CA2241617A1 - Utility of water-soluble polymers having pendant derivatized amide functionalities for scale control - Google Patents
Utility of water-soluble polymers having pendant derivatized amide functionalities for scale control Download PDFInfo
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- CA2241617A1 CA2241617A1 CA002241617A CA2241617A CA2241617A1 CA 2241617 A1 CA2241617 A1 CA 2241617A1 CA 002241617 A CA002241617 A CA 002241617A CA 2241617 A CA2241617 A CA 2241617A CA 2241617 A1 CA2241617 A1 CA 2241617A1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
- C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
- C08F20/52—Amides or imides
- C08F20/54—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
- C08F20/58—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide containing oxygen in addition to the carbonamido oxygen, e.g. N-methylolacrylamide, N-acryloylmorpholine
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
- C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
- C02F5/10—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
- C02F5/12—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances containing nitrogen
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
- C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
- C02F5/10—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
- C02F5/12—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances containing nitrogen
- C02F5/125—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances containing nitrogen combined with inorganic substances
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
- C04B35/632—Organic additives
- C04B35/634—Polymers
- C04B35/63404—Polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C04B35/6344—Copolymers containing at least three different monomers
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
- C04B35/632—Organic additives
- C04B35/634—Polymers
- C04B35/63404—Polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C04B35/63444—Nitrogen-containing polymers, e.g. polyacrylamides, polyacrylonitriles, polyvinylpyrrolidone [PVP], polyethylenimine [PEI]
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/08—Corrosion inhibition
Abstract
Methods for preventing corrosion and scale deposition in aqueous media are disclosed. The methods utilize water-soluble polymers having pendant derivatized amide functionalities for scale inhibition.
Description
. CA 02241617 1998-06-26 The present application is a continuation-in-part of Serial No. 08/79~.610~ filed Januar~ 31~ 1997 by Christopher P. Howland et al., entitled " Preparation and Utility of Water-Soluble Polymers Having Pendant Derivatized Amide, Ester or Ether Functionalities as Ceramics Dispersants and Binders", the disclosure of which is 5 incorporated herein by reference.
Field of the Invention Methods for preventing corrosion and scale deposition in aqueous media are disclosed. The methods utilize water-soluble polymers having pendant derivatized amide functionalities for scale inhibition.
Back~round of the Invention The utilization of water which contains certain inorganic impurities and the production and processing of crude oil water mixtures containing such impurities~ is pla_ued by the precipitation of these impurities with subsequent scale formation. In the case of water which contains these contaminants the harmful effects of scale formation 1 ~ are oenerally confined to the reduction of the capacitv or bore of receptacles and conduits cmplo! ed to store and conve! the contaminated water. In the case of conduits, the impedance of flov~ is an obvious consequence. However a number of equally consequential problems are realized in specific utilizations of contaminated water. For c~;ample. scale formed upon the surfaces of storage vessels and conveying lines for '0 process water may breal; loose and these large masses of deposit are entrained in and conve! ed by the process water to damage and clog equipment through which the water is passed. e.g.. tubes. ~alves. filters and screens. In addition. these crystalline deposits may appear in. and detract from. the final product which is derived from the process. e.g, paper formed from an aqueous suspension of pulp. Furthermore~ when the contaminated water is involved in a heat exchange process~ as either the "hot" or ''cold" medium, scale will be formed upon the heat exchange surfaces which are contacted by the water. Such scale formation forms an insulating or thermal opacifying barrier which impairs heat transfer efficiency as well as impeding flow through the system.
While calcium sulfate and calcium carbonate are primary contributors to scale formation. other salts of alkaline-earth metals and the aluminum silicates are also offenders. e.g.. magnesium carbonate. barium sulfate~ the aluminum silicates provided by silts of the bentonitic, illitic. }~aolinitic. etc., types.
Most industrial waters contain all;aline earth metal cations, such as calcium~
barium. maonesium. etc. and several anions such as bicarbonate, carbonate, sulfate.
o~;alate. phosphate. silicate, fluoride. etc. When combinations of these anions and cations arc present in concentrations which e~;ceed the solubility of their reaction products, pr~cipitates form until these product solubility concentrations are no longer exceeded.
or e~;ample. w hen the concentrations of calcium ion and carbonate ion e:;ceed the soluhilit\ of tile calcium carbonate reaction products. a solid phase of calcium carbonate will form Calcium carbonate is the most common form of scale.
Solubility product concentrations are e~;ceeded for various reasons, such as partial c~ aporation of the water phase. chan~e in pH. pressure or temperature~ and the '() inlroduction of additional ions which form insoluble compounds with the ions already prcsent in the solution As these reaction products precipitate on surfaces of the water carrying system, the! form scale or deposits. This accumulation prevents effective heat transfer~ interferes with fluid flow~ facilitates corrosive processes and harbors bacteria. This scale is an expensive problem in many industrial water systems causing delays and shutdowns for cleaning and removal.
Scale deposits are generated and extended principally by means of crystal growth;
5 and various approaches to reducing scale development have accordingly included inhibition of crystal growth. modification of crystal growth and dispersion of the scale-forrnin~ minerals.
Many other industrial waters~ while not being scale forming, tend to be corrosive.
Such waters. when in contact with a variety of metal surfaces such as ferrous metals, 10 aluminum. copper and its allo,vs. tend to corrode one or more of such metals or alloys. A
v ariety of compounds have been su~gested to alleviate these problems. Such materials are lou molecular weight polyacr,vlic acid polymers. Corrosive waters of this type are usually acidic in pH and are commonl~ found in closed recirculating systems.
Numerous compounds have been added to these industrial waters in an attempt to I S prevent or reduce scale and corrosion. One such class of materials are the well known oroanophosphonates ~ hich are illustrated by the compounds hydroxyethylidene diphosphonic acid (HEDP) and phosphonobutane tricarboxylic acid (PBTC). Another oroup of active scale and corrosion inhibitors are the monosodium phosphinicobis (succinic acids) which are described in U. S. Pat. No. 4.088~678.
'() Polymeric treatments have heen disclosed in U.S. Patent Nos. 4,680~339;
4.7~1.419: 4.885.,45 and 5.084.5~0. Utility for the treatments has been disclosed to be as dispersants in water treatment. scale inhibitors in industrial and natural waters, tlocculants. coagulants and thicl;eners.
Moreover, methods of controlling calcium oxalate scale with an effective amount of a water-soluble (meth)acrylic acid/allyl ether copolymer have been disclosed in U.S.
Patent No. 4,872,995. A method for controlling silica/silicate deposition, including calcium and magnesium silicate by addition of a phosphonate and a water-soluble terpolymer of an unsaturated carboxylic acid monomer, an unsaturated sulfonic compound and an unsaturated polyalkylene oxide is disclosed in U.S. Patent No.
4.933.090. Acrylate/acrylamide copolymers have been disclosed as useful for the inhibition of gypsum scale in flue gas desulfurization processes in U.S. Patent No.
4.8 1 8.506.
A method of inhibiting phosphonate scale formation on and corrosion of iron containing solid surfaces in contact with industrial waters with a water-soluble zinc stabilizing polvmer is disclosed in U.S. Patent No. ~.049,310. A method for preventing condensate corrosion in boilers comprising treating the condensate with a water-soluble pol! meric composition comprising a an acrylic acid polymer containin~ acrylic acid roups in the form of amides of a ~vater-insoluble aliphatic primary or secondary amine is disclosed in U.S. Patent No. 4.999.161. However. there is still a need for polymeric treatnlents w hich provide an increased efficienc! for corrosion and scale control.
.'iummar} of the Invention Methods for preventinn corrosion and scale deposition in aqueous media are '() disclosed. The methods utilize water-soluble polvmers having pendant derivatized amide functionalities for scale inhibition.
I)escription of the Invention The invention is a method for preventing scale formation on metal surfaces in contact with scale-forming Industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a ~vater-soluble polymer having distributed repeating mer units represented by the formula f_ CH
C =O
NRI
(I~HR-CHR3 Hetl~CHR2CHR3Het~~4 ~herein Rl is selected from the group consisting of hydrogen, and Cl - C3 alkyl; p and q are integers from I - 10; R- and R- are selected from the group consisting of hvdrogen alld Cl - C, al};yl: Hetl and Het~ selected from the group consisting of oxygen and 1(~ nitrogen: R~ is selected from the group consisting of hydrogen. and Cl - C,(, alkyl; R- and R'' are selected from the roup consisting of hvdrogen. carboxylate~ C~ - C3 all;yl~ and a cycloal~yl group of 3 to 6 carbon atoms formed by the linkage of R5 and R6 as a rin~.
For any embodiment of this invention~ the industrial water may be cooling water.
Furtllermore. the scale may selected from the group consisting of calcium phosphate, zinc I ~ phosphate. iron (hydr)oxide. aluminum hydroxide~ calcium sulfate, barium sulfate, clay, silt.-ma~mesium phosphate. magnesium carbonate and calcium carbonate Any embodiment of the polymers of this invention are also active against scale caused by c~lcium and magnesium salts of HEDP and calcium and magnesium salts of PBTC.
Furthermore, the cooling water may contain a biocide, corrosion inhibitors. or other scale inhibitors. The industrial water may be industrial process water selected from the group consisting of mining process water, pulp and paper process water and oilfield process water.
The invention is also a method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said uater uith an effective scale-inhibiting amount of a uater-soluble polvmer having:
A) a mer unit of the formula R~ R6 f _ CH
C =O
NRI
(CHR-CHR- Hetl~CHR~CHR3Het~~R4 ~-hcrcin Rl is selected from the group consisting of hydrogen, and C~ - C3 alkyl; p and q ~r. inteoers from 1 - 10; R- and R are selected from the group consisting of hydrogen I ~ alld C'l - C~ all;yl: Hetl and Het~ selected from the group consisting of oxygen and nilro~en: R~ is selected from the group consisting of hydrogen, and Cl - C7n alkyl; R5 and R'' are selected from the group consistino of hydrogen. carboxylate, Cl - C3 alkyl~ and a c~ cloall;yl ~roup of, to 6 carbon atoms formed by the linkage of R- and R6 as a ring;
and B) a mer unit selected from the group consisting of acrylic acid, methacrylic acid.
acrylamide. methacrylamide. maleic arlhydride. itaconic acid, vinyl sulfonic acid, styrene sulfonate, N-tertbutylacrylamide, butoxymethylacrylamide, N,N-dimethylacrylamide.
sodium acr lamidomethvl propane sulfonic acid, vinyl alcohol, vinyl acetate. N-vinvl S pyrrolidone, maleic acid, and combinations thereof. For any of structures I-III, the salts of the comonomers will also have utility.
A specific polymer applicable is identified as one wherein p=l; q=l; Rl, R2, R3.
R~. R-. and R6 are hydrogen: and Het~ and Het~ are oxygen in formula I of step A; and the mer units of step B are acrylic acid arld acrylamide for the water-soluble polymer.
Another useful polymer is one wherein p=l; q=l; Rl, R2, R3, R4, R5, and R6 are hydrogen: and Het~ and Het~ are oxygen in forrnula I of step A; and the mer units of step B are acrylic acid for the water-soluble polvmer. Yet another useful polymer is one wllerein p=l: q=l; R~. R-. R-'. R~. R . and R6 are hydrogen; and Het~ and Het~ are ~X! ~en in formula I of step A: and the mer units of step B are maleic acid and acrvlic I ~ acid for the ~ater-soluble polymer Another useful polymer is one wherein p=l, q=l, t~etl is nitrogen. Het~ is oxy~en and Rl. R-. R;, R~. R- and R6 are hydrogen in formula I
of step A: and the mer units of step B are acrylic acid and acrylamide for the water-sc)luble polymer Moreover. ~herein p=l. q=l. Heti is nitrogen. Het2 is oxygen and Rl, R-. R-'. R~. R and R~' are hvdrogen in formula I of step A: and the mer units of step B are '() acr! lic acid is also a useful ~ater-soluble polvmer. Wherein p=l, q=l, Hetl is nitrogen, Het~ is oxy~en and Rl. R-~ R . R~ R and Rt' are hydrogen in formula I of step A; and the mer units of step B are maleic acid and acrylic acid~ is another applicable water-soluble pol!~mer.
The invention is also a method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polvmer having distributed repeating mer units of the formula F--CH
1=~
NH
H ;C CHCH7 ( OCHR CH7 )p OR-wherein Rl is selected from the group consisting of hydrogen and C~ - C3 ali;yl oroups. p is an integer from 0-50: R- is selected from the group consisting of llvdro~en and C l-C~(, ali~yi groups: R- and Rh are selected from the group consisting of hvdrogen, 1(1 carho~;! lates Cl-C3 ali;yl groups. and a cvcloall~vl group of 3 to 6 carbon atoms formed h! Ihe lini;aoe of R- and Rh as a ring. v ith the proviso that when p is 0. R- is not h! drogen.
