[0001] This invention relates to an apparatus for surface treatment effectively applicable
for treating or finishing the surface of metal articles or objects when chemical coating,
plating, etching, etc., is carried out.
[0002] Various methods have conventionally been known for treating or finishing the surface
of metal articles, such as chemical coating, plating, etching, etc. Above all chemical
conversion treatment for forming some kinds of corrosion resistant films on the surface
of steel plates or steel bars by means of chemical reaction or electro-chemical reaction
is known, and more particularly phosphating, wherein zinc phosphate, manganese phosphate,
ferrous phosphate, etc., are employed, is widely known. And it is widely practiced
as a method of surface preparation when steel members are coated in the field of,
for example, car assemblying, bridge building, or manufacturing of household electrical
appliances.
[0003] When practicing such a surface treatment objects-to-be-treated must be in general
contacted with the treating liquid, and either of two ways, a spraying method in which
the liquid is sprayed over the surface of the objects-to-be-treated and a dipping
method in which the objects are dipped in the liquid, is selected for contacting the
objects with the liquid. The former spraying method is unsuitable for treating objects
of complicated shape, for example car bodies which have portions difficult to be uniformly
treated by spraying such as a fender, a door, or a constructed part into a box-like
shape. The liquid is liable not to sufficiently reach the inside surface of complicated
corner, leaving sometimes untreated portions or sometimes unsatisfactorily treated
portions. The latter dipping method is much better than the former in respect of the
liquid reaching to many quarters of the objects-to-be-treated, but it still leaves
something to be desired because the sludge produced in the period of dipping of the
objects-to-be-treated into the liquid is deposited on the bottom of a treating vessel
so as to cause some troubles in a continuous surface treatment.
[0004] In the course of chemical reaction taking place between a steel plate as an object-to-be-treated
and a treating liquid containing phosphate by-products called sludge are produced.
This chemical conversion sludge created in the course of a side reaction did not give
rise to so serious problematical trouble in the conventional spray method wherein
phosphate conversion coating was made on the surface of the object by means of the
spraying, because the forced pressure of the spraying naturally prevented sticking
of the sludge onto the coated surface of the object. The sludge has however recently
become a serious factor for deteriorating the quality of the articles since the surface
treatment had been gradually changed to the full dipping treatment method, wherein
the object is completely dipped in the treating liquid. In this full dipping method
the sludge is liable to be floated in suspension in the treating liquid. This kind
of chemical conversion sludge is not only floated in a treating vessel containing
the liquid but also flung up from the bottom of the vessel on which it has once been
deposited due to the movement of the object-to-be-treated W
3 in the vessel. The sludge possibly stuck to the crystal' coating or contained in
the formed coating deteriorates the corrosion resistance of the coating or adversely
affects the forthcoming electrodepositing process. It is therefore highly desirable
to advantageously discharge or exhaust such harmful problem-arising sludge out of
the vessel.
[0005] Conventionally leading the liquid out of the system or vessel, by recycling the same
outside and inside the vessel, was practiced for removing the sludge. A sludge removing
apparatus disposed outside the vessel is apt to occupy an innegligible space and impose
an innegligible cost. It is naturally accompanied by some other problems such as complicacy
of piping for recycling, increasing of the recycled amount of the liquid, etc., and
a still unsolved problem is flinging up of the deposited sludge on the vessel bottom.
[0006] It is an object of this invention, which was made against such a background, to provide
an apparatus for the surface treatment, being substantially relieved of the conventional
disadvantages, capable of continuously removing the sludge produced in the full dipping
method from the bottom of the treating vessel.
[0007] The apparatus for performing the above- mentioned surface treatment in accordance
with this invention is provided, as an essential feature, at the bottom portion of
the treating vessel with one or more hoppers, which function to collect the deposited
sludge. for exhausting the same through the lower portion of the hopper outside the
treating vessel wherein a plurality of slant plates disposed above the bottom of the
treating vessel are provided containing the treating liquid for performing an aimed
surface treatment by dipping an object-to-be-treated in a treating liquid such as
chemical conversion solution like phosphate; the slant plates are disposed, being
inclined in the same direction, with a predetermined inter- distance among them. The
sludge produced in the treating liquid is gradually precipitated, while being floated
therein, on the bottom of the vessel through the gap or clearance between the slant
plates, which are not contacted with the vessel bottom. This disposition of the slant
plates facilitates the sludge produced in the vessel to be gradually precipitated
or deposited down on the bottom thereof, by well functioning as protecting walls,
almost not being affected by the flowing of the liquid and the movement of the objects-to-be-treated.
