Serial flow continuous separation process

• US 4,498,991 A
• Filed: 06/18/1984
• Issued: 02/12/1985
• Est. Priority Date: 06/18/1984
• Status: Expired due to Fees

• Current Assignee: UOP Des Plaines IL A NY General Partnership
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: Oroskar, Anil R.
• Primary Examiner(s): NOT, DEFINED
• Application Number:
  US06/622,031
• Time in Patent Office: 239 Days
• Field of Search: 55/67, 55/74, 55/197, 55/387, 127/46.1, 127/46.2, 127/46.3, 210/659, 210/672, 210/676, 210/677, 210/691
• US Class Current: 210/659
• CPC Class Codes: B01D 15/1828 characterized by process features
• CPC Class Codes: B01D 2215/023 Simulated moving beds
• CPC Class Codes: B01D 2259/41 using plural beds of the same adsorbent in series
• CPC Class Codes: B01D 53/04 with stationary adsorbents B01D53/025 takes precedence
• CPC Class Codes: B01D 53/0423 Beds in columns
• CPC Class Codes: B01D 53/0446 Means for feeding or distributing gases

Abstract

A process for separating an extract component from a raffinate component contained in a feed mixture. A unidirectional fluid flow system is maintained through a series of separating units through which the components travel at different rates. The units are interconnected in series so as to form a single closed loop. A component concentration distribution is established within the system of units so as to comprise a series of zones. Feed and displacement fluid are each mixed with a different intercolumn stream prior to being passed into the inlets of two of the units and extract and raffinate are taken only as portions of streams from outlets of two or more of the units at appropriate points on the component concentration distribution. At the appropriate times the inlets and outlets are shifted so as to simulate movement of the units in a direction downstream with respect to the direction of fluid flow and thereby enable the inlets and outlets to continually lie in the appropriate zones.

Claims

1. A process for separating an extract component from a raffinate component contained in a feed mixture comprising the steps of:

(a) maintaining a unidirectional fluid flow system through a series of separating units in which said components have differential rates of travel due to selective retardation or acceleration of each of said components in each of said units, each of said units having a fluid inlet and a fluid outlet, said separating units being interconnected so as to achieve serial flow through said units in a single closed loop;

(b) mixing said feed mixture with the fluid emanating from one of said fluid outlets and passing the resultant first mixture into the next inlet downstream of said outlet in said series and mixing said displacement fluid with the fluid emanating from another of said fluid outlets and passing the resultant second mixture into the next inlet downstream of said other outlet in said series;

(c) establishing within said separating units a component concentration distribution, zones of which comprise, sequentially, progressing in the direction of fluid flow, extract and raffinate component mixture with the proportion of the raffinate component to extract component being greater than in the feed mixture, extract and raffinate component mixture with the proportion of extract component to raffinate component being greater than in the feed mixture, concentrated extract component, extract component diluted with displacement fluid, raffinate component diluted with displacement fluid, and concentrated raffinate component;

(d) withdrawing as an extract product stream a portion of at least one of the streams between an adjacent pair of separating units, and withdrawing as a raffinate product stream a portion of at least one other of the streams between a different adjacent pair of separating units, the selection of the streams from which said product streams are withdrawn being consistent with the desired composition of each of said product streams;

(e) periodically simultaneously advancing in an upstream direction with respect to fluid flow in said separating units, all of said inlets and outlets to effect the shifting of zones in a downstream direction with respect to said fluid flow, said shifting being effected prior to the progression through said units of said component concentration distribution to the extent that the composition of the inlet or outlet streams to or from any zone becomes inconsistent with the desired composition of that zone.

2. The process of claim 1 wherein the flow rates of the fluid streams to said fluid inlets and from said fluid outlets are adjusted to provide the desired transition compositions of each inlet and outlet stream at the start and end of each flow period between said shifting.

3. The process of claim 1 wherein said separating units comprise columns at least partially packed with adsorbent having adsorptive selectivity for said extract component as compared to said raffinate component, said displacement fluid comprising a desorbent capable of effecting desorption of said extract component from said adsorbent, said first mixture of step (b) being contacted with said adsorbent at adsorption conditions and said second mixture of step (b) being contacted with said adsorbent at desorption conditions.

4. The process of claim 3 wherein said fluid flow system is in liquid phase and said adsorption and desorption conditions comprise temperatures and pressures which effect said liquid phase.

5. The process of claim 1 wherein there are three or more components in said feed mixture, the rates of travel of which in said units are all different and which comprise a spectrum ranging from the rate of the most selectively retarded component to the rate of the least selectively retarded component, each pair of components having adjacent rates of travel on said spectrum being considered, as between said pair, an extract component and raffinate component for the most retarded and least retarded, respectively, there being a component concentration distribution as in step (c) for each such pair, the selection of the stream from which product streams are withdrawn in step (d) being consistent with the desired purity and concentration of each of said components.

6. The process of claim 5 wherein there is at least one separating unit for each component to be separated.