AU641902B2 - Wastewater treatment system - Google Patents

Wastewater treatment system Download PDF

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Publication number
AU641902B2
AU641902B2 AU42261/89A AU4226189A AU641902B2 AU 641902 B2 AU641902 B2 AU 641902B2 AU 42261/89 A AU42261/89 A AU 42261/89A AU 4226189 A AU4226189 A AU 4226189A AU 641902 B2 AU641902 B2 AU 641902B2
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Australia
Prior art keywords
wastewater
substratum
particulate material
coarser
layer
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AU4226189A (en
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Peter Francis Breen
Alan John Chick
David Searle Mitchell
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Commonwealth Scientific and Industrial Research Organization CSIRO
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Commonwealth Scientific and Industrial Research Organization CSIRO
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Water Treatment By Sorption (AREA)

Description

OPI DATE 02/04/90 APPLN. ID 42261 89 PCT AOJP DATE 10/05/90 PCT NUMBER PCT/AU89/00372 INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (51) International Patent Classification 4: (11) International Publication Number: WO 90/02710 C02F 3/32 Al C2F3/32 A (43) International Publication Date: 22 March 1990 (22.03.90) (21) International Application Number: PCT/AU89/00372 (74) Agents: KILBORN, Paul, Anthony et al.; Sirotech Limited, 580 Church Street, Richmond, VIC 3121 (AU).
(22) International Filing Date: 5 September 1989 (05.09.89) (81) Designated States: AT (European patent), AU, BB, BE Priority data: (European patent), BF (OAPI patent), BG, BJ (OAPI PJ 0245 5 September 1988 (05.09 38) AU patent), BR, CF (C PI patent), CG (OAPI patent), CH (European patent), '4 (OAPI patent), DE (European patent), DK, FI, FR .European patent), GA (OAPI pa- (71) Applicant (for all designated States except US): COMMON- tent), GB (European patent), HU, IT (European patent), WEALTH SCIENTIFIC AND INDUSTRIAL RE- JP, KP, KR, LK, LU (European patent), MC, MG, ML SEARCH ORGANISATION [AU/AU]; Limestone (OAPI patent), MR (OAPI patent), MW, NL (European Avenue, Campbell, ACT 2601 patent), NO, RO, SD, SE (European patent), SN (OAPI patent), SU, TD (OAPI patent), TG (OAPI patent), US.
(72) Inventors; and Inventors/Applicants (for US only) BREEN, Peter, Francis [AU/AU]; 4 Montrose Court, Murrumbeena, VIC 3163 Published CHICK, Alan, John [AU/AU]; Flat 2, 73 Hood With internationalsearch report.
Street, Coffs Harbour, NSW 2450 MITCHELL, David, Searle [AU/AU]; 69 Buller Crescent, Albury, NSW 2640 (AU).
(54) Tite: WASTEWATER TREATMENT SYSTEM (54)TitIe: WASTEWATER TREATMENT SYSTEM 52 84 (57) Abstract A wastewater treatment system and method utilising emergent aquatic plants wherein the plants (48, 68, 26) are planted in a porous substrate (41, 72, 28) enclosed by a water impervious boundary (44, 74, 80). The roots of the plants extend into the substratum to form a root zone. An inlet means (50, 76, 82) is arranged such that wastewater enters the system below the rootzone and flows upwardly through the substratum. The wastewater is removed by outlet means (60, 86) located adjacent the rootzone.
PCT/AU89/00372 WO 90/02710 WASTEWATER TREATMENT SYSTEM This invention relates to a water treatment system and method and is particularly concerned with a system and method for wastewater treatment using aquatic plants.
Artificial wetlands have a potential for low maintenance, low-cost treatment of rural, urban and industrial wastewaters for removal of nutrients and heavy metals and particulate material.
A combination of physiological, microbiological and physico-chemical processes, which are most active in the rootzone, are important in the treatment of wastewater.
These are: absorption of nutrients by the plants; the conversion of the organic forms of nitrogen and ammonia to nitrate at aerobic microsites where small amounts of oxygon leak from the plant roots into the otherwise anaerobic system; adsorption of waste substances onto the inorganic and organic particles in the substratum; sedimentation of particles so the the water becomes clear.
