CA2069722C - Method for functionalizing synthetic mesoporous crystalline material - Google Patents

Method for functionalizing synthetic mesoporous crystalline material Download PDF

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CA2069722C
CA2069722C CA002069722A CA2069722A CA2069722C CA 2069722 C CA2069722 C CA 2069722C CA 002069722 A CA002069722 A CA 002069722A CA 2069722 A CA2069722 A CA 2069722A CA 2069722 C CA2069722 C CA 2069722C
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grams
elements
product
moles
benzene
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CA2069722A1 (en
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Sharon Brawner Mccullen
Bruce Patrick Pelrine
Kirk Douglas Schmitt
James Clarke Vartuli
Jeffrey Scott Beck
David Charles Calabro
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ExxonMobil Oil Corp
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Abstract

A method is described for modifying a synthetic mesoporous crystalline material by contacting with a treatment composition M'X'Y'n wherein M' is an element of Groups IIA, IIIA, IVA, VA, VIA, VIIIA, IB, IIB, IVB, VB or VIB; X' is halide, hydride, al~oxide of C1-6, or acetate; Y' is X or phosphine, sulfide, carbonyl or cyano; and n = 1-5. The contacted crystalline material becomes functionalized and the functionalized material can be used as a sorbent or a catalyst component.

Description

~~~i~~~~
F'- ~ G 4 ~ ~. 1 -- d N
METHOD OF' FUNCTIONALIZING A SYNTHETIC
MESOPOROUS CRYSTALLINE rSATERIAL
This invention relates to a method of modifying a synthetic mesoporous material by incorporating one or more functional groups into the material.
Porous inorganic solids have found great utility as catalysts and separation media for industrial application. The openness of their microstructure allows molecules access to the relatively large surface area of these materials that enhance their catalytic and sorptive activity. The porous materials in use today can be sorted into three broad categories using the details of th~.ir microstructure as a basis for classification. These categories are the amorphous and paracrystalline supports, the crystalline malecular sieves and modified layered materials. The detailed differences in the microstructures of these materials manifest themselves as important differences in the catalytic and sorptive behavior of the materials, as well as in differences in various observable properties used to characterize them, such as their surface area, the sizes of pores and the variability in those sizes, the presence or absence of X-ray diffraction patterns and the details in such patterns, and the appearance of the materials when their microstructure is studied by transmission electron microscopy and electron diffraction methods.
Amorphous and paracrystalline materials represent an important class of porous inorganic solids that have been used for many years in industrial applications.
Typical examples of these materials are the amarphous silicas commonly used in catalyst formulations and the paracrystalline transitional aluminas used as solid acid catalysts and petroleum reforming catalyst supports. The term °°amo:rphous°° is used here to indicate a material with no long range order and can be 2~~~~~~

somewhat misleading, since almost all materials are ordered to some degree, at least on the local scale.
An alternate term that has been used to described these materials is "X-ray indifferent". The microstructure of the silicas consists of 100°250 Angstrom particles of dense amorphous silica (Kirk-Othmer Encyclopedia of Chemical Technology, 3rd Edition, Vol. 20, John Wiley &
Sons, New York, p. 765-781, 1982j, with the porosity resulting from voids between the particles. Since there is no long range order in these materials, the pore sizes tend to be distributed over a rather large range. This lack of order also manifests itself in the X-ray diffraction pattern, which is usually featureless.
Paracrystalline materials such as the transitional aluminas also have a wide distribution of pore sizes, but better defined X-ray diffraction patterns usually consisting of a few broad peaks. Tie microstructure of these materials consists of tiny crystalline regions of condensed alumina phases and the porosity of the materials results from irregular voids between these regions (K, Wefers and Chanakya Misra, "Oxides and Hydroxides of Aluminum", Technical Paper No. 19 Revised, Alcoa Research Laboratories, p. 54-59, 1987).
Since, in the case of either material, there is no long range order controlling the sizes of poxes in the material, the variability in pore size is typically quite high. The sizes of pores in these materials fall into a regime called the mesoporous range, which, for the purposes of this application, is from 13 to 200 Angstroms.
In sharp contrast to these structurally ill-defined solids are materials whose pore size distribution is very narrow because it is controlled by the precisely repeating crystalline nature of the materials' microstructure. These materials are called "molecular sieves", the most important examples of F-6246 -3- ~ ~~ ~ i7'6 which are zeolites. The precise crystalline microstructure of most zeolites manifests itself in a well-defined X-ray diffraction pattern that usually contains many sharp maxima and that serves to uniquely define the material. Similarly, the dimensions of pores in these materials are very regular, due to the precise repetition of the crystalline microstructure.
All molecular sieves discovered to date have pore sizes in the microporous range, which is usually quoted as 2 to 20 Angstroms, with the largest reported being about 12 Angstroms.
Certain layered materials, which contain layers capable of being spaced apart with a swelling agent, may be pillared to provide materials having a large degree of porosity. Examples of such layered materials include clays. Such clays may be swollen with water, whereby the layers of the clay are spaced apart by water molecules. Other layered materials are not swellable with water, but may be swollen with certain organic swelling agents such as amines and quaternary ammonium compounds. Examples of such non-water swellable layered materials are described in U.S.
Patent 4,859,648 and include layered silicates, magadiite, kenyaite, trititanates and perovskites.
Another example of a non-water swellable layered material, which can be swollen with certain organic swelling agents, is a vacancy-containing titanometallate material, as described in U.S. Patent 4,831,006.
Once a layered material is swollen, the material may be pillared by interposing a thermally stable substance, such as silica, between the spaced apart layers. The aforementioned U.S. Patents 4,831,006 and 4,859,648 describe methods for pillaring the non-water swellable layered materials described therein. The X-ray diffraction patterns of pillared layered materials can vary considerably, depending on the 1; _. q> 14 (;
J
degree that swelling and pillaring disrupt the otherwise usually well-ordered layered microstructure.
The regularity of the microstructure in some pillared layered materials is so badly disrupted that only one peak in the low angle region of the X-ray diffraction pattern is observed, at a d-spacing corresponding to the interlayer repeat in the pillared material. Less disrupted materials may show several peaks in this region that are generally orders of this fundamental repeat. X-ray reflections from the crystalline structure of the layers are also sometimes observed.
The pore size distribution in these pillared layered materials is narrower than that in amorphous and paracrystalline materials but broader than that in zeolitic materials.
In our International Patent Publication No. WO
91/11390, we have described a novel class of inorganic, porous, non-layered, crystalline material which is distinguished from other porous inorganic solids by the regularity of its large open pores, whose size is in the mesoporous range and hence more nearly resembles the pore size of amorphous or paracrystalline materials, but whose regular arrangement and uniformity of size more closely resemble those of crystalline materials such as zeolites. In particular, this novel class of material exhibits, after calcination, an X-ray diffraction pattern with at least one peak at a d-spacing greater then about 18 Angstrom Units and has a benzene adsorption capacity of greater than 15 grams benzene per 100 grams of said material at 50 torr and 25°C.
