Threats and Challenges Associated with Ammonia Transport via Pipeline Systems
Abstract
1. Introduction
- Quantity of transported gas—the volume of ammonia to be shipped directly influences the selection of an appropriate transportation mode.
- Transport distance—the distance between the production site and the destination (storage or consumption facility) is a decisive factor in the economic viability of specific transport modes.
- Locational considerations of the manufacturing and storage site (including access to appropriate infrastructure—road and rail networks, location in relation to the river network, ports, etc.).
- Transport safety—ammonia is a hazardous substance, so issues related to the risk of spills, fires, or explosions are present.
- Transportation costs—these vary depending on the selected mode of transport (road, rail, waterway, pipeline) and include infrastructure, logistics operations, and compliance with safety regulations.
- Phase of ammonia—ammonia can be transported in either liquid or gaseous form. The choice of the form of transport depends on the temperature and pressure at which the ammonia is stored.
- Transport and storage time—optimization of transport processes may also depend on how quickly the ammonia must reach its destination. Longer transport durations may require ammonia to be stored under controlled conditions, which can generate additional costs.
- Environmental factors, such as greenhouse gas emissions and potential impacts on local ecosystems, may also influence the selection of the transportation mode.
- Regulatory and legal perspectives—compliance with national and international regulations for the transport of hazardous materials can further constrain or dictate the choice of transportation method.
2. Materials and Methods
3. Results
3.1. Global Experience in Ammonia Pipeline System Transportation
3.2. Accident Prevention in Ammonia Pipeline Transport
- ▪
- Polyethylene, epoxies, and certain elastomers: Nitrile Butadiene Rubber (NBR), Ethylene Propylene Diene Monomer (EPDM), neoprene or Chloroprene Rubber (CR), and Perfluoroelastomer (FFKM) are suitable for use with ammonia.
- ▪
- Polyurethane, epichlorohydrin rubber (ECO), and fluorosilicone should not come into contact with ammonia.
- ▪
- Polytetrafluoroethylene (PTFE), nylons, and elastomers such as certain fluorocarbons, PTFE, and SBR are highly incompatible with ammonia [28].
3.3. Environmental Risks Associated with Ammonia Pipeline Systems
- As a result of short-term exposure: coughing, throat irritation, runny nose, and a feeling of tightness in the chest,
4. Discussion
- Pipeline transport of ammonia is already in operation, implemented at various scales and across different distances.
- Pipeline-based ammonia transport is less common compared to rail and maritime transport.
- Since the 1960s, ammonia pipelines have been subject to failures, caused both by material defects and by third-party activities.
- Experience gained during the construction and operation of ammonia pipelines has made it possible to identify materials that are compatible with ammonia (e.g., carbon steel) as well as those that are incompatible (e.g., copper alloys).
- The compatibility of polymeric materials is diverse and, according to the authors of the reviewed reports, requires further research.
- In the long term, it appears necessary to establish technical standards and regulatory frameworks dedicated specifically to ammonia pipeline transport, analogous to those already in place for natural gas and being developed for hydrogen.
- Existing monitoring and safety technologies used in gas pipelines may require adaptation to the specific conditions of ammonia transport, particularly with regard to leak detection and corrosion protection.
- The development of pipeline infrastructure for ammonia transport should take into account environmental and social aspects, including impacts on ecosystems and the social acceptance of new investments.
- Occupational safety considerations require the development of comprehensive emergency procedures, personnel training programs, and early warning systems to mitigate the risks associated with accidental releases of ammonia.
- Economic aspects need to be evaluated, including comparative cost analyses of pipeline construction and operation versus rail and maritime transport, as well as the costs associated with safety measures and potential accident mitigation.
- Integration with the emerging hydrogen economy should be considered, particularly the role of ammonia pipelines as part of future infrastructure for hydrogen storage and distribution, including options for on-site ammonia cracking to supply hydrogen.
