Abstract:
The present invention is directed to processes for removing a contaminant from dental effluents and includes transporting a three-phase effluent through a suction line into a particle collection vessel, introducing a suction line cleaning solution which includes a reagent into the suction line, and introducing the three phase effluent and the line cleaning solution into the collection vessel, wherein the effluent separates into solid, liquid, and gas phases in the collection vessel and the reagent includes a flocculant and/or a precipitant, and removing the gaseous and liquid phases from the collection vessel. The contaminant includes mercury, lead, and arsenic.

Description:
CROSS REFERENCE TO RELATED APPLICATION 
     The present application claims the benefits of U.S. Provisional Application Serial Nos. 60/191,916, filed Mar. 24, 2000; No. 60/239,463, filed Oct. 10, 2000; and No. 60/267,614, filed Feb. 9, 2001, all of which are incorporated herein by reference in their entireties. 
    
    
     NOTIFICATION OF FEDERAL RIGHTS 
     This invention was made with Government support under Grant No. 5R44DE13081-03 awarded by the National Institutes of Health. The government has certain rights in the invention. 
    
    
     FIELD OF THE INVENTION 
     The present invention relates generally to removing mercury and mercury-containing compounds from liquid wastes and specifically to removing mercury and mercury-containing compounds from dental effluents. 
     BACKGROUND OF THE INVENTION 
     Each year tens of thousands of pounds of mercury-containing wastes are discharged by dental offices into municipal waste systems. Amalgam fillings typically contain about 50% mercury by weight. Mercury is a known environmental contaminant, classified by the USEPA as a persistent, bioaccumulative, and toxic material. Waste water treatment plants must meet strict limits on the amount of mercury they can release. The discharged form of mercury is typically highly toxic (i.e., unstable) and in violation of applicable environmental regulations. Although particulate removal systems used in some dental offices remove mercury-containing particles, they do not remove dissolved mercury and mercury-containing compounds. Examples of such devices are described in U.S. Pat. Nos. 5,885,076; 5,797,742; 5,795,159; 5,577,910; 5,227,053; 4,753,632; 4,591,437; 4,385,891; and 5,114,578, all of which are incorporated herein by this reference. 
     SUMMARY OF THE INVENTION 
     The present invention provides a method and apparatus for removing solid amalgam particles and/or soluble forms of mercury and other metals (such as silver) and other contaminants from dental effluents. 
     In one embodiment, a contaminant removal system is provided for treating a three-phase effluent. The system includes: 
     (a) a particle collection vessel for separating a gas phase, a liquid phase, and a solid (particulate) phase in the three-phase of effluent; 
     (b) a first discharge line from the vessel for removing the liquid phase from the vessel; 
     (c) a second discharge line from the vessel for removing the gas phase from the vessel; and optionally 
     (d) a liquid treatment device for removing and/or stabilizing contaminants in the liquid phase to form a treated liquid phase. The contaminant can be any undesirable organic or inorganic material in the effluent. Examples include metals (e.g., mercury, lead, arsenic, etc.), metal compounds, bacteria, pathogens, inorganic and organic solvents, and mixtures thereof. 
     The particle collection vessel can be of any suitable design. For example, the vessel can be a settling tank, a sedimentation device, a centrifuge, or any other device that utilizes gravity or centrifugal forces for effectuating solids/liquid separation. In one configuration, the particle collection vessel includes one or more baffles to facilitate solid/liquid/gas separation. 
     To remove the liquid phase from the particle collection vessel, the system can include a timer connected to a pump on the first discharge line to cause periodic removal of the liquid phase from the vessel during periods when no waste is incoming (e.g., overnight). In this manner, the liquid is provided with a relatively quiescent period for effective settlement of entrained particles such as amalgam particles. 
     The liquid treatment device can be any suitable device for removing and/or stabilizing contaminants in the liquid phase to form the treated liquid phase. In one configuration, the liquid treatment device includes one or more devices for adding chemical additives, such as one or more of a pH adjustor, an oxidant, a reductant, and a precipitant with the liquid phase. In one configuration, the liquid treatment device includes one or more sorbent columns that contact the liquid phase with one or more sorbents. 
