WO1999032406A2 - Improved effluent treatment system - Google Patents
Improved effluent treatment system Download PDFInfo
- Publication number
- WO1999032406A2 WO1999032406A2 PCT/NZ1998/000184 NZ9800184W WO9932406A2 WO 1999032406 A2 WO1999032406 A2 WO 1999032406A2 NZ 9800184 W NZ9800184 W NZ 9800184W WO 9932406 A2 WO9932406 A2 WO 9932406A2
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- WO
- WIPO (PCT)
- Prior art keywords
- treatment
- effluent
- filtering
- filter
- numeral
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/32—Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
- C02F3/327—Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae characterised by animals and plants
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/04—Aerobic processes using trickle filters
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/04—Aerobic processes using trickle filters
- C02F3/046—Soil filtration
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Abstract
The improved effluent treatment system provides a manmade biocenosis, sealed against the ground, preferably gravity-driven free flow, where inflow (Figure 1, numeral 4 and 9), waterlevel (Figure 2, numeral 18 and following adjoined parts) and outflow (Figures 1 and 2, numeral 6 and 10) can be controlled (Figure 2, numeral 18 and following adjoined parts). Three co-dependent components, gravel in layers (Figure 1, numeral 5 and 10), microorganisms amongst the gravel (Figure 1, numeral 5 and 10) and plants (Figure 1, numeral 8 and 11) create a two-stage treatment device (Figure 1, numeral 2 and 3) in which solids become separated from the effluent to remain on top of the filter body (Figure 1, numeral 5) and become transformed into a soil-peat similar structure with the help of the plant species phragmitis Australis (Figure 1, numeral 8). The solid free effluent percolates through the filterbody (Figure 1, numeral 5) and flows via a flange (Figure 2, numeral 15-16-17) the outlet-pipe (Figure 1, numeral 6 and 12) and a controlshaft (Figure 1, numeral 7) to the treatment area two (Figure 1, numeral 3) where the final cleansing takes place. A variety of marshland plants (Figure 1, numeral 11) assists the final cleansing process. The discharge out of the treatment area is the same like out of treatment area one (Figure 2, numeral 15-16-17; Figure 1, respective 2, numeral 6; Figure 1, numeral 14). The described installation gives an alternative to septic tank systems or any other effluent treatment devices.
Description
TITLE : Improved Effluent Treatment System
FIELD OF INVENTION
This invention relates to an effluent treating system, and is applicable particularly, but not
exclusively, to the treatment of effluent containing solid material.
BACKGROUND
During the past few decades the complexity and efficiency of effluent treatment plants
installed by large urban developments and major cities has increased considerably.
While complexity and efficiency have increased, a number of problems still exist with
current treatment plants. These include the absence of effective methods and processes to
deal with the solid waste, generally referred to as "sludge", produced from such plants, and
the absence of smaller, more cost-efficient plants for smaller sized towns, rural and remote
areas, or even individual dwellings. These space requirements, costly maintenance and
environmental impacts of existing treatment plants often detract from the advantages of
treating effluent for reuse.
There is an absence of an effective, simple and low cost effluent treatment system which
solves a number of these problems, while remaining cost-effective and efficient over time.
OBJECT
It is therefore an object of the invention to provide an improved effluent treatment system, or
one which will at least provide the public with a useful choice.
STATEMENT OF INVENTION
Accordingly in one aspect the invention may broadly be said to consist of an improved
effluent treatment installation comprising a plurality of filtering and treatment areas, said
areas having means for allowing the ingress of effluent into each area, means for the filtering
or treatment of the effluent, or means for both the filtering and treatment of the effluent, and
means for allowing the egress of the effluent from each of the treatment and filtering areas.
Preferably the installation is comprised of at least two filtering and treatment areas. It is
desirable to refer to these areas as the first treatment area and the second treatment area.
Where the effluent contains solid material, it is desirable to separate the solid material from
the fluid or liquid so as to treat both the material and the fluid or liquid separately. Hence
when the effluent is first passed into the first treatment area it is desirable to filter as much of
the solid material from the fluid or liquid as possible. Preferably any solid material separated
from the effluent is to be retained for treatment in the first treatment area. More preferably
said treatment area contains a plurality of filter means to effect the removal of solid material
from the effluent once said effluent is passed into the first treatment area and before it is
passed into the second treatment area.
