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5,454,876 Process for reducing lead leachate in brass plumbing components

5,454,876

Oct. 3, 1995

[11]

[45]

111111111111111111111111111111111111111111111111111111111111111111111111111

US005454876A

Patent Number:

Downey Date of Patent:

United States Patent [19]

Primary Examiner-Scott Kastler

Attorney, Agent, or Firm-Dom, McEachran, Jambor &

Keating

[54] PROCESS FOR REDUCING LEAD

LEACHATE IN BRASS PLUMBING

COMPONENTS

[75] Inventor: Jerome P. Downey, Parker, Colo.

[73] Assignee: 21st Century Companies, Inc., Tyler,

Tex.

[21] Appl. No.: 285,007

[22] Filed: Aug. 2, 1994

[51] Int. CI.6 F23J 1/00

[52] U.S. CI 134/3; 134/22.1

[58] Field of Search 134/2, 3, 22.1,

134/22.11; 148/240,250 [57]

4,006,041

4,182,639

4,233,088

4,452,650

4,478,651

4,582,556

4,615,643

4,699,889

4,737,356

4,981,553

5,076,941

5,118,367

5,193,936

2/1977 Fabregas et al 148/6.16

111980 Pignocco et al 148/6.17

1111980 Kronstein 148/6.16

611984 Caule 148/31.5

1011984 Brock et al 148/31.5

411986 Butt et al. 156/525

1011986 Gouvenot 405/128

1011987 Sales et al 501/22

411988 O'Hara et al 423/659

111991 Tytgat et al 156/666

12/1991 Boffardi et al 210/753

6/1992 Starinshak 148/262

311993 Pal et al 4051128

ABSTRACT

[56] References Cited

U.S. PATENT DOCUMENTS

3,669,765 6/1972 Bradshaw et al 148/6.16

3,764,399 10/1973 Caule 148/6.15

3,779,842 12/1973 Grunwald et al 156/18

3,898,137 8/1975 Dueber et al 204143 G

3,905,907 9/1975 Shiga 252/79.4

3,940,303 2/1976 Caule : 148/31.5

3,950,193 4/1976 Caule 148/31.5

3,975,308 8/1976 Myles et al 2521520

A process for treating brass plumbing components to reduce

leachable lead when the component is subsequently exposed

to water includes exposing the brass component in an

aqueous solution containing a desired concentration of chloride

and pyrophosphate, with the chloride ion promoting the

dissolution of lead from the brass component and the

pyrophosphate ion preventing saturation of the solution with

lead insuring continuation of the dissolution process.

20 Claims, No Drawings

5,454,876

2

DESCRIPTION OF THE PREFERRED

EMBODIMENT

5

only economical and readily available chemicals and process

equipment

Another purpose of the invention is to render faucet

components in typical designs and typical materials acceptable

without perceptible deterioration of the cosmetic

appearance or function due to discoloration or excessive

removal of copper or zinc.

Another purpose of the invention is a process for treating

brass components which uses chloride and pyrophosphate

10 ions in aqueous solution.

Another purpose is a treatment process of the type

described in which the brass component is exposed to an

aqueous solution of chloride and pyrophosphate ions for a

15 predetermined time period, the solution being maintained at

predetermined temperature.

Another purpose is a treatment process as described in

which the aqueous treatment solution is re-circulated to

continually remove dissolved lead or insoluble lead precipi20

tate from the treatment tank..

Another purpose of the invention is to provide a brass

treatment process in which a brass component is exposed to

an aqueous solution containing a mixture of active ingredients

which both selectively dissolve metallic lead at an

25 accelerated rate while leaving the brass substantially unaffected

and also sequester the lead in solution such that the

solution reaction for lead does not naturally come to a halt

Another purpose of the invention is to provide a brass

treatment process which prevents lead from subsequently

30 leaching from the brass into water by creating a barrier about

any lead particles which remain on the brass.

Other purposes will appear in the ensuing specification

and claims.