This new class of molecular sieves has the unique property that a nigh concentration of hydroxyl groups may be present within the pore openings of the as-synthesized or calcined material. An object of the present invention is to use the hydroxyl groups to react with an organic treatment compound to anchor or incorporate functional groups into the molecular sieve material. The functional groups can provide unique catalytic sites within the pores or can act as pore size reducing agents so that the pore size can tailored as desired. The functional groups can also serve as precursors to ceramic materials.
Accordingly, the invention resides in a method of modifying an inorganic, porous, non-layered crystalline phase material exhibiting, after calcination, an X-ray diffraction pattern with at least one peak at a d-spacing greater than about 18 Angstrom Units and having a benzene adsorption capacity of greater than 15 grams of benzene per 100 grams of said material at 6.7 kPa (50 torr) and 25°C, comprising contacting the crystalline material, before or after calcination, with a treatment composition which comprises M'X'Y'n wherein M' is selected from Groups IIA, IIIA, IVA, VA, VIA, VIIIA, IB, IIB, IIIB, IVB, VB and VIB of the Periodic Table of the Elements; X' is selected from halides, hydrides, alkoxides of C1-6, alkyl of C1-18, alkenyl of C1-18 and aryl of C3-8, acetate, aryloxide of C3-18, sulfonates and nitrates; Y' is selected from X, amines, phosphines, sulfides, carbonyls and cyanos; and, n =
1-5.
In a preferred embodiment, the inorganic, porous crystalline phase material has a hexagonal arrangement of uniformly-sized pores at least about 13 Angstroms in diameter and exhibits, after calcination, a hexagonal electron diffraction pattern that can be indexed with a d100 value greater than 18 Angstrom Units.
Advantageously, the modification can be carried out on the as-synthesized crystalline material without the necessity for removing residual organics. In addition, essentially all internal hydroxyl sites can be functionalized if desired.
The functionalization reaction of the invention may be described according to the formula:

Si-O-R' + M'X'Y'n ----> SiOM'Y'n + R'X' wherein Si-O-R' is a site in the lattice of the crystalline material.
R' - H+ or R4N+ which is the organic cation specified in the crystallization methods described hereinbelow.
M' - Elements of Groups IIA, IIIA, IVA, VA, VIA, VIIIA, IB, IIB, IIIB, IVB, VB, or VIB of the Periodic Table of the Elements, (Sargent-Welch Scientific Co.
Cat. No. S-18806, 1979). Preferred elements for M' are Groups IVA, VIA, VIIIA, IIIB and IVB, and most preferred elements for M are titanium, chromium, iron, cobalt, nickel, boron, aluminum and silicon.
X' - halides, hydrides, alkoxides of 1-6 carbon atoms, alkyl of 1-18 carbon atoms, aryl of 3-18 carbon atoms, acetates, aryloxides of 3-18 carbon atoms, sulfonates and nitrates. Preferred substituents for X
are halides, alkoxides of 1-6 carbon atoms and acetates.
Y' can be selected from the substituents described for X', or amines, phosphines, sulfides, carbonyls and cyanos. Preferred substituents for Y' are those described for X', amines, sulfides and alkyls with 1-18 carbon atoms. Most preferred substituents for Y' are those described for X', amines and alkyls with 1-18 carbon atoms; n = 1-5.
Non-limiting examples for M'X'Y'n include chromium acetate, chromium nitrate, tetraethylorthosilicate, tetramethylorthosilicate, titanium tetraethoxide, aluminum isopropoxide, aluminum tri-sec butoxide, hexamethyldisilazane, di-sec-butoxyaluminoxytriethoxy-silane, diethylphosphatoethyltriethyoxysilane, trimethylborate, chlorodimethylalkylsilane wherein alkyl has 1-18 carbon atoms, ammonia-borane, borane-tetrahydrofuran and dimethylsulfide-dibromoborane.

-The ratio of treatment composition to treated composition of matter, duration of treatment and temperature are not critical and may vary within wide limits. The temperature may be, for example, from -70°C to 250°C, with 25°C to 100°C being preferred; and the time may be from 0.1 to 100 hours, with a time of 0.1 to 30 hours being preferred and a time of 0.1 to 24 hours most preferred.
The treated crystalline material can be used as is or may be further subjected to a thermal treatment or treatment with a reactive gas such as oxygen or carbon monoxide for activation. The treated material may be calcined in a reactive or inert gas such as NH3, PH3, air, 02 , N2 , Ar, H2 , SiH4 or B2H6 .
The treated crystalline material may be described as having functional groups within it according to the formula SiOM'Y'n These functionalized sites may be, for example:
O
-SiOP(OMe)2, -SiOB(OMe)2, -SiOB(Br)2.SMe2, -SiOTi(OEt)3, -SiOCr(acetate)2, -SiOCr(nitrate)z, -SiOSi(OMe)3, -Si0A1(s-OPr)2, -Si0A1(s-OBu )2, -SiOSi(OEt)3, OEt O-s-Bu ~ O
-SiOAl~ -SiOSi-CH2CH2-P(OEt)Z, \0S1. (OEt) 3 , OEt -.fl.~.f1(~.'H3)3, -fl~.Sl(CH3)2C6H13r -SlOSl(CH3)yC19H37i -SiOSi (CH3) ZC6Hs. where Me=CH3, Et=C2H5, Pr=C3H~, Bu=C4H9 .

g-~szab -~- ~ ~> ~ ~ l %' l 3n these examples, -Si represents a site in the lattice of the crystalline material. Two additional bonds on the Si are not shown. The invention is not limited to these listed functionalized sites.
In its calcined form, the crystalline material treated by the method of the invention exhibits an X-ray diffraction pattern with at least one peak at a position greater than about 18 Angstrom Units d-spacing (4.909 degrees two-theta for Cu K-alpha radiation).
More particularly, the calcined crystalline non-layered material of the invention may be characterized by an X-ray diffraction pattern with at least two peaks at positions greater than about 10 Angstrom Units d-spacing (8.842 degrees two-theta for Cu K-alpha radiation), at least one of which is at a position greater than about 18 Angstrom Units d-spacing, and no peaks at positions less than about 10 Angstrom units d-spacing with relative intensity greater than about 20~ of the strongest peak. Still more particularly, the X-ray diffraction pattern of the calcined material of this invention will have no peaks at positions less than about 10 Angstrom units d-spacing with relative intensity greater than about l00 of the strongest peak.
X-ray diffraction data were collected on a Scintag pAD X automai~ed diffraction system employing theta-theta geometry, Cu K-alpha radiation, and an energy dispersive X~-ray detector. Use of the energy dispersive X--ray detector eliminated the need for incident or diffracted beam monochramators. Both the incident and diffracted X-ray beams were collimated by double slit incident and diffracted collimation systems. The slit sizes used, starting from the X-ray tube source, were 0.5, 1.0, 0.3 and 0.2 mm, respectively. Different slit systems may produce differing intensities for the peaks. The materials of the present invention treat have the largest pore sizes may require more highly collimated incident X-ray beams <.,"~~~~'l~w f-6246 -9-in order to resolve the low angle peak from the transmitted incident X-ray beam.
