# Patent

## Title
Porous inorganic/organic homogenous copolymeric hybrid materials for chromatographic separation and process for the preparation thereof

## Abstract

The present invention relates to porous inorganic/organic homogenous copolymeric hybrid material materials, including particulates and monoliths, methods for their manufacture, and uses thereof, e.g., as chromatographic separations materials.

## Background
RELATED APPLICATIONS
This application is a division of U.S. patent application Ser. No. 11/119,111, filed Apr. 29, 2005, which claims the benefit of and is a continuation of International Application No. PCT/US03/34776, filed Oct. 30, 2003 and designating the United States, which claims the benefit of and priority to U.S. Provisional Application No. 60/422,580, filed Oct. 30, 2002. The entire contents of these applications are incorporated herein by reference.


BACKGROUND OF THE INVENTION
Packing materials for liquid chromatography (LC) are generally classified into two types: organic materials, e.g., polydivinylbenzene, and inorganic materials, e.g., silica.
As stationary phases for HPLC, silica-based materials result in columns that do not show evidence of shrinking or swelling and are mechanically strong. However, limited hydrolytic stability is a drawback with silica-based columns, because silica may be readily dissolved under alkaline conditions, generally pH>8.0, leading to the subsequent collapse of the chromatographic bed. Additionally, the bonded phase on a silica surface may be removed from the surface under acidic conditions, generally pH<2.0, and eluted off the column by the mobile phase, causing loss of analyte retention.
On the other hand, many organic materials are chemically stable against strongly alkaline and strongly acidic mobile phases, allowing flexibility in the choice of mobile phase pH. However, organic chromatographic materials generally result in columns with low efficiency, leading to inadequate separation performance, particularly with low molecular-weight analytes. Furthermore, many organic chromatographic materials shrink and swell when the composition of the mobile phase is changed. In addition, most organic chromatographic materials do not have the mechanical strength of typical chromatographic silica.
In order to overcome the above-mentioned deficiencies while maintaining the beneficial properties of purely organic and purely inorganic materials, others have attempted to simply mix organic and inorganic materials. For example, others have previously attempted to produce such materials for optical sensors or gas separation membranes that are mixtures of organic polymers (e.g., poly(2-methyl-2-oxazoline), poly(N-vinylpyrrolidone), polystyrene, or poly(N,N-dimethylacrylamide) dispersed within silica. See, e.g., Chujo, Polymeric Materials: Science & Engineering, 84, 783 (2001); Tamaki, Polymer Bull., 39, 303 (1997); and Chujo, MRS Bull., 389 (May 2001). These materials, however, were not useful for any liquid based separation application because they are translucent and non-porous. As a result, these materials lack capacity as a separation material.
Still others have attempted to make materials that have inorganic and organic components covalently bound to each other. See, e.g., Feng, Q., J. Mater. Chem. 10, 2490-94 (2000), Feng, Q., Polym. Preprints 41, 515-16 (2000), Wei, Y., Adv. Mater. 12, 1448-50 (2000), Wei, Y. J. Polym. Sci. 18, 1-7 (2000). These materials, however, only contain very low amounts of organic material, i.e., less than 1% C, and as a result they function essentially as inorganic silica gels. Furthermore, these materials are non-porous until they are ground to irregular particles and then extracted to remove template porogen molecules. Accordingly, it is not possible to make porous monolithic materials that which have a useful capacity as a separation material. Also, irregularly-shaped particles are generally more difficult to pack than spherical particles. It is also known that columns packed with irregularly-shaped particles generally exhibit poorer packed bed stability than spherical particles of the same size. The template agents used in the synthesis of these materials are nonsurfactant optically active compounds, and the use of such compounds limits the range of porogen choices and increases their cost. The properties of these materials make them undesirable for use as LC packing materials.
SUMMARY OF THE INVENTION
The present invention provides a solution to the above-mentioned deficiencies. In particular, the present invention relates to a novel material for chromatographic separations, processes for its preparation, and separations devices containing the chromatographic material. For example, the invention pertains to a porous inorganic/organic homogenous copolymeric hybrid material having at least about 10% carbon content by mass. Also, the invention relates to a porous inorganic/organic homogenous copolymeric hybrid material of spherical particles. Additionally, the invention relates to a porous inorganic/organic homogenous copolymeric hybrid monolith material. The present invention provides porous inorganic/organic homogenous copolymeric hybrid materials of the formula:

(A)x(B)y(C)z 

wherein the order of repeat units A, B, and C may be random, block, or a combination of random and block;
A is an organic repeat unit which is covalently bonded to one or more repeat units A or B via an organic bond;
B is an organosiloxane repeat unit which is bonded to one or more repeat units B or C via an inorganic siloxane bond and which may be further bonded to one or more repeat units A or B via an organic bond;
C is an inorganic repeat unit which is bonded to one or more repeat units B or C via an inorganic bond; and
x, y are positive numbers and z is a non negative number, wherein
when z=0, then 0.002≦x/y≦210, and when z≠0, then
0.0003≦y/z≦500 and 0.002≦x/(y+z)≦210.
Certain other porous inorganic/organic homogenous copolymeric hybrid materials provided by the present invention include those materials of the formula:

(A)x(B)y(B*)y*(C)z 

wherein the order of repeat units A, B, B*, and C may be random, block, or a combination of random and block;
A is an organic repeat unit which is covalently bonded to one or more repeat units A or B via an organic bond;
B is an organosiloxane repeat unit which is bonded to one or more repeat units B, B* or C via an inorganic siloxane bond and which may be further bonded to one or more repeat units A or B via an organic bond;
B* is an organosiloxane repeat unit that does not have reactive (i.e., polymerizable) organic components and may further have a protected functional group that may be deprotected after polymerization;
C is an inorganic repeat unit which is bonded to one or more repeat units B or B* or C via an inorganic bond; and
x, y are positive numbers and z is a non negative number, wherein
when z=0, then 0.002≦x/(y+y*)≦210, and when z≠0, then
0.0003≦(y+y*)/z≦500 and 0.002≦x/(y+y*+z)≦210.
In particular, one aspect of the invention is a porous inorganic/organic homogenous copolymeric hybrid material (either a monolith or particles) of the formula:

(A)x(B)y(C)z  Formula I

wherein the order of repeat units A, B, and C may be random, block, or a combination of random and block; A is an organic repeat unit which is covalently bonded to one or more repeat units A or B via an organic bond (e.g., a polymerized olefin); B is an organosiloxane repeat unit which is bonded to one or more repeat units B or C via an inorganic siloxane bond and which may be further bonded to one or more repeat units A or B via an organic bond; C is an inorganic repeat unit which is bonded to one or more repeat units B or C via an inorganic bond; and 0.0003≦y/z≦500 and 0.002≦x/(y+z)≦210.

One skilled in the art will appreciate that such materials may have unreacted end groups, e.g., SiOH, Si(OH)2, or Si(OH)3, or unpolymerized olefins.
Additionally, the present invention relates to a novel material for chromatographic separations, processes for its preparation, and separations devices containing the chromatographic material. In particular, one aspect of the invention is a porous inorganic/organic homogenous copolymeric hybrid material of the formula:

(A)x(B)y(B*)y*(C)z  Formula II

wherein the order of repeat units A, B, B*, and C may be random, block, or a combination of random and block; and A, B, B*, C, x, y, and z are as defined above. The relative stoichiometry of the A to (B+B*) to C components is the same as above, e.g, 0.0003≦(y+y*)/z≦500 and 0.002≦x/(y+y*+z)≦210.

Repeat unit A may be derived from a variety of organic monomer reagents possessing one or more polymerizable moieties, capable of undergoing polymerization, e.g., a free radical-mediated polymerization. A monomers may be oligomerized or polymerized by a number of processes and mechanisms including, but not limited to, chain addition and step condensation processes, radical, anionic, cationic, ring-opening, group transfer, metathesis, and photochemical mechanisms.
Repeat unit B may be derived from several mixed organic-inorganic monomer reagents possessing two or more different polymerizable moieties, capable of undergoing polymerization, e.g., a free radical-mediated (organic) and hydrolytic (inorganic) polymerization. B monomers may be oligomerized or polymerized by a number of processes and mechanisms including, but not limited to, chain addition and step condensation processes, radical, anionic, cationic, ring-opening, group transfer, metathesis, and photochemical mechanisms.
Repeat unit C may be —SiO2— and may be derived from an alkoxysilane, such as tetraethoxysilane (TEOS) or tetramethoxysilane (TMOS).
Another aspect of the invention is a porous inorganic/organic homogenous copolymeric hybrid material of the formula:

(A)x(B)y  Formula III

wherein the order of repeat units A and B may be random, block, or a combination of random and block; A is an organic repeat unit which is covalently bonded to one or more repeat units A or B via an organic bond (e.g., a polymerized olefin); B is an organosiloxane repeat unit which may or may not be bonded to one or more repeat units B via an inorganic siloxane bond and which may be further bonded to one or more repeat units A or B via an organic bond; and 0.002≦x/y≦210.

Repeat unit A may be derived from a variety of organic monomer reagents possessing one or more polymerizable moieties, capable of undergoing polymerization, e.g., a free radical-mediated polymerization. A monomers may be oligomerized or polymerized by a number of processes and mechanisms including, but not limited to, chain addition and step condensation processes, radical, anionic, cationic, ring-opening, group transfer, metathesis, and photochemical mechanisms.
Repeat unit B may be derived from several mixed organic-inorganic monomer reagents possessing two or more different polymerizable moieties, capable of undergoing polymerization, e.g., a free radical-mediated (organic) and hydrolytic (inorganic) polymerization. B monomers may be oligomerized or polymerized by a number of processes and mechanisms including, but not limited to, chain addition and step condensation processes, radical, anionic, cationic, ring-opening, group transfer, metathesis, and photochemical mechanisms.
One skilled in the art will appreciate that such materials may have unreacted end groups, e.g., SiOR, Si(OR)2, or Si(OR)3, where R═H or C1-C5 alkane, or unpolymerized olefins.
Another aspect of the invention is a porous inorganic/organic homogenous copolymeric hybrid material of the formula:

(A)x(B)y(B*)y*  Formula IV

wherein the order of repeat units A, B, and B* may be random, block, or a combination of random and block; A is an organic repeat unit which is covalently bonded to one or more repeat units A or B via an organic bond (e.g., a polymerized olefin); B is an organosiloxane repeat unit which may or may not be bonded to one or more repeat units B or B* via an inorganic siloxane bond and which may be further bonded to one or more repeat units A or B via an organic bond; B* is an organosiloxane repeat unit that does not have reactive (i.e., polymerizable) organic components and may further have a protected functional group that may be deprotected after polymerization. The relative stoichiometry of the A to (B+B*) components is the same as above, e.g., 0.002≦x/(y+y*)≦210.

Repeat unit A may be derived from a variety of organic monomer reagents possessing one or more polymerizable moieties, capable of undergoing polymerization, e.g., a free radical-mediated polymerization. A monomers may be oligomerized or polymerized by a number of processes and mechanisms including, but not limited to, chain addition and step condensation processes, radical, anionic, cationic, ring-opening, group transfer, metathesis, and photochemical mechanisms.
Repeat unit B may be derived from several mixed organic-inorganic monomer reagents possessing two or more different polymerizable moieties, capable of undergoing polymerization, e.g., a free radical-mediated (organic) and hydrolytic (inorganic) polymerization. B monomers may be oligomerized or polymerized by a number of processes and mechanisms including, but not limited to, chain addition and step condensation processes, radical, anionic, cationic, ring-opening, group transfer, metathesis, and photochemical mechanisms.
One skilled in the art will appreciate that such materials may have unreacted end groups, e.g., SiOR, Si(OR)2, or Si(OR)3, where R═H or C1-C5 alkane, or unpolymerized olefins.
By way of example, the present invention pertains to a porous inorganic/organic homogenous copolymeric hybrid material of the formula:




where R1 is H, F, Cl, Br, I, lower alkyl (e.g., CH3 or CH2CH3); R2 and R3 are each independently H, F, Cl, Br, I, alkane, substituted alkane, alkene, substituted alkene, aryl, substituted aryl, cyano, ether, substituted ether, embedded polar group; R4 and R5 are each independently H, F, Cl, Br, I, alkane, substituted alkane, alkene, substituted alkene, aryl, substituted aryl, ether, substituted ether, cyano, amino, substituted amino, diol, nitro, sulfonic acid, cation or anion exchange groups, 0≦a≦2x, 0≦b≦4, and 0≦c≦4, provided that b+c≦4 when a=1; 1≦d≦20, and 0.0003≦y/z≦500 and 0.002≦x/(y+z)≦210.

