2023 MARAD Shipboard Chemistry Program - Performance Work Statement - FINAL.docx

Contents

1.0 General

1.1 Background

The U.S Maritime Administration (MARAD) is an agency of the United States Department of Transportation (DOT). As outlined in the Merchant Marine Act of 1946, the Secretary of Transportation, acting through MARAD, is required to maintain a National Defense Reserve Fleet (NDRF), including any ship assigned by the Secretary to the Ready Reserve Force (RRF) component of the Fleet.

Consistent with that purpose, MARAD has developed strategic goals, including the following:

1. Strategic Goal #1: Supporting U.S. Maritime Capabilities, meaning to strengthen and ensure the safety, security, and efficiency of maritime capabilities that are essential to U.S. economic and national security.

1. This includes an accompanying long-term objective:

1. Continue to ensure ready availability of ships, training billets, crews, and strategic ports.

The RRF, and the surge sealift capacity that it provides, is the method that MARAD will support the Department of Defense warfighting capabilities. Accordingly, MARAD will maintain RRF ships in accordance with the readiness level promulgated by the DoD’s Functional Combatant Commander, the U.S. Transportation Command (USTRANSCOM), enabling activation to Full Operating Status (FOS) within the prescribed timeline and sustained operations at designated parameters for up to 180 days.

Presently, the RRF fleet consists of approximately 50 ships located at various ports throughout the United States on the Atlantic, Gulf and Pacific Coasts. Included in this number are training ships for the nation’s Maritime Academies, and two ships supporting the Missile Defense Agency (operated similarly to the RRF). We anticipate several additional ships to be added to the fleet in the near future.

The United States Department of Transportation’s Maritime Administration (MARAD) requires products and services for providing shipboard chemical treatment of various shipboard systems as described herein. The Government is contracting not only for specific products and services, but also for the delivery of these products and services, both within the continental United States and at ports worldwide, within specific time constraints defined by the contract.

The Contractor shall provide products and services, with the possibility of worldwide basis, for MARAD ships, and for other government owned assets, as directed by MARAD. Service under the scope of this contract includes engineering support services (e.g. service calls, training, laboratory analysis), technical evaluation, and troubleshooting services. The Contractor agrees to deliver the products and services set forth in this Contract when ordered by the Government or Ship Managers in accordance with the Contract terms and conditions.

1.2 RRF Program

MARAD's programmatic responsibilities for maintenance and operation are assigned to the Ship Operations and Maintenance Officers (SOMOs) in each MARAD Area Division. These Area Divisions are in the following locations: Division of Atlantic Operations (DAO) - Norfolk, Virginia; Division of Gulf Operations (DGO) - New Orleans, Louisiana; and Division of Pacific Operations (DPO) - Oakland, California. The SOMOs execute the management and operation of RRF ships and other ships operated by Ship Managers and/or General Agents who are under contract to MARAD and are directly responsible for performing the program/phase technical requirements for their cognizant ships. A listing of individuals with their name, title, phone and cell number will be provided within five (5) business days from the NTP.

The RRF maintenance and repair program incorporates regularly scheduled maintenance activations to conduct dock and/or sea trials. The frequency with which these activations occur is based on the assigned Readiness Status (R-Status) for each ship. Some of these maintenance activations are done in conjunction with program "No-Notice" Turbo Activations. Others may be done as "Notice" Activations in support of a scheduled Military Exercise.

1.3 NDRF/RRF Ships

Ships in the NDRF/RRF are of various designs and classes and of both U.S. and foreign construction. Ships are acquired from various sources; i.e. transfer from the U.S. Navy, upgrades from the National Defense Reserve Fleet (NDRF), or direct purchase from U.S. or foreign ship owners and operators.

In addition to the RRF, MARAD also maintains and operates school ships for the various Maritime Academies and special mission ships for the Missile Defense Agency. Ships included are those that are assigned to the RRF/NDRF and any other ship in which the Maritime Administration maintains an interest (i.e. training ships and special mission ships). See list of ships in Appendix A: Ship Characteristics.

1.3.1 Ship Types

The mix of ships (types and numbers) within the RRF is dictated by the Department of Defense. As of early 2023, there are (47) ships in the RRF, of the following types:

4) (9) Training Ships

5) (2) Special Purpose Ships (MDA)

1.3.2 Ship Propulsion

The propulsion plants for the RRF and other ships are listed below:

· Gas Turbine – 1

· Diesel Propulsion (Medium and Low Speed) – 33

· Diesel Electric - 4

· Steam Turbine – 20 The tables provided in Appendix A contain specific information about the propulsion and auxiliary equipment, including capacities, installed onboard these ships.

1.3.3 Ship Locations

RRF/NDRF ships may be physically located at one (1) of three (3) MARAD - NDRF sites or berthed at one of several layberths locations throughout the East, Gulf, or West Coasts of the U.S.