The present invention is specifically directed to a process

for treating brass, and more specifically brass plumbing

components such as faucet bodies, shower heads and well

pumps, so as to reduce the leachable lead. The process

described will economically reduce leachable lead to an

amount which will be acceptable under the anticipated

standards to be set by the National Sanitation Foundation

and specifically the standard known as NSF-61. It is currently

anticipated that the NSF-61 standard will require the

concentration of lead found in solution ejected from the

faucet, to be on average, less than 11 micrograms per liter

50 (ug/L) overthe first 19 days of testing when the solution is

collected and the concentration calculated according to the

NSF-61 standard. This is an accumulated leachable lead

total and is basically determined in a protocol issued by the

NSF. Although there are a number of processes which may

55 treat brass to reduce the potential leachable lead, it is

essential that such a process be commercially viable in terms

of the cost and time involved in the treatment process so that

the faucets or other plumbing products which are treated will

continue to be viable in the marketplace.

The present invention is specifically directed to a process

in which the brass component, either a faucet body for single

handle or double handle use, is exposed to an aqueous

solution containing desired concentrations of chloride and

pyrophosphate. Sodium chloride and sodium pyrophosphate

65 are the preferred salts for introducing chloride and pyrophosphate

in solution although those skilled in the art will

understand that other chloride and pyrophosphate sources

THE FIELD OF THE INVENTION

SUMMARY OF THE INVENTION

1

PROCESS FOR REDUCING LEAD

LEACHATE IN BRASS PLUMBING

COMPONENTS

Leaded brass has been used in the manufacture of water

flow fixtures such as shower heads, faucets, tub spouts and

the like since such devices first came into modem use. The

Environmental Protection Agency has issued regulations

which limit the maximum quantity of lead that is permitted

to be leached into the water from such plumbing fixtures

during an overnight dwell or extensive period of non-use.

Most faucets presently in use will meet the maximum

leachable lead limits established by the EPA prior to 1993.

However, the EPA is now reducing the maximum permissible

limits, and it is widely anticipated that by the end of

1994, many faucet products currently in production will not

meet the revised limits. Consequently, most of the manufacturers

of water flow devices such as faucets are expending

substantial effort in the redesign of their products or their

manufacturing processes to meet the anticipated EPA guidelines

for leachable lead.

The EPA has delegated to the National Sanitation Foundation

responsibility to develop the protocol which will

determine the quantity of lead leaching into the potable

water supply from regulated devices such as faucets. It is

anticipated that the protocol will evaluate the lead leached

into the water supply during the first 19 days after installation,

and that on average faucets will be required to contribute

less than 11 micrograms per liter of lead per day to

the water sampled after filling and testing according to the

precisely defined procedure. The procedure will be defined

in a document known as the NSF-61 standard.

The present invention is directed to a process for treating 35

brass plumbing products in order to significantly reduce the

quantity of lead leached into the water. The process is

specifically directed toward reducing the total leachable lead

over the prescribed time period in the most cost effective

40 manner. Clearly, there are processes which will reduce the

leachable lead to amounts which meet the standard, but these

processes are so expensive or time consuming as to be

commercially unacceptable. The present invention provides

a process which is both commercial and one which will

45 provide a product which will meet or exceed the anticipated

NSF-6l standard for leachable lead.

The present invention relates to a process for treating

brass to reduce the quantity of lead which may subsequently

be leached from the brass when it is exposed to water.

The primary purpose of the invention is to provide a

process for the treatment of brass components which rapidly

removes at least a portion of the lead on the surface of the

brass, thus reducing the potential for lead to leach from the

brass when subsequently exposed to water.

Another purpose of the invention is to render typical

faucet designs made out of typical materials (most notably 60

CDA 360 brass and CDA 844 cast red brass) acceptable

under the anticipated NSF-61 standard after treatment times

of less than five minutes, which are relatively easy to

implement in a production facility.

Another purpose of the invention is to render faucet

components in typical designs and typical materials acceptable

under the NSF-61 standard after a treatment which uses

5,454,876

3

such as other polyphosphates and hydrochloric acid may

also be used. The invention will be described using sodium

chloride and sodium pyrophosphate, although it should not

be so limited. The brass component will be exposed to the

described solution, for example, by immersion or by flush- 5

ing.

