Cleaning apparatus having a partitioned boil sump

In a cleaning apparatus, a boil sump containing a cleaning solvent within four sidewalls and a bottom. Additionally, the boil sump has a partition extending between two opposing sidewalls that separates the boil sump into a boiling compartment and a cleaning compartment. Furthermore, the partition contains a conduit therethrough that permits the solvent to flow between the cleaning and boiling compartments. The boiling compartment contains a heater that heats the solvent to a boil while the cleaning compartment contains an ultrasonic transducer array for ultrasonically cleaning an object placed in the cleaning compartment. In addition to the boil sump, the cleaning apparatus contains a rinsing compartment for rinsing an object that has been cleaned in the cleaning compartment. The boil sump, as well as the rinsing compartment, are contained in a single, enclosed chamber within the cleaning apparatus.

BACKGROUND OF THE DISCLOSURE 
1. Field of the Invention 
The invention relates to cleaning apparatus and more particularly, to 
cleaning apparatus that contains a partitioned boil sump. 
2. Description of the Prior Art 
Conventional apparatus for cleaning objects, such as piece parts of 
manufactured goods, circuit boards, screws, bolts, nuts, and the like, 
typically use a multi-stage cleaning process in which an object is 
sequentially immersed in a series of chambers or tanks. Typically, these 
tanks contain a single solvent and, as such, the apparatus is known as a 
mono-solvent cleaning apparatus. Furthermore, conventional apparatus 
continuously cleanses the solvent during operation of the apparatus using 
a distilling process. Such distilling processes use a distinct boil sump 
to boil the solvent into a vapor and a condenser to condense the vapor 
into the solvent solution. The boil sump is generally separate from the 
tanks used for cleaning and rinsing an object. 
Conventional solvents used for degreasing and cleaning metal and other 
non-absorbent objects include 1,1,1-trichloroethane, trichloroethylene, 
perchloroethylene, methylene chloride and the like. However, these 
solvents are suspected of depleting the earth's ozone layer. Consequently, 
so-called "ozone safe" solvents have recently been used in commercial 
cleaning apparatus. Illustratively, volatile solvents that are ozone safe 
include perflourocarbons (PFCs) and hydroflourocarbons (HFCs). 
Additionally, non-volatile, ozone safe solvents include hydrocarbon-based 
products such as dimethylsiloxane produced by DOW Chemical of Midland, 
Mich. and AXEREL produced by E. I. duPont de Nemours and Company of 
Wilmington, Del. 
A typical cleaning apparatus using a multi-stage, single solvent cleaning 
process is disclosed in U.S. Pat. No. 4,886,082 issued Dec. 12, 1989 to S. 
Kato et al. (the '082 Kato et al. patent). This patent specifically 
teaches a three stage process by which objects are cleaned in three 
separate tanks of solvent. 
To clean an object in accordance with the teachings of the '082 Kato et al. 
patent, the object is first placed in a vapor cleaning tank wherein a 
solvent is heated above its boiling point and the vapor of the solvent 
cleans the object. The object is not immersed in the solvent itself, but 
rather is positioned above the boiling liquid solvent. 
After vapor cleaning for a pre-defined duration, the object is moved from 
the vapor cleaning tank to an ultrasonic cleaning tank. The vapor cleaning 
tank and the ultrasonic cleaning tank contain the same solvent. The object 
is immersed in the liquid solvent contained in the ultrasonic cleaning 
tank and ultrasonic transducers located at the bottom of the tank apply 
ultrasonic waves to the solvent. As is well known in the art, ultrasonic 
cavitation of the solution caused by the ultrasonic waves removes 
particulate material from the object. 
Lastly, the cleaning process taught by the '082 Kato et al. patent teaches 
immersing the object into a liquid solvent in a rinse tank. The solvent 
contained in the rinse tank is the same solvent as that used in the vapor 
cleaning and ultrasonic cleaning tanks. The object, now that it is clean, 
is then removed from the cleaning apparatus and air dried. 
