Paint drying furnace

Disclosed is a paint drying furnace for baking and drying paint films on painted objects following a painting process. In the furnace of the invention, a shunt gas passage is provided for dividing a gas outputted from inner gas passages of a radiator means from a position of a radiator circulating gas passage upstream of a connecting point of a fresh air passage and mixing this divided gas into the gas circulating through the furnace interior circulating gas passage. With provision of this shunt gas passage, a combustion type radiator heating device acts also as furnace interior heating means.

TECHNICAL FIELD 
This invention relates to paint drying furnaces for baking and drying paint 
films on painted objects following a painting process, and more 
particularly to a paint drying furnace having furnace interior circulating 
gas passages for withdrawing furnace gases from furnace interiors and 
returning the withdrawn gas to the furnace interiors again, furnace 
interior heating means for heating, to a high temperature, the gases 
returned from the furnace interior circulating gas passages to the furnace 
interiors to heat the furnace interiors, hot gas heat source type radiator 
means with surfaces heated by passing a heat source hot gas through inner 
gas passages to radiate heat from the radiating surfaces to a furnace 
interior, a radiator circulating gas passage for returning a gas outputted 
from the inner gas passages of the radiator means, to the inner gas 
passages of the radiator means again, a combustion type radiator heating 
device mounted on the radiator circulating gas passage for heating the gas 
circulating through the radiator circulating gas passage, and a fresh air 
passage connected to a gas passage portion of said radiator circulating 
gas passage which transmits the gas outputted from the inner gas passages 
of the radiator means, to the combustion type radiator heating device, for 
mixing fresh air into the gas circulating through the radiator circulating 
gas passages, said combustion type radiator heating device being a direct 
heating type, combustion type heating device for burning a fuel directly 
in an atmosphere of the gas circulating through said radiator circulating 
gas passage. 
BACKGROUND ART 
Conventionally, as shown in FIG. 5, a paint drying furnace as noted above 
has, apart from a combustion type radiator heating device 19a mounted on a 
radiator circulating gas passage 20, and acting as furnace interior 
heating means Ha for heating, to a high temperature, gas RA' returned from 
a furnace interior circulating gas passage 9a to a furnace interiors 1a, a 
combustion type furnace interior heating device 19a' disposed on the 
furnace interior circulating gas passage 9a for heating gas RA circulating 
through the furnace interior circulating gas passage 9a by burning 
operation of a burner b. 
For the radiator circulating gas passage 20 having gas PA circulating 
therein and containing no paint solvent vapor generated in the furnace 
interior during baking and drying treatment, the combustion type radiator 
heating device 19a mounted thereon comprises a direct heating type, 
combustion type heating device (i.e. the type for burning a fuel directly 
in the atmosphere of the circulating gas PA to be heated) which is 
advantageous in terms of thermal efficiency. On the other hand, for the 
furnace interior circulating gas passage 9a having gas RA circulating 
therein and containing paint solvent vapor generated in the furnace 
interior, the combustion type furnace interior heating device 19a' mounted 
thereon comprises an indirect heating type, combustion type heating device 
in which burning flames and combustion gas G produced by the burning 
operation of burner b and the gas RA circulating through the furnace 
interior circulating gas passage 9a to be heated exchange heat in a 
non-contact mode through an inner heat exchanger hx. 
It has been necessary to employ, as the above combustion type furnace 
interior heating device 19a', an indirect heating type, combustion type 
heating device in which burning flames and combustion gas G, and the gas 
RA to be heated exchange heat in a non-contact mode, in order to avoid a 
situation in which the paint solvent vapor included in the gas RA 
circulating through the furnace interior circulating gas passage 9a is 
directly exposed and reacts to the burning flames in the combustion type 
heating device 19a', to produce a reaction product which lowers paint film 
quality (i.e. a reaction product which adheres to the paint films after 
return to the furnace interiors 1b, 1c to lower paint film quality). 
In FIG. 5, 7 denotes radiator means for radiating heat to the furnace 
interior by passing the gas PA' heated by the combustion type radiator 
heating device 19a, as a heat source hot gas through inner gas passages 
ip. 
18a denotes a fresh air passage for mixing fresh air OA (usually ambient 
air) into the gas RA circulating through the radiator circulating gas 
passage 20. 