It is desirable to separate as much of any solid material as possible contained in the effluent
from the fluid or liquid once the effluent has entered the first treatment area. To achieve this
it is preferable said filter means comprises a plurality of individual filter layers through
winch the effluent may pass, each individual filter layer containing filter material of a
particular type and size. More preferably the plurality of filter layers include a final filter
layer, immediately under which is a top filter layer, a plurality of intermediate filter layers,
and a bottom filter layer.
Preferably, but not necessarily, each filter layer is of substantially the same depth.
Preferably said final, top, bottom and inteπnediate filter layers are arranged in order
depending on the size of the filter material contained in each layer. More preferably said
layers are arranged such that the bottom layer contains filter material having the greatest
diameter, the final layer contains filter material of the smallest diameter, and the intermediate
layers are arranged in order of decreasing filter material diameter from the bottom layer to
the final layer.
Preferably said filter material is comprised of gravel or some other similar type of non-
reactive sub-strata.
It is desirable to ensure the maximum amount of solid material is removed from the effluent
as it is passed through treatment area one. Preferably the final filter layer of treatment area
one comprises a mixture of sand and bark, or some other similar combination of materials.
Preferably means are provided to allow the filtered effluent to pass from treatment area one
to treatment area two. It is desirable to refer to this filtered effluent as outlet water.
Once any solid material contained in the effluent has been substantially removed by passing
the effluent through treatment area one, it is desirable to further subject the resulting outlet
water to a cleaning process in treatment area two. Preferably treatment area two contains
substantially similar filter means as to those described herein for treatment area one. More
preferably said filter means may be arranged in a substantially identical configuration to the
filter means as herein described for treatment area one.
It is desirable to take advantage of the various biological characteristics of a variety of plants
for the treatment of the solid material extracted from the effluent, and the resulting outlet
water. Preferably the final filter layer of each treatment area is capable of supporting a
plurality of selected plants. More preferably the filter material provided in each treatment
area provides the required support needed for said plants to survive and prosper. Preferably
the final filter layer alone contains organic material such as peat or bark to achieve this.
It is desirable to use treatment area one for the purpose of treating the solid material filtered
from the effluent. Preferably the plants used in treatment area one are selected from
predetermined genera which shows suitable characteristics for assisting in the treatment of
the solid material. More preferably the plants used in treatment area one are capable of
creating root systems into the solid material and exhibit desirable characteristics in the
mineralisation of said solid material into a substantially soil-like material.
It is desirable to use treatment area two for the purpose of treating the outlet water filtered
from the effluent. Preferably the plants used in treatment area two are selected from
predetermined genera which shows suitable characteristics for assisting in the treatment of
the outlet water. More preferably the plants used in treatment area two exhibit desirable
biological characteristics so as to assist in the treatment and cleaning of the outlet water.
Preferably the first treatment area is elevated above the second treatment area. Where more
than two treatment areas are being used, it is preferable the first treatment area is positioned
above the second treatment area, this area itself being positioned above the third treatment
area and so on.
Preferably the required sizes of the filtering and treatment areas and the complexity and
composition of the filtering means may be determined through a number of criteria,
including, but not limited to, the expected volume and quality of the effluent, the expected
volume and quality of the filtered solid material, and the number of inhabitants from the
town, city or the like relying on the treatment plant.
It is desirable to ensure effluent under treatment, or any solid content of that effluent, is
contained within each of the treatment areas, irrespective of the location of said treatment
areas. Preferably then means are provided which prevent the uncontrolled egress of any
effluent under treatment, or any contents of said effluent, from the treatment areas.
Preferably means provided for the controlling of the ingress of the effluent and the treated
effluent, and the egress of same, are sealed to prevent the uncontrolled leaking of any
effluent under treatment or any contents of said effluent from the treatment areas.
In another aspect the invention provides an effluent treatment installation including a first
treatment zone and a second treatment zone, means for supplying fluid effluent to said first
treatment zone, said first treatment zone comprising filtering means for filtering out solids
therefrom, an outlet from the said first treatment zone for the supplying of filtered fluid to
said second treatment zone, wherein the first treatment zone supports one or more first plant
species capable of utilising the solids filtered out by the filtering means, said second
treatment zone comprising a support zone for one or more second plant species capable of
producing secretions for the treatment of fluid passing through said second treatment zone,
and an outlet from said second treatment zone.
Preferably the second plant species are capable of releasing antibiotic secretions.
