Use of contaminated low-rank coal for combustion

• US 9,328,920 B2
• Filed: 09/27/2013
• Issued: 05/03/2016
• Est. Priority Date: 10/01/2012
• Status: Active Grant

• Current Assignee: Sure Champion Investments Limited
• Original Assignee: GreatPoint Energy, Inc.
• Inventors: Sirdeshpande, Avinash, Keckler, Kenneth P., Robinson, Earl T., Raman, Pattabhi K.
• Primary Examiner(s): Laux, David J
• Application Number:
  US14/040,058
• Publication Number:
  US 20140090584A1
• Time in Patent Office: 949 Days
• US Class Current: 1/1
• CPC Class Codes: C10L 5/366 Powders
• CPC Class Codes: C10L 9/00 Treating solid fuels to improve their combustion
• CPC Class Codes: C10L 9/08 by heat treatments, e.g. calcining
• CPC Class Codes: F23C 10/10 the separation apparatus being located outside the combustion chamber
• CPC Class Codes: F23K 1/00 Preparation of lump or pulverulent fuel in readiness for delivery to combustion apparatus
• CPC Class Codes: F23K 1/02 Mixing solid fuel with a liquid, e.g. preparing slurries
• CPC Class Codes: F23K 1/04 Heating fuel prior to delivery to combustion apparatus
• CPC Class Codes: F23K 2201/10 Pulverizing
• CPC Class Codes: F23K 2201/20 Drying
• CPC Class Codes: F23K 2900/01001 Cleaning solid fuel before combustion to achieve reduced emissions
• CPC Class Codes: F23K 3/02 Pneumatic feeding arrangements, i.e. by air blast
• 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 an inorganic sodium and/or chlorine contaminated low-rank coal feedstock for combustion in a fluidized fuel combustor to generate steam and, desirably, co-generate electricity.

Claims

1. A process for generating steam from a particulate low-rank coal feedstock, the process comprising the steps of:

(a) providing a raw low-rank coal feedstock comprising an initial contaminant content, wherein the initial contaminant content comprises

(1) an initial inorganic chlorine content of at least about 0.1 wt % based on the dry weight of the raw low-rank coal feedstock, or

(2) an initial inorganic sodium content of at least about 1.0 wt % based on the dry weight of the raw low-rank coal feedstock, or

(3) both (1) and (2);

(b) grinding the raw low-rank coal feedstock to produce a ground low-rank coal feedstock;

(c) washing the ground low-rank coal feedstock with an aqueous wash stream to generate a washed ground low-rank coal feedstock and a wastewater stream, the washed ground low-rank coal feedstock having

(1) a washed inorganic chlorine content of less than about 50 wt % of the initial inorganic chlorine content, but no greater than about 0.1 wt % based on the dry weight of the washed ground low-rank coal feedstock, and

(2) a washed inorganic sodium content of less than about 50 wt % of the initial inorganic sodium content, but no greater than about 0.1 wt % based on the dry weight of the washed ground low-rank coal feedstock;

(d) contacting the washed ground low-rank coal feedstock with a dry gas stream and thermal energy in a thermal drying unit to generate a reduced-moisture washed ground low-rank coal feedstock and a moisture recovery stream, wherein at least a portion of the thermal energy is provided by a lower-pressure steam stream at a pressure of from about 10 psig (about 170 kPa absolute) to about 50 psig (about 446 kPa absolute), and wherein the reduced-moisture washed ground low-rank coal feedstock is free flowing with a moisture content no greater than about 40 wt % based on the total weight of the reduced-moisture washed ground low-rank coal feedstock;

(e) feeding the reduced-moisture washed ground low-rank coal feedstock and an oxygen-containing gas stream into a combustor;

(f) combusting the reduced-moisture low-rank coal feedstock in the combustor with oxygen to generate a combustion gas stream comprising steam, carbon dioxide and heat energy;

(g) recovering heat energy from the combustion gas stream by generating a higher-pressure steam stream at a pressure of at least about 150 psig (at least about 1136 kPa absolute),

(h) converting at least a portion of the higher-pressure steam stream to generate the lower-pressure steam stream;

(i) condensing the moisture stream from step (d) to generate a condensed moisture stream;

(j) treating the wastewater stream from washing step (c) to generate a recovered water stream; and

(k) recycling (1) at least a portion of the condensed moisture stream, or (2) at least a portion of the recovered water stream, or (3) both (1) and (2), to the washing step (c), wherein the aqueous wash stream comprises at least in part the recycled portion of the condensed moisture stream and the recovered water stream.

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 1, wherein the washing step and the grinding step occur concurrently.

7. The process of claim 1, wherein there is a washing step that occurs after the grinding step.

8. The process of claim 1, wherein the washed ground low-rank coal feedstock is agglomerated subsequent to step (c) and before step (d).

9. The process of claim 1, wherein the reduced-moisture washed ground low-rank coal feedstock fed into the combustor has a particle size distribution in which the dp(50) is a value between about 100 microns and about 6000 microns.

10. The process of claim 9, wherein the dp(50) is a value in the range of from about 3000 microns to about 6000 microns.

11. The process of claim 1, wherein the combustor is a circulating fluidized-bed combustor.

12. The process of claim 10, wherein the combustor is a circulating fluidized-bed combustor.

13. The process of claim 9, wherein the dp(50) is a value in the range of from about 100 microns to about 200 microns.

14. The process of claim 1, wherein the combustor is a pulverized coal boiler.

15. The process of claim 10, wherein the combustor is a pulverized coal boiler.

16. The process of claim 1, wherein the raw low-rank coal feedstock possesses an initial moisture content, and the moisture content of the reduced-moisture washed ground low-rank coal feedstock is less than the initial moisture content of the raw low-rank coal feedstock (total wt/wt basis).

17. The process of claim 16, wherein the initial moisture content of the raw low-rank coal feedstock is at least about 25 wt % based on total weight of the raw low-rank coal feedstock.