In general, ships are placed in Reduced Operating Status (ROS) with partial crews. All others are in laid-up status at the NDRF fleet sites. It is possible that several RRF ships may be pre-positioned in the Far East, Middle East, Europe, or elsewhere.

See attached “Ship Characteristics” for a listing of current RRF ships, types of propulsion systems, etc. This list of ships is not all-inclusive and is subject to change throughout the life of the contract.

1.4 General Requirements

The chemical products, dosing equipment, and analytical supplies shall comply with the requirements listed below:

· In accordance with the dosing instructions, all chemical products must comply with all applicable laws regarding pollution from ships and the Vessel General Permit.

· Electrical Equipment must be able to support 120 VAC or 240 VAC and 60 cycle service.

· Analytical supplies used to monitor chemical levels should minimize hazardous materials while maintaining simplicity of use for operators.

1.5 Glossary of Terms Used in the Performance Work Statement

The following definitions apply to the terms used in this Performance Work Statement:

2.0 Chemical Products

2.1 Boiler Chemical Treatment

2.1.1 Propulsion and Auxiliary Boilers

2.1.1.1 High Pressure Propulsion Boilers

The Contractor shall provide boiler (pH control, corrosion inhibitors, and scale preventer) and condensate treatment systems for propulsion boilers operating over 59 bar. High pressure boiler treatment systems shall use a coordinated phosphate treatment system with use of hydrazine as a volatile oxygen scavenger.

2.1.1.2 Medium Pressure Propulsion Boilers

The Contractor shall provide boiler (pH control, corrosion inhibitor, and scale preventer) and condensate treatment system for propulsion boilers operating between 40 to 59 bar. Medium pressure boiler treatment systems may use either a hydrazine or a non-hydrazine oxygen scavenger.

2.1.1.3 Auxiliary Boilers

The Contractor shall provide boiler (pH control, corrosion inhibitor, and scale preventer) and condensate treatment system for auxiliary boilers operating between 2 to 17 bar that complies with CFR, Title 21, Part 173.310. These boiler treatment systems shall use a non-hydrazine oxygen scavenger.

2.1.2 Deionized Water

The contractor shall provide deionizing equipment to MARAD ships within CONUS. These distilled water units shall have the capacity of processing a minimum of 100 metric tons per day of shore potable water, providing a maximum conductivity of 10 μS, a maximum of 1 ppm Chloride, and a maximum of 2 ppm Silica. In-stream monitoring shall be available to stop flow whenever conductivity exceeds 1 ppm Chloride. These processing units will be made available within 48 hours, when required, and will remain on-site to support the activation period (minimum of 3 days up to the option of 14 days) of ships.

2.1.3 Shipboard Ion-Exchange Resin

The Contractor shall provide replacement resin, comprised of both carbon and mixed resin, for Ion-Exchange equipment permanently installed onboard ships. Indications of resin exhaustion from either in-stream monitoring or flow totalizer must not be impeded by replacement of resin.

2.1.4 Boiler Sludge Conditioner/Pre-Cleaner for Layup

The Contractor shall provide a boiler sludge conditioner that can be used in high, medium, and low-pressure boilers that prevents hardness scale, sludge, or iron oxides from adhering to interior boiler surfaces. This product shall assist in causing solids to remain in suspension with boiler water, so that they can be removed as the boiler is drained. The purpose of this product is to treat the boiler prior to securing so that the suspended solids can be removed from the boiler prior to laying up the boiler for an extended period.

2.1.5 Boiler Oil Coagulant for Oil Contamination

The Contractor shall provide a product capable of coagulating oil contamination that may enter the boiler from leaking heating coils in fuel oil or lubricating oil tanks and heat exchangers. This product shall not impede removal of oil via surface blowdown.

2.1.6 Boiler Dry Lay-up Corrosion Inhibitor

The Contractor shall provide a product that acts as a Vapor Phase Corrosion Inhibitor for use in placing propulsion and auxiliary boilers in a dry lay-up condition. Desiccants are not an acceptable substitute.

2.2 Cooling Water Systems

2.2.1 Diesel Engine Cooling Systems

The Contractor shall provide both nitrite and non-nitrite based cooling system treatments. The treatment shall have pH controls and corrosion inhibitors that minimize corrosion in diesel engine cooling systems. Additionally, the chemical treatments shall prevent scale formation and corrosion from minor levels of contamination when hardness is maintained below 120 ppm and Chlorides are maintained below 80 ppm. The treatment chemical shall be compatible with ethylene glycol. Whenever possible, the treatment chemicals should meet OEM specifications.

2.2.1.1 Emergency and Auxiliary Diesel Engine Nitrite-Based Jacket Water Coolant The Contractor shall provide nitrite-based coolant treatment that minimizes corrosion between the dissimilar metals such as iron, aluminum, bronze, copper/nickel, and copper found in jacket water cooling systems used in high-speed and medium-speed diesel engine cooling systems. This treatment must be buffered to control normal makeup pH variances.

