After the blood has been separated into its main components (typically
through centrifugation) the resulting components are blood plasma, platelets
and white blood cells and red blood cells. The plasma still contains valuable
dissolved substances which are separated by changing conditions. One of the
most effective process has been developed by Dr. Edwin Cohn which involves
cooling and changing the acidity of the plasma Single use bioreactor.
Normally, the process starts out with pure plasma at 3-5oC and a pH of
roughly 7. Both ethanol and octanoic acid are slowly added which reduces the pH
of the liquid until the first proteins are precipitated, forming large clumps.
These insoluble proteins can be collected by centrifugation or filtration. The
collected filtrated can then treated further with more ethanol and octanoic
acid to precipitate the next type of proteins. Above steps are repeated until a
total of approx. 40% ethanol is added and a pH of 4.8 is reached, where Albumin
is recovered single use systems.
Fractionation issues
One of the main issues in the fractionation process is the purity and
yield of each fraction. If the precipitation at one stage is not complete the
yield is lowered. If too much acid is added the purity of each fractionation
stage is reduced. In case the acid is added too fast there is a local
overdosage, reducing the pH to lower levels and hence fractioning out more
proteins. These proteins will not redissolve once the batch is homogenized and
the pH stable disposable mixer.
Blood samples
Blood DNA
Mixing of fractionation additives
Often, certain additives such as oxalic acid need to be introduced
into the fractionation liquids. Gentle mixing is of prime importance in such
cases.
Often, rotating
stirrers are not suitable or must be reduced to very low rotation speeds to
prevent alterations of the product. At such speeds the agitator cannot perform
well contained filter.
It becomes obvious that the faster the mixing can be done the faster
the batch can be homogenized while constantly adding ethanol and octanoic acid.
At the same time a gentle mixing system must be chosen to prevent any damage on
the precipitates. The FUNDAMIX® has become the state of the art equipment for
these fractionation steps. It incorporates three main advantages in one
equipment:
The vibrating mixing plate exerts much lower shear forces on the fluid
than any rotating agitator on the market cell harvesting.
The displacement volume of liquid is exceptionally high, assuring
extremely fast homogenization.
The vertical mixing direction creates high up flow in the center and
down flow on the walls, which prevents local pH concentrations at the surface
of the liquid where the precipitation agents are added single-use
filtration.
Albumin Production
Albumin is a family of globular proteins, which are water soluble and
experience heat denaturation. Serum albumin is the most common of this family
and the main protein of the human blood plasma. It binds water and many other
substances and regulates the osmotic pressure of the blood. Albumin is used for
the preparation of vaccines, treatment of burn victims and other medical
applications.
The FUNDAMIX® is very well suited for the mixing of fractionation
liquids and for the preparation of suspensions for sterile filtration in
Albumin production. Tank sizes up to 9300 liters are in operation for this
duty. For such large quantities, the largest (Type 4+) of the FUNDAMIX® family
is applied.
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