Method and reactor for cracking hydrocarbon
US-9499747-B2 · Nov 22, 2016 · US
US9969941B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9969941-B2 |
| Application number | US-201615196771-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 29, 2016 |
| Priority date | Sep 23, 2011 |
| Publication date | May 15, 2018 |
| Grant date | May 15, 2018 |
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The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.
Opening claim text (preview).
The invention claimed is: 1. A process for removing combustible non-volatiles from a reactor system, comprising: (A) depositing combustible non-volatiles by pyrolysis at a temperature ≥800° C. of hydrocarbon comprising alkane during a pyrolysis step of duration t 1 , wherein (a) the combustible non-volatiles are deposited in first and second conduits of a first reactor, (b) the first reactor is located within the reactor system, and (c) the pyrolysis converts at least a portion of the alkane to unsaturated hydrocarbon in the first reactor; (B) during a first time interval having a duration t 2a of a heating step having a total duration t 2 , (a) conducting a fuel through the first conduit and an oxidant through the second conduit, (b) heating the reactor system by combusting at least a portion of the oxidant with (i) at least a portion of the combustible non-volatiles located in the second conduit and (ii) at least a portion of the fuel; and (C) during a second time interval having a duration t 2b of the heating step, wherein t 2a +t 2b ≤t 2 , (a) conducting at least a portion of the oxidant through the first conduit, (b) reacting the oxidant with at least a portion of the combustible non-volatiles located in the first conduit, (c) conducting the fuel through a third conduit of the first reactor, (d) conducting a second portion of the oxidant through the second conduit, and (e) heating the reactor system by combusting at least a portion of the oxidant with (i) at least a portion of the combustible non-volatiles located in the first and/or second conduits and (ii) at least a portion of the fuel; wherein the first, second, and third conduits comprise at least one channel in a reactor bed. 2. The process of claim 1 , wherein t 1 is the range of 0.1 seconds to 10.0 seconds. 3. The process of claim 1 , wherein t 2 is in the range of 0.1 seconds to 10.0 seconds. 4. The process of claim 1 , wherein t 2a is substantially the same as t 2b . 5. The process of claim 1 , wherein the heating steps (B) and (C) together heat at least part of the reactor system to a temperature ≥800° C. for the pyrolysis. 6. The process of claim 5 , wherein step (A) further comprises: transferring at least a portion of the unsaturated hydrocarbon away from the reactor via the first and second conduits, wherein at least a portion of the depositing of the combustible non-volatiles occurs during the transfer. 7. The process of claim 6 , further comprising repeating steps (A)-(C).
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