The diffraction data were recorded by step-scanning at 0.04 degrees of two-theta, where theta is the Bragg angle, and a counting time of 10 seconds for each step.
The interplanar spacings, d°s, were calculated in Angstrom units (A), and the relative intensities of the lines, I/Io, where Io is one-hundredth of the intensity of the strongest line, above background, were derived with the use of a profile fitting routine. The intensities were uncorrected for Lorentz and polariza-tion effects. The relative intensities are given in terms of the symbols vs = very strong (75-100), s =
strong (50-74), m = medium (25-49) and w = weak (0-24).
It should be understood that diffraction data listed as single lines may consist of multiple overlapping lines which under certain conditions, such as very high experimental resolution or crystallographic changes, may appear as resolved or partially resolved lines.
Typically, crystallographic changes can include minor changes in unit cell parameters and/or a change in crystal symmetry, without a substantial change in structure. These minor effects, including changes in relative intensities, can also occur as a result of differences in cation content, framework composition, nature and ds~gree of pore fil:Ling, thermal and/or hydrothermal history, and peak width/shape variations due to particle size/shape effects, structural disorder or other factors known to those skilled in the art of X-ray diffraction.
The material treated by the method of the invention is further characterised by an equilibrium benzene adsorption capacity of greater than about 15 grams benzene/100 grams crystal at 6.7 kPa (50 torr) and 25°C. The equilibrium benzene adsorption capacity characteristic of this material is measured on the basis of no pore blockage by incidental contaminants.

F-624(i -10-For instance, the sorption test will be conducted on the crystalline material phase having any pore blockage contaminants and water removed by ordinary methods.
Water may be removed by dehydration techniques, e.g.
thermal treatment. Pore blocking inorganic amorphous materials. e.g. silica, and organics may be removed by contact with acid or base or other chemical agents such that the detrital material will be removed without detrimental effect on the crystal of the invention.
The equilibrium benzene adsorption capacity is determined by contacting the material of the invention, after dehydration or calcination at, for example, 450 to 700°C, typically 540°C, for at least one hour and other treatment, if necessary, in an attempt to remove any pore blocking contaminants, at 25°C and 50 torr benzene until equilibrium is reached. The weight of benzene sorbed is then determined as more particularly described hereinafter.
The materials treated by the method of the invention are generally mesoporous, by which is meant they have uniform pores within the size range of 13 to 200 Angstroms, more usually 15 to 100 Angstroms. sn a preferred embodiment, the material appears to have a hexagonal arrangement of large channels with open internal diameters from 13 to 200 Angstroms. This structure cars be revealed by transmission electron microscopy arid electron diffraction. Thus, electron micrographs of properly oriented specimens of the material show a hexagonal arrangement of large channels and the corresponding electron diffraction patterns give an approximately hexagonal arrangement of diffraction maxima. The d100 spacing of the electron diffraction patterns is the distance between adjacent spots on the hk0 projection of the hexagonal lattice and is related to the repeat distance a0 between channels observed in the electron micrographs through 'the formula d100 = a0 3/2. This d100 spacing observed ~~i ~3e~ ~~~
F-Ea2.46 -11-in the electron diffraction pattern corresponds to the d-spacing of the low angle peak (>18 Angstrom d-spacing) in the X-ray diffraction pattern. The most highly ordered preparations of the material obtained so far have 20-40 distinct spots observable in the electron diffraction patterns. These patterns can be indexed with the hexagonal hko subset of unique reflections of 100, 110, 200, 210, etc., and their symmetry-related reflections.
As demonstrated hereinafter, the inorganic, non-layered mesoporous crystalline material used in this invention typically has the following composition:
Mn/q(Wa Xb Yc Zd Oh) wherein W is a divalent element, such as a divalent first row transition metal, e.g. manganese, cobalt and iron, and/or magnesium, preferably cobalt; X is a trivalent element, such as aluminum, boron, iron and/or gallium, preferably aluminum; Y is a tetravalent element such as silicon and/or germanium, preferably silicon: Z is a pentavalent element, such as phosphorus; M is one or more ions, such as, for example, ammonium, Group IA, IIA and VIIB ions, usually hydrogen, sodium and/or fluoride ions; n is the charge of the composition excluding M expressed as oxides: q is the weighted molar average valence of M; n/q is the number of moles or mole fraction of M; a, b, c and d are mole fractions of W, X, Y and Z, respectively: h is a number of from 1 to 2.5; and (a+b+c+d) - 1.
A preferred embodiment of the above crystalline material is when (a+b+c) is greater than d, and h = 2.
A further embodiment is when a and d = 0, and h = 2.
In the as-synthesized form, the material employed in this invention typically has a composition, on an anhydrous basis, expressed empirically as follows:
rRMn/q(Wa Xb Yc Zd Oh) wherein R is the total organic material not included in M as an ion, and r is the coefficient for R, i.e. the F-624Ei -12- ~,~ d~ ~F z~ ~ ~ ~, number of moles or mole fraction of R. The M and R
components are associated with the material as a result of their presence during crystallization, and are easily removed or, in the case of M, replaced by conventional post-crystallization methods.
Synthesis of the ultra-large pore crystalline material treated by the method of the invention is described in detail in our International Patent Publication No. WO 91/11390. In particular, materials having the composition defined by the above formula can be prepared from a reaction mixture having a composition in terms of mole ratios of oxides, within the following ranges:
Reactants Useful Preferred X203/Y02 0 to 0.5 0.001 to 0.5 X203/(Y02+Z205) 0.1 to 100 0.1 to 20 X203/(Y02+WO+Z205) 0.1 to 100 0.1 to 20 Solvent/
(Y02+WO+Z205+X203) 1 to 1500 5 to 1000 Ofi /Y02 0 to 10 0 to 5 (M2/eO+R2/f0)/
(Y02+WO+Z2O5+X203) 0.01 to 20 0.05 to 5 M2/e0/
(Y02+WO+Z205+X203) 0 to 10 0 to 5 R2/fO/
(Y02+WO+Z205+X203) 0.01 to 2.0 0.03 to 1.0 wherein a and f are the weighted average valences of M
and R, respectively, wherein the solvent is a C1 to C6 alcohol or diol, or, more preferably, water and wherein R comprises an organic directing agent having the formula R1R2R3R4Q+ wherein ~ is nitrogen or phosphorus and wherein at least one of R1, R2, R3 and R4 is aryl or alkyl group having 6 to 36 carbon atoms, e.g.
C6N13' C10H21 ' -C16H33 and C18H37' 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.

F-E>246 --13- ~ fj ~ ~ ~~
J N
The compound from which the above ammonium or phosphonium ion is derived may be, for example, the hydroxide, halide, silicate or mixtures thereof.
The particular effectiveness of tre above directing agent, when compared with other such agents known to direct synthesis of one or more other crystal structures, is believed due to its ability to function as a template in the nucleation and growth of the desired ultra-large pore materials. Non-limiting examples of these directing agents include cetyltrimethylammonium, cetyltrimethylphosphonium, octadecyltrimethylphosphonium, benzyltrimethylammonium, cetylpyridinium, myristyltrimethylammonium, decyltrimethylammonium, dodecyltrimethylammonium and dimethyldidodecylammonium compounds.
