O2 output 350m3/h±5%
O2 pudicitia ≥99.6%O2
O2 pressa ~0.034MPa(G)
N2 output 800m3/h±5%
N2 pudicitia ≤10ppmO2
N2 pressa ~0.012 MPa(G)
Product output status (ad 0℃, 101.325Kpa)
Satus pressura 0.65MPa(G)
Continua operatio tempus inter duos defrosting temporibus 12months
Satus tempus ~ XXIV Horae
Imprimis potentia consummatio ~0.64kWh/mO2 (not incl. O2 compressor)
Model | NZDON-50/50 | NZDON-80/160 | NZDON-180/300 | NZDON-260/500 | NZDON-350/700 | NZDON-550/1000 | NZDON-750/1500 | NZDON-1200/2000/0y |
O2 0utput (Nm3/h) | 50 | 80 | 180 | 260 | 350 | 550 | 750 | 1200 |
O2 Puritas (%O2) | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 |
N2 0utput (Nm3/h) | 50 | 160 | 300 | 500 | 700 | 1000 | 1500 | 2000 |
N2 Munditia (PPm O2) | 9.5 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 |
Liquid Argon Ouput (Nm3/h) | -- | -- | -- | -- | -- | -- | -- | 30 |
Liquid Argon Purity ( Ppm O2 + PPm N2) | -- | -- | -- | -- | -- | -- | -- | ≤1.5ppmO2 + 4 pp mN2 |
Liquid Argon Purity ( Ppm O2 + PPm N2) | -- | -- | -- | -- | -- | -- | -- | 0.2 |
Consummatio (Kwh/Nm3 O2) | ≤1.3 | ≤0.85 | ≤0.68 | ≤0.68 | ≤0.65 | ≤0.65 | ≤0.63 | ≤0.55 |
Area occupati (m3) | 145 | 150 | 160 | 180 | 250 | 420 | 450 | 800 |
1. Air Compressor : Aer pressus humili 5-7 bar (0.5-0.7mpa comprimitur).Id factum est utendo compressoribus proximis (Type Screw/Centrifuga).
2. Pre Cooling System: Secundus gradus processus involvit usum refrigerandi ad refrigerandum processum aeris ad temperaturam circa 12 gradus C antequam purificator intret.
3. Purificatio Aeris Per Purificatorium : Aer intrat emundans, qui conficitur ex geminis sicciis hypotheticis quae alternatim agunt.Sieve moleculares carbonem dioxidum & humorem ab aere processu separat, antequam aer attingit ad aeris separationem Unit.
4. Cryogenic refrigeratio aeris By Expander: Aer refrigerandus est ad nullas temperaturas sub liquatione liquefactionis.Refrigerium cryogenicum et refrigeratio providetur a turbo propagatore valde efficiente, quae aerem refrigerat ad temperaturam infra -165 ad-170 grad C.
5. De separatione Liquidi Aeris in Oxygen et Nitrogen ab Aeris Separatione
6. Columna : Aer qui ingreditur humilis pressione laminam pinni generis caloris commutatoris est humor gratis, oleum liberum et dioxide carbo liberum.Refrigeretur intus caloris commutatoris infra sub zephyris temperaturis per processum expansionis aeris in expansione.
7. Exspectatur nos consequi differentiam della tam infima quam Celsius 2 gradu in calido fine nummulariorum.Aer liquescit cum ad columnam separationis aerem pervenit et in oxygenium et nitrogenum processu rectificationis separatur.
Liquid Oxygen in Liquid Repono Tank: Liquid oxygenii impletur in piscina liquida reposita quae cum liquefier systemate automatic formante coniungitur.Fistula caligarum adhibetur ad oxygenium liquidum e piscina eximendum.
SI MORE INFORMATION scire curas, Contact Us: 0086-18069835230
Q1: Esne mercatura societas vel opificem?
A: Depending on what type of machine you are purchased. Cryogenic ASU, the delivery time is at least 3 months. Cryogenic liquid plant, the delivery time is at least 5 months. Welcome to have a contact with our salesman: 0086-18069835230, Lyan.ji@hznuzhuo.com
Focus ad solutiones mong pu per 5 annos providenda.