O2 output 350m3 / h ± V%
O2 puritate ≥99.6% O2
O2 Pressure ~ 0.034MPA (G)
N2 output 800m3 / H ± V%
N2 Puritas ≤10ppMM2
N2 pressura ~ 0.012 MPA (G)
Product output status (ad 0 ℃, 101.325kpa)
Satus pressura 0.65MPA (G)
Continua operatio inter duo defrosting temporibus 12months
Satus tempore ~ XXIV horas
Imprimis Power consummatio ~ 0.64kwh / Mo2 (non incl. O2 compressor)
Exemplar | Nzdon-L / L | Nzdon-LXXX / CLX | Nzdon-CLXXX / CCC | Nzdon CCLX / D | Nzdon-CCCL / DCC | Nzdon-DL / M | Nzdon-DCCL / MD | Nzdon-MCC / MM / 0y |
O2 0utput (NM3 / h) | 50 | 80 | CLXXX | CCLX | CCCL | DL | DCCL | MCC |
O2 puritatem (% O2) | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 |
N2 0utput (NM3 / h) | 50 | CLX | CCC | D | DCC | M | MD | MM |
N2 Puritas (PPM O2) | 9,5 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 |
Liquid Argon Ouput (NM3 / h) | - | - | - | - | - | - | - | 30 |
Liquid Argon Puritas (PPM O2 + PPM N2) | - | - | - | - | - | - | - | ≤1.5ppmo2 + IV PP MN2 |
Liquid Argon Puritas (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 |
Occupatum regio (M3) | CXLV | CL | CLX | CLXXX | CCL | CDXX | CDL | DCCC |
I. Aeris compressor: Aeris est compressa a humilis pressura de 5-7 bar (0.5-0.7MPA). Factum est per usura tardus compressors (screw / centrifugal genus).
II. Pre refrigerationem system: Secundum scaena processu involves uti a Refrigerant pro pre-refrigerationem processionaliter aeris ad temperatus circa XII g Deg C ante eam intrat purificator.
III. Purificacionis aeris purificator: aere intrat a purificator, quod factum est de geminis moceular cribro vilibus, quae function alternatively. Molecular cribrum separat carbonis dioxide & humorem a processus aer ante caeli ad aer separationem unitas.
IV. Cryogenic refrigerationem aeris per Expander: Aeris debet refrigerari sub nulla temperaturis liquefactionibus. Cryogenic refrigerationem et refrigerationem provisum est a valde efficiens Turbo Expander, quod refrigerat aere ad temperatus infra -165 ad-CLXX deg C.
V. Separatio liquidae Aeris in oxygeni et nitrogen aerem separationis
VI. Columna: et aere quod intrat humilis pressura laminam fin type calor exchanger est humorem liberum, oleum liberum et ipsum dioxide liberum. Est refrigeratum intra calorem exchanger infra sub nullus temperaturis per aerem expansion processus in Expander.
VII. Expectatur quod consequi differentiam Delta sicut humilis quod II gradus Celsius ad calidum finem de exchangers. Aeris sudatio liquefacta cum aere separationem columnae et separata in oxygeni et nitrogen processus rectificationis.
Liquid oxygeni conditur in liquore repono tristique, liquid oxygeni repleti in liquore repono cisternina quod pertinet ad liquefier formans automatic ratio. A caligarum pipe adhibetur ad taking out liquidum oxygeni de piscina.
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Q1: Tu es negotiatione turba et fabrica?
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
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