The document discusses how advanced oil and gas production processes like SAGD and fracking have increased requirements for lining systems that protect infrastructure from high heat, chemicals, and abrasion. Traditional lining materials are insufficient for these conditions and often fail. A new high-performance lining called Enviroline 405HTR was developed to address these issues with properties like chemical resistance up to 300°F, abrasion resistance, fast cure times, and low VOCs. It has been extensively tested and shown effective in real-world applications. Proper surface preparation and technical support are also important to maximize lining performance for oil and gas facilities.
Tnemec is a leading manufacturer of industrial and architectural coatings that was founded in 1921. It produces over 150 coatings designed for extreme durability in demanding environments. Tnemec coatings protect infrastructure in industries such as water storage tanks, processing facilities, bridges, and buildings. The company focuses on innovation through research and offers full product support to customers.
Tnemec has developed coatings and linings that provide protection against corrosion, abrasion, chemicals, and other harsh conditions for water and wastewater infrastructure for over 50 years. Their products shield steel, concrete, and other materials from environments in treatment facilities, pipelines, and other assets. Tnemec works to innovate new coatings through extensive testing and developing standards like the Severe Wastewater Analysis Test. Their coatings experts provide customized recommendations and support to optimize protection for customers' unique needs and conditions.
Cancel #corrosion in sanitary #faucets and shower assemblies by replacing metal with #SABIC specialty thermoplastics. Besides reducing pesky mineral deposits that inhibit #water flow, NORYL™ and ULTEM™ resins and LNP™ compounds deliver high performance properties including hydrolytic and dimensional stability, burst strength and wear resistance. They also comply with key drinking water certifications including NSF61, ACS, WRAS, REG4 and KTW-BWGL and certain low-lead regulations. Plus, you can potentially save on the costs of raw materials, manufacturing and logistics.
Evaluated alternative computer simulation software to model processes and optimize performance. Obtained trial of HYSIS software and used it to evaluate performance of columns on site. While it proved better than existing software, financial circumstances prevented purchase or lease. Contacted packing vendor for data demonstrating existing packed columns met federal design requirements for stripping wastewater. Upgraded instrumentation and ensured continuous monitoring and steam quality compliance to avoid sampling and maintain production. Assured compliance of stripping column design and operation.
IRJET- Evaluation of Concrete Properties with Impregnated Different PolymersIRJET Journal
This document discusses a study that evaluated the properties of concrete impregnated with different polymers. M30 grade concrete was prepared with polymers like SBR latex, polycarboxylate ether (PCE), and polyethylene glycol (PEG). The study tested the workability, strength, compaction, and flexural strength of the concrete mixes. Polymers can enhance concrete properties by reducing the water-cement ratio and improving hydration. The objective was to determine the effects of these different polymer types on the plasticity, curing, and strength of the concrete.
A life cycle approach to corrosion management and asset integrityOkeme Esegine PMP
The document discusses corrosion management and asset integrity through a lifecycle approach. It outlines 5 key phases: 1) Design, emphasizing avoiding design flaws that could compromise integrity. 2) Material selection, choosing materials suited for each process. 3) Construction, using proper welding techniques. 4) Operations, adhering to operating parameters. 5) Asset management, using inspection, integrity and reliability assessments to extend asset life through proper maintenance and shutdowns. The author advocates a lifecycle approach and interdisciplinary expertise to reliably manage assets.
Art upgrading the use of recycled aggregates collins (1998)Petiano Camilo Bin
The document discusses efforts to increase the use of recycled concrete and masonry aggregates in the UK construction industry. It describes several collaborative projects that demonstrated recycled aggregates can successfully replace natural aggregates in applications like concrete blocks and precast concrete. It also discusses developing quality control standards and an online materials exchange to help promote broader use of recycled aggregates. The goal is to improve recycling and reduce reliance on landfills and primary aggregates.
The StrataShield product line from Tnemec offers specialized floor and wall coating systems designed to withstand physical and chemical abuse in a variety of environments. The coatings provide protection while also having an attractive finish. They are high-performance alternatives for conditions requiring extra protection. Tnemec representatives provide expertise to select the best coating system tailored for the intended environment.
Tnemec is a leading manufacturer of industrial and architectural coatings that was founded in 1921. It produces over 150 coatings designed for extreme durability in demanding environments. Tnemec coatings protect infrastructure in industries such as water storage tanks, processing facilities, bridges, and buildings. The company focuses on innovation through research and offers full product support to customers.
Tnemec has developed coatings and linings that provide protection against corrosion, abrasion, chemicals, and other harsh conditions for water and wastewater infrastructure for over 50 years. Their products shield steel, concrete, and other materials from environments in treatment facilities, pipelines, and other assets. Tnemec works to innovate new coatings through extensive testing and developing standards like the Severe Wastewater Analysis Test. Their coatings experts provide customized recommendations and support to optimize protection for customers' unique needs and conditions.
Cancel #corrosion in sanitary #faucets and shower assemblies by replacing metal with #SABIC specialty thermoplastics. Besides reducing pesky mineral deposits that inhibit #water flow, NORYL™ and ULTEM™ resins and LNP™ compounds deliver high performance properties including hydrolytic and dimensional stability, burst strength and wear resistance. They also comply with key drinking water certifications including NSF61, ACS, WRAS, REG4 and KTW-BWGL and certain low-lead regulations. Plus, you can potentially save on the costs of raw materials, manufacturing and logistics.
Evaluated alternative computer simulation software to model processes and optimize performance. Obtained trial of HYSIS software and used it to evaluate performance of columns on site. While it proved better than existing software, financial circumstances prevented purchase or lease. Contacted packing vendor for data demonstrating existing packed columns met federal design requirements for stripping wastewater. Upgraded instrumentation and ensured continuous monitoring and steam quality compliance to avoid sampling and maintain production. Assured compliance of stripping column design and operation.
IRJET- Evaluation of Concrete Properties with Impregnated Different PolymersIRJET Journal
This document discusses a study that evaluated the properties of concrete impregnated with different polymers. M30 grade concrete was prepared with polymers like SBR latex, polycarboxylate ether (PCE), and polyethylene glycol (PEG). The study tested the workability, strength, compaction, and flexural strength of the concrete mixes. Polymers can enhance concrete properties by reducing the water-cement ratio and improving hydration. The objective was to determine the effects of these different polymer types on the plasticity, curing, and strength of the concrete.
A life cycle approach to corrosion management and asset integrityOkeme Esegine PMP
The document discusses corrosion management and asset integrity through a lifecycle approach. It outlines 5 key phases: 1) Design, emphasizing avoiding design flaws that could compromise integrity. 2) Material selection, choosing materials suited for each process. 3) Construction, using proper welding techniques. 4) Operations, adhering to operating parameters. 5) Asset management, using inspection, integrity and reliability assessments to extend asset life through proper maintenance and shutdowns. The author advocates a lifecycle approach and interdisciplinary expertise to reliably manage assets.
Art upgrading the use of recycled aggregates collins (1998)Petiano Camilo Bin
The document discusses efforts to increase the use of recycled concrete and masonry aggregates in the UK construction industry. It describes several collaborative projects that demonstrated recycled aggregates can successfully replace natural aggregates in applications like concrete blocks and precast concrete. It also discusses developing quality control standards and an online materials exchange to help promote broader use of recycled aggregates. The goal is to improve recycling and reduce reliance on landfills and primary aggregates.
