Abstract:
A filter system for receiving an oil-in-water emulsion contaminated with an emulsified contaminant oil, and separating the emulsified contaminant oil from the oil-in-water emulsion includes a filter media for receiving the oil-in-water emulsion and emulsified contaminant oil, having an inner filter element formed from a 95 percent single pass efficiency 48 micron (5 micron nominal) filtering material of needle punch polypropylene felt, an outer filter element formed from a 95 percent single pass efficiency 19 micron absolute filtering material of a polypropylene microfiber material and a porous spunbond polypropylene sandwiching the outer filter media. The filter element de-emulsifies the emulsified contaminant oil from the oil-in-water emulsion into the contaminant oil and the oil-in-water emulsion, separates the de-emulsified contaminant oil from the oil-in-water emulsion, coalesces the separated contaminant oil and passes both the coalesced de-emulsified contaminant oil and the oil-in-water emulsion. A first tank supports the filter element and is further configured to hold a quantity of the separated coalesced contaminant oil and the oil-in-water emulsion. The first tank has an overflow passing to a second tank. The second tank has an oil separation assembly for removing the oil-in-water emulsion from the contaminant oil and passing the oil-in-water emulsion therefrom. A method for separating the emulsified contaminant oil from the oil-in-water emulsion and recovering the oil-in-water emulsion is also disclosed.

Description:
CROSS-REFERENCE TO RELATED APPLICATION DATA 
     This application claims the benefit of priority of U.S. Provisional patent Application Ser. No. 60/367,441, filed Mar. 25, 2002. 
    
    
     BACKGROUND OF THE INVENTION 
     The present invention is directed to a particle filtration, oil de-emulsifying, oil coalescing and oil collecting system. More particularly, the present invention is directed to a particle filtration, oil de-emulsifying, oil coalescing and oil collecting system that uses a needle punch polymer primary filter and a microfiber polymer secondary filter in a coiled tubular arrangement. 
     Devices, systems and methods for the removal of particles, free oil (such as dispersed, finely divided oil droplets), and emulsified oil contaminants in aqueous fluids is in widespread use in all types of commercial and industrial facilities. Known devices include cartridge and bag filters either permanently installed or as a part of portable systems, conventional oil coalescing systems that require many stages, baffles, filters, and weirs to coalesce and then separate and accumulate the coalesced oil, membrane filtration systems that concentrate emulsified oils and particles in an aqueous fluid for disposal, and conventional oil skimmers that remove oils in aqueous fluid sumps or baths after the oil droplets begin to coalesce due to time and gravity. Known methods include periodically pumping out the old fluid and pumping in new coolant 
     However, each of these known systems has its drawbacks. For example, cartridge and bag filters are subject to blinding by oil emulsions and contaminants and require high pressure pumps and housings. Oil coalescing systems are relatively expensive and difficult to clean and usually require a relatively large dedicated floor space, and do not remove emulsified tramp oils. 
     Membrane filters are unreliable due to their sensitivity to fouling by various contaminants and damage by pH and temperature. Membrane filters remove coalesced oils by holding back the oil and allowing aqueous fluids to pass through the filter. This concentrates the emulsion on one side of the membrane. As the concentration of oil increases, the efficiency of the filtration system decreases (due to increased resistance across the membrane) and the membrane becomes increasingly susceptible to fouling. 
     Periodic change-out of the coolant results in labor time and costs, machine down-time, coolant costs and disposal costs. Moreover, once the coolant is changed, it begins accumulating unwanted contaminants such that the quality of the coolant continually degrades until the next change-out. 
     Various attempts have been made to reduce fouling in membrane filters. These include using spinning discs near the surface of the membrane; however, these disks require relatively large amounts of energy and generate heat in the fluid. Moreover, membrane pore sizes are such that bacteria concentrates with the emulsion. The heat generated from the antifouling mechanisms tends to colonize bacteria and create offensive odors. Further, membrane filtration systems cannot be used to filter emulsified oil coolants for reuse because the membrane blinds (clogs or fouls) when it is used to filter out finely divided oil-in-water emulsions. 