Most artificial wetland systems have been based on horizontal flow formats, either the longitudinal flow trench style design (Seidel, 1976; Pope 1981), or the transverse flow rootzone method design (Kickuth, 1977; Brix 1987).
Artificial wetlands have typically been simple earth structures (usually trench shaped) filled with a porous SUBSTITUTE SHEET WO 90/02710 PCT/AU89/00372 2 substratum such as gravel and planted with emergent aquatic macrophytes. In this conventional system, wastewater is introduced into the system and allowed to percolate down through and out of the system under gravity. The performance of these common trench-style systems is variable. The main problem with the conventional system is considered to be the non-ideal hydrology resulting in poor wastewater-root zone contact.
Tracer experiments carried out by us on flow patterns in trench style systems have shown divergence from the ideal plug flow condition for that system. The results indicate short circuiting of between half to three quarters of the upper strata of the trench profile. These hydraulic results are considered to be a direct function of the system design and to have a major influence on the system treatment process. Plant root densities usually decrease with the depth down the profile. As a result, the growth of aquatic plants in trench systems results in a profile with increasing hydraulic conductivity with depth, as roots progressively occupy the interstitial spaces in the upper strata. Consequently the wastewater short circuits the rootzone.
It is an object of the present invention to overcome or at least mitigate the abovementioned problem attending conventional systems. In particular it is an object to provide a system and method which improve wastewater-root zone contact.
The term "wastewater" as used herein is to be construed in its widest sense and includes domestic, agricultural and industrial effluent for example primary settled sewage, effluent from abattoirs and feedlots, seepage from mine tailings and water impoundments at mine sites.
SUBSTITUTE SHEET -3- In one aspect the present invention provides a method of treating wastewater, said method comprising the steps of: providing treatment system comprising a substratum of particulate material having a particle diameter of at least 3mm contained within a substantially water impervious boundary planted with a plurality of emergent aquatic plants the roots thereof extending at least partially into the substratum to form a rootzone therein; a layer of coarser particulate material below said substratum; and means to avoid short-circuiting of. influent. wastewater up at least one system surface prone to causing short-circuiting, the means to avoid short-circuiting extending from said at least one prone surface into the particulate material of the substratum or of the coarser layer; supplying the wastewater to the layer of coarser particulate material for vertical upflow of the wastewater to the rootzone; and removing treated wastewater from one or more locations adjacent the rootzone.
In a further aspect the invention provides a wastewater treatment system comprising: a substratum Of particulate material having a particle diameter of at least about 3mm contained within a substantially water impervious boundary; a plurality of emergent aquatic plants planted in the substratum such that the roots thereof extend at least partially into the substratum to form a rootzone therein; -3a- A layer of coarser particulate material below said substratum; means for supplying influent wastewater to the layer of coarser particulate material for vertical upflow of the wastewater to the rootzone; one or more system effluent outlets located adjacent the root zone; and means to avoid short-circuiting of influent wastewater up at least one system .surface prone to causing short-circuiting, the means to avoid short-circuiting extending tirom said at least one prone surface into the particulate material of the substratum or of the coarser layer.
The plants utilised may be any suitable aquatic plant and may be, for example, Typha domingensis, Phragmites australis, Schoenoplectus lacustris or Schoenoplectus validus.
t
S
i S WO 90/02710 PCT/AU89/00372 4 Scw.en_pl ectufs va. j1 id-'.
Preferably the system is conditioned before use by controlling the amount of nutrient entering the system so as to ensure sufficient root mass. If high nutrient material such as primary settled sewage is provided too early, insufficient root mass may develop.
The system may be above-ground or in-ground. In the case of the former, the substantially impervious boundary may be a plastic, cement, metal or like containment material. In the case of an in-ground system the boundary may be consolidated earth, such as that used in an earth dam, clay or plastic lining. By "substantially water impervious" we mean that the boundary is sufficiently impervious to prevent significant seepage from the system.
