Membrane reactor
US-9217202-B2 · Dec 22, 2015 · US
US9932679B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9932679-B2 |
| Application number | US-201414516934-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 17, 2014 |
| Priority date | Oct 31, 2013 |
| Publication date | Apr 3, 2018 |
| Grant date | Apr 3, 2018 |
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An electrochemical conversion method for converting at least a portion of a first mixture comprising hydrocarbon to C 2+ unsaturates by repeatedly applying an electric potential difference, V(τ 1 ), to a first electrode of an electrochemical cell during a first time interval τ 1 ; and reducing the electric potential difference, V(τ 1 ), to a second electric potential difference, V(τ 2 ), for a second time interval τ 2 , wherein τ 2 ≤τ 1 . The method is beneficial, among other things, for reducing coke formation in the electrochemical production of C 2+ unsaturates in an electrochemical cell. Accordingly, a method of reducing coke formation in the electrochemical conversion of such mixtures and a method for electrochemically converting carbon to C 2+ unsaturates as well as an apparatus for such methods are also provided.
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What is claimed is: 1. A method of reducing coke formation in the electrochemical production of C 2+ unsaturates in an electrochemical cell comprising a first electrode, a second electrode, and at least one membrane situated between the first and second electrodes, the method comprising: (a) providing to the first electrode of the electrochemical cell a first mixture comprising≥1.0 wt. % methane based on the weight of the first mixture; (b) applying an electric potential difference to the electrochemical cell to establish a first electric potential V 1 across the electrochemical cell sufficient to convert at least a portion of the methane during a first time interval of duration τ 1 , wherein (i) the conversion is carried out substantially without oxidant, and (ii) τ 1 is in the range of from 1×10 −10 sec. to 1.0 sec.; (c) establishing a second electric potential difference V 2 across the cell during a second time interval of duration τ 2 , wherein τ 2 ≤τ 1 ; and (d) repeating steps (b) and (c), and at least during step (c) producing C 2+ unsaturates. 2. The method of claim 1 , further comprising conducting at least a portion of the C 2+ unsaturates away from the first electrode at a rate ≥1.0×10 −7 mole min. −1 cm −2 for ≥100.0 minutes. 3. The method of claim 1 , wherein during step (c) the first mixture is exposed to a temperature in the range of from 100° C. to 500° C. at a pressure in the range of from 0.1 bar to 100.0 bar. 4. The method of claim 1 , wherein the first electrode and/or the second electrode comprises ≥1.0 wt. % of at least one noble metal. 5. The method of claim 1 , wherein the current density through the membrane during step (c) achieves a value in the range of from 1.0 mA cm −2 to 100.0 mA cm −2 . 6. The method of claim 1 , wherein V 1 achieves a value in the range of from 0.1 Volts to 20 Volts during step (b). 7. The method of claim 1 , wherein V 1 and V 2 satisfy at least one of: (i) V 1 >0, V 2 ≥0, and V 2 =A 1 ·V 1 , wherein A 1 is in the range of from about 0.00 to about 0.99; (ii) V 1 ≥0 and V 2 <0; (iii) V 1 <0, V 2 <0, and |V 2 |=A 2 |V 1 |, wherein A 2 ≥1.01; (iv) V 2 is more negative or less positive than V 1 ; or (v) V 1 ≥0, and |V 2 |<|V 1 |. 8. The method of claim 1 , wherein τ 2 is in the range of from 0.01·τ 1 to 0.9·τ 1 . 9. The method of claim 1 , further comprising a step of oligomerization, polymerization, hydroxylation, or hydrogenation of at least a portion of the C 2+ unsaturates.
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