ray diffraction pattern in which the largest d-spacing amounted to 6.5 nm. Example VI: A synthesis mixture was prepared by admixing colloidal acid-stabilised silica commercially available from Nalco, water, aqueous NH 4 F solution, dodecyltrimethylammoniumbromide (DTMABr) , triethylammoniumchloride (TEAC1) and aluminiumchloride (AICI3.6H 2 0) . The synthesis mixture had the following molar composition: 15.3 Si0 2 / 1.0 A10 2 " / 3.0 TEAC1/ 3.25 DTMABr/ 300 H 2 0/ 1.0 NH 4 F The mixture was heated for 75 hours at 108 °C in a teflon-lined autoclave under autogeneous pressure. After washing and filtering a crystalline material was obtained having a X-ray diffraction pattern in which the largest d-spacing amounted to 5.1 nm.

Claims: C L A I M S 1. A process for the preparation of a large-pore molecular sieve, comprising crystallising the molecular sieve from a starting mixture at a pH in the range of from 3 to 8, and recovering a large-pore molecular sieve, the said starting mixture having a molar composition satisfying the following molar ratio's: (0.01 - 2) R 2 / n 0) : (0 - 1.5) M 2 / m O : (0 - 0.5) X 2 0 3 : 1 Y0 2 : (5 - 1000) H 2 0 : (0.01 - 3) F ~ , wherein n and m are the weighted average valences of R and M respectively, M is an alkali- or alkaline earth metal, X is a trivalent metal and Y is a tetravalent element, wherein R comprises at least one main organic template R... having the formula R^R 2 R 3 R 4 Q + wherein Q is nitrogen or phosphorus and wherein at least one and at most three of R j _, R 2 , R 3 and R 4 is an aryl or alkyl group having 6 to 36 carbon atoms and each of the remainder of R j _, R 2 , R 3 and R 4 is selected from hydrogen and an alkyl group having 1 to 5 carbon atoms. 2. A process as claimed in claim 1, characterised in that the starting mixture has a molar composition satisfying the following molar ratio's: (0.01 - 2) R 2 / n 0 : (0 - 0.5) X 2 0 3 : 1 Y0 2 : (5 - 1000) H 2 0 : (0.01 - 3) F " . 3. A process as claimed in claim 2, characterised in that the starting mixture has a molar composition satisfying the following molar ratio's: (0.02 - 1) R 2 / n O : (0.0001 - 0.5) X 2 0 3 : 1 Y0 2 : (10 - 900) H 2 0 : (0.05 - 2.5) F-. 4. A process as claimed in any preceding claim, characterised in that R comprises an additional organic template R a in the form of an ammonium or phosphonium ion of the formula of claim 1 but wherein each R^, R , R 3 and R 4 is selected from hydrogen and an alkyl group having 1 to 5 carbon atoms, wherein 2 alkyl groups can be interconnected to form a cyclic compound. 5. A process as claimed in any preceding claim, characterised in that the starting mixture comprises an auxiliary organic compound R c selected from the group of aromatic hydrocarbons and amines having 5 to 20 carbon atoms and halogen- and Ci - C_4 alkyl-substituted derivatives thereof; or cyclic and polycyclic aliphatic hydrocarbons and amines of 5 to 20 carbon atoms and halogen- and Ci - C14 alkyl- substituted derivatives thereof; or straight and branched chain aliphatic hydrocarbons and amines having 3 to 16 carbon atoms and hydroxyl- or halogen-substituted derivatives thereof. 6. A process as claimed in claim 5, characterised in that the molar ratio R c /Y0 ranges from 0.05 to 20, preferably from 0.1 to 10. 7. A process as claimed in any preceding claim, characterised in that the reaction temperature is chosen from 60 to 250 β C, preferably from 90 to 200 °C. 8. A process as claimed in any preceding claim, characterised in that the crystallisation time is chosen from 2 to 336 hours, preferably from 12 to 240 hours, more preferably from 24 to 120 hours. 9. A process as claimed in any preceding claim, characterised in that the pH is chosen from 3 to 7.5, preferably from 4 to 7. 10. A process as claimed in any preceding claim, characterised in that as a fluorine source HF or NH 4 F, preferably NH 4 F, is used. 11. A process as claimed in any preceding claim, characterised in that X is chosen from Ga, Fe, B and/or Al, preferably Al. 12. A process as claimed in any preceding claim, characterised in that Y is chosen from Ti, Zr and/or Si, preferably Si. 13. A process substantially as described hereinbefore, with reference to the Examples. 14. A large-pore crystalline molecular sieve whenever prepared by a process according to any one of the preceding claims. 15. A process for preparing an organic template-free molecular sieve comprising calcining a molecular sieve as claimed in claim 14 at a temperature in the range of from 350 to 600 °C for 1 to 24 hours . 16. A process for preparing an organic template-free molecular sieve comprising contacting a molecular sieve as claimed in claim 14 with a polar solvent capable of extracting the organic template from the molecular sieve. 17. A large-pore crystalline molecular sieve whenever prepared by a process as claimed in claim 15 or 16. 18. A large-pore crystalline molecular sieve having in its calcined state an X-ray diffraction pattern with at least one peak at a d- spacing of at least 1.8 nm, a benzene sorption capacity of more than 15 grams benzene per 100 grams of the crystalline molecular sieve at 6.7 kPa and 25 β C, and a chemical composition which can be expressed as follows: 0 - 0.5 M 2/n O : 0 - 0.5 X 2 0 3 : 1 Y0 2 : 0 - 6 H 2 0 : 0.001 - 2 F. 19. A large pore crystalline molecular sieve as claimed in claim 17 or 18, having a chemical composition which can be expressed as follows: 0.001 - 0.5 X 2 0 3 : 1 Y0 2 : 0 - 6 H 2 0 : 0.001 - 2 F. 20. Use of a molecular sieve as claimed in any one of claims 17-19 as a catalyst, catalyst carrier, adsorbent or as component in a washing composition.

Inventors: JONGKIND HERMANUS, SEIVE ALAIN, STORK WILLEM HARTMAN JURRIAAN, VAN KOTEN MARTIJN ARJEN, JONGKIND, HERMANUS, SEIVE, ALAIN, STORK, WILLEM, HARTMAN, JURRIAAN, VAN KOTEN, MARTIJN, ARJEN
Applicants: SHELL CANADA LTD, SHELL INT RESEARCH, SHELL CANADA LIMITED, SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1995
Main classification: C01B39
IPC codes: B01J20, B01J29, C01B37, C01B39, C11D3