Abstract:
A method for inhibiting microbial growth in aqueous fluid media, particularly media containing fatty oil or petroleum base components and modified metalworking fluids is described. The antimicrobial method involves adding an antimicrobially effective amount of n-hexyl ethanolamine to the aqueous fluid medium.

Description:
BACKGROUND OF THE INVENTION 
     Antimicrobial compositions are generally added to various kinds of aqueous fluid media to reduce or inhibit the growth of microorganisms. In particular, a wide variety of industrial aqueous fluid media such as metalworking fluids used with metalworking equipment require antimicrobial compositions to control the growth microorganisms which eventually render the fluids rancid. 
     The development of high speed metal cutting and grinding has resulted in the creation of lubricants containing oils and chemicals stabilized in water. These fluids impart the cooling qualities of water and the lubricating properties of oil which prolong the life of cutting tools, reduce heat production, improve surface finish of the metal being machined, prevent warping and leave a rust-inhibiting film of oil on the worked piece. 
     Normally these fluids include fatty or petroleum oils, soaps, or synthetic based materials and additional additives such as antifoam agents, preservatives, coupling agents and rust inhibitors. The coolants are generally marketed in the form of concentrates which are normally diluted with water by the user in ratios of 1 part oil to about 20-40 parts of water, but these ratios may vary with particular operations. The lubricant is supplied to a machine from either an individual tank containing 50 to 100 gallons or from a large sump containing thousands of gallons which supplies many machines. 
     One of the problems often associated with such aqueous fluid media arises from the susceptibility of the media to the infestation and growth of various microorganisms such as bacteria and fungi (which particularly feed on the organic components thereof). The presence and buildup of such microorganisms can often lead to interference in the metalworking operations as a result of the clogging of filters, buildup of slime and sludge, development of odors, rust, emulsion instability, reduced tool life and poor finish. Furthermore, in machine shops where the workers&#39; hands necessarily come in contact with the cutting oil, usually containing finely divided sharp metal cuttings, serious problems of dermatitis may arise. These and other such similar problems have resulted in the continuing need for better antimicrobial additives for aqueous fluid media such as metalworking fluids. Much effort has been devoted in recent years to controlling this problem; however, it continues to be a major annoyance which costs the metalworking industry many millions of dollars each year. 
     A number of suggestions have been made for inhibiting the growth of bacteria in aqueous fluids such as those described in U.S. Pat. Nos. 4,172,140, 3,951,830, 3,799,876, 3,515,671, and 2,976,244. The use of various formaldehyde preservatives for metalworking fluids including monomethylol dimethyl hydantoin and dimethylol dimethyl hydantoin has also been proposed (see Bennett, E. O., Int. Biodetn. Bull. 9: 95-100 (1973) and Maeda et al, Agr. Biol. Chem., 40: 1111-2222 (1976)). 
     Gray and Wilkinson in J. Gen. Microbiol., 39: 385-399 (1965) and J. App. Bact., 28: 153-164 (1965) describe the action of the ethylenediaminetetraacetic acid (EDTA) on some bacteria. The effectiveness of such chelating agents as EDTA along for bacterial control in aqueous systems is disputed as evidenced by U.S. Pat. Nos. 3,240,701, 3,408,843, and 3,591,679. 
     The antimicrobial compositions used in metalworking fluids seem to suffer from one or more disadvantages including high cost, unacceptable toxicity or low degree of effectiveness at the present state of the art. 
     Considerable advantages would result if a coolant could be formulated with an ingredient which has several different functions in regard to metalworking while, at the same time, exhibiting antimicrobial properties to provide partial or complete rancidity control. In this way, it might be possible to partially control increasing costs of these lubricants, as well as provide increased life under industrial conditions. 
     Antimicrobial agents and corrosion inhibitors constitute two important ingredients of metalworking fluids which commonly are depleted faster than the other components of the products. Quite often, both of these materials must be added to a coolant at periodic intervals in order to compensate for their loss from the coolants. 
     Preservatives are removed from the fluid as the chemicals combine with the microbes to bring about their inhibition or death. The greater the microbial population, the more cuickly they are lost from the system. Thus, the concentration of any preservative declines with time and may be reduced to subinhibitory levels in only a few weeks. 