The invention also relates to porous inorganic/organic homogenous copolymeric hybrid materials prepared, e.g., by the steps of copolymerizing an organic olefin monomer with an alkenyl-functionalized organosiloxane, and hydrolytic condensation of the product of the other step with a tetraalkoxysilane. The copolymerizing and condensation steps may be performed substantially simultaneously or sequentially.
The material of the invention may be used as a liquid chromatography stationary phase; a sequestering reagent; a solid support for combinatorial chemistry; a solid support for oligosaccharide, polypeptide, or oligonucleotide synthesis; a solid support for a biological assay; a capillary biological assay device for mass spectrometry; a template for a controlled large pore polymer film; a capillary chromatography stationary phase; an electrokinetic pump packing material; a polymer additive; a catalyst; or a packing material for a microchip separation device.



BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a plot of the mechanical strength results for two porous inorganic/organic homogenous copolymeric hybrid materials of the invention (Examples 3b and 3v; 3 μm fractions), commercially available silica based (5 μm Symmetry® C18, Waters Corporation) and polymeric based (7 μm UltrastyragelTM 106 Å and 7 μm UltrastyragelTM 104 Å, Waters Corporation) materials wherein the FIGURE legend is A=Symmetry® C18, B=3 μm Example 3b, C=3 μm Example 3v, D=7 μm UltrastyragelTM 106 Å, E=7 μm UltrastyragelTM 104 Å.



DETAILED DESCRIPTION OF THE INVENTION
The present invention will be more fully illustrated by reference to the definitions set forth below.
The term “monolith” is intended to include a porous, three-dimensional material having a continuous interconnected pore structure in a single piece. A monolith is prepared, for example, by casting precursors into a mold of a desired shape. The term monolith is meant to be distinguished from a collection of individual particles packed into a bed formation, in which the end product comprises individual particles. Such monolith materials are described in detail in international patent application number PCT/US02/25193, filed Aug. 8, 2002, and U.S. provisional patent application No. 60/311,445, filed Aug. 9, 2001, both of which are incorporated herein by reference.
The terms “coalescing” and “coalesced” are intended to describe a material in which several individual components have become coherent to result in one new component by an appropriate chemical or physical process, e.g., heating. The term coalesced is meant to be distinguished from a collection of individual particles in close physical proximity, e.g., in a bed formation, in which the end product comprises individual particles.
As used herein, the term “porous inorganic/organic homogenous copolymeric hybrid material” or “porous inorganic/organic homogenous copolymeric hybrid monolith material” includes materials comprising inorganic repeat units (e.g., comprising O—Si—O bonds between repeat units), organic repeat units (e.g., comprising C—C bonds between repeat units), and mixed organic-inorganic repeat units (e.g., comprising both C—C and O—Si—O bonds between repeat units). The term “porous” indicates that the microscopic structure of the material contains pores of a measurable volume, so that the materials can be used, for example, as solid supports in chromatography. The term “inorganic/organic copolymeric hybrid” indicates that the material comprises a copolymer of organic, inorganic, and mixed organic/inorganic repeat units. The term “homogenous” indicates that the structure of the material at the chemical level is substantially interconnected via chemical bonds, as opposed to the prior art materials that simply comprise mixtures of discrete organic and inorganic materials. The term “hybrid” refers to a material having chemical bonds among inorganic and organic repeat units of a composite material thereby forming a matrix throughout the material itself, as opposed to a mixture of discrete chemical compounds.
Polyorganoalkoxysiloxane (POS) and polyalkylalkoxysiloxane (PAS) are large molecules, either linear or preferably three-dimensional networks, that are formed by the condensation of silanols, where the silanols are formed, e.g., by hydrolysis of halo- or alkoxy-substituted silanes.
As used herein, the term “protecting group” means a protected functional group which may be intended to include chemical moieties that shield a functional group from chemical reaction or interaction such that upon later removal (“deprotection”) of the protecting group, the functional group can be revealed and subjected to further chemistry. For example, a monomer used in the synthesis of the materials of the present invention may contain The term also includes a functional group which that does not interfere with the various polymerization and condensation reactions used in the synthesis of the materials of the invention, but which that may be converted after synthesis of the material into a functional group which that may itself be further derivatized. For example, an organic monomer reagent A may contain an aromatic nitro group which that would not interfere with the polymerization or condensation reactions. However, after these polymerization and condensation reactions have been carried out, the nitro group may be reduced to an amino group (e.g., an aniline), which itself may then be subjected to further derivatization by a variety of means known in the art. In this manner, additional functional groups may be incorporated into the material after the syntheses of the material itself. See generally, Greene, T. W. and Wuts, P. G. M. “Protective Groups in Organic Synthesis,” Second Edition, Wiley, 1991. In some cases, preferable protecting groups strategies do not involve the use of heavy metals (e.g., transition metals) in the protection or deprotection step as these metals may be difficult to remove from the material completely.
The porous inorganic/organic homogenous copolymeric hybrid particles and monolith materials possess both organic groups and silanol groups which may additionally be substituted or derivatized with a surface modifier. “Surface modifiers” include (typically) organic groups which impart a certain chromatographic functionality to a chromatographic stationary phase. Surface modifiers such as disclosed herein are attached to the base material, e.g., via derivatization or coating and later crosslinking, imparting the chemical character of the surface modifier to the base material. In one embodiment, the organic groups of the hybrid materials react to form an organic covalent bond with a surface modifier. The modifiers may form an organic covalent bond to the material's organic group via a number of mechanisms well known in organic and polymer chemistry including, but not limited to, nucleophilic, electrophilic, cycloaddition, free-radical, carbene, nitrene, and carbocation reactions. Organic covalent bonds are defined to involve the formation of a covalent bond between the common elements of organic chemistry including, but not limited to, hydrogen, boron, carbon, nitrogen, oxygen, silicon, phosphorus, sulfur, and the halogens. In addition, carbon-silicon and carbon-oxygen-silicon bonds are defined as organic covalent bonds, whereas silicon-oxygen-silicon bonds that are not defined as organic covalent bonds. In general, the porous inorganic/organic homogenous copolymeric hybrid particles and monolith materials may be modified by an organic group surface modifier, a silanol group surface modifier, a polymeric coating surface modifier, and combinations of the aforementioned surface modifiers.
For example, silanol groups are surface modified with compounds having the formula Za(R′)bSi—R, where Z═Cl, Br, I, C1-C5 alkoxy, dialkylamino, e.g., dimethylamino, or trifluoromethanesulfonate; a and b are each an integer from 0 to 3 provided that a+b=3; R′ is a C1-C6 straight, cyclic or branched alkyl group, and R is a functionalizing group. R′ may be, e.g., methyl, ethyl, propyl, isopropyl, butyl, t-butyl, sec-butyl, pentyl, isopentyl, hexyl or cyclohexyl; preferably, R′ is methyl. In certain embodiments, the organic groups may be similarly functionalized.
The functionalizing group R may include alkyl, aryl, cyano, amino, diol, nitro, cation or anion exchange groups, or embedded polar functionalities. Examples of suitable R functionalizing groups include C1-C30 alkyl, including C1-C20, such as octyl (C8), octadecyl (C18), and triacontyl (C30); alkaryl, e.g., C1-C4-phenyl; cyanoalkyl groups, e.g., cyanopropyl; diol groups, e.g., propyldiol; amino groups, e.g., aminopropyl; and alkyl or aryl groups with embedded polar functionalities, e.g., carbamate functionalities such as disclosed in U.S. Pat. No. 5,374,755, the text of which is incorporated herein by reference. Such groups include those of the general formula




wherein l, m, o, r, and s are 0 or 1, n is 0, 1, 2 or 3 p is 0, 1, 2, 3 or 4 and q is an integer from 0 to 19; R3 is selected from the group consisting of hydrogen, alkyl, cyano and phenyl; and Z, R′, a and b are defined as above. Preferably, the carbamate functionality has the general structure indicated below:





wherein R5 may be, e.g., cyanoalkyl, t-butyl, butyl, octyl, dodecyl, tetradecyl, octadecyl, or benzyl. Advantageously, R5 is octyl, dodecyl, or octadecyl.

