Search engine for discovering works of Art, research articles, and books related to Art and Culture
ShareThis
Javascript must be enabled to continue!

Standards for Evaluating Oil Field Corrosion Inhibitors in the Laboratory

View through CrossRef
Abstract The success of a corrosion inhibitor in controlling internal corrosion depends on (1) when the application of it has started, (2) efficiency of it, (3) interference of it with other chemicals and processes, and (4) presence of intact inhibitor film on the surface to be protected. Several standards and industry best practices are available to evaluate these properties. They include: ASTM(A) G170, “Standard Guide for Evaluating and Qualifying Oilfield and Refinery Corrosion Inhibitors in the Laboratory”ASTM G184, “Standard Practice for Evaluating and Qualifying Oil Field and Refinery Corrosion Inhibitors using Rotating Cage”ASTM G185, “Standard Practice for Evaluating and Qualifying Oil Field and Refinery Corrosion Inhibitors using Rotating Cylinder Electrode”ASTM G202, “Standard Test Method for Using Atmospheric Pressure Rotating Cage”ASTM G205, “Standard Guide for Determining Corrosivity of Crude Oils”ASTM G208, “Standard Practice for Evaluating and Qualifying Oil Field and Refinery Corrosion Inhibitors using Jet Impingement”NACE 1D182, “Wheel Test Method Used for Evaluation of Film-Persistent Corrosion Inhibitors for Oil Field Applications”NACE 1D196, “Laboratory Test Methods for Evaluating Oil Field Corrosion Inhibitors”European Federation of Corrosion (EFC)(B), “Test Methods for Corrosion Inhibitors”, Working Party Report #11 (1985)EFC, “Corrosion Inhibitors for Oil and Gas Production”, Working Party Report #39, 2004 This paper describes these standards, explains hierarchy of standards, and provides guidelines to obtain reliable and relevant data on corrosion inhibitors from laboratory.
Title: Standards for Evaluating Oil Field Corrosion Inhibitors in the Laboratory
Description:
Abstract The success of a corrosion inhibitor in controlling internal corrosion depends on (1) when the application of it has started, (2) efficiency of it, (3) interference of it with other chemicals and processes, and (4) presence of intact inhibitor film on the surface to be protected.
Several standards and industry best practices are available to evaluate these properties.
They include: ASTM(A) G170, “Standard Guide for Evaluating and Qualifying Oilfield and Refinery Corrosion Inhibitors in the Laboratory”ASTM G184, “Standard Practice for Evaluating and Qualifying Oil Field and Refinery Corrosion Inhibitors using Rotating Cage”ASTM G185, “Standard Practice for Evaluating and Qualifying Oil Field and Refinery Corrosion Inhibitors using Rotating Cylinder Electrode”ASTM G202, “Standard Test Method for Using Atmospheric Pressure Rotating Cage”ASTM G205, “Standard Guide for Determining Corrosivity of Crude Oils”ASTM G208, “Standard Practice for Evaluating and Qualifying Oil Field and Refinery Corrosion Inhibitors using Jet Impingement”NACE 1D182, “Wheel Test Method Used for Evaluation of Film-Persistent Corrosion Inhibitors for Oil Field Applications”NACE 1D196, “Laboratory Test Methods for Evaluating Oil Field Corrosion Inhibitors”European Federation of Corrosion (EFC)(B), “Test Methods for Corrosion Inhibitors”, Working Party Report #11 (1985)EFC, “Corrosion Inhibitors for Oil and Gas Production”, Working Party Report #39, 2004 This paper describes these standards, explains hierarchy of standards, and provides guidelines to obtain reliable and relevant data on corrosion inhibitors from laboratory.

Related Results

Evaluating Corrosion Inhibitors For Sour Gas Subsea Pipelines
Evaluating Corrosion Inhibitors For Sour Gas Subsea Pipelines
Abstract Using subsea carbon steel pipelines to transport wet sour gas possesses huge challenges to the operators to maintain the high level of the Assets and Ope...
Spectral Analysis Of CO2 Corrosion Product Scales On 13Cr Tubing Steel
Spectral Analysis Of CO2 Corrosion Product Scales On 13Cr Tubing Steel
Abstract CO2 corrosion product scales formed on 13Cr tubing steel in autoclave and in the simulated corrosion environment of oil field are investigated in the pap...
Corrosion Of Copper-Base Alloys In A Geothermal Brine
Corrosion Of Copper-Base Alloys In A Geothermal Brine
Abstract The geothermal environment and the experimental procedures and schedules for corrosion tests of copper-base procedures and schedules for corrosion tests ...
Fragrant Flower Extracts as Corrosion Inhibitors in the Oil and Gas Industry
Fragrant Flower Extracts as Corrosion Inhibitors in the Oil and Gas Industry
Abstract Corrosion inhibitors used in the petroleum industry are a necessity to include in any acid job. When corrosion occurs to downhole tubulars and equipment, hu...
Effect of Organic and Inorganic Corrosion Inhibitors on Strength Properties of Concrete
Effect of Organic and Inorganic Corrosion Inhibitors on Strength Properties of Concrete
In the current study, the M25 grade concrete mixes are admixed with various locally available organic and non-organic corrosion inhibitors such as Calcium Nitrite, Sodium Nitrite, ...
Two-dimensional numerical analysis of differential concentration corrosion in seawater pipeline
Two-dimensional numerical analysis of differential concentration corrosion in seawater pipeline
Purpose The purpose of this paper is to develop a new two-dimensional differential concentration corrosion mathematical model based on the knowledge that oxygen distribution on the...
Predictive Modeling for Corrosion Rate on Pipeline Corrosion in Seawater
Predictive Modeling for Corrosion Rate on Pipeline Corrosion in Seawater
ABSTRACT Marine oil pipelines are critical for the transportation of oil and gas from offshore production facilities to onshore processing plants. However, exposure ...

Back to Top