Tel: +86-15837392368
Fax: +86-373-2677103
E-mail: chengde@cryocontainer.com
Address: Fengquan Industrial Zone, Xinxiang city, Henan Province China
Briefing of process technology
This device adopts the molecular sieve adsorb purification, expander refrigeration, single-stage rectification, waste gas reflux expansion to produce nitrogen. On the premise of stable operation, high efficiency and energy saving design patterns.
The nitrogen plant including:air compression system、air pre-cooling system、molecular sieve purify system、fractionation system、expander unit、instrument control system and electronic control system.
Process description
Firstly raw air got into air compressor, be compressed to required pressure, came into cooling unit to be cooled, and then enter into molecular sieve adsorber to get rid of water、CO2、C2H2 and other impurity.
The purified air got into rectification column, through main heat exchanger to exchange heat with reflux waste gas and product nitrogen, be cooled and then came into bottom of rectifying column, be rectified to the product nitrogen and oxygen-enriched liquid air. The liquid air in column bottom be sub-cooled and throttled, then got into condensing evaporator to exchange heat with nitrogen, the nitrogen be liquefied and to be as the reflux liquid of rectification column.
Product nitrogen be lead from the top of rectification column, through main heat exchanger to be reheated and then get out of cold box. Then the product nitrogen came into nitrogen compressor, be compressed to 30~50 bar and got into electrical heater, be heated to user required temperature and then be sent out of battery limited to user.
The waste gas be lead from the top of condensing evaporator, through main heat exchanger for reheating, and adiabatic expansion in turbine expander to compensate cooling capacity of the plant. The waste gas from expander through sub-cooler and main heat exchanger to be reheated, and then got out of cold box to be as the regeneration air of purification system.
The liquid nitrogen product be suction from condensing evaporator to liquid nitrogen storage tank, the liquid nitrogen be vaporized in vaporizer and then got into nitrogen pipeline to sent to user.
Air compressor unit 1 set
Technical data:
·model oil-free screw
·inlet pressure 98 KPa
·inlet temperature 30℃
·outlet temperature ≤40℃
·discharge pressure 0.73 MPaA
·discharge capacity 1800 Nm³/h
Main scope of supply
·compressor and accessory
·main motor
·gas pipeline and accessory
·water pipeline and accessory
·lubrication oil pipeline and accessory
·special tools
Cooling unit 1set
·model screw machine
·handle gas capacity 1800 Nm³/h
·working pressure 0.73 MPa
·refrigerating capacity 37 KW
Purification system
·handle gas capacity 1800Nm3/h
·regeneration gas capacity 360Nm3/h
·regeneration gas waste nitrogen
·adsorption period 8 hours
(16 hours switchover)
·type skid-mounted package
Molecular sieve 2 units
Technical data
·model Vertical single bed
·overall size φ800×3300
·weight 850kg
·design pressure 1.0 MPa
·shell material Q345R
·inner parts material stainless steel
Electrical heater 2 units
Design data
·fluid: waste nitrogen
·flow rate: 360Nm3/h
·inlet pressure : 0.015MPaG
·inlet temperature: 15℃
·outlet temperature: 175℃
·overall size φ400×3400
·weight 500kg
Silencer 1 unit
·overall size φ500×4000
·weight 550kg
·shell material carbon steel
Adsorbent
Filling capacity: about 2×0.8t
Automatic switchover valve 1set
Other valve, pipeline and accessory in system 1set
rectification column system 1set
Cold box filled compressed waste nitrogen to avoid moist air enter into cold box.
Most of connecting in cold box adopt welding structure.
Support and structural parts in cold box adopt resist low temperature material.
This plant has 2 expanders to supply needed cooling capacity.
Main heat exchanger 1 group
·type Vacuum brazing aluminum plate-fin
·design temperature -196℃
·design pressure 1.0MPa
·material aluminum alloy
Sub-cooler 1group
·type Vacuum brazing aluminum plate-fin
·design temperature -196℃
·design pressure 1.0MPa
·material aluminum alloy
Rectification column (including vaporizing condenser) 1unit
·type Vacuum brazing aluminum plate-fin
·design temperature -196℃
·design pressure 1.0MPa
·material aluminum alloy
Liquid measurement tank 1 unit
·material: 5052-0
·size: φ400×3460mm
·weight: 100Kg
Drainage tank 1unit
·type Vertical
·overall size ~φ800×2500
·weight ~120kg
·material aluminum alloy
Nitrogen vent silencer 1unit
·overall size φ500×4000
·weight 550kg
·main material carbon steel
Pipeline and accessory in cold box 1set
·main material aluminum alloy
Valve/pipe/equipment support in cold box 1set
·main material stainless steel
Ladder、platform and railing 1set
·main material carbon steel
Cold box(skid-mounted package) 1set
·overall size ~2500×3000×16000
·main material carbon steel
Valve in cold box 1set
·cryogenic regulating valve: KOSO
Perlite sufficiency
Gas bearing expander 2 units(1 use 1 standby)
Technical data
design data of expander:
·medium dry air
·flow rate ~1000±15%Nm3/h
·inlet pressure 0.32 MPaA
·outlet pressure 0.126 MPaA
Scope of supply
·expander 2 units
·system valve and accessory 2 sets
·drive fan suction type filter 2 units
·drive fan type silencer 2 units
·special tools 2sets
·complete sealing system 2sets
·commissioning spare parts 1set
Nitrogen compressor 2 units (1 use 1 standby)
medium: nitrogen
flow rate: 600 Nm3/h
inlet temperature: 12 ℃
inlet pressure : 0.66MPa(G)
outlet temperature: 160℃
outlet pressure : 5.0 MPa
water consumption: 6 t/h
compressor motor power: 75KW
Nitrogen heater 1unit
Design data
·fluid: nitrogen
·flow rate: 600Nm3/h
·inlet pressure : 5.0MPaG
·inlet temperature: 160℃
·outlet temperature: 400℃
Liquid storage and vaporization system 1set
Cryogenic liquid nitrogen storage tank 1unit
·type vacuum powder insulation storage tank
·volume 50 m3
·working pressure 0.8MPa
Liquid nitrogen vaporizer 1unit
·type air warming type
·vaporizing capacity 600 Nm3/h
·working pressure 0.8Mpa
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