WO1996013464A1 - Methods of coagulating and decolorizing waste streams - Google Patents
Methods of coagulating and decolorizing waste streams Download PDFInfo
- Publication number
- WO1996013464A1 WO1996013464A1 PCT/US1995/013089 US9513089W WO9613464A1 WO 1996013464 A1 WO1996013464 A1 WO 1996013464A1 US 9513089 W US9513089 W US 9513089W WO 9613464 A1 WO9613464 A1 WO 9613464A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- polyamine
- parts
- weight
- polymer
- acid colloid
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/26—Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof
- C02F2103/28—Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof from the paper or cellulose industry
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S210/00—Liquid purification or separation
- Y10S210/902—Materials removed
- Y10S210/917—Color
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S210/00—Liquid purification or separation
- Y10S210/928—Paper mill waste, e.g. white water, black liquor treated
Definitions
- This invention generally relates to the clarification of waste waters or raw waters, more specifically to the coagulation and decolo ⁇ zation of process waters resulting from deinking, pulp and paper mills using melamme-aldehyde polymer combined with polyamine.
- the paper typically goes through a deinking process which initially defibers the paper, e.g., waste newspnnt, in an aqueous bath containing a deinking agent and a detergent or other surface active agent in addition to the paper
- the waste newspnnt is defibered
- the ink is removed from the fibers
- Vanous combinations of washing, flotation and cleaning steps are used to separate the fibers from one another and from the ink and to remove the ink and other materials from the repupled stock Effluent streams resulting from this process, also called process waters, contain color bodies which generally include inks - - both water-based inks such as flexographic ink and oil-based inks such as nonimpact inks and lithographic inks - - as well as lignms, lignin degradation products, humic acids and pectins Color bodies may be found in other types of wastestreams and raw waters such as fresh water bodies
- MacroDorous aminot ⁇ azinealdehyde resins are described as being useful for treating paper pulp mill effluent
- a melamine formaldehyde acid colloid poiyme' is taught as being useful for separating ink-laden solids and turbidity from deinking process waters.
- an effective amount of flocculant may subsequently be added to assist the solids/liquid separation.
- acid colloid polymers have been found to be relatively poor coagulants.
- Polyamines have been used as coagulants, often in conjunction with a flocculant, in treating waste waters.
- copolymers of diallyldimethylammonium chloride and anionic monomer are disclosed in US 5,013,456 and US 5,207,924 as being useful for coagulating suspended solids from deinking process waters.
- copolymers of diallyldimethylammonium chloride and certain anionic comonomers are taught as being useful to decolorize pulp mill waste waters. See also U.S. 4,746,457 and 5,330,656.
- Polyamines made from epoxy compounds and secondary amines are also taught as being useful for clarifying raw water in US 3,894,944 and US 3,894,945 and for flocculating industrial wastes in US 3,894,947, each of which are incorporated by reference. These polyamines, however, tend to exhibit insufficient efficacy for color removal at normal doses. Polyamines have been used in conjunction with other clarification aids to treat certain wastewaters. Water soluble polyamine epichlorohyd ⁇ n polymers, among other cationic polymers, are taught in WO 93/02967 as being useful in combination with an anionic colloidal material for flocculating suspended solids in ink-laden waste waters.
- EP 529 865 describes methods of decolorizing effluent streams from pulp mill plants using ferrous sulfate and any water-soluble cationic polyamine such as diallyldimethylammonium chloride polymers or polyamines made from epihalohydrin and lower alkyl diamine.
- Polyamines made from epichlorohydrin have also been used together with a melamine formaldehyde acid colloid polymer to treat wastestreams resulting from paper production and municipal sludge treatment. In such instances, the polyamine and acid colloid polymer were fed separately into the effluent waste stream in a 1 :1 or 2:1 ratio on site. But this resulted in less than satisfactory water clarification.
- melamine aldehyde polymers are less expensive than polyamines the improved coagulant compositions of the present invention are also economically desirable.
- handling and processing advantages are obtained by the ability of using only one feed line for the polyamine/melamme aldehyde acid colloid polymer mixture instead of two separate feed lines for the two polymer components.
- the present invention provides a composition for separating, preferably by coagulation, suspended solids and color bodies in effluent or waste water streams, preferably those resulting from deinking, paper or pulp mill operations.
