Reverse Osmosis System Analysis for FILMTEC™ Membranes |
ROSA v6.1 ConfigDB 35240041 |
Project: расчет установок обратного осмоса НВ АЭС-2 |
Case: 1 |
8/13/2008 |
Design Warnings
-None- |
Solubility Warnings
Langelier Saturation Index > 0 |
Stiff & Davis Stability Index > 0 |
Antiscalants may be required. Consult your antiscalant manufacturer for dosing and maximum allowable system recovery. |
Stage Details
Stage 1 |
Element |
Recovery |
Perm Flow (m³/h) |
Perm TDS (mg/l) |
Feed Flow (m³/h) |
Feed TDS (mg/l) |
Feed Press (bar) |
1 |
0.10 |
1.04 |
1.82 |
10.70 |
594.09 |
10.03 |
|
2 |
0.10 |
1.01 |
2.03 |
9.66 |
658.06 |
9.66 |
|
3 |
0.11 |
0.98 |
2.29 |
8.65 |
734.43 |
9.35 |
|
4 |
0.12 |
0.95 |
2.63 |
7.67 |
827.38 |
9.09 |
|
5 |
0.14 |
0.92 |
3.08 |
6.73 |
943.19 |
8.86 |
|
6 |
0.15 |
0.89 |
3.71 |
5.81 |
1091.70 |
8.68 |
Stage 2 |
Element |
Recovery |
Perm Flow (m³/h) |
Perm TDS (mg/l) |
Feed Flow (m³/h) |
Feed TDS (mg/l) |
Feed Press (bar) |
1 |
0.08 |
0.83 |
4.27 |
9.83 |
1289.16 |
8.19 |
|
2 |
0.09 |
0.79 |
4.90 |
9.00 |
1407.51 |
7.87 |
|
3 |
0.09 |
0.76 |
5.66 |
8.20 |
1542.89 |
7.58 |
|
4 |
0.10 |
0.73 |
6.61 |
7.44 |
1699.34 |
7.33 |
|
5 |
0.10 |
0.70 |
7.79 |
6.71 |
1882.23 |
7.11 |
|
6 |
0.11 |
0.67 |
9.29 |
6.02 |
2098.84 |
6.93 |
Permeate Flux reported by ROSA is calculated based on ACTIVE membrane area. DISCLAIMER: NO WARRANTY, EXPRESSED OR IMPLIED,AND NO WARRANTY OF MERCHANTABILITY OR FITNESS, IS GIVEN. Neither FilmTec Corporation nor The Dow Chemical Company assume liability for results obtained or damages incurred from the application of this information. FilmTec Corporation and The Dow Chemical Company assume no liability, if, as a result of customer's use of the ROSA membrane design software, the customer should be sued for alleged infringement of any patent not owned or controlled by the FilmTec Corporation nor The Dow Chemical Company.
Scaling Calculations
Raw Water |
Adjusted Feed |
Concentrate |
||
pH |
7.50 |
7.50 |
7.89 |
|
Langelier Saturation Index |
0.23 |
0.23 |
1.59 |
|
Stiff & Davis Stability Index |
0.79 |
0.79 |
1.66 |
|
Ionic Strength (Molal) |
0.01 |
0.01 |
0.05 |
|
TDS (mg/l) |
531.44 |
538.27 |
2359.15 |
|
HCO3 |
256.22 |
256.22 |
1004.88 |
|
CO2 |
10.50 |
10.50 |
14.06 |
|
CO3 |
0.66 |
0.66 |
10.21 |
|
CaSO4 (% Saturation) |
2.30 |
3.56 |
25.23 |
|
BaSO4 (% Saturation) |
0.00 |
0.00 |
0.00 |
|
SrSO4 (% Saturation) |
0.00 |
0.00 |
0.00 |
|
CaF2 (% Saturation) |
0.00 |
0.00 |
0.00 |
|
SiO2 (% Saturation) |
9.76 |
9.76 |
37.90 |
|
Mg(OH)2 (% Saturation) |
0.00 |
0.00 |
0.01 |
To balance: 6.83 mg/l Na added to feed.
1.6 Обоснования по изменению технологической схемы установки химводоочистки (применению осветлителей).
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