     Rust inhibitors have an ability to absorb to metal surfaces. They usually coat the metal being worked, as well as the surfaces of the machine and circulation system. They sometimes even prevent the coating of metals with the oils commonly encountered in cutting fluids. Thus, the concentration of the rust inhibitor in a cutting fluid also declines with time as it is removed from the system on the metal parts being worked. 
     It would be worthwhile then to search for chemicals which can function both as corrosion inhibitors, as well as antimicrobial agents. 
     SUMMARY OF THE INVENTION 
     The present invention provides an antimicrobial composition useful for inhibiting the growth of microorganisms in an aqueous medium susceptible to microbial growth. The method involves adding to the aqueous medium an antimicrobially effective amount of n-hexyl ethanolamine. N-hexyl ethanolamine, when added to an aqueous fluid medium, provides an unexpected degree of preservation and antimicrobial activity over what one would expect from results obtained by using the chemically close structural antimicrobial ethanolamine agents, 2-(N-amyl) ethanolamine and 2-cyclohexyl ethanolamine. 
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     The antimicrobial composition of the present invention comprises an antimicrobially effective amount of n-hexyl ethanolamine as the active antimicrobial ingredient. 
     Preparation of N-hexyl Ethanolamine 
     This procedure outlines the steps involved in ethoxylating n-hexyl amine to n-hexyl ethanolamine and n-hexyl diethanolamine. A suitable reactor must have cooling water, a heat source of 350° F., and pressure rating of 100 psig. The material of construction may be carbon steel, stainless steel, or glass-lined steel. 
     The reactor was charged with various weights of n-hexyl amine for 100 pounds of reaction product. See CHART I showing analysis of crude product versus charge weights of n-hexyl amine and ethylene oxide. The maximum n-hexyl ethanolamine production occurs at approximately a ratio of 70% n-hexyl amine and 30% ethylene oxide. The typical industrial n-hexyl amine raw material specification is as follows: 
     
         ______________________________________N--Hexyl AmineRaw Material Specification______________________________________n-Hexyl Amines   95.0%        min.Water            0.2%         max.Imines           0.2%         max.Other primary amines            4.0%         max.Unknowns without .6%          max.primary amines______________________________________ 
    
     
         __________________________________________________________________________CHART IETHOXYLATING n-HEXYLAMINEMolar Ratio  CHARGE PER            Analysis of Crude Productof Reactants  100 lbs. of Reactant            NHA      NHEA     NHDEA    HeaviesNHA EO lbs. NHA       lbs. EO            Wt %                Mole %                     Wt %                         Mole %                              Wt %                                  Mole %                                       Wt %                                           Mole %__________________________________________________________________________1   0.602  79.2 20.8 48  60   29  26   21  14   --  --1   1.004  69.6 30.4 30  42   34  33   33  25   --  --1   1.406  62.0 38.0 22  33   29  30   47  37   --  --1   1.900  54.7 45.3 3.2 5.8  9.1 11.4 85.6                                  82.8 --  --1   2.02  53.2 46.8 0.1 0.2  0.4 .5   90.6                                  93.9 6.4 5.4__________________________________________________________________________ Note: Weight and Mole % were based on uncorrected area % from GC data. As a result, NHEA and NHDEA are slightly understated. Response factors will be published later. 
    
     The reactor was pressured to 30 psig with nitrogen, then vented to 0 psig. This pressuring and venting cycle was repeated five times to remove all oxygen. Thereafter, the reactor vent was closed. 
     The n-hexyl amine was heated to 265° F., plus or minus 5° F. The pressure increased slightly to above atmospheric (about 15 psig). Next, ethylene oxide was added to the reactor. The reaction proceeded exothermicly to 310° F., plus or minus 5° F., at which point cooling was begun. (More than five percent of the ethylene oxide charge should not be added before the cooling procedure is begun.) The temperature of the reaction was controlled at 320° F., plus or minus 5° F., by the rate of ethylene oxide addition. The pressure was noted as between 30-60 psig. At the end of ethylene oxide addition, the temperature held at 320° F., plus or minus 5° F., for one hour. 
     Next, the reactor was cooled to below 150° F. The product was discharged to storage and the color protected with a nitrogen pad. 
     N-Hexyl Ethanolamine Purification 
     This procedure outlines the separation of n-hexyl ethanolamine from the crude reaction products of n-hexyl amine and ethylene oxide by distillation. The major components in feed to distillation included: water, n-hexyl amine, unknown lights, n-hexyl ethanolamine, n-hexyl diethanolamine, and heavy ethoxylated amines. 