- Raw waters containing suspended solids and/or color bodies may also be treated by the compositions herein.
- coagulant as used for purposes of this invention p ⁇ marily refers to agents which cause the agglomeration or precipitation of solids by, for example, charge neutralization (technically known as coagulation) and can also include agents that combine solids into larger agglomerates or "floes" by, for example, bridging (technically known as flocculation).
- compositions comprising a polyamine and a melamine aldehyde acid colloid polymer in a ratio of about 90.0 - 99.9 parts by weight polyamine to about 10.0 - 0.1 parts by weight of acid colloid polymer; wherein the polyamine is a reaction product of a secondary amine and a difunctional epoxy compound or precursor thereof.
- the compositions of the present invention which comp ⁇ se polyamine and melamine aldehyde polymer in the amounts specified herein are also called “coagulant compositions" for purposes of this invention.
- the compositions of the present invention consist essentially of melamine formaldehyde acid colloid polymer and polyamine
- the present invention also provides a method for separating suspended solids from a wastewater stream or raw water which comD ⁇ ses: (i) adding to said wastewater stream in an amount sufficient to coagulate said solids a composition comp ⁇ sing polyamine and melamine aldehyde acid colloid polymer in a ratio of about 90.0 - 99.9 parts by weight of polyamine to about 10.0 - 0.1 parts by weight of acid colloid polymer; wherein said polyamine is a reaction product of a secondary amine and a difunctional epoxy compound or precursor thereof; and (ii) separating said solids from said wastewater stream or raw water.
- the ratio of polyamine to acid colloid polymer ranges from about 96.5 to about 99.9 parts by weight polyamine to about 3.5 - 0.1 parts by weight acid colloid polymer.
- a method for separating suspended solids and color bodies from deinking process waters resulting from the processing of recycle paper which comp ⁇ ses: (i) adding to said process water from about .5 to about 150 parts per million, based on said process water, of a composition comprising a polyamine and a melamine formaldehyde acid colloid polymer in a ratio of about 96.5 - 99.9 parts by weight of polyamine to about 3.5 - 0.1 parts by weight of acid colloid polymer; wherein said polyamine is a reaction product of a secondary amine and a difunctional epoxy compound or precursor thereof; and (ii) separating said solids and said color bodies from said process water.
- the polyamines used in the instant invention are those formed by the reaction of difunctional epoxy compounds with lower alkyl secondary amines. These polyamines are well known in the art and disclosed in, for example, US Patent 3,894,944; US Patent 3,894,945; US Patent 3,894,946; US Patent 3.894,947; and US Patent 3,894,947 each disclosure of which are incorporated by reference.
- the difunctional epoxy compounds used to make the polyamines are usually halohydrins such as epihalohyd ⁇ ns and precursors of epihalohydrins which are converted into corresponding epoxy compounds under alkaline conditions. Epichlorohydrin is preferred.
- Typical secondary amines used to prepare the polyamines used in the present invention include those containing alkyl groups having 1 to 3 carbon atoms; dimethylamines are preferred.
- the molecular weight of the polyamines used in the present invention is not critical. Usually, the molecular weight ranges from about 25,000 to about 1 million, preferably
- Suitable melamine aldehyde acid colloid polymers also called “melamine aldehyde polymers” or “acid colloid polymers” (or MFAC) herein unless the context dictates otherwise, include any polymer prepared from the following two components: 1 ) a melamine or substituted melamine, and 2) a compound having the following general formula- O
- R, - C - R 2 wherein R, and R, are selected from the group consisting of H and straight or branched alkyl groups having from 1-4 carbons and wherein R, and R- may be the same or different
- suitable substituted melamine are known in the art or can be ascertained by one skilled in the art through routine expe ⁇ mentation; preferred substituted melammes include tnmethylolmelamine, N-guanylmelamine, N-phenylmelamine, N- benzylmelamine and benzoguanamine
- aldehydes such as formaldehyde, acetaldehyde, and propionaldehyde, t ⁇ oxane, paraformaldehyde and mixtures thereof and the like are preferred with formaldehyde as most preferred
- the mole ratio of the first component (melamine) to second component preferably ranges from about 1 1 to about 1 6, more preferably from about 1.2 to about 1 4, most preferably about 1.3 to about 1
- the melamine aldehyde polymer tends to be insoluble in water it usually exists in the form of an acid colloid polymer which means that the melamine aldehyde polymer is maintained in acidic aqueous solution, generally a colloidal suspension, which typically contains anywhere from about 0.1 to about 20 weight percent melamine aldehyde, preferably about 1 to about 15 weight percent and most preferably about 4 to about 12 weight percent melamine aldehyde, acid is present in amounts sufficient to maintain a low pH such that the melamine aldehyde polymer will remain as a colloidal suspension and not precipitate
- the pH of the colloidal suspension of melamine aldehyde polymer ranges from about 1 4 to about 2 2, more preferably from about 1 6 to about 1 8
- a broad range of acids may be used to prepare the melamine aldehyde acid colloid sucn as, for example, acetic, hydrochloric, pnosphoric, formic, propionic, hydrochloric acid is most pre
- the molecular weight of the melamine aldehyde acid colloid polymer is not critical.
