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This report presents the economics of a naphtha-based steam cracker, equipped with an electricity cogeneration unit. In this process, naphtha is thermally cracked at low severity conditions, maximizing propylene to Ethylene ratio. The analysis is based on a plant located in Germany.
Details: 800 kta Germany-based plant | Q1 2026 | Issue A | Compact | Printable
Companion Reports:
This report presents the economics of Polymer Grade (PG) Ethylene production from ethane in the United States. In the process under analysis, ethane is thermally cracked in pyrolysis furnaces through the use of steam, yielding Ethylene. A hydrogen-rich gas is generated as by-product.
Details: 1200 kta United States-based plant | Q1 2026 | Issue B | Compact | Printable
Companion Reports:
This report presents the economics of Polymer Grade (PG) Ethylene production from ethane and propane in the United States. In the process under analysis, the mixture is submitted to a steam cracking process, yielding PG Ethylene. A hydrogen-rich gas and polymer grade propylene are generated as by-products,
Details: 1700 kta United States-based plant | Q1 2026 | Issue C | Compact | Printable
Companion Reports:
This report presents the economics of Polymer Grade (PG) Ethlyene production from propane in the United States. In the study under analysis, propane is submitted through a steam cracking process, producing PG Ethylene. Pygas, a crude C4s stream, and PG propylene are generated as by-products.
Details: 1200 kta United States-based plant | Q1 2026 | Issue D | Compact | Printable
Companion Reports:
This study presents an economic analysis of n-butane steam cracking for Polymer Grade Ethylene production in the United States. In this process, n-butane is thermally cracked in pyrolysis furnaces through the use of steam to obtain ethylene and other hydrocarbons. Polymer grade propylene, butadiene. Raffinate-1 and pygas are also generated as by-products.
Details: 900 kta United States-based plant | Q1 2026 | Issue E | Compact | Printable
Companion Reports:
This study presents an economic analysis of isobutane steam cracking for Polymer Grade Ethylene production in the United States. In this process, n-butane is thermally cracked in pyrolysis furnaces through the use of steam to obtain ethylene and other hydrocarbons. Polymer grade propylene, butadiene. Raffinate-1 and pygas are also generated as by-products.
Details: 400 kta United States-based plant | Q1 2026 | Issue F | Compact | Printable
Companion Reports:
This feasibility study presents an economic analysis of a steam cracking process for Polymer Grade Ethylene production from atmospheric gas oil (AGO) feedstock in China. In this process, AGO is thermally cracked in pyrolysis furnaces through the use of steam to obtain ethylene and other hydrocarbons. Polymer grade propylene, pygas and fuel oil are also generated as by-products.
Details: 1000 kta China-based plant | Q1 2026 | Issue G | Compact | Printable
Companion Reports:
This report provides the economics of Polymer Grade (PG) Ethylene production from light naphtha feedstock in Germany using a steam cracking process. In this process, naphtha is thermally cracked in pyrolysis furnaces at high severity conditions to maximize Ethylene yield. Polymer grade propylene, pygas and a mixed C4s stream are also generated as by-products.
Details: 1000 kta Germany-based plant | Q1 2026 | Issue H | Compact | Printable
Companion Reports:
This study presents a techno-economic analysis of Green PG Ethylene production from hydrous ethanol in the United States using a dehydration process similar to the TechnipFMC’s Hummingbird process (former BP Chemicals). The reaction is carried out in multiple stage reactors with inter stage heaters in vapor phase.
Details: 210 kta United States-based plant | Q1 2026 | Issue I | Compact | Printable
Companion Reports:
This report provides the economics of Green Polymer Grade (PG) Ethylene production from hydrous ethanol in the United States using a dehydration process examined in this report is similar to the processes developed by Chematur and Petron. In this process, the reaction is carried out multiple reactors in series and a single furnace.
Details: 300 kta United States-based plant | Q1 2026 | Issue J | Compact | Printable
Companion Reports:
Summary
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Ethylene Production from Methane
Compact Edition | Q1 2026
1058 kta @ Q1 2026
Downloadable PDF
$799 -
Companion Report @ Australia
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Companion Report @ Belgium
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Companion Report @ Brazil
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Companion Report @ Canada
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Companion Report @ Chile
$999 -
Companion Report @ China
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Companion Report @ Colombia
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Companion Report @ Czech Republic
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Companion Report @ Finland
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Companion Report @ France
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Companion Report @ Germany
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Companion Report @ Hungary
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Companion Report @ India
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Companion Report @ Indonesia
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Companion Report @ Japan
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Companion Report @ Mexico
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Companion Report @ Norway
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Companion Report @ Philippines
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Companion Report @ Saudi Arabia
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Companion Report @ Singapore
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Companion Report @ Spain
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Companion Report @ Taiwan
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Companion Report @ Thailand
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Companion Report @ Turkey
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Companion Report @ United Kingdom
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Subtotal$799 USD
Summary
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Ethylene Production from Methane Report
Production Costs Report | Compact Edition$799 -
Total$799 USD