The invention is also a metllod for preventing scale formation on metal surfaces in contact ~ith scale-forminn industrial water within an industrial system which comprises I ~ the step of treating said water w ith an effective scale-inhibiting amount of a water-soluble pol! mer having: A) a mer unit of thc formula CH
1=0 NH
H3C CHCH, (OCHRICH~ )p OR-wherein Rl is selected from the group consisting of hydrogen and Cl - C3 alkvl groups p is an inte_er from 0-50: R- is seleeted from the group eonsisting of hydrogen and C,-C20 5 all;yl groups: R- and R6 are seleeted from the group eonsisting of hydrogen. earboxylates~
C~-C; all;yl groups. and a eycloall;yl group of 3 to 6 carbon atoms formed by the linl;age of R and R6 as a ring~ w ith the proviso that when p=07 R2 is not hydrogen; and B) a mer unit selected from the group consisting of acrylic acid~ methacrylic acid~ acrylamide~
methacr! lamide. maleie anhvdride~ itaeonie acid~ vinyl sulfonic acid~ styrene sulfonate~
I () I\ -tertbutylacrylamide. butoxvmeth! lacr- lamide. N.N-dimethylacrylamide~ sodium acrylamidomethyl propane sulfonic acid. vinyl alcohoh vinyl acetate~ N-vinyl py rrolidone. maleic acid. and combinations thereof.
For the practice of this invention. p may be an integer of from 10 to 25~ Rl may he selected from the group consistin~ of hydrogen and methyl groups~ R may be a I ~ meth! l group. R- may be hydro~en and R" may be hydrogen and the mer units of step B
ma! he acrylic acid. Additionally. p may be an integer of from 10 to 25. Rl may be selected from the group consistin ~ of hydrogren and methyl groups, R2 may be a methyl ~roup. R- and R6 may be hvdrogen and the mer units of step B may be acrylic acid and acrylamide. Furthermore~ another useful polymer is one wherein p is an integer of from 10 to 25, R~ is selected from the group consisting of hydrogen and methyl groups. R- is a methyl group. Rs is hydrogen and R6 is hydrogen and the mer units of step B are maleic S acid and acrvlic acid.
Another aspect of this invention is a method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial svstem which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polymer having distributed repeating mer units of the formula _f _ CH
l =O
NR
(CH,)r I (i R~
lll ~herein Rl is selected from the group consisting of hydrogen. and C~ - C3 alkyl; p is an inteoer from 1 - 10: R~ is selected from the group consisting of Cl-C~, alkyl groups. C~-C6 15 alk! l ether g roups and morpholino groups; R and R6 are selected from the group c~nsisting of hydrogen. carboxylate~ Cl - C3 alkyL and a cycloalkyl group of I to 6 carbon atoms formed by the linkage of R5 and R6 as a ring.
Yet another aspect of this invention is a method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polymer having: A) a mer unit of the formula Rs R6 C CH
C = O
NRI
I
(CH,)p erein Rl is selected from the group consisting of hydrogen, and C~ - C, alkyl; p is an hlteger from I - 10; R~ is selected t'rom the ~roup consisting of Cl-C6 alkyl groups~ Cl-C6 aik! l ether groups and morpholino ~roups: R- and R6 are selected from the group consisting of hydrogen~ carbo~;ylate. Cl -C3 alkvk and a cycloalkyl group of I to 6 carbon atoms formed by the linkaoe ot R- and R6 as a ring; and B) a mer unit selected I ~ frc rn the group consistino of acrylic acid~ methacrylic acid, acrylamide~ methacrylamide, maleic anhydride~ itaconic acid~ vin~l sulfonic acid, styrene sulfonate~ N-t~itbutvlacrvlarnide. butoxymethylacrylamide. N~N-dimethylacrylamide. sodium acrvlamidomethyl propane sulfonic acid, vinyl alcohol? vinyl acetate. N-vinyl pyrrolidone, maleic acid, and combinations thereof.
For the practice of the method described above, a useful polymer is one wherein 5 Rl. R- and R6 are hydro~en, p is ~ and R~ is a morpholino group in forrnula III of step A
and the mer units of step B are acrvlic acid and acrylamide. Another example of a useful polymer is one wherein Rl. R and R6 are hydrogen, p is 2 and R4 is a morpholino group in formula III of step A and the mer units of step B are acrylic acid for the water-soluble polymer. Yet another useful polymer is one wherein Rl, R5 and R6 are hydrogen. p is 2 10 and R' is a morpholino group in formula III of step A and the mer units of step B are acrylamide for the ~ater-soluble polymer. Furthermore, wherein Rl, R- and R6 are hydrogen. p is 3 and R4 is a methoxy group in formula III of step A; and the mer units of slep B are acrvlic acid and acrylamide: wherein Rl, R5 and R6 are hydrogen. p is 3 and R4 is a metho~;! group in formula III of step A; and the mer units of step B are acrylic acid:
herein Rl. R- and R~i are hydrooen p is 3 and R4 is a methoxy group in formula III of slep A: and the mer units of step B are maleic acid and acrylic acid are all examples of a~ licahle ~ater-soluble polymers The polymers described herein for the practice of this invention may range in nlol~cular ~eight from about ROOO to about 1.000.000. Preferably, the molecular weight ill he from about 5.000 to about 100.000 For the polymers defined herein. the mer unil~ defmed by formulas 1-111 ~A ill ran~e from 1 to 75% of the total number of mer units in lhe polymer Preferably the mer units defined as formulas l-III will be 5-50% of the lo~al number of mer units in the polvmer The polymer classes described herein contain amide mer units which are functionalized with pendant groups. These pendant groups confer favorable properties to the polymer for use as scale Inhibitors. The polymers may be produced by polymerization using specific monomers, such as might be produced by the copolvmerization of acrylic acid with an N-methoxy propyl acrylamide, methoxyethoxy acrylate. methoxyethoxv maleate or N-methoxypropyl acrylate comonomer. The polvmer so produced would contain a hydrophilic backbone with pendant groups.
Alternatively, pendant groups could be introduced into the polymer after polvmerization. For example, polyacrylic acid could be amidated with an 10 ethoxvlated/propoxylated amine, such as those available from Texaco under the trade name Jeffamine series. to produce a polvmer with a hydrophilic backbone and ethyleneoxy/propyleneoxy pendant groups. During the amidation process. cyclic imide structures might form between two adjacent carboxylate or carboxamide units on the polymer bac,!ibone. These imide structures are not expected to have an adverse effect on I ~ the performance of the polymers.
Typical metal surfaces in coolin~c water systems which may be subjected to ccorrosion or scale deposition are made of stainless steel. mild steel and copper alloys such as brass amon~ others.
The polymers may be effective a~,~ainst other types of scale including magnesium '() silicate. calcium sulfate. barium sulfate and calcium oxalate. The polymers are also effective in extremely hard water.
The polvmers may be utilized in conjunction with other treatments, for example biocides. other ferrous metal corrosion inhibitors, yellow metal corrosion inhibitors. scale inhibitors. dispersants. and additives. Such a combination may exert a synergistic effect in terms of corrosion inhibitors, scale inhibition. dispersancy and bacterium control.
Examples of biocides which can be used in combination with the pol!,~mers include: stabilized bleach~ chlorine and hypobromite, bromine (oxidizlng biocides). Also~
5 non-oxidizing biocides such as glutaraldehyde, isothiazolones (mixtures of 5-chloro-~-methyl-4-isothiazolin-3-one and ~-methyl-4-isothiazolin-3-one), sulfamic acid-stabilized bleach and sulfamic acid-stabilized bromine are applicable.
Additionall~, the polymers mav be utilized in conjunction with other corrosion and scale inhibitors Thus~ the polymers may be effective in combination with other 10 inhibitors such as hydroxyeth~,ylidene-l~l-diphosphonic acid (HEDP), ~-phosphonobutane- I ~.4-tricarboxylic acid (PBTC)~ ~-hydroxyethylimine bis(methylene phosphonic acid) N-oxide (EBO)~ methylene diphosphonic acid (MDP), he~;ameth! lenediamine-N~N~N~N'-tetra(methylene phosphonic acid), amino and Iris(methylene phosphonic acid)~ phosphorus-containing inorganic chemicals such as I ~ orthopllosph3tes~ pyrophosphates~ polyphosphates: hydroxvcarboxylic acids and their s, lls such as oluconic acids: ~lucaric acid: Zn~ ~ Ce~, MoO62~, W O4--~ and nitrites.
The polymers may also be effecti~ely utilized in conjunction with other p ol! meric treating agents. for e~;ample anionic polymers of under ~00.000 MW Such polymers include acrylic. methacrylic or maleic acid containing homo-, co- or ter-~() polymers.
Examples of yello~ metal corrosion inhibitors that can be used in combination~ilh the polymers include benzotriazole. tolyltriazole, mercaptobenzothiazole and other azole compounds Examples of other scale inhibitors that can be used in conjunction with the polymers include polvacrylates~ polymethacrylates, copolymers of acrylic acid and methacrylate~ copolymers of acrylic acid and acrylamide, poly(maleic acid) copolymers of acrylic acid and maleic acid. polyesters~ polyaspartic acid, fimctionalized polyaspartic 5 acid, terpolymers of acrylic acid. and acrylamide/sulfomethylated acrylamide copolvmers. HEDP (l-hydroxyethylidene~ diphosphonic acid), PBTC (2-phosphonobutane~ .4-tricarboxylic acid), and AMP (amino tri(methylene phosphonic acid).
To treat a cooling water system, the compounds may be added to the cooling 10 to- er basin or at any other location wherein good mixing can be achieved in a short time.
The term system as utilized herein is defined as any industrial process which utilizes water. The system could contain primarily aqueous fluids, or primarily non-aqueous fluids. but also contain water. Such systems are found in industrial processes ullich utilize boilers or cooling uater towers. For example. the food processing industry 15 is an industry u hich requires such a svstem.
The polymers may be added to the scale-forming or corrosive industrial process uater in an amount of from about 0.5 ppm to about 500 ppm. Preferably, the polymers ma! be added in an amount of from about 2 ppm to about 100 ppm. Most preferably, the pol~ mers ma~ be added in an amount of from about 5 ppm to about 50 ppm.
'() The following examples are presented to describe preferred embodiments and utilities of the invention and are not meant to limit the invention unless otherwise stated in the claims appended hereto.
E~ample 1 The synthesis of an ammonium acrylate/ N-(hydroxyethoxy)ethyl acrylamide copolymer was effected with the following reactants in the following arnounts:
Reactant Amount (~) S Poly(AA), 25.6 weight % in water 100.00 Aminoethoxyethanol 1 1.92 Ammonium Hydroxide, 29 weight % 2.51 To prepare the polymer, poly(AA) (25.6 weight percent poly(acrylic acid) solution. pH = 3.8, 16,000 MW) was placed in a beaker, which was cooled using an ice bath. Aminoethoxyethanol (available from Hllnt~m~n Petrochemical Co., in Houston, Texas) was added dropwise into the poly(acrylic acid)/water solution with vigorous stirring. Afterwards, the solution was stirred for another 15 minutes. Aqueous caustic was added to adjust the pH to about S. Next, the reaction mixture was transferred into a I ~ ~00 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then was assembled and purged w ith nitrogen for approximately 60 minutes. The Parr reactor was ~hen slo~ Iy heated to 1 60~C (or less. as the case may be) and held at that temperature for 8 hours (or more. as the case may be). Afterwards. the reactor was cooled to room temperature and the pressure released. The product was then transferred to storage.
'C NMR confirmed product formation. The content of N-(hydroxyethoxy)ethyl acrylamide ~ as ~ I mole %. based on the total moles of mer units on the polymer, which represents both secondary amide and imide mer units. The polymer's molecular weight S ~.000.
. CA 02241617 1998-06-26 Example 2 The s,vnthesis of an ammonium acrylate/acrylamide/N-(hydroxvethoxy)ethyl acrylamide terpolvmer was effected in the following manner with the reactants in the amounts listed belou:
Reactant Amount (~
Poly(NH4AAJAcAm). 50/50 mol %
solution polymer. 38.~ weight % 300.00 Aminoethoxyethanol 1 14.00 To prepare the polymer. Poly(NH4AA/AcAm) (50/50 mol % ammonium acrylate/acrvlamide copolymer, 38.~ weight percent, pH = 5.5, 33,000 MW) was placed in a beaker. which was cooled using an ice bath. Aminoethoxyethanol (available from Huntsman Petrochemical Co., in Houston, Texas) was added dropwise into the above I 5 u ater solution with vigorous stirring (pH = 10.1). Afterwards, the solution u as stirred for another I 5 minutes. Next~ the reaction mixture was transferred into a 600 mL Parr reactor ~ ith a pressure rating of at least 800 psi. The reactor then was assembled and puroed uith nitrogen for approximately 60 minutes. The Parr reactor was then slowly heated to I 38~C and held at that temperature for 14 hours. Afterwards. the reactor was '() eooled to room temperature and the pressure released. The product was then transferred to storalle.
I-'C NMR confirmed product formation. The content of N-(hydroxyethoxy)ethyl acr! lamide uas 33.3 mole %. based on the total moles of mer units on the polymer. The pc l!:mer had a molecular wei-~ht of 35.000. and a mole ratio of N-(hydroxyethoxy)ethyl acrylamide/acrylic acid/acrvlamide of about 331411~6.
