Study on Suitability Evaluation Method of Non-Metallic Seals in Long Distance Hydrogen-Doped Natural Gas Pipelines
Abstract
:1. Introduction
2. Procedures
2.1. Experimental Study on the Performance of Non-Metallic Seals Under Hydrogen-Doping Conditions
2.1.1. Hydrogen-Doped Sealing Test and Result Analysis
2.1.2. Hydrogen-Doped Anti-Explosion Test and Result Analysis
2.1.3. Hydrogen-Doped Aging Test and Result Analysis
2.2. Comprehensive Evaluation of the Applicability of Non-Metallic Seals Based on Hydrogen-Doped Physical and Chemical Properties and SEW-FCE
2.2.1. Construction of Suitability Index System Based on Physicochemical Properties of Hydrogen Blending
2.2.2. Structure Entropy Weight Method
- Step 1: Gather expert opinions and form a typical ranking.
- Step 2: Uncertainty analysis of typical ordering.
- Step 3: Normalization process.
2.2.3. Fuzzy Comprehensive Evaluation Method
- Step 1: Establish the set of assessment indicators
- Step 2: Establish a collection of assessment indicator weights:
- Step 3: Establish the collection of rubrics:
- Step 4: The establishment of the affiliation matrix: the experts scored each indicator separately, thus forming a set of comments within the five risk intervals for a particular indicator, and the aggregation of the scoring results for all indicators is called the affiliation matrix, as follows:
- Step 5: Establish the assessment matrix: according to the combination of the set of weights obtained by the weight calculation method and the affiliation matrix, the assessment matrix can be obtained as:
- Step 6: Determine the risk level.
3. Application of the Proposed Methodology in a Long-Distance Natural Gas Pipeline
3.1. Calculation of Indicator Weights
3.2. Applicability Evaluation Based on Physicochemical Properties of Seals and FCE-SEW Model
3.2.1. Establish a Set of Evaluation Indicators
3.2.2. Establish the Weight Set of Evaluation Indicators
3.2.3. Building a Collection of Rubrics
3.2.4. Establish Membership Matrix
3.2.5. Calculation of the Assessment Matrix
3.2.6. Determination of the Level of the Indicator
4. Conclusions
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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Sample Name | Test Conditions | Number of Samples | Gasket Preload (MPa) | Test Medium Pressure (MPa) | Test Result (mL/h) |
---|---|---|---|---|---|
Fluorine rubber | Hydrogen-free condition | 4 | 7 | 1 | 0.957 |
5% hydrogen-doped condition | 4 | 7 | 1 | 0.892 | |
Nitrile rubber | Hydrogen-free condition | 4 | 7 | 1 | 0.914 |
5% hydrogen-doped condition | 4 | 7 | 1 | 0.968 | |
Nylon | Hydrogen-free condition | 4 | 35 | 4 | 0.917 |
5% hydrogen-doped condition | 4 | 35 | 4 | 0.957 | |
Graphite-polytetrafluoroethylene | Hydrogen-free condition | 4 | 35 | 4 | 0.809 |
5% hydrogen-doped condition | 4 | 35 | 4 | 0.831 | |
Para-polyphenylene-Polytetrafluoroethylene | Hydrogen-free condition | 4 | 35 | 4 | 0.907 |
5% hydrogen-doped condition | 4 | 35 | 4 | 0.882 |
Condition | Material | Specimen Appearance | Overall Rating |
---|---|---|---|
Hydrogen-free condition | Fluorine rubber | Cracks, no holes, bubbles | Grade 4 |
Nitrile rubber | No cracks, no holes, no bubbles | Grade 0 | |
Nylon | No cracks, no holes, no bubbles | Grade 0 | |
Graphite-polytetrafluoroethylene | No cracks, no holes, no bubbles | Grade 0 | |
Para-polyphenylene-polytetrafluoroethylene | No cracks, no holes, no bubbles | Grade 0 | |
5% hydrogen-doped condition | Fluorine rubber | Cracks, no holes, bubbles | Grade 4 |
Nitrile rubber | No cracks, no holes, no bubbles | Grade 0 | |
Nylon | No cracks, no holes, no bubbles | Grade 0 | |