To continuously cleanse the solvent while it is used in the cleaning 
apparatus, the '082 Kato et al. patent teaches continuously removing a 
portion of the solvent from the vapor cleaning tank and channeling the 
removed solvent to a separate distilling tank, also known in the art as a 
boil sump. In the distilling tank, the solvent is heated to a boil to 
produce solvent vapor. A condenser, located above the distilling tank and 
maintained at a temperature substantially below the boiling point of the 
solvent, condenses the solvent vapor into a solution. The solvent solution 
is channeled from the condenser into the rinse tank. The rinse tank is 
separated from the ultrasonic tank by a spillway that enables the solvent 
from the rinse tank to overflow into the ultrasonic cleaning tank. A 
conduit connects the ultrasonic tank to the vapor cleaning tank to provide 
solvent thereto. Lastly, the vapor cleaning tank is connected, via a 
conduit, to the distilling tank. As such, a closed system is produced that 
requires the solvent to sequentially circulate through each of the tanks 
and ultimately be boiled in the distilling tank before recirculation. 
Therefore, particulate contaminants, grease and oil contained in the 
solvent solution are continuously removed from the solvent by the 
distilling process and those contaminants remain in the distilling tank. 
The '082 Kato et al. patent teaches using a distinct distilling tank that 
is separate from the cleaning and rinsing tanks. To reduce the footprint 
of the cleaning apparatus and, also, simplify the overall design thereof, 
it would be advantageous to have a single tank that can be used for both 
ultrasonic cleaning of objects and distilling the solvent, i.e., an 
integrated cleaning and distilling tank. 
Furthermore, in cleaning some objects, a single solvent is not sufficient 
and two different solvents, i.e., co-solvent cleaning, must be used to 
facilitate complete cleansing of the object. For example, some types of 
grease and oils are best removed by a non-volatile hydrocarbon-based 
solvent. However, such non-volatile solvents do not dry very quickly and 
may not remove all forms of contaminants from the object. Moreover, when 
air dried, a non-volatile solvent may leave a solid residue on the object. 
Therefore, a second solvent, typically a volatile solvent, is used to 
remove the residual non-volatile solvent from the object and also remove 
any remaining oils, greases or particulate matter not removed from the 
object by the non-volatile solvent. Advantageously, volatile solvents dry 
by evaporation in a relatively short period of time. Thus, a co-solvent 
cleaning process removes a variety of particulate matter, grease and oil 
from an object as well as produce a dry object within a relatively short 
period of time. Thus, it would be also advantageous to have a cleaning 
apparatus that is capable of both mono-solvent and co-solvent cleaning 
operations. 
Therefore, a need exists in the art for a single cleaning apparatus having 
a distilling tank that is an integral portion of the cleaning tank and 
that performs both mono-solvent and co-solvent cleaning. 
SUMMARY OF THE INVENTION 
Our invention advantageously overcomes the disadvantages heretofore 
associated with cleaning apparatus. Specifically, our invention contains a 
single boil sump that is partitioned into a boiling compartment and a 
cleaning compartment, i.e., contains integrated distilling and cleaning 
compartments. Furthermore, through our invention, either one solvent 
(mono-solvent operation) or two solvents (co-solvent operation) can be 
used in a single cleaning apparatus. In mono-solvent operation, one 
solvent is used for both cleaning and rinsing of an objection. In 
co-solvent operation, an object is first cleaned in a first solvent, then 
rinsed in a second solvent to remove residual first solvent from the 
object. To facilitate optimal cleaning, ultrasonic cleaning techniques are 
used during both cleaning and rinsing of the object. Additionally, to 
maintain a clean solvent in mono-solvent operation or a clean second 
(rinsing) solvent in co-solvent operation, the solvent is continuously 
cleaned using a distilling process. 
More specifically, our inventive cleaning apparatus contains a single 
chamber having two portions. The two portions are a boil sump and a 
rinsing compartment. The boil sump is adjacent the rinsing compartment and 
separated therefrom by a first wall portion. The boil sump is partitioned 
by a second wall portion into a boiling compartment and a cleaning 
compartment. The second wall portion contains at least one conduit 
therethrough connecting the cleaning compartment to the boiling 
compartment. 
During co-solvent operation, the second solvent is contained in both the 
boiling and cleaning compartments and flows through the conduit 
therebetween. The first solvent, having a density that is less than the 
density of the second solvent and a boiling point that is higher than the 
boiling point of the second solvent, is also contained in both the boiling 
and cleaning compartments. Consequently, the first solvent floats above 
the second solvent and has a level that exceeds a height of the second 
wall portion separating the boiling and cleaning compartments. Thus, both 
the first and second solvents flow between the boiling and cleaning 
compartments within the boil sump. 
