Nomen Producti | Instrumenta separationis aeris cryogenici |
Numerus exemplaris | NZDON - 5/10/20/40/60/80/AD CONSUMPTUS |
Nota | NuZhuo |
Accessoria | Compressor aeris et systema refrigerationis et expansor |
Usus | Machina productionis oxygenii, nitrogenii et argonis altae puritatis |
Modellum | 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 emissus (Nm3/h) | 50 | 80 | CLXXX | 260 | 350 | 550 | DCCCL | 1200 |
Puritas O2 (%O2) | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 |
N2 0 productum (Nm3/h) | 50 | CLX | trecenti | quingenti | DCC | mille | 1500 | MM |
Puritas N₂ (PPm O₂) | 9.5 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 |
Argonis Liquidi Emissio (Nm³/h) | —— | —— | —— | —— | —— | —— | —— | 30 |
Puritas Argonis Liquidi (Ppm O₂ + PPm N₂) | —— | —— | —— | —— | —— | —— | —— | ≤1.5ppmO₂ + 4ppmN₂ |
Puritas Argonis Liquidi (Ppm O₂ + PPm N₂) | —— | —— | —— | —— | —— | —— | —— | 0.2 |
Consumptio (kWh/Nm³ O₂) | ≤1.3 | ≤0.85 | ≤0.68 | ≤0.68 | ≤0.65 | ≤0.65 | ≤0.63 | ≤0.55 |
Area Occupata (m³) | 145 | CL | CLX | CLXXX | 250 | 420 | 450 | DCCC |
1. Compressio et purificatio aeris
Aer, postquam pulvis et sordes mechanicas per filtrum aereum amoventur, in compressorem aeris intrat, ad pressionem requisitam compressus, deinde ad refrigeratorem aeris mittitur ut temperatura aeris reducatur. Deinde in purificatorem aeris siccantem intrat ut humiditatem, dioxidum carbonis, acetylenum et alia hydrocarbona ex aere removeat.
2. Separatio aeris
Aer purificatus permutatorem caloris principalem in turri separationis aeris intrat, deinde a gaso refluxu (nitrogenio producti, gaso residuo) ad temperaturam saturationis refrigeratur, et ad imum turris rectificationis mittitur, ubi nitrogenium in summo turris obtinetur, et aer liquidus suffocatur et deinde ad imum turris rectificationis mittitur. In evaporatorem condensationis intrat ut evaporet, et simul pars nitrogenii a turri rectificationis emissi condensatur, pars nitrogenii liquidi condensati ut liquor refluxus turris rectificationis adhibetur, et altera pars a turri separationis aeris ut productum nitrogenii liquidi emittitur.
Gas exhaustum ex evaporatore condensante a principali permutatore caloris ad circiter 130K recalefacitur et expansorem intrat ad refrigerationem expansionis ut capacitatem refrigerandi turri separationis aeris praebeat. Pars gasis expansi ad regenerationem et refrigerationem cribri molecularis adhibetur, deinde in atmosphaeram silentiatoris emittitur.
3. Vaporizatio nitrogenii liquidi
Nitrogenium liquidum e turri separationis aeris in cisterna nitrogenii liquidi conditur. Cum apparatus separationis aeris reficitur, nitrogenium liquidum in cisterna vaporarium intrat et calefacitur, deinde ad fistulam nitrogenii producti mittitur.
Productio nitrogenii cryogenici nitrogenium cum puritate ≧ 99.999% producere potest.
Productum commendare
Q1: Esne societas mercatoria an fabricator?
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
In providendis solutionibus mong pu per quinquennium operam damus.