Allama Muhmmad Iqbal Words, without power, is mere philosophy.
Quaid-e-Azam Expect the best, Prepare for the worst...
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 […]
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 […]
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 […]
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 […]
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 […]
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 […]
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 […]
Drying process in industrial sector – Part 2 However, for this process the drum and spray dryers are the types most commonly considered. Firstly, drum dryers are used for liquids and dilute slurry feeds. It and can be an alternative to the spray drier if the product is to be produced in the form of […]
Drying process in industrial sector – Part 1 Drying is the final unit operation in the manufacture of the protein supplement. The performance of this stage determines the component make up of the final product which is to be sold in the market. As throughout the rest of the process the first decision is whether […]
Protein Supplement production in industrial sector – Part 8 Separation Cell Flocculation The efficiency of solid-liquid separation processes can be often improved by increasing the particle size (yeast cells) through flocculation prior to centrifuge separator and also it contribute to reduce the overall manufacturing cost. The reason is the rate of sedimentation of spherical particles […]
Protein Supplement production in industrial sector – Part 7 However, with increasing mass growth comes an increase in the requirements for substrate and more importantly oxygen. The oxygen requirement for large amount biomass is difficult to meet and requires a very large air flow rate which equally requires increasingly higher power inputs (Stanbury and Whitaker, […]
Protein Supplement production in industrial sector – Part 6 A fed-batch process offers a method to eliminate this production. If the concentration of the substrate is kept below 0.25 g/l then fermentative metabolism will be restricted (Daramola and Zampraka, 2008). This is achieved by the substrate being fed to the reactor incrementally. One advantage the […]
