P1043WTP_Industry_Event_24Feb21.pptx

P-1043 Hadnot Point Water Treatment Plant Replacement Industry Event MCB Camp Lejeune Jacksonville, NC

24FEBRUARY 2021

Notify Industry of the upcoming solicitation for the P-1043 Hadnot Point Water Treatment Plant Replacement, MCB Camp Lejeune

Inform Industry as to the project scope and timeline

Solicit innovative private sector input to help shape the acquisition strategy, technical solution, and other aspects of the project procurement

Conduct one-on-one discussions

NOTE: Everything you see today is a DRAFT and is subject to change P-1043 Industry Event Goals

P-1043 Hadnot Point WTP Replacement Industry Event Technical Information

Jarrett Selig, PE Design Manager Jacobs Engineering Group, Inc.

MCB Camp Lejeune Jacksonville, NC Wilmington, NC = 1.0 hours Fayetteville, NC = 2.0 hours Raleigh, NC = 2.5 hours

The Portsmouth Naval Shipyard is located in Kittery ME on Seavey Island. The island sits in the Piscataqua River and is located between Kittery ME and Portsmouth NH. The shipyard is located an hour from Boston, MA and less than an hour from both Portland, ME and Manchester, NH.

Security/Access Requirements Security requirements only applicable while on site.

Access Badges required for access to the installation, includes background check Cameras, laptops, and video equipment require approval from security

Site Location Map

Holcomb Blvd Wilson Blvd Seth Williams Blvd Morgan Bay

Major Project Components DD1N Caisson DD1W Caisson

8.0 MGD nanofiltration water treatment plant (WTP) to be located on a greenfield site WTP foundations: aggregate pier/rigid inclusion ground improvements Supervisory Control and Data Acquisition (SCADA) system ≈ 2-1/2 miles of 12” concentrate pipeline with submerged outfall in Morgan Bay Seven buried utility crossings utilizing trenchless technology Decommissioning & demolition of existing Hadnot Point WTP (Bldg. 20) Improvements to existing raw water supply wells ≈ 5-1/4 miles of overhead primary power “express feeder” to Site

Morgan Bay Holcomb Blvd WTP Site Concentrate Line

Outfall Sanitary Force Main Discharge Buried Linear Infrastructure

Existing WTP Site (to be demolished)

Proposed WTP Site

Holcomb Blvd

Wooded site has been harvested.

Grubbing required.

Proposed WTP Overall Site Plan Holcomb Blvd

Process Flow Diagram

South Closure Wall

DD1W Entrance

DD1N

DD1N Entrance

DD1W

Pump Station

Utility Enclosure

DD1E

Center Wall

Berth 1

Berth 11

Nanofiltration (NF) Membrane System Four NF trains, each rated 2.0 MGD permeate production 2-stage, 34:14 pressure vessel array with seven 8-inch 400 SF elements/ vessel 15 gallons per SF per day (gfd) average flux 80% to 87% design recovery Includes interstage booster pump for flux balancing Future Considerations:

Designed for brackish water reverse osmosis (RO) elements Withstand increased feed pressure Stainless steel materials of construction

Operations/Treatment Building Architectural Concept

Operations/Treatment Building West Elevation

East Elevation

Procurement Strategy

Philip Cole Contracting Officer, Naval Facilities Engineering Systems Command Mid-Atlantic

Procurement Strategy Project Budget DFARS 236.204 Magnitude of Construction: Between $25M and $100M Overall Contract Duration Approx 3 years (minimum) Request for Proposals (Single Solicitation Package) Best Value - Tradeoffs Proposal Evaluation Price: Price will be evaluated equally to non-price factors Non-Price Factors:

Corporate Experience (minimum of one to maximum of 5 relevant projects) Safety (DART and TRC rates going back 5 years and written safety narrative) Small Business (proposed plan to utilize small businesses as a part of this contract) Management Approach and Schedule (Technical Narrative and Baseline Schedule) Past Performance (CPARS, PPQs, etc.)

Best Value – Tradeoffs FAR 15.1 Competitive acquisitions – proposals will be evaluated in an impartial and comprehensive manner, ultimately leading to the selection of the proposal that represents the best value to the Government.

Best value - the expected outcome of an acquisition that, in the Government's estimation, provides the greatest overall benefit in response to the requirement.

FAR 15.101-1 – Tradeoff process Used when it may be in the best interest of the Government to consider award to other than the lowest priced offeror or other than the highest technically rated offeror.

All evaluation factors that will affect contract award and their relative importance shall be clearly stated in the solicitation.

The solicitation shall state whether all evaluation factors other than cost or price, when combined, are significantly more important than, approximately equal to, or significantly less important than cost or price.

Past performance will be evaluated in accordance with FAR 15.305.

Draft Non-Price Factor – Corporate Experience

RELEVANT PROJECT EXPERIENCE

Submit a minimum of one (1) to a maximum of five (5) construction projects completed in the past ten (10) years that best demonstrates your experience on Water Treatment Plant (WTP) projects that are similar in size, scope, and complexity. For the purposes of this evaluation, a relevant project is further defined as:

Size: Similar Size: Projects demonstrating new construction, retrofit, or expansion of Water Treatment Plants (WTP) or Wastewater Treatment Plants (WWTP) with a total construction value of $10,000,000 or greater.

Scope: Projects demonstrating new construction, retrofit or expansion of one (1) or more water treatment facilities with a rated design capacity of 2.0 million gallons per day (mgd) or larger.

Complexity: Projects demonstrating experience furnishing, installing, and commissioning programmable logic controller (PLC) based water or wastewater treatment plant supervisory control and data acquisition (SCADA) systems.

NAVFAC Draft Non-Price Factors – Corporate Experience - Continued Additionally, offerors that clearly demonstrate the following experience, in addition to meeting the Size and Scope as defined above, by means of providing sufficient evidence may be considered more favorably than those that do not:

WTP projects that have a rated finished water design capacity greater than 4.0 million gallons per day (MGD).

Projects that employ membrane filtration technology. For the purposes of this solicitation, membrane filtration is defined as a pressure- or vacuum-driven separation process in which particulate matter larger than 1 micron is rejected by an engineered barrier.

Construction of a Restricted Crossing U-Turn (RCUT) intersection.

Construction/installation of medium-voltage electrical distribution systems.

Construction/installation of marine outfalls.

Integrating PLC based SCADA systems with existing infrastructure.

JUN 2019

Question and Answer Panel George Sparrow, PE Project Manager NAVFAC MIDLANT Christopher Schmitt, PE Design Manager NAVFAC MIDLANT Phil Cole Supervisory Contract Specialist, Contracting Officer

NAVFAC MIDLANT

Jarrett Selig, PE Design Manager Jacobs Engineering Group, Inc.

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