delivery of compressor-jet unit for new production, delivery of compressor-jet unit for existing production.
3.1 Flowrate of gas: kg/h
with range from % up to %
3.2 Composition of gas (concentration in %mass., %mol.):
3.3 Temperature of gas - °C.
3.4 Suction pressure - Atm. G.
3.5 Required pressure at compressor outlet - Atm. G.
3.6 Dew-point temperature (gas condensation) before transportation - °C.
4.1 Name of motive fluid: .
4.2 Available flowrate of motive fluid delivered for makeup of the system: m3/h.
4.3 Composition (distillation) of motive fluid
(chemical composition , ASTM D86 , D1160 or TBP ):
4.4 Density of motive fluid at 20°C - kg/m3
water-cooling
air-cooling
other .
6.1 Electricity
6.1.1 Voltage - V,
6.1.2 Current frequency - Hz,
6.1.3 Number of phases - .
6.2 For cooling agent:
6.2.1 Maximum of initial temperature of cooling water - °C
6.2.2 Maximum allowed temperature at outlet of system - °C.
6.3 Energy cost:
Operating steam ,
Cooling water ,
Electric energy .
7.1 Operating mode:
continuous,
batch - in average: hours per day.
7.2 Run length - operating hours.
7.3 External or internal installation.
- yes, - no.
Transportation for the distance of km.
Own consumption.
Generation of electricity.
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Design RICO Perevod Technovacuum © 2006