Example 3 The synthesis of a sodium acrylate/acrylamide/N-(hydroxyethoxy)ethyl acrylamide terpolymer was effected in the following manner with the reactants in the amounts listed belou: , Reactant Amount (g) Poly(NaAA/AcAm), 50/50 mol %
solution pol,vmer. 32.0 weight % 100.00 Aminoethoxyethanol 32.00 Sulfuric Acid (95~/O) 11.5 To prepare the polymer. Poly(NaAA/AcAm) (50/50 mol % sodium acr late/acr,vlamide copolymer. 3~.0 weight %, pH = 5.2, 11,000 MW) was placed in a beai~er. which was cooled using an ice bath. Aminoethoxyethanol (available from 15 Huntsman Petrochemical Co.~ in Houston, Texas) was added dropwise into the above water solution v~ith vigorous stirring.. Afterwards, the solution was stirred for another 15 minutes. Sulfuric acid was added to adjust the pH to about 5.6. Next. the reaction mixture was transferred into a 300 mL Parr reactor with a pressure rating of at least 800 p .si. Tl-e reactor then was assembled and purged with nitrogen for approximately 60 '~) n~ utes. The Parr reactor was then slowly heated to 138~C and held at that temperature lor 1~ hours. Afterwards. the reactor was cooled to room temperature and the pressure rcleased. The product was then transferred to storage.
I 'C NMR conflrmed product formation. The content of N-(hydroxyethoxy)ethyl acr! lamide was 33 mole %~ based on the total moles of mer units on the polymer. The ~5 moie ratio ~as about 4~ 13, of'acrvlic acid/acrylamide(including 3% imide mer units)/N-(hydroxyethoxy)ethyl acrylamide (including imide mer units). The product polymer had a molecular wei~ht of 12~000.
Example 4 The synthesis of a sodium acrylate/acrylamide/N -Methoxypropyl acrvlamide 5 terpolymer was effected in the following manner with the reactants in the amounts listed below:
Reactant Amount(~y) Poly(NaAA/AcAm), 50/50 mol %
solution polymer, 32.0 weight % 100.00 Methoxypropylamine 23.32 Sulfuric Acid (95%) 11.23 To prepare the polymer. Poly(NaAAJAcAm) (50/50 mol%, 32.0 weight %. pH =
5.~. 11.000 MW) was placed in a beaker. which was cooled using an ice bath.
15 Methoxypropylamine (available from Aldrich Chem. Co.. in Milwaukee, WI) was added dropwise into the above water solution with vi~orous stirring. Afterwards, the solution was stirred for another 15 minutes. Sulfuric acid was added to adjust the pH to about 5.6.
Ne:;t. the reaction mixture was transferred into a 300 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then was assembled and purged with nitrogen for '() approximately 60 minutes. The Parr reactor was then slowly heated to 13~~C and held at that temperature for 1~ hours. Afterwards. the reactor was cooled to room temperature and the pressure released. The product was then transferred to storage.
l-'C NMR confirmed product forrnation. The content of N-methoxypropyl acrylamide was 34.2 mole %. based on the total moles of mer units on the polymer. The '5 mole ratio of the product was about 41/17/34 which represents acrylic acid/acrylamide (including 6% imide mer units)/methoxypropyl acrylamide (including imide mer units).
The product's molecular weight was 11,000.
Example 5 The synthesis of a sodium acrylate/acrylamide/N-hydroxy(ethylarnino)ethyl 5 acrylamide terpolymer was effected in the following manner with the reactants in the amounts listed below:
Reactant ~mount(~) Poly(NaAA/AcAm)~ 50/50 mol %
solution polymer. 24.0 weight % 80.00 (Aminoethylamino)ethanol 19.02 Sulfuric Acid (95%) 12.23 To prepare the polvmer, Poly(NaAA/AcAm) (50/50 mol%, 24.0 weight %~ pH =
,.~. 15.000 MW) was placed in a beaker. which was cooled using an ice bath.
l ~ ( Aminoeth- lamino)ethanol (available from Aldrich Chem. Co., in Milwaukee. WI) was added dropwise into the above water solution with vigorous stirring. Afterwards. the solution uas stirred for another 15 minutes. Sulfuric acid was added to adjust the pH to ahout ~.6. Ne~:t. the reaction mixture uas transferred into a 300 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then was assembled and purged with '() ni~rogen for approximately 60 minutes. The Parr reactor was then slowly heated to l .~~C and held at that temperature for 14 hours. Afterwards, the reactor was cooled to room temperature and the pressure released. The product was then transferred to storage.
'~'C NMR confirmed product formation. The content of N-hydroxy(ethylamino) eth! l acrylamide w.as 46 mole %. based on the total moles of mer units on the polymer, representing both secondary amide and imide mer units. The mole ratio of the product was about 46151/3 N-hydroxy(ethylamino)ethyl acrylamide/acrylic acid/acrylamide. The product polymer s molecular weight was 15,000.
Example 6 The synthesis of an acrylic acid/acrylarnide/ N-(hydroxyethoxy)ethyl acrylarnide 5 terpolymer was effected in the following manner with the reactants in the arnounts listed belou:
Reactant Amount(~
Poly(AcAm)~ 50 weight % 50.00 Aminoethoxyethanol 12.9 Deionized water 50.0 Sulfuric Acid (95%) 6.1 To prepare the polymer. Poly(AcAm) (50wt%, available from Aldrich Chemical Co.. 10.000 MW) was placed in a beal;er~ which was cooled using an ice bath.
15 Aminoethoxyethanol (available from Huntsman Petrochemical Co., in Houston~ Texas) was added dropwise into the above water solution with vigorous stirring. Afterwards~ the solution was stirred for another 15 minutes. Sulfuric acid was added to adjust the pH to about 5.6. Next. the reaction mixture was transferred into a 300 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then was assembled and purged with '() nitrogen for approximately 60 minutes. The Parr reactor was then slowly heated to 1 ' 8~C and held at that temperature for 14 hr. ARerwards. the reactor was cooled to room temperature and the pressure released. The product was then transferred to storage.
'~'C NMR conflrmed product formation. The content of N-(hydroxyethoxy) ethyl . CA 02241617 1998-06-26 acrylarnide was 19.6 mole %. based on the total moles of mer units on the polymer. The product's mole ratio was about 32/44/20 which represents acrylic acid/acrylamide/N-(hydroxyethoxy) ethyl acrylarnide.
Example 7 The synthesis of a ammonium acrylate/N-Methoxypropyl acrylarnide copolymer was effected in the following manner with the reactants in the arnounts listed below:
Reactant Amount(g) Poly(AA).~5.6 wei~ht % in water 100.00 Methxypropylarnine 1 0.09 Ammonium Hvdroxide. '9 wei~ht % in water 0.86 To prepare the polymer. Polv(AA)(32.0 wt%, pH = 3.3, 15,000 MW) was placed in a beal;er. which was cooled using an ice bath. Methoxypropylamine (available from I 0 Aldrich Chem. Co.. in Mil~au~;ee. Wl) was added dropwise into the above water solution ~ ith v igorous stirrin_ Afterwards. the solution was stirred for another 15 minutes.
Aqueous caustic ~as added to adjust the pH to about 5. Next, the reaction mixture was Iransferred into a 300 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then ~vas assembled and puroed ~ ith nitrogen for approximately 60 minutes. The I ~ Parr reactor ~as then slo~ heated to 1 60~C and held at that temperature for 8 hours.
After~vards. the reactor ~as cooled to room temperature and the pressure released. The product ~as then transferred to storage.
I-'C NMR confrmed product formation. The content N-methoxypropyl acrylamide ~as 22.4 mole %. based on the total moles of mer units on the polymer, which represents both secondary amide and imide mer units. The polymer's molecular wei_ht was 15~000.
Example 8 The synthesis of an acr,vlic acid/acrylamide/N-Methoxyprop,vl acrylamide 5 terpolymer was effected in the following marmer with the reactarlts in the amounts listed below:
Reactant Amount(g) Poly(AcAm). 50 wei~ht % in water 100.00 Methoxypropvlamine 1 0.99 Sulfuric Acid (95%) 6.75 Sodium Hvdroxide (50 wei~ht %) 1.8 To prepare the polymer, Poly(AcAm) (50.0 wt%, Available from Aldrich Chemical Co.~ 10~000 MW) was placed in a bea~;er, which was cooled using an ice bath.
I () ~lethoxypropylamine (available from Aldrich Chemical Co.. in Milwaul;ee. Wl) was added dropwise into the above water solution with vigorous stirring. ARerwards. the .solution was stirred for another 15 minutes. Aqueous caustic was added to adjust the pH
~o about 5.6. Next. the reaction mixture was transferred into a 300 mL Parr reactor ~vith a prcssure ratin~ of at least 800 psi. The reactor then was assembled and pur~ed with I 5 nitrogen for approximately 60 minutes. The Parr reactor was then slowly heated to 138~
C and held at that temperature for 12 hours. ARerwards. the reactor was cooled to room tcmperature and the pressure released. The product was then transferred to storage.
~ I-'C NMR confirmed product forrnation. The content N-methoxypropyl acrylamide was 20.~ mole %. based on the total moles of mer units on the polymer.
which represents both secondary amide and imide mer units. The product's mole ratio was about 33.8/45/20 which represents acrylic acid/acrylarnide/N-(methox~propyl) acrylarnide. The polymer's molecular weight was 18~500.
Example 9 S The synthesis of an acr~lic acidlacrylarnide/N-Methoxyethyl acrylarnide terpolymer was effected in the following manner with the reactants in the following manner with the reactants in the amounts listed below:
Reactant Amount(g) Poly(AA/AcAm)~ 31.4 wei~ht % in water100 Methoxyethylamine 1 9.65 Sulfuric Acid (95%) 10.20 To prepare the polvmer. Poly(A/AcAm) (31.4 wt%, 11,000 MW) was placed in a 1 () beal;er. which was cooled usinP an ice bath. Methoxyethylarnine (available from Aldrich C hemical Co.. in Milwaul;ee. Wl) was added dropwise into the above water solution with ~ ioorous stirrin~. Afterwards. the solution was stirred for another 15 minutes. The pH of the reactioll mixture was measured usin~ water-wet pH strips. Aqueous caustic was added to ad just the pH to about 5.6. ~le~;t. the reaction mixture was transferred into a 300 I 5 nll p arr reactor with a pressure ratin~ of at least 800 psi. The reactor then was assembled all(l pur~ed w ith nitro~en for appro~;imatel)~ 60 minutes. The Parr reactor was then slowl! heated to 138~C and held at that temperature for 12 hours. Afterwards. the reactor ~as cooled to room temperature and the pressure released. The product was then ransfcrred to stora~e.
I;C NMR confirmed product formation. The content N-methoxypropyl acrylamide was 40.8 mole %. based on the total moles of mer units on the polymer~
which represents both secondary amide and imide mer urlits. The product's mole ratio was about 40/14/41 which represents acrylic acid/acrylamide/N-(methoxypropyl) 5 acrylarnide. The polymer's molecular weight was 11,000.
Example 10 The s,vnthesis of a sodium acrylate/acrylamide/N-alkoxylated acrylamide copolymer was effected in the following manner with the reactants in the amounts listed below:
Reactant Amount(g) Polv(AA/AcAm), 50/50 mole % 43.8 weight % in water 100 Jeffamine M- 1000 60 Sodium Hydroxide (50 weight %) 11.78 Deionized Water 100 To prepare the polvmer. Poly(A/AcAm) (43.8 wt%~ pH = 4Ø 18.000 MW) was placed in a beal;er. which was cooled using an ice bath. Jeffamine M-1000 (available from Te:;aco Chemical Co. ) was added dropwise into the above water solution with v ioorous stirring. Afterwards. the solution w as stirred for another 15 minutes. Aqueous I ~ caustic was added to adjust the pH to about 6.9. Next, the reaction mixture was ~ransferred into a 300 mL parr reactor with a pressure rating of at least 800 psi. The reactor then was assembled and purged with nitrogen for approximately 60 minutes. The Parr reactor was then slowl~ heated to 1 50~C and held at that temperature for 5 hours.
Afterwards, the reactor was cooled to room temperature and the pressure released. The product was then transferred to storage.
Example 1I
The synthesis of a sodium acrylate/ N-hydroxy(ethylarnino)ethyl acrylamide 5 terpolymer was effected in the following marmer with the reactants in the amounts listed below:
Reactant Amo--nt(~
Poly(AA). 27.0 weight % in ~water 100.00 (Aminoethylamino)ethanol 12.89 Sulfuric Acid (95%) 0.6 To prepare the polymer. Poly(AA) (27.0 weight %, pH = 3.4, 17.000 MW) ~was placed in a beaker. which was cooled using an ice bath. (Aminoethylamino)ethanol (a~ailable from Aldrich Chem. Co.. in Milwaukee, WI) was added dropwise into the I ~ abo~e uater solution with ~~igorous stirring. Afterwards, the solution was stirred for anotller I 5 minutes. Sulfuric acid u as added to adjust the pH to about 5.6. Next. the reaction mixture uas transferred into a 300 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then ~ as assembled and purged with nitrogen for approximately 60 minutes. The Parr reactor uas then slowly heated to 138~C and held at '() that temperature for 14 hours. Afterwards. the reactor was cooled to room temperature and the pressure released. The product uas then transferred to storage.
I C NMR confirmed product formation. The content of N-hydroxy(ethylamino) eth! l acrylamide was about 30 mole %. based on the total moles of mer units on the polymer. representin~~ both secondary amide and imide mer units. The product's mole ratio was approximately 70/30 which represents acrylic acid/N-(hydroxyethylamino) ethyl acrylamide. The product polymer's molecular weight was 32,000.
