Membrane bioreactor (MBR) is a combination of membrane processes like microfiltration or ultrafiltration with a biological wastewater treatment process, the activated sludge process. It is now widely used for municipal and industrial wastewater treatment. In general, there are two different MBR configurations; (1) submerged membrane bioreactor (SMBR) and (2) side stream membrane bioreactor.  In the first configuration, the membrane is located inside the biological reactor, submerged in the wastewater. In the latter configuration, the membrane is located outside the reactor, as an additional step after biological treatment.
The water resource scarcity implies the need to reuse water, once it has been properly treated, thus guaranteeing environmental protection. Among the treatment technologies available to regenerate wastewater, those that use membranes stand out for their capacity to retain solids, salts and even disinfect water, producing water suitable for reuse in irrigation and other applications.
A membrane is a material that allows the selective flow of certain substances. In case of the water purification or regeneration, the aim is for the water to flow through the membrane, retaining undesirable species on the other side. Depending on the type of membrane it is possible to get better pollutant retention. Different types of materials can be used to manufacture the membrane. However, in the field of wastewater treatment and due to the several operational restrictions, the number of materials that can be used to construct a membrane is different than that in the other fields.  Some of the required characteristics in a membrane for wastewater treatments are chemical and mechanical resistance for a period of 5 years of operation, highly acidic or basic properties, or adaptability to operate ina a wide range of pH.
There are two main types of membrane materials available on the market: organic based polymeric membranes and ceramic membranes. Polymeric membranes are the most commonly used material in water and wastewater treatment. In particular, the polyvinylidenedifluoride (PVDF) is the most popular one due to its long lifetime and chemical and mechanical ressitance. 
|Polymeric Membrane Materials|
|(HD)PE||(High density) polyethylene|
|Ceramic Membrane Materials|
|Aluminium oxide / Alumina
Titanium dioxide / Titania
Zirconium dioxide / Zirconia
|Comparison: Polymeric vs Ceramic Membranes|
|Subject to mechanical damage||Higher mechanical strength|
|Bundles of hundreds of hollow fibers||One "piece" per element|
|Vulnerable to chemicals||Good chemical resistance|
|Lower cost in terms of capacity||High capital costs|
|Very common product||Little operational experience|
|Majority of comercial products||Few applications|
When used with domestic wastewater, MBR processes can produce effluent of high quality enough to be discharged to the coastal, surface, or brackish waterways or to be reclaimed for urban irrigation. Other advantages of MBRs over conventional processes include small footprint, easy retrofit, and upgrading old wastewater treatment plants.
It is possible to operate MBR processes at higher mixed liquor suspended solids (MLSS) concentrations compared to conventional settlement separation systems, thus reducing the reactor volume to achieve the same loading rate.
Two MBR configurations exist: internal/submerged, where the membranes are immersed in and integral to the biological reactor; and external/side stream, where membranes are a separate unit process requiring an intermediate pumping step.
Recent technical innovation and significant membrane cost reduction have enabled MBRs to become an established process option to treat waste waters. As a result, the MBR process has now become an attractive option for the treatment and reuse of industrial and municipal waste waters, as evidenced by their constantly rising numbers and capacity. The current MBR market has been estimated to value around US$216 million in 2006 and to rise to US$363 million by 2010.
Based on the estimated global MBR market of US$838.2 million in 2011, the MBR is projected to grow at an average rate of 22.4%, reaching a total market size of US$3.44 billion in 2018.
The global membrane bioreactor market is expected to grow in the near future because of various driven factors for instance scarcity of water worldwide, which makes wastewater reclamation necessary. This will be further aggravated by climate change. The growing environmental concerns over industrial wastewater disposal along with the declining freshwater resources across developing economies also accounts for the demand of MBR technology. Population growth, urbanization, and industrialization will further complement the business outlook. Contingent on their composition, these changes can be demanding on natural resources and pose unsustainable challenges for environment. Therefore, membrane bioreactor (MBR) technology is regarded as a key element of advanced wastewater treatment and reuse schemes and it is focused to grow towards sustainable water management across the municipal and industrial sectors.
However, high initial investments and operational expenditure may hamper the global membrane bioreactor market. In addition, technological restraints including the recurrence of fouling in the MBRs are likely to hinder production adoption. Ongoing R&D progressions toward increasing output and minimizing sludge formation are anticipated to fuel industry growth.
Membrane bioreactors can be used to reduce the footprint of an activated sludge sewage treatment system by removing some of the liquid components of the mixed liquor. This leaves a concentrated waste product that is then treated using the activated sludge process.
