NF-8040
Nā hiʻohiʻona huahana
Hoʻopili ia i ka hoʻomaʻemaʻe brine, ka lawe ʻana i nā metala kaumaha, ka desalination a me ka ʻike ʻana o nā mea waiwai, ka hoʻihoʻi ʻana i ka solution sodium chloride a me ka wehe ʻana o COD i ka wai. Me ka molecualr kaumaha oki-off ma kahi o 200 dalton, he kiʻekiʻe rejection rate no ka hapa nui divalent a me multivalentions, a hoʻouna monovalent paʻakai i ka ia manawa.
Hoʻohana ʻia ʻo 34mil Feed channel spacer e hōʻemi i ka hāʻule o ke kaomi a hoʻonui i ka anti-fouling a me ka maʻalahi o ka hiki o ka membraneelement.
Hoʻohana nui ʻia ia i nā kula o ka hoʻokuʻu ʻana i ka wai ʻole o ka wai, chloralkali denitration, lithium extractionfrom Salt Lake, material decolorization.materialseparation a koke.
ʻAno Pepa
TU14
TU15
TU16
TU23
TU31
TU32
NĀ HOʻOPIʻI & PARAMETER
| Hoʻohālike | Hoole Paa | Min Hoole | Kahe Kahe | Wahi Membrane Pono | Mānoanoa Spacer | Nā huahana hiki ke hoʻololi |
| (%) | (%) | GPD(m³/d) | ft2(m2) | (mil) | ||
| TN3-8040-400 | 98 | 97.5 | 9000(34.0) | 400(37.2) | 34 | DK8040F30 |
| TN2-8040-400 | 97 | 96.5 | 10500(39.7) | 400(37.2) | 34 | DL8040F30 |
| TN1-8040-400 | 97 | 96.5 | 12000(45.4) | 400(37.2) | 34 | NF270-400/34i |
| Nā Kūlana hoʻāʻo | Pumi hana | 100psi(0.69MPa) | ||||
| ʻO ka wela hoʻonā hoʻāʻo | 25 ℃ | |||||
| ʻO ka hoʻonā hoʻāʻo ʻana (MgSO4) | 2000ppm | |||||
| Waiwai PH | 7-8 | |||||
| Ka helu hoʻihoʻi ʻana o ka mea membrane hoʻokahi | 15% | |||||
| Kahe kahe o ka mea membrane hookahi | ±15% | |||||
| Nā Kūlana Hana a me nā palena | ʻO ke kaomi hana kiʻekiʻe | 600 psi (4.14MPa) | ||||
| Ka wela kiʻekiʻe | 45 ℃ | |||||
| ʻO ka wai hānai kiʻekiʻe loa | Ka nui o ka wai hānai manu: 8040-75gpm(17m3/h) 4040-16gpm(3.6m3/h) | |||||
| Ke kahe wai hānai kiʻekiʻe loa SDI15 | 5 | |||||
| ʻO ka manaʻo kiʻekiʻe loa o ka chlorine manuahi: | ＜0.1ppm | |||||
| ʻAe ʻia ka pae pH no ka hoʻomaʻemaʻe kemika | 3-10 | |||||
| ʻAe ʻia ka pae pH no ka wai hānai i ka hana | 2-11 | |||||
| ʻO ka hāʻule kaomi kiʻekiʻe no kēlā me kēia mea | 15psi(0.1MPa) | |||||
