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 fluidizing dense bed.
1. A process, comprising:
i) introducing char and heat transfer particles to a fluidized dense phase of a reheater;
ii) passing air upwardly through the fluidized dense phase;
iii) combusting a portion of the char to form upwardly flowing flue gas;
iv) carrying a further portion of the char in the upwardly flowing flue gas to form entrained char; followed by
v) recovering at least some of the entrained char, comprising:
a) a first gas-solid separation in a dilute phase of the reheater, whereby a first portion of the entrained char is returned to the dense phase through a dipleg, the dipleg immersed below a top surface of the fluidized dense bed; and
b) a second gas-solid separation, whereby a second portion of the entrained char is returned to the dense phase.
2. The process of claim 1 , wherein the recovering is effective to reduce afterburn in the reheater and/or downstream lines of a rapid thermal processing system.
3. The process of claim 2 , wherein the recovering is effective to reduce carbon monoxide afterburn in the reheater and/or downstream lines of a rapid thermal processing system.
4. The process of claim 1 , wherein the recovering further comprises: reducing loss of heat transfer particles from the reheater.
5. The process of claim 1 , wherein the velocity of the upwardly-passed air is optimized exclusive of any limitations imposed by an entrainment rate of char and/or heat transfer particles in the upwardly flowing flue gas.
6. The process of claim 1 , wherein the velocity of the upwardly-passed air is optimized exclusive of any limitations imposed by a particle size of the heat transfer particles.
7. The process of claim 1 , wherein the velocity of the upwardly-passed air is optimized exclusive of any limitations imposed by a heat transfer surface area of the heat transfer particles.
8. The process of claim 1 , wherein the velocity of the upwardly-passed air is 2.5-3 feet per second.
9. The process of claim 1 , wherein the upwardly-passed air initially contains in excess of the theoretical stoichiometric amount of oxygen for complete combustion of the char.
10. The process of claim 1 , further comprising: combusting, in the fluidized dense phase, at least a portion of the recovered entrained char.
11. The process of claim 1 , wherein the first gas-solid separation comprises vortex separation.
12. The process of claim 1 , wherein the first gas-solid separation comprises cyclone separation.
13. The process of claim 1 , wherein the second gas-solid separation is in the dilute phase of the reheater.
14. The process of claim 1 , wherein the second gas-solid separation is exterior to the reheater.
15. The process of claim 1 , wherein the first gas-solid separation and the second gas-solid separation occur in parallel.
16. The process of claim 1 , wherein at least a portion of the heat transfer particles are combined with biomass in a rapid thermal processing reactor.
17. The process of claim 1 , wherein the char and heat transfer particles are a product of rapid thermal processing of biomass.
18. The process of claim 1 , wherein the heat transfer particles are not combustible.
19. The process of claim 1 , wherein the heat transfer particles are inert solid particles.
20. The process of claim 1 , wherein the heat transfer particles are catalyst particles.