Abstract:
For extracting phosphorous from algae-in a body of water, the algae are deposited into a sealable tank ( 200 ) that is then evacuated, thereby rupturing the algal cell walls. The ruptured algae are then moved to a second tank ( 260 ), mixed with water and bacterial cultures, and allowed to settle until the lipids rise to the top and the oil-less debris settles to the bottom. The second tank also contains sacrificial ( 295 ) and rusted electrodes ( 320 ). The phosphorous from the algae combines with the rust. The lipids and debris are then removed. Next, an electrical source ( 315 ) causes the rust to be removed from the rusted electrodes and settle. In addition, a phosphorous-rich scum floats to the top. These components are placed in storage containers for later use and the water is returned, thereby reducing its phosphorous content.

Description:
CROSS REFERENCE TO RELATED APPLICATIONS 
     This application claims priority of my provisional patent application, Ser. No. 61/298,275, filed Jan. 26, 2010. This application is related to application Ser. No. 12/399,323, filed Mar. 6, 2009 now U.S. Pat. No. 8,017,366 and Ser. No. 12/341,380, filed Dec. 22, 2008 now U.S. Pat. No. 8,043,496. 
    
    
     BACKGROUND 
     1. Field 
     The field hereof relates to the extraction of substances, and in particular the extraction of phosphate and oil from algae and their water environment. 
     2. Prior Art 
     The following is a list of some prior art that presently appears relevant: 
     
       
         
               
               
               
               
             
           
               
                   
               
               
                 U.S. Pat. No.  
                 Kind  
                 Issue or  
                 Patentee or  
               
               
                 or Pub. Nr. 
                 Code 
                 Pub. Date 
                 Applicant 
               
               
                   
               
             
             
               
                 4,023,734 
                 B1 
                 May 17, 1977 
                 Herve et al. 
               
               
                 4,897,266 
                 B1 
                 Jan. 30, 1990 
                 Herve et al. 
               
               
                 6,346,252 
                 B1 
                 Feb. 12, 2002 
                 Moigne 
               
               
                 7,311,838 
                 B2 
                 Dec. 25, 2007 
                 Herold et al. 
               
               
                 7,419,596 
                 B2 
                 Sep. 02, 2008 
                 Dueppen et al. 
               
               
                 7,431,841 
                 B2 
                 Oct. 07, 2008 
                 Herold et al. 
               
               
                 7,431,952 
                 B2 
                 Oct. 07, 2008 
                 Bijl et al. 
               
               
                 7,435,707 
                 B2 
                 Oct. 14, 2008 
                 Langer et al. 
               
               
                 7,435,715 
                 B2 
                 Oct. 14, 2008 
                 Broeckx et al. 
               
               
                 7,439,034 
                 B2 
                 Oct. 21, 2008 
                 Weiner et al. 
               
               
                   
               
             
          
         
       
         
         Non-Patent Literature: U.S. Dept. of Energy, Natl. Algal Biofuels Tech. Roadmap, (June, 2009). 
       