In such an apparatus the deposited sludge can not be flung up into the liquid again
by virtue of the slant plates, but can be easily taken away out of the vessel.
[0008] A few concrete examples will be described hereunder with reference to the appended
drawings, in which:
Figures 1 and 2 are respectively a schematic transverse sectional view of two different
embodiments of an apparatus for surface treatment in accordance with this invention.
[0009] An apparatus shown in Figure 1 relates to, for example, zinc phosphating process
as a preliminary treatment on an object-to-be-treated W
3 such as a car body when it is applied with coating. As a first step for applying
the zinc phosphate treatment the object W
3 is degreased with a trichloroethylene or alkaline solution, followed by water cleaning
and contact with titanium phosphate solution as a second step. In this way nuclei
of phosphate coating crystals are formed on the surface of the object W
3. An object W
3 which has been applied with such surface preparation is conveyed, being suspended
from a hanging conveyor 27 as shown in Figure 1, from right to left for being dipped
into treating liquid of a treating vessel 20.
[0010] The object W
3 which has been dipped into the treating liquid 4 at the initial stage of the process,
is gradually conveyed toward the final stage on the left side end for being completely
covered in the meantime by the continuously grown zinc phosphate crystals all over
the surface thereof. The time required for this process is within the range of 60-300
seconds.
[0011] In this surface treatment process of the objects sludge consisting of ferrous phosphate
and others is produced, and four hoppers 22 (generally several in number) of funnel
shape are formed as extensions from the bottom portion of the vessel 20 for depositing
or precipitating the sludge on the bottom of the hopper 22.
[0012] The four hoppers 22 are horizontally arranged in series in parallel to a conveying
direction Y of the objects-to-be-treated W
3. Within those hoppers 22 a multiplicity of slant plates 24 inclined by an angle (a)
of 45-90° against the conveying direction of the objects W
3 are arranged parallelly with each other, keeping away from a wall surface 23 of the
hopper 22 with a predetermined distance, viz., being not in contact therewith. Those
slant plates 24 function as protector walls for preventing the deposited sludge from
being stirred by the flowing movement of the treating liquid. Besides, each hopper
22 is provided at the lower end thereof with a one-way valve 26.
[0013] The treating vessel 20 is further provided with undermentioned several devices: a
slant gush-spraying pipe 28 and a horizontal gush-spraying pipe 30 disposed on the
rightward end portion, in Figure 1, of the vessel 20 for gush-spraying the treating
liquid to the objects W
3 which are moved by a inclined conveyor 27 into the liquid in the vessel 20; a gushing
nozzle 34 disposed, above a horizontal bottom portion 32 of the vessel 20 on the rightward
side away from the hoppers 22, in communication with the slant gush-spraying pipe
28, for gushing the liquid toward the hoppers-arranged direction; and a recovering
tank 36 for reservoiring the liquid overflowed out of the treating vessel 20.
[0014] In this embodiment of such a structure the objects W
3 are transported in suspended state from the conveyor 27 in the direction designated
with the arrow Y for being dipped into the liquid, while a part of the liquid reservoired
in the recovering tank 36 is led, via conduits 38, 40, to the slant gush-spraying
pipe 28 and via conduits 38, 42 to the horizontal gush-spraying pipe 30 by the action
of a pump P
4, for being gush-sprayed onto the just incoming objects W
3. The rest of the liquid in the recovering tank 36 is led, by the action of pumps
P
5, P
6. via conduits 38, 44 back into the vessel 20 for being recycled, while making a counterflow
in the direction designated by an arrow X against the movement of the objects W
3 in the liquid, to the recovering tank 36.