Example 12 The activity of polymers for calcium phosphate scale inhibition were evaluated in 5 the following manner.
An acidic stock solution ~vas prepared cont~inin~ calcium chloride, magnesium sulfate, and phosphoric acid. Aliquots of this stock solution were transferred to flasks so that on dilution, the final concentration of calcium was 750 or 1500 ppm as CaCO3. Iron or aluminum were added in 750 ppm Ca tests. The appropriate volume of inhibitor was l 0 added to _ive ~0 ppm polymer for the 1500 ppm Ca tests, 25 ppm polymer for the iron tests or 30 ppm polymer for the aluminum tests. Dl water was added, and the flasks were heated to 70~C. in a water bath. Stirring was maintained at ~50 rpm with l" stir bars.
Once the solutions were at temperature~ the pH was adjusted to 8.5. pH was cllecl;ed frequently to maintain 8.5. Filtered samples were taken aRer four hours. Then.
l S l 00 ml of the solution was taken and boiled for l 0 minutes in a covered flask. The volume ~ as brou~ht bacl; to l00 ml with Dl water. and filtered samples were taken again.
Standard colorimetric analvses determined ortho phosphate concentration in the samples.
Percent phosphate is reported as l00*P(filt)/P(unfilt). When no polymer was added~ 4-6~/o ~llterable phosphate ~as obtained.
'() Percent inhibition numbers above 80% indicate exceptional dispersant activity.
Polymers w hich disperse the phosphate in this test are observed to prevent calcium phosphate scale in recirculating cooling water svstems under similar high stress conditions. Numbers less than about 40% indicate poor dispersant activity. Such . CA 02241617 1998-06-26 polymers may or may not work under milder conditions (softer, cooler water)~ but do allow scale to form under high stress conditions. Polymers with intermediate activitv are still good dispersants for low stress conditions. but will lose activity at higher stress.
TABLE I
Calcium Phosphate Dispersancy Test - High Stress Conditions Polymer Percent Inhibition at 20 p ~m Polvmer CaTest Fe Test Al Test A' 37 46 34 C 60 --- ~0 D~ 89 --- ---F~ 82 44 58 G' 70 57 46 K" 26 --- ---I = conventional treatment 1~ sulfonated p(AA/AcAm) 2 = polvmer prepared according to a procedure similar to Example 10; 10/40/50 mole 5 ratio of JeffamineiAA/AcAm~ 60.000 MW
, = pol- mer prepared according to a procedure similar to Example 10; 20/40/40 mole ratio of Jeffamine/AA/AcAm~ 10~000 MW
= pol~mer prepared according to a procedure similar to Example I0; 40/40/20 moleratio of Jeffamine!AA/AcAm~ 20~000 MW
10 5 = pol~ mer prepared according to a procedure similar to Example 3 = pol~ mer prepared according to a procedure similar to Example I
7 = pol~ mer prepared according to the procedure of Example 2; 33141/26 mole ratio of AEE/AA/AcAm g = pol~ mer prepared according to the procedure of Example 4; 34/41/17 mole ratio of 1 5 ~lOPA/AA,AcAm 9 = pol! mer prepared according to the procedure of Example 5: 5114613 mole ratio of AA 'AEAE/AcAm 1 () = pol~ mer prepared according to the procedure of Example 9 1 1 = con~entional treatment 2~ p(AA/AcAm) available from Nalco Chemical Co.
'() ~'aperville. IL
Example 13 The follo~ing dispersancy test procedure was utilized to obtain the results sho~n in Table II. 200 mL of a test solution containing 20 ppm of a polymer dispersant and ~0 ppm of PBTC dissolved in distilled water was prepared. Then the test solution was added 5 to a ~50 mL erlenmeyer flask magnetically stirred at 40~C. Hardness and m-alkalinity are added to the solution over seven minutes to achieve a final solution composition (ppm as Ca COj) of 700 ppm Ca2 350 ppm Mg2, and 700 ppm Co32-. As calcium carbonate precipitation proceeds, the particle monitor responds to the fraction of calcium carbonate particles greater than 0.5 microns in diameter. The more effectively dispersed the l O calcium carbonate particles. the lower the fraction of large particle agglomerates. Better performing test solutions are indicated by (I ) lower particle monitor intensities. and (2) intensity ma~;ima achieved at longer times (60 minute limit).
E:;amples 1 and 7 are the best performing dispersants for preventing calcium c~rbon~te particle ag_lomeration e~idenced by (I) the smallest particle mollitor intensity I ~ and (') requiring longer times to achieve their ma~;imum signal response. Traditional dispcrsants (polyacrylic acid) provide improved dispersancy over the blank. but do not pcrform as ~ell as the e!;amples cited.
TABLE II
Dispersant (20 ppm total actives) Particle Monitor Intensit~ (time) Blank' 100 (12 minutes) Poly(acrylic acid) 57 (45 minutes) L lS (55 minutes) M~ 12 (60 minutes) I = 20 ppm PBTC
2= polymer prepared according to the procedure of Example 1 3= polvmer prepared according to the procedure of Example 7 Chan~es can be made in the composition, operation and arrangement of the method of the present invention described herein without departing from the concept and l 0 scope of the invention as defined in the following claims:
Field of the Invention Methods for preventing corrosion and scale deposition in aqueous media are disclosed. The methods utilize water-soluble polymers having pendant derivatized amide functionalities for scale inhibition.
Back~round of the Invention The utilization of water which contains certain inorganic impurities and the production and processing of crude oil water mixtures containing such impurities~ is pla_ued by the precipitation of these impurities with subsequent scale formation. In the case of water which contains these contaminants the harmful effects of scale formation 1 ~ are oenerally confined to the reduction of the capacitv or bore of receptacles and conduits cmplo! ed to store and conve! the contaminated water. In the case of conduits, the impedance of flov~ is an obvious consequence. However a number of equally consequential problems are realized in specific utilizations of contaminated water. For c~;ample. scale formed upon the surfaces of storage vessels and conveying lines for '0 process water may breal; loose and these large masses of deposit are entrained in and conve! ed by the process water to damage and clog equipment through which the water is passed. e.g.. tubes. ~alves. filters and screens. In addition. these crystalline deposits may appear in. and detract from. the final product which is derived from the process. e.g, paper formed from an aqueous suspension of pulp. Furthermore~ when the contaminated water is involved in a heat exchange process~ as either the "hot" or ''cold" medium, scale will be formed upon the heat exchange surfaces which are contacted by the water. Such scale formation forms an insulating or thermal opacifying barrier which impairs heat transfer efficiency as well as impeding flow through the system.
While calcium sulfate and calcium carbonate are primary contributors to scale formation. other salts of alkaline-earth metals and the aluminum silicates are also offenders. e.g.. magnesium carbonate. barium sulfate~ the aluminum silicates provided by silts of the bentonitic, illitic. }~aolinitic. etc., types.
Most industrial waters contain all;aline earth metal cations, such as calcium~
barium. maonesium. etc. and several anions such as bicarbonate, carbonate, sulfate.
o~;alate. phosphate. silicate, fluoride. etc. When combinations of these anions and cations arc present in concentrations which e~;ceed the solubility of their reaction products, pr~cipitates form until these product solubility concentrations are no longer exceeded.
or e~;ample. w hen the concentrations of calcium ion and carbonate ion e:;ceed the soluhilit\ of tile calcium carbonate reaction products. a solid phase of calcium carbonate will form Calcium carbonate is the most common form of scale.
Solubility product concentrations are e~;ceeded for various reasons, such as partial c~ aporation of the water phase. chan~e in pH. pressure or temperature~ and the '() inlroduction of additional ions which form insoluble compounds with the ions already prcsent in the solution As these reaction products precipitate on surfaces of the water carrying system, the! form scale or deposits. This accumulation prevents effective heat transfer~ interferes with fluid flow~ facilitates corrosive processes and harbors bacteria. This scale is an expensive problem in many industrial water systems causing delays and shutdowns for cleaning and removal.
Scale deposits are generated and extended principally by means of crystal growth;
5 and various approaches to reducing scale development have accordingly included inhibition of crystal growth. modification of crystal growth and dispersion of the scale-forrnin~ minerals.
Many other industrial waters~ while not being scale forming, tend to be corrosive.
Such waters. when in contact with a variety of metal surfaces such as ferrous metals, 10 aluminum. copper and its allo,vs. tend to corrode one or more of such metals or alloys. A
v ariety of compounds have been su~gested to alleviate these problems. Such materials are lou molecular weight polyacr,vlic acid polymers. Corrosive waters of this type are usually acidic in pH and are commonl~ found in closed recirculating systems.
Numerous compounds have been added to these industrial waters in an attempt to I S prevent or reduce scale and corrosion. One such class of materials are the well known oroanophosphonates ~ hich are illustrated by the compounds hydroxyethylidene diphosphonic acid (HEDP) and phosphonobutane tricarboxylic acid (PBTC). Another oroup of active scale and corrosion inhibitors are the monosodium phosphinicobis (succinic acids) which are described in U. S. Pat. No. 4.088~678.
'() Polymeric treatments have heen disclosed in U.S. Patent Nos. 4,680~339;
4.7~1.419: 4.885.,45 and 5.084.5~0. Utility for the treatments has been disclosed to be as dispersants in water treatment. scale inhibitors in industrial and natural waters, tlocculants. coagulants and thicl;eners.
Moreover, methods of controlling calcium oxalate scale with an effective amount of a water-soluble (meth)acrylic acid/allyl ether copolymer have been disclosed in U.S.
Patent No. 4,872,995. A method for controlling silica/silicate deposition, including calcium and magnesium silicate by addition of a phosphonate and a water-soluble terpolymer of an unsaturated carboxylic acid monomer, an unsaturated sulfonic compound and an unsaturated polyalkylene oxide is disclosed in U.S. Patent No.
4.933.090. Acrylate/acrylamide copolymers have been disclosed as useful for the inhibition of gypsum scale in flue gas desulfurization processes in U.S. Patent No.
4.8 1 8.506.
A method of inhibiting phosphonate scale formation on and corrosion of iron containing solid surfaces in contact with industrial waters with a water-soluble zinc stabilizing polvmer is disclosed in U.S. Patent No. ~.049,310. A method for preventing condensate corrosion in boilers comprising treating the condensate with a water-soluble pol! meric composition comprising a an acrylic acid polymer containin~ acrylic acid roups in the form of amides of a ~vater-insoluble aliphatic primary or secondary amine is disclosed in U.S. Patent No. 4.999.161. However. there is still a need for polymeric treatnlents w hich provide an increased efficienc! for corrosion and scale control.
.'iummar} of the Invention Methods for preventinn corrosion and scale deposition in aqueous media are '() disclosed. The methods utilize water-soluble polvmers having pendant derivatized amide functionalities for scale inhibition.
I)escription of the Invention The invention is a method for preventing scale formation on metal surfaces in contact with scale-forming Industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a ~vater-soluble polymer having distributed repeating mer units represented by the formula f_ CH
C =O
NRI
(I~HR-CHR3 Hetl~CHR2CHR3Het~~4 ~herein Rl is selected from the group consisting of hydrogen, and Cl - C3 alkyl; p and q are integers from I - 10; R- and R- are selected from the group consisting of hvdrogen alld Cl - C, al};yl: Hetl and Het~ selected from the group consisting of oxygen and 1(~ nitrogen: R~ is selected from the group consisting of hydrogen. and Cl - C,(, alkyl; R- and R'' are selected from the roup consisting of hvdrogen. carboxylate~ C~ - C3 all;yl~ and a cycloal~yl group of 3 to 6 carbon atoms formed by the linkage of R5 and R6 as a rin~.
For any embodiment of this invention~ the industrial water may be cooling water.
Furtllermore. the scale may selected from the group consisting of calcium phosphate, zinc I ~ phosphate. iron (hydr)oxide. aluminum hydroxide~ calcium sulfate, barium sulfate, clay, silt.-ma~mesium phosphate. magnesium carbonate and calcium carbonate Any embodiment of the polymers of this invention are also active against scale caused by c~lcium and magnesium salts of HEDP and calcium and magnesium salts of PBTC.
Furthermore, the cooling water may contain a biocide, corrosion inhibitors. or other scale inhibitors. The industrial water may be industrial process water selected from the group consisting of mining process water, pulp and paper process water and oilfield process water.
The invention is also a method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said uater uith an effective scale-inhibiting amount of a uater-soluble polvmer having:
A) a mer unit of the formula R~ R6 f _ CH
C =O
NRI
(CHR-CHR- Hetl~CHR~CHR3Het~~R4 ~-hcrcin Rl is selected from the group consisting of hydrogen, and C~ - C3 alkyl; p and q ~r. inteoers from 1 - 10; R- and R are selected from the group consisting of hydrogen I ~ alld C'l - C~ all;yl: Hetl and Het~ selected from the group consisting of oxygen and nilro~en: R~ is selected from the group consisting of hydrogen, and Cl - C7n alkyl; R5 and R'' are selected from the group consistino of hydrogen. carboxylate, Cl - C3 alkyl~ and a c~ cloall;yl ~roup of, to 6 carbon atoms formed by the linkage of R- and R6 as a ring;
and B) a mer unit selected from the group consisting of acrylic acid, methacrylic acid.
acrylamide. methacrylamide. maleic arlhydride. itaconic acid, vinyl sulfonic acid, styrene sulfonate, N-tertbutylacrylamide, butoxymethylacrylamide, N,N-dimethylacrylamide.
sodium acr lamidomethvl propane sulfonic acid, vinyl alcohol, vinyl acetate. N-vinvl S pyrrolidone, maleic acid, and combinations thereof. For any of structures I-III, the salts of the comonomers will also have utility.