Preferably, the total organic, R, present in the reaction mixture comprises an additional organic directing agent in the form of an ammonium or phosphonium ion of the above directing agent formula but wherein each R1, R2, R3 and R4 is selected from hydrogen and an alkyl group of 1 to 5 carbon atoms (2 of the alkyl groups can be interconnected to form a cyclic compound). Examples of the additional organic directing agent include tetramethylammonium, tetraethylammonium, tetrapropylammonium, tetrabutylammonium and pyrrolidinium compounds. The molar ratio of the first-mentioned organic directing agent to the additional organic directing agent can be in the range 100/1 to 0.01/1. Where the additional organic directing agent is present, the molar ratio R2/f~/(Ya2+WO+Z205+X203) in the reaction mixture is preferably 0.1 to 2.0, most preferably 0.12 to 1Ø
In addition, to vary the pore size of the final crystalline phase material, the total organic, R, in the reaction mixture can include an auxiliary organic in addition to the organic directing agents) described above. This auxiliary organic is selected from (1) F-624 f --1~-aromatic hydrocarbons and amines having 5-20 carbon atoms and halogen-- and C1-C14 alkyl-substituted derivatives thereof, (2) cyclic and polycyclic aliphatic hydrocarbons and amines of 5 to 20 carbon atoms and halogen- and C1-C1~ alkyl-substituted derivatives thereof and (3) straight and branched chain aliphatic hydrocarbons and amines having 3-16 carbon atoms and halogen-substituted derivatives thereof.
In the above auxiliary organics, the halogen substituent is preferably bromine. The C1-C14 alkyl substituent may be a linear or branched aliphatic chain, such as, for example, methyl, ethyl, propyl, isopropyl, butyl, pentyl and combinations thereof.
Examples of these auxiliary organics include, for example, p-xylene, trimethylbenzene, triethylbenzene arid triisopropylbenzene.
Edith the inclusion of the auxiliary organic in the reaction mixture, the mole ratio of auxiliary organic/Y02 will be from 0.05 to 20, preferably from ?0 0.1 to 10, and the mole ratio of auxiliary organic/organic directing agents) will be from 0.02 to 100, preferably from 0.05 to 35.
When a source of silicon is used in the synthesis method, it is preferred to use at least in part an organic silicate, such as, for example, a quaternary ammonium silicate. Non-limiting examples of such a silicate include tetramethylammonium silicate and tetraethylorthosilicate.
Non-limiting examples of various combinations of W, ~, Y and Z contemplated for the above reaction mixture include:

I'°6246 -15-~1 X Y Z
-- A1 Si --__ A1 -_ p -- A1 Si P
Co Al -- p Co A1 Si P
__ __ Si __ including the combinations of W being Mg, or an element selected from the divalent first row transition metals, e.g. Mn, Co and Fep ~C being B, Ga or Fe; and Y being Ge.
To produce the crystalline material of the invention, the reaction mixture described above is maintained at a temperature of 25 to 250°C, preferably 50 to 175°C, and preferably a pH of 9 to 14 for a period of time until the required crystals form, typically 5 minutes to 14 days, more preferably 1 to 300 hours.
When the crystalline material of the invention is an aluminosilicate, the synthesis method conveniently involves the following steps:
(1) Mix the organic (R) directing agent with the solvent or solvent mixture such that the mole ratio of solvent/R2/f0 is within the range of 50 to 800, preferably from 50 to 500. This mixture constitutes the "primary template°° for the synthesis method.
(2) To the primary template mixture of step (1) add the silica and alumina such that the ratio of R2/f~/(Si02+A1203) is within the range 0.01 to 2Ø
(3) Agitate the mixture resulting from step (2) at a temperature of 20 to 40°C, preferably for 5 minutes to 3 hours.
(4) Allow the mixture to stand with or without agitation, preferably at 20 to 50°C, and preferably for 10 minutes to 24 hours.

~~'~~~;~".~
(5) Crystallize the product from step (4) at a temperature of 50 to 150°C, preferably for 1 to 72 hours.
The treatment methad of the invention can be used to enhance the activity and/or selectivity of the the present mesoporous crystalline materials for a wide range of catalytic conversion processes. Examples of such processes include cracking and hydrocracking, especially of high molecular weight, high boiling or non-distillable feeds, particularly residual feeds, NOx reduction and oligomerization of olefins, for example to produce high viscosity lubricants. The treated material of the invention can also be used as a sorbent.
In order to more fully illustrate the nature of the invention and the manner of practicing same, the following examples are presented. In the examples, whenever sorption data are set forth for comparison of sorptive capacities for water, cyclohexane, benzene and/or n-hexane, they are equilibrium adsorption values determined as follows:
A weighed sample of the adsorbent, after calcin-ation at about 540°C for at least about 1 hour and other treatm~:nt, if necessary, to remove any pore blocking contaminants, is contacted with the desired pure adsorbate vapor in an adsorption chamber. The increase in weight of the adsorbent is calculated as the adsorption capacity of the sample in terms of grams/100 grams adsorbent based on adsorbent weight after calcination at about 540°C. The present composi-tion exhibits an equilibrium benzene adsorption capacity at (6.7 kPa) 50 Torr and 25°C of greater than about 15 grams/100 grams, particularly greater than about 17.5 grams/100 grams and more particularly greater than about 20 grams/100 grams.

A preferred way to determine equilibrium adsorption values is to contact the desired pure adsorbate vapor in an adsorption chamber evacuated to less than 1 mm at conditions of 1.6 kPa (12 Torr) of water vapor, 5.3 kPa (40 Torr) of n-hexane or cyclohexane vapor, or 6.7 kPa (50 Torr) of benzene vapor, at 25°C. The pressure is kept constant (within about + 0.5 mm) by addition of adsorbate vapor controlled by a manostat during the adsorption period. As adsorbate is adsorbed by the crystalline material, the decrease in pressure causes the manostat to open a valve which admits more adsorbate vapor to the chamber to restore the above control pressures. Sorption is complete when the pressure change is not sufficient to activate the manostat.
Another method for benzene adsorption data is on a suitable thermogravimetric analysis system, such as a computer-controlled 990/951 duPont TGA system. The adsorbent sample is dehydrated (physically sorbed water removed) by heating at, for example, about 350°C or 500°C to constant weight in flowing helium. If the sample is in as-synthesized form, e.g. containing organic directing agents, it is calcined at about 540°C
in air and held to constant weight instead of the previously described 350°C or 500°C treatment. Benzene adsorption isotherms are measured at 25°C by blending a benzene saturated helium gas stream with a pure helium gas stream in the proper proportions to obtain the desired benzene partial pressure. The value of the adsorption at 6.7 kPa (50 Torr) of benzene is taken from a plot of adsorption isotherm.
In the examples, percentages are by weight unless otherwise indicated.