2.2.1.2. Propulsion Diesel Engine Nitrite-Based Central Cooling Water System The Contractor shall provide a low-speed and medium-speed diesel engine nitrite-based coolant chemical treatment system that provides corrosion protection for these engines that do not have copper/nickel and aluminum lube oil and inlet air coolers. This treatment must be buffered to control normal make up pH variances.

2.2.1.3 Auxiliary and Emergency Diesel Engine Non-Nitrite Jacket Water Treatment and Antifreeze The Contractor shall provide a combined non-nitrite cooling system treatment that provides both corrosion inhibitors, and freeze protection using ethylene glycol. The primary use of this product will be for high-speed (35-450 horsepower diesel) life boats, rescue boats, forklifts, and emergency diesel engines. Due to the large number of engines using aluminum components, the proposed product shall provide protection to minimize the effects of electrolysis and maximize corrosion protection for the combination of aluminum, iron, copper, and copper/nickel materials used in these engines. This treatment shall be buffered to control normal makeup pH variances.

2.2.1.4 Propulsion Engine Non-Nitrite Treatment

The Contractor shall provide a low-speed and medium-speed diesel engine non-nitrite coolant treatment that provides corrosion and scale protection for engines containing aluminum, copper/nickel, or lube oil and inlet air coolers containing aluminum. This treatment must be buffered to control normal makeup pH variances.

2.2.2 Chill Water Cooling System Non-Nitrite

The Contractor shall provide a chill water cooling system corrosion inhibitor that contains no chromates or nitrites. The chemical shall contain proven anti-corrosion inhibitors to prevent the effects of electrolysis in systems containing multiple dissimilar metals, such as aluminum, copper, copper/nickel, iron, and stainless steel. The chemical shall also be compatible with ethylene glycol.

2.2.3 Ethylene Glycol Anti-Freeze

The Contractor shall provide ethylene glycol anti-freeze to protect engine, central cooling water, and chill water systems down to -30°F.

2.2.4 Closed-Loop Cooling System Biocide

The Contractor shall provide a closed-loop biocide that prevents aerobic and anaerobic bacteria, fungus, and algae growth in chill water and diesel engine cooling systems. Additionally, the Contractor shall provide a biocide capable of shock treatment of closed loop cooling systems. The biocides shall be compatible with both the nitrite and non-nitrite based cooling system chemicals provided by the Contractor. As per Federal law, this product must have Environmental Protection Agency registration for the intended application as a closed-loop biocide.

2.3 Evaporator Feed Treatment System

The Contractor shall provide a scale prevention and anti-foaming treatment system for moderate and high temperature flash-type evaporators. Evaporators are classified as moderate temperature evaporators when the feed heater inlet temperature is 90 °C or less. Evaporators are classified as high temperature when the feed heater temperature is greater than 90 °C. The proposed treatment systems shall be approved by the National Sanitation Foundation (NSF).

2.3.1 Moderate-Temperature Evaporators

The Contractor shall provide a treatment system that will prevent scaling and foaming of the saltwater injection system within moderate temperature flash-type evaporators. The proposed treatment shall prevent the formation of calcium and magnesium carbonate scale within the evaporator seawater feed heater and shell plates.

2.3.2 High-Temperature Evaporators

The Contractor shall provide a treatment system that prevents calcium and magnesium carbonate, and calcium and magnesium sulfate scale in high temperature flash-type evaporators operating in excess of 90°C.

2.3.3 Descaling Compound

The Contractor shall provide an inhibited compound with pH color indicator that will remove calcium and magnesium carbonate deposits from the seawater side of evaporator heat exchangers and evaporator shells. The pH indicator is intended to provide a visual indication of when the descaling compound is no longer effective in the descaling of the components or system being cleaned. If an acid is utilized as a descaling compound, then the Contractor shall also provide a neutralizer. Due to the copper/nickel materials used in evaporator construction, phosphoric acid formulations are unacceptable. Sulfamic and citric acids are acceptable.

2.3.4 Seawater Anti-Fouling Dispersant

The Contractor shall provide a saltwater dispersant that is approved for use in sea chest and saltwater cooling systems. The chemical shall not have any prohibition for use within the territorial waters of the U.S. exclusive of the inland waterways. The chemical shall prevent adhesion of bio-growth on all surfaces of seawater cooling systems. This product shall be allowed to be discharged overboard by the Environmental Protection Agency’s Vessel General Permit.

2.3.5 Seawater Cooling System Biocide

The Contractor shall provide a biocide that will kill bacteria, fungi, and barnacle larvae inside saltwater heat exchangers operating in international waters. This product shall be allowed to be discharged overboard by the Environmental Protection Agency’s Vessel General Permit.

