Process
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Chlorine Generator Process

The i-chlor chlorine generator is as simple as a battery with no moving parts.  This page is intended to help you understand the simplicity of the i-chlor chlorine generator leaving you thinking... why hasn't anyone thought of this before! 

On this page you will discover:

To view a video demonstration on the chlorine generation process, please click here!  This may take a few minutes, so please be patient. 

Process Components

The i-chlor chlorine generator requires a cell, DC power supply (battery charger, battery, solar power), energy source (power outlet, generator), a pressurized water supply to operate the venturi ejector, and a vacuum relief reservoir to prevent collapse of the salt reservoir.  Please note that the use of a union pipe fitting in the cell configuration as well as the i-chlor chlorine generator system are patented.  Purchase of systems and/or components from Chlorine Generators, Inc. will not be considered patent infringement. 

Cell:  The cell includes the anode and cathode compartments that are hydraulically isolated by an ion selective membrane located between the two cell compartments.  The anode compartment contains the anode (electrode),  saltwater electrolyte, and chlorine.   The cathode compartment contains the cathode (electrode), sodium hydroxide (caustic soda) electrolyte, and hydrogen.  The hydrogen produced from the cathode compartment is vented to the outside atmosphere.  The two cell compartments are joined together by a union pipe fitting that also holds the ion selective membrane between the union flanges. 

Salt Reservoir:  The anode compartment of the cell is connected to the salt reservoir.  The salt reservoir contains the salt, saltwater, and chlorine.  Chlorine gas generated from the anode compartment bubbles up into the salt reservoir which is swept under vacuum by the venturi ejector into the water supply. 

DC Power Supply:  The DC power supply can be any DC battery charger of adequate size to handle the needed chlorine demand.  Our i-chlor system utilizes a power supply having an adjustable amperage setting that once set, maintains a constant amperage output regardless of temperature, conductivity, and resistance changes.  This means a constant chlorine output, even at very small chlorine dosage levels. 

Energy Source:  The energy source is basically the 120 VAC power outlet supply. 

Pressurized Water Supply:  The water passes through a venturi creating a vacuum that is applied to the salt reservoir.   The discharge from the vacuum ejectors is highly chlorinated water in the form of hypochlorous acid and/or hypochlorite ion. 

Vacuum Relief Reservoir: Water or sodium hydroxide is added to the vacuum relief reservoir which allows excess atmospheric air to be added to the venturi vacuum system preventing collapse of the salt reservoir.  

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Process Installation

Provided the plumbing for the system is complete (existing vacuum ejector, or simply using a garden hose connected to the ejector) It should not take longer than 30 minutes to an hour to have your chlorine generator completely operational.    The installation includes the following steps:

  • remove components from the box, check contents for any missing or broken parts
  • soak the membrane in warm water
  • install the membrane on the cell flange
  • connect tubing between the cell and the salt reservoir
  • fill vacuum relief reservoir with water
  • add salt and water to the salt reservoir
  • add water and dry sodium hydroxide to the cathode compartment
  • connect water supply to venturi ejector
  • connect the vacuum tubing from the anode compartment to the venturi ejector
  • plug electrode connector into the power supply connector 
  • turn on power supply switch
  • plug power supply into power circuit
  • operate venturi ejector and energize power circuit, adjust power supply to desired chlorine level. 

System Operation

The system operation includes the control of the system, addition of salt and water to the salt reservoir, periodic dilution of the sodium hydroxide in the cathode compartment, and occasional cleaning of the cell membrane.

There are several ways the chlorine generator can be operated.  The simplest way is to plug the power controller into a power outlet that is only energized at times when the generator is needed for chlorine production.  This on/off operation procedure can be accomplished by installing a power control relay on the power outlet circuit.   Nearly all municipal well installations include this type of circuit typically used for a hypochlorination pump. A PLC programmable controller (PLC) can also be used to energize the circuit when needed. 

The power supply has a constant amperage feature that allows precise chlorine dosage control regardless of brine temperature, membrane resistance, or solution ionic strength.

At a booster pump station having multiple pumps, a chlorine generator for each pump circuit will supply the step chlorine dosage needed depending on the number of pumps operating.  This operational procedure eliminates the need for an electronic logic controlled loop and/or pacing valve systems.

