Optimised method and device loop combustion on liquid hydrocarbon feedstock

Patent metadata

Field	Value
Publication number	US-9638412-B2
Application number	US-200913120185-A
Country	US
Kind code	B2
Filing date	Sep 21, 2009
Priority date	Sep 23, 2008
Publication date	May 2, 2017
Grant date	May 2, 2017

Abstract

The invention relates to a device and to an improved method for chemical looping combustion of at least one liquid hydrocarbon feed, comprising: mixing the liquid feed with an atomization gas so as to feed it into a metal oxide particle transport zone ( 2 ), upstream from combustion zone ( 3 ), through atomization means ( 6 ) allowing to form finely dispersed liquid droplets in the atomization gas; vaporization of the liquid feed in form of droplets into contact with at least part of metal oxide particles in transport zone ( 2 ), the operating conditions in transport zone ( 2 ) being so selected that the superficial gas velocity after vaporization of the liquid feed is higher than the transport velocity of the metal oxide particles; sending all of the effluents from transport zone ( 2 ) to a combustion zone ( 3 ) allowing reduction of the metal oxide particles, said combustion zone ( 3 ) comprising at least one dense-phase fluidized bed. The invention can be advantageously applied to CO 2 capture and energy production.

First claim

The invention claimed is:

1. An improved method for chemical looping combustion of at least one liquid hydrocarbon feed, comprising:
atomizing the at least one liquid hydrocarbon feed with an atomization gas so as to form an atomized liquid hydrocarbon feed comprising finely dispersed liquid droplets in the atomization gas and to feed it into a substantially elongated and substantially vertical metal oxide particle transport zone, the metal oxide particle transport zone being provided upstream from a combustion zone comprising at least one dense-phase fluidized bed, the metal oxide particle transport zone opening into the at least one dense-phase fluidized bed of the combustion zone;
feeding metal oxide particles to the metal oxide particle transport zone;
vaporizing the atomized liquid hydrocarbon feed when in contact with the metal oxide particles in the transport zone to provide a vaporized hydrocarbon feed, the operating conditions in the transport zone being so selected that the superficial gas velocity in the transport zone after vaporization of the atomized liquid hydrocarbon feed is higher than the transport velocity of the metal oxide particles allowing the metal oxide particles to be transported while minimizing the energy dissipation in form of pressure drop;
sending all of the effluents from the transport zone to the at least one dense-phase fluidized bed of the combustion zone, the vaporized hydrocarbon feed and metal oxide particles flowing together in the same direction into a first portion of the at least one dense-phase fluidized bed of the combustion zone, the combustion zone allowing reduction of the metal oxide particles.

2. An improved chemical looping combustion method as claimed in claim 1 , wherein the dense-phase fluidized bed in the combustion zone is so dimensioned that the hydrodynamics of the particles in the dense-phase fluidized bed(s) correspond to at least two perfectly stirred reactors in series or to at least two fluidized bed stages in series.

3. An improved chemical looping combustion method as claimed in claim 1 , wherein the atomization means are arranged on a wall of a reactor of the transport zone and so selected as to form a jet oriented towards the centre of the transport zone.

4. An improved chemical looping combustion method as claimed in claim 1 , wherein the liquid feed droplets injected have a Sauter mean diameter ranging between 0.5 and 2 times the mean diameter of the particles.

5. An improved chemical looping combustion method as claimed in claim 1 , further comprising transporting the metal oxide particles reduced in the combustion zone to an oxidation zone and oxidizing the metal oxide particles in the oxidation zone, wherein the metal oxide particles reach the transport zone from the oxidation zone through a line, or through recycle of the particles coming from the combustion zone, or in form of a mixture of re-oxidized metal oxides from the oxidation zone and of metal oxides from the combustion zone, and
wherein the main part of the combustion of coke deposited on the metal oxide particles is achieved in the combustion zone such that gaseous effluents of the oxidation zone comprise less than 10% of the CO 2 resulting from the combustion of the liquid feed fed into the transport zone.

