WO1999001385A1 - Waste water treatment system - Google Patents

Waste water treatment system Download PDF

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Publication number
WO1999001385A1
WO1999001385A1 PCT/AU1998/000534 AU9800534W WO9901385A1 WO 1999001385 A1 WO1999001385 A1 WO 1999001385A1 AU 9800534 W AU9800534 W AU 9800534W WO 9901385 A1 WO9901385 A1 WO 9901385A1
Authority
WO
WIPO (PCT)
Prior art keywords
chamber
liquid
filter medium
filter
site
Prior art date
Application number
PCT/AU1998/000534
Other languages
French (fr)
Inventor
Humberto Urriola
Original Assignee
Humberto Urriola
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Humberto Urriola filed Critical Humberto Urriola
Priority to AU82003/98A priority Critical patent/AU8200398A/en
Priority to EP98931837A priority patent/EP1017638A4/en
Publication of WO1999001385A1 publication Critical patent/WO1999001385A1/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1242Small compact installations for use in homes, apartment blocks, hotels or the like
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/04Aerobic processes using trickle filters
    • 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

Definitions

  • the present invention refers to a waste water treatment system, and in
  • wastes such as sewerage and slurries:- known as a point source solution.
  • liquid wastes and sewerage In the present treatment of liquid wastes and sewerage, the liquid waste
  • a centralised treatment system requires the use
  • liquid waste is high in phosphorus and nitrogenous compounds, which cause algae blooms and high COD (chemical oxygen demand) and BOD (biological
  • the present invention seeks to ameliorate the above problems by
  • biodegradable solids comprising:
  • a first chamber adapted to receive untreated effluent, said chamber
  • said second chamber containing a suitable filter
  • a third chamber located below the second chamber to receive the
  • the liquid in the third chamber can be oxygenated with air or oxygen, or
  • the present invention provides an on site waste water
  • a first holding chamber adapted to receive the waste water mixture
  • first holding chamber percolates through the filter medium ;
  • FIG 1 illustrates an on site liquid effluent treatment apparatus
  • FIG. 2 illustrates an on site liquid effluent treatment apparatus
  • FIG. 3 illustrates the liquid effluent treatment apparatus shown in figure
  • FIG. 4 illustrates the liquid effluent treatment apparatus shown in
  • FIG. 5 illustrates an on site liquid effluent treatment apparatus
  • Figure 6 illustrates an on site liquid effluent treatment apparatus
  • FIG. 7 illustrates an on site liquid effluent treatment apparatus
  • FIG. 8 illustrates an oil water separator according to an embodiment of
  • Figure 9 illustrates a view of a piece of drainage cell as shown in
  • Figure 10 shows actual test results of a trail of the filtration system of the
  • centre provides an on site treatment apparatus which could be used for a
  • apparatus (1 ) comprises an inlet pipe (2) to convey waste from the toilet system
  • the chamber (3) contains a geofabric or micro
  • filter bag (4) shaped so as to line the walls of the chamber (3).
  • the base (5) of the waste receiving chamber (3) is perforated and could
  • the worms are capable of eating their own
  • a filter chamber (11 ) lies directly below the receiving chamber (3), to
  • microfilter medium (4) such as a geofabric lies below the bottom surface (10) of
  • the chamber can be filled with a granulated filter medium (13).
  • This medium 13
  • the material is a granulate mixture of zeolite, with Borax as
  • Suitable bacteria is also preferably used in the filter
  • the granulated filter medium (13) could be
  • microfilter medium (4) contained in several bags (6) of microfilter medium (4), which are secured
  • Each bag could have a different strain of bacteria.
  • liquid In the process of liquid passing through a granular layer, liquid will be
  • perch water Further as liquid
  • filter medium (13) is sufficient to remove the impurities to a predetermined
  • the treated water is useable, for example, for watering the
  • the treated water then drips into a holding chamber (14) where it is
  • FIG 2 A further embodiment is shown in figure 2, which is of similar
  • the lower walls of the waste receiving chamber (3) have an impervious insert (7) to form a well (15) to retain a depth of the liquid as well as the faecal solids
  • the bacteria digest the faecal solids in a very fast time.
  • the present invention provides separation of the faecal solids from the
  • wastes flushing water, urine, faecal liquids, and liquids liberated by the
  • the bacteria breaks down the organic material into water and carbon dioxide,
  • waste receiving chambers each chamber with an air gap surrounding it, with a
  • the walls of the waste receiving chambers are porous and could be
  • the waste water treatment apparatus (1 ) could be
  • the tanks (16) could be contained in an impervious well
  • a pump (25) can be used to control
  • the various tanks (16) and their walls can be constructed, as shown in
  • FIG 1 of modules of ATLANTIS® DRAINAGE CELLS, the subject of
  • FIG. 5 A further embodiment is shown in figure 5, for use with a larger dwelling
  • chamber 19 could have a layer of filter medium (13) containing only
  • chamber (19) could be made of tank modules (16) as described in International
  • Filter medium (13), as mentioned in the first embodiment is used, and
  • each filter chamber (11 & 22) is separated by an air gap (8).
  • generated ozone can be used to increase the efficiency of the system and
  • the treated water percolates through the various filter chambers (11 &
  • FIG. 6 A further embodiment is shown in figure 6, which is similar in
  • Figure 7 illustrates a further embodiment which is similar to that shown in
  • drainage cells have small wells (30) to hold liquids in which bacteria collects
  • variable perch water through the filter medium variable perch water through the filter medium
  • FIG. 8 A further embodiment is shown in figure 8 for the purification of water
  • a filtered oil water mixture is fed into the initial holding chamber (24)
  • the filter chambers can be of any suitable thickness and porosity to suit
  • the various chambers and their walls can be constructed, as
  • FIG. 1 shown in figure 1 , of modules of ATLANTIS® DRAINAGE CELLS.
  • the on-site units could be adapted for connection to a single toilet or a