A specific polymer applicable is identified as one wherein p=l; q=l; Rl, R2, R3.
R~. R-. and R6 are hydrogen: and Het~ and Het~ are oxygen in formula I of step A; and the mer units of step B are acrylic acid arld acrylamide for the water-soluble polymer.
Another useful polymer is one wherein p=l; q=l; Rl, R2, R3, R4, R5, and R6 are hydrogen: and Het~ and Het~ are oxygen in forrnula I of step A; and the mer units of step B are acrylic acid for the water-soluble polvmer. Yet another useful polymer is one wllerein p=l: q=l; R~. R-. R-'. R~. R . and R6 are hydrogen; and Het~ and Het~ are ~X! ~en in formula I of step A: and the mer units of step B are maleic acid and acrvlic I ~ acid for the ~ater-soluble polymer Another useful polymer is one wherein p=l, q=l, t~etl is nitrogen. Het~ is oxy~en and Rl. R-. R;, R~. R- and R6 are hydrogen in formula I
of step A: and the mer units of step B are acrylic acid and acrylamide for the water-sc)luble polymer Moreover. ~herein p=l. q=l. Heti is nitrogen. Het2 is oxygen and Rl, R-. R-'. R~. R and R~' are hvdrogen in formula I of step A: and the mer units of step B are '() acr! lic acid is also a useful ~ater-soluble polvmer. Wherein p=l, q=l, Hetl is nitrogen, Het~ is oxy~en and Rl. R-~ R . R~ R and Rt' are hydrogen in formula I of step A; and the mer units of step B are maleic acid and acrylic acid~ is another applicable water-soluble pol!~mer.
The invention is also a method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polvmer having distributed repeating mer units of the formula F--CH
1=~
NH
H ;C CHCH7 ( OCHR CH7 )p OR-wherein Rl is selected from the group consisting of hydrogen and C~ - C3 ali;yl oroups. p is an integer from 0-50: R- is selected from the group consisting of llvdro~en and C l-C~(, ali~yi groups: R- and Rh are selected from the group consisting of hvdrogen, 1(1 carho~;! lates Cl-C3 ali;yl groups. and a cvcloall~vl group of 3 to 6 carbon atoms formed h! Ihe lini;aoe of R- and Rh as a ring. v ith the proviso that when p is 0. R- is not h! drogen.
The invention is also a metllod for preventing scale formation on metal surfaces in contact ~ith scale-forminn industrial water within an industrial system which comprises I ~ the step of treating said water w ith an effective scale-inhibiting amount of a water-soluble pol! mer having: A) a mer unit of thc formula CH
1=0 NH
H3C CHCH, (OCHRICH~ )p OR-wherein Rl is selected from the group consisting of hydrogen and Cl - C3 alkvl groups p is an inte_er from 0-50: R- is seleeted from the group eonsisting of hydrogen and C,-C20 5 all;yl groups: R- and R6 are seleeted from the group eonsisting of hydrogen. earboxylates~
C~-C; all;yl groups. and a eycloall;yl group of 3 to 6 carbon atoms formed by the linl;age of R and R6 as a ring~ w ith the proviso that when p=07 R2 is not hydrogen; and B) a mer unit selected from the group consisting of acrylic acid~ methacrylic acid~ acrylamide~
methacr! lamide. maleie anhvdride~ itaeonie acid~ vinyl sulfonic acid~ styrene sulfonate~
I () I\ -tertbutylacrylamide. butoxvmeth! lacr- lamide. N.N-dimethylacrylamide~ sodium acrylamidomethyl propane sulfonic acid. vinyl alcohoh vinyl acetate~ N-vinyl py rrolidone. maleic acid. and combinations thereof.
For the practice of this invention. p may be an integer of from 10 to 25~ Rl may he selected from the group consistin~ of hydrogen and methyl groups~ R may be a I ~ meth! l group. R- may be hydro~en and R" may be hydrogen and the mer units of step B
ma! he acrylic acid. Additionally. p may be an integer of from 10 to 25. Rl may be selected from the group consistin ~ of hydrogren and methyl groups, R2 may be a methyl ~roup. R- and R6 may be hvdrogen and the mer units of step B may be acrylic acid and acrylamide. Furthermore~ another useful polymer is one wherein p is an integer of from 10 to 25, R~ is selected from the group consisting of hydrogen and methyl groups. R- is a methyl group. Rs is hydrogen and R6 is hydrogen and the mer units of step B are maleic S acid and acrvlic acid.
Another aspect of this invention is a method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial svstem which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polymer having distributed repeating mer units of the formula _f _ CH
l =O
NR
(CH,)r I (i R~
lll ~herein Rl is selected from the group consisting of hydrogen. and C~ - C3 alkyl; p is an inteoer from 1 - 10: R~ is selected from the group consisting of Cl-C~, alkyl groups. C~-C6 15 alk! l ether g roups and morpholino groups; R and R6 are selected from the group c~nsisting of hydrogen. carboxylate~ Cl - C3 alkyL and a cycloalkyl group of I to 6 carbon atoms formed by the linkage of R5 and R6 as a ring.
Yet another aspect of this invention is a method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polymer having: A) a mer unit of the formula Rs R6 C CH
C = O
NRI
I
(CH,)p erein Rl is selected from the group consisting of hydrogen, and C~ - C, alkyl; p is an hlteger from I - 10; R~ is selected t'rom the ~roup consisting of Cl-C6 alkyl groups~ Cl-C6 aik! l ether groups and morpholino ~roups: R- and R6 are selected from the group consisting of hydrogen~ carbo~;ylate. Cl -C3 alkvk and a cycloalkyl group of I to 6 carbon atoms formed by the linkaoe ot R- and R6 as a ring; and B) a mer unit selected I ~ frc rn the group consistino of acrylic acid~ methacrylic acid, acrylamide~ methacrylamide, maleic anhydride~ itaconic acid~ vin~l sulfonic acid, styrene sulfonate~ N-t~itbutvlacrvlarnide. butoxymethylacrylamide. N~N-dimethylacrylamide. sodium acrvlamidomethyl propane sulfonic acid, vinyl alcohol? vinyl acetate. N-vinyl pyrrolidone, maleic acid, and combinations thereof.
For the practice of the method described above, a useful polymer is one wherein 5 Rl. R- and R6 are hydro~en, p is ~ and R~ is a morpholino group in forrnula III of step A
and the mer units of step B are acrvlic acid and acrylamide. Another example of a useful polymer is one wherein Rl. R and R6 are hydrogen, p is 2 and R4 is a morpholino group in formula III of step A and the mer units of step B are acrylic acid for the water-soluble polymer. Yet another useful polymer is one wherein Rl, R5 and R6 are hydrogen. p is 2 10 and R' is a morpholino group in formula III of step A and the mer units of step B are acrylamide for the ~ater-soluble polymer. Furthermore, wherein Rl, R- and R6 are hydrogen. p is 3 and R4 is a methoxy group in formula III of step A; and the mer units of slep B are acrvlic acid and acrylamide: wherein Rl, R5 and R6 are hydrogen. p is 3 and R4 is a metho~;! group in formula III of step A; and the mer units of step B are acrylic acid:
herein Rl. R- and R~i are hydrooen p is 3 and R4 is a methoxy group in formula III of slep A: and the mer units of step B are maleic acid and acrylic acid are all examples of a~ licahle ~ater-soluble polymers The polymers described herein for the practice of this invention may range in nlol~cular ~eight from about ROOO to about 1.000.000. Preferably, the molecular weight ill he from about 5.000 to about 100.000 For the polymers defined herein. the mer unil~ defmed by formulas 1-111 ~A ill ran~e from 1 to 75% of the total number of mer units in lhe polymer Preferably the mer units defined as formulas l-III will be 5-50% of the lo~al number of mer units in the polvmer The polymer classes described herein contain amide mer units which are functionalized with pendant groups. These pendant groups confer favorable properties to the polymer for use as scale Inhibitors. The polymers may be produced by polymerization using specific monomers, such as might be produced by the copolvmerization of acrylic acid with an N-methoxy propyl acrylamide, methoxyethoxy acrylate. methoxyethoxv maleate or N-methoxypropyl acrylate comonomer. The polvmer so produced would contain a hydrophilic backbone with pendant groups.
Alternatively, pendant groups could be introduced into the polymer after polvmerization. For example, polyacrylic acid could be amidated with an 10 ethoxvlated/propoxylated amine, such as those available from Texaco under the trade name Jeffamine series. to produce a polvmer with a hydrophilic backbone and ethyleneoxy/propyleneoxy pendant groups. During the amidation process. cyclic imide structures might form between two adjacent carboxylate or carboxamide units on the polymer bac,!ibone. These imide structures are not expected to have an adverse effect on I ~ the performance of the polymers.
Typical metal surfaces in coolin~c water systems which may be subjected to ccorrosion or scale deposition are made of stainless steel. mild steel and copper alloys such as brass amon~ others.
The polymers may be effective a~,~ainst other types of scale including magnesium '() silicate. calcium sulfate. barium sulfate and calcium oxalate. The polymers are also effective in extremely hard water.
The polvmers may be utilized in conjunction with other treatments, for example biocides. other ferrous metal corrosion inhibitors, yellow metal corrosion inhibitors. scale inhibitors. dispersants. and additives. Such a combination may exert a synergistic effect in terms of corrosion inhibitors, scale inhibition. dispersancy and bacterium control.
Examples of biocides which can be used in combination with the pol!,~mers include: stabilized bleach~ chlorine and hypobromite, bromine (oxidizlng biocides). Also~
5 non-oxidizing biocides such as glutaraldehyde, isothiazolones (mixtures of 5-chloro-~-methyl-4-isothiazolin-3-one and ~-methyl-4-isothiazolin-3-one), sulfamic acid-stabilized bleach and sulfamic acid-stabilized bromine are applicable.
Additionall~, the polymers mav be utilized in conjunction with other corrosion and scale inhibitors Thus~ the polymers may be effective in combination with other 10 inhibitors such as hydroxyeth~,ylidene-l~l-diphosphonic acid (HEDP), ~-phosphonobutane- I ~.4-tricarboxylic acid (PBTC)~ ~-hydroxyethylimine bis(methylene phosphonic acid) N-oxide (EBO)~ methylene diphosphonic acid (MDP), he~;ameth! lenediamine-N~N~N~N'-tetra(methylene phosphonic acid), amino and Iris(methylene phosphonic acid)~ phosphorus-containing inorganic chemicals such as I ~ orthopllosph3tes~ pyrophosphates~ polyphosphates: hydroxvcarboxylic acids and their s, lls such as oluconic acids: ~lucaric acid: Zn~ ~ Ce~, MoO62~, W O4--~ and nitrites.
The polymers may also be effecti~ely utilized in conjunction with other p ol! meric treating agents. for e~;ample anionic polymers of under ~00.000 MW Such polymers include acrylic. methacrylic or maleic acid containing homo-, co- or ter-~() polymers.
Examples of yello~ metal corrosion inhibitors that can be used in combination~ilh the polymers include benzotriazole. tolyltriazole, mercaptobenzothiazole and other azole compounds Examples of other scale inhibitors that can be used in conjunction with the polymers include polvacrylates~ polymethacrylates, copolymers of acrylic acid and methacrylate~ copolymers of acrylic acid and acrylamide, poly(maleic acid) copolymers of acrylic acid and maleic acid. polyesters~ polyaspartic acid, fimctionalized polyaspartic 5 acid, terpolymers of acrylic acid. and acrylamide/sulfomethylated acrylamide copolvmers. HEDP (l-hydroxyethylidene~ diphosphonic acid), PBTC (2-phosphonobutane~ .4-tricarboxylic acid), and AMP (amino tri(methylene phosphonic acid).
To treat a cooling water system, the compounds may be added to the cooling 10 to- er basin or at any other location wherein good mixing can be achieved in a short time.
The term system as utilized herein is defined as any industrial process which utilizes water. The system could contain primarily aqueous fluids, or primarily non-aqueous fluids. but also contain water. Such systems are found in industrial processes ullich utilize boilers or cooling uater towers. For example. the food processing industry 15 is an industry u hich requires such a svstem.
The polymers may be added to the scale-forming or corrosive industrial process uater in an amount of from about 0.5 ppm to about 500 ppm. Preferably, the polymers ma! be added in an amount of from about 2 ppm to about 100 ppm. Most preferably, the pol~ mers ma~ be added in an amount of from about 5 ppm to about 50 ppm.
'() The following examples are presented to describe preferred embodiments and utilities of the invention and are not meant to limit the invention unless otherwise stated in the claims appended hereto.