     With respect to oil-in-water emulsions, these are liquid systems that are particularly difficult to filter. Such liquid systems include, for example, coolant systems having a (desired) oil droplet “surrounded” by coolant. That is, the oil-in-water forms a micelle-like liquid system with a desirable oil in the nucleus of the micelle and the coolant surrounding the oil nucleus. The “desirable” oil may be, for example, a particular lubricating oil. In such systems, tramp oils such as (other, undesirable) lubricating oils, hydraulic fluids and part coating oils (collectively contaminants) maybe present in the coolant system. These contaminants adhere or attach to the outer liquid of the system. It is these contaminants that must be removed, without removing the desirable oils. 
     Oil skimmers are essentially a remediation strategy to remove unwanted oils after they have become a problem. Floating oils typically prevent the movement of oxygen and create an environment for the cultivation of anaerobic bacteria. Floating oils can also form dry floating patches of material that are not effectively picked up by conventional skimming techniques. However, oil skimmers do not remove emulsified tramp oils. The emulsified oils can also become food to cultivate bacteria as well as change the cooling and machining enhancement properties of the coolant. 
     Accordingly, there is a need for a filter system that is less susceptible to fouling and that can remove unwanted contaminants. Desirably, such a filter system is configured to allow contaminants to first pass over a used area of the filter prior to exposing the contaminants to unexposed areas of the filter. Most desirably, such a filter system increases the ability of oil and particulate contaminants to be removed without prematurely blinding the filter media. Such a system most desirably operates at low pressure differentials to promote high efficiency and to eliminate the need for high pressure pumps and additional structural elements to support these higher operating pressures. 
     BRIEF SUMMARY OF THE INVENTION 
     A filter system for receiving an oil-in-water emulsion contaminated with an emulsified contaminant oil, and separating the emulsified contaminant oil from the oil-in-water emulsion includes a filter media for receiving the oil-in-water emulsion and emulsified contaminant oil. The filter media has an inner filter element formed from a 5 micron nominal, 48 micron 95 percent efficiency single pass filtering material of needle punch polypropylene felt, an outer filter element formed from a 19 micron 95 percent efficiency single pass filtering material of a polypropylene microfiber material and a porous spunbond polypropylene surrounding the outer filter media. 
     The filter element de-emulsifies the emulsified contaminant oil from the oil-in-water emulsion into the contaminant oil and the oil-in-water emulsion, coalesces the de-emulsified contaminant oil, separates the coalesced de-emulsified contaminant oil from the oil-in-water emulsion, and passes both the coalesced de-emulsified contaminant oil and the oil-in-water emulsion. 
     A first tank supports the filter element, The first tank is further configured to hold a quantity of the coalesced de-emulsified contaminant oil and the oil-in-water emulsion. The first tank includes an overflow passing to a second tank. 
     The second tank has an oil separation assembly for removing the oil-in-water emulsion from the contaminant oil and passing the oil-in-water emulsion therefrom. In a present system, the oil separation assembly includes a vertical conduit extending to about a bottom of the tank and a tee in flow communication with the vertical conduit. The tee provides flow communication from the second tank such that the oil-in-water emulsion flows upward into the vertical conduit, into the tee and out of the second tank. The lighter coalesced oil, however, floats on top of the oil-in-water emulsion in the second tank and is precluded from exiting the second tank until the oil depth exceeds the depth of the vertical conduit. 
     Preferably, the oil-in-water emulsion is recovered and reused. The contaminant oil is also recovered for subsequent treatment and/or disposal. 
     The filter system can include an over-pressurization arrangement to prevent over-pressurizing the filter media. 
     In a present filter system, an optional pre-separation system is disposed prior to the first tank. The pre-separation system separates contaminant oil (e.g., tramp oils “floating” on the surface) from the oil-in-water emulsion that is contaminated with the emulsified contaminant oil. A present separation system is a belt skimmer. 