Abstract

A waste water treatment apparatus (1) for effluent containing biodegradable solids having a first chamber (3) for retaining the solids while allowing liquid effluents to pass therethrough to a filtering chamber (11) which contains a filter medium (13, 32). The solids (biomass) are digested by worms and/or bacteria in the first chamber (3) and the liquid effluents from the first chamber (3) are treated by bacteria which is in the filter medium (13, 32). The thus purified water passes into the holding chamber (14) from where it is used for gardening or as required.

Description

Waste Water Treatment System
The present invention refers to a waste water treatment system, and in
particularly a waste water treatment system for on site treatment of liquid
wastes, such as sewerage and slurries:- known as a point source solution..
In the present treatment of liquid wastes and sewerage, the liquid waste
is transported by underground impervious piping or open channel, to a central
treatment system or in extreme cases simply discharged into waterways or in
the case of mine effluent, the effluent is usually discharged into tile dams or
open basins without treatment. A centralised treatment system requires the use
of pumps, clarification equipment, and chemicals. The cost of maintaining and
installing such systems is extremely high, as it requires an extensive network of
impervious piping or open channels which usually occupies a large area of
valuable land. Further problems arise during heavy rain, because excess storm
water run off in some areas are directed into the sewerage system, which
results in raw sewage discharge from the sewerage systems into the streets
and the river systems or held in tile dams or open basins. Other problems occur
with broken pipes leaking untreated effluent into the local environment and
eventually into the water table, aquifers and river systems. Such leakage of untreated effluent can cause problems such as polluted
aquifers, river ways, soil contamination, algae blooms, unpleasant toxic
smells, air pollution, and illnesses, as well as reduction in the fauna and flora..
Further in isolated communities, such as mining settlements, and in
other areas where sewerage is not connected, individual on site sewerage
collection systems such as septic tanks, biological toilets and incinerator toilets
have been used, with varying degrees of success. However, increasingly, laws
are being enacted to prevent inefficient and unsafe system, including burning of
waste, because of the resultant air and water pollution, and to phase out septic
systems.
Problems, also, occur with the treatment of other waste water, both
domestic and industrial. In some systems bathroom and kitchen sink water are
fed directly into the sewerage system, thus greatly increasing the volume of
effluent, containing contaminated biomass in various degrees of decomposition,
travelling through the sewerage system. In other systems, these waste waters
are fed into anaerobic grease traps where the overflow percolates into the soil
and into the water table, or as run off and into the water ways. Some of this
liquid waste is high in phosphorus and nitrogenous compounds, which cause algae blooms and high COD (chemical oxygen demand) and BOD (biological
oxygen demand), hence deoxygenate the river systems.
The present invention seeks to ameliorate the above problems by
providing an on site liquid effluent treatment apparatus for effluent, containing
biodegradable solids, comprising:
a first chamber adapted to receive untreated effluent, said chamber
having at least a permeable portion to allow liquids to pass therethrough and to
retain the biodegradable solids in the first chamber, thereby substantially
dewatering the solids, and containing bacteria and/or worms to digest the
biodegradable solids;
a second chamber in cascade with the first chamber and separated
therefrom with an air gap, said second chamber containing a suitable filter
medium, such that liquid which passes through the first chamber percolates
through the filter medium ;
a third chamber located below the second chamber to receive the
treated liquid from the second chamber; and
an outlet from said third chamber to allow removal of the treated liquid
from the third chamber. The liquid in the third chamber can be oxygenated with air or oxygen, or
ozone, depending upon their toxicity levels.
In another form, the present invention provides an on site waste water
purification apparatus for purifying water containing liquid or dissolved
contaminants, comprising:
a first holding chamber adapted to receive the waste water mixture, said
chamber having a permeable base to allow liquids to pass therethrough;
a first filter chamber, in cascade with the first holding chamber, and
containing a suitable filter medium, such that liquids which passes through the
first holding chamber percolates through the filter medium ;
at least a second holding chamber, located below the first filter chamber
to receive the filtered liquid from the first filter chamber, and having a
permeable base; and
at least a second filter chamber in cascade with the at least second
holding chamber, and containing a suitable filter medium, such that liquid which
