초록 ▼

In a process for selectively separating 1-butene from a C4 feed stream comprising at least 1-butene, cis-2-butene and trans-2-butene, the feed stream is passed through a first bed of an adsorbent comprising a crystalline microporous material to form a substantially trans-2-butene-free effluent strea

In a process for selectively separating 1-butene from a C4 feed stream comprising at least 1-butene, cis-2-butene and trans-2-butene, the feed stream is passed through a first bed of an adsorbent comprising a crystalline microporous material to form a substantially trans-2-butene-free effluent stream. Then, the substantially trans-2-butene-free effluent stream is passed through a second bed of an adsorbent comprising a crystalline microporous material to form a substantially 1-butene-free effluent stream, whereby the 1-butene is separated from the feed stream. The adsorbed 1-butene is then typically desorbed from the second adsorbent bed either by lowering the pressure or raising the temperature of the bed.

대표청구항 ▼

What is claimed is: 1. A process for selectively separating 1-butene from a C 4 feed stream comprising at least 1-butene, trans-2-butene and cis-2-butene, the process comprising the steps of: (a) passing the feed stream through a first bed of an adsorbent comprising a crystalline microporous materi

What is claimed is: 1. A process for selectively separating 1-butene from a C 4 feed stream comprising at least 1-butene, trans-2-butene and cis-2-butene, the process comprising the steps of: (a) passing the feed stream through a first bed of an adsorbent comprising a crystalline microporous material to form a substantially trans-2-butene-free effluent stream; and (b) passing the effluent stream through a second bed of an adsorbent comprising a crystalline microporous material to form a substantially 1-butene-free effluent stream, whereby the 1-butene is separated from the feed stream, wherein the crystalline microporous materials of steps (a) and (b) comprise different cation-free non-acidic crystalline microporous materials, wherein the window size of the cation-free non-acidic crystalline microporous material of step (b) is larger than the window size of the cation-free non-acidic crystalline microporous material of step (a). 2. The process of claim 1 wherein the crystalline microporous materials of steps (a) and (b) comprise crystalline microporous materials having at least one system of channels, wherein each system is defined by an 8-membered ring of tetrahedrally coordinated framework T-atoms. 3. The process of claim 2 wherein the crystalline microporous materials of steps (a) and (b) comprise crystalline microporous materials having a system of three interconnecting 8-membered ring channels. 4. The process of claim 2 wherein the framework T-atoms of step (a) comprise silicon and derivatives thereof. 5. The process of claim 4 wherein the crystalline microporous material of step (a) comprises Si-CHA. 6. The process of claim 4 wherein the crystalline microporous material of step (a) comprises ITE. 7. The process of claim 4 wherein the framework T-atoms of step (b) comprise phosphorus and derivatives thereof. 8. The process of claim 7 wherein the crystalline microporous material of step (b) is selected from the group consisting of aluminophosphates, gallophosphates, galloaluminophosphates, metalloaluminophosphates, metalloaluminophosphosilicates and derivatives thereof. 9. The process of claim 7 wherein the crystalline microporous material of step (b) is selected front the group consisting of AIPO-34, AIPO-18, GaPO-34 and GaPO-18. 10. The process of claim 1 wherein steps (a) and (b) are performed under kinetic-based adsorption conditions. 11. The process of claim 10 wherein steps (a) and (b) are performed under pressure swing adsorption conditions. 12. The process of claim 10 wherein steps (a) and (b) are performed under temperature swing adsorption conditions. 13. The process of claim 10 wherein steps (a) and (b) are performed under a combination of pressure and temperature swing adsorption conditions. 14. The process of claim 1 wherein each of steps (a) and (b) are performed within prescribed adsorption times. 15. The process of claim 14 wherein the adsorption times of steps (a) and (b) comprise durations maximizing the uptake of trans-2-butene and J-butene, respectively. 16. The process of claim 1 further comprising the step of desorbing the 1-butene from the second adsorbent bed, whereby the 1-butene is recovered from the feed stream. 17. The process of claim 1 further comprising the steps of: (c) desorbing the trans2-butene from the first adsorbent bed; (d) collecting the effluent stream from step (b) above and the desorbed trans-2-butene from step (c) above to form a secondary feed stream; (c) isomerizing the secondary feed stream to form an equilibrium mixture of at least 1-butene, trans-2-butene and cis-2-butene; and (f) repeating the steps of claim 1.