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The necessity as well the possibilities to save substantial amounts of municipal drinking water have quickly developed in recent years. In addition to obvious measures such as using low-flow fixtures and simply less water, it goes without saying that treatment of previously used or lightly-contaminated water on-site is also essential.

Water treatment

Water can be obtained from a number of water sources, such as:

Rainwater
Greywater from households
Surface water
Effluent water from small wastewater treatment systems
Laundry water
Groundwater
etc…

Depending on the level of treatment and source, the treated water can be substituted either as non-potable water for reuse water applications or if it fulfils higher requirements for potable water applications as follows:

Treatment to non-potable water quality for toilet flushing, irrigation, cleaning purposes, washing machines, cooling water, industrial applications, etc....
Treatment to potable water quality for showering, washing, drinking, etc....

The areas of application range from single-family dwellings to multiple-family dwellings, sports halls, public buildings, industrial facilities, etc. Therefore water treatment and reuse brings along a bunch of advantages with it:

Advantages for consumers:

Saving potable water and sewage expenses
Independence from the water provider
Consistent supply
High quality

Advantages for communities

Reduced costs toward sewer construction, sewer rehabilitation and operating/planned sewage treatment plants
Reduced costs toward potable water connections, pump stations and operating/planned water treatment plants
Savings potential in development of new housing areas
Reduced demand on local water supplies

The huge potential for decentralized water treatment has not yet been exploited. This is partly a result of municipalities requiring connection to the main water supply in order to cover costs. But, by incentivizing decentralized systems, municipalities could also save a lot of costs while creating a thriving business market.

The other hindrance till now was the availability of technology for decentralized water treatment. In the last few years this technology has matured and is now reliable, economical and safe. These factors mean decentralized water treatment should become more common in a variety of applications based on regional needs.

Fundamentals of water quality

Water quality parameters

There are a variety of substances of concern when dealing with untreated water. Different uses including non-potable and drinking water follow different regulations regarding the same or additional water quality parameters. In the following section the most important parameters are described including; COB, BOB₅, TOC, conductivity, turbidity, DO, pH and heavy metal concentration.

Hygiene indicators

Hygiene indicators are bacteria, viruses and protozoa.

What these organisms describe and their measurement are very different in water quality terms. This fact is based on the detection methods that were and are applied in different countries and laboratories. An example is that today in the EU bathing water quality is determined by measuring intestinal Enterococci and E. coli present in the water. There is no one organism that can describe and indicate the complete water quality in reference to the regulations.

The following requirements are stated for organisms to be considered hygiene indicators <ref name="isa">ISA - Institut für Siedlungswasserwirtschaft der RWTH Aachen</ref>:

They should be part of the normal gut microbiota in healthy people (ideally, they should only be present in the human gastrointestinal tract).
They should only be present when it is likely that pathogens of faecal origin are present.
They should be present in larger numbers than the pathogens indicated by them.
They should also grow outside the digestive tract and be more resistant than pathogenic microorganisms (pathogens).
They should be more resistant than pathogens under natural conditions as well as after water treatment and survive in greater numbers.
They should be easily isolated, identified and counted.
They should themselves not cause a disease.
Their number should be in relation to the quantity of pathogenic microorganisms.

Quality of potential source waters

River water with high turbidity and TSS

Greywater from households

Effluent from small wastewater treatment systems

Laundry water

Surface water must be individually examined.

Groundwater unless in areas of agricultural usage, usually has a very low BOD5, but may contain dissolved metals. Must be individually examined.

Rainwater, even after coming off the roof, generally has little to no BOD5 and no anthropogenic or other substances of concern.

Water quality requirements

Non-potable systems

In order for water treatment systems to be accepted both by end-consumers, as well as communities and countries, non-potable treated water must fulfill the highest minimum standards of water quality and present no health hazards to the user or general public.

Requirements from market arranged according priority:

No particulates and good aesthetics (protection of pipework, no odour, low turbidity (clarity))
DIN 19650 quality requirements for irrigation water
Low bacterial contamination, corresponding to the EU bathing water guidelines
USA, UK (BSRIA) non-detectable coliform level
Multi-barrier approach: Filtration followed by additional disinfection (USA, CA and other countries)

Orienteering oneself around organic contamination and total suspended solids (TSS) the highest worldwide standards prescribe the following water quality parameters for treated non-potable water:

Parameter	Unit	Limit value
TSS	mg/L	10
Escherichia Coli	1/100 mL	Non-detectable
Total coliform bacteria	1/100 mL	Non-detectable

In Canada, the USA and Japan a minimum chlorine residual or equivalent disinfection is required when treating for non-potable uses (≥ 0.5 mg/L). Below are some of the different regulations and their requirements from around the world.

