IP Library Granted Patent US 8,701,412
Granted Patent B2
US 8,701,412 · App. 13/190,425 · Granted Apr 22, 2014

System for recovering heat from a biomass gasifier

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Quick Facts
Patent No.
US 8,701,412
App. No.
13/190,425
Granted
Apr 22, 2014
Kind
B2
Abstract

Systems for recovering heat from a biomass gasifier are provided. One gasification system includes a gasifier having an inlet section configured to receive a biomass feedstock and air, and a reactor section configured to gasify a mixture of the biomass feedstock and the air to generate a producer gas. The gasifier also has an outlet section configured to output the producer gas from the reactor section. The gasification system also includes a heat exchanger system coupled to the gasifier. The heat exchanger system is configured to recover heat from the gasifier by transferring heat to a fluid to create a heated fluid.

Claims (21)

1. A gasification system, comprising:

a gasifier having an inlet section configured to receive a biomass feedstock and air, a reactor section configured to gasify a mixture of the biomass feedstock and the air to generate a producer gas, and an outlet section configured to output the producer gas from the reactor section;

a heat exchanger system coupled to the outlet section of the gasifier, wherein the heat exchanger system is configured to recover heat from the gasifier by transferring heat to a fluid to create a heated fluid;

a dryer configured to dry the biomass feedstock prior to delivery into the gasifier, wherein the fluid comprises a dryer exhaust from the dryer, and the heat exchanger system is configured to heat the dryer exhaust to create a heated dryer exhaust; and

a gas engine configured to combust the producer gas from the gasifier to produce energy, wherein the gasification system is configured to mix the heated dryer exhaust with an engine exhaust from the gas engine to create an exhaust mixture of the heated dryer exhaust and the engine exhaust, and to reduce a temperature of the engine exhaust.

2. The gasification system of claim 1 , wherein the heat exchanger system comprises a first heat exchanger coupled to an upstream section of the outlet section, and a second heat exchanger coupled to a downstream section of the outlet section, wherein the gasification system is configured to flow the fluid through both the first and second heat exchangers.

3. The gasification system of claim 1 , wherein the heat exchanger system is configured to transfer heat to the fluid to generate steam directed to an ammonia removal unit.

4. The gasification system of claim 1 , wherein the gasification system is configured to deliver the exhaust mixture to the dryer for use in drying the biomass feedstock.

5. The gasification system of claim 1 , wherein the heat exchanger system comprises a limpet coil.

6. A gasification system, comprising:

a gasifier having an inlet section configured to receive a biomass feedstock and air, a reactor section configured to gasify a mixture of the biomass feedstock and the air to generate a producer gas, and an outlet section configured to output the producer gas from the reactor section;

a heat exchanger system coupled to the gasifier, wherein the heat exchanger system is configured to recover heat from the gasifier by transferring heat to a fluid to create a heated fluid, and wherein the heat exchanger system is coupled to the outlet section of the gasifier;

a vapor absorption machine coupled to the heat exchanger system, wherein the vapor absorption machine is configured to use the heated fluid to refrigerate a medium;

a dryer configured to dry the biomass feedstock prior to delivery into the gasifier, wherein the fluid comprises a dryer exhaust from the dryer, and the heat exchanger system is configured to heat the dryer exhaust to create a heated dryer exhaust; and

a gas engine configured to combust the producer gas from the gasifier to produce energy, wherein the gasification system is configured to mix the heated dryer exhaust with an engine exhaust from the gas engine to create an exhaust mixture of the heated dryer exhaust and the engine exhaust, and to reduce a temperature of the engine exhaust.

7. The gasification system of claim 6 , wherein the heat exchanger system comprises a first heat exchanger coupled to an upstream section of the outlet section, and a second heat exchanger coupled to a downstream section of the outlet section, wherein the gasification system is configured to flow the fluid through both the first and second heat exchangers.

8. The gasification system of claim 6 , wherein the heat exchanger system is configured to transfer heat to the fluid to generate steam directed to an ammonia removal unit.

9. The gasification system of claim 6 , wherein the heated fluid from the heat exchanger system is used by a steam turbine to generate power.

10. The gasification system of claim 6 , wherein the gasification system is configured to deliver the exhaust mixture to the dryer for use in drying the biomass feedstock.

11. The gasification system of claim 6 , wherein the heat exchanger system comprises a limpet coil.

12. The gasification system of claim 6 , wherein the heat exchanger system is coupled to an ash extraction system of the gasifier, the ash extraction system is configured to receive hot ash from the reactor section, and the heat exchanger system is configured to transfer heat from the hot ash in the ash extraction system to the fluid.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 22, 2019
From: GENERAL ELECTRIC COMPANY
To: AIR PRODUCTS AND CHEMICALS, INC.
Reel/Frame 050787/0642 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 26, 2011
From: MAJMUDAR, JINMESH PRANAV; MALL, OMPRAKASH; SUBRAMANIAN, LAKSHMANAN; DSOUZA, AVISH IVAN
To: GENERAL ELECTRIC COMPANY
Reel/Frame 026648/0704 →