In a preferred embodiment, the surface modifier may be an organotrihalosilane, such as octyltrichlorosilane or octadecyltrichlorosilane. In an additional preferred embodiment, the surface modifier may be a halopolyorganosilane, such as octyldimethylchlorosilane or octadecyldimethylchlorosilane. In certain embodiments the surface modifier is octadecyltrimethoxysilane or octadecyltrichlorosilane.
In another embodiment, the hybrid material's organic groups and silanol groups are both surface modified or derivatized. In another embodiment, the hybrid materials are surface modified by coating with a polymer.
The term “aliphatic group” includes organic compounds characterized by straight or branched chains, typically having between 1 and 22 carbon atoms. Aliphatic groups include alkyl groups, alkenyl groups and alkynyl groups. In complex structures, the chains may be branched or cross-linked. Alkyl groups include saturated hydrocarbons having one or more carbon atoms, including straight-chain alkyl groups and branched-chain alkyl groups. Such hydrocarbon moieties may be substituted on one or more carbons with, for example, a halogen, a hydroxyl, a thiol, an amino, an alkoxy, an alkylcarboxy, an alkylthio, or a nitro group. Unless the number of carbons is otherwise specified, “lower aliphatic” as used herein means an aliphatic group, as defined above (e.g., lower alkyl, lower alkenyl, lower alkynyl), but having from one to six carbon atoms. Representative of such lower aliphatic groups, e.g., lower alkyl groups, are methyl, ethyl, n-propyl, isopropyl, 2-chloropropyl, n-butyl, sec-butyl, 2-aminobutyl, isobutyl, tert-butyl, 3-thiopentyl, and the like. As used herein, the term “nitro” means —NO2; the term “halogen” designates —F, —Cl, —Br or —I; the term “thiol” means SH; and the term “hydroxyl” means —OH. Thus, the term “alkylamino” as used herein means an alkyl group, as defined above, having an amino group attached thereto. Suitable alkylamino groups include groups having 1 to about 12 carbon atoms, preferably from 1 to about 6 carbon atoms. The term “alkylthio” refers to an alkyl group, as defined above, having a sulfhydryl group attached thereto. Suitable alkylthio groups include groups having 1 to about 12 carbon atoms, preferably from 1 to about 6 carbon atoms. The term “alkylcarboxyl” as used herein means an alkyl group, as defined above, having a carboxyl group attached thereto. The term “alkoxy” as used herein means an alkyl group, as defined above, having an oxygen atom attached thereto. Representative alkoxy groups include groups having 1 to about 12 carbon atoms, preferably 1 to about 6 carbon atoms, e.g., methoxy, ethoxy, propoxy, tert-butoxy and the like. The terms “alkenyl” and “alkynyl” refer to unsaturated aliphatic groups analogous to alkyls, but which contain at least one double or triple bond respectively. Suitable alkenyl and alkynyl groups include groups having 2 to about 12 carbon atoms, preferably from 1 to about 6 carbon atoms.
The term “alicyclic group” includes closed ring structures of three or more carbon atoms. Alicyclic groups include cycloparaffins or naphthenes which are saturated cyclic hydrocarbons, cycloolefins which are unsaturated with two or more double bonds, and cycloacetylenes which have a triple bond. They do not include aromatic groups. Examples of cycloparaffins include cyclopropane, cyclohexane, and cyclopentane. Examples of cycloolefins include cyclopentadiene and cyclooctatetraene. Alicyclic groups also include fused ring structures and substituted alicyclic groups such as alkyl substituted alicyclic groups. In the instance of the alicyclics such substituents may further comprise a lower alkyl, a lower alkenyl, a lower alkoxy, a lower alkylthio, a lower alkylamino, a lower alkylcarboxyl, a nitro, a hydroxyl, —CF3, —CN, or the like.
The term “heterocyclic group” includes closed ring structures in which one or more of the atoms in the ring is an element other than carbon, for example, nitrogen, sulfur, or oxygen. Heterocyclic groups may be saturated or unsaturated and heterocyclic groups such as pyrrole and furan may have aromatic character. They include fused ring structures such as quinoline and isoquinoline. Other examples of heterocyclic groups include pyridine and purine. Heterocyclic groups may also be substituted at one or more constituent atoms with, for example, a halogen, a lower alkyl, a lower alkenyl, a lower alkoxy, a lower alkylthio, a lower alkylamino, a lower alkylcarboxyl, a nitro, a hydroxyl, —CF3, —CN, or the like. Suitable heteroaromatic and heteroalicyclic groups generally will have 1 to 3 separate or fused rings with 3 to about 8 members per ring and one or more N, O or S atoms, e.g., coumarinyl, quinolinyl, pyridyl, pyrazinyl, pyrimidyl, furyl, pyrrolyl, thienyl, thiazolyl, oxazolyl, imidazolyl, indolyl, benzofuranyl, benzothiazolyl, tetrahydrofuranyl, tetrahydropyranyl, piperidinyl, morpholino and pyrrolidinyl.
The term “aromatic group” includes unsaturated cyclic hydrocarbons containing one or more rings. Aromatic groups include 5- and 6-membered single-ring groups which may include from zero to four heteroatoms, for example, benzene, pyrrole, furan, thiophene, imidazole, oxazole, thiazole, triazole, pyrazole, pyridine, pyrazine, pyridazine and pyrimidine, and the like. The aromatic ring may be substituted at one or more ring positions with, for example, a halogen, a lower alkyl, a lower alkenyl, a lower alkoxy, a lower alkylthio, a lower alkylamino, a lower alkylcarboxyl, a nitro, a hydroxyl, —CF3, —CN, or the like.
The term “alkyl” includes saturated aliphatic groups, including straight-chain alkyl groups, branched-chain alkyl groups, cycloalkyl (alicyclic) groups, alkyl substituted cycloalkyl groups, and cycloalkyl substituted alkyl groups. In certain embodiments, a straight chain or branched chain alkyl has 30 or fewer carbon atoms in its backbone, e.g., C1-C30 for straight chain or C3-C30 for branched chain. In certain embodiments, a straight chain or branched chain alkyl has 20 or fewer carbon atoms in its backbone, e.g., C1-C20 for straight chain or C3-C20 for branched chain, and more preferably 18 or fewer. Likewise, preferred cycloalkyls have from 4-10 carbon atoms in their ring structure, and more preferably have 4-7 carbon atoms in the ring structure. The term “lower alkyl” refers to alkyl groups having from 1 to 6 carbons in the chain, and to cycloalkyls having from 3 to 6 carbons in the ring structure.
Moreover, the term “alkyl” (including “lower alkyl”) as used throughout the specification and claims includes both “unsubstituted alkyls” and “substituted alkyls,” the latter of which refers to alkyl moieties having substituents replacing a hydrogen on one or more carbons of the hydrocarbon backbone. Such substituents may include, for example, halogen, hydroxyl, alkylcarbonyloxy, arylcarbonyloxy, alkoxycarbonyloxy, aryloxycarbonyloxy, carboxylate, alkylcarbonyl, alkoxycarbonyl, aminocarbonyl, alkylthiocarbonyl, alkoxyl, phosphate, phosphonato, phosphinato, cyano, amino (including alkyl amino, dialkylamino, arylamino, diarylamino, and alkylarylamino), acylamino (including alkylcarbonylamino, arylcarbonylamino, carbamoyl and ureido), amidino, imino, sulfhydryl, alkylthio, arylthio, thiocarboxylate, sulfate, sulfonato, sulfamoyl, sulfonamido, nitro, trifluoromethyl, cyano, azido, heterocyclyl, aralkyl, or an aromatic or heteroaromatic moiety. It will be understood by those skilled in the art that the moieties substituted on the hydrocarbon chain may themselves be substituted, if appropriate. Cycloalkyls may be further substituted, e.g., with the substituents described above. An “aralkyl” moiety is an alkyl substituted with an aryl, e.g., having 1 to 3 separate or fused rings and from 6 to about 18 carbon ring atoms, e.g., phenylmethyl (benzyl).
The term “aryl” includes 5- and 6-membered single-ring aromatic groups that may include from zero to four heteroatoms, for example, unsubstituted or substituted benzene, pyrrole, furan, thiophene, imidazole, oxazole, thiazole, triazole, pyrazole, pyridine, pyrazine, pyridazine and pyrimidine, and the like. Aryl groups also include polycyclic fused aromatic groups such as naphthyl, quinolyl, indolyl, and the like. The aromatic ring may be substituted at one or more ring positions with such substituents, e.g., as described above for alkyl groups. Suitable aryl groups include unsubstituted and substituted phenyl groups. The term “aryloxy” as used herein means an aryl group, as defined above, having an oxygen atom attached thereto. The term “aralkoxy” as used herein means an aralkyl group, as defined above, having an oxygen atom attached thereto. Suitable aralkoxy groups have 1 to 3 separate or fused rings and from 6 to about 18 carbon ring atoms, e.g., O-benzyl.
The term “amino,” as used herein, refers to an unsubstituted or substituted moiety of the formula —NRaRb, in which Ra and Rb are each independently hydrogen, alkyl, aryl, or heterocyclyl, or Ra and Rb, taken together with the nitrogen atom to which they are attached, form a cyclic moiety having from 3 to 8 atoms in the ring. Thus, the term “amino” includes cyclic amino moieties such as piperidinyl or pyrrolidinyl groups, unless otherwise stated. An “amino-substituted amino group” refers to an amino group in which at least one of Ra and Rb, is further substituted with an amino group.
Porous inorganic/organic homogenous copolymeric hybrid material of the invention may be made as described below and in the specific instances illustrated in the Examples. Porous spherical particles of hybrid silica may, in one embodiment, be prepared by the steps of (a) hydrolytically condensing an alkenyl-functionalized organosilane with a tetraalkoxysilane, (b) copolymerizing the product of step (a) with an organic olefin monomer, and (c) further hydrolytically condensing the product of step (b) to thereby prepare a porous inorganic/organic homogenous copolymeric hybrid material. In this embodiment, steps (b) and (c) may be performed substantially simultaneously. Steps (a) and (b) may be performed in the same reaction vessel.
Alternatively, the materials of the invention may be prepared by the steps of (a) copolymerizing an organic olefin monomer with an alkenyl-functionalized organosilane, and (b) hydrolytically condensing the product of step (a) with a tetraalkoxysilane in the presence of a non-optically active porogen to thereby prepare a porous inorganic/organic homogenous copolymeric hybrid material. Steps (a) and (b) may be performed in the same reaction vessel.
Also, the materials may be prepared by the steps of substantially simultaneously copolymerizing an organic monomer with an alkenyl-functionalized organosilane and hydrolytically condensing said alkenyl-functionalized organosilane with a tetraalkoxysilane to thereby prepare a porous inorganic/organic homogenous copolymeric hybrid material.
The copolymerizing step of the foregoing methods may be free radical-initiated and the hydrolytically condensing step of the foregoing methods may by acid- or base-catalyzed. In the case of acid catalysis, the acid may be, e.g., hydrochloric acid, hydrobromic acid, hydrofluoric acid, hydroiodic acid, sulfuric acid, formic acid, acetic acid, trichloroacetic acid, trifluoroacetic acid, or phosphoric acid. Likewise, in the case of base catalysis, the base may be ammonium hydroxide, hydroxide salts of the group I and group II metals, carbonate and hydrogencarbonate salts of the group I metals, or alkoxide salts of the group I and group II metals. In the case of free radical-mediated polymerizations, a free radical polymerization initiator may be added. Suitable examples of free radical polymerization initiator include 2,2′-azobis-[2-(imidazolin-2-yl)propane]dihydrochloride, 2,2′-azobisisobutyronitrile, 4,4′-azobis(4-cyanovaleric acid), 1,1′-azobis(cyclohexanecarbonitrile), 2,2′-azobis(2-propionamidine) dihydrochloride, 2,2′azobis(2,4-dimethylpentanenitrile), 2,2′-azobis(2-methylbutanenitrile), benzoyl peroxide, 2,2-bis(tert-butylperoxy)butane, 1,1-bis(tert-butylperoxy)cyclohexane, 2,5-bis(tert-butylperoxy)butane,-2,5-dimethylhexane, 2,5-bis(tert-butylperoxy)-2,5-dimethyl-hexyne, bis(1-(tert-butylperoxy)-1-methyethyl)benzene, 1,1-bis(tert-butylperoxy)-3,3,5-trimethylcyclohexane, tert-butyl hydroperoxide, tert-butyl peracetate, tert-butyl peroxide, tert-butyl peroxybenzoate, tert-butylperoxy isopropyl carbonate, cumene peroxide, cyclohexanone hydroperoxide, dicumyl peroxide, lauroyl peroxide, 2,4-pentanedione peroxide, peracetic acid, and potassium persulfate. Additionally, the reaction may be heated following the addition of the free radical polymerization initiator.
The solvent used in the synthesis of the materials of the invention may be, e.g, water, methanol, ethanol, propanol, isopropanol, butanol, tert-butanol, pentanol, hexanol, cyclohexanol, hexafluoroisopropanol, cyclohexane, petroleum ethers, diethyl ether, dialkyl ethers, tetrahydrofuran, acetonitrile, ethyl acetate, pentane, hexane, heptane, benzene, toluene, xylene, N,N-dimethylformamide, dimethyl sulfoxide, 1-methyl-2-pyrrolidinone, methylene chloride, chloroform, and combinations thereof, although those skilled in the art will readily appreciate that others may be used.
In the synthesis of the materials of the invention, a porogen may be used. Examples of suitable porogens include cyclohexanol, toluene, 2-ethylhexanoic acid, dibutylphthalate, 1-methyl-2-pyrrolidinone, 1-dodecanol, and Triton X-45.
Some examples of organic olefin monomers of the invention include divinylbenzene, styrene, ethylene glycol dimethacrylate, 1-vinyl-2-pyrrolidinone and tert-butylmethacrylate, acrylamide, methacrylamide, N,N′-(1,2-dihydroxyethylene)bisacrylamide, N,N′-ethylenebisacrylamide, N,N′-methylenebisacrylamide, butyl acrylate, ethyl acrylate, methyl acrylate, 2-(acryloxy)-2-hydroxypropyl methacrylate, 3-(acryloxy)-2-hydroxypropyl methacrylate, trimethylolpropane triacrylate, trimethylolpropane ethoxylate triacrylate, tris[(2-acryloyloxy)ethyl] isocyanurate, acrylonitrile, methacrylonitrile, itaconic acid, methacrylic acid, trimethylsilylmethacrylate, N-[tris(hydroxymethyl)methyl]acrylamide (THMMA) (3-acrylamidopropyl)trimethylammonium chloride (APTA), [3-(methacryloylamino)propyl]dimethyl(3-sulfopropyl)ammonium hydroxide inner salt (MAPDAHI),




Some examples of alkenyl-functionalized organosiloxane monomers include methacryloxypropyltrimethoxysilane, methacryloxypropyltriethoxysilane, vinyltriethoxysilane, vinyltrimethoxysilane, N-(3-acryloxy-2-hydroxypropyl)-3-aminopropyltriethoxysilane, (3-acryloxypropyl)trimethoxysilane, O-(methacryloxyethyl)-N-(triethoxysilylpropyl)urethane, N-(3-methacryloxy-2-hydroxypropyl)-3-aminopropyltriethoxysilane, methacryloxymethyltriethoxysilane, methacryloxymethyltrimethoxysilane, methacryloxypropylmethyldiethoxysilane, methacryloxypropylmethyldimethoxysilane, methacryloxypropyltris(methoxyethoxy)silane, 3-(N-styrylmethyl-2-aminoethylamino)propyltrimethoxysilane hydrochloride,




wherein each R is independently H or a C1-C10 alkyl group (preferably hydrogen, methyl, ethyl, or propyl) and wherein R′ is independently H or a C1-C10 alkyl group (preferably hydrogen or methyl, ethyl, or propyl). Also, the R groups may be identical and selected from the group consisting of hydrogen, methyl, ethyl, or propyl.

