AU4232800A - Novel composition of ferric chloride and a dialkyl diallyl ammonium polymer and process of preparing the same - Google Patents

Novel composition of ferric chloride and a dialkyl diallyl ammonium polymer and process of preparing the same Download PDF

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Publication number
AU4232800A
AU4232800A AU42328/00A AU4232800A AU4232800A AU 4232800 A AU4232800 A AU 4232800A AU 42328/00 A AU42328/00 A AU 42328/00A AU 4232800 A AU4232800 A AU 4232800A AU 4232800 A AU4232800 A AU 4232800A
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Australia
Prior art keywords
diallyl ammonium
composition
water
parts
fec1
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Abandoned
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AU42328/00A
Inventor
Denis E. Hassick
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Calgon Corp
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Calgon Corp
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K3/00Materials not provided for elsewhere
    • C09K3/32Materials not provided for elsewhere for absorbing liquids to remove pollution, e.g. oil, gasoline, fat
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56Macromolecular compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02Separation of non-miscible liquids
    • B01D17/04Breaking emulsions
    • B01D17/047Breaking emulsions with separation aids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/01Separation of suspended solid particles from liquids by sedimentation using flocculating agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D3/00Differential sedimentation
    • B03D3/02Coagulation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • C02F1/5245Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/16Halogen-containing compounds

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Public Health (AREA)
  • Materials Engineering (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