21' denotes an exhaust passage of a radiator system for discharging from 
the system part of the gas PA circulating through the radiator circulating 
gas passage 20, in a quantity corresponding to the fresh air introduced 
through the fresh air passage. 
8a denotes a furnace interior exhaust passage for discharging as exhaust 
gas EA from the system, part of furnace interior gas ZA withdrawn from the 
furnace interior 1a. 
18a' denotes a fresh air passages for mixing fresh air OA (usually ambient 
air) in a quantity corresponding to the exhaust gas from the furnace 
interior exhaust gas passage 8a into the gas RA circulating through the 
furnace interior circulating gas passage 9a to dilute the solvent vapor 
produced in the furnace interior 1a. 
However, the above conventional furnace discharges from the system the 
combustion gas G retaining a large amount of heat after the heat exchange 
in the indirect heating type, combustion type heating device 19a' with the 
gas RA circulating through the furnace interior circulating gas passage 9a 
(specifically, the circulating gas mixed with fresh air OA), and thus 
involves a great heat loss. Further, part of the gas PA circulating 
through the radiator circulating gas passage 20 and retaining a large 
amount of heat is discharged from the system, which involves a great heat 
loss. Moreover, the indirect heating type, combustion type heating device 
19a' including the inner heat exchanger hx has a large heat capacity, and 
requires a large heating load in start-up times. These points pose a 
problem of high running cost. 
In addition, the indirect heating type, combustion type furnace interior 
heating device 19a', with the inner heat exchanger hx, has a large, 
complicated construction, which poses a problem of requiring high 
apparatus cost and large installation space. 
Having regard to the state of the prior art noted above, a primary object 
of this invention is to reduce the heat loss noted above while preventing 
formation of a reaction product which lowers paint film quality. 
Another object is to reduce the heating load in start-up times, and yet to 
downsize and simplify the apparatus construction. 
SUMMARY OF THE INVENTION 
The above objects are fulfilled by the invention defined in the claims. 
That is, a paint drying furnace of this invention is a paint drying furnace 
noted in the outset hereof and characterized by: 
a furnace interior circulating gas passage for withdrawing a furnace 
interior gas from a furnace interior and returning the withdrawn gas to 
the furnace interior again; 
furnace interior heating means for heating, to a high temperature, the gas 
returned from this furnace interior circulation gas passage to the furnace 
interior, thereby to heat the furnace interior; 
hot gas heat source type radiator means with radiating surfaces heated by 
passing a heat source hot gas through inner gas passages to radiate heat 
from the radiating surfaces to the furnace interior; 
a radiator circulating gas passage for returning a gas outputted from the 
inner gas passages of this radiator means to the inner gas passages of the 
radiator means; 
a combustion type radiator heating device disposed on this radiator 
circulating gas passage for heating the gas circulating through the 
radiator circulating gas passage; and 
a fresh air passage connected to a gas passage portion of said radiator 
circulating gas passage which transmits the gas outputted from the inner 
gas passages of said radiator means to said combustion type radiator 
heating device, for mixing fresh air into the gas circulating through the 
radiator circulating gas passage; 
wherein a shunt gas passage is provided for dividing the gas outputted from 
the inner gas passages of said radiator means, from a position of said 
radiator circulating gas passage upstream of a connecting point of said 
fresh air passage, and mixing this divided gas into the gas circulating 
through said furnace interior circulating gas passage; 
with provision of this shunt gas passage, said combustion type radiator 
heating device acting also as said furnace interior heating means. 
According to this invention, a mode of heating, to a high temperature, the 
gas to be returned from the furnace interior circulating gas passage to 
the furnace interior is employed, in which a hot, cleaned gas containing 
no reaction product lowering paint film quality is mixed from the radiator 
circulating gas passage through the shunt gas passage into the gas 
circulating through the furnace interior circulating gas passage. This 
minimizes heat loss. Moreover, it reliably avoids the problem that the 
reaction product lowering paint film quality mixes into the furnace 
interior heating gas returned from the furnace interior circulating gas 
passage to the furnace interior. Preferably, said combustion type radiator 
heating device is a direct heating type, combustion type heating device 
for burning a fuel directly in an atmosphere of the gas circulating 
through said radiator circulating gas passage. 