The StrataShield product line from Tnemec offers specialized floor and wall coating systems designed to withstand physical and chemical abuse in a variety of environments. The coatings provide protection while also having an attractive finish. They are high-performance alternatives for conditions requiring extra protection. Tnemec representatives provide expertise to select the best coating system tailored for the intended environment.
This document provides information about SKAFS International LLC and their products and services for storage and material handling solutions. It introduces SKAFS and their focus on MEP services, construction, and maintenance. It also introduces Rostfrei Steels and their experience and standards for products like liquid storage tanks and grain storage silos. The document discusses various tank materials and products offered, including steel SMC tanks, Zincalume tanks, glass fused to steel tanks, grain storage silos, and related fittings and accessories.
Edouard Kaeterle has over 37 years of experience in consulting, R&D, scale-up, optimization, and modeling of coating and drying processes. He has specialized expertise in fluid mixing, slot die coating, and coater/dryer optimization. Recently he has focused on battery slurry rheology optimization and electrode manufacturing processes for lithium-ion batteries.
Selection and Use of Printed Circuit Heat ExchangersGerard B. Hawkins
Selection and Use of Printed Circuit Heat Exchangers
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 CONSTRUCTION
5 HEAT TRANSFER AND PRESSURE DROP
6 FOULING
7 MECHANICAL AND MATERIALS ASPECTS
8 COMPACTNESS
9 FLEXIBILITY
10 COST
11 GBHE EXPERIENCE 5
12 BIBLIOGRAPHY
APPENDICES
A HEAT TRANSFER AND PRESSURE DROP IN
WAVY PASSAGES
This document provides guidelines for using construction chemicals for repairing and rehabilitating reinforced concrete structures. It discusses the causes of concrete deterioration, including poor workmanship and environmental stresses. The key steps in the repair process are outlined, including surface preparation, protecting exposed reinforcement, treating cracks, applying a bond coat and coarse repair mortar. The appropriate materials for different types and widths of cracks are described. Finally, the document recommends applying a fine filling coat, hydrophobic impregnation if needed, and a protective concrete coating or carbonation inhibitor to form a durable repair system.
Lubricants
Engineering Design Guide
0 INTRODUCTION
1 SCOPE
2 LUBRICATION BASICS
2.1 Basic Functions of a Lubricant
2.2 Hydrostatic Fluid Film Lubrication
2.3 Hydrodynamic Fluid Film Lubrication
2.4 Boundary Lubrication
2.5 Mixed Lubrication
3 VISCOSITY
3.1 General
3.2 Dynamic Viscosity
3.3 Kinematic Viscosity
3.4 Measurement of Viscosity
3.5 Viscosity Classification of Lubricants
3.6 Viscosity Index
3.7 Viscosity Change with Pressure
4 MINERAL OILS
4.1 General Characteristics
4.2 British Standard 4475 Commentary
4.3 Oil Additives
4.4 Synthetic Oils
5 GREASES
5.1 Composition
5.2 Properties
6 SOLID LUBRICANTS
7 SELECTION OF LUBRICANTS
8 OPERATING FACTORS
8.1 Filtration
8.2 Operating Temperatures
8.3 Total Loss Lubrication Systems
9 LUBRICANT SUPPLY AND SCHEDULING
9.1 Selection of Supplier
9.2 Lubrication Schedules
10 HEATH AND SAFETY
11 MONITORING & MAINTENANCE OF OIL IN SERVICE
11.1 Analyze or Change?
11.2 Visual Analysis
1 I.3 Laboratory Analysis
11.4 Contamination Problems
BIBLIOGRAPHY
APPENDICES
A VISCOSITY EQUIVALENTS
B SYMBOLS AND PREFERRED UNITS
FIGURES
I LUBRICANT CHANGE PERIODS AND TESTS
2 CHARACTERISTICS OF MINERAL LUBRICATING OILS VG32 TO VG 460.
3 SERVICE MONITORING AND MAINTENANCE OF OIL IN SERVICE ON LARGE SYSTEMS
TABLES
1 ISO VISCOSITY CLASSIFICATION
2 OILS TO BS 4475 RECOMMENDED FOR USE BY GBHE
3 SUGGESTED OIL CHANGE PERIODS FOR SMALL INDUSTRIAL SYSTEMS
4 VISUAL EXAMINATION OF USED LUBRICATING OILS
5 SUMMARY OF ROUTINE ANALYTICAL TESTS FOR INDUSTRIAL OILS
Shell and Tube Heat Exchangers Using Cooling Water
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
3.1 HTFS
3.2 TEMA
4 CHECKLIST
5 QUALITY OF COOLING WATER
6 COOLING WATER ON SHELL SIDE OR TUBE SIDE
7 COOLING WATER ON THE SHELL SIDE
7.1 Baffle Spacing
7.2 Impingement Plates
7.3 Horizontal or Vertical Shell Orientation
7.4 Baffle Cut Orientation
7.5 Sludge Blowdown
7.6 Removable Bundles
8 FOULING RESISTANCES AND LIMITING TEMPERATURES
9 PRESSURE DROP
9.1 Pressure Drop Restrictions
9.2 Fouling and Pressure Drop
9.3 Elevation of a Heat Exchanger in the Plant
10 MATERIALS OF CONSTRUCTION
11 WATER VELOCITY
11.1 Low Water Velocity
11.1.1 Tube Side Water Flow
11.1.2 Shell Side Water Flow
11.2 High Water Velocity
12 ECONOMICS
13 DIRECTION OF WATER FLOW
14 VENTS AND DRAINS
15 CONTROL
15.1 Operating Variables
15.2 Heat Load Control
15.2.1 General
15.2.2 Heat load control by varying cooling water flow
15.3 Orifice Plates
16 MAINTENANCE
Pipeline Design for Isothermal, Turbulent Flow of Non-Newtonian FluidsGerard B. Hawkins
Pipeline Design for Isothermal, Turbulent Flow of Non-Newtonian Fluids
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 DESCRIPTION OF ANOMALOUS EFFECTS
4.1 Wall Slip
4.2 Drag Reduction in Polymeric Materials
4.3 Transition Delay by Polymeric Materials
4.4 Drag Reduction in Suspensions
5 DESIGN PROCEDURE FOR PRESSURE DROP
IN TURBULENT PIPE FLOW IN THE ABSENCE
OF DRAG REDUCTION
5.1 Pressure Drop in the Absence of Wall Slip and
Drag Reduction
5.2 Wall Slip
5.3 Pipe Roughness
5.4 Pipe Fittings
6 DESIGN PROCEDURE FOR DRAG REDUCING
POLYMERIC MATERIALS
6.1 General
6.2 Transition Delay
6.3 Pipe Roughness
6.4 Pipe Fittings
7 DESIGN PROCEDURE FOR DRAG REDUCING
FIBRE SUSPENSIONS
8 BIBLIOGRAPHY
9 NOMENCLATURE
FIGURES
1 DRAG REDUCTION PHENOMENA
2 TRANSITION DELAY PHENOMENA
3 PROCEDURE FOR THE CALCULATION OF
PRESSURE DROP IN TURBULENT NON-NEWTONIAN
PIPE FLOW
4 TYPICAL RELATIONSHIP FOR Ψ VERSUS ʋ*
This document summarizes BASF's approach to sustainable building and infrastructure called BEYOND.High Performance. It provides integrated solutions to construction challenges by selecting sustainable materials, connecting clients with building experts, and recommending cost-effective solutions. BASF aims to preserve resources, provide energy efficient strategies, and make an impact throughout the built environment. The BASF Center for Building Excellence collaborates directly with clients to explore innovative approaches.
