
•
FEATURE Groundwater Replenishment in California
JOURNAL AWWA • APRIL 2025 45
OCWD staff put the two newer polyvinylidene fluoride
(PVDF) membranes into full-scale cells, testing them and
collecting data for more than six months. These full-scale
tests supported procurement of the best-fit design to
handle the potential for high-fouling influent.
Once operations staff saw the effectiveness, they com-
petitively bid the membranes; the testing and selection
process saved the district $8 million over what was bud-
geted. The use of more chemically tolerant PVDF micro-
filtration membranes reduces the frequency of cleanings
and extends the service life of the membranes.
OCWD implemented a universal design for the micro-
filtration membrane system that could fit several types
of membranes, giving it flexibility in membrane selection
during the bidding process. This innovative design also
kept the expansion plans moving forward, even if all the
specifics weren’t yet finalized. Considering the space
limitations of the expanded plant, the delivery system
for chlorine, which is used for PVDF membrane cleaning,
was located in two separate areas at the GWRS to ease
chemical deliveries by trucks.
Repurposing a Little-Used Pipeline
Since the GWRS expansion would use wastewater from
a new source, a suitable pipeline was needed to link the
facilities. Three pipelines already connected OC San’s
Plant No. 1 (next to the GWRS) and Plant No. 2, and one
of the pipelines—a full 66 inches in diameter—was a
little-used overflow line. This line was originally built
in 1957, and after it was rebuilt with a new liner, it
would serve as the connector. Since the GWRS is uphill
from Plant No. 2, the rebuild was especially critical as
the line was changing from being gravity-driven to a
pressure line.
The 3-mile conveyance pipeline was relined with
fiberglass-reinforced plastic as part of a process consist-
ing of digging numerous “launch pits” along the route,
inserting the liner in a special mechanism and pushing it
through the pipeline to the next launch pit. Aside from a
few locations that required a steel liner for short distanc-
es, fiberglass-reinforced plastic was used throughout.
Relining gave the pipeline a second life and avoided
the challenges of trenching and tunneling a new pipeline
through a narrow right-of-way. In addition, the relining
process and the pipe’s large diameter are expected to re-
duce energy needs, ultimately saving $200,000 annually.
Interstage Boosting at RO Units
The expansion project closely examined the existing
facilities to determine whether upgrades or modifica-
tions were needed. When it came to the RO system, the
higher salt content in the new wastewater source meant
higher operating pressures. So rather than pumping the
water through all three RO stages using a single feed
pump, whereby the flow would be weaker at the end than
the beginning, an interstage booster pump was added
between the first and second stages to help balance the
flow and ultimately use less energy.
Interstage boosting was installed on the six new RO
units (each rated at 5 mgd) and retrofitted into the orig-
inal 15 units. This new system maintains the flows and
balances production, allowing the plant to achieve longer
run times between membrane cleanings. In addition,
flowmeters were installed on all stages of the units to
better track and analyze performance. Achieving more
constant flow should save more than $10 million in ener-
gy costs over the lifespan of the equipment while main-
taining an 85% recovery rate through the RO units.
Monte Carlo Simulations
Key parameters considered when designing a water recy-
cling system included temperatures, total dissolved sol-
ids, amount of salt, and the organic materials in the
water. A series of Monte Carlo simulations were used to
screen a variety of data from more than 1,000 scenarios
to determine the most probable water quality, which sub-
sequently guided the selection of equipment, pumps, and
pressure lines.
Treatment for the final expansion was designed using
the statistical analysis from Monte Carlo projections for
influent water quality. Ultimately, the design used the
95th percentile of quality to ensure the system wasn’t
over-designed for the occasional times when quality was
worse than expected. This simply means that during
those occasions, the plant wouldn’t produce as much
water for a short period.
Equalization Tanks
During the latest GWRS expansion, some key modi-
fications were taking place at OC San’s Plant No. 2 to
better optimize its performance. For instance, the RO
membranes are best operated at a constant feed rate
rather than a variable flow. Wastewater systems have
more activity during the day and less activity at night,
so to achieve a constant flow, OCWD installed two large
flow-equalization tanks for Plant No. 2; now the RO units
can hum along at a constant pace and keep production
going at maximum capacity. Flow-equalization tanks
were installed during the initial expansion at the GWRS
plant in 2015, and now the practice of using them before
RO treatment has become a common practice.
Other improvements at Plant No. 2 included the in-
stallation of a weir in the existing pipe. Instead of using
a pump station for the tanks, the water was intercepted
15518833, 2025, 3, Downloaded from https://awwa.onlinelibrary.wiley.com/doi/10.1002/awwa.2419, Wiley Online Library on [19/03/2025]. See the Terms and Conditions (https://onlinelibrary.wiley.com/terms-and-conditions) on Wiley Online Library for rules of use; OA articles are governed by the applicable Creative Commons License