U.S. patent number 3,627,289 [Application Number 05/048,324] was granted by the patent office on 1971-12-14 for apparatus and method for removing oil from metal turnings.
Invention is credited to Walter Erman.
United States Patent |
3,627,289 |
Erman |
December 14, 1971 |
APPARATUS AND METHOD FOR REMOVING OIL FROM METAL TURNINGS
Abstract
An apparatus and method are provided for use in removing oil
from metal turnings. The apparatus includes a rotatable dryer
equipped with an internal baffle arrangement used to suspend oily
turnings in a stream of hot combustion gases which vaporize oil
contained on the turnings, and a combustion chamber which generates
hot combustion gases from a mixture of air and vaporized oil
removed from the turnings and recirculates a portion of the
combustion gases to the dryer. In addition, the apparatus is
provided with a natural gas burner which generates secondary
combustion gases for the combustion chamber when insufficient heat
is generated by the combustion of the air-vaporized oil mixture
alone, a blower which circulates air vaporized oil and secondary
combustion gases to the combustion chamber and a control assembly
to balance the flow of the air-vaporized oil mixture and secondary
combustion gases. The method for removing oil from oily turnings
generally involves the use of heat of combustion of the removed oil
to effect the removal of additional oil from the turnings.
Inventors: |
Erman; Walter (Chicago,
IL) |
Family
ID: |
21953954 |
Appl.
No.: |
05/048,324 |
Filed: |
June 22, 1970 |
Current U.S.
Class: |
134/19; 110/190;
110/246; 134/15; 75/403; 110/236; 134/2; 432/72 |
Current CPC
Class: |
C22B
1/005 (20130101); C23G 5/00 (20130101); Y02P
10/212 (20151101); Y02P 10/20 (20151101) |
Current International
Class: |
C23G
5/00 (20060101); C22B 1/00 (20060101); F27b
007/00 () |
Field of
Search: |
;263/33,34 ;110/14
;134/10,15 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Camby; John J.
Claims
I claim:
1. An apparatus for cleaning oily turnings comprising:
means for suspending said oily turnings in a stream of hot
combustion gases for a time sufficient to permit vaporization of
oil therefrom;
means for transmitting said oily turnings to said turnings
suspension means;
means for introducing air into the vaporized oil discharging from
said turnings suspension means;
primary combustion means, communicating with said turnings
suspension means, for burning said vaporized oil with air to form
hot combustion gases therefrom, and for discharging a stream of
said combustion gases to said turnings suspension means; and
secondary combustion means for generating additional hot combustion
gases for said turnings suspension means when the quantity of hot
gases generated from said primary combustion means is insufficient
to effect substantially complete vaporization of oil from said
turnings;
whereby oil contained on said turnings is removed therefrom and
vaporized substantially by means of hot combustion gases generated
by said primary and secondary combustion means.
2. The apparatus of claim 1 wherein said means for suspending oily
turnings is a rotatable dryer comprising an outer shell, an inner
conduit disposed concentrically within said outer shell, whereby
said oily turnings are transmitted in the annular space formed
between said outer shell and said inner conduit, and said stream of
hot combustion gases discharging from said combustion means first
flows within and along the length of said inner conduit counter to
the flow of said oily turnings and then flows within and along the
length of said annular space in a direction of flow of said oily
turnings so as to come in intimate contact with said turnings and
effect the removal of oil therefrom.