- Preferred molecular weight ranges from about 500 to about 200,000, more preferably from about 75,000 to about 175,000.
- Suitable melamine aldehyde acid colloid polymers are known in the art and commercially available, for example, from Cytec Industnes Inc. under the trademark PARAMEL®.
- the ratio of polyamine to MFAC is important and usually ranges from about 90.0 - 99.9 parts by weight polyamine to about 10 - 0.1 parts by weight MFAC preferably from about 93.0 - 99.1 parts by weight polyamine to about 7.0 - 0.1 parts by weight MFAC, more preferably from about 96.5 - 99.9 parts by weight polyamine to about 3.5 - 0.1 parts by weight MFAC and most preferably from about 98.0 - 99.9 parts by weight polyamine to about 2.0 - 0.1 parts by weight MFAC.
- a most preferred range also includes about 98.04 - 99.64 parts by weight polyamine to about 1.96 - 0.36 parts by weight MFAC.
- the amount of MFAC in the coagulant composition is usually at least 0.1 parts, preferably at least 0.2 parts, more preferably at least 0.36 parts.
- the melamine aldehyde polymers are mixed into the polyamine or polyamine aqueous solution with mild agitation, usually for 15-20 minutes. Additional materials may be added to the coagulant composition as long as the materials do not inhibit the coagulation performance of the composition. Such additional mate ⁇ als include, for example, alcohols, glycols and mixtures thereof and the like.
- compositions of the present invention may be added to the water being treated by any conventional method.
- the coagulant composition is added to the wastestream or raw water being treated in a feed water line.
- the addition of an effective amount of coagulant composition generally causes formation of distinct floes by coagulation.
- wastestreams such as sludge, preferably any wastestream or raw water that contains color bodies and suspended solids, more preferably pulp and paper mill wastestreams, most preferably wastestreams resulting from deinking processes.
- the amount of coagulant composition to be used should generally be an amount sufficient to coagulate the suspended solids in the wastestream or raw water being treated, preferably an amount sufficient to coagulate the suspended solids and color bodies therein to facilitate the separation of suspended solids and color bodies from the water treated.
- coagulant composition dosage may range from about 0.5 to about 150 parts per million, based on the wastewater or raw water treated, preferably from about 7.5 to about 50 parts per million.
- the dosage usually ranges from about 5 to about 150 parts per million, based on the process water treated, preferably from about 1 to about 100 parts per million.
- the dosage usually ranges from about 1 to about 20 parts per million, based on the process water treated.
- the coagulated solids and color bodies are separated from the wastestream or raw water being treated by any conventional solid/liquid separation means, such as clarifiers, dissolved air flotation or settling clarifiers.
- a flocculant i.e., agent that combines solids into larger agglomerates or floes
- a flocculant may be added in an amount sufficient to flocculate the agglomerated solids and thereby further facilitate the solid liquid separation.
- suitable flocculants include conventional anionic, cationic, nonionic and amphoteric polymers, mixtures thereof and the like. It is preferred to use an anionic flocculant, especially in treating deinking process waters and paper and pulp waste waters.
- Preferred anionic polymer flocculant includes those made from the following monomers: acrylic acid, methacrylic acid, ethacrylic acid and their alkali metal or ammonium salts, vinyl sulfonic acid, 2-acrylamidc-2-alkylsulfonic acids and 2-acrylamido-2-alkylsulfonates where the alkyl group contains 1 to 6 carbon atoms, such as acrylamido 2-methyl propanesulfonic acid or mixtures of any of the foregoing and their alkali metal or ammonium salts. Hydrolyzed acrylamide may also be used.