E~ample 1 The synthesis of an ammonium acrylate/ N-(hydroxyethoxy)ethyl acrylamide copolymer was effected with the following reactants in the following arnounts:
Reactant Amount (~) S Poly(AA), 25.6 weight % in water 100.00 Aminoethoxyethanol 1 1.92 Ammonium Hydroxide, 29 weight % 2.51 To prepare the polymer, poly(AA) (25.6 weight percent poly(acrylic acid) solution. pH = 3.8, 16,000 MW) was placed in a beaker, which was cooled using an ice bath. Aminoethoxyethanol (available from Hllnt~m~n Petrochemical Co., in Houston, Texas) was added dropwise into the poly(acrylic acid)/water solution with vigorous stirring. Afterwards, the solution was stirred for another 15 minutes. Aqueous caustic was added to adjust the pH to about S. Next, the reaction mixture was transferred into a I ~ ~00 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then was assembled and purged w ith nitrogen for approximately 60 minutes. The Parr reactor was ~hen slo~ Iy heated to 1 60~C (or less. as the case may be) and held at that temperature for 8 hours (or more. as the case may be). Afterwards. the reactor was cooled to room temperature and the pressure released. The product was then transferred to storage.
'C NMR confirmed product formation. The content of N-(hydroxyethoxy)ethyl acrylamide ~ as ~ I mole %. based on the total moles of mer units on the polymer, which represents both secondary amide and imide mer units. The polymer's molecular weight S ~.000.
. CA 02241617 1998-06-26 Example 2 The s,vnthesis of an ammonium acrylate/acrylamide/N-(hydroxvethoxy)ethyl acrylamide terpolvmer was effected in the following manner with the reactants in the amounts listed belou:
Reactant Amount (~
Poly(NH4AAJAcAm). 50/50 mol %
solution polymer. 38.~ weight % 300.00 Aminoethoxyethanol 1 14.00 To prepare the polymer. Poly(NH4AA/AcAm) (50/50 mol % ammonium acrylate/acrvlamide copolymer, 38.~ weight percent, pH = 5.5, 33,000 MW) was placed in a beaker. which was cooled using an ice bath. Aminoethoxyethanol (available from Huntsman Petrochemical Co., in Houston, Texas) was added dropwise into the above I 5 u ater solution with vigorous stirring (pH = 10.1). Afterwards, the solution u as stirred for another I 5 minutes. Next~ the reaction mixture was transferred into a 600 mL Parr reactor ~ ith a pressure rating of at least 800 psi. The reactor then was assembled and puroed uith nitrogen for approximately 60 minutes. The Parr reactor was then slowly heated to I 38~C and held at that temperature for 14 hours. Afterwards. the reactor was '() eooled to room temperature and the pressure released. The product was then transferred to storalle.
I-'C NMR confirmed product formation. The content of N-(hydroxyethoxy)ethyl acr! lamide uas 33.3 mole %. based on the total moles of mer units on the polymer. The pc l!:mer had a molecular wei-~ht of 35.000. and a mole ratio of N-(hydroxyethoxy)ethyl acrylamide/acrylic acid/acrvlamide of about 331411~6.
Example 3 The synthesis of a sodium acrylate/acrylamide/N-(hydroxyethoxy)ethyl acrylamide terpolymer was effected in the following manner with the reactants in the amounts listed belou: , Reactant Amount (g) Poly(NaAA/AcAm), 50/50 mol %
solution pol,vmer. 32.0 weight % 100.00 Aminoethoxyethanol 32.00 Sulfuric Acid (95~/O) 11.5 To prepare the polymer. Poly(NaAA/AcAm) (50/50 mol % sodium acr late/acr,vlamide copolymer. 3~.0 weight %, pH = 5.2, 11,000 MW) was placed in a beai~er. which was cooled using an ice bath. Aminoethoxyethanol (available from 15 Huntsman Petrochemical Co.~ in Houston, Texas) was added dropwise into the above water solution v~ith vigorous stirring.. Afterwards, the solution was stirred for another 15 minutes. Sulfuric acid was added to adjust the pH to about 5.6. Next. the reaction mixture was transferred into a 300 mL Parr reactor with a pressure rating of at least 800 p .si. Tl-e reactor then was assembled and purged with nitrogen for approximately 60 '~) n~ utes. The Parr reactor was then slowly heated to 138~C and held at that temperature lor 1~ hours. Afterwards. the reactor was cooled to room temperature and the pressure rcleased. The product was then transferred to storage.
I 'C NMR conflrmed product formation. The content of N-(hydroxyethoxy)ethyl acr! lamide was 33 mole %~ based on the total moles of mer units on the polymer. The ~5 moie ratio ~as about 4~ 13, of'acrvlic acid/acrylamide(including 3% imide mer units)/N-(hydroxyethoxy)ethyl acrylamide (including imide mer units). The product polymer had a molecular wei~ht of 12~000.
Example 4 The synthesis of a sodium acrylate/acrylamide/N -Methoxypropyl acrvlamide 5 terpolymer was effected in the following manner with the reactants in the amounts listed below:
Reactant Amount(~y) Poly(NaAA/AcAm), 50/50 mol %
solution polymer, 32.0 weight % 100.00 Methoxypropylamine 23.32 Sulfuric Acid (95%) 11.23 To prepare the polymer. Poly(NaAAJAcAm) (50/50 mol%, 32.0 weight %. pH =
5.~. 11.000 MW) was placed in a beaker. which was cooled using an ice bath.
15 Methoxypropylamine (available from Aldrich Chem. Co.. in Milwaukee, WI) was added dropwise into the above water solution with vi~orous stirring. Afterwards, the solution was stirred for another 15 minutes. Sulfuric acid was added to adjust the pH to about 5.6.
Ne:;t. the reaction mixture was transferred into a 300 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then was assembled and purged with nitrogen for '() approximately 60 minutes. The Parr reactor was then slowly heated to 13~~C and held at that temperature for 1~ hours. Afterwards. the reactor was cooled to room temperature and the pressure released. The product was then transferred to storage.
l-'C NMR confirmed product forrnation. The content of N-methoxypropyl acrylamide was 34.2 mole %. based on the total moles of mer units on the polymer. The '5 mole ratio of the product was about 41/17/34 which represents acrylic acid/acrylamide (including 6% imide mer units)/methoxypropyl acrylamide (including imide mer units).
The product's molecular weight was 11,000.
Example 5 The synthesis of a sodium acrylate/acrylamide/N-hydroxy(ethylarnino)ethyl 5 acrylamide terpolymer was effected in the following manner with the reactants in the amounts listed below:
Reactant ~mount(~) Poly(NaAA/AcAm)~ 50/50 mol %
solution polymer. 24.0 weight % 80.00 (Aminoethylamino)ethanol 19.02 Sulfuric Acid (95%) 12.23 To prepare the polvmer, Poly(NaAA/AcAm) (50/50 mol%, 24.0 weight %~ pH =
,.~. 15.000 MW) was placed in a beaker. which was cooled using an ice bath.
l ~ ( Aminoeth- lamino)ethanol (available from Aldrich Chem. Co., in Milwaukee. WI) was added dropwise into the above water solution with vigorous stirring. Afterwards. the solution uas stirred for another 15 minutes. Sulfuric acid was added to adjust the pH to ahout ~.6. Ne~:t. the reaction mixture uas transferred into a 300 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then was assembled and purged with '() ni~rogen for approximately 60 minutes. The Parr reactor was then slowly heated to l .~~C and held at that temperature for 14 hours. Afterwards, the reactor was cooled to room temperature and the pressure released. The product was then transferred to storage.
'~'C NMR confirmed product formation. The content of N-hydroxy(ethylamino) eth! l acrylamide w.as 46 mole %. based on the total moles of mer units on the polymer, representing both secondary amide and imide mer units. The mole ratio of the product was about 46151/3 N-hydroxy(ethylamino)ethyl acrylamide/acrylic acid/acrylamide. The product polymer s molecular weight was 15,000.
Example 6 The synthesis of an acrylic acid/acrylarnide/ N-(hydroxyethoxy)ethyl acrylarnide 5 terpolymer was effected in the following manner with the reactants in the arnounts listed belou:
Reactant Amount(~
Poly(AcAm)~ 50 weight % 50.00 Aminoethoxyethanol 12.9 Deionized water 50.0 Sulfuric Acid (95%) 6.1 To prepare the polymer. Poly(AcAm) (50wt%, available from Aldrich Chemical Co.. 10.000 MW) was placed in a beal;er~ which was cooled using an ice bath.
15 Aminoethoxyethanol (available from Huntsman Petrochemical Co., in Houston~ Texas) was added dropwise into the above water solution with vigorous stirring. Afterwards~ the solution was stirred for another 15 minutes. Sulfuric acid was added to adjust the pH to about 5.6. Next. the reaction mixture was transferred into a 300 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then was assembled and purged with '() nitrogen for approximately 60 minutes. The Parr reactor was then slowly heated to 1 ' 8~C and held at that temperature for 14 hr. ARerwards. the reactor was cooled to room temperature and the pressure released. The product was then transferred to storage.
'~'C NMR conflrmed product formation. The content of N-(hydroxyethoxy) ethyl . CA 02241617 1998-06-26 acrylarnide was 19.6 mole %. based on the total moles of mer units on the polymer. The product's mole ratio was about 32/44/20 which represents acrylic acid/acrylamide/N-(hydroxyethoxy) ethyl acrylarnide.
Example 7 The synthesis of a ammonium acrylate/N-Methoxypropyl acrylarnide copolymer was effected in the following manner with the reactants in the arnounts listed below:
Reactant Amount(g) Poly(AA).~5.6 wei~ht % in water 100.00 Methxypropylarnine 1 0.09 Ammonium Hvdroxide. '9 wei~ht % in water 0.86 To prepare the polymer. Polv(AA)(32.0 wt%, pH = 3.3, 15,000 MW) was placed in a beal;er. which was cooled using an ice bath. Methoxypropylamine (available from I 0 Aldrich Chem. Co.. in Mil~au~;ee. Wl) was added dropwise into the above water solution ~ ith v igorous stirrin_ Afterwards. the solution was stirred for another 15 minutes.
Aqueous caustic ~as added to adjust the pH to about 5. Next, the reaction mixture was Iransferred into a 300 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then ~vas assembled and puroed ~ ith nitrogen for approximately 60 minutes. The I ~ Parr reactor ~as then slo~ heated to 1 60~C and held at that temperature for 8 hours.
After~vards. the reactor ~as cooled to room temperature and the pressure released. The product ~as then transferred to storage.
I-'C NMR confrmed product formation. The content N-methoxypropyl acrylamide ~as 22.4 mole %. based on the total moles of mer units on the polymer, which represents both secondary amide and imide mer units. The polymer's molecular wei_ht was 15~000.
Example 8 The synthesis of an acr,vlic acid/acrylamide/N-Methoxyprop,vl acrylamide 5 terpolymer was effected in the following marmer with the reactarlts in the amounts listed below:
Reactant Amount(g) Poly(AcAm). 50 wei~ht % in water 100.00 Methoxypropvlamine 1 0.99 Sulfuric Acid (95%) 6.75 Sodium Hvdroxide (50 wei~ht %) 1.8 To prepare the polymer, Poly(AcAm) (50.0 wt%, Available from Aldrich Chemical Co.~ 10~000 MW) was placed in a bea~;er, which was cooled using an ice bath.
I () ~lethoxypropylamine (available from Aldrich Chemical Co.. in Milwaul;ee. Wl) was added dropwise into the above water solution with vigorous stirring. ARerwards. the .solution was stirred for another 15 minutes. Aqueous caustic was added to adjust the pH
~o about 5.6. Next. the reaction mixture was transferred into a 300 mL Parr reactor ~vith a prcssure ratin~ of at least 800 psi. The reactor then was assembled and pur~ed with I 5 nitrogen for approximately 60 minutes. The Parr reactor was then slowly heated to 138~
C and held at that temperature for 12 hours. ARerwards. the reactor was cooled to room tcmperature and the pressure released. The product was then transferred to storage.
~ I-'C NMR confirmed product forrnation. The content N-methoxypropyl acrylamide was 20.~ mole %. based on the total moles of mer units on the polymer.
which represents both secondary amide and imide mer units. The product's mole ratio was about 33.8/45/20 which represents acrylic acid/acrylarnide/N-(methox~propyl) acrylarnide. The polymer's molecular weight was 18~500.
Example 9 S The synthesis of an acr~lic acidlacrylarnide/N-Methoxyethyl acrylarnide terpolymer was effected in the following manner with the reactants in the following manner with the reactants in the amounts listed below:
Reactant Amount(g) Poly(AA/AcAm)~ 31.4 wei~ht % in water100 Methoxyethylamine 1 9.65 Sulfuric Acid (95%) 10.20 To prepare the polvmer. Poly(A/AcAm) (31.4 wt%, 11,000 MW) was placed in a 1 () beal;er. which was cooled usinP an ice bath. Methoxyethylarnine (available from Aldrich C hemical Co.. in Milwaul;ee. Wl) was added dropwise into the above water solution with ~ ioorous stirrin~. Afterwards. the solution was stirred for another 15 minutes. The pH of the reactioll mixture was measured usin~ water-wet pH strips. Aqueous caustic was added to ad just the pH to about 5.6. ~le~;t. the reaction mixture was transferred into a 300 I 5 nll p arr reactor with a pressure ratin~ of at least 800 psi. The reactor then was assembled all(l pur~ed w ith nitro~en for appro~;imatel)~ 60 minutes. The Parr reactor was then slowl! heated to 138~C and held at that temperature for 12 hours. Afterwards. the reactor ~as cooled to room temperature and the pressure released. The product was then ransfcrred to stora~e.