     The effluent can be any contaminated effluent regardless of the source. In a preferred configuration, the effluent is produced by dental work on a patient. The effluent is collected by a liquid collection device, such as a sink, suction tube or, evacuation line, and conveyed to the particle collection vessel via a waste discharge line. A single particle collection vessel can service a plurality of such liquid collection devices corresponding to a plurality of dental chairs. 
     In another embodiment, a process is provided for removing dissolved contaminants from the three-phase effluent. The process includes the steps of: 
     (a) introducing the three-phase effluent into a particle collection vessel; 
     (b) reducing the velocity of and/or redirecting the direction of movement of the effluent, thereby causing a solid phase and a liquid phase to separate from a gas phase; 
     (c) removing the gas phase from the collection vessel; 
     (d) removing the liquid phase from the collection vessel; and optionally 
     (e) contacting the liquid phase with at least one of an additive and a sorbent to form a treated liquid phase. 
     As noted, the liquid phase can be removed discontinuously from the collection vessel to provide more effective separation of the entrained particles from the liquid phase. 
     In one configuration, the contacting step further includes the steps of; 
     (f) first contacting the liquid phase with one or more of a reductant, an oxidant, a participant, and a pH adjustor I (typically prior to removal of the liquid phase); and 
     (g) second contacting the liquid phase with a sorbent to remove mercury therefrom. In another configuration, step (g) is optional. 
     As will be appreciated, the additive, preferably a reactant (a compound that will react with the contaminant, such as a reductant, oxidant, and/or precipitant), may be used in the absence of (or without) a sorbent. For example, the reactant could be a precipitant that forms a precipitate with the contaminant. The precipitate could be removed from the effluent by filtration techniques, gravity separation techniques, etc. A flocculent, such as aluminum or commercially available polymers, could be further added to the effluent to act as a filter and/or settling aid. 
     The system and method can provide numerous benefits. For example, the system can remove not only solid amalgam particles but also remove and/or stabilize dissolved elemental mercury and speciated mercury. The system and method can be effective at capturing a high percentage of the amalgam particles. The vessel typically captures or collects at least most and more typically at least about 95% of all amalgam particles that are about 10 microns or greater in size. The chemical treatment device can further remove at least most of the amalgam particles that are less than about 10 microns in size. Amalgam particles typically represent at least 95% of the total mercury sent to the system. Any of the system components can be used as a recycling device. For example, the collection vessel or sorbent column can be operated for a predetermined period (typically 6-12 months) after which the vessel and/or column is replaced. The used vessel and/or column is shipped to a recycling facility to recover the captured amalgam particles and/or elemental and speciated mercury. The system can operate effectively without a sorbent. Proper selection of the additives can remove the need for a sorbent. 
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS 
     FIG. 1A is a perspective view of a particulate collection vessel in accordance with one embodiment of the present invention; 
     FIG. 1B is a flow schematic of the embodiment of FIG. 1A; 
     FIG. 2 is a side view of the vessel; 
     FIG. 3 is a side view of the baffle assembly; 
     FIG. 4 is a side view of the cap to the vessel; 
     FIG. 5A is a plan view of the cap; 
     FIG. 5B is a cross-sectional view of the particulate collection vessel in operation; 
     FIG. 6 is a top view of the cap according to another embodiment of the present invention; 
     FIG. 7 is a perspective view of the particulate collection system; 
     FIG. 8 is a side view of the baffle assembly engaging the spacing assembly; 
     FIG. 9 is a top view of the spacing assembly; 
     FIG. 10 is a side view of the cap; 
     FIG. 11 is a block diagram showing the various components of a mercury removal system according to another embodiment of the present invention; 
     FIG. 12 is a view of the various components installed in an enclosure; 
     FIG. 13 is a cross-sectional view taken along line  10 — 10  of the sorbent column of FIG. 9; 
     FIG. 14 is a graph of final mercury concentration (PPB) (vertical axis) against reagent (horizontal axis); and 
     FIG. 15 is a plot of mercury concentration (ppb) (vertical axis) versus sample number (horizontal axis). 
    