Mixing of Immiscible Liquids
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 EQUIPMENT
4.1 Agitated Tanks
4.2 Flow Mixers
4.3 'High Shear' Mixers
5 SYSTEM PHYSICAL PROPERTIES
5.1 Density
5.2 Viscosity
5.3 Interfacial Tension
6 STIRRED VESSELS
6.1 Design for Complete Dispersion
6.2 Prediction of Phase Inversion
6.3 Design for Mass Transfer
6.4 Design for Dispersed Phase Mixing
6.5 Hold-Up in Continuous Vessels
7 FLOW MIXERS
7.1 Design for Turbulent Conditions
7.2 Design for Laminar Conditions
TABLES
1 REYNOLDS NUMBER RANGES
FIGURES
1 STANDARD TANK CONFIGURATION
2 EXPERIMENTAL RELATIONSHIP BETWEEN MASS
TRANSFER COEFFICIENT AND POWER DENSITY
Air Cooled Heat Exchanger Design
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 SUITABILITY FOR AIR COOLING
4.1 Options Available For Cooling
4.2 Choice of Cooling System
5 SPECIFICATION OF AN AIR COOLED HEAT
EXCHANGER
5.1 Description and Terminology
5.2 General
5.3 Thermal Duty and Design Margins
5.4 Process Pressure Drop
5.5 Design Ambient Conditions
5.6 Process Physical Properties
5.7 Mechanical Design Constraints
5.8 Arrangement
5.9 Air Side Fouling
5.10 Economic Factors in Design
6 CONTROL
7 PRESSURE RELIEF
8 ASSESSMENT OF OFFERS
8.1 General
8.2 Manual Checking Of Designs
8.3 Computer Assessment
8.4 Bid Comparison
9 FOULING AND CORROSION
9.1 Fouling
9.2 Corrosion
10 OPERATION AND MAINTENANCE
10.1 Performance Testing
10.2 Air-Side Cleaning
10.3 Mechanical Maintenance
10.4 Tube side Access
11 REFERENCES
Hydrogen Compressors
Engineering Design Guide
1 SCOPE
2 PHYSICAL ROPERTIES
2.1 Data for Pure Hydrogen
2.2 Influence of Impurities
3 MATERIALS OF CONSTRUCTION
3.1 Hydrogen from Electrolytic Cells
3.2 Pure Hydrogen
4 DESIGN
4.1 Pulsation
4.2 Bypass
5 TESTING OR COMMISSIONING RECIPROCATING COMPRESSORS
6 LUBRICATION
7 LAYOUT
8 REFERENCES
FIGURES
1 MOLLIER CHART - HYDROGEN
2 COMPRESSIBILITY CHART
3 NELSON DIAGRAM
4 WATER CONTENT IN HYDROGEN FOR OIL-LUBRICATED COMPRESSORS AS GRAMM/M2 SWEPT CYLINDER AREA
Gas Solid Mixing
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 GAS-SOLID FLUIDIZED BED
5 MIXING IN FLUIDIZED BEDS
5.1 Group A Powders
5.2 Group B Powders
5.3 Group C Powders
5.4 Group D Powders
6 MECHANISMS OF MIXING AND SEGREGATION
6.1 Particle Segregation
6.2 Rate of Mixing
6.3 Solids Circulation
7 GRID DESIGN
7.1 Choice of Configuration
8 PLENUM CHAMBER DESIGN
9 SPOUTED BED
10 NOMENCLATURE
11 BIBLIOGRAPHY
FIGURES
1 POWDER CLASSIFICATION DIAGRAM FOR
FLUIDIZATION BY AIR
2 DIAGRAMMATIC REPRESENTATION OF MIXING BY A SINGLE RISING BUBBLE IN A BED OF SMALL
PARTICLES
3 SEGREGATION PATTERNS WITH 'PRACTICAL'
MATERIALS
4 SPOUTED BED – DIAGRAMMATIC
Pipeline Design for Isothermal, Laminar Flow of Non-Newtonian FluidsGerard B. Hawkins
Pipeline Design for Isothermal, Laminar Flow of Non-Newtonian Fluids
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 RHEOLOGICAL BEHAVIOR OF PURELY VISCOUS
NON-NEWTONIAN FLUIDS
4.1 Experimental Characterization
4.2 Rheological Models
5 PRESSURE DROP-FLOW RATE RELATIONSHIPS
BASED DIRECTLY ON EXPERIMENTAL DATA
5.1 Use of Shear Stress – Shear Rate Data
5.2 Tubular Viscometer Data
6 PRESSURE DROP – FLOW RATE RELATIONSHIPS BASED ON RHEOLOGICAL MODELS
7 LOSSES IN PIPE FITTINGS
7.1 Entrances Losses
7.2 Expansion Effects
7.3 Contraction Losses
7.4 Valves
7.5 Bends
8 EFFECT OF WALL SLIP
9 VELOCITY PROFILES
9.1 Velocity Profile from Experimental Flow-Curve
9.2 Velocity Profile from Rheological Model
9.3 Residence Time Distribution
10 CHECKS ON THE VALIDITY OF THE
DESIGN PROCEDURES
10.1 Rheological Behavior
10.2 Validity of Experimental Data
10.2 Check on Laminar Flow
11 NOMENCLATURE
12 REFERENCES
FIGURES
1 FLOW CURVES FOR PURELY VISCOUS FLUIDS
2 PLOTS OF D∆P/4L VERSUS 32Q/ɳD3 FOR PURELY VISCOUS FLUIDS
3 LOG-LOG PLOT OF t VERSUS ý
4 FLOW CURVE FOR A BINGHAM PLASTIC
5 LOG-LOG PLOT FOR A GENERALIZED BINGHAM
PLASTIC
6 CORRELATION OF ENTRANCE LOSS
7 CORRELATION OF EXPANSION LOSS
8 EFFECT OF “WALL SLIP” ON VELOCITY PROFILE
9 D∆P/4L VERSUS Q/ɳR3 WITH WALL SLIP
10 EVALUATION OFUs WITH Ʈw
11 VARIATION OF Us WITH Ʈw
12 PLOT OF D∆P/4L VERSUS 8 (ū- Us)/D FOR
CONDITIONS OF WALL SLIP
13 CUMULATIVE RESIDENCE TIME DISTRIBUTION
TO POWER LAW FLUIDS
14 EFFECTS OF TUBE LENGTH AND DIAMETER ON
RELATIONSHIP BETWEEN D∆P/4L AND 32Q/ɳD3
This document provides a summary of Tony L. De Vera's career and qualifications. He has over 25 years of experience managing research and development projects in industrial chemistry. Some of his accomplishments include developing new materials for biopharma and semiconductors, inventing organic-inorganic hybrid technologies, and optimizing chemical processes to increase efficiency and reduce costs. Currently he is commercializing enabling technologies through partnerships that are projected to generate $3 million in net income.
