Salmon City Master Plan

SALMON CITY MASTER PLAN

OVERVIEW

Completion of this phase will occur in stages. The first stage (5 kT) is planned for completion in early 2023; the second stage (10 kT) is planned for mid-2023. Once fully operational, Phase 2 will produce 15 kT.

STATUS

ADMINISTRATION

Future Phases 3-to-8, with an average production capacity of 32.9 kT per phase, will build on lessons learned from Phases 1 and 2, as well as research and development. Based on this approach the current concept for future ongrowing systems includes a modular approach connected to centralized services constructed along common corridors for power, water, wastewater, oxygen, and communications.

MECHANICAL/POWER

The modules, or pods, are independent ongrowing systems that contain fish production facilities and recirculating aquaculture systems. The Pods are intended to allow for efficient construction and highly efficient operation. The construction technique includes typical tank design to ease construction. Individual components, such as insulating tanks and providing limited head space to reduce cooling costs will help conserve energy.

FPL SUBSTATION

Phases 7 & 8 will be developed on a neighboring site.

CHEMICAL STORAGE

PERSONNEL

FISH FEED BUILDING

FUTURE CHILLER PLANT

COOLING TOWER

WATER SUPPLY

PROCESS BUILDING

WASTEWATER TREATMENT

FARMING

PHASE 1

PHASE 2

PHASE 3

PHASE 4

Phase 1 of the Bluehouse Salmon Farm is a facility with capacity to produce 10 kT of salmon. The facility includes a hatchery, a smolt plant, an ongrowing plant,a processing plant, and several other systems to support the salmon farming process.

PHASE 5

PHASE 6

ELECTRICAL DISTRIBUTION BLDG

PHASE 7

PHASE 8

GENERATOR

CHILLER PLANT

WORKSHOP & STORAGE

WATER TREATMENT

BROODSTOCK

SMOLT

WWTP

RESEARCH

GO TO “FACILITIES” FOR MORE DETAILSON DESIGN CRITERIA

Phase 1 of the Bluehouse has been completed and is currently operational.

OXYGEN PLANT

The design and construction of Phase 2A is currently underway.

PHASES

This new facility includes several centralized facilities: a chiller plant, a water plant, a wastewater plant, and oxygen production facilities.

SALMON CITY | GMP | UPDATED 09.22.22

HAZEN INTERACTIVES

FACILITIES

TIMELINE

Salmon City Grand Master Plan (GMP)

GMP DEVELOPMENT FRAMEWORK

World-Class Salmon Farming Facility

• Captures Vision & Integrates Production Plan• Strategic Plan • Conceptual Layouts• Physical Influences • No-physical Influences EndFragment

Phased Increase in Production

Qualitative

WATER SUPPLY

WASTEWATER TREATMENT

Quantitative

PERSONNEL

The GMP provides a development framework for addressing programmatic, quantitative, and qualitative aspects of Salmon City facilities and space in both the immediate and long term.

• Space Consolidation • Shared Collaborative Spaces • What, When, How Much Materials and Utilities • Handling Methods • Communication Means • Order-of-Magnitude CostsEndFragment

MECHANICAL/ POWER

Programmatic

FARMING

• Support Spaces• Accessibility Improvements• Sustainability GoalsEndFragment

WATER SUPPLY Saltwater Treatment Freshwater Treatment Aquifer Wells

WASTEWATER TREATMENT WWTP

PERSONNEL Employee Center Warehouse

MECHANICAL/ POWER Chiller Plant FPL Substation Generator

FARMING Broodstock | Feed Building Process Building | Smolt Oxygen Plant

Salmon City Grand Master Plan (GMP)

WATER SUPPLY

PERSONNEL

FARMING

MECHANICAL/POWER

WASTEWATER TREATMENT

AADF Hydraulic Retention Time

FINAL DENSITY

130

Quantity

*Per Ongrowing System

Number of Tanks per System

REPLAY TANK DESIGN

180

FEED (Kg)

Treatment Process

Wells

OVERVIEW

Concentric Tank Design

VOLUME REQUIRED (m3)

Aquifers

Skretting, a Norwegian global manufacturer and supplier of fish feed to landbased aquaculture companies, plans a new feed facility in South Miami-Dade, close to Atlantic Sapphire. The capacity of the fish feed facility will be sufficient to keep up with the growth of Atlantic Sapphire and the USA market. The plant will produce cost competitive feed that meet all the requirements of the Bluehouse Salmon while using zero marine ingredients in the diet and maintaining high levels of healthy Omega-3s in the finished product. A local feed plant will minimize the carbon footprint of transporting the feed to the facility, and is expected to cut the Company's logistics cost, and thereby its cost of production, by approximately USD 0.3/Kg HOG.