The applicant herein has cause to be instituted numerous

tests of the described process in which the time of exposure,

the concentration of sodium chloride and sodium pyrophosphate

decahydrate and the temperature have all been varied. 10

Specifically, tests have established that brass plumbing components

immersed in an aqueous solution containing 15 gIL

of sodium chloride (a concentration of 0.26 molar chloride),

and 90 gIL of sodium pyrophosphate (a concentration of

0.20 molar pyrophosphate), at a temperature of 60° C. and

immersed at time intervals from 3.5 min. to 30 min. will 15

subsequently pass the NSF-61 leachable lead test. The tests

involved immersing brass faucet products for time periods

of 3.5 min., 7.5 min., 15 min. and 30 min. In each instance

the products all passed the NSF-61 test in that the amount of

lead leached over the 19-day test period was substantially 20

less than the anticipated standard of 11 ug of lead per liter

of water.

Further tests were run in which the treatment lasted for 3.5

min. and the following temperatures and concentrations 25

were utilized. In all instances the concentration of sodium

chloride was 15 gIL (a concentration of 0.26 molar chloride).

Brass faucet parts were immersed for 3.5 min. in the

following aqueous solutions, including the described sodium

chloride: 90 gIL of sodium pyrophosphate (a concentration 30

of 0.20 molar pyrophosphate) with the solution being maintained

at 35° c.; 90 gIL of sodium pyrophosphate (a concentration

of 0.20 molar pyrophosphate) with the solution

being maintained at 70° c.; 81 gIL of sodium pyrophosphate

(a concentration of 0.18 molar pyrophosphate) with the 35

aqueous solution being maintained at 60° C.; and 45 gIL of

sodium pyrophosphate (a concentration of 0.10 molar pyrophosphate)

with the aqueous solution being maintained at

60° C. In each of the above tests the accumulated total of

leachable lead over the 19-day test period prescribed in 40

NSF-61 was less than 11 uglL.

Additional tests were run in which the solution was

maintained at a temperature of 60° c., the immersion time

was 3.5 minutes, and the amounts of sodium chloride and

sodium pyrophosphate each varied from 25 gIL to 120 gIL 45

(a concentration of 0.42 molar to 2.1 molar chloride and 0.06

molar to 0.27 molar pyrophosphate). In each instance the

accumulated leachable lead, as per the NSF-61 protocol, was

less than 11 uglL.

Based on the tests described above, a brass faucet product 50

immersed in an aqueous solution of from 10 gIL to 120 gIL

of sodium chloride (a concentration of 0.17 molar chloride

to 2.1 molar chloride); sodium pyrophosphate in an amount

ranging from approximately 25 gIL to approximately 120

gIL (a concentration of 0.06 molar pyrophosphate to 0.27 55

molar pyrophosphate); an immersion time of from approximately

3.5 min. to approximately 30 min.; with the solution

maintained at a temperature offrom approximately 35° C. to

approximately 70° C., will result in a brass product which

will pass the NSF-611eachable lead protocol. The preferred 60

embodiment of the invention is to utilize a time period of 3.5

min., although it is anticipated that initial use of the invention

may have an immersion time of 5 min. The preferred

concentration is 15 gIL of sodium chloride (0.26 molar

chloride) and 90 gIL of sodium pyrophosphate (0.20 molar 65

pyrophosphate). It is preferred to maintain the aqueous

solution at a temperature of approximately 60° C. In addition

4

to the above-described parameters, it is preferred that the

aqueous solution be continuously circulated and be air

agitated for a constant infusion of oxygen. The solution pH

should be maintained in a range of 9.5 to 10.5, with a pH of

10 being preferred.

When the brass component is immersed in the described

aqueous solution, dissolved oxygen is converted to hydroxyl

ions by an electron accepting reduction reaction with water,

the electrons being provided by conversion of metallic lead

at the brass surface to lead ions in aqueous solution.

2Pb(s)+02(aq)+2H20(I)=2Pb

2

+(aq)+40H-(aq)

The chloride ions in solution accelerate the dissolution of

metallic lead. The pyrophosphate ions in solution chelate the

lead ions in a complex such as PbP2h2-, thus reducing the

chemical activity of the Pb2+ species and preventing the

above-described conversion of metallic lead from terminating.

In summary, five factors in the invention ensure that lead

is removed expeditiously:

1. Aeration of the solution is required to ensure an

adequate supply of dissolved oxygen, without which the

lead solution reaction set forth above would not occur.