    
     Phosphorus, a multivalent nonmetal of the nitrogen group, is essential to all life forms. It is essential for the structure of every cell and many biological functions. It is allotropic, i.e., it is capable of existing in two or more distinct forms. 
     Phosphorus is an integral part of most fertilizers. Concentrated phosphoric acids are used in fertilizers for agriculture and farm production. Fertilizer phosphorus is now primarily derived from phosphorus rocks processed with ammonium nitrate and sulfur. Recovery costs are dependent upon sulfur prices (an oil production byproduct), ammonium nitrate (made with natural gas), and the increased cost to process the decreasing quality of available ore. Since many conditions limit the discovery and exploitation of new sources, it is very desirable that fertilizer makers be able to recover phosphates from local ecosystems for reuse. 
     In the natural world phosphorous is too active to exist in its pure or elemental form, but only in the form of phosphates, which consists of a phosphorous atom bonded to four oxygen atoms. Phosphates can exist as the negatively charged phosphate ion, which is how they occur in minerals, or as organophosphates in which there are organic molecules attached to one, two, or three of the oxygen atoms. Phosphates can be found in ponds, lakes, and rivers. 
     Phosphorus moves within the environment mainly through soil, water, and living organisms. Plants absorb and incorporate phosphates from soil. The plants are consumed by herbivores, which are in turn consumed by carnivores. When the carnivores die, their decay returns phosphates to the soil and the process repeats. The movement of phosphorus through the environment is called the phosphorus cycle. 
     The constant addition of phosphates to the environment by humans conducting agricultural activities causes their concentrations to exceed natural levels, so the phosphorous cycle is strongly disrupted. Phosphorous concentrations have thus been increasing in surface waters, raising the growth of phosphate-dependent organisms, such as algae and duckweed. These organisms use great amounts of oxygen and restrict sunlight from entering the water. This affects the growth cycle of other organisms. The process by which bodies of water become enriched in dissolved nutrients is known as eutrophication; the nutrients stimulate the growth of algae and other plant life and thereby deplete the amount of dissolved oxygen in the water. 
     The removal of anything from an ecosystem&#39;s water is a delicate art. The basic ecological relationships are typically complex. If too much or too little of anything is removed, it can cause a critically deleterious situation. For ecological maintenance ecologists therefore desire to keep phosphorus levels under control in water environments to maintain a natural habitat, while at the same time recovering the excess for other uses. Careful attention is required to leave the originating water environment safe. 
     Fish excrete phosphorous in their waste materials but the phosphorus can be taken up in part by the plant life and remain in the ecosystem. Excess amounts of phosphorous that would have degraded the environment can be taken up instead by the use of ferric oxide media, which has been shown to remove phosphate from water in a safe, consistent, and repeatable fashion. It is used in aquariums, for example. Typically, in an aquarium setting, after saturation by phosphorus, ferric oxide media is added to collect the excess phosphorus, whereafter the iron particles are removed, discarded, and replaced with new materials. 
     Ferric oxide media are known by a number of names, including ferric oxide, ferric iron, hematite, red iron oxide, synthetic maghemite, or simply rust. Rust is a general term for a series of iron oxides, usually red oxides, formed by the reaction of iron and oxygen in the presence of water or air moisture. Several forms of rust are distinguishable visually and by spectroscopy, and form under different circumstances including hydrated iron(III) oxides Fe2O3.H2O and iron(III) oxide-hydroxide (FeO(OH), Fe(OH)3). 
     In settings other than aquaria, the water containing excess phosphorus is urged to flow through a container and to come into contact with the rust surfaces suspended within it. The surfaces are positioned as baffles. The baffle sheets are sized to equivalently match approximately one gram of rust for each 3.8 liters (1 gallon) of water in the container over a production cycle. The orthophosphate levels in the water can be measured using an appropriate instrument both before and after exposure to rust to help estimate the size of the surfaces necessary in a particular ecological setting. In practice, phosphate levels are measured at the start, and then hourly until levels fail to decline further, which may be in as little as two hours, depending upon water pH and temperature. 
     Green looking pond water is caused by an excessively large number of phytoplankton, which are part of the algae family that has thousands of distinct species. The algae are distributed worldwide in the sea, in freshwater and in damp situations on land. Algae represent a large group of different organisms from different taxonomic divisions. In general, algae can be referred to as plant-like organisms that are usually photosynthetic and aquatic, but do not have true roots, stems, leaves, or vascular tissue, and have simple reproductive structures. The algae have chlorophyll and can manufacture their own food through the process of photosynthesis. In turn, the algae can be processed to harvest their various components for making fuels and various other useful compounds. These organisms are often very small, with the most common ones found in ponds being around 15 microns in diameter. Algae this small are best processed as described in the above copending &#39;380 application. Algae larger than this are more amenable to bulk processing by the method described below, although the smaller micro-algae will also be processed. 
     The cell walls of algae are generally the same as those of plants. Different plants have slightly different chemical makeups in their cell walls. A rigid layer of cellulose strengthens the cell and provides structural support. One interesting organic component of the cellulose is lignin, a complex aromatic polymer that provides the primary strength of the cell wall. The cell wall protects the very thin, highly flexible, but structurally weak cytoplasm membrane that lies under the wall and surrounds the interior of the cell. 
     The cell interior, the cytoplasm, consists of a solution of salts, sugars, amino acids, vitamins, and a wide variety of other soluble materials in water. Since the cytoplasm has a higher solute concentration than the water surrounding the cell, osmosis causes water to pass from outside the cell through the relatively permeable cell wall, continue through the cytoplasm membrane, and dilute the cytoplasm. This builds up pressure within the cell until it equalizes to the effective osmotic pressure and, if not for the rigidity of the cell wall, the cell would burst. Other chemical compounds necessary for the life of the cell are selectively passed through this membrane and waste products are evacuated through it. There are gasses that enter, such as nitrogen, and those that leave, such as oxygen. It is because of the gases in respiration, and the lipids to store energy, that the healthiest of the microscopic algae are normally found at the top layer of the pond water. 
     SUMMARY 
     According to one embodiment, a small, portable apparatus provides a systematic process for a low cost, simple, safe, and rapid separation of phosphate from both algae and the ambient water environment. The process is conducted in a manner that is non-polluting to the environment, non-contaminating of feedstock for other uses, and operations can be conducted on a massive scale by a small crew even in remote settings. The apparatus and process improve the economics of producing alternative energy, maintain the ecosystem, and recover excess phosphorus material for other uses. 
    
