Server maintenance is scheduled for Saturday, December 21st between 6am-10am CST.
During that time, parts of our website will be affected until maintenance is completed. Thank you for your patience.
Use GIVING24 at checkout to save 20% on eCourses and books (some exclusions apply)!
In hydrocarbon production systems, mild steel is overwhelmingly used for the construction of pipelines and tanks for the transmission and storage of crude oil, natural gas, and derived petroleum products. Although mild steel has excellent mechanical properties and low cost, it is susceptible to corrosion attack in typical service environments. Inhibition of internal corrosion is essential for assuring asset integrity of oil and gas transportation pipelines.
In the oil and gas industry, carbon steel is widely used in the construction of infrastructure, such as pipelines and tanks, for the transmission and storage of crude oil as well as petroleum products. This is due to its excellent mechanical properties, ease to work with, and low cost. However, it is vulnerable to corrosion. Ionic surfactant type of corrosion inhibitors have been widely applied against pipeline corrosion due to their high mitigation efficiency at low applied concentrations. Corrosion inhibition efficiency is closely related to the inhibitor adsorption mechanism. However, past corrosion inhibition research has generally focused on the electrochemical mechanisms of inhibition processes and associated corrosion rate reductions. In this current work, in situ tapping mode AFM phase imaging and contact mode AFM nano-scratching techniques have been applied to investigate the influence of different tetradecylbenzyldimethylammonium (BDA-C14) concentrations on inhibitor adsorption morphology and inhibition mechanisms. Analysis of tapping mode topography and phase images on mica show that multiple small holes/defects were present in the uniform inhibitor film at 50 and 100 ppm, which are above the surface saturation concentration. While at 25 ppm (below the surface saturation concentration), a non-uniform inhibitor film with different sizes of holes was detected. At 5 ppm, discontinuous inhibitor aggregates were observed. The contact mode AFM scratching technique was used to obtain the inhibitor film thickness at each concentration, which was consistent with the corresponding depth of holes measured by tapping mode topography. The molecular orientations and inhibitor film structures at each concentration are postulated based on the measured inhibitor film thickness. Observed adsorption morphologies on mica are connected with the corrosion inhibition behavior observed on UNS G1018 steel at each concentration.
Fired heaters in coking service are susceptible to carburization damage, which needs to be predicted and managed to prevent unexpected downtime and expedited replacement costs. Carburization damage occurs when carbonaceous material, i.e., coke, is deposited on a steel surface and exposed to high metal temperatures; such are the internal conditions present in fired heater tubes in coking services. At these high temperatures, the carbon diffuses into the steel microstructure and increases the hardness while reducing ductility. At an advanced state, this reduction in ductility may lead to tube failure if a mechanical or thermal shock is applied. The diffusion of carbon can also cause the formation of deleterious chromium carbides in the steel microstructure, reducing the high temperature corrosion resistance in those areas.
We are unable to complete this action. Please try again at a later time.
If this error continues to occur, please contact AMPP Customer Support for assistance.
Error Message:
Please login to use Standards Credits*
* AMPP Members receive Standards Credits in order to redeem eligible Standards and Reports in the Store
You are not a Member.
AMPP Members enjoy many benefits, including Standards Credits which can be used to redeem eligible Standards and Reports in the Store.
You can visit the Membership Page to learn about the benefits of membership.
You have previously purchased this item.
Go to Downloadable Products in your AMPP Store profile to find this item.
You do not have sufficient Standards Credits to claim this item.
Click on 'ADD TO CART' to purchase this item.
Your Standards Credit(s)
1
Remaining Credits
0
Please review your transaction.
Click on 'REDEEM' to use your Standards Credits to claim this item.
You have successfully redeemed:
Go to Downloadable Products in your AMPP Store Profile to find and download this item.
Traditionally, sour severity of high-pressure, high temperature (HPHT) oil and gas production wells were assessed by H2S partial pressure (PH2S): The mole fraction of H2S in the gas (yH2S) multiplied by the total pressure (PT). While PH2S is appropriate for characterizing the sour severity of wellbores operating at low total pressures (e.g., PT < 35 MPa) and/or for highly sour systems (e.g., yH2S > 1 mol%), PH2S usually over-predicts the actual sour severity of HPHT systems, leading to sub-optimal material selection options.
Additive manufacturing (AM) is a transformative technology that has opened areas of design space that were previously inaccessible by enabling the production of complex, three-dimensional parts and intricate geometries that were impractical to produce via traditional manufacturing methods. However, the extreme thermo-mechanical conditions in the AM build process (e.g., cooling rates ranging from 103 K/sto 106 K/s and repeated heating/cooling cycles) generate deleterious microstructures with high residual stresses, and extreme compositional gradients.