Overview of worldwide parameters for non-potable water quality:

Country	EU	DE	UK	CA	USA	AU
Standard	Bathing water quality Directive 2006/7/EC [1]	DWA-M 277 Recommendations for construction of systems for handling and usage of greywater and greywater partial flows [2]	Greywater systems – BS 8525-1:2010 for spray applications [3]	Canadian Guidelines for Domestic Reclaimed Water for Use in Toilet and Urinal Flushing [4]	NSF/ANSI 350 – 2014 Onsite Residential and Commercial Water Reuse Treatment Systems [5]	Class A reclaimed water quality objectives (EPA Victoria) [6]
BOD₅ (mg/L)		< 5		Median 10 Maximum 20	Median 10 Maximum 25	< 10
TSS (mg/L)				Median ≤ 10 Maximum ≤ 20	Median 10 Maximum 30	< 5
PH		6.5 - 9.5	5 - 9.5		6.0 - 9.0	6 - 9
UV-Transmission		> 60 %
Turbidity (NTU)		< 2	< 10	Median 2 Maximum 5	Median 2 Maximum 5	< 2
Colour					Zu messen
Odour					Non-offensive
Oily film and foam					Non-detectable
Dissolved oxygen %O2		> 50
Residual chlorine (mg/L)			< 2.0	≥ 0.5	≥ 0.5 - ≥ 2.5 (or equivalent disinfection)	1 (or equivalent disinfection)
Residual bromine (mg/L)			0.0
Sodium adsorption ratio (SAR)					Measured and reported only
Total coliforms		< 10,000/100 mL	10	Median non-detectable Maximum 200 cfu/100 mL
E.coli	500-1000 cfu/100 mL (Inland waters) 250-500 cfu/100 mL (Coastal and transistional waters)	< 1,000/100 mL	Non-detectable	Median non-detectable Maximum 200 cfu/100 mL	Median 2.2/100 mL Maximum 200/100 mL	< 10/100 mL
Legionalla pneumophila		10/100 mL
Intestinal enterrococci	200-400 cfu/100 mL (Inland waters) 100-200 cfu/100 mL (Coastal and transistional waters)		Non-detectable
Pseudomonas aeruginosa		< 100/100 mL
Helminths						< 1 helminth/L
Protozoa						< 1 protozoa/50 litres
Virus						< 1 virus/50 litres

Potable water systems

If non-potable water is to be further treated for potable water quality, then the requirements of drinking water regulations of the respective country must be followed. A sample of the parameters to be investigated for the Drinking Water Ordinance 2001 (amendment of Nov. 2011) in Germany is listed in the following overview. <ref name="Gesetz">http://www.gesetze-im-internet.de/trinkwv_2001/index.html</ref>

Part I: General requirements of drinking water
Attachment 1 (for § 5 paragraph 2 and 3) Microbiological requirements

Serial No.	Parameter	Limit value
1	Escherichia coli (E. coli)	0/100 mL
2	Enterococci	0/100 mL

Attachment 2 (for § 6 paragraph 2) Chemical requirements

Part I: Chemical parameters, whose concentration will not increase within the distribution network of the connected drinking water installation.

Serial No.	Parameter	Limit value mg/L
1	Acrylamide	0.00010
2	Benzene	0.0010
3	Boron	1.0
4	Bromate	0.010
5	Chromium	0.050
6	Cyanide	0.050
7	1,2-Dichlorethane	0.0030
8	Fluoride	1.5
9	Nitrate	50
10	Pesticide and biocide products	0.00010
11	Combined pesticide and biocide products	0.00050
12	Mercury	0.0010
13	Selenium	0.010
14	Tetrachlorethene und Trichlorethene	0.010
15	Uranium	0.010

Part II: Chemical parameters, whose concentration can increase within the distribution network of the connected drinking water installation.

Serial No.	Parameter	Limit value mg/L
1	Antimony	0.0050
2	Arsenic	0.010
3	Benzo(a)pyrene	0.000010
4	Lead	0.010
5	Cadmium	0.0030
6	Epichlorhydrine	0.00010
7	Copper	2.0
8	Nickel	0.020
9	Nitrite	0.50
10	Polycyclic aromatic hydrocarbons	0.00010
11	Trihalogenmethanes	0.050
12	Vinylchloride	0.00050

Attachment 3 (for § 7 Drinking Water Ordinance + amendment of Nov. 2011) Indicator parameters

Part I: General indicator parameters

Serial No.	Parameter	Unit	Limit value
1	Aluminium	mg/L	0.200
2	Ammonium	mg/L	0.50
3	Chloride	mg/L	250
4	Clostridium perfringens (including spores)	number/100 mL	0
5	Coliform bacteria	number/100 mL	0
6	Iron	mg/L	0.200
7	Colour (Spectral absorption coefficient Hg 436 nm)	1/m	0.5
8	Odour	TON	3 at 25°C (analysis according to DIN EN 1622)
9	Taste	-	Acceptable for the consumer and without special modifications
10	Coliform count at 22 °C	-	Without special modifications
11	Coliform count at 36 °C	-	Without special modifications
12	Electrical conductivity	µS/cm	2790 at 25°C
13	Manganese	mg/L	0.050
14	Sodium	mg/L	200
15	Total organic carbon (TOC)		Without special modifications
16	Oxidation potential	mg/L O₂	5.0
17	Sulphate	mg/L	250
18	Turbidity	NTU	1.0
19	Acidity	pH	≥ 6.5 und ≤ 9.5
20	Hardness	mg/L CaCO₃	5
21	Tritium	Bq/L	100
22	Totale indicative dose	mSv/year	0.1

Treatment technology

Effluent treatment process

There are a large number of treatment options for water treatment.