Tank Volume (each)

NEW SYSTEMS

65 m3 / 17,200 gal

Maximum Fish Density

01 (hatchery)

50 kg/m3 / 3.1 lb/ft3

Smolt

Fish Feed Plant Processing Flow

Oxygen Plant

Equalization

Click on buttons to learn more about elements in PHASE 1

Procurement of Feed Ingredients

Broodstock

Oxygen Demand @ 100 Purity

Pretreatment

Grinding

Type

Chiller Plant

Fish Feed Building

144,000

PROCESS FLOW DIAGRAM

Unit

Process Building

Value

Prestressed Concrete Tank

Smolt

-Eggs every 7 weeks (two hatches in parallel) -Super smolt feed only (SSFO) smoltification method -Appendix 1 production plan -Appendix 2 water quality requirements

Protein Skimmers with Ozone Addition (5% of flow)

LIFE CYCLE

WEIGHT CLASS (WC)

Settled solids from the clarifiers are further concentrated by belt filter presses, which contain independent thickening and dewatering sections to produce a solids "cake" for offsite disposal. Water removed by thickening and dewatering is recycled to the WWTP for further treatment.

Fixed Bed Biofilm Reactor

PHASES 4-6

PARR TANKS

03 (2-12g)

PARR WTS

Trickling Filter Degasser

PROCESSING CENTER

700

Route to Distribution Center

Return Pumps

1000

17 m3 / 4,490 gal

The International Commerce Center located in Doral, Florida serves as Atlantic Sapphire’s main distribution center. Three main routes exist to access the distribution center. Key factors for consideration in selection of the route to the distribution include time of departure as well as number of axles of the trucks as most expressways are tolled facilities.

SW 264 Street → Krome Avenue → SW 8 Street → SW 137 Avenue → SR 836

In-Line Oxygen Injectors

Water Treatment

CONTENT AREA (1800x700)

35 kg/m3 / 2.2 lb/ft3

Feet

Process Building

04 (12-54g)

PHASE 5

Dolphin Expressway at NW 137 Ave

Design Feed Capacity per System

23.5

Oxygen supply infrastructure is critical to support fish life and optimize fish growth and production output potential. This demand drives oxygen supply chain design decisions in areas including resiliency, capacity, redundancy and reliability. Prudent technology and equipment selection is pivotal to the overall economic cost structure competitive- ness of the operation including initial CAPEX and the long term OPEX costs, primarily due to energy footprint. Liquid oxygen (LOX) storage on-site provides the capability to provide oxygen to the fish during normal operation and passively during emergency periods when power is interrupted. On-site oxygen production, i.e., example Vacuum Pressure Swing Adsorption (VPSA) technology, provides reliable supply untethered by logistical transport issues. The overall strategy is to utilize an optimized combination of supply technologies as best fits the operation expansion Phases as the Grand Master Plan progresses.

PARR Several months old, develops “finger” markings

Dolphin Expressway at NW 87 Ave

100 kg/d / 220 lb/d

2000

FPL Substation

SMOLT 1-3 years old. will group and head out to sea from spawning grounds.

$0.94

Water Exchanges

Volume

Generator

3000

ADULT Spends 1-8 years ar sea before returning to spawn

$1.88

Gallons

SALMON LIFE-CYCLE

Surface Area (each)

1.7M

Workshop & Storage

An important additional component of the development is a decentralized smolt facility. An area of approximately 130,000 sql (260 ft x 500 ft) has been designated at tge Bluefouse site to house the installations of a smolt facility with ultimate capacity of 20 million smolts (100 T).

Sq. Feet

3,848

DESIGN CRITERIA

Expected Effluent TSS Concentration

Number of Systems

Mg/L

30-70

Phases 7 & 8 will be developed on a neighboring site.

