Pollution-free low temperature slurry combustion process utilizing the super-critical state

Claim 2

A continuous pressurized combustion process comprising the steps of: preparing an aqueous slurry of fuel particles containing alkali in an amount at least the chemical equivalent of the sulfur in the fuel as alkali sulfate; pressurizing the fuel slurry; preheating the fuel slurry; pressurizing an oxygen-containing gas; preheating the oxygen-containing gas; mixing the preheated fuel slurry and the preheated oxygen-containing gas at the entrance to an inlet zone of an elongated combustion reactor, forming a gaseous phase comprising the oxygen-containing gas and water vapor in which the fuel and alkali particles are entrained; providing a water vapor pressure of at least 3 atmospheres in the gaseous phase, as measured at the outlet of the reactor: permitting the fuel particles to burn at a temperature not exceeding 1600° F. as the gaseous phase flows from the inlet zone to the reactor outlet, forming gaseous and entrained solid combustion products; cooling the combustion products at essentially combustion pressure, by extracting useful heat therefrom, to a temperature below their dewpoint; and separating from uncondensed gaseous products an aqueous condensate containing suspended and dissolved solid products.

Claim 3

A process as in claim 1 and which also comprises the step of mixing steam with the preheated fuel slurry and the preheated oxygen-containing gas at the entrance to the inlet zone.

Claim 4

A process as in claim 1 and which also comprises the steps of: dividing the preheated fuel slurry into at least two portions; mixing one portion with the preheated oxygen-containing gas at the extrance to the inlet zone; and injecting remaining portions into the reactor downstream of the inlet zone at intervals such that combustion of previously injected fuel has increased the heat content of the gaseous phase at least sufficiently to vaporize the water in the portion.

Claim 5

A process as in claim 1 and which also comprises the step of recycling uncooled combustion products to the inlet zone in an amount sufficient to appreciably increase the temperature in the zone.

Claim 6

A process as in claim 1 and which also comprises the step of exposing the gaseous phase in which the burning fuel particles are entrained to heat transfer surface through which sufficient heat is extracted that the temperature in the reactor does not exceed a predetermined maximum.

Claim 7

A process as in claim 1 and which also comprises the step of injecting water into the reactor, downstream of the inlet zone, in an amount such that the temperature in the reactor does not exceed a predetermined maximum.

Claim 8

A process as in claim 6 and which also comprises the steps of: dividing the water injected into the reactor downstream of the inlet zone into at least two portions; and injecting the portions at intervals such that the reactor temperature prior to each injection does not exceed a predetermined maximum.

Claim 9

A process as in claim 6 in which the water injected downstream of the inlet zone is at least partially comprised of the aqueous condensate separated from the uncodensed gaseous products.

Claim 10

A process as in claim 1 and which also comprises the step of passing the gaseous and entrained solid combustion products through a gas-solids separating device, forming a dry solids product and cleaned combustion products carrying unseparated fine solid particles.

Claim 11

A process as in claim 9 and which also comprises the step of recycling uncooled cleaned combustion products to the inlet zone in an amount sufficient to appreciably increase the temperature in the zone.

Claim 12

A process as in claim 1 and which also comprises the step of further cooling the uncondensed gaseous products, by the extraction of useful heat therefrom, so as to condense a second aqueous condensate essentially free of solid particles.

Claim 13

A process as in claim 1 and which also comprises the step of cooling and washing the uncondensed gaseous products with a recirculating stream of water, which has been cooled by the extraction therefrom of useful heat, freeing them of traces of solid matter and reducing their water vapor content to less than 12 volume percent.

Claim 14

A process as in claim 12 and which also comprises the step of adding alkali to the recirculating stream of water.

Claim 15

A continuous pressurized combustion process for hydrophilic fuels characterized by a content of bound water, not separable by mechanical means, in excess of 35 weight precent comprising the steps of: preparing an aqueous slurry of hydrophilic fuel particles; pressurizing the fuel slurry; preheating the fuel slurry to a temperature at which the molecular structure of the fuel undergoes a spontaneous modification, freeing formerly bound water: separating freed water, forming a concentrated fuel slurry; pressurizing an oxygen-containing gas; mixing the concentrated fuel slurry and the oxygen-containing gas at the entrance to an inlet zone of an elongated combustion reactor; permitting the modified fuel particles to burn at a temperature not exceeding 1600° F. as the mixture flows from the inlet zone to the reactor outlet, under a water vapor pressure, measured at the outlet, of at least 3 atmospheres, forming gaseous and entrained solid combustion products; cooling the combustion products at essentially combustion pressure, by extracting useful heat therefrom, to a temperature below their dewpoint; and separating from uncondensed gaseous products an aqueous condensate containing suspended and dissolved solid products.

Claim 16

A continuous pressurized combustion process for hydrophilic fuels characterized by a content of bound water, not separable by mechanical means, in excess of 35 weight precent comprising the steps of: preparing an aqueous slurry of hydrophilic fuel particles; pressurizing the fuel slurry; preheating the fuel slurry to a temperature at which the molecular structure of the fuel undergoes a spontaneous modification, freeing formerly bound water: separating freed water, forming a concentrated fuel slurry; pressurizing an oxygen-containing gas; mixing the concentrated fuel slurry and the oxygen-containing gas at the entrance to an inlet zone of an elongated combustion reactor; permitting the modified fuel particles to burn at a temperature not exceeding 1600° F. as the mixture flows from the inlet zone to the reactor outlet, under a water vapor pressure, measured at the outlet, of at least 3 atmospheres, forming gaseous and entrained solid combustion products; cooling the combustion products at essentially combustion pressure, by extracting useful heat therefrom, to a temperature below their dewpoint; and separating from uncondensed gaseous products an aqueous condensate containing suspended and dissolved solid products.

Claim 17

A process as in claim 14 in which the step of preheating the fuel slurry is accomplished by direct contact with the uncondensed gaseous products, simultaneously cooling them and reducing their water vapor content to less than 14 volume percent.

Claim 18

A process as in claim 14 in which the freed water separated from the concentrated fuel slurry comprises a source of the water used to prepare the aqueous slurry of hydrophilic fuel.