passes through the at least second holding chamber percolates through the
filter medium,
whereby the liquid or dissolved contaminants are separated from the
water as the water, firstly, percolates through the various filter medium, with the liquid or dissolved contaminants remaining in the filter medium, where it is
digested by bacteria.
The present invention will now be described with reference to the
accompanying drawings in which:
Figure 1 illustrates an on site liquid effluent treatment apparatus
according to one embodiment of the present invention;
Figure 2 illustrates an on site liquid effluent treatment apparatus
according to another embodiment of the present invention;
Figure 3 illustrates the liquid effluent treatment apparatus shown in figure
2, in a system for treating domestic washing water;
Figure 4 illustrates the liquid effluent treatment apparatus shown in
figures 1 or 2, in a system for treating sewerage;
Figure 5 illustrates an on site liquid effluent treatment apparatus
according to a further embodiment of the present invention; Figure 6 illustrates an on site liquid effluent treatment apparatus
according to a further embodiment of the present invention;
Figure 7 illustrates an on site liquid effluent treatment apparatus
according to a further embodiment of the present invention;
Figure 8 illustrates an oil water separator according to an embodiment of
the present invention;
Figure 9 illustrates a view of a piece of drainage cell as shown in
Australian patent no. 593085 which is suitable for use in the present invention;
and
Figure 10 shows actual test results of a trail of the filtration system of the
present invention.
In a full flush of a toilet, normally a minimum of six litres of flushing water
is used. Thus during a day a large volume of water is as well as the faecal
solids, which contain approximately 82-92% water, are flushed into the sewer
system. As the population of areas grow the load on the sewerage system
increases, and in some cases the system cannot cope. However the present invention, rather than have a centralised treatment
centre, provides an on site treatment apparatus which could be used for a
single toilet or a series of toilets, as well as bathroom and kitchen liquid waste,
thereby eliminating the need for a large network of piping throughout the city
and suburbs, and the subsequent maintenance cost and risks of major
overflows. Further the retention of the treated water, which could be used for
gardens , washing or other non potable uses, would lower the water usage from
the reservoirs.
The invention will now be described with reference to treatment of
domestic liquid effluent. As shown in figure 1 , the liquid waste treatment
apparatus (1 ) comprises an inlet pipe (2) to convey waste from the toilet system
(see figure 4) or the kitchen sink or bathroom (see figure 3) of a house into a
waste receiving chamber (3). The chamber (3) contains a geofabric or micro
filter bag (4), shaped so as to line the walls of the chamber (3).
The base (5) of the waste receiving chamber (3) is perforated and could
® be constructed, as shown in figure 9, of modules of ATLANTIS DRAINAGE
CELLS, which are shown in Australian patent no. 593085. These modules have
two parallel perforated surfaces (9 &10), joined by columnar members (27), forming an air gap (8) therebetween. On the under side of the support surfaces
(28) are upturned walls (29) which form wells (30) in which effluent is retained.
Therefore when the toilet is flushed the liquid waste and the faecal solids
are collected in the waste receiving chamber (3) as shown in figure 1 , where
the urine and liquid wastes drain through the bottom (5) of the waste receiving
chamber (3) . Suitable bacteria is placed in the waste receiving chamber (3),
together with manure worms. The worms and the bacteria digest the faecal
solids, which remain in the waste receiving chamber (3), in a very fast time, and
leave, as residue, worm castings. The worms are capable of eating their own
weight a day.
A filter chamber (11 ) lies directly below the receiving chamber (3), to
receive the filtered liquid waste from the waste receiving chamber (3). A
microfilter medium (4) such as a geofabric lies below the bottom surface (10) of
the base (5) of the receiving chamber (3), and a further microfilter medium (4)
such as a geofabric lies above the top surface of the perforated base (12) of the
filter chamber (11 ), which could be constructed, as shown in figure 1 , of
modules of ATLANTIS " DRAINAGE CELLS. Between the micro filter layers
(4), the chamber can be filled with a granulated filter medium (13). This medium
could be any suitable material such as sand or a mixture of sand and zeolite, together with a decontamination agent and of any suitable grain size. In the
embodiment shown the material is a granulate mixture of zeolite, with Borax as
the decontamination agent. Suitable bacteria is also preferably used in the filter
medium, to assist in the removal of contaminants.
However as shown in figure 1 , the granulated filter medium (13) could be
contained in several bags (6) of microfilter medium (4), which are secured
across the filter chamber (11 ) to ensure that all liquid must pass through the
