Note: Descriptions are shown in the official language in which they were submitted.
5~3
BACKGROUND OF THE INVENTION
FIELD OF THE INVENTION
The present invention relates generally to the field of
electroplating systems and more specifically, to an electro-
plating system designed to operate without access to public
sewers.
PRI~R ART
With the plethora of state and federal regulations on
control of toxic materials in waste water, it has become
incumbent on plating enterprises to control the level of
materials such as cyanide, heavy metals and the like in waste
water leaving a plant. The source of the vast majority of this
~aste water is the rinse water used between the various steps in
the plating procedure. Typically, the simplest plating cycles
require three steps. These include cleaning to remove such
soiling materials as buffing compounds, stamping or cutting
lubricants and the like; an acîd dip to remove metal oxides,
often called pickling; and finally, electroplating with one or
~ore metals. Upon withdrawal of parts from each of the
~0 processing tanks used in the aforementioned plating steps, the
p~rts to be plated are covered with a film of the processing
solution commonly referred to as dragout. This material is
invariably a contaminant to the following process tank and must
be removed by water rinsing before the parts enter the following
process tank. These rinses must be constantly overflowed with
clean or cleaner water to prevent buildup in the levels of
process tank constituents
,
~5~83
so that contamination of the Eollowing process tank does
not result. Therefore, a major problem in controlling
plant effluen-t is the control of quantity and content of
the rinse waters that are generated in the plating
sequence.
The present invention solves this problem by improving
rinsing efficiency while minimizing water requirements.
Rinsing efEiciency is improved by providing air agitation
in the rinse tank to ensure that the dragout is diluted to
1~ the maximum extent consistent with the rinse volume and
the amount of dragin. In addition, the invention provides
sprays over each tank which are active during withdrawal
of the part or workpiece. This further dilutes the dragout
and provides fresh water to prevent excessive buildup of
the contaminants in the rinse water. Typically, the volume
of water through a single rinse tank has to be rather high
to keep the contaminants in the rinse water at a
sufficiently low level to be tolerated in the following
p~ocess tank. The present invention significantly reduces
~n the amount of water by multiple rinses. For example, it
can be seen in a series of three consecutive rinses that
e~ch rinse would be cleaner than the rinse ahead of it.
This makes it feasible to "backflow" the water from the
third to the second to the first rinse in each tank. As a
result, the incoming water is significantly cleaner than
the contaminant level in the tank. The contaminants in
the rinse waters are the constituents of the previous
process tank. It is therefore feasible to return water to
a previous process tank.
. ~ .
~ . ~ ~ .
1 ~Z9~i~83
The use of multiple rinses is one means for reducing the
volume of rinse water, but ordinarily in most cases, the rinse
water volume is still more than that which can be returned to
the process tank. The present invention makes room in the
process tank for these rinse waters by using an evaporator
consisting of a device for pumping the solution continuously
through a chamber designed to provide maximum surface area for
liquid. At the same time a blower provides maximum air flow
through the chamber which results in a significant amount of
1~ evaporation and makes room in the tank for the return o
backflow rinse water from the sequence of tanks.
Although there are prior art patents which disclose some of
the individual features of the present invention, no patents
have been found which disclose the specific combination of
~eatures which permit operation of a plating system without
access to public sewers.
United States Patent No. 2,984,081 to Hahn is directed to
tha cooling of
chromium plating solution and provides for a plating solution
tank in which fluid is passed through a conduit into an
evaporator.
United States Patent No. 3,616,437 to Yagishita is
directed to a system for
reclaiming plating wastes wherein a liquid rinse water is
brought into a tower where it is heated by steam in order to
partially vaporlze it. ~he vapor is then passed to an ejector
where it is introduced into cooling water to be condensed and
then brought to a reservoir.
~2~ 33
United States Patent No. 3,637,467 to Spatz is directed
to a metal reclamation process and system which uses a
primary rinse tank
and a secondary rinse tank. Liquid is drawn off through a
conduit and passed to a pump where it is brought into a reverse !
osmosis unit, the concentrate of which passes back to the
plating tank and wherein permeate is brought through a conduit
back to the primary rinse tank.
