1
Chemically Bonded, Porcelain Enamel Coated Pipe for Corrosion Protection and Flow Efficiency Acknowledgments This project is funded by DOT/PHMSA’s Competitive Academic Agreement Program under Contract No. DTPH5615HCAP10. Liang Fan 1 , Genda Chen 1 , Michael L. Koenigstein 2 1. Department of Civil, Architectural, and Environmental Engineering Missouri University of Science and Technology, Rolla, MO 65409-0030, United States 2. Pro-Perma Engineered Coatings, Roesch Inc., Belleville, IL 62226, United States Main Objective The aims of this project are to explore chemically-bonded porcelain enamel coating for corrosion protection and safety of metallic pipes, and to develop a rapid field-applicable coating process for flow efficiency and cost reduction in the operation of metallic pipelines. Figure 1. Enameling: wet vs. dry process. Project Approach/Scope Optimization of enamel materials for durability and thermal compatibility with steel Enameling process for coating uniformity, low surface roughness, and efficiency Characterization of enamel coated pipes for microstructure, chemical adhesion on steel, and corrosion resistance Corrosion resistance of pipeline steel with damaged enamel coating and cathodic protection System performance of in-situ enamel coated pipelines - stress distribution under thermal effect, external and internal pressure Effect of cathodic polarization on the stress corrosion cracking (SCC) of enamel coated API X65 pipeline steel Results to Date Cathodic protection (CP), when applied to decelerate the degradation process of enamel coating, does not compromise the integrity of bonding between the enamel coating and its substrate steel. Once the coating is damaged, however, CP does not improve the coating performance. The more negative the applied potential, the more susceptible the steel to SCC in the NS4 solution. The fracture surfaces of specimens tested in air include small dimples and micro voids, experiencing apparent necking and ductile failure. When tested at CP-1200 mV, the fracture surfaces do not show apparent necking, indicating cleavage fractures. Figure 2. (a) Impact induced coating damage and (b) electrochemical tests with a two-cell set-up. Figure 3. Glass autoclave and INSTRON tensile instrument used to perform slow strain rate tests. Figure 4. Cross-sectional SEM images of enamel coated samples under the OCP (a and c) and -1.15 V/SCE (b and d). Figure 5. Bode diagrams of enamel coated samples at (1) intact coating zone, and (2) damaged coating zone under (a) CP -1.15 vs. SCE/V and (b) the OCP. Public Project Page: https ://primis.phmsa.dot.gov/matrix/PrjHome.rdm?prj=631 -2 0 2 4 3 5 7 9 11 Phase angle(degree) 0 20 40 60 80 100 Logf(Hz) LogZ(cm 2 ) Meas. 1d 10d 20d 30d 40d 50d 60d 70d Ftd -2 0 2 4 0 2 4 6 Logf(Hz) Phase angle(degree) LogZ(cm 2 ) 0 20 40 60 80 Meas. 1d 4d 7d 10d Ftd -2 0 2 4 3 5 7 9 11 Logf(Hz) Phase angle(degree) LogZ(cm 2 ) 0 20 40 60 80 100 Meas. 1d 10d 20d 30d 40d 50d 60d 70d Ftd -2 0 2 4 0 2 4 6 LogZ(cm 2 ) Phase angle(degree) Logf(Hz) Meas. 1d 4d 7d 10d Ftd 0 20 40 60 80 0 0.1 0.2 0.3 0 100 200 300 400 500 600 700 Stress(MPa) Strain(%) in air E corr -790 mV -900 mV -1200 mV Figure 7. Surface fracture morphology of enamel coated X65 steel tested (a and b) in the air and (c and d) at CP -1200 mV after the slow strain rate tests. Figure 6. (a) Stress vs. strain curves obtained from slow strain rate tests, (b) reduction in cross-sectional area as a function of the cathodic potential, (c) polarization curves of the steel measured at high (50 mV/s) and low (0.5 mV/s) potential scanning rates in the NS4 solution. (a) (b) (d) (c) (a-1) (a-2) (b-1) (b-2) -1.2 -1.0 -0.8 -0.6 30 60 90 I II III HE mechanism AD +HE mechanism RA(%) Pontential(mV) AD mechanism -1.2 -1.0 -0.8 -0.6 -8 -7 -6 -5 -4 -3 -2 III II I log i (mA/cm 2 ) 50 mV/s 0.5 mV/s Potential (mV SCE ) (a) (c) (b) (a) (d) (c) (b) (a) (b)

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Page 1: Chemically Bonded, Porcelain Enamel Coated Pipe for ... · Chemically Bonded, Porcelain Enamel Coated Pipe for Corrosion Protection and Flow Efficiency. Acknowledgments . This project

Chemically Bonded, Porcelain Enamel Coated Pipe for Corrosion Protection and Flow Efficiency

Acknowledgments This project is funded by DOT/PHMSA’s Competitive Academic Agreement Program under Contract No. DTPH5615HCAP10.

