Process for the Production of Xylenes
US-2015376086-A1 · Dec 31, 2015 · US
US9115315B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9115315-B2 |
| Application number | US-96898910-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 15, 2010 |
| Priority date | Apr 26, 2006 |
| Publication date | Aug 25, 2015 |
| Grant date | Aug 25, 2015 |
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Petrochemical processes, including reforming processes are described herein. The reforming processes generally include introducing an input stream to a reforming unit having a reforming catalyst disposed therein, wherein the input stream includes a naphtha having an N+2A value of from about 65 to about 85 and contacting the input stream with the reforming catalyst and hydrogen to form an output stream.
Opening claim text (preview).
What is claimed is: 1. A petrochemical process comprising: introducing a first input stream to a cracking unit, wherein the first input stream comprises a virgin naphtha feedstock, wherein said virgin naphtha feedstock is a former reformer input stream; cracking the virgin naphtha feedstock within the cracking unit to form a first output stream comprising light olefins and pygas; passing the pygas from the cracking unit to an extraction unit; separating benzene and toluene from the pygas within the extraction unit; recovering a raffinate from the extraction unit having a higher N+2A than the virgin naphtha feedstock; passing the raffinate from the extraction unit to a reforming unit having a reforming catalyst disposed therein; contacting the raffinate with the reforming catalyst to form a second output stream; and recovering the second output stream from the reforming unit. 2. The process of claim 1 , wherein the virgin naphtha feedstock comprises a N+2A value of from about 40 to about 55. 3. The process of claim 1 , wherein the cracking unit comprises a steam cracker. 4. The process of claim 1 further comprising hydrogenating the pygas prior to extraction. 5. The process of claim 1 , wherein the raffinate comprises a N+2A value of from about 75 to about 85. 6. The process of claim 1 , wherein the reforming catalyst comprises a Group VIII noble metal. 7. The process of claim 1 , wherein the reforming catalyst comprises a promoter selected from gallium, tin, copper, chromium, rhenium, iridium and combinations thereof. 8. The process of claim 1 further comprising supplying hydrogen to the reforming unit.
Catalytic reforming · CPC title
including at least one cracking step · CPC title
Light distillates, e.g. LPG, naphtha · CPC title
Thermal processes {(C07C4/025 takes precedence)} · CPC title
essentially based on blends of hydrocarbons · CPC title
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