With this construction, the gas circulating through the furnace interior 
circulating gas passage and containing paint solvent vapor not passed 
through the direct heating type, combustion type heating device. It is 
therefore unnecessary for the furnace interior circulating gas passage to 
include, as means for heating the furnace interior, an indirect heating 
type, combustion type heating device which discharges, from the system, 
the combustion gas retaining a large amount of heat after a heat exchange 
with the circulating gas to be heated. Heat loss is markedly reduced as a 
whole since the mode is employed in which the hot, cleaned gas is divided 
and supplied from the radiator circulating gas passage through the shunt 
gas passage into the furnace interior circulating gas passage for heating 
the furnace interior, in place of the conventional mode in which part of 
the gas circulating through the radiator circulating gas passage is 
discharged from the system, while retaining a large amount of heat, and in 
a quantity corresponding to the fresh air introduced from the fresh air 
passage. Further, the heating load in start-up times is reduced since an 
indirect heating type, combustion type heating device is not required 
which has an increased heat capacity with an inner heat exchanger 
provided. Consequently, running cost may be reduced markedly, compared 
with the conventional furnace. 
In addition, the entire construction is made simple and compact since no 
indirect heating type, combustion type heating device is required which 
has a large and complicated construction with an inner heat exchanger 
provided. Thus, compared with the conventional furnace, the apparatus cost 
may be reduced and the required installation space may be diminished. 
In this invention, a combustion type exhaust cleaning device may be 
provided for burning paint solvent vapor contained in exhaust gas from the 
furnace interiors to clean the exhaust gas, and a heat recovering heat 
exchanger may be provided for allowing a heat exchange between the exhaust 
gas cleaned by this exhaust cleaning device and the fresh air to preheat 
the fresh air, said fresh air passage acting as a gas passage for mixing 
the fresh air preheated at said heat recovering heat exchanger, into the 
gas circulating through said radiator circulating gas passage. 
With this construction, in burning a fuel in the direct heating type, 
combustion type heating device disposed on the radiator circulating gas 
passage as the combustion type heating means acting also as furnace 
interior heating means, in the atmosphere of the gas mixture of the gas 
outputted from the inner gas passages of the radiator means and the fresh 
air supplied from the fresh air passage, this fresh air has been preheated 
for mixing into the gas outputted from the inner gas passages of the 
radiator means. Compared with a mode of mixing fresh air without being 
preheated, a gas mixture of higher temperature may be supplied to the 
direct heating type, combustion type heating device while checking a 
temperature reduction of the gas mixture due to the fresh air mixing. This 
improves the combustion efficiency of the combustion type heating device 
to promote a reduction in the running cost more effectively. 
Further, in this invention, said shunt gas passage may include a combustion 
type auxiliary heating device for further heating the gas circulating 
through said shunt gas passage. 
With this construction, a furnace interior heating amount and a heat 
radiating amount of the radiator means may be adjusted independently of 
each other according to required furnace operating conditions by a 
combination of a burning amount adjustment for the combustion type 
radiator heating device disposed on the radiator circulating gas passage 
and a burning amount adjustment for the combustion type auxiliary heating 
device disposed on the shunt gas passage. This realizes an improved baking 
and drying performance of the furnace. 
The various features of novelty which characterize the invention are 
pointed out with particularity in the claims annexed to and forming a part 
of this specification. For a better understanding of the invention, its 
operating advantages and specific objects obtained by its use, reference 
should be had to the accompanying drawings and descriptive matter in which 
there is illustrated and described a preferred embodiment of the invention 
.

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS 
In FIG. 1, 1 denotes a paint drying furnace for baking and drying paint 
films on painted objects 2 (which are automobile bodies in this example) 
following a painting process. The painted objects 2 mounted on carts 3a 
are transported by a conveyor apparatus 3 successively through a 
temperature increasing zone 1a, a first heat retaining zone 1b and a 
second heat retaining zone 1c in the furnace. 
The respective zones 1a, 1b, 1c in the furnace have gas supply chambers 5a, 
5b, 5c defining a plurality of hot gas supply openings 4, and exhaust 
openings 6a, 6b, 6c for withdrawing zone interior gases ZA. The 
temperature increasing zone 1a has, in addition to the gas supply chamber 
5a and exhaust opening 6a, radiator panels 7 for radiating heat to the 
painted objects 2. 