5. Conclusions
Author Contributions
Funding
Conflicts of Interest
Abbreviations
| AE | Acoustic Emission |
| AI | Artificial Intelligence |
| CFD | Computational Fluid Dynamics |
| CR | Chloroprene Rubber |
| CRDS | Cavity Ring-Down Spectroscopy |
| ECO | Epichlorohydrin Rubber |
| EPDM | Ethylene Propylene Diene Monomer |
| FFKM | Perfluoroelastomer |
| HSE | Health and Safety Executive |
| MAPCO | Mid-America Pipeline Company |
| MOS | Metal Oxide Semiconductor |
| NBR | Nitrile Butadiene Rubber |
| NDIR | Non-Dispersive Infrared Spectroscopy |
| PTFE | Polytetrafluoroethylene |
| RES | Renewable Energy Sources |
| RTTM | Real-Time Transient Model |
| SBR | Styrene-Butadiene Rubber |
| SCADA | Supervisory Control and Data Acquisition |
| SIS | Safety instrumented systems |
| TDLAS | Tunable Diode Laser Absorption Spectroscopy |
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| Location | Characteristics | Under/Above Ground | Operating Pressure [barg]/Diameter [mm]/Capacity [t/d] | Pipeline Material |
|---|---|---|---|---|
| USA |
| Mainly underground | -/200–250/5500 tonnes/day | Carbon steel |
| Russia/Ukraine | The longest ammonia pipeline in the world (2424 km) has been in operation since 1983. The biggest challenge during construction was crossing the Danube river, which required building a 720 m hanging construction. It connects the large production facilities Togliatti/Gordlovska in Russia with the Black Sea port of Odessa in Ukraine. | no data | -/350 mm/- | no data |
| Belgium | 2 pipelines (10 km and 12 km) | underground and above-ground | 22 barg/100 and 150 mm/3100 tonnes/day | Carbon steel TTSt35 (P255 QL) and stainless steel 1.4541 (X10CrNiTi1810) |
| Germany | 3 pipelines (2.8 km, 12 km, and 24 km) | underground and above-ground | 10–21 barg/50–200 and 150 and 27 5 mm/2600 and 1900 and 3600 tonnes/day | Carbon steel (unspecified) and carbon steel (H52-3 approximately equivalent to TSTE 355 or ASTM A535) (P355 NL1) |
| Italy | 1 pipeline (74 km) | above-ground | 17 barg/200 mm/900 tonnes/day | API 5L GrB, (P 235 GH) |
| Netherlands | 2 pipelines (1 km and 5.8 km) | underground | 16 and 10 barg/100–200 and 80 mm/3000 and 1000 tonnes/day | Carbon steel (ASTM 333 Gr6 (L245MB) and stainless steel (TP304L) |
| Portugal | 1 pipeline (1.9 km) | above-ground | 13 barg/100 mm/900 tonnes/day | A 333 Gr.6 (L245MB/TT st.35/A333 Gr.1) (P255QL) |
| Spain | 4 pipelines (1.5 km, 2.4 km, 4.2 km, 10 km) | underground and above-ground | 14.5 and 3.5–4.5 and 6 and 15–18 barg/150 and 350 and 300 and 100/860 and 10,000 and 12,000 and 390 tonnes/day | A 333 Gr.6 (L245MB) and St-35 (P255 QL) |
| Poland | 5 pipelines (1.2 km, 1,2 km, 1.5 km, 5.9 km, and 6.0 km) | above-ground | 10–15 and 13 and 8–13 and 5–22 barg/200 and 75–150 and 350 and 100 and 150 mm/1500 and 120 and 14,000 and 600 and 1680 tonnes/day | Carbon steel, Carbon steel type 18G2A (S355J2) and API 5L GrB seamless (P235 GH) |
| United Kingdom | 7 pipelines (1.6 km, 2.0 km, 2.2 km, 2.2 km, 6.8 km, 6.9 km, and 8.8 km) | above-ground | 30 and 21 and 14 and 2–5/100 and 150 and 300 and 75 mm/240 and 1440 and 290 and 240 and 12,000 and 600 tonnes/day | LT50 and SS (type not specified) carbon steel (no particular specification) |
| Region/Country | Selected Series of Technical Documents and Standards |
|---|---|
| USA | ASME B31 series (B31.3, B31.4, etc.)—widely used family of piping/pipeline design codes. For process piping and hazardous liquids, different parts are referenced (B31.3 for process piping; B31.4 is often referenced for liquid pipelines). |
| Russia | Russia uses GOST (state standards) and national pipeline/pressure equipment regulations. For ammonia and ammonia-derived products, several GOSTs and design rules cover materials, transport, and pressure equipment. Projects in Russia commonly reference the relevant GOSTs for material spec, welding, pressure piping design, and industrial safety. |