[0015] In the initial stage of the dipping of the objects W
3, from the beginning of dipping to the start of leftward movement in Figure 1 after
the complete dipping, strong or vehement chemical reaction progresses between the
object W
3 and the treating liquid while producing large amount of sludge. The sludge is however
precipitated by the action of gravity in each of the hoppers 22 extended from the
lower portion of the vessel 20 and on the horizontal portion 32 is collected into
the hopper 22 by virture of the gush-spraying of the liquid from the gushing nozzle
34 disposed on the conduit 40. The sludge precipitated into the hoppers 22 comes first
onto each of the parallelly arranged slant plates 24 and then drops through the gap
therebetween as far as the wall surface of the individual hoppers 22, for finally
being collected along the wall surface in the lower portion 46 of the respective hopper
22. The sludge collected there in this way is intermittently delivered to a separater
50, by the action of a pump P
7, via the one-way valve 26 and the conduit 48. The liquid containing the thus collected
sludge is separated at the separater 50, which is located out of the recycling circuit,
for being returned to the recovering tank 36 or to a gush-spraying device disposed
on the final stage side of the vessel 20.
[0016] As the slant plates 24 arranged horizontally with each other in the lower portion
of the vessel 20, and particularly in this case within the hoppers 22, are inclined
against the flowing direction X of the liquid, i.e., the same direction to the object
conveyance, stirring of the sludge collected in the lower portion 46 by the liquid
flowed into between the slant plate 24 can not occur. And the conveyance operation
of the objects as well as the gush-spraying of the liquid from the slant gush-spraying
pipe 28 and the horizontal gush-spraying pipe 30 can not cause stirring or flinging
uo of the sludge, either, because the slant plates 24 well prevent the phenomenon
by functioning as protector walls. In other words, the above described structure effectively
protects the objects-to-be-treated W
3 from being deteriorated in quality by sticking of the sludge in floatation or flung
up from the lower portion 46 of the hopper 22 in the course of the surface treatment.
As described earlier the sludge deposited on the horizontal portion 32 is also removed
therefrom into the lower portion 46 of the hopper 22 by the gushing of the liquid
from the gushing nozzle 34, which means complete relief of the sludge from the bottom
portion of the vessel 20.. This invention can be said to have succeeded, through remarkable
decrease of the floating and depositing sludge, in improving the quality of the surface
treatment, particularly the anti-corrosion coating quality, of the objects-to-be-treated
W
3.
[0017] In the description of the above embodiment all of the hoppers 22 arranged in series
are of the same size, but a modified type wherein the nearest hopper 22 to the object
incoming side end is made the largest in capacity and others are made gradually smaller
toward the leftward end is preferably recommended, because the sludge producing rate
is largest at the initial stage of contact between the object W
3 and the liquid.
[0018] Still another embodiment will be described with reference to Figure 2, wherein an
object W
4 suspended by a conveyor 62 is, after it has been completely dipped in zinc phosphating
solution contained in a treating vessel 60, moved therein for being given chemical
conversion treatment in the meantime just like in the previous embodiment. The only
difference lies in the structure of the bottom portion of the vessel 60. In this embodiment
only one hopper 64 of funnel shape is formed at the leftward end of the bottom portion,
and the rest of the bottom portion is left as a flat portion 66. Above the flat portion
66 a multiplicity of slant plates 68 inclined at an angle (f3) of 45-90° are arranged,
parallelly to each other with a predetermined interdistance, in the horizontal direction
and along the conveyance direction Y of the objects-to-be-treated W
4. They are not in contact with the flat portion 66, just like slant plates 70 which
are similarly arranged in the hopper 64 parallelly with each other and kept away from
a wall surface 72 of the hopper 64 by a predetermined distance.
[0019] On the flat portion 66 a suitable number of gushing nozzles 74 are arranged parallelly
thereto for gushing the liquid toward the hopper 64 so as to wash away the deposited
sludge thereon.
[0020] When an object W
4 suspended from a conveyor 62 is transported in the direction designated with an arrow
Y to be dipped into the liquid in an apparatus of such a structure, producing of the
sludge is begun by the chemical conversion treatment. And the sludge thus produced
is precipitated through the clearance(s) between the slant plates 68 onto the flat
portion 66 of the vessel 60 and also to the lower portion of the hopper 64 along the
slant plates 70 while passing the clearance(s) therebetween. The liquid in a recovering
tank 76 is via conduits 78, 80 by the action of a pump P
8 led to each of the gushing nozzles 74 for being gushed therefrom respectively. The
sludge deposited on the flat portion 66 is therefore collected to the hopper 64 passing
through the clearance formed between the slant plates 68 and the flat portion 66.