The zone interior gases ZA withdrawn through the exhaust openings 6a, 6b, 
6c are divided into parts to be led as zone exhaust gases EA to furnace 
interior exhaust gas passages 8a, 8b, 8c assigned to the respective zones, 
and parts to be led as zone circulating gases RA to furnace interior 
circulating gas passages 9a, 9b, 9c assigned to the respective zones. The 
exhaust gases EA led to the furnace interior exhaust gas passages 8a, 8b, 
8c are collected into an exhaust gas collection passage 10, and 
transmitted through a main exhaust gas passage 11 to a combustion type 
exhaust cleaning device 12. Fe denotes an exhaust fan. 
The exhaust cleaning device 12 includes a burner b and catalyst layers s. 
This exhaust cleaning device 12 cleans the exhaust gas EA by burning paint 
solvent vapor (i.e. paint solvent vapor generating from paint films as a 
result of a baking and drying process in the furnace) contained in the 
exhaust gas EA under catalysis. Cleaned exhaust gas EA' is outputted to an 
exhaust gas discharge passage 13. 
14 denotes a heat recovering heat exchanger at a hot side for allowing a 
heat exchange between the untreated exhaust gas EA transmitted through the 
main exhaust gas passage 11 to the exhaust cleaning device 12 and the hot, 
cleaned exhaust gas EA' outputted to the exhaust gas discharge passage 13 
after the burning treatment, thereby to preheat the untreated exhaust gas 
EA transmitted to the exhaust cleaning device 12. 
15 denotes a heat recovering heat exchanger at a cold side for allowing a 
heat exchange between fresh air OA (which is ambient air drawn from 
outside in this example) introduced through a main fresh air passage 16 
and the cleaned exhaust gas EA' in the exhaust gas discharge passage 13 
after passing through the heat recovering heat exchanger 14 at the hot 
side, thereby to preheat the fresh air OA. The cleaned exhaust gas EA' 
after being used for preheating the fresh air OA in the heat recovering 
heat exchanger 15 at the cold side is discharged from the system through 
the exhaust gas discharge passage 13. 
Each furnace interior circulating gas passage 9a, 9b, 9c has a downstream 
end thereof connected to the gas supply chamber 5a, 5b, 5c of the 
corresponding zone, and a filter 17 for cleaning circulating gas RA and a 
fan Fr for causing the circulation mounted in intermediate positions 
thereof. 
Individual fresh air passages 18a, 18b, 18c for the respective zones 1a, 
1b, 1c are branched from the main fresh air passage 16. Each of these 
fresh air passages 18a, 18b, 18c has a fan Fo mounted thereon for drawing 
the fresh air. Of these fresh air passages 18a, 18b, 18c, the fresh air 
passages 18b, 18c for the first and second heat retaining zones 1b, 1c are 
connected to the furnace interior circulating gas passages 9b, 9c of the 
corresponding zones. 
The fresh air passages 18b, 18c for the first and second heat retaining 
zones 1b, 1c have, acting as furnace interior heating means Hb, Hc for the 
respective heat retaining zones 1b, 1c, combustion type furnace interior 
heating devices 19b, 19c arranged upstream of points of passage connection 
to the furnace interior circulating gas passages 9b, 9c for heating 
passing fresh air OA by burning operation of burners b. The combustion 
type furnace interior heating devices 19b, 19c employed are the direct 
heating type for burning a fuel directly in the atmosphere of fresh air OA 
flowing through the fresh air passages 18b, 18c. 
That is, for the first and second heat retaining zone 1b, 1c, hot fresh air 
OA' (in particular, air containing combustion gas) heated by the 
combustion type furnace interior heating devices 19b, 19c is mixed into 
the gases RA circulating through the furnace interior circulating gas 
passages 9b, 9c, thereby heating, to a high temperature, the gases RA' 
returned to the heat retaining zones 1b, 1c from the furnace interior 
circulating gas passages 9b, 9c (i.e., gas mixtures of the zone 
circulating gas RA and hot fresh air OA'). The gases RA' heated to a high 
temperature are delivered as hot gases from the hot gas supply openings 4 
of gas supply chambers 5b, 5c into the heat retaining zones to heat the 
heat retaining zones by convection, thereby to adjust the interior 
temperatures of the respective heat retaining zones 1b, 1c to a 
predetermined temperature and to dilute the solvent vapor generated in the 
respective heat retaining zones 1b, 1c. 