    
     DETAILED DESCRIPTION 
     The Particulate Collection System 
     A first embodiment of the present invention is depicted in FIGS. 1A-5B and  7 . The particulate collection system  100  includes a collection vessel  104 , a pump  108  (e.g., a peristaltic pump), and a timer  112  (e.g., an electronic 24/7 timer). The collection vessel  104  is located between the vacuum line  116  to the chairs  118   a-n  and the vacuum line  120  to the vacuum pump  124 . Thus, the vessel  104  is typically installed on the suction side of the vacuum pump  124 , preferably close to the vacuum pump. A liquid discharge line  128  is connected to the pump  108  and from the pump  108  to the exhaust hose  132  from the vacuum pump  124  to the sewer (not shown). 
     The timer  112  is connected to the pump  108  to cause discontinuous discharge of the liquid waste (or liquid phase) from the collection vessel  104 . The timer  108  ensures that there is a sufficient (predetermined) settling time (in which the liquids and solid phases are relatively quiescent) prior to activating the pump  108  to discharge the (supernatant) wastewater or liquid phase. Typically, the predetermined settling time (between pump activation cycles) ranges from about 1 to about 24 hrs and more typically from about 8 to about 12 hrs. The discharge is performed at a controlled, slow rate (typically in the range of from about 10 to about 1000 ml/min and more typically in the range of from about 20 to about 200 ml/min). 
     FIGS. 2-5B depict the various components of the collection vessel  104 . The collection vessel  104  includes a central housing  150 , a base  154  attached to the bottom of the housing  150 , a cap  158  attached to the top of the housing  150 , a dip tube  162  connected to passage  166  in the cap  158 , and a baffle assembly  170 . The dimensions of the vessel  104  typically range from about 10 to about 25 inches high and about 5 to about 25 inches in diameter. 
     The baffle assembly  170  includes a cylindrical baffle tube  174  having a plurality of supporting legs  178   a-c  spaced at intervals around the bottom of the baffle tube  174 . The inner and outer radii of the baffle tube  174  are less than the inner radius of the housing  150  so that the baffle assembly can be received inside of the housing. Typically, the inner and outer radii of the baffle tube  174  are no more than about 50% of the inner housing  150  radius and typically are no less than about 10% of the inner housing  150  radius. The baffle tube  174 , of course, has a hollow interior to permit fluids to flow upwardly and/or downwardly through the tube as shown. The dip tube  162  is positioned inside of the baffle tube  174  during use and at or near the central vertical axes of the housing  150 . The baffle tube  174  is located such that the dip tube  162  and the cap outlet port  180   a  are located inside the cylindrical housing of the tube. 
     The cap  158  includes two conduits  180   a,b  that pass through the cap  158  and project a distance “D 1 ” (typically from about 0.5 to about 3 inches below the cap surface  184 . The conduits  180   a,b  connect to the vacuum lines  120  and  116 , respectively. The distance “D” is sufficient to hold the baffle tube  174  in position within the housing  150  (i.e., under ports  166  and  180   a ) during use. 
     The collection vessel  104  and baffle assembly  170  can be made of any suitable material, with corrosion resistant plastics, such as PVC being preferred. 
     In operation, a three-phase mixture  117  of gas, solids or particles (e.g., mercury amalgam particles), and liquid from the dental chair(s) passes through vacuum line  116  and into the annular area  190  between the exterior surface  192  of the baffle tube  170  and the interior surface  188  of the housing  150 . The velocity of the mixture is slowed by the large flow area within the vessel, causing solid particles  189  to settle out of the mixture and collect in the bottom of the housing  150 . The gas phase  118  of the mixture passes above (i.e., the top  190  of the baffle tube  170  is typically spaced from the cap bottom  184 ) and around baffle tube  170  (i.e., the baffle tube exterior  192  is typically spaced from the housing interior around the baffle tube&#39;s periphery). The liquid phase  119  also settles out of the gas phase (due to the decrease in gas velocity) and collects in the bottom of the housing with the particles. Baffle tube  170  forces the liquid flow between legs  178   a-c  in order to exit vessel  150  via either dip tube  162  or outlet port  180   a . This flow path will create some particle separation (albeit less than in normal operation) in the event that the vessel  150  overflows. Periodically, the pump  108  is activated by the timer  112  and draws collected liquid phase out of the bottom of the housing via dip tube  162  and discharges the liquid phase through discharge line  128  into the exhaust hose  132 . The pump  108  is typically activated at a time interval ranging from about 5 mins. to about 12 hrs, more typically from about 2 to about 12 hours, and even more typically from about 2 to about 6 hours. The flow rate of pump  108  is low enough, typically about 0.02 to about 1 l/min., to prevent entrainment of the settled particles. The dip tube  162  design prevents particles from being withdrawn with the liquid and, therefore, the particles remain in the bottom of the housing  150 . 
