This document presents information on upflow anaerobic sludge blanket (UASB) reactors. It discusses that the UASB technology was developed in the 1970s to treat industrial and sewage wastewater using anaerobic digestion. The key factors affecting UASB reactor performance are identified as organic loading rate, nutrients, hydraulic retention time, volatile fatty acids, operational temperature, and operational pH. Advantages of UASB reactors include high efficiency, simplicity, flexibility, low space and energy requirements, and low sludge production, while disadvantages include low pathogen/nutrient removal, long start-up times, potential for odors, and need for post-treatment.
Deals with what is activated sludge, mechanisms and kinetics of treatment, design of activated sludge process, secondary clarifiers and their design and bulking sludge, raising sludge and foaming of ASP.
Deals with UASB reactors for the primary treatment of sewage, stabilization of sludge and removal of BOD. Various components of a UASB reactor are described and design details are included. Modifications to UASB such as UASB ponds, Anaerobic baffle reactors, migrating blanket reactors are also described here.
Lecture notes of Environmental Engineering-II as per Solapur university syllabus of TE CIVIL.
Prepared by
Prof S S Jahagirdar,
Associate Professor,
N K Orchid college of Engg and Technology,
Solapur
Deals with what is activated sludge, mechanisms and kinetics of treatment, design of activated sludge process, secondary clarifiers and their design and bulking sludge, raising sludge and foaming of ASP.
Deals with UASB reactors for the primary treatment of sewage, stabilization of sludge and removal of BOD. Various components of a UASB reactor are described and design details are included. Modifications to UASB such as UASB ponds, Anaerobic baffle reactors, migrating blanket reactors are also described here.
Lecture notes of Environmental Engineering-II as per Solapur university syllabus of TE CIVIL.
Prepared by
Prof S S Jahagirdar,
Associate Professor,
N K Orchid college of Engg and Technology,
Solapur
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The presentation includes Wastewater microbiology. The presentation includes information about sources as well as methods of wastewater treatment.
Wastewater Treatment for Sugar Industry Hülya Pala
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Hydrocarbon are major constituents of crude oil and petroleum. They can be biodegraded by naturally-occurring microorganisms in freshwater and marine environments under a variety of aerobic and anaerobic conditions. The ability of microorganisms - bacteria, archaea, fungi, or algae - to break down hydrocarbons is the basis for natural and enhanced bioremediation. To promote biodegradation, amendments such as nitrogen and phosphorous fertilizer are often added to stimulate microbial growth and metabolism
CH-3. Anaerobic treatment of wastewaterTadviDevarshi
Anaerobic treatment process, Effects of pH, temperature and other parameters on anaerobic treatment, Concept of anaerobic contact process, anaerobic filter, anaerobic fixed film reactor, fluidized bed and expanded bed reactors and up flow anaerobic sludge blanket (UASB) reactor.
This presentation is made for S.Y.Bsc. Students.
The presentation includes Wastewater microbiology. The presentation includes information about sources as well as methods of wastewater treatment.
Wastewater Treatment for Sugar Industry Hülya Pala
I decided to share my another presentation about wastewater treatment which is especially about sugar industry to be beneficial for you.( The link for slide 5: https://www.youtube.com/watch?v=EP_fgp7zYKk)
In his PPT you will come to know about the TREATMENT OF SOLID WASTE, ITS MANAGEMENT and MICROORGANISMS INVOLVED IN THE TREATMENT OF SOLID WASTE. do like, share and follow me to get more such PPT to be uploaded.
Hydrocarbon are major constituents of crude oil and petroleum. They can be biodegraded by naturally-occurring microorganisms in freshwater and marine environments under a variety of aerobic and anaerobic conditions. The ability of microorganisms - bacteria, archaea, fungi, or algae - to break down hydrocarbons is the basis for natural and enhanced bioremediation. To promote biodegradation, amendments such as nitrogen and phosphorous fertilizer are often added to stimulate microbial growth and metabolism
CH-3. Anaerobic treatment of wastewaterTadviDevarshi
Anaerobic treatment process, Effects of pH, temperature and other parameters on anaerobic treatment, Concept of anaerobic contact process, anaerobic filter, anaerobic fixed film reactor, fluidized bed and expanded bed reactors and up flow anaerobic sludge blanket (UASB) reactor.
Review of research on bio reactors used in wastewater ijsit 2.4.6IJSIT Editor
The review presented in this paper focuses on reactors used in wastewater treatment for bio
hydrogen production (e.g. batch reactors, complete mix reactors, plug flow reactors, bio-film reactors,
suspended reactors, upflow anaerobic sludge blanket reactor, anaerobic baffled reactors, upflow packed-bed
attached growth reactors, attached growth fluidized bed reactors, anaerobic sequencing batch reactor, hybrid
/ high rate reactors and membrane separation reactors. It is clear from the review that development of these
reactors can be considered a grown up research for which good design and scale-up guidelines are available
Upflow anaerobic sludge blanket (UASB) technology, normally referred to as UASB reactor, is a form of anaerobic digester that is used in the treatment of wastewater.
The UASB reactor is a methanogenic (methane-producing) digester that evolved from the anaerobic clarigester. A similar but variant technology to UASB is the expanded granular sludge bed (EGSB) digester. A diagramatic comparison of different anaerobic digesters can be found here.
