Purification of carbon dioxide

• US 10,655,912 B2
• Filed: 10/22/2014
• Issued: 05/19/2020
• Est. Priority Date: 04/26/2012
• Status: Active Grant

• Current Assignee: Air Products and Chemicals Incorporated (Linde Plc)
• Original Assignee: Air Products and Chemicals Incorporated (Linde Plc)
• Inventors: Higginbotham, Paul, Palamara, John Eugene, Guvelioglu, Galip Hakan
• Primary Examiner(s): Pettitt, III, John F
• Application Number:
  US14/521,062
• Publication Number:
  US 20150114032A1
• Time in Patent Office: 2,036 Days
• CPC Class Codes: B01D 2256/22 Carbon dioxide
• CPC Class Codes: B01D 2257/304 Hydrogen sulfide
• CPC Class Codes: B01D 53/002 by condensation
• CPC Class Codes: C01B 17/167 Separation
• CPC Class Codes: F25J 1/0027 Oxides of carbon, e.g. CO2
• CPC Class Codes: F25J 2200/02 in a single pressure main column system
• CPC Class Codes: F25J 2200/04 in a dual pressure main column system
• CPC Class Codes: F25J 2200/30 using a side column in a single pressure column system
• CPC Class Codes: F25J 2200/40 Features relating to the provision of boil-up in the bottom of a column
• CPC Class Codes: F25J 2200/50 using multiple (re-)boiler-condensers at different heights of the column
• CPC Class Codes: F25J 2200/74 Refluxing the column with at least a part of the partially condensed overhead gas
• CPC Class Codes: F25J 2200/76 Refluxing the column with condensed overhead gas being cycled in a quasi-closed loop refrigeration cycle
• CPC Class Codes: F25J 2200/78 Refluxing the column with a liquid stream originating from an upstream or downstream fractionator column
• CPC Class Codes: F25J 2210/06 Splitting of the feed stream, e.g. for treating or cooling in different ways
• CPC Class Codes: F25J 2215/80 Carbon dioxide
• CPC Class Codes: F25J 2220/84 Separating high boiling, i.e. less volatile components, e.g. NOx, SOx, H2S
• CPC Class Codes: F25J 2230/80 the fluid being carbon dioxide
• CPC Class Codes: F25J 2235/02 using a pump in general or hydrostatic pressure increase
• CPC Class Codes: F25J 2235/80 the fluid being carbon dioxide
• CPC Class Codes: F25J 2240/02 Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. of the feed stream
• CPC Class Codes: F25J 2240/30 : Dynamic liquid or hydraulic expansion with extraction of work, e.g. single phase or two-phase turbine
• CPC Class Codes: F25J 2245/02 : Recycle of a stream in general, e.g. a by-pass stream
• CPC Class Codes: F25J 2260/20 : Integration in an installation for liquefying or solidifying a fluid stream
• CPC Class Codes: F25J 2260/80 : Integration in an installation using carbon dioxide, e.g. for EOR, sequestration, refrigeration etc.
• CPC Class Codes: F25J 2270/02 : Internal refrigeration with liquid vaporising loop
• CPC Class Codes: F25J 2270/80 : Quasi-closed internal or closed external carbon dioxide refrigeration cycle
• CPC Class Codes: F25J 2270/88 : Quasi-closed internal refrigeration or heat pump cycle, if not otherwise provided
• CPC Class Codes: F25J 2290/40 : Vertical layout or arrangement of cold equipments within in the cold box, e.g. columns, condensers, heat exchangers etc.
• CPC Class Codes: F25J 3/0266 : separation of carbon dioxide production of carbon dioxide in general C01B32/00
• CPC Class Codes: F25J 3/08 : Separating gaseous impurities from gases or gaseous mixtures or from liquefied gases or liquefied gaseous mixturescold traps B01D8/00
• CPC Class Codes: Y02P 20/129 : Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
• CPC Class Codes: Y02P 20/151 : Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Abstract

Impurities that are less volatile than carbon dioxide, e.g. hydrogen sulfide, are removed from crude carbon dioxide by processes involving distillation of said crude carbon dioxide in a distillation column system operating at super-atmospheric pressure(s) to produce carbon dioxide-enriched overhead vapor and bottoms liquid enriched with said impurities. Where such processes involve a single heat pump cycle, significant savings in power consumption are realized when the distillation column system is re-boiled by at least partially vaporizing liquid in or taken from an intermediate location in the column system.