     The system has numerous operational benefits. The system can be effective at capturing about 95% of all particles that are greater than about 10 micron in size. This fraction of particles typically amounts to about 95% of the total mercury sent to the system. The system can be a self-priming system and will hold a vacuum when turned off. The pump can run dry without damaging the motor or the drive unit. The unit can be used as a recycling device. After the unit operates for a predetermined period (typically six to twelve months) the vessel is replaced with a new vessel and the used vessel shipped to a recycling facility to recover the captured amalgam particles. The vessel can remove fine amalgam particles that can damage the dental vacuum pump. 
     Installation of the system depends on the application. The system is designed to work with either wet- or dry-vacuum systems. In a dry-vac system, it is preferred that the vessel be installed upstream of the dry vac&#39;s air/water separator. The existing air/water separator may be removed; however, it is recommended that the existing air/water separator be left in place to protect the vacuum pump in the event that the vessel overfills. Because liquids will not damage a wet-vac pump, no such precaution is required for a wet system. If installed downstream of an existing air/water separator, the system is typically installed to receive the liquid outlet flow from the air/water separator. Different size clinics can be accommodated by adjusting the overall size of the system. In one configuration, the system is designed so that if any problem occurs with the unit, fluid flow will bypass the vessel and allow continued operation of the dental suction system. 
     FIGS.  6  and  8 - 10  show a particle collection system according to another embodiment of the present invention. The baffle assembly  200  includes a spacer assembly  204  that engages the upper end of the baffle tube  170 . Spacers  208   a-c  are positioned at intervals around the periphery of the baffle tube  170  to maintain the correct, spaced relationship between the tube wall and the housing interior. Because the spacer assembly  204  maintains the tube exterior in a spaced apart relationship relative to the housing wall, the cap  210  does not require downwardly projecting conduits  180   a,b.    
     The Combined Particulate Removal and Purification System 
     Referring to FIGS. 11-13, the combined particulate removal and purification system  300  will now be discussed. The system removes and/or stabilizes soluble forms of mercury as well as solid-phase mercury. Soluble forms of mercury are typically present in the dental wastewater from the reaction of the mercury in amalgam particles with the wastewater which releases soluble forms of mercury into the wastewater. 
     The system  300  includes the particulate collection vessel  104  described above and, in addition, a chemical doser  304  and a sorbent column  308  and sub-micron filter  309 . The doser  304  and sorbent column  308  are in communication with discharge line  312  and pump  108 . Pump output line  312   b  is connected to the doser  304  and an output line  312   c  from the doser  304  is connected to the sorbent column  308 . The output line  312   d  from the sorbent discharges into the sewer or line  128 . 
     As will be appreciated, the dissolved mercury-containing compounds, colloidal mercury, and small (e.g., less than about 10 microns) amalgam particles in the waste liquid from the particulate collection vessel are removed and/or stabilized by the doser  304  and sorbent column  308  and polishing sub-micron filter  309 . 
     One or more dosers  304  can be used to directly reduce mercury levels in the wastewater and/or adjust wastewater chemistry. A doser will typically release one or more suitable additives to the wastewater to maintain desirable chemical properties, to convert dissolved mercury to a less soluble form of mercury, or enhance the performance of a mercury-selective sorbent in the sorbent column  308  in removing dissolved mercury from dental amalgam wastewater, and/or to kill or neutralize organic material in the wastewater. Suitable solid additives are preferably nontoxic and sparingly soluble in the wastewater so that they are slowly released into the water. Alternately, the additive could be added by any other suitable technique. For example, the additive can be slowly added (as a liquid, solid, or gas) via a dosing mechanism (e.g., a pump) or by encapsulation in a slowly dissolving substance. 
     In another embodiment, the reagent can be added to the collection vessel via the dental suction line. For example, most dental offices flush a suction line cleaning solution through their evacuation system. The reagent could be added in the same method, or be co-blended, with the line cleanser. In this case, the additive is added to and in the effluent upstream of the collection vessel and further additive addition(s) in or downstream of the collection vessel is/are optional. The blending could be done during or after production of the cleanser. The blending can be done by known techniques such as by using a ribbon blender. Typical dental line cleansers contain surfactants and disinfectants and may range in pH from acid to highly basic. Active ingredients include sodium hydroxide (Alprojet™), chloramine T (Tiutol™, Aseptoclean 2™), sodium perborate or another percarbonate, hydrogen peroxide (Orotol Ultra™), ammonium chloride (S&amp;M matic™, Vacusol™), sodium hypochlorite (bleach), pyridine compounds (Green &amp; Clean™), phosphoric acid (Purevac™), glycolic acid, citric acid, isopropanol, chlorhexidine gluconate (Biovac™), and/or enzymes (Vacukleen™). In this case, any of these cleansers would further include one or more of the additives of the present invention. 
