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Working cell

Figure Bl.27.8. Schematic view of Picker s flow microcalorimeter. A, reference liquid B, liquid under study P, constant flow circulating pump and 2, Zener diodes acting as heaters T and T2, thennistors acting as temperature sensing devices F, feedback control N, null detector R, recorder Q, themiostat. In the above A is the reference liquid and C2is the reference cell. When B circulates in cell C this cell is the working cell. (Reproduced by pemiission from Picker P, Leduc P-A, Philip P R and Desnoyers J E 1971 J. Chem. Thermo. B41.)... Figure Bl.27.8. Schematic view of Picker s flow microcalorimeter. A, reference liquid B, liquid under study P, constant flow circulating pump and 2, Zener diodes acting as heaters T and T2, thennistors acting as temperature sensing devices F, feedback control N, null detector R, recorder Q, themiostat. In the above A is the reference liquid and C2is the reference cell. When B circulates in cell C this cell is the working cell. (Reproduced by pemiission from Picker P, Leduc P-A, Philip P R and Desnoyers J E 1971 J. Chem. Thermo. B41.)...
Biotechnology feniientation/ cell culture Establishment of master cell bank and working cell bank Maintenance of working cell bank Cell culture and/or fermentation Isolation and purification Physical processing, and packaging... [Pg.210]

Cell suspensions which were exposed to 1.0 ppm zinc were combined, and to this matrix known amounts of Zn were added, to allow measurement of the amount of zinc accumulated by the cells via GFAA. In related work, cells treated with known concentrations of zinc solutions were systematically combined and thereby "diluted" with cells not exposed to zinc, to determine If GFAA and EMI analyses yield confirmatory results. [Pg.89]

Possible contamination by chemical or biological substances is one of the most important concerns when producing pharmaceutical proteins. Plant cell cultures ensure the production of the desired protein in a controlled, sterile and sealed environment and can be adapted to cGMP conditions. Therefore, the risk of contamination is minimized and the production conditions can be modified more easily in a contained reactor than in the field. Another advantage is the ability to freeze plant suspension cells in liquid nitrogen [66, 67] so that master and working cell banks can be established, a prerequisite for cGMP procedures [68]. [Pg.99]

Upstream processing is deemed to commence when a single vial of the working cell bank system (see later) is taken from storage and the cells therein cultured in order to initiate the biosynthesis of a batch of product. The production process is deemed complete only when the final product is filled in its final containers and those containers have been labelled and placed in their final product packaging. [Pg.121]

The cell bank s construction design is normally two tiered, consisting of a master cell bank and a working cell bank (Figure 5.6). The master cell bank is constructed first, directly from a culture of the newly constructed production cell line. It can consist of several hundred individually stored ampoules. [Pg.121]

Figure 5.6 The master cell bank/working cell bank system. For simplicity, each bank shown above contains only five ampoules. In reality, each bank would likely consist of several hundred ampoules. Working cell bank number 2 will be generated from master cell bank vial number 2 only when working cell bank number 1 is... Figure 5.6 The master cell bank/working cell bank system. For simplicity, each bank shown above contains only five ampoules. In reality, each bank would likely consist of several hundred ampoules. Working cell bank number 2 will be generated from master cell bank vial number 2 only when working cell bank number 1 is...
The upstream processing element of the manufacture of a batch of biopharmaceutical product begins with the removal of a single ampoule of the working cell bank. This vial is used to inoculate a small volume of sterile media, with subsequent incubation under appropriate conditions. This describes the growth of laboratory-scale starter cultures of the producer cell line. This starter culture is, in turn, used to inoculate a production-scale starter culture that is used to inoculate the production-scale bioreactor (Figure 5.7). The media composition and fermentation conditions required to... [Pg.122]

