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U-TOP PIONEER
Research project title Focus Area 3

Development of integrated oil removal and water treatment process equipment technology for produced water systems

Vision

Through development of next-generation unconventional resource produced-water reuse and zero liquid discharge technologies and overseas T/B demonstration

Growing into small but competitive global leaders in future markets

Research objectives

In accordance with site conditions and local regulations

Independent high-efficiency produced-water reuse and zero liquid discharge technologies using domestically produced materials

Final research outcome targets

Modularization · Reduction · Recovery

Modularization
Construction and operation
  • Construction within 10 days
  • Continuous operation for at least 90 days
  • 600 bpd · Localization rate: 80%
Reduction
Oil and organic matter removal
  • 99% oil removal · 90% organic matter removal
  • Treatment cost: 2.0 $/barrel
  • 12.5 $/m³
Recovery
Reuse and zero liquid discharge
  • 90% reuse rate
  • 30% concentrate recovery · Cost: 8 $/m³
  • Zero liquid discharge technology compliant with local regulations

Technology framework

Four constituent modules

  1. 01
    Constituent modules Treatment of oil and corrosive organic matter
  2. 02
    Constituent modules Treatment of high-temperature steam circulation water
  3. 03
    Constituent modules High-recovery reclaimed-water production
  4. 04
    Constituent modules Compact zero liquid discharge unit
Integrated produced-water reuse and zero liquid discharge process Pretreatment, main treatment, and post-treatment modules

Research outcome targets and performance indicators by technology

Operating principles · Key performance · Beneficiaries

Component Technology 1
Research Outcome Target 01

Integrated modular construction and operation

Unit processes are fabricated as modules, connected on site, and operated as an integrated process. The illustration is a conceptual diagram of module assembly.
01 Module fabrication 02 On-site assembly and connection 03 Integrated operation

Unit processes are fabricated as modules, connected on site, and operated as an integrated process. The illustration is a conceptual diagram of module assembly.

Key performance
Construction and operating performance
  • Construction within 10 days
  • 90 days of operation (0% downtime)
  • Design capacity: 20,000 bpd
Research activities and expected benefits
  • Modularization and compliance with local regulations
  • Simulation optimization
  • Remote support

Beneficiaries · Target market Technology and engineering companies Engineering

Component Technology 2-1
Research Outcome Target 02

Induced Gas Flotation for oil removal

Gas dissolved in pressurized produced water forms microbubbles as pressure is released. The bubbles attach to oil droplets dispersed in the water and carry them to the surface. The floated oil is recovered, and treated water is discharged. Produced water and dissolved gas Pressure release Microbubble generation Floated oil Treated water
01 Pressure release and microbubble generation 02 Oil attachment and flotation 03 Oil–treated water separation

Gas dissolved in pressurized produced water forms microbubbles as pressure is released. The bubbles attach to oil droplets dispersed in the water and carry them to the surface. The floated oil is recovered, and treated water is discharged.

Key performance
Oil removal performance
  • 90% oil removal
Research activities and expected benefits
  • Oil removal accounting for bitumen API gravity
  • Minimizing impact on downstream processes
  • Remote support

Beneficiaries · Target market Technology companies and manufacturers Engineering, fabrication, and procurement

Component Technology 2-2
Research Outcome Target 03

Electrodes and membranes for high-temperature produced water

Electrode treatment and membranes reduce contaminants in produced water. The diagram illustrates the separation of water passing through the membrane from the stream containing residual contaminants. Electrode treatment Membrane Treated water Residue
01 Electrode treatment 02 Passage through the membrane 03 Treated water–residue separation

Electrode treatment and membranes reduce contaminants in produced water. The diagram illustrates the separation of water passing through the membrane from the stream containing residual contaminants.

Key performance
Contaminant reduction performance
  • 90% organic matter removal
  • Oil concentration: 1 ppm
Research activities and expected benefits
  • Handling high-temperature produced water
  • Reduction of corrosive membrane fouling
  • Productivity improvement
  • Chemical-free operation and environmental sustainability

Beneficiaries · Target market Technology companies and manufacturers Engineering, fabrication, and procurement

Component Technology 3
Research Outcome Target 04

High-recovery reuse and zero liquid discharge

Reclaimed water is obtained through membranes, and the remaining concentrate is treated separately for additional water recovery. Concentration and condensation illustrate the principle of additional recovery; this is not an actual fabrication drawing.RO Concentrate Reclaimed water Additional recovered water Residue
01 Reclaimed water–concentrate separation 02 Additional concentrate treatment 03 Recovered water–residue separation

Reclaimed water is obtained through membranes, and the remaining concentrate is treated separately for additional water recovery. Concentration and condensation illustrate the principle of additional recovery; this is not an actual fabrication drawing.

