US2304805A - Method of treating waters including boiler waters and compositions therefor - Google Patents

Method of treating waters including boiler waters and compositions therefor Download PDF

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US2304805A
US2304805A US321141A US32114140A US2304805A US 2304805 A US2304805 A US 2304805A US 321141 A US321141 A US 321141A US 32114140 A US32114140 A US 32114140A US 2304805 A US2304805 A US 2304805A
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amine
water
foam
amines
waters
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Wayne L Denman
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Dearborn Chemical Co
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/02—Foam dispersion or prevention
    • B01D19/04—Foam dispersion or prevention by addition of chemical substances
    • B01D19/0404—Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance
    • B01D19/0413—Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance compounds containing N-atoms

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  • the present invention relates to the treatment of waters, or aqueous baths, having present ingredients inducing foaming. More particularly, waters of the above character are treated with amines or more especially aliphatic amines, which are sparingly soluble, or substantially insoluble in the water being treated, preferably do not steam distill to any substantial extent, and exhibit little tendency to saponify with the ingredients of the water or aqueous bath.
  • the invention in its narrower form, contemplates the treatment of waters with saturated and/or unsaturated aliphatic amines, said compounds containing eleven (11) or more carbon atoms, being substantially insoluble in water, and showing little tendency to steam distill.
  • said compounds are used to inhibit the foaming tendency of raw or softened alkaline waters and particularly boiler waters having excess alkalinity, or an alkalinity present in a quantity more than sufdcient to combine with the calcium and/or magnesium ions, salts or their equivalents contained in the water.
  • the invention is directed to the utilization, in an antifoam composition, of dodecyl amine and di-octyl amine, the former being a primary amine and the latter being a secondar amine.
  • solubility of the aliphatic amines in water decreases with the mo- 1% lecular weight thereof, and, therefore, in accordance with the present invention, it is preferred to use those amine compounds which have a high molecular weight, and by this is meant compounds having eleven (11) carbon atoms or more, I
  • aliphatic amines which are sparingly soluble, or substantially insoluble, may be used as the primary anti-foam agent in a composition adapted to inhibit the foaming in waters containing ingredients inducing foaming therein. These amines are particularly capable of giving satisfactory results in inhibiting the foaming tendency of waters containing excess alkalinity, and particularly excess sodium and potassium alkalinity. These amines as a group show substantially no tendency to saponify in the water or aqueous bath treated. Preierably, where the water treated is subjected to a high temperature, the aliphatic amines should not steam distill to any material extent.
  • aliphatic amines which may be used in accordance with the present invention are stantially insoluble in water, and which prevent the foaming of the water or the aqueous bath treated.
  • it is the amines of high molecular weight which are the most satisfactory, and as a general rule, it may be stated that the most insoluble ones are the amines which contain more than ten (10) carbon atoms, particularly the straight chain primary amines.
  • the split chain primary amines, as well as the straight chain and split chain secondary and tertiary amines may be used in accordance with the present invention.
  • Undecyl amine (C11H23NH2) Dodecyl amine (C12H25NH2) Tridccyl amine (C13H27NH2) Tetradecyl amine (C14H29NH2) Pentadecyl amine (C15H31NH2) Nonadecyl amine (CIQHSQNHZ) Eicosyl amine (C2oH41NH2) Heneicosyl amine (C21H43NH2) Docosyl amine 1C22H45NH2) Tricosyl amine (C23H47NH2) Tetracosyl amine (CziHnNHz) Pentacosyl amine (C25H51NH2) Hexacosyl amine (CzsHssNHz) Heptacosyl amine (C27H55NH2) Octacosyl amine (CzaHswNHz) Nonacosyl amine (C29H59NH2) and the like.
  • amines are known under other names, as for example lauryl amine (C12H25NH2), myristyl amine (CMHZQNHZ), mellisyl amine (CKUHGINH2), and cerotyl amine (CzsI-IsaNHz)
  • lauryl amine C12H25NH2
  • CMHZQNHZ myristyl amine
  • CKUHGINH2 mellisyl amine
  • CzsI-IsaNHz cerotyl amine
  • the amine group may be attached to the first, or the second, or the third, or any other subsequent carbon atom in the chain.
  • amine being as for example undecyl amine having the formula (CH3(CH2)10NH2).
  • the isomeric amine thereof is methyl, nonyl, methyl amine (CH3 (CH2) aCHNHzCHa)
  • Similar isomeric amines may be prepared from other normal straight chain amines.
  • the material is a straight chain primary amine. Not only is it possible to use straight chain and split chain secondary and tertiary amines, but the isomeric forms of such amines may be used, and these compounds may differ from each other only in having an alkyl group substituted for one or both of the hydrogens in the amine group. If one hydrogen is substituted for, it would of course, be a secondary amine, and if both of the hydrogens are substituted for, it would be a tertiary amine. Substituting alkyl groups for hydrogens in the amine group, would tend to result in products of lower water solubility.
  • the amine irrespective of the substitution that has been made, should be one that has negligible water solubility. Further, the amines herein disclosed should preferably have a specific gravity less than water, so as to eliminate any tendency of the anti-foam agents to settle to the bottom of the treatment vessel.
  • waters containing sodium or potassium alkalinity that is, water in which the sodium or potassium alkalies, or their equivalents, and particularly sodium or potassium hydroxides, carbonates or bi-carbonates, exist in excess of that capable of combining with or existing in combination with calcium and/or magnesium ions present in the water.
  • Alkalinity of this type can exist naturally in the water or may be derived from zeolite treatment of the water, or may be derived in other ways.
  • the present invention may be applied to raw waters either hard or soft and beneficial results obtained.