A solution of 2.7 grams of NaAl02 (43.5% A1203, 30% NaZO) in 146.9 grams of water was mixed with 34.5 grams of NaOH, 189.1 grams of cetyltrimethylammonium hydroxide solution prepared by contacting a 29 wt %
N,N,N-trimethyl-1-hexadecanaminium chloride solution with an excess of~hydroxide for halide resin, and 110.7 grams of Ultrasil (92% Si02). After stirring overnight it was loaded into a 600 cc autoclave and reacted at 150°C with 400 rpm stirring for 72 hours. The mixture had the following relative molar composition:
0.25 moles A1203 10 moles Na20 36 moles SiOa 2.5 moles (CTMA)20 362.5 moles H20 Following filtration of the mixture, the solid product which precipitated from the filtrate was recovered by filtration, washed with water, then calcined at 550°C for 10 hours in air.
The calcined product proved to have a surface area of 1193 m2/g and the following equilibrium adsorption capacities in grams/100 grams anhydrous sorbent:
H20 10.2 Cyclohexane > 50 n-Hexane 48.9 Benzene 68.1 The X-ray diffraction pattern of the calcined product of this example may be characterized as including a very strong relative intensity line at 50.7 +_ 3.0 Angstroms d-spacing and a weak line at 30.7 +
1.0 Angstroms.

A 0.50 gram portion of a calcined product prepared as in Example I was added to a rapidly stirred solution of 10 grams chlorotrimethylsilane in 15 grams hexamethyldisiloxane. The mixture was refluxed under N2 overnight, cooled, the reagents removed on a rotary evaporator, the product washed with two 10 mL portions of acetone and air dried to yield 0.53 grams of product, A solid state magic angle spinning NMR spectrum of this product was obtained using 90 degree pulses at 1200 s intervals with proton deeoupling. This spectrum showed peaks at 15 and -108 ppm. The peak at ppm has been assigned to trimethylsilyl groups (T.
Yanagisawa, et al., Reactivity of Solids, Vol. 5, IS7 15 (1988)) and shows that the product has reacted.
Integration of the two peaks showed that 17.9% of the silicons in the original product had been converted.
The internal pore volume of the trimethylsilylated product was compared to that of the starting material by both benzene sorption and argon physisorption. The total reduction in pore volume was measured as 48~ by benzene and 34~ by argon. The diameter of the TMS
group was measured to be about 0.4-0.5 nm from CPK
molecular mociels. An onion skin coating of TMS groups on the inside of the pore should, therefore, cause a decrease of 0.8-1.0 nm in pore diameter. The Horvath-Kowazoe transform of the argon isotherm shows the pore diameter to have decreased from 3.94 to 3.04 nm (0.90 nm) in agreement with what was predicted from the models.
Water sorption was measured before and after the chlorotrimethylsilane treatment. The calcined product of Example 1 sorbed 10.0 weight percent water at 30°C
and 12.5 torn while the treated material sorbed 3.3 weight percent water. This demonstrates that trichloromethylsilane treatment increases the hydro-phobic character of the novel crystalline material.

A 0.50 gram portion of a product prepared as in Example 1 was added to a rapidly stirred solution of 15 mL hexamethyldisilazane in 15 grams hexamethyl-disiloxane. The mixture was refluxed under N2 overnight, cooled, the reagents removed on a rotary evaporator, the product washed with two 10 mL portions of acetone and air dried to yield 0.52 grams of product.
A solid state magic angle spinning NMR spectrum of this product obtained using 90 degree pulses at 1200 s intervals with proton decoupling. This spectrum showed peaks at 15 and -108 ppm. The peak 15 ppm has been assigned to trimethylsilyl groups (Id.) and shows that the product has reacted. Integration of the two peaks showed that 16.8% of the silicons in the original product had been converted. Within the experimental error of the Si-nmr experiment, the conversion by chlorotrimethylsilane and hexamethyldisilazane was the same.
Examples 2 and 3 show pore size reduction using the treatment method of the invention.

Four hundred grams of cetyltrimethylammonium (CTMA) hydroxide solution, prepared by contacting a 29 wt% N,N,N-trimethyl-1-hexadecanaminium chloride solution with an excess of hydroxide-for-halide resin, was combined with two hundred grams of tetramethylammonium (TMA) silicate solution (10% by wt.
silica, l:l,TMA:Si) with stirring. Fifty grams of HiSil, a precipitated hydrated silica containing about 6 wt% free water and about 4.5 wt% bound water of hydration and having an ultimate particle size of about 0.02 micron, was added. The resulting mixture was placed in a polypropylene bottle and put into a steam box (about 100°C) for 48 hours. The mixture had a composition in terms of moles per mole of A1Z03:
391.4 moles of Si02 71.4 moles of (CTMA)20 61.6 moles of (TMA)20 9144 moles of H20 The resulting solid product was recovered by filtration and dried in air at ambient temperature.
The chemical analyses of the as-synthesized product were:
Si02 23.7 wt%
A1z03 0.2 wt%
N 2 . 3 wt%
C 33.9 wt%
Ash, 1000°C 22.1 wt%

A portion of the product from Example 4 was then calcined at 540°C for one hour in nitrogen, followed by six hours in air. The benzene sorption for this material was 39.5 wt%.

One gram of the air dried product of Example 4 was mixed with one gram titanium tetraethoxide at room temperature for overnight. The mixture was then reacted with 5 grams of water for one hour. The product was calcined in nitrogen at 538°C for one hour then air for 6 hours at 538°C. The benzene sorption at 30°C was 25.0 wt%.

One gram of the air dried product of Example 4 was mixed with one gram aluminum tri-sec-butoxide at room temperature for overnight. The mixture was then r-e~aac> --22-~V A J
reacted with 5 grams of water for one hour. The product was calcined in nitrogen at 538°G for one hour then air for 6 hours at 538°C. The benzene sorption at 30°C was 37.5 wt$.

Ten grams of the air-dried product from Example 4 was combined with Di-s-butoxyaluminoxy-triethyoxylsilane (DBAIAS), an a 1/1 gram for gram basis, and fifty grams of absolute ethanol and allowed to mix overnight. This mixture was then combined with one hundred grams of water and stirred for one hour.
The resulting solid product was recovered by filtration and dried in air at temperature. The functionalized product was then calcined at 540°C for one hour in nitrogen, followed by six hours in air.

Ten grams of the air-dried product from Example 4 was combined with Di-s-butaxyaluminoxy-triethyoxylsilane (DBALS), on a 1/1 gram for gram basis, and fi:Ety grams of hexamethyldisiloxane and allowed to mix overnight. This mixture was combined with one hundred grams of water and stirred for one hour. The resulting solid product was recovered by filtration and dried in air at ambient temperature.
The functionalized product was then calcined at 540°C
for one hour in nitrogen, followed by six hours in air.

Ten grams of the air-dried product from Example 4 was combined with Diethylphosphatoethyltriethoxysilane, on a 1/1 gram for gram basis, and fifty grams of absolute ethanol and allowed to mix overnight. This mixture was then combined with one hundred grams of water and stirred for one hour. The resulting solid product was recovered by filtration and dried in air at F-fi24(i -.-23-ambient temperature. The functionalized product was then calcined at 540°C for one hour in nitrogen, followed by six hours in air.