Graphite-polytetrafluoroethylene | No cracks, no holes, no bubbles | Grade 0 | |
Para-polyphenylene-polytetrafluoroethylene | No cracks, no holes, no bubbles | Grade 0 |
Secondary Index | Three-Level Index | Grading Criteria for Three Indexes | Score | |
---|---|---|---|---|
Non-metal seal performance P1 | P11 | Leakage rate | The leakage rate of hydrogen-doped non-metallic seals is >6 mL/h. | 4 |
Leakage rate of hydrogen-doped non-metallic seals 4 < a ≤ 6 mL/h. | 3 | |||
Leakage rate of hydrogen-doped non-metallic seals 2 < a ≤ 4 mL/h. | 2 | |||
Leakage rate of hydrogen-doped non-metallic seal test a ≤ 2 mL/h. | 1 | |||
P12 | Explosive resistance | Non-metallic seals are Class IIV or V for hydrogen-doped anti-explosion performance. | 4 | |
Non-metallic seals are Class II or Class III for hydrogen-doped anti-explosion performance. | 3 | |||
Non-metallic seals are Class I for hydrogen-doped anti-explosion performance. | 2 | |||
Non-metallic seals are Class zero for hydrogen-doped anti-explosion performance. | 1 | |||
P13 | Anti-aging properties | For rubber, the maximum value of 50% constant elongation modulus, rate of change in tensile strength, and elongation at break is ≤50%; for plastics, elongation at break ≤50%, yield strength ≤50%, and hardness is +10/−20 units. All indicators meet the above conditions. | 4 | |
For rubber, the maximum value of 50% constant elongation modulus, rate of change in tensile strength, and elongation at break is ≤37.5%; for plastics, elongation at break ≤37.5%, yield strength ≤37.5%, and hardness is +10/−20 units. All indicators meet the above conditions. | 3 | |||
For rubber, the maximum value of 50% constant elongation modulus, rate of change in tensile strength, and elongation at break is ≤25%; for plastics, elongation at break ≤25%, yield strength ≤25%, and hardness is +10/−20 units. All indicators meet the above conditions. | 2 | |||
For rubber, the maximum value of 50% constant elongation modulus, rate of change in tensile strength, and elongation at break is ≤12.5%; for plastics, elongation at break ≤12.5%, yield strength ≤12.5%, and hardness is +10/−20 units. All indicators meet the above conditions. | 1 | |||
Running parameter P2 | P21 | Length of service | Service time factor (service time/design life) > 0.8. | 4 |
Service time factor (service time/design life) = 0.6–0.8. | 3 | |||
Service time factor (service time/design life) = 0.4–0.6. | 2 | |||
Service time factor (service time/design life) < 0.4. | 1 | |||
P22 | Service pressure | Operating pressure P > 10 MPa (ultra-high pressure). | 4 | |
Operating pressure 1.6 ≤ P ≤ 10 MPa (high pressure). | 3 | |||
Operating pressure 0.1 ≤ P ≤ 1.6 MPa (medium pressure). | 2 | |||
Operating pressure 0 ≤ P ≤ 0.1 MPa (low pressure). | 1 | |||
P23 | Environmental temperature | Annual minimum ambient temperature ≤ low-temperature brittleness temperature of non-metallic seals. | 4 | |
Annual minimum ambient temperature > low-temperature brittleness temperature of non-metallic seals. | 1 | |||
P24 | Gas composition | In the natural gas pipeline, the hydrogen content accounts for a ≥ 20%. | 4 | |
In the natural gas pipeline, the hydrogen content is 10 ≤ a < 20%. | 3 | |||
In the natural gas pipeline, the hydrogen content accounts for 5% ≤ a < 10%. | 2 | |||
In the natural gas pipeline, the hydrogen content accounts for 0 ≤ a < 5%. | 1 | |||
Management level P3 | P31 | Personnel management | Non-metal seal service management and maintenance personnel have not had any training in related technical fields. | 4 |
Non-metal seal service management and maintenance personnel have received formal training in related technical fields. | 3 | |||