Stormw and Sanitary Trenchless RehabilitationSteve Neschleba
Highly engineered polymer that can be cast inside of an existing large diameter storm/sanitary sewer. This is an innovative structural repair system from Milliken Infrastructure. For more info please email steve.neschleba@milliken.com
Zach Szczepanski is seeking a position in industrial and organic chemistry. He has over 5 years of experience in polymer formulation, chemical analysis, and organic synthesis. His experience includes positions at Superior Essex as a Polymer Formulation Chemist, Cummins Inc. as a Chemist/Materials Engineer, and Albany Molecular Research as a Research Scientist. He has a Bachelor's degree in Chemistry from Indiana University Purdue University Fort Wayne with a GPA of 3.79.
This newsletter provides updates on various corrosion protection projects completed by Corrocoat and its partners around the world. In the first story, Corrocoat USA solved a costly corrosion problem for a pellet mill in the US by applying Plasmet HTE to protect an exhaust elbow. In other stories, Corrocoat Benelux provided long-term protection of flue ducts in gas desulphurization plants, Corroserve developed a coating system to protect road tankers transporting acidic waste, and Corrocoat Vietnam extended the life of power transformer insulators. The newsletter highlights many other successful applications of Corrocoat coatings around the world and in different industries.
The document discusses the challenges of developing offshore oil and gas fields, particularly in deep waters and remote locations. It notes that while offshore development technologies have enabled projects in up to 3,000m of water, developing fields in ultra-deep waters and frontier regions requires further technological advances. Specifically, it focuses on the need for high-capacity pipe-lay vessels using J-lay or reel-lay methods to install thick-walled pipes in these challenging environments, with each method having advantages depending on the characteristics of the specific field development project. Saipem's new flexible lay and construction vessel, the Normand Maximus, is presented as an innovative vessel designed to aid in ultra-deep water SURF installation and field
PETRONAS has developed a new pipeline repair technology called PIPEASSURE that can be applied underwater to repair pipelines damaged by corrosion or degradation. PIPEASSURE uses an epoxy-based composite material that is wrapped around pipelines and adheres strongly even in wet environments. It provides a minimally invasive repair method and extends pipeline lifespans with minimal downtime, saving oil and gas companies millions in lost revenue compared to traditional repair methods like underwater welding. Testing shows PIPEASSURE adheres much stronger than competing technologies and can withstand underwater conditions for 5 years.
This document provides information about SKAFS International LLC and their products and services for storage and material handling solutions. It introduces SKAFS and their focus on MEP services, construction, and maintenance. It also introduces Rostfrei Steels and their experience and standards for products like liquid storage tanks and grain storage silos. The document discusses various tank materials and products offered, including steel SMC tanks, Zincalume tanks, glass fused to steel tanks, grain storage silos, and related fittings and accessories.
Edouard Kaeterle has over 37 years of experience in consulting, R&D, scale-up, optimization, and modeling of coating and drying processes. He has specialized expertise in fluid mixing, slot die coating, and coater/dryer optimization. Recently he has focused on battery slurry rheology optimization and electrode manufacturing processes for lithium-ion batteries.
Selection and Use of Printed Circuit Heat ExchangersGerard B. Hawkins
Selection and Use of Printed Circuit Heat Exchangers
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 CONSTRUCTION
5 HEAT TRANSFER AND PRESSURE DROP
6 FOULING
7 MECHANICAL AND MATERIALS ASPECTS
8 COMPACTNESS
9 FLEXIBILITY
10 COST
11 GBHE EXPERIENCE 5
12 BIBLIOGRAPHY
APPENDICES
A HEAT TRANSFER AND PRESSURE DROP IN
WAVY PASSAGES
This document provides guidelines for using construction chemicals for repairing and rehabilitating reinforced concrete structures. It discusses the causes of concrete deterioration, including poor workmanship and environmental stresses. The key steps in the repair process are outlined, including surface preparation, protecting exposed reinforcement, treating cracks, applying a bond coat and coarse repair mortar. The appropriate materials for different types and widths of cracks are described. Finally, the document recommends applying a fine filling coat, hydrophobic impregnation if needed, and a protective concrete coating or carbonation inhibitor to form a durable repair system.
