High efficiency furnace

Claim 2

In a high efficiency furnace, multiple fluidized bed means for heat exchange between two gas streams comprising: flue gas duct means for conveyance of flue gas from a burner; a first quantity of solid particles capable of operation at flue gas temperatures of about 200° to about 1200° F. comprising a first fluidized bed within said flue gas duct means; distributor means for supporting said first fluidized bed and for admitting flue gas thereto and distributing flue gas throughout said first fluidized bed; air duct means exterior to said flue gas duct means for the portion of its length passing through said first fluidized bed for conveyance of an air stream to be heated for introduction to heat an enclosed volume; a second quantity of solid particles comprising a second fluidized bed within said air duct means; distributor means for supporting said second fluidized bed and for admitting air thereto and distributing the air to be heated throughout said second fluidized bed; thermal exchange means comprising at least one heat pipe in communication with said first and second fluidized beds transferring heat from said first to said second fluidized bed; each of said fluidized beds having a depth, when in fluidized state, of about 1/2 inch to about 4 inches.

Claim 3

The high efficiency furnace of claim 1 wherein each of said fluidized beds has a depth, when in the fluidized state, of about 1 to about 4 inches.

Claim 4

The high efficiency furnace of claim 1 wherein said solid particles have mean particle diameters of about 0.06 to about 0.60 millimeters.

Claim 5

The high efficiency furnace of claim 3 wherein said solid particles have mean particle diameters of about 0.20 to about 0.60 millimeters.

Claim 6

The high efficiency furnace of claim 1 wherein said solid particles are selected from the group consisting of silica and alumina.

Claim 7

The high efficiency furnace of claim 1 wherein said thermal exchange means comprises a heat pipe having one end in thermal communication with said first fluidized bed and the opposite end in thermal communication with said second fluidized bed.

Claim 8

The high efficiency furnace of claim 6 wherein said heat pipe has extended surfaces extending into each of said fluidized beds.

Claim 9

The high efficiency furnace of claim 1 wherein said thermal exchange means comprises a thin thermal conductive wall between and in thermal conductive relation with said first and second fluidized beds.

Claim 10

The high efficiency furnace of claim 8 wherein said thin thermal conductive wall has extended surfaces extending into each of said fluidized beds.

Claim 11

A high efficiency furnace for heating an enclosed space comprising: a combustion chamber; a burner within said combustion chamber; flue gas duct means having a first and second open end in communication at said first open end with said combustion chamber and at said second end with the ambient atmosphere; a first blower means for movement of flue gas through said flue gas duct from said first to said second open end; a first quantity of solid particles capable of operation at flue gas temperatures of about 200° to about 1200° F. comprising a first fluidized bed within said flue gas duct means; distributor means for supporting said first fluidized bed and for admitting flue gas thereto and distributing flue gas throughout said first fluidized bed; air duct means exterior to said flue gas duct means for the portion of its length passing through said first fluidized bed and having a first and second open end in communication at said first open end with the space to be heated and/or ambient air and at said second open end with the space to be heated; a second blower means for movement of said air stream through said air duct means from said first to said second open end; a second quantity of solid particles comprising a second fluidized bed within said air duct means; distributor means for supporting said second fluidized bed and for admitting air thereto and distributing the air to be heated throughout said second fluidized bed; thermal exchange means comprising at least one heat pipe in communication with said first and second fluidized beds transferring heat from said first to said second fluidized bed; each of said fluidized beds having a depth, when in fluidized state, of about 1/2 inch to about 4 inches.

Claim 12

A high efficiency furnace for heating an enclosed space comprising: a combustion chamber; a burner within said combustion chamber; flue gas duct means having a first and second open end in communication at said first open end with said combustion chamber and at said second end with the ambient atmosphere; a first blower means for movement of flue gas through said flue gas duct from said first to said second open end; a first quantity of solid particles capable of operation at flue gas temperatures of about 200° to about 1200° F. comprising a first fluidized bed within said flue gas duct means; distributor means for supporting said first fluidized bed and for admitting flue gas thereto and distributing flue gas throughout said first fluidized bed; air duct means exterior to said flue gas duct means for the portion of its length passing through said first fluidized bed and having a first and second open end in communication at said first open end with the space to be heated and/or ambient air and at said second open end with the space to be heated; a second blower means for movement of said air stream through said air duct means from said first to said second open end; a second quantity of solid particles comprising a second fluidized bed within said air duct means; distributor means for supporting said second fluidized bed and for admitting air thereto and distributing the air to be heated throughout said second fluidized bed; thermal exchange means comprising at least one heat pipe in communication with said first and second fluidized beds transferring heat from said first to said second fluidized bed; each of said fluidized beds having a depth, when in fluidized state, of about 1/2 inch to about 4 inches.

