nitrate and nitrite removal from municipal drinking water supplies with

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Water Technologies & Solutions technical paper

nitrate and nitrite removal from municipal drinking water supplies with electrodialysis reversal Authors: Ted Prato and Richard G. Parent, Ionics Reprinted from Proceedings of 1993 AWWA Membrane Conference, by permission. Note: SUEZ purchased Ionics in 2005.

summary Nitrate contamination of drinking water is a widespread problem. It has long been known that levels of nitrates exceeding the 10 ppm (mg/l) (as Nnitrogen) limit are associated with certain health problems. Although high nitrogen concentrations in drinking water are found mainly in regions of intensive agricultural use, there are sources of nitrate contamination other than agricultural. Nitrates and nitrites are removed efficiently and economically using electrodialysis reversal (EDR), a process where overall demineralization takes place via transfer of ions through anion and cation-selective membranes by application of a direct current (DC) electric field. Data are presented demonstrating excellent long-term nitrate removal using EDR.

human health problems The best known and documented human health risk associated with high levels of nitrates in drinking water is methemoglobenemia, also known as asphyxia or “blue-baby syndrome,” which can affect infants under six months of age. In methemoglobenemia, enteric bacteria convert the elevated levels of nitrate to nitrite. The nitrite then competes with oxygen for active sites on hemoglobin resulting in oxygen deprivation. Infants are predisposed to this effect due to a number of physiological factors including “higher fluid intake per body weight, a higher percentage of fetal hemoglobin and higher stomach pH, permitting survival of reducing-type” bacteria. 1

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Other potential health effects related to high nitrate levels include the risk of cancer and birth defects. These risks are less well-known and documented than methemoglobenemia. Nitrates combine with amines to form nitrosamines, suspected of being potential human carcinogens. Other reactions include the formation of nitrosamides which can also produce tumors in humans. In general, the long-term effect of consumption of high nitrate drinking water is unknown, but some potential for health problems exists from nitrite reactivity.

sources of nitrates in drinking water Fertilizer runoff, farm animal wastes, and septic tank discharge all percolate through the soil into groundwater aquifers and ultimately into water supplies. Agricultural sources of nitrates are by far the most common. Regions of the country where corn is grown experience peak levels of nitrates in groundwater from heavy fertilization. Other sources of nitrate and nitrite contamination are natural and industrial in origin. Industrial sources include chemical manufacturing operations and nitrate-containing cutting oils. Natural sources include atmospheric precipitation (as NH ) and local mineral deposits such as potassium nitrate (saltpeter). Decomposing plant materials contribute as well via nitrogen-fixing bacteria. The overall contribution of natural sources is small in relation to the contribution from human activities. 3

allowable limits of contaminants Standards for maximum levels of nitrates in drinking water have been established by the Federal Government in 1975 with passage of the Safe Drinking Water Act (SDWA). As of the May 1990

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SDWA regulations, some major allowable inorganic contaminants are as follows: Contaminant

MCL or SMCL

Chloride

250 ppm (mg/l)

Fluoride

2 ppm (mg/l)

Nitrate (as N)

10 ppm (mg/l)

prevent passage. See Figures 1 and 2, which illustrate the EDR process. 4

1

(as NO ) 45 ppm (mg/l) 3

Nitrite (as N)

1 ppm (mg/l)

(as NO ) 3.3 ppm (mg/l) 2

TDS

Figure 1: Electrodialysis Diagram

500 ppm (mg/l)

Maximum contaminant level or secondary maximum contaminant level 1

Prior to the SDWA, there was no requirement or a practical, affordable method to remove nitrates from drinking water. Since that time a number of demineralization technologies have been given a best available technology (BAT) status for nitrate removal. These BAT processes include EDR, reverse osmosis (RO) and ion exchange (IE). Effective removal constitutes reducing the level of nitrates to the maximum contaminant level (MCL) or lower. 3

The EDR process can effectively reduce nitrate concentrations to the MCL or lower in public water supplies. The reduction in nitrite concentration is directly related to the design demineralization rate of the EDR system.