WO00/63316 PCT/US00/09725 Novel Composition Of Ferric Chloride And A Dialkyl Diallyl Ammonium Polymer And Process Of Preparing The Same Background of the Invention The use of various coagulants for the flocculation of suspended solids from aqueous solutions is well known in the art. Many coagulants are known including alum, aluminum sulfate, ferric chloride, ferric sulfate and lime. Commonly used polyelectrolytes for this purpose include polydimethyl (pDMDAAC) and Epi-DMA polyamine. Blends of the inorganic coagulants with polyelectrolytes are known in the art. These blends combine the desirable properties of each component in the system to be treated without the need of feeding two separate additives at different points in the system. This presents a cost advantage in many circumstances and greatly simplifies treatment for many systems. United States Patent No. 5,035,808, teaches the blending of commercial grade solutions of ferric salts and cationic polymers. Commercial grade ferric sulfate solution can be blended with either polyamine or p-DMDAAC to form stable products. However, it was not possible to prepare a viable product by blending commercial grade ferric chloride solutions (38-42 wt% active raw material) with p-DMDAAC. Such a blend was not possible because a gel would be formed immediately upon mixing. This problem is noted in column 3, lines 3-6 of United States Patent No. 5,035,808. Instead, it was only possible to blend commercial grade ferric chloride solutions with polyamine. Each group of polyelectrolyte has its own set of unique properties that it brings to the blend of polymer and inorganic coagulant. It would be very desirable to be able to combine the benefits of ferric chloride with WO00/63316 PCT/US00/09725 2 those of p-DMDAAC in a composition that could be added as a single component to treat water systems. Summary of the Invention The composition according to the present invention comprises FeC1 3 and a dialkyl diallyl ammonium polymer, where the FeC1 3 has been diluted with water prior being mixed with the polymer. The process according to the present invention for the production of a composition comprises the dilution of a FeC1 3 solution with water and the subsequent addition of a dialkyl diallyl ammonium polymer. This process results in a stable blend of FeC1 3 and the dialkyl diallyl ammonium polymer which resulting composition may be utilized as an effective coagulant for various applications. Detailed Description of the Invention A method has been discovered by the inventor to combine FeC1 3 and a dialkyl diallyl ammonium polymer to make a stable blend. This method consists of diluting an FeC1 3 solution with water prior to mixing with the dialkyl diallyl ammonium polymer. The inventor has unexpectedly discovered that if the FeC1 3 is dilute prior to the addition of dialkyl diallyl ammonium polymer, a stable blend of the two components is possible. This is a dramatic discovery and permits the addition of a single component to a system that normally required the addition of two separate additives at two separate points for an effective treatment of the system's water. The FeC1 3 is preferably present in the composition of the present invention in a concentration of about 0.5% to about 20% by weight active FeC1 3 , more preferably about 5% to about 16% by weight. Blends with concentrations of FeC1 3 much above 20% by weight are not stable and gel, WO00/63316 PCT/US00/09725 3 whereas dilute blends as low as 0.5% by weight and below do not have enough FeC1 3 to cause a significant effect in the water system to be treated. If the dialkyl diallyl ammonium polymer is diluted first and then blended with the ferric chloride, stirring must be constant or the material gels. Thus, this method of preparation is less preferred. Additionally, the inventor has unexpectedly discovered that this gel, as well as the gel formed when the neat (undiluted) components are blended, can be reconstituted by dilution and agitation. However, the resulting product is not as clear and clean as when the FeC1 3 is diluted first and then blended with the dialkyl diallyl ammonium polymer. The present invention relates to a novel composition and process of preparation wherein a commercial grade ferric chloride (FeC1 3 ) solution can be blended with a dialkyl diallyl ammonium polymer by diluting the ferric chloride prior to addition of the dialkyl diallyl ammonium polymer. This commercial grade ferric chloride (FeC1 3 ) solution is preferably diluted approximately 1:1 with water, and then such diluted composition is combined with the dialkyl diallyl ammonium polymer. The dialkyl diallyl ammonium polymer is preferably a water-soluble C-C8 dialkyl diallyl ammonium polymer. This C1-Cs dialkyl diallyl ammonium polymer is more preferably selected from the group consisting of polydimethyl diallyl ammonium chloride, polydiethyl ammonium chloride, polydiethyl diallyl ammonium chloride, polydimethyl diallyl ammonium bromide, and polydiethyl diallyl ammonium bromide. The most preferred water soluble Cl-Cs dialkyl diallyl ammonium polymer is polydimethyl diallyl ammonium chloride (polyDMDAAC or p DMDAAC). For the purpose of this description, the commercial WO00/63316 PCT/US00/09725 4 grade ferric chloride is a FeCl 3 solution generally contains 38-42 wt% active raw material. Similarly, the dialkyl diallyl ammonium polymer is preferably p-DMDAAC and is a 40 wt % solution. One skilled in the art will understand that the ratios of these two compounds set forth below are specific to these concentrations. However, the process of this invention is easily applicable to compounds of varying concentrations if the ratios are modified accordingly. Utilizing these concentrations, the most preferred ratios (in parts per volume) of FeC1 3 solution, water and p-DMDAAC are 10 FeC1 3 , 10 H 2 0 and 5 p-DMDAAC. When this ratio is utilized, a solution is immediately formed which remains stable for months. When the ratios of 10 FeC1 3 and 5 p-DMDAAC are utilized, a volume of water less that ten parts can be used to obtain a relatively stable blend. However, a volume of water less that 7.5 parts should not be used. At 7.5 parts the resultant mixture immediately thickens and is hazy. This mixture is somewhat stable over time, it precipitates, but it never quite solidifies. It is thus more preferred that the volume of water be greater than 7.5 parts and as close to a 1:1 ratio with the FeC13 solution as possible. At the above noted concentrations of each component, the most preferred combination, in parts by volume, is 10 FeC1 3 , 10 H 2 0 and 5 p-DMDAAC. The preferred process for preparing the claimed composition is to add the 10 parts deionized water to the 10 parts FeC1 3 solution (a 1:1 ratio), while mixing, in order to dilute the FeCl 3 solution. Following the water, 5 parts p-DMDAAC should be added to the mixture while stirring. A clear solution will result which does not exhibit precipitation. The resulting composition is an excellent coagulant WO00/63316 PCTUS00/09725 5 for use in many applications including general wastewater, municipal wastewater, wastewater containing metals, papermaking wastewater, water containing chemical compounds, water containing biological compounds, poultry processing waste, ink containing solutions, raw surface water, oil/water mixtures, colored solutions, coal waste, oily waste, water with suspended solids raw municipal drinking water, electrolytic primer coating wastewater and industrial wastewater.

Claims (20)

