Agglomerated particulate low-rank coal feedstock and uses thereof

• US 9,034,061 B2
• Filed: 09/27/2013
• Issued: 05/19/2015
• Est. Priority Date: 10/01/2012
• Status: Active Grant

• Current Assignee: Sure Champion Investments Limited
• Original Assignee: GreatPoint Energy, Inc.
• Inventors: Robinson, Earl T., Keckler, Kenneth P., Raman, Pattabhi K., Sirdeshpande, Avinash
• Primary Examiner(s): Toomer, Cephia D
• Application Number:
  US14/039,321
• Publication Number:
  US 20140091258A1
• Time in Patent Office: 599 Days
• Field of Search: 445/50, 445/92, 445/93, 445/95, 445/96
• US Class Current: 44/551
• CPC Class Codes: C10J 3/72 Other features
• CPC Class Codes: C10L 5/04 Raw material of mineral origin to be used; Pretreatment thereof pretreatment of fuels of non-mineral origin C10L5/40
• CPC Class Codes: C10L 5/10 with the aid of binders, e.g. pretreated binders
• CPC Class Codes: C10L 5/363 Pellets or granulates
• CPC Class Codes: F23K 1/00 Preparation of lump or pulverulent fuel in readiness for delivery to combustion apparatus
• CPC Class Codes: F23L 7/007 Supplying oxygen or oxygen-enriched air
• CPC Class Codes: Y02E 20/34 Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Abstract

The present invention relates generally to processes for preparing agglomerated particulate low-rank coal feedstocks of a particle size suitable for reaction in a fluidized-bed reactor and certain other gasification reactors and, in particular, for coal gasification and combustion applications. The present invention also relates to integrated coal gasification and combustion processes including preparing and utilizing such agglomerated particulate low-rank coal feedstocks.

Claims

1. A process for preparing a free-flowing agglomerated particulate low-rank coal feedstock of a specified particle size distribution, the process comprising the steps of:

(a) selecting a specification for the particle size distribution of the free-flowing agglomerated particulate low-rank coal feedstock, the specification comprising

(i) a target dp(50) that is a value in the range of from about 100 microns to about 6000 microns,

(ii) a target upper end particle size that is a value greater than the target dp(50), and

(iii) a target lower end particle size that is a value less than the target dp(50);

(b) providing a raw particulate low-rank coal feedstock having an initial particle density;

(c) grinding the raw particulate low-rank coal feedstock to a ground dp(50) of from about 2% to about 50% of the target dp(50), to generate a ground low-rank coal feedstock;

(d) pelletizing the ground low-rank coal feedstock with water and a binder to generate free-flowing agglomerated low-rank coal particles having a pelletized dp(50) of from about 90% to about 110% of the target dp(50), and a particle density of at least about 5% greater than the initial particle density, wherein the binder is selected from the group consisting of a water-soluble binder, a water-dispersible binder and a mixture thereof; and

(e) removing all or a portion of

(i) particles larger than the upper end particle size,

(ii) particles smaller than the lower end particle size, or

(iii) both (i) and (ii),

from the free-flowing agglomerated low-rank coal particles to generate the free-flowing agglomerated low-rank coal feedstock.

2. The process of claim 1, wherein about 90 wt % or greater of

(i) particles larger than the upper end particle size, and

(ii) particles smaller than the lower end particle size,

are removed from the free-flowing agglomerated low-rank coal particles to generate the free-flowing agglomerated low-rank coal feedstock.

3. The process of claim 1, wherein the raw low-rank particulate coal feedstock has a Hardgrove Grinding Index of about 50 or greater.

4. The process of claim 3, wherein the raw low-rank particulate coal feedstock has a Hardgrove Grinding Index of about 70 or greater.

5. The process of claim 4, wherein the raw low-rank particulate coal feedstock has a Hardgrove Grinding Index of from about 70 to about 130.

6. The process of claim 1, wherein the grinding step is a wet grinding step.

7. The process of claim 6, wherein an acid is added in the wet grinding step.

8. The process of claim 1, wherein the process further comprises the step of washing the raw ground low-rank coal feedstock from the grinding step to generate a washed ground low-rank coal feedstock.

9. The process of claim 8, wherein the raw ground low-rank coal feedstock is washed to remove one or both of inorganic sodium and inorganic chlorine.

10. The process of claim 8, wherein the washed ground low-rank coal has a water content, and the process further comprises the step of removing a portion of the water content from the washed ground low-rank coal feedstock to generate the ground low-rank coal feedstock for the pelletizing step.

11. The process of claim 1, wherein the binder comprises an alkali metal.

12. The process of claim 1, wherein the pelletization is a two-stage pelletization performed by a first type of pelletizer followed in series by a second type of pelletizer.

13. The process of claim 1, wherein the particle density of the free-flowing agglomerated low-rank coal particles is at least about 10% greater than the initial particle density.

14. The process of claim 1, wherein the raw particulate low-rank coal feedstock is ground to a ground dp(50) of from about 5% to about 50% of the target dp(50).

15. The process of claim 1, wherein the target dp(50) is a value in the range of from about 1000 microns to about 5000 microns.

16. The process of claim 15, wherein the target upper end particle size is a value greater than the target dp(50), and less than or equal to 6350 microns;

and the target lower end particle size is a value less than the target dp(50), and greater than or equal to about 149 microns.

17. The process of claim 1, wherein the target dp(50) is a value in the range of from about 3000 microns to about 6000 microns.

18. The process of claim 17, wherein the target upper end particle size is a value greater than the target dp(50), and less than or equal to 8000 microns;

and the target lower end particle size is a value less than the target dp(50), and greater than or equal to about 2000 microns.

19. The process of claim 1, wherein the target dp(50) is a value in the range of from about 100 microns to about 200 microns.

20. A process for gasifying a low-rank coal feedstock to a raw synthesis gas stream comprising carbon monoxide and hydrogen, the process comprising the steps of:

(A) preparing a low-rank coal feedstock of a specified particle size distribution;

(B) feeding into a fluidized-bed gasifying reactor

(i) low-rank coal feedstock prepared in step (A), and

(ii) a gas stream comprising one or both of steam and oxygen;

(C) reacting low-rank coal feedstock fed into gasifying reactor in step (B), at elevated temperature and pressure, with the gas stream, to generate a raw gas comprising carbon monoxide and hydrogen; and

(D) removing a stream of the raw gas generated in the gasifying reactor in step (C) as the raw synthesis gas stream,

wherein step (A) comprises the process as set forth in claim 1.

21. The process of claim 20, wherein step (A) comprises the process as set forth in claim 15.

22. The process of claim 20, wherein step (A) comprises the process as set forth in claim 16.

23. The process of claim 20, wherein step (A) comprises the process as set forth in claim 17.

24. The process of claim 20, wherein step (A) comprises the process as set forth in claim 18.

25. A process for combusting a low-rank coal feedstock to generate heat energy, the process comprising the steps of:

(A1) preparing a low-rank coal feedstock of a specified particle size distribution;

(B1) feeding into a fluidized-bed combustor

(i) low-rank coal feedstock prepared in step (A1), and

(ii) oxygen;

(C1) combusting low-rank coal feedstock fed into the combustor in step (B1), at elevated temperature and pressure, with oxygen to generate a combustion gas comprising carbon dioxide and heat energy; and

(D1) recovering heat energy from the combustion gas,

wherein step (A1) comprises the process as set forth in claim 1.

26. The process of claim 25, wherein step (A1) comprises the process as set forth in claim 17.

27. The process of claim 25, wherein step (A1) comprises the process as set forth in claim 19.