Extraction of oxygenates from a hydrocarbon stream
A technology for oxygenates and hydrocarbon streams, applied in and below, the field of extracting oxygenates, can solve difficult and uneconomical problems
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Embodiment 1
[0039] This example shows a process according to the invention in which C 10 -C 13 The fraction removes oxygenates to low levels. Extraction column 20 was operated at a solvent / feed ratio of 1.25 and a temperature of 50°C. The overall olefin / paraffin recovery in stream 24 was 89.9%. The olefin / paraffin ratio was 1:3.7 in the feed and 1:3.6 after oxygenate extraction. The olefin / paraffin ratio is thus substantially maintained. The oxygenate content in stream 24 was only 0.0145%.
[0040] Extraction tower 20
[0041]
[0042] Raffinate stripper 23
[0043]
[0044] Solvent Recovery Tower 27
[0045]
Embodiment 2
[0047] This example shows a process according to the invention in which C 10 -C 13 The fraction removes oxygenates to a low level with a higher oxygenate feedstock concentration than Example 1 (12.36% by weight). Extraction column 20 was operated at a solvent / feed ratio of 2:1 and a temperature of 50°C. The overall recovery of olefins / paraffins in stream 24 was 91.4%. Again, the olefin / paraffin ratio was substantially maintained. The oxygenate content in stream 24 was only 0.0154%.
[0048] Extraction tower 20
[0049]
[0050] Raffinate stripper 23
[0051]
[0052] Solvent Recovery Tower 27
[0053]
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