Jamaica Bay Water Pollution Control Plan
Queens, NY
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CLIENT: Metcalf
& Eddy of New York, Inc. 60 East 42nd Street, 43rd
Floor
New York, NY 10165
Paul
F. Storella
212-984-7379
CONSTRUCTION
COST:
$130,000,000
CONSTRUCTION
COMPLETION DATE: 2006
DiGeronimo PA as Architectural Design Subconsultant to Metcalf
& Eddy (M&E) is responsible for the coordination of the work
with M&E and all other subconsultants in order to ensure the satisfactory
completion of the contract within the scheduled contract completion
date. The other five
subcontracts related to Phase 2 design work: Structural Design works;
HVAC/Plumbing Design work; Civil Design work; Cost Estimated Services;
and Technical Assistance.
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AERIAL VIEW
- SITE PLAN
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DiGeronimo PA is design architect for appropriate support facilities
to accommodate plant personnel, both administrative and maintenance
staff, in an 50,000 sq. ft. administration and maintenance building
at the Jamaica Water Pollution Control Plan (WPCP) situated in Jamaica,
Queens, adjacent to JFK airport, New York.
DiGeronimo PA is also designing two major new process buildings
and alterations to several existing buildings to accommodate new water
treatment processes and related equipment.
| ADMINISTRATION
BUILDING |
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| DIGESTER
ELECTRICAL BUILDING 1-2 |
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| EFFLUENT
WATER PUMP STATION |
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| MAIN
BUILDING |
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| SECONDARY
SCREENING BUILDING |
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Project
History
Construction of
the Jamaica WPCP Improvements has two main phases, each consisting
of four prime contracts.
Phase
I construction began in April 1997 and is scheduled for completion
in October 2003.
Phase
2 will have a 5½ year construction period, beginning in January 2003
and ending in June 2006. The
estimated construction cost of Phase 2 is approximately $130 million.
The
original Jamaica plant built in the late 1920s consisted of a grit
chamber, fine screening chamber, pumping station, and chlorination
facilities.
The
pumping station and screening chamber were housed in a 70-foot-diameter
caisson commonly referred to as the “Round House.”
These facilities had a capacity for an average flow of approximately
50 mgd.
The
plant expansion to a 65-mgd modified aeration facility occurred in
the early 1940s. Plant
expansion to 100 mgd with upgrading occurred in 1960-1964.
Further upgrading in 1970 modernized the plant and further
improved operations. The
new Sludge Dewatering Building began operation in 1993.
The existing plant wastewater treatment process includes screening,
primary settling, activated sludge treatment by step aeration, and
chlorination. Cyclone
degritters separate inorganic solids (grit) from the preliminary sludge.
Sludge treatment includes gravity thickening followed by two-stage
digestion and centrifuge dewatering.
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