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Picture for New Test Method for Measurement of Water-Soluble Corrosion Inhibitor Residual in Oil Samples for Low Water-Cut Oil System
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New Test Method for Measurement of Water-Soluble Corrosion Inhibitor Residual in Oil Samples for Low Water-Cut Oil System

Product Number: 51321-16344-SG
Author: Anwaar Al Kindi/Anwaar Al Kindi/Emilya Abdullayeva/Monica Fernandez/Hecham M.Ali
Publication Date: 2021
$20.00
New Test Requirement for Evaluating Temperature Resistance of Nonskid Coatings
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New Test Requirement for Evaluating Temperature Resistance of Nonskid Coatings

Product Number: 51218-155-SG
Author: Colton Spicer, Cameron Miller, James Tagert, John Wegand, Bruce Nelson
Publication Date: 2018
$20.00
Picture for New Thermal Management Raw Materials Platform Gives Flexibility to Develop Next Generation Thermal Insulation Coatings (TIC) with Improved Performance
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New Thermal Management Raw Materials Platform Gives Flexibility to Develop Next Generation Thermal Insulation Coatings (TIC) with Improved Performance

Product Number: 51324-20913-SG
Author: Gary Fisher
Publication Date: 2024
$40.00
Picture for New Two-Stage Corrosion Protection System Extends the Life of Concrete Structures
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New Two-Stage Corrosion Protection System Extends the Life of Concrete Structures

Product Number: 51319-13011-SG
Author: David Whitmore
Publication Date: 2019
$20.00

Corrosion of reinforcing steel is a leading cause of concretedeterioration such as spalling cracking and delamination of reinforced concrete structures.This paper describes a new self-powered two stage anode system used to control corrosion in reinforced concrete structures. This two-stage system combines the high level performance of an impressed current cathodic protection system (ICCP) with the long-term maintenance-free capabilities of an alkali-activated galvanic cathodic prevention system (GCP).Impressed current and galvanic corrosion protection systems are beneficial in extending the service life ofchloride contaminated and damaged concrete structures. ICCP systems are typically powered by an outside DC power source such as a transformer/rectifier and can provide a lifetime of corrosion protection if suitably maintained. Galvanic systems use metals such as zinc that are more electronegative than steel in concrete. Galvanic systems are often used when simplicity is desired as there is no power supply involved and maintenance is minimal.This single-unit second generation hybrid system does not require complex wiring or an external DC power supply. Once installed the anode automatically provides an initial phase of high charge density that passivates active corrosion (Stage 1). The anode automatically switches to provide long-term maintenance-free galvanic protection (Stage 2) when the impressed current stage is complete.As a result this self-powered two-stage system provides a long-term maintenance-free corrosion protection alternative for reinforced concrete structures.

Picture for New Understanding on Calcium Carbonate Scaling Kinetics
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New Understanding on Calcium Carbonate Scaling Kinetics

Product Number: 51319-12935-SG
Author: Qiwei Wang
Publication Date: 2019
$20.00

Calcium carbonate (CaCO3) is the predominate type of mineral scale formed in many industrial water processes including oil and gas production. Comprehensive and accurate knowledge on the CaCO3 scaling risk is critical for the effective scale management. Currently scale risk assessment is largely depends on thermodynamic simulation which predicts the saturation state under given conditions there are very limited experimental or field data on scaling kinetics. Previous works on temperature effect were investigated on nucleation and precipitation in bulk solutions which didn’t involve the CaCO3 adhesion and accumulation on existing surface. The pressure effect is considered in scaling tendency calculation but its potential impact on scaling kinetics is usually neglected.This paper presents the laboratory results of CaCO3 scaling kinetics at various temperatures (80-150°C) and pressures (500-5000 psia). Tests were conducted with a dynamic tube blocking apparatus which measures CaCO3 scale buildup by monitoring hydrostatic pressure differential (DP) across a capillary tubing and the time for scale formation was determined. Test waters were maintained at similar CaCO3 supersaturation state at different temperatures and pressures by adjusting bicarbonate concentration. Results show that under the test conditions scaling rate was accelerated by both temperature and pressure. CaCO3 scaling time was shortened approximately 2 times when pressure was increased from 500 psi to 5000 psi at the same temperature and similar supersaturation state. For examples scaling timeis decreased from ~65minutes to ~40minutes at 80°C and from ~40 minutes to < 20 minutes at 125°C with pressure changed from 500 psi to 5000 psi..This study provides new understanding on the mineral scaling kinetics by identifying the pressure dependence of CaCO3 scale formation process. Experimental results show that pressure other than its impact on solubility has additional kinetic effect on CaCO3 scaling rate. This kinetic effect should be included in the scaling risk assessment especially for the high pressure systems.