  • Water. which has been softened by the lime-soda-ash process or by phosphates, sodium silicates, or other alkaline treatment, may be treated with an anti-foam composition of the character herein set forth.
  • Castor oil and sperm oil typify such substances.
  • oils of the above type When oils of the above type are added to boiler water, there is a tendency for them to be saponified or react chemically with the alkali hydroxides or other alkali compounds, with the resultant formation of soluble sodium and/or potassium soaps.
  • the foaming tendencies of sodium and potassium soaps are well recognized and the f ormation of such soaps accelerate the tendencies of the boiler water to foam.
  • water containing alkalinity, and particularly sodium or potassium alkalinity is treated with a material that is unsaponifiable and does not steam distill to any marked degree.
  • Waters softened by base exchange processes, and especially those which have been treated with zeolites or waters having a high natural sodium carbonate or sodium bicarbonate alkalinity are typical of waters having foaming properties and which may be treated in accordance with the present invention, which resides not only in said method, but also in the utilization of a particular class of anti-foam materials, and the method of preparing the same. While the average operating boiler pressure is around 200 pounds per square inch, it is to be understood that the present invention is applicable to boiler pressures materially higher or lower than 200 pounds per square inch.
  • the amines of the present invention may be mixed with a dispersing agent, and in the narrower form of the invention, the preferred dispersing agent is tannin, as will be hereinafter more fully pointed out.
  • the first class comprises inorganic colloidal material, such as clays or bentonite; the second class, organic materials which contain appreciable quantities of soap in one form or another; and the third class, organic materials which are characterized by colloidal properties and which contain no soap of any kind.
  • This third class of materials includes the extracts of various woods and barks which would normally be referred to as tannin extracts; extracts of various aquatic plants, such as seaweeds or kelp; and extracts of certain plants and shrubs, such as cactus plants.
  • Clays or bentonite may, of course, be used, but the disadvantages of this type of material makes it inadvisable to use it as the sole dispersion agent, since it does not lend itself to the very great dispersion that is necessary when a very small quantity of an anti-foaming compound is dissolved in a relatively large amount of boiler feed water.
  • the clays or bentonite may be used as the dispersion agent when mixed with other materials, as hereinafter set forth.
  • the soap dispersion agents may under some circumstances be used, but certainly not where there is an excess of alkali present, because the soap, in this case, remaining water soluble would tend to counteract the anti-foam properties of the anti-foam agent, and, moreover, in some cases. function to increase the foaming properties of the boiler Water instead of decreasing them.
  • tannin is a very desirable dispersing agent, because at least when waters having alkaline constituents are treated, and particularly boiler waters, the tannin has better dispersing properties than the clays or soap, while at the same time it does not have the disadvantages of the latter classes of materials.
  • tannin in certain cases and in certain types of waters. has fairly good anti-foam properties and, therefore, the use of tannin in conjunction with a more active antifoam agent results in a composition having antifoam properties superior to that of either the materials used separately.
  • the tannin acts as an active dispersing agent for the more active or primary anti-foam material, and this is highly desirable in a good anti-foam composition.
  • the tannin performs the function of conferring upon the resulting composition noncorrosive properties. This is due to the tendency of the tannin extract and similar materials to absorb dissolved oxygen from the boiler feed water or from any other water containing oxygen, which oxygen, if not removed, is one of the principal causes of boiler corrosion.
  • Tannin is an example of a material which is an active dispersing medium and also acts as a corrosion inhibitor to prevent corrosion of the boiler metal. It is within the province of the present invention in its broad form to use other equivalent materials which perform the same functions as the tannin performs.
  • the composition may have present a viscosityincreasing agent or bodying material.
  • a number of compounds may be used as the bodying agent, but it is preferable to use corn meal or a material containing starch.
  • the corn-meal or starch acts not only as a bodying material, but also as an additional dispersing agent and increases the dispersion characteristics of the composition.
  • the anti-foam composition has present a primary dispersion agent, and a secondary dispersion agent, the secondary dispersion agent preferably acting also as a bodying agent or to increase the viscosity of the anti-foam composition, which, of course, contains anti-foam agents, as hereinbefore pointed out.
  • the increase in the viscosity of the anti-foam composition is desirable since this prevents separation of the active anti-foam constituents from the remainder of the composition.
  • the meal or starch is heated in the presence of added water or that contained in the liquid tannin extract to a temperature high enough to produce a hydrolysis of the meal.
  • This hydrolyzed meal upon cooling takes on the form of starch paste and acts to increase the viscosity of the anti-foam composition in proportion to the amount of starch or meal used.
  • the amount of bodying agent used in the anti-foam composition may, of course, vary.
  • the primary, secondary or tertiary anti-foam agent may be a simple amine saturated or unsaturated, or a mixed amine, saturated or unsaturated. Further, the primary anti-foam agent may be a mixture of simple amines saturated or unsaturated, or a mixture of mixed amines, saturated or unsaturated.
  • the amine compound or the free amine may be formed in situ by decomposition of a suitable salt, said salt upon being added to the water, converting at least a part of the free salt to the free amine.
  • R denotes an alkyl group
  • R and R represent hydrogen, or an alkyl group.
  • This formula is intended to cover the primary, secondary and tertiary amines.
  • RNHz which contains the amino group NI-Iz.
  • the secondary amine is represented by RR'NH, and contains an imino group; and when three hydrogen are replaced, the tertiary amine is formed having the formula: RRR"N.
  • the amines Since it is desired that the amines be insoluble in the water treated and do not steam distill to any substantial extent, when boiler water is being treated, it is desirable and in fact practically necessary, that the amines have a high molecular weight of the character herein set forth.