2.3.6 Reverse Osmosis Purifying System

The Contractor shall provide a deposit control chemical designed to control scale formations in reverse osmosis (R/O) filters within purifying systems. The product shall be NSF Standard 60 certified as an R/O anti-scalant.

2.3.6.1 Reverse Osmosis Preservation

The Contractor shall provide a membrane preservative for treating the R/O unit membranes when not in use.

2.3.6.2 Reverse Osmosis Scale Remover

The Contractor shall provide an R/O cleaner designed for rapid, aggressive removal of metal oxides and secondary mineral scale.

2.3.6.3 Reverse Osmosis Organic Cleaner

The Contractor shall provide a scale removing compound that safely and effectively removes a variety of foulants including mineral scales, such as calcium carbonates, phosphates, and sulfates; hydrated oxides, such as iron, copper, and nickel oxides; mixed colloids, such as iron, organics, and silicates; organic deposits and bacterial fouling from R/O membranes.

2.4 Maintenance Cleaners

The Contractor shall provide shipboard general use and equipment cleaners as specified in the sections below:

All cleaning products shall have a minimum flash point greater than 60°C.

2.4.1 General Purpose Cleaner

The Contractor shall provide a water-based general purpose cleaner that shall be a blend of detergents and wetting agents, non-flammable, bio-degradable, and suitable for use in habitability spaces, galley areas, and topside decks.

2.4.2 Engine Room Degreaser

The Contractor shall provide an Engine Room Degreaser that can remove carbonized oil and greases from machinery equipment surfaces in addition to normal dirt and grime found in a marine engine room environment. The proposed product must be tested and pass the Emulsion Separation Test per IMO MEPC/Circ 289 and be generally compatible with Oily Water Separators. The product shall contain no chlorinated solvents, carcinogens, or surfactants. The intended use of this product is for cleaning engine room deck plates, tank tops, machinery surfaces, and bilges.

2.4.3 Bilge Water Demulsifier

The Contractor shall provide a chemical that is quick breaking on all types of hydrocarbons, greases, and fats normally found on deck and in the bilge water allowing the water to separate from the emulsion aiding the process of oily water separation. The proposed product must be tested and pass the Emulsion Separation Test per IMO MEPC/Circ 289 and be generally compatible with Oily Water Separators.

2.4.4 Deck Cleaner

The Contractor shall provide a neutral cleaner used for cleaning cargo vehicle stowage decks and heavily soiled topside decks. The cleaner shall be capable of removing mineral and synthetic greases and oils from the painted or non-skid coated surfaces without degrading the surface coating.

2.4.5 Electric Motor and Electric Parts Cleaner

The Contractor shall provide a high dielectric strength, non-chlorinated electric component cleaner, which is non-corrosive to the metals, such as aluminum, iron, and copper normally found in propulsion and auxiliary motors, and associated electrical equipment (except solid state circuitry). The cleaner shall be compatible with Class “F” and Class “H” electrical motor wire insulation varnish. The product shall also have a high dielectric strength and be capable of being safely applied to large motors, generators, and electrical components found in electric control cabinets, such as electrical brushes, contacts, and terminal boards.

2.4.6 Diesel Air Cooler Cleaner

The Contractor shall provide a hydrocarbon based cleaning agent which is non-abrasive, contains no chlorinated solvents, and consists of corrosion inhibitors and detergents which can be readily mixed with fresh/distilled water or used in situations when cleaning inlet air coolers both online and offline. The cleaner shall not oxidize or corrode aluminum, copper alloy, composite nickel-chromium, and iron materials.

2.4.7 Diesel Engine Jacket Water System Cleaner

The Contractor shall provide a water-based cooling system in-line cleaner that can be used when diesel engines are in operation, but not necessarily loaded. The cleaner shall remove, at a minimum, rust, magnesium/calcium scale, and light mineral and synthetic engine oil accumulation. The cleaner shall be compatible with gasket materials normally used by diesel engine manufacturers. The product shall not corrode aluminum, brass, copper, mild steel, and stainless steel components and shall have corrosion inhibitors to prevent flash rusting of the cooling system after cleaning is complete.

2.4.8 Purifier Disc Cleaner

The Contractor shall provide a cleaner to clean separator discs from both the lube oil and fuel oil system purifiers. The cleaner shall be suitable for cleaning stainless steel and non-ferrous metal parts. Phosphoric acids are acceptable. The product shall contain no chlorinated hydrocarbons. In those cases, where the OEM does not certify chemicals by specific brand name, the Contractor shall provide a product that meets the OEM chemical specifications.

2.4.9 Turbine Water Wash Detergent

The Contractor shall provide a detergent for water washing of gas turbines. The product shall be approved by General Electric for use water washing LM2500 gas turbines.