Key performance
Reuse and recovery performance
  • 90% reuse rate
  • 30% concentrate recovery
  • Low cost: 8 $/m³
Research activities and expected benefits
  • Achieving high recovery and zero liquid discharge
  • Efficient operation
  • System stability

Beneficiaries · Target market Technology companies and manufacturers Engineering, fabrication, and procurement

Implementation strategy and direction

Five implementation strategies

01

Strengthening core design capabilities

Design data analysis → Modeling and analysis → Core design
Design data analysis → Modeling and analysis → Core design
02

Implementation linked to existing research outcomes

Utilization of existing technologies → Linkage and integration → Expansion
Utilization of existing technologies → Linkage and integration → Expansion
03

Improving technology maturity

Performance testing → Validation → Improvement and retesting
Performance testing → Validation → Improvement and retesting
04

Utilizing domestic and international networks

Exchange and collaboration in design, research, and testing capabilities
Exchange and collaboration in design, research, and testing capabilities
05

Promoting practical application and commercialization

Fabrication preparation → Module fabrication → Field application
Fabrication preparation → Module fabrication → Field application

Research activities and outcomes

Project Year 1–Project Year 7

01

Project Years 1 and 2 · Design and development

  • Building a database of overseas produced-water conditions
  • Domestic demonstration site survey
  • Basic modular design
  • Process simulation model
02

Project Years 3 and 4 · Domestic T/B

  • Domestic demonstration T/B construction and evaluation
  • Detailed modular design
  • Localization of materials and equipment
  • Integrated process simulation model
03

Project Year 5 · Overseas cooperation

  • Securing an overseas T/B in coordination with the program
  • Overseas T/B site survey
  • Modular improvements tailored to local conditions
  • Securing a domestic T/B operational database
04

Project Years 6 and 7 · Overseas T/B

  • Support for construction and operation of overseas demonstration plants
  • Establishment of an overseas plant support system
  • Localization of modules
  • Securing 20,000 bpd FEED

AS-IS / TO-BE

Transition objectives for three component technologies

Component Technology 1

Construction and operation management technologies for integrated water treatment processes tailored to unconventional oil

AS-IS
  • Large plant footprint and limited mobility
  • Distributed construction of functional facilities at remote sites
  • Difficulty responding to problems at remote sites
  • Wear, corrosion, and heat loss in materials for each unit process
  • Construction within 30 days · Downtime within 15 days
TO-BE
  • Modular design of unit processes for transport and one-touch assembly
  • Securing technology for high silica concentrations under local conditions and developing modules
  • Overseas demonstration through domestic test bed validation
  • Rapid response to problems at remote sites
  • Construction within 10 days · Uninterrupted continuous operation for at least 90 days
Component Technology 2

Pre-pretreatment and pretreatment technologies to address variations in the quality of water treated by the gathering and separation process

AS-IS
  • Insufficient standardization of pre-pretreatment and pretreatment processes
  • Insufficient measures for managing and controlling corrosive organic matter
  • Use of imported ceramic membrane technology for pretreatment
  • Organic matter removal efficiency of 85% or less
  • Oil component removal efficiency of 90% or less
  • Pretreatment cost of 3.0 $/barrel or more
  • Process technology localization rate of 30% or less
TO-BE
  • Securing IGF optimization technology through the introduction of on-site mixed gas
  • Reduction of corrosive organic matter to prevent membrane fouling
  • Securing and demonstrating ceramic membrane modularization and localization technologies
  • Organic matter removal efficiency of at least 90%
  • Oil component removal efficiency of at least 99%
  • Pretreatment cost of 2.0 $/barrel or less
  • Achieving a process technology localization rate of at least 80%
Component Technology 3

High-recovery main treatment and post-treatment technologies for high-quality reclaimed-water production

AS-IS
  • Environmental regulations require environmentally sound technologies
  • Use of ion-exchange resins with high dependence on imports
  • Water reuse rate of 85% or less
  • Concentrate recovery rate of 20% or less
  • Process technology localization rate of 30% or less
TO-BE
  • Participation of a Korean mid-sized enterprise holding foundational patents for zero liquid discharge
  • Demonstration of domestically developed high-recovery RO modules to improve water reuse
  • Water reuse rate of at least 95%
  • Concentrate recovery rate of at least 30%
  • Achieving a process technology localization rate of at least 80%