  • the amines having a relatively low molecular weight are soluble in the boiler water, or other water, and steam distill to an appreciable extent. It is recognized that the branching of the chain in the chain amines lowers the boiling points of even the high molecular weight amine compounds having at least eleven carbon atoms in the basic R, R or B" group. However, if the boiling point is not greatly reduced, these branch chain compounds may be used in the treatment of boiler water.
  • the compounds coming within the scope of the present invention should have at least eleven carbon atoms in the basic alkyl group and preferably in each alkyl group of the secondary and tertiary amines.
  • the following is an illustrative example of how the present invention may be carried out, there being utilized in addition to the amine anti-foam agent, a dispersing agent and/or a bodying agent. While it may not be necessary in some instances to use a dispersing and/or bodying agent. as a general rule, it is desirable.
  • amine having a high molecular weight By this term it is intended to cover amines of the character set forth having eleven or more carbon atoms.
  • the higher amines of the series CnH2n+1).rNHy (where 1:0, 1 or 2) which have given very satisfactory results, are heptadecyl amine, stearyl amine, secondary stearyl amine and tertiary stearyl amine.
  • Polysubstituted amines and particularly those having eleven (11) or more carbon atoms present in each alkyl group may also be used.
  • the amine such as heptadecyl amine or stearyl amine may be mixed with a small percentage of corn meal and a predominating quantity of a liquid tannin extract well known in the prior art, and the mixture is heated to a temperature sufficient to produce a hydrolysis of the meal and to gelatinize the final product. Satisfactory results have been obtained by heating the mixture to about 180 F. Higher temperatures may be used. This mixture is fed into the boiler in the form of a water suspension.
  • the preferred form of the antifoam composition for introduction into the boiler feed water is that of a gelatinized product.
  • a gelatinized composition may be madeby mixing together an amine, such as heptadecyl amine, stearyl amine, or any other amine or amine mixture herein set forth with corn meal and tannin extract.
  • the ingredients may be mixed in suitable proportions, of which th following Tables I to IV are illustrative:
  • the amine content of th mixture may vary between about 1% to 2% to 35%.
  • the primary antifoam base such as the aliphatic amine
  • the primary anti-foam agent be used in conjunction with the tannin, as the tannin assists in the dis- 1) extract-94%,
  • dextrine As for example, dextrine, various other such agents may be used, as for example, dextrine. When using dextrine, satisfactory results have been obtained when the mixture contained from 5% to 50% of dextrine, which is a degradation product of starch. Instead of using corn meal, starch or dextrine, other bodying agents may be used. Gums, such as gum tragacanth, gum acacia and locus bean gum, which are additional examples of suitable bodying agents, give good results.
  • Tannin Corn Amme extract meal Per cent Per cen Per cent
  • Tannin Bcnton- Corn Amine extract lie starch Per can! Per cent British gum Tannin Amine extract Per cent Per cent Per cent 50% by weight of the mixture may be dextrine
  • the lower limit be 2%. Less than 2% may be used, and while 2% may be considered a satisfactory lower limit for starch, if the starch is used in conjunction with other thickening agents, such as a gum, then the starch may be reduced to less than 2%.
  • a paste mixture prepared as set forth and containing a primary anti-foam agent, a secondary anti-foaming agent, which preferably has dispersing properties, and a bodying agent of the character herein set forth may be added to boiler Water to prevent foaming thereof. More specifically, any of the compositions herein set forth may be added to the boiler water in the ratio of one-quarter pound of the composition per 1000 gallons of water. The amount which may be added is strictly illustrative, and is not to be taken by way of limitation. Obviously, the amount of anti-foam material which is added to the water will depend upon the characteristics of the water.
  • Tests taken immediately after the introduction of the anti-foam composition showed no foaming occurring.
  • Tests made two and one-half (2%) hours after the introduction of the anti-foam material showed the foaming to be practically nil.
  • Tests which were made after continuous heating of the anti-foam material in the boiler water, under the above conditions, for eight (8) hours, showed a tendency to foam, which was only a small fraction of the foaming occurring before the anti-foam was added. After twenty (20) hours the tendency to foam was not quite as great as that exhibited by the untreated water.
  • the amount of foaming in the presence of the anti-foam material may vary from a very small percentage to 25% to 40% of the foaming that occurs before the anti-foam material is added.
  • the compounds herein set forth give markedly superior results when treating water containing excess alkalinity. If castor oil, which is a well known anti-foaming agent for water which does not contain excess alkalinity, were used, the oil would become saponified and thereby rendered ineffective and/or harmful. In raw water and water softened in any well known manner, as for example by the lime-soda-ash process, the amines as hereinbefore described are also effectlve.
  • the herein referred to amines and amine compounds can each be mixed with the other to form the active anti-foam agent.
  • the mixture may contain more than two amines or amine compounds.
  • the primary amines may have an additional primary amine of the character herein set forth, or a plurality of amines mixed therewith to form the amine anti-foam agent.
  • the secondary amines may be mixed with a single amine or a plurality of other secondary amines, and the tertiary amines may be mixed with a single other tertiary amine, or a plurality of tertiary amines to form the active anti-foam agent.
  • any of the primary amines herein referred to may be mixed with any of the secondary amines or the anti-foam agent may comprise a mixture of a primary amine compound, a secondary amine compound, and a tertiary amine compound, or a mixture thereof.
  • the tertiary amines may also be mixed with each other to form the active anti-foam compound. It is not thought necessary to refer to all of the mixtures of primary amine compounds and/or secondary amine compounds and/or tertiary amine compounds which may be used in carrying out the present invention. However, as a specific example, it may be stated that secondary stearyl amine and tertiary stearyl amine may be mixed together with the tannin compounds herein referred to and a bodying agent, and excellent results be obtained.