     Crude reaction product was charged to a distillation unit. For ease of operation, suitable apparatus should contain at least ten theoretical trays. The product was protected with nitrogen; thereafter, a vacuum was pulled to 90 mmHg in an overhead condenser. Heating was begun at a reflux ratio of 1:1. The water, unknown lights, and free amines were removed. The vapor temperature in the overhead condenser was between 150°-160° F. The water came overhead at 150° F. and the amine at 160° F. The bottoms temperature remained below 350° F. to prevent cracking. 
     The boiling point difference between n-hexyl amine and n-hexyl ethanolamine is at least 200° F. at reduced pressures. Essentially, complete removal of the amine was indicated by a quick temperature rise from 160° F. to 200° F. in the overhead condenser. 
     When the overhead temperature rose to about 200° F., the batch pot composition was confirmed by gas chromatography. The ratio of n-hexyl amine to n-hexyl ethanolamine was less than 0.004. The water content was less than 0.1% by Karl Fisher. 
     After the n-hexyl amine was removed from the batch pot, heating was stopped and the pressure reduced to 50 mmHg. After pressure reached 50 mmHg, the heating began to 302° F., plus or minus 5° F., and reflux maintained at 1:1 ratio. N-hexyl ethanolamine was removed overhead as a product and protected with nitrogen, then analyzed by gas chromatography. 
     
         ______________________________________N--HEXYLETHANOLAMINEC.A.S. REGISTRY NO. 54596-69-9______________________________________SpecificationsN--Hexylethanolamine             98.0% min. by weightWater             0 5% max.Color             50 APHA max.Appearance        Clear liquid, free of             suspended matter.Typical AnalysisProperties        ValueBoiling Point (at 20 mm Hg.)             133° C.Molecular Weight  145CompositionTotal Hexyl Ethanolamine             98.5%N--n-Hexyl ethanolamine             94-97%Other C.sub.6 ethanolamines             3-8%Water              0.2%n-Hexylamine      0.2-0.4%Volatiles         0.1-0.2%Hexyl diethanolamine             0.8-1.0%and heavier ethoxylates______________________________________ 
    
     Alternate N-Hexyl Ethanolamine Synthesis Scheme 
     In an alternate synthesis scheme for n-hexyl ethanolamine, the ethoxylation steps remained the same as above in sequence, temperature and pressure. However, the preferred weight fraction of n-hexyl amine to ethylene oxide was lowered to approximately 88 pounds n-hexyl amine to 12 pounds ethylene oxide to yield 100 pounds of reaction mass. The weight ratio of mono to di ethoxylates in the reaction mass was approximately 4.0-4.2 mono to 1.0 di. The purification section was also the same except the process was stopped after removal of n-hexyl amine overhead. The final bottoms fraction contained n-hexyl ethanolamine and some diethoxylates byproducts (less than 20% by weight). 
     Antimicrobial Compositions 
     In use, the n-hexyl ethanolamine antimicrobial composition is added to an aqueous fluid medium as a solution. 
     In order to achieve practical level of inhibition of microorganism growth in the aqueous fluid medium, it is necessary to include therein the n-hexyl ethanolamine in an amount sufficient to inhibit the growth of microorganisms. As used herein, the term &#34;antimicrobial amount&#34; is to be understood as that amount of n-hexyl ethanolamine which, when added to an aqueous fluid medium, will acceptably inhibit the growth of microorganisms in the use of said medium. 
     Generally at least 1000 parts of the n-hexyl ethanolamine are added per million parts of the aqueous fluid medium. Amounts ranging from about 1000-4000 parts by weight of n-hexyl ethanolamine per million parts by weight of the aqueous fluid medium provides effective antimicrobial activity. 
     As used herein, the term &#34;aqueous fluid medium&#34; is meant to encompass water, oil in water, water in oil emulsions (including concentrates) and like compositions susceptible to the infestation and growth of microorganisms. Thus, for instance, metalworking fluids or cutting oil fluids (in diluted as well as undiluted form), together with conventional additives such as corrosion inhibitors, etc., are included. 