Lubricants
Engineering Design Guide
0 INTRODUCTION
1 SCOPE
2 LUBRICATION BASICS
2.1 Basic Functions of a Lubricant
2.2 Hydrostatic Fluid Film Lubrication
2.3 Hydrodynamic Fluid Film Lubrication
2.4 Boundary Lubrication
2.5 Mixed Lubrication
3 VISCOSITY
3.1 General
3.2 Dynamic Viscosity
3.3 Kinematic Viscosity
3.4 Measurement of Viscosity
3.5 Viscosity Classification of Lubricants
3.6 Viscosity Index
3.7 Viscosity Change with Pressure
4 MINERAL OILS
4.1 General Characteristics
4.2 British Standard 4475 Commentary
4.3 Oil Additives
4.4 Synthetic Oils
5 GREASES
5.1 Composition
5.2 Properties
6 SOLID LUBRICANTS
7 SELECTION OF LUBRICANTS
8 OPERATING FACTORS
8.1 Filtration
8.2 Operating Temperatures
8.3 Total Loss Lubrication Systems
9 LUBRICANT SUPPLY AND SCHEDULING
9.1 Selection of Supplier
9.2 Lubrication Schedules
10 HEATH AND SAFETY
11 MONITORING & MAINTENANCE OF OIL IN SERVICE
11.1 Analyze or Change?
11.2 Visual Analysis
1 I.3 Laboratory Analysis
11.4 Contamination Problems
BIBLIOGRAPHY
APPENDICES
A VISCOSITY EQUIVALENTS
B SYMBOLS AND PREFERRED UNITS
FIGURES
I LUBRICANT CHANGE PERIODS AND TESTS
2 CHARACTERISTICS OF MINERAL LUBRICATING OILS VG32 TO VG 460.
3 SERVICE MONITORING AND MAINTENANCE OF OIL IN SERVICE ON LARGE SYSTEMS
TABLES
1 ISO VISCOSITY CLASSIFICATION
2 OILS TO BS 4475 RECOMMENDED FOR USE BY GBHE
3 SUGGESTED OIL CHANGE PERIODS FOR SMALL INDUSTRIAL SYSTEMS
4 VISUAL EXAMINATION OF USED LUBRICATING OILS
5 SUMMARY OF ROUTINE ANALYTICAL TESTS FOR INDUSTRIAL OILS
Shell and Tube Heat Exchangers Using Cooling Water
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
3.1 HTFS
3.2 TEMA
4 CHECKLIST
5 QUALITY OF COOLING WATER
6 COOLING WATER ON SHELL SIDE OR TUBE SIDE
7 COOLING WATER ON THE SHELL SIDE
7.1 Baffle Spacing
7.2 Impingement Plates
7.3 Horizontal or Vertical Shell Orientation
7.4 Baffle Cut Orientation
7.5 Sludge Blowdown
7.6 Removable Bundles
8 FOULING RESISTANCES AND LIMITING TEMPERATURES
9 PRESSURE DROP
9.1 Pressure Drop Restrictions
9.2 Fouling and Pressure Drop
9.3 Elevation of a Heat Exchanger in the Plant
10 MATERIALS OF CONSTRUCTION
11 WATER VELOCITY
11.1 Low Water Velocity
11.1.1 Tube Side Water Flow
11.1.2 Shell Side Water Flow
11.2 High Water Velocity
12 ECONOMICS
13 DIRECTION OF WATER FLOW
14 VENTS AND DRAINS
15 CONTROL
15.1 Operating Variables
15.2 Heat Load Control
15.2.1 General
15.2.2 Heat load control by varying cooling water flow
15.3 Orifice Plates
16 MAINTENANCE
Pipeline Design for Isothermal, Turbulent Flow of Non-Newtonian FluidsGerard B. Hawkins
Pipeline Design for Isothermal, Turbulent Flow of Non-Newtonian Fluids
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 DESCRIPTION OF ANOMALOUS EFFECTS
4.1 Wall Slip
4.2 Drag Reduction in Polymeric Materials
4.3 Transition Delay by Polymeric Materials
4.4 Drag Reduction in Suspensions
5 DESIGN PROCEDURE FOR PRESSURE DROP
IN TURBULENT PIPE FLOW IN THE ABSENCE
OF DRAG REDUCTION
5.1 Pressure Drop in the Absence of Wall Slip and
Drag Reduction
5.2 Wall Slip
5.3 Pipe Roughness
5.4 Pipe Fittings
6 DESIGN PROCEDURE FOR DRAG REDUCING
POLYMERIC MATERIALS
6.1 General
6.2 Transition Delay
6.3 Pipe Roughness
6.4 Pipe Fittings
7 DESIGN PROCEDURE FOR DRAG REDUCING
FIBRE SUSPENSIONS
8 BIBLIOGRAPHY
9 NOMENCLATURE
FIGURES
1 DRAG REDUCTION PHENOMENA
2 TRANSITION DELAY PHENOMENA
3 PROCEDURE FOR THE CALCULATION OF
PRESSURE DROP IN TURBULENT NON-NEWTONIAN
PIPE FLOW
4 TYPICAL RELATIONSHIP FOR Ψ VERSUS ʋ*
This document summarizes BASF's approach to sustainable building and infrastructure called BEYOND.High Performance. It provides integrated solutions to construction challenges by selecting sustainable materials, connecting clients with building experts, and recommending cost-effective solutions. BASF aims to preserve resources, provide energy efficient strategies, and make an impact throughout the built environment. The BASF Center for Building Excellence collaborates directly with clients to explore innovative approaches.
Mixing of Immiscible Liquids
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 EQUIPMENT
4.1 Agitated Tanks
4.2 Flow Mixers
4.3 'High Shear' Mixers
5 SYSTEM PHYSICAL PROPERTIES
5.1 Density
5.2 Viscosity
5.3 Interfacial Tension
6 STIRRED VESSELS
6.1 Design for Complete Dispersion
6.2 Prediction of Phase Inversion
6.3 Design for Mass Transfer
6.4 Design for Dispersed Phase Mixing
6.5 Hold-Up in Continuous Vessels
7 FLOW MIXERS
7.1 Design for Turbulent Conditions
7.2 Design for Laminar Conditions
TABLES
1 REYNOLDS NUMBER RANGES
FIGURES
1 STANDARD TANK CONFIGURATION
2 EXPERIMENTAL RELATIONSHIP BETWEEN MASS
TRANSFER COEFFICIENT AND POWER DENSITY
Air Cooled Heat Exchanger Design
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 SUITABILITY FOR AIR COOLING
4.1 Options Available For Cooling
4.2 Choice of Cooling System
5 SPECIFICATION OF AN AIR COOLED HEAT
EXCHANGER
5.1 Description and Terminology
5.2 General
5.3 Thermal Duty and Design Margins
5.4 Process Pressure Drop
5.5 Design Ambient Conditions
5.6 Process Physical Properties
5.7 Mechanical Design Constraints
5.8 Arrangement
5.9 Air Side Fouling
5.10 Economic Factors in Design
6 CONTROL
7 PRESSURE RELIEF
8 ASSESSMENT OF OFFERS
8.1 General
8.2 Manual Checking Of Designs
8.3 Computer Assessment
8.4 Bid Comparison
9 FOULING AND CORROSION
9.1 Fouling
9.2 Corrosion
10 OPERATION AND MAINTENANCE
10.1 Performance Testing
10.2 Air-Side Cleaning
10.3 Mechanical Maintenance
10.4 Tube side Access
11 REFERENCES
Hydrogen Compressors
Engineering Design Guide
1 SCOPE
2 PHYSICAL ROPERTIES
2.1 Data for Pure Hydrogen
2.2 Influence of Impurities
3 MATERIALS OF CONSTRUCTION
3.1 Hydrogen from Electrolytic Cells
3.2 Pure Hydrogen
4 DESIGN
4.1 Pulsation
4.2 Bypass
5 TESTING OR COMMISSIONING RECIPROCATING COMPRESSORS
6 LUBRICATION
7 LAYOUT
8 REFERENCES
FIGURES
1 MOLLIER CHART - HYDROGEN
2 COMPRESSIBILITY CHART
3 NELSON DIAGRAM
4 WATER CONTENT IN HYDROGEN FOR OIL-LUBRICATED COMPRESSORS AS GRAMM/M2 SWEPT CYLINDER AREA
Gas Solid Mixing
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 GAS-SOLID FLUIDIZED BED
5 MIXING IN FLUIDIZED BEDS
5.1 Group A Powders
5.2 Group B Powders
5.3 Group C Powders
5.4 Group D Powders
6 MECHANISMS OF MIXING AND SEGREGATION
6.1 Particle Segregation
6.2 Rate of Mixing
6.3 Solids Circulation
7 GRID DESIGN
7.1 Choice of Configuration
8 PLENUM CHAMBER DESIGN
9 SPOUTED BED
10 NOMENCLATURE
11 BIBLIOGRAPHY
FIGURES
1 POWDER CLASSIFICATION DIAGRAM FOR
FLUIDIZATION BY AIR
2 DIAGRAMMATIC REPRESENTATION OF MIXING BY A SINGLE RISING BUBBLE IN A BED OF SMALL
PARTICLES
3 SEGREGATION PATTERNS WITH 'PRACTICAL'
MATERIALS
4 SPOUTED BED – DIAGRAMMATIC
Pipeline Design for Isothermal, Laminar Flow of Non-Newtonian FluidsGerard B. Hawkins
Pipeline Design for Isothermal, Laminar Flow of Non-Newtonian Fluids
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 RHEOLOGICAL BEHAVIOR OF PURELY VISCOUS
NON-NEWTONIAN FLUIDS
4.1 Experimental Characterization
4.2 Rheological Models
5 PRESSURE DROP-FLOW RATE RELATIONSHIPS
BASED DIRECTLY ON EXPERIMENTAL DATA
5.1 Use of Shear Stress – Shear Rate Data
5.2 Tubular Viscometer Data
6 PRESSURE DROP – FLOW RATE RELATIONSHIPS BASED ON RHEOLOGICAL MODELS
7 LOSSES IN PIPE FITTINGS
7.1 Entrances Losses
7.2 Expansion Effects
7.3 Contraction Losses
7.4 Valves
7.5 Bends
8 EFFECT OF WALL SLIP
9 VELOCITY PROFILES
9.1 Velocity Profile from Experimental Flow-Curve
9.2 Velocity Profile from Rheological Model
9.3 Residence Time Distribution
10 CHECKS ON THE VALIDITY OF THE
DESIGN PROCEDURES
10.1 Rheological Behavior
10.2 Validity of Experimental Data
10.2 Check on Laminar Flow
11 NOMENCLATURE
12 REFERENCES
FIGURES
1 FLOW CURVES FOR PURELY VISCOUS FLUIDS
2 PLOTS OF D∆P/4L VERSUS 32Q/ɳD3 FOR PURELY VISCOUS FLUIDS
3 LOG-LOG PLOT OF t VERSUS ý
4 FLOW CURVE FOR A BINGHAM PLASTIC
5 LOG-LOG PLOT FOR A GENERALIZED BINGHAM
PLASTIC
6 CORRELATION OF ENTRANCE LOSS
7 CORRELATION OF EXPANSION LOSS
8 EFFECT OF “WALL SLIP” ON VELOCITY PROFILE
9 D∆P/4L VERSUS Q/ɳR3 WITH WALL SLIP
10 EVALUATION OFUs WITH Ʈw
11 VARIATION OF Us WITH Ʈw
12 PLOT OF D∆P/4L VERSUS 8 (ū- Us)/D FOR
CONDITIONS OF WALL SLIP
13 CUMULATIVE RESIDENCE TIME DISTRIBUTION
TO POWER LAW FLUIDS
14 EFFECTS OF TUBE LENGTH AND DIAMETER ON
RELATIONSHIP BETWEEN D∆P/4L AND 32Q/ɳD3
This document provides a summary of Tony L. De Vera's career and qualifications. He has over 25 years of experience managing research and development projects in industrial chemistry. Some of his accomplishments include developing new materials for biopharma and semiconductors, inventing organic-inorganic hybrid technologies, and optimizing chemical processes to increase efficiency and reduce costs. Currently he is commercializing enabling technologies through partnerships that are projected to generate $3 million in net income.
