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)
Initium 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 Munditia (%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 : Aeris presso 5-7 bar humili comprimitur (0.5-0.7mpa).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 qui vice versant.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 dioxidum carbonii liberum.Refrigeretur intus caloris commutatoris infra sub zephyris temperaturis per processum expansionis aeris in dilatatore.
7. Exspectatur nos consequi differentiam della tam infima quam Celsius in calido fine 2 graduum commutantium.Aer liquefactum accipit cum ad columnam separationis aerem pervenit et in oxygenium et nitrogenum processu rectificationis separatur.
Liquid Oxygenium in Liquid Repono Tank: Liquid oxygenii impletur in piscina liquida reposita quae cum liquefier systemate automatic formando coniungitur.Fistula caligarum adhibetur ad oxygenium liquidum e piscina eximendum.
SI MIHI INTERSTS MORE INFORMATION COGNOSCENDUM, CONTACT US: 0086-18069835230
Focus ad solutiones mong pu per 5 annos providenda.