- the anionic monomers may be copolyme ⁇ zed with (alk)acrylamide, preferably acrylamide or methacrylamide.
- Preferred cationic polymer flocculants include those prepared from the following monomers: dialkylaminoalkyl (meth)acrylates and dialkylaminoalkyl (meth. acrylamides, including their acid addition or quaternary ammonium salts, diallyl dialkyi ammonium halides, vinyl benzylt ⁇ alkyl ammonium salts, and the like.
- Quaternized Mannich or dialkyi ammo methylated (alk)acrylam ⁇ de polymers such as quaternary N-t ⁇ methylaminomethylacrylamide prepared by functionalizing (alk)acrylam ⁇ de or poly(alk)acrylam ⁇ de may be particularly preferred for certain applications.
- preferred cationic monomers include, N-d ⁇ methylam ⁇ nomethyl acrylam ⁇ de;acryloxyethyltnmethylammon ⁇ umchlo ⁇ de;methacryloxyethylt ⁇ methylammon ⁇ um chlonde; 2-methacryloyloxyethyl tnmethyl ammonium methosulfate, 2-methacryloyloxyethyl tnmethyl ammonium chlonde; diallydimethylammonium chlonde; 3-acrylam ⁇ do-3-methyl butyl tnmethyl ammonium chloride, 2-acrylam ⁇ do-2-methylpropyltnmethylammon ⁇ um chlonde, 3- methacryloyl-2- hydroxypropylt ⁇ methylammonium chlonde, dimethylaminoethylacrylate, dimethylaminoethylmethacrylate or mixtures of any of the foregoing. Mixtures of any of the above cationic monomers together with
- Preferred nonionic polymer flocculants include those prepared from the following monomers acrylamide, methacrylamide; dialkylaminoethyl acrylamides, N,N- dialkylacrylamides; N-alkylacrylamides, N-vinyl-acetamide; N-vinyl formamide, N-vinyl pyrrolidone and mixtures thereof Especially preferred is acrylamide and methacrylamide
- amphoteric polymers for use in the present invention comp ⁇ se copolymers of one or more of the foregoing anionic monomers and one or more of the cationic ethylenically unsaturated monomers listed above or monomers which contain both anionic and cationic functionalities
- suitable polyampholytes include polymers comprising i) acrylic acid, methacrylic acid, 2-acrylam ⁇ do-2-methyl- propylsulfonic acid or 2-methacrylam ⁇ do-2-methylpropylsulfon ⁇ c acid, alone or in combination, and u) dimethyldiallyl ammonium chlonde, dimethyldiallylammomum bromide, diethyldiallylammonium chloride or diethyldialylammonium bromide, alone or in combination, wherein the weight ratio of component i) to component n) ranges from about 90:10 to about
- the polyampholytes may also contain nonionic moieties such as acrylamide or methacrylamide
- the most preferred flocculants to be used with the compositions of the instant invention are anionic polymers, preferably anionic polymers that contain from about 2 to about 50 mole percent anionic functionality, based on monomer, more preferably from about 10 to about 40 mole percent anionic functionality, based on monomer
- anionic polymers preferably have a molecular weight of at least about 16 million, more Dreferablv at least about 30 million
- anionic flocculants which may be used in the present invention include hvdrolyzed polyacrvlamide acrviamide/acrvlic acid copolymers. acrylamide/acrylate copolymers, polyacrylates and acrylamide/acrylamido methylpropane sulfonic acid copolymers.
- polymer flocculant may vary depending on the water being treated and the coagulant composition dosage. In this sense, optimal flocculant dosage may be readily determined by one skilled in the art by routine expe ⁇ mentation. For process waters resulting from a deinking process waters, for example, flocculant dosages ranging from about 1 to about 125 ppm, based on the process water, may be preferred.
- the suspended solids and color bodies may be removed by any conventional means known in the art, such as, for example clanfiers, settling tank.