     A method for separating an oil-in-water emulsion from a liquid system having an oil-in-water emulsion contaminated with an emulsified contaminant oil includes the steps of introducing the oil-in-water emulsion contaminated with the emulsified contaminant oil through a filter media to form an oil-in-water emulsion and a separated contaminant oil stream, passing the oil-in-water emulsion through the filter media, passing the contaminant oil through the filter media, separating the oil-in-water emulsion from the contaminant oil and recovering the oil-in-water emulsion. 
     The present systems use the natural ability of the coiled tubular filter configuration to de-emulsify and coalesce oils and makes use of gravity to facilitate separating and accumulating the coalesced oils, in a container, for ease of removal. A present system can be provided in a modular design having a relatively small footprint, which provides a cost effective, machine-dedicated system for example, for parts cleaners, machine tools and the like. Moreover, the present coalescing/de-emulsifying coiled tubular filter system is less susceptible to fouling and bacteria colonization than membrane filters because the coalesced oil, aqueous fluid, and any bacteria pass through the filter. 
     These and other features and advantages of the present invention will be apparent from the following detailed description, in conjunction with the appended claims. 
    
    
     
       BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS 
       The benefits and advantages of the present invention will become more readily apparent to those of ordinary skill in the relevant art after reviewing the following detailed description and accompanying drawings, wherein: 
         FIG. 1A  illustrates the phenomena of de-emulsifying, filtration and coalescing as carried out by the present filter system; 
         FIG. 1B  illustrates an exemplary arrangement for use of the filter system; 
         FIGS. 2 and 3  are plan and elevational views of one embodiment of the coalescing/de-emulsifying coil tubular filter embodying the principles of the present invention; 
         FIG. 4  is a partial view of the filter system illustrating one way in which the filter media can be connected to the overall system; 
         FIGS. 5A-5E  are still other views of the filter illustrated in cross-section and showing various alternate seam arrangements; 
         FIG. 6  illustrates the de-emulsifying/coalescing coil tubular filter used in a dialysis configuration; 
         FIG. 7  illustrates the de-emulsifying/coalescing coil tubular filter used in a recirculating reuse configuration; 
         FIG. 8  illustrates the de-emulsifying/coalescing coil tubular filter is used in a recirculating discharge configuration; 
         FIG. 9  illustrates the de-emulsifying/coalescing coil tubular filter used in a dialysis and recirculating configuration; 
         FIG. 10  illustrates the de-emulsifying/coalescing coil tubular filter used in an inline discharge configuration; and 
         FIG. 11  illustrates a portable, compact, filly contained embodiment of the filter system of the present invention. 
     
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     While the present invention is susceptible of embodiment in various forms, there is shown in the drawings and will hereinafter be described a presently preferred embodiment with the understanding that the present disclosure is to be considered an exemplification of the invention and is not intended to limit the invention to the specific embodiment illustrated. 
     It should be further understood that the title of this section of this specification, namely, “Detailed Description Of The Invention”, relates to a requirement of the United States Patent Office, and does not imply, nor should be inferred to limit the subject matter disclosed herein. 
     Referring now to the figures, and in particular to  FIGS. 1B ,  4 ,  6  and  11 , there is shown a one embodiment of a coalescing/de-emulsifying coiled tubular filter system  10 . The system  10  is configured to receive a contaminated liquid stream, such as an oil-in-water emulsion, de-emulsify the contaminants from the emulsion and pass both the contaminants and the emulsion through a filter  12 , such that the contaminants and the emulsion remain separated from one another with the contaminants being coalesced and passed as seen in  FIG. 1A . 
     The coalescing/de-emulsifying coiled tubular filter system  10  includes the coiled tubular filter  12  media having an inlet fitting  8  and an outlet fitting  16  connected to the tubular filter  12  media at each end. The fittings  8 ,  16  can be connected by, for example, conventional hose clamps. The inlet fitting  8  connects the coiled tubular filter  12  to the fluid to be filtered. The outlet fitting  16  connects a filter change indicator  18  which is formed from of a length of tubing having an open end elevated a predetermined distance above the filtered fluid. Optionally, and preferably, a pressure gauge and bypass and/or relief valve is used. The change indicator  18  provides a controlled backpressure to the filter  12 , a visual and measurable indicator of backpressure, and a bypass to maintain fluid flow and prevent over pressurizing the filter element. Again, optionally and preferably, a pressure gauge and bypass is used to prevent over-pressurization. 