    
     
       DRAWINGS 
         FIG. 1  is a flow diagram illustrating the steps in the procedure for the collection of phosphate and fractionated biofuel feedstock. 
         FIG. 2  shows apparatus according to a preferred embodiment. 
         FIG. 3  is a top view of a tank used in the embodiment of  FIG. 2 . 
     
    
    
     
       
         
               
             
               
               
               
               
             
           
               
                   
               
               
                 REFERENCE NUMERALS 
               
               
                   
               
             
             
               
                   
               
             
          
           
               
                 100-155  
                 Steps 
                 200 
                 Vessel 
               
               
                 205  
                 Tank 
                 210 
                 Lid 
               
               
                 215  
                 Port 
                 220 
                 Valve 
               
               
                 225  
                 Conduit 
                 230 
                 Vacuum source 
               
               
                 231  
                 Water source (pond) 
                 232 
                 Valve 
               
               
                 233  
                 Conduit 
                 235 
                 Conduit 
               
               
                 240  
                 Inlet 
                 245 
                 Valve 
               
               
                 250  
                 Outlet 
                 255 
                 Valve 
               
               
                 258  
                 Surface 
                 260 
                 Tank 
               
               
                 261  
                 Surface 
                 265 
                 Legs 
               
               
                 266 
                 Container 
                 268 
                 Container 
               
               
                 270 
                 Pump 
                 271 
                 Conduit 
               
               
                 275 
                 Conduit 
                 280 
                 Valve 
               
               
                 281 
                 Valve 
                 282 
                 Valve 
               
               
                 283 
                 Conduit 
                 284 
                 Conduit 
               
               
                 285 
                 Conduit 
                 290 
                 Container 
               
               
                 295 
                 Electrode 
                 296 
                 Connector 
               
               
                 300 
                 Fingers 
                 305 
                 Conductor 
               
               
                 315 
                 Source 
                 320 
                 Electrode 
               
               
                 325 
                 Conductor 
               
               
                   
               
             
          
         
       
     