Some examples of tetraalkoxysilanes include tetramethoxysilane, tetraethoxysilane, tetrapropoxysilane, tetrabutoxysilane.
The methods of the invention may also comprise adding a surfactant or stabilizer. Suitable examples of surfactants include Triton X-45, sodium dodecylsulfate, tris(hydroxymethyl)aminomethane, and any combination thereof. Still other examples of surfactants include Triton X100, Triton X305, TLS, Pluronic F-87, Pluronic P-105, Pluronic P-123, sodium dodecylsulfate (SDS), and Triton X-405. Examples of stabilizers include methocel and poly(vinyl alcohol).
The method of the invention may also include a step of endcapping free silanol groups according to methods which are readily known in the art.
The methods of the invention may also include a step of chemically modifying the organic olefin or alkenyl-functionalized organisiloxane prior to copolymerization.
Additionally, the methods of the invention may also include a step of modifying surfaces of the hybrid particles by formation of an organic covalent bond between an organic group of the particle and a surface modifier. In this regard, the method may include a further step of by adding a surface modifier selected from the group consisting of an organic group surface modifier, a silanol group surface modifier, a polymeric coating surface modifier, and combinations thereof, such as Za(R′)bSi—R, as described herein above. Likewise, the surface modifier may be a polymer coating, such as Sylgard®. Other examples of reagents include octyltrichlorosilane, octadecyltrichlorosilane, octyldimethylchlorosilane, and octadecyldimethylchlorosilane.
In one embodiment of the invention, the surface organic groups of the hybrid silica are derivatized or modified in a subsequent step via formation of an organic covalent bond between the particle's organic group and the modifying reagent. Alternatively, the surface silanol groups of the hybrid silica are derivatized into siloxane organic groups, such as by reacting with an organotrihalosilane, e.g., octadecyltrichlorosilane, or a halopolyorganosilane, e.g., octadecyldimethylchlorosilane. Alternatively, the surface organic and silanol groups of the hybrid silica are both derivatized. The surface of the thus-prepared material is then covered by the organic groups, e.g., alkyl, embedded during the gelation and the organic groups added during the derivatization process or processes.
In one embodiment, the pore structure of the as-prepared hybrid material is modified by hydrothermal treatment, which enlarges the openings of the pores as well as the pore diameters, as confirmed by nitrogen (N2) sorption analysis. The hydrothermal treatment is performed by preparing a slurry containing the as-prepared hybrid material and a solution of organic base in water, heating the slurry in an autoclave at an elevated temperature, e.g., about 143 to 168° C., for a period of about 6 to 28 h. The pH of the slurry can be adjusted to be in the range of about 8.0 to 12.7 using tetraethylammonium hydroxide (TEAH) or TRIS and concentrated acetic acid. The concentration of the slurry is in the range of about 1 g hybrid material per 5 to 10 mL of the base solution. The thus-treated hybrid material is filtered, and washed with water until the pH of the filtrate reaches about 7, washed with acetone or methanol, then dried at about 100° C. under reduced pressure for about 16 h. The resultant hybrid materials show average pore diameters in the range of about 100-300 Å. The surface of the hydrothermally treated hybrid material may be modified in a similar fashion to that of the hybrid material that is not modified by hydrothermal treatment as described in the present invention.
Moreover, the surface of the hydrothermally treated hybrid silica contains organic groups, which can be derivatized by reacting with a reagent that is reactive towards the hybrid materials' organic group. For example, vinyl groups on the material can be reacted with a variety of olefin reactive reagents such as bromine (Br2), hydrogen (H2), free radicals, propagating polymer radical centers, dienes, and the like. In another example, hydroxyl groups on the material can be reacted with a variety of alcohol reactive reagents such as isocyanates, carboxylic acids, carboxylic acid chlorides, and reactive organosilanes as described below. Reactions of this type are well known in the literature, see, e.g., March, J. “Advanced Organic Chemistry,” 3rd Edition, Wiley, New York, 1985; Odian, G. “The Principles of Polymerization,” 2nd Edition, Wiley, New York, 1981; the texts of which are incorporated herein by reference.
In addition, the surface of the hydrothermally treated hybrid silica also contains silanol groups, which can be derivatized by reacting with a reactive organosilane. The surface derivatization of the hybrid silica is conducted according to standard methods, for example by reaction with octadecyltrichlorosilane or octadecyldimethylchlorosilane in an organic solvent under reflux conditions. An organic solvent such as toluene is typically used for this reaction. An organic base such as pyridine or imidazole is added to the reaction mixture to catalyze the reaction. The product of this reaction is then washed with water, toluene and acetone and dried at about 80° C. to 100° C. under reduced pressure for about 16 h. The resultant hybrid silica can be further reacted with a short-chain silane such as trimethylchlorosilane to endcap the remaining silanol groups, by using a similar procedure described above.
More generally, the surface of the hybrid silica materials may be surface modified with a surface modifier, e.g., Za(R′)bSi—R, as described herein above.
The functionalizing group R may include alkyl, alkenyl, alkynyl, aryl, cyano, amino, diol, nitro, cation or anion exchange groups, or alkyl or aryl groups with embedded polar functionalities. Examples of suitable R functionalizing groups include C1-C30 alkyl, including C1-C20, such as octyl (C8), octadecyl (C18), and triacontyl (C30); alkaryl, e.g., C1-C4-phenyl; cyanoalkyl groups, e.g., cyanopropyl; diol groups, e.g., propyldiol; amino groups, e.g., aminopropyl; and alkyl or aryl groups with embedded polar functionalities, e.g., carbamate functionalities such as disclosed in U.S. Pat. No. 5,374,755, the text of which is incorporated herein by reference, and as detailed hereinabove. In a preferred embodiment, the surface modifier may be an organotrihalosilane, such as octyltrichlorosilane or octadecyltrichlorosilane. In an additional preferred embodiment, the surface modifier may be a halopolyorganosilane, such as octyldimethylchlorosilane or octadecyldimethylchlorosilane. Advantageously, R is octyl or octadecyl.
The surface of the hybrid silica materials may also be surface modified by coating with a polymer. Polymer coatings are known in the literature and may be provided generally by polymerization or polycondensation of physisorbed monomers onto the surface without chemical bonding of the polymer layer to the support (type I), polymerization or polycondensation of physisorbed monomers onto the surface with chemical bonding of the polymer layer to the support (type II), immobilization of physisorbed prepolymers to the support (type III), and chemisorption of presynthesized polymers onto the surface of the support (type IV). See, e.g., Hanson et al., J. Chromat. A656 (1993) 369-380, the text of which is incorporated herein by reference. As noted above, coating the hybrid material with a polymer may be used in conjunction with various surface modifications described in the invention. In a preferred embodiment, Sylgard® (Dow Corning, Midland, Mich., USA) is used as the polymer.
The term “porogen” refers to a pore forming material, that is a chemical material dispersed in a material as it is formed that is subsequently removed to yield pores or voids in the material.
The term “end capping” a chemical reaction step in which a resin that has already been synthesized, but that may have residual unreacted groups (e.g., silanol groups in the case of a silicon-based inorganic resin) are passivated by reaction with a suitable reagent. For example, again in the case of silicon-based inorganic resins, such silanol groups may be methylated with a methylating reagent such as hexamethyldisilazane.
A stabilizer describes reagents which inhibit the coalescence of droplets of organic monomer and POS or PAS polymers in an aqueous continuous phase. These can include but are not limited to finely divided insoluble organic or inorganic materials, electrolytes, and water-soluble polymers. Typical stabilizers are methyl celluloses, gelatins, polyvinyl alcohols, salts of poly(methacrylic acid), and surfactants. Surfactants (also referred to as emulsifiers or soaps) are molecules which have segments of opposite polarity and solubilizing tendency, e.g., both hydrophilic and hydrophobic segments.
The instant invention relates to a porous inorganic/organic homogenous copolymeric hybrid material having at least about 10% carbon content by mass. In preferred embodiments, the materials of the invention are porous inorganic/organic homogenous copolymeric hybrid particles, particularly spherical particles. The carbon content of the material may be from about 15% to about 90% carbon content by mass, from about 25% to about 75% carbon content by mass, from about 30% to about 45% carbon content by mass, from about 31% to about 40% carbon content by mass, from about 32% to about 40% carbon content by mass, or from about 33% to about 40% carbon content by mass.
In embodiments where the materials of the invention are in the form of particles, they have an average diameter of about 0.1 μm to about 30 to 60 μm, or about 2.0 μm to about 15 μm. The particulate materials of the invention also have a large specific surface area, e.g., about 50-800 m2/g or 400-700 m2/g.
The materials of the invention also have defined pore volumes that may be engineered by choosing an appropriate porogen during synthesis (vide supra). By way of example, the materials of the invention may have specific pore volumes of about 0.25 to 2.5 cm3/g, about 0.4 to 2.0 cm3/g, or 0.5 to 1.3 cm3/g. Likewise, the pore diameters of the material of the invention may be controlled during synthesis (vide supra). For example, the materials of the invention may have an average pore diameter of about 20 to 300 Å, about 50 to 200 Å, or about 75 to 125 Å.
Because of their hybrid nature, the materials of the invention are stable over a broad pH range. Typically, the material may be hydrolytically stable at a pH of about 1 to about 13, about 4 to about 11, about 4 to about 10, about 5 to about 9, or about 6 to about 8.
An advantageous feature of the materials of the invention is their reduced swelling upon solvation with organic solvents than conventional organic LC resins. Therefore, in one embodiment, the material swells by less than about 25% (or 15% or 10% or even 5%) by volume upon solvation with an organic solvent, such as acetonitrile, methanol, ethers (such as diethyl ether), tetrahydrofuran, dichloromethane, chloroform, hexane, heptane, cyclohexane, ethyl acetate, benzene, or toluene.
The materials of the invention, either particles or monoliths, may be surface modified by formation of an organic covalent chemical bond between an inorganic or organic group of the material and a surface modifier. The surface modifier may be an organic group surface modifier, a silanol group surface modifier, a polymeric coating surface modifier, or combinations thereof. For example, the surface modifier may have the formula Za(R′)bSi—R, as described herein above. Also, the surface modifier may be a polymer coating, such as Sylgard®. Likewise, the surface modifier may be octyltrichlorosilane, octadecyltrichlorosilane, octyldimethylchlorosilane, or octadecyldimethylchlorosilane. Additionally, the surface modifier is a combination of an organic group surface modifier and a silanol group surface modifier; a combination of an organic group surface modifier and a polymeric coating surface modifier; a combination of a silanol group surface modifier and a polymeric coating surface modifier; or a combination of an organic group surface modifier, a silanol group surface modifier, and a polymeric coating surface modifier. The surface modifier may also be a silanol group surface modifier.
The invention also pertains to porous inorganic/organic homogenous copolymeric hybrid monolith materials. In preferred embodiments, the monoliths comprise coalesced porous inorganic/organic homogenous copolymeric hybrid particles having at least about 10% carbon content by mass, about 15% to about 90% carbon content by mass, about 25% to about 75% carbon content by mass, about 30% to about 45% carbon content by mass, about 31% to about 40% carbon content by mass, about 32% to about 40% carbon content by mass, about 30% to about 45% carbon content by mass, about 15 to about 35% carbon content by mass, or about 15 to about 20% carbon content by mass.
The inorganic portion of the hybrid monolith materials of the invention may be alumina, silica, titanium oxide, zirconium oxide, or ceramic materials.
For example, the invention relates to aporous inorganic/organic homogenous copolymeric hybrid material of the formula:

(A)x(B)y(C)z  Formula I

wherein the order of repeat units A, B, and C may be random, block, or a combination of random and block; A is an organic repeat unit which is covalently bonded to one or more repeat units A or B via an organic bond; B is an organosiloxane repeat unit which is bonded to one or more repeat units B or C via an inorganic siloxane bond and which may be further bonded to one or more repeat units A or B via an organic bond; C is an inorganic repeat unit which is bonded to one or more repeat units B or C via an inorganic bond; and 0.0003≦y/z≦500 and 0.002≦x/(y+z)≦210. The relative values of x, y, and z may also be 0.003≦y/z≦50 and 0.02≦x/(y+z)≦21 or 0.03≦y/z≦5 and 0.2≦x/(y+z)≦2.1.