Claims

1. A process for purifying crude carbon dioxide comprising at least one impurity that is less volatile than carbon dioxide, said process comprising:

feeding crude carbon dioxide to a distillation column system operating at super-atmospheric pressure(s) for separation to produce carbon dioxide-enriched overhead vapor and bottoms liquid enriched with said at least one impurity;

providing carbon dioxide-enriched liquid as reflux for said distillation column system;

re-boiling said distillation column system by at least partially vaporizing said impurity-enriched bottoms liquid and at least one intermediate liquid in or taken from an intermediate location in said distillation column system by indirect heat exchange to provide vapor for said distillation column system;

removing said carbon dioxide-enriched overhead vapor from said distillation column system; and

removing said impurity-enriched bottoms liquid, or a liquid derived from said impurity-enriched bottoms liquid, from said distillation column system,

wherein said process comprises a heat pump cycle using as working fluid said carbon dioxide-enriched overhead vapor from said distillation column system, said heat pump cycle comprising;

(a) warming said carbon dioxide-enriched overhead vapor by indirect heat exchange to produce warmed carbon dioxide-enriched gas;

(b) compressing said warmed carbon dioxide-enriched gas to produce compressed carbon dioxide-enriched recycle gas;

(c) using said compressed carbon dioxide-enriched recycle gas to provide at least a part of the reboil duty required to vaporize said impurity-enriched bottoms liquid thereby cooling said compressed carbon dioxide-enriched recycle gas;

(d) using said compressed carbon dioxide-enriched recycle gas to provide at least a part of the reboil duty required to vaporize said intermediate liquid(s) thereby cooling and at least partially condensing said compressed carbon dioxide-enriched recycle gas to produce carbon dioxide-enriched liquid;

(e) expanding said carbon dioxide-enriched liquid to produce expanded carbon dioxide-enriched liquid; and

(f) using at least a portion of said expanded carbon dioxide-enriched liquid to provide said reflux to said distillation column system;

wherein the compressed carbon dioxide-enriched recycle gas is at substantially the same pressure in steps (c) and (d).

2. The process of claim 1, wherein the, or at least one of the intermediate liquids, is enriched in the said at least one less volatile impurity.

3. The process of claim 1, wherein said compressed carbon dioxide-containing recycle gas is at a pressure from 15 bar to 60 bar.

4. The process of claim 1, wherein a portion of said working fluid is purged from said process.

5. The process of claim 1, wherein said crude carbon dioxide is crude carbon dioxide fluid derived from a natural source of carbon dioxide and expanded prior to feeding to said distillation column system.

6. The process of claim 5, wherein, prior to said expansion, said crude carbon dioxide fluid is at a super-critical pressure and a sub-critical temperature.

7. The process of claim 5, wherein said crude carbon dioxide fluid is cooled by indirect heat exchange prior to expansion.

8. The process of claim 7, wherein at least a portion of the duty required to cool said crude carbon dioxide fluid is provided by indirect heat exchange against at least one “

cold”

process stream.

9. The process of claim 5, wherein said expanded crude carbon dioxide is used as a “

cold”

process stream to provide refrigeration duty for said process.

10. The process of claim 1, wherein said crude carbon dioxide is derived from supercritical crude carbon dioxide fluid and carbon dioxide-enriched liquid is produced as a product.

11. The process of claim 10, wherein said carbon dioxide-enriched liquid is removed from said distillation column system, pumped and warmed by indirect heat exchange to produce warmed carbon dioxide-enriched liquid as said product.

12. The process of claim 11, wherein at least a portion of the duty required to warm said pumped carbon dioxide-enriched liquid is provided by indirect heat exchange against at least a portion of said working fluid from said heat pump cycle, after said portion of said working fluid has been compressed.

13. The process of claim 11, wherein said pumped carbon dioxide-enriched liquid is used as a “

cold”

process stream to provide refrigeration duty for the process.

14. The process of claim 1, wherein said impurity-enriched bottoms liquid, or said liquid derived from impurity-enriched bottoms liquid, is pumped and warmed by indirect heat exchange to provide impurity-rich waste liquid.

15. The process of claim 14, wherein at least a portion of the duty required to warm said pumped impurity-enriched bottoms liquid is provided by indirect heat exchange against at least a portion of said working fluid from said heat pump cycle, after said portion of said working fluid has been compressed.

16. The process of claim 14, wherein said impurity-enriched bottoms liquid, or said liquid derived from impurity-enriched bottoms liquid, is used as a “

cold”

process stream to provide refrigeration duty for the process.

17. The process of claim 1, wherein the operating pressure(s) said distillation column system is from 10 bar to 25 bar.

18. The process of claim 1, wherein said at least one impurity is hydrogen sulfide (H2S).

19. The process of claim 1, wherein said process is auto-refrigerated.

20. The process of claim 1, wherein a bulk of boil-up duty for said distillation column system is provided by said at least partial vaporization of said at least one intermediate liquid.

21. The process of claim 1 wherein the compressed carbon dioxide-enriched recycle gas is cooled but not condensed in step (c).