Menu
Search
Filters
Close
Menu

Save 20% on select titles with code HIDDEN24 - Shop The Sale Now

00043 INHIBITION OF MULTIPHASE WET GAS CORROSION

Picture for 00043 INHIBITION OF MULTIPHASE WET GAS
Available for download
Product Number: 51300-00043-SG
ISBN: 00043 2000 CP
Author: D. Vedapuri, C. Kang, D. Dhanabalan and M. Gopal
$0.00
$20.00
$20.00
Corrosion rates at the top and bottom of the pipe have been measured in wet gas multiphase flow at carbon dioxide partial pressures of 0.46 MPa and 0.79 MPa and temperatures of 40 C and 60 C in a high pressure 10-cm diameter system. Gas velocities up to 30 lm/s and liquid velocities up to 0.5 m/s were used. The liquid consisted of a mixture of de-ionized water and low viscosity oil at two water cuts of 80% and 40%, and carbon dioxide was used in the gas phase. Corrosion inhibition studies were carried out at 50 ppm and 100 ppm dosage levels. The inhibitor used was an oleic imidazoline active compound dissolved in isopropyl alcohol and water. The corrosion rate was found to increase with increase in gas velocity, liquid velocity, temperature and CO2 partial pressure. The corrosion rate at the top of the pipe is negligible up to a gas velocity of 20 m/s. However, at a gas velocity of 30 m/s, there is substantial and measurable corrosion at the top of the pipe. This was attributed to wave spreading. Addition of inhibitors reduced the corrosion rate at the top and bottom of the pipe significantly. However, the corrosion rates are not negligible.
Corrosion rates at the top and bottom of the pipe have been measured in wet gas multiphase flow at carbon dioxide partial pressures of 0.46 MPa and 0.79 MPa and temperatures of 40 C and 60 C in a high pressure 10-cm diameter system. Gas velocities up to 30 lm/s and liquid velocities up to 0.5 m/s were used. The liquid consisted of a mixture of de-ionized water and low viscosity oil at two water cuts of 80% and 40%, and carbon dioxide was used in the gas phase. Corrosion inhibition studies were carried out at 50 ppm and 100 ppm dosage levels. The inhibitor used was an oleic imidazoline active compound dissolved in isopropyl alcohol and water. The corrosion rate was found to increase with increase in gas velocity, liquid velocity, temperature and CO2 partial pressure. The corrosion rate at the top of the pipe is negligible up to a gas velocity of 20 m/s. However, at a gas velocity of 30 m/s, there is substantial and measurable corrosion at the top of the pipe. This was attributed to wave spreading. Addition of inhibitors reduced the corrosion rate at the top and bottom of the pipe significantly. However, the corrosion rates are not negligible.
PRICE BREAKS - The more you buy, the more you save
Quantity
1+
5+
Price
$20.00
$20.00
Product tags
Also Purchased
Picture for 00042 CO2 AND H2S CORROSION OF API 5L-B AND
Available for download

00042 CO2 AND H2S CORROSION OF API 5L-B AND 5L-X52 GRADE STEELS

Product Number: 51300-00042-SG
ISBN: 00042 2000 CP
Author: J.J. Perdomo, J.L. Morales, A. Viloria, A.J. Lusinchi
Publication Date: 2000
$20.00
Picture for 00040 EFFECT OF CRUDE OIL CONTAMINANTS ON THE
Available for download

00040 EFFECT OF CRUDE OIL CONTAMINANTS ON THE INTERNAL CORROSION IN GAS PIPELINES

Product Number: 51300-00040-SG
ISBN: 00040 2000 CP
Author: J.L. Morales, J.J. Perdomo, M. Ramirez, A. Viloria
$20.00
Picture for 00055 Inhibitor Selection for Internal Corrosion
Available for download

00055 Inhibitor Selection for Internal Corrosion Control of Pipelines: Comparison of Rates of General Corrosion and Pitting Corrosion under Gassy-Oil Pipeline Conditions

Product Number: 51300-00055-SG
ISBN: 00055 2000 CP
Author: S. Papavinasam, R.W. Revie, M. Attard, A. Demoz, H. Sun, J.C. Donini, and K. Michaelian
$20.00
Categories
Industry
Recently viewed
Popular tags
View all

Association for Materials Protection and Performance

© AMPP All Rights Reserved.
Membership Terms of Content Use
Contact Customer Support