A heater, typically an electric heating element, is located in the boiling 
compartment in contact with the second solvent. The heater increases the 
temperature of the second solvent above its boiling point to produce a 
second solvent vapor. Furthermore, the heater temperature is controlled 
such that the temperature of the second solvent remains below the boiling 
point of the first solvent. Thus, only second solvent vapor is produced. 
As such, the second solvent vapor rises through the first solvent and into 
a vapor space above the compartments. The vapor space has a bottom defined 
by the compartments, four sides defined by four sidewalls of the 
apparatus, and a top defined by a vapor barrier. The vapor barrier is 
produced by a condenser that surrounds an opening to the chamber and cools 
the vapor in the opening below its boiling point to produce condensed 
second solvent vapor, i.e., the condenser reproduces the second solvent. A 
trough, connected to the condenser and also surrounding the opening to the 
chamber, channels the condensed second solvent into a water separator that 
removes water from the second solvent. Once the water is removed, a 
conduit carries the second solvent into the rinsing compartment. Once 
filled, the solvent in the rinsing compartment cascades over the first 
wall portion into the cleaning compartment of the boil sump. The second 
solvent then flows back into the boiling compartment via the conduit 
between the cleaning and boiling compartments. In this manner, the 
apparatus provides a closed distillation process that cleanses the second 
solvent. Consequently, the second solvent is continuously distilled to 
produce clean second solvent for the rinsing compartment and contaminants 
are collected in the boiling compartment. 
In operation, to clean an object using two solvents, the object is first 
immersed into the first solvent contained in the cleaning compartment and 
is thereafter rinsed by immersing the object into the second solvent 
contained in the rinsing compartment. Typically, the first solvent is a 
non-volatile solvent. As such, the solvent will not dry quickly after the 
object is removed from the cleaning compartment. Additionally, 
non-volatile solvents may leave unwanted residue on the object after 
drying. To alleviate these problems, the second solvent is typically a 
volatile solvent that removes any residue of the first solvent from the 
object. After a pre-defined duration, the object is removed from the 
second solvent and allowed to dry. Since the first solvent is volatile, 
the drying time is relatively short. 
To facilitate improved cleaning of the object, an array of ultrasonic 
transducers is located at the bottom of both the cleaning and rinsing 
compartments. By generating ultrasonic cavitation within the solvents, the 
object is cleaned to a greater extent than without using ultrasonic 
cleaning. 
During mono-solvent operation, the first solvent is not used and the second 
solvent, typically a volatile solvent, is used to clean as well as rinse 
the object.

DETAILED DESCRIPTION 
Our cleaning apparatus performs a multi-step cleaning process using either 
one or two solvents. To facilitate understanding of our invention, first 
the apparatus is described as used with two solvents (co-solvent 
operation); then we describe the apparatus as used with one solvent 
(mono-solvent operation). 
FIG. 1 shows a section view of our inventive cleaning apparatus during 
co-solvent operation; while FIG. 2 depicts a top plan view of chamber 122 
within apparatus 100 shown in FIG. 1. To best understand the 
implementation and operation of the cleaning apparatus during co-solvent 
operation, the reader should simultaneously consult both FIGS. 1 and 2. 
The entire cleaning process is accomplished by apparatus and solvents 
contained within a single, enclosed chamber. During co-solvent operation 
of the apparatus, one solvent is used in a cleaning step of the cleaning 
process and another solvent is used in a rinsing step. Additionally, using 
a distilling process, the cleaning apparatus continuously cleans the 
solvent used in the rinsing step. Furthermore, to optimize the cleaning 
process, the apparatus uses an ultrasonic cleaning technique during both 
the cleaning and rinsing steps. 