Recent studies show the opportunity to use nanomaterials for the realization of more efficient and sustainable membrane bioreactors (Nanomaterials Membrane Bioreactor - NMs-MBR) for wastewater treatment.
The MBR process was introduced in the late 1960s, as soon as commercial-scale ultrafiltration (UF) and microfiltration (MF) membranes were available. The original process was introduced by Dorr-Oliver Inc. and combined the use of an activated sludge bioreactor with a cross-flow membrane filtration loop. The flat sheet membranes used in this process were polymeric and featured pore sizes ranging from 0.003 to 0.01 μm. Although the idea of replacing the settling tank of the conventional activated sludge process was attractive, it was difficult to justify the use of such a process because of the high cost of membranes, the low economic value of the product (tertiary effluent) and the potential rapid loss of performance due to membrane fouling. As a result, the focus was on the attainment of high fluxes, and it was, therefore, necessary to pump the MLSS at high cross-flow velocity at significant energy penalty (of the order 10 kWh/m3 product) to reduce fouling. Because of the poor economics of the first-generation MBRs, they only found applications in niche areas with special needs, such as isolated trailer parks or ski resorts.
The breakthrough for the MBR came in 1989 with Yamamoto and co-workers' idea of submerging the membranes in the bioreactor. Until then, MBRs were designed with a separation device located external to the reactor (sidestream MBR) and relied on high trans-membrane pressure (TMP) to maintain filtration. With the membrane directly immersed in the bioreactor, submerged MBR systems are usually preferred to sidestream configuration, especially for domestic wastewater treatment. The submerged configuration relies on coarse bubble aeration to produce mixing and limit fouling. The energy demand of the submerged system can be up to 2 orders of magnitude lower than that of the sidestream systems and submerged systems operate at a lower flux, demanding more membrane area. In submerged configurations, aeration is considered as one of the major parameters in process performance both hydraulic and biological. Aeration maintains solids in suspension, scours the membrane surface, and provides oxygen to the biomass, leading to better biodegradability and cell synthesis.
The other key steps in the recent MBR development were the acceptance of modest fluxes (25 percent or less of those in the first generation), and the idea to use two-phase bubbly flow to control fouling. The lower operating cost obtained with the submerged configuration along with the steady decrease in the membrane cost encouraged an exponential increase in MBR plant installations from the mid-90s. Since then, further improvements in the MBR design and operation have been introduced and incorporated into larger plants. While early MBRs were operated at solid retention times (SRT) as high as 100 days with MLSS up to 30 g/L, the recent trend is to apply lower solid retention times (around 10–20 days), resulting in more manageable MLSS levels (10 to 15 g/L). Thanks to these new operating conditions, the oxygen transfer and the pumping cost in the MBR have tended to decrease and overall maintenance has been simplified. There is now a range of MBR systems commercially available, most of which use submerged membranes although some external modules are available; these external systems also use two-phase flow for fouling control. Typical hydraulic retention times (HRT) range between 3 and 10 hours. In terms of membrane configurations, mainly hollow fiber and flat sheet membranes are applied for MBR applications.
Despite the more favorable energy usage of submerged membranes, there continued to be a market for the side stream configuration, particularly in smaller flow industrial applications. For ease of maintenance, the side stream configuration can be installed on a lower level in a plant building. Membrane replacement can be undertaken without specialized lifting equipment. As a result, research continued with the side stream configuration, during which time it was found that full-scale plants could be operated with higher fluxes. This has culminated in recent years with the development of low energy systems which incorporate more sophisticated control of the operating parameters coupled with periodic backwashes, which enable sustainable operation at energy usage as low as 0.3 kWh/m3 of product.
In the immersed Membrane Bioreactor (iMBR) configuration, the filtration element is installed in either the main bioreactor vessel or in a separate tank. The modules are positioned above the aeration system, fulfilling two functions, the supply of oxygen and the cleaning of the membranes. The membranes can be a flat sheet or tubular or a combination of both and can incorporate an online backwash system which reduces membrane surface fouling by pumping membrane permeate back through the membrane. The backwash system can be optimized using IPC membranes, as developed by Blue Foot Membranes. In systems where the membranes are in a separate tank to the bioreactor, individual trains of membranes can be isolated to undertake cleaning regimes incorporating membrane soaks, however, the biomass must be continuously pumped back to the main reactor to limit MLSS concentration increase. Additional aeration is also required to provide air scour to reduce fouling. Where the membranes are installed in the main reactor, membrane modules are removed from the vessel and transferred to an offline cleaning tank. Usually, the internal/submerged configuration is used for larger-scale lower strength applications. In order to optimize the reactor volume and minimize the production of sludge, submerged MBR systems typically operates with MLSS concentrations comprised between 12000 mg/L and 20000 mg/L, hence they offer good flexibility in the selection of the design Sludge retention time. It is mandatory to take into account that an excessively high content of Mixed liquor suspended solids may render the aeration system not so effective and the useful flux of water treated by the membrane would decrease; the classical solution of this optimization problem is to ensure a concentration of mixed liquor suspended solids which approaches to 10.000 mg/L, in order to guarantee a good mass transfer of oxygen with a good permeate flux. This type of solution is widely accepted in larger-scale unit, where the internal/submerged configuration is typically used, because of the higher relative cost of the membrane, compared to the additional volume required into the tank.
