Control of hard water scaling in electrochemical cells

a technology of hard water scaling and electrochemical cells, applied in the field of water electrolysis, can solve the problems of increasing voltage demand, affecting the efficiency and convenience of electrolysis systems, and affecting the efficiency of electrolysis systems, and achieve the effect of effective cleaning and/or sanitizing surfaces

Inactive Publication Date: 2011-07-14
ECOLAB USA INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

According to still further aspects of the invention the threshold agent may be added in the amount of up to about 1,000 ppm or in the amount of from about 50 ppm to about 500 ppm. The threshold agent may have a molecular weight less than 5,000, preferably less than 2,000. Preferably, the hypochlorite produced according to embodiments of the invention effectively cleans and / or sanitizes surfaces without depositing streaks or spotting.

Problems solved by technology

The effectiveness and convenience of utilizing electrolysis systems are frequently limited due to the failure of the electrodes and membranes of the cells caused by both corrosion and hard water scaling.
Most often, calcium and magnesium ions are contained in either the water source or salt solutions added to electrochemical cells, resulting in the previously considered unavoidable scaling in cells, resulting in detrimental effects to the cells by forming hydroxide precipitates and scale.
The precipitate and scale eventually coat the surface of the electrodes and membranes causing an increased voltage demand by the cell and may potentially lead to short-circuiting of the cell.
Therefore, a significant disadvantage to the use of electrochemical cells, such as for the production of hypochlorite, is the required use of softened water to prevent hard water scaling.
This is undesirable as acids are very corrosive and may erode the electrodes, specifically the electrode coatings.
However, these and other means of maintaining and repairing electrochemical cells are undesirable and costly for consumers.
Despite the various means for preventing scaling and corrosion, eventually the electrochemical cells become permanently fouled or ineffective, requiring consumers to pay for expensive maintenance and repairs and / or replacement.

Method used

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  • Control of hard water scaling in electrochemical cells
  • Control of hard water scaling in electrochemical cells
  • Control of hard water scaling in electrochemical cells

Examples

Experimental program
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Effect test

example 1

Electrode Scaling in Hard Water. A clean 1″×6″ pair of ruthenium (Ru) coated DSA electrodes for hypochlorite production was analyzed for hard water scaling. The pair of electrodes were placed in a stirred 4 L solution of 1000 ppm of sodium chloride. The sodium chloride solution was made using 17 grain (gpg) hard water. The electrodes in the sodium chloride solution were energized with about 8-12 volts / 0.5 amps from a DC power source. After 4 hours in the electrochemical cell of the sodium chloride solution, the electrodes were removed and air dried. The electrodes were visually examined, revealing a heavy white scale covering the inside of the cathode.

example 2

Prevention of Electrode Scaling in Hard Water With Threshold Agent. The same methods from Example 1 were repeated using a variety of polyacrylate threshold agents and a known reverse EO-PO copolymer threshold agent. The threshold agents were added to the 17 grain hard water sodium chloride solution.

First, using a clean 1″×6″ pair of Ru-coated DSA electrodes for hypochlorite production. The electrodes were placed in a stirred 4 L solution of 1000 ppm of sodium chloride and 100 ppm Acumer 1000 (an acrylic homopolymer of about 2000 molecular weight, available from Rohm & Haas as a 48% solids product). The electrodes in the sodium chloride solution were energized with about 8-12 volts / 0.5 amps from a DC power source. After 4 hours, the electrodes were removed and air dried. No build-up of hard water scale was observed on the cathode submerged in the electrochemical cell containing the threshold agent.

The methods were repeated using solutions containing alternative threshold agents. Elec...

example 3

Effect of Threshold Inhibiter on Hypochlorite Formation Rate. A stirred 4 L solution of 1000 ppm of sodium chloride and 100 ppm Acumer 1000 (a polyacrylate of about 2000 molecular weight available from Akzo) was made using 17 grain hard water. A clean 1″×6″ pair of Ru-coated DSA electrodes for hypochlorite production were placed in the solution. The electrodes were energized with about 8-12 volts / 0.5 amps from a DC power source in the electrochemical cell. Samples were periodically removed from the solution and titrated for available chlorine. FIG. 1 shows a plot of the titration data versus time, demonstrating that the threshold agent Acumer 1000 did not result in any decrease in the rate of hypochlorite formation in the electrochemical cell. Therefore, the polyacrylate threshold agent is capable of preventing hard water scale formation on the cathodes of the electrolyzed cell without decreasing the product of hypochlorite.

The methods were repeated using the same threshold agent (A...

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Abstract

A threshold agent composition and methods of using the same to produce hypochlorite and other effluent streams from an electrochemical cell without the detrimental effects of hard water scaling are disclosed. The invention further discloses use of chemistries to prevent hard water scale formation in various electrochemical cells to enhance cell longevity without decreasing chlorine, hypochlorite or other effluent production.

Description

FIELD OF THE INVENTIONThe invention pertains to the field of water electrolysis and more particularly, threshold agent compositions and methods of use for preventing hard water scale formation in electrochemical cells to enhance cell longevity. In particular, hard water scale formation is prevented through the use of a threshold agent without having to soften the water source for the electrochemical cell or cause any decrease in the production rate of sodium hypochlorite or other effluent from an electrochemical cell.BACKGROUND OF THE INVENTIONElectrolysis as a water treatment process produces two forms of altered water: a reduced or alkaline water; and an oxidized or acidic water. Electrolysis uses an electric current to split water into its two constituent elements: hydrogen and oxygen. Electricity enters the water at a cathode, a negatively charged terminal, passes through the water and exits through an anode, a positively charged terminal. Hydrogen is collected at the cathode (n...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C25B15/00C25B1/26
CPCC02F1/4674C02F1/76C25B1/26C02F2001/46119C02F5/10
Inventor SMITH, KIM R.JOHNSON, JENNA M.OLSON, ERIK C.KILAWEE, PATRICK H.
Owner ECOLAB USA INC
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