The porous substratum may be formed from gravel and the like or any other suitable particulate water insoluble material. Preferable the porous substratum is formed from gravel having a diameter of approximately 3 to 10 mm, preferably 5 to 10 mm.
The means for supplying wastewater may be a pipe or conduit extending downwardly into the body of the porous substratum. There may be a network of pipes into the system. Alternatively, the means may be external to the system and have an outlet communicating with the substratum. The system outside walls may, together with one or more substantially water impervious partitions, form the sides of the means for supplying wastewater. For example, a partition may be located vertically within the system boundary so that it extends between opposite walls of the boundary to form a trench-like structure adjacent the substratum. The bottom of the partition may be spaced from SUBSTITUTE
SHEET
the system base so as to allc? influent to pass to the substratum.
The means for supplying wastewater may be filled with relatively large particulate material to augment the treatment of the influent wastewater. The particle diameter of the relatively large particulate material may be larger than that of the substratum material. Preferably the diameters of this particulate material are in the range of about 40 to 50 mm. This relatively large particulate material may extend horizontally in the body of the system and so support the relatively fine particulate material of the substratum and allow a relatively even supply of influent across the horizontal profile of the substratum. Further the relatively large particulate material is less prone to blocking by solid material in influent such as primary settled sewage.
The one or more system outlets are located adjacent the rootzone. It is particularly advantageous to locate the system S: .outlet(s) at least 5 cm below the substratum surface as this prevents both obnoxious odours being produced and insect (eg mosquitoes) breeding in the system. The system outlet(s) may be S a pipe or other conduit. The diameter of the pipe may be 100 mm and conventional agricultural PVC pipe may be used. The capacity of the system outlet(s) may be choseni to equalise flow paths between the system inlet(s) and outlet(s).
The means to avoid short circuiting of influent may be one or more flanges extending from the system outside wall(s) and/or from around the outlet of the means for supplying wastewater.
These means may be one or more flanges extending from the system outside wall(s) and/or from around the outlet of the means for supplying wastewater. These flanges may be made from any suitable "AF WO 90/02710 PC/AU9/00372 6 material such as plastic film, marine board, compacted clay the like.
The performance of experimental systems. using the vertical upflow regime of the present invention with respect to concentration and reduction of impurities in primary settled sewage using a 5 day retention time is given in Table 1.
TABLE 1 Typical System Performance Daily summary Variable Summer Winter Concentration In Out In Out (mg 1-1) TN 20.5 1.0 36.0 2.1 TP 4.6 0.2 6.8 0.4 TCOD 122.1 59.1 208.1 52.3 Load In Out In Out (mg removal removal m-2d-1
TN
TP
TCOD
310.6 69.0 1849.0 7.2 1.8 449.0 97.7 97.3 75.7 545.2 102.9 3159.5 23.6 4.0 602.4 95.7 96.1 80.9 SUBSTITUTE
SHET
I
SWO 90/02710 PCT/AU89/00372 7 Temperature conditions Mean max. 32.7 21.2 min. 17.2 3.1 daily 24.9 12.2 Median 25.0 12.3 Range 12-40 1-27 Abbreviation: TN Total Nitrogen TP Total Phosphorus TCOD Total Chemical Oxygen Demand It will be clear from these results that the present invention provides essentially a single unit alternative to a conventional secondary-tertiary system combination. The invention provides high treatment performance particularly for removal of problem elements such as phosphorous.
The system of the invention is a particularly attractive alternative when the cost advantage is considered. We have found that loads can be increased, and retention times decreased several-fold with no drop-off in performance.
Thus the system of the present invention is particularly flexible and easily managed under a range of operating conditions. A particular advantage of the system of the present invention is that the influent can be primary settled sewage thus reducing the need for extra plant.