     The doser  304  can be of any suitable design. The doser may include a separator contacting chamber or may add reagent directly into collection vessel  104 . In one design, the doser  304  includes inner and outer containment vessels  320   a,b  forming annulus  322  therebetween and a bed  336  of additive particles contained within the inner containment vessel  320   b . Wastewater  328  flows in the annulus  322  between the inner and outer containment vessels, through the space  332  between the bottoms  336 ,  340  of the inner and outer containment vessels  320   b,a , and through the (fluidized) bed  336  in the inner containment vessel  320   b . In another design, the dosing occurs within the amalgam separator  104  itself. 
     In one configuration, the doser contacts an additive (or pH adjustor) for controlling wastewater pH. The additive can be any suitable substance for controlling pH, such as a base, e.g. hydroxides, carbonates, and phosphates with hydroxides and carbonates being preferred, or acid, e.g., organic acid and mineral acids, with mineral acids being preferred. Sufficient pH adjustor added to maintain a pH preferably ranging from about pH2 to about pH6 or from about pH8 to about pH10, depending on the application. pH adjustment is used to enhance the performance of other additives or of sorbent materials. Sorbents often work better at low pH, whereas many precipitating additives require a high pH. 
     In one configuration, the doser  304  contacts an oxidant with the wastewater to oxidize organic matter before passing the wastewater through the sorbent column. As will be appreciated, organic matter can clog, bio-foul, or otherwise impair the performance of the sorbent material. Any suitable oxidant can be used. Preferred oxidants include organic halogen derivatives (e.g., symclosene, oxyhalide salts (e.g., hypochlorite), ozone, hydrogen peroxide and/or organic peroxides). In typical applications, the amount of oxidant added will range from about 10 to about 1000 ppm. 
     In another configuration, a reductant is contacted by the doser with the wastewater to reduce mercury-containing compounds and materials. Reducing agents minimize oxidation and release of mercury from captured amalgam and helps to chemically reduce incoming oxidized mercury, thereby making it less soluble. For example, reduced elemental mercury has a very low solubility—on the order of 20 micrograms/L. Any suitable reductant can be used. Preferred reductants include stannous chloride, iron, tin oxalate, bisulfites, and/or polyvalent metals. 
     A reducing additive should create a solution oxidation/reduction potential capable of reducing oxidized forms of mercury back to elemental mercury. The standard electrode potentials (E°) for mercurous (Hg 2   ++ + 2   c = 2   {overscore (e)} ) and mercuric (Hg ++ + 2   {overscore (e)} =Hg) reduction are about +0.789 V and +0.854 V respectively. These are measured versus a standard hydrogen electrode. Thus to create a solution environment where the concentration of oxidized mercury is no greater than that for elemental mercury (the assumed minimum limit for a solution in contact with amalgam) the required potential is given by:              Eh   =     E°   +     0.059                 log                   (       [     Hg   oxidized     ]       a   Hg       )                 Eq.(1)                                
     at 25° C. In Equation (1), the activity of elemental mercury, a Hg , is equal to unity by convention, and [Hg oxidized ] represents the molar concentration of oxidized mercury. The equation is exact if species activity is used in place of concentration. Assuming a desired minimum concentration of 10 −7  molar (˜20 ppb), the solution Eh is preferably about ≦+0.38 V. In typical applications, the amount of reductant added will range from about 10 to about 1000 ppm. 
     In another configuration, a precipitant is contacted by the doser with the wastewater to cause precipitation of mercury-containing compounds as insoluble mercury precipitates. Any suitable precipitant can be used. Preferred precipitants include iodates, sulfides and polysulfides, thioamides (e.g., thioacetamide), carbamates and thiocarbamates (e.g., sodium diethylthiocarbamate), polycarbamates, thiocarbamides, and polymeric or immobilized variants of these functional groups and mixtures and derivatives thereof. Carbamates are preferred as they are generally nontoxic and pH insensitive. In general, the precipitant can be any chemical which forms a sparingly soluble or readily filterable complex with mercury or mercury-bearing compounds. In typical applications, the amount of precipitant added will range from about 10 to about 1000 ppm. 
