Black liquor gasifier
AssigneeThe Babcock & Wilcox Company
InventorsJohn E. Monacelli, Dennis W. Johnson
Life of this patent
Estimating the term…
Abstract
A system and method for producing product gas using residual waste liquor is described with a gasifier reactor having a fluidized bed located therein. The gasifier reactor is heated to a predetermined temperature range with either an external heater or a second fluidized bed located at a position below the first fluidized bed. A heat exchanger may be positioned in the first fluidized bed and/or the second fluidized bed for indirectly heating the respective fluidized beds. Condensing heat exchanger means recovers heat from the product gas and condenses an acid gas therefrom for recycling the chemicals. A reagent is sprayed in the condensing heat exchanger means to clean the product gas. Pressurization allows the cleaned product gas to be directly fired in a turbine.
Claims4
An apparatus for recovering heat from a product gas and removing an acid gas therefrom, comprising:
- an inlet for receiving a product gas stream;
- first tubular heat exchanger means positioned downstream from said inlet, said first tubular heat exchanger means having tubes situated therein with an inert covering on each tube, the tubes being constructed to be cooled with a cooling fluid and exposed to the product gas stream, said first tubular heat exchanger means cooling the product gas to a temperature of about 200.degree. F.-300.degree. F.;
- second tubular heat exchanger means operating in a condensing mode and being connected in series to the first tubular heat exchanger means, said second tubular heat exchanger means having tubes situated therein with an inert covering, the tubes being constructed to be cooled with a cooling fluid and exposed to the product gas stream, said second tubular heat exchanger means being connected to said first tubular heat exchanger means by a duct, said second tubular heat exchanger means cooling the product gas to a temperature below its adiabatic saturation temperature;
- means for spraying reagent into the product gas stream into an inlet and an exit of said second tubular heat exchanger means for scrubbing an acid gas therefrom, said spraying means causing droplets to form around product gas particulate which condense on tubes and are removed in said second tubular heat exchanger means, the duct connecting the first and second tubular heat exchanger means having a sump for receiving condensed liquid and liquid separated from the product gas stream, the sump supplying the condensed liquid and liquid separated from the product gas stream to means for recycling the liquid separated from the product gas stream for use in a pulping process;
- third tubular heat exchanger means positioned adjacent to said second tubular heat exchanger means and constructed to receive the product gas therefrom, said third tubular heat exchanger means providing further scrubbing with said spraying means by spraying reagent in an exit of said third tubular heat exchanger means and further providing counter current gas liquid contact;
- and
- means for separating liquid from the gas stream positioned downstream from said third tubular heat exchanger means.
Dependencies are inferred from the claim text.