Non-metal seal service management and maintenance personnel have received formal training in related technical fields many times. | 2 | |||
Non-metal seal service management and maintenance personnel receive regular training in related technical fields and have rich experience. | 1 | |||
P32 | Operating parameter | Non-metal seal application equipment and piping operating procedure documents are missing. | 4 | |
Non-metal seal application equipment and pipe operating procedure documentation are incomplete. | 3 | |||
The operating procedures of non-metallic seal application equipment and pipelines are complete, but the operating procedures are complex. | 2 | |||
The operating procedures of non-metallic seal application equipment and pipelines are complete, and the operating procedures are simple. | 1 | |||
P33 | Emergency measure | There is no special emergency plan for the operation and management of hydrogen-doped pipelines. | 4 | |
Special emergency plans have been formulated for hydrogen-doped pipelines, and emergency drills have not been carried out regularly. | 3 | |||
Special emergency plans have been formulated for hydrogen-doped pipelines, and emergency drills have been carried out regularly. | 2 | |||
Special emergency plan for hydrogen-doped pipeline has been formulated, and the emergency plan is easy to implement, and the emergency drill effect is remarkable. | 1 |
Calculated Value | P1 | P2 | P3 |
---|---|---|---|
Group 1 | 1 | 2 | 3 |
Group 2 | 1 | 3 | 2 |
Group 3 | 1 | 2 | 3 |
bj (three-round mean) | 1 | 0.695 | 0.5975 |
bi (max) | 1 | 0.7925 | 0.7925 |
max-bj | 0 | 0.0975 | 0.195 |
1-Qj | 1 | 0.9513 | 0.9513 |
cj | 1 | 0.6612 | 0.5684 |
wj | 0.4486 | 0.2965 | 0.2549 |
Index | P11 | P12 | P13 | P21 | P22 |
---|---|---|---|---|---|
Weight | 0.4029 | 0.3730 | 0.2241 | 0.3357 | 0.3039 |
Index | P23 | P24 | P31 | P32 | P33 |
Weight | 0.2024 | 0.1580 | 0.3659 | 0.3615 | 0.2726 |
Grade | Excellent | Good | Medium | Poor |
---|---|---|---|---|
Score | (0, 1] | (1, 2] | (2, 3] | (3, 4] |
Serial Number | Evaluation Factor | Y1 | Y2 | Y3 | Y4 |
---|---|---|---|---|---|
1 | P11 | 10 | 0 | 0 | 0 |
2 | P12 | 0 | 0 | 0 | 10 |
3 | P13 | 0 | 0 | 0 | 10 |
4 | P21 | 10 | 0 | 0 | 0 |
5 | P22 | 0 | 0 | 10 | 0 |
6 | P23 | 10 | 0 | 0 | 0 |
7 | P24 | 0 | 10 | 0 | 0 |
8 | P31 | 0 | 0 | 10 | 0 |
9 | P32 | 10 | 0 | 0 | 0 |
10 | P33 | 0 | 10 | 0 | 0 |
Suitability Level Assessment Results | Soft Seals (Rubber) | Hard Seals (Plastic) | |||
---|---|---|---|---|---|
Fluoroelastomer | Nitrile Rubber | Nylon (Loanword) | Graphite-Polytetrafluoroethylene | Para-Polyphenylene-Polytetrafluoroethylene | |
Values of assessment results | 2.387 | 1.7845 | 1.7845 | 1.5988 | 1.7141 |
Level of assessment results | Medium | Good | Good | Good | Good |
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Liang, X.; Fei, F.; Ma, W.; Wang, K.; Ren, J.; Yao, J. Study on Suitability Evaluation Method of Non-Metallic Seals in Long Distance Hydrogen-Doped Natural Gas Pipelines. Processes 2024, 12, 2353. https://doi.org/10.3390/pr12112353
Liang X, Fei F, Ma W, Wang K, Ren J, Yao J. Study on Suitability Evaluation Method of Non-Metallic Seals in Long Distance Hydrogen-Doped Natural Gas Pipelines. Processes. 2024; 12(11):2353. https://doi.org/10.3390/pr12112353
Chicago/Turabian StyleLiang, Xiaobin, Fan Fei, Weifeng Ma, Ke Wang, Junjie Ren, and Junming Yao. 2024. "Study on Suitability Evaluation Method of Non-Metallic Seals in Long Distance Hydrogen-Doped Natural Gas Pipelines" Processes 12, no. 11: 2353. https://doi.org/10.3390/pr12112353