Specifically, cleaning apparatus 100 contains chamber 122, solvent A 
filtration module 102, solvent B filtration module 184, chiller module 116 
and heating module 112. Chamber 122 contains two portions; boil sump 123 
and rinsing compartment 148. The boil sump is further partitioned into 
boiling compartment 124 and cleaning compartment 132. In operation, 
cleaning compartment 132 performs object cleaning using solvent A, rinsing 
compartment 148 performs object rinsing using solvent B, and boiling 
compartment 124 facilitates continuously cleansing solvent B during 
operation of the apparatus. Moreover, compartments 132 and 148, 
respectively, contain ultrasonic transducer arrays 138 and 140. Leads 142 
and 144 connect each ultrasonic array to ultrasonic array power supply 
146. Additionally, boiling compartment 124 contains heating element 126 
connected, via leads 114, to heating module 112 such that solvent B is 
heated to a boil. Proximate to the top of the chamber and surrounding an 
opening therein are a plurality of condensing coils 160 that are supplied 
with a refrigerant by chiller module 116. These coils produce a vapor 
barrier that confines solvent B vapor to the chamber. As such, condensing 
coils 160 condense the solvent B vapor and, subsequently, trough 162 
channels the condensed vapor into water separator 172. Solvent B is then 
reintroduced into chamber 122 via conduit 178 connecting water separator 
172 to rinsing compartment 148. 
Although non-ozone safe solvents can be used in our inventive cleaning 
apparatus, current industry trends suggest such solvents will be replaced 
with ozone safe solvents. In view of this trend, our inventive apparatus 
is described using ozone safe solvents. Specifically, the cleaning solvent 
(solvent A) is typically a non-volatile solvent such as a 
hydrocarbon-based solvent and the rinsing solvent (solvent B) is typically 
a volatile solvent such as a perflourocarbon solvent. Generally speaking, 
the two solvents are not miscible. For example, solvent A is AXEREL-9000 
and solvent B is VERTREL 245 both manufactured by E. I. duPont de Nemours 
of Wilmington, Del. Alternatively, the hydrocarbon-based, non-volatile 
solvent could be a dimethylsiloxane such as OS-30 produced by DOW Chemical 
of Midland, Mich. and the perflourocarbon could be PF-5070 produced by 
Minnesota Mining and Manufacturing (3M) Industrial Chemical Products 
Division of St. Paul, Minn. Generally speaking, these solvents are 
manufactured in a variety of forms that have various boiling points and 
vapor pressures. Those skilled in the art would be able to select an 
appropriate solvent for cleaning a specific object. For the remainder of 
this discussion, it is assumed that the apparatus is using PF-5070 as the 
rinsing solvent (solvent B) and AXEREL-9000 as the cleaning solvent 
(solvent A). Empirical studies have shown that the PF-5070 is only 2% 
miscible with AXEREL-9000. As such, the two solvents remain separate when 
contained in the boil sump such that AXEREL-9000, being lighter than 
PF-5070, floats above the PF-5070. 
More specifically, boil sump 123 contains four sidewalls 125, 127, 129, 131 
and bottom 133. Within boil sump 123, boiling compartment 124 is adjacent 
to and separated from cleaning compartment 132 by wall portion 128 that 
connects sidewall 127 to sidewall 131. Additionally, boil sump 123 is 
adjacent to and separated from rinsing compartment 148 by wall portion 
136. To clearly identify the two wall portions, hereinafter wall portion 
136 is referred to as the first wall portion and wall portion 128 is 
referred to as the second wall portion. 
Second wall portion 128 contains conduit 130 that connects compartments 124 
and 132. Conduit 130 is located below the fluid level of solvent B such 
that the solvent flows through the conduit from the cleaning compartment 
to the boiling compartment. As such, the fluid level of solvent B is equal 
in both compartments of the boil sump. 
The boiling compartment contains heater 126 that is connected, via leads 
114, to heater module 112. The heater module supplies a controlled 
electric current to the heating element of the heater. The heater 
increases the temperature of solvent B above its boiling point, i.e., 
above 173 degrees F. for PF-5070, but not above the boiling point of 
solvent A, i.e., not greater than 200 degrees F. for AXEREL-9000. 
Consequently, solvent B boils into a vapor that passes through solvent A 
and into chamber 122. The vapor is contained within vapor space 168 by the 
sidewalls of apparatus 100, by the surface of the solvent A in the boil 
sump and solvent B in the rinse compartment, and by vapor barrier 158. 