filter medium (13). Each bag could have a different strain of bacteria.
The liquid waste, that passes from the receiving chamber (3), falls
through the air gap (8), onto the filter medium (13), and spreads along the filter
medium bed and percolates through the interstices between the grains of the
filter medium (13), where the pollutants are digested by the bacteria in the filter
medium (13).
In the process of liquid passing through a granular layer, liquid will be
retained in the granular layer in an increasing amount from the top of the layer
to the bottom, with very little or no liquid being present at the top to being
almost fully saturated with water at or adjacent the bottom of the layer. However
there are still air pockets in the interstices between the grains, in the lower level of the layers This retained water is known as "perch water". Further as liquid
percolates down through the layers, air flows upwardly. Therefore, as the
pollutants percolate through the granular layer, they pass from an aerobic
region through an increasingly anaerobic region. The thickness and top surface
area of the filter medium (13) is such that the retention time of the liquid in the
filter medium (13) is sufficient to remove the impurities to a predetermined
degree, such that the treated water is useable, for example, for watering the
garden.
The treated water then drips into a holding chamber (14) where it is
aerated as it falls into the chamber (14), and exits through the outlet (17). To
assist in the treatment process air or oxygen could be pumped into the treated
water in the holding chamber (14), to increase the aeration of the treated water
and also to increase the flow of oxygen through the filter medium (13). Also air
or oxygen could be fed into the lower levels of the filter medium (13).
Additionally a small mercury lamp could be used to convert some of the oxygen
into ozone, in the air that is pumped into the treatment system.
A further embodiment is shown in figure 2, which is of similar
construction to the embodiment shown in figure 1 except that the base (5) and
the lower walls of the waste receiving chamber (3) have an impervious insert (7) to form a well (15) to retain a depth of the liquid as well as the faecal solids
in the waste receiving chamber (3), while the remainder of the liquid effluent
flows over the impervious insert (7) and passes through to the filter chamber
(11 ). Suitable bacteria and a quantity of water is placed in the well (15), where
the bacteria digest the faecal solids in a very fast time.
The present invention provides separation of the faecal solids from the
liquid wastes, so that each can be treated separately. The solids being
separated, and digested by worms and/or specific bacteria, and the liquid
wastes: flushing water, urine, faecal liquids, and liquids liberated by the
digestion of the faecal solids, percolating through a reactive filter material where
the bacteria breaks down the organic material into water and carbon dioxide,
and breaks down ammonia and ammonium ions into nitrogen and water while
producing oxygen, and retains metal ions and phosphorus, within the filter
medium (13).
The results of a trial on a stormwater drainage system, using of a
waste water treatment system according to an embodiment of the present
invention is shown in figure 10. As can be readily seen the pollutants have been
greatly removed. In an embodiment of the present invention, not shown, there are three
waste receiving chambers; each chamber with an air gap surrounding it, with a
barrier between each chamber to prevent flow between the chambers. Hence
when the first chamber becomes full of worm casings or bacteria and over flows
into an adjacent chamber, the feed of sewerage waste is then transferred to
one of the other chambers and the process continued. The full chamber is then
left to mature; ie all faecal waste has been converted into worm casings or
digested down to a safe product, and after maturing the microfilter bag (4) and
its contents is removed and a new bag inserted for future use.
The walls of the waste receiving chambers are porous and could be
constructed, as could be the base, as shown in figure 1 , of modules of
® ATLANTIS DRAINAGE CELLS, so as to provide an adequate air flow around
each chamber.
As shown in figure 3, the waste water treatment apparatus (1 ) could be
connected to sink or bathroom waste water outlet and the treated and filtered
water passed to underground percolation tanks (16) which supply water to the
surrounding plants. The tanks (16) could be contained in an impervious well
(23). In figure 4, the outlet from the toilet is feed into the waste water
treatment apparatus (1 ), as shown in figure 2, and the water fed to a series of
tanks (16) contained in an impervious well (24). A pump (25) can be used to
spray water held in the well (24) onto gardens. Further instead of using the
impervious well (15) to maintain a head of water in the waste receiving chamber
(3), the outlet pipe (17) could be raised vertically, thereby creating the head at
the level of the outlet.
The various tanks (16) and their walls can be constructed, as shown in