For water treatment and particularly applications of reuse water there are three general treatment steps: primary or mechanical/physical pre-treatment, secondary or biological treatment and tertiary disinfection. A fourth stage can also be introduced in the most advanced water treatment system, quaternary or advanced oxidation technologies.

Primary physical treatment

Example of fine bar screen, 0.8 mm from the PURAIN filter series

Primary treatment is responsible for removing larger particles from the influent water streams. This can be done in a variety of different ways, see Treatment technology. In general the process begins by filtering large debris through progressively finer bar screens which is then collected and disposed of.

Other primary treatment includes grit, particle and scum removal chambers and clarifiers. These can be combined or separate depending on the design of the treatment plant. The goal in these chambers is to remove both large heavy particles and floating scum which cannot be treated easily in the following stages.

Example of sedimentation and sludge removal
Example of skimmer overflow removal with the PURAIN filter series

Sedimentation systems provide a large volume that reduces flow so particles can sink and be collected and disposed of. Floating scum is removed by skimmers.

Secondary biological treatment

AQUALOOP membrane cartridges (blue modules) function as aeration diffusors

Example of the “moving-bed” growth carriers in the MBBR

Water after primary treatment can still be rich in biologically degradable contaminants (BOD). This is actually food for microorganisms and by suppling oxygen to the water, the organisms are encouraged to grow and multiply, consuming the contaminants in an aerobic process.

A kg of BOD needs approximately 1.2 kg of Oxygen to be broken down by the microorganisms in the secondary treatment stage. By knowing the BOD content, flow rate, temperature and dimensions of the tank, engineers can determine exactly how much Oxygen to add through aeration.

Since pure air contains a variety of gases wherein Oxygen is only a portion, ca. 21%, much more air must be provided to a system in order to achieve the necessary conversion of BOD. Diffusors introduce Oxygen from the bottom of the tank by bubbles.

The efficiency of the treatment system depends on the ability of the organisms to reach the food and oxygen. This means that a large surface area for the bacteria growth versus volume is needed.

A particularly efficient design for this required large surface area versus volume is the Moving-bed Biological Reactor (MBBR).

In an AQUALOOP moving bed for example a surface area to volume ratio of 320 m²/m³ is reached.

Tertiary disinfection

Ultrafiltration process, example of the AQUALOOP membranes with 0.02 µm

Stricter environmental regulations increasingly call for further wastewater treatment measures before discharge into the environment is allowed (surface water or infiltration).

Microfiltration or even better ultrafiltration provides a purely mechanical form of disinfection without producing chemical by-products as with Chlorine disinfection. This filtration is usually provided by flat or hollow-fibre membranes with pore sizes down to 0,02 µm.

The microscopic size of the pores within the filter membrane withholds bacteria and viruses from passing through. The fibres are cleaned by a backwash process and by air bubbles passing over the membrane surface.

Tab.: Pore sizes for different levels of filtration <ref name="TU">TU Berlin, GW Recycling Vortrag 24.2.2004</ref>

Type	Sizes [µm]	Filterable
Filtration	10 - 100	Yeast cells
Microfiltration	10^-1 - 10	Bacteria
Ultrafiltration	10^-2 - 10^-1	Viruses
Nanofiltration	10^-2 - 10^-3	Partial dissolved salts
Reverse Osmosis	10^-4 - 10^-3	Dissolved salts

For treatment of non-potable water and sterilization, micro or ultrafiltration is necessary. Dissolved substances however cannot be filtered out.

UV Disinfection

Especially in cases of reuse of greywater or wastewater some treatment standards require further disinfection of the already treated and stored water in order to eliminate the risk of re-contamination. UV disinfection is designed for this purpose when installed behind the pressure increasing system.

Quaternary treatment

Also known as Advanced Oxidation Processes or AOP,this treatment step is only included in the most advanced water treatment plants. Advanced oxidation processes, in a broad sense, are a set of chemical treatment procedures designed to remove organic (and sometimes inorganic) materials in water and wastewater by oxidation through reactions with hydroxyl radicals (OH).

Planning and dimensioning

Simple dimensioning of various system applications can be found here.

Below is an example of how a greywater recycling system is dimensioned and the most important considerations involved.

