Processes for controlling afterburn in a reheater and for controlling loss of entrained solid particles in combustion product flue gas
View Patent ↗Processes for controlling afterburn in a reheater and loss of entrained solid particles in reheater flue gas are provided. Carbonaceous biomass feedstock is pyrolyzed using a heat transfer medium forming pyrolysis products and a spent heat transfer medium comprising combustible solid particles. The spent heat transfer medium is introduced into a fluidizing dense bed. The combustible solid particles of the spent heat transfer medium are combusted forming combustion product flue gas in a dilute phase above the fluidizing dense bed. The combustion product flue gas comprises flue gas and solid particles entrained therein. The solid particles are separated from the combustion product flue gas to form separated solid particles. At least a portion of the separated solid particles are returned to the fludizing dense bed.
1. A pyrolysis system, comprising:
i) a pyrolysis reactor configured to pyrolyze solid biomass in the presence of heat transfer particles to produce pyrolysis vapors, char, and cooled heat transfer particles;
ii) a reheater in communication with the pyrolysis reactor, the reheater configured to contain—
a) a fluidized dense phase, wherein the reheater is operated to combust at least a portion of the char with an upwardly flowing air stream to form reheated cooled heat transfer particles and upwardly flowing flue gas, the upwardly flowing flue gas containing a further portion of the char; and
b) a dilute phase above the fluidized dense phase;
iii) a gas-solid separator positioned in the dilute phase; and
iv) a dipleg configured to extend from a solids-outlet of the gas-solid separator to a position below a top surface of the fluidized dense phase.
2. The pyrolysis system of claim 1 , wherein the pyrolysis system is a rapid thermal processing system.
3. The pyrolysis system of claim 2 , further comprising a reheater outlet configured to communicate at least a portion of the reheated cooled heat transfer particles to the pyrolysis reactor.
4. The pyrolysis system of claim 1 , wherein a portion of the pyrolysis vapors are condensable to form a liquid pyrolysis oil.
5. The pyrolysis system of claim 1 , wherein the reheater is operated to optimize the velocity of the upwardly flowing air stream exclusively of any limitations imposed by an entrainment rate of char and/or heat transfer particles in the upwardly flowing flue gas.
6. The pyrolysis system of claim 1 , wherein the reheater is operated to optimize the velocity of the upwardly flowing air stream exclusively of any limitations imposed by a particle size of the heat transfer particles.
7. The pyrolysis system of claim 1 , wherein the reheater is operated to optimize the velocity of the upwardly flowing air stream exclusively of any limitations imposed by a heat transfer surface area of the heat transfer particles.
8. The pyrolysis system of claim 1 , wherein the reheater is operated whereby the velocity of the upwardly flowing air stream is 2.5-3 feet per second.
9. The pyrolysis system of claim 1 , wherein the reheater is operated wherein the upwardly flowing air stream initially contains in excess of the theoretical stoichiometric amount of oxygen for complete combustion of the char.
10. The pyrolysis system of claim 1 , wherein the reheater is operated to combust at least a portion of a char-containing stream received from the dipleg below the top surface of the fluidized dense phase.
11. The pyrolysis system of claim 1 , wherein the gas-solid separator comprises a vortex separator.
12. The pyrolysis system of claim 1 , wherein the gas-solid separator comprises a cyclone separator.
13. The pyrolysis system of claim 1 , wherein the pyrolysis system further comprises a further gas-solid separator in the dilute phase of the reheater.
14. The pyrolysis system of claim 1 , wherein the pyrolysis system further comprises a further gas-solid separator exterior to the reheater.
15. The pyrolysis system of claim 14 , wherein the gas-solid separator and the further gas-solid separator are configured to operate in parallel.
16. The pyrolysis system of claim 14 , wherein the gas-solid separator and the further gas-solid separator are configured to operate in series.
17. The pyrolysis system of claim 1 , wherein the reheater is a vertical substantially cylindrical vessel.
18. The pyrolysis system of claim 1 , wherein the heat transfer particles are not combustible.
19. The pyrolysis system of claim 1 , wherein the heat transfer particles are inert solid particles.
20. The pyrolysis system of claim 1 , wherein the heat transfer particles are catalyst particles.