Combustion system incorporating temperature swing adsorptive gas separation
A combustion system and process of operating the combustion system incorporating an electrostatic precipitator, an optional flue gas desulfurizer, and a temperature swing adsorptive gas separator, for post-combustion emission abatement is provided. A very low pressure steam stream may be employed as a first regeneration stream for the temperature swing adsorptive gas separator where the very low pressure steam stream may optionally be recovered from, a very low pressure steam turbine or an auxiliary boiler. A fluid stream at a suitable temperature for regeneration of at least one adsorbent material in the temperature swing adsorptive gas separator may be employed as a second regeneration stream where the fluid stream may optionally be recovered from an electrostatic precipitator, an oxidant preheater, or an auxiliary heater.
1. A combustion system comprising:
an oxidant preheater fluidly connected to a primary oxidant source and to a secondary oxidant source and operable to provide a preheated primary oxidant stream and a preheated secondary oxidant stream;
a fuel source;
a combustor, fluidly connected to recover at least one of said preheated primary oxidant stream and said preheated secondary oxidant stream from said oxidant preheater, and a fuel stream from said fuel source for combustion, to produce a combustion gas stream, and fluidly connected to admit said combustion gas stream into said oxidant preheater;
a feedwater source;
an integrated heat exchanger having a hot side fluidly connected to said combustor and a cold side fluidly connected to recover at least one of a water and/or a condensate stream from said feedwater source, to produce a high pressure steam stream from said cold side;
a particulate collector fluidly connected to recover said combustion gas stream from said oxidant preheater, for forming a first treated combustion gas stream;
a direct contact cooler fluidly connected to recover a first portion of said first treated combustion gas stream from said particulate collector;
a temperature swing adsorptive gas separator fluidly connected to recover said first portion of said treated combustion gas stream from said direct contact cooler as a feed stream comprising at least a first component, fluidly connected to recover a steam stream from at least one of a turbine or a boiler as a first regeneration stream, fluidly connected to recover a second portion of said first treated combustion gas stream from said particulate collector as a second regeneration stream, and fluidly connected to release a first product stream into an ambient environment, wherein said temperature swing adsorptive gas separator is operable to separate at least a portion of said first component from said feed stream to produce a second product stream;
a condenser fluidly connected to recover said second product stream from said temperature swing adsorptive gas separator to form said condensate stream and a purified second product stream;
an ejector having a low pressure port and a high pressure port, said low pressure port fluidly connected to admit said purified second product stream recovered from said condenser; and
a compressor for producing a compressed second product stream, fluidly connected to receive said purified second product stream from said ejector and fluidly connected to admit said compressed second product stream into said high pressure port of said ejector.
2. The combustion system of claim 1 , further comprising a first steam turbine fluidly connected to recover said high pressure steam stream from said integrated heat exchanger, and a second steam turbine fluidly connected to recover a low pressure steam stream from said first steam turbine and to produce a very low pressure steam stream, where said second steam turbine is fluidly connected to admit said very low pressure steam stream into said temperature swing adsorptive gas separator.
3. The combustion system of claim 1 , further comprising said condenser fluidly connected to recover said second product stream from said temperature swing adsorptive gas separator to form said condensate stream, and an auxiliary boiler fluidly connected to recover at least a portion of said condensate stream from said condenser to produce a low pressure steam stream where said auxiliary boiler is fluidly connected to admit said low pressure steam stream into said temperature swing adsorptive gas separator.
4. The combustion system of claim 1 , wherein said temperature swing adsorptive gas separator is operable to produce a third product stream and is fluidly connected to recover said third product stream from said temperature swing adsorptive gas separator and admit said third product stream as a portion of said feed stream admitted into said temperature swing adsorptive gas separator.
5. The combustion system of claim 1 , further comprising a conditioning source fluidly connected to admit a conditioning stream into said temperature swing adsorptive gas separator for producing a fourth product stream, wherein said temperature swing adsorptive gas separator is fluidly connected to admit said fourth product stream into said oxidant preheater.
6. The combustion system of claim 1 , further comprising a flue gas desulfurizer for reducing a level of sulfur oxides in said first treated combustion gas stream, fluidly connected to recover said first portion of said first treated combustion gas stream from said particulate collector and fluidly connected to admit said first portion of said first treated combustion gas stream into said direct contact cooler.
7. The combustion system of claim 1 , further comprising a diverter valve fluidly connected to said particulate collector, for directing said first treated combustion gas stream into said first portion of said first treated combustion gas stream and said second portion of said first treated combustion gas stream.