- the coagulant composition used was prepared by adding .5g of a melamine formaldehyde acid colloid (MFAC) (9% by weight active; pH about 1.8) to 25g of polyamine (50% by weight active)
- the polyamine was made from epichlorohydrin and dimethylamine and had a molecular weight of about 75,000
- the MFAC had a molecular weight of about 175,000
- the coagulant composition compnsed polyamine and MFAC in a ratio of 98.04 parts by weight polyamine to 1.96 parts by weight MFAC
- To the process water was added an amount of coagulant composition to deliver 50ppm polymer (real) based on the process water
- the cylinder was then inverted six times to ensure adequate mixing and initiate coagulation.
- a hydrolyzed polyacrylamide flocculant (molecular weight of about 32 million) containing about 40 mole percent anionic functionality, based on monomer, was subsequently added at a dosage of 3 8 ppm polymer, based on the process water, to facilitate liquid/solid separation
- the cylinder was inverted twice to commence the flocculation process Floe size, stability, and the rate of liquid/solid separations were evaluated
- a portion of the resulting filtrate was removed and the following parameters were measured turbidity (NTU). color (L ' ,a ) as measured by the CIELAB color space system and percentage total suspended solids (%TSS) removed. The results are presented in TABLE 1.
- Example 1 The procedure used in Example 1 was followed except that the coagulant composition was prepared by adding .09g of MFAC (9 weight % active; pH about 1.8) to 25g of polyamine (50% by weight active). The ratio of polyamine to MFAC in the composition was 99.64 parts by weight polyamine to 0.36 parts by weight MFAC. The results for filtrate turbidity, floe stability, color measurements and total suspended solids removed appear in TABLE 1.
- Example 1 The procedure in Example 1 was followed except that the coagulant composition was prepared by adding 0.09g of MFAC (9 % by weight active; pH about 1.8) to 10g polyamine (50% by weight active). The ratio of polyamine to MFAC in the composition was 99.14 parts by weight polyamine to 0.89 parts by weight MFAC. The results are listed in TABLE 1.
- Example 4 The tests in Examples 4-6 were performed as controls and do not represent the invention.
- Example 4 the procedure used in Example 1 was followed except that no coagulant and no flocculant was added.
- Example 5 the procedure used in Example 1 was followed except that 50 ppm of polyamine was added to the process water, based on the process water. Subsequently 3.8ppm of the anionic flocculant used in Example 1 was also added with agitation. The results are listed in TABLE 1
- Example 6 the procedure used in Example 1 was followed except that 50 ppm of MFAC, based on the process water, was added to the process water. Subsequently 3.8ppm of the anionic flocculant used in Example 1 was added. The results appear in TABLE 1
- compositions comprising polyamine and MFAC in a general ratio of about 97.5 to about 99.9 parts polyamine to about 2.5 to about 0.1 MFAC, preferably 98.04 to about 99.64 parts polyamine to about 1.96 to about 0.36 parts MFAC as shown in Table 1 above provide superior performance with respect to coagulation and color removal as compared to the use of a polyamine or an MFAC alone at the same dosage.
- Example 7 the procedure in Example 1 was used to treat a process water from a paper deinking mill using compositions containing polyamine (molecular weight 50,000) and MFAC (9% active, pH about 1.8, molecular weight about 175,000) in various ratios as set forth in Table II, except that 3.9 ppm of 30 mole percent hydrolyzed polyacrylamide was used as the flocculant.