Preferably both the first and second plant species are helophytic.
In another aspect the invention provides a method of effluent treatment comprising the steps
of supplying fluid effluent to a first treatment zone and filtering out any solid material
contained therein from the effluent by passing said effluent through a variety of filtering
means, and then treating the solid material extracted from the effluent in said first treatment
zone, and then passing the filtered fluid out of the said first treatment zone to a second
treatment zone where further filtering may take place, followed by the treating and cleaning
of the filtered effluent in said second treatment zone, and the removal of the treated effluent
from said second treatment zone.
To those skilled in the art to which the invention relates, many changes in construction and
widely differing embodiments and applications of the invention will suggest themselves
without departing from the scope of the invention as defined in the appended claims. The
disclosures and the description herein are purely illustrative and are not intended to be in any
sense limiting.
DRA WINGS
One preferred forai of the invention will now be described with reference to the
accompanying drawings in which;
Figure 1 shows a two stage effluent treatment system as herein described by the
specification; and
Figure 2 shows a cross-section of part of the effluent treatment system shown in figure
1.
PREFERRED EMBODIMENT
In figure 1 a two stage botanical effluent treatment plant 1 is shown.
In the preferred form of the invention, the treatment plant is separated into two areas, refeired
to for the purposes of this description as treatment area one and treatment area two, shown in
figure 1 by the numerals 2 and 3 respectively.
It is desirable for effluent being processed in the plant to move freely by the force of gravity
from treatment area one through to treatment area two, subject to any flow control
mechanisms in place to regulate the flow of the effluent through the facility. In the preferred
embodiment treatment area one is constructed above treatment area two so that a natural
downward flow of effluent through the facility is achieved.
The sizes of treatment areas one and two will depend on a variety of criteria. In particular
however the effectiveness and efficiency of each effluent treatment facility is a factor of a
variety of integers including the quantity of effluent, the expected solid content of the
effluent, and where the treatment facility is being used to treat effluent from a community,
town or city, the number of inhabitants of the community, town or city.
In addition the shape and configuration of each treatment facility may be adjusted to fit the
geography of almost any installation site, and nearly any configuration may be created for
meeting the requirements and demands of the circumstances. However it is expected that
this type of effluent treatment system will require at least 40% more area than a conventional
treatment plant.
It is of course desirable to ensure any effluent treatment and the material extracted from the
effluent remains under the control of the treatment facility at all times. In particular each
facility will need to be designed to ensure material cannot leak from the treatment areas and
into the surrounding environment. In the preferred embodiment each treatment area will be
completely sealed from ground contact by a foil layer, reinforced concrete, or density-
enhanced clay, or any other kind of combination of materials which will guarantee the
integrity of the treatment areas. It is envisaged similar efforts will be required to seal the
inflow and outflow pipes, the control shafts, and any other channelling in use through the
facility.
The function of the treatment plant is in two stages. Firstly treatment area one separates
solid material from the liquid, while treatment area two acts upon the output from treatment
area one, the solid-free liquid, in a treatment process.
In the preferred embodiment treatment area one is constructed as follows.
An inflow pipe 4 brings the effluent into treatment area one. In the preferred embodiment it
is expected some form of flow control mechanism will interact with inflow pipe 4, although
this is not shown in figure 1.
The effluent is passed over a filter bed 5, the purpose of which is to separate solid material
from the effluent, allowing solid-free liquid to pass vertically through the filter bed and on
into treatment area two via outflow pipe 6 and control shaft 7.
Filter bed 5 may be constructed in a variety of ways, but the general requirement is for the
filter material used in the bed to be arranged in order of decreasing size, such that the filter
material at the base of the bed has the greatest diameter, whereas the filter material at the top
of the bed has the smallest diameter. The combination of filter material chosen should reflect
the desire to ensure the maximum yield of solid material is left on the surface, allowing the
solid-free liquid to pass through to the next stage of the treatment process. For example, in
the preferred embodiment the filter bed consists of a number of layers of gravel or some
other similar non-reactive material, arranged as follows:
1. a coarse bottom layer, approximately 16-32mm in size and approximately 100mm
thick;
2. a second layer, approximately 8-16mm in size and approximately 50mm thick;
3. a third layer, approximately 4-8mm in size and approximately 50mm thick; and
4. a final layer of sand approximately 100mm thick, or a layer of sand approximately
70mm thick with yet another layer approximately 30mm thick on top of the sand
comprising a mixture of sand and peat or fine bark.
