Production Cost Report
mtbe-e11a,mtbe-e21c,mtbe-e31c,mtbe-e41a,mtbe-e51a
methanol-e12a,isobutylene-e13a,isobutylene-e11a
MTBE
Methyl tert-Butyl Ether (MTBE) is a major compound in the octane enhancer industry, its main application area. The remaining MTBE is used as a solvent and in the production of other chemical compounds.

MTBE Production Cost Reports - 2019/20

Capital Investment & Operating Cost of MTBE Plants

Methyl tert-Butyl Ether (MTBE) is a major compound in the octane enhancer industry, its main application area. The remaining MTBE is used as a solvent and in the production of other chemical compounds.

Intratec offers professional, easy-to-understand reports examining MTBE production. Each study describes an industrial plant, including main process units and site infrastructure, and presents an independent analysis of capital and operating costs. All reports are based on the most recent economic data available (2019/20).

MTBE Production from Raffinate-1 - Cost Analysis | MTBE E21C
Feasibility analysis of Methyl tert-Butyl Ether (MTBE) production from a raffinate-1 stream and methanol using a process similar to UOP's Ethermax process for isobutylene etherification in China.

Analysis Basis: China   |   2019 Q1   |   101 pages   Starting at $1,099

MTBE Production from FCC C4 Raffinate - Cost Analysis | MTBE E31C
The process examined in this report is the same etherification process examined in the report "MTBE E21A", with the exception that the raw materials used are FCC C4 raffinate and methanol.

Analysis Basis: China   |   2019 Q1   |   101 pages   Starting at $1,099

MTBE Production from Butane - Cost Analysis | MTBE E41A
Feasibility analysis of an on-purpose Methyl tert-Butyl Ether (MTBE) production plant from butane and methanol in the United States.

Analysis Basis: USA   |   2019 Q1   |   98 pages   Starting at $1,499

MTBE Production from Isobutylene - Cost Analysis | MTBE E51A
The process examined in this report is the same etherification process examined in the report "MTBE E21A", with two exceptions: (1) the plant is constructed in the United States and (2) the raw materials used are methanol and an isobutylene rich stream from an isobutane dehydrogentaion process.

Analysis Basis: USA   |   2019 Q1   |   98 pages   Starting at $1,199

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Isobutylene Production from Crude C4s - Cost Analysis | Isobutylene E11A
This study presents the economics of Isobutylene production from a crude C4s stream in the USA, using an extraction process similar to Total Isobutylene Acid Extraction process.

Analysis Basis: USA | 2019 Q1 | 101 pages Starting at $1,099

Isobutylene Production from Isobutane - Cost Analysis | Isobutylene E13A
This report presents the economics of Isobutylene production from isobutane in the USA. Differently from the report "Isobutylene E12A", the process examined is a dehydrogenation process similar to CB&I Lummus CATOFIN.

Analysis Basis: USA | 2019 Q1 | 101 pages Starting at $1,099

Methanol Production from Natural Gas - Cost Analysis | Methanol E12A
In this report, as in the report "Methanol E11A", the economic analysis concerns a process in which Methanol is generated from natural gas. However, this study examines a combined reforming process similar the technologies developed by Lurgi, Toyo, KBR, Johnson Matthey/Davy and Haldor-Topsoe. The plant is also located in the United States.

Analysis Basis: USA | 2019 Q1 | 100 pages Starting at $899

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