     The antimicrobial compositions may be added directly to undiluted metalworking fluids. As used herein, the term &#34;metalworking fluid&#34; is intended to encompass those compositions known in the art as &#34;metal cutting fluids&#34;, &#34;cutting fluids&#34;, &#34;coolants&#34;, &#34;lubricants&#34;, &#34;rolling oils&#34;, &#34;drawing fluids&#34;, &#34;mold release fluids&#34;, &#34;grinding fluids&#34; and like products used in the processinc of metals as described more fully by Springborn, R. K. &#34;Cutting and Grinding Fluids&#34;: Selection and Application, ASTME (1967) and Wilbert J. Olds, &#34;Lubricants, Cutting Fluids and Coolants&#34;, Cahner&#39;s Books, the entire contents of each being incorporated herein by reference. Emulsifiable or water miscible oils are widely used in the industry. Mixed with water, they form emulsions for use in rolling, drawing, machining and grinding where the need is for both cooling and lubrication. More recently, water miscible fluids using less oil (or no oils) and based on chemicals with or without surface active agents, have provided industry with products of even greater heat conducting properties for still higher machining rates. 
     The following examples are offered in order to more fully illustrate the invention, but are not to be construed as limiting the scope thereof. 
     Experimental Procedures 
     The test units consisted of quart jars placed in rows. Above each row, a metal framework was constructed to support the aeration system which consisted of aquarium valves connected together with plastic tubing. The amount of aeration of each unit was controlled by adjusting the valves. Capillary pipettes were employed as aerators to produce a fine steam of bubbles in the diluted coolants. 
     Five hundred ml of tap water (120 ppm hardness) was added to each jar. The n-hexyl ethanolamine was added to each jar along with 15.0 ml of coolant concentrate to produce the desired coolant concentration. Each unit was then made up to a total volume of 600.0 ml by adding additional tap water. 
     Each test unit was inoculated with a mixture of bacteria and fungi which were obtained and maintained as described in Bennett, &#34;The Deterioration of Metal Cutting Fluids&#34;, Prog. Indust. Microbiol. 13: 121-249 (1974), the entire contents of which are incorporated herein by reference. Each unit was inoculated once each week with 1.0 ml of a 50-50 mixture of both inocula. 
     Each unit was examined once each week for its microbial content for as long as the count remained below 100,000 organisms/ml. Two consecutive counts in excess of this figure at weekly intervals was considered to constitute a failure and the test was discontinued at that time. In addition, all units which contained less than 100,000 organisms/ml were studied for a 182-day test period and discarded at that time. 
     Two different types of control experiments were included. Each shipment of fresh coolant was tested upon arrival to determine if the product exhibited any inhibitory properties, as defined in the previous paragraph. All of the coolants used in the investigation were especially prepared by coolant manufacturers for this work and they did not contain a preservative. None of the products employed in this investation exhibited any inhibitory properties and failed in the first week of testing. The second set of controls consisted of a particular cutting fluid preserved with a commonly used cutting fluid preservative. Normally, these control units fail in 21 to 28 days due to mold growth and have done so for the past several years. The controls functioned normally during the test period. 
     Since the test units were under constant aeration, there was considerable evaporation from each unit. The units were calibrated at the 600.0 ml mark and, once or twice each week, depending upon environmental conditions, distilled water was added to each unit to bring the liquid level back to this mark. Distilled water was used in order to avoid a buildup of inorganic salts in the test units. 
     Results 
     A series of sample jars were prepared according to the procedure outlined above to ascertain the antimicrobial effects of n-hexyl ethanolamine made according to the alternate synthesis scheme described above. The sample coolants were mixed with water in a ratio of 1:40 (coolant to water). The results are set forth in CHART II below, wherein the time in days is recorded when the count in such test reached the level of 100,000 or the test discontinued. 