  • the method of treating boiler water comprising subjecting said boiler water to the action of a composition containing a tannin dispersing agent and as its essential anti-foam agent a small amount, of the order of 500 parts per million, of dodecyl amine.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
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  • Chemical Kinetics & Catalysis (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)

Description

Patented Dec. 15, T942 UNTTE STATES PATENT FFICE METHOD OF TREATING WATERS INCLUD- ING BOILER WATERS AND COMPOSITIONS THEREFOR Wayne L. Denman, Berwyn, Ill., assignor to Dearborn Chemical Company, Chicago, 111., a corporation of Illinois 8 Claims.
The present invention relates to the treatment of waters, or aqueous baths, having present ingredients inducing foaming. More particularly, waters of the above character are treated with amines or more especially aliphatic amines, which are sparingly soluble, or substantially insoluble in the water being treated, preferably do not steam distill to any substantial extent, and exhibit little tendency to saponify with the ingredients of the water or aqueous bath.
The invention, in its narrower form, contemplates the treatment of waters with saturated and/or unsaturated aliphatic amines, said compounds containing eleven (11) or more carbon atoms, being substantially insoluble in water, and showing little tendency to steam distill. In one form of the invention, said compounds are used to inhibit the foaming tendency of raw or softened alkaline waters and particularly boiler waters having excess alkalinity, or an alkalinity present in a quantity more than sufdcient to combine with the calcium and/or magnesium ions, salts or their equivalents contained in the water. In its more specific form, the invention is directed to the utilization, in an antifoam composition, of dodecyl amine and di-octyl amine, the former being a primary amine and the latter being a secondar amine.
It may be stated that the solubility of the aliphatic amines in water decreases with the mo- 1% lecular weight thereof, and, therefore, in accordance with the present invention, it is preferred to use those amine compounds which have a high molecular weight, and by this is meant compounds having eleven (11) carbon atoms or more, I
and typified by undecyl amine, dodecyl amine, tridecyl amine, and the like, these all being straight chain primary amines.
As previously pointed out, aliphatic amines which are sparingly soluble, or substantially insoluble, may be used as the primary anti-foam agent in a composition adapted to inhibit the foaming in waters containing ingredients inducing foaming therein. These amines are particularly capable of giving satisfactory results in inhibiting the foaming tendency of waters containing excess alkalinity, and particularly excess sodium and potassium alkalinity. These amines as a group show substantially no tendency to saponify in the water or aqueous bath treated. Preierably, where the water treated is subjected to a high temperature, the aliphatic amines should not steam distill to any material extent. Examples of aliphatic amines which may be used in accordance with the present invention are stantially insoluble in water, and which prevent the foaming of the water or the aqueous bath treated. Generally, it is the amines of high molecular weight which are the most satisfactory, and as a general rule, it may be stated that the most insoluble ones are the amines which contain more than ten (10) carbon atoms, particularly the straight chain primary amines. However, it may be pointed out that the split chain primary amines, as well as the straight chain and split chain secondary and tertiary amines, may be used in accordance with the present invention.
Other straight chain primary amines which may be used as an anti-foam agent are:
Undecyl amine (C11H23NH2) Dodecyl amine (C12H25NH2) Tridccyl amine (C13H27NH2) Tetradecyl amine (C14H29NH2) Pentadecyl amine (C15H31NH2) Nonadecyl amine (CIQHSQNHZ) Eicosyl amine (C2oH41NH2) Heneicosyl amine (C21H43NH2) Docosyl amine 1C22H45NH2) Tricosyl amine (C23H47NH2) Tetracosyl amine (CziHnNHz) Pentacosyl amine (C25H51NH2) Hexacosyl amine (CzsHssNHz) Heptacosyl amine (C27H55NH2) Octacosyl amine (CzaHswNHz) Nonacosyl amine (C29H59NH2) and the like.
Several of the above amines are known under other names, as for example lauryl amine (C12H25NH2), myristyl amine (CMHZQNHZ), mellisyl amine (CKUHGINH2), and cerotyl amine (CzsI-IsaNHz) It is within the province of the present invention to use the isomeric forms of the straight chain amines or any other amines which are sparingly soluble or substantially insoluble in water and which inhibit the foaming of the water or aqueous bath being treated. For example, the amine group may be attached to the first, or the second, or the third, or any other subsequent carbon atom in the chain.
Examples of such isomeric forms are as follows.
Considering the normal straight chain primary amine, as set forth in the immediately preceding table, said amine being as for example undecyl amine having the formula (CH3(CH2)10NH2). the isomeric amine thereof is methyl, nonyl, methyl amine (CH3 (CH2) aCHNHzCHa) Similar isomeric amines may be prepared from other normal straight chain amines.
Secondary amines which are suitable for carrying out the present invention are:
Secondary heptylamine C'1Hl5HNC7Hl5 Secondary octyl amine CaHnNI-ICaHn Tertiary amines suitable for carrying out the present invention are:
Tertiary octylamine (CsH1'l)3N Tertiary heptylamine (C'lHlEi) 3N Secondary and tertiary amines typified by the above mentioned amines have a number of isomerlc forms which may be used in carrying out the present invention. Unbalanced straight chains or split chains result in many isomers for each amine having all alkyl groups the same.