Other density and diameter combinations may be used depending on the volume and type of
effluent being treated, and also the weight constraints of the facility. Gravel is however
preferred as it provides very good permeability throughout the filter bed.
Once the solid matter has been separated from the effluent, it is desirable to further treat this
matter. To achieve this in the preferred embodiment reed 8 such as Phragmatis australis may
be planted in the surface of the filter bed, which provides the necessary biosphere for the reed
to grow. It is envisaged approximately three plants per square metre will be required. Reed
is particularly suitable for this purpose as it is able to create new root systems into the solid
matter filtered from the effluent, and by the process of mineralisation is able to convert this
filtering material into a soil-type material.
Other genera of plants may be used, and it is foreseen there may be particular advantages in
using species which, for example, could be used as a fodder source or as a renewable source
of building supplies, particularly where the facility is being used in developing countries.
To ensure the quality and effectiveness of the plants being used in the system is maintained,
it is envisaged regular pruning and cutting back of the plants will be required, the off-cuts of
which may be removed and composted.
In the preferred embodiment treatment area two is constructed as follows.
Treatment area two comprises the actual cleaning and treatment area for the now solid-free
liquid effluent or outlet water, which flows into treatment area 2 via inflow pipe 9. It is
similarly constructed as treatment area one, having in the preferred embodiment a filter bed
10 consisting of three layers of gravel or some other similar non-reactive material, arranged
as follows:
1. a coarse bottom layer, approximately 16-32mm in size and approximately 100mm
thick;
2. an intermediate layer, approximately 8-16mm in size and approximately 100mm
thick; and
3. a final layer, approximately 4-8mm in size and approximately 100mm thick.
Again other density and diameter combinations may be used depending on the volume and
type of outlet water being treated.
If the outlet water contains no solid material, only one type of gravel or similar material is
required, ideally having a depth of 300mm and a particle diameter of 8-16mm.
The inflow pipe 9 should preferably discharge the effluent into a coarse gravel area (with
particle sizes 30mm in diameter or larger) in the first instance so as to assist in the
oxygenation of the inflow outlet water.
A number of plants produce antibiotic secretions for their self-protection, thereby treating the
outlet water over time as it settles in treatment area two. To achieve this in the preferred
embodiment a variety of marshland plants 11 may be planted in the surface of filter bed 10,
which provides the necessary biosphere for the plants to grow and prosper. It is envisaged
approximately ten different genera of plants are required, with a planting density of 3 plants
per square metre. The recommended species of plants are as follows:
1. Eleocharis palustris;
2. Iris pseudacorus;
3. Schoenoplectus lacustris;
4. Mimulus luteus;
5. Filipendula ulmaria;
6. Juncus compressus;
7. Lythrum salicaria;
8. Juncus inflexus;
9. Menta aquatica; and
10. Carex acutiformis .
.Any other combination of similar helophytic plants may be used to achieve the desired
results.
Over a period of time the outlet water is slowly treated by the plants 11 and cleansed, at
which stage the treated outlet water may be removed from the facility via control shaft 14
and outlet pipes 12 and 13.
In figure 2 an example of a control shaft configuration is shown. It is assumed in this
example the solid-free liquid is passing from treatment area one via filter bed 5 and outflow
pipe 6, into control shaft 7.
A triangular shaped body 15, possibly but not necessarily constructed of a polyester
composite or the like, is positioned at the end of the filter bed for treatment area one with a
flange 16 constructed of an appropriate wastewater resistant material, such as stainless steel
or the like. Bolts are laminated into the triangular body around pipe 17, which is required to
be glued and laminated into the triangular body.
A hole of equivalent diameter to pipe 17 is cut into the foil which encases the treatment area
allowing the pipe to be passed through from the treatment area. A matching flange squeezes
a liner together with the help of the bolts to prevent leakage from the join. The pipe 17 and
the pipe 6 lead into the shaft 7 by a short piece of tube 18 attached to the shaft. Inside the
shaft a piece of tube 19a, at a 90° angle, is fitted together with tube 18 in such a way that it
may be turned vertically, in order to adjust the level of the wastewater in the filter body. Into
tube 19a two other pieces 23 and 19b are installed as shown in figure 2.