     DETAILED DESCRIPTION 
     First Embodiment—Process Steps—FIG.  1   
     One key to reaching the resources within the algae relates to establishing a pressure differential to exceed cell wall strength, but perhaps not in the way assumed. If the pressure within the cell expands suddenly relative to the pressure on the outside, then the cell wall will burst like popcorn. Ultimately, the way into the cell is by having its internal pressure exceed the elasticity of the cell wall by exposing the cell to a critical difference between internal and external pressures. If the gas expansion within the cell is sufficient and sudden, the cell wall will have a popcorn-like rupture. Once an algae&#39;s cell wall is breached, the resources that were within the call can be more easily recovered. 
     Algae and its water environment may play a meaningful role in phosphorous recovery if a way is found that is economical, i.e., if a sufficient volume can be processed in a short enough time at a low-enough cost, regardless of the location. E.g., a portable recovery unit can be used and can be delivered by boat, barge, road, rail, or air transportation, especially to remote settings. In such settings, it may be possible to support a small and portable collection station by a flotation device, on the water of the river or pond surface itself, or in an adjacent cove especially constructed for that purpose. In remote settings, where finances for fertilizer acquisition are limited, a method of phosphorus and biofuel feedstock recovery would be most desirable. 
     There is more than the phosphorus recovery to be gained. Once the cell wall is disrupted, the lipids may float free and to the top of the container for recovery and use as feedstock for biodiesel production. The carbohydrates and other cell debris may drop to the bottom of the container and be selectively recovered for ethanol and methane production. See the copending applications supra. The middle layer of clear water may be returned to the environment. Thus, the process economics of biofuel generation is enhanced by the co-recovery of the feedstock and the fertilizer component. 
     There is still more at stake than just harvesting algae, recovering phosphorous, and feedstock for biofuel. Ultimately, we want to leave the ecosystem in a healthy and balanced condition, which is better than the way we found it. Proper pond maintenance should keep micro-algae to some minimum where blooms are avoided as they cause fish kill-off and a resulting disagreeable stench to human populations in the area. Removing excess phosphorus means removing the excess over what the existing life forms could process in the current quasi-stationary equilibrium of the pond. 
     There is another way in which we can help to reestablish the ecosystem: return bio-available carbon to the water, as in converting feedstock to bio-alcohol and releasing it back into the pond. Related is the notion that micro-algae, which cause the kill-off, thrive only where macro-algae populations are insufficient to handle the nitrogen and phosphorous in the water. Thus, giving the pond carbon should help the macro-algae thrive, which in turn is more feedstock for biofuel, but should also proportionally reduce micro-algae populations. It is common practice of aquarium managers to put a few drops of vodka in the tank as a temporary means of controlling micro-algae. Also, the introduction of appropriate bacteria populations can digest micro-algae blooms, making the more rapid return to non-bloom conditions. Once the healthy pond is functioning, the temporary measures will no longer be necessary. The result of these activities should be a sustainable harvest of feedstock and a healthy pond. 
       FIG. 1  is a flow diagram describing the steps used in phosphate recovery according to a first embodiment, while  FIG. 2  shows a suitable apparatus for realizing the steps of  FIG. 1 . A pond containing sufficient algae for harvesting is selected, step  100 . Algae are gathered from the pond, step  105 , and processed into sausage-like packs for easy handling and storage, step  110 . When it is desired to process the algae, as described below, they are first treated in a vacuum chamber to rupture their cell walls and release their inner contents, step  115 . After this treatment, the contents of the vacuum chamber are delivered to a settling and electrolysis tank for further treatment, step  120 . 
     After settling, as described below, lipids (oils) are skimmed and delivered to a container for lipids, step  125 , and settled debris is delivered to a container for oil-less debris, step  130 . Next, an electrolysis step is activated in the settling and electrolysis tank for a predetermined period of time, step  135 . After electrolysis has been stopped, a phosphorous-rich scum layer has formed at the top of the water in the settling container and phosphorus-rich rust has settled to the bottom, step  140 . 