Immersed MBR has been the preferred configuration due to its low energy consumption level, high biodegradation efficiency, and low fouling rate compared to side stream membrane bioreactors. In addition, iMBR systems can handle higher SSLM concentration, while traditional systems work with a MLSS concentration between 2.5-3.5, iMBR can handle concentration between 4-12 g/L, an increase of 300%. This type of configuration is adopted in industrial sector including textile, food & beverages, oil & gas, mining, power generation, pulp & paper in light of its benefits.
In sMBR technology the filtration modules are outside the aerobic tank, hence the name side-stream configuration. Like the iMBR configuration, the aeration system is also used to clean and supply oxygen to the bacteria that degrade the organic compounds. The biomass is either pumped directly through a number of membrane modules in series and back to the bioreactor, or the biomass is pumped to a bank of modules, from which a second pump circulates the biomass through the modules in series. Cleaning and soaking of the membranes can be undertaken in place with the use of an installed cleaning tank, pump, and pipework. The quality of the final product is such that it can be reused in process applications due to the filtration capacity of the micro and ultrafiltration membranes.
Usually, external/sidestream configuration is used for small-scale higher strength applications; the main advantage that the external/sidestream configuration shows is the possibility to design and size the tank and the membrane separately, with practical advantages for the operation and the maintenance of the unit. As in other membrane processes, a shear over the membrane surface is needed to prevent or limit fouling; the external/sidestream configuration provides this shear using a pumping system, while the internal/submerged configuration provides the shear through the aeration in the bioreactor, and since there is an energy requirement to promote the shear, this configuration shows this additional cost. Moreover, the MBR module fouling is more consistent, due to the higher fluxes involved into this configuration.
Finally, in order to have a comparison of the characteristics and capabilities of the two configurations, a few points are given below where they are compared: - iMBR offers a lower cleaning frequency, and lower energy consumption, but, otherwise, sMBR can handle higher than iMBR MLSS (Mixed liquor suspended solids) concentration. For this reason, it is easier to carry out the maintenance operations and module replacements and cleanings since the system is more compacted.
The MBR filtration performance inevitably decreases with filtration time. This is due to the deposition of soluble and particulate materials onto and into the membrane, attributed to the interactions between activated sludge components and the membrane. This major drawback and process limitation has been under investigation since the early MBRs, and remains one of the most challenging issues facing further MBR development.
Fouling is the process by which the particles (colloidal particles, solute macromolecules) are deposited or adsorbed onto the membrane surface or pores by physical and chemical interactions or mechanical action. This produces a reduced in size or blocked membrane pores.
Membrane fouling can cause severe flux drops and affects the quality of the water produced. Severe fouling may require intense chemical cleaning or membrane replacement.  This increases the operating costs of a treatment plant. Membrane fouling has traditionally been thought to occur through four mechanisms: 1) complete pore blocking, 2) standard blocking, 3) intermediate blocking, and 4) cake layer formation.  There are various types of foulants: biological (bacteria, fungi), colloidal (clays, flocs), scaling (mineral precipitates), and organic (oils, polyelectrolytes, humics).
Membrane fouling can be recognized either by the reduction in permeation flux while holding Transmembrane pressure (TMP) constant or an increase in Transmembrane Pressure in constant flux mode. Nevertheless, most of the wastewater treatment plants are operated in constant flux mode. Hence, fouling phenomena generally is perceived by observing the variation of TMP with time. In recent reviews covering membrane applications to bioreactors, it has been shown that, as with other membrane separation processes, membrane fouling is the most serious problem affecting system performance. Fouling leads to a significant increase in hydraulic resistance, manifested as permeate flux decline or transmembrane pressure (TMP) increase when the process is operated under constant-TMP or constant-flux conditions respectively. In systems where flux is maintained by increasing TMP, the energy required to achieve filtration increases. Alternatively, frequent membrane cleaning is therefore required, increasing significantly the operating costs as a result of cleaning agents and production downtime. More frequent membrane replacement is also expected.