Expected TSS Removal

1,720 m3 / 454,400 gal

Florida’s Turnpike at Biscayne Dr

The new chiller plant will have eight (8) new chillers, each rated for 3,000 tons output. These chillers will be identical in size, capacity, make, and model. The chillers include N+1 design and will be piped in parallel. Seven chillers will be capable of serving the chilled water loads of Pahse 1 and Phase 2. The building footprint will be sized to accommodate the eight chillers, eight chill water pumps, and both chill and cooling water piping. Cooling Towers (CT) will serve as a heat sink for chiller heat rejection. The cooling tower will be sized for 22,000 tons of heat rejection and 40,5000 gpm of cooling water flow. The cooling tower will be located next to the chiller building to reduce piping and pump costs. The CT will have 3-4 pumps to circulate cooling water to seven chillers. One to two chillers will be served by wastewater effluent to maximize energy recovery.

Flocc/Coag

Dolphin Expressway at NW 87 Ave

93 kg/m3 / 5.8 lb/ft3

Clarifiers

HOG FISH PRODUCTION

$2.80

Design Feed Capacity/System

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Pump Station

Submerged belt filter

TREATMENT PROCESS

$7.74

5,400 kg/d / 11,900 lb/d

The flocculation/coagulation tank incorporates polymer and ferric chloride to bind the smaller wastewater particles to facilitate settling. The flocculation/ coagulation tank incorporates polymer and ferric chloride to bind the smaller wastewater particles to facilitate settling.

Thickening

QUANTITY

Phases 7 & 8 will be developed on a neighboring site.

Manufacturer

Normal Diffusers

Route

Secondary Drum Filters

Emergency Diffusers

No.

First Toll

Heat Exchangers and Circ Pumps

Four 32kt modules HOG 400 tons/day 2 lines | 2 shifts 5-6 truckloads/day

Last Toll

Parameter

Phase 1 Smolt + Phase 1 Ongrowing + 1st Phase of New Smolt Facility

PRODUCTION FACILITY

Total

The transfer pump station is used to pump the wastewater effluent to the injection well pump station.

DETAIL TEXT Detail text about rhe features in the popup with pertinent information and other data.

The pretreatment building is the first step in the wastewater treatment process. Submerged belt filters are used to remove large particles from the wastewater stream.

% Solids

02 (0,18-2g)

Research Center

MOD 1

Ongrowing Side Tank Each ongrowing side-tank water treatment system is designed to treat 11,250 m3/hr (71 mgd). The WTS removes solids from the water. The water is then cooled and oxygenated before it returns to the ongrowing tanks. Waste streams go tthe WWTP and exchange water goes to the Chiller Plant for coldness recovery.

Sec

ONGROWING TANKS

ONGROWING SIDE TANK

2 times/hour

PHASE 2 | Design Criteria

Flocculation Zone (per stage)

Min

8 million smolts stocked/year 40kt biomass gain 32kt HOG harvest

HOG: Head-On Gutted

-Eggs every 7 weeks (two hatches in parallel) -Super smolt feed only (SSFO) smoltification method

Rapid Mix Tank Mixer

222 m3 / 58,800 gal

Chiller Plant

65 kg/m3 / 4.0 lb/ft3

FPL Substation

Generator

2,000 kg/d / 4,400 lb/d

Aquifers

Wells

Smolt Tanks Smolt is the stage where the salmon continue smoltification as they transition from fresh water to salt water. Salmon in the smolt system grow from 13 to 90 grams (0.5 to 3.2 ounces) before proceeding to the Post-smolt system to complete smoltification.

Saltwater

7.8-8 million smolts per year (batches every 10 weeks)

Delivery Route Map

The equalization tank allows for the equalization of intermittent flows from the fixed bed bioreactors at Phase 1. Here, waste streams are stored and conveyed to the wastewater plant at a steady flow rate as to not overload the system.

Freshwater

2024

MOD 3

Concentric Tank Design

MOD 4

Canopy

0.25

Process Building

The outermost circular structure will be the fish ongrowing portion of the tank with an effective volume of 8,000 m3.

Fish Feed Building

From the ongrowing section, the water flows towards the center to be treated in the RAS system, which with be composed of mechanical filtration units and a moving bed biofilter (MBBR), to finally be returned to the ongrowing portion by a pumping system.

Broodstock

Freshwater

Oxygen Plant

Saltwater

The clarifier is a large settling tank. The particles from the flocculation/ coagulation tank settle out at the bottom of the clarifier and are sent to the thickening/dewatering building. The clarified wastewater flows over an effluent weir and is conveyed to the transfer pump station.