Liang Fan1, Genda Chen1, Michael L. Koenigstein2

1. Department of Civil, Architectural, and Environmental EngineeringMissouri University of Science and Technology, Rolla, MO 65409-0030, United States

2. Pro-Perma Engineered Coatings, Roesch Inc., Belleville, IL 62226, United States

Main ObjectiveThe aims of this project are to explore chemically-bonded porcelain enamel coating for corrosion protection and safety of metallic pipes, and to develop a rapid field-applicable coating process for flow efficiency and cost reduction in the operation of metallic pipelines.

Figure 1. Enameling: wet vs. dry process.

Project Approach/Scope• Optimization of enamel materials for durability and thermal compatibility with steel• Enameling process for coating uniformity, low surface roughness, and efficiency• Characterization of enamel coated pipes for microstructure, chemical adhesion on steel, and

corrosion resistance• Corrosion resistance of pipeline steel with damaged enamel coating and cathodic protection• System performance of in-situ enamel coated pipelines - stress distribution under thermal

effect, external and internal pressure• Effect of cathodic polarization on the stress corrosion cracking (SCC) of enamel coated API

X65 pipeline steel

Results to Date• Cathodic protection (CP), when applied to decelerate the degradation process of enamel coating, does

not compromise the integrity of bonding between the enamel coating and its substrate steel. Once the coating is damaged, however, CP does not improve the coating performance.

• The more negative the applied potential, the more susceptible the steel to SCC in the NS4 solution.• The fracture surfaces of specimens tested in air include small dimples and micro voids, experiencing

apparent necking and ductile failure. When tested at CP-1200 mV, the fracture surfaces do not show apparent necking, indicating cleavage fractures.

Figure 2. (a) Impact induced coating damage and (b) electrochemical tests with a two-cell set-up.

Figure 3. Glass autoclave and INSTRON tensile instrument used to perform slow strain rate tests.

Figure 4. Cross-sectional SEM images of enamel coated samples under the OCP (a and c) and -1.15 V/SCE (b and d).

Figure 5. Bode diagrams of enamel coated samples at (1) intact coating zone, and (2) damaged coating zone under (a) CP -1.15 vs. SCE/V and (b) the OCP.

Public Project Page: https://primis.phmsa.dot.gov/matrix/PrjHome.rdm?prj=631

-2 0 2 43

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-2 0 2 43

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cm2 )

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Meas. 1d 10d 20d 30d 40d 50d 60d 70d Ftd

-2 0 2 40

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Phas

e an

gle(

degr

ee)

Logf(Hz)

Meas. 1d 4d 7d 10d Ftd

0

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0 0.1 0.2 0.30

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Stre

ss(M

Pa)

Strain(%)

in air Ecorr

-790 mV -900 mV -1200 mV

Figure 7. Surface fracture morphology of enamel coated X65 steel tested (a and b) in the air and (c and d) at CP -1200 mV after the slow strain rate tests.

Figure 6. (a) Stress vs. strain curves obtained from slow strain rate tests, (b) reduction in cross-sectional area as a function of the cathodic potential, (c) polarization curves of the steel measured at high (50 mV/s) and low (0.5 mV/s) potential scanning rates in the NS4 solution.

(a)

(b)

(d)(c)

(a-1) (a-2)

(b-1) (b-2)

-1.2 -1.0 -0.8 -0.630

60

90IIIIII

HEmechanism

AD +HEmechanism

RA

(%)

Pontential(mV)

AD mechanism

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-7

-6

-5

-4

-3

-2III II I

log

i (m

A/c

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50 mV/s 0.5 mV/s

Potential (mVSCE)

(a)(c)(b)

(a) (d)(c)(b)(a)

(b)