United States Patent No. 4,197,167 to Wright ~r. is
directed to a process for recovery and reuse of
metal electroplating baths. The
system includes a reservoir which is supplied with a portion of
the rinse mixture from a tank. Acid is added to the rinse
mixture in the reservoir and the rinse and acid mixture is then
recirculated through filters and back to the reservoir.
United States Patent No. 3,146,195 to Berardi is
directed to purification of water in a lobster tank
wh~xein the force of water coming
out of the tube provides an aspirating action and draws air
through the air tube and mixes the air with purified water
issuing ~rom the tube. The mixture of water and air is
projected out of the end of the submerged tube.
United States Patent No. 2,773,029 to Sebald is
directed to a water treating system in which water
is led to a primary water
softener through a water conduit which is connected to spray
valves disposed at the upper end of the softener.
None o~ these patents discloses a system which may operated
e~ficiently without any access at all to public sewers for the
disposal of the waste produced by an electroplating system.
Il ~Z~5~3
SUMMAR~ OF T~E INVENTION
-
3 The present invention comprises a plating system which can be
4 operated without acce~s to public sewers. It comprises four
principal subsystems including a nickel-chrome plating
6 subsystem, a copper-brass plating subsystem, a strip line
7 subsystem and a waste water treatment subsystemO In the
8 nickel-chrome subsystem, the only waste water produced is the
9 rlnse after an acid dip which is disposed of in an inplant
sump. Three backflow rinse cycles are provided, one for the
1 cleaning operation, one for the nickel ~latmg operat~on ~ld one
for the chrome plating operation. The number of rinses in each
3 cycle varies as the tolerance for the dragover into the
1~ following process tank varies in each case. Clean water i8
13 added to each of the last rinses from an overhead spray on a
1~ hoist which operates only on the withdrawal of parts from the
1~ - last rinse. The second subassembly, namely, the copper-brass
13 line is typically used for work limited to small parts on an
19 intermittent basis. In order to minimize rinse water carry-
~0 over, thereby keeping rinse water requirements to minimum, a
21 hang-up bar is provided over each plating tank and each rinse
12 tank This hang-up bar allows parts to drain thoroughly and
13 reduces the carry-over to the following tank. Backflow water
~ generated by two rinses progresses through a separate tank for
.~ destruction of the cyanide content of the solution by chemical
~6 oxidation accomplished by controlled addition of sodium
'7 hypochlorite. An air-water spray wand is used over the second
,~ rinse tank. The backflow water is then transferred to an
9 inplant sump for waste water evaporation after treatment in a
neutralization sump.
3~
~ i283
I The strip line assembly employs tanks which are used
2 intermittently for stripping plated metal from parts that are
3 to be replated. ~ang-up bars are provided over each strip tank
4 and each rinse tank to assure good drainage of parts. A wand
consisting of a water spray with air atomization is provided
6 for rinsing with clean water over the rinse tank. The rinses
7 are also overflowed to the water evaporation tank.
9 The waste water treatment subassembly is connected by means
lo of an inplant sump to the other suba~semblies from which waste
ll water is received. The waste water from the three other
12 subassemblies enters the inplant sump and is eventually
13 transferred to a neutralizer ~ump. ~he waste water pH level is
1~ adjusted to 7.0 to 8.0 and then it progresses through a sump
Is pump to an evaporator tank. The amount of rinse water is held
1~ to an absolute minimum in each subsystem. The contaminants in
17 the waste waters are primarily heavy metals which after cyanide
18 destruction to break the copper and brass complex, precipitate
1~ as metal hydrates. The waste water treatment 6ubsystem employs
~o a continuously operating sludge filter to remove these metal
21 hydrates along with silicates precipitated from spent cleaners
21 during neutraliza~ion. Sulfates are precipitated by the
23 addition of calculated amounts of lime. An evaporator tank is
24 maintained at a sufficiently high temperature to promote
2~ evaporation and is run continuously. The sludge is
26 accummulated as a dewatered cake and is oven dried to further
reduce water content. This cake can then be accummulated and
;O roved to a Cla~s A landf'll at periodic intervals.
31
,~' ','' '
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~ ;2~3
l OBJE~TS OF THE INVENTIO~
4 It is therefore a principal object of the present invention
to provide a plating system capable of nickel-chrome plating,
6 copper-brass plating and plate stripping without requiring
~ access to public sewers.