     
         ______________________________________CHART IIANTIMICROBIAL EFFECTIVENESS OFN--HEXYL ETHANOLAMINE IN CUTTING FLUIDS        CONCEN-        TRATION        (PPM)        DAYS OF TESTING        OF N--HEXYL  BEFORE COUNTS        ETHANOL-     EXCEEDED 100,000PRODUCT      AMINE        ORGANISMS/ML______________________________________1.  Anderson Lusol            1500         28            2500         1142.  Anderson     2500         14    Shamrock3.  Applied      2500         70    Chemicals 1-144.  Ashland Adcool            1500          0    2            2000         182*5.  Ashland Adsol            2500         182*    36.  Baum&#39;s Macson            2500         182*    4357.  Baum&#39;s ProSol            2500         182*    K-428.  Berocut 8501 2500         709.  Berocut 8503 2500         182*10. Buckeye      2000         365*11. Castrol 7100 2500         5612. Celanese 2J20            2500         182*13. Chemtool 174 2000         1414. Chemtool 250 1500         14            2500         16115. Chemtrend    1500         98    CT-54016. Cimcool Five 2500         182*    Star17. Cimcool (H)  2500         5618. Conoco OS    2500         Sample lost at    547L                      49 days19. Cook Coolex  2500         182*    4020. Dober Lub A  2500         6321. Dober Lube B 1500          0            2000         1422. Emory 2885   2000         9823. Emory 2885-A 2000         2824. Etna Master  2500         63    Draw A25. Etna Master  2500         49    Draw B26. Exxon Kutwell            1500          0    40           2500         5627. Exxon Kutwell            2500         182*    24028. Gulfcut H.D. 2500         182*29. Hodson EZ    2500         182*    Cool 85030. Houghton     2500         161    1133-4131. IRMCO emulsion            2000         24532. IRMCO 103    2500         182*33. Ironsides    2000         182*34. Ironsides 381            2500         9835. Ironsides 379            2500         182*36. S. C. Johnson            1500         70    511337. Larson PL 95K            2500         182*38. S. H. Mack   1500          0    PTL 4184     2000         11239. Master Trim  2500         182*    Regular40. Mobil P-174  1500         91            2000         11241. Mobil        2500         182*    Emulsilube42. Monroe       2500         365*    Primecut (Old)43. Monroe       2500         182*    Primecut (New)44. Monroe Choice            2500         182*    Cut45. Nalco XL174-L            2500         4946. Oil Craft    1500          0            2500         1447. Petron 54-4  1500          048. Petron II 54-4            2500         182*49. Petron K.sub.3 -4            2500         182*50. Polar Chip   2500         182*51. Process      2500         91    Research    Products52. Quaker coolant            1500          0            2000         182*53. Rust Lick    2500         182*    Alucut WS54. Rusk Lick 600B            2500         4255. Sanson       2500         182*    emulsion56. Shell Dromus B            1500          057. Shell DM     2500         42    soluble 250058. Sintolin E   2500         1459. Sintolin S   2500         182*60. D. A. Stuart 2000         245    emulsion61. Sun Seco     2500         182*62. Tapmatic Mole-            2500         182*    cular Edge II63. TCI 4800     2500         182*64. TCI 3900     2500         182*65. Tower A-1344 2500         16166. Tower W-2122 2500         182*67. Union 501    1500          0            2500         4268. Union Soluble            2500         182*    1069. Vantrol      2000         365*70. Vasu soluble 2500         2171. White &amp; Bagley            2500         182*    X-586472. Yusiro A     2500         182*73. Yusiro B     2500         182*______________________________________ *Still inhibitory when taken off test or at time of report. 
    
     Test failures in less than 60 days or less were considered unacceptable from the standpoint of potential industrial and commercial applications. 
     On reviewing previous experiments of tested ethanolamines, the presently tested n-hexyl ethanolamine exhibited unexpectedly high antimicrobial activity as compared to the chemically close structurally related compounds: 2-(N-amyl) ethanolamine and 2-cyclohexyl ethanolamine. The antimicrobial test results of several ethanolamine compositions have previously been reported in Bennett, &#34;Corrosion Inhibitors as Preservatives for Metal Working Fluids--Ethanolamines&#34;, J. Amer. Soc. Lubri. Engin. 35: 137-144 (1979), the entire reference of which is incorporated herein by reference. 
     The antimicrobial composition formulations of the present invention are particularly attractive due to the low toxicity of their components when present in the amounts indicated. Furthermore, while prior known antimicrobial formulations appear to be effective at best in only about 42% of the commercially available metalworking fluids, the formulations of the present invention are more universally effective. 
     While the invention has been explained in relation to certain illustrative embodiments of it, it is understood that many modifications and substitutions may be made in any of the specific embodiments within the scope of the appended claims which are intended also to cover equivalents of them. Furthermore, the invention may comprise, consist or consist essentially of the herein recited steps and materials.