Problem
A pharmaceutical company had a
5,000 SCFM oxidizer that they were looking to relocate to another
facility across the United States. The destruction efficiency
rate and heat recovery expectation at the new location differed
from the original design conditions at the current facility.
Action
An Anguil field service
engineer went to site to inspect the unit. A report detailing
the current condition of the oxidizer at its current location was
generated as well as a written procedure for the proper disassembly
and reassembly of the equipment. The service engineer
evaluated the unit and made recommendations outlining the
modifications necessary to make the unit run at the new facility's
desired destruction efficiency rate and the energy
requirements.
Solution
Anguil worked closely with the
customer to modify and upgrade the system based on the detailed
site inspection report. The work included a control package
upgrade and a new hot gas bypass damper.
To address the energy
recovery requirements at the new facility, a new economizer was
installed between the oxidizer and exhaust stack to transfer heat
to water. The exhaust heat from the stack was transferred to
the Anguil economizer which in turn created hot water. This
otherwise lost energy is captured and can be used in various
applications such as boiler feedwater, cold makeup water, process
water, glycol, and thermal fluids.
The stainless steel system is
a tube and fin style heat exchanger with access doors for
inspecting and cleaning of the tubes. The exhaust flow from
the catalytic oxidizer is 5,400 SCFM and the temperature is
450°F. Roughly 160 GPM of water is heated to 140°F with the
economizer. The total energy recovered is 1.43 MM BTU/hr or
an estimated total savings of $120,512 per year.
REPORTED VALUES

PROJECTED VALUES WITH ENERGY RECOVERY SYSTEM

| ESTIMATED HOURLY SAVINGS OPPORTUNITY |
$14.35/HOUR |
| ESTIMATED YEARLY SAVINGS OPPORTUNITY |
$120,512.45/YEAR |
Job Pictures