The system is a particularly suitable for small community sewage requirements. For example, for a 1,000 person equivalent system, where the population will be becoming on-line over a period of time, four 250 person equivalent units may be used. The depth of each unit may be about 1.
metre, have a Pore Volume factor of about 3 and a retention time in the order of 5 days. For the following person equivalent discharge rates, the 250 person equivalent sizes are:- 35 -1 -1 7 C 9 2 200 L person d system area 4P&em (27 x 27m) SUBSTITUTE
SHEET
'y WO 90/02710 PCT/AU89/00372 -1 -1 m2 300 L person d system area f5; m (33 x 33m) Retention times may be as low as 1.25 days. The upper limit on size of the system of the invention is set by the ability to provide the plants with sufficient water.
The invention will now be described more particularly, by way of example only, with reference to the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is top plan view of one embodiment of the invention; Figure 2 is a sectional view taken generally along A-A of Figure 1; Figure 3 shows a top plan view of a further embodiment of wastewater treatment system in accordance with the invention; Figure 4 a sectional view taken along B-B of Figure 3; Figure 5 illustrates a domestic system in accordance with the invention.
BEST MODES FOR CARRYING OUT THE INVENTION It is to be understood that invention is not limited to the following described embodiments.
Referring first to Figures 1 and 2 there is shown a wastewater treatment system 30 which comprises an approximately 700 mm deep substantially porous substratum 41 comprising 5 to 10 mm washed gravel contained within a retaining wall 44 formed from consolidated earth. If the L- SUBSTITUTE
SH£ET
RECEIVED 0 8 AU8V M PC/MA C3 0 3 7 1 earth is not sufficiently water impervious a clay lining may be provided.
The substratum 41 is planted with plants 48 such that their roots extend therein. The planted surface of the system may have an area ranging from llxll m to 35x35 m, although it will be clear that the size of the planted area may be selected to suit the load to be placed on the system.
Wastewater for treatment is supplied through pipe which may be 1.2 -1.8 m standard culvert pipe. This pipe is filled with 40 to 50 mm cobbles and communicates with the substratum via a layer of cobbles of 40 to 50 imm diameter on the floor of the system. Preferably the cobbles in the pipe extend above the level of the substratum surface so that the influent wastewater passes over dry cobbles to assist in the treatment of carbon. This layer may have a depth of 200 to 300 mm. In this form the treatment of the invention acts as an aerobic organic matter degradation process and as an anaerobic BOD filter, the former in the inlet setup and the latter in the cobbles extending below the substratum.
Flange 52 is located around the outlet of the pipe so as to prevent short circuiting of the wastewater up the level exterior surface of the pipe. The flange may be formed from plastic film. A flange 54 is also provided at the inside wall of the structure so as to prevent short circuiting up the level surfaces of the containing wall(s).
One or more system outlets 60 are provided at least 5 cm below the substratum surface. These outlet may be conventional 100 mm PVC agricultural pipe.
SUBSTITUTE SHEET RECEIVED 3 AUG 1990 -sa- P/AU 8 9 0 03 7 2 1 In operation wastewater 10 is introduced into the system through pipe 50 setting up vertical upflow of wastewater so that the wastewater is forced upwards against gravity towards the rootzone of plants 48. The purified SUBSTITUTE
SHEET
WO 90/0:,:10 PCT/AU89/00372 10 wastewater then exits from the system through the one or more outlets We have found that the a.ove system maximises wa-te water-root zone contact and reduces short circuiting. The upflow movement of wastewater also results in the system being virtually flood proof. The system can be operated so that there is no freestanding surface water for pests, for example mosquitoes, and odour is minimised.
Figures 3 and 4 illustrate alternative arrangement of the system of the invention in which the wastewater is introduced to the system via a trench like structure. Here substratum 72 of washed 5 to 10 mm gravel, planted with plants 68 is contained within retaining walls 74. In this case the planted surface area is 15x5 m. A 15 m water impervious partition 78 extends between opposite walls 74 and is located approximately 1 metre from the parallel retaining wall 74a to form a trench inlet 76. Inlet 76 is filled with 40 to 50 mm cobbles and communicates with the substratum 72 via a layer of cobbles 70, the combined depth of the substratum and cobbles being approximately 1 m. A flange 80 is located perpendicularly to the base of the partition 78 to prevent short circuiting up the partition. Flange 82 extends from the wall(s) 74 to prevent short circuiting up the retaining walls. One or more system outlets 86 are located adjacent the rootzone at least 5 cm under the substratum surface.
