Complete Plant for Oxygen Production
Complete Plant for Oxygen Production
Special Sales-Price 1.250.000,- Euro
Please take note: On offered prices written here you have to add 10 % for Euromid International services.
Description:
Plant for production of 3,000 Nm³/h oxygen with a purity of min. 99, 5 %-mol. O2. In the following please find our budgetary proposal of a second hand air separation plant, manufactured by Air Liquide, Engineering by A.L.E.C. Canada.
The air separation plant is located in South – Europe, operating with 50 Hz. The plant was started-up in 1976 and was in operation till end of December 1999.
The particular features of the proposed air separation plant are the design and the completeness of the plant and the excellent technical conditions for production of oxygen( LOX).
Additional to your inquiry the plant is able to produce 80 Nm³/h pure argon. Therefore some quantities of H2 are needed for further purification. Since this plant has for the Main Compressors radiator coolers, those radiators have to be re-calculated and adapted to local maximum ambient temperature conditions.
1 PROCESS DESIGN BASIS
The air separation plant was designed and operated at the following conditions and products:
Ø Air:
Pressure 1.01325 bar(a)
Temperature 25 OC
Max. Temperature 40 OC
Min. Temperature – 40 OC
Relative humidity 80 %
Air consumption approx. 19,000 Nm³/h
Ø Products:
- Operation mode 1:
Capacity in Nm³/h Purity in %-mol.
Liquid oxygen 3,200 ³ 99.6 % oxygen
Gaseous nitrogen 2,300 £ 10 ppmV oxygen
Liquid nitrogen 400 £ 2 ppmV oxygen
Liquid argon 60 – 80 £ 2 ppmV oxygen
- Operation mode 2:
Capacity in Nm³/h Purity in %-mol.
Gaseous oxygen 2,000 ³ 99.6 % oxygen
Liquid oxygen 3,200 ³ 99.65 % oxygen
Liquid nitrogen 400 £ 2 ppmV oxygen
Liquid argon 60 – 80 £ 2 ppmV oxygen
2 UTILITIES
The air separation plant requires the following utilities:
Ø Electricity:
Voltage 220/380/600/6.000 V
Frequency 50 Hz
Total consumption approx. 9.850 kW
Trafo – Performance 2X 8 MVA, 30/6 KV and 3×630 KVA, 6/0,4 KV
Ø Cooling water:
Temperature supply / return OC
Temperature difference OC
Total hardness max. 18 OdH
Total consumption approx. m³/h
Ø Instrument air (dry and oil free):
Pressure about bar(a)
Dew point below minimum ambient temperature 10 OC
Total consumption approx. Nm³/h
Ø Hydrogen for argon purification:
Purity 99.8 %-mol.
Consumption Nm³/h.
3 SELLER’S SCOPE OF SUPPLY :
We will supply the following equipment and the following services:
Ø Second hand air separation plant, complete as inspected and consisting of the following main equipment:
Air compressor unit including motor, lubrication system,intercooler, filter, separator and heat exchanger, radiator coolers
Molsieve drier station including regeneration system
Refrigeration unit including cooler
Turbine
Liquefier Unit
Cold Box
Expander section
Silencers
Instrument air drier station
Argon purification unit including DEOXO reactor, drier stationand heat exchangers
Valves and instruments
Control system
Interconnecting piping within battery limits
Steel structure consisting of pipe racks, ladders, platforms, channels and pipe supports
Electrical cabling
Ø Dismantling of the air separation plant
Ø Packing and preparation for transportation
Ø Transportation of the plant equipment CIP Serov
Ø Insurance for transportation for the plant in amount to …???. ( upon request )
Ø Rockwool for new insulation of the cold box, approx. 70 tons, according to German standard LS 152-01
Ø General overhauling of valves and instrumentation after dismantling
Ø New pipe material for interconnecting piping within battery limits of the plant
Ø Primer, protection materials and special tools for re-erection
Ø Re-erection of the air separation plant at Serov site
Ø Supervision services for dismantling, re-erection, instrument check-out, commis-sioning, start-up and operator training
Ø Optionally supply of cryogenic storage tanks for oxygen, nitrogen and argon
Ø Optionally supply of vaporisers and filling station for oxygen, nitrogen and argon.
5.1 The total PRICE includes :
- Air separation plant as inspected; preliminary, please refer to note 1
- Dismantling and packing
- Transportation cost
- Non-returnable containers for transportation
- Supervision during re-erection
- Supervision for adjustment and start-up
- Rockwool for insulation
- Rookwool transportation cost
- Primer and protection materials
- Miscellaneous and special tools
In case of exclusions of SELLER’s scope of supply the total price can be adjusted accordingly. The given take out prices of the respective positions can be deducted from the total prices.