Claim 13

The high efficiency furnace of claim 10 wherein each of said fluidized beds has a depth, when in the fluidized state, of about 1 to about 4 inches.

Claim 14

The high efficiency furnace of claim 10 wherein said solid particles have mean particle diameters of about 0.06 to about 0.60 millimeters.

Claim 15

The high efficiency furnace of claim 10 wherein said solid particles have mean particle diameters of about 0.20 to about 0.60 millimeters.

Claim 16

The high efficiency furnace of claim 10 wherein said solid particles are selected from the group consisting of silica and alumina.

Claim 17

The high efficiency furnace of claim 10 wherein said thermal exchange means comprises a heat pipe having one end in thermal communication with said first fluidized bed and the opposite end in thermal communication with said second fluidized bed.

Claim 18

The high efficiency furnace of claim 15 wherein said heat pipe has extended surfaces extending into each of said fluidized beds.

Claim 19

The high efficiency furnace of claim 10 wherein said thermal exchange means comprises a thin thermal conductive wall between and in thermal conductive relation with said first and second fluidized beds.

Claim 20

The high efficiency furnace of claim 17 wherein said thin thermal conductive wall has extended surfaces extending into each of said fluidized beds.

Claim 21

The high efficiency furnace of claim 10 having two to four sets of said fluidized beds in series in each of said flue gas duct means and air duct means.

Claim 22

The high efficiency furnace of claim 19 wherein said series of fluidized beds in said flue gas duct means is in thermal exchange communication with said series of fluidized beds in said air duct means in countercurrent flow relation to the flow of flue gas and air within said duct means.

Claim 23

The high efficiency furnace of claim 20 additionally having an air bypass duct means in communication with said air duct means first and second open end whereby a portion of the air for heating said enclosed space bypasses said fluidized beds within said air duct means.

Claim 24

The high efficiency furnace of claim 20 wherein said burner is a power burner.

Claim 25

The high efficiency furnace of claim 10 having two or more stages of heat exchange in series with respect to said flue gas duct means and in parallel with respect to said air duct means comprising: a first heat exchange means toward said first open end of said flue gas duct means; a second heat exchange means toward said second open end of said flue gas duct means comprising said first and second fluidized beds; said air duct means toward said first open end being divided providing first portion air duct passage in said first heat exchange means and second portion air duct passage in said second heat exchange means, said first and second portion air duct passages rejoining said air duct means prior to said air duct means second open end.

Claim 26

The high efficiency furnace of claim 23 wherein said first heat exchange means is a convective heat exchange means.

Claim 27

The high efficiency furnace of claim 23 wherein said first heat exchange means comprises: a third quantity of solid particles capable of operation at flue gas temperatures of about 200° to about 1200° F. comprising a third fluidized bed within said flue gas duct means; distributor means for supporting said third fluidized bed and for admitting flue gas thereto and distributing flue gas throughout said third fluidized bed; air duct means exterior to said flue gas duct means for the portion of its length passing through said third fluidized bed and having a first and second open end in communication at said first open end with the space to be heated and/or ambient air and at said second open end with the space to be heated; a fourth quantity of solid particles comprising a fourth fluidized bed within said air duct means; distributor means for supporting said fourth fluidized bed and for admitting air thereto and distributing the air to be heated throughout said fourth fluidized bed; thermal exchange means in communication with said third and fourth fluidized bed transferring heat from said third to said fourth fluidized bed; and each of said fluidized beds having a depth, when in fluidized state, of about 1/2 inch to about 4 inches.

Claim 28

The high efficiency furnace of claim 23 wherein said solid particles have mean particle diameters of about 0.06 to about 0.60 millimeters.

Claim 29

The high efficiency furnace of claim 23 wherein said solid particles are selected from the group consisting of silica and alumina.

Claim 30

The high efficiency furnace of claim 23 wherein said thermal exchange means comprises a heat pipe having one end in thermal communication with said first fluidized bed and the opposite end in thermal communication with said second fluidized bed.

Claim 31

The high efficiency furnace of claim 23 additionally having an air bypass duct means in communication with said air duct means first and second open end whereby a portion of the air for heating said enclosed space bypasses said fluidized beds within said air duct means.