- polyamine molecular weight 50,000
- MFAC 9% active, pH about 1.8, molecular weight about 175,000
- compositions containing polyamine (molecular weight about 75,000) and MFAC (molecular weight about 175,000) in various ratios were prepared and their physical appearance was observed and set forth in Table III. The observations indicate that levels of MFAC generally greater than 30 parts, preferably greater than 10 parts decreases stability and clarity of coagulant compositions. TABLE III
- Example 1 The procedure in Example 1 was used to treat a process water from a paper deinking mill (70% old newsprint/ 30% old magazine) using compositions containing polyamine (molecular weight 75,000, 50% active) and MFAC (9% active) in various ratios as set forth in Table IV. On this particular process water the optimal ratio appears to be about 1.96% MFAC to 98.04% polyamine, based on real solids. Improved performance was generally obtained from using compositions containing from about 0.1% - 10.0% by weight MFAC to 99.9% - 90.0 by weight polyamine. TABLE IV
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP95937427A EP0789673B1 (en) | 1994-10-31 | 1995-10-04 | Methods of coagulating and decolorizing waste streams |
DE69506736T DE69506736T2 (en) | 1994-10-31 | 1995-10-04 | METHOD FOR COAGULATING AND DECOLORATING WASTEWATER |
MXPA/A/1997/002741A MXPA97002741A (en) | 1994-10-31 | 1997-04-15 | Methods of coagulation and decoloration decorrientes residua |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US33222094A | 1994-10-31 | 1994-10-31 | |
US08/332,220 | 1994-10-31 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1996013464A1 true WO1996013464A1 (en) | 1996-05-09 |
Family
ID=23297258
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1995/013089 WO1996013464A1 (en) | 1994-10-31 | 1995-10-04 | Methods of coagulating and decolorizing waste streams |
Country Status (7)
Country | Link |
---|---|
US (2) | US5707532A (en) |
EP (1) | EP0789673B1 (en) |
AT (1) | ATE174579T1 (en) |
CA (1) | CA2203883A1 (en) |
DE (1) | DE69506736T2 (en) |
ES (1) | ES2125671T3 (en) |
WO (1) | WO1996013464A1 (en) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6132625A (en) | 1998-05-28 | 2000-10-17 | E. I. Du Pont De Nemours And Company | Method for treatment of aqueous streams comprising biosolids |
US6149822A (en) * | 1999-03-01 | 2000-11-21 | Polymer Ventures, Inc. | Bio-film control |
US6395189B1 (en) | 1999-03-01 | 2002-05-28 | Polymer Ventures, Inc. | Method for the control of biofilms |
US6482943B1 (en) | 1999-04-30 | 2002-11-19 | Slil Biomedical Corporation | Quinones as disease therapies |
WO2002038105A2 (en) * | 2000-11-08 | 2002-05-16 | Slil Biomedical Corporation | Novel polyamine analog-amino acid conjugates useful as anticancer agents |
US6649587B1 (en) | 1999-04-30 | 2003-11-18 | Slil Biomedical Corporation | Polyamine analog conjugates and quinone conjugates as therapies for cancers and prostate diseases |
EP1177197B1 (en) | 1999-04-30 | 2006-08-09 | Cellgate, Inc. | Polyamines and their use in therapy |
AU4678300A (en) * | 1999-04-30 | 2000-11-17 | Slil Biomedical Corporation | Novel polyamine analog conjugates and quinone conjugates as therapies for cancers and prostate diseases |
FI112315B (en) | 1999-05-11 | 2003-11-14 | Nokia Corp | Integrity protection method for radio network signaling |
US6203711B1 (en) * | 1999-05-21 | 2001-03-20 | E. I. Du Pont De Nemours And Company | Method for treatment of substantially aqueous fluids derived from processing inorganic materials |
US6454961B1 (en) * | 2000-09-19 | 2002-09-24 | Baffin, Inc. | Elixir for inducing high-speed settlement of precipitates |
US6780330B2 (en) | 2001-03-09 | 2004-08-24 | E. I. Du Pont De Nemours And Company | Removal of biomaterials from aqueous streams |
US20020179538A1 (en) * | 2001-03-23 | 2002-12-05 | Johnson Brian S. | Polyamphoteric polymers for raw water treatment |
CA2469354A1 (en) * | 2001-12-07 | 2003-06-19 | Slil Biomedical Corporation | Cycloalkyl substituted polyamines for cancer therapy and methods of synthesis therefor |