In the preferred embodiment the lowest part of pipe 18 should be level with the bottom of the
filter bed 5 from which it connects. The pipe pieces 19a, 23 and 19b may be turned to adjust
the level of the wastewater in the filter. At point 20, the highest level of wastewater in the
filter may be adjusted, which is also substantially identical with the top level of the filter
body. Opposite at the very bottom of the shaft 21 is the outlet, which is installed in a similar
fashion as pipe 17. From there an inflow pipe 9 transfers the effluent into treatment area two.
A similar configuration may be used throughout the filtering and treatment installation to
control the flow of effluent and the like from one treatment area to another. This
configuration ensures a satisfactory leak-proof handling of the effluent throughout the plant.
ADVANTAGES OF THE PREFERRED EMBODIMENT
With sensible location and layout the necessity of the use of pumps in the facility may be
reduced or even excluded, allowing gravity to be the major driver of the effluent through the
facility.
If pumps are required to drive effluent through the facility, it is envisaged solar powered
pumps alone may be sufficient to achieve this due to the minimal amount of energy required
to run the facility.
The water generated through the filtering process may be suitable for irrigation or for other
similar purposes. It is highly unlikely however that the water would be suitable for human
consumption or for personal hygiene uses without considerable further treatment.
There are many environmental advantages of such a system, including a reduction in the
volume of insect pests normally associated with open pond-based treatment plants such as
mosquitoes, and the ability of this system to effectively treat effluent naturally without the
need for added chemicals. Further, the use of various types of plants as part of the treatment
process may assist developing communities with the production of animal fodder and/or a
renewable supply of construction materials.
In addition, depending on site restraints, the second stage of the facility may be positioned on
a building rooftop to take advantage of the evaporation process which takes place over time
as outlet water is purified, thereby providing a cooling effect to the roof of the building, as
well as shielding the roof from the direct impact of the sun's rays. This same
evaporation/cooling process could be applied commercially where factories or the like
require a cooling process to cool their products. Alternatively the system may be positioned
on a rooftop as an insulative measure to prevent heat loss through the roof in cooler or cold
conditions.
Clearly one of the main advantages of this system is the ability to treat the solid material
from the effluent and the liquid effluent in the same facility. This is particularly useful
where effluent is generated from large scale plants, in which case the liquid effluent is often
treated at technical wastewater treatment plants while the resulting sludge has to be de-
watered. This normally happens on the same premises and requires an enormous input of
energy. However, the so-called first stage of this system replaces all of the complicated
technical devices required to achieve this. These devices are expensive to purchase and to
maintain. Provided that the size and handling of the basin(s) is well set up, the solid-free
effluent from the basin may be returned into the technical plant. The resulting soil-similar
material from the "full" basin may then be composted and after marginal testing can be used
in landscaping or for whatever other applications are appropriate. If the solid material is
toxic, it could be used for covering over garbage or waster dumps which are full or almost at
capacity, or could be burned in conjunction with fossil fuel in thermal power plants.
However, one of the advantages of the present system is the sludge is able to be mineralised
and the volume reduced by up to 90% without the requirements of other inputs. Exactly the
same procedure may be used for sludge generated from a variety of other sources such as, for
example, septic tanks or other similar devices.
Claims
1. A multi-stage effluent treatment installation for the treatment of effluent containing
solid material comprising at least two "filtering and treatment areas", means for
supplying said effluent into a first filtering and treatment area where in use said solid
material is separated from said effluent by filtering means in said first filtering and
treatment area, means for supplying the resulting filtered fluid into a second filtering
and treatment area, leaving said solid material retained within said first filtering and
treatment area wherein said solid material is acted upon by a group of plants, and said
filtered fluid, having passed into said second filtering and treatment area and being
retained in said second filtering and treatment area is acted upon by a second group of
plants.
2. A multi-stage effluent treatment installation as claimed in claim 1, wherein said first
filtering and treatment area contains filter means comprising a plurality of individual
filter layers through which the effluent may pass, with each filter layer containing
filter material of a particular type and size.
3. A multi-stage effluent treatment installation as claimed in claim 2, wherein the said
plurality of filter layers include a final filter layer, immediately under which is a top
filter layer, a plurality of intermediate filter layers, and a bottom filter layer, with said
filter layers arranged in order depending on the size of the filter material contained in
each layer such that the bottom layer contains filter material having the greatest
diameter, the final layer contains filter material of the smallest diameter, and the inteimediate layers are arranged in order of decreasing filter material diameter from
the bottom layer to the final layer.