Input values for dimensioning

Values for dimensioning can vary greatly between systems, regions and countries and depend heavily on different consumption patterns. Below are descriptions of each dimensioning step as well as example calculations in which specific values can be substituted.

Water supply

Liter/person/day;

a. Drinking	e. Teeth brushing	i. Washing machines	m. Garden
b. Cooking	f. Bathing- 2x per week	j. Cleaning
c. Dishwasher	g. Showering - 2x per week	k. Car washing
d. Washing	h. Toilet flushing	l. Indoor plants

<ref> der Jahre 1993 bis 1997 in Siegen Forschungsstelle Wasserwirtschaft fwu Universität Siegen DIN 1989-1, Universität Oldenburg</ref>

In general, the average daily water usage can be found and calculated from the different streams i.e. Bath & Shower, using the above diagram. These can also be measured directly on-site or taken from national associations and standards as seen below for Germany and Australia.

The values can be looked at in one of two ways: as the daily water needs and the supply of water for reuse purposes.

Supply/person/day	Germany (fbr)	Australia (NSW)
Shower, bath and sinks	40 L	66 L
Washing machine	13 L	47 L
Total supply	53 L	113 L

Water needs

Needs/person/day	Germany (fbr)	Australia (NSW)
Toilet	25 L(average)	14,4 L
Washing machine	13 L	47 L
Cleaning	5 L	-
Irrigation	5 L	35 L
Total needs	48 L	96,4 L

In the example shown, the existing greywater sources equalling 52 L cover the daily demand of 48 L. For larger demands other sources such as rainwater can cover the extra demand.

Reuse water parameters

The quality of water to be recycled depends heavily on its source. As an example of greywater, see below for some typical ranges that are used in dimensioning of systems.

COD - 250-430 mg/L Germany (fbr)
BOD - 125-250 mg/L Germany (fbr) Average = 187.5 mg/L
N - 0.7-48 mg/L Australia (NSW) (Greywater from washing machine)

Reuse water pipework dimensioning

Information in this section is based on the German standard DIN 1986-100:2016-12: Contaminated water discharge from collection pipework within buildings. This is an example only and the necessary regional or national standards should be consulted during dimensioning of your reuse water system.

Table: Discharge ability of drainage pipework with a fill volume of h/d = 0.5 from Tab. A.3 from DIN 1986 with a minimum grade of 1.00 cm/m.

DN	d_{i, min} mm	Q_{ww, max} L/s
100	96	2.5
150	146	7.7
200	184	14.2
300	290	47.4

Determination of discharge ability:

$Q_{ww}=K{\sqrt {\sum DU}}$

According to

Q_ww	Discharge ability in litres per second, (L/s)
K	Discharge ratio
∑DU	Sum of discharge values

Table: Discharge ratios (K)

Building type and usage	K
Unregular usage e.g. in apartment buildings, old-age and boarding homes, offices	0.5
Regular usage e.g. hospitals, schools, restaurants, hotels	0.7
Frequent usage e.g. in public toilets, and/or showers	1.0

Table: Connection and size values from ventilated and unventilated single connection piping taken from Tab. A.6 of DIN 1986.

Drainage object	Connection value DU L/s	Single connection piping
Sinks	0.5	DN40
Showers	0.8	DN50
Baths	0.8	DN50
Washing machines	1.5	DN 56/60

Example:

Table: Example calculation from an apartment building

Drainage object	Total connection value DU L/s
20 x Showers	16.0
20 x Sinks	10.0
20 x Washing machines	30.0
Total	56.0

$Q_{ww}=K{\sqrt {\sum DU}}$

$Q_{ww}=0.5\times {\sqrt {56.0\ {\frac {l}{s}}}}$

$Q_{ww}=3.74\ {\frac {l}{s}}$

=> From Tab. A.3 a DN150 collection connection would be adequate.

Packing bed dimensioning

While the design for activated sludge process relies on the sludge load (kg BOD/kg TS/day), a maximum surface loading is generally determined for packing bed processes. This is calculated from the amount of pollutants entering the system per day (g BOD or COD), the area available on lava rocks, plastic growth carriers or equivalent and is given in kg BOD or COD/m²/day.<ref name="isa" />

In small wastewater treatment systems, a surface load of <0.004 kg BOD₅/m²/day should be maintained to ensure proper operation with a factor of safety. Based on this and since the COD content is on average twice the BOD content, the COD surface loading can be assumed to be 0.008 kg COD/m²/day.

In addition to the oxygen consumption for BOD degradation, the oxidation of nitrogen from ammonium NH4 to nitrate NO3 is to be considered. This increases the required amount of air depending on the nitrogen content in the reuse water (approx. 10 mg N/L with greywater). With greywater this leads to three times the amount of oxygen required, approx. 30 mg/L. Normally the water is not continuously distributed throughout the day in reuse systems Therefore it must be ensured that the packing bed receives sufficient time (> 2 h) after loading to reduce pollution. During this period, the clean water should not be drawn from discontinuous system, because otherwise it may lead to increased COD/BOD₅.