9 It is an additional object of the present invention to
provide an apparatus for accomplishing the typical plating
ll processes in which the quantity and content of rinse waters
12 used in the plating sequence are carefully controlled to
13 preclude a necessity for access to public sewers for disposing
14 of the waste waters.
1~
16 It is still an additional object of the present invention to
17 provide a novel electroplating facility and waste water
18 treatment combination which permits normal plating and
19 stripping operations in such a facility without generating
2~ waste rinse water which must be otherwise disposed o~ in a
~1 public sewage system~
22
~3 It is an additional object of the present invention to
2~ provide an apparatus for accomplishing typical metal plating
2~ processes in which the quantity and content of rinse waters in
26 the plating sequence are carefully controlled to preclude a
27 necessity for having access to public sewers for disposing of
28 the waste rinse waters used between the various steps in the
79 plating procedure.
3~
"
' ;;,; ~
It is still an additional object of the present invention to
, provide a metal plating facility comprising subassemblies for
3 nickel-chrome plating, copper-brass plating and plate stripping
4 while at the same time recovering waste waters used for rinsing
in the various subassemblies in a common waste water treatment
6 subassembly which permits treatment and disposal of waste water
7 effluents without requiring sewage disposal which might fall
S outside of the disposal regulations of federal, state and local
9 agencies.
In a preferred embodiment the present invention is directed
11 to an improved electroplating system comprising: at least one
1. electroplating tank for plating parts; at least one water
13 rinse tank, said plated parts being transferred from said
1~ electroplating tank to said water rinse tank; means for pro-
1~ viding a source of uncontaminated water positioned adjacent
1~ said rinse tank for (1) rinsing plated parts during a removal
1~ of said plated parts from said rinse tank and (2) inserting
1~ substantially uncontaminated water into said rinse tank for
Ig reducing the contamination level of said rinse tank; means
~0 ~ox transferring overflow water from said rinse tank to a
,1 spray positioned above said plating tank for decreasing the
contamination level of said rinse tank while removing dragout
~3 from said plated parts while they are being removed from said
.~ plating tank; and an evaporator connected to said plating
~5 tank for receiving contaminated effluent from said plating
~6 tank for disposal of said plating tank effluent without
~7 cess to puùlic sewers.
31
32
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t~
~ !
BPIEF DESCRIP~l!IOli OE Tlll: DP~WINGS
3 The aforementioned objects and advantages of the present
~ invention, as well as additional objects and advantages
thereof, will be more full~ understood hereinafter as a result
6 of a detailed description of a preferred embodiment when taken
7 in conjunction with the following drawings:
9 FIG~ l is a block diagram representation of the nickel-chrome
plating subassembly of the present invention;
ll
1~ FIG. ~ is a block diagram representation of the copper-brass
3 plating subassembly of the present invention;
14
1~ FIG. 3 is a block diagram representation of the strip line
1~ subassembly of the present invention;
1~
13 FIG. 4 is a block diagram representation of the waste water
19 treatment subassembly of the present invention; and
21 FIG. 5 is a block diagram representation of a typical
~ ckilow sequence utilized in the pre~ent invention.
77
\
3~
~2~ 3
l DETAILED DESCRIPTION OF A PREFERRED EMBODIMENT
~ Reference will first be made to FIG~ 1 which illustrates the
5 nickel-chrome pla~ing æubassembly of the pxesent invention.
6 Each separa~e rectangle represents a functional operation of
7 the nickel-chrome plating sequence used in the present
i invention and also represents a tank which constitutes a
g portion of the subassembly apparatus for accomplishing the
lo method of ~he present invention. Metal parts to be plated are
loaded on the left side of the subassembly and placed in the
12 first tank 12 which compri~es a soak cleaner for removing
13 caked-on dirt from the parts to be plated as well as such soils
14 as buffing compound~, stamping or cutting lubricants and the
l~ like. The parts are subsequently placed in an electrocleaner
l6 14 for further removal of organic materials. Generally
l7 speaking, the purpose o~ the soak cleaning and electrocleaning
l8 tanks 12 and 14 is to dislodge all foreign materials on the
l9 parts to be electroplated.