Membrane fouling results from the interaction between the membrane material and the components of the activated sludge liquor, which include biological flocs formed by a large range of living or dead microorganisms along with soluble and colloidal compounds. The suspended biomass has no fixed composition and varies with feed water composition and MBR operating conditions. Thus though many investigations of membrane fouling have been published, the diverse range of operating conditions and feedwater matrices employed, the different analytical methods used, and the limited information reported in most studies on the suspended biomass composition, has made it difficult to establish any generic behaviour pertaining to membrane fouling in MBRs specifically.
The air-induced cross flow obtained in submerged MBR can efficiently remove or at least reduce the fouling layer on the membrane surface. A recent review reports the latest findings on applications of aeration in submerged membrane configuration and describes the enhancement of performances offered by gas bubbling. As an optimal air flow rate has been identified behind which further increases in aeration have no effect on fouling removal, the choice of aeration rate is a key parameter in MBR design.
Many other antifouling strategies can be applied to MBR applications. They comprise, for example:
In addition, different types/intensities of chemical cleaning may also be recommended:
Intensive cleaning is also carried out when further filtration cannot be sustained because of an elevated transmembrane pressure (TMP). Each of the four main MBR suppliers (Kubota, Evoqua, Mitsubishi and GE Water) have their own chemical cleaning recipes, which differ mainly in terms of concentration and methods (see Table 1). Under normal conditions, the prevalent cleaning agents remain NaOCl (sodium hypochlorite) and citric acid. It is common for MBR suppliers to adapt specific protocols for chemical cleanings (i.e. chemical concentrations and cleaning frequencies) for individual facilities.
Simply due to the high number of microorganisms in MBRs, the pollutants uptake rate can be increased. This leads to better degradation in a given time span or to smaller required reactor volumes. In comparison to the conventional activated sludge process (ASP) which typically achieves 95 percent, COD removal can be increased to 96 to 99 percent in MBRs (see table,). COD and BOD5 removal are found to increase with MLSS concentration. Above 15 g/L COD removal becomes almost independent of biomass concentration at >96 percent. Arbitrary high MLSS concentrations are not employed, however, as oxygen transfer is impeded due to higher and non-Newtonian fluid viscosity. Kinetics may also differ due to easier substrate access. In ASP, flocs may reach several 100 μm in size. This means that the substrate can reach the active sites only by diffusion which causes an additional resistance and limits the overall reaction rate (diffusion-controlled). Hydrodynamic stress in MBRs reduces floc size (to 3.5 μm in sidestream MBRs) and thereby increases the apparent reaction rate. Like in the conventional ASP, sludge yield is decreased at higher SRT or biomass concentration. Little or no sludge is produced at sludge loading rates of 0.01 kgCOD/(kgMLSS d). Because of the imposed biomass concentration limit, such low loading rates would result in enormous tank sizes or long HRTs in conventional ASP.
Nutrient removal is one of the main concerns in modern wastewater treatment especially in areas that are sensitive to eutrophication. Nitrogen (N) is a pollutant present in wastewater that must be eliminated for multiple reasons: it reduces dissolved oxygen in surface waters, is toxic to the aquatic ecosystem, poses a risk to public health, and together with phosphorus (P), are responsible for the excessive growth of photosynthetic organisms. All these factors make its reduction focus on wastewater treatment. In wastewater, nitrogen can be present in multiple forms. Like in the conventional ASP, currently, the most widely applied technology for N-removal from municipal wastewater is nitrification combined with denitrification, carried out by bacteria nitrifying and facultative. Besides phosphorus precipitation, enhanced biological phosphorus removal (EBPR) can be implemented which requires an additional anaerobic process step. Some characteristics of MBR technology render EBPR in combination with post-denitrification an attractive alternative that achieves very low nutrient effluent concentrations. For this, a MBR benefits the retention of solids, which provides a better biotreatment, supporting the development of slower-growing microorganisms, especially nitrifying ones, so that it makes them especially effective in the elimination of N (nitrification).
Anaerobic MBRs (sometimes abbreviated AnMBR) were introduced in the 1980s in South Africa and currently see a renaissance in research. However, anaerobic processes are normally used when a low-cost treatment is required that enables energy recovery but does not achieve advanced treatment (low carbon removal, no nutrients removal). In contrast, membrane-based technologies enable advanced treatment (disinfection), but at a high energy cost. Therefore, the combination of both can only be economically viable if a compact process for energy recovery is desired, or when disinfection is required after anaerobic treatment (cases of water reuse with nutrients). If maximal energy recovery is desired, a single anaerobic process will be always superior to a combination with a membrane process.