Similarly, the invention relates to a porous inorganic/organic homogenous copolymeric hybrid material of the formula:

(A)x(B)y(B*)y*(C)z  Formula II

wherein the order of repeat units A, B, B*, and C may be random, block, or a combination of random and block; A is an organic repeat unit which is covalently bonded to one or more repeat units A or B via an organic bond; B is an organosiloxane repeat unit which is bonded to one or more repeat units B or B* or C via an inorganic siloxane bond and which may be further bonded to one or more repeat units A or B via an organic bond, B* is an organosiloxane repeat unit that does not have reactive (i.e., polymerizable) organic components and may further have a protected functional group that may be deprotected after polymerization; C is an inorganic repeat unit which is bonded to one or more repeat units B or B* or C via an inorganic bond; and 0.0003≦(y+y*)/z≦500 and 0.002≦x/(y+y*+z)≦210.

Another aspect of the invention is a porous inorganic/organic homogenous copolymeric hybrid material of the formula:

(A)x(B)y  Formula III

wherein the order of repeat units A and B may be random, block, or a combination of random and block; A is an organic repeat unit which is covalently bonded to one or more repeat units A or B via an organic bond (e.g., a polymerized olefin); B is an organosiloxane repeat unit which may or may not be bonded to one or more repeat units B via an inorganic siloxane bond and which may be further bonded to one or more repeat units A or B via an organic bond; and 0.002≦x/y≦210.

Another aspect of the invention is a porous inorganic/organic homogenous copolymeric hybrid material of the formula:

(A)x(B)y(B*)y*  Formula IV

wherein the order of repeat units A, B, and B* may be random, block, or a combination of random and block; A is an organic repeat unit which is covalently bonded to one or more repeat units A or B via an organic bond (e.g., a polymerized olefin); B is an organosiloxane repeat unit which may or may not be bonded to one or more repeat units B via an inorganic siloxane bond and which may be further bonded to one or more repeat units A or B via an organic bond; B* is an organosiloxane repeat unit that does not have reactive (i.e., polymerizable) components and has a protected functional group that may be deprotected after polymerization, but added as a third repeat unit. The relative stoichiometry of the A to (B+B*) components is the same as above, e.g., 0.002≦x/(y+y*)≦210.

Repeat unit A may be derived from a variety of organic monomer reagents possessing one or more polymerizable moieties, capable of undergoing polymerization, e.g., a free radical-mediated polymerization. A monomers may be oligomerized or polymerized by a number of processes and mechanisms including, but not limited to, chain addition and step condensation processes, radical, anionic, cationic, ring-opening, group transfer, metathesis, and photochemical mechanisms.
A may also be one of the following:




wherein each R is independently H or a C1-C10 alkyl group (e.g, methyl, ethyl, or propyl); m is an integer of from 1 to about 20; n is an integer of from 0 to 10; and Q is hydrogen, N(C1-6alkyl)3, N(C1-6alkyl)2(C1-6alkylene-SO3), or C(C1-6hydroxyalkyl)3.
Repeat unit B may be derived from several mixed organic-inorganic monomer reagents possessing two or more different polymerizable moieties, capable of undergoing polymerization, e.g., a free radical-mediated (organic) and hydrolytic (inorganic) polymerization. B monomers may be oligomerized or polymerized by a number of processes and mechanisms including, but not limited to, chain addition and step condensation processes, radical, anionic, cationic, ring-opening, group transfer, metathesis, and photochemical mechanisms.
B may also be one of the following:







Repeat unit C may be —SiO2— and may be derived from an alkoxysilane, such as tetraethoxysilane (TEOS) or tetramethoxysilane (TMOS).
In one embodiment, A is a substituted ethylene group, B is a oxysilyl-substituted alkylene group, and C is a oxysilyl group, for example the following:




In another example, the invention relates to a porous inorganic/organic homogenous copolymeric hybrid material of the invention may be represented by the following formula:




wherein R1 is H, F, Cl, Br, I, lower alkyl (e.g., CH3 or CH2CH3); R2 and R3 are each independently H, F, Cl, Br, I, alkane, substituted alkane, alkene, substituted alkene, aryl, substituted aryl, cyano, ether, substituted ether, embedded polar group; R4 and R5 are each independently H, F, Cl, Br, I, alkane, substituted alkane, alkene, substituted alkene, aryl, substituted aryl, ether, substituted ether, cyano, amino, substituted amino, diol, nitro, sulfonic acid, cation or anion exchange groups, 0≦a≦2x, 0≦b≦4, and 0≦c≦4, provided that b+c≦4 when a=1; 1≦d≦20, and 0.0003≦y/z≦500 and 0.002≦x/(y+z)≦210.

The invention also relates to materials made by the novel methods of the present invention. For example, the invention pertains to a porous inorganic/organic homogenous copolymeric hybrid material prepared by the steps of (a) copolymerizing an organic olefin monomer with an alkenyl-functionalized organosiloxane, and (b) hydrolytic condensation of the product of step (a) with a tetraalkoxysilane. Likewise, the invention pertains to a porous inorganic/organic copolymeric hybrid material prepared by the steps of (a) copolymerizing an organic olefin monomer with an alkenyl-functionalized organosiloxane, and (b) hydrolytic condensation of the product of step (a) with a tetraalkoxysilane, said material having at least 15% carbon content by mass.
The materials of the invention may be used as a liquid chromatography stationary phase; a sequestering reagent; a solid support for combinatorial chemistry; a solid support for oligosaccharide, polypeptide, or oligonucleotide synthesis; a solid support for a biological assay; a capillary biological assay device for mass spectrometry; a template for a controlled large pore polymer film; a capillary chromatography stationary phase; an electrokinetic pump packing material; a polymer additive; a catalyst; or a packing material for a microchip separation device. The materials of the invention are particularly suitable for use as a HPLC stationary phase or, in general, as a stationary phase in a separations device, such as chromatographic columns, thin layer plates, filtration membranes, sample cleanup devices, and microtiter plates.
The porous inorganic/organic homogenous copolymeric hybrid particles have a wide variety of end uses in the separation sciences, such as packing materials for chromatographic columns (wherein such columns may have improved stability to alkaline mobile phases and reduced peak tailing for basic analytes), thin layer chromatographic (TLC) plates, filtration membranes, microtiter plates, scavenger resins, solid phase organic synthesis supports (e.g., in automated peptide or oligonucleotide synthesizers), and the like having a stationary phase which includes porous inorganic/organic homogenous copolymeric hybrid particles. The stationary phase may be introduced by packing, coating, impregnation, etc., depending on the requirements of the particular device. In a particularly advantageous embodiment, the chromatographic device is a packed chromatographic column, such as commonly used in HPLC.
EXAMPLES
The present invention may be further illustrated by the following non-limiting examples describing the preparation of porous inorganic/organic hybrid materials, and their use.
Example 1
One or more organoalkoxysilanes alone or in combination with a one or more alkoxysilanes (all from Gelest Inc., Tullytown, Pa.) were mixed with an alcohol (HPLC grade, J. T. Baker, Phillipsburgh, N.J.) and 0.1 N hydrochloric acid (Aldrich Chemical, Milwaukee, Wis.) in a flask. The resulting solution was agitated and refluxed for 16 hours in an atmosphere of argon or nitrogen. Alcohol was removed from the flask via distillation at atmospheric pressure. Residual alcohol and volatile species were removed by heating at 115-140° C. for 1-2 hours in a sweeping stream of argon or nitrogen or by heating at 125° C. under reduced pressure for 1-2 hours. The resulting polyorganoalkoxysiloxanes were colorless viscous liquids. The chemical formulas are listed in Table 1 for the organotrialkoxysilanes and alkoxysilanes used to make the product polyorganoalkoxysiloxanes (POS). Specific amounts are listed in Table 2 for the starting materials used to prepare these products. Example 1e was made from 298 g of (3-methacryloxypropyl)trimethoxysilane and 221 g of octyltriethoxysilane. Example 1j was made from bis(trimethoxysilylpropyl)acrylamide and tetramethoxysilane. The bis(trimethoxysilylpropyl)acrylamide was prepared separately from the reaction of 2 equivalents of bis(trimethoxysilylpropyl)amine (Gelest Inc., Tullytown, Pa.) and 1 equivalent of acryloyl chloride (Aldrich Chemical, Milwaukee, Wis.) in dry hexane (HPLC grade, J. T. Baker, Phillipsburgh, N.J.). The second equivalent of amine sequestered the HCl condensate of the amide formation, where the amine hydrochloride salt was removed from the amide solution by filtration. The product structure was confirmed by 1H, 13C, and 29Si NMR spectroscopy.










TABLE 1






Organoalkoxysilanes
Alkoxysilane
Alcohol


Product
Chemical Formula
Chemical Formula
Chemical Formula







1a
H2C═C(CH3)CO2C3H6Si(OCH3)3
na
CH3OH


1b
H2C═C(CH3)CO2C3H6Si(OCH3)3
Si(OCH3)4
CH3OH


1c, d
H2C═C(CH3)CO2C3H6Si(OCH3)3
Si(OCH2CH3)4
CH3CH2OH


1e
H2C═C(CH3)CO2C3H6Si(OCH3)3
na
CH3OH



and



C8H17Si(OCH2CH3)3


1f, g
H2C═CHC6H4(CH2)2Si(OCH3)3
Si(OCH2CH3)4
CH3CH2OH


1h, i
H2C═CHSi(OCH2CH3)3
Si(OCH2CH3)4
CH3CH2OH


1j
H2C═CHCON[C3H6Si(OCH3)3]2
Si(OCH2CH3)4
CH3CH2OH




















TABLE 2






Organotrialkoxysilane
Alkoxysilane
0.1N HCl
Alcohol


Product
(g)
(g)
(g)
(mL)



