~o
~l The next two tanks in the sequence of nickel-chrome
22 subassembly 10 are rinse and spray tanks 16 and 18. Upon the
~3 withdrawal of parts from each of the processing tanks, the
,~ parts to be plated are covered with a film of the processing
solution, commonly referred to as dragout. This material is
26 invariably a contaminant to the following process tank and must
27 be removed by water rinsing before the parts enter the
~8 following process tank. ~hese rinses must be constantly
~9 overflowed with clean or cleaner water to prevent buildup in
the levels of process tank constituents, otherwise
3l contamination of the following process tank will result. In
3~ order to make the rinsing efficiency high while reducing the
11
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,.,~ '; ~,:
i~ . ,.,~ i
~52~3
l water requirements, each rinse tank is provided with a source
2 of air agitation to engure that the dragout film is diluted to
3 the maximum consis~ent with the rinse volume and the amount of
4 dragin. ~urthermore, overhead sprays are provided in some
s cases and these sprays are active over the tank during
6 withdrawal o~ the part. This further dilutes the dragout film
~ and provides fresh water to prevent excessive buildup of
8 contaminants in ~he rinse wa~er. In the present invention the
g amount of water used ~or rinses is greatly reduced by utilizing
multiple rinses. By way of exxmple, it can be seen that in a
series of three rinses, each rinse would be cleaner than the
12 rinse ahead of it~ This makes it feasible to backflow the
13 water for example, from a third rinse to a preceding second
14 rinse and in turn to a preceding first rinse, in a series of
three rinse tanks As a result, the incoming water in each
16 tank is si~nificantly cleaner than the contaminant level in
17 that particular tank. To illustrate, in a rinse sequence which
18 would normally reguire 27 gallons of water an hour in a single
19 rinse to keep contaminants at an acceptable level, a double
rinse would require only 9 gallons per hour and a triple rinse
21 would require only 3 gallons per hour.
2~
23 It can be understood from the above discussion that the so
24 called acontaminants" in the rinse waters are the necessary
constituents of the previous process tank. It is therefore
26 feasible to return that water to the previous process tank, and
27 reducing the volume of rinse water by using multiple rinses is
28 one of the features of the present invention that renders it
2g possible to preclude the need for access to public sewers.
This multiple rinsing and backflow technique i~ utilized in the
31 nickel-chrome subassembly of FIG. l. More specifically, as
32 seen in FIG. l, the cleaner rinse water of tank 18 is
12
,i '"", ?,
i ., . !
~ Z~%83
l back~lowed to the more contaminated rinse water of tank 16
2 which is in turn backflowed to the even more contaminated
3 solution of electrocleaner tank 14. ~n order to permit the
4 backflow process and ~till leave room in the process tank for
these rinse waters, an evaporator is used at critical points in
the process of each subassembly. For example, in the
7 subassembly of FIG. 1 an 80 gallon per hour evaporator unit 20
8 is connected to electrocleaner 14. Evaporator 20 comprises a
~ device for pumpiny the solution of electrocleaner tank 14
lo continuously through a chamber designed to provide maximum area
1l for the liquid. At the same time a blower provides maximum air
l~ flow through the chamber and combined with the surface area of
t3 the chamber, provides the level of evaporation required for
J4 that particular processing tank. The back water flow from
1~ rinse tank 18 is replenished by rinse water from an overhead
l6 hoist spray which remains active during withdrawal of the work.
l7 The hoist spray dilutes the dragout film and provides fresh
l8 water to prevent excessive buildup of the contaminants in the
l~ rinse water.
