Macroporous resins having large pores but with high crush...

Synthetic resins or natural rubbers -- part of the class 520 ser – Synthetic resins – Ion-exchange polymer or process of preparing

Reexamination Certificate

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C521S028000, C521S033000

Reexamination Certificate

active

06323249

ABSTRACT:

FIELD OF INVENTION
The invention relates to crosslinked macroporous resins and ion-exchange resins produced therefrom which are strong enough to be useful in the removal of colloidal silica and the removal of iron, aluminum and other metal hydroxides from aqueous media containing the same. More particularly, this invention relates to a process for producing a macroporous resin having extremely large pores along with higher pore volume, higher crush strength and a narrower pore distribution than such macroporous resins heretofore known in the art.
BACKGROUND OF THE INVENTION
Methods of preparing crosslinked polymers, and anion and cation exchange resins derived therefrom, which are characterized by macroporous structures and which show improved properties compared to traditional gel resins, are known. In contrast to conventional gel resins formed by copolymerization of monovinylidene and polyvinylidene monomers and characterized by the presence of micropores, the pore structure being the distance between the crosslinked polymeric chains, macroporous resins contain a significant nongel porosity in addition to normal gel porosity. This nongel porosity arises from channels present between the gel lattice. These microscopic channels are separate and distinct from the micropores, which are present in all crosslinked copolymers, as is well known to those skilled in the art. While the channels are themselves relatively small, they are large when compared with the micropores of the prior art, gel type resins.
A number of patents have issued on macroporous resins and various methods for generating macroporosity. The terms macroporous, macroreticular, sponge-like and channelled have been used, more or less interchangeably, by those skilled in the art to characterize the opaque beads and resins. Pore-forming, phase-separating, precipitant and porogen have, likewise, been used to refer to the agent used to produce the macroporous structure.
British Patent 785,157 and U.S. Pat. No. 3,122,514 disclose the use of pre-polymerized styrene dissolved in mixtures of divinylbenzene, styrene and a polymerization initiator yielding opaque beads with microchannels and pores through which molecules can diffuse more readily than in conventional resins. Ion exchange resins prepared from these copolymer beads are disclosed in British Patent 785,157 as being much more resistant to shock, superior as anion exchangers in color removal and, as cation exchangers, were directly hydratable after sulfonation with little or no breakage. However, this technology did not improve resistance to oxidative de-crosslinking of the polymeric matrix itself and introduced the problem of leaching of the original linear polystyrene additive in cation exchange products produced by this process. That is, the linear polymer chains, which are not crosslinked, become on sulfonation at least partially water soluble and leach from the resin, causing contamination of any fluid passing through the resin. Such resins not only contaminate the fluids they were intended to purify but also process fluids, which affects production economics adversely since reagents cannot be recycled. Moreover, environmental pollution must be addressed. In the process of U.S. Pat. No. 3,122,514 linear polystyrene is either formed-in or dissolved-in the styrene monomer mix which is thereafter polymerized. The linear polystyrene that is tangled into the crosslinked copolymer bead is then leached out of the bead leaving channels through the bead.
U.S. Pat. Nos. 3,367,889 and 3,627,708 disclose a system whereby an emulsion of water in styrene-divinylbenzene is polymerized as droplets in a surrounding aqueous suspension. These patents disclose the use of water in combination with a surfactant as the porogen in forming macroporous resins.
U.S. Pat. Nos. 4,221,871, 4,224,415, 4,256,840 and 4,501,826 are each directed to methods of preparing crosslinked macroreticular resins, containing at least one monovinylidene and a polyvinylidene monomer, which are phase separated by the use of a precipitant in the monomer mixture during aqueous suspension polymerization. The precipitant is disclosed as being either a liquid or solid in its natural state, the preferred class of precipitants being liquid under the polymerization conditions. Suitable precipitants are materials which are solvents for the monomers being copolymerized but exert essentially no solvent action on the copolymer. Examples include butanol, sec-butanol, tert-amyl alcohol, 2-ethylhexanol and decanol. By adding the precipitant to the monomer phase, the solubility of the. copolymer formed is decreased and the copolymer separates from the monomer phase as it is formed. This phenomenon is referred to as ‘phase separation’. As the concentration of monomer in the polymerizing mass decreases due to polymerization and as the concentration of the precipitant increases thereby, the newly formed polymer is more strongly repelled.
U.S. Pat. No. 3,454,493 discloses macroreticular resins achieved by copolymerizing monoethylenically unsaturated monomers with polyvinylidene monomers in the presence of a precipitant by the phase-separating technique as defined heretofore. The anion exchange resins subsequently formed are characterized by having average pore diameters in the range of 10,000 to about 500,000 Angstroms. The Example set forth in this patent discloses a macroreticular resin having a range of pore diameters from 30,000 to 200,000 Angstroms and a mean pore diameter of 70,000 Angstroms. The macroreticular anion exchange resin is claimed to remove colloidal particulate matter from aqueous media.
European Patent Application 0,135,292 discloses crosslinked macroporous resins using water-soluble polymeric porogens (such as poly (vinyl methyl ether) which are soluble in polymerizing monomers under the conditions of polymerization and which are at least partially soluble in water under certain physical conditions to facilitate removal following polymerization. After separation of the resulting copolymer from the mixture, any remaining porogen is extracted with water as solvent. The polymeric porogens disclosed in the European Patent Application are described as being more effective porogens at lower levels than polystyrene porogens or other precipitants previously used in the art as porogens, yielding greater porosities. The resulting resins are disclosed as having a mean pore radius as high as 2,052 Angstoms.
SUMMARY OF THE INVENTION
A process has now been discovered by which macroporous resins may be produced which exhibit desirable properties not present in prior art macroporous resins. The nature of the pore distribution of these prior-art resins was such that the resins were physically very weak. As a result, potential users of ion exchange processes for the removal of colloidal matter chose alternative methods such as ‘reverse osmosis’. The macroporous resins produced by the novel process have extremely large-sized pores, but their narrower distribution of pore sizes gives them sufficiently high crush strength for most, purposes. This narrower pore distribution also results in the bulk of the resin's porosity being in the useful size range for removal of colloidal matter, thereby increasing its effectiveness in this respect.
The resins may be sulfonated to form cation exchange resins or, alternatively, may be chloroalkylated and subsequently aminated to form anion exchange resins. Both weak and strong base anion exchangers are encompassed by the invention, strong base anion exchange resins being preferred for the removal of colloidal silica and other such colloidal matter from aqueous media.


REFERENCES:
patent: 3454493 (1969-07-01), Kien
patent: 3767600 (1973-10-01), Albright
patent: 4256840 (1981-03-01), Meitzner et al.
patent: 4501826 (1985-02-01), Meitzner et al.
patent: 4818773 (1989-04-01), Cornette et al.
patent: 1918399 (1970-12-01), None
patent: 0135292 (1985-03-01), None

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