Irrespective of to which carbon atom the amine group is attached, the material is a straight chain primary amine. Not only is it possible to use straight chain and split chain secondary and tertiary amines, but the isomeric forms of such amines may be used, and these compounds may differ from each other only in having an alkyl group substituted for one or both of the hydrogens in the amine group. If one hydrogen is substituted for, it would of course, be a secondary amine, and if both of the hydrogens are substituted for, it would be a tertiary amine. Substituting alkyl groups for hydrogens in the amine group, would tend to result in products of lower water solubility. However, the point is here made that the amine, irrespective of the substitution that has been made, should be one that has negligible water solubility. Further, the amines herein disclosed should preferably have a specific gravity less than water, so as to eliminate any tendency of the anti-foam agents to settle to the bottom of the treatment vessel.
Very satisfactory results have been obtained when the present invention has been applied to waters containing sodium or potassium alkalinity, that is, water in which the sodium or potassium alkalies, or their equivalents, and particularly sodium or potassium hydroxides, carbonates or bi-carbonates, exist in excess of that capable of combining with or existing in combination with calcium and/or magnesium ions present in the water.
Alkalinity of this type can exist naturally in the water or may be derived from zeolite treatment of the water, or may be derived in other ways.
The present invention may be applied to raw waters either hard or soft and beneficial results obtained. Water. which has been softened by the lime-soda-ash process or by phosphates, sodium silicates, or other alkaline treatment, may be treated with an anti-foam composition of the character herein set forth.
It is well known that many substances have decided anti-foam properties when used in conjunction with normal types of water which are free from excess alkalinity, such as sodium alkalinity,
asoaeoc or which have a low percentage of sodium alkalinity. Castor oil and sperm oil typify such substances.
When materials of this type are added to waters of excess alkalinity, and especially excess sodium and/or potassium alkalinity, poor or mediocre results are obtained in reducing the foaming tendency of the water. It seems probable that the foaming occurring in boiler water is the result of the concentration of soluble salts and insoluble solids in a state of suspension. In waters ,of excess alkalinity there may be present sodium and/or potassium bi-carbonates and/or carbonates, and there may be present sodium and/or potassium carbonates and/or hydroxides. Under conditions prevailing in an operating boiler, a large percentage of the bi-carbonates and carbonates originally present in the water are converted into hydroxides. It may well be that because of the presence of these hydroxides that the usual anti-foam materials are ineffective when added to boiler waters having high or moderately high concentrations of alkali hydroxides or other alkali materials.
When oils of the above type are added to boiler water, there is a tendency for them to be saponified or react chemically with the alkali hydroxides or other alkali compounds, with the resultant formation of soluble sodium and/or potassium soaps. The foaming tendencies of sodium and potassium soaps are well recognized and the f ormation of such soaps accelerate the tendencies of the boiler water to foam.
The following is a specific example, illustrating such acceleration and foaming tendency. An experimental boiler operating at a pressure of 200 lbs. per square inch, with an excess caustic alkalinity in the neighborhood of 200 grains per gallon, was treated with'a standard anti-foam material containing 16% of castor oil by weight, the proportion being one-quarter pound of the castor oil material per 1000 gallons ofwater. Immediately after the introduction of the anti-foam material, a test showedno foaming occurring. One hour after the introduction of the anti-foam material, the amount of foaming occurring was approximately 25% greater than that taking place before the anti-foam material was added. The
increase in foaming occurring one hour after the introduction of the anti-foam material, namely, castor oil. is due to the saponification of the same by the alkalies present in the boiler water.
Steam distillation of the usual anti-foam materials may, in some measure, reduce the effectiveness of these anti-foam materials in boiler Water of high or excess sodium or equivalent alkalinity. However, since most of the usual anti-foam materials can be used effectively in water containing little or no sodium alkalinity, and their effectiveness maintained, to a large degree at least, for several hours, steam distillation of the anti-foam material is probably of minor importance.
In one form of the present invention, water containing alkalinity, and particularly sodium or potassium alkalinity, is treated with a material that is unsaponifiable and does not steam distill to any marked degree. Waters softened by base exchange processes, and especially those which have been treated with zeolites or waters having a high natural sodium carbonate or sodium bicarbonate alkalinity are typical of waters having foaming properties and which may be treated in accordance with the present invention, which resides not only in said method, but also in the utilization of a particular class of anti-foam materials, and the method of preparing the same. While the average operating boiler pressure is around 200 pounds per square inch, it is to be understood that the present invention is applicable to boiler pressures materially higher or lower than 200 pounds per square inch.
The amines of the present invention may be mixed with a dispersing agent, and in the narrower form of the invention, the preferred dispersing agent is tannin, as will be hereinafter more fully pointed out.
It may be stated that three principal typical classes of dispersing agents are available. The first class comprises inorganic colloidal material, such as clays or bentonite; the second class, organic materials which contain appreciable quantities of soap in one form or another; and the third class, organic materials which are characterized by colloidal properties and which contain no soap of any kind. This third class of materials includes the extracts of various woods and barks which would normally be referred to as tannin extracts; extracts of various aquatic plants, such as seaweeds or kelp; and extracts of certain plants and shrubs, such as cactus plants.
Clays or bentonite may, of course, be used, but the disadvantages of this type of material makes it inadvisable to use it as the sole dispersion agent, since it does not lend itself to the very great dispersion that is necessary when a very small quantity of an anti-foaming compound is dissolved in a relatively large amount of boiler feed water. However, the clays or bentonite may be used as the dispersion agent when mixed with other materials, as hereinafter set forth.
The soap dispersion agents may under some circumstances be used, but certainly not where there is an excess of alkali present, because the soap, in this case, remaining water soluble would tend to counteract the anti-foam properties of the anti-foam agent, and, moreover, in some cases. function to increase the foaming properties of the boiler Water instead of decreasing them.