UASB uses an anaerobic process whilst forming a blanket of granular sludge which suspends in the tank. Wastewater flows upwards through the blanket and is processed (degraded) by the anaerobic microorganisms. The upward flow combined with the settling action of gravity suspends the blanket with the aid of flocculants. The blanket begins to reach maturity at around 3 months. Small sludge granules begin to form whose surface area is covered in aggregations of bacteria. In the absence of any support matrix, the flow conditions creates a selective environment in which only those microorganisms, capable of attaching to each other, survive and proliferate. Eventually the aggregates form into dense compact biofilms referred to as "granules".A picture of anaerobic sludge granules can be found here.
Biogas with a high concentration of methane is produced as a by-product, and this may be captured and used as an energy source, to generate electricity for export and to cover its own running power. The technology needs constant monitoring when put into use to ensure that the sludge blanket is maintained, and not washed out (thereby losing the effect). The heat produced as a by-product of electricity generation can be reused to heat the digestion tanks.
The blanketing of the sludge enables a dual solid and hydraulic (liquid) retention time in the digesters. Solids requiring a high degree of digestion can remain in the reactors for periods up to 90 days. Sugars dissolved in the liquid waste stream can be converted into gas quickly in the liquid phase which can exit the system in less than a day.
The demand for efficient and cost effective wastewater treatment technology in the refining and petrochemical sector is being driven by not only ever-tightening environmental legislation, but also by the sectors own desire to follow a meaningful sustainability agenda and to take its responsibilities around product stewardship seriously.
Treatment of wastewater from petrochemical plants can be a challenging and costly matter; particularly when needing to comply with the requirements of operational permits and national environmental legislation governing the discharge of treated wastewater into community treatment plants or natural water bodies such as rivers, lakes and oceans.
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AKS UNIVERSITY Satna Final Year Project By OM Hardaha.pdf
UPFLOW ANAEROBIC SLUDGE BLANKET REACTOR
1. * LUCKNOW MODEL INSTITUTE OF
TECHNOLOGY AND MANAGEMENT
PRESENTATION ON
UPFLOW ANAEROBIC
SLUDGE BLANKET
REACTOR
SUBMITTED TO: SUBMITTED BY:
SHIVAM SINGH (1448400026)
SANDEEP KUMAR (1448400023)
DANISH IQBAL (1448400009)
ER RIYAZ (1448400022)
2. INTRODUCTION
The UASB technology was developed by
Lettinga and his co-workers in the late
1970’s.
Originally the reactor was designed to
treat industrial waste water but later its
application was extended to treatment of
sewage.
Nowadays, the use of UASB rector is
extensively for the treatment of several
types of waste water, forming a part of the
high rate of anaerobic technology.
3. UASB reactor Setup
The UASB scheme basically consisted of
Influent tank, peristaltic pump, cylindrical
UASB reactor, Gas/liquid/solid separator,
effluent outlet, gas outlet and collection
system. Figure 18.7 showing the basic scheme
of the UASB reactor.
5. FACTORS AFFECTING PERFORMANCE OF UASB
REACTOR
Organic Loading Rate
Nutrients
Hydraulic Retention Time
Volatile Fatty Acids
Operational Temperature
Operational pH
6. 1. Organic Loading Rate
Organic loading rate (OLR) is an important
parameter that considerably affects the
performance of a UASB reactor. The fluctuations
in organic load depends on the sludge
properties, mixing intensity, SRT (sludge
retention time), HRT (hydraulic retention time),
duration of the variation, bacterial mass and
activity.
7. 2. Nutrients
The growth of anaerobic microorganisms
depends on the availability of the essential
nutrients present in the wastewater.
Deficiency of these nutrients could
negatively affect their growth of microbes
and also the efficiency of the anaerobic
degradation.
8. 3. Hydraulic Retention Time
The hydraulic retention time (HRT) is defined as
the average time that wastewater spends inside
the reactor. HRT is affected by both the flow
rate and composition of wastewater entering
the UASB reactor. High HRT increases the
contact time of wastewater with the sludge and
hence improves the effluent quality and biogas
production rate.
9. Volatile fatty acids are important intermediate
products in the formation of CH4. The right
concentration determines the efficiency of
substrate removal from the reactor. For a typical
reactor, overloading, or sudden variations in HRT
and OLR could cause the accumulation of VFA and
stressful conditions in the reactor during the break
down of complex organic matter.
4. Volatile Fatty Acids
10. Operational temperature is an important
parameter in anaerobic degradation
processes. It determines the dominant
bacterial flora and the growth rates of
microorganisms present in a reactor.
Different species of bacteria can survive at
different temperature ranges.
5. Operational Temperature
11. 6. Operational pH
pH is a very important parameter for an
anaerobic digester as microbes are highly pH
dependent and require suitable conditions of pH
to grow optimally. pH far below or higher than
the required range could cause an accumulation
of acetate, thereby inhibiting the methanogens
and leading to conversion of COD to volatile
acids instead of CH4 production. Therefore,
mostly anaerobic digestion reactors have been
operated at pH of between 6.5–7.5.