     Referring to  FIG. 4 , the coalescing/de-emulsifying coiled tubular filter  12  includes an inlet hose  14 , hose to thread adapter  20 , thread to pipe adaptor  22 , inlet hose clamp  24 , tubular filter material  26 , outlet hose clamp  28 , outlet pipe to thread adaptor  30 , outlet thread to hose adapter  7 , bypass pressure relief tube  34 , and bypass pressure relief opening  36 . Preferably, as set forth above, instead of the tube  34  and opening  36  arrangement, a pressure gauge and relief valve (not shown) are used to prevent system  10  over-pressurization. A cross-sectional view of the filter shown in  FIG. 5B  illustrates the normal shape of the tube filter  12  as a collapsed flat. The tube  12  is made by folding one or more strips of material or materials and either heat sealing or sewing the edges  38  to one another.  FIG. 5C  shows an alternate construction in which two strips of material are either heat sealed or sewn along both edges  38   a  and  38   b . The double edge construction provides a stronger bias to maintain the two surfaces of filter material together. 
       FIG. 5A  illustrates a cross-sectional view of one embodiment of the coalescing/de-emulsifying coiled tubular filter  112 . The filter  112  is formed having an inner filter  112   a  and an outer filter  112   b . In a current embodiment, the inner filter  112   a  is fabricated from a 48 micron 95 percent efficiency single pass (5 micron nominal) needle punch polypropylene material, and the outer filter  112   b  is made out of a 19 micron 95 percent efficiency single pass microfiber polypropylene that is sandwiched between layers of spunbond polypropylene to retain any loose microfibers. The layers of filter media  112   a ,  112   b  are formed into a tubular configuration by joining the longitudinal edges  138  to one another and forming a seam. In the present embodiment, the seam is a standard industrial sewn seam. However, other seaming methods such as gluing, ultrasonic welding, vibratory friction welding, heat welding and the like are contemplated. An exemplary microfiber material is commercially available from AET Specialty Nets &amp; Non-Woven of Middletown, Del. The outer filter inner and outer covers are spunbond polypropylene commercially available as Snopro 8 and Snopro 20, respectively, from Snow Filtration of West Chester, Ohio. The materials are ½ ounce and 2 ounce weight, respectively. 
       FIGS. 5D and 5E  illustrate still other alternate seam seals that are used to prevent leakage through the seam holes. When the filter  12 ,  112  becomes pressurized the forces are such that the seam threads may start to elongate the thread holes, thus creating a small leak path.  FIG. 5E  shows an embodiment in which the seam seal is a triple folded strip of polyethylene film (about 6 mil ( 6/1000) inch thick) that is sandwiched between the two layers of the inner filter.  FIG. 5D  shows an embodiment in which a strip of polyethylene is wrapped over the seam of the inner filter. In both embodiments, the seal strip material is sufficiently elastic to seal around the seam threads. The strips are located such that they “float” and are unaffected by the stresses in the filter media when the filter becomes pressurized. 
     In a present embodiment, the coalescing/de-emulsifying coiled tubular filter  12 ,  112  has ¼″ ID×⅜″ OD high density polyethylene (HDPE) tubing  40  running almost all of its length. The filter tubing  40  is approximately 8″ shorter than the coalescing/de-emulsifying tubular filter  12  media to allow for the attachment of the inlet fitting  8  and outlet fitting  16 . In the preferred embodiment, the filter tubing  40  has a natural coiled shape to impart a coiled shape to the coiled tubular filter  12  media. The filter tubing  40  also prevents the coiled tubular filter  12  media from kinking. The inner filter  112   a  removes particles and absorbs free floating oils to prevent premature blinding of the much finer outer filter  112   b.    
     The inner filter  112   a  has a 95 percent single pass filtration efficiency of 48 microns and the outer filter  112   b  has a 95 percent single pass filtration efficiency of 19 microns. Finally, the outer filter  112   b  is made out of a material capable of adsorbing and coalescing water-in-oil emulsions (dark colored fluids) while passing oil-in-water emulsions (milky colored fluids). 