Figure 5.7 Outline of the upstream processing stages involved in the production of a single batch of product. Initially, the contents of a single ampoule of the working cell bank (a) are used to inoculate a few hundred millilitres of media (b). After growth, this laboratory-scale starter culture is used to inoculate several litres/tens of litres of media present in a small bioreactor (c). This production-scale starter culture is used to inoculate the production-scale bioreactor (d), which often contains several thousands/tens of thousands litres of media. This process is equally applicable to prokaryotic or eukaryotic-based producer cell lines, although the bioreactor design, conditions of growth, etc., will differ in these two instances... Figure 5.7 Outline of the upstream processing stages involved in the production of a single batch of product. Initially, the contents of a single ampoule of the working cell bank (a) are used to inoculate a few hundred millilitres of media (b). After growth, this laboratory-scale starter culture is used to inoculate several litres/tens of litres of media present in a small bioreactor (c). This production-scale starter culture is used to inoculate the production-scale bioreactor (d), which often contains several thousands/tens of thousands litres of media. This process is equally applicable to prokaryotic or eukaryotic-based producer cell lines, although the bioreactor design, conditions of growth, etc., will differ in these two instances...
Information processing in production scheduling is essentially the same as in planning. Both plants and individual process equipment take orders and make products. For a plant, the customer is usually external, but for a process (or work cell in discrete manufacturing parlance), the order comes from inside the plant or factory. In a plant, the final product can be sold to an external customer for a process, the product delivered is an intermediate or partially finished product that goes on to the next stage of processing (internal customer). [Pg.559]

Master Cell Bank and Working Cell Bank Origin... [Pg.328]

The need to transport temperature-sensitive raw materials and products, such as cell line, medium, large molecule drugs, and vaccines, means that some form of control during transportation is needed. For example, a working cell bank for the production of proteins may be transported in liquid nitrogen (-196 °C) and that of protein and vaccines in dry ice (-78 °C) in order to protect the integrity of the materials. Data loggers are used to record the temperature... [Pg.351]

Fig. 6.6 Schematic arrangement of work cell for Karl Fischer titrator [27]. Fig. 6.6 Schematic arrangement of work cell for Karl Fischer titrator [27].
For a PEMFC, fed with reformate hydrogen and air, the working cell voltage is typically 0.8 V at 500mAcm, which leads to a voltage efficiency Eg given by... [Pg.9]

The upstream processing element of the manufacture of a batch of biopharmaceutical product begins with the removal of a single ampoule of the working cell bank. This vial is used to inoculate a small volume of sterile growth medium, with subsequent incubation under... [Pg.128]

Production is based on a validated seed-lot system using a host-vector combination that has been shown to be suitable to the satisfaction of the competent authority. The seed-lot system uses a master cell bank and a working cell bank derived from the master seed lot of the host-vector combination. A detailed description of cultivation, extraction and purification steps and a definition of the production batch shall be established. [Pg.516]

The working cell bank is a homogeneous suspension of the cell material derived from the master cell bank(s) at a finite passage level, distributed in equal volumes into individual containers for storage (e.g. in liquid nitrogen). [Pg.516]

All containers of master or working cell banks and seed lots should be treated identically during storage. Once removed from storage, the containers should not be returned to the stock. [Pg.531]

Reiner, S.L. (2007). Development in motion helperT cells at work. Cell 6,129(1) 33-36. [Pg.173]

In a number of instances, it has been found not only possible but profitable to utilize electrical energy in the preparation of chemical materials, both in the laboratory and in the industries. For success in such work, careful attention must be paid to many details such as accurate control of intensity of current, current density at the electrodes, and the concentration of the electrolyte and there must be available a suitable source of current (three or four storage cells), ammeter, voltmeter, and a variable resistance—best, a slide rheostat. It is usually possible to construct the working cells from ordinary... [Pg.52]


See other pages where Working cell is mentioned: [Pg.327]    [Pg.613]    [Pg.615]    [Pg.29]    [Pg.30]    [Pg.136]    [Pg.219]    [Pg.219]    [Pg.122]    [Pg.122]    [Pg.122]    [Pg.234]    [Pg.341]    [Pg.440]    [Pg.2]    [Pg.7]    [Pg.87]    [Pg.127]    [Pg.128]    [Pg.128]    [Pg.128]    [Pg.53]    [Pg.92]    [Pg.708]    [Pg.113]    [Pg.114]   
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