     In some configurations, the processes and compositions of U.S. Pat. Nos. 5,880,060; 5,667,695; 5,370,827; 5,330,658; 5,080,799; 4,108,769; and/or 4,072,605, all of which are incorporated herein by this reference, are used as or in lieu of the doser. 
     When a precipitant is used, a particle filter, such as a fine screen or membrane, can be located in or downstream of the doser and in or upstream of the sorbent column (if a sorbent column is present) to remove precipitated mercury particles. The filter preferably has a pore size sufficient to remove the particles, which typically ranges from about 10 to about 0.45 microns. In one configuration, the particle filter is located downstream of the sorbent column (FIG.  11 ). 
     The sorbent column  308  can be of any suitable design. The sorbent column can be configured to contain one or multiple sorbent beds of the same or differing sorbents. The typical column design is a packed-bed of sorbent particles. Other column designs include monolithic sorbent structures and fluidized bed designs. 
     Referring to FIG. 13, the sorbent column  308  of one design includes a column housing  350 , a bottom  354  having an input port  358 , a top  362  having an output port  366 , a plurality of retaining rings  370   a-c , and a plurality of screens  374   a-c . The screens prevent intermixing of the sorbent beds  380  and  384  and restrain movement of the sorbent particles in the beds so as to prevent clogging of the input port  358  or output port  366  or removal of the sorbent particles from the column with the wastewater. 
     The sorbent can be any sorbent capable of collecting mercury. Preferred sorbents include one or more of activated carbon, ion exchange resins such as cellulosic resins (e.g., as discussed in U.S. Pat. No. 5,907,037 which is incorporated herein by this reference) chelating resins and porous silica, and zeolites. 
     In a preferred configuration, the first sorbent bed  380  of activated carbon is located near the input port  358  to remove dissolved mercury and residual oxidant (if added previously by a chemical doser  304 ) from liquid  119  and the second sorbent bed  384  of an ion exchange resin is located above the first sorbent bed near the output port  366  to remove further dissolved mercury from liquid  119 . 
     The purified wastewater  390  is fully compliant with pertinent environmental regulations. Typically, the purified wastewater  390  contains no more than about 10 ppb mercury. 
     In operation, the wastewater  328  is removed from the vessel  104  as described above and passed through the input at the top of the doser  304 , through the annulus  322  and through the additive bed  336 , and is removed through the output at the top of the doser  304  to form a treated wastewater. The treated wastewater  400  is introduced into the sorbent column  308  through input  358 , passed sequentially first through sorbent bed  380  and second through sorbent bed  384  to form a purified wastewater  390 . The wastewater is filtered with a polishing filter  308  to remove sorbent residue. Purified wastewater  390  can be discharged directly into the sewer. 
     EXPERIMENTAL 
     ISO CERTIFICATION 
     The international organization for standardization (ISO) is a worldwide federation of national standards bodies. ISO standards provide safety and performance guidelines for a variety of equipment categories, including dental equipment. International standard ISO 11143 was prepared by the ISO dentistry technical committee to assess the performance of dental amalgam separators. 
     Amalgam separators are defined as items of dental equipment designed to retain amalgam particles carried by the wastewater from the dental treatment system, so as to reduce the number of amalgam particles and therefore the mercury entering the sewage system. The use of a centrifuge, filtration, sedimentation or combination of any of these methods may achieve separation of the amalgam particles. 
     ISO 11143 specifies requirements for amalgam separators used in connection with dental equipment in the dental treatment system. It specifies the efficiency of the amalgam separator (minimum of 95%) in terms of the level of retention of the amalgam based on a laboratory test. The standard also describes the test procedure for determining this efficiency, as well as requirements for the safe functioning of the separator, labeling, and instructions for use of the device. The ground amalgam sample for the efficiency test of the amalgam separator is divided into three different fractions: 
     6.0 g of particles sized 3.15 mm to 0.5 mm 
     1.0 g of particles sized 0.5 mm to 0.1 mm 
     3.0 g of particles smaller than 0.1 mm 
     In addition, 50% of the fine fraction particles should be less than 0.01 mm. The test sample used to assess the efficiency of the amalgam separator has a particle size distribution that reflects the situation found in dental treatment systems. The size fractions used in the standard are based on investigations that have been carried out to determine the particle size distribution of amalgam particles in water from dental treatment systems. 
     In summer 2000, the BullfroHg™ amalgam separator was independently tested following ISO 11143. The separator received a score of 99.6% removal efficiency when empty and 98.6% efficiency when full, easily passing the required test efficiency of 95%. 
     ISO CERTIFICATION TEST RESULTS 
     