       FIG. 6  illustrates a dialysis configuration  50  of the coalescing/de-emulsifying coiled tubular filter system  12 ,  112 . The dialysis configuration  50  is typically the configuration that is used for filtering particles and de-emulsifying and coalescing unwanted emulsified oils in a coolant sump and parts cleaning systems. The dialysis configuration  50  includes a coalescing tubular filter reservoir  52  that houses the coalescing/de-emulsifying coiled tubular filter  12  and that empties into an oil/water separator reservoir  54 . The fluid in the oil/water separator reservoir  54  passes through an oil trap back to the fluid reservoir  56  containing the fluid being filtered. In a present embodiment, the filter reservoir  52  and the oil/water separator  54  are 6-gallon containers. The oil/water separator  54  is a translucent plastic material to provide visual indication of the level of any floating oil and accumulated sediment inside. 
     A pump  58  in the fluid reservoir delivers fluid to the inlet end  14  of the coalescing/de-emulsifying coiled tubular filter through a flow restrictor  60  and a shutoff valve  62 . The flow restrictor  60  is used to establish a desired flow rate. The shutoff valve  62  is used to stop flow to the coalescing/de-emulsifying coiled tubular filter  12  during change-out or maintenance of the filter  12  media. The pump  58  can be a dedicated pump. Alternately, the fluid can be split from a machine fluid recirculating system, such as a parts cleaner fluid, machine tool coolant, or the like. 
     Fluid that is pumped into the deemulsifying/coalescing coiled tubular filter  12  passes through the deemulsifying/coalescing tubular filter media which traps particles, absorbs oils, and de-emulsifies and coalesces water-in-oil emulsions, while passing the desired oil-in-water emulsions. The coalesced oil from the coalescing/de-emulsifying tubular filter media overflows into the oil/water separator  54  where the oil is trapped by the oil trap  57  and the aqueous fluid passes on to the fluid reservoir  56 . The oil trap  57  consists of a tee fitting  64  with an upper pipe  66  and lower pipe  68 . The upper pipe  66  acts as a vent to prevent the fluid in the oil/water separator  54  from being siphoned into the fluid reservoir  56 . The lower pipe  68  prevents floating oil from passing into the fluid reservoir  56 . The filter change indicator  18  shows whether the tubular filter media needs to be changed. As the coalescing/de-emulsifying tubular filter  12 ,  112  media begins to blind, fluid rises in the filter change indicator providing a backpressure to help force fluid through the coalescing/de-emulsifying tubular filter  12 ,  112  media. Higher elevation of the filter change indicator  18  provides a higher backpressure that can be achieved before the fluid exits the change indicator tube  34  into the filtered fluid. The fluid change indicator  18  helps to assure that the coiled tubular filter  12 ,  112  media is optimally used prior to changeout. A pressure gauge and relief valve (not shown) can be used to monitor pressure in the filter system  10  and to prevent over-pressurization of the system  10 . As necessary, the filtration system  10  may be raised to allow gravity flow back to the fluid reservoir  56 . 
       FIG. 7  illustrates a recirculating reuse configuration  76  that includes a dirty fluid reservoir  78  that collects dirty fluid from sources such as floor cleaning machines  80 , mop buckets  82 , or any other aqueous process waste requiring removal of particulate and emulsified oils. The fluid in the dirty fluid reservoir  78  is transferred into the oil/water separator reservoir  84  by, for example, a pump  86  which is controlled by a dirty fluid level switch  88  and flow control valve. The fluid in the oil/water separator reservoir  84  passes through an oil/water separator oil trap  90 , through a flow control valve  92 , into the coalescing/de-emulsifying coiled tubular filter  12 ,  112  inside the filter container, which is exemplified by the dialysis system  50  configuration. Fluid in the oil/water separator reservoir  84  also overflows any accumulated floating oil back to the dirty fluid reservoir  78  via an oil/water separator reservoir overflow  94 . 