Stormw and Sanitary Trenchless RehabilitationSteve Neschleba
Highly engineered polymer that can be cast inside of an existing large diameter storm/sanitary sewer. This is an innovative structural repair system from Milliken Infrastructure. For more info please email steve.neschleba@milliken.com
Zach Szczepanski is seeking a position in industrial and organic chemistry. He has over 5 years of experience in polymer formulation, chemical analysis, and organic synthesis. His experience includes positions at Superior Essex as a Polymer Formulation Chemist, Cummins Inc. as a Chemist/Materials Engineer, and Albany Molecular Research as a Research Scientist. He has a Bachelor's degree in Chemistry from Indiana University Purdue University Fort Wayne with a GPA of 3.79.
This newsletter provides updates on various corrosion protection projects completed by Corrocoat and its partners around the world. In the first story, Corrocoat USA solved a costly corrosion problem for a pellet mill in the US by applying Plasmet HTE to protect an exhaust elbow. In other stories, Corrocoat Benelux provided long-term protection of flue ducts in gas desulphurization plants, Corroserve developed a coating system to protect road tankers transporting acidic waste, and Corrocoat Vietnam extended the life of power transformer insulators. The newsletter highlights many other successful applications of Corrocoat coatings around the world and in different industries.
The document discusses the challenges of developing offshore oil and gas fields, particularly in deep waters and remote locations. It notes that while offshore development technologies have enabled projects in up to 3,000m of water, developing fields in ultra-deep waters and frontier regions requires further technological advances. Specifically, it focuses on the need for high-capacity pipe-lay vessels using J-lay or reel-lay methods to install thick-walled pipes in these challenging environments, with each method having advantages depending on the characteristics of the specific field development project. Saipem's new flexible lay and construction vessel, the Normand Maximus, is presented as an innovative vessel designed to aid in ultra-deep water SURF installation and field
PETRONAS has developed a new pipeline repair technology called PIPEASSURE that can be applied underwater to repair pipelines damaged by corrosion or degradation. PIPEASSURE uses an epoxy-based composite material that is wrapped around pipelines and adheres strongly even in wet environments. It provides a minimally invasive repair method and extends pipeline lifespans with minimal downtime, saving oil and gas companies millions in lost revenue compared to traditional repair methods like underwater welding. Testing shows PIPEASSURE adheres much stronger than competing technologies and can withstand underwater conditions for 5 years.
Foam Assisted Surfactant-Alternating-Gas Injection for Heavy Oil Recovery thr...Antonio B. Mejia Jr.
This document proposes a method for producing heavy oil through permafrost in Alaska's North Slope region. A vertical well will be drilled and completed with two deviated laterals, one for injection and one for production. Carbon dioxide injection will be used to reduce oil viscosity and interfacial tension. Special casing, cementing, and insulation techniques will maintain permafrost integrity. Foam assisted surfactant-alternating gas injection combined with artificial lift will enable heavy oil production while preserving the permafrost layer.
Oil and gas pipelines are critical infrastructure that require effective corrosion protection to ensure long-term operational effectiveness. Internally coating pipelines with epoxy provides benefits like increased gas flow capacity, faster drying times, and reduced operational costs from decreased pumping needs. Externally, fusion-bonded epoxy coatings form an electrical barrier against corrosion and have proven effective for onshore and offshore pipelines. Pipeline coating technologies continue to evolve to meet industry needs for transporting oil and gas from more challenging environments.
This document discusses polyurethane coatings as an efficient solution for corrosion protection of onshore pipelines. Some key points:
1) Polyurethane coatings provide effective corrosion protection as a barrier for steel pipelines through their physical and chemical properties like adhesion, resistance to water and salts, and electrical insulation.
2) They are well-suited for pipeline applications due to properties like fast curing, good mechanical resistance, and compatibility with application and cathodic protection conditions.
3) International standards like EN 10290 ensure polyurethane coatings meet industry requirements for properties and performance over a wide temperature range for pipeline use.
This document discusses polyurethane coatings as an efficient solution for corrosion protection of onshore pipelines. Polyurethane coatings provide effective corrosion barriers for metal structures through their physical and chemical properties. They adhere well to steel substrates, resist corrosion through their barrier effect, and are resistant to chemicals in soils and water. Polyurethane coatings have been used successfully since the 1970s to protect pipelines due to these protective properties.
This document summarizes different methods of curing concrete and their effectiveness. It discusses that proper curing is crucial to obtaining design strength and maximum durability in concrete. Various curing methods are described, including ponding, fogging, wet coverings using burlap or impervious paper, membrane-forming compounds, internal curing using lightweight aggregates, leaving forms in place, and steam curing. Ponding and wet coverings using saturated materials are identified as most effective at maintaining moisture, while membrane compounds are more practical. The document concludes that curing method has a fundamental effect on concrete's mechanical properties and strengths. Immersion curing generally provides the best results.
Internal Coatings on the Rise - World Pipelines September 2016Craig Thomas
1) Internally coating gas transmission pipelines with epoxy provides enhanced gas flow and reduced operational costs. Over 60% of major oil and gas companies now specify these internal coatings.
2) Usage of internal coatings for gas pipelines has increased rapidly in the last decade and is expected to continue rising. Internal coatings allow for 14-21% increased pipeline capacity and provide benefits like reduced corrosion, optimized precommissioning, and lower energy costs.
3) In addition to flow enhancement, internal coatings provide protection from corrosion during storage and precommissioning, allowing for easier cleaning of pipelines and more rapid commissioning. Significant amounts of corrosion can form in uncoated pipes exposed to seawater during construction.