PHASE 1 SMOLT

Current: 450 kg/d / 990 lb/d Future: 700 kg/d / 1,540 lb/d

Ongrowing Water Treatment System (WTS) Each ongrowing water treatment system is designed to treat 20,640 m3/hr (131 mgd). The WTS removes solids, ammonia, carbon dioxide and other fish byproducts from the water. The water is then cooled and oxygenated before it returns to the ongrowing tanks. Waste streams go to Sludge Treatment (in the future, streams go to the WWTP). Exchange water will go the the future Chiller Plant for coldness recovery.

ONGROWING WTS

7.8-8 million smolts

Mixing

Parr Tanks Parr is the stage just before the salmon begin smoltification where they transition from fresh water to salt water. Salmon in the parr system grow from 2 to 13 grams (0.071 to 0.46 ounces) before proceeding to the Pre-smolt system to begin smoltification.

QUANTITY*

2026

Extruding

Drum Filters

Generators

PHASE 2 PERMITTING PLAN

Drying

Electrical Distribution Buildings

PRIMARY ENERGY CENTER

PARAMETER

Weighing

SMOLT TANKS

Packing

VALUE

Pretreatment

POST-SMOLT TANKS

Crom

Equalization

Atlantic Sapphire hatches its fish from eggs sourced from a land-based farm in Iceland. Their ideal broodstock is reared in pure waters pumped from geothermal and freash water boreholes to create an ideal, disease-free environment. The eggs are carefully hatched into newborn, freshwater alevins with yolk-sacks, then raised into freshwater fry and parr to smolts that are ready to transition to saltwater and finally adult salmon. Salmon eat continuously and are extremely efficient growers: just 1 lb, of food results in 1 lb. of growth.

Tank Diameter

Diameter

115

EGGS Hatch in about 3 months

Side Water Depth

Research Center

ALEVIN Feeds off yolk-sac for several weeks

FRY 5-10 weeks old and swimming

Sidewater Depth

2.5 times/hour

Parr Water Treatment System The parr water treatment system is designed to treat 255 cubic meters per hour (m3/hr) (1.6 million gallons per day [mgd]). A small amount (2.1 m3/hr / 0.013 mgd) of clean water is added to offset the waste and exchange water. The water treatment system removes solids, ammonia, carbon dioxide, and other fish byproducts from the water. The water is then cooled and oxygenated before it returns to the tanks The waste streams go to Sludge Treatment (in the future they will go to the Centralized Wastewater Treatment Plant), and the exchange water will go to the future Chiller Plant for coldness recovery.

Ongrowing Tanks Comprises six (6) Ongrowing Sectors. Each Ongrowing Sector (OG1, OG2, OG 3, OG4, OG5 & OG6) consists of 6 cylindrical fish tanks, each tank 17.5 m in diameter and 7.15 m of maximum water height with a maximum operational volume of 1,720 m3 per tank, with individual water supply and discharge pipes from / to a water treatment system. The total water volume per OG Sector is 10320 m3. The Ongrowing Sectors 1 to 6 are designed for a maximum feed load of 5,400 kg per day, in order to produce Atlantic salmon up to 5,250 g weight.

PHASE

SW 280 Street → Florida’s Turnpike → SR 874 → SR 826

PHASE 6

OPERATIONAL STARTUP YEAR

CAPACITY

Module Concept 120kt HOG Production and Processing

COMMENTS

Don Shula Parkway at SW 88 St

PRELIMINARY DESIGN CRITERIA

MATURATION STORAGE

$1.53

1,200 tons of HOG storage

$5.07

Parameter

SW 280 Street → Florida’s Turnpike → SR 836

95-97%

Broodstock Building SITE RENDERING

Phase 2 Ongrowing

Oxygen Need Oxygen Need Feed Per Day Total Space Requirement Daily Water Change Max Cooling Total Installed Power

7.7 kg/hr 185.6 kg/day 236.3 kg 2,428 m2 114.7 m3 2,032.2 kW 1,022.1 kW

SUMMARY DESIGN

Processing Center The processing facility combines both primary processing, which consists of slaughtering and gutting, and secondary processing focused on filleting and some value added products. The products will be head-on gutted (HOG) salmon, fillets and value-added products stored and transported to the end market at a temperature between 0 and 2 degrees Celsius. Atlantic Sapphire uses sustainable packaging since there is no need to meet packaging requirements necessary for airfreight transportation.