       
         
               
               
             
               
               
               
             
               
               
             
               
               
               
             
               
               
             
               
               
             
               
               
             
               
               
               
             
               
               
             
               
               
               
             
               
               
             
               
               
             
               
             
               
               
             
               
             
               
               
             
               
             
               
               
             
               
             
           
               
                   
               
             
             
               
                 Reference/Equipment: 
                 Amalgam Separator BullfroHg ™ 
               
             
          
           
               
                 Rating: 
                 Rated voltage: 
                 120 V AC 
               
               
                   
                 Rated current: 
                     1.5 amp 
               
               
                 Date of receipt: 
                 6/22/00 
               
             
          
           
               
                 Type of examination: 
                 Alternate construction test. 
               
               
                 Test regulations: 
                 ISO 11142: 1999-12 
               
               
                 Testing period: 
                 July/August 2000 
               
               
                 Test location: 
                 Technology Centre of RWTUV 
               
               
                   
                 Analagentechnik GmbH 
               
               
                   
                 Classification: Type 2: Sedimentations 
               
               
                   
                 system 
               
             
          
           
               
                   
                 Amalgam 
                 Becker MeBtechnik 
               
               
                   
                 sample: 
                 GmbH, 
               
               
                   
                   
                 71364 Winnenden, 
               
               
                   
                   
                 Germany 
               
               
                   
                   
                 ISO 10 g, January 2000 
               
             
          
           
               
                   
                 Maximum water floulrate: 750 ml/mn., 
               
               
                   
                 10 l altogether 
               
               
                   
                 Type of membrane filters: Schleicher + 
               
               
                   
                 Schuell 
               
             
          
           
               
                   
                 Membrane filters 
               
               
                   
                 AE 100 + ME29 + 
               
               
                   
                 ME28 
               
             
          
           
               
                   
                 Number of tests performed: 6 
               
               
                   
                 Separation degrees of empty amalgam 
               
               
                   
                 separator: after 12 to 14 hours 
               
             
          
           
               
                   
                 1. 
                 99.9% 
               
               
                   
                 2. 
                 99.7% 
               
               
                   
                 3. 
                 99.3% 
               
             
          
           
               
                   
                 Average 99.6% 
               
               
                   
                 Separation degrees of full amalgam 
               
               
                   
                 separators: after 12 to 14 hours 
               
             
          
           
               
                   
                 1. 
                 99.0% 
               
               
                   
                 2. 
                 98.0% 
               
               
                   
                 3. 
                 97.9% 
               
             
          
           
               
                   
                 Average: 98.3% 
               
               
                   
                 Value of the efficiency: 98.3% 
               
             
          
           
               
                 Annex (No. Of pages): 
                 None 
               
               
                 Test result: 
                 The referenced units are in compliance 
               
               
                   
                 with the above requirements. 
               