Figure 2: Electrodialysis Reversal

A number of EDR plant designs are available to treat contaminated water. Figure 3 presents a diagram of a typical three-stage plant. In general, a two stage plant removes 50% of the influent minerals and nitrates, a three-stage plant removes about 75%, a four-stage plant removes about 83%, and so on.

what is EDR? Electrodialysis (ED) is a process which uses ion exchange resin in sheet form assembled into a stack of components. ED is widely used for total dissolved solids (TDS) removal in a number of different types of plants and applications, including many public and municipal drinking water supplies. EDR uses a reversible DC field applied across a stack of components to remove dissolved ions: the components consist of ion-selective membranes which transport either positive or negative ions, flowdirecting spacers, and electrodes at each end of the stack. Water flows in a thin sheet between membranes. Under the influence of the applied DC electric field, ions migrate toward the electrode opposite in charge, passing through membranes which also have fixed oppositely-charged groups bonded to a polymer surface. Membranes with the same charge as the ionic species repel the ions and Page 2

Figure 3: EDR Process Flow Diagram

In the course of removing charged ions in solution, EDR also removes nitrate and nitrite ions. In this next section, operating data are presented for several EDR plants used for nitrate removal.

nitrate removal using the EDR process Operating data illustrate the practicality of the EDR demineralization process for removing nitrates and nitrites as well as TDS. The examples represent a variety of EDR plants and include three public drinking water installations and one industrial TP1072EN.docx

application. Descriptions of the four plants follow. All of the feed waters contain high levels of nitrate, and the industrial feedwater contains exceptionally high levels of nitrite. Bermuda: 3 desalting stages, 600,000 gpd (2,271 m /day) total production 3

In Bermuda, there are two Aquamite* XX units capable of producing a total of 600,000 gpd (2271 m /day) of demineralized drinking-quality water from a brackish well. The plants were installed to reduce hardness in the existing water supply and to cut back on the amount of purchased water. The brackish water lens under the island is contaminated from septic tank leach fields, making nitrate removal important. The EDR plants yield 81% demineralization and reduce the nitrate concentration from 66 ppm to 8.8 ppm. 3

Delaware: 3 desalting stages, 400,000 gpd (1,514 m /day) total production 3

This plant was installed to improve operating economics (by predemineralizing the IE feedwater to a power plant boiler makeup system) and to reduce NO in the agriculturally-contaminated drinking water supply. This three-stage EDR plant yields 88% demineralization and reduces the nitrate concentration from 60 to 4.5 ppm (mg/l).

Table 1: EDR Plant Data - Bermuda/Delaware Plant Specifications

Model

Bermuda

Delaware

Two Aquamite XX

Aquamite XX Aquamite X

Production

300,000 gpd (1,136 m /day) 600,000 gpd (2,271 m /day) 3

3

300,000 gpd (1,136 m /day) 300,000 gpd (1,136 m /day) 400,000 gpd (1,514 m /day) 3

3

3

Recovery Product Purity

Raw Water

90%

90%

278 ppm TDS

11 ppm TDS

8.8 ppm NO

4.5 ppm NO

3

3

1,614 ppm TDS

114 ppm TDS

66 ppm NO

61 ppm NO

3

Desalting Stages

3

3

Percent Removal

81% TDS

88% TDS

3

3

Industrial: 3 desalting total production

stages,

100,000

86.7% NO

Italy: 2 desalting stages, 300,000 gpd (1,136 m /day) total production 3

Both plants were installed specifically to remove nitrates from municipal wells in agriculture-intensive regions of Italy. These two-stage Aquamite XX plants yield 53% demineralization with reductions in TDS from 1,012 to 474 ppm (mg/l) and nitrate from 120 to 37 ppm (mg/l). The approach here is not only to remove nitrate but also to comply with EC standards in overall TDS reduction.

92.6% NO

3

Water Quality

gpd

This plant was installed as a roughing demineralizer. Nitrite concentration is also quite high. Here an Aquamite X produces 100,000 gpd with 66% demineralization. Nitrate concentration is reduced from 655 ppm to 128 ppm, and Nitrite concentration is reduced from 64 ppm to 21 ppm.