For the temperature increasing zone 1a, on the other hand, radiator panels 
of the hot gas heat source type are employed as radiator panels 7, in 
which radiating surfaces 7a are heated by passing a heat source hot gas 
through inner gas passages ip to radiate heat from the radiating surfaces 
7a to the painted objects 2. A radiator circulating gas passage 20 is 
provided to return gas PA outputted from the inner gas passages ip of the 
radiator panels 7, to the inner gas passages ip of the radiator panels 7. 
A combustion type radiator heating device 19a is mounted on the radiator 
circulating gas passage 20 for heating the gas PA circulating through the 
radiator circulating gas passage 20 by burning operation of a burner b. 
The combustion type radiator heating device 19a employed is the direct 
heating type, as are the combustion type furnace interior heating devices 
19b, 19c for the first and second heat retaining zones 1b, 1c, for burning 
a fuel directly in the atmosphere of gas PA circulating through the 
radiator circulating gas passage 20. 
A shunt gas passage 21 is branched from a gas passage portion of the 
radiator circulating gas passage 20 which leads the gas PA outputted from 
the inner gas passages ip of radiator panels 7 to the combustion type 
radiator heating device 19a. The shunt gas passage 21 is connected to the 
furnace interior circulating gas passage 9a of the temperature increasing 
zone 1a. The fresh air passage 18a for the temperature increasing zone 1a 
is connected to the radiator circulating gas passage 20 in a position 
closer to the combustion type radiator heating device 19a than a branching 
position of the shunt gas passage 21. Fp denotes a circulating fan mounted 
in the radiator circulating gas passage 20. 
That is, for the temperature increasing zone 1a, the combustion type 
radiator heating device 19a heats a gas mixture of the remainder of the 
gas PA outputted from the radiator panels 7, after part thereof is 
branched off into the shunt gas to passage 21, and the fresh air OA 
supplied through the fresh air passage 18a. The heated gas PA' (in 
particular, a gas containing combustion gas) is passed through the inner 
gas passages ip of radiator panels 7 to radiate heat from the radiating 
surfaces 7a of radiator panels 7 to the painted objects 2. 
The hot gas PA branched off into the shunt gas passage 21 is mixed into the 
gas RA circulating through the furnace interior circulating gas passage 9a 
of the temperature increasing zone 1a to heat, to a high temperature, the 
gas RA' (i.e. a gas mixture of zone circulating gas RA of the temperature 
increasing zone 1aand hot gas PA" supplied from the shunt gas passage 21) 
returned from the furnace interior circulating gas passage 9a to the 
temperature increasing zone 1a. The gas RA' heated to a high temperature 
is delivered as hot gas from the hot gas supply openings 4 of gas supply 
chamber 5a into the temperature increasing zone to heat the temperature 
increasing zone by convection, thereby to adjust the interior temperature 
of the temperature increasing zone 1a to a predetermined temperature. At 
the same time, the gas mixture is introduced from the shunt gas passage 21 
as a fresh gas into the temperature increasing zone 1a to dilute the 
solvent vapor generated therein. 
That is, zone heating of the temperature increasing zone 1a is done by 
employing a mode in which the gas RA' returning from the furnace interior 
circulating gas passage 9a to the furnace interior 1a is heated to a high 
temperature by dividing and supplying the hot gas PA" by the shunt gas 
passage 21 from the radiator circulating gas passage 20 to the furnace 
interior circulating gas passage 9a as noted above. Thus, the combustion 
type radiator heating device 19a on the radiator circulating gas passage 
20 is made to serve also as furnace interior heating means Ha for the 
temperature increasing zone. 
