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FERMENTER
• A Fermenter may refer to a device
or system meant to
grow cells or tissues in the context
of cell culture.
• These devices are being developed
for use in tissue
engineering or biochemical
engineering.
TYPES OF FERMEMTER
• STIRRED TANK FERMENTER
• BUBBLE COLUMN FERMENTER
• AIRLIFT FERMENTER
• PACKED BED FERMENTER
• FLUIDIZED BED FERMENTER
STIRRED TANK
FERMENTER
• A continuous stirred tank bioreactor consists of a cylindrical
vessel with motor driven central shaft that supports one or
more agitators (impellers). The shaft is fitted at the bottom of
the bioreactor . The number of impellers is variable and
depends on the size of the bioreactor i.e., height to diameter
ratio, referred to as aspect ratio
• The aspect ratio of a stirred tank bioreactor is usually between
3-5.
• There are many advantages of STRs over other types. These
include the efficient gas transfer to growing cells, good mixing
of the contents and flexible operating conditions, besides the
commercial availability of the bioreactors
STIRRED TANK
FERMENTER
BUBBLE COLUMN
FERMENTER
• Air or gas is introduced at the base of the column
through perforated pipes or plates, or metal micro
porous spargers . The flow rate of the air/gas influences
the performance factors —O2 transfer, mixing. The
bubble column bioreactors may be fitted with perforated
plates to improve performance.
• The vessel used for bubble column bioreactors is usually
cylindrical with an aspect ratio of 4-6 (i.e., height to
diameter ratio).
BUBBLE COLUMN
FERMENTER
AIRLIFT FERMENTER
• In air lift fermenter medium of the vessel is divided into
two interconnected zones.
• Riser :- broth rises through this tube
• Down comer :- broth flow down through this tube.
• Homogenization of all components present.
• Bacterial, animal, plant, fungi and yeast cells culture can
be grown in this fermenter
PACKED BED FERMENTER
• A bed of solid particles, with biocatalysts on or within the
matrix of solids, packed in a column constitutes a packed
bed bioreactor . The solids used may be porous or non-
porous gels, and they may be compressible or rigid in
nature.
• A nutrient broth flows continuously over the immobilised
biocatalyst. The products obtained in the packed bed
bioreactor are released into the fluid and removed.
• While the flow of the fluid can be upward or downward,
down flow under gravity is preferred.
PACKED BED FERMENTER
FLUIDIZED BED FERMENTER
• Fluidized bed bioreactor is comparable to bubble column
bioreactor except the top position is expanded to reduce
the velocity of the fluid. The design of the fluidized
bioreactors (expanded top and narrow reaction column)
is such that the solids are retained in the reactor while
the liquid flows out.
• These bioreactors are suitable for use to carry out
reactions involving fluid suspended biocatalysts such as
immobilized enzymes, and immobilized cells.
FLUIDIZED BED FERMENTER
Fermenter 1

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Fermenter 1

  • 1. FERMENTER • A Fermenter may refer to a device or system meant to grow cells or tissues in the context of cell culture. • These devices are being developed for use in tissue engineering or biochemical engineering.
  • 2. TYPES OF FERMEMTER • STIRRED TANK FERMENTER • BUBBLE COLUMN FERMENTER • AIRLIFT FERMENTER • PACKED BED FERMENTER • FLUIDIZED BED FERMENTER
  • 3. STIRRED TANK FERMENTER • A continuous stirred tank bioreactor consists of a cylindrical vessel with motor driven central shaft that supports one or more agitators (impellers). The shaft is fitted at the bottom of the bioreactor . The number of impellers is variable and depends on the size of the bioreactor i.e., height to diameter ratio, referred to as aspect ratio • The aspect ratio of a stirred tank bioreactor is usually between 3-5. • There are many advantages of STRs over other types. These include the efficient gas transfer to growing cells, good mixing of the contents and flexible operating conditions, besides the commercial availability of the bioreactors
  • 5. BUBBLE COLUMN FERMENTER • Air or gas is introduced at the base of the column through perforated pipes or plates, or metal micro porous spargers . The flow rate of the air/gas influences the performance factors —O2 transfer, mixing. The bubble column bioreactors may be fitted with perforated plates to improve performance. • The vessel used for bubble column bioreactors is usually cylindrical with an aspect ratio of 4-6 (i.e., height to diameter ratio).
  • 7. AIRLIFT FERMENTER • In air lift fermenter medium of the vessel is divided into two interconnected zones. • Riser :- broth rises through this tube • Down comer :- broth flow down through this tube. • Homogenization of all components present. • Bacterial, animal, plant, fungi and yeast cells culture can be grown in this fermenter
  • 8.
  • 9. PACKED BED FERMENTER • A bed of solid particles, with biocatalysts on or within the matrix of solids, packed in a column constitutes a packed bed bioreactor . The solids used may be porous or non- porous gels, and they may be compressible or rigid in nature. • A nutrient broth flows continuously over the immobilised biocatalyst. The products obtained in the packed bed bioreactor are released into the fluid and removed. • While the flow of the fluid can be upward or downward, down flow under gravity is preferred.
  • 11. FLUIDIZED BED FERMENTER • Fluidized bed bioreactor is comparable to bubble column bioreactor except the top position is expanded to reduce the velocity of the fluid. The design of the fluidized bioreactors (expanded top and narrow reaction column) is such that the solids are retained in the reactor while the liquid flows out. • These bioreactors are suitable for use to carry out reactions involving fluid suspended biocatalysts such as immobilized enzymes, and immobilized cells.