Agglomerated particulate low-rank coal feedstock and uses thereof

• US 9,034,058 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): JOHNSON, EDWARD M
• Application Number:
  US14/039,454
• Publication Number:
  US 20140091259A1
• Time in Patent Office: 599 Days
• Field of Search: 233/14, 233/13.R
• US Class Current: 23/314
• CPC Class Codes: C10J 3/46 Gasification of granular or pulverulent flues in suspension
• CPC Class Codes: C10L 5/10 with the aid of binders, e.g. pretreated binders
• CPC Class Codes: C10L 5/363 Pellets or granulates

Abstract

The present invention relates generally to processes for preparing agglomerated particulate low-rank coal feedstocks of a particle size suitable for reaction in certain gasification reactors and, in particular, for coal gasification. The present invention also relates to integrated coal gasification 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 upper end particle size of about 72600 microns of less,

(ii) a target lower end particle size of about 6350 microns or greater, and

(iii) a target dp(50) between the target upper end particle size and target lower end particle size;

(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 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,

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 the raw low-rank particulate coal feedstock has a Hardgrove Grinding Index of about 50 or greater.

3. The process of claim 2, wherein the raw low-rank particulate coal feedstock has a Hardgrove Grinding Index of about 70 or greater.

4. The process of claim 3, wherein the raw low-rank particulate coal feedstock has a Hardgrove Grinding Index of from about 70 to about 130.

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

6. The process of claim 5, wherein an acid is added in the wet grinding step.

7. 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.

8. The process of claim 7, wherein the raw ground low-rank coal feedstock is washed to remove one or both of inorganic sodium and inorganic chlorine.

9. The process of claim 7, 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.

10. 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.

11. 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.

12. 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).

13. 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 fixed-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.

14. The process of claim 13, wherein step (A) comprises the process as set forth in claim 2.

15. The process of claim 14, wherein step (A) comprises the process as set forth in claim 3.

16. The process of claim 15, wherein step (A) comprises the process as set forth in claim 4.

17. The process of claim 15, wherein step (A) comprises the process as set forth in claim 10.