figure 1 , of modules of ATLANTIS® DRAINAGE CELLS, the subject of
International patent application no. PCT/AU94/00771.
A further embodiment is shown in figure 5, for use with a larger dwelling
such as a block of units. In this case the treatment systems uses a large
moveable container (18), which, when full, could be disconnected from the
system and removed and replaced by a fresh container.
The system works similarly to the system described previously, toilet
wastes and kitchen and bathroom wastes are fed in through an inlet pipe (2)
into a waste holding chamber (19), which contains suitable bacteria and worms,
as mentioned previously, to digest the faecal solids, while the liquid wastes flow from the waste receiving chamber (19), through the perforated side walls (20)
and base (21 ), through an air gap (8) to a lower first filter chamber (11 ).
Further the chamber 19 could have a layer of filter medium (13) containing only
bacteria, as described previously. As shown the walls of the waste receiving
chamber (19), could be made of tank modules (16) as described in International
patent application no. PCT/AU 94/00771. Further the waste receiving chamber
In this embodiment several filter chambers (11 & 22) are used in
cascade. Filter medium (13), as mentioned in the first embodiment is used, and
each filter chamber (11 & 22) is separated by an air gap (8). Hence a "perch
water" table is formed in each filter chamber (11 & 22), with the resultant
gradient of aerobic to increasingly anaerobic reaction down through the filter
medium of each filter chamber (11 & 22).
By using multiple layered filter chambers, separated by an air gap,
different reactive material and bacteria, can be placed in each filter chamber to
target specific pollutants. Again, as described above, the input of air or
generated ozone can be used to increase the efficiency of the system and
The treated water percolates through the various filter chambers (11 &
22) and is collected in the lower chamber (23), where it is removed for use for watering the gardens or, depending upon the degree of treatment, for washing
or drinking.
A further embodiment is shown in figure 6, which is similar in
construction to that shown in figure 5 except that a well (15) is formed in the
waste receiving chamber (3) by an impervious insert (7) and air (31 ) is passed
into the holding chamber (14).
Figure 7 illustrates a further embodiment which is similar to that shown in
figure 6 except that the filter medium in the filter chamber (11 ) is replaced by
layers of modules (32) of ATLANTIS " DRAINAGE CELLS, according to
Australian patent no. 593085, an example of which is shown in figure 9. The
drainage cells have small wells (30) to hold liquids in which bacteria collects
and the layers of drainage cell modules act as a trickle tower. Further the
surfaces of the plastics material of the drainage cells become coated with
bacteria and the bacteria digest the effluent.
Thus the above embodiments provide the following features:
• diluting or dewatering of the faecal solids;
• anaerobic or aerobic degradation of the faecal solids by bacteria
and/or worms to provide a useable by product • filtration through the filter medium with, in the case of granulated filter
medium, variable perch water through the filter medium;
• removal of pollutants from the water systems; and
• saving of valuable land due to on site treatment and disposal or
usage.
A further embodiment is shown in figure 8 for the purification of water
contaminated with liquid or dissolved effluent The operation of this apparatus
will now be described with reference to the separation of water and oil. This
embodiment works in the similar way to the previous embodiments, except
there are no worms or bacteria in the initial receiving chamber (24).
A filtered oil water mixture is fed into the initial holding chamber (24)
where the water (25) and oil (26) begin to separate, depending upon the
amount of liquid in the chamber. The water and oil permeates through
successive layers of filter chambers, filled with suitable filter medium, such as
those mentioned previously, containing oil digesting bacteria, and holding
chambers.
Thus after using a predetermined number of stages the water has been
separated from the oil, which remains in the filter material for digestion. When the filter medium becomes spent, either the whole container is replaced or the
system dismantled and the spent filter medium replaced.
The filter chambers can be of any suitable thickness and porosity to suit
the requirements. The various chambers and their walls can be constructed, as
shown in figure 1 , of modules of ATLANTIS® DRAINAGE CELLS.
The on-site units could be adapted for connection to a single toilet or a
single sink outlet and then fed to appropriate holding tanks for use in gardening
washing or drinking, or dispersion tanks which are surrounded by a layer of
suitable sand to allow the treated water to disperse back into the soil where it is
used by surrounding trees and plants.
It should be obvious to people skilled in the art that alterations and
modifications could be made to the above described embodiments without
departing from the scope and spirit of the present invention.

