Methanol: The Basic Chemical and Energy Feedstock of the Future 2014
DOI: 10.1007/978-3-642-39709-7_4
|View full text |Cite
|
Sign up to set email alerts
|

Methanol Generation

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
16
0

Year Published

2017
2017
2022
2022

Publication Types

Select...
5
1

Relationship

0
6

Authors

Journals

citations
Cited by 14 publications
(16 citation statements)
references
References 10 publications
0
16
0
Order By: Relevance
“…Overall, the endothermic steam‐CH 4 reforming reaction required nearly 0.2 Nm 3 of CH 4 for every Nm 3 of biogas entering the system (Table ). This amounts to about 30% of the total energy content in the total biogas added to the system . Similarly, Zhang et al estimated that 31–32 Nm 3 of fuel natural gas was needed for every 100 Nm 3 of feed natural gas for a large scale methanol production plant (2500–5000 MT per day; carbon conversion efficiency = 88–89%).…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…Overall, the endothermic steam‐CH 4 reforming reaction required nearly 0.2 Nm 3 of CH 4 for every Nm 3 of biogas entering the system (Table ). This amounts to about 30% of the total energy content in the total biogas added to the system . Similarly, Zhang et al estimated that 31–32 Nm 3 of fuel natural gas was needed for every 100 Nm 3 of feed natural gas for a large scale methanol production plant (2500–5000 MT per day; carbon conversion efficiency = 88–89%).…”
Section: Resultsmentioning
confidence: 99%
“…Thermochemical conversion of biogas to methanol consisted of five process sections: 1) biogas cleaning via PWS; 2) steam‐CH 4 reforming to syngas in a plug flow reactor; 3) syngas to methanol conversion in a plug flow reactor; 4) methanol purification; and 5) energy recovery from unreacted gases (Fig. S.3) . The thermochemical biogas to methanol process was modeled based on previous techno‐economic studies on natural gas‐to‐methanol, biomass‐to‐methanol, and biogas‐to‐liquid processes .…”
Section: Modeling Overviewmentioning
confidence: 99%
“…Nowadays, the production capacity for a large-scale methanol plant can reach up to more than 5000 metric tons per day [29] and mainly comprise of three processes: synthesis gas production, methanol synthesis and methanol distillation, as shown in Figure 2. The synthesis gas, which mainly contains CO, CO 2 , H 2 , H 2 O, some methane, inert gases and sulphur traces depending on the source, is predominantly produced by reforming of natural gas [32][33][34] or gasification of coal, with the latter especially used in China [22]. Other feedstocks for syngas production include liquefied petroleum gas, naphtha and biomass [33].…”
Section: Traditional Methodsmentioning
confidence: 99%
“…Methanol possesses great potential as carbon source in microbial fermentation processes as it is a non‐food feedstock, pure, and can be completely utilized . With a production of about 60 million metric tons per year, methanol is a broadly available substrate . Methanol synthesis is primarily based on the conversion of synthesis gas (syngas), a mixture of mainly H 2 and CO. Renewable alternatives include the formation of methanol using hydrogen derived from water electrolysis and CO .…”
Section: Introductionmentioning
confidence: 99%
“…With a production of about 60 million metric tons per year, methanol is a broadly available substrate . Methanol synthesis is primarily based on the conversion of synthesis gas (syngas), a mixture of mainly H 2 and CO. Renewable alternatives include the formation of methanol using hydrogen derived from water electrolysis and CO . Further, the catalytic conversion of methane into methanol is progressing rapidly .…”
Section: Introductionmentioning
confidence: 99%