This structure may have a substratum bed area of 6m by Wastewater such as primary settled sewage is introduced into the system through inlet 76 and enters the substratum 72 via cobbles 70 and then vertically upwards towards the rootzone.
SUBSTITUTE SHEET m i J WO 90/02710 PCT/AU89/00372 11 Figure 5 illustrates a single house domestic treatment unit 24 in accordanc with the invention. The system comprises a 5 m diameter containment wall 80 fabricated from fibreglass, concrete or other suitable material.
Plants 26 are planted in a 5 mm gravel layer 28.
Influent from a septic tank is introduced into the system through pipe 82. The wastewater passes from the pipe 82 upwardly towards the rootzone via cobble layer (40 mm) 84. Purified effluent is removed at points 86. The capacity of the unit can be set by the cubic metres of gravel used in the system.
Finally, it is to be understood that various alterations, modifications and/or additions may be introduced into the constructions and arrangements of parts previously described without departing from the spirit or ambit of the invention.
REFERENCES
SEIDEL, K. (1976). Macropnytes and water purification. In Biological control of water pollution (eds. Tourbier, J. Pierson, University of Pennsylvania Press, Philadelphia, pp. 109-121 POPE, P.R. (1981). Wastewater treatment by rooted aquatic plants in sand and gravel trenches. (EPA-600/2/81-091), US Environmental Protection Agency, Cincinnatti, Ohio.
KICKUTH, R. (1977) Degradation and incorporation of nutrients from rural wastewaters by plant rhizosphere under Limnic conditions. In Utilization of manure by land spreading. (Ed Voorburg, Commission of European Communities EUR 567Ze, London, pp 335-343.
SUBSTITUTE
SHEET
hrs r+ -11imir WO 90/02710 PIAU8/07 PCr/AU89/00372 12 BRIX H. (1987) Treatment of wastewater in the rhizosphere of wetland plants the rootzone method.
Water Science Technology. 19: 107-118 SUBSTITUTE SKEET

Claims (34)

1. A wastewater treatment system comprising: a substratum of particulate material having a particle diameter of at least 3mm contained within a substantially water impervious boundary; a plurality of emergent aquatic plants planted in the substratum such that the roots thereof extend at least partially into the substratum to form a rootzone therein; A layer of coarser particulate material below said substratum; a i means for supplying influent wastewater to the layer of coarser particulate material for vertical upflow of the wastewater to the rootzone; one or more system effluent outlets located adjacent the root zone; and means to avoid short-circuiting of influent wastewater up at least one system surface prone to causing Sshort-circuiting, the means to avoid short-circuiting extending from said at least one prone surface into the particulate material of the substratum or of the coarser layer.
2. The system of claim 1 wherein the porous substratum comprises particulate material of a diameter in the range of 5mm to 14
3. The system of claims 1 or 2 wherein the means for supplying wastewater is one or more pipes or the like conduits.
4. The system of claim 3 wherein the wastewater supply means is centrally located in, and extends downwardly into the system.
The system of claim 1 or 2 wherein the means for supplying wastewater is formed by the association of one or more partitions with one or more walls of the system boundary.
6. The system of claim 5 wherein the means for supplying wastewater comprises a vertical partition extending between opposite sides of the system boundary to form a trench-like structure, the structure having an outlet communicating with the layer of coarser material. S.
7. The system of claim 6 wherein the partition is spaced from the floor of the system boundary so as to allow wastewater to pass to the layer of coarser material.
8. The system of any one of the preceding claims wherein the means for supplying wastewater contains particulate material of a larger diameter than that of the substratum.
9. The system of claim 8 wherein the particulate material in the wastewater supply means extends above the substratum.
The system of claim 8 or claim 9 wherein the particulate material in the wastewater supply means are cobbles of diametez ranging from 40mm to 15
11. The system of any one of the preceding claims wherein the layer of coarser particulate material comprises cobbles of diameter ranging from 40mm to
12. The system of any one of the preceding claims wherein the one or more system outlets is located at least below the surface of the substratum.