     The fluid in the coalescing/de-emulsifying coiled tubular filter system  50  passes through the walls of the coalescing/de-emulsifying tubular filter  12 ,  112  media which traps particles, absorbs oils, and de-emulsifies and coalesces water-in-oil emulsions as provided above. The oil coalesced by the tubular filter  12 ,  112  media overflows to the oil/water separator  54  via the coalescing coiled tubular filter container overflow  67 . Referring to  FIGS. 6 and 7 , the filtered fluid pump  96  (which replaces pump  58 ) transfers filtered fluid from the transfer container  56  to the filtered fluid reservoir  98 . A filtered fluid level switch turns off the filtered fluid pump  96  when the fluid level drops below a preset level. 
     A flow control valve controls the rate of transfer of filtered fluid from the transfer container  56  to the filtered fluid reservoir  98 . Excess fluid in the filtered fluid reservoir  98  returns to the dirty fluid reservoir  78  by way of a filtered fluid reservoir overflow  100 . The filtered fluid reservoir overflow  100  provides continuous recirculation to aerate the liquid. Aeration reduces the opportunity for bacterial growth and the overflow  100  returns any additional oil separation in the filtered fluid reservoir to the dirty fluid reservoir. A drain valve  102 , connected to a filtered fluid oil trap  104 , is used to dispense filtered fluid into a mop bucket  106 . A filtered fluid reservoir pump  108  with a shutoff valve and electrical on/off switch is used to dispense filtered fluid into floor cleaning machines. 
     The oil that accumulates in the dirty fluid reservoir  78  is removed by a belt skimmer  110  that transfers the oil into the used oil reservoir  113 . Any dirty aqueous fluid picked up by the belt skimmer  110  is returned to the dirty fluid reservoir  78  through an oil trap  114 . The oil trap has a lower tube which prevents oil from flowing into the dirty fluid reservoir. The oil trap has an upper tube that is a vent to prevent siphoning. A fluid change indicator  18  or pressure gauge and bypass can be used to monitor system pressure and to prevent over-pressurization of the system. 
     The present configuration provides that any oils that are separated in any of the containers (oil/water separator reservoir  84  and filtered fluid reservoir  98 ) are automatically returned to the dirty fluid reservoir  78  where the belt skimmer  110  transfers the oil into the used oil reservoir drum  112  for easy removal. If necessary, a biocide such as a 0.1% solution of Proxyl GXL is used to prevent bacteria growth. 
       FIG. 8  illustrates an embodiment of the coalescing/de-emulsifying coiled tubular filter system, again, exemplified by the system configuration  50 , in which processing of waste water, such as mop water, is carried out for subsequent discharge to, for example, a sanitary sewer for further processing at a local Publicly Owned Treatment Works (POTW). Typically, POTW&#39;s have discharge concentration limits in the 250-500 mg/l range for fats, oils, and greases (FOG) usually requiring processing of waste waters from floor cleaning prior to discharge to the sanitary sewer. The inline configuration for discharge is similar to the configuration shown in  FIG. 7 , the filtered fluid reservoir and related components have been eliminated. In  FIG. 8  it can be seen that the dirty fluid in the oil/water separator reservoir  120  passes through the filtration system (see  FIG. 6 ) before passing through a discharge valve  122  to the sewer  124 . The oil/water separator reservoir  120  has an oil trap  51  that includes a lower tube with an opening near the bottom of the oil trap canister to prevent floating oil from being discharged to the sewer. The oil trap  51  also has a vent to prevent siphoning fluid from the oil/water separator reservoir  120 . 
       FIG. 9  illustrates an embodiment of the coalescing/de-emulsifying coiled tubular filter system again exemplified by the system configuration  50 , that provides continuous dialysis filtration, similar to that of  FIG. 6  while recirculating filtered fluid back to the process from where the fluid is supplied. A vibratory finishing process  130  is illustrated as but one exemplary process, however, other processes such as parts cleaning and the like that can uses such a system will be recognized by those skilled in that art. The function of the various components in the dialysis mode of filtration  50  is the same as that described in reference to the dialysis configuration above shown in  FIG. 6 .  FIG. 9  shows that an inline function is achieved through the addition of a filtered fluid pump  132  in the filter canister  54  (see  FIG. 6 ) and a flow control on an end of a hose that returns the filtered fluid to the exemplary vibratory finishing machine  130 . The vibratory finisher  130  drains into the dirty fluid reservoir  134  to complete the fluid circuit. The dialysis mode flow rate is the difference between the sump pump  136  flow rate into the coalescing/de-emulsifying tubular filter  12 ,  112  and the return flow rate through the flow control back to the vibratory finisher  130 . 