The chlorine generator's small size and portability allows the operator to use the chlorine generator practically anywhere with multiple seasonal uses.  In the northern cold regions, use the chlorine generator to fill you laundry tub when you are not needing the system on your frozen swimming pool. 

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Dose Control

Chlorine output is adjusted by the power input of the process.  Every 15 amperes of direct current (DC) provide a chlorine production rate of 1 pound per day (24 hours).  The graph below illustrates the equivalent chlorine production at the desired amperage setting. 

 

Amperage to Chlorine Relationship Graph

Note:  With time, the membrane accumulates calcium and other mineral deposits that increase the resistance between the electrodes.  The increased resistance causes the power supply voltage to increase to maintain the desired amperage output.  When the high end voltage is reached, a reduced amperage output and a corresponding reduced chlorine output will also be observed.  The system needs periodic membrane cleaning to recover the desired amperage output.  A water softener system can be added to the system water supply to reduce the amount of calcium, thus increasing the service life of the membrane. 

 

The power supply includes both constant voltage and constant current (amperage) adjustments.  Since dosage is a direct relationship with amperage, the power supply's constant current setting is desired in most applications.  To set the power supply at constant current, the voltage adjustment potentiometer is set to its full on level (10 turns clockwise)Adjustment of the amperage potentiometer will then increase or decrease the amperage output to the desired current setting, and maintain that current setting regardless of any voltage changes in the process.  For example, a chlorine output of 0.5 lbs per day is desired for a 100 gpm well.  Based on amperage conversions, approximately 8 amperes of DC power is needed for the well.  The operator would adjust the voltage control dial full on allowing for the power supply to operated on constant current, then adjust the current dial to achieve a power output of 8 DC amperes for the cell.

 

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Salt Addition

For every 50 lb bag of water softener salt, approximately 30 lbs of chlorine is made.   The frequency of salt addition depends on the operating cycle.  For example:

A 150 gpm municipal well operating a total of 6 hours per day (54,000 gpd) using a 1.5 lb/day (22 amperes) chlorine dosage rate (0.5 mg/l chlorine residual w/ a 0.35 mg/l chlorine demand) will need to have salt added every 80 days (30 lbs/cell / [1.5 lb/day * 6 hr / 24 hr]).     

Salt replenishment in the salt reservoir requires the drainage of the brine, flushing the anode compartment with water, and addition of new salt and water to the brine reservoir.  Adding of salt to the cell without flushing and cleaning is not recommended for several reasons.  First, the anode compartment contains residual chlorine gas that will be displaced when salt is added.  The amount of chlorine gas in this space is small (0.05 lbs); however, this amount of chlorine gas is irritating especially if in a confined space. Second, the brine contains concentrated mineral impurities that will foul the membrane at a more rapid rate if it is not removed.  It is also recommended that the membrane be cleaned during a salt replenishment cycle which will increase the membrane's life.

Replenishing the salt consists of:

  • Turn off the power supply to the cell. 
  • Add roughly 1/2 gallon of sodium hydroxide to the salt reservoir (few ounces for the 0.2 model).  The sodium hydroxide will neutralize the residual chlorine in the brine and make a salt saturated hypochlorite solution.
  • Drain the brine solution to waste and flush out the cell removing all the residual matter in the bottom of the cell.
  • Add new salt and water to the anode compartment (it is desirable to use softened water to reduce the mineral fouling of the membrane). 
  • Place system back into service.

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Sodium Hydroxide Dilution

SAFETY:  Please note that sodium hydroxide is corrosive and irritating to the skin.  If sodium hydroxide touches the skin, wash with water immediately to prevent chemical burn.  Wear protective clothing such as rubber gloves and goggles when handling sodium hydroxide.

The  i-chlor chlorine generator requires periodic dilution of the sodium hydroxide. Dilution can be done manually, or automatically.  For every 50 lb bag of water softener salt, approximately 60 gallons of 10 percent sodium hydroxide solution is made.  For every 1-pound of chlorine made, 2 gallons of 10 percent NaOH is made.  The actual amount of sodium hydroxide produced is dependent upon the level and frequency of dilution. Using the same 80-day operational cycle as discussed above, approximately 0.75 gallon of sodium hydroxide solution is produced every day of operation. 