3. An apparatus for cleaning oily metallic turnings comprising:
a rotatable dryer means having an inlet adapted to receive said
oily turnings, baffle means to suspend said turnings within said
dryer for intimate contact with a stream of hot combustion gases,
and an outlet adapted to discharge vaporized oil removed from said
turnings by said stream of hot gases;
means for transmitting said oily turnings to the inlet of said
dryer means;
means for mixing air with said vaporized oil discharged from the
outlet of said dryer means;
a combustion chamber communicating with said dryer means and
adapted to burn said vaporized oil with air to form hot combustion
gases and to discharge a stream of said combustion gases into said
dryer means;
a burner for generating secondary combustion gases for said
combustion chamber;
blower means interconnecting said burner and the outlet of said
dryer means with said combustion chamber, said blower means being
adapted to receive air, vaporized oil discharging from the outlet
of said dryer means, and combustion gases generated in said burner
and to transmit said combustion gases, air and vaporized oil into
said combustion chamber; and
control means for balancing the quantity of secondary combustion
gases generated in said burner with the quantity of vaporized oil
discharging from the outlet of said dryer means whereby the
temperature of the combined combustion gases emitted from said
chamber is maintained at some predetermined value.
4. The apparatus of claim 3 wherein said rotatable dryer means
comprises an outer shell and an inner conduit disposed
concentrically within said outer shell and wherein said oily
turnings are discharged into the annular space formed between said
outer shell and said inner conduit, whereby the stream of hot
combustion gases discharging from said combustion chamber first
flows within and along the length of said inner conduit counter to
the flow of said oily turnings to provide conductive heat transfer
to said oily turnings and then flows within and along the length of
said annular space in an opposite direction so as to come in
intimate contact with said oily turnings and effect the removal of
oil therefrom.
5. The apparatus of claim 4 wherein said inner conduit is provided
with a plurality of fin members disposed along the outer surface of
said conduit to provide a conductive heat transfer surface for said
oily turnings.
6. The apparatus of claim 4 wherein said rotatable dryer means has
a plurality of perforated baffles spaced about the inside surface
of said outer shell, said baffles being adapted simultaneously to
suspend said oily turnings in said stream of hot combustion gases
allowing said gases to vaporize said oil and to transmit said
turnings along the annular space between said inner conduit and
said outer shell upon rotation of said dryer means.
7. The apparatus of claim 6 wherein said rotatable dryer means is
capable of controlled rotation at rates in the range of about 1.25
to 2.5 revolutions per minute.
8. The apparatus of claim 3 wherein said rotatable dryer means
comprises an outer shell having a plurality of spaced baffles
disposed about the inside surface of said shell, said baffles being
adapted to suspend said oily turnings in said stream of hot
combustion gases;
an inner conduit disposed concentrically within said outer shell
and having a plurality of fin members spaced along the outer
surface of said conduit;
whereby the stream of hot combustion gases discharging from said
combustion chamber first flows within and along the length of said
inner conduit counter to the flow of said oily turnings to provide
conductive heat transfer to said oily turnings and then flows
within and along the length of the annular space formed between
said outer shell and said inner conduit in the direction of flow of
said oily turnings so as to come in intimate contact with said
turnings and effect the removal of oil therefrom.
9. The apparatus of claim 3 wherein said control means terminates
the flow of secondary combustion gases from said burner when the
quantity of combustible gases generated by the combustion of air
and said vaporized oil discharging from the outlet of said dryer
means is sufficient to provide a stream of hot combustion gases to
said dryer capable of vaporizing oil from said turnings.
10. An apparatus for cleaning oily metallic turnings as defined in
claim 3 which is further characterized in that:
an afterburner means adapted to receive an air vaporized oil
mixture from said blower means is positioned in a parallel flow
arrangement with said combustion chamber;
a control valve is provided to automatically divert from said
combustion chamber into said afterburner a portion of the
air-vaporized oil mixture discharging from said blower; and
whereby said control means for the apparatus reduces the flow of
secondary combustion gases from said burner as the heat generated
in said combustion chamber from the combustion of said
air-vaporized oil mixture increases and whereby said control means
terminates the flow of secondary combustion gases, activates said
afterburner and diverts a portion of the flow of air-vaporized oil
from said combustion chamber to said afterburner when the heat
generated in said combustion chamber exceeds the requirements for
vaporization of oil in said dryer means and prevents overheating of
the recirculating apparatus.