The sludge collected in the hopper 64 is led via a one-way valve 82 and a conduit
84 by the action of a pump P
. to a separater 86 which is located outside the recycle circuit of the liquid. The
separated liquid in the separater 86 is returned to a recovering tank 76 or to a gush-spraying
device 15, disposed on the final stage side of the vessel 60. The remaining liquid
in the recovering tank 76 is led via conduits 78, 88 by the action of pumps P
10 and P11 to the vessel 60 for being flowed in the direction designated with an arrow
X so as to be re-utilized to the chemical conversion treatment of the objects W
4.
[0021] As the slant plates 68, 70 are, just like in the previous embodiment, inclined in
the reversed direction X of that of the flowing of the liquid, they not only prevent
the liquid from flowing therebetween but also prevent the deposited sludge from being
flung up when the objects W
4 are moved in the liquid by functioning as protective walls.
[0022] This embodiment is particularly featured in eliminating disposition of many hoppers
and consequently simplifying the structure of the bottom portion of the vessel, and
besides in uni- formalizing the shape of, as well as reducing the size of, the slant
plates.
[0023] In the foregoing embodiments the slant plates 24, 68, 70 are all inclined with an
angle (a, A) of 45-90° in the conveying direction of the objects W, the direction
marked the arrow Y, that is reversed against the flowing direction of the liquid marked
the arrow X. And it is true that the inclined direction of the slant plates is in
the same way as the direction of conveyance of the objects W for the better effect
of the slant plates as the protective walls, but this invention is not limited to
this way of arrangement. A multiplicity of slant plates inclined in the inverted direction
to the above embodiments are also allowable. As to the angle of inclination (α, β)
of the slant plates 24, 68, 70, in this instance, the preferable range lies within
45-90°, as an angle larger than 45° is favorable for smoothly sliding down the sludge
without staying on the plate, an angle less than 45° being contrary undesirable because
of easy piling up of the sludge on the plate. This tendency of arresting the sludge
of smoothly falling down from the surface of the plate, which consequently obliges
the plate to be curtailed its length according to the extent of turbulence of the
treating liquid.
[0024] Summarising the above described details of this invention, structure of the bottom
portion of the treating vessel used for the surface treatment has been improved, accompanied
by disposition of a multiplicity of slant plates functioning as the protective walls,
with a remarkable result of preventing the sludge from being flung up in the course
of the treatment for being smoothly removed out of the treating vessel. This effect
of having enhanced the quality of treatment by preventing the once deposited sludge
from being stirred up into the treating liquid and the recycling efficiency of the
treating liquid by effectively removing the sludge therefrom is very significant from
the standpoint of industrial efficiency.
1. An apparatus for applying a predetermined surface treatment on an object-to-be-treated
by means of dipping said object in a treating liquid contained in a treating vessel,
said apparatus comprising one or more hoppers (18, 22, 64) of funnel shape which are
disposed at the bottom portion of said treating vessel (3, 20, 60) for collecting
precipitated sludge into said hoppers (18, 22, 64), said collected sludge being removed
out of said treating vessel (3, 20, 60) from the lower portion of said hoppers (18,
22, 64), characterized in that a multiplicity of slant plates (24, 68, 70) inclined
in the same direction are disposed, above the bottom portion of said treating vessel
(3, 20, 60) with a predetermined inter-distance so that floating sludge in said liquid
may be precipitated through the clearance between said slant plates (24, 68, 70) onto
the bottom portion of said treating vessel (3, 20, 60).
2. The apparatus in accordance with claim 1, characterized in that said slant plates
(24, 70) are arranged in said hoppers (22, 64).
3. The apparatus in accordance with claim 1 or claim 2, characterized in that the
multiplicity of slant plates (24, 68, 70) inclined in the same direction are disposed
in a horizontal arrangement above flat portion (32, 66) of the bottom portions of
said treating vessel (20, 60) where said hopper (22, 64) is not disposed, and at least
one gushing nozzle (34, 74) is disposed above said flat portion (32, 66) for washing
away the sludge precipitated on said flat portion (32, 66) with the gushing liquid
into said hoppers (22, 64).
4. The apparatus in accordance with claim 3, characterized in that the angle (a, A)
formed between said slant plates (24, 68, 70) and the direction of conveyance of the
object-to-be-treated (W) is within the range of 45-90°.
