Combustion of fuel containing alkalines

• US 4,771,712 A
• Filed: 06/24/1987
• Issued: 09/20/1988
• Est. Priority Date: 06/24/1987
• Status: Expired due to Term

• Current Assignee: Foster Wheeler Energia Oy (John Wood Group PLC)
• Original Assignee: Ahlstrom Corporation
• Inventors: Tormikoski, Pekka, Kiiskila, Erkki, Engstrom, Folke
• Primary Examiner(s): Warner, Steven E.
• Application Number:
  US07/065,757
• Time in Patent Office: 454 Days
• Field of Search: 110/245, 110/263, 110/342, 110/343, 110/344, 110/345, 110/347, 110/203, 110/204, 122/4 D, 431/7, 431/170, 432/15, 432/58, 34/57 A, 60/39, 60/464, 165/104.16
• US Class Current: 110/347
• CPC Class Codes: C10L 9/10 by using additives
• CPC Class Codes: F23C 10/10 the separation apparatus being located outside the combustion chamber
• CPC Class Codes: F23C 2206/101 Entrained or fast fluidised bed
• CPC Class Codes: F23J 7/00 Arrangement of devices for supplying chemicals to fire
• 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

A method of burning solid fuel having low melting point alkaline compositions, such as alkali metal salts, particularly lignite and salty brown coal. The fuel is introduced into the reaction chamber of a circulating fluidized bed reactor, and is mixed prior to introduction to the reaction chamber with a reactant material capable of reacting with the low melting point alkaline compositions of the fuel to produce high melting point alkali metal compounds during combustion. The temperature in the reaction chamber is kept below the melting point of the formed alkali metal compounds. The reactant material comprises silica oxide or a metal oxide, or hydroxide, of the group consisting of aluminum, calcium, magnesium, iron, titanium, and mixtures of two or more thereof. Kaolin is particularly effective, especially when the molar ratio of Al/(Na and K) is at least 1.0.

Claims

1. A method of burning solid fuel having low melting point alkaline compositions, to produce and recover heat energy, utilizing a circulating fluidized bed reactor having a reaction chamber, comprising the steps of:

(a) introducing solid fuel having low melting point alkaline compositions, and gas containing oxygen, into the reaction chamber, so that combustion occurs in a fluidized bed, and hot exhaust gases containing solid particles are discharged from the reaction chamber;

(b) recirculating solid particles, separated from the exhaust gases discharged from the reaction chamber, back into the reaction chamber;

(c) introducing into the reaction chamber, with the fuel, a reactant material capable of reacting with the low melting point alkaline compositions of the fuel to produce high melting point alkali metal compounds during combustion of the fuel; and

(d) controlling addition of oxygen and fuel into the reaction chamber, and/or other parameters affecting combustion temperature, so that the temperature in all portions of the reaction chamber is lower than the melting point of the alkali metal compounds produced during reaction of the reactant material with alkaline compositions of the fuel.

2. A method as recited in claim 1 wherein the fuel is selected from the group consisting of lignite and salty brown coal, and the fuel is mixed together with the reactant material and solid particulates before it is added to the reaction chamber.

3. A method as recited in claim 1 wherein step (d) is practiced by recovering heat energy directly from the reaction chamber utilizing heat recovery apparatus disposed on the surface of or in the reactor chamber, and the fuel is mixed together with the reactant material and solid particulates before it is added to the reaction chamber.

4. A method as recited in claim 1 wherein the reactant material is an oxide, or a hydroxide which is converted to an oxide during combustion, of the group consisting of aluminum, calcium, magnesium, silica, iron, titanium, and mixtures of two or more of aluminum, calcium, magnesium, silica, iron, and titanium;

and wherein step (c) is practiced by introducing the reactant material in solid particulate form into the reaction chamber.

5. A method as recited in claim 4 wherein the reactant material is a metal oxide, or hydroxide which is converted to an oxide during combustion, and wherein the alkaline compositions in the fuel contain alkali metal salts;

and wherein step (c) is practiced so that the ratio of metal of the metal oxide to metal of the alkali metal salts is at least about 1.0.

6. A method as recited in claim 5 wherein the reactant material is kaolin which is added in solid particulate form, and wherein the alkali metal salts include sodium and potassium salts, and wherein step (c) is practiced so that the ratio of Al/(Na and K) is at least 1.0.

7. A method as recited in claim 4 wherein the reactant material is kaolin.

8. A method as recited in claim 7 wherein the alkaline compositions contained in the fuel include sodium and potassium compositions;

and wherein sufficient kaolin is added so that the molar ratio of Al/(Na and K) is at least 1.0, and unreacted kaolin particles are separated and recirculated in the practice of step (b).

9. A method as recited in claim 7 wherein step (d) is practiced by recovering heat energy directly from the reaction chamber utilizing heat recovery apparatus disposed on the surface of or in the reactor chamber.

