Anaerobic Treatment - PowerPoint PPT Presentation

1 / 17
About This Presentation
Title:

Anaerobic Treatment

Description:

Anaerobic Treatment PreetiBala Adatiya Lecturer School of Biotechnology DAVV Anaerobic Treatment Anaerobik Ar tma Biyoteknolojisi The use of microbes in the absence ... – PowerPoint PPT presentation

Number of Views:380
Avg rating:3.0/5.0
Slides: 18
Provided by: Pre9159
Category:

less

Transcript and Presenter's Notes

Title: Anaerobic Treatment


1
Anaerobic Treatment
  • PreetiBala Adatiya
  • Lecturer
  • School of Biotechnology
  • DAVV

2
Anaerobic Treatment
Anaerobik Aritma Biyoteknolojisi
The use of microbes in the absence of oxygen for
the stabilization of organic material by
conversion to methane, carbon dioxide, new
biomass and inorganic products.
Anaerobic treatment is most suitable for
wastewaters with COD concentrations in the high
strength range (gt2000 mg/l)
3
Anaerobic Digestion Process
Anaerobik Aritma Biyoteknolojisi
4
Anaerobic Digestion Process
  • Three Mechanisms Occurring
  • Hydrolysis Process conversion of insoluble high
    molecular compounds (lignin, carbohydrates, fats)
    to lower molecular compounds
  • Acidogenesis Process conversion of soluble
    lower molecular components of fatty acids, amino
    acids and sugars (monosaccharides) to lower
    molecular intermediate products (volatile acids,
    alcohol, ammonia, H2 and CO2)
  • Methanogenesis Process conversion of volatile
    acids intermediate products to final product of
    methane and CO2

Anaerobik Aritma Biyoteknolojisi
5
ANAEROBIC SLUDGE DIGESTION
Anaerobik Aritma Biyoteknolojisi
  • Anaerobic digestion is one of the oldest process
    used for the stabilization of sludges. It
    involves the decomposition of organic and
    inorganic matter in the absence of molecular
    oxygen.

6
Process description
  • In the anaerobic digestion process, the organic
    material in mixture of primary settled and
    biological sludges is converted biologically.
    Under anaerobic conditions, to a variety of and
    products including methane (CH4) and
    carbondioxide. The process is carried out in an
    airtight reactor. Sludge, introduced continuously
    or intermittently, is retained in the reactor for
    varying periods of time. The stabilized sludge,
    withdrawn from the reactor, is reduced in organic
    and pathogen content.

Anaerobik Aritma Biyoteknolojisi
7
Anaerobik Aritma Biyoteknolojisi
  • The two types of commanly used anaerobic
    digesters are identified as
  • Standard-rate
  • High-rate

8
Standard-Rate Digester
  • In the standard-rate digestion process the
    contents of digesters are usually unheated and
    unmixed. Detention times for the standard-rate
    process vary from 30 to 60 days.
  • They are usually carried out as a single-stage
    process. The functions of digestion, sludge
    thickening, and supernatant formation are
    carried out simultaneously. As a result of
    digestion, the sludge stratifies by forming a
    supernatant layer above the digesting sludge and
    becomes more mineralized. As a result of the
    stratification and the lack of mixing, not more
    than 50 of the volume of a standard-rate
    single-stage digester is used. Because of these
    limitations, the standard-rate process is used to
    small installations.

Anaerobik Aritma Biyoteknolojisi
9
High-Rate Digester
  • In the high-rate digestion process the contents
    of digesters are heated and mixed completely. The
    required detention time for high-rate digestion
    is typically 15 days or less with the exception
    of higher loading rates and improved mixing,
    there are only a few difference between the
    primary digester in a conventional two-stage
    process and a single-stage high-rate digester.

Anaerobik Aritma Biyoteknolojisi
10
  • Two-stage digestion frequently, a high-rate
    digester is coupled in series with a second
    digestion tank. The first tank is used for
    digestion and is heated and equipped wirh mixing
    facilities. The primary function of the second
    stage is to separate the digested solids from the
    sopernatant, however additional digestion and gas
    production may occur.

Anaerobik Aritma Biyoteknolojisi
11
Process design
  • An anaerobic digester is well mixed with no
    liquid solids separation. Consequently, the
    bioreactor can be treated as a continuous stirred
    tank reactor (CSTR) in wich the HRT (hydraulic
    retention time) and SRT (sludge retention time or
    sludge age) are identical, the quantity of
    methane gas can be calculate as below
  • VCH4 (L/day) 0,35 (L/gas)(EQS0-1,42Px)

Anaerobik Aritma Biyoteknolojisi
12
AEROBIC SLUDGE DIGESTION
  • Aerobic sludge digestion may be used to treat
    only
  • waste activated sludge
  • Mixtures of waste activated siudge and primary
    siudge
  • Activated sludge treatment plant without primary
    settling

Anaerobik Aritma Biyoteknolojisi
13
Advantages
Anaerobik Aritma Biyoteknolojisi
  • Volatile solids reduction is equal that obtained
    anaerobically
  • Lower BOD concentrations in supernatant liquor
  • Production of an odorless, humus-like,
    biologically stable end
  • Operation is relativeluy easy
  • Lower capital cost

14
Disadvantages
Anaerobik Aritma Biyoteknolojisi
  • A high power cost is associated with supplying
    the required O2
  • A digested sludge is produced with poor
    mechanical dewatering characteristics
  • A useful by-product such as methane is not
    recovered

15
Process description
Aerobic digestion is similar to the
activated-sludge process. As the supply of
available substrate (food) is depleted, the
microorganisms begin to consume their own
protoplasm to obatin energy for cell maintenance
reactions when this occurs, the microorganisms
are ssaid to be in the endogenous phase.
Anaerobik Aritma Biyoteknolojisi
5CO2 NO3- 3H2O H
C5H7NO2 7O2
Cell tissue is oxidized aerobically to CO2 and
H2O and ammonia. The ammonia form this oxdation
is subsequently oxidized to nitrate.
16
  • An actuality, only about 75 to 80 percent of the
    cell can be oxidized, the remaining 20 to 25
    percent is composed of inert component.
  • A pH drop can occur when ammonia is oxidized to
    nitarte if the alkalinity of the wastewater is
    insufficient, chemical addition may be required.
  • Two variation of the process are commonly used
  • conventional aerobic digestion (with air)
  • high-purity oxygen aerobic digestion
  • Aerobic digestion with air is the most commonly
    used process.

Anaerobik Aritma Biyoteknolojisi
17
Process design
  • Factors taht must be considered in designing
    aerobic digesters include
  • Solid reduction
  • Hydraulic retention time
  • Oxygen requirements
  • Energy requirements for mixing
  • environmental condition such as pH, temperature.

Anaerobik Aritma Biyoteknolojisi
Write a Comment
User Comments (0)
About PowerShow.com