6. An improved chemical looping combustion method as claimed in claim 1 , further comprising transporting the metal oxide particles reduced in the combustion zone to an oxidation zone and oxidizing the metal oxide particles in the oxidation zone, wherein metal oxide particles coming directly from the oxidation zone are fed into the dense-phase fluidized bed(s) of the combustion zone, so that a fraction less than or equal to 50% of the total amount of metal oxide particles circulating between the oxidation zone and the combustion zone takes part in the vaporization of the liquid feed in the transport zone.

7. An improved chemical looping combustion method as claimed in claim 1 , wherein the gas and the particles from the transport zone are fed together to the base of at least one fluidized bed of the combustion zone, the upper part of the transport zone being equipped with dispersion means in said fluidized bed.

8. An improved chemical looping combustion method as claimed in claim 1 , wherein the gas and the particles are separated at an outlet of the transport zone:
either to feed separately into the combustion zone the gas freed of the major part of the metal oxide particles and the metal oxide particles freed of the major part of the gas,
or to feed into the combustion zone the metal oxide particles freed of the major part of the gas, and to discharge the gas phase out of the combustion zone.

9. An improved chemical looping combustion method as claimed in claim 1 , wherein the liquid feed is made up of hydrocarbon fractions, alone or in admixture, less than 10% thereof having a boiling point temperature below 340° C.

10. An improved chemical looping combustion method as claimed in claim 1 , wherein at least one dense-phase fluidized bed of the combustion zone is equipped with means allowing the flow of the metal oxide particles to be staged.

11. An improved chemical looping combustion method as claimed in claim 1 , wherein the combustion zone comprises at least two dense-phase fluidized bed reactors arranged in series.

12. A device for chemical looping combustion of at least one liquid hydrocarbon feed, comprising:
a substantially elongate and substantially vertical metal oxide particle transport zone comprising:
liquid feed injection means comprising means for mixing the at least one liquid hydrocarbon feed with an atomization gas arranged on the periphery of said transport zone upstream of an outlet of the transport zone to form an atomized liquid hydrocarbon feed,
feed means for feeding metal oxide particles to the transport zone upstream of the outlet of the transport zone for vaporization of the atomized liquid hydrocarbon feed when in contact with at least part of the metal oxide particles in the transport zone to provide a vaporized hydrocarbon feed,
a combustion zone for the vaporized hydrocarbon feed through metal oxide particle reduction, comprising at least one dense-phase fluidized bed, the transport zone being arranged upstream from said combustion zone and opening into the at least one dense-phase fluidized bed of the combustion zone such that the vaporized hydrocarbon feed and metal oxide particles flow together in the same direction into a first portion of the at least one dense-phase fluidized bed of the combustion zone, wherein at least a part of the metal oxide particles comprise coke deposited during at least the vaporization of the at least one liquid hydrocarbon feed and wherein the main part of the combustion of coke is achieved in the combustion zone such that gaseous effluents of an oxidation zone for the metal oxide particles comprise less than 10% of the CO 2 resulting from the liquid feed fed into the transport zone.

13. A device as claimed in claim 11 , wherein the combustion zone comprises a number of dense-phase fluidized beds, in one or more combustion reactors, greater than two.

14. A device as claimed in claim 11 , wherein the metal oxide particle feed means comprise a transport line from the oxidation zone, and/or a recycle line for the particles coming from the combustion zone.

15. A device as claimed in claim 11 , wherein the transport zone comprises, at the outlet thereof, dispersion means for gas and solid particles dispersion in the combustion zone.

16. A device as claimed in claim 11 , wherein the transport zone comprises,

Assignees

• Gauthier Thierry
• Hoteit Ali
• Forret Ann
• Ifp Energies Now
• Total Sa

Inventors

• Gauthier Thierry
• Hoteit Ali
• Forret Ann

Classifications

• F23C2900/99008

  Unmixed combustion, i.e. without direct mixing of oxygen gas and fuel, but using the oxygen from a metal oxide, e.g. FeO · CPC title

• F23C10/01

  in a fluidised bed of catalytic particles · CPC title

• B01J2208/00902

  Nozzle-type feeding elements · CPC title

• B01J8/26

  with two or more fluidised beds, e.g. reactor and regeneration installations · CPC title

• B01J8/388

  externally, i.e. the particles leaving the vessel and subsequently re-entering it · CPC title