Claims

The claims defining the invention are as follows:
1. An on site liquid effluent treatment apparatus for effluent, containing biodegradable solids, comprising:
a first chamber adapted to receive untreated effluent, said chamber
having at least a permeable portion to allow liquids to pass therethrough and to
retain the biodegradable solids in the first chamber, thereby substantially
dewatering the solids, and containing bacteria and/or worms to digest the
biodegradable solids;
a second chamber in cascade with the first chamber and separated
therefrom with an air gap, said second chamber containing a suitable filter
medium, such that liquid which passes through the first chamber percolates
through the filter medium ;
a third chamber located below the second chamber to receive the
treated liquid from the second chamber; and
an outlet from said third chamber to allow removal of the treated liquid
from the third chamber.
2. An on site liquid effluent treatment apparatus according to claim 1 ,
wherein the filter medium contains bacteria to digest the effluent.
3. An on site liquid effluent treatment apparatus according to claim 1
or 2, wherein the first chamber has perforated walls and floor covered in a
geofabric or micro filter material.
4. An on site liquid effluent treatment apparatus according to any
one of the preceding claims, wherein the filter material is a granulated material
layered between two layers of geofabric or micro filter material.
5 An on site waste water purification apparatus for purifying water
containing liquid or dissolved contaminants, comprising:
a first holding chamber adapted to receive the waste water mixture, said
chamber having a permeable base to allow liquids to pass therethrough;
a first filter chamber, in cascade with the first holding chamber, and
containing a suitable filter medium, such that liquids which passes through the
first holding chamber percolates through the filter medium ;
at least a second holding chamber, located below the first filter chamber
to receive the filtered liquid from the first filter chamber, and having a
permeable base; and
at least a second filter chamber in cascade with the at least second
holding chamber, and containing a suitable filter medium, such that liquid which passes through the at least second holding chamber percolates through the
filter medium,
whereby the liquid or dissolved contaminants are separated from the
water as the water, firstly, percolates through the various filter medium, with the
liquid or dissolved contaminants remaining in the filter medium, where it is
digested by bacteria.
6. An on site waste water purification apparatus according to claim
5, wherein the first chamber has perforated walls and floor covered in a
geofabric or micro filter material.
7. An on site waste water purification apparatus according to any
one of claims 5 or 6, wherein the filter material is a granulated material layered
between two layers of geofabric or micro filter material.
PCT/AU1998/000534 1997-07-02 1998-07-02 Waste water treatment system WO1999001385A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
AU82003/98A AU8200398A (en) 1997-07-02 1998-07-02 Waste water treatment system
EP98931837A EP1017638A4 (en) 1997-07-02 1998-07-02 Waste water treatment system

