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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Humsafar – the most watched drama of the past decade Humsafar, the most watched drama in Pakistan these days, is brilliantly directed by Sarmad Sultan Khoosat. It consists of 22 episodes and the first episode was aired on September 24th, 2011 on Hum TV. It stars Mahira Khan and Fawad Afzal Khan as the […]
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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Mark Webber may be considered as playing second fiddle to Sebastian Vettel but there is no doubt that the Aussie holds enough skill and mettle to win a world title. Webber made his debut in 2002 for Minardi and had a slow start to his career. Jaguar acquired Webber in 2003 and the Aussie had […]
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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Protein supplements production, example plant overview – Pakistan industrial sector update part 1 Here I have given a systematic run through of the process flow diagram providing the methodology behind the design while also providing the compositions and flow rates throughout each pipe and vessel through the system. It also details the design specifications of […]
Feb 7 2012 | Posted in
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Protein supplements production, example plant overview – Pakistan industrial sector update part 2 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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Protein supplements production – Pakistan Industrial Sector- Part 1 Process Science In this section the final chosen design of process for the plant is explained. This involves an overview of the plant diagram, which is done in conjunction and reference to the PID. Each line present is analysed and its constitution explained. This is also […]
Feb 6 2012 | Posted in
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Protein supplements production – Pakistan Industrial Sector- Part 2 Process Science In this section the final chosen design of process for the plant is explained. This involves an overview of the plant diagram, which is done in conjunction and reference to the PID. Each line present is analysed and its constitution explained. This is also […]
Feb 2 2012 | Posted in
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Effluent treatment for manufacturing protein supplements – Pakistan Industrial sector The effluent treatment section is the last part of the process. The problem originates because typically discharge from a process such as this has a BOD of 3000mg/L (Stanbury, 1987) and the acceptable level of discharge into rivers is 30mg/l. Therefore, it important to discharge […]
Jan 30 2012 | Posted in
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