2.4.10 Carbon Remover

The Contractor shall provide a high solvency carbon cleaner that contains no chlorinated solvents. The primary purpose of this product is for cleaning carbonized organic and inorganic compounds from boiler burner tips and diesel engine fuel oil injectors.

2.4.11 Rust Stain Remover (RSR)

The Contractor shall provide an RSR which has a phosphoric acid base for removal of surface running rust (alpha hematite). The product shall also have an emulsifier and passivator to aid in cleaning and passivating the surfaces with which it comes into contact. The product shall be compatible with ferrous metals.

2.5 Fuel Systems

2.5.1 Soot Combustion Catalyst

The Contractor shall provide combustion catalysts for use in marine boilers, waste heat systems, and 6 to 9 bar auxiliary boilers. Medium/High temperature catalyst shall aid in the removal of soot deposits with operating temperatures of approximately 200-600°C.

2.5.2 Fuel Oil Conditioner

The Contractor shall provide a fuel oil stabilizer with dispersants and detergents that stabilize oxidation products found in distillate and residual fuel. This product shall maintain a homogeneous mixture when fuel stability exceeds 3.0 on ASTM D5304 and improve combustion in both distillate and residual fuels.

2.5.3 Fuel Oil Biocide

The Contractor shall provide a biocide designed to eliminate bacteria and fungus growth in fuel tanks and associated piping systems living at the fuel/water interface. As per Federal law, this product shall have EPA registration for the intended application as a biocide.

2.5.4 Combustion Improver/Deposit Modifier

The Contractor shall provide a deposit modifier, slag preventative, and corrosion inhibitor for use with residual fuel (ISO 8217:2005 RME and RMG).

2.5.5 Low Sulfur Diesel Fuel Oil Lubricity Additive

The Contractor shall provide a fuel oil additive that prevents cylinder and piston ring wear in low sulfur fuel, conditions the fuel, and contains detergents that maintain fuel systems cleanliness. The product shall meet the maximum wear scar performance criteria of 460 μm as per requirements of ASTM D6079-04.

2.6 Potable Water Systems

The Contractor shall provide potable water chemical systems for treatment of potable water manufactured from evaporators and reverse osmosis systems.

2.6.1 Potable Water System Corrosion Inhibitor

The Contractor shall provide a NSF approved corrosion inhibitor that will prevent potable water system corrosion.

2.6.2 Potable Water Treatment

The Contractor shall provide NSF approved bromine and chlorine potable water treatment chemicals. The chemicals shall be capable of being injected into the distillate output prior to entry into the ship’s potable water tanks. The chemical shall be packaged in a container that allows for air shipment and prevents spoilage onboard a ship.

2.7 Gray Waste and Black Waste Water Systems

The Contractor shall provide chemical treatment and injection systems for the treatment of ship’s gray water and sewage treatment systems including the sewage drain lines.

2.7.1 Sewage and Organic Waste Treatment

The Contractor shall provide waste degrading bacteria that reduces waste and prevents sludge buildup in sewage holding tanks, vacuum tanks, and associated equipment. The product shall be compatible with drain treatment enzymes provided by the Contractor for use in the piping systems and the CHT / Type II MSD. In those cases, where the OEM does not certify specific chemicals, the Contractor shall provide a product that meets the OEM chemical specifications.

2.7.2 Sewage Effluent Disinfectant (Sodium Hypochloride)

The Contractor shall provide an 8.5% or 15% Sodium Hypochloride concentration liquid.

2.7.3 Sewage Treatment System Defoaming Agent

The Contractor shall provide a sewage treatment system defoaming agent to reduce the surface tension of the organic material being processed and prevent foaming. This product shall not inhibit biological activity in MSD and CHT systems.

2.7.4 Shipboard Waste System Drain Treatment System

The Contractor shall provide a biological enzyme that attacks and degrades Uric Acid in low water usage sanitation or vacuum sewage systems. This product shall also minimize scale and sludge formation in black and grey water drainage piping systems. The product shall contain no acids or caustics. The product shall also promote and sustain optimal biological activity in MSD and CHT systems. In those cases, where the OEM does not certify chemicals, the Contractor shall provide a product that meets the OEM chemical specifications.

2.7.5 Shipboard Drain Cleaner

The Contractor shall provide a drain cleaning agent suitable for the shipboard environment to remove clogs in gray water and black water drain lines due to organic substances, such as hair or grease.

2.8 Corrosion Inhibitors

The Contractor shall provide Corrosion Inhibitors that are compatible with the systems listed below. Whenever possible, the products shall meet OEM specifications or technical bulletins.

2.8.1 Turbine Lubricating Oil Corrosion Inhibitor

The Contractor shall provide a Corrosion Inhibitor that is compatible with lubricating oil systems on propulsion turbines. If possible, this product shall be a Vapor Phase Corrosion Inhibitor.