Vapor barrier 158 is established by refrigeration coils 160 which surround 
an opening into chamber 122. Chiller module 116 provides refrigerant, via 
conduits 118, to coils 160 such that the air at the vapor barrier is 
cooled to approximately -20 degrees F. Consequently, at the vapor barrier, 
solvent B vapor condenses upon refrigeration coils 160. Trough 162 is 
located below the coils and also surrounds the opening into chamber 122. 
The condensed vapor from the coils drips into trough 162 and conduit 176 
channels the liquid into water separator 172 located in housing 170. The 
water separator is a holding tank wherein water (indicated by reference 
number 174) separates from the condensed solvent B vapor. For example, 
since PF-5070 has a density of 1.73 gm/cc, water, having a density of 1 
gm/cc, floats on the PF-5070. Consequently, PF-5070 can be easily 
separated from water. Solvent B is removed from the water separator via 
conduit 178 and reintroduced into rinsing compartment 148 within chamber 
122. Using the boiling-condensing process described above, i.e., a 
distilling process, any particulate contaminants contained in solvent B 
accumulate in the boiling compartment of the boil sump. Thus, relatively 
clean solvent B is continuously introduced into the rinsing compartment. 
The introduction of solvent B into the rinsing compartment raises the fluid 
level within this compartment. As the level of solvent B rises above first 
wall portion 136, solvent B cascades over the wall portion into cleaning 
compartment 132 of boil sump 123. In this compartment, solvent B sinks 
below solvent A. Subsequently, as solvent B is boiled into a vapor within 
boiling compartment 124, solvent B flows through conduit 130 into boiling 
compartment 124. From this compartment, the distilling process 
continuously cleans solvent B and reintroduces the solvent into the 
rinsing compartment. 
Additionally, to further cleanse solvent B, filtration module 184 is 
provided. This module contains pump 190, filter 186 and heat exchanger 
188. The pump continuously circulates solvent B from the rinsing 
compartment via conduit 180, through the filter, and back to the rinsing 
compartment via conduit 182. In series with the filter and pump is heat 
exchanger 188. The heat exchanger maintains the temperature of solvent B 
in the rinsing compartment well below its boiling point. For example, the 
temperature of PF-5070 when used as solvent B is maintained at 
approximately 150 degrees F. Additionally, the continuous circulation of 
the solvent minimizes possible temperature gradients within the rinsing 
solvent. Any such temperature gradients would detrimentally impact the 
ultrasonic cavitation within the solvent. 
Additionally, to ensure that the oils, greases, and residual solvent A flow 
over first wall portion 136, pump 181 generates a current across the 
surface of solvent B. Pump 181 intermittently removes solvent from the 
rinsing compartment via conduit 185. Specifically, the pump is activated 
after an object has been removed from the rinsing compartment, i.e., 
whenever contaminants are floating in the rinsing compartment. When 
activated, pump 181 transfers the removed solvent back to the rinsing 
compartment via conduit 183. Sparge 192 connects conduit 183 to rinsing 
compartment 148. The sparge is located in the wall of the compartment at 
the highest level of solvent such that, as fluid exits the sparge, it 
produces a current across the surface of the solvent. As such, oils, 
greases, and residual solvent A that float on the surface of solvent B are 
urged to flow over first wall portion 136. Thus, solvent B in the rinsing 
compartment remains relatively free of contaminants. 
Solvent A is contained in both the boiling compartment and the cleaning 
compartment. Solvent A is provided at such a fluid level that it freely 
flows between the two chambers over second wall portion 128. Typically, 
enough solvent A is contained in the two compartments to absorb oil and 
particulate matter produced while cleaning an object in solvent A. 
Alternatively, the level of solvent A can be maintained below the height 
of the second wall portion and the two compartments connected to one 
another by one or more conduits 130' or 130". Such a conduit connection 
can be produced either through the second wall portion or around the wall 
portion using plumbing. 
Filtration module 102 provides cleansing for solvent A. Module 102 contains 
filter 105 and pump 104 connected to the boiling chamber by conduits 108 
and 110. The pump continuously circulates solvent A through the filter 
such that the filter removes particulate matter from the solvent. 
Ultrasonic arrays 138 and 140 are "off-the-shelf" components. 
