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70.0 tonnes: Hydrolysate residue (bone dry) 6.75 tonnes: Power: 875 kWh (This residue has 63% moisture and a net calorific value of 5 442 kJ/kg) Labour (3 shifts of 8 hrs) 216 man-hours daily : Maintenance: 10% of production cost: Secondary steam (125°C saturated) 7.5 tonnes: Overheads: 10% of production cost : Depreciation: 10% yearly of capital cost

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CHAPTER 39. CONDENSERS

As an example of the effect on system performance experiments performed on a 250 ton R-11 chiller condenser revealed that 2% noncondensables by volume caused a 15% reduction in the condensing coefficient. Also 3% and 8% noncondensables by volume caused power increases of 2.6% and 5% respectively (Wanniarachchi and Webb 1982).

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(PDF) SYNTHESIS OF DIMETHYL ETHER | Azat Yerkinova Ruslan ...

This project considers the design of dimethyl ether (DME) production plant that is aimed to produce 200000 tons of DME annually. In order to reach that production rate methanol should be fed at a rate of 280000 tons per year. The DME production

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Tables 2 to 6 show flow amounts and compositions in main portions in the case of the production of 5000 tons/day of methanol. In Tables 2 to 6 values for CH 3 OH include values of byproduct. As a result there was obtained a methanol process achieving an energy unit consumption of 6.948 MMkcal per ton of purified methanol.

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Mar 07 2016 · The boiler efficiency was assumed to be 80%. 31 Flue gas leaving the boiler preheats the air required to burn the bagasse. A turbogenerator uses a multistage turbine with two steam extraction ports and a final condenser. The first extracted steam (1.48 MPa 268 °C) is used to preheat the water before entering the boiler.

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(PDF) SYNTHESIS OF DIMETHYL ETHER | Azat Yerkinova Ruslan ...

This project considers the design of dimethyl ether (DME) production plant that is aimed to produce 200000 tons of DME annually. In order to reach that production rate methanol should be fed at a rate of 280000 tons per year. The DME production

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