~0
~l After the part to be plated is removed from electrocleaner
2~ 14, it is placed in rinse tank 16 and subsequen~ly in rinse
~3 tank 18. Thereafter it is placed in an acid dip tank 22. The
~ acld dip process, often called pickling, is designed to remove
.~ metal oxides from the part. It also removes rust, scale and
26 other inorganic coatings that still adhere to the metal after
27 the soak and electrocleaning proce~es are completed. After
~8 the part is removed from the acid dip tank 22 it is transferred
~9 to the rinse and spray tank 24. Rinse and spray tank 24 is the
only tank in the nickel-chrome æubassembly which produces waste
3l water in the form of an overflow which is transferred to the
3~ waste sump of the waste water treatment subassembly to be
13
` #~ J~ i
l discussed hereinafter in conjunction with FIG. 4. The water in
2 rinse and spray tank 24 is replenished by the overhead rinse
3 water from the hoi~t spray above the tank which also keeps the
4 level of contaminants in rinse and spray tank 24 to a minimum.
s
6 Rinse and spray tank 24 completes the portion of the nickel-
7 chrome subassembly 10 which is devoted to cleaning the part to
8 be plated. The part is next transferred to the nickel-plate
9 tank 26. The backflow process previously described in
lo conjunction with rinse and spray tanks 16 and 18 and
electrQcleaner tank 14 is again employed in the nickel plating
12 portion of the nickel-chrome subassembly. More specifically,13 as seen in FIG. 1, the nickel plating tank 26 is followed bythree water cleaning tanks, namely, rinse and spray tank 28,
rinse and spray tank 30 and rinse tank 32. Rinse tank 32,
l6 which has the lowest level of contaminants of the three rinse
17 tanks ollowing the nickel plate tank 26, has its water
18 constantly replenished by rinse water applied from the overhead
Is hoist spray. The overflow from rinse tank 32 is backflowed
~o into rinse and spray tank 30 and the overflow from rinse and~l spray tank 30 is backflowed into rinse and spray tank 28.
~2 Finally, the overflow from rin~e and spray tank 28 is back-
~3 10wed into the nickel plating tank 26 which is connected to an
evaporator 34 which operates in the same manner as previously
2i described for evaporator 20. In this particular embodiment,
26 the evaporator 34 has a 60 gallon per hour capacity. The
27 number of rinses in each cycle varies as the tolerance for the
28 dragover to the following proce~s tank varies in each case.
29 The clean water added to each of the last rinses comes from a
spray on the hoist which operates only on the withdrawal of the
3l parts from the last rinse. This relates the rinse water volume
32 directly to the number of parts being processed.
14
' ',''' /, ,
' !
~2~ 33
When the nickel plating process i8 used as an undercoating
~ for chromium plating, the parts that are removed from rinse
3 tank 32 are thereaf~er placed in the chrome plating tank 36
which employs a two-stage rinsing process represented by rinse
and spray tank 38 and rinse tank 40. The rinse water in rinse
6 tank 40 is replenished by the overhead hoist spray and the
7 overflow is channeled to the rinse and spray tank 38. The
8 overflow from rinse and spray tank 38 is channeled back to the
~ chrome plate tank 36 and the overflow ~rom chrome plate tank 36
is disposed of in evaporator 42 which in the particular
~I embodiment illustrated, has a 16 gallon per hour capacity.
1~
13 In the case of tubular or other hollow parts, the spray
l~ rinses are effective only on the outside surfaces of the work.
l~ Therefore, it is preferable to double dip these parts in rinses
l6 with sufficient time between these dips to allow complete
l7 drainage. This ensures maximum possible dilution of the dragin
l8 of the process solution which is carried by the parts. Return
l~ of the dragout to each of the process tanks can result in the
~0 buildup of impurities in the process tanks. However, methods
~1 are available to control the level of these impurities in the
~2 process tanks. For example, organic impurities in the nickel
~3 plating tank are controlled b~ continuous activated carbon
2~ filtration and metallic impurities can be controlled by high pH
2~ filtration or by low current density electrolytic
~6 purifications. Similar steps are employed to control the level
~7 of impurities in the trivalent chrome solution of chrome
.~ plating tank 36. The cleaning portion of subassembly 10
'9 accummulates soil6 which fall into two cla~se , solids which
settle into the bottom of the tank and oils and greases which
3l float on the surface of the tank. Surface contaminan~s are
3~ removed by periodic skimming of the tank and solids are removed
, ' . , : .
:.
~ 3
when the spent solution is removed to the sump tank for
~ disposal as hereina~ter described.