Investigation has shown that tannin is a very desirable dispersing agent, because at least when waters having alkaline constituents are treated, and particularly boiler waters, the tannin has better dispersing properties than the clays or soap, while at the same time it does not have the disadvantages of the latter classes of materials.
It may be pointed out that tannin in certain cases and in certain types of waters. has fairly good anti-foam properties and, therefore, the use of tannin in conjunction with a more active antifoam agent results in a composition having antifoam properties superior to that of either the materials used separately. Further, the tannin acts as an active dispersing agent for the more active or primary anti-foam material, and this is highly desirable in a good anti-foam composition. Again, the tannin performs the function of conferring upon the resulting composition noncorrosive properties. This is due to the tendency of the tannin extract and similar materials to absorb dissolved oxygen from the boiler feed water or from any other water containing oxygen, which oxygen, if not removed, is one of the principal causes of boiler corrosion. Tannin, of course, is an example of a material which is an active dispersing medium and also acts as a corrosion inhibitor to prevent corrosion of the boiler metal. It is within the province of the present invention in its broad form to use other equivalent materials which perform the same functions as the tannin performs.
The composition may have present a viscosityincreasing agent or bodying material. A number of compounds may be used as the bodying agent, but it is preferable to use corn meal or a material containing starch. The corn-meal or starch acts not only as a bodying material, but also as an additional dispersing agent and increases the dispersion characteristics of the composition. In accordance with one form of the present invention, the anti-foam composition has present a primary dispersion agent, and a secondary dispersion agent, the secondary dispersion agent preferably acting also as a bodying agent or to increase the viscosity of the anti-foam composition, which, of course, contains anti-foam agents, as hereinbefore pointed out.
The increase in the viscosity of the anti-foam composition is desirable since this prevents separation of the active anti-foam constituents from the remainder of the composition.
The following are examples of methods which may be used to obtain the bodying effect.
In one method the meal or starch is heated in the presence of added water or that contained in the liquid tannin extract to a temperature high enough to produce a hydrolysis of the meal. This hydrolyzed meal upon cooling takes on the form of starch paste and acts to increase the viscosity of the anti-foam composition in proportion to the amount of starch or meal used. The amount of bodying agent used in the anti-foam composition may, of course, vary.
In carrying out the present invention, the primary, secondary or tertiary anti-foam agent may be a simple amine saturated or unsaturated, or a mixed amine, saturated or unsaturated. Further, the primary anti-foam agent may be a mixture of simple amines saturated or unsaturated, or a mixture of mixed amines, saturated or unsaturated. The amine compound or the free amine may be formed in situ by decomposition of a suitable salt, said salt upon being added to the water, converting at least a part of the free salt to the free amine.
The compounds which are useful in carrying out the present invention are generally represented by the following formula:
In said formula, R denotes an alkyl group; R and R", represent hydrogen, or an alkyl group. This formula is intended to cover the primary, secondary and tertiary amines. When one hydrogen is replaced in NH; the resulting compound may be designated RNHz, which contains the amino group NI-Iz. When two hydrogen are replaced, the secondary amine is represented by RR'NH, and contains an imino group; and when three hydrogen are replaced, the tertiary amine is formed having the formula: RRR"N.
Since it is desired that the amines be insoluble in the water treated and do not steam distill to any substantial extent, when boiler water is being treated, it is desirable and in fact practically necessary, that the amines have a high molecular weight of the character herein set forth. The amines having a relatively low molecular weight are soluble in the boiler water, or other water, and steam distill to an appreciable extent. It is recognized that the branching of the chain in the chain amines lowers the boiling points of even the high molecular weight amine compounds having at least eleven carbon atoms in the basic R, R or B" group. However, if the boiling point is not greatly reduced, these branch chain compounds may be used in the treatment of boiler water. For the above reasons, in the preferred form of the invention, the compounds coming within the scope of the present invention, should have at least eleven carbon atoms in the basic alkyl group and preferably in each alkyl group of the secondary and tertiary amines.
The following is an illustrative example of how the present invention may be carried out, there being utilized in addition to the amine anti-foam agent, a dispersing agent and/or a bodying agent. While it may not be necessary in some instances to use a dispersing and/or bodying agent. as a general rule, it is desirable.
The above indicates What is meant by the term amine having a high molecular weight. By this term it is intended to cover amines of the character set forth having eleven or more carbon atoms. The higher amines of the series CnH2n+1).rNHy (where 1:0, 1 or 2) which have given very satisfactory results, are heptadecyl amine, stearyl amine, secondary stearyl amine and tertiary stearyl amine. Polysubstituted amines and particularly those having eleven (11) or more carbon atoms present in each alkyl group may also be used. The amine, such as heptadecyl amine or stearyl amine may be mixed with a small percentage of corn meal and a predominating quantity of a liquid tannin extract well known in the prior art, and the mixture is heated to a temperature sufficient to produce a hydrolysis of the meal and to gelatinize the final product. Satisfactory results have been obtained by heating the mixture to about 180 F. Higher temperatures may be used. This mixture is fed into the boiler in the form of a water suspension.
As indicated, the preferred form of the antifoam composition for introduction into the boiler feed water is that of a gelatinized product. Such a gelatinized composition may be madeby mixing together an amine, such as heptadecyl amine, stearyl amine, or any other amine or amine mixture herein set forth with corn meal and tannin extract.
The ingredients may be mixed in suitable proportions, of which th following Tables I to IV are illustrative:
Table I Corn meal--2%, tannin amine-4% Corn meal-4%,
amine8% Corn meal6%, amine-16% Corn meal-8%, amine-25% Corn mea18%, amine-35% In general, the amine content of th mixture may vary between about 1% to 2% to 35%.