2.8.2 Diesel Engine Lubricating Oil Corrosion Inhibitor

The Contractor shall provide a Corrosion Inhibitor that is compatible with lubricating oil systems on diesel engines. If possible, this product shall be a Vapor Phase Corrosion Inhibitor.

2.8.3 Hydraulic Oil Corrosion Inhibitor

The Contractor shall provide a Corrosion Inhibitor that is compatible with hydraulic oil and controllable pitch propeller systems. If possible, this product shall be a Vapor Phase Corrosion Inhibitor.

2.8.4 Electronic Enclosure Corrosion Inhibitor

The Contractor shall provide a Corrosion Inhibitor that is designed for use in electronic enclosures. Electronic enclosures may range in size from 0.5 m3 to over 10 m3, and a variety of sizes or dose should be available. If possible, this product shall be a Vapor Phase Corrosion Inhibitor.

2.8.5 Ballast Water Corrosion Inhibitor

The Contractor shall provide a Corrosion Inhibitor that is compatible with fresh water and sea water tanks to prevent the corrosion of carbon steel surfaces. This product shall be allowed to be discharged in accordance with the Environmental Protection Agency’s Vessel General Permit.

2.8.6 Spare Part Preserver

The Contractor shall provide a series of products to prevent corrosion for the long-term storage of spare parts. If possible, this product shall be a Vapor Phase Corrosion Inhibitor.

2.9 Chemical Cleaning Products

2.9.1 Chemical Cleaning Circulating Pump and Tank Set

The Contractor shall provide an air driven pump circulating system (and associated spare parts) that shall be used in the process of cleaning heat exchangers, cooling systems, and evaporators with acids and alkaline cleaners. The entire system shall be corrosion resistant to both alkaline and acid solutions. The pump shall have shall have a capacity between 6 and 10 liters per minute.

2.10 Injection/Metering/Dosing Systems

2.10.1 Boiler Water and Evaporator Injection Equipment

The Contractor shall provide boiler treatment injection equipment for High, Medium, and Low-pressure boilers and evaporator injection equipment. The Injection system shall consist of a pump(s), tank(s), and metering capability. The metering pump shall be adjustable from zero to 4.5 liters/hours (minimum). The Injection System shall minimize odors from entering the work space. Additionally, the system shall meet the following requirements:

· Power Supply: 100-230 VAC

· Max Output Pressure: 16 bar

· Tank Capacity: 60 liters (minimum)

· Sensor and Shutdown: Low chemical level

2.10.2 Seawater Injection Systems

The Contractor shall provide an injection system capable of injecting saltwater dispersant and/or biocide treatment chemical into saltwater cooling water systems. The injection system shall consist of a pump(s), tank(s), and metering capability. The system shall be capable of being programmed for 24-hour operation and have automatic shutdown capability. The chemical pick-up tube shall be capable of being affixed to the container of the chemical being used. Each injection point shall be capable of being timed for a minimum of one hour. The injection rate at the designated sites must meet maximum chemical dosage rate of the chemical. Additionally, the system shall meet the following requirements:

· Power Supply: 100-230 VAC

· Max Output Pressure: 4 bar

· Max Discharge Quantity: 17 liters/hour

· Tank Capacity: 100 liters (minimum)

· Sensor and Shutdown: Low chemical level

2.10.3 Eductor Dosing Systems

The Contractor shall provide an injection system that is capable of metering chemicals for introduction to a system by using an eductor. This system shall include flow meters and throttling valves, to allow for the adjustment of flow rate. The Contractor may suggest this system be used as an alternative for systems that are non-critical or require minimal chemical treatment.

2.11 Meters and Test Kits

The Contractor shall provide meters and test kits to manage chemical treatment of all systems for chemicals provided, monitor effluent discharged from the ship, and ensure potable water is safe for consumption. Wherever possible, the Contractor shall minimize the use of hazardous materials.

2.11.1 Meters

The following meters shall be provided under this contract:

2.11.1.1 Conductivity meter that measures neutralized conductivity on boiler water samples and other types of water. The meter shall be able to conduct at least 365 tests per year per ship.

2.11.1.2 pH meter that measures pH in makeup water, feed water, boiler water, cooling water, potable water, and waste water. The meter shall be able to conduct at least 730 tests per year per ship. The meter shall also be portable, water resistant, and measure full scale pH (0.0 – 14.0) at ±0.1 pH accuracy.