4 Reference will now be made to FIG. 2 which illustrates the
, copper-brass subassembly of the present invention. Plating in
6 the copper-brass subassembly is typically limited to small
7 parts on an intermittent basis. Therefore the cost of
~ evaporating the brass tank and the copper tank and providing
9 separate rinse cycles is not generally justified. These rinses
lo therefore are run continuously while work is in process. In
Il order to minimize carry-over thereby keeping rinse water
l~ requirements to a minimum, a hang-up bar is provided over each
l3 plating tank and each rinse tank. This allows the parts to
l~ drain thoroughly and reduces the carry-over into the following
l~ tanks. Parts to be copper or brass plated or gold and silver
1~ plated are transferred to the copper-brass subassembly,
l7 typically from the rinse and spray tank 24 of the nickel-chrome
l~ subassembly. Thus, for example, a part which is to be copper
1~ plated either a an external plating layer or as an
~0 undercoating for other metal platingt is transferred to copper
.1 plate tank 44. After the copper plating process has been
completed, the part is transferred to the rinse tank 46 and
en ~lnRe tank 48.
~8
3_
16
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-~ ~z~ 3
The backflow process for reducing contaminants is provided in
~ the copper-brass subassembly between rinse tank 48 and rinse
3 tank 46. After backflowinq through two rinses, the water
~ progresses through a separate tank 50 for destruction of the
5 cyanide content of the solution~ This chemical oxidation is
6 accomplished by controlled addition of sodium hypochlorite.
7 The overflow water is ~hen trans~erred to the was~e water
8 treatment subassembly through the inplant sump ~o be described
9 hereinafter in conjunction with FIG. 4. Brass plating may also
lo be accomplished by means of brass plate tank 52, silver plating
is accomplished in silver plate tank 54 and gold plating is
accomplished in gold plate tank 56~ Because of the value of
3 the metal involved in the gold plating process, the gold plated
parts are transferred first to a gold rinse tank 58 from which
l~ dissolved gold can be recovered prior to transferring the parts
l6 to rinse tank 46 and rinse tank 48 as previously described. An
l7 air-water spray wand is used over the second rinse tank.
l8
19 The strip line subassembly of the present invention is shown
in FIG. 3. The tanks in this line are used intermittently for
~1 stripping plated metal from rejects or from worn parts that are
22 to be replated. Therefore, it iB not usually economically
~3 feasible to provide evaporators or multiple rinses for each
24 tank in this subassembly. Accordingly, hang-up bars are
2~ provided over each tank and each rinse tank to ensure good
26 drainage of the parts. A wand consisting of a water spra~ with
~7 air atomization is provided for rinsing with clean water over
28 the rinse tank. The methods for stripping previously plated
29 parts for replating vary with the metal to be stripped. Some
methods involve purely chemical reactions and some involve
31 making the part anodic in a proce~ that i8 substantially the
32 reverse of the electroplating process. Thus, strip line
17
~ 83
l subassembly 60 of FIG. 3 is provided with a muriatic strip tank
2 62, a pair of reverse sulfuric strip ~anks 64 and 66 and a
3 reverse caustic strip tank 68. In addition, three rinse tanks
are provided including rinse tank 70, rinse tank 72 and rinse
tank 74. Rinse tank 70 is used primarily for rinsing the part
6 after muriatic strip treatment and rinse tanks 72 and 74 are
7 employed to rinse the part after reverse treatment in either
reverse sulfuric strip tanks 64 and 66 or reverse caustic tank
~ 68. Rinse tank 72 and 74 employ the previously described
lo backflow process similar to that employed in nickel-chrome
subassembly 10 of FIG. 1. Each rinse tank is connected to
1~ appropriate plumbing for channeling the waste water to the
13 inplant waste sump of the waste water treatment subassembly of
1~ FIG. 4 which will now be described.
1~
18 Waste water treatment subassembly 80 comprises an inplant
17 sump 82, a neutralization sump 84 and a waste water evaporation
18 tank 86 to which is connected a sludge filter 88 and an
19 evaporator 89 and a spent cleaner dump 90. All o~ the various
~o rinses described in conjunction with the subassemblies of
~1 FIGs. 1, 2 and 3 are overflowed through the inplant sump 82 and
22 neutralization sump 84 to water evaporation tank 86. Inplant
23 sump 82 collects the waste water from all of the subassemblies
~ and pumps it to the neutralization sump 84. ~eutralization
2~ sump 84 adjusts the pH level of the waste water so that it is
26 within the range of 7.0 to 7.5. Then a pump transfers the
27 neutralized waste water to waste water evaporation tank 86.