This case study describes corrosion issues in knock-out drums (KODs) used in oil and gas processing and a novel solution. KODs are susceptible to corrosion from chemicals like hydrogen sulfide, ammonia, and chlorides. A major US oil company needed protection for an ammonia acid gas KOD. Belzona 1523 and 1593 coatings were selected due to their high chemical resistance, temperature performance, and ability to withstand pressure fluctuations. The coatings were applied and successfully protected the KOD from corrosion in harsh conditions for over 7 years without need for replacement.
This paper summarizes the development of an innovative bearing and seal package for roller cone drill bits used in demanding applications. Analysis found that mud intrusion into seals was a primary cause of bit failure. A new dual dynamic seal design was created with harder elastomers and a central energizer to compensate for vibration. Field testing of 28 bits with the new design showed a 26.9% improvement in seal life compared to previous designs. The new seal package improved bit reliability in challenging wells with formation transitions in southwest Oklahoma.
International Journal of Engineering Research and Development (IJERD)IJERD Editor
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This document summarizes improvements in cutter technology that have led to faster drilling in hard, abrasive formations in the East Texas Basin. New cutter manufacturing processes using tighter diamond packing and synthesis under extreme high pressure/high temperature have yielded a highly abrasion resistant cutter. Field testing found the new cutter achieved around a 15% increase in rate of penetration while improving the condition of dull bits. Further refinements to the manufacturing process, including reducing residual stress through post-processing, have addressed challenges and produced a cutter that laboratory tests show has around a 10% reduction in diamond volume loss compared to previous cutters.
l The document discusses how applying an epoxy coating to the internal surface of gas pipelines can increase gas flow capacity and reduce operational costs. International oil and gas companies now commonly use internal pipeline coatings.
l Applying internal coatings can increase gas throughput by 10-20% by reducing surface roughness. Studies have shown coated pipelines require fewer compressor stations and use less fuel. Internal coatings also protect against corrosion during storage and make commissioning and inspection easier.
l Specifications for internal coatings aim to ensure coatings can withstand conditions like saltwater submersion and exposure to hydrocarbons. Developments include higher-solids and solvent-free coatings to reduce emissions while still meeting specifications.
Epoxy Coatings For Oil and Gas PipelinesDonald Jukee
Master Bond offers protective epoxy coatings for oil and gas pipelines that provide chemical and heat resistance. Current pipeline coating technologies have disadvantages, including requiring open flames for application which poses a safety risk. Master Bond coatings can be applied at ambient temperatures, are less toxic, and offer superior temperature resistance and protection from chemicals compared to other methods. They have formulations tailored for specific applications like natural gas pipelines and fuels containing ethanol.
Solutions that Integrate - White Paper Series Part III: Oil and Gas Connectio...NorthwireCable
Continuing LEMO and Northwire’s collaborative white paper series is an in-depth analysis of the extreme environmental factors and electrical, mechanical, regulatory, and end-user demands of the oil and gas industry. These fuel sources continue to be dominant players in energy production around the world, and the extraction and refinement of oil and natural gas is constantly being examined and improved to increase efficiency and lower costs.
The document discusses potential alternative materials for waterproofing in construction. It begins by outlining the importance of waterproofing and issues with high costs of standard materials. Potential substitutes for the liquid and powder components of standard two-part waterproofing mixtures are identified, including neem glue, tar, and Fevicol synthetic adhesive as substitutes for the liquid part and cement or lime as substitutes for the powder part. The document then provides details on standard waterproofing materials like MasterSeal 540 and K11 slurry to use as baselines for comparison. Further experiments are planned to evaluate suitable mixtures and costs.
Selecting the Correct Underslab MembraneW. R. Meadows
The document discusses underslab vapor retarders and their importance in controlling moisture movement below concrete slabs. It outlines how moisture can enter structures through liquid water, air, and water vapor transmission. Industry standards like ASTM and ACI are referenced which provide classifications for vapor retarders and guidelines on their proper installation. Both arguments for and against the use of cushion courses below vapor retarders are presented.
IRJET- Experimental Study on Durability Characteristics of Poly- Vinyl Alcoho...IRJET Journal
This study experimentally investigates the durability characteristics of concrete with partial replacement of coarse aggregate with polyvinyl alcohol (PVA) treated oil palm shell (OPS). Tests are conducted to determine the water absorption, sorptivity, compressive strength, volume of permeable voids, and salt ponding resistance of normal concrete versus concrete with 10-30% OPS replacement. Results show 30% OPS replacement concrete achieves maximum strength and durability. This concrete demonstrates improved water absorption, voids, and sorptivity over normal concrete, but has higher chloride penetration making it unsuitable for marine structures. Using PVA treated OPS can reduce construction costs due to use of an abundant agricultural waste as aggregate.
IRJET- Experimental Study on Durability Characteristics of Poly- Vinyl Alcoho...
WP_Extreme_2016 (2)
1. THE WAY
LINING
W
ith the expansion of
steam assisted gravity
drainage (SAGD) and
hydraulic fracturing (fracking)
production technology in North America over the
last 15 - 20 years, Canada and the US are now squarely positioned
amongst the world’s top producers of bitumen and natural gas.
Although the industry has experienced significant technological
advances in these processes, traditional lining systems used in the
industry to protect equipment assets are not keeping up with
the higher standards of protection required by these production
developments. As a result, owners and operators are turning to
their coating manufacturing vendor partners for new technology
solutions that will help ensure their facility structures and
infrastructures continue to keep up with global
production and environmental compliance demands.
Assessing the damage
The oil and gas industry has historically relied on linings systems
formulated from conventional epoxy phenolics, fusion bonded
epoxies, and novolac epoxies. These formulations have provided
fairly reliable protection over the years; however as SAGD and
fracking production processes continue to evolve, a troubling
pattern of systems failures is also emerging:
)) Ultra-high heat steam and harsh chemical additives are both
utilised in the SAGD and fracking processes to help loosen
the thick viscous bitumen found in underground oilsands
and natural gas deposits trapped inside tight shale and rock
Advanced oil
and gas production
processes raise the bar
on lining performance and
compliance requirements,
explain Stephen Streich
and Darryl Corbin,
AkzoNobel, USA.
2. formations. The continuous thermal cycling of extreme high
heat, followed by periods of cool down, combined with
chemical immersion and exposure, can severely compromise
a lining’s integrity and corrode the carbon steel substrate
underneath, causing ruptures.
)) Pipeline exteriors must have the durability to withstand the
abrasive elements of being buried below ground as well as
high temperature cathodic protection. Backfilling operations
and constant movement in the earth can cause rocks and
boulders to shift and scrape against the pipe causing cracks
in the coating material, which expose the steel substrate to
potentially corrosive soil. Likewise, pipeline interiors can also
crack when exposed to continuous radiating heat, chemical
attacks, and pressure of the water solution flowing through
the pipeline.
)) Onsite storage tanks and process vessels used in separating
the oil from the abrasive, chemically-laden water solutions
are especially susceptible to interior corrosion and leakage,
as are those used to clean and treat the toxic water after use.
Tank leakage can result in a complete halt in operation, often
costing millions in lost revenues while repairs are being made.
)) Without proper protection, rapid deterioration of pipeline
and tank interior and exterior linings can have a devastating
impact on the environment through contamination. Health
and safety concerns associated with these repairs and
re-linings must also be addressed each and every time
maintenance and repair operations are performed.