     The scum layer is manually skimmed from the top of the water in the container and the rust is drained from the bottom of the container. These are moved to a phosphorous storage container, step  145 , where they can be dispensed for agricultural uses. Next, the water in the settling container is returned to the pond from which it came, step  150 . 
     Optionally, a portion of the oil-less debris can be further processed by methods such as those taught in my above-mentioned pending patent applications to yield, among other things, ethanol. A portion of the ethanol so produced can be delivered back to the pond to retard the growth of micro-algae, step  155 . 
     The above process rectifies the phosphorus cycle in the pond so that macro-algae, i.e., those of diameter greater than 15 microns, flourish. The above process can be repeated indefinitely, as required to maintain a healthy phosphorous level in the pond. 
     —Apparatus— FIG. 2   
       FIG. 2  shows apparatus for accomplishing the above process steps according to a preferred embodiment. A first vessel  200  comprises a lower tank portion  205  that has a removable lid  210 . Tank  205  is generally cylindrical with a flat bottom. Lid  210  is dome-shaped and sized so that its lower edge mates securely in an airtight fashion with the upper edge of tank  205  when the two are joined together. Clamps and guides (not shown) can be used to ensure that lid  210  remains in its proper, sealing position on tank  205 , if desired. Depending upon the size of vessel  200 , lid  210  can be lightweight enough to be removed manually or if it is heavy it can be lifted by a crane (not shown). 
     Lid  210  further includes a port  215  that terminates in a two-way valve  220 . In a first position, valve  220  opens port  215  to ambient air through a conduit  225 . In a second position, valve  220  connects port  215  to a vacuum source  230  via a conduit  235 . 
     Tank  205  optionally includes an inlet  240  with a valve  245  and an outlet  250  with a valve  255 . Inlet  205  can be omitted if tank  205  is filled from above while lid  210  is removed. Tank  205  is supported on a rigid surface  258  by a plurality of footed legs  265  or other means. Alternatively, tank  205  can rest directly on surface  258 . The bottom of tank  205  is generally flat and level, although it can be sloped toward outlet  250 , if desired. 
     A second tank  260  is arranged to receive the contents of tank  205  when valve  255  is opened and no vacuum is present in vessel  200 . A water source  231 , preferably the pond from which the algae are harvested, supplies water to tank  260  via a conduit  233  and a valve  232  when valve  232  is open. 
     Tank  260  rests on a rigid surface  261 , which may or may not be at the same level as surface  258 . A plurality of footed legs  266  supports tank  260 . If surface  261  is sufficiently lower than surface  258 , the contents of tank  205  can flow through outlet  250  and open valve  255  into tank  260  by gravity. Otherwise, an optional pump  270  can be used to move the contents of tank  205  via a conduit  271  into tank  260  at the proper time. 
     An outlet conduit  275  is located at the bottom of tank  260 . Outlet  275  is connected to one-way valves  280 ,  281 , and  282 . A storage container for oil-less debris  290  is connected to valve  280  via a conduit  283 . A storage container for scum and rust  268  is connected to valve  281  via a conduit  284 . A conduit  285  connected to valve  282  returns the contents of tank  260  to pond  231 . 
     Valves  280 ,  281 , and  282  are normally closed and are opened one-at-a-time, as described below. The bottom of tank  260  is optionally sloped to permit all contents of tank  260  to easily exit via conduit  275  at the proper times. 
     A plurality of electrodes  295  are arranged around the perimeter of tank  260 . A connector  296  is affixed to each electrode  295 . Connectors  296  can be hanged from above (not shown) in order to support electrodes  295 , or electrodes  295  can be captured along the sides of tank  260  by a series of fingers or slots  300  ( FIG. 3 ) that are affixed to the inner surface of tank  260 . Fingers or slots  300  do not cover electrodes  295 , but are just sufficient to hold electrodes  295  in place while exposing the maximum area of electrodes  295  to the contents of tank  260 . 
       FIG. 3  shows a top view of tank  260  and the arrangement of electrodes  295  and a second set of electrodes  320 . All of electrodes  295  are connected together by a conductor  305 . Conductor  305  in turn is connected to the positive terminal of an electrical source  315 , such as a battery, solar cell array, generator or other direct-current source that can deliver between 12 and 24 volts to the electrical load comprising the contents of tank  260  during electrolysis, as described below. Other voltages are possible. 