The above percentages are merely illustrative as to the amount of tannin extract and aliphatic amine, and may vary beyond the limit of the maxim m and minimum above set forth and still come within the spirit of the present invention. As hereinbefore pointed out, the primary antifoam base, such as the aliphatic amine, may be used by itself, but it is desirable that the primary anti-foam agent be used in conjunction with the tannin, as the tannin assists in the dis- 1) extract-94%,
(2) tannin extract-88%,
3) tannin extract-78%,
( 4) tannin extract-67%.
() tannin extract-57%,
persion, and further is in itself an anti-foam agent. It is preferred to form a gelatinized product of the ingredients, but here again, it is within the spirit of the present invention to use the primary anti-foam agent in an anti-foam composition which is not reduced to paste form.
Instead of using corn meal or starch as the viscosity-increasing or bodying agent, various other such agents may be used, as for example, dextrine. When using dextrine, satisfactory results have been obtained when the mixture contained from 5% to 50% of dextrine, which is a degradation product of starch. Instead of using corn meal, starch or dextrine, other bodying agents may be used. Gums, such as gum tragacanth, gum acacia and locus bean gum, which are additional examples of suitable bodying agents, give good results.
The following examples illustrate how the dispersion agents and the bodying agents may be varied:
Table II Tannin Corn Amme extract meal Per cent Per cen Per cent Table III Tannin Bcnton- Corn Amine extract lie starch Per can! Per cent British gum Tannin Amine extract Per cent Per cent Per cent 50% by weight of the mixture may be dextrine,
and again it is not necessary with some of the bodying agents that the lower limit be 2%. Less than 2% may be used, and while 2% may be considered a satisfactory lower limit for starch, if the starch is used in conjunction with other thickening agents, such as a gum, then the starch may be reduced to less than 2%.
A paste mixture prepared as set forth and containing a primary anti-foam agent, a secondary anti-foaming agent, which preferably has dispersing properties, and a bodying agent of the character herein set forth may be added to boiler Water to prevent foaming thereof. More specifically, any of the compositions herein set forth may be added to the boiler water in the ratio of one-quarter pound of the composition per 1000 gallons of water. The amount which may be added is strictly illustrative, and is not to be taken by way of limitation. Obviously, the amount of anti-foam material which is added to the water will depend upon the characteristics of the water. For example, in another experiment it was found that as low as one-twentieth /o) of a pound of the anti-foam composition per 1000 gallons of water was satisfactory. In still another case two (2) pounds of the anti-foam composition per 1000 gallons of water positively inhibited the anti-foam tendency of the boiler feed.
The above mixtures and similar mixtures were added to water of the character that the castor oil, previously referred to, was added, and the conditions of the tests were the same.
Tests taken immediately after the introduction of the anti-foam composition showed no foaming occurring. Tests made two and one-half (2%) hours after the introduction of the anti-foam material showed the foaming to be practically nil. Tests which were made after continuous heating of the anti-foam material in the boiler water, under the above conditions, for eight (8) hours, showed a tendency to foam, which was only a small fraction of the foaming occurring before the anti-foam was added. After twenty (20) hours the tendency to foam was not quite as great as that exhibited by the untreated water. Even in the presence of the anti-foam material, there is some tendency to foam, and the amount of foaming in the presence of the anti-foam material, may vary from a very small percentage to 25% to 40% of the foaming that occurs before the anti-foam material is added.
The compounds herein set forth give markedly superior results when treating water containing excess alkalinity. If castor oil, which is a well known anti-foaming agent for water which does not contain excess alkalinity, were used, the oil would become saponified and thereby rendered ineffective and/or harmful. In raw water and water softened in any well known manner, as for example by the lime-soda-ash process, the amines as hereinbefore described are also effectlve.
The herein referred to amines and amine compounds can each be mixed with the other to form the active anti-foam agent. Moreover, the mixture may contain more than two amines or amine compounds. The primary amines may have an additional primary amine of the character herein set forth, or a plurality of amines mixed therewith to form the amine anti-foam agent. The secondary amines may be mixed with a single amine or a plurality of other secondary amines, and the tertiary amines may be mixed with a single other tertiary amine, or a plurality of tertiary amines to form the active anti-foam agent. Moreover, any of the primary amines herein referred to may be mixed with any of the secondary amines or the anti-foam agent may comprise a mixture of a primary amine compound, a secondary amine compound, and a tertiary amine compound, or a mixture thereof. The tertiary amines may also be mixed with each other to form the active anti-foam compound. It is not thought necessary to refer to all of the mixtures of primary amine compounds and/or secondary amine compounds and/or tertiary amine compounds which may be used in carrying out the present invention. However, as a specific example, it may be stated that secondary stearyl amine and tertiary stearyl amine may be mixed together with the tannin compounds herein referred to and a bodying agent, and excellent results be obtained.
' The present application is a division of application Serial No. 193,368, filed March 1, 1938, and a continuation-in-part of applications Serial Nos. 193,366 and 193,367, each of said applications being a continuation-in-part of application Serial No. 579, filed January 5, 1935.
I claim:
1. The process of treating water which includes adding to the water a small amount, not to exceed five hundred parts per million, of dodecyl amine.
2. The process of treating water which includes adding to the water a small amount, not to exceed five hundred parts per million of dioctyl amine,
3. The method of treating an aqueous bath having present an alkaline constituent inducing foaming therein, comprising subjecting the bath to the action of a composition containing as its essential anti-foam agent a small amount, of the order of 500 parts per million, of dodecyl amine.
4. The method of treating boiler water to prevent foaming, comprising subjecting said boiler water to the action of a composition containing a dispersing agent, and as its essential anti-foam agent a small amount, of the order of 500 parts per million, of dodecyl amine.