I;C NMR confirmed product formation. The content N-methoxypropyl acrylamide was 40.8 mole %. based on the total moles of mer units on the polymer~
which represents both secondary amide and imide mer urlits. The product's mole ratio was about 40/14/41 which represents acrylic acid/acrylamide/N-(methoxypropyl) 5 acrylarnide. The polymer's molecular weight was 11,000.
Example 10 The s,vnthesis of a sodium acrylate/acrylamide/N-alkoxylated acrylamide copolymer was effected in the following manner with the reactants in the amounts listed below:
Reactant Amount(g) Polv(AA/AcAm), 50/50 mole % 43.8 weight % in water 100 Jeffamine M- 1000 60 Sodium Hydroxide (50 weight %) 11.78 Deionized Water 100 To prepare the polvmer. Poly(A/AcAm) (43.8 wt%~ pH = 4Ø 18.000 MW) was placed in a beal;er. which was cooled using an ice bath. Jeffamine M-1000 (available from Te:;aco Chemical Co. ) was added dropwise into the above water solution with v ioorous stirring. Afterwards. the solution w as stirred for another 15 minutes. Aqueous I ~ caustic was added to adjust the pH to about 6.9. Next, the reaction mixture was ~ransferred into a 300 mL parr reactor with a pressure rating of at least 800 psi. The reactor then was assembled and purged with nitrogen for approximately 60 minutes. The Parr reactor was then slowl~ heated to 1 50~C and held at that temperature for 5 hours.
Afterwards, the reactor was cooled to room temperature and the pressure released. The product was then transferred to storage.
Example 1I
The synthesis of a sodium acrylate/ N-hydroxy(ethylarnino)ethyl acrylamide 5 terpolymer was effected in the following marmer with the reactants in the amounts listed below:
Reactant Amo--nt(~
Poly(AA). 27.0 weight % in ~water 100.00 (Aminoethylamino)ethanol 12.89 Sulfuric Acid (95%) 0.6 To prepare the polymer. Poly(AA) (27.0 weight %, pH = 3.4, 17.000 MW) ~was placed in a beaker. which was cooled using an ice bath. (Aminoethylamino)ethanol (a~ailable from Aldrich Chem. Co.. in Milwaukee, WI) was added dropwise into the I ~ abo~e uater solution with ~~igorous stirring. Afterwards, the solution was stirred for anotller I 5 minutes. Sulfuric acid u as added to adjust the pH to about 5.6. Next. the reaction mixture uas transferred into a 300 mL Parr reactor with a pressure rating of at least 800 psi. The reactor then ~ as assembled and purged with nitrogen for approximately 60 minutes. The Parr reactor uas then slowly heated to 138~C and held at '() that temperature for 14 hours. Afterwards. the reactor was cooled to room temperature and the pressure released. The product uas then transferred to storage.
I C NMR confirmed product formation. The content of N-hydroxy(ethylamino) eth! l acrylamide was about 30 mole %. based on the total moles of mer units on the polymer. representin~~ both secondary amide and imide mer units. The product's mole ratio was approximately 70/30 which represents acrylic acid/N-(hydroxyethylamino) ethyl acrylamide. The product polymer's molecular weight was 32,000.
Example 12 The activity of polymers for calcium phosphate scale inhibition were evaluated in 5 the following manner.
An acidic stock solution ~vas prepared cont~inin~ calcium chloride, magnesium sulfate, and phosphoric acid. Aliquots of this stock solution were transferred to flasks so that on dilution, the final concentration of calcium was 750 or 1500 ppm as CaCO3. Iron or aluminum were added in 750 ppm Ca tests. The appropriate volume of inhibitor was l 0 added to _ive ~0 ppm polymer for the 1500 ppm Ca tests, 25 ppm polymer for the iron tests or 30 ppm polymer for the aluminum tests. Dl water was added, and the flasks were heated to 70~C. in a water bath. Stirring was maintained at ~50 rpm with l" stir bars.
Once the solutions were at temperature~ the pH was adjusted to 8.5. pH was cllecl;ed frequently to maintain 8.5. Filtered samples were taken aRer four hours. Then.
l S l 00 ml of the solution was taken and boiled for l 0 minutes in a covered flask. The volume ~ as brou~ht bacl; to l00 ml with Dl water. and filtered samples were taken again.
Standard colorimetric analvses determined ortho phosphate concentration in the samples.
Percent phosphate is reported as l00*P(filt)/P(unfilt). When no polymer was added~ 4-6~/o ~llterable phosphate ~as obtained.
'() Percent inhibition numbers above 80% indicate exceptional dispersant activity.
Polymers w hich disperse the phosphate in this test are observed to prevent calcium phosphate scale in recirculating cooling water svstems under similar high stress conditions. Numbers less than about 40% indicate poor dispersant activity. Such . CA 02241617 1998-06-26 polymers may or may not work under milder conditions (softer, cooler water)~ but do allow scale to form under high stress conditions. Polymers with intermediate activitv are still good dispersants for low stress conditions. but will lose activity at higher stress.
TABLE I
Calcium Phosphate Dispersancy Test - High Stress Conditions Polymer Percent Inhibition at 20 p ~m Polvmer CaTest Fe Test Al Test A' 37 46 34 C 60 --- ~0 D~ 89 --- ---F~ 82 44 58 G' 70 57 46 K" 26 --- ---I = conventional treatment 1~ sulfonated p(AA/AcAm) 2 = polvmer prepared according to a procedure similar to Example 10; 10/40/50 mole 5 ratio of JeffamineiAA/AcAm~ 60.000 MW
, = pol- mer prepared according to a procedure similar to Example 10; 20/40/40 mole ratio of Jeffamine/AA/AcAm~ 10~000 MW
= pol~mer prepared according to a procedure similar to Example I0; 40/40/20 moleratio of Jeffamine!AA/AcAm~ 20~000 MW
10 5 = pol~ mer prepared according to a procedure similar to Example 3 = pol~ mer prepared according to a procedure similar to Example I
7 = pol~ mer prepared according to the procedure of Example 2; 33141/26 mole ratio of AEE/AA/AcAm g = pol~ mer prepared according to the procedure of Example 4; 34/41/17 mole ratio of 1 5 ~lOPA/AA,AcAm 9 = pol! mer prepared according to the procedure of Example 5: 5114613 mole ratio of AA 'AEAE/AcAm 1 () = pol~ mer prepared according to the procedure of Example 9 1 1 = con~entional treatment 2~ p(AA/AcAm) available from Nalco Chemical Co.
'() ~'aperville. IL
Example 13 The follo~ing dispersancy test procedure was utilized to obtain the results sho~n in Table II. 200 mL of a test solution containing 20 ppm of a polymer dispersant and ~0 ppm of PBTC dissolved in distilled water was prepared. Then the test solution was added 5 to a ~50 mL erlenmeyer flask magnetically stirred at 40~C. Hardness and m-alkalinity are added to the solution over seven minutes to achieve a final solution composition (ppm as Ca COj) of 700 ppm Ca2 350 ppm Mg2, and 700 ppm Co32-. As calcium carbonate precipitation proceeds, the particle monitor responds to the fraction of calcium carbonate particles greater than 0.5 microns in diameter. The more effectively dispersed the l O calcium carbonate particles. the lower the fraction of large particle agglomerates. Better performing test solutions are indicated by (I ) lower particle monitor intensities. and (2) intensity ma~;ima achieved at longer times (60 minute limit).
E:;amples 1 and 7 are the best performing dispersants for preventing calcium c~rbon~te particle ag_lomeration e~idenced by (I) the smallest particle mollitor intensity I ~ and (') requiring longer times to achieve their ma~;imum signal response. Traditional dispcrsants (polyacrylic acid) provide improved dispersancy over the blank. but do not pcrform as ~ell as the e!;amples cited.
TABLE II
Dispersant (20 ppm total actives) Particle Monitor Intensit~ (time) Blank' 100 (12 minutes) Poly(acrylic acid) 57 (45 minutes) L lS (55 minutes) M~ 12 (60 minutes) I = 20 ppm PBTC
2= polymer prepared according to the procedure of Example 1 3= polvmer prepared according to the procedure of Example 7 Chan~es can be made in the composition, operation and arrangement of the method of the present invention described herein without departing from the concept and l 0 scope of the invention as defined in the following claims:
Claims (57)
1. A method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polymer having distributed repeating mer units represented by the formula wherein R1 is selected from the group consisting of hydrogen, and C1 - C3 alkyl; p and q are integers from 1 - 10; R2 and R3 are selected from the group consisting of hydrogen and C1 - C3 alkyl; Het1 and Het2 selected from the group consisting of oxygen and nitronen: R4 is selected from the group consisting of hydrogen, and C1 - C20, alkyl: R5 and R6 are selected from the group consisting of hydrogen, carboxylate, C1- C3 alkyl, and a cycloalkyl group of 3 to 6 carbon atoms formed by the linkage of R5 and R6 as a ring.
2. The method of claim 1 wherein the industrial water is cooling water.
3. The method of claim 1 wherein the scale is selected from the group consisting of calcium phosphate, zinc phosphate, iron (hydr)oxide, aluminum hydroxide, calcium sulfate, barium sulfate, clay, silt, magnesium carbonate, magnesium phosphate and calcium carbonate.
4. The method of claim 2 wherein the cooling water contains a biocide.
5. The method of claim 2 wherein the cooling water contains a corrosion inhibitor.
6. The method of claim 2 wherein the cooling water contains a scale inhibitor.
7. The method of claim 1 wherein the industrial water is industrial process water selected from the group consisting of mining process water, pulp and paper process water and oilfield process water.
8. A method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polymer having:
A) a mer unit of the formula wherein R1 is selected from the group consisting of hydrogen, and C1 - C3 alkyl: p and q are integers from 1 - 10; R2 and R3 are selected from the group consisting of hydrogen and C1 - C3 alkyl: Het1 and Het2 selected from the group consisting of oxygen and nitrogen: R4 is selected from the group consisting of hydrogen and C1 - C20, alkyl: R5 and R6 are selected from the group consisting of hydrogen, carboxylate, C1 - C3 alkyl and a cycloalkyl group of 3 to 6 carbon atoms formed by the linkage of R5 and R6 as a ring: and B) a mer unit selected from the group consisting of acrylic acid, methacrylic acid, acrylamide, methacrylamide, maleic anhydride, itaconic acid, vinyl sulfonic acid, styrene sulfonate, N-tertbutylacrylamide, butoxymethylacrylamide, N,N-dimethylacrylamide, sodium acrylamidomethyl propane sulfonic acid, vinyl alcohol, vinyl acetate, N-vinyl pyrrolidone, maleic acid, and combinations thereof.
A) a mer unit of the formula wherein R1 is selected from the group consisting of hydrogen, and C1 - C3 alkyl: p and q are integers from 1 - 10; R2 and R3 are selected from the group consisting of hydrogen and C1 - C3 alkyl: Het1 and Het2 selected from the group consisting of oxygen and nitrogen: R4 is selected from the group consisting of hydrogen and C1 - C20, alkyl: R5 and R6 are selected from the group consisting of hydrogen, carboxylate, C1 - C3 alkyl and a cycloalkyl group of 3 to 6 carbon atoms formed by the linkage of R5 and R6 as a ring: and B) a mer unit selected from the group consisting of acrylic acid, methacrylic acid, acrylamide, methacrylamide, maleic anhydride, itaconic acid, vinyl sulfonic acid, styrene sulfonate, N-tertbutylacrylamide, butoxymethylacrylamide, N,N-dimethylacrylamide, sodium acrylamidomethyl propane sulfonic acid, vinyl alcohol, vinyl acetate, N-vinyl pyrrolidone, maleic acid, and combinations thereof.
9. The method of claim 8 wherein the industrial water is cooling water.
10. The method of claim 8 wherein the scale is selected from the group consisting of calcium phosphate, zinc phosphate, iron (hydr)oxide, aluminum hydroxide, calcium sulfate, barium sulfate, clay, silt, magnesium phosphate, magnesium carbonate and calcium carbonate.
11. The method of claim 9 wherein the cooling water contains a biocide.
12. The method of claim 9 wherein the cooling water contains a corrosion inhibitor.
13. The method of claim 9 wherein the cooling water contains a scale inhibitor.
14. The method of claim 8 wherein the industrial water is industrial process water selected from the group consisting of mining process water, pulp and paper process water and oilfield process water.
15. The method of claim 8 wherein p=1; q=1; R1, R2, R3, R4, R5 and R6 are hydrogen; and Het1 and Het2 are oxygen in formula I of step A; and the mer units of step B are acrylic acid and acrylamide for the water-soluble polymer.
16. The method of claim 8 wherein p=1; q=1; R1, R2, R3, R4, R5, and R6 are hydrogen; and Het1 and Het2 are oxygen in formula I of step A: and the mer units of step B are acrylic acid for the water-soluble polymer.
17. The method of claim 8 wherein p=1; q=1; R1, R2, R3, R4, Rs, and Rfi are hydrogen: and Het1 and Het2 are oxygen in formula I of step A: and the mer units of step B are maleic acid and acrylic acid for the water-soluble polymer.
