Phase 2 – Comprehensive Design, Fabrication and Testing

On this Page :

Phase 2 – Comprehensive Design, Fabrication & Testing

Turning drawings into a living, breathing pilot or demonstration plant

Phase 2 is the make-or-break stretch of any scale-up project. The careful concepts agreed in Phase 1 now pass through an intense engineering crucible: every weld length, PLC tag, and relief-valve orifice is calculated, reviewed, built, and proven. Below is a deep dive into how OSVARD executes this phase so the plant arrives on site ready to run—not ready to rework.


1 | Detailed Engineering: locking in every dimension and datum

From PFD to bullet-proof P&ID

  • Instrumentation detail. Each tag gets a calibrated range, material compatibility check, and installation orientation. Even small pilot valves are sized with ISA guidelines so controller tuning later is painless.

  • Mechanical integrity. Shell‐thickness calculations follow ASME VIII or EN 13445, including wind/earthquake loads; nozzle loads are checked against WRC 537 to ensure piping strain won’t crack a flange six months in.

  • Control philosophy. OSVARD writes cause-and-effect charts, ESD matrices, and interlock logic before a single line of PLC code is drafted. This freezes safety intent early and avoids “feature creep” later.

3-D CAD and clash detection
A full SolidWorks®/Plant 3D model is built, including cable trays and service corridors. Virtual walk-throughs catch ergonomic issues—operator can’t reach that sample valve, handrail blocks lifting eye—while changes cost nothing more than a mouse-click.

Modularisation strategy
Whenever transport permits, we pack equipment on skids no wider than 2.4 m (standard container width). Shop-built modules:

  • improve weld quality (controlled environment)

  • slash field hours (fewer hot-work permits)

  • let functional checks run before shipping.


2 | Fabrication & Assembly: turning drawings into hardware

Vendor kick-off and quality plans
OSVARD issues a Manufacturing Quality Plan (MQP) that lists hold-points for material certificates, weld procedure qualification, PMI, hydrotest pressures, and paint DFT checks. Nothing ships without a signed inspection release note.

Code welding & non-destructive examination

  • WPS/PQR approval ensures the welder, filler metal, and heat input meet code toughness requirements.

  • 100 % radiography on Category A seams for pressure vessels over 50 bar; dye-penetrant or ultrasonic on others according to risk ranking.

  • Hydrotests at 1.3 × design pressure catch early leaks; we often run a nitrogen pressure hold afterwards for sensitive internals.

Control-panel integration
Panels are assembled in a clean electrical shop. All I/O channels undergo loop checks—voltage range, signal integrity, and fail-safe direction—long before the skid sees process fluids.


3 | Factory Acceptance Testing (FAT): proving the build in a safe environment

FAT is more than a box-ticking exercise; it is the first opportunity for operators and engineers to treat the unit as if it were already on their site.

  1. Mechanical run-in – Pumps turn with water; vibration and seal temperatures are logged for baseline data.

  2. Safety-instrumented function tests – Simulated pressure trips, level highs, or flow-fail signals validate every shutdown path.

  3. Control-loop checkout – PID gains are rough-tuned, interlocks verified, alarms rationalised.

  4. Process functionality demo – Where chemicals are safe to handle, OSVARD performs a short “mini-campaign” so heat-transfer, residence-time, or filtration rates can be proven on real materials.

Each punch-list item is cleared, and the client signs a detailed FAT dossier—complete with calibration certs, as-built P&IDs, wiring diagrams, and material traceability records.


4 | Performance Trials: optional but gold-standard assurance

For catalytic or bio-process rigs, OSVARD offers extended shop trials—24 h to several days—using genuine feeds. Benefits include:

  • early catalyst light-off and deactivation data,

  • confirmation that heat-duty predictions match reality,

  • operator training with the actual control screens.

These runs often reveal subtle tuning tweaks that make Phase 3 start-up markedly smoother.