5. The method of treating boiler water comprising subjecting said boiler water to the action of a composition containing a tannin dispersing agent and as its essential anti-foam agent a small amount, of the order of 500 parts per million, of dodecyl amine.
6. The method of treating an aqueous bath having present an alkaline constituent inducing foaming therein, comprising subjecting the bath to the action of a composition containing as its essential anti-foam agent a small amount, of the order of 500 parts per million, of dioctyl amine.
7. The method of treating boiler water to prevent foaming, comprising subjecting said boiler water to the action of a composition containing a dispersing agent, and as its essential anti-foam agent a small amount, of the per million, of dioctyl amine.
8. The method of treating boiler water comprising subjecting said boiler water to the action of a composition containing a tannin dispersing agent and as its essential anti-foam agent a small amount, of the order of 500 parts per million, of
dioctyl amine.
WAYNE L. DENMAN.
order of 500 parts
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US2428801A (en) * 1942-03-27 1947-10-14 Nat Aluminate Corp Process for the prevention of foaming in steam boilers
US2428776A (en) * 1942-03-27 1947-10-14 Nat Aluminate Corp Prevention of foaming in steam boilers
US2428775A (en) * 1942-03-27 1947-10-14 Nat Aluminate Corp Product and process for the prevention of foaming in steam boilers
US2442768A (en) * 1939-11-24 1948-06-08 Dearborn Chemicals Co Method of conditioning water
US2461730A (en) * 1942-09-12 1949-02-15 Dearborn Chemicals Co Method of inhibiting foam formation in an aqueous gas-liquid system
US2481899A (en) * 1942-09-19 1949-09-13 Nat Aluminate Corp Prevention of foaming in steam generation
US2485378A (en) * 1943-12-08 1949-10-18 Dearborn Chemicals Co Method of inhibiting foaming in steam boilers
US2528273A (en) * 1947-09-09 1950-10-31 Dearborn Chemicals Co Method of inhibiting foaming in steam boilers
US2534441A (en) * 1945-03-19 1950-12-19 Dearborn Chemicals Co Method of and composition for inhibiting foaming in steam boilers
US2562571A (en) * 1945-05-30 1951-07-31 Hall Lab Inc Treatment of steam systems
US2563856A (en) * 1945-10-12 1951-08-14 Nopco Chem Co Defoaming agent for pulp and paper stock
US2580922A (en) * 1942-09-19 1952-01-01 Nat Aluminate Corp Prevention of foaming in steam generation
US2580880A (en) * 1942-03-27 1952-01-01 Nat Aluminate Corp Prevention of foaming in steam generation
US2976240A (en) * 1958-10-21 1961-03-21 Gulf Research Development Co Foam-inhibited aqueous oil emulsions
US5707553A (en) * 1994-02-25 1998-01-13 Sawyer; Melvyn Lloyd Anti-corrosion, quick drying distilled water solution for autoclave sterilizers

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US2612478A (en) * 1948-06-03 1952-09-30 Dearborn Chemicals Co Method and composition for inhibiting foam in aqueous systems
US2600361A (en) * 1948-06-09 1952-06-10 Dearborn Chemicals Co Prevention of foaming in steam generation
US2683692A (en) * 1949-12-23 1954-07-13 Monsanto Chemicals Nonfoaming surface-active alkyl benzene sulfonate composition
US3317431A (en) * 1964-10-08 1967-05-02 Wright Chem Corp Water treating reagent and method
US4404167A (en) * 1979-05-14 1983-09-13 Rozenfeld Iosif L Protecting steel and ferrous metals against H2 S corrosion

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2442768A (en) * 1939-11-24 1948-06-08 Dearborn Chemicals Co Method of conditioning water
US2428776A (en) * 1942-03-27 1947-10-14 Nat Aluminate Corp Prevention of foaming in steam boilers
US2428775A (en) * 1942-03-27 1947-10-14 Nat Aluminate Corp Product and process for the prevention of foaming in steam boilers
US2428801A (en) * 1942-03-27 1947-10-14 Nat Aluminate Corp Process for the prevention of foaming in steam boilers
US2580880A (en) * 1942-03-27 1952-01-01 Nat Aluminate Corp Prevention of foaming in steam generation
US2461730A (en) * 1942-09-12 1949-02-15 Dearborn Chemicals Co Method of inhibiting foam formation in an aqueous gas-liquid system
US2580922A (en) * 1942-09-19 1952-01-01 Nat Aluminate Corp Prevention of foaming in steam generation
US2481899A (en) * 1942-09-19 1949-09-13 Nat Aluminate Corp Prevention of foaming in steam generation
US2485378A (en) * 1943-12-08 1949-10-18 Dearborn Chemicals Co Method of inhibiting foaming in steam boilers
US2534441A (en) * 1945-03-19 1950-12-19 Dearborn Chemicals Co Method of and composition for inhibiting foaming in steam boilers
US2562571A (en) * 1945-05-30 1951-07-31 Hall Lab Inc Treatment of steam systems
US2563856A (en) * 1945-10-12 1951-08-14 Nopco Chem Co Defoaming agent for pulp and paper stock
US2528273A (en) * 1947-09-09 1950-10-31 Dearborn Chemicals Co Method of inhibiting foaming in steam boilers
US2976240A (en) * 1958-10-21 1961-03-21 Gulf Research Development Co Foam-inhibited aqueous oil emulsions
US5707553A (en) * 1994-02-25 1998-01-13 Sawyer; Melvyn Lloyd Anti-corrosion, quick drying distilled water solution for autoclave sterilizers

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