2. Chloride ions are required to accelerate the rate of lead

dissolution.

3. Pyrophosphate ions are required to sequester the dissolved

lead in solution, thus preventing the above lead

solution reaction from reaching equilibrium.

4. Agitation of the solution is required to ensure that fresh

supplies of the reagents participating in the reaction rapidly

are brought to the reaction site at the faucet surface, and that

the products of reaction are rapidly removed.

5. A moderately elevated temperature is required to accelerate

the rate of reaction. However, too high a temperature

would reduce the availability of the required dissolved

oxygen.

His believed that with the pH in the described range of9.5

to 10.5 the surface lead will be dissolved as described. lithe

pH is acidic it is anticipated that a barrier of chloropyromorphite

or other lead phosphate compounds may form

about lead particles remaining on the brass.

Whereas the preferred form of the invention has been

shown and described herein, it should be realized that there

may be many modifications, substitutions and alterations

within the scope of the following claims.

The embodiments of the invention in which an exclusive

property or privilege is claimed are defined as follows:

1. A process for treating brass components to reduce

leachable lead when the component is subsequently exposed

to water, the process including:

(a) exposing the brass component to an aqueous solution

containing chloride in a concentration of from about

0.17 molar to about 2.1 molar and pyrophosphate in a

concentration of from about 0.06 molar to about 0.27

molar;

(b) the brass component remaining exposed to the aqueous

solution for a time period of from approximately

3.5 min. to approximately 30 min., with the temperature

of the aqueous solution being in the range of from

approximately 35° C. to approximately 70° C.

2. The process of claim 1 in which the concentration of

pyrophosphate is approximately 0.20 molar.

3. The process of claim 1 in which the concentration of

chloride is approximately 0.26 molar.

4. The process of claim 1 in which the time period of

immersion is from approximately 3.5 min. to approximately

7.5 min.

5,454,876

5 6

* * * * *

tration of from about 0.06 molar to about 0.27 molar.

14. The-process of claim 13 wherein the concentration of

pyrophosphate is approximately 0.20 molar.

15. The process of claim 10 wherein the brass component

remains exposed to the aqueous solution for a time period

ranging from approximately 3.5 min. to approximately 7.5

min.

16. The process of claim 13 wherein the concentration of

chloride is approximately 0.26 molar.

10 17. The process of claim 10 wherein the solution pH is

maintained from 9.5 to 10.5.

18. The process of claim 10 wherein the solution is

continually air agitated.

19. A process for treating brass components to reduce

leachable lead when the component is subsequently exposed

to water, the process including exposing the brass component

to an aqueous solution containing two kinds of active

species, one of the species promoting the dissolution of lead

from the brass component, with the other species sequestering

the dissolved lead in solution preventing the lead

solution reaction from reaching equilibrium.

20. The process of claim 19 wherein the solution is

aerated to provide dissolved oxygen to insure lead dissolution.

5. The process of claim 4 wherein the immersion time is

approximately 3.5 min.

6. The process of claim 1 wherein the solution is maintained

at a temperature of approximately 60° C.

7. The process of claim 1 wherein the solution pH is 5

maintained from 9.5 to 10.5.

8. The process of claim 7 wherein the solution pH is

maintained at about 10.

9. The process of claim 1 wherein the solution is continually

air agitated.

10. A process for treating brass components to reduce

leachable lead when the component is subsequently exposed

to water including exposing the brass component to an

aqueous solution containing concentrations of chloride and

pyrophosphate with the chloride ions promoting the disso- 15

lution of lead from the brass component and the pyrophosphate

ions sequestering the dissolved lead in solution, preventing

the lead solution reaction from reaching

equilibrium.

11. The process of claim 10 wherein the aqueous solution 20

is maintained at a temperature in the range of from approximately

35° C. to approximately 70° C.

12. The process of claim 11 wherein the aqueous solution

is maintained at a temperature of approximately 60° C.

13. The process of claim 10 wherein the aqueous solution 25

contains chloride in a concentration of from about 0.17

molar to about 2.1 molar and pyrophosphate in a concen-

30

35

40

45

50

55

60

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