Combustion process for fuel containing vanadium compounds
Oxycombustion process for producing energy wherein low ranking gaseous, liquid, solid, optionally solid melting hydrocarbon fractions are used as fuels, having a vanadium content in amounts by weight from 50 to 5,000 ppm or higher, and alkaline metals Ma in amounts from 20 to 10,000 ppm, wherein magnesium is added as oxide, or as a magnesium compound forming MgO in the combustion process, or mixtures thereof and a silico-aluminate wherein the molar ratio SiO 2 :Al 2 O 3 ranges from 2:1 to 6:1; the combustor being refractored, isotherm or quasi-isotherm, flameless, working at temperatures in the range 1,250°-1,450° C. and under pressurized conditions, wherein the oxidant being used in admixture with water or steam, the ratio by moles oxidant:(water/steam) being comprised between about 1:0.4 and about 1:3, or the oxidant is used in admixture with flue gases recycled from the flue gases outletting the energy recovery equipments, wherein the water/steam amount is higher than 30% by volume, optionally by adding water to the recycled flue gases, the molar ratio oxidant:(water/steam) in flue gases being comprised from about 1:0.4 to about 1:3; the hydrocarbon fraction being fed in admixture with water or steam, the amount of water/steam being at least 30% by weight with respect to the hydrocarbon fraction.
1. Oxycombustion process comprising feeding to a combustor:
a fuel selected from low ranking gaseous, liquid, solid, also solid melting hydrocarbon fractions, having a vanadium content in amounts by weight from 50 to 5,000 ppm or higher, and alkaline metals Ma in amounts from 20 to 10,000 ppm, the hydrocarbon fractions being fed in admixture with water or steam, the amount of water/steam being at least 30% by weight with respect to the hydrocarbon fractions;
magnesium as oxide, or as a magnesium compound forming MgO in the combustion process, or mixtures thereof;
a silico aluminate wherein the molar ratio SiO 2 :Al 2 O 3 ranges from 2:1 to 6:1;
oxygen as oxidant, having a titre higher than 80% by volume, the complement to 100% being formed of inert gases and/or nitrogen, being in admixture with:
water or steam, the ratio by moles oxidant:(water or stream) being between 1:0.4 and 1:3,
or
recycled flue gases having a water or stream amount higher than 30% by volume, the molar ratio oxidant:(water or stream) in flue gases being comprised between 1:0.4 and 1:3, the recycled flue gases coming from the energy recovery equipments;
the combustor being refractored, isotherm or quasi-isotherm, flameless, operating at temperatures in the range 1,250°-1,450° C. and under pressurized conditions.
2. A process according to claim 1 wherein a pressure in the combustor is comprised from higher than or equal to 102 kPa to 5,000 kPa.
3. A process according to claim 1 wherein a pressure in the combustor is comprised from higher than or equal to 200 kPa to 3,500 kPa.
4. A process according to claim 1 wherein the oxidant is pure oxygen.
5. A process according to claim 1 wherein the Mg:V molar ratio is in the range 1:1-2:1.
6. A process according to claim 5 wherein the Mg:V molar ratio ranges from 1.25:1 to 1.75:1.
7. A process according to claim 1 wherein the molar ratio of Mg:Al is comprised between 0.5:1 and 1:1.
8. A process according to claim 7 , wherein the molar ratio of Mg:Al is comprised between 0.6:1 and 0.8:1.
9. A process according to claim 1 wherein the added amount of silico aluminate, on a molar basis, with respect to the alkaline metals Ma contained in the fuel is in the molar ratio Al/Ma>1.
10. A process according to claim 9 , wherein the molar ratio Al/Ma is between 1 and 1.5.
11. A process according to claim 1 wherein the temperature in the combustor ranges from 1300° to 1400° C.
12. A process according to claim 1 wherein the hydrocarbon fractions are selected from asphaltene, petrolene, carbonaceous substances, Petcoke, carbonaceous residues of petrochemical processes, and heavy refinery bottoms.
13. A process according to claim 1 wherein the addition of magnesium is carried out by feeding an aqueous solution of magnesium sulphate.
14. A process according to claim 1 wherein the silico aluminate is a magnesium silico aluminate, optionally added of SiO 2 in order to have a SiO 2 :Al 2 O 3 ratio ranging from 2:1 to 6:1.
15. A process according to claim 1 , wherein the residence time of the fuel in the combustor ranges from 0.5 seconds up to 30 minutes.
16. Flue gases obtainable with the process according to claim 1 , wherein (data on a flue gas dry basis):
absent soot and IPA <10 −4 mg/Nm 3 ,
TOC<1 ppm,
fly ash <100 mg/Nm 3 ,
magnesium <1 mg/Nm 3 ,
vanadium and its compounds orthovanadate and pyrovanadate≦1 mg/Nm 3 expressed as vanadium, and V 2 O 5 <0.01 mg/Nm 3 ,
SO 3 ≦2 mg/Nm 3 ,
NiO≦1 mg/Nm 3 ,
NaVO 3 not detectable by XRD, and SEM analysis of the microaggregates.
17. The process according to claim 1 wherein the water is added to the recycled flue gases.