4. A multi-stage effluent treatment installation as claimed in claim 3, wherein the filter
material is comprised of gravel or some other type of non-reactive sub-strata.
5. A multi-stage effluent treatment installation as claimed in claim 4, wherein the final
filter layer comprises a mixture of sand and bark, or some other similar combination
of materials.
6. A multi-stage effluent treatment installation as claimed in claim 5, wherein said final
filter layer is capable of supporting a plurality of selected plants, with said final filter
layer containing organic material such as peat or bark which will provide the required
support needed for said plants to survive and prosper.
7. A multi-stage effluent treatment installation as claimed in claim 6, wherein said
plants are capable of creating root systems into the solid material extracted from the
effluent.
8. A multi-stage effluent treatment installation as claimed in claim 7, wherein said
plants are selected from predetermined genera which shows suitable characteristics
for assisting in the treatment of said solid material and the mineralisation of said solid
material extracted from the effluent.
9. A multi-stage effluent system as claimed in claim 1, wherein said second filtering and
treatment area contains filter means comprising a plurality of individual filter layers
through which the filtered fluid may pass and be retained in said second filtering and
treatment area, with each filter layer containing filter material of a particular type and
size.
10. A multi-stage effluent system as claimed in claim 9, wherein the said plurality of
filter layers include a final filter layer, immediately under which is a top filter layer, a
plurality of intermediate filter layers, and a bottom filter layer, with said filter layers
arranged in order depending on the size of the filter material contained in each layer
such that the bottom layer contains filter material having the greatest diameter, the
final layer contains filter material of the smallest diameter, and the intermediate
layers are arranged in order of decreasing filter material diameter from the bottom
layer to the final layer.
11. A multi-stage effluent treatment installation as claimed in claim 10, wherein the filter
material is comprised of gravel or some other similar type of non-reactive sub-strata.
12. A multi-stage effluent treatment installation as claimed in claim 10 or 11 , wherein the
final filter layer comprises a mixture of sand and bark, or some other similar
combination of materials.
13. A multi-stage effluent treatment installation as claimed in claim 12, wherein said final
filter layer is capable of supporting a plurality of selected plants, with said filter layer containing organic material such as peat or bark which will provide the required
support needed for said plants to survive and prosper.
14. A multi-stage effluent treatment installation as claimed in claim 13, wherein said
plants are selected predetermined genera which show suitable characteristics for
assisting in the treatment and cleansing of the filtered fluid.
15. A multi-stage effluent system as claimed in any one of the preceding claims, wherein
the second plant species are capable of releasing antibiotic secretions.
16. A multi-stage effluent system as claimed in any one of the preceding claims, wherein
both the first and second plant species are helophytic.
17. A multi-stage effluent system as claimed in any one of the preceding claims, wherein
the first filtering and treatment area is elevated above the second filtering and
treatment area, and where said effluent system comprises more than two filtering and
treatment areas, the first filtering and treatment area is elevated above the second
filtering and treatment area, with the second filtering and treatment area being
positioned above the third filtering and treatment area and so on.
18. A multi-stage effluent treatment installation as claimed in any one of the preceding
claims, wherein the size of the installation and the complexity and composition of the
filtering means included therein are determined with respect to a number of criteria,
including but not limited to the expected volume and quality of the effluent, the
expected volume .and quality of the filtered solid material, and the number of inhabitants from the town, city or the like relying on the effluent treatment
installation.
19. A multi-stage effluent treatment installation as claimed in any one of the preceding
claims, wherein means are provided which prevent the uncontrolled egress of any
effluent under treatment, or any contents of said effluent, from the filtering and
treatment areas.
20. A multi-stage effluent treatment installation as claimed in any one of the preceding
claims, wherein means are provided for controlling the ingress of the effluent and the
treated effluent, and the egress of same, and said means are sealed to prevent the
uncontrolled leaking of any effluent under treatment of any contents of said effluent
from the treatment areas.
21. A multi-stage effluent treatment installation including a first treatment zone and a
second treatment zone, means for supplying fluid effluent to said first treatment zone,
said first treatment zone comprising filtering means filtering out solids therefrom, an
outlet from the said first treatment zone for the supplying of filter fluid to said second
treatment zone, wherein the first treatment zone supports one or more first plant
species capable of utilising the solids filtered out by the filtering means, said second
treatment zone comprising a support zone for one or more second plant species
capable of producing secretions for the treatment of fluid passing through said second
treatment zone, and an outlet from said second treatment zone.