     A second set of electrodes  320  is connected to a second conductor  325 . Conductor  325  is connected to the negative terminal of source  315 . The length of electrodes  320  is generally equal to the length of electrodes  295 , i.e. they extend from the top of tank  260  to the bottom. Electrodes  320  are generally hung from the top of tank  260  so that they can be easily lifted out for cleaning. The combined surface areas of electrodes  295  is preferably about equal to the combined areas of electrodes  320  and the volume of electrodes  295  is preferably greater than the volume of electrodes  320 , as explained below. 
     Tank  205  is preferably made of stainless steel and has diameter and height equal to 1.5 and 0.3 meters, respectively. Tank  205  must be able to hold a mixture of water and algae to a depth of about ⅓ full, and withstand a moderate vacuum of about 0.2 bar. All plumbing fittings attached to vessel  200  are preferably brass, but other materials can be used. Tank  260  preferably holds about 2,000 liters and is made of a nonmetallic, electrically non-conductive material such as plastic. Electrodes  295  and  320  are preferably made of iron that does not contain chromium, zinc or other materials normally used in steelmaking. Such materials can contaminate the contents of tank  260  and may produce compounds that are toxic to algae and animals. Ordinary reinforcing bar used in concrete construction is an ideal material for this use since it is inexpensive and widely available. Electrodes  320  are alternatively made of sheet iron and are deliberately prepared with a layer of rust. 
     Tank  260  is preferably open at the top. During the electrolysis phase of operation, gaseous oxygen and hydrogen are liberated from the contents of tank  260  and it is necessary that these gases be disposed of by venting into open air in order to prevent the possibility of an explosion. Alternatively, these gases can be disposed of by being captured and retained for another use. 
     —Operation— FIGS. 1 and 2   
     The following steps are conducted prior to processing. A pond is selected where algae are plentiful in the aquatic environment and the operators, ecological technicians, or biologists suspect that phosphate levels may be excessive ( FIG. 1 , step  100 ). Well-known testing procedures are used to confirm these levels. When the levels are high, a dredge is used to harvest healthy macro and micro-algae that concentrate at the surface of the water ( FIG. 1 , step  105 ). After harvesting, the algae are first delivered to a collection station where they are ground and packaged in preparation for processing as discussed below. The ground algae can be wrapped in cheesecloth for ease of handling, if desired. The algae are now ready for processing in the apparatus according to the present embodiment. 
     Vacuum Treatment 
     Moist algae are placed in tank  205  ( FIG. 1 , step  110 ), the cheesecloth used in transporting them (if any) is removed, and lid  210  is secured on tank  205 . Tank  205  is filled about one-third full since the algae will bubble and foam when closed vessel  200  is evacuated. Next, vacuum source  230  is activated and valve  220  is turned to connect pump  230  to vessel  200  ( FIG. 1 , step  115 ). 
     When the pressure within vessel  200  has decreased to about 0.5 bar (about 0.5 atmosphere or 7 psi) and the temperature is about 20° C., the algae cell walls will burst. The operation of pump  230  continues until the pressure within vessel  200  reaches about 0.2 bar in order to ensure that most of the algae walls have burst. 
     Next, valve  220  is turned so that air is admitted into vessel  200 , and vacuum pump  230  is deactivated. When the interior of vessel  200  has reached atmospheric pressure, lid  210  is removed. The operator (not shown) then opens valve  255  and optionally activates pump  270  in order to deliver the contents of tank  205  to tank  260  ( FIG. 1 , step  120 ). The operator can use water spray to clean out tank  205  at this time in preparation for vacuum treating another load. Valve  232  is opened to supply water from source  231  to tank  260  via conduit  233 . Water is added from source  231  until the contents of tank  260  rise to a level just below the tops of electrodes  295 , and below the top of tank  260 . 
     Settling Treatment 
     At this point, the contents of tank  260  include water and algae with burst cell walls. Although their cell walls are burst, it is still necessary to remove the contents of the algae from their burst cells in order to perform the next steps. A number of biological materials are used to assist in removing the contents. Live, active cultures of bacteria such as  Bifidus lactus, L. acidophilus, L. bulgaricus, L. casei, L. paracasei, L. plantarium, L. rhamnosus , and  S. thermophilus  are used. These are among the biologicals that produce the enzymes that digest the results of algae blooms in nature and, therefore, are introduced here to dissolve the artificially created algae bloom produced in the controlled conditions of this setting. The desired biological materials are stored in a container  264  for manual addition to tank  260  at the start of the settling step. 