13. The system of any one of the preceding claims wherein the means to avoid short circuiting is one or more flanges extending from the walls of the boundary.
14. The system of any one of the preceding claims wherein the means to avoid short circuiting is a flange extending from the outlet of the wastewater supply means.
15. The system of any one of the preceding claims wherein the emergent aquatic plants are selected from one or more of Typha domingensis, Phragmites australis, Schoenoplectus lacustris, or Schoenoplectus validus.
16. A method for treating wastewater, said method comprising the steps of: providing a substratum of particulate material having a particle diameter of at least 3mm contained within a substantially water impervious boundary planted with a plurality of emergent aquatic plants the roots thereof extending at least partially into the substratum to form a rootzone therein; a layer of coarser particulate material below said substratum; and means to avoid short-circuiting of influent wastewater up at least one surface prone to causing short-circuiting, the means to avoid short-circuiting extending from said at least one 16 prone surface into the particulate material of the substratum or of the coarser layer; supplying the wastewater to the layer of coarser particulate material for vertical upflow of the wastewater to the rootzone; and removing treated wastewater from one or more locations adjacent the rootzone.
17. The method of claim 16 wherein the porous substratum comprises particulate material of a diameter in the range of 5mm to
18. The method of claim 16 or claim 17 wherein the wastewater is supplied to the coarser layer by one or more pipes or the like conduits.
19. The method of any one of claims 16 to 18 wherein the wastewater supply means is centrally located in, and extends downwardly into, the system.
The method of claim 16 or claim 17 wherein the *wastewater is supplied by supply means formed by the association of one or more partitions with one or more walls of the system boundary.
21. The method of claim 20 wherein the means for supplying wastewater comprises a vertical partition extending between opposite sides of the system boundary to form a trench-like structure, the structure having an outlet communicating with the layer of coarser material.
22. The method of claim 21 wherein the partition is spaced from the floor of the system boundary so as to allow wastewater to pass to the layer of coarser material. ^LL' 17
23. The method of any one of claims 16 to 22 wherein the means for supplying wastewater contains particulate material of a larger diameter than that of the substratum.
24. The method of claim 23 wherein the particulate material in the wastewater supply means extends above the substratum.
The method of claim 24 wherein the particulate material in the wastewater supply means are cobbles of diameter ranging from 40mm to
26. The method of any one of claims 16 to 26 wherein the layer of coarser particulate material comprises cobbles of diameter ranging from 40mm to 4
27. The method of any one of claims 16 to 26 wherein the wastewater is removed from the system from a location at least 5cm below the surface of the substratum. 4
28. The method of any one of claims 16 to 27 wherein '4 the means to avoid short circuiting is one or more flanges extending from the walls of the boundary. I
29. The method of any one of claims 16 to 28 wherein the means to avoid short-circuiting is a flange extending from the outlet of the wastewater supply means.
The method of any one of claims 16 to 29 wherein the emergent aquatic plants are selected from one or more of Typha domingensis, Phracmites australis, Schoenoplectus lacustris, or Schoenoplectus validus.
31. The method of any one of of claims 16 to wherein the wastewater is sewage. Y4) 4 B 18
32. The method of claim 31 wherein the wastewater is primary settled sewage.
33. A wastewater treatment system as claimed in any.one of claims 1 to 15 as herein described with reference to the accompanying drawings.
34. A method for treating wastewater as defined in any one of claims 16 to 32 as herein described with reference to the accompanying drawings. 4 I i I 0 I S It l t..
AU42261/89A 1988-09-05 1989-09-05 Wastewater treatment system Expired AU641902B2 (en)

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AUPJ024588 1988-09-05
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Publication number Priority date Publication date Assignee Title
AU651828B2 (en) * 1990-07-02 1994-08-04 University Of New South Wales, The Wastewater treatment system

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4415450A (en) * 1981-12-28 1983-11-15 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Method for treating wastewater using microorganisms and vascular aquatic plants

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4415450A (en) * 1981-12-28 1983-11-15 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Method for treating wastewater using microorganisms and vascular aquatic plants

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