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 . fig1 is a flow diagram describing the steps used in phosphate recovery according to a first embodiment , while fig2 shows a suitable apparatus for realizing the steps of fig1 . 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 . fig2 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 ( fig3 ) 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 . fig3 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 . 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 ( fig1 , 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 ( fig1 , 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 . moist algae are placed in tank 205 ( fig1 , 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 ( fig1 , 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 ( fig1 , 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 . 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 ( fig1 , 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 ( fig1 , 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 ( fig1 , 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 . 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 ( fig1 , 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 fig3 . 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 ( fig1 , 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 ( fig1 , 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 ( fig1 , 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 ( fig1 , 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 . 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 .