Illustratively, model VIBRA-BAR manufactured by Crest Ultrasonics 
Corporation of Trenton, N.J. is an appropriate array for use in both 
chambers. Additionally, illustrative power supplies also manufactured by 
Crest Ultrasonics Corporation include models 4G-250-3-WSA and 
4G-500-6-WSA. Use of such arrays and their associated power supplies is 
old in the art and needs no further explanation to understand the 
operation of the invention. 
The close proximity of the boiling compartment to the cleaning compartment 
and the conduit connection between these two compartments could cause the 
temperature of solvent B in the cleaning compartment to exceed its boiling 
point. Such boiling would produce excessive turbulence within solvent A in 
the cleaning compartment and detrimentally impact ultrasonic cavitation 
therein. Therefore, solvent B within the cleaning compartment is 
maintained at a temperature below its boiling point. To this end, 
refrigeration coils 134 are provided within cleaning compartment 132. The 
coils are supplied refrigerant from chiller module 116 along conduits 120. 
These coils directly contact solvent B and maintain the temperature 
thereof significantly below the solvent B boiling point, e.g., at 
approximately 150 degrees F. for PF-5070. As such, boil sump 123 contains 
heated solvent in boiling compartment 124 and a cooled solvent in cleaning 
compartment 132. 
In operation, an operator of the apparatus slides, on door guides 164, door 
166 into an open position and places an object upon lift basket 154. 
Thereafter, the operator closes door 166 that initiates a cleaning cycle. 
The lift basket is then mechanically lowered along rail 150 into cleaning 
compartment 132 such that the object is immersed in solvent A, but does 
not become immersed in solvent B. Once immersed, power is supplied to 
ultrasonic array 138. Consequently, solvent A in combination with 
ultrasonic cavitation removes particulate matter, grease, and oils from 
the object. 
Alternatively, the operator can lower a basket containing the object into 
the cleaning compartment by hand. The specific use of a mechanically 
operated lift basket is only shown as an illustrative manner in which to 
implement the cleaning process. 
After a pre-defined duration, power to ultrasonic array 138 is discontinued 
and the lift basket is slowly raised from the cleaning compartment. 
Solvent A drips from the basket and object into the cleaning compartment. 
Being a non-volatile solvent, solvent A does not evaporate from the object 
very quickly. However, the rinsing step will remove any residual solvent A 
from the object. 
When lift basket 154 reaches its top-most position, the operator opens 
access door 166 and moves the object from lift basket 154 to lift basket 
156. The operator then closes the door and initiates a rinsing cycle. Of 
course, transfer of the object from one lift basket to another could be 
automated. Lift basket 156 lowers the object, along rail 152, until the 
object is immersed in solvent B. Subsequent to immersion, ultrasonic array 
140 is powered and ultrasonic cavitation facilitates removal of any 
residual particulate matter, grease, or oils as well as residual solvent 
A. All grease, oil or solvent A that is removed from the object cascades 
over first wall portion 136 into the cleaning compartment. All particulate 
matter that is denser than solvent B is removed from the rinsing 
compartment by filtration module 184. Thus, the rinsing solvent is 
maintained substantially contaminant free. 
After a pre-defined duration, power to ultrasonic array 140 is discontinued 
and lift basket 156 is returned to its top-most position. Since solvent B 
is a volatile solvent, the solvent evaporates from the object during 
ascent of the lift basket. Consequently, when the user opens access door 
166, the object is completely dry and ready for use. 
Alternatively, shown in FIG. 3, is a second embodiment of the cleaning 
apparatus. In this embodiment, the apparatus is configured for 
mono-solvent operation. In this configuration, solvent B is used as both a 
cleaning and rinsing solvent and solvent A is not used at all. Operation 
of the apparatus is substantially similar to that discussed above. The 
only difference being that, during the cleaning step, the object is 
immersed in solvent B within cleaning compartment 132 rather than solvent 
A. The fluid level of solvent B is shown as being below the height of 
second wall portion 128. However, the fluid level can exceed the height of 
the second wall portion without any detriment to the operation of the 
cleaning apparatus. 
Although various embodiments which incorporate the teachings of the present 
invention have been shown and described in detail herein, those skilled in 
the art can readily devise many other varied embodiments that still 
incorporate these teachings.