BRENT511
Chemical
- Nov 16, 2016
- 2
Hello all,
I am trying to develop a spreadsheet that will calculate the service time of both cation and anion exchangers based on the feed water quality. I have done a calculation based on the design feed water quality and capacity of the ion resin, however I am not getting the 12 hr service time that was calculated from the design conditions.
The documentation I have on the exchangers states that the service duration is 12 hours based on a 1100 gpm feed flow with the following cationic and anionic amounts:
Cations- 92.5 ppm CaCO3
Anions- 136.4 ppm CaCO3
The Cation Resin documentation gives the following
Total Capacity(min.) - 2000 meq/L(43.7 Kgr/cubic ft) (Na form)
Moisture Retention - 44 - 48% (Na form)
Reversible Swelling Na to H(max.)- 8%
Total Cation Resin Volume - 282.5 cubic ft(8000 L)
The Anion Resin documentation gives the following
Total Capacity(min.)- 1300 meq/L (28.4 Kgr/cubic feet) (Cl form)
Moisture Retention - 48 - 54% (Cl form)
Reversible Swelling Cl to OH(max.) - 20%
Total Anion Resin Volume - 494.5 cubic feet(14000 L)
Calculation:
Since the Cation and Anion resin capacities are in Na and Cl meq/l respectively, I converted the feed water anionic and cationic concentrations from ppm CaCO3 to meq/L.
92.5 ppm CaCO3 - 4.02 meq/L as Na
136.4 ppm CaCO3 - 3.85 meq/L as Cl
I then converted the incoming water flow rate of 1100 gpms to Liters/hr
1100 gpm = 249810 Liters/hr
I then multiplied the water flow rate by the cation and anion concentrations
Cation Exchanger: 1005249.9 meq/hr
Anion Exchanger : 961199.8 meq/hr
Total Resin Capacity = Resin Volume* Resin Capacity
Cation Exchanger = (8000)*(2000) = 16000000 meq
Anion Exchanger = (14000)*(1300) = 18200000 meq
To determine the cycle time I then divided the resin capacity by the cation and ion meq. flow rate. The service times I calculated for the cation and anion exchangers are as follows
Cation Exchanger: 15.9 hrs
Anion Exchanger : 18.9 hrs
Could someone please help me understand why I am not getting the 12 hr design cycle time?
Thanks
I am trying to develop a spreadsheet that will calculate the service time of both cation and anion exchangers based on the feed water quality. I have done a calculation based on the design feed water quality and capacity of the ion resin, however I am not getting the 12 hr service time that was calculated from the design conditions.
The documentation I have on the exchangers states that the service duration is 12 hours based on a 1100 gpm feed flow with the following cationic and anionic amounts:
Cations- 92.5 ppm CaCO3
Anions- 136.4 ppm CaCO3
The Cation Resin documentation gives the following
Total Capacity(min.) - 2000 meq/L(43.7 Kgr/cubic ft) (Na form)
Moisture Retention - 44 - 48% (Na form)
Reversible Swelling Na to H(max.)- 8%
Total Cation Resin Volume - 282.5 cubic ft(8000 L)
The Anion Resin documentation gives the following
Total Capacity(min.)- 1300 meq/L (28.4 Kgr/cubic feet) (Cl form)
Moisture Retention - 48 - 54% (Cl form)
Reversible Swelling Cl to OH(max.) - 20%
Total Anion Resin Volume - 494.5 cubic feet(14000 L)
Calculation:
Since the Cation and Anion resin capacities are in Na and Cl meq/l respectively, I converted the feed water anionic and cationic concentrations from ppm CaCO3 to meq/L.
92.5 ppm CaCO3 - 4.02 meq/L as Na
136.4 ppm CaCO3 - 3.85 meq/L as Cl
I then converted the incoming water flow rate of 1100 gpms to Liters/hr
1100 gpm = 249810 Liters/hr
I then multiplied the water flow rate by the cation and anion concentrations
Cation Exchanger: 1005249.9 meq/hr
Anion Exchanger : 961199.8 meq/hr
Total Resin Capacity = Resin Volume* Resin Capacity
Cation Exchanger = (8000)*(2000) = 16000000 meq
Anion Exchanger = (14000)*(1300) = 18200000 meq
To determine the cycle time I then divided the resin capacity by the cation and ion meq. flow rate. The service times I calculated for the cation and anion exchangers are as follows
Cation Exchanger: 15.9 hrs
Anion Exchanger : 18.9 hrs
Could someone please help me understand why I am not getting the 12 hr design cycle time?
Thanks