1a
497
na
54
300


1b
497
61
68
300


1c
170
1428
170
347


1d
671
2250
304
788


1e
298
na
54
300



and



221


1f
15
355
42
99


1g
20
156
19
47


1h
160
875
119
253


1i
799
1750
297
736


1j
27
395
47.3
229









Example 2
A solution of poly(vinyl alcohol) (PVA; 87%-89% hydrolyzed; Ave Mw 13,000-23,000; Aldrich Chemical, Milwaukee, Wis.) in water was prepared by mixing and heating to 80° C. for 0.5 hours. Upon cooling, the PVA solution was combined with a solution comprising divinylbenzene (DVB; 80%; Dow Chemical, Midland, Mich.), a POS selected from Example 1, 2,2′-azobisisobutyronitrile (AIBN; 98%, Aldrich Chemical), and or more of the following coporogens: 2-ethylhexanoic acid (2-EHA; Aldrich Chemical), toluene (HPLC grade, J. T. Baker, Phillipsburgh, N.J.), cyclohexanol (CXL; Aldrich Chemical), 1-methyl-2-pyrrolidinone (NMP; Aldrich Chemical). The two solutions were mixed initially using a mechanical stirrer with Teflon paddle and then emulsified by passing the mixture through a static mixer for 10 minutes under an argon flow. With continuous static mixing, the emulsification was heated to 70-80° C. in a period of 30 minutes. Thereafter, the emulsion was agitated mechanically at 70-80° C. for 16 hours. Upon cooling, the suspension of formed particles was filtered and then washed consecutively with copious amounts of water and then methanol. The particles were then dried at 100° C. at a reduced pressure for 16 hours. Specific reagent amounts and reaction conditions are listed in Table 3. The specific surface areas (SSA), specific pore volumes (SPV) and the average pore diameters (APD) of these materials were measured using the multi-point N2 sorption method and are listed in Table 3 (Micromeritics ASAP 2400; Micromeritics Instruments Inc., Norcross, Ga., or equivalent). The specific surface area was calculated using the BET method, the specific pore volume was the single point value determined for P/P0>0.98, and the average pore diameter was calculated from the desorption leg of the isotherm using the BJH method.
Example 3
A solution of Triton® X-45 (Aq X-45; Fluka, Milwaukee, Wis.), Triton® X-100 (Aq X-100; Fluka, Milwaukee, Wis.), or Methocel E15 (M E15, Dow, Grove City, Ohio; aqueous solution prepared by preheating water to 90° C. before addition of M E15 and cooling to 25° C.) in water and or ethanol was prepared by mixing and heating to 60° C. for 0.5-1.0 hours. In a separate flask, a solution was prepared under a nitrogen purge at ambient temperature by mixing for 0.5 hours divinylbenzene (DVB; 80%; Dow Chemical, Midland, Mich.; washed 3× in 0.1 N NaOH, 3× in water, and then dried MgSO4 from Aldrich Chemical), a POS selected from Example 1, 2,2′-azobisisobutyronitrile (AIBN; 98%, Aldrich Chemical), and one or more of the following reagents: toluene (HPLC grade, J. T. Baker, Phillipsburgh, N.J.), cyclohexanol (CXL; Aldrich, Milwaukee, Wis.), dibutylphthalate (DBP; Sigma; Milwaukee, Wis.), Triton® X-45 (Oil X-45; Fluka, Milwaukee, Wis.). For example 3f, 14 g of Pluronic® F-87 (F-87; BASF; Mount Olive, N.J.), was further added to the aqueous phase prior to mixing. For examples 3k, 3l, 3m, 3n, 3r, and 3v, 0.8 g (3k-3n) and 4.5 g (3r, 3v) of tris(hydroxymethyl)aminomethane lauryl sulfate (TDS; Fluka, Milwaukee, Wis.) was further added to the aqueous solution prior to combination with the oil solution. For examples 3p and 3q, 2.8 and 0.4 grams respectively of poly(vinyl alcohol) (PVA; 87%-89% hydrolyzed; Ave Mw 13,000-23,000; Aldrich Chemical) was further added to the aqueous solution prior to combination with the oil solution. The two solutions were combined and then emulsified using a rotor/stator mixer (Model 100L, Charles Ross & Son Co., Hauppauge, N.Y.) for 4 minutes under an argon flow. Next, a solution of 14.8 M ammonium hydroxide (NH4OH; J. T. Baker, Phillipsburgh, N.J.) was added to the emulsion over a minute, and the emulsification was continued for 20 minutes. For example 3m and 3aa, the mixture was emulsified first, then heated at 80° C. for 1 hour prior to ammonium hydroxide addition. Thereafter, the emulsion was agitated mechanically at 80° C. for 16-24 hours. Upon cooling, the suspension of formed particles was filtered and then washed consecutively with copious amounts of methanol, water and then methanol. The particles were then dried at 80° C. at a reduced pressure for 16 hours. Specific reagent amounts and reaction conditions are listed in Table 4. The specific surface areas (SSA), specific pore volumes (SPV) and the average pore diameters (APD) of these materials are listed in Table 4 and were measured as described in Example 2. The % C values of these materials were measured by combustion analysis (CE-440 Elemental Analyzer; Exeter Analytical Inc., North Chelmsford, Mass., or equivalent).
Example 4
A solution of Triton® X-45 (Aq X-45; Fluka, Milwaukee, Wis.) in water and ethanol was prepared by mixing and heating to 60° C. for 0.5-1.0 hours. In a separate flask, a solution was prepared under a nitrogen purge at ambient temperature by mixing for 0.5 hours one or more organic monomers selected from the following; divinylbenzene (DVB; 80%; Dow Chemical, Midland, Mich.; washed 3× in 0.1 N NaOH, 3× in water, and then dried MgSO4 from Aldrich Chemical), Styrene (STY, 96%; Aldrich Chemical; washed 3× in 0.1 N NaOH, 3× in water, and then dried MgSO4 from Aldrich Chemical), tert-butyl methacrylate (TBM, 98%, Aldrich Chemical), ethylene glycol dimethacrylate (EGD, 98%, Aldrich Chemical), 1,4-Butanediol dimethacrylate (BDM, 95%, Aldrich Chemical), 1-vinyl-2-pyrrolidinone (NVP, 99%, Aldrich Chemical), a POS selected from Example 1, 2,2′-azobisisobutyronitrile (AIBN; 98%, Aldrich Chemical), cyclohexanol (CXL; Aldrich, Milwaukee, Wis.), and Tritong X-45 (Oil X-45; Fluka, Milwaukee, Wis.). The two solutions were combined and then emulsified using a rotor/stator mixer (Model 100L, Charles Ross & Son Co., Hauppauge, N.Y.) for 4 minutes under an argon flow. Next, a solution of 14.8 M ammonium hydroxide (NH4OH; J. T. Baker, Phillipsburgh, N.J.) was added to the emulsion over a minute, and the emulsification was continued for 15 minutes. Thereafter, the emulsion was agitated mechanically at 80° C. for 16-24 hours. Upon cooling, the suspension of formed particles was filtered and then washed consecutively with copious amounts of methanol, water and then methanol. The particles were then dried at 80° C. at a reduced pressure for 16 hours. Specific reagent amounts and reaction conditions are listed in Table 5. The specific surface areas (SSA), specific pore volumes (SPV), the average pore diameters (APD) and the % C of these materials are listed in Table 5 and were measured as described in Examples 2 and 3.





















TABLE 3






POS
POS
DVB
AIBN
Toluene
2-EHA
CXL
NMP
Water
PVA

SSA
SPV
APD


Product
Reagent
(g)
(g)
(g)
(mL)
(g)
(g)
(g)
(mL)
(g)
% C
(m2/g)
(cm3/g)
(Å)





























2a
1a
102
174
1.8
242
0
0
0
1500
20
74.0
622
0.60
45


2b
1a
138
138
1.8
242
0
0
0
1480
20
68.0
522
0.45
38


2c
1a
108
174
1.8
121
121
0
0
1500
20
—
506
0.57
50


2d
1a
75
75
1.1
0
182
0
0
1750
16
—
434
0.72
69


2e
1a
55
96
1.1
0
182
0
0
1750
16
—
566
0.96
82


2f
1b
55
96
1.1
0
182
0
0
1750
16
72.3
585
1.12
95


2g
1b
55
96
1.1
0
132
0
0
1750
16
73.6
552
0.79
71


2h
1b
55
96
1.1
80
52
0
0
1750
16
72.2
510
0.57
51


2i
1b
55
96
1.1
33
0
99
0
1750
16
—
545
0.41
37


2j
1b
55
96
1.2
83
0
0
83
1750
16
—
512
0.34
32


2k
1b
60
90
1.2
33
0
0
132
1750
16
—
3
3
535































TABLE 4













Oil


Aq







POS



Copor-
Copor-
Surfactant
Surfac-


Surfac-


Prod-
Re-
POS
DVB
AIBN
ogen
ogen
Type
tant
Ethanol
Water
tant

SSA
SPV
APD


uct
agent
(g)
(mL)
(g)
Type
(mL)
Oil/Aq
(g)
(mL)
(mL)
(g)
% C
(m2/g)
(cm3/g)
(Å)






























3a
1c
58
14
0.58
na
na
X-45/X-45
3.0
66
280
2.6
33.6
454
0.48
46


3b
1c
58
14
0.10
toluene
7
X-45/X-45
3.5
66
280
2.5
31.3
479
0.59
50


3c
1c
58
11
0.11
toluene
7
X-45/X-45
11.5
66
280
2.5
28.2
557
0.75
55


3d
1c
58
14
0.15
CXL
20
X-45/X-45
3.5
66
280
2.5
32.3
557
0.85
64


3e
1c
58
14
0.19
CXL
20
X-45/X-45
11.5
66
280
2.5
33.3
630
1.11
72


3f
1c
58
14
1.78
na
na
X-45/X-45
11.5
66
280
2.5
33.7
476
0.80
66


3g
1c
58
14
1.55
DBP
20
X-45/X-45
11.5
66
280
2.5
31.2
608
1.09
74


3h
1c
58
14
1.35
CXL
27
X-45/X-45
4.5
66
280
2.5
32.4
556
0.95
72


3i
1c
59
14
0.15
CXL
30
X-45/X-45
11.5
66
280
2.5
32.3
572
1.21
84


3j
1c
58
14
0.15
CXL
40
X-45/X-45
16.5
66
280
3.5
34.1
632
1.78
109


3k
1c
58
14
0.15
CXL
40
X-45/X-45
16.5
66
280
2.5
31.8
628
1.00
62


3l
1c
58
14
0.15
CXL
40
X-45/X-45
16.5
7
280
3.5
30.6
666
1.16
79


3m
1c
58
14
0.15
CXL
40
X-45/X-45
16.5
7
280
3.5
31.3
634
1.6
100


3n
1c
59
14
0.15
CXL
40
X-45/X-45
16.5
7
280
3.5
32.5
571
1.56
113


3o
1c
58
14
0.15
CXL
40
X-45/X-45
20.0
0
280
0
31.7
566
1.39
96


3p
1c
58
14
0.15
CXL
40
X-45/X-45
20.0
0
280
0
34.3
545
1.49
110


3q
1c
58
14
0.15
CXL
40
X-45/X-45
20.0
0
280
0
31.4
568
1.45
104


3r
1c
500
112
1.30
CXL
344
X-45/X-45
142
60
2400
30.2
31.5
573
1.67
117


3s
1c
58
14
0.15
CXL
40
X-45/X-45
16.5
7
280
3.5
31.3
608
1.51
97


3t
1c
58
7
0.08
CXL
36
X-45/X-45
14.5
7
280
3.5
24.5
592
1.86
123


3u
1c
45
25
0.25
CXL
40
X-45/X-45
16.5
7
280
3.5
50.0
604
1.40
97


3v
1c
500
121
1.30
CXL
344
X-45/X-45
142
60
2400
30.2
31.0
508
1.53
116


3w
1c
500
121
1.30
CXL
344
X-45/X-45
142
60
2400
30.2
37.4
417
1.36
116


3x
1d
58
14
0.15
CXL
40
X-45/X-45
3.5
7
280
3.5
40.7
760
1.08
54


3y
1c
58
14
0.15
toluene
26
 —/X-100
0
66
280
14.0
37.5
514
1.09
83


3z
1c
58
14
0.15
CXL
14
 —/X-100
0
14
280
5.6
32.0
463
0.53
51


3aa
1c
58
14
0.20
CXL
18
 —/M E15
0
0
280
5.9
32.2
490
0.52
45


3ab
1j
50
5.0
0.02
toluene
6
 —/X-100
0
57
241
4.8
16.9
455
0.81
71.6































TABLE 5






POS




Copor-
Copor-
Oil









Prod-
Re-
POS
Organic
Monomer
AIBN
ogen
ogen
X-45
Ethanol
Water
Aq X-45

SSA
SPV
APD


uct
agent
(g)
Monomer
(mL)
(g)
Type
(mL)
(g)
(mL)
(mL)
(g)
% C
(m2/g)
(cm3/g)
(Å)







4a
1c
58
EGD
14
0.17
CXL
26
3.5
66
280
3.5
25.1
560
0.99
77


4b
1c
58
BDM
14
0.15
CXL
26
3.5
66
280
3.5
25.8
528
0.93
78


4c
1c
58
DVB/TBM
14/3
0.15
CXL
26
3.5
66
280
3.5
33.9
559
0.97
76


4d
1c
58
DVB/NVP
12/3
0.15
CXL
26
3.5
66
280
3.5
33.5
428
0.84
74


4e
1c
58
DVB/STY
 7/7
0.15
CXL
26
3.5
66
280
3.5
26.9
544
0.90
70


4f
1c
58
DVB/STY
 3/11
0.15
CXL
26
3.5
66
280
3.5
27.1
514
0.91
72


4g
1c
58
STY
14
0.15
CXL
26
3.5
66
280
3.5
20.2
530
0.94
71

























TABLE 6






POS
POS
DVB
AIBN
Coporogen
Coporogen
SSA
SPV
APD


Product
Reagent
(g)
(g)
(g)
Type
(g)
(m2/g)
(cm3/g)
(Å)
























