Process for boiler flue gas cleaning by absorption, separation and liquefaction

Claim 1

A process for separating, removing sulfur dioxide and carbon dioxide from a fossil fueled boiler flue gas stream by condensing, absorption and liquefaction processes; the process which comprises: receiving a relatively hot flue gas at above 270° F. flowing from a fossil fueled boiler after removing most of flue gas particulate matter in an electrostatic dust collector; electronically treating the already cleaned flue gas in an electrostatic gas treater to neutralize ultra-fine particulate matter electrostatic charges to cause an agglomeration effect; cooling the electrostatically neutralized flue gas stream flowing from the electrostatic gas treater through a cooling section of a reverse flow heat exchanger to condense its acidic water vapor while preheating an ambient combustion air stream flowing to the fossil fueled boiler; removing the acidic water vapor condensate flowing from the condensing section of the reversing heat exchanger; absorbing the sulfur dioxide contained in the cooled flue gas stream flowing from the condensing section of the reversing heat exchanger by using a regenerative organic amine solvent-absorbent sprayed in a centrifugal gas separator-absorber to form a relatively rich SO 2 absorbent liquor in a relatively heavier fraction of the flue gas stream while releasing a cleaned relatively lighter fraction of the flue gas stream; separating the relatively rich SO 2 absorbent liquor from the relatively heavier gas stream flowing from a bottom outlet of the centrifugal gas separator-absorber; receiving, cleaning and purifying the relatively rich SO 2 absorbent liquor stream; pressurizing and heating the relatively rich SO 2 absorbent stream to a relatively higher pressure and higher temperature levels; spraying the pressurized and heated rich SO 2 absorbent liquor in a vacuum stripping column to co-strip sulfur dioxide with water vapor contained in the rich SO 2 absorbent liquor and to produce a lean SO 2 absorbent liquor; purifying, pressurizing, cooling and recycling the lean SO 2 absorbent liquor back to the centrifugal gas separator-absorber; cooling, condensing and removing most of the water vapor contained in the stripped mixture of sulfur dioxide and water vapor flowing from the vacuum stripping column; drying and liquefying the sulfur dioxide gas after condensing and removing most of the water vapor; liquefying the carbon dioxide gas contained in the relatively heavier gas stream flowing from the separator-absorber after removing the rich SO 2 liquor; continuously treating and recycling a slip stream of the lean SO 2 absorbent liquor; continuously adding a controlled flow of a fresh stream of said regenerative organic amine solvent-absorbent mixed with treated water to compensate for any losses, and to maintain a required composition of the SO 2 lean absorbent-liquor entering the centrifugal separator-absorber; continuously releasing the cleaned relatively lighter fraction of the flue gas flowing from the centrifugal separator step and the uncondensed flue gas streams flowing from the sulfur dioxide and carbon dioxide liquefaction steps into a recirculating cooling tower air release system for an embedded disbursing into the atmosphere.