Metallo-organic polymers for gas separation and purification

Abstract: The present invention provides for methods and compositions for gas separation and purification utilizing a metallo-organic polymer adsorbent in processes for separating carbon dioxide, water, nitrogen oxides and hydrocarbons from gas streams. The metallo-organic polymer adsorbent composition has the formula: [R(L) n ] m M n , wherein R represents an organic spacer selected from the group consisting of an organic cyclic or acyclic compound; L represents a ligation group substituted on the organic spacer selected from the group consisting of carboxylate group, -C(=O)O - ; dithiocarboxylate group, -C(=S)S - ; and β-diketonate group, -C(=O)C(R')=C(-O - )-, wherein R' = H, or an aliphatic or aromatic group; M represents a transition metal or a rare earth metal m is the oxidation state of the transition or rare earth metal; and n is the number of the ligation group substituted on the organic spacer.

Description: This invention relates to gas separation and purification employing microporous adsorbents in the form of metallo-organic polymers. Presently, numerous microporous materials that are mainly based on zeolites, other zeo-type inorganic solids, various types of activated carbon, such as carbon molecular sieves and super-activated carbons, are being used as solid adsorbents for gas separation and purification. Zeolites are porous crystalline aluminosilicates, whose framework is constructed by SiO 4 and AlO 4 tetrahedra, which are joined together in various regular arrangements through shared oxygen atoms, to form an open crystal lattice containing uniform pores. Each aluminum atom within that lattice introduces one negative charge on zeolite framework which must be balanced by a positive charge of an exchangeable cation. After activation of zeolites, the exchangeable cations are located, in most cases, at preferred extra- framework sites within the voids formed by the lattice. These cations play a significant role in determining the adsorption properties of the particular zeolites. Moreover, zeolites have high chemical and thermal stability owing to their inorganic nature of the framework. Unlike zeolites, the structure of activated carbons mainly consists of elementary microcrystallites of graphite. These microcrystallites are stacked together in random orientation. The micropores are formed by the spaces between those microcrystallites, the diameter of which range from ~3 Å to ~20 Å. In addition, there may exist mesopores (20 to 500 Å) and macropores (>500 Å), as well. Therefore, activated carbon adsorbents generally show very little selectivity over molecules with different sizes. However, due to the nonpolar surface of carbon, an activated carbon tends to be hydrophobic and organophilic. With respect to carbon molecular sieves, their structure is similar to that of activated carbon in most general terms, but they have a very narrow distribution of micropore sizes ranging from about 3 to 9 Å, for the various types, and thus they behave as molecular sieves. Clearly, all of these materials, zeolites, activated carbon, and carbon molecular sieves, combine microporosity with high chemical and thermal stability, which are essential for gas separation and purification. Although it is difficult to design and build the microporous structures of these sieve materials with specific pore sizes in a systematic way, a wealth of structures is known by now. Variation of chemical formulation and functionality, however, meets limits due to complexity of phenomena and costs involved. US-A-3 192 236 discloses polymeric metal chelate complexes of anthraquinone. The metal may be nickel, copper, cobalt or zinc. US-A-2 659 711 discloses a wide range of polymeric metal chelate complexes of tetraketones. The metal may, for example, be nickel, copper or zinc. Phenylene and biphenylene groups may be employed in the tetraketone complexes. EP-A-727 608 discloses adsorbents for the storage of methane comprising various organometallic complexes, for example, aryl carboxylate complexes of copper. GB-A-939 191 discloses various molybdenum containing polymers including those containing the repeating structural unit [(C 6 H 5 COO) 2 Mo]. In accordance with the purposes of the invention there is provided according to a first aspect