Manual Dilution:  

Dilution of sodium hydroxide in the cathode compartment requires the removal of approximately one-half gallon of sodium hydroxide and the addition of dilution water to the top overflow of the cathode compartment (Note: more sodium hydroxide is produced than water added for dilution).  Water can also be directly added to the cathode reservoir with excess overflowing through the overflow and into the vacuum relief reservoir, or other reservoir.   It is desirable to use softened water for the dilution to reduce the mineral fouling of the membrane. 

Maintenance of the sodium hydroxide solution within the optimum range (10 percent or less) provides extended life of the membrane.  Daily testing of the sodium hydroxide solution with a hydrometer will verify the need to dilute the sodium hydroxide.   The following table illustrates the specific gravity and concentration of sodium hydroxide at a temperature of 60 degrees F (15.5 degrees C):

 % NaOH

Specific Gravity

 2

 1.023

 4

 1.045

 6

 1.067

10 

 1.090

12

 1.112

14

 1.134

16

 1.156

18

 1.178

20

 1.201

 22

 1.223

 
Dilution of the sodium hydroxide consists of:

  • Turn off the power supply to the cell. 
  • Removal of 1/2 gallon of solution (or more if operating the cell at higher rates or longer periods of time), and dispose/store as desired (this could be disposal down a sanitary drain if solution is not needed; however, sodium hydroxide is needed for pH adjustment in the pool, CIP cleaning, lift station cleaning in sewer systems, and/or pH adjustment of water for lead and copper corrosion control in municipal drinking water).   
  • Add dilution water (preferably softened water) to a level at the top overflow of the cathode compartment.
  • Place system back into service.
  • Check small amount of solution daily with a hydrometer

Automatic Dilution: 

The i-chlor system can be equipped with an optional automatic density control system.    Excess sodium hydroxide is captured through the vacuum relief reservoir, or in a separate system (i.e. tank/jug) as desired. 

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System Maintenance

The chlorine generator has no moving parts and requires minimal maintenance.  The system maintenance involves the periodic cleaning of the membrane.  The salt and water added to the chlorine generator contain calcium and other minerals that accumulate on the surface of the membrane.  These mineral deposits increase the electrical resistance across the membrane eventually reducing the amperage to the cell thus reducing the chlorine production.  These minerals also wear on the membrane polymers during membrane flexing causing pinholes.  Using the same 80-day operational cycle as discussed above, it is desirable to clean the membrane at the same time as the salt change.  Operating the cell at 1 lb/day for 24 hours/day may require membrane cleaning every month (again, depending on the dilution water quality). 

Cleaning the membrane involves the following:

  • Turn off the power supply to the cell. 
  • Remove brine and salt from anode compartment as described above.
  • Draining and storage of sodium hydroxide fro the cathode compartment.
  • Flushing the interior of both compartments with water to remove all loose deposits. 
  • The membrane cleaning requires the removal of the membrane from the union fitting and replacement with a cleaned membrane.  The membrane removed from the cell is then soaked in a weak hydrochloric acid solution (muriatic or pool acid), or vinegar to dissolve the mineral deposits.  After cleaning, observe the condition of the membrane and discard if pin-holes are observed in the membrane.  Otherwise, store membrane in a water solution for the next cleaning cycle. 
  • Install the membrane back onto the cell union and tighten fitting.
  • Restore sodium hydroxide to the cathode chamber and salt and water to the anode chamber.
  • Reconnect power to cell and resume operation

Items that wear and need eventual replacement include the vacuum tubing, rubber gasket/o-ring, membrane, and the anode. The anode has an expected life of five years based on a chlorine rate of 1 lb/day under moderate usage.  The membrane has an anticipated life of one year depending on the frequency and dilution of the sodium hydroxide (see above). The rubber gasket in the cathode compartment may also need to be replaced every few years as needed. The vacuum tubing should be check annually and replace when cracks are observed.  Use chlorine compatible tubing such as polyethylene tubing when replacing.

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