10. A method as recited in claim 9 wherein the fuel is selected from the group consisting of lignite and salty brown coal.

11. A method as recited in claim 9 comprising the further step of adding limestone to the reaction chamber with the reactant material, to adsorb sulphur.

12. A method of operating a circulating fluidized bed reactor after startup, the reactor having a reaction chamber, comprising the steps of, after startup:

(a) feeding fuel, selected from the group consisting essentially of lignite and salty brown coal, into the reaction chamber, along with gas including oxygen, to provide a fluidized bed in the reaction chamber in which combustion takes place to produce exhaust gases;

(b) feeding kaolin into the reaction chamber;

(c) withdrawing solid particles and ash from the exhaust gases from the reaction chamber, and recirculating them to the reaction chamber; and

(d) withdrawing and utilizing heat energy from the reactor;

steps (a)-(d) being practiced so that the circulating bed material comprises mainly fuel, kaolin, and ash, with little sand or other bed-forming constituents, and agglomeration of the bed material and sintering of the fuel do not occur.

13. A method as recited in claim 12 wherein the fuel contains sodium and potassium salts, and wherein step (b) is practiced so that sufficient kaolin is added so that the molar ratio of Al/(Na and K) is at least about 1.0.

14. A method as recited in claim 13 comprising the further steps of withdrawing and recovering heat directly from the reaction chamber using heat recovery surfaces disposed on the surfaces of, or within the reaction chamber, and controlling the temperature of combustion so that the temperature in all parts of the reaction chamber is between about 750°

-950°

C.

15. A method of combusting fuel containing low melting point alkaline compositions, utilizing a circulating fluidized bed reactor having a reaction chamber, comprising the steps of:

(a) establishing a fluidized bed within the reaction chamber, including gas containing oxygen, fuel containing low melting point alkaline compositions, and solids, to combust the fuel and produce exhaust gases leaving the reaction chamber;

(b) separating solids in the off gases from the off gases, and recirculating them to the reaction chamber to form part of the fluidized bed;

(c) adding a reactant material to the reaction chamber which reacts with the low melting point alkaline compositions of the fuel to produce alkali metal compounds having a melting temperature of above about 950°

C.; and

(d) maintaining the combustion within the reaction chamber, including by withdrawing and recoverying heat directly therefrom, so that the maximum temperature in the reaction chamber is below about 950°

C. so that agglomeration of the bed material, sintering of the fuel, and enhanced formation of deposits on operable components of the fluidized bed reactor are avoided.

16. A method as recited in claim 15 comprising the further step of adding limestone to the reaction chamber at the same time as the reactant material, to adsorb sulphur, and wherein the fuel and reactant material are mixed together prior to adding them to the reaction chamber.

17. A method as recited in claim 15 wherein the reactant material is an oxide, or a hydroxide which is converted to an oxide during combustion, of the group consisting of aluminum, calcium, magnesium, silica, iron, titanium, and mixtures of two or more of aluminum, calcium, magnesium, silica, iron, and titanium;

and wherein step (c) is practiced by introducing the reactant material in solid particulate form into the reaction chamber.

18. A method as recited in claim 15 wherein the reactant material is kaolin which is added in solid particulate form, and wherein the alkali metal salts include sodium and potassium salts, and wherein step (c) is practiced so that the ratio of Al/(Na and K) is at least 1.0.

19. A method of burning a fuel selected from the group consisting of lignite and salty brown coal utilizing a fluidized bed reactor having a reaction chamber, comprising the steps of:

(a) establishing and maintaining a fluidized bed including fuel, oxygen containing gas, and solid bed particles, to effect combustion of the fuel and produce exhaust gases which exit the reaction chamber;

(b) maintaining the temperature substantially uniform throughout the reaction chamber, and in the range of about 750°

-950°

C.; and

(c) preventing agglomeration of the bed material, sintering of the fuel, and enhanced formation of deposits on operable components of the fluidized bed reactor, by adding to the reaction chamber sufficient solid particulate metal oxide, or hydroxide which is converted to oxide during combustion, selected from the group consisting of aluminum, calcium, magnesium, silica, iron, titanium, and mixtures of two or more of aluminum, calcium, magnesium, silica, iron, and titanium, so that the metal oxides react with constituents of the lignite or salty brown coal to prevent agglomeration, sintering, or enhanced formation of deposits on operable components of the reactor.

20. A method as recited in claim 19 wherein the metal oxide includes aluminum, and the fuel includes sodium and potassium salts, and wherein step (c) is practiced so that the molar ratio of Al/(Na and K) is at least about 1.0.

21. A method as recited in claim 19 comprising the further step of withdrawing and utilizing heat directly from the reaction chamber.

22. A method as recited in claim 21 wherein the metal oxide includes aluminum, and the fuel includes sodium and potassium salts, and wherein step (c) is practiced so that the molar ratio of Al/(Na and K) is at least about 1.0, and the fuel and metal oxide are mixed together prior to addition to the reaction chamber.