5.2 OPTIONALLY PRICES
The following positions can be selected optionally:
- Overhauling of valves and instruments approx. 120,000.- Euro
- Spare part package for first 5 years operation approx. 220,000.- Euro
- New piping and cabling materials approx. 220,000.- Euro
- 2 new cryogenic tanks, vaporisers and filling station,
excluding transportation cost approx. 575,000.- Euro
- alternative 2 second hand cryogenic tanks, vaporisers
and filling station, excluding transportation cost approx. 335,000.- Euro
| Equipment basic specification-Mechanical | |||||||
| Dimensions(m) | Description | Position dwg | Unit | No. | Weight (kg) | ||
| AREA 1 | |||||||
| 6,852×2,489×2,388(3,308) | N-100 | Air compress./motor | Pcs | 1 | 30.772 | ||
| 1,9891×2,394×2,201 | N-100 | Oil lubricat.system | ” | 1 | 1.000 | ||
| 2,807×0,951×1,473 | LU-100 | Oil lubricat.cooler | ” | 1 | 1.000 | ||
| 8,334×4,197×3,029 | N-102 | Air intercooler | ” | 1 | 9.072 | ||
| 1,514×1,324 | N-99 | Air inlet filter | ” | 1 | 800 | ||
| 2,3×1,00 | Separator | ” | 1 | 900 | |||
| AREA 2 | |||||||
| 10,001×3,134×3,029 | N-202 | Nitrogen intercooler | ” | 1 | 8.164 | ||
| 8,334×3,502×3,029 | N-204 | Nitrogen aftercooler | ” | 1 | 7.212 | ||
| 10,001×2,524×3,029 | N-105 | Air aftercooler | ” | 1 | 6.804 | ||
| 1,803×0,838 | Separator | ” | 1 | 500 | |||
| AREA 3 | |||||||
| 7,017×2,565×2,200(3,664) | N-200 | Nitrogen compress./motor | ” | 1 | 35.013 | ||
| 1,981×2,394×2,201 | N-200 | Oil lubricat.system | ” | 1 | 1.180 | ||
| 3,061×1,165×1,473 | LU-200 | Oil lubricat.cooler | ” | 1 | 1.180 | ||
| 6,242×2,319×2,162 | N-366 | Booster cooler | ” | 1 | 4.763 | ||
| d=1,820×9,83 | N-126 | Surge tank | ” | 1 | 5.902 | ||
| AREA4,5-piping/rack/no equipment | |||||||
| AREA 6 | |||||||
| d=0,775×4,978 | N-15 | Silencer | ” | 1 | 1.173 | ||
| d=0,568×4,978 | N-16 | Silencer | ” | 1 | 973 | ||
| AREA 7 | |||||||
| 6,636×3,099×2,896 | R-10 | Refrigeration unit R10 | ” | 1 | 15.423 | ||
| 4,496×2,413×1,981 | R-10 | Refrigeration unit cooler | ” | 2 | 4.082 | ||
| AREA 8 | |||||||
| 2,921×1,848×2,720 | No.5040-173-1-B | TURBINE-Main skid | ” | 1 | 2.730 | ||
| 1,597×1,286×0,762 | No.5040-173-1-B | Oil cooler | ” | 1 | 910 | ||
| d=1,143X3,254 | N 180-679 | Dryers | ” | 2 | 5.444 | ||
| d=0,360X3,600 | N 19-348 | El.Heater | ” | 1 | 501 | ||
| AREA 9 | |||||||
| 6,299×3,048×3,048 | R-11-446 | Refrigeration unit R11 | ” | 1 | 15.930 | ||
| 4,496×2,413×1,981 | R-11-446 | Refrigeration unit cooler | ” | 1 | 2.041 | ||
| AREA 10 | |||||||
| Argon dryers A17 A/B | ” | 2 | 1.100 | ||||
| 2,010×1,02×0,480 | No. 5040-391-1-B | Argon Dryers A18 A/B | 2 | 770 | |||
| d=1,066×1,270 | No. 5040-393-1-C | Deoxo unit | ” | 1 | 220 | ||
| 1,423×1,194×0,635 | No. 5040-395-1-B | Atm.Argon cooler | ” | 1 | 350 | ||
| Main skid | ” | 1 | 9.550 | ||||
| AREA COLD BOX | |||||||
| 3,66×2,90×10,820(115m3) | No. 5040-161-101-B | Unit 1-Liquifier | ” | 1 | 13.154 | ||
| 3,66×3,66×31,318(420m3) | No. 5040-161-201-B | Unit 2-COLD-BOX | ” | 1 | 31.751 | ||
| No. 5040-132-11-B | Column | ” | 1 | 16.647 | |||
| 3,66×3,34×9,754(119m3) | No. 5040-161-301-B | Unit 3 Rev.Exchangers | ” | 1 | 20.865 | ||
| 3,66×2,44×6,86 | No. 5040-161-401-B | Unit 4 Rev. valves | ” | 1 | 11.855 | ||
| 3,11×1,830×1,524 | No.5040-161-601-B | Unit 6 Expander sect. | ” | 1 | 2.270 | ||
| 6,096×3,353×2,896 | No. 5040-990-7-D | Unit9 Argon pur. skid | ” | 1 | 9.072 | ||
| Steel structure consisting of:Pipe rack/platforms/ladders/channels/supports kg 87.804 | |||||||
| Piping | kg | 53.730 | |||||
| TOTAL: | kg | 422.607 | |||||