22. A method for the treatment of effluent comprising the steps of supplying fluid
effluent to a first treatment zone filtering out any solid material contained therein
from the effluent by passing said effluent through a variety of filtering means, and
then treating the solid material extracted from the effluent in said first treatment zone,
and then passing the filtered fluid out of the said first treatment zone to a second
treatment zone where further filtering may take place, followed by the treating and
cleaning of the filtered effluent in said second treatment zone, and the removal of the
treated effluent from said second treatment zone.
23. A method of filtering and cleaning effluent substantially as described herein by the
accompanying specification.
24. A multi-stage effluent treatment installation substantially as described herein by the
accompanying specification.
25. A multi-stage effluent treatment installation substantially as described herein by the
accompanying drawings.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU18931/99A AU1893199A (en) | 1997-12-19 | 1998-12-17 | Improved effluent treatment system |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NZ329455 | 1997-12-19 | ||
NZ329455A NZ329455A (en) | 1997-12-19 | 1997-12-19 | Effluent treatment by two filtering and treating areas having two groups of plants |
Publications (2)
Publication Number | Publication Date |
---|---|
WO1999032406A2 true WO1999032406A2 (en) | 1999-07-01 |
WO1999032406A3 WO1999032406A3 (en) | 1999-11-11 |
Family
ID=19926565
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/NZ1998/000184 WO1999032406A2 (en) | 1997-12-19 | 1998-12-17 | Improved effluent treatment system |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU1893199A (en) |
NZ (1) | NZ329455A (en) |
WO (1) | WO1999032406A2 (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2799457A1 (en) * | 1999-10-08 | 2001-04-13 | Ganster Jacqueline Mongin | FILTER, PLANT OF ROWS, DOMESTIC, INDUSTRIAL EFFLUENT CLEANER, COMPOSED OF 2 AERATED BASINS, WORKING, ALTERNATE BY PERCOLATION OF GROSS EFFLUENT ON 1M2 / INHABITANT |
ES2203321A1 (en) * | 2002-05-03 | 2004-04-01 | Universidade De Santiago De Compostela | Modular cleaner for waste water in general includes pipe connections and valving, and ditches, for controlled filtration |
WO2004069756A1 (en) * | 2003-02-06 | 2004-08-19 | Grafinger, Rainer | Biological purification of water |
WO2005108310A1 (en) * | 2004-05-07 | 2005-11-17 | Deere & Company | Waste water purification plant by means of plants |
FR2900921A1 (en) * | 2006-05-09 | 2007-11-16 | Philippe Michel | Treatment of effluents comprises biological pretreatment of effluents using bacterial bed, and biological treatment of nitrification-denitrification of clarification sludge obtained at an exit of the bed using vertical-flow reed bed filter |
US7407577B2 (en) | 2004-09-17 | 2008-08-05 | Curt Kerns | Tertiary filter septic system and method |
ITFI20100229A1 (en) * | 2010-11-19 | 2012-05-19 | Initram Impresa Italia S R L | BIDIRECTIONAL FLANGE FOR PIPES PASSA SHEATH IN PVC. |
FR2975390A1 (en) * | 2011-05-17 | 2012-11-23 | Leroux Philippe Paul | Device, useful for purifying domestic wastewater, comprises first and second biological processing cells with vertical percolation, a unit for feeding the first processing cell in effluent, an effluent collection unit, and a rigid plate |
Citations (5)
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US5174897A (en) * | 1991-09-24 | 1992-12-29 | The United States Of America As Represented By The Secretary Of Agriculture | Constructed wetlands to control nonpoint source pollution |
DE4332234A1 (en) * | 1993-09-22 | 1995-03-23 | Axel Dipl Ing Buechner | Phytomechanical sewage treatment plant for wastewater treatment in closed water circuits |
DE4422496A1 (en) * | 1994-06-28 | 1996-01-11 | Juergen Stadelmann | Sub-surface biological filter for surface waters drains through gravel layers |