In short, for the first and second heat retaining zones 1b, 1c, while using 
the direct heating type, combustion type furnace interior heating devices 
19b, 19c, fresh air OA containing no paint solvent vapor is heated by the 
combustion type furnace interior heating devices 19b, 19c. A furnace 
interior heating mode is employed in which the heated fresh air OA' is 
mixed into the gases RA circulating through the furnace interior 
circulating gas passages 9b, 9c to heat the zone interiors. For the 
temperature increasing zone 1a including the radiator panels 7, a furnace 
interior heating mode is employed in which part of the hot clean gas PA in 
the radiator circulating gas passage 20 containing no paint solvent vapor 
is divided, and the divided hot clean gas PA" is mixed into the gas RA 
circulating through the furnace interior circulating gas passage 9a to 
heat the furnace interior. By employing these, the paint solvent vapor 
contained in the gases RA circulating through the furnace interior 
circulating gas passages 9a, 9b, 9c is exposed and reacts to burning flame 
in the direct heating type, combustion type heating devices, to produce a 
reaction product which would lower paint film quality. It is possible to 
avoid a situation where the reaction product mixes into the gases 
returning to the furnace interiors from the furnace interior circulating 
gas passages 9a, 9b, 9c. 
On the other hand, hoods 22a, 22b are arranged at the inlet and outlet of 
the furnace, respectively, for collecting furnace interior gases ZA' 
leaking out through the inlet and outlet. Hood exhaust gas passages 23a, 
23b connected to these hoods 22a, 22b include hood gas exhaust fans Ff and 
gas passage opening and shutting dampers Df. The exhaust gas collection 
passage 10 is connected to the hood exhaust gas passages 23a, 23b in 
positions closer to the hoods than the gas passage opening and shutting 
dampers Df. 
That is, in a regular operation as an operating mode of the furnace to 
perform baking and drying treatment of the painted objects 2 in the 
furnace, gas passage opening and shutting dampers De of the furnace 
interior exhaust gas passages 8a, 8b, 8c of the respective zones 1a, 1b, 
1c are opened, and gas passage opening and shutting dampers Df of the hood 
exhaust gas passages 23a, 23b are closed. Consequently, exhaust gases EA 
from the respective zones 1a, 1b, 1c and gases ZA' collected by the hoods 
22a, 22b are transmitted to the exhaust cleaning device 12, and the 
exhaust cleaning device 12 burns the paint solvent vapor contained in 
these exhaust gases EA and collected gases ZA'. 
In a start-up operation as a stage preceding the regular operation to 
increase the zone temperatures of the respective zones 1a, 1b, 1c to the 
predetermined temperatures with no painted objects 2 present in the 
furnace yet, the gas passage opening and shutting dampers De of the 
furnace interior exhaust gas passages 8a, 8b, 8c of the respective zones 
1a, 1b, 1c are closed to stop the exhaust gases from the respective zones 
1a, 1b, 1c, thereby to expedite start-up of the zone temperatures. On the 
other hand, the gas passage opening and shutting dampers Df of the hood 
exhaust gas passages 23a, 23b are opened, whereby the hood exhaust fans Ff 
cause the gases ZA' collected by the hoods 22a, 22b (i.e. gases not 
containing paint solvent vapor yet) to be discharged to a fixed discharge 
location through the hood exhaust gas passages 23a, 23b. 
24a, 24b in the drawing denote panel heaters for preventing the paint 
solvent vapor in the furnace interior gases from condensing on ceilings 
adjacent the inlet and outlet of the furnace. By preventing condensation 
of the paint solvent vapor with theses panel heaters 24a, 24b, a situation 
is avoided where condensed paint solvent drips on the painted objects 2 to 
lower paint film quality. Moreover, this assures that paint solvent vapors 
adjacent the inlet and outlet of the furnace are promptly collected along 
with the furnace interior gases ZA' by the hoods 22a, 22b and transmitted 
to the exhaust cleaning device 12. 
The panel heaters 24a, 24b employed are the hot gas heat source type to 
pass heat source hot gases through inner gas passages 1a, 1b. For the 
panel heater 24a at the furnace inlet, part of the hot gas PA' transmitted 
through the radiator circulating gas passage 20 from the combustion type 
radiator heating device 19a to the radiator panels 7 is supplied as heat 
source hot gas to the inner gas passage 1a of panel heater 24a The gas 
having passed through the inner gas passage ia of panel heater 24a is 
joined to the gas PA outputted from the radiator panels 7. For the panel 
heater 24b at the furnace outlet, part of the hot gas RA' supplied to the 
gas supply chamber 5c in the second heat retaining zone 1c is supplied as 
heat source hot gas to the inner gas passage ib of panel heater 24b. The 
gas having passed through the inner gas passage ib of panel heater 24b is 
joined to the gas ZA withdrawn from the zone 1c through the exhaust 
opening 6c. 
FIG. 2 shows a specific inner structure of the first and second heat 
retaining zones 1b, 1c. As shown in FIG. 2, a pair of gas supply chambers 
5b, 5c extending in the direction of transport of the painted objects 2 
are arranged at opposite, left and right ends in the zone bottom. Each of 
these gas supply chambers 5b, 5c defines, as the hot gas supply openings 
4, upward supply openings 4a for blowing hot gas RA' upward along a 
furnace wall, and oblique supply openings 4b for blowing hot gas RA' 
obliquely upward toward the right and left center in the zone. 
As shown in FIG. 3, these upward supply openings 4a and oblique supply 
openings 4b are arranged in respective rows in the direction of transport 
of the painted objects 2, with each opening in the form of a slit. Gas 
flow guides 25a, 25b extending in the direction of transport of the 
painted objects 2 are formed at the right and left center of the zone 
ceiling and at opposite, right and left ends of the zone ceiling for 
guiding zone interior gas flows as shown in arrows in the drawing. A 
furnace wall structure comprises a double wall structure including an 
outer wall panel 26 with an insulating material 26a applied thereto, and 
an inner wall panel 27 with an insulating material 27a applied thereto, an 
insulating layer of air 28 being formed between the inner and outer walls. 
While the gas supply chambers 5b, 5c are arranged in the zones as described 
above, as for the exhaust side, exhaust chambers are omitted and each heat 
retaining zone 1a, 1b has one or two exhaust openings 6b, 6c opening at 
the right and left center of the zone ceiling. By omitting exhaust 
chambers in this way, each heat retaining zone 1a, 1b has a reduced heat 
capacity to diminish a start-up heating load during an initial period of 
operation. 
On the other hand, a specific inner structure of the temperature increasing 
zone 1a, as shown in FIG. 4, has a pair of gas supply chambers 5a 
extending in the direction of transport of the painted objects 2 and 
arranged at opposite, right and left ends of the zone bottom. Each of 
these gas supply chambers 5a defines upward supply openings 4a and oblique 
supply openings 4b as in the heat retaining zones 1b, 1c. The radiator 
panels 7 are arranged on opposite furnace walls above these gas supply 
chambers 5a. 
Gas flow guides 25a, 25b are provided as in the heat retaining zones 1b,1c. 
As for the exhaust, exhaust chambers are omitted as in the heat retaining 
zones 1b, 1c, and one or two exhaust openings 6a open at the right and 
left center of the zone ceiling. By omitting exhaust chambers in this way, 
large areas of the radiating surfaces 7a are secured for the radiator 
panel 7. 
In the furnace wall structure of temperature increasing zone 1a in the 
example shown in FIG. 4, the furnace wall in the temperature increasing 
zone 1ais formed only of a single wall panel 29 with an insulating 
material 29a applied thereto. Where appropriate, a double wall structure 
as in the heat retaining zones 1b, 1c may be employed also for the 
temperature increasing zone 1a. 
(1) As shown in broken lines in FIG. 1, the shunt gas passage 21 may 
include an auxiliary heating device 30 for heating the gas PA" circulating 
through the shunt gas passage 21. Since the gas PA" circulating through 
the shunt gas passage 21 is a gas containing no paint solvent vapor, the 
auxiliary heating device 30 may be the direct heating type or indirect 
heating type. 
(2) In the foregoing embodiment, the invention defined in claim 1 is 
applied to the temperature increasing zones 1a in the furnace. In a 
furnace construction in which the furnace interior is divided into a 
plurality of zones, the invention defined in claim 1 may be applied to all 
of these zones. The invention defined in claim 1 may be applied to a 
furnace construction having no divided zones. 
(3) In the foregoing embodiment, ambient air is used as fresh air OA. Fresh 
air OA may be varied types of air as long as furnace interior gas ZA is 
not contained, such as indoor air of a painting plant, or cleaned exhaust 
air from a different apparatus. 
(4) The inner structure of the furnace is not limited to the inner 
structures shown in FIGS. 2 and 4 but may be varied in may ways.