Ten grams of the air-dried product from Example 4 was combined with Trimethylborate, on a 2/1 gram for gram basis, and fifty grams of absolute ethanol and allowed to mix overnight. This mixture was then combined with one hundred grams of water and stirred for one hour. The resulting solid product was recovered by filtration and dried in air at ambient temperature. The functionalized product was then calcined at 540°C for one hour in nitrogen, followed by six hours in air.
EXAMPLE 1~
Ten grams of the air-dried product from Example 4 was combined with 7.5 grams of aluminum isopropoxide and fifty grams of absolute ethanol and allowed to mix overnight. This mixture was then combined with one hundred grams of water and stirred for one hour. The resulting solid product was recovered by filtration and dried in air at ambient temperature. The functional-ized product was then calcined at 540°C for one hour in nitrogen, followed by six hours in air.
Elemental Analysis of the product of untreated Example 4 is compared with, the treated products of Example 8-12 in Table 1 below.

ELEI~NTAL ANALYSES OF SYNTHESIS PRODUCTS
ASH
C N Si A1 P B (1000C,, Ex. 4 33.0 2.32 10.9 0.052 - - 22.1 Ex. 8 - - 25.9 11.2 - - 77.0 Ex. 9 - - 32.3 5.2 - - 84.5 Ex. 10 - - 32.9 - 4.7 - 74.3 Ex. 11 - - 32.1 - - 2.6 76.3 Ex. 12 - - 16.2 17.7 - - g0.g Examples 6-12 illustrate other types of functional groups which can be incorporated into the crystalline material using the method of the invention.

In this example. 1.65 grams of NaAl~z was added to 80 grams of cetyltrimethylammonium hydroxide (CTMAOH) solution, prepared by contacting a 29 wt.%
N,N,N-trimethyl-1-hexadecanaminium chloride solution with a hydroxide-for-halide exchange resin. The mixture was stirred until the NaAlOz was completely dissolved.
To this solution was added 40.0 grams of tetramethylammonium silicate solution (10 wt.% Si02), 10.0 grams of HiSil (90 wt.% SiOz), and 6.01 grams of 1,3,5-trimethylbenzene. The resulting mixture was stirred at room temperature for several minutes. The gel was then loaded into a 300 ml autoclave and heated to 105°C while stirring at 150 RPM. After about 4 hours of heating, the reaction was quenched with cold water, and the contents removed. The product was filtered and washed several times with warm (60-70°C) distilled water and with acetone. The final product was calcined at 538°C in a Nz/air mixture for 8 hours. The gel reaction mixture had a composition in terms of moles per mole A1z03 as follows:

1.25 moles Na20 27.8 moles SiOz 5.1 moles (CTMA)20 2.24 moles (TMA)20 650 moles Hz0 6.91 moles 1,3,5-trimethylbenzene The calcined product of this example proved to have a surface area of 948.6 m2/g and a benzene adsorption capacity of 64.0 wt.%.

One gram of the product of Example 13 was mixed with one gram tetr3ethylorthosilicate at room temperature for overnight. The mixture was then reacted with 5 grams of water for one hour. The product was calcined,in nitrogen at 538°C for one hour then air for 6 hours at 538°C. The benzene sorption at 25°C was 40.0 wt%. Since the crystalline material had an initial benzene sorption of 64.0 wt%, the pore volume was reduced by 37% suggesting that the pore diameter was reduced by 8 Angstroms.

To 18.7 gm of N-clear (Na-silicate) dissolved in 30.0 gm of distilled water was added 1.2 gm of sulfuric acid dissolved in l0 gm of water. After allowing the resulting mixture to stir for ten minutes, 16.77 gm cetyltrimethylammonium bromide in 50.2 gm HZO was added and the resulting gel was allowed to stir for 0.5 h.
At this point 20 gm of water was added to the reaction.
The gel was then crystallized under static, autogenous conditions in a polypropylene bottle (100C). The resulting product was washed thoroughly with distilled water, dried and calcined to 538C. The X-ray diffraction pattern of the calcined product of this example included a very strong relative intensity line at 33.2 ~ 2.0 Angstroms d-spacing and weak lines at 19.8 ~ 1.0 Angstroms and 17.5 ~ 1.0 Angstroms. The benzene sorption for this material was 50%.

0.5 gm of the product of Example 15 was combined with 10 mL of (CH3)2S:BH3 in 20 mL of toluene. After stirring for ca. 5 minutes the solid was isolated by vacuum filtration, washed with n-hexanes and then washed with acetone. The dried product was then calcined in air to 538°C.
The X-ray diffraction pattern of the product of this example included a very strong relative intensity line at 32.4 ~ 2.0 Angstroms d-spacing and weak lines at 19.5 ~ 1.0 and 17.2 + 1.0 Angstroms. The benzene sorption was 41 wt.%. Since the crystalline material of Example 15 had a benzene sorption value of 50%, the pore volume of the material of the present example appears to have been reduced.

Three grams of calcined crystalline material prepared as described in Example 4 were added to a solution of 0.14 grams chromium acetate monohydrate in 10 grams water. This mixture was reacted overnight at room temperature. Excess moisture was removed under vacuum. The catalyst was dried in nitrogen at 250°C
for 5 hours then air at 600°C for 9 hours. The temperature was lowered to 350°C and the sample reduced in carbon monoxide for 30 minutes.

The product of Example 17 was contacted at 120°C
with 1-decene at 1.91 LHSV. An oligomerization product was isolated and had a viscosity of 2419 centistokes (cS) at 40°C and 238 cS at 100°C. The calculated viscosity index was 237.

An oligomerization of 1-decene was carried out as in Example 18 except that the reaction temperature was increased to 182°C at 1.95 LHSV. The product was isolated by distillation and its viscosity was 197 cS
at 40°C and 27.6 cS at 100°C. The viscosity index was 178.
The products of the oligomerization of Examples 18 and 19 over a crystalline material treated according to the invention, have much higher viscosities than expected using prior art Cr/Si02 catalysts.

Claims (10)

1. A method of modifying an inorganic, porous, non-layered crystalline phase material exhibiting, after calcination, an X-ray diffraction pattern with at least one peak at a d-spacing greater than 18 Angstrom Units and having a benzene adsorption capacity of greater than 15 grams of benzene per 100 grams of said material at 6.7 kPa (50 torr) and 25°C, comprising contacting the crystalline material, before or after calcination, with a treatment composition which comprises M'X'Y'n wherein M' is selected from Groups IIA, IIIA, IVA, VA, VIA, VIIIA, IB, IIB, IIIB, IVB, VB
and VIB of the Periodic Table of the Elements: X' is selected from halides, hydrides, alkoxides of C1-6, alkyl of C1-18, alkenyl of C1-18 and aryl of C3-8, acetate, aryloxide of C3-18, sulfonates and nitrates; Y' is selected from X, amines, phosphines, sulfides, carbonyls and cyanos: and, n = 1-5.