     After introduction of the biological materials from container  264  to tank  260  and a brief stirring to disperse them, the contents of tank  260  are allowed to rest undisturbed for about two hours ( FIG. 1 , step  120 ). During this time, the biological materials will cause the algae to release their contents; these comprise lipids (oils), phosphorous, and the oil-less mash including carbohydrates and proteins. 
     During the settling process, the contents of tank  260  are in contact with the rusty iron metal comprising electrodes  320 . The phosphorus in the contents of tank  260  combines chemically with the rust on electrodes  320 . Well-known means (not shown) can be used to measure the phosphorus content in the rust on electrodes  320 . When little or no more phosphorus is being collected in the rust, preparation is made for the next step in the process, the treatment by electrolysis. 
     The lipids, which will have risen to the top of tank  260 , are skimmed and stored for another use, such as biodiesel production ( FIG. 1 , step  125 ). Oil-less debris comprising cell walls will have settled to the bottom of tank  260  and are delivered through valve  280  to container  290  ( FIG. 1 , step  130 ). Valve  280  is open only long enough for the oil-less debris to move from tank  260  to container  290 ; then it is closed again. 
     Electrolysis Treatment 
     After the lipids and oil-less debris have been removed, the water level in tank  260  is brought back to just below the tops of electrodes  295  and  320 . Electrolysis will now be used to remove the phosphorus from the rust on the electrodes ( FIG. 1 , step  135 ). 
     Electrolysis is a technique used for removing rust from iron. It is a standard technique well known to tool collectors. It uses the effect of a low voltage direct current and a suitable electrolyte solution. This electrolytic method returns the rusted surface to metallic iron, rust scale is loosened, and can be easily removed along with the phosphorous that has adhered to it. The technique and the solutions used can be selected to be not hazardous. The voltages and currents are low, so there is minimal electrical hazard. The procedure can be conducted in a manner that no noxious fumes are produced. The method is self-limiting in that it is impossible to over-remove either the rust or the phosphorous. When there is no more rust to remove, the reaction stops. If desired, an ionic conductor such as sodium carbonate can be added to the contents of tank  260  in order to increase their electrical conductivity and speed the electrolysis. However, this is usually not necessary. 
     Source  315  is attached to electrodes  295  and  320 , as shown in  FIG. 3 . Electrodes  295  are connected to the positive terminal of source  315  and electrodes  320  are connected to the negative terminal. Good electrical contact is essential. Multi-part objects must have good electrical connections between them. Positive electrodes  295  are sacrificial and will erode over time and need to be replaced. During electrolysis the water, which will eventually be returned to pond  231  ( FIG. 1 , step  150 ), will become iron-rich but that is usually a benefit to many plants rather than a problem. Evaporation and electrolysis will deplete some of the water from the container. The lost water can be replaced as needed by temporarily opening valve  232 . 
     When source  315  is turned on, there will soon be a large volume of tiny bubbles in the solution. These bubbles are oxygen and hydrogen and are flammable. Some of the rust and anything attached to it will bubble up to the top and form a cloudy looking layer there. More such material will form on the electrodes. Eventually they will need to be cleaned or replaced. The electrodes give up metal over time. Re-bar (concrete reinforcing bars or rods) are such a good choice for the electrodes as they are inexpensive and easy to acquire in any length. The solution is electrically live. The power must be turned off before making adjustments or placing hands into the solution. 
     Typical cleaning time for removal of phosphate-bearing rust from electrodes  320  by electrolysis is a few hours. This time depends on the size of the rust surface and of the iron electrode. Visual inspection or manual disturbance by rubbing will provide clues as to the amount of rust remaining. When most of the rust is removed from electrodes  320 , source  315  is deactivated and electrolysis stops ( FIG. 1 , step  140 ). 
     The scum material that has risen to the top is skimmed and placed in storage container  268 . Then the bottom of tank  260  is opened to flush the remaining phosphorus-rich rust to storage container  268  ( FIG. 1 , step  145 ). This phosphorous rich material is ready for agricultural purposes. The remaining water in tank  260  is now returned to pond  231  from which it came ( FIG. 1 , step  150 ). 
     The iron collection surfaces that had rust at the beginning of the collection effort, are now rest free, and may now be returned to a rusty state for the next production run by simply allowing them to be exposed to air under wet or damp conditions. They may be ready for reuse as soon as over night. When exposed to the air, the wet iron surface will acquire surface rust very quickly again. 
