Numerical Study of CH<sub>4</sub> Generation and Transport in XLPE-Insulated Cables in Continuous Vulcanization
In this work, we apply a computational diffusion model based on Fick’s laws to study the generation and transport of methane (CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics&...
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doaj-e0fbd59e952743cb97c20b3e663e106c2020-11-25T03:04:03ZengMDPI AGMaterials1996-19442020-07-01132978297810.3390/ma13132978Numerical Study of CH<sub>4</sub> Generation and Transport in XLPE-Insulated Cables in Continuous VulcanizationMohd Fuad Anwari Che Ruslan0Dong Joon Youn1Roshan Aarons2Yabin Sun3Shuyu Sun4Computational Transport Phenomena Laboratory, King Abdullah University of Science and Technology, Thuwal 23955, Saudi ArabiaComputational Transport Phenomena Laboratory, King Abdullah University of Science and Technology, Thuwal 23955, Saudi ArabiaDow Chemical Europe, 8810 Horgen, SwitzerlandDow Chemical (China) Investment Co., Ltd., Shanghai 200203, ChinaComputational Transport Phenomena Laboratory, King Abdullah University of Science and Technology, Thuwal 23955, Saudi ArabiaIn this work, we apply a computational diffusion model based on Fick’s laws to study the generation and transport of methane (CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula>) during the production of a cross-linked polyethylene (XLPE) insulated cable. The model takes into account the heating process in a curing tube where most of the cross-linking reaction occurs and the subsequent two-stage cooling process, with water and air as the cooling media. For the calculation of CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> generation, the model considers the effect of temperature on the cross-linking reaction selectivity. The cross-linking reaction selectivity is a measure of the preference of cumyloxy to proceed either with a hydrogen abstraction reaction, which produces cumyl alcohol, or with a <inline-formula> <math display="inline"> <semantics> <mi>β</mi> </semantics> </math> </inline-formula>-scission reaction, which produces acetophenone and CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula>. The simulation results show that, during cable production, a significant amount of CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> is generated in the XLPE layer, which diffuses out of the cable and into the conductor part of the cable. Therefore, the diffusion pattern becomes a non-uniform radial distribution of CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> at the cable take-up point, which corresponds well with existing experimental data. Using the model, we perform a series of parametric studies to determine the effect of the cable production conditions, such as the curing temperature, line speed, and cooling water flow rate, on CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> generation and transport during cable production. The results show that the curing temperature has the largest impact on the amount of CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> generated and its distribution within the cable. We found that under similar curing and cooling conditions, varying the line speed induces a notable effect on the CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> transport within the cable, while the cooling water flow rate had no significant impact.https://www.mdpi.com/1996-1944/13/13/2978cable insulationXLPEcontinuous vulcanization linecross-linking reactionbyproduct degassingreaction selectivity |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Mohd Fuad Anwari Che Ruslan Dong Joon Youn Roshan Aarons Yabin Sun Shuyu Sun |
spellingShingle |
Mohd Fuad Anwari Che Ruslan Dong Joon Youn Roshan Aarons Yabin Sun Shuyu Sun Numerical Study of CH<sub>4</sub> Generation and Transport in XLPE-Insulated Cables in Continuous Vulcanization Materials cable insulation XLPE continuous vulcanization line cross-linking reaction byproduct degassing reaction selectivity |
author_facet |
Mohd Fuad Anwari Che Ruslan Dong Joon Youn Roshan Aarons Yabin Sun Shuyu Sun |
author_sort |
Mohd Fuad Anwari Che Ruslan |
title |
Numerical Study of CH<sub>4</sub> Generation and Transport in XLPE-Insulated Cables in Continuous Vulcanization |
title_short |
Numerical Study of CH<sub>4</sub> Generation and Transport in XLPE-Insulated Cables in Continuous Vulcanization |
title_full |
Numerical Study of CH<sub>4</sub> Generation and Transport in XLPE-Insulated Cables in Continuous Vulcanization |
title_fullStr |
Numerical Study of CH<sub>4</sub> Generation and Transport in XLPE-Insulated Cables in Continuous Vulcanization |
title_full_unstemmed |
Numerical Study of CH<sub>4</sub> Generation and Transport in XLPE-Insulated Cables in Continuous Vulcanization |
title_sort |
numerical study of ch<sub>4</sub> generation and transport in xlpe-insulated cables in continuous vulcanization |
publisher |
MDPI AG |
series |
Materials |
issn |
1996-1944 |
publishDate |
2020-07-01 |
description |
In this work, we apply a computational diffusion model based on Fick’s laws to study the generation and transport of methane (CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula>) during the production of a cross-linked polyethylene (XLPE) insulated cable. The model takes into account the heating process in a curing tube where most of the cross-linking reaction occurs and the subsequent two-stage cooling process, with water and air as the cooling media. For the calculation of CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> generation, the model considers the effect of temperature on the cross-linking reaction selectivity. The cross-linking reaction selectivity is a measure of the preference of cumyloxy to proceed either with a hydrogen abstraction reaction, which produces cumyl alcohol, or with a <inline-formula> <math display="inline"> <semantics> <mi>β</mi> </semantics> </math> </inline-formula>-scission reaction, which produces acetophenone and CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula>. The simulation results show that, during cable production, a significant amount of CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> is generated in the XLPE layer, which diffuses out of the cable and into the conductor part of the cable. Therefore, the diffusion pattern becomes a non-uniform radial distribution of CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> at the cable take-up point, which corresponds well with existing experimental data. Using the model, we perform a series of parametric studies to determine the effect of the cable production conditions, such as the curing temperature, line speed, and cooling water flow rate, on CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> generation and transport during cable production. The results show that the curing temperature has the largest impact on the amount of CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> generated and its distribution within the cable. We found that under similar curing and cooling conditions, varying the line speed induces a notable effect on the CH<inline-formula> <math display="inline"> <semantics> <msub> <mrow></mrow> <mn>4</mn> </msub> </semantics> </math> </inline-formula> transport within the cable, while the cooling water flow rate had no significant impact. |
topic |
cable insulation XLPE continuous vulcanization line cross-linking reaction byproduct degassing reaction selectivity |
url |
https://www.mdpi.com/1996-1944/13/13/2978 |
work_keys_str_mv |
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