2.11.2 Kits

The following test kits shall be provided under this contract:

2.11.2.1 Low range chloride test kit with 1 to 100 ppm range and ±1 ppm accuracy.

2.11.2.2 High range chloride test kit with a range up to 500 ppm with a ±10 ppm accuracy.

2.11.2.3 Silica test kit with a minimum of ±1 ppm accuracy.

2.11.2.4 Hardness test kit measuring between 20 to 200 ppm with ±5 ppm accuracy.

2.11.2.5 Phosphate reserve test kit in ppm meeting the operational control limits proposed by the Contractor.

2.11.2.6 Oxygen scavenger test kit in ppm meeting the operational control limits proposed by the Contractor.

2.11.2.7 Nitrite cooling water test kit meeting the operational control limited proposed by the Contractor.

2.11.2.8 Non-Nitrite cooling water test kit meeting the operational control limits proposed by the Contractor.

2.11.2.9 Seawater dispersant test kit meeting the operational control limits proposed by the Contractor.

2.11.2.10 Potable water test kit capable of testing reserve bromine or chlorine.

2.11.2.11 Potable water test kit capable of testing fecal coliform and E. coli.

2.11.2.12 Biological cooling water test for the presence of aerobic bacteria fungi in cooling systems.

2.11.3 Supporting Equipment

2.11.3.1 Test Cabinets: The Contractor shall provide a test cabinet enclosure assembly, suitable for the shipboard environment, and capable of safely storing sampling equipment, meters, test kits, and chemical reagents. At least one option of the test cabinets shall include internal lighting to aid in the execution of chemistry testing.

2.11.3.2 Lab Equipment: The Contractor shall provide all assorted laboratory equipment, such as test tubes, graduated cylinders, beakers, glass stirring rods, and casseroles dishes, which will be necessary to perform all chemistry tests required by the chemistry program that the Contractor will be overseeing. Wherever possible, substitutions should be made for materials that are less likely to be damaged in the shipboard environment.

2.11.3.3 Sample Cooler: The Contractor shall provide a sample cooler model(s) for safe and effective sample collection of boiler and feedwater samples from propulsion and auxiliary boilers. The cooling source will either be potable water or an existing fresh water cooling loop.

3.0 Personnel

3.1 Key Personnel

3.1.1 Key Personnel Minimum Qualifications

The Contractor shall provide a Program Manager and a Technical Manager. Resumes for personnel in these positions shall be submitted.

3.1.1.1 Program Manager

The program manager shall have a minimum of a Bachelor of Science degree in Marine, Mechanical, or Chemical Engineering and five (5) years of relevant experience.

3.1.1.2 Technical Manager

The technical manager shall have a minimum of five (5) years of experience in the chemistry control of ships and/or power plants.

3.2 Substitution of Key Personnel

The key personnel (Program Manager and Technical Manager) will be evaluated by the Contracting Officer or his/her authorized representative. All requests for substitutions must provide a detailed explanation of the circumstances necessitating the proposed substitution.

3.3 Other Personnel

3.3.1 Other Personnel Minimum Qualifications

The Contractor shall provide field service engineers, lab scientists, and a customer service representative(s).

3.3.1.1 Field Service Engineer

The field service engineer shall have either a Bachelor of Science degree in Chemical, Marine, Mechanical, or Electrical Engineering, or two (2) years of experience as a chemical field service engineer or shipboard engineer.

3.3.1.2 Lab Scientist(s)

The Contractor shall provide the services of lab scientist(s) with a Master of Science degree in Chemistry, Biology, Chemical Engineering, or an equivalent field acceptable to the Government.

3.3.1.3 Customer Service Representative

The Contractor shall provide customer service representative(s) with a H.S. diploma and a minimum of two (2) years of experience in the chemical marine field involving management of customer service functions.

4.0 Support of the Program

4.1 Staff Support of the Program

The Contractor shall provide engineering support, training, and quality assurance to ensure the chemicals and equipment provided under the Contract are properly used and maintained. Support shall include engineering personnel, technical field and training material development, and laboratory support on an as needed basis. Specific requirements are outlined in the following paragraphs.

4.1.1 Program Manager

The Program Manager is responsible for the overall management of the contract. The Program Manager shall be the single point of contact for all matters pertaining to the performance of the contract. The Program Manager is expected to be available during working hours and respond to requests/inquiries in a timely manner. The Program Manager shall keep MARAD informed of all changes to any domestic or foreign environmental requirements that affect the products and services provided under this contract. All recommendations for substitution of personnel as defined by the contract shall originate from the Program Manager. The Program Manager shall have the authority to direct all field offices to fulfill contract requirements.

4.1.2 Technical Manager

The Technical Manager is responsible for all matters pertaining to chemicals, test equipment, and technical training provided under this contract. The Technical Manager shall have a cell phone and shall be available 24 hours a day / seven (7) days a week. The Technical Manager is responsible for reviewing ship chemical logs, service call reports, technical reports, and providing guidance and comments to correct any deficiencies noted to the COR. MARAD expects that this contract will be the Technical Manager’s primary, but not necessarily, sole duty.