             
          
           
               
                 Test program ISO 11143 Dental Equipment-Amalgam Separators: 1999 
               
             
          
           
               
                 Test object: 
                 Amalgam Separator Model BullfroHg ™ 
               
               
                 Classification: 
                 Type 2: Sedimentation system 
               
               
                 Amalgam sample: 
                 Becker MeBtechnik GmbH 
               
               
                   
                 71364 Winnenden, Germany 
               
               
                   
                 ISO 10 g, January 2000 
               
               
                 Maximum water flow/rate: 
                 750 ml/min., 10 l altogether 
               
               
                 Type of membrane filters: 
                 Schleicher + Schuell 
               
               
                   
                 Membrane Filters AE 100 + ME29 + 
               
               
                   
                 ME28 
               
               
                 Number of tests performed: 
                 6 
               
             
          
           
               
                 Separation degrees of empty amalgam separator: after 12 to 14 hours 
               
             
          
           
               
                 1. 
                 99.9% 
               
               
                 2. 
                 99.75 
               
               
                 3. 
                 99.3% 
               
             
          
           
               
                 Average: 99.6% 
               
               
                 Separation degrees of full amalgam separators after 12 to 14 hours 
               
             
          
           
               
                 1. 
                 99.0% 
               
               
                 2. 
                 98.0% 
               
               
                 3. 
                 97.9% 
               
             
          
           
               
                 Average. 
               
               
                 Value of the efficiency: 98.3% 
               
               
                   
               
             
          
         
       
     
     The BullfroHg™ Hg amalgam separator passed the test. 
     In addition to the ISO test, ADA further performed an initial screening of the doser concept. The tests were intended to demonstrate that mercury levels could be reduced by reagent addition. Dental waste from a Denver-area clinic was used in these tests. The wastewater was first filtered through a 10-micron filter to remove large particles. Some of the wastewater was sent through a 0.45-micron filter to determine the amount of “soluble” mercury. The tests consisted of 150 mL of waste and 10 g of reagent placed into 250-mL shaker flasks. The flasks were shaken overnight and the solutions in each flask were again filtered with a 10-micron filter to remove solids. Half of the samples were then filtered through a 0.45-micron filter. The results are plotted in FIG.  16 . 
     Sixteen different reagent combinations were tested in these first trials. Several reduced the amount of mercury in the wastewater sample. Of those tested, iron, calcium carbonate, potassium iodate and tin oxalate appear to yield the best results. Some tested reagents successfully reduced the mercury levels, but are not believed to be practical for other reasons. 
     These initial tests were intended to demonstrate that mercury levels could be reduced by addition of a reagent. Reagents other than those tested are also possible. 
     In addition to the above tests, the City of Toronto carried out independent testing of a system as depicted in FIGS. 11 and 12. The system was connected to a city dental clinic suction system and the effluent  390  was analyzed for total mercury concentration. The results are depicted in FIG.  15 . The system consistently reduced the mercury concentration to less than 10 micrograms per liter—levels that cold not be achieved through particle separation alone. 
     The foregoing description of the present invention has been presented for purposes of illustration and description. Furthermore, the description is not intended to limit the invention to the form disclosed herein. Consequently, variations and modifications commensurate with the above teachings, in the skill or knowledge of the relevant art, are within the scope of the present invention. For example, the particulate collection vessel can be used without the addition of an additive or the use of a sorbent. The embodiments described here and above are further intended to explain best modes for practicing the invention and to enable others skilled in the art to utilize the invention in such, or other, embodiments and with various modifications required by the particular applications or uses of the present invention. It is intended that the appended claims be construed to include alternative embodiments to the extent permitted by the prior art.