Установка разделения воздуха К-0,15 (2 штуки), Николаев

Title
rate
1. Processed air:
Pressure MPa (kgf / cm2)
4,5-7 (45-70)
Volumetric flow rate m 3 / s (m3 / h)
0,266 (960)
Brand compressor used
305ВП-16/70
2. Plant capacity:
Mode I - Getting Technical gaseous oxygen I-st grade, m3 / s (m3 / h)
0,0047 (168)
Mode II - Getting Technical gaseous oxygen of high purity, m3 / s (m3 / h)
0,0367 (132)
Mode III - production of liquid oxygen I-st class, kg / s (kg / h)
0,025 (90)
Mode IV - preparation of liquid nitrogen 2nd class kg / s (lbs / hr)
0,019 (70)
3. Clean separation products (oxygen content in volume percent)
Gaseous oxygen 1st grade, not less than
99,7
Oxygen gas of high purity, not less than
99,7
Liquid oxygen, 1st grade, not less
99,7
Liquid nitrogen 2nd grade, no more
1
4. Pressure resulting products separation without a
Oxygen gas, MPa (kgf / cm2)
19,61 (200)
Liquid oxygen at an altitude of 1 + m, MPa (kgf / cm2)
0,039 (0,4)
Liquid nitrogen, MPa (kgf / cm2)
0,39 (4)
5. Installed capacity, kW, not more, including:
239
Compressor motor (2h160)
200
Motor pump liquefied gases
5,5
Electric Heaters
30
Motor oil pump turbine expander
1,5
control board
2
6. Power consumption, kW, not more
Mode I, II
170
Mode III, IV
216
7. Specific energy consumption
Mode I, kWh / m3 O2
1,01
Mode II, kWh / m3 O2
1,3
Mode III, kWh / kg of liquid O2>
2,4
Mode IV, kWh / kg of liquid O2
3,08
8. The duration of the campaign to stop working for the warming, not less than h
4320
9. The duration of the startup period, h. Max
12
10. Duration warming, h max
5
11. The duration of draining of the liquid in is¬paritel, c (h), no more than
3600 (1)
12. The total mass of the installation (without compressor), kg
114000±570