5a
1e
1.3
2.2
0.04
2-EHA
5.5
517
0.82
88


5b
1e
1.3
2.2
0.04
DDL
5.9
452
0.71
100


5c
1e
1.3
2.2
0.04
CXL
5.5
501
0.81
88


5d
1e
1.3
2.2
0.04
toluene/DDL
3.0/3.0
534
0.83
90









Example 5
Pyrex glass tubes (VWR, Bridgeport, N.J.) were derivatized using the following procedure: Treat the glass surface to 2.5 molar sodium hydroxide solution (Aldrich Chemical) for 16 hours at ambient room temperature, wash with copious amounts of water, treat the glass surface with concentrated hydrochloric acid (J. T. Baker) for 1 hour at ambient room temperature, wash with copious amounts of water, and then dry at 100° C. under reduced pressure. The glass surface was subsequently derivatized by treating for 16 hours at 50° C. with a mixture prepared from 19 g of pyridine (J. T. Baker), 12.5 g (3-methacryloxypropyl)trichlorosilane (Gelest Inc.), and 40 g of toluene (HPLC grade, J. T. Baker). The glass tubes were then washed with tetrahydrofuran (THF; J. T. Baker), water, and THF, and then dried at 100° C. and reduced pressure.
To the derivatized tubes were added a solution comprising divinylbenzene (DVB; 80%; Dow Chemical), a POS selected from Example 1, 2,2′-azobisisobutyronitrile (AIBN; 98%, Aldrich Chemical), and on or more of the following coporogens: 2-ethylhexanoic acid (2-EHA; Aldrich Chemical), toluene (HPLC grade, J. T. Baker), cyclohexanol (CXL; Aldrich Chemical), 1-dodecanol (DDL; Aldrich Chemical). The filled tubes were subsequently heated for 20 hours at 75° C. The resultant monolithic materials were washed by Soxhlet extraction using methanol (HPLC grade, J. T. Baker) for 16 hours and then dried at 80-100° C. and reduced pressure. The specific surface areas (SSA), specific pore volumes (SPV) and the average pore diameters (APD) of these materials are listed in Table 6 and were measured as described in Example 2.
Example 6
A solution of Triton® X-45 (Aq X-45; Fluka, Milwaukee, Wis.), Triton® X-100 (Aq X-100; Fluka, Milwaukee, Wis.), Triton® X-165 (Aq X-165; Sigma, St. Louis, Mo.), Triton® X-305 (Aq X-305; Sigma, St. Louis, Mo.), Triton® X-705 (Aq X-705; Sigma, St. Louis, Mo.), or ammonium laurylsulfate (Aq ALS, Fluka, Milwaukee, Wis., 30% solution by weight in water) in water and or ethanol was prepared by mixing and heating to 60° C. for 0.5-1.0 hours. In a separate flask, a solution was prepared under a nitrogen purge at ambient temperature by mixing for 0.5 hours divinylbenzene (DVB; 80%; Dow Chemical, Midland, Mich.; washed 3× in 0.1 N NaOH, 3× in water, and then dried MgSO4 from Aldrich Chemical), a POS selected from Example 1, 2,2′-azobisisobutyronitrile (AIBN; 98%, Aldrich Chemical), and on or more of the following reagents: toluene (HPLC grade, J. T. Baker, Phillipsburgh, N.J.), cyclohexanol (CXL; Aldrich, Milwaukee, Wis.), and Triton® X-45 (Oil X-45; Fluka, Milwaukee, Wis.). For example 6b, 6c, and 6k, 0.4-1.9 g of ammonium laurylsulfate (Aq ALS, Fluka, Milwaukee, Wis., 30% solution by weight in water) was further added to the aqueous phase prior to combination with the oil solution. The two solutions were combined and then emulsified using a rotor/stator mixer (Model 100L, Charles Ross & Son Co., Hauppauge, N.Y.) for 13-27 minutes under an argon flow. Next, a solution of 14.8 M ammonium hydroxide (NH4OH; J. T. Baker, Phillipsburgh, N.J.) was added to the emulsion over a minute, and the emulsification was continued for 20 minutes. Thereafter, the emulsion was agitated mechanically at 80° C. for 16-24 hours. Upon cooling, the suspension of formed particles was filtered and then washed consecutively with copious amounts of methanol, water and then methanol. The particles were then dried at 80° C. at a reduced pressure for 16 hours. Specific reagent amounts and reaction conditions are listed in Table 7. The specific surface areas (SSA), specific pore volumes (SPV), the average pore diameters (APD) and the % C of these materials are listed in Table 7 and were measured as described in Examples 2 and 3.
Example 7
Spherical, porous, hybrid inorganic/organic particles of Examples 3, 4, and 6 were mixed with either tris(hydroxymethyl)aminomethane (TRIS, Aldrich Chemical, Milwaukee, Wis.) or tetraethylammonium hydroxide (35 weight % in water, TEAH, Aldrich Chemical, Milwaukee, Wis.) in a solution comprised of one or more of the following; water, ethanol (HPLC grade, J. T. Baker, Phillipsburgh, N.J.), and pyridine (J. T. Baker, Phillipsburgh, N.J.), yielding a slurry. The resultant slurry was then enclosed in a stainless steel autoclave and heated to between 140-165° C. for 20 hours. After the autoclave cooled to room temperature the product was filtered and washed repeatedly using water and methanol (HPLC grade, J. T. Baker, Phillipsburgh, N.J.), and then dried at 80° C. under vacuum for 16 hours. Specific hydrothermal conditions are listed in Table 8 (mL of base solution/gram of hybrid silica particle, concentration and pH of initial TRIS solution, reaction temperature). The specific surface areas (SSA), specific pore volumes (SPV), the average pore diameters (APD) and the % C of these materials are listed in Table 8 and were measured as described in Examples 2 and 3.






















TABLE 7






POS



Copor-
Copor-
Oil


Aqueous
Aq






Prod-
Re-
POS
DVB
AIBN
ogen
ogen
X-45
Ethanol
Water
Surfactant
Surfactant

SSA
SPV
APD


uct
agent
(g)
(mL)
(g)
Type
(mL)
(g)
(mL)
(mL)
Type
(g)
% C
(m2/g)
(cm3/g)
(Å)






























6a
1c
58
14
0.15
toluene
10
0
66
300
X-45
4.9
32.6
475
0.57
48


6b
1c
58
11
0.11
toluene
7
11.5
66
280
X-45/ALS
2.5/1.9
28.4
557
0.74
55


6c
1c
58
11
0.11
toluene
7
11.5
66
280
X-45/ALS
2.5/0.4
29.3
567
0.81
57


6d
1c
58
14
0.15
toluene
10
0
14
300
X-100
7.0
31.2
491
0.57
51


6e
1c
58
14
0.15
toluene
10
0
66
300
X-100
7.0
34.2
518
0.64
55


6f
1c
58
14
0.15
toluene
10
0
66
300
X-165
7.0
32.3
463
0.65
62


6g
1c
58
14
0.15
toluene
10
0
0
300
X-165
7.0
31.3
427
0.55
54


6h
1c
58
14
0.15
toluene
10
0
66
300
X-165
1.0
31.6
392
0.49
48


6i
1c
58
14
0.15
toluene
10
0
66
300
X-165
0.5
33.1
396
0.51
52


6j
1c
58
14
0.15
toluene
10
0
7
300
X-165
7.0
33.0
446
0.56
53


6k
1c
58
14
0.15
toluene
10
0
7
300
X-165/ALS
7.0/1.1
33.0
435
0.57
55


6l
1c
58
14
0.15
CXL
11
0
7
300
X-165
7.0
33.9
442
0.59
60


6m
1c
58
14
0.15
toluene
10
0
66
300
X-305
7.0
33.0
424
0.67
50


6n
1c
58
14
0.15
toluene
10
0
0
300
X-305
7.0
31.7
379
0.52
50


6o
1c
58
14
0.15
toluene
10
0
66
300
X-705
7.0
31.3
382
0.62
48


6p
1c
58
14
0.15
toluene
10
0
132
300
X-705
7.0
31.9
396
0.80
59





























TABLE 8








Ethanol
Pyridine













Amount
Composition
Composition

Conc.

Temp.

SSA
SPV
APD
Loss in SSA


Product
Precursor
(mL/g)
(% Volume)
(% Volume)
Base
(Molarity)
pH
(° C.)
% C
(m2/g)
(cc/g)
(Å)
(m2/g)




























7a
3i
5
0
10
TRIS
0.30
10.4
160
32.0
547
1.28
98
25


7b
3h
10
0
30
TRIS
0.30
10.3
160
33.0
548
0.99
80
8


7c
3h
10
0
10
TRIS
0.60
10.5
160
33.1
506
0.91
81
50


7d
3e
10
0
0
TEAH
0.10
12.7
165
35.0
469
1.09
97
161


7e
3e
10
20
0
TRIS
0.30
10.1
155
32.3
570
1.12
82
60


7f
3e
10
20
0
TEAH
0.10
12.7
155
34.5
525
1.12
90
105


7g
4e
10
0
0
TEAH
0.10
12.4
165
27.6
373
0.86
95
171


7h
4f
10
0
0
TEAH
0.10
12.4
165
27.3
339
0.85
103
175


7i
3a
10
0
0
TEAH
0.10
12.7
165
33.4
331
0.45
56
123


7j
3c
10
0
0
TEAH
0.10
12.7
165
28.6
397
0.76
81
160


7k
6f
10
0
0
TEAH
0.10
12.8
165
33.6
345
0.62
83
118









Example 8
The particles of hybrid silica prepared according to Examples 3r, 3v, and 3w were blended and then separated by particle size into  ̃3,  ̃5, and  ̃7 μm fractions. A 5.0 g amount of 3 μm fraction was combined with 100 mL of concentrated sulfuric acid (EM Science, Gibbstown, N.J.) and stirred at room temperature in a 1 L round-bottom flask. After stirring for 1 hour, the solution was slowly added to a stirred solution of 400 mL water, and the mixture was stirred for 10 minutes. The modified hybrid silica particles were filtered and washed successively with water, methanol (J. T. Baker), and then dried at 80° C. under reduced pressure for 16 hours. The particles were analyzed as described in Examples 2 and 3 and shown to have the following properties: 30.3% C, 607 m2/g specific surface area (SSA), 1.51 cc/g specific pore volume (SPV), and 113 Å average pore diameter (APD). The loading of sulfonic acid groups was determined to be 1.0 meq/gram as measured by titration with 0.1 N NaOH (Metrohm 716 DMS Titrino autotitrator with 6.0232.100 pH electrode; Metrohm, Hersau, Switzerland, or equivalent).
Example 9
The particles of hybrid silica prepared according to Examples 3r, 3v, and 3w were blended and then separated by particle size into  ̃3,  ̃5, and  ̃7 μm fractions. The surface of a 3 μm material fraction was modified with chlorodimethyloctadecylsilane (Aldrich Chemical, Milwaukee, Wis.) as follows: 5×10−6 moles of silane per square meter of particle surface area and 1.6 equivalents (per mole silane) of imidazole (Aldrich Chemical, Milwaukee, Wis.) were added to a mixture of 15 g of hybrid silica particle in 100 mL of toluene (J. T. Baker) and the resultant mixture was refluxed for 20 hours. The modified hybrid silica particles were filtered and washed successively with water, toluene, 1:1 v/v acetone/water, and acetone (all solvents from J. T. Baker), and then dried at 80° C. under reduced pressure for 16 hours. The particles were analyzed as described in Examples 2 and 3 and shown to have the following properties: 40.2% C, 333 m2/g specific surface area (SSA), 1.13 cc/g specific pore volume (SPV), and 118 Å average pore diameter (APD). The surface concentration of octadecylsilyl groups was determined to be 1.44 μmol/m2 by the difference in particle % C before and after the surface modification as measured by elemental analysis.
Example 10
The particles of hybrid silica prepared according to Example 3b and 3v were separated by particle size into  ̃3 μm fractions. The 3 μm fractions were tested for mechanical strength in the following manner: The material of interest was slurry packed using a downward slurry technique in a 3.9×10 mm cartridge at 500 psig to insure no crushing of particles occurs. The column packing apparatus comprised a high-pressure liquid packing pump (Model No: 10-500FS100 SC Hydraulic Engineering Corp., Los Angeles, Calif., or equivalent). After packing, the cartridge was taken off the packing chamber and any excess material was wiped off flush with the cartridge face. The packed cartridge was then reattached to the chamber, which was filled with methanol. The cartridge was subjected to increasing pack pressures where the time to displace 20 mL of methanol was recorded at each 500 psig pressure increments from 500 psig to 9500 psig. Approximately 30 to 40 seconds were allowed at each pressure increment for the packed bed to stabilize at that pressure before the displacement time was measured. The time to displace 20 mL of methanol was then converted into flow rate (mL/min) by dividing the 20 mL displaced by the time (in seconds) and multiplying the result by 60.