AL-2

2025

Primary Energy Center Eight chillers provide cold refrigerant in a close-loop cooling system for Phase 1 heat exchangers and heating, ventilation, and air-conditioning (HVAC) units. There are three cooling loop systems: Loop A supplies the northern portion of the building (Hatchery, Start-Feeding, Parr, Pre-Smolt, and Smolt) Loop B supplies the west side of the building (Post-Smolt; Ongrowing Systems 1, 3, and 5; and the western portion of the Processing Plant) Loop C supplies the eastern side of the building (Ongrowing Systems 2, 4, and 5, and the eastern portion of the Processing Plant) Cooling water for the chillers comes from two sources: Exchange water from the water treatment systems Closed-loop Biscayne Aquifer cooling well system. There are 4 cooling water supply wells and 4 cooling water return wells. Once the future Chiller Plant is in service, it will replace in the Primary Energy Center in providing cooling for Phase 1.

Phase 3 features independent, modular ongrowing systems that integrate fish ongrowing capacity with recirculating aquaculture systems. The concentric tanks have a diameter of 43 meters and stand about 12 meters high. Each ongrowing tank will have an average annual production capacity of 1.175 kT and each Phase will have an average annual production capacity of 32.9 kT. The modular systems will be interconnected to centralized services (power, water, wastewater, oxygen, communications, etc.) constructed along common corridors.

Flocc/Coag

Filter Opening Size

2 Axle

Clarifiers

Microns

4 Axle

Post-Smolt Tanks Post-Smolt is the stage where the salmon complete smoltification before transitioning from brackish water to salt water. Salmon in the Post-Smolt Systems grow from 90 to 400 grams (3.2 to 14 ounces) before proceeding to the Ongrowing Systems.

Pump Station

500

Total Toll Amount

Ongrowing Tanks Comprises six (6) Ongrowing Sectors. Each Ongrowing Sectors (OG7, OG8, OG9, OG10, 0G11 & OG12) consist of 6 cylindrical fish tanks, each tank 17 m in diameter and 10 m of maximum water height with a maximum operational volume of 2,270 m3 per tank, with individual water supply and discharge pipes from / to a water treatment system. The total water volume per ongrowing system is 13,620 m3. The Ongrowing Sectors 7 to 12 are designed for a maximum feed load of 5,400 kg per day, in order to produce Atlantic salmon up to 5,250 g weight.

Thickening

Route 1 is the costliest route in terms of tolls; however, this route would serve as the fastest route during the morning peak hour. Route 3 is the least costly route and generally has slightly longer travel times (approximately 5 minutes more) than Routes 1 and 2 outside of the peak hours. Route 3 has the potential to incur significant delays during the morning peak hour as the intersection of SW 8 Street and SW 137 Avenue is a locally known traffic bottleneck for motorists destined for SR 836 westbound.

PHASE 9

Capacity Per Unit

Download Traffic Study

MGD

120kt/year 8 parallel filleting and proportioning lines 25 people/line/shift 2 shifts

1.6

Miami International Commerce Center

PACKING & SHIPPING

Atlantic Sapphire Bluehouse Salmon

Loading Dock

Overview provided based on design criteria + process flow diagram.

Rapid Mix Zone

PHASE 1 | Design Criteria

2027

FBL Substation

Special trucks transport HOG fish on ice

Workshop & Storage

Delivery bay

Unloading

Stage 1 Mixer

HOG on ice

Maturation

0.75

Filleting

Portioning

Stage 2 Mixer

Designed to be installed in modules

Packing

0.50

MOD 2

Stage 3 Mixer

FBL Substation

WWTP

Feed Building

Biocare

REPLAY TANK DESIGN

PHASE 6 Short description about the building and its function, etc.

The deep ongrowing tanks are crystal clear, with chilly temps the fish prefer, offer the perfect salinity, and continuously provide the salmon fresh currents to swim against.

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ADMIN BUILDING

PHASE 7 Short description about the building and its function, etc.

FBL SUBSTATION

PHASE 8 Short description about the building and its function, etc.

SEE “PHASES” AND “FACILITIES” FOR MORE DETAILS

PHASE 1 The design and construction of Phase 1 of the Bluehouse has been completed and its currently operational. Phase 1 of the Bluehouse Salmon Farm is a facility with capacity to produce 10,000KT of salmon. The facility includes a hatchery, a smolt plant, a processing plant, and several other systems to support the salmon farming process.

Land based salmon fish farming is a carefully staged process. Salmon eggs are hatched in freshwater tanks. The young salmon are raised in tanks for twelve to eighteen months. They are then transferred to larger ongrowing tanks where they grow to maturity. Atlantic Saphhire salmon is raised in an innovative, land based Bluehouse in Florida. The Bluehouse is safe, sustainable, fish-friendly, fully controlled environment where the salmon swim healthy and stress free, without antibiotics or hormones. Throughout the farming cycle, the fish are continually fed, enjoy calm surroundings, and the seasonal rhythms they need for healthy growth and swimming.

