Abstract:
Ion exchange resins exhibiting increased crush strength and/or higher density are prepared from a cross-linked polymer by imbibing a halo-substituted olefin within the cross-linked polymer's structure and subsequently polymerizing the imbibed olefin. For example, imbibing vinylidene chloride within a chloromethylated, cross-linked copolymer of styrene and subsequently polymerizing the vinylidene chloride forms a high density resin, which resin is useful in the preparation of ion exchange and chelate type resins having improved crush strength.
Abstract:
A process for producing reagents useful in organic synthesis, for removing metal values from solutions thereof, for the capture of aldehydes, of the general formula ##STR1## wherein Z designates a recurring part (CH.sub.2 --CH--CH.sub.2) of a polymeric backbone of a polymer like polystyrene, of a copolymer comprising polystyrene and divinylbenzene, and butadiene, or other copolymers comprising styrene moieties; or wherein Z is the aliphatic moiety of a long-chain aralkyl compound having a terminal aryl group; or wherein Z designates alkyl; corresponding compounds wherein instead of the optionally substituted phenyl group there is present an optionally substituted naphthyl group; wherein n is an integer of from 1 to 15, and wherein Q designates a group selected from: ##STR2## wherein R designates --H, lower alkyl, aryl, which may be substituted and wherein R" designates --H, alkyl, aryl, halogen, nitro or carboxy, or ##STR3## wherein R is --H, lower alkyl, aryl (which may be substituted), R.sub.1 is --H, alkyl, aryl (which may be substituted), R.sub.2 is --H, alkyl, aryl or substituted aryl, and wherein Y is --H or a non-interferring substituent, which comprises chemically binding an activated chemical moiety to a group ##STR4## or a corresponding naphthyl-containing group, wherein Z is as defined above, according to the reaction scheme: ##STR5## wherein Q is as defined above, or a functional group which can be converted to such group after the chemical bonding; and X is --Cl or --Br.
Abstract:
An ion exchange resin having functional groups of the formula :- ##STR1## wherein :- A and B, independently of each other, represent groups forming together with the attached carbon and nitrogen atoms, an optionally substituted five or six membered heterocyclic ring which may embody a further heteroatom and wherein at least one of such heterocyclic rings is an aromatic ring; R* may be totally absent or it may represent an optionally substituted alkyl radical and Z represents a resin to which the functional groups are attached.
Abstract translation:具有下式的官能团的离子交换树脂:其中:-A和B彼此独立地表示与连接的碳和氮原子一起形成的基团,任选取代的五元或六元杂环,其可以 体现另外的杂原子,其中至少一个这样的杂环是芳环; R *可以完全不存在,或者其可以表示任选取代的烷基,Z表示与官能团连接的树脂。
Abstract:
Novel complexes of macrocyclic polyethers such as 1,4,7,10,13,16-hexaoxacyclooctadecane (18-crown-6) and disulfonates of the formula I ##STR1## wherein X represents barium or strontium and R.sup.1 is an alkylene moiety, optionally substituted with an alkyl group, are described as well as a process for isolating said macrocylic polyethers through formation of said novel complexes. In the isolation process disclosed, a macrocyclic polyether containing solution is contacted with a disulfonate of formula I to afford the polyether-disulfonate complex as a solid suspension in the solution, the suspended complex is separated from the solution and the separated complex is extracted with a solvent for the macrocyclic polyether.
Abstract:
A method and system combining filtration and ion-exchange structures for removing contaminants from liquids. In overall concept, contaminated liquid is passed through filtering mediums to remove particulate matter from the incoming contaminated liquid. Organics are removed from the liquid by passage through adsorbent non-ionic type resins. The liquid is then passed through strong acid cation exchange resins, weak base anion exchange resins, weak acid cation exchange resins, and strong base anion exchange resins arranged in a predetermined location in the liquid flow path to provide optimized contaminant removal. One of the optimization techniques is through the pH adjustment of the liquid at predetermined points in the flow path. Additionally, the liquid to be purified is passed through mixed bed polisher resins as well as chelation resins to provide a final substantially contaminant free liquid which is returned to use in a closed loop fashion.
Abstract:
Ferric ions are removed from a concentrated aqueous zinc solution having a pH value in the range of about 0 to about 1.3, by contacting the zinc solution with a cation exchange chelate resin containing aminocarboxylic acid and/or iminodicarboxylic acid groups.
Abstract:
The present invention relates to ion exchange compounds on cellulose basis having formula ##STR1## wherein R is a group that forms chelate complexes with metal ions, and Cell stands for the cellulose matrix. Suitable functional groups R are derivatives of known metal reactants, which show a high degree of selectivity for specific metal ions. The ion exchange compounds are able to fix specifically preferred ions e.g. metal ions even in a considerable excess of foreign ions, for example in concentrated salt solutions.The improved ion exchange compounds of this invention are prepared by reacting the compound ##STR2## with cellulose in the presence of alkali, diazotizing the cellulose derivative resulting therefrom and subsequently coupling couplable compounds which form chelate complexes with metal ions.
Abstract:
New chelate exchange resins capable of selective recovery of copper, nickel, and other valuable metals from an acidic aqueous leach liquor are prepared by reacting a crosslinked haloalkyl polymer matrix resin (I) with certain aminopyridines (II) to give a resin (III) ##STR1## with pendent methyleneaminopyridine groups attached to the matrix resin. Particularly useful resins are obtained by reacting chloromethylated styrene-divinylbenzene copolymer beads with an aminomethylpyridine, such as 2-picolylamine, N-methyl-2-picolylamine, N-(2-hydroxyethyl)-2-picolylamine, N-(2-methylaminoethyl)-2-picolylamine, or bis-(2-picolyl)amine. At a typical copper ore leach liquor pH of about 2, the picolylamine resins will absorb 15-30 mg copper/ml resin with a 5-10 fold selectivity for copper over ferric iron.
Abstract:
A phenolic chelate resin having a high heavy-metal chelating ability and capable of being reused is produced by polycondensing a phenol containing an iminodiacetic acid group with an aldehyde.
Abstract:
PASSING AN AQUEOUS SOLUTION OF SALTS OF THE TITLE METALS AT A PH OF 1.5 TO 3.5 AND AT A TEMPERATURE OF 30 TO 80* C. THROUGH AT LEAST TWO SERIALLY CONNECTED RESIN COLUMNS CONTAINING A COMPLEX-FORMING ION EXCHANGE RESIN HAVING AMINOCARBOXYLIC ACID AND/OR IMINODICARBOXYLIC ACID GROUPS AS THE ACTIVE EXCHANGE GROUPS UNTIL NICKEL AND/OR COBALT IONS APPEAR IN THE EFFLUENT OF THE LAST RESIN COLUMN AND THEN DISCONNECTING AND ELUTING NICKEL AND/OR COBALT FROM THE FIRST RESIN COLUMN.