thereof a method for separating a component from a gas mixture comprising subjecting said gas mixture to an adsorption process comprising the steps: a) passing said gas mixture through at least one adsorbent zone containing an organo-metallic polymer having the formula: [R(L) n ] m M n wherein R represents an organic spacer selected from the group consisting of an organic cyclic or acyclic compound; L represents a ligation group substituted on the organic spacer selected from the group consisting of carboxylate group, -C(=O)O - ; dithiocarboxylate group, -C(=S)S - ; and β-diketonate group, -C(=O)C(R')=C(-O - )-, wherein R' = H, or an aliphatic or aromatic group; M represents a transition metal or rare earth metal m is the oxidation state of the transition metal or rare earth metal; and n is the number of the ligation group substituted on the organic spacer as adsorbent at a selected temperature and pressure thereby preferentially adsorbing said component from said gas mixture; and b) regenerating said adsorbent at a temperature higher than said selected temperature, at a pressure lower than said selected pressure, or at both a temperature higher than said selected temperature and a pressure lower than said selected pressure. Structural modification of the metallo-organic polymers can be made to further enhance desirable functionalities. For example, the channel linings can be chemically functionalized using organic bases, or they can be doped with inorganic salts such as lithium, silver, copper(I/II) salts to create specific adsorption sites that are tailored for a particular gas separation and purification. The invention also provides a metallo-organic polymer for use as adsorbent in a method according to any one of the preceding claims, the metallo-organic polymer having the formula: [R(L) n ] m M n wherein R represents an organic spacer selected from the group consisting of an organic cyclic or acyclic compound; L represents a ligation group substituted on the organic spacer selected from the group consisting of carboxylate group, -C(=O)O - ; dithiocarboxylate group, -C(=S)S - ; and β-diketonate group, -C(=O)C(R')=C(-O - )-, wherein R' = H, or an aliphatic or aromatic group; M represents a transition metal or rare earth metal m is the oxidation state of the transition metal or rare earth metal; and n is the number of the ligation group substituted on the organic spacer and being doped with lithium, silver, copper (I), or copper (II) salts, or mixtures thereof. Unlike zeolites, other microporous zeo-type materials and carbons, the metallo-organic polymeric adsorbent materials used in the method according to the invention provide unique surfaces which are comprised of carbon, hydrogen, oxygen and nitrogen atoms, and framework metal sites. Owing to their tunable organic and metallic parts of the microporous structures, they have advantages over presently utilized adsorbents in engineering of specific pore sizes and sorption sites in a systematic way. Therefore, along with zeolites, carbon molecular sieves and other carbonaceous adsorbents, this new class of adsorbents expand material selections for industrial gas separation applications. Methods and adsorbents according to the invention will now be described by way of example with reference to the accompanying drawings in which: Figure 1 is a graph of adsorption equilibrium data for the use of an adsorbent of the present invention for CO 2 and CH 4 . Figure 2 is a graph of adsorption equilibrium data for the use of an adsorbent of the present invention for N 2 , O 2 , CO 2 and N 2 O. Figure 3 is a graph of adsorption equilibrium data for the use of an adsorbent of the present invention for N 2 , O 2 , CH 4 , CO 2 and ethylene. Figure 4 is a graph of adsorption equilibrium data for the use of an adsorbent of the present invention for ethylene and ethane. Figure 5 is a graph of adsorption equilibrium data for the use of an adsorbent of the present invention for H 2 O. The methods according to the invention may be used in PSA PPU and TSA PPU processes for CO 2 , H 2 O, N 2 O, separation of hydrocarbon/CO 2 mixtures, and syngas. The metallo-organic polymers are microporous and can be produced by metal-ligand dative bonds from transition metal ions, and bi-, tri-, tetra-, or multicarboxylates, and the like. Typically, the