1. A composition comprising FeC1 3 and a dialkyl diallyl ammonium polymer, where the FeC1 3 has beendiluted with water prior being mixed with the polymer.
2. The composition of claim 1 wherein the FeC1 3 is present in the composition in a concentration of about 0.5 to about 20% by weight active FeC1 3 .
3. The composition of claim 1 wherein the FeCl 3 is a solution containing 38 to 42 percent active raw material and is diluted with water in a ratio of 7.5 parts by volume or more water to 10 parts by volume FeC13 solution.
4. The composition of claim 3 wherein the ratio of parts of water to parts of FeC1 3 solution by volume is one by one.
5. The composition of claim 1 wherein: a. the FeC1 3 is a solution containing 38 to 42 percent active raw material and is 10 parts by volume of the composition; b. the water is 10 parts by volume of the composition; and c. the dialkyl diallyl ammonium polymer is of 40% weight percent and is 5 parts by volume of the composition.
6. The composition of claim 1 wherein the dialkyl diallyl ammonium polymer is a water-soluble Cl-Cs dialkyl diallyl ammonium polymer.
7. The composition of claim 6 wherein the water soluble C 1 -Cs dialkyl diallyl ammonium polymer is selected from the group consisting of polydimethyl diallyl ammonium chloride, polydiethyl ammonium chloride, polydiethyl diallyl ammonium chloride, polydimethyl WO00/63316 PCT/US00/09725 7 diallyl ammonium bromide, and polydiethyl diallyl ammonium bromide.
8. The composition of claim 7 wherein the water soluble C 1 -Cs dialkyl diallyl ammonium polymer is polydimethyl diallyl ammonium chloride (polyDMDAAC).
9. A process for the production of a composition comprising the dilution of a FeC1 3 solution with water and the subsequent addition of a dialkyl diallyl ammonium polymer.
10. The process of claim 9 wherein the FeCl 3 is present in the final composition in a concentration of about 0.5 to about 20% by weight active FeC1 3 .
11. The process of claim 9 wherein the FeC13 solution contains 38 to 42 percent active raw material and is diluted with water in a ratio of 10 to 7.5 parts by volume.
12. The process of claim 11 wherein the ratio of parts of water to parts of FeC1 3 solution by volume is one to one.
13. The process of claim 9 wherein: a. the FeC1 3 is a solution containing 38 to 42 percent active raw material and is 10 parts by volume of the composition; b. the water is 10 parts by volume of the composition; and c. the dialkyl diallyl ammonium polymer is a 40% weight percent and is 5 parts by volume of the composition.
14. The process of claim 9 wherein the dialkyl diallyl ammonium polymer is a water-soluble Cj-Cs dialkyl diallyl ammonium polymer.
15. The process of claim 14 wherein the water soluble C 1 -C 8 dialkyl diallyl ammonium polymer is selected from the group consisting of polydimethyl diallyl WO00/63316 PCT/US00/09725 8 ammonium chloride, polydiethyl ammonium chloride, polydiethyl diallyl ammonium chloride, polydimethyl diallyl ammonium bromide, and polydiethyl diallyl ammonium bromide.
16. The process of claim 15 wherein the water soluble C1-Cs dialkyl diallyl ammonium polymer is polydimethyl diallyl ammonium chloride (polyDMDAAC).
17. A composition of matter comprising the product produced according to the process of claim 8.
18. A process for treating a solution comprising contacting the solution with an effective amount of the composition of claim 1.
19. A process for treating a solution comprising contacting the solution with an effective amount of the product produced according to the process of claim 8. INTERNATIONAL SEARCH REPORT International application No. PCT/USOO/09725 A. CLASSIFICATION OF SUBJECT MATTER IPC(7) :Please See Extra Sheet. US CL :156/142; 210/728, 735, 736; 252/180, 181; 524/435 According to International Patent Classification (IPC) or to both national classification and IPC B. FIELDS SEARCHED Minimum documentation searched (classification system followed by classification symbols) U.S. : 156/142; 210/728, 735, 736; 252/180, 181; 524/435 Documentation searched other than minimum documentation to the extent that such documents are included in the fields searched NONE Electronic data base consulted during the international search (name of data base and, where practicable, search terms used) WEST C. DOCUMENTS CONSIDERED TO BE RELEVANT Category* Citation of document, with indication, where appropriate, of the relevant passages Relevant to claim No X US 3,655,552 A (FLOCK JR, et al.) 11 April 1972, see column 2, 1-19 lines 24-75 and column 3, lines 60-61. X US 3,642,619 A (LO SASSO et al.) 15 February 1972, see column 1-19 2, lines 41-75, column 3, lines 1-17 and Table 1. X US 4,026,794 A (MAUCERI) 31 May 1977, see column 2, lines 29- 1-19 50, column 4, lines 8-23. X US 4,450,092 A (HUANG) 22 May 1984, see Abstract and column 1-19 2, lines 1-12. X US 5,035,808 A (HASSICK et al.) 30 July 1991 see column 4, 1-19 lines 7-8 and claim 3. Further documents are listed in the continuation of Box C. See patent family annex. * Special categories of cited documents: "T" later document published after the international filing date or priority date and not in conflict with the application but cited to understand the "A" document defining the general state of the art which is not considered principle or theory underlying the invention to be of particular relevance '"X" document of particular relevance; the claimed invention cannot be "E" earlier document published on or after the international filing date considered novel or cannot be considered to involve an inventive step "L" document which may throw doubts on priority claim(s) or which is when the documeca is taken alone cited to establish the publication date of another citation or other special reason (as specified) Y" document of particular relevance; the claimed invention cannot be considered to involve an inventive step when the document is "O" document referring to an oral disclosure, use, exhibition or other means combined with one or more other such documents, such combination "P" document published prior to the international filing date but later than being obvious to a person skilled in the art the priority date claimed "&" document meminber of the same patent family Date of the actual completion of the international search Date of mailing of the international search report 08 JUNE 2000 2 4 JUL 2000 Name and mailing address of the ISA/US Au rized officer Commissioner of Patents and TrademarksETER SZEKELY /- Box PCT PETER SZEKELYA lL7 Itl Washington, D.C. 20231 Facsimile No. (703) 305-3230 elephone No. (703) 308-0661 Form PCT/ISA/210 (second sheet) (July 1998)* INTERNATIONAL SEARCH REPORT International application No. PCT/US00/09725 C (Continuation). DOCUMENTS CONSIDERED TO BE RELEVANT Category* Citation of document, with indication, where appropriate, of the relevant passages Relevant to claim No. X US 4,067,806 A (MAUCERI) 10 January 1978, see col. 2, lines 1-19
25-34; col. 4, lines 1-3 and lines 50-68. Form PCT/ISA/210 (continuation of second sheet) (July 1998)* INTERNATIONAL SEARCH REPORT International application No. PCT/US00/09725 A. CLASSIFICATION OF SUBJECT MATTER: IPC (7): CO9K 3/32; C02F 1/00, 5/10; C08K 3/10, 3/16; B03D 3/06; BOID 21/01 Form PCT/ISA/210 (extra sheet) (July 1998)*
AU42328/00A 1999-04-20 2000-04-12 Novel composition of ferric chloride and a dialkyl diallyl ammonium polymer and process of preparing the same Abandoned AU4232800A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US13009899P 1999-04-20 1999-04-20
US60130098 1999-04-20
PCT/US2000/009725 WO2000063316A1 (en) 1999-04-20 2000-04-12 Novel composition of ferric chloride and a dialkyl diallyl ammonium polymer and process of preparing the same

