Search
Filters
Close

11069 Predicting Iron Production From Sweet Gas-Condensate Pipelines

Product Number: 51300-11069-SG
ISBN: 11069 2011 CP
Author: Michel R. Bonis and Per Tobiassen
Publication Date: 2011
$0.00
$20.00
$20.00
This paper describes a very simple model built to predict the quantities of dissolved iron and corrosion products which can be produced from sweet gas condensate pipelines. The key drivers of this model are fully described and compared to practical operational experience.

Several documented field cases are used to confront the hypotheses used and to determine relevant corrosion criteria.

In particular, it is shown that corrosion mitigation using MEG + pH control reduces the average bottom line corrosion rate down to 1 to 3 µm/yr, while corrosion inhibition will only reduce it to the range of 20 to 50 µm/yr depending on the operating temperatures, or up to 75- 80 µm/yr for temperatures higher than 80- 90°C. These corrosion rates still do not jeopardize pipeline integrity.

It is also shown from these field results that iron contents exceeding 100 to 200 mg/l at the outlet of sweet gas pipelines are not necessarily alarming. For quite long pipelines these counts correspond to fully acceptable residual corrosion rates. In case of such high iron levels, the present model and the associated residual corrosion criteria can be used to compare these iron contents with predictions.

Pre-existing corrosion products from mill scale and atmospheric rusting are also evaluated in this approach. The huge amount of rust formed on the surface of pipes prior to laying is particularly troublesome when no precaution is taken to minimize atmospheric corrosion during storage or to remove this rust after installation. Large pipelines of a few hundred kilometers may contain up to several hundreds of tons of rust which may dramatically impact downstream gas receiving facilities. This is a key factor in the decision to apply an internal coating in long and large gas export pipelines.

Keywords: CO2 corrosion, corrosion products, dissolved iron, solids, rust, mill scale
This paper describes a very simple model built to predict the quantities of dissolved iron and corrosion products which can be produced from sweet gas condensate pipelines. The key drivers of this model are fully described and compared to practical operational experience.

Several documented field cases are used to confront the hypotheses used and to determine relevant corrosion criteria.

In particular, it is shown that corrosion mitigation using MEG + pH control reduces the average bottom line corrosion rate down to 1 to 3 µm/yr, while corrosion inhibition will only reduce it to the range of 20 to 50 µm/yr depending on the operating temperatures, or up to 75- 80 µm/yr for temperatures higher than 80- 90°C. These corrosion rates still do not jeopardize pipeline integrity.

It is also shown from these field results that iron contents exceeding 100 to 200 mg/l at the outlet of sweet gas pipelines are not necessarily alarming. For quite long pipelines these counts correspond to fully acceptable residual corrosion rates. In case of such high iron levels, the present model and the associated residual corrosion criteria can be used to compare these iron contents with predictions.

Pre-existing corrosion products from mill scale and atmospheric rusting are also evaluated in this approach. The huge amount of rust formed on the surface of pipes prior to laying is particularly troublesome when no precaution is taken to minimize atmospheric corrosion during storage or to remove this rust after installation. Large pipelines of a few hundred kilometers may contain up to several hundreds of tons of rust which may dramatically impact downstream gas receiving facilities. This is a key factor in the decision to apply an internal coating in long and large gas export pipelines.

Keywords: CO2 corrosion, corrosion products, dissolved iron, solids, rust, mill scale
Product tags
Also Purchased
Picture for 09356 Corrosion Management of the Karachaganak Gas/Condensate Field
Available for download

09356 Corrosion Management of the Karachaganak Gas/Condensate Field

Product Number: 51300-09356-SG
ISBN: 09356 2009 CP
Author: John M. Graham and Philip A. Attwood
Publication Date: 2009
$20.00
Picture for 10327 Corrosion Control in Vega Gas-Condensate Pipeline
Available for download

10327 Corrosion Control in Vega Gas-Condensate Pipeline

Product Number: 51300-10327-SG
ISBN: 10327 2010 CP
Author: Jan Ivar Skar and Anne Marie Koren Halvorsen
Publication Date: 2010
$20.00
Picture for 98100 EXPERIENCES IN PRODUCTION AND CORROSION
Available for download

98100 EXPERIENCES IN PRODUCTION AND CORROSION MONITORING FOR A GAS CONDENSATE FIELD CONTAINING CO2

Product Number: 51300-98100-SG
ISBN: 98100 1998 CP
Author: Markus Oberndorfer, Karin Dornstauder, Walter Brunner
$20.00