     It is likely that the pond was brought to the attention of the process implementer initially because of a problem with excess of the wrong kind of plant life. The pond maintenance project can be used as part of an overall plan to return it to a healthy state. A healthy pond presents a better opportunity for sustainable harvest of macro-algae for bio-fuel feedstock. An overall plan would show that removal of the excess phosphorous is most efficiently achieved by placing many rust sheet collectors all over the pond to soak up as much material as possible in a short time. This may require employing several extra temporary crews and operating several extra processors just to get the phosphorous levels down to a sustainable replacement level. The crews&#39; only job would be to process the phosphorous by retrieving the many rust surfaces and performing the electrolysis operation on a massive scale. 
     As the feedstock is harvested and the carbohydrates in the oil-less mash are converted to bio-alcohol, the operators may choose to flush the material back into the pond to provide an ample supply of carbon to complement the nitrogen and phosphorus that are present. The reason the phosphorus is excess is that the plants are not able to process it and the nitrogen because they lack sufficient carbon. Those skilled in the art will find a balance point where the introduction of the ethanol would selectively control the micro-algae by allowing the macro-algae to flourish. Proof of success is that there is never again an algae bloom and fish die-off. The water will look relatively clear. Additionally, there are bacteria that produce enzymes that would help disperse the bloom and minimize its effects if it should occur before achieving ecological balance. The procedure introduced here causes a bloom of sorts under controlled conditions outside the pond. Such bacteria would be introduced as a temporary measure and would remain in the pond at sustainable levels for future use as necessary. 
     Conclusion, Ramifications, and Scope 
     Accordingly the reader will see that, according to one or more aspects, I have provided a method and apparatus for removing phosphorous compounds from pond water. The apparatus is relatively small, low cost, simple, safe, and portable. The process is rapid and simple enough to be performed by a small crew of semi-skilled operators, even in remote settings. It will not pollute the environment and will not contaminate feedstock for other uses. The process and apparatus maintain the ecosystem, improve the economics of producing alternative energy, and recover excess phosphorous material for other uses. 
     While the above description contains many specificities, these should not be construed as limitations on the scope, but as exemplifications of some presently preferred embodiments. Many other ramifications and variations are possible within the teachings. For example, vacuum disruption of the plant cell walls will work with other waterborne or water-rich vegetative matters in addition to algae. Other plants in the pond will contain phosphorous and after the phosphorous removal, they can be used as feedstocks for other processes. For example, cattails also take up phosphorous and they can yield carbohydrates for ethanol production. They can be ground up and used in the same ways as algae. Yeast, fungi, and other micro-biologicals can be used to extract the contents from the burst cells. Selection of the biologicals depends upon their suitability for use in a particular location. A cocktail of biologicals can used initially, then after a few weeks the population of biologicals will adjust to a particular setting. In addition, native and wild strains will appear. All aspects of the preferred embodiments are scalable to any size and to handle any volume of material. Many kinds of vegetative material can be harvested and treated. Instead of manual operation, the operation of the separation system can be automated. Instead of one settling tank, there can be many. In a properly treated pond, aquaculture, the growing of fish and shellfish is possible since the water is cleaned and its acid-base level is properly adjusted. Excretions from the fish will add nitrogen and phosphorous to the pond and contribute to the cycle of harvesting phosphorous from the pond. Besides extracting the phosphorous the combination of several yields is possible, thereby increasing the cost-effectiveness of the project. Electrical energy used to power the vacuum source, pumps, and electrolysis can be at least partially supplied by solar collectors. If the pond is strongly acidic, it can be turned into a source of energy by placing one electrode in the pond and another electrode into the ground nearby, thereby using the pond as a battery with the pond water being an electrolyte. Of course once the pond is properly cleaned the latter option will no longer be viable. 
     Thus the scope should be determined by the appended claims and their legal equivalents, and not only by the examples given.