Finding the right protection
In order to properly identify and specify an appropriate lining
system for use in new pipeline or tank construction, maintenance
or repair projects, the owner or operator must first have a
thorough understanding of the operating conditions as well as
their ultimate objectives for installation of the lining system.
They must provide a detailed list of project operating
conditions and the owner’s expectations to the specifier, who
will in turn provide that information to the coating manufacturer.
That list will include items required to maintain proper
application, such as:
)) Variable operating temperatures.
)) Exact chemical concentrations used and duration of
exposure.
)) Abrasion and impact exposures, especially in below ground
pipeline installations.
)) Whether or not the pipeline or tank must be insulated.
)) Application capabilities of the contractor.
)) Climate conditions according to location (i.e. a dry, typically
warmer desert biome, or extreme low temperature tundra
biome such as the North Slope in Alaska).
)) Environmental conditions.
These factors will help the linings manufacturer recommend
and/or develop the appropriate lining technology to meet all of
these requirements and ensure compliance.
In addition, effective linings systems require the optimisation
of other material ingredients that might affect things like
wetting and levelling properties, flexibility, cure times, pot life
and VOC emissions. Together, these elements can make a big
impact on critical performance issues such as temperature and
chemical resistance, abrasion resistance, adhesion characteristics,
application properties and regulatory compliance. Most
importantly, these lining formulations must undergo extensive
laboratory and field testing to demonstrate and prove
effectiveness during actual in-service evaluation.
In an effort to address specific performance and compliance
issues associated with SAGD and fracking production processes,
AkzoNobel developed a proprietary high build, low volatile
compound (VOC) lining in 2004. That technology known as
Enviroline 405HT, has been repeatedly and rigorously tested for
more than a decade and has proven its effectiveness in field
applications across the globe, with successful results validating
its superior performance in high temperature and corrosive
environments.
Figure 1. The unique glass fibre and flake reinforced
technology offers improved durability and corrosion protection,
with efficient application to both interior and exterior of pipes.
Figure 2. Pipeline exteriors must be able to withstand the
abrasive elements of backfilling operations, being buried below
ground with shifting rocks and boulders, and high temperature
cathodic exposure. Cracks in the coating material can expose
the steel substrate to potentially corrosive soil.
REPRINTED FROM WORLD PIPELINES / / 2016
3. Building upon that same technology to raise the bar on
environmental compliance and improved performance in North
American and global applications, AkzoNobel introduced
Enviroline 405HTR into the oil and gas industry in 2015. This
product improvement is in line with the company’s core value of
sustainability.
A leader in global sustainability initiatives, the coatings
manufacturer celebrated its fourth consecutive year with a
number one ranking on the Dow Jones Sustainability Index within
the Materials Industry group.
The unique glass fibre and flake reinforced technology
offers added durability and protection within a broad range
of environments and temperatures – from continuous
immersion in chemicals including crude oil and hydrocarbon
water mixtures of up to 300˚F (149˚C) – to applications with
temperatures as low as 50˚F (10˚C). Highly durable and flexible,
the new formulation provides greater abrasion resistance
and high temperature cathodic protection for underground
pipeline applications and can be efficiently applied in both
the interiors and exteriors of the pipe. The ultra-fast cure
times enables piping to be handled faster and provides for
quicker throughput and increased production. In addition,
the improved substrate wetting and levelling properties
reduce the likelihood of holidays and lining defects, which
decreases the overall time required to identify and repair
lining imperfections. For a pipe manufacturer, this translates
to a speedier inspection process, operational throughput, and
greater efficiency.
These same features allow storage and process vessels to
return to service in as little as 14 hours after coating to minimise
production downtime. Environmental impact is further reduced
through the ultra-low VOC, single coat high build application
(20 - 60 mm), which will help extend the service life of structures
and infrastructures and provide significant savings in labour and
materials costs.
Maximising lining effectiveness
Proper surface preparation of steel substrates is critical for
achieving optimal lining performance – especially in high
temperature immersion conditions. Surfaces must be cleaned
and abrasive blasted to the SSPC SP-5 White Metal Blast
Cleaning standard with no detectable soluble salt limits for
better resistance to corrosive cell formation and coating
adhesion.
Provided that the manufacturer’s product test data meets
the performance requirements of a given project and proper
surface preparation has been completed, other factors
such as trained technical service can improve application
outcomes. For example, AkzoNobel has a dedicated team
of highly trained technical service managers that provide
ongoing customer support throughout the project, as well as
a web-based project and facility asset management program
called Interplan that can manage any coating/lining project
size from initial installation to decommissioning. This type of
support goes a long way in helping owners and maintenance
engineers identify the most urgent areas of repair and relining,
determine the projected cost of the lining installation,
estimated production downtime, and the schedule of facility
maintenance long-term.
Aligning with the future
Some oil and gas experts question whether or not these
advanced production processes will have ultimate cost and
environmental viability in the future, yet recent data indicates
that with better cost-control practices, a clearly defined
project scope during planning to avoid unanticipated events
and ongoing technical process improvements will all play
an important role in these production processes, becoming
established players in large-scale commercial projects long-
term. Indeed, SAGD alone is already being hailed as one of the
least invasive production techniques with lower environmental
impact over conventional open-pit oilsands operations – and
with the highest recovery rate of up to 80%.
Owners staking a claim in this production technology will
continue to strive for operational excellence, better regulatory
compliance and improved cost-efficiencies. Being aligned
with coating manufacturing vendor partners who have shared
innovative vision, a commitment to sustainable practices that
enhance the quality of human lives and the planet, and who
continually seek ways to improve customer productivity and
profitability will help them realise those goals now – and well
into the future.
Table 1. Testing procedures used to evaluate external buried
pipeline coatings for suitability
Test Acceptance
criteria
Test type 405HTR
results
Film thickness Manufacturers
recommendations
SSPC-PA2 20 - 60 mm
DFT
Shore D
hardness
Manufacturers
recommendations
Clause 12.1 of
the standard
80+
28 day cathodic
disbondment at
maximum rate
10 mm maximum
radius
CSA Z245.20,
clause 12.8
5.2 mm at
203˚F (95˚C)
1.5J impact
resistance
No holiday CSA Z245.20,
clause 12.12
Pass
3.0J impact
resistance
No holiday CSA Z245.20,
clause 12.12
Pass
*Testing procedures carried out via CAN/CSA Z245.30-14, coating
type FC1 requirements: liquid-applied or fusion bond epoxy (FBE)
with glass transition temperature of up to 239˚F (115˚C).
Table 2. Additional testing conducted
Test Test type 405HTR results
Adhesion ASTM D4541 Standard
test method of pull-off
strength of coatings
using portable adhesion
testers
Steel: >1500 psi, 11 MPa
Abrasion
resistance
ASTM D4060 CS17 –
wheel 1 kg load, 1000
cycles
65 mg
Elevated
temperature
ASTM D5499 method A 400˚F (204˚C) continuous
exposure
Flexibility
ASTM D5043 standard
test method for plane-
strain fracture touchness
and strain energy
release rate for plastic
materials
Average flexural strength
54 MPa, average flexural
strain 1.55%, average
flexural modulus 4324
MPa
REPRINTED FROM WORLD PIPELINES / / 2016 EX