US7380125B2 (en) | 2003-05-22 | 2008-05-27 | International Business Machines Corporation | Smart card data transaction system and methods for providing high levels of storage and transmission security |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0493987A1 (en) * | 1991-01-04 | 1992-07-08 | Betz Europe, Inc. | Clarification of water |
EP0529865A1 (en) * | 1991-08-12 | 1993-03-03 | Nalco Chemical Company | Pulp mill wastewater color removal |
Family Cites Families (31)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2862901A (en) * | 1958-12-02 | Aqueous solution of amino-aldehyde | ||
US2609307A (en) * | 1949-11-14 | 1952-09-02 | American Cyanamid Co | Treatment of wool with acid aminotriazine resin colloids |
US3894948A (en) * | 1973-04-02 | 1975-07-15 | American Cyanamid Co | Process for treating sewage sludge |
US3894944A (en) * | 1973-04-02 | 1975-07-15 | American Cyanamid Co | Process for raw water clarification |
US3894946A (en) * | 1973-04-02 | 1975-07-15 | American Cyanamid Co | Process for treating industrial wastes |
US3894947A (en) * | 1973-04-02 | 1975-07-15 | American Cyanamid Co | Process for treating industrial wastes |
US3894945A (en) * | 1973-04-02 | 1975-07-15 | American Cyanamid Co | Process for raw water clarification |
JPS5435185A (en) * | 1977-08-24 | 1979-03-15 | Kyoritsu Yuki Kogyo Kenkyusho:Kk | Cationic polymeric coagulant |
US4307201A (en) * | 1978-08-31 | 1981-12-22 | Diamond Shamrock Corporation | Highly adsorptive macroporous polymers |
US4786364A (en) * | 1984-08-02 | 1988-11-22 | Calgon Corporation | DMDAAC/AM copolymers as deinkers |
US4880498A (en) * | 1986-08-04 | 1989-11-14 | American Cyanamid Company | Dry strength resin of amino/aldehyde acid colloid with acrylamide polymer, process for the production thereof and paper produced therefrom |
US4800039A (en) * | 1987-03-05 | 1989-01-24 | Calgon Corporation | Flocculation of suspended solids from aqueous solutions |
JPH0783869B2 (en) * | 1987-03-20 | 1995-09-13 | 三井サイテック株式会社 | Method for treating starch-containing water |
US4913825A (en) * | 1988-05-27 | 1990-04-03 | W. R. Grace & Co.-Conn. | Method for controlling overspray in paint spray booths |
US5002999A (en) * | 1988-09-07 | 1991-03-26 | Mobay Corporation | Internal mold release agent for use in reaction injection molding |
US5286346A (en) * | 1988-11-23 | 1994-02-15 | Henkel Kommanditgesellschaft Auf Aktien | Deinking of wastepaper with quaternized hydroxyethyl cellulose |
DE3839479A1 (en) * | 1988-11-23 | 1990-06-07 | Henkel Kgaa | THINKING OF WASTE PAPER |
DE3934893A1 (en) * | 1989-10-19 | 1991-04-25 | Gruenau Gmbh Chem Fab | WAFER, ERDALKALISEIFEN AND / OR EARTHALKALIHARSE SOAPS CONTAINING DISPERSIONS FOR DEFINING PRINTED ALTPAPERS |
US5013456A (en) * | 1990-04-13 | 1991-05-07 | Nalco Chemical Company | Diallyldimethyl ammonium chloride polymers with anionic monomers for coagulating deinking process waters |
US5240509A (en) * | 1991-05-28 | 1993-08-31 | Calgon Corporation | Method for removing solids from systems containing water-based paints |
GB9116701D0 (en) * | 1991-08-02 | 1991-09-18 | Allied Colloids Ltd | Dewatering of aqueous suspensions |
GB9116702D0 (en) * | 1991-08-02 | 1991-09-18 | Allied Colloids Ltd | Dewatering of aqueous suspensions |
US5433824A (en) * | 1993-02-26 | 1995-07-18 | Calgon Corporation | Melamine-formaldehyde polymer for controlling stickies |
US5207924A (en) * | 1992-06-19 | 1993-05-04 | Nalco Chemical Company | Diallyl dimethyl ammonium chloride copolymers in deinking process water clarification |
US5209854A (en) * | 1992-06-29 | 1993-05-11 | Nalco Chemical Company | Pulp waste color removal with diallyl dimethyl ammonium chloride copolymers |
US5302291A (en) * | 1992-09-30 | 1994-04-12 | Calgon Corporation | Method for improving the dispersibility of solvent-based paints in aqueous systems |
US5286390A (en) * | 1992-09-30 | 1994-02-15 | Calgon Corporation | Method for treating deink wastes using melamine aldehyde-type polymers |
US5330656A (en) * | 1993-03-05 | 1994-07-19 | Calgon Corporation | Polysalt compositions and the use thereof for treating an oil and water system |
US5415733A (en) * | 1993-05-27 | 1995-05-16 | High Point Chemical Corp. | Method of removing hydrophilic ink |