28 The amount of rinse water i8 held to an absolute minimum by the
~9 methods described above in conjunction with FIGs. 1, 2 and 3.
The contaminants in these waters will typically be primarily
31 heavy metals while the output of cyanide destruction tank 50 of
3~ subassembly 43 of FIG. 2, which breaks the copper and brass
18
~ !
2 ~3
l complex, precipitates contaminants as metal hydrates. Spent
2 cleaner dump 90 is u~ilized to collect ~he spent cleaners
3 during neutralization. A continuously operational sludge
4 filter 88 removes the heavy metals, metal hydrates along with
silicates precipitated from spent cleaners during
6 neutralization. Sulfates are precipitated by the addition of
7 calculated amounts of lime. Evaporation tank 86 is maintained
at a temperature of 160 degrees Fahrenheit with evaporator 89
running continuously at a capacity in the preferred embodiment
o hereof of 80 gallons per hour. Sludge is accu~mulated as a
dewatered cake and is oven dried to further reduce water
l content. This cake is accummulated and removed to a Class A
13 landfill at periodic interval~.
1~
FIG. 5 represents in generalized form, one of the features of
l6 the present invention. More specifically, FIG. 5 illustrates a
l7 typical backflow sequence which enables the electroplating
8 system of the present invention to operate without the need for
s access to public sewers. As shown in FIG. 5, there is
~o typically a tank devoted to the plating operation followed by a
.1 plurality of tanks devoted to rinsing operations. Thus, shown
22 in FIG. 5 is a plating tank 100, a first rinse tank 102 and a
~3 second rinse tank 104. Second rinse tank 104 receives fresh
24 water replenishment from a suitable source such as an overhead
2~ spray line 106 as shown in FIG. 5. The water from second rinse
26 tank 104 is backflowed to first rinse tank 102, the water in
27 which is backflowed into the plating tank 100. The overflow
28 from plating tank 100 is pumped into an evaporator 108 which is
29 designed to provide a minimum required level of evaporation of
the overflow water from the plating tank as a means for
31 disposal thereof. Except for the second rinse tank 104 which
32 receives a pure water hois~ spray from source 106, ~he backflow
19
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~ ~2~83
1 to the two preceding tanks 102 and 100 i8 typically provided in
2 the form of an overhead spray of aerated water from a
3 stationary tank source that is less contaminated than the water
4 contained within the tank over which the spray is situated as
shown in FIG. 5. In this manner, the part and the accompanying
6 dragout adhering to each part as it is removed from a tank, are
7 subjected to a spray rinse of water which is purer than the
8 water in which the part has been sitting while residing in the
g tank.
ll It will now be understood that what has been disclosed herein
12 comprises a novel and highly advantageous electroplating system
13 which does not require access to public sewage systems for
1~ disposal of waste water. Two unique features of this system
l~ make it possible to process metal parts for electroplating
16 through the present invention without that requirement. More
1~ specifically, one such feature involves the care~ul control and
18 high efficiency use of input water by use of overhead sprays,
19 backflows and evaporator units. The other such feature is
employed in the form of a water water treatment subassembly
21 wherein waste water for whicb it would not be economically
22 feasible to provide an evaporator to dispose thereof with
23 respect to each individual source in the plating process, is
2~ directed to an inplant sump, a neutralization sump and
as eventually to a unitary waste water evaporation tank which
26 utilizes its own evaporator unit for disposing of the common
27 nte water.
31
32
~LZ~35~83
Those having skill in the art to which the present invention
~ pertains will now perceive of various modifications and
3 additions which can be made to the invention. By way of
4 examplet the general features disclosed herein may be used
advantageously in other forms of elec~roplating assemblies for
6 plating metals other than those specifically shown as examples
7 herein. However, it will be understood that all such
modifications and additions are deemed to be within ~he scope
~ of the present invention which is to be limited only by the
lo claims appended hereto.
Il
¦ We claim:
.~
79
37
21
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