Recently, anaerobic MBRs have seen successful full-scale application to the treatment of some types of industrial wastewaters—typically high-strength wastes. Example applications include the treatment of alcohol stillage wastewater in Japan and the treatment of salad dressing/barbecue sauce wastewater in the United States.
Like in any other reactors, the hydrodynamics (or mixing) within an MBR plays an important role in determining the pollutant removal and fouling control within an MBR. It has a substantial effect on the energy usage and size requirements of an MBR, therefore the whole life cost of an MBR is high.
The removal of pollutants is greatly influenced by the length of time fluid elements spend in the MBR (i.e. the residence time distribution or RTD). The residence time distribution is a description of the hydrodynamics/mixing in the system and is determined by the design of the MBR (e.g. MBR size, inlet/recycle flowrates, wall/baffle/mixer/aerator positioning, mixing energy input). An example of the effect of mixing is that a continuous stirred-tank reactor will not have as high pollutant conversion per unit volume of reactor as a plug flow reactor.
The control of fouling, as previously mentioned, is primarily undertaken using coarse bubble aeration. The distribution of bubbles around the membranes, the shear at the membrane surface for cake removal and the size of the bubble are greatly influenced by the mixing/hydrodynamics of the system. The mixing within the system can also influence the production of possible foulants. For example, vessels not completely mixed (i.e. plug flow reactors) are more susceptible to the effects of shock loads which may cause cell lysis and release of soluble microbial products.
Many factors affect the hydrodynamics of wastewater processes and hence MBRs. These range from physical properties (e.g. mixture rheology and gas/liquid/solid density etc.) to the fluid boundary conditions (e.g. inlet/outlet/recycle flow rates, baffle/mixer position etc.). However, many factors are peculiar to MBRs, these cover the filtration tank design (e.g. membrane type, multiple outlets attributed to membranes, membrane packing density, membrane orientation, etc.) and its operation (e.g. membrane relaxation, membrane backflush, etc.).
The mixing modeling and design techniques applied to MBRs are very similar to those used for conventional activated sludge systems. They include the relatively quick and easy compartmental modelling technique which will only derive the RTD of a process (e.g. the MBR) or the process unit (e.g. membrane filtration vessel) and relies on broad assumptions of the mixing properties of each sub-unit. Computational fluid dynamics modelling (CFD) on the other hand does not rely on broad assumptions of the mixing characteristics and attempts to predict the hydrodynamics from a fundamental level. It is applicable to all scales of fluid flow and can reveal much information about the mixing in a process, ranging from the RTD to the shear profile on a membrane surface. Visualization of MBR CFD modeling results is shown in the image.
Investigations of MBR hydrodynamics have occurred at many different scales, ranging from examination of shear stress at the membrane surface to RTD analysis of the whole MBR. Cui et al. (2003) investigated the movement of Taylor bubbles through tubular membranes. Khosravi, M. (2007) examined the entire membrane filtration vessel using CFD and velocity measurements, while Brannock et al. (2007) examined the entire MBR using tracer study experiments and RTD analysis.
The market of MBR is segmented based on end-user, which includes municipal and industrial, and geography, which comprises Europe, Middle East and Africa (EMEA), Asia-Pacific (APAC) and the Americas.
In this line in 2016 some studies and reports showed that APAC region took the leadership position in terms of market share, owning 41.90% of it. On the other hand, EMEA's market share is approximately 31.34% and eventually the Americas own 26.67% of it.
APAC has the largest membrane bioreactors market. Developing economies such as India, China, Indonesia, and the Philippines are majorly contributing to the growth. APAC is considered one of the most disaster-prone regions in the world. In 2013, thousands of people died from water-related disasters in the region, accounting for nine-tenth of the water-related deaths, globally. In addition to this, the public water supply system is the region is not as developed when compared to other countries as the US, Canada, Europe's countries, etc.
The membrane bioreactors market in EMEA has witnessed stable growth. Countries as Saudi Arabia, the UAE, Kuwait, Algeria, Turkey, and Spain are majorly contributing to that growth rate. The scarcity of clean and fresh water is the key driver for the increasing demand for efficient water treatment technologies. In this regard, the increased awareness about water treatment and safe drinking water is also driving the growth.
Ultimately, the Americas has been witnessing major demand from countries such as the US, Canada, Antigua, Argentina, Brazil, and Chile. MBR market has grown on account of stringent regulatory enforcement towards adequate discharge of wastewater. The claim of using this emerging technology comes mainly from pharmaceuticals, food & beverages, automotive, and chemicals industries.
The following points provide a summary of the features and improvements involved in dealing with membrane bioreactors.
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