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AUPO7688A AUPO768897A0 (en) 1997-07-02 1997-07-02 Waste water treatment system
AUPO7688 1997-07-02

Publications (1)

Publication Number Publication Date
WO1999001385A1 true WO1999001385A1 (en) 1999-01-14

Family

ID=3801977

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/AU1998/000534 WO1999001385A1 (en) 1997-07-02 1998-07-02 Waste water treatment system

Country Status (3)

Country Link
EP (1) EP1017638A4 (en)
AU (1) AUPO768897A0 (en)
WO (1) WO1999001385A1 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004092079A1 (en) * 2003-04-16 2004-10-28 Aqua Clarus Holdings Pty Ltd Apparatus and method for the treatment of waste
US6991728B2 (en) 2001-05-10 2006-01-31 Aqua Clarus Holdings Pty Ltd Apparatus and method for the treatment of waste
US7794592B2 (en) 2006-06-29 2010-09-14 Ralph Brown Wastewater disinfection apparatus and methods
WO2010146386A1 (en) * 2009-06-20 2010-12-23 Colin Gavin Edward Webb Apparatus and method for disposal and treatment of waste water, sewage and/or effluent
WO2011009954A1 (en) * 2009-07-23 2011-01-27 Tariq Kaddoura Wastewater treatment plant and method for treating wastewater, and wastewater treatment system
WO2012034118A2 (en) * 2010-09-10 2012-03-15 Jere Northrop Process for the treatment of biological materials and wastewater
US9681644B2 (en) 2010-02-25 2017-06-20 Timberfish, Llc Process and method for optimizing production of food and feed

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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6991728B2 (en) 2001-05-10 2006-01-31 Aqua Clarus Holdings Pty Ltd Apparatus and method for the treatment of waste
WO2004092079A1 (en) * 2003-04-16 2004-10-28 Aqua Clarus Holdings Pty Ltd Apparatus and method for the treatment of waste
US7294272B2 (en) 2003-04-16 2007-11-13 Aqua Clarus Holdings Pty Ltd Method for the treatment of waste
US7323107B2 (en) 2003-04-16 2008-01-29 Aqua Clarus Holdings Pty Ltd Apparatus and method for the treatment of waste
US7794592B2 (en) 2006-06-29 2010-09-14 Ralph Brown Wastewater disinfection apparatus and methods
WO2010146386A1 (en) * 2009-06-20 2010-12-23 Colin Gavin Edward Webb Apparatus and method for disposal and treatment of waste water, sewage and/or effluent
WO2011009954A1 (en) * 2009-07-23 2011-01-27 Tariq Kaddoura Wastewater treatment plant and method for treating wastewater, and wastewater treatment system
US9681644B2 (en) 2010-02-25 2017-06-20 Timberfish, Llc Process and method for optimizing production of food and feed
WO2012034118A2 (en) * 2010-09-10 2012-03-15 Jere Northrop Process for the treatment of biological materials and wastewater
WO2012034118A3 (en) * 2010-09-10 2012-06-28 Jere Northrop Process for the treatment of biological materials and wastewater
US9764977B2 (en) 2010-09-10 2017-09-19 Timberfish, Llc Process for the treatment of biological materials and wastewater

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EP1017638A4 (en) 2001-03-14
AUPO768897A0 (en) 1997-07-24

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