Smolt Atlantic Sapphire hatches its fish from eggs sourced from a land-based farm in Iceland. The eggs are carefully hatched into newborn, freshwater spawn with yolk-sacks, and raised into small, freshwater fry and parr, then to smolts that are ready to transition to saltwater and adulthood.

PHASE 2 The design and construction of Phase 2A is currently underway. Completion of this phase will occur in stages. The first stage (7,500 kT) is planned for completion mid-2022; the second stage (7,500 kT) is planned for mid-2023. Once fully operational, Phase 2 will produce 15,000 kT. This new facility in the northwest corner of the property includes several centralized facilities: a chiller plant, a water plant, a wastewater plant, and oxygen production facilities.

Oxygen Plant Liquid oxygen (LOX) storage on-site provides the capability to provide oxygen to the fish during normal operation and passively during emergency periods when power is interrupted. On-site oxygen productionprovides reliable supply untethered by logistical transport issues.

PHASE 3 Short description about the building and its function, etc.

Broodstock Short description about the building and its function, etc.

Process Building Short description about the building and its function, etc.

PHASE 4 Short description about the building and its function, etc.

OX PLANT

The facilities are designed to provide plenty of space to swim, dive, and jump. The design provides salmon room to range with a density ratio of 95% water, 5% fish - but their natural behavior is to school together.

Feed Building Short description about the building and its function, etc.

PHASE 5 Short description about the building and its function, etc.

100

Chiller Plant The new chiller plant will have eight (8) chillers each rated for 3,000 tons output. These chillers will be identical in size, capacity, make, and model. The 8 chillers include N+1 design and will be piped in parallel. Seven chillers will be cable of serving the chill water loads of Phase I and Phase II. The building footprint will be sized to accommodate the eight chillers, eight chill water pumps, and both chill and cooling water piping.

FPL Substation FPL is going to build a new FPL Substation on the northeast corner of the site to serve Phases 4 and beyond. FPL will bring a 22.8-kV transmission line to the new FPL Substation. 22.8-kV feeders will be provided for future phases from the FPL Substation.

Power Distribution

Power Demand

‘27

‘20

FUTURE COOLER

‘21

‘28

Power Demand

‘29

‘22

SEE “PHASES” AN “FACILITIES” FOR MORE DETAILS

Atlantic Sapphire receives 22.8-kilovolt (kV) power from Florida Power & Light (FPL). 22.8-kV power is distributed across the site from Electrical Distribution Buildings (EDBs) 1 and 2 to provide power to individual facilities. Power is stepped down to 4160-volt (V) or 480-V at each facility, as appropriate for the loads. Backup generators provide power to critical equipment during FPL power outages.

200

‘30

‘23

300

Generator Backup Generators will provide power to critical equipment during emergency situations when Florida Power & Light (FPL) power is not available. 2,000-kilowatt (kW) diesel generators will be used. The generators will product 13.2-kilovolt (kV) power which be stepped up to 22.8-kV and connected Electrical Distribution Buildings (EDBs) 1 and 2. A bulk diesel storage facility will be provided for the generators.

30 AMPS

Cooling Tower Cooling towers (CT) will serve as a heat sink for chiller heat rejection. The cooling tower will be sized for 22,000 ton of heat rejection and 40,500 gpm of cooling water flow. The cooling tower will located next to the chiller building to reduce piping and pump costs. The CT will have 3-4 pumps to circulate cooling water to seven chillers. One to two chillers will be served by the wastewater effluent to maximize energy recovery.

‘24

Power Demand

‘25

(In 000 KW)

Metric Tons

‘26

Research Short description about the building and its function, etc.

Administration Short description about the building and its function, etc.

FEED BUILDING

Workshop & Storage Short description about the building and its function, etc.

Chemical Storage Short description about the building and its function, etc.

The Grand Master Plan includes several facilities to plan for the expected increase in its number of employees as the Miami Salmon City moves towards full-scale production. Atlantic Sapphire works to ensure a safe and healthy environment for all employees. Accordingly, it relies on proactive and consistent leadership throughout the organization, providing adequate protective equipment, information, and signage in all venues. Currently, Atlantic Sapphire manages cross-facility training and knowledge exchange by educating some of its US based employees in AS facility in Denmark. This builds up competence and know-how that has been transferred to the Miami Salmon City.