MBBR growth carriers

One type of biological water treatment is called MBBR (Moving-bed biological reactor). The so-called moving-bed consists of numerous growth carriers (growth bodies) within the treatment reactor, which have a high surface-to-volume ratio. The required quantity of growth bodies can be determined from the permissible surface load of 0.004 kg BOD/m²/day which is based on the inlet flow rate and organic loading. Example: 300 L/day greywater system for a single-family home As stated previously the average BOD concentration in greywater is on average 187.5 mg/L.

$Daily\ loading=300\ {\frac {L}{d}}\times 187.5\ {\frac {mg}{L}}\div 1000^{2}=0.056\ kgBOD/d$

By dividing by the maximum surface load allowed, determine the surface area needed,

$Required\ su{\mathit {rf}}ace\ area=0.056\ {\frac {kgBOD}{d}}\div 0.004\ {\frac {kgBOD}{m^{2}\cdot d}}=14\ m^{2}$

Now take the surface area/volume ratio from the growth carrier manufacturer, in this case 320 m²/m³ and divide the required surface area,

$Required\ volume\ of\ floating\ elements=14\ m^{2}\div 320\ {\frac {m^{2}}{m^{3}}}=0.044\ m^{3}=44\ L$

=> For this single-family home system 44 L of growth carriers are needed.

Determining the oxygen requirement

In the bioreactor the bacteria must be supplied with oxygen and nutrients. The nutrients are the BOD content of the source water. The average BOD of greywater systems is approximately 187 mg/L. A specific amount of air is required for treating this.

Some of the parameters influencing the air requirement are:

Temperature
Chemical inlet parameters (see greywater inflow data)
Aeration depth
Diffusor area

For simplicity, an oxygen content of 23 %wt. can be assumed.

Experience has shown that approximately 1.2 kg of oxygen are required for the conversion of 1 kg of BOD.

The efficiency of the oxygen exchange into the water depends on the bubble size and the duration of the bubbles in the water. Coarse bubble diffusors generally have an oxygen exchange efficiency of 1% per meter due to their low surface area to volume ratio. Fine bubble diffusors generally have an efficiency of 5% per meter. The deeper the diffusors are installed in the water, the more oxygen is exchanged into the water.

If an intermittent aeration cycle is used then the blower size may change.

Example: Aeration of a 6-person greywater system with coarse bubble diffuser

$Air\ oxygen\ content=1.2041\ {\frac {kg}{m^{3}}}\times 23\%=0.2769\ {\frac {kg}{m^{3}}}$

$BOD\ Daily\ inlet=360\ {\frac {L}{day}}\times 187.5\ {\frac {mg}{L}}\div 1000^{2}=0.0675\ {\frac {kg}{day}}$

$BOD\ Inlet\ rate=0.0675\ {\frac {kg}{day}}\times 1000^{2}\div 24\ {\frac {hrs}{day}}\div 60\ {\frac {min}{hrs}}=46.9\ {\frac {mg}{min}}$

$O2\ Inlet\ rate=46.9\ {\frac {mg}{min}}\times 1.2\ {\frac {mgO2}{mgBOD}}=56.3\ {\frac {mg}{min}}$

$Air\ inlet\ rate=56.3\ {\frac {mg}{min}}\div 1000^{2}\div 0.2769\ {\frac {kg}{m^{3}}}\times 1000\ {\frac {L}{m^{3}}}=0.203\ {\frac {L}{min}}$

$Di{\mathit {ff}}usor\ rate=0.203\ {\frac {L}{min}}\div (1\%\times 2m)=10.2\ {\frac {L}{min}}$

=> The quantity of air 10.2 L/min is for constant blower operation.

Table: Dry air requirement for greywater systems with a coarse bubble diffuser and an aeration depth of 2 m

Air density	1.293	kg/m³		Supply	60	l/person/day
O2	23%	Molar mass fraction		BOD content	187.5	mg/L
O2 in air	0.29739	kg/m³		O2 need	1.2	kgO2/kgBOD
	GW inlet	BOD inlet		O2 requirement			with 1% efficiency	Air demand
PE	L/day	kgBOD/day	mg BOD/min	mgO2/min	m³Air/min	LAir/min	LAir/min	m³/day
6	360	0.0675	46.9	56.3	0.000203	0.203	10.2	14.7

Dimensioning blower

With AQUALOOP technology, air is supplied through the blower which performs several functions at the same time:

Cleaning of the membrane fibres by creating turbulence through the fibres (> 30 litres/min/membrane)
Cleaning the fluidized-bed growth bodies (> 30 litres/min/30 litres of growth bodies)
Introduction of oxygen (see Determining the oxygen requirement)

Example: Single-family house with 6 inhabitants, coarse-pore diffusor

Blower cycle: 5 minutes aeration, 10 minutes pause

Blower operation: 20 minutes/hour or 8 hours/day

The system must therefore provide the same amount of air as a continuous operating system but in 1/3 of the operation time.