18. The method of claim 8 wherein p=1, q=1, Het1 is nitrogen, Het2 is oxygen and R1, R2, R3, R4, R5 and R6 are hydrogen in formula I of step A; and the mer units of step B are acrylic acid and acrylamide for the water-soluble polymer.
19. The method of claim 8 wherein p=1, q=1, Het1 is nitrogen, Het2 is oxygen and R1, R2, R3, R4, R5 and R6 are hydrogen in formula I of step A; and the mer units of step B are acrylic acid for the water-soluble polymer.
20. The method of claim 8 wherein p=1, q=1, Het1 is nitrogen, Het2 is oxygen and R1, R2, R3, R4, R5 and R6 are hydrogen in formula I of step A; and the mer units of step B are maleic acid and acrylic acid for the water-soluble polymer.
21. A method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polymer having distributed repeating mer units of the formula wherein R1 is selected from the group consisting of hydrogen and C1 - C3 alkyl groups, p is an integer from 0-50; R2 is selected from the group consisting of hydrogen and C1-C20 alkyl groups: R5 and R6 are selected from the group consisting of hydrogen, carboxylates, C1-C3 alkyl groups, and a cycloalkyl group of 3 to 6 carbon atoms formed by the linkage of R5 and R6 as a ring, with the proviso that when p=0. R2 is not hydrogen.
22. The method of claim 21 wherein the industrial water is cooling water.
23. The method of claim 21 wherein the scale is selected from the group consisting of calcium phosphate, zinc phosphate, iron (hydr)oxide, aluminum hydroxide, calcium sulfate, barium sulfate, clay, silt, magnesium phosphate, magnesium carbonate and calcium carbonate.
24. The method of claim 22 wherein the cooling water contains a biocide.
25. The method of claim 22 wherein the cooling water contains a corrosion inhibitor.
26. The method of claim 22 wherein the cooling water contains a scale inhibitor.
27. The method of claim 21 wherein the industrial water is industrial process water selected from the group consisting of mining process water, pulp and paper process water and oilfield process water.
28. A method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polymer having:
A) a mer unit of the formula wherein R1 is selected from the group consisting of hydrogen and C1 - C3 alkyl groups, p is an integer from 0-50; R2 is selected from the group consisting of hydrogen and C1-C20 alkyl groups; R5 and R6 are selected from the group consisting of hydrogen, carboxylates, C1-C3 alkyl groups, and a cycloalkyl group of 3 to 6 carbon atoms formed by the linkage of R5 and R6 as a ring, with the proviso that when p = 0, R2 is not hydrogen; and B) a mer unit selected from the group consisting of acrylic acid, methacrylic acid, acrylamide, methacrylamide, maleic anhydride, itaconic acid, vinyl sulfonic acid, styrene sulfonate, N-tertbutylacrylamide, butoxymethylacrylamide, N,N-dimethylacrylamide, sodium acrylamidomethyl propane sulfonic acid, vinyl alcohol, vinyl acetate, N-vinyl pyrrolidone, maleic acid, and combinations thereof.
A) a mer unit of the formula wherein R1 is selected from the group consisting of hydrogen and C1 - C3 alkyl groups, p is an integer from 0-50; R2 is selected from the group consisting of hydrogen and C1-C20 alkyl groups; R5 and R6 are selected from the group consisting of hydrogen, carboxylates, C1-C3 alkyl groups, and a cycloalkyl group of 3 to 6 carbon atoms formed by the linkage of R5 and R6 as a ring, with the proviso that when p = 0, R2 is not hydrogen; and B) a mer unit selected from the group consisting of acrylic acid, methacrylic acid, acrylamide, methacrylamide, maleic anhydride, itaconic acid, vinyl sulfonic acid, styrene sulfonate, N-tertbutylacrylamide, butoxymethylacrylamide, N,N-dimethylacrylamide, sodium acrylamidomethyl propane sulfonic acid, vinyl alcohol, vinyl acetate, N-vinyl pyrrolidone, maleic acid, and combinations thereof.
29. The method of claim 28 where in p is an integer of from 10 to 25, R1 is selected from the group consisting of hydrogen and methyl groups, R2 is a methyl group, R5 is hydrogen and R6 is hydrogen and the mer units of step B are acrylic acid.
30. The method of claim 28 wherein p is an integer of from 10 to 25, R1 is selected from the group consisting of hydrogen and methyl groups, R2 is a methyl group, R5 is hydrogen and R6 is hydrogen and the mer units of step B are acrylic acid and acrylamide.
31. The method of claim 28 wherein p is an integer of from 10 to 25, R1 is selected from the group consisting of hydrogen and methyl groups, R2 is a methyl group, R5 is hydrogen and R6 is hydrogen and the mer units of step B are maleic acid and acrylic acid.
32. The method of claim 28 wherein the industrial water is cooling water.
33. The method of claim 28 wherein the scale is selected from the group consisting of calcium phosphate, zinc phosphate, iron (hydr)oxide, aluminum hydroxide, calcium sulfate, barium sulfate, clay, silt, magnesium phosphate, magnesium carbonate and calcium carbonate.
34. The method of claim 32 wherein the cooling water contains a biocide.
35. The method of claim 32 wherein the cooling water contains a corrosion inhibitor.
36. The method of claim 32 wherein the cooling water contains a scale inhibitor.
37. The method of claim 32 wherein the industrial water is industrial process water selected from the group consisting of mining process water, pulp and paper process water and oilfield process water.
38. A method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polymer having distributed repeating mer units of the formula wherein R1 is selected from the group consisting of hydrogen, and C1 - C3 alkyl; p is an integer from 1 - 10: R4 is selected from the group consisting of C1-C6 alkyl groups. C1-C6 alkyl ether groups and morpholino groups; R5 and R6 are selected from the group consisting of hydrogen, carboxylate, C1 - C3 alkyl, and a cycloalkyl group of 1 to 6 carbon atoms formed by the linkage of R5 and R6 as a ring.
39. The method of claim 38 wherein the industrial water is cooling water.
40. The method of claim 38 wherein the scale is selected from the group consisting of calcium phosphate, zinc phosphate, iron (hydr)oxide, aluminum hydroxide, calcium sulfate, barium sulfate, clay, silt, magnesium phosphate, magnesium carbonate and calcium carbonate.
41. The method of claim 39 wherein the cooling water contains a biocide.
42. The method of claim 39 wherein the cooling water contains a corrosion inhibitor.
43. The method of claim 39 wherein the cooling water contains a scale inhibitor.
44. The method of claim 38 wherein the industrial water is industrial process water selected from the group consisting of mining process water, pulp and paper process water and oilfield process water.
45. A method for preventing scale formation on metal surfaces in contact with scale-forming industrial water within an industrial system which comprises the step of treating said water with an effective scale-inhibiting amount of a water-soluble polymer having:
A) a mer unit of the formula wherein R1 is selected from the group consisting of hydrogen, and C1 - C3 alkyl; p is an integer from 1 - 10; R4 is selected from the group consisting of C1-C6 alkyl groups, C1-C6 alkyl ether groups and morpholino groups; R5 and R6 are selected from the group consisting of hydrogen, carboxylate, C1 - C3 alkyl, and a cycloalkyl group of 1 to 6 carbon atoms formed by the linkage of R5 and R6 as a ring; and B) a mer unit selected from the group consisting of acrylic acid, methacrylic acid, acrylamide, methacrylamide, maleic anhydride, itaconic acid, vinyl sulfonic acid, styrene sulfonate, N-tertbutylacrylamide, butoxymethylacrylamide, N,N-dimethylacrylamide, sodium acrylamidomethyl propane sulfonic acid, vinyl
A) a mer unit of the formula wherein R1 is selected from the group consisting of hydrogen, and C1 - C3 alkyl; p is an integer from 1 - 10; R4 is selected from the group consisting of C1-C6 alkyl groups, C1-C6 alkyl ether groups and morpholino groups; R5 and R6 are selected from the group consisting of hydrogen, carboxylate, C1 - C3 alkyl, and a cycloalkyl group of 1 to 6 carbon atoms formed by the linkage of R5 and R6 as a ring; and B) a mer unit selected from the group consisting of acrylic acid, methacrylic acid, acrylamide, methacrylamide, maleic anhydride, itaconic acid, vinyl sulfonic acid, styrene sulfonate, N-tertbutylacrylamide, butoxymethylacrylamide, N,N-dimethylacrylamide, sodium acrylamidomethyl propane sulfonic acid, vinyl
46. The method of claim 45 wherein the industrial water is cooling water.
47. The method of claim 45 wherein the scale is selected from the group consisting of calcium phosphate, zinc phosphate, iron (hydr)oxide, aluminum hydroxide, calcium sulfate, barium sulfate, clay, silt, magnesium phosphate, magnesium carbonate and calcium carbonate.
48. The method of claim 46 wherein the cooling water contains a biocide.
49. The method of claim 46 wherein the cooling water contains a corrosion inhibitor.
50. The method of claim 46 wherein the cooling water contains a scale inhibitor.
51. The method of claim 45 wherein the industrial water is industrial process water selected from the group consisting of mining process water, pulp and paper process water and oilfield process water.
52. The method of claim 45 wherein R1, R5 and R6 are hydrogen, p is 2 and R4 is a morpholino group in formula III
of step A and the mer units of step B are acrylic acid and acrylamide for the water-soluble polymer.
of step A and the mer units of step B are acrylic acid and acrylamide for the water-soluble polymer.
53. The method of claim 45 wherein R1, R5 and R6 are hydrogen, p is 2 and R4 is a morpholino group in formula III
of step A and the mer units of step B are acrylic acid for the water-soluble polymer.
of step A and the mer units of step B are acrylic acid for the water-soluble polymer.
54. The method of claim 45 wherein R1, R5 and R6 are hydrogen, p is 2 and R4 is a morpholino group in formula III of step A and the mer units of step B are acrylic acid and maleic acid for the water-soluble polymer.
55. The method of claim 45 wherein R1, R5 and R6 are hydrogen, p is 3 and R4 is a methoxy group in formula III of step A; and the mer units of step B are acrylic acid and acrylamide for the water-soluble polymer.
56. The method of claim 45 wherein R1, R5 and R6 are hydrogen, p is 3 and R4 is a methoxy group in formula III of step A; and the mer units of step B are acrylic acid for the water-soluble polymer.
57. The method of claim 45 wherein R1, R5 and R6 are hydrogen, p is 3 and R4 is a methoxy group in formula III of step A; and the mer units of step B are maleic acid and acrylic acid for the water-soluble polymer.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/884,154 | 1997-06-27 | ||
| US08/884,154 US6017994A (en) | 1997-01-31 | 1997-06-27 | Utility of water-soluble polymers having pendant derivatized amide functionalities for scale control |
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| CA2241617A1 true CA2241617A1 (en) | 1998-12-27 |
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| EP (1) | EP0887316A1 (en) |
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| AR (1) | AR013141A1 (en) |
| AU (1) | AU6599898A (en) |
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| JPH07133160A (en) * | 1993-11-09 | 1995-05-23 | Murata Mfg Co Ltd | Ceramic slurry composition |
| JPH07144970A (en) * | 1993-11-22 | 1995-06-06 | Asahi Glass Co Ltd | Aluminum nitride green sheet |
| DE4411536A1 (en) * | 1994-04-02 | 1995-10-05 | Cassella Ag | Water-swellable hydrophilic polymers |
| US5475047A (en) * | 1994-05-17 | 1995-12-12 | The B. F. Goodrich Company | Carboxylic acid thickener having improved performance under alkaline conditions |
| US5532307A (en) * | 1995-04-13 | 1996-07-02 | Rohm And Haas Company | Method for forming an aqueous dispersion of ceramic material |
| US5567353A (en) * | 1995-04-13 | 1996-10-22 | Rohm And Haas Company | Method for dispersing ceramic material in an aqueous medium |
| US5726267A (en) * | 1997-01-31 | 1998-03-10 | Nalco Chemical Company | Preparation and utility of water-soluble polymers having pendant derivatized amide, ester or ether functionalities as ceramics dispersants and binders |
-
1997
- 1997-06-27 US US08/884,154 patent/US6017994A/en not_active Expired - Fee Related
-
1998
- 1998-05-15 AU AU65998/98A patent/AU6599898A/en not_active Abandoned
- 1998-06-24 SG SG1998001516A patent/SG75853A1/en unknown
- 1998-06-24 EP EP98304984A patent/EP0887316A1/en not_active Withdrawn
- 1998-06-26 AR ARP980103101A patent/AR013141A1/en unknown
- 1998-06-26 CA CA002241617A patent/CA2241617A1/en not_active Abandoned
- 1998-06-26 BR BR9802297-0A patent/BR9802297A/en not_active Application Discontinuation
- 1998-06-26 KR KR1019980024368A patent/KR19990007382A/en not_active Application Discontinuation
- 1998-06-29 JP JP10182027A patent/JPH1170398A/en active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| AR013141A1 (en) | 2000-12-13 |
| SG75853A1 (en) | 2000-10-24 |
| KR19990007382A (en) | 1999-01-25 |
| BR9802297A (en) | 1999-10-05 |
| EP0887316A1 (en) | 1998-12-30 |
| JPH1170398A (en) | 1999-03-16 |
| US6017994A (en) | 2000-01-25 |
| AU6599898A (en) | 1999-01-07 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FZDE | Discontinued |