3,345

Projected Ozone Demand (kg/Day)

364

(MMcf/Day)

4,000

3,026

Preliminary Ozone Demand Projection

1,109

3,000

The Bluehouse facility uses advanced water systems, which include 99% recycled and filtered water, and release no harmful toxins into ocean waters.

2,706

789

AQUIFER WELLS

1,000

2,387

Water, a key component required for the Bluehouse aquaculture system is facilitated by the unique South Florida hydrogeology that underlies the Bluehouse farm. The stratigraphy consist of confined aquifers and confining layers that provide sources of fresh water, blackish water, salt water, and a zone for disposal of aquaculture effluent.

2,000

1,748

(kg/Day)

1,428

2,067

626

2,500

AQUIFER DETAILS

1,500

500

114

SEE “PHASES” AND “FACILITIES” FOR MORE DETAILS

147

180

213

246

Freshwater Lorem ipsum dolor sit amet, consectetuer adipiscing elit, sed diam nonummy nibh euismod tincidunt ut laoreet dolore magna aliquam erat volutpat. Ut wisi enim ad minim veniam, quis nostrud exerci tation ullamcorper suscipit lobortis nisl ut aliquip ex ea commodo consequat. Duis autem vel eum iriure dolor in hendrerit in vulputate velit esse molestie consequat.

278

311

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344

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Projected Oxygen Demand (MMcf/Year)

Oxygen Demand

Ozone Demand

Projected Oxygen Demand (Tons/Day)

Preliminary Oxygen Demand Projection

‘31

‘32

Saltwater Salt water is currently supplied from two Floridan Aquifer wells. These produce water from both the Middle and Upper Floridan formations. The Middle Floridian formation is located about 2500 feet below ground surface and produces water greater than 30 ppt salinity. The Upper Floridan is located about 1200 feet BGS and produces water with salinity of 12-15 PPT.

400

(Tons/Day)

Transfer Pump Station

PRETREATMENT

2025

Thickening/Dewatering

EQUALIZATION

2026

Pretreatment The pretreatment building is the first step in the wastewater treatment process. Submerged belt filters are used to remove large particles from the wastewater stream.

Salmon City’s wastewater treatment plant provides treatment of the waste produced as a by-product of salmon farming. The treatment facility uses filtration and settling technologies prior to injection well disposal.

CLARIFIERS

2027

WWTP TIMELINE

2028

FLOCC/COAG

2028

Year

2029

TRANSFER PUMP STATION

2029

Equalization The equalization tank allows for the equalization of intermittent flows from the fixed bed bioreactors at Phase 1. Here, waste streams are stored and conveyed to the wastewater plant at a steady flow rate as to not overload the system.

25,000 45,000 65,000 85,000 105,000 125,000 145,000 185,000

THICKENING/DEWATERING

2022 2023 2024 2025 2026 2027 2028 2029

Flocc/Coag The flocculation/coagulation tank incorporates polymer and ferric chloride to bind the smaller wastewater particles to facilitate settling. The flocculation/ coagulation tank incorporates polymer and ferric chloride to bind the smaller wastewater particles to facilitate settling.

Clarifiers The clarifier is a large settling tank. The particles from the flocculation/ coagulation tank settle out at the bottom of the clarifier and are sent to the thickening/dewatering building. The clarified wastewater flows over an effluent weir and is conveyed to the transfer pump station.

7 13 18 24 29 35 41 46

15 28 40 52 65 77 89 101

Cumulative Production (metric tons)

2022

Transfer Pump Station The transfer pump station is used to pump the wastewater effluent to the injection well pump station.

Annual Avg. Daily Flow (MGD)

2023

Thickening/Dewatering Settled solids from the clarifiers are further concentrated by belt filter presses, which contain independent thickening and dewatering sections to produce a solids "cake" for offsite disposal. Water removed by thickening and dewatering is recycled to the WWTP for further treatment.

Peak Houly Flow (MGD)

2024

2022

10,000

39,423.08

59,273.24

252,445.41

167,903.34

105,000.00

Specific Numbers

2,700

Biscane Aquifer OUT: Fresh water for process and potable uses, fresh water chiller cooling supply. IN: Fresh water cooling water return wells to the Biscayne Aquifer

4,000+

Confining Zone (Typ.) Monitor Well in the Middle Floridan Confining Unit.