$Blower\ size=10.2\ {\frac {L}{min}}\times ({\frac {24hrs}{8hrs}})=30.6\ {\frac {L}{min}}$

=> A blower with a flow rate of > 30.6 L/min is needed.

For larger systems, that require more oxygen introduction, a fine-pore diffusor should be installed.

Example: Aeration with fine-pore diffusor at 2 m depth for 20,000 L greywater / day

$Oxygen\ content=1.2041\ {\frac {kg}{m^{3}}}\times 23\%=0.2769\ {\frac {kg}{m^{3}}}$

$BOD\ loading=20,000\ {\frac {L}{day}}\times 187.5\ {\frac {mg}{L}}\div 1000^{2}=3.75\ {\frac {kg}{day}}$

$BOD\ loading=3.75\ {\frac {kg}{day}}\times 1000^{2}\div 24\ {\frac {hrs}{day}}\div 60\ {\frac {min}{hrs}}=2,604\ {\frac {mg}{min}}$

$O2\ requirement=2,604\ {\frac {mg}{min}}\times 1.2\ {\frac {mgO2}{mgBOD}}=3,125\ {\frac {mg}{min}}$

$Inlet\ air\ requirement=3,125\ {\frac {mg}{min}}\div 1000^{2}\div 0.2769\ {\frac {kg}{m^{3}}}\times 1000\ {\frac {L}{m^{3}}}=11.29\ {\frac {L}{min}}$

$Blower\ size=11.29\ {\frac {L}{min}}\div (5\%\times 2m)=112.9\ {\frac {L}{min}}$

=> A blower with a flow rate of > 112.9 L/min is needed.

Due the efficiency difference between coarse-pore and fine-pore diffusors, in particular for larger systems, continuous fine.pore diffusors should be installed to have the most efficient operation as possible.

Membrane technology

Membrane technology has been established in recent years as a promising method to deliver hygienically pure water. Membrane filtration will, as with a sieve, be dependent on the membrane pores for filtering out fine particles down to dissolved substances as well as bacteria and viruses.

The often stated disadvantages of membrane filtration

higher energy requirement due to required pressure differential
membrane fouling increases the required pressure differential
fats and oils block the membrane
limited suction and backwash pressure with sheet membranes
higher maintenance effort due to specialized chemical cleaning performed by specialists
low membrane lifetime
higher price of the membrane

can be resolved wherever possible by optimization of the pre-filtration, biological degradation and with new membrane technology so that today membrane technology can be successfully introduced into an expanded application range.

Pore sizes, pressure differential

	Size [µm]	required pressure differential [bar]	Filterable
Filtration	10 – 100	10^-1 – 1	Yeast
Microfiltration	10^-1 – 10	ca. 1	Bacteria
Ultrafiltration	10^-2 – 10^-1	ca. 5	Viruses
Nanofiltration	10^-3 – 10^-2	10	Partial salts
Reverse Osmosis	10^-4 – 10^-3	100	Salts

<ref name="TU Berlin">TU Berlin, GW Recycling Vortrag 24.2.2004</ref>

Micro and ultrafiltration are designed for non-potable water treatment and disinfection. Dissolved substance however cannot be filtered out.

Membranes for ultra and microfiltration

For cleaning special organic fibres are deployed in ultra and microfiltration for water and wastewater treatment. The basic principal of this filtration is the use of porous, organic hollow-fibre membranes with microscopic pores as a filter medium. The fibres have an outside diameter of less than 1 mm. In order to maintain an adequate surface area and a constant flow, hundreds of fibres are bundled together and wound around a module. Regular chemical cleaning can be eliminated. Advantages oft he new membranes are:

The membrane fibres are permanently hydrophilic so they function immediately when immersed in water, drying does not damage the membrane
Backwashable with up to 3 bar
Special additives in the PE membrane prevent growth of microorganisms, suppression of 99.97% according to the Japanese standard JIS Z 2801
The membrane is stable against acidic, alkaline as well as chlorine-based cleaning solutions

Membrane flow rate, flux-stabilization curve without chemical cleaning

Over time, the flow through a membrane decreases, approaching a so-called stabilization flux. This is the flow that remains constant for a very long time without further cleaning.

A biolayer forms on the membrane fibres
Depending on the water quality and cleaning mode with backwash and aeration, the membrane will stabilize to a constant flow rate
The stabilization value is used for flow rate simulations. In the example, the stabilization value is approximately 50 L/m²/hr/bar. The stabilization value is dependent on operation settings, flow rate, wastewater quality, temperature and pre-treatment.

