34 Analytical Instrumentation BIO-ETHANOL FOR SAF
Fermentation of maize to ethanol is common in North America. Carbon dioxide (CO2
) can
readily be captured from the fermentation broth and purifi ed for industrial applications such as food freezing and beverage carbonation. Ethanol can be blended with petroleum derived gasoline to improve the sustainability of automotive transportation fuels.
Ethanol can be converted to jet fuel
Ethanol can also be converted to the paraffi nic fraction of synthetic aviation fuel (SAF) through the ethanol to JET (ETJ) or alcohol to JET (ATJ) pathway (JET is the term used to describe aviation kerosene). The chemistry of the ETJ conversion relies initially on dehydration to strip water out of multiple ethanol molecules followed by oligomerisation, which is a controlled amount of polymerisation.
The properties of JET from refi ned petroleum products and JET that contains SAF are stated in relevant ASTM specifi cations. A key aspect is the maximum allowable fraction of aromatic compounds in JET containing SAF is capped at around 25% by the ASTM 7566-22a.
On the other hand, volatile aromatics are required to be blended with the heavier paraffi nic olefi ns that are produced by the ETJ process so that the mixture can meet the specifi ed distillation curve. The distillation curve is prescribed as the amount of JET recovered at various distillation temperatures.
The maize crop, along with other plants absorbs CO2 photosynthesis. Plants use carbon from CO2
produce valuable chemicals such as ethanol.
LanzaTech utilises anaerobic acetobacter bacteria in a fermenter to convert CO rich feed gases, such as syngas, to ethanol and a range of biochemicals. Subsequently, the complimentary LanzaJet process can be used to convert the bioethanol to SAF in their proprietary ‘Ethanol to Jet’ or ETJ process which converts the ethanol to ethylene, through dehydration then oligomerises the ethylene to paraffi nic olefi ns.
The ideal feedstocks for the LanzaTech fermenter are CO-rich. CO2
rich streams can potentially be utilised in combination with
hydrogen. But a high CO content in the feed to the bioreactor, or fermenter, reduces the green hydrogen feed requirement. Syngas derived from waste or biomass gasifi cation is generally CO-rich and is a good feedstock for the LanzaTech process.
during to make
carbohydrates and, starches to build their leaves and structure. Bacteria can also consume CO2
and carbon monoxide (CO) to E-fuels, e-fertilizers and e-chemicals production
Iron and steel making also yields CO-rich fl ue gases which are ideal feedstocks to the LanzaTech process. Blast furnace gas (BFG) contains 20% CO and converter gas (also known as basic oxygen furnace gas or BOFG) contains 60% CO. Utilisation of BFG and BOFG in the LanzaTech process can generate valuable bioethanol.
LanzaTech’s process was demonstrated at pilot-scale in 2008 using fl ue gases from the BlueScope Steel mill in Glenbrook, NZ. Since then, LanzaTech has successfully deployed its technology at two 300 tonne per annum demonstration facilities at Baosteel
Shanghai and Shougang Steel Caofeidian in China. These LanzaTech fermenters are fed with a range of iron and steel making off gases including BOFG, BFG, and coke oven gas (COG).
The term CCT or ‘Carbon Capture and Transformation’ has been used to describe the LanzaTech fermentation process. Whilst it is highly effective at transforming carbon monoxide to ethanol, the LanzaTech process has more in common with carbon utilisation than CO2
sequestration.
LanzaTech operates the Freedom Pines Biorefi nery in Soperton, Georgia which uses bio fermenters to generate ethanol and other chemicals. The LanzaJet ethanol to jet SAF production process will soon also be implemented at that location to utilise captured carbon to make fuels that can substitute aviation kerosene, a fossil fuel distilled from crude oil.
Life Cycle Analysis (LCA) of the LanzaTech process shows that the holistic CO2
emissions reduction is primarily due to
the substitution of fossil fuels with SAF derived from ethanol recovered from the fermentation broth.
Also integral to the LanzaTech LCA is consideration of whether the feedstock, such as iron and steel making fl ue gases are fl ared, or utilised. If they are fl ared, their recovery and conversion to ethanol is a signifi cant environmental benefi t.
Jet airliner refuelling
Author Contact Details Stephen B. Harrison • sbh4 GmbH • Address: Kranzlstraße 21, 82538 Geretsried, Germany • Tel: +49 (0)8171 24 64 954 • Email:
sbh@sbh4.de • Web:
www.sbh4.de
PIN OCTOBER / NOVEMBER 2023
Page 1 |
Page 2 |
Page 3 |
Page 4 |
Page 5 |
Page 6 |
Page 7 |
Page 8 |
Page 9 |
Page 10 |
Page 11 |
Page 12 |
Page 13 |
Page 14 |
Page 15 |
Page 16 |
Page 17 |
Page 18 |
Page 19 |
Page 20 |
Page 21 |
Page 22 |
Page 23 |
Page 24 |
Page 25 |
Page 26 |
Page 27 |
Page 28 |
Page 29 |
Page 30 |
Page 31 |
Page 32 |
Page 33 |
Page 34 |
Page 35 |
Page 36 |
Page 37 |
Page 38 |
Page 39 |
Page 40 |
Page 41 |
Page 42 |
Page 43 |
Page 44