Embedded alkane dehydrogenation systems and processes

Patent metadata

Field	Value
Publication number	US-10246386-B2
Application number	US-201515509902-A
Country	US
Kind code	B2
Filing date	Sep 9, 2015
Priority date	Sep 12, 2014
Publication date	Apr 2, 2019
Grant date	Apr 2, 2019

Abstract

Systems for dehydrogenating an alkane are provided. An exemplary system includes a furnace and further includes alkane heating chambers, regeneration mixture heating chambers, and two groups of reaction chambers, all located within the furnace. The alkane heating chambers and regeneration mixture heating chambers can preheat an alkane feed and a regeneration mixture feed, respectively. The two groups of reaction chambers can be switchably coupled to an alkane feed and a regeneration mixture feed such that an alkane can flow through one group of reaction chambers while a regeneration mixture flows through the other group of reaction chambers. Processes for dehydrogenating an alkane are also provided.

First claim

What is claimed is:

1. A system for dehydrogenating an alkane, comprising:
a furnace;
one or more alkane heating chambers located within the furnace for preheating an alkane feed;
one or more regeneration mixture heating chambers located within the furnace for preheating a regeneration mixture feed;
a first group of two or more reaction chambers located within the furnace for dehydrogenating an alkane, the first group of reaction chambers being switchably coupled to the one or more alkane heating chambers to receive a heated alkane feed therefrom, and switchably coupled to the one or more regeneration mixture heating chambers to receive a heated regeneration mixture feed therefrom; and
a second group of two or more reaction chambers located within the furnace for dehydrogenating an alkane, the second group of reaction chambers being switchably coupled to the one or more alkane heating chambers to receive a heated alkane feed therefrom, and switchably coupled to the one or more regeneration mixture heating chambers and configured to receive a heated regeneration mixture feed therefrom;
the system being configured such that when the first group of reaction chambers are switched to receive the heated alkane feed, the second group of reaction chambers are switched to receive the heated regeneration mixture feed; and
when the first group of reaction chambers is switched to receive the heated regeneration mixture feed, the second group of reaction chambers is switched to receive the heated alkane feed;
wherein the system further comprises a first heated alkane feed line coupled to a heated alkane outlet line and further coupled to the first group of reaction chambers, for feeding the heated alkane from the heated alkane outlet line to the first group of reaction chambers, the first heated alkane feed line comprising a first heated alkane feed line valve;
a second heated alkane feed line coupled to the heated alkane outlet line and further coupled to the second group of reaction chambers, for feeding the heated alkane from the heated alkane outlet line to the second group of reaction chambers, the second heated alkane feed line comprising a second heated alkane feed line valve;
a first heated regeneration mixture feed line coupled to a heated regeneration mixture outlet line and further coupled to the first group of reaction chambers, for feeding the heated regeneration mixture from the heated regeneration mixture outlet line to the first group of reaction chambers, the first heated regeneration mixture feed line comprising a first heated regeneration mixture feed line valve; and
a second heated regeneration mixture feed line coupled to the heated regeneration mixture outlet line and further coupled to the second group of reaction chambers, for feeding the heated regeneration mixture from the heated regeneration mixture outlet line to the second group of reaction chambers, the second heated regeneration mixture feed line comprising a second heated regeneration mixture feed line valve;
wherein the first heated alkane feed line and the second heated alkane feed line each extend out of the furnace and each are separately directed back into the furnace after passing through the first heated alkane feed line valve and the second heated alkane feed line valve, respectively;
wherein the first heated regeneration mixture feed line and the second heated regeneration mixture feed line each extend out of the furnace and each separately are directed back into the furnace after passing through the first heated regeneration mixture feed line valve and the second heated regeneration mixture feed line valve, respectively;
where the first heated alkane feed line and the second heated alkane feed line are separate from one another and from the first heated regeneration mixture feed line and the second heated regeneration mixture feed line and wherein the first heated regeneration mixture feed line and the second heated regeneration mixture feed line are separate from one another and from the first heated alkane feed line and the second heated alkane feed line.

2. The system of claim 1 , wherein
the heated alkane outlet line is coupled to the one or more alkane heating chambers, for removing the heated alkane from the one or more alkane heating chambers.

3. The system of claim 1 , wherein
the heated regeneration mixture outlet line is coupled to the one or more regeneration mixture heating chambers, for removing the heated regeneration mixture from the one or more regeneration mixture heating chambers.

4. The system of claim 1 , wherein the one or more alkane heating chambers and the one or more regeneration mixture heating chambers are positioned near the top of the furnace.

5. The system of claim 1 , wherein the one or more alkane heating chambers and the one or more regeneration mixture heating chambers are positioned adjacent to one another.

6. The system of claim 1 , wherein the first group of reaction chambers and the second group of reaction chambers are positioned adjacent to one another.

7. The system of claim 5 , wherein the one or more alkane heating chambers and the one or more regeneration mixture heating chambers are positioned within the furnace above the first group of reaction chambers and above the second group of reaction chambers.

8. The system of claim 1 , wherein the first group of reaction chambers and the second group of reaction chambers comprise a Pt- or Cr-based catalyst.

9. The system of claim 8 , wherein the catalyst comprises chromium oxide.

10. The system of claim 1 , wherein the first group of reaction chambers and the second group of reaction chambers comprise a catalyst-filled plate.

11. The system of claim 1 , wherein an alkane heating temperature and a regeneration mixture heating temperature are within 100° C. of one another.

12. A system for dehydrogenating an alkane, comprising:
a furnace;
means for alkane heating located within the furnace, means for regeneration mixture heating located within the furnace, a first group of reaction chambers located within the furnace, and a second group of reaction chambers located within the furnace; and
means for switchably feeding a heated alkane feed and a heated regeneration mixture feed into the first group of reaction chambers and the second group of reaction chambers;
wherein the means for switchably feeding the heated alkane feed and the heated regeneration mixture feed comprises a first heated alkane feed line coupled to a heated alkane outlet line and further coupled to the first group of reaction chambers, for feeding the heated alkane from the heated alkane outlet line to the first group of reaction chambers, the first heated alkane feed line comprising a first heated alkane feed line valve;
a second heated alkane feed line coupled to the heated alkane outlet line and further coupled to the second group of reaction chambers, for feeding the heated alkane from the heated alkane outlet line to the second group of reaction chambers, the second heated alkane feed line comprising a second heated alkane feed line valve;
a first heated regeneration mixture feed line coupled to a heated regeneration mixture outlet line and further coupled to the first group of reaction chambers, for feeding the heated regeneration mixture from the heated regeneration mixture outlet line to the first group of reaction chambers, the first heated regeneration mixture feed line comprising a first heated regeneration mixture feed line valve; and
a second heated regeneration mixture feed line coupled to the heated regeneration mixture outlet line and further coupled to the second group of reaction chambers, for feeding the heated re

Assignees

• Sabic Global Technologies Bv

Inventors

• Nawaz Zeeshan

Classifications

• B01J23/96

  of catalysts comprising metals, oxides or hydroxides of the noble metals · CPC title

• F23C2900/05081

  Disposition of burners relative to each other creating specific heat patterns · CPC title

• F27B1/005

  wherein no smelting of the charge occurs, e.g. calcining or sintering furnaces · CPC title

• C07C11/02

  Alkenes · CPC title

• C07C5/3335

  with metals · CPC title