Flow rate and membrane life with chemical cleaning

The AQUALOOP membrane can be loaded with 1 Mio. ppm free chlorine without limitation on its 10-year lifespan. With the recommended cleaning concentration of 0.25% (= 2500 ppm) approx. 400 chemical cleanings can be conducted without limiting the lifespan. To calculate a reduced lifespan due to chlorine cleaning, the following formula can be used:

$L={\frac {chlorine_{total}}{chlorine_{conc}\times N\times 12}}$

L [years]:	lifespan in years (maximum 10 years)
Chlorine_total: [ppm]	1 Mio. (total allowable load with free chlorine)
Chlorine_conc: [ppm]	cleaning concentration (max. 0.5% = 5,000 ppm)
N [-]	number of cleanings per month

Example:
Cleaning 4 times per month (N = 4) with a 0.25% cleaning solution (chlorineconc = 2500 ppm):

$L={\frac {1,000,000}{2,500\times 4\times 12}}=8.3\ years$

The membrane lifespan therefore amounts to 8.3 years.

Beispieldurchfluss einer AQUALOOP-Membran in Abhängigkeit der Wartungsintervalle bei einem Grauwasserrecycling System

Membrane station

1. Backwash container
2. Backwash pump
3. Suction pump
4. Permeate distribution nozzle
5. Central blower connection
6. Membrane
7. Weights
8. Aeration distribution nozzle

In the application example shown the membranes are installed on a type of station. The integrated suction pump draws the water uniformly through the membrane and supplies it to a treated water tank through a filtrate hose. To guarantee over time a high flow rate the membrane is periodically flushed with an integrated backwash pump. The required volume for backwash water is taken by the system out of the backwash tank which is found above the pumps. Furthermore the membrane will be periodically blown clean with air directed through the fibres to remove deposits. To this end the membrane station is connected to a blower through a hose attachment. The air is uniformly distributed through a connection manifold with symmetric connections and supplies simultaneously the bioreactor with oxygen. For larger water treatment systems multiple membrane stations can be connected in parallel.

Since the work is over a very large membrane surface area the pressure differential and required energy needs for filtration are low. Demonstration systems have shown an energy requirement of less than 2.5 kWh/m³.

Membrane process advantages

Quality criteria for filtrate (TSS, turbidity, coliforms) is easily achieved
No or little sludge yield on the treated water side
Stable operation, not susceptible to load fluctuations
Compact system sizes, smaller bioreactor required
Less operating effort
The biological pre-treatment cleans the water so the membrane must filter only the remaining sludge so that odour-forming compounds are also removed

Tank Dimensioning

In a greywater recycling system two types of tanks are distinguished:

Bioreactor
Treated water storage

The size of the bioreactor depends on the degree of water contamination, the treatment volume and the flow through the filter membranes. The size of the treated water storage depends on the daily demands of the user as well as the flow through the membrane filters.

Bioreactor

A bioreactor is only needed for reuse system with > 5 mgBOD/L such as with greywater or wastewater. Below this amount aeration is not required for treatment but the tank dimensioning principals are the same.

The bioreactor usually contains the aeration and growth carriers for water treatment as well as biological sludge removal as well.

Example of bioreactor with pre-filtration (1), biodegradation (2 & 3), sludge removal (5) and ultrafiltration (4)
Example of the working volume of the bioreactor

Example: Greywater recycling system in a 112-person apartment building in Europe

$Greywater\ need=112\times 48\ {\frac {L}{person\cdot day}}\ (toilet,{\mathit {wa}}shing,cleaning,irrigation)=5,376\ {\frac {L}{day}}$

The so-called "working volume" should be > 50% of the daily need.

$Working\ volume=5,376{\frac {L}{day}}\times 0.5=2,688\ L$

In the example system the minimum water level is set at 700 mm so that the membrane filters are always submerged in the water.

Using a tank with the following dimensions, the working volume for the example system can be calculated:

Height: 2.1 m
Overflow height: 1.55 m
Length: 2.39 m
Width: 1.35 m

Working height = 1.55 m - 0,7 m = 0.85 mm Working volume = 2.39 m x 1.35 x 0.85 = 2.74 m³

=> The tank has a working volume greater than the 50% daily needs of the users.

Treated water storage

Example of the working volume of a treated water tank from the AQUALOOP system

A treated water tank depends on the daily water needs of the building and should provide for 50% of the daily needs. The working volume of the treated water storage is the volume between the emergency overflow and the suction inlet.

Degree of usage

The degree of usage of a water treatment system is the ratio of need versus yield.