DE29613235U1 (en) * | 1996-07-31 | 1996-10-02 | Dernbach Heinrich Gmbh | Plant wastewater treatment plant with horizontal and vertical flow |
DE29707646U1 (en) * | 1997-04-23 | 1997-08-07 | Fahry Thomas | Sewage treatment plant for the biological purification of organically polluted wastewater |
-
1997
- 1997-12-19 NZ NZ329455A patent/NZ329455A/en not_active IP Right Cessation
-
1998
- 1998-12-17 AU AU18931/99A patent/AU1893199A/en not_active Abandoned
- 1998-12-17 WO PCT/NZ1998/000184 patent/WO1999032406A2/en unknown
Patent Citations (5)
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---|---|---|---|---|
US5174897A (en) * | 1991-09-24 | 1992-12-29 | The United States Of America As Represented By The Secretary Of Agriculture | Constructed wetlands to control nonpoint source pollution |
DE4332234A1 (en) * | 1993-09-22 | 1995-03-23 | Axel Dipl Ing Buechner | Phytomechanical sewage treatment plant for wastewater treatment in closed water circuits |
DE4422496A1 (en) * | 1994-06-28 | 1996-01-11 | Juergen Stadelmann | Sub-surface biological filter for surface waters drains through gravel layers |
DE29613235U1 (en) * | 1996-07-31 | 1996-10-02 | Dernbach Heinrich Gmbh | Plant wastewater treatment plant with horizontal and vertical flow |
DE29707646U1 (en) * | 1997-04-23 | 1997-08-07 | Fahry Thomas | Sewage treatment plant for the biological purification of organically polluted wastewater |
Non-Patent Citations (1)
Title |
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DERWENT ABSTRACT, Accession Number 90-381851/51, Class D15, F09; & SU 1542919 A (ASTRAKHAN CELL-PAPE) 15 February 1990. * |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001027039A1 (en) * | 1999-10-08 | 2001-04-19 | Pierre Mongin | Method for purifying domestic, agricultural and industrial wastewater |
FR2799457A1 (en) * | 1999-10-08 | 2001-04-13 | Ganster Jacqueline Mongin | FILTER, PLANT OF ROWS, DOMESTIC, INDUSTRIAL EFFLUENT CLEANER, COMPOSED OF 2 AERATED BASINS, WORKING, ALTERNATE BY PERCOLATION OF GROSS EFFLUENT ON 1M2 / INHABITANT |
ES2203321A1 (en) * | 2002-05-03 | 2004-04-01 | Universidade De Santiago De Compostela | Modular cleaner for waste water in general includes pipe connections and valving, and ditches, for controlled filtration |
US7332082B2 (en) | 2003-02-06 | 2008-02-19 | Rainer Grafinger | System and method for biological purification of water |
WO2004069756A1 (en) * | 2003-02-06 | 2004-08-19 | Grafinger, Rainer | Biological purification of water |
WO2005108310A1 (en) * | 2004-05-07 | 2005-11-17 | Deere & Company | Waste water purification plant by means of plants |
US7718062B2 (en) * | 2004-05-07 | 2010-05-18 | Deere & Company | Wastewater purification plant by means of plants |
US7695620B2 (en) | 2004-09-17 | 2010-04-13 | Curt Kerns | Tertiary filter septic system and method |
US7407577B2 (en) | 2004-09-17 | 2008-08-05 | Curt Kerns | Tertiary filter septic system and method |
EP1857419A1 (en) * | 2006-05-09 | 2007-11-21 | M. Philippe Michel | Method and installation for processing effluent |
FR2900921A1 (en) * | 2006-05-09 | 2007-11-16 | Philippe Michel | Treatment of effluents comprises biological pretreatment of effluents using bacterial bed, and biological treatment of nitrification-denitrification of clarification sludge obtained at an exit of the bed using vertical-flow reed bed filter |
ITFI20100229A1 (en) * | 2010-11-19 | 2012-05-19 | Initram Impresa Italia S R L | BIDIRECTIONAL FLANGE FOR PIPES PASSA SHEATH IN PVC. |
FR2975390A1 (en) * | 2011-05-17 | 2012-11-23 | Leroux Philippe Paul | Device, useful for purifying domestic wastewater, comprises first and second biological processing cells with vertical percolation, a unit for feeding the first processing cell in effluent, an effluent collection unit, and a rigid plate |
Also Published As
Publication number | Publication date |
---|---|
NZ329455A (en) | 1998-05-27 |
WO1999032406A3 (en) | 1999-11-11 |
AU1893199A (en) | 1999-07-12 |
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