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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Designing of the dryer section of nutritional yeast production plant – Industrial sector review – Part 1 The aim of the project is to design the dryer section of nutritional yeast production plant that produces 2,800 tons of protein supplements with 8% w/w moisture per annum. The dryer section runs in continues process for 330 […]
Feb 18 2012 | Posted in
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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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Kishore Lulla of Eros International, the global integrated media and entertainment company, believes Bollywood industry will rule the world in the next ten years. Kishore, one of the richest Indian with a net worth of 240 million pounds and with a family fortune of 206 million pounds as per The Sunday Times rich list in […]
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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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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Protein supplements production, example plant overview – Pakistan industrial sector update part 4 The feed into T004 via stream 10 is at a constant flow rate 2.25m3/hr. This is provided to the tank on a continuous basis and operates for a 24 hours per day whereas; the stream exiting the tank flows for only a […]
Feb 8 2012 | Posted in
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Protein supplements production, example plant overview – Pakistan industrial sector update part 3 Stream 7 is pumped via a centrifugal pump, P107, through to the clarifier, L001. L001 is present to remove any of the non-diluted molasses and therefore ensure the uniformity of the flow. Uniformity in the flow is desired as to enable the […]
Feb 7 2012 | Posted in
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