Claim 32

A high efficiency furnace for heating an enclosed space having two or more stages of heat exchange in series in a combustion flue gas duct comprising: a combustion chamber; a burner within said combustion chamber; flue gas duct means having a first and second open end in communication at said first open end with said combustion chamber and at said second end with the ambient atmosphere; a first blower means for movement of flue gas through said flue gas duct from said first to said second open end; a first heat exchange means toward said first open end of said flue gas duct means for heating supply air to said enclosed space; a second heat exchange means toward said second open end of said flue gas duct means comprising: (a) a first quantity of solid particles capable of operation at flue gas temperatures of about 200° to about 1200° F. comprising a first fluidized bed within said flue gas duct means; (b) distributor means for supporting said first fluidized bed and for admitting flue gas thereto and distributing flue gas throughout said first fluidized bed; (c) air duct means exterior to said flue gas duct means for the portion of its length passing through said first fluidized bed and having a first and second open end in communication at said first open end with ambient air and at said second open end with said burner to be provided preheated air; (d) a second blower means for movement of said air stream through said air duct means from said first to said second open end; (e) a second quantity of solid particles comprising a second fluidized bed within said air duct means; (f) distributor means for supporting said second fluidized bed and for admitting air therto and distributing the air to be heated throughout said second fluidized bed; (g) thermal exchange means comprising at least one heat pipe in communication with said first and second fluidized beds transferring heat from said first to said second fluidized bed; (h) each of said fluidized beds having a depth, when in fluidized state, of about 1/2 inch to about 4 inches.

Claim 33

A high efficiency furnace for heating an enclosed space having two or more stages of heat exchange in series in a combustion flue gas duct comprising: a combustion chamber; a burner within said combustion chamber; flue gas duct means having a first and second open end in communication at said first open end with said combustion chamber and at said second end with the ambient atmosphere; a first blower means for movement of flue gas through said flue gas duct from said first to said second open end; a first heat exchange means toward said first open end of said flue gas duct means for heating supply air to said enclosed space; a second heat exchange means toward said second open end of said flue gas duct means comprising: (a) a first quantity of solid particles capable of operation at flue gas temperatures of about 200° to about 1200° F. comprising a first fluidized bed within said flue gas duct means; (b) distributor means for supporting said first fluidized bed and for admitting flue gas thereto and distributing flue gas throughout said first fluidized bed; (c) air duct means exterior to said flue gas duct means for the portion of its length passing through said first fluidized bed and having a first and second open end in communication at said first open end with ambient air and at said second open end with said burner to be provided preheated air; (d) a second blower means for movement of said air stream through said air duct means from said first to said second open end; (e) a second quantity of solid particles comprising a second fluidized bed within said air duct means; (f) distributor means for supporting said second fluidized bed and for admitting air therto and distributing the air to be heated throughout said second fluidized bed; (g) thermal exchange means comprising at least one heat pipe in communication with said first and second fluidized beds transferring heat from said first to said second fluidized bed; (h) each of said fluidized beds having a depth, when in fluidized state, of about 1/2 inch to about 4 inches.

Claim 34

The high efficiency furnace of claim 30 wherein said first heat exchange means is a convective heat exchange means.

Claim 35

The high efficiency furnace of claim 30 wherein said first heat exchange means comprises: a third quantity of solid particles capable of operation at flue gas temperatures of about 200° to about 1200° F. comprising a third fluidized bed within said flue gas duct means; distributor means for supporting said third fluidized bed and for admitting flue gas thereto and distributing flue gas throughout said third fluidized bed; air duct means surrounding said flue gas duct means for the portion of its length passing through said third fluidized bed and having a first and second open end in communication at said first open end with the space to be heated and/or ambient air and at said second open end with the space to be heated; a fourth quantity of solid particles comprising a fourth fluidized bed within said air duct means; distributor means for supporting said fourth fluidized bed and for admitting air thereto and distributing the air to be heated throughout said fourth fluidized bed; thermal exchange means in communication with said third and fourth fluidized bed transferring heat from said third to said fourth fluidized bed; and each of said fluidized beds having a depth, when in fluidized state, of about 1/2 inch to about 4 inches.

Claim 36

The high efficiency furnace of claim 30 wherein said solid particles have mean particle diameters of about 0.06 to about 0.60 millimeters.

Claim 37

The high efficiency furnace of claim 30 wherein said solid particles are selected from the group consisting of silica and alumina.

Claim 38

The high efficiency furnace of claim 30 wherein said thermal exchange means comprises a heat pipe having one end in thermal communication with said first fluidized bed and the opposite end in thermal communication with said second fluidized bed.