Designing of the dryer section of nutritional yeast production plant – Industrial sector review – Part 6 Choice of Pieces of Equipment The key pieces of equipment that required careful selection were the atomizer and the separation equipment to be used in the spray dryer design. In each case there were number of variants which […]
Feb 25 2012 | Posted in
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Designing of the dryer section of nutritional yeast production plant – Industrial sector review – Part 5 Spray Dryer Spray dryers are also used for liquids and dilute slurry feeds but it can also be used to dry ‘any material that can be pumped’. As an alternate to the drum dryer, the spray dryer offers […]
Feb 24 2012 | Posted in
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Designing of the dryer section of nutritional yeast production plant – Industrial sector review – Part 4 Spray Dryer Spray dryers are also used for liquids and dilute slurry feeds but it can also be used to dry ‘any material that can be pumped’. As an alternate to the drum dryer, the spray dryer offers […]
Feb 24 2012 | Posted in
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Designing of the dryer section of nutritional yeast production plant – Industrial sector review – Part 3 Continues Dryers Out of the many Continues Dryers available, the drum dryer and spray drier is of most interest as these are specially designed in drying of liquids or liquid suspensions. Note that our feed to the dryer […]
Feb 22 2012 | Posted in
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Designing of the dryer section of nutritional yeast production plant – Industrial sector review – Part 2 Review of alternative processes This section details the research carried out into main equipment variants that can be used to carry out the process. Drying is the final unit operation in the manufacture of protein supplement. The Choice […]
Feb 21 2012 | Posted in
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Poverty and Property Rights in Pakistan Policy debates aimed at alleviating poverty usually emphasize on the monetary aspects of the issue. They tend to overlook the fact that factors like access to and ownership of the natural resources and land has also got a crucial role to play in this regard. They usually disregard the […]
Protein supplements production, example plant overview – Pakistan industrial sector update part 9 Baker’s yeast, Saccharomyces Cerevisiae, can grow either aerobically or anaerobically. The energy for growth is obtained from glucose. In the presence of oxygen, baker’s yeast respire glucose into carbon dioxide and water. Ethanol can also be produced if the concentration of glucose […]
Feb 15 2012 | Posted in
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Protein supplements production, example plant overview – Pakistan industrial sector update part 8 After the first hour of the batch the product of R001 is pumped equally in to the three final reactors, R002, R003 and R004 through P114 and flows through stream 46, stream 47 and stream 48. The total final volume of R001 […]
Feb 13 2012 | Posted in
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Protein supplements production, example plant overview – Pakistan industrial sector update part 7 The first hour of the batch will occur solely in R001. The feed yeast for this reactor will be supplied for the storage tank T008. The feed yeast will be prepared previously to ensure that the yeast is entering R001 already in […]
Feb 13 2012 | Posted in
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Protein supplements production, example plant overview – Pakistan industrial sector update part 6 Water is separated from the cream by spraying the cream into a drying vessel through which a stream of hot air is passed. In this a large interfacial area of the cream is generated resulting in high rate of moisture evaporation. Due […]
Feb 10 2012 | Posted in
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Neuroethology group Cajal Institute, CSIC has launched a Facebook application to study visual intelligence. This is an application that offers a series of games, all based on the estimated number of pencils that appear in images. The game asks to spend just three minutes to the users. Polavieja Gonzalo Garcia, who runs the studio with […]
Feb 10 2012 | Posted in
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Protein supplements production, example plant overview – Pakistan industrial sector update part 5 For the first hour of the batch process the substrate flow is directed via the valve, FCV 14, to stream 45. This supplies it to the inoculant reactor, R001, at a rate off 0.73m3/hr for one hour. The flow through stream 45 […]
Feb 9 2012 | Posted in
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