PACKING CONDITIONS













Slurry Solvent:
Methanol




Restriction:
0.009′′ × 60′′











Slurry/Chamber Vol.:
50
mL
Valve Actuation:
Closed


Material Amount:
0.25
g
Pump Stroke Rate:
180/min.


Pack Pressure:
500
psig
Displacement:
 55 mL










PACK PRESSURE at OPEN FLOW RATES













440 mls/min
9000 psig



360 mls/min
6000 psig



240 mls/min
3000 psig










The principle of the test is as follows: The packed material in the steel chromatographic cartridge (3.9×10 mm) is exposed to different pressures (500-9000 psig) of a methanol effluent. At high pressures the particle beds of weak materials can compact or crush, which results in a restriction of methanol flow. The closer the methanol flow remains to the linear trend predicted for an ideal particle, the greater the mechanical stability of the packed bed material. As a means to normalize differences in particle size and packing parameters, and make direct comparisons of the effect of pressure on the stability of the base materials, the methanol flow rates are normalized to the flow obtained for the respective columns at 1000 psig back pressure.
A comparison of mechanical strength results is shown in FIG. 1 for commercially available silica based (5 μm Symmetry® C18, Waters Corporation) and polymeric based (7 μm UltrastyragelTM 106 Å and 7 μm UltrastyragelTM 104 Å, Waters Corporation) materials and the two 3 μm fractions of Examples 3b and 3v. It is evident that the hybrid packing material 3b is mechanically stronger than the polymeric based materials and has comparable strength to the silica based material.
Example 11
A solution was prepared using 5 mL of an acetic acid solution (J. T. Baker, Phillipsburgh, N.J.), Pluronic F-38 (BASF Corporation, Mount Olive, N.J.), 2,2′-azobisisobutyronitrile (AIBN; 98%, Aldrich Chemical, Milwaukee, Wis.) and a water soluble monomer, including N-[tris(hydroxymethyl)methyl]acrylamide (THMMA, Aldrich Chemical, Milwaukee, Wis.), (3-acrylamidopropyl)trimethylammonium chloride (APTA, 75 wt. % solution in water, Aldrich Chemical, Milwaukee, Wis.), [3-(methacryloylamino)propyl]dimethyl(3-sulfopropyl)ammonium hydroxide inner salt (MAPDAHI, Aldrich Chemical) or polyethylene glycol dimethacrylate (PEGDMA, Aldrich Chemical). This mixture was stirred for 2 hours at room temperature, and then sonicated for 5 minutes. A 2 mL aliquot of a 4:1 v/v mixture of tetramethylorthosilicate (TMOS, Aldrich Chemical, Milwaukee, Wis.) and 3-(trimethoxysilyl)propylmethacrylate (MAPTMOS, Aldrich Chemical, Milwaukee, Wis.) was added to the solution, which was then stirred in an ice water bath for 1 hour, and for a further 1 hour at room temperature. The solution was transferred to a cylindrical glass container, and placed in a oven for 16-24 hours at 45° C. Following removal from the cylindrical container, the monoliths were rinsed with water and then left for 24 hours in a 0.1 N ammonium hydroxide solution at 65° C. After this treatment, the monoliths were washed with water, refluxed in methanol for 24 hours, and then dried for 16-24 hours at 85° C. under reduced pressure. Specific reagent amounts and reaction conditions are listed in Table 9. The specific surface areas (SSA), specific pore volumes (SPV), the average pore diameters (APD) and the % C of these materials are listed in Table 9 and were measured as described in Examples 2 and 3.
















TABLE 9







Monomer











Amount
F-38
AIBN
AcOH

SSA
SPV
APD


Product
Monomer
(g)
(g)
(mg)
(Molarity)
% C
(m2/g)
(cm3/g)
(Å)
























11a
PEGDMA- Mn ~875
0.4987
0.2001
5.7
0.02
29.5
380
0.38
40


11b
PEGDMA- Mn ~875
0.7569
0.2001
6.5
0.02
23.2
260
0.33
47


11c
PEGDMA- Mn ~875
0.7557
0.3980
5.8
0.10
19.7
232
0.3
46


11d
PEGDMA- Mn ~875
1.0099
0.3992
5.8
0.02
19.9
205
0.38
57


11e
PEGDMA- Mn ~875
0.5021
0.4019
5.1
0.01
16.3
494
0.7
60


11f
PEGDMA- Mn ~258
0.5052
0.2052
5.5
0.02
32.1
411
0.4
41


11g
PEGDMA- Mn ~258
0.5091
0.1985
5.5
0.01
27.3
505
0.5
43


11h
PEGDMA- Mn ~258
0.5132
0.4017
5.4
0.01
27.3
270
0.28
41


11i
MAPDAHI
0.5003
0.2026
5.2
0.02
16.3
539
0.63
48


11j
MAPDAHI
0.5021
0.4007
5.4
0.02
15.1
542
0.66
49


11k
MAPDAHI
0.5006
0.6000
5.9
0.02
15.4
536
1.25
109


11l
APTA
0.6661
0.4008
7.3
0.02
15.9
459
1.33
133


11m
APTA
0.6533
0.4012
7.5
0.05
16.1
484
1.18
107


11n
THMMA
0.5368
0.4062
5.6
0.01
14.9
575
0.66
49


11o
THMMA
0.5311
0.4019
5.2
0.05
17.3
583
0.53
38









Example 12
Monoliths synthesized in Example 11 were placed in a stainless steel autoclave and immersed in a solution of 0.3 N tris(hydroxymethyl)aminomethane (TRIS, Aldrich Chemical, Milwaukee, Wis.). The solution was then heated to 155° C. for 22 hours. After the autoclave cooled to room temperature the products were washed repeatedly using water and methanol (HPLC grade, J. T. Baker, Phillipsburgh, N.J.), and then dried at 85° C. under reduced pressure. The specific surface areas (SSA), specific pore volumes (SPV), the average pore diameters (APD) and the % C of these materials are listed in Table 10 and were measured as described in Examples 2 and 3.














TABLE 10










SSA
SPV
APD



Product
Precursor
% C
(m2/g)
(cm3/g)
(Å)























12a
11a
28.3
145
0.28
60



12b
11c
31.6
104
0.23
65



12c
11e
20.6
149
0.67
172



12d
11f
29.9
75
0.13
47



12e
11g
27.3
76
0.21
70










Example 13
Monoliths made by the formulation of Examples 11e and 11h were immersed in glass vials containing a) dichloromethane, b) diethyl ether, c) toluene, d) methanol, e) water (pH 10—NaOH), f) water (pH 3—HCl), g) acetonitrile, h) dimethylsulfoxide, i) hexanes or j) tetrahydrofuran for 24 hours. The diameter and length of each of the monoliths showed no dimensional changes in any of the solvents within experimental error as measured by electronic caliper (Model 62379-531, Control Company, Friendswood, Tex. or equivalent).
Example 14
A solution of poly(vinyl alcohol) (PVA; 87%-89% hydrolyzed; Ave Mw 13,000-23,000; Aldrich Chemical, Milwaukee, Wis.) in 1000 mL water was prepared by mixing and heating to 80° C. for 0.5 hours. Upon cooling, the PVA solution was combined with a solution comprising divinylbenzene (DVB; 80%; Dow Chemical, Midland, Mich.), N-vinyl pyrrolidinone (NVP, Aldrich Chemical, Milwaukee, Wis.), 3-(trimethoxysilyl)propyl methacrylate (MAPTMOS, Aldrich Chemical, Milwaukee, Wis.), 2,2′-azobisisobutyronitrile (AIBN; 98%, Aldrich Chemical), and toluene (HPLC grade, J. T. Baker, Phillipsburgh, N.J.). The two solutions were mixed initially using a mechanical stirrer with Teflon paddle and then emulsified by passing the mixture through a static mixer for 30 minutes under an argon flow. The emulsion was heated to 70° C. with mechanical agitation, and left to stir at this temperature for 16 hours. Upon cooling, the suspension of formed particles was filtered and then washed consecutively with copious amounts of hot water (80-100° C.) and then methanol. The particles were then dried at 85° C. at a reduced pressure for 16 hours. Specific reagent amounts and reaction conditions are listed in Table 11. The specific surface areas (SSA), specific pore volumes (SPV), the average pore diameters (APD) and the % C of these materials are listed in Table 11 and were measured as described in Examples 2 and 3.

















TABLE 11






DVB
AIBN
Toluene
NVP
MAPTMOS
PVA

SSA
SPV
APD


Product
(g)
(g)
(mL)
(g)
(g)
(g)
% C
(m2/g)
(cm3/g)
(Å)

























14a
175
1.9
243
77.3
39
20
79.8
622
0.81
64


14b
174
1.9
243
103
77
20
77.3
394
0.32
35


14c
175
1.9
244
103
39
20
80.0
642
0.81
60









Example 15
Spherical, porous, hybrid inorganic/organic particles of Example 14 were mixed in either 1.0 or 2.5 M solutions of NaOH in water (Aldrich Chemical, Milwaukee, Wis.), yielding a suspension. The resultant suspension was then heated at 85-100° C. for 24-48 hours. After the reaction was cooled to room temperature the products were filtered and washed repeatedly using water and methanol (HPLC grade, J. T. Baker, Phillipsburgh, N.J.), and then dried at 80° C. under vacuum for 16 hours. This processing yielded free silanol groups, as evidenced by 29Si CP-MAS NMR spectroscopy. Specific amounts and conditions are listed in Table 12 (mL base solution/gram hybrid particle, base concentration, reaction temperature, and reaction time). The specific surface areas (SSA), specific pore volumes (SPV), the average pore diameters (APD) and the % C of these materials are listed in Table 12 and were measured as described in Examples 2 and 3.
















TABLE 12







Base
Base










Amount
Conc.
Time
Temp.

SSA
SPV
APD


Product
Precursor
(mL/g)
(Molarity)
(h)
(° C.)
% C
(m2/g)
(cm3/g)
(Å)







15a
14a
2.5
1.0
24
85
79.8
675
0.86
65


15b
14b
2.5
1.0
24
85
76.6
536
0.40
35


15c
14c
2.5
1.0
24
85
79.0
700
0.90
63









Incorporation by Reference
The entire contents of all patents, published patent applications and other references cited herein are hereby expressly incorporated herein in their entireties by reference.
EQUIVALENTS
Those skilled in the art will recognize, or be able to ascertain using no more than routine experimentation, numerous equivalents to the specific procedures described herein. Such equivalents were considered to be within the scope of this invention and are covered by the following claims. The contents of all references, issued patents, and published patent applications cited throughout this application are hereby incorporated by reference.

## Claims

1. A porous inorganic/organic homogenous copolymeric hybrid material of the formula:



wherein
R1 is H, F, Cl, Br, I, lower alkyl;
R2 and R3 are each independently H, F, Cl, Br, I, alkane, substituted alkane, alkene, substituted alkene, aryl, substituted aryl, cyano, ether, substituted ether, embedded polar group;
R4 and R5 are each independently H, F, Cl, Br, I, alkane, substituted alkane, alkene, substituted alkene, aryl, substituted aryl, ether, substituted ether, cyano, amino, substituted amino, diol, nitro, sulfonic acid, cation or anion exchange groups,
0≦a≦2, 0≦b≦4, and 0≦c≦4, provided that b+c≦4 when a=1;
1≦d≦20,
0.0003≦y/z≦500 and 0.002≦x/(y+z)≦210;
wherein the porous inorganic/organic homogenous copolymeric hybrid material has specific pore volumes of about 0.25 to 2.5 cm3/g and an average pore diameter of about 20 to 300 Å.

2. A separations device comprising a material according to claim 1.

3. The separations device according to claim 2, wherein said device is selected from the group consisting of chromatographic columns, thin layer plates, filtration membranes, sample cleanup devices, and microtiter plates.

4. The material according to claim 1, wherein 0.003≦y/z≦50 and 0.02≦x/(y+z)≦21.

5. The material according to claim 1, wherein said material has a specific surface area of about 50-800 m2/g.

6. The material according to claim 1, wherein said material is hydrolytically stable at a pH of about 1 to about 13.