| China | China uses GB (national) standards and industry standards (SY for petroleum, SH for chemical industry, etc.). Recent Chinese literature and technical reviews recommend referencing GB 50253 (oil-pipeline engineering design) and other GB/SY standards as starting points for liquid-ammonia pipeline design (material quality, allowable flow velocity, corrosion allowance, etc.). Chinese practice often adapts oil/gas pipeline rules because liquid ammonia shares some transport characteristics with LPG and petroleum liquids. Example: Engineers in China often check GB 50253 and SY/T documents for allowable speeds and wall thickness calculations for long liquid-ammonia. |
| European Union | References in EU are used national + EN/PED/ISO standards: e.g., DIN, Koninklijk (Belgium), pN 40, TGL 190-354 01/03/04/16 (Germany), SNAM specification (Italy), ASME B31.3 or equivalent ASA B31.3 (Italy, Netherlands, Portugal, Spain) |
| Location, Year | Cause of Failure and Recommended Preventive Measures |
|---|---|
| USA, Texas City, Texas, 1969 | Freezing and thawing cycle in the annular space containing water in a double-walled ammonia pipe. The cause of the failure was the lack of double-wall construction of the pipeline. |
| USA, McPherson, Kansas, 1973 | Overpressure in a part of the pipeline previously damaged mechanically. The cause was the lack of relief devices for the system. |
| USA, Texas City, Texas, 1975 | External corrosion is caused by mechanical damage to the pipe coating and disruption of cathodic protection. The cause was the lack of cathodic protection, resulting from the fact that the pipeline was located above-ground. Recommended regular external inspections. |
| United Kingdom, Ince, 1981 | The leak originated from a small branch of a liquid ammonia pipeline that was not in continuous operation. The primary cause was external corrosion caused by rainwater seeping onto the surface of the pipe. In order to prevent it, recirculation of deactivated parts of the RU pipeline was recommended, which can prevent external corrosion. |
| USA, Iowa, 2001 | Ammonia leak developed in a liquid ammonia pipeline as a result of maintenance work on a valve in that pipeline. The reason is unclear. |
| USA, Louisiana, 2001 | The Human Factor caused the incident. The ammonia thief drilled through a pipeline valve, probably in order to obtain ammonia for the production of methamphetamine. To prevent similar incidents, it was recommended to restrict access for the general public by fencing off part of the pipeline. |
| USA, Kansas, 2004 | A huge leak developed after a rupture liquid ammonia pipeline. Probable cause was metal fatigue cracking in combination with previous mechanical pipe damage. Recirculation prevents thermal fatigue. A preventative measure was applied in the form of recirculation, with the aim of preventing thermal fatigue. |
| USA, 2006 | Weld damage. The cause has not been determined or has not been made public. |
| USA, Florida, 2007 | A hole was drilled in a pipeline by an unauthorized person. |
| USA, Nebraska, 2010 | There was a leak during operations related to pipeline modification. The pipeline bent and ruptured while an O-ring threaded joint was being welded, resulting in the release of liquid ammonia and the formation of subsequent vapor clouds. The root cause analysis revealed inherent risks associated with ammonia pipelines, highlighting the need for independent layers of protection. These include safety instrumented systems (SIS) and comprehensive change management procedures involving hazard analysis prior to infrastructure modifications. Improved emergency response training is also required for personnel involved in such projects. |
| Togliatti-Odessa pipeline, 2015 | The leak is causing an unprecedented environmental and health disaster that has gone underreported in both Russian and international media. The leak is still under investigation. |