SALMON CITY AQUIFERS

Upper Floridan Aquifer Brackish water from the Upper Floridan Aquifer.

Avon Park Permeable Zone Saline water from the Middle Floridan Aquifer

3,350

250

3ppt

Depth (feet)

0.36ppt

2,000

Lower Floridan Aquifer Lorem ipsum dolor sit amet, consectetuer adipiscing elit, sed diam nonummy nibh euismod tincidunt ut laoreet dolore magna aliquam erat volutpat.

35ppt

1,300

36ppt

Salinity (part-per-1000)

WATER SUPPLY

1,050

Boulder Injection Zone Efluent disposal in the Lower Floridan Aquifer aka Boulder Zone

1,750

2021 – 2031 The Salmon City Timeline shows an impressive scale up in production capacity within 10-years. From 10,000 tons in Phase 1 to 200,000 tons at the end of Phase 8. While phases 1 to 6 will be developed within the existing property, phases 7 and 8 will be developed on a neighboring site. Phase 3– is a 775,000 GSF salmon fish farm that includes 30 modular concentric, 2-million gallon systems for ongrowing operations. The design of Phase 3 is currently underway for a production capacity of 32,900 tons. This phase also includes the development of the first stage of a new smolt facility with capacity of 7.5 million smolts.

2021 – 2031 The Salmon City Timeline shows an impressive scale up in production capacity within 10-years. From 10,000 tons in Phase 1 to 200,000 tons at the end of Phase 8. While phases 1 to 6 will be developed within the existing property, phases 7 and 8 will be developed on a neighboring site. Phase 4–8 Future phases 4 to 8 of the salmon fish farm will be developed using the same modular concept used in Phase 3 and will ramp-up the production capacity in 162,000 tons to bring the total production capacity of the Salmon City farm to 220,000 tons. During phases 4 to 8, the new smolt facility developed in Phase 3 will be expanded in 7.5 million smolt stages to bring the total new smolt capacity to 45 smolts.

PHASE 5: July 3, 2023 — Apr. 30, 2025 Lorem ipsum dolor sit amet, consectetuer adipiscing elit, sed diam nonummy nibh euismod tincidunt ut laoreet dolore magna aliquam erat volutpat. Ut wisi enim ad minim veniam, quis nostrud exerci tation ullamcorper suscipit lobortis nisl ut aliquip ex ea commodo conse

PHASE 6: July 1, 2024 — Apr. 30, 2026 Lorem ipsum dolor sit amet, consectetuer adipiscing elit, sed diam nonummy nibh euismod tincidunt ut laoreet dolore magna aliquam erat volutpat. Ut wisi enim ad minim veniam, quis nostrud exerci tation ullamcorper suscipit lobortis nisl ut aliquip ex ea commodo conse

PHASE 7: July 1, 2025 — Apr. 30, 2027 Lorem ipsum dolor sit amet, consectetuer adipiscing elit, sed diam nonummy nibh euismod tincidunt ut laoreet dolore magna aliquam erat volutpat. Ut wisi enim ad minim veniam, quis nostrud exerci tation ullamcorper suscipit lobortis nisl ut aliquip ex ea commodo conse

PRELIMINARY

TIMELINE

PHASE 2: 2021 – 2031 The Salmon City Timeline shows an impressive scale up in production capacity within 10-years. From 10,000 tons in Phase 1 to 200,000 tons at the end of Phase 8. While phases 1 to 6 will be developed within the existing property, phases 7 and 8 will be developed on a neighboring site. PHASE 2 – is a 353,000 GSF salmon fish farm that includes six (6) ongrowing systems (36 tanks total, each tank of 600,00 gallons), and all centralized supporting utilities (power supply, cogeneration, wastewater treatment, oxygen plant, etc.) for the fish farm operation. The design and construction of Phase 2 is currently underway for a production capacity of 15,000 tons.

2021 – 2031 The Salmon City Timeline shows an impressive scale up in production capacity within 10-years. From 10,000 tons in Phase 1 to 200,000 tons at the end of Phase 8. While phases 1 to 6 will be developed within the existing property, phases 7 and 8 will be developed on a neighboring site. Phase 1 is a 366,000 GSF salmon fish farm that includes a hatchery, parr, pre-smolt, smolt, six (6) ongrowing systems (36 tanks total, each tank of 454,400 gallons), a processing facility, all supporting utilities for the fish farm operation and administrative offices. The construction of Phase 1 has been completed for a production capacity of 10,000 tons.