US5454955A (en) * | 1994-03-25 | 1995-10-03 | Nalco Chemical Company | Use of hectorite as a clarification aid for deink plant effluent |
US5435921A (en) * | 1994-05-09 | 1995-07-25 | Nalco Chemical Company | Vinylamine polymers and coagulants for removing color from paper mill effluents |
-
1995
- 1995-10-04 DE DE69506736T patent/DE69506736T2/en not_active Expired - Fee Related
- 1995-10-04 AT AT95937427T patent/ATE174579T1/en active
- 1995-10-04 CA CA002203883A patent/CA2203883A1/en not_active Abandoned
- 1995-10-04 EP EP95937427A patent/EP0789673B1/en not_active Expired - Lifetime
- 1995-10-04 WO PCT/US1995/013089 patent/WO1996013464A1/en active IP Right Grant
- 1995-10-04 ES ES95937427T patent/ES2125671T3/en not_active Expired - Lifetime
-
1996
- 1996-09-17 US US08/714,877 patent/US5707532A/en not_active Expired - Fee Related
- 1996-09-19 US US08/724,264 patent/US5807496A/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0493987A1 (en) * | 1991-01-04 | 1992-07-08 | Betz Europe, Inc. | Clarification of water |
EP0529865A1 (en) * | 1991-08-12 | 1993-03-03 | Nalco Chemical Company | Pulp mill wastewater color removal |
Also Published As
Publication number | Publication date |
---|---|
DE69506736D1 (en) | 1999-01-28 |
US5807496A (en) | 1998-09-15 |
ATE174579T1 (en) | 1999-01-15 |
US5707532A (en) | 1998-01-13 |
MX9702741A (en) | 1997-09-30 |
ES2125671T3 (en) | 1999-03-01 |
EP0789673B1 (en) | 1998-12-16 |
EP0789673A1 (en) | 1997-08-20 |
DE69506736T2 (en) | 1999-05-20 |
CA2203883A1 (en) | 1996-05-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0789673B1 (en) | Methods of coagulating and decolorizing waste streams | |
TWI227704B (en) | Anionic and nonionic dispersion polymers for clarification and dewatering | |
US5013456A (en) | Diallyldimethyl ammonium chloride polymers with anionic monomers for coagulating deinking process waters | |
US5178770A (en) | Method of treating bctmp/ctmp wastewater | |
EP0952118B1 (en) | Water clarification by addition of colloidal silica followed by addition of polyelectrolyte | |
KR100468554B1 (en) | Hydrophilic Dispersion Polymers for the Clarification of Deinking Process Waters | |
US20040035800A1 (en) | Flocculation of mineral suspensions | |
US5286390A (en) | Method for treating deink wastes using melamine aldehyde-type polymers | |
EP0630858B1 (en) | Composition and method for water clarification and wastewater treatment | |
US5601725A (en) | Hydrophobically modified polymers for sludge dewatering | |
KR20010033893A (en) | Dewatering of sludges deriving from paper industry | |
US5429749A (en) | Polymers for treatment of food processing wastes | |
CA2023735C (en) | Compositions and process for removing toxic resin acids and derivatives from effluent | |
US5589075A (en) | Use of silicon containing polyelectrolytes in wastewater treatment | |
US5961838A (en) | Amphoteric polymer/polyamine combinations for color removal and clarification of paper mill waste water | |
JP3064878B2 (en) | Organic sludge treatment | |
WO2000032519A1 (en) | Hydrophilic dispersion polymers of diallyldimethyl ammonium chloride and acrylamide for the clarification of deinking process waters | |
MXPA97002741A (en) | Methods of coagulation and decoloration decorrientes residua | |
JPH1133563A (en) | Treatment of used paper pulp waste water | |
AU764315B2 (en) | Hydrophilic dispersion polymers of diallyldimethyl ammonium chloride and acrylamide for the clarification of deinking process waters | |
WO1993002968A1 (en) | Dewatering of aqueous suspensions |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): CA MX |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 1995937427 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: PA/a/1997/002741 Country of ref document: MX |
|
ENP | Entry into the national phase |
Ref document number: 2203883 Country of ref document: CA Ref country code: CA Ref document number: 2203883 Kind code of ref document: A Format of ref document f/p: F |
|
WWP | Wipo information: published in national office |
Ref document number: 1995937427 Country of ref document: EP |
|
WWG | Wipo information: grant in national office |
Ref document number: 1995937427 Country of ref document: EP |