| USA, Tekamah, 2016 | The assessment of events during the incident revealed delays in detecting pressure drops and emergency isolation procedures, contributing to the scale of the leak. Root cause analysis identified factors related to corrosion, highlighting the need for careful material selection. Inspection and maintenance deficiencies, including a significant distance between isolation valves, allowed a large amount of ammonia to remain in the pipelines (2587 barrels). The impact and consequences of the incident that occurred were made worse by these inadequacies/deficiencies. |
| Ukraine, Masyutivka-Kharkiv, 2023 | Military operations in Ukraine caused damage to a 2500 km pipeline running through the conflict zone. An explosion related to the military operations caused a leak. The effects are still being investigated. |
| Category | Parameter | Description | Example/Standard Reference |
|---|---|---|---|
| Material Properties | Material composition and grade | Determines resistance to ammonia-induced corrosion and cracking | Low-alloy steel (ASTM A106 Grade B), stainless steel (AISI 304/316) |
| Tensile and yield strength | Mechanical stability under pressure | Tested per EN ISO 6892-1 | |
| Toughness/impact resistance | Prevents brittle fracture at low temperatures | Charpy impact test (ISO 148-1) | |
| Weld quality/HAZ properties | Welding may introduce weak spots or residual stress | EN ISO 5817, EN 13480-4 | |
| Operating Conditions | Operating pressure and temperature | Affects stress levels, ammonia phase, and corrosion rate | 25–40 bar, −33 °C (liquid ammonia) |
| Pressure fluctuations/transients | Cause fatigue and microcracks | Repeated pump starts/stops | |
| Temperature cycling | Leads to thermal fatigue | Seasonal operation, defrost cycles | |
| Corrosion and Chemical Degradation | Stress corrosion cracking (SCC) susceptibility | Certain steels crack under tensile stress + ammonia exposure | Carbon steel with high residual stress |
| Internal corrosion rate | Depends on moisture and impurities | <0.1 mm/year acceptable | |
| External corrosion | Influenced by soil, coating, and cathodic protection | EN ISO 15589-1 | |
| Mechanical Integrity | Wall thickness/corrosion allowance | Determines lifetime before thinning becomes critical | 2–3 mm allowance typically |
| Fatigue life | Estimated from cyclic stress analysis | ASME B31.5 fatigue curves | |
| Residual stress | From welding or cold bending | Measured by X-ray diffraction | |
| Inspection & Maintenance | Leak detection rate | Sensitivity of detection systems | ≤0.1% of flow per hour |
| Integrity test interval | Frequency of NDT, pressure tests, or pigging | Every 5–10 years | |
| Corrosion monitoring | Using probes or coupons | Regular corrosion rate readings | |
| Environmental & Operational Factors | Soil resistivity and moisture | Affect underground corrosion rate | Measured by Wenner method |
| Vibration and mechanical loads | From nearby infrastructure or ground movement | Measured with accelerometers | |
| Ammonia purity | Contaminants accelerate degradation | ≥99.5% purity |
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Kuchta, T.; Wróblewska, A.; Holewa-Rataj, J.; Król, A. Threats and Challenges Associated with Ammonia Transport via Pipeline Systems. Appl. Sci. 2025, 15, 11465. https://doi.org/10.3390/app152111465
Kuchta T, Wróblewska A, Holewa-Rataj J, Król A. Threats and Challenges Associated with Ammonia Transport via Pipeline Systems. Applied Sciences. 2025; 15(21):11465. https://doi.org/10.3390/app152111465
Chicago/Turabian StyleKuchta, Tomasz, Anna Wróblewska, Jadwiga Holewa-Rataj, and Anna Król. 2025. "Threats and Challenges Associated with Ammonia Transport via Pipeline Systems" Applied Sciences 15, no. 21: 11465. https://doi.org/10.3390/app152111465
APA StyleKuchta, T., Wróblewska, A., Holewa-Rataj, J., & Król, A. (2025). Threats and Challenges Associated with Ammonia Transport via Pipeline Systems. Applied Sciences, 15(21), 11465. https://doi.org/10.3390/app152111465