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EP (1) EP1109874A4 (en)
JP (1) JP2003508548A (en)
KR (1) KR20010072626A (en)
CN (1) CN1302320A (en)
AR (1) AR023538A1 (en)
AU (1) AU4232800A (en)
BR (1) BR0006074A (en)
CA (1) CA2335715A1 (en)
NO (1) NO20006490L (en)
WO (1) WO2000063316A1 (en)
ZA (1) ZA200007702B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8407143B2 (en) * 2002-03-27 2013-03-26 The Western Union Company International negotiable instrument payment
JP5786218B2 (en) * 2012-03-26 2015-09-30 樫原 宏 Synthesis and utilization of new ferromagnetic organic ferrofluids
CN105565454A (en) * 2015-12-31 2016-05-11 浙江大川新材料股份有限公司 Preparation method of inorganic/organic flocculating agent compounded water purifying agent

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3642619A (en) * 1970-08-31 1972-02-15 Calgon Corp Conditioning sewage waste sludges for dewatering
US3655552A (en) * 1971-02-16 1972-04-11 Calgon Corp Method for removing phosphate from waste water
US4026794A (en) * 1976-08-30 1977-05-31 Nalco Chemical Company Process for resolving oil-in-water emulsions by the use of a cationic polymer and the water soluble salt of an amphoteric metal
US4067806A (en) * 1976-09-16 1978-01-10 Nalco Chemical Company Formulation and application of compositions for the detackification of paint spray booth wastes
US4450092A (en) * 1982-06-11 1984-05-22 Nalco Chemical Company Reducing turbidity in turbid waters
US5035808A (en) * 1988-06-15 1991-07-30 Calgon Corporation Flocculation of suspended solids from aqueous solutions

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NO20006490D0 (en) 2000-12-19
EP1109874A1 (en) 2001-06-27
CA2335715A1 (en) 2000-10-26
JP2003508548A (en) 2003-03-04
EP1109874A4 (en) 2001-10-31
ZA200007702B (en) 2001-06-14
WO2000063316A1 (en) 2000-10-26
KR20010072626A (en) 2001-07-31
NO20006490L (en) 2001-02-05
AR023538A1 (en) 2002-09-04
BR0006074A (en) 2001-03-20
CN1302320A (en) 2001-07-04

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