metal is Zn, Cu, Co, Ru, Os, or a rare earth metal. (Some polymers for use according to the invention are known ie, in the case where the organic spacer is a benzene ring, and the ligation group is a carboxylate and n = 2 or 3, it is known that M may be Co, Cu, Zn or Tb.) The following examples are given to demonstrate novel microporous adsorbents for use in the present invention characterized by the formula [R(L) n ] m M n , where the ligation groups are dithiocarboxylate and β-diketonate groups, such as Table 1 below sets forth, for illustrative purposes, various multicarboxylic acids suitable for use in the formation of the novel microporous adsorbents of the present invention characterized by the formula [R(L) n ] m M n . The microporous metallo-organic polymers for use in the present invention are either X-ray crystalline, amorphous or at the borderline of such crystallinity. In general, their micropore topologies are mostly different from those of the inorganic zeo-type ones, but in a number of cases they may be analogous to the latter, in terms of structural patterns. Important features of such adsorbents were a very narrow (homogeneous) pore size distribution, a high pore volume and the opportunity of tailoring the pore size, intentionally. Unlike zeolites, the channel linings can be functionalized chemically. They can also be doped comparatively easily with inorganic salts such as lithium, silver, or copper(I) salts or mixtures thereof, to create specific adsorption sites for gas separation and purification. For example, copper(I/II) metal salts can be supported on these adsorbents for their use as CO-selective adsorbents. In order to do so, a cuprous compound or a cupric compound, such as CuCl or CuCl 2 , can be impregnated into a microporous metallo-organic framework such as that of copper (II) benzene-1,3,5-tricarboxylate, Cu-BTC, with the aid of solvents. The solvents include water, alcohol, acetone, ethyl acetate, acetonitrile. The most preferred solvents are water and alcohol. It is envisaged that the novel microporous metallo-organic polymer adsorbents can be utilized in: a) PSA PPU and TSA PPU for removal of CO 2 , H 2 O, N 2 O, and oil vapor from air streams; b) Removal (trapping) of heavy hydrocarbons, in particular compressor oil vapor, in N 2 PSA and O 2 VSA / PSA processes; c) PSA / TSA processes for bulk phase removal of CO 2 , H 2 O and high level of hydrocarbons (> C 2 ) from CH 4 ; d) PSA / TSA processes for separation of hydrocarbon / CO 2 mixtures such as ethylene / CO 2 ; e) PSA / TSA processes for bulk phase separation and purification of CO from CO 2 , CH 4 , H 2 , N 2 , O 2 and Ar; f) Removal of CO 2 from CO 2 / C 2 H 2 mixtures (bulk and trace); g) Separation of gaseous olefin / paraffin mixtures of low molecular weight, e.g., ethylene-ethane mixtures; h) Drying agent and moisture sensor utilization. The following examples are set forth below for illustrative purposes. EXAMPLE 1 Preparation of copper(II) benzene-1,3,5-tricarboxylate (Cu-BTC): Benzene-1,3,5-tricarboxylic acid (1 g, 4.76 mmol) was dissolved into ethanol (12 ml), and cupric nitrate hydrate (Cu(NO 3 ) 2 •2.5H 2 O; 2 g, 8.60 mmol) was dissolved into ethanol (12 ml). The two solutions were mixed at ambient temperature for 30 minutes. Then they were poured into an autoclave with a 45-ml teflon cup. The autoclave was heated at 110°C under hydrothermal conditions for 17 hours. The reaction vessel was cooled to ambient temperature, and then the blue hexagonal crystals of Cu-BTC were isolated by filtration, and washed with water. The product was dried at 110°C overnight. The yield was 87%. Analysis by TGA showed that a fully hydrated product contained up to 40 wt.