Нововоронежская АЭС-2 с энергоблоками 1 и 2: Пояснительная записка, страница 35

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).