Membrane BioReactor (MBR)
Sheets

13-jun-2006, STOWA

 

 

Country

 

Japan - The Netherlands

Stage of development

Full scale

Process -

Line

Water

 

Function

Secondary treatment and clarification

 

Input

Effluent from primary treatment

 

Concept

Ultra- and microfiltration using porous membranes

Keywords: decrease area demand; improve effluent quality; water line; SS removal effluent

 

 

Background

The term membrane bioreactor (MBR) defines a combination of an activated sludge process and membrane separation. Due to recent technical innovations and significant cost reductions the applicability for the MBR technology in municipal wastewater treatment has sharply increased.

 

Description and working principle

The MBR process can be employed in activated sludge processes, using the membranes as liquid-solid separation instead of the usual settling. Suspended solids can be removed completely and bacteria-free treated water produced. The sludge concentration and hydraulic loading rates are considerably higher than in conventional treatment.

Pre-treated, screened influent enters the membrane bioreactor, where biodegradation takes place. The mixed liquor from the bioreactor is withdrawn and pumped along submerged or semi-crossflow filtration membrane modules. The permeate from the membranes constitutes the treated effluent.

The reject stream, consisting of concentrated biosolids, is returned to the bioreactor. Excess biosolids are wasted from the bioreactor or from the return line. Due to the membranes acting as an absolute barrier to solids, it is possible to improve the effluent quality, especially with regard to suspended solids as well as bacteria and viruses.

The separation of hydraulic and solids retention times provides a good control of biological reactions. Due to the high biomass concentration in the bioreactor, the reactor can be much more compact compared to conventional activated sludge systems.

 

Design guidelines / Technical data

Kubota

Membrane geometry

flat plate

Process configuration

submerged

Material

hydrophilic polypropylene

Pore size

0,4 mm

Surface area of one plate

0,8 m2

Distance between plates

7mm

Process mode

Ralaxation (optional)

Cleaning procedure

intensive cleaning every 6 to 12 months

Design flux

30 - 40 l/m2.h

 

 

Mitsubishi (Sterapore membrane - www.sterapore.com/eigo0)

Membrane geometry

hollow fibre

Process configuration

submerged

Material

hydrophilic polyethylene

Pore size

0,4 mm

Outer diameter of fibre

540 mm

Inner diameter of fibre

360 mm

Process mode

relaxation and back-flush

Cleaning procedure

maintenance cleaning every week

 

intensive cleaning every 3 to 6 months

Design flux

10 -20 l/m2.h

 

Design and operational parameters as well as removal efficiencies are strongly dependent on the wastewater characteristics. The membranes described above have been extensively tested on pilot scale for the Dutch wastewater situation. In the table below some technical parameters are given (WWTP Beverwijk).

 

Parameter

Range

Unit

Sludge load

0.05 - 0.1

kg COD/(kg MLSS.d)

Sludge load

0.008 - 0.012

kg N/(kg MLSS.d)

MLSS conc.

10 12

g/l

Temperature

5 - 25

C

Sludge age

30 - 60

days

 

Performance

General performance

Some general indications of the removal efficiencies of the MBR systems were given by [3]:

         In general only COD, BOD, SS and nutrient removal in MBR systems are described in literature. The results on nutrient removal were often very good due to the very low loading of the systems. The SS permeate concentration was usually below detection level. For a number of (full scale) installations the microbial parameters were measured and published. In general, the removal of total and faecal coliforms was around log 6, the removal of viruses was varying between log 2 - 4. An advantage of the MBR is that the micro-organisms are totally removed and not just inactivated with a risk of reactivation.

         Only few publications were found in which attention was paid to the removal of micro-pollutants. In one publication a research was presented in which AOX's, medical substances, pesticides and endocrine substances were measured in both the MBR's permeate and a conventional WWTP's effluent. The AOX level in the MBR permeates was equal to the conventional effluent. For all the other substances significant lower concentrations were measured in the MBR permeate.

Removal efficiencies for the most common parameters are given in the table below. In a MBR all of the suspended solids are removed. As a consequence the removal of heavy metals and micropollutants attached to the suspended solids is also improved.

Parameter

Unit

MBR

Conventional treatment

Suspended solids

mg/l

0

10

COD

mg/l

30

40 - 50

NTotal

mg/l

10

10

PTotal

mg/l

0,15 - 0,5

0,5 - 1,0

 

Operational stability and maintenance

Pre-treatment

From experiences on several municipal MBR plants it is known that membrane systems can be very sensitive for macro-fouling by debris. The occurrence of debris has led to problems regarding throughput and eventual membrane damage. The main purpose of the pre-treatment is to remove solids (screenings) which are harmful for membranes, such as coarse solids (plastics, leaves, seeds, sand particles), oils, fats and hairs.