% water, and it was stable up to ca. 340°C. The product had a polymeric structure. If the polymer contains x copper atoms its formula is [(BTC) 2 Cu x ] x Adsorption equilibrium properties for gas separation processes: The Cu-BTC adsorbent of Example 1 was tested for its adsorption equilibrium properties and suitability in a number of gas separation processes. The adsorption data were obtained using a piezometric (constant volume - variable pressure) method at 22°C. The results of these tests are set forth in Figures 1 to 5. Figure 1 presents the adsorption equilibrium data for CO 2 and CH 4 . The data demonstrates that the adsorbent can be used in separation of gaseous mixtures containing CO 2 and CH 4 , such as syngas separations, due to preferential adsorption of CO 2 . Adsorption equilibrium data for N 2 , O 2 , CO 2 and N 2 O on Cu-BTC sorbent are presented in Figure 2. The data demonstrates that the adsorbent can be used in PSA PPU processes for removal of CO 2 and N 2 O from air streams , due to preferential adsorption of CO 2 and N 2 O. Adsorption equilibrium data for N 2 , O 2 , CH 4 , CO 2 and ethylene on Cu-BTC sorbent are presented in Figure 3. The adsorption data demonstrates that the adsorbent preferentially adsorbing ethylene to other gases can be used in recovery of ethylene in ethylene partial oxidation processes. Adsorption equilibrium data for ethylene and ethane on Cu-BTC adsorbent are presented in Figure 4. The adsorbent preferentially adsorbs ethylene as compared to ethane. It can also be used to separate other olefin / paraffin mixtures. Adsorption equilibrium data for H 2 O on Cu-BTC sorbent are presented in Figure 5. The adsorbent provides a very large saturation capacity for water, and its color changes from dark purple when it is dry to light blue when water is adsorbed. Thus, the material can be used both as a drying agent and as moisture sensor, and also as an adsorbent for moisture removal using PSA / TSA processes, such as in PPU processes upfront to cryogenic air distillation. EXAMPLE 2 Impregnation of CuCl 2 into Cu-BTC for CO-selective adsorbent: Cu-BTC was dried at 150°C for 4 hours before use. CuCl 2 •6H 2 O (1.22 g) were dissolved into absolute alcohol (20 ml). Cu-BTC (3 g) was then added to the solution. The mixture was stirred for 30 minutes using a magnetic stirrer before putting it in a mechanical shaker for 22 hours at ambient temperature. Next, all solvent was removed under a reduced pressure yielding a blue material. It was then dried at 110°C under vacuum. The yield was 97%. The adsorbent was heated at 190°C under CO atmosphere for 3 hours and evacuated before the CO uptake test was performed on a microbalance. As a result, at 25°C, this adsorbent has a CO adsorption capacity of 1.08 mmol/g at a CO pressure of 984 mbar. EXAMPLE 3 Oil vapor removal test without moisture: Sorbent beads of the metallo-organic polymer, made of Cu-BTC powder by shaping the latter at appropriate conditions, were evaluated for oil vapor removal from compressed air in an n-dodecane sorption breakthrough experiment. About 94 gram of the adsorbent beads was packed in a 1" adsorbent vessel. A feed consisting of dry N 2 and about 10 ppm n-dodecane vapor at total pressure of 80 psia, temperature, 25 °C, and flowrate, 100 scfh, was used in an sorption breakthrough experiment to determine the sorption capacity of the novel sorbent for n-dodecane. The sorbent takes up ca . 68 wt.% of n-dodecane at n-dodecane partial pressure, 0.04 torr, by a physical sorption process, before the n-dodecane concentration in the effluent stream reaches 1 ppm. This experiment proves that the new sorbent has an extremely large sorption capacity for hydrocarbons. EXAMPLE 4 Oil vapor removal test with moisture: Similar n-dodecane sorption breakthrough experiments as described in Example 3 were also carried out with a moisture-saturated N 2 stream and an n-dodecane concentration therein, that amounts to 100 ppm. A sorption capacity of 1.85 wt.% was measured at an n-dodecane partial pressure of 0.4 torr before the n-dodecane concentration in the effluent stream reaches 0.2 ppm. Thus, it has proven that the novel sorbent can still sorb a significant amount of hydrocarbons under conditions of relatively high humidity. EXAMPLE 5 PSA cyclic experiments of 30 minutes feed and 30 minutes N 2 purge were also performed to demonstrate the regeneration properties of the novel Cu-BTC sorbent. The feed step was carried out at a total pressure, 80 psia, temperature, 25° C, with both dry and moisture-saturated gas streams containing 10 ppm n-dodecane at a flow rate of 100 scfh. House nitrogen at a flowrate, 50 scfh, was used to purge the adsorber at 25° C and 15.0 psia. Cyclic experimental results with both dry and wet gas streams as feed have shown that the sorbed amount of n-dodecane can be desorbed, and the sorbent was gradually regenerated in the PSA cycles with a purge-to-feed ratio of ca . 2.6 for both cases.

