Method in the operation of a firing plant, and a firing plant for performing the method
OwnerHenrik G. Olrikinventor
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OwnerHenrik G. Olrikinventor
Estimating the term…
In a method in the operation of a firing plant of the type comprising a combustion furnace and heat exchanger means to transfer thermal energy from the flue gas of the furnace to its combustion air, wherein a vaporizable liquid, such as water, is added to the combustion air of the furnace, the combustion air pressure is reduced in the portion of the heat exchanger means where the said liquid is caused to evaporate, the necessary evaporation heat being taken from the flue gas of the furnace before the flue gas is discharged to the atmosphere. A plant for performing the method is characterized by containing a pump (11) which has a relatively small inlet opening (10) so that the pump (11) creates a negative pressure in the portion (12) of the heat exchanger (9) where the liquid, fed by means of a nozzle (13), evaporates. This allows large amounts of water to evaporate, and flue gas, which flows through the heat exchanger portion (14), is cooled to a low temperature. The flue gas will then condense, and this procedure is accelerated by the constriction (at 16) of the flue (15) so that there is a positive pressure in the heat exchanger portion (14). According to the heat pump principle, the advantages are an unprecented low temperature level and humidity content of the discharged flue gas and a correspondingly high efficiency of the firing plant.
A method in the operation of a firing plant of the type comprising a combustion furnace and heat exchanger means which at least comprise a heat exchanger with a first portion through which the combustion air flows, and a second portion which is separated from the first portion and through which the flue gas flows for transfer of thermal energy from the flue gas of the furnace to the combustion air, wherein a vaporizable liquid is added to the combustion air, characterized by reducing the combustion air pressure in the first portion of the heat exchanger to sufficiently below atmospheric pressure so that the first portion of the heat exchanger serves as a low pressure evaporator for the said liquid.
Dependencies are inferred from the claim text.