Membrane reactor
US-9217202-B2 · Dec 22, 2015 · US
US2016281246A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016281246-A1 |
| Application number | US-201615078784-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 23, 2016 |
| Priority date | Mar 23, 2015 |
| Publication date | Sep 29, 2016 |
| Grant date | — |
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A system and process are disclosed for electrochemically upgrading bio-oils and bio-crudes that enhance yields of selected reduction products for subsequent production of bio-based fuels.
Opening claim text (preview).
What is claimed is: 1 . A process for electrochemical hydrogenation, comprising the steps of: introducing a feed comprising a bio-oil and/or a biocrude to an electrolysis cell comprising electrodes operatively coupled to at least one ion-selective membrane; passing a current through the electrolysis cell to convert molecules in the feed to a reduced product comprising reduced molecules containing a higher proportion of hydrogen than the feed molecules. 2 . The process of claim 1 , wherein introducing the feed includes introducing the bio-oil and/or the biocrude to a cathode. 3 . The process of claim 1 , wherein the hydrogen in the reduced molecules is derived from water. 4 . The process of claim 1 , wherein the hydrogen in the reduced molecules is derived from protons. 5 . The process of claim 1 , wherein the reduced product includes a total acid number less than the total acid number of the feed. 6 . The process of claim 1 , wherein introducing the feed includes flowing the feed continuously into the electrolysis cell. 7 . The process of claim 1 , wherein the feed is introduced to an electrolysis cell that is a PEM cell. 8 . The process of claim 1 , wherein introducing the feed includes introducing a gas containing hydrogen to a cathode and/or an anode of the electrolysis cell. 9 . The process of claim 8 , wherein the gas containing hydrogen is obtained from an external gas source, from gas evolved at the cathode, or a combination thereof. 10 . The process of claim 1 , wherein passing the current includes applying a controlled potential or a controlled current. 11 . The process of claim 1 , wherein passing the current includes applying a pulsed potential or a pulsed current. 12 . The process of claim 1 , wherein passing the current includes applying a ramped potential or a ramped current. 13 . The process of claim 1 , wherein converting the feed includes converting aromatic rings in feed molecules to reduced molecules that are aliphatic-containing molecules. 14 . The process of claim 1 , wherein converting the feed includes converting carbonyl groups in feed molecules to alcohol-containing reduced molecules. 15 . The process of claim 1 , wherein the feed is introduced into the electrolysis cell absent addition of a supporting electrolyte. 16 . The process of claim 1 , wherein passing current includes transferring anions and protons into a concentrate stream located between at least two ion-selective membranes to remove acids from the bio-oil. 17 . The process of claim 1 , further including recycling the reduced product to the same electrolysis cell or one or more additional electrolysis cells to further increase the proportion of hydrogen in the reduced product. 18 . The process of claim 1 , further including passing the reduced product through a thermal hydrotreating reactor to further increase the proportion of hydrogen in the reduced product. 19 . The process of claim 1 , further including passing the reduced product to a thermal alcohol dehydration reactor to decrease the oxygen content in the reduced product. 20 . The process of claim 1 , further including passing the reduced product to a thermal alkylation reactor to increase the average molecular weight of the reduced product.
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