4.1.3 Customer Service Representative(s)

The Customer Service Representative(s) is the point of contact to process and provide status on all orders. The Customer Service Representative(s) will maintain a 24hours a day / 7 days a week tracking system on delivery requirement status. The Customer Service Representative(s) shall be able to provide the status of all requirements placed against the contract. Also, the Customer Service Representative(s) shall be available for emergency support when needed during after working hours. The Customer Service Representative(s) functions include, at a minimum, the process of receiving, processing, and tracking the status of orders placed and scheduling worldwide deliveries. The Customer Service Representative(s), or the customer service representative’s designated back-up, shall respond to phone calls, voicemails or email inquiries for information from the COR within 24 hours.

4.2 Working Hours/Business Day

Working hours and business day where referred to in this contract, unless specifically defined otherwise, are defined as 0800-1600 local time on weekdays in the location serviced, any day the U.S. Federal Government is open for business.

4.3 Training and Technical Reference Documentation

4.3.1 General

The Contractor shall update and revise all training materials, manuals, and handbooks developed during the Phase-In Services as defined in Paragraph 5.1, and when contract is modified. The Contracting Officer’s Representative will review and accept all materials prior to distribution.

4.3.2 Training Materials

The Contractor shall develop a training syllabus and training manual, tailored to steam ships, diesel ships with and without auxiliary boilers, and gas turbine power ships.

4.3.2.1 Training Syllabus

The Contractor shall prepare a syllabus to accommodate both shipboard and shoreside training. Training shall be completed in one (1) business day. The training syllabus shall address all topics identified in Paragraph 4.3.2.2 with a target audience of licensed Marine Engineers and shoreside technical support staff.

4.3.2.2 Training Manual

The training manual shall follow the Contractor’s training syllabus in format and provide additional background information for the material presented. The training manual shall also provide a section for notes and include worksheets for any activities conducted during the training.

The training manual shall address the following topics:

a) Overview of the products and services provided under this contract

b) Logistics

c) Ordering Process

d) Storage and Handling

e) Basics of Hazardous Materials

f) Disposal

g) Basic Chemistry Treatment Theory

h) Water Systems Treatment:

1) Steam

2) Cooling

3) Seawater

4) Potable

i) Fuel Treatment

j) Cleaning Chemicals

k) Electronic Ship Chemistry Logs

4.3.3 Additional Materials

4.3.3.1 Chemical CD Handbook

The Contractor shall develop CD handbooks for distribution to all the ships and selected shoreside staff. The handbook shall include the following:

a) Program Overview

1) Scope

2) Ordering Process

3) Foam Sample Procedures

b) Points of Contact

1) MARAD Staff

2) Contractor

c) Order Forms

d) Ship/Class specific Chemical Treatment Charts (see paragraph 4.3.4)

e) Products

1) Specific details of proper operation, dosage, and use of all test kits, equipment, and chemicals provided

2) Chemical Treatment Theory

f) Product Technical Data Sheets

g) Safety Data Sheets for all products offered under this contract

h) Technical Bulletins

i) Electronic Ship Chemistry Logs (see paragraph 4.3.5)

j) Chemical Storage Charts (see paragraph 4.3.6) The Government can provide the Contractor with the existing handbook as a guide during Phase-In Services.

4.3.4 Chemical Treatment Charts

The Contractor shall maintain a spreadsheet that will list all systems requiring chemical treatment, the recommended treatment chemicals, recommended storage quantities, and the test kits required. The chemical charts shall include only items provided under this contract. The Chemical Treatment Charts will be distributed as part of the Chemical CD Handbook.

4.3.5 Electronic Ship Chemistry Logs

Electronic Logs will need to be provided to the ship and have specific directions about identifying data required, submission requirements, where Electronic Logs are to be sent, and any specific details regarding log number schemes, etc. The Contractor shall provide a separate Electronic Log for either each class of ship or individual system being treated. These logs should be capable of online submission via e-mail or portal. The Electronic Logs will be distributed as part of the Chemical CD Handbook.

4.3.6 Chemical Storage Charts

Chemical Storage Charts will need to be provided to the ship and have specific directions on how the chemicals are to be stored. The chemical storage chart shall include only items provided under this contract.

4.3.7 Shipboard Training

The Contractor shall provide shipboard training regarding the proper use of chemicals used onboard the ship. Start of shipboard training shall commence on the initial service call. Crew members shall be trained to use industry best practices when employing the firm’s products of services. At a minimum, training shall address the topics outlined in Paragraph 4.3.2.1. Training shall be conducted as per the approved training syllabus and be tailored to discuss issues relevant to the ship being visited. The shipboard training can be an addition to the initial and periodic service calls.

4.4 Semi-Annual Business Meetings

4.4.1 Semi-Annual Business Meetings

Semi-Annual Business Meetings will be scheduled approximately every six (6) months during the period of performance of the contract at a location and time agreed to by MARAD and the Contractor. The Semi-Annual Business Meeting shall include a review of all data and reports generated over the past half-year.

4.4.2…