       FIG. 10  shows an embodiment of the coalescing/de-emulsifying coiled tubular filter  12 ,  112  that is used to process fluid in a single pass for discharge to a sanitary sewer  140  for further processing by, for example, the local POTW. A typical application is processing air compressor condensate which can contain significant amounts of oil in excess of POTW discharge limits. A waste fluid stream  142  enters the accumulation drum  144 . Fluid in the accumulation drum  144  overflows into the coalescing tubular filter reservoir  146  (see also  52  in  FIG. 6 ) through a shutoff valve  148 . Operation is identical to that described above in reference to the dialysis configuration illustrated in  FIG. 6 , except that there is no recirculating pump circuit and associated components (flow restrictor and shutoff valve), and the output through the outlet on the oil/water separator reservoir  54  discharges to the sewer  140  rather than back to the fluid reservoir. In the event that the coiled tubular filter blinds before changeout, the change indicator will go into a bypass mode. 
       FIG. 11  illustrates one embodiment of the filter system  10  that is configured as a compact, self-contained unit  50 . The filter system,  10  includes the coiled filter  12  present in the filter reservoir  52 . The flow restrictor  60  and shut-off valve  62  are positioned at about an inlet of the reservoir  52 . The coalesced oil from the coalescing/de-emulsifying tubular filter overflows into the oil/water separator  54  through overflow  67  where the oil is trapped by the oil trap  57 . The oil trap  57 , as set forth above, includes a tee fitting  64  with an upper pipe  66  and lower pipe  68 . The upper pipe  66  acts as a vent to prevent siphoning fluid from the oil/water separator  54 . The lower pipe  68  prevents passage of floating oil. The filter change indicator  18  includes a pressure gauge (e.g., 0-5 psig) which shows whether the tubular filter media needs to be changed. As the coalescing/de-emulsifying tubular filter  12 ,  112  media begins to blind, fluid pressure rises providing a backpressure to help force fluid through the filter  12 ,  112  media. A bypass valve  19  vents fluid into the reservoir  52  through opening  21  when the pressure in the filter exceeds a predetermined set point (e.g., about 2 psig). The coiled filter  12 ,  112  is still de-emulsifying, coalescing and filtering, because emulsified oil and particles are required to traverse the complete length of the filter before being able to exit through the bypass opening  21 . 
     The overflow from the reservoir  52  to the separator includes a downwardly extending standpipe  71  and a vent  69 . The standpipe opens at a level below the outlet of the oil trap to prevent splashing and re-emulsifying of the oil in the oil-in-water emulsion. 
     The above-described configurations optimize the features of the coalescing/de-emulsifying coiled tubular filter configuration by providing a flow path which continually skims off any coalesced oils and deposits them in a location and form for easy removal during service. The exemplary illustrated configurations use low flow rate, low pressure drop, multiple pass filtration configurations, which are more efficient in removing particles and emulsified oils than known high flow rate, high pressure drop, single pass filtration systems. 
     The present configurations operate on the principle that waste streams such as soluble oil coolants, aqueous parts cleaning fluids, vibratory finishing systems, used mop water, and air compressor condensate have the ability to loosely emulsify oils from machine lubrication systems, cutting/forming oils from previous machining operations, hydraulic oils, etc. By continually de-emulsifying, coalescing and removing the unwanted loosely emulsified oils, the quality of the process fluid is continually maintained for reuse or proper discharge to the sewer. Furthermore, by continually removing emulsified oils in the fluid, the loosely emulsified oils are not allowed to accumulate in the fluid and later separate out when not in use. It is also important to note that stagnant layers of oil on top of aqueous fluids prevent oxygen from coming into contact with the aqueous fluid. This provides an environment for the buildup of anaerobic bacteria often associated with rancid or foul smells. 