2. The method of claim 1 wherein said contacting is conducted at a temperature of -70°C to 250°C for a time of 0.1 to 100 hours.
3. The method of claim 1 wherein said contacting is conducted at a temperature of 25°C to 100°C for a time of 0.1 to 30 hours.
4. The method of any one of claims 1 to 3 wherein M' is selected from Groups IVA, VIA, VIIIA, IIIB
and IVB.
5. The method of claim 4 wherein M' is selected from Ti, Cr, Fe, Co, Ni, B, Al and Si.
6. The method of any one of claims 1 to 5 wherein X' is selected from halides, hydrides, alkoxides of C1-6 and acetates.
7. The method of claim 6 wherein Y' is selected from amines, sulfides and alkyls of C1-15.
8. The method of any one of claims 1 to 7 wherein M'X'Y'n is selected chromium acetate, chromium nitrate, tetraethylorthosilicate, tetramethylorthosilicate, titanium tetraethoxide, aluminum isopropoxide, aluminum tri-sec-butoxide, hexamethyldisilazane, di-sec-butoxyaluminoxytriethoxysilane, diethylphosphatoethyltriethoxysilane, trimethylborate, chlorodimethylalkylsilane wherein alkyl is C1-18, ammonia-borane, borane-tetrahydrofuran, dimethylsulfide-dibr~oborane and mixtures thereof.
9. The method of any one of claims 1 to 8 wherein the crystalline phase material has a composition expressed as follows:
Mn/q(WaXbYcZdOh) wherein M is one or more ions; n is the charge of the composition excluding M expressed as oxides; q is the weighted molar average valence of M: n/q is the number of moles or mole fraction of M: W is one or more divalent elements; X is one or more trivalent elements: Y
is one or more tetravalent elements; Z is one or more pentavalent elements; a, b, c, and d are mole fractions of W, X, Y, and Z, respectively; h is a number of from 1 to 2.5; and (a+b+c+d)=1.
10. The method of any one of claims 1 to 9 wherein the crystalline phase material has a composition on an anhydrous basis, expressed as follows:
rRMn/q(Wa Xb Yc ZdOh) wherein R is the total organic material not included in M: r is the number of moles or mole fraction of R; M is one or more ions: n is the charge of the composition excluding M expressed as oxides; q is the weighted molar average valence of M: n/q is the number of moles or mole fraction of M; W is one or more divalent elements; X is one or more trivalent elements; Y is one or more tetravalent elements: Z
is one or more pentavalent elements; a, b, c, and d are mole fractions of W, X, Y, and Z, respectively; h is a number of from 1 to 2.5: and (a + b + c + d) = 1.
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Families Citing this family (60)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5378440A (en) * 1990-01-25 1995-01-03 Mobil Oil Corp. Method for separation of substances
US5304363A (en) * 1990-01-25 1994-04-19 Mobil Oil Corp. Porous materials
US5200058A (en) * 1990-01-25 1993-04-06 Mobil Oil Corp. Catalytic conversion over modified synthetic mesoporous crystalline material
US5370785A (en) * 1990-01-25 1994-12-06 Mobil Oil Corp. Hydrocarbon conversion process employing a porous material
US5308808A (en) * 1992-02-19 1994-05-03 United States Department Of Energy Organic or organometallic template mediated clay synthesis
US5364797A (en) * 1993-05-20 1994-11-15 Mobil Oil Corp. Sensor device containing mesoporous crystalline material
ZA944114B (en) * 1993-06-17 1995-02-07 Univ Queensland Kaolin derivatives
US5348687A (en) * 1993-11-26 1994-09-20 Mobil Oil Corp. M41S materials having nonlinear optical properties
DE4408302C2 (en) * 1994-03-11 1996-04-04 Zeochem Kft Process for the manufacture and use of a solid composite product for water treatment
US5560748A (en) * 1994-06-10 1996-10-01 The Procter & Gamble Company Detergent compositions comprising large pore size redox catalysts
DE19515932C2 (en) * 1995-05-02 2000-09-21 Feistel Gmbh Industrievertretu Use of a zeolite composite product
US6054052A (en) * 1995-12-14 2000-04-25 Mobil Oil Corporation Selective sorption of organics by metal-containing M41S
DE19543638A1 (en) * 1995-11-23 1997-05-28 Basf Ag Mesoporous molecular sieves
DE19781813B8 (en) * 1996-06-07 2006-12-07 Asahi Kasei Kabushiki Kaisha Mesoporous molecular sieve and process for its preparation
US5718878A (en) * 1996-07-12 1998-02-17 Akzo Nobel N.V. Mesoporous titania and process for its preparation
US5922299A (en) 1996-11-26 1999-07-13 Battelle Memorial Institute Mesoporous-silica films, fibers, and powders by evaporation
WO1998046353A1 (en) 1997-04-15 1998-10-22 Massachusetts Institute Of Technology Synthesis and application of vapor grafted porous materials
US5965474A (en) * 1997-04-29 1999-10-12 Mobil Oil Corporation FCC metal traps based on ultra large pore crystalline material
CN1073887C (en) * 1997-08-08 2001-10-31 北京燕化石油化工股份有限公司化工二厂 Catalyst for alkylation to prepare ethylbenzene, its preparation process, and new technology for preparing ethylbenzene by alkylation
US6331500B1 (en) 1997-08-25 2001-12-18 California Institute Of Technology Functionalized molecular sieves
DE19745905A1 (en) * 1997-10-17 1999-04-22 Hoechst Ag Supported catalysts with high sintering stability and process for their production
US6326326B1 (en) * 1998-02-06 2001-12-04 Battelle Memorial Institute Surface functionalized mesoporous material and method of making same
US5925330A (en) * 1998-02-13 1999-07-20 Mobil Oil Corporation Method of m41s functionalization of potentially catalytic heteroatom centers into as-synthesized m41s with concomitant surfactant extraction
US6319872B1 (en) * 1998-08-20 2001-11-20 Conoco Inc Fischer-Tropsch processes using catalysts on mesoporous supports
US6383466B1 (en) 1998-12-28 2002-05-07 Battelle Memorial Institute Method of dehydroxylating a hydroxylated material and method of making a mesoporous film
US6329017B1 (en) 1998-12-23 2001-12-11 Battelle Memorial Institute Mesoporous silica film from a solution containing a surfactant and methods of making same
US6096469A (en) * 1999-05-18 2000-08-01 3M Innovative Properties Company Ink receptor media suitable for inkjet printing
WO2001014060A2 (en) 1999-08-25 2001-03-01 Massachusetts Institute Of Technology Surface-confined catalytic compositions
US6930219B2 (en) * 1999-09-07 2005-08-16 Abb Lummus Global Inc. Mesoporous material with active metals