3

Bermuda

Delaware

Feed (ppm [mg/l])

Product (ppm [mg/l])

Feed (ppm [mg/l])

Product (ppm [mg/l])

Sodium

349

72

12

1.6

Calcium

138

13

9

0.5

Magnesium

40

4

8

0.6

Potassium

19

2

-

-

Chloride

656

92

15

1.2

Bicarbonate

259

75

9

2.4

Sulfate

85

10

-

-

Nitrate

66

8.8

61

4.5

pH

7.9

7.0

6.2

5.4

TDS

1,614

278

114

11

Constituent

Tables 1 and 2 present operating data on all of the various EDR units.

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concentration to below the MCL as established by both the SDWA and the World Health Organization.

Table 2: EDR Plant Data - Industrial/Italian Plant Specifications

Model Production

Industrial

Italian

Two Aquamite X

Aquamite XX

100,000 gpd (379 m /day)

300,000 gpd (1,136 m /day)

80%

90%

3

Recovery Product Purity

534 ppm TDS 128 ppm NO 21 ppm NO

Raw Water

3

3

ppm TDS 37 ppm NO

3

3

1,753 ppm TDS 655 ppm NO 64 ppm NO

Desalting Stages

3

Percent Removal

66% TDS

3

3

2

80.4% NO3 67.2% NO3

All nitrate product levels for the public water supply applications are within the Safe Drinking Water Act MCL requirement. Average percent removal of nitrate from the three-stage plants is 86.6% with an average percent TDS removal of 78.3%. Percent removal from the two-stage plant is 69.2% for nitrate and 53% for TDS. Nitrite removal in the industrial application is 67.2% with a 68% TDS removal. In addition, graphs of three of the four plants show analytical data for feed and product salinity and nitrate concentrations over time (Figures 4 and 5). The small variations in the product quality reflect changes in feedwater quality or operating conditions, such as seasonal temperature changes or increases in feedwater TDS. These EDR units consistently meet or exceed SDWA MCL standards for nitrate removal from public water supplies.

53% TDS 69.2% NO

3

Water Quality Industrial

Italian

Feed (ppm [mg/l])

Product (ppm [mg/l])

Feed (ppm [mg/l])

Product (ppm [mg/l])

Sodium

24

14

73

49

Calcium

141

28

127

63

Magnesium

34

8

34

13

Potassium

-

-

4

1.7

Chloride

35

11

120

44

Bicarbonate

514

235

449

240

Sulfate

113

23

85

25

Nitrate

655

128

120

37

Nitrate

64

21

7.3

7.1

pH

7.3

7.0

7.3

7.1

TDS

1,753

534

1,012

474

Constituent

Figure 4: Nitrate and TDS Removal

All of these plants have three desalting stages with the exception of the Italian municipal plant which requires only two desalting stages to reduce the nitrate Page 4

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references

Figure 5: Nitrate, TDS and NO3 Removal

conclusions EDR effectively removes nitrates and nitrites from feed waters, as demonstrated by the plant data. EDR plants are easily designed and operated to yield product water quality to meet SDWA MCLs or SMCLs or lower. Other EDR process advantages include: •

Self-cleaning membrane process



Low operating and maintenance costs



Long membrane life



High recovery operation



No chemical feeds



Low chemical usage



No regenerant wastes



Reduction in TDS in addition to nitrate and nitrite

1.

O’Brien, W.J., “Control Options for Nitrates and Fluorides”, Water/Engineering and Management, July, 1983.

2.

Bouchard, D.C., Surampalli, R.Y., Williams, M.K., “Nitrate Contamination of Groundwater: Sources and Potential Health Effects”, Journal AWWA, Management and Operations, September, 1992.

3.

Kartinen, E.O., Jr., “Nitrate Removal from Municipal Water Supplies”, AWWA Conference at Grand Island, Nebraska, November, 1991.

4.

Meller, F. H., “Electrodialysis & Electrodialysis Reversal Technology”, March, 1984.

Although there are only a few very specific health problems identified as a result of high nitrate levels in drinking water, stricter regulations are driving public water suppliers to provide suitable technology for reducing nitrate and nitrite concentrations in the interest of addressing avoidable health risks.

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