Sample calculation for a greywater recycling system:

Building: Single-family home with 4 inhabitants

Usage: Toilet, washing machine, cleaning and irrigation, see 3.1.2 water needs for Germany

$Q_{daily\ need}=4\ \times \left({\dfrac {25\ {\frac {L}{Person}}}{toilet}}+{\dfrac {13\ {\frac {L}{person}}}{{\mathit {wa}}shing\ machine}}+{\dfrac {5\ {\frac {L}{person}}}{cleaning}}+{\dfrac {5\ {\frac {L}{person}}}{irrigation}}\right)=192\ {\frac {L}{day}}$

$Q_{daily\ yeald}=4\ \times \left({\dfrac {40\ {\frac {L}{person}}}{shower,baths,sinks}}+{\dfrac {13\ {\frac {L}{person}}}{{\mathit {wa}}shing\ machine}}\right)=212\ {\frac {L}{day}}$

$Degree\ of\ usage=192\ {\frac {L}{day}}\div 212\ {\frac {L}{day}}=0.9$

=> The greywater yield in this example is slightly higher than the demand. This is optimal in order to compensate for daily fluctuations (see table "Daily fluctuations of greywater daily production percentages in an apartment building as an example").

If the yield is significantly higher than the demand then, for example, the connection to the washing machine discharge can be disconnected. The discharge water from the washing machine is more polluted and this reduces the maintenance intervals of the reuse systems.

If the yield is lower than the demand, then it should be checked whether the discharge from a wastewater treatment system or rainwater harvesting can be connected. With new technologies, such as reverse osmosis or advanced oxidation, multiple re-processing of the reuse water is now a possibility.

When dimensioning a reuse water system it is also necessary to take in account when the water volumes are produced and consumed within a day. Depending on the building type, large fluctuations can occur within the day. The following table illustrates this

Table: Daily fluctuations of greywater daily production percentages in an apartment building as an example

Time interval	Percentage proportion of daily volume %
6 hrs to 9 hrs	30
9 hrs to 12 hrs	15
12 hrs to 18 hrs	0
18 hrs to 20 hrs	40
20 hrs to 23 hrs	15
23 hrs to 6 hrs	0

Dimensioning of sludge pump

Sludge removal inside of a tank

Sludge pumps should be positioned so that no „dead zones“ exist. Dead zones are areas with little aeration or mixing of the water.

Installation of water treatment systems

Connection of water treatment system to pipework

Example of gravity-fed greywater system

Example of a lift pump system

Many homes and buildings provide the option to install water treatment systems so that the collection of the water is achieved simply by gravity. The size of the pipe needed can be calculated as under section 3.1. These gravity systems must simply be installed below the outlet of the collection points like showers and can be in basements, underground, indoor/outdoor, etc.

Many homes and buildings are also single-story structures and the location may prevent installation of the water treatment systems below the outlet collection level. In this case, a lift pump is needed to raise the water to the level of inlet to the water treatment system.

Quality requirements at pipeline system

In water treatment systems, piping and hoses are required for the non-potable water as well as the aeration (blowers) supply. Many regulations governing reuse and non-potable water require that the piping supplying this water be indicated as such using either colours (purple in the case of Australia and California) or labels or both.

Experience has shown that blower hoses, suction hoses for distribution pumps and filtrate hoses are best installed using EPDM material piping.
The non-potable or reuse piping from the distribution pumps to the connected fixtures is recommended as pressure-resistant plastic or if desired, copper piping.
Do not use copper piping in the storage tank because it oxidizes even at low concentrations of hydrogen sulphide (foul odour) in combination with humidity.
All PVC hoses, as well as those chemically resistant, are eventually bleached due to contact with water. The softening agents serve as an ideal breeding ground for bacteria. Odours are also possible.

Blower piping

The loss of pressure $p_{V}$ by friction is to be considered with a long blower piping. This is primarily dependent on the pipe cross-section, wall roughness and the flow rate of supply air.

Dimensioning is done based on the pump curve of the installed blower. The maximum pressure $p_{ges,max}$ at the dimensioning point is calculated by:

$p_{ges,max}=p_{W,max}+p_{V,max}$

According to:
$p_{ges,max}$ Total required pressure at maximum
$p_{W,max}$ Water level above air inlet
$p_{V}$ Pressure losses in piping

Blower type	p_ges,max [mbar]	p_W,max [mbar]	p_{V, max} [mbar]	½“- max. pipe length [m]	1“- max. pipe length [m]
AL-BL30	130	110	20	66	--
AL-BL60	170	150	20	20	500
AL-BL100	200	180	20	--	220
AL-BL120	200	180	20	--	140
AL-BL200	200	180	20	--	70

Table: Pipe cross-sections and maximum lengths with AQUALOOP blowers

Ventilation system

Example of ventilation of gravity pipework inside a building for greywater recycling.

The ventilation of sanitary pipes within buildings is governed by DIN EN 12056. The German supplementary standard DIN 1986-100 is used.

AQUALOOP does not require separate ventilation if connected to a ventilated inlet supply pipe. Individual AQUALOOP tanks are connected together above the maximum water level. This does not apply to multiple tanks connected together for either bioreactor or clear water storage volume. Drainage fixtures to AQUALOOP systems are equipped with a siphon when required according to national or regional plumbing standards. If a lift pump after the overflow is to be provided, attention must be paid to the connection in regard to national or regional standards.

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Water treatment and greywater recycling