Claims: A method for separating a component from a gas mixture comprising subjecting said gas mixture to an adsorption process comprising the steps: a) passing said gas mixture through at least one adsorbent zone containing an organo-metallic polymer having the formula: [R(L) n ] m M n wherein R represents an organic spacer selected from the group consisting of an organic cyclic or acyclic compound; L represents a ligation group substituted on the organic spacer selected from the group consisting of carboxylate group, -C(=O)O - ; dithiocarboxylate group, -C(=S)S - ; and β-diketonate group, -C(=O)C(R')=C(-O - )-, wherein R' = H, or an aliphatic or aromatic group; M represents a transition metal or rare earth metal m is the oxidation state of the transition metal or rare earth metal; and n is the number of ligation groups substituted on the organic spacer as adsorbent at a selected temperature and pressure thereby preferentially adsorbing said component from said gas mixture; and b) regenerating said adsorbent at a temperature higher than said selected temperature, at a pressure lower than said selected pressure, or at both a temperature higher than said selected temperature and a pressure lower than said selected pressure. A method as claimed in claim 1, wherein R is a benzene ring. A method as claimed in claim 1 or claim 2, wherein L is carboxylate group, -C(=O)O - . A method as claimed in any one of the preceding claims wherein M is selected from the group consisting of Zn, Cu, Co, Ru, Os, and the rare earth metals, except Co, Cu, Zn, and Tb when L is -C(=O)O - and n = 2 and 3. A method as claimed in anyone of the preceding claims, wherein said metallo-organic polymer is doped with lithium, silver or copper (I/II) salts or mixtures thereof. A method as claimed in anyone of the preceding claims wherein said metallo-organic polymer is in the form of shaped particles. A method as claimed in any one of the preceding claims, wherein carbon dioxide, water, and N 2 O are removed from a gas stream containing them. A method as claimed in any one of claims 1 to 6, wherein hydrocarbons are removed from a gas stream containing them. A method as claimed in claim 7 or claim 8, wherein said gas stream is air. A method as claimed in any one of claims 1 to 6, wherein said adsorption process is a cyclic adsorption process selected from pressure swing adsorption or temperature swing adsorption. A method as claimed in any one of claims 1 to 6 and 10, wherein said component is ethylene and said gas mixture is CO 2 /ethylene. A method as claimed in claim 10, wherein said component is CO and said gas mixture contains CO 2 , CH 4 , H 2 , N 2 , O 2 and Ar. A metallo-organic polymer for use as adsorbent in a method according to any one of the preceding claims, the metallo-organic polymer having the formula: [R(L) n ] m M n wherein R represents an organic spacer selected from the group consisting of an organic cyclic or acyclic compound; L represents a ligation group substituted on the organic spacer selected from the group consisting of carboxylate group, -C(=O)O - ; dithiocarboxylate group, -C(=S)S - ; and β-diketonate group, -C(=O)C(R')=C(-O - )-, wherein R' = H, or an aliphatic or aromatic group; M represents a transition metal or rare earth metal m is the oxidation state of the transition metal or rare earth metal; and n is the number of ligation groups substituted on the organic spacer and being doped with lithium, silver, copper (I), or copper (II) salts, or mixtures thereof. A polymer as claimed in claim 13, wherein R is a benzene ring. A polymer as claimed in claim 13 or claim 14, wherein L is a carboxylate group -C(=O)O - . A polymer as claimed in any one of claims 13 to 15, wherein M is selected from the group consisting of Zn, Cu, Co, Ru, Os, and the rare earth metals, except Co, Cu, Zn, and Tb when L is -C(=O)O - and n = 2 and 3. A polymer as claimed in any one of claims 13 to 16, in the form of shaped particles. Use as an adsorbent in gas separation and purification of a metallo-organic polymer as claimed in any one of claims 13 to 17.

Inventors: BUELOW MARTIN, DENG SHUGUANG, FITCH FRANK R, LAU MIU LING, SHEN DONGMIN, WANG QING MIN, BUELOW, MARTIN, DENG, SHUGUANG, FITCH, FRANK R., LAU, MIU LING, SHEN, DONGMIN, WANG, QING MIN, Bülow, Martin 
Applicants: BOC GROUP INC, THE BOC GROUP, INC.
Application year: 2000
Main classification: B01J20
IPC codes: C08G79, B01J20, B01D53