Membrane fouling and cleaning

Two main types of cleaning can be distinguished: chemical cleaning and mechanical cleaning. Chemical cleaning is essentially a physical-chemical reaction between the cleaning chemical and the foulant. Mechanical cleaning is a term used for the physical removal of suspended solids from the membrane material. Mechanical cleaning is usually based on turbulence and fluid mechanics, caused by (coarse) bubble aeration, permeate back-flushing, relaxation and circulation.

Cleaning of the membranes, irrespective of the procedure used, has a knock on effect to the membrane life-expectancy and operational replacement costs. Moreover, the chemical usage required for cleaning purposes has an impact on the biological system and the membrane integrity.

In municipal MBR systems mainly bio-fouling, and cake formation occur. Bio-fouling can be treated with a NaOCl cleaning eventually followed by an acid cleaning. Cake formation can be treated hydraulically.

The most important aspect is the operation of the MBR to prevent the forming of a cake on the membranes, followed by the removal of the cake layer and the cleaning of the membranes with chemicals. Some basic rules to prevent cake formation on the membranes are given below:

           use a membrane with a high maintainable permeability; lower suction pressures on the membrane surface prevent cake formation

           reduce dead zones in the membrane module/tank, and avoid a too higher packing density of the membranes

           select responsible operating fluxes, however, during peaks temporary higher fluxes can be maintained

           generate larger sludge flocs to allow a more permeable cake layer on the membrane

           install and maintain good biological conditions thus preventing the formation of EPS and filamentous organisms

Alpha factor and energy consumption

The transfer of oxygen from air into water depends on the characteristics of the transfer layer, air bubble size and mean residence time of the bubble in the water. These last two parameters depend strongly on the viscosity of the solution to be aerated. Viscosity itself can be influenced by reactor configuration, the mixing/aeration device, and the concentration and characteristics of the activated sludge. In general the concentration and as a result the viscosity of MBR sludge is higher than in a conventional sludge system.

Sludge treatment

In comparison with conventional waste activated sludge the MBR sludge contains smaller flocs and has a somewhat higher viscosity. Based on tests executed [3], it can be concluded that MBR sludge thickening and de-watering shows results comparable with conventional activated sludge.

 

 

 

 

 

 

 

 

 

Capital and operating cost

General information

Information on costs is available from different feasibility studies in which the costs for a MBR- and traditional installation under different circumstances were compared. In the figure below investment costs for a new WWTP are compared [4].

 

Distribution of the capital costs for a 2,500 m3/h treatment plant

The annual costs of a MBR installation are strongly influenced by the depreciation for the mechanical equipment and the replacement of the membranes. At the moment the latter is still difficult to predict, practical experiences from 3 to 8 years being not enough for a realistic estimation. With manufacturers, the discussion around the membrane lifetime has led to capacity guarantees.

Regarding variable costs, especially the energy consumption is an interesting item, which is mainly determined by the alpha-factor and consequently the energy for aeration. In the feasibility studies mentioned before, alpha‑factors of 0.40 - 0.45 have been used for calculation purposes. Based on the results of pilot scale measurements, side study 3 and full scale measurements at WWTPs in Germany it is expected that these values are too low. Cost differences between a MBR and traditional WWTP concerning manpower, chemical consumption and sludge treatment are supposed to be minimal.

 

Reference installations

About 600 Kubota reference installations are reported world-wide for industrial and municipal applications. Of the 21 installations in Europe, eight are treating municipal sewage. Hydraulic capacities are ranging from 200 to 13.000 m3/d. The largest installation realised so far is the WWTP Swanage (23.000 p.e./1999) in the UK.

About 700 Mitsubishi reference installations are reported, most of them are situated in Japan. A third of these installations is used for the treatment of domestic wastewater.

Suppliers / Patents

Kubota Corporation

London Office, Membrane System Department

8 Hanover Street - London W1S 1TYE - UK

Tel: +44 - 20 7290 2730 - Fax: +44 20 7290 2733 - E-mail : membrane@kubota.co.jp - Web: www.kubota.co.jp/english/index.html

Kubota has a co-operation agreement with SOLIS Engineering in the Benelux.

Mitsubishi Rayon Co.,Ltd

Membrane Products Department

6-41, Konan 1-chome - Minato-ku - Tokyo - Japan

Tel : +81 - 3 5495 3152 - Fax : +81 3 5495 3217 - E-mail : membrane@mrc.co.jp - Web: www.mrc.co.jp/english/

 

Literature references

[1]

Websites owned by Kubota and Mitsubishi Corporation

[2]

DHV Visit report Japan

[3]

Magazine H2O: MBR Special.11/2001.

[4]

Stowa report 2002-11A: MBR for municipal wastewater treatment. Pilot plant research Beverwijk WWTP. 2002.

 

Graphics

Kubota - process design

Mitsuibishi - process design

Kubota - top view

Mitsubishi - top view