11. A method for removing oil from oily metallic turnings which
comprises:
continuously suspending said oil turnings within a turnings
suspension means in a stream of hot combustion gases for a time
sufficient to vaporize oil from said turnings;
mixing said vaporized oil removed from said oily turnings with
air;
burning said air and vaporized oil to form a stream of hot
combustion gases; and
recirculating a quantity of said hot combustion gases to said
turnings suspension means sufficient to vaporize oil contained on
said turning.
12. A method for removing oil from oily metallic turnings which
comprises:
continuously suspending said oily turnings within a rotatable dryer
in a stream of hot combustion gases for a time sufficient to
vaporize oil from said turnings:
mixing said vaporized oil removed from said oily turnings with
air;
burning said air and vaporized oil in a combustion chamber to form
hot combustion gases;
providing secondary combustion gases to said combustion chamber
when said burning of air and vaporized oil in said combustion
chamber generates insufficient hot combustion gases to remove oil
from said turnings;
balancing the flow of secondary combustion gases and air-vaporized
oil mixture to said combustion chamber to provide sufficient hot
combustion gases to remove oil from said turnings; and
circulating hot combustion gases from said combustion chamber to
said dryer.
Description
BACKGROUND OF THE INVENTION
This invention concerns an apparatus and method for treating metal
turnings, and more specifically, deals with an apparatus and method
for removing oil from metal turnings without generating excessive
smoke or other air-contaminating materials.
It is well known that large quantities of oil are frequently
applied to metals being processed on machine shop tools, such as
lathes and the like, and that a variety of metal shavings, chips,
and turnings are formed as a waste byproduct of such operations.
Typically, the oil used in the metal processing adheres to the
metal turnings making them ill-suited for direct reclamation
operations.
It is known, for example, that the presence of large quantities of
oil on steel or steel alloy turnings make such turnings unusuable
for direct steel recovery processes because only poor quality, high
carbon steel can be obtained. Accordingly, a variety of techniques
have evolved for removing oil from metal turnings.
One such method merely involves the burnings of oil from the
turnings, with the consequent disadvantage of incomplete combustion
and significant air pollutant emissions. In addition, the exposure
of oil turnings to direct flames at the extremely high temperatures
required for oil removal causes a high degree of oxidation to occur
on the turnings.
Another oil removal technique which has proved equally unsuccessful
involves: burning oil from the turnings in the presence of excess
oxygen, mixing hot turnings with water, and then cooling and drying
the turnings by evaporation of water therefrom. This technique,
however, is still accompanied by incomplete removal of the oil,
unsatisfactory air pollution rates, low operating throughput and
extremely poor thermal efficiency for the overall oil removal
process.
As a result of the many deficiencies in existing oil removal
processes, an urgent need has developed for a new apparatus and
method to efficiently remove oil from turnings while at the same
time minimize the risk of discharge of air pollutants from the
removal apparatus.
SUMMARY OF THE INVENTION
According to this invention, a new apparatus and method are
provided for efficiently cleaning oily metallic turnings with
minimal heat losses, high thermal efficiency, and vastly reduced
potential of significant air pollution.
The oil removal apparatus of this invention generally includes: a
rotatable dryer equipped with an internal baffle arrangement
designed to permit intimate contact between oily turnings and a
stream of hot combustion gases used to vaporize oil contained on
the turnings; an assembly for transmitting oily turnings to the
dryer; a device for mixing air with the vaporized oil discharging
from the dryer; a combustion chamber used to burn vaporized oil and
air to form hot combustion gases for the dryer; a natural gas
burner for generating secondary combustion gases for the combustion
chamber; a blower interconnecting the dryer, the burner, and the
combustion chamber which receives air, vaporized oil, and secondary
combustion gases and transmits them to the combustion chamber; and
a control assembly to balance the quantity of secondary combustion
gases and vaporized oil discharging from the dryer so as to
maintain a constant temperature for the gases emitted from the
combustion chamber.
The method of this invention for removing oil from oily turnings
generally involves: the continuous suspension of oily turnings in a
