Processing of high normal paraffin concentration naphtha feedstocks

• US 4,595,490 A
• Filed: 04/01/1985
• Issued: 06/17/1986
• Est. Priority Date: 04/01/1985
• Status: Expired due to Term

• Current Assignee: UOP Des Plaines IL A NY General Partnership
• Original Assignee: Union Carbide Corporation (Dow, Inc.)
• Inventors: Gray, Robert L. Jr., Oetinger, Peter L.
• Primary Examiner(s): Gantz, D. E.
• Assistant Examiner(s): Caldarola, Glenn A.
• Application Number:
  US06/718,368
• Time in Patent Office: 442 Days
• Field of Search: 208/310 Z, 208/310 R, 208/DIG. 1, 585/820, 585/821, 585/822
• US Class Current: 208/310.00R
• CPC Class Codes: C10G 25/03 with crystalline alumino-silicates, e.g. molecular sieves

Abstract

Normal paraffins present in high concentrations in light naphtha streams are separated from non-normal paraffins in a four or more bed adsorption system employing, on a cyclic basis, the processing steps of (1) cocurrent purge/adsorption, (2) cocurrent feed/adsorption, (3) countercurrent purge and (4) countercurrent displacement. A processing sequence is employed wherein the cocurrent purge/adsorption and countercurrent purge steps are carried out on a discontinuous basis, while cocurrent feed/adsorption and countercurrent displacement steps are carried out in overlapping sequence. Control means are provided to assure that the high normal paraffin-containing hydrocarbon feed gas and stripping gas are passed to the appropriate beds for said cocurrent purge/adsorption and countercurrent purge steps on a non-continuous basis, said feed gas being continuously fed to a mix drum for mixture with countercurrent purge effluent before removal for use in said cocurrent purge/adsorption step and in said cocurrent feed/adsorption step of the overall four-step process.

Claims

1. In an isobaric process for separating normal paraffins from non-normal hydrocarbons in a vapor feed stream by (1 ) cocurrent purge/adsorption with the selective adsorption of normal paraffins by passage of said feed gas stream to the feed end of an adsorbent bed in a system having four or more beds, with unadsorbed non-normal hydrocarbons displacing residual purge gas from the effluent end of the bed, (2) cocurrent feed/adsorption with additional quantities of said feed gas mixed with purge effluent from the next succeeding countercurrent purge step (3) being passed to the feed end of the bed, thereby advancing an adsorption front of adsorbed normal paraffins toward the effluent end of the bed, thus displacing non-normal hydrocarbons from the effluent end of the bed for recovery as a co-product stream, (3) countercurrent purge with a stripping gas being introduced to the effluent end of the bed and a purge effluent comprising stripping gas, residual unadsorbed non-paraffins and some desorbed normal paraffins being withdrawn from the feed end of the bed and recycled for mixture with feed gas to the bottom of a bed in said system, and (4) countercurrent displacement with the introduction of stripping gas to the top of the bed and the withdrawal of normal paraffins, together with stripping gas, as a product stream from the bottom of the bed, the improvement comprising carrying out said processing sequence so that, at the end of the cocurrent purge/adsorption and the countercurrent purge steps in one bed, the passage of said feed gas for said cocurrent purge/adsorption step and said stripping gas for said countercurrent purge step are discontinued for an interval of time during which said cocurrent feed/adsorption and countercurrent displacement steps are carried out in an overlapping manner such that at least two beds are on each of said steps during said interval, said feed gas entering the system by initial passage to a mix drum from which said feed gas for the cocurrent purge/adsorption step and said cocurrent feed/adsorption step are passed, said countercurrent purge effluent from step (3) being passed to said mix drum for mixture with said feed gas therein and passage to an adsorbent bed as part of the feed gas for said cocurrent purge/adsorption step and said cocurrent feed step, whereby the overlap of steps enables concentration and/or flow fluctuations inherent in the process to be obviated, and the process can advantageously be carried out with a desirable reduction in the size of the adsorption system and associated equipment.

2. The process of claim 1 in which said adsorption system comprises four adsorbent beds.

3. The process of claim 2 in which said feed gas stream contains at least about 35% normal paraffins.

4. The process of claim 3 in which said feed gas stream comprises a petroleum naphtha feedstock at least about 80% of which would be required for the selective adsorption step in the absence of said discontinuity of said selective adsorption and said countercurrent purge steps in a four bed system in which the feed for the selective adsorption step is withdrawn from the feed gas stream before said feed gas stream is passed to the mix drum.

5. The process of claim 4 in which said stripping gas comprises hydrogen.

6. The process of claim 1 and including controlling the flow of feed gas for the cocurrent purge/adsorption step and the flow of stripping gas for said countercurrent purge step such as to freeze said controls in the position reached at the end of said cocurrent purge/adsorption and countercurrent purge steps for the duration of said interval of time in which no flow of feed gas and of stripping gas for said steps is in effect, whereby undesired pressure bumps and adsorbent movement within the adsorbent beds due to surges in gas upon resumption of the passage of feed gas and stripping gas for said steps are effectively avoided.

7. The process of claim 6 in which said adsorption system comprises four beds.

8. The process of claim 7 in which said feed gas stream contains at least about 35% normal paraffins.

9. The process of claim 8 in which said feed gas stream contains at least about 40% normal paraffins.