US20040089238A1 (en) * 1999-10-04 2004-05-13 Jerome Birnbaum Vacuum/gas phase reactor for dehydroxylation and alkylation of porous silica
FR2806643B1 (en) 2000-03-27 2002-05-03 Ceca Sa METHOD FOR THE SEPARATION OF GAS PHASE MOLECULES BY ADSORPTION USING AGGREGATED SOLID INORGANIC ADSORBENTS WITH NARROW AND CALIBRATED MESOPOROUS DISTRIBUTION
US6585863B2 (en) 2000-08-08 2003-07-01 Procter & Gamble Company Photocatalytic degradation of organic compounds
AUPR113700A0 (en) * 2000-10-31 2000-11-23 Australian Nuclear Science & Technology Organisation Transition metal oxide compositions
US6960551B2 (en) * 2002-08-23 2005-11-01 Exxonmobil Research And Engineering Company Functionalized periodic mesoporous materials, their synthesis and use
US6812373B2 (en) * 2002-12-12 2004-11-02 Exxonmobil Chemical Patents Inc. Modified metalloaluminophosphate molecular sieves
US6906233B2 (en) * 2002-12-12 2005-06-14 Exxon Mobil Chemical Patents Inc. Modified metalloaluminophosphate molecular sieves
US20060018966A1 (en) * 2003-07-22 2006-01-26 Lin Victor S Antimicrobial mesoporous silica nanoparticles
US7563451B2 (en) 2003-07-22 2009-07-21 Iowa State University Research Foundation, Inc. Capped mesoporous silicates
US20050033102A1 (en) * 2003-08-06 2005-02-10 Randolph Bruce B. Supported ionic liquid and the use thereof in the disproportionation of isopentane
US20050176978A1 (en) * 2003-12-15 2005-08-11 Verkade John G. Immobilized iminophosphatranes useful for transesterification
US7151073B2 (en) * 2004-01-16 2006-12-19 Exxonmobil Chemical Patents Inc. Mesoporous catalyst support, a catalyst system, and method of making and using same for olefin polymerization
KR100830726B1 (en) 2004-07-09 2008-05-20 아사히 가세이 케미칼즈 가부시키가이샤 Catalyst for cycloolefin production and process for production
JP2006069877A (en) * 2004-09-06 2006-03-16 Marukatsu Sangyo Kk Mesoporous titania
US7838461B2 (en) 2004-11-01 2010-11-23 Asahi Kasei Kabushiki Kaisha Catalyst for exhaust gas purification
US7494951B2 (en) 2005-08-15 2009-02-24 China Petroleum & Chemical Corporation Process for the manufacture of catalysts used for producing para-xylene by toluene shape selective alkylation
US7678955B2 (en) * 2005-10-13 2010-03-16 Exxonmobil Chemical Patents Inc Porous composite materials having micro and meso/macroporosity
JP2007222842A (en) * 2006-02-27 2007-09-06 Asahi Kasei Corp CATALYST FOR CLARIFYING EMITTED NOx, AND ITS CARRIER
US8383079B2 (en) * 2006-04-17 2013-02-26 Exxonmobil Chemical Patents Inc. Molecular sieves having micro and mesoporosity, their synthesis and their use in the organic conversion reactions
US8647644B1 (en) 2006-04-19 2014-02-11 Iowa State University Research Foundation, Inc. Methods of using capped mesoporous silicates
US20090191458A1 (en) * 2007-07-23 2009-07-30 Matsushita Electric Industrial Co., Ltd. Porous network negative electrodes for non-aqueous electrolyte secondary battery
TWI435765B (en) * 2007-12-27 2014-05-01 Exxonmobil Res & Eng Co Aromatic hydrogenation catalyst and process
WO2009114951A1 (en) * 2008-03-21 2009-09-24 Queen's University At Kingston Multi-channel electrospray emitter
KR100945020B1 (en) * 2008-03-27 2010-03-05 한국원자력연구원 Absorbent, preparation method thereof and Sr-90/Y-90 generator using the same
US20100087610A1 (en) * 2008-10-06 2010-04-08 Vaughn Stephen N Method Of Preparing And Using A Molecular Sieve
JP5426869B2 (en) * 2008-11-19 2014-02-26 パナソニック株式会社 Method for producing mesoporous silica fine particles, mesoporous silica fine particle-containing composition, and mesoporous silica fine particle-containing molded product
CN101804324B (en) * 2010-04-16 2012-06-20 南京大学 Modified molecular sieve with high selectivity to ammonia nitrogen in waste water and preparation method thereof
JP2010265174A (en) * 2010-07-27 2010-11-25 Asahi Kasei Chemicals Corp Modified mesoporous oxide
JP6196035B2 (en) * 2012-12-21 2017-09-13 千代田化工建設株式会社 Method for treating water containing water-insoluble substances
LU92783B1 (en) * 2015-07-22 2017-01-31 Luxembourg Inst Of Science And Tech (List) Highly aminated self-assembling fuctionalized Mesoporous Silicia Nanoparticles and methods of synthesis
EP3517500A1 (en) 2018-01-24 2019-07-31 Technische Universität Berlin A method for obtaining mesoporous silica particles with surface functionalisation

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3274120A (en) * 1964-02-20 1966-09-20 Cabot Corp Catalyst composition having increased hydroxyl groups bound thereto and method for producing same
US3725302A (en) * 1969-06-17 1973-04-03 Texaco Inc Silanized crystalline alumino-silicate
US3698157A (en) * 1971-06-01 1972-10-17 Mobil Oil Corp Separation of mixtures with modified zeolites
CA1051855A (en) * 1974-10-07 1979-04-03 David E.W. Vaughan Zeolite vk-2
ZA794221B (en) * 1978-09-05 1981-03-25 British Petroleum Co Process for the preparation of a functionalised solid product
US4292205A (en) * 1979-07-20 1981-09-29 Mobil Oil Corporation Ion exchange and impregnation of catalysts
DE3117135A1 (en) * 1981-04-30 1982-11-18 Bayer Ag, 5090 Leverkusen CRYSTALLINE ALUMOSILICATE, METHOD FOR THE PRODUCTION THEREOF AND THE USE THEREOF FOR CATALYTICALLY CONVERTING METHANOL AND / OR DIMETHYL ETHER IN HYDROCARBONS
US4390414A (en) * 1981-12-16 1983-06-28 Exxon Research And Engineering Co. Selective dewaxing of hydrocarbon oil using surface-modified zeolites
US4954325A (en) * 1986-07-29 1990-09-04 Mobil Oil Corp. Composition of synthetic porous crystalline material, its synthesis and use
EP0319538A1 (en) * 1986-08-22 1989-06-14 3i RESEARCH EXPLOITATION LIMITED Modification of zeolites
US4933161A (en) * 1987-02-04 1990-06-12 Exxon Research And Engineering Company Tin substitution into zeolite frameworks
JPH0761858B2 (en) * 1987-03-19 1995-07-05 日揮株式会社 Precision control of zeolite pore size
EP0321177B1 (en) * 1987-12-15 1994-08-03 Uop Substitution of Cr and/or Sn in place of A1 in the framework of molecular sieve via treatment with fluoride salts
CA2072352C (en) * 1990-01-25 1999-06-01 Jeffrey Scott Beck Synthetic porous crystalline material, its synthesis and use

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