     The proposed coalescing/de-emulsifying filter uses a polymer, such as polypropylene, that has a surface tension that wets (adsorbs) oils and repels water. A filter media of many fine fibers of polypropylene therefore provides a good surface to de-emulsify and coalesce oils from droplets of aqueous fluid that have oil on the outside and water on the inside (water-in-oil emulsions). These characteristics are often associated with unwanted oils picked up by aqueous solutions such as coolants and air compressor condensates. Likewise, such a filter media passes aqueous fluids that have oil on the inside and water on the outside (oil-in-water emulsions) often associated with stable soluble oil coolants (milky white in color) and semi-synthetic coolants (cloudy in color). In this manner the filter, coupled with low shear stresses due to low pressures and velocities, can effectively remove unwanted oils from fluids without removing the desired soluble oils such as those found in coolant formulations. 
     It has been found that the present configurations use the natural ability of the polypropylene coiled tubular filter configuration to de-emulsify and coalesce oils and makes use of gravity to facilitate separating and accumulating the coalesced oils, in a container, for ease of removal. A present system can be provided in a modular design having a relatively small footprint, which provides a cost effective, machine-dedicated system for example, for parts cleaners, machine tools and the like. Moreover, the present coalescing/de-emulsifying coiled tubular filter system is less susceptible to fouling and bacteria colonization than membrane filters because the coalesced oil, aqueous fluid, and any bacteria pass through the filter. 
     Without being held to the specifics of the phenomena occurring, it is believed that the microfiber of the filter material strips off the emulsified oil from the oil-in-water micelle by adsorbing the oil onto the tiny fibers. The adsorbed oil then gradually coalesces and migrates through the filter media forming droplets on the outer surface of the filter media which eventually release and float to the surface. The oil coated microfibers also provide a good “sticky” surface for adhering small particles (smaller than the 19 micron 95 percent filtration efficiency of the microfiber filter material). The small particles entrained in the oil also migrate with the oil and become trapped in the subsequently coalesced oil droplets which are eventually separated out from the oil-in-water desirable emulsion. As such, it has been found that the present filtration system efficiently removes particles smaller than the rated filtration efficiency of the microfiber filter media. In addition, because the small particles are trapped by, and migrate with, the de-emulsified oil, the particles do not accumulate in the filter and therefore do not decrease the filter life. 
     Advantageously, it has been found that the present filter system does not significantly raise the temperature of the fluid. Oil de-emulsifying and coalescing followed by cascade oil trap separation separates the coalesced oils from the aqueous fluid rather than concentrates the separated emulsion. During routine service the only waste materials generated are accumulated oil and filter element. The proposed coalescing/de-emulsifying coiled tubular filter can effectively coalesce unwanted oil present in water-in-oil emulsions without breaking down desirable oil-in-water emulsions found in soluble oil and semi-synthetic coolants. It has also been found that the present coalescing/de-emulsifying coiled tubular filtration systems continuously removes emulsified tramp oils as they are forming, to eliminate the accumulation of unwanted oils in an aqueous fluid sump or bath. By removing unwanted oils as they are introduced, the unwanted cumulative effects, such as colonization of anaerobic bacteria, caked floating scum, food for general bacteria, and degradation of the cooling and machining enhancement properties of the coolant, are eliminated or greatly minimized. The proposed filtration system actually uses the ability of the aqueous fluid to emulsify unwanted oils to help eliminate them. 
     All patents referred to herein, are hereby incorporated herein by reference, whether or not specifically do so within the text of this disclosure. 
     In the present disclosure, the words “a” or “an” are to be taken to include both the singular and the plural. Conversely, any reference to plural items shall, where appropriate, include the singular. 
     From the foregoing it will be observed that numerous modifications and variations can be effectuated without departing from the true spirit and scope of the novel concepts of the present invention. It is to be understood that no limitation with respect to the specific embodiments illustrated is intended or should be inferred.