5 | Project-management discipline: keeping time, cost, and quality in balance

  • Stage-gate reviews tie payment milestones to tangible deliverables—approved drawings, finished modules, successful FAT—so budgets stay predictable.

  • Long-lead procurement tracking flags items such as exotic-alloy agitators or SIL-rated transmitters months in advance.

  • Risk registers are live documents: if a weld repair pushes schedule, shipping dates and site-prep timelines are auto-re-baselined.


6 | Deliverables at Phase 2 hand-off

  • As-built 3-D model and intelligent P&IDs (with tag-linked datasheets)

  • Material data book – MTRs, welding maps, NDE reports, paint certs

  • Control system back-ups – PLC/DCS programs, HMI graphics, and alarm set-points

  • FAT & performance-test report – summary of procedures, raw data, deviations, and resolutions

  • Shipping release – packing lists, centre-of-gravity sheets, and lifting drawings for each module

With every bolt torqued and every sensor calibrated, the plant is ready for Phase 3—delivery, on-site setup, and commissioning—without hidden surprises.


“Measure twice, weld once, test thrice: that’s how prototypes become production assets.”

Need your pilot or demo plant built fast and fault-free? OSVARD’s Phase 2 execution framework delivers workshop-tested hardware that performs on day one—so your innovations can sprint toward commercial reality.

Connect with our
Competency
Connect
featured insights
Process Scale-Up
Article
Bridging the Gap – Understand a Key Differences Between a Small Beakers to Larger Sizes.
The journey from a laboratory experiment to a commercially viable process is challenging step i.....
OSVARD
Process Scale-Up
Article
Bridging the Gap – Understand a Key Differences Between a Small Beakers to Larger Sizes.
The journey from a laboratory experiment to a commercially viable process is challenging step i.....
OSVARD
Engineering Design
Article
Why is Ideal flow pattern crucial for upscaling Fixed-bed reactor ?
The challenge in fixed-bed reactor scale up is partial similarity of laboratory, pilot, and commerci
OSVARD
Chemical Technology Development
Article
Top 10 Mistakes Kill Timing in Your New Product Launch in the Chemical Industry.
Timing your product launch refers to the strategic planning and execution of introducing a new p....
OSVARD
High Performance Culture
Article
How to properly apply inert bed dilution for catalyst testing in fixed-bed reactor
Nowadays, computing systems with extremely high computational power, well-known as High performance
OSVARD
Process Scale-Up
Article
To Make it Perfect: Where Should You Set Up Your Pilot/Demonstration Plant?
In the development of chemical industry, "pilot plant" is frequently used of innovation and expe....
OSVARD
High Performance Culture
Article
How to Conquer the Loop of Death Valley
To ensure the success in catalyst development, the business direction and engineering design must be
OSVARD
Engineering Design
Article
Too Small to be Viable, Small Modular Nuclear Reactors (SMNRs)
the NuScale project faced a significant cost increase, with the target price for power generatio....
OSVARD
Chemical Technology Development
Article
H2 or kWh – Evaluating the Potential of Hydrogen and Electron Economies in Decarbonization
Hydrogen's potential for decarbonization lies in its versatility. It can be produced from water.....
OSVARD
Engineering Design
Article
Industrial Heat Pumps: Even It is Hard to Implement, But Non-Negotiable.
An industrial heat pump (IHP) is a large-scale device designed to capture and repurpose heat fro....
OSVARD
Engineering Design
Article
Death of Elon Musk’s Hyperloop, The Next is Direct-air Capture (DAC)
Hyperloop One, initially a high-profile venture, raised over $450 million and constructed a sm....
OSVARD
Process Scale-Up
Article
What’s Challenges in Scaling up or down of Single-phase Catalytic Fixed-bed Reactors ?
Fixed-bed reactors is commonly used in commercial-scale. Laboratory-scale fixed-bed reactors might b
OSVARD
Safety Engineering
Article
The Death Valley of Brand-new Technology Development.
In the bottom-up development approach, the multi-stage process starts in the laboratory, moves to th