1. Un appareil pour appliquer un traitement de surface pré-déterminé à un objet devant
être traite, au moyen du trempage dudit objet dans un liquide traitant contenu dans
une cuve de traitement, ledit appareil comprenant une ou plusieurs trémies (18, 22,
64) en forme d'entonnoir qui sont disposées au fond de la dite cuve de traitement
(3, 20, 60) pour recueillir la boue précipitée dans lesdites trémies (18, 22, 64),
ladite boue recueillie étant extraite de ladite cuve de traitement (3, 20, 60) par
la partie inférieure desdites trémies (18, 22, 64), caractérisé en ce que'une pluralité
de plaques en pente (24, 68, 70) inclinées dans la même direction sont disposées au
dessus du fond de ladite cuve de traitement (3, 20, 60), avec une distance prédéterminée
entre elles de sorte que la boue flottant dans ledit liquide puisse être précipitée
à travers l'espace libre entre lesdites plaques en pente (24, 68, 70) vers le fond
de ladite cuve de traitement (3, 20, 60).
2. Appareil suivant la revendication 1, caractérisé en ce que lesdites plaques en
pente (24, 70) sont disposées dans lesdites trémies (22, 64).
3. Appareil suivant la revendication 1 ou la revendication 2, caractérisé en ce que
la pluralité de plaques en pente (24, 68, 70) inclinées dans la même direction est
disposée suivant un agencement horizontal zu dessus de parties plates (32, 66) du
fond de ladite cuve de traite- . ment (20, 60) où ladite trémie (22, 64) n'est pas
disposée, et en ce qu'au moins une buse de projection (34, 74) est disposée au dessus
de ladite partie plate (32, 66) pour laver et chasser la boue précipitée sur ladite
partie plate (32, 66) avec le liquide jaillissant dans lesdites trémies (22, 64).
4. Appareil suivant la revendication 3, caractérisé en ce que l'angle (a, fJ) formé
entre lesdites plaques en pente (24, 68, 70) et la direction de transporte de l'objet
devant être traité (W) est compris dans la plage de 45-90°.
1. Vorrichtung zur Durchführung einer bestimmten Oberflächenbehandlung auf einem zu
behandelnden Objekt, indem dieses in eine in einem Verfahrenskessel enthaltende Verfahrensflüssigkeit
eingetaucht wird, wobei die Vorrichtung eine oder mehrere trichterförmige Zuführeinrichtungen
(22, 64) umfaßt, die an einem Bodenabschnitt des Verfahrenskessels (20, 60) zur Sammlung
abgesetzten Schlamms in ihnen angeordnet sind, wobei der gesammelte Schlamm vom unteren
Abschnitt der Zuführeinrichtungen (22, 64) aus dem Verfahrenskessel (20, 60) entfernt
wird, dadurch gekennzeichnet, daß eine Vielzahl von schrägen in gleicher Richtung
geneigten Platten (24, 68, 70) über dem Bodenbereich des Verfahrenskessels (20, 60)
unter einem bestimmten Abstand angeordnet sind, so daß sich der in der Flüssigkeit
schwimmende Schlamm durch den Zwischenraum zwischen den schrägen Platten (24, 68,
70) auf dem Bodenbereich des Verfahrenskessels (20, 60) absetzt.
2. Vorrichtung nach Anspruch 1, dadurch gekennzeichnet, daß die schrägen Platten (24,
70) in den Zuführeinrichtungen (22, 64) angeordnet sind.
3. Vorrichtung nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß die Vielzahl von
schrägen in gleicher Richtung geneigten Platten (24, 68, 70) horizontal über dem flachen
Abschnitt (32, 66) derjenigen Bodenbereiche des Verfahrenskessels (20, 60) angeordnet
ist, an denen die Zuführeinrichtung (22, 64) nicht angeordnet ist, und daß zumindest
eine Rieseldüse (34, 74) über dem flachen Abschnitt (32, 66) angeordnet ist, um den
auf dem flachen Abschnitt (32, 66) abgesetzten Schlamm mit der Rieselflüssigkeit in
die Zuführeinrichtungen (62, 64) zu waschen.
4. Vorrichtung nach Anspruch 3, dadurch gekennzeichnet, daß der zwischen den schrägen
Platten (24, 68, 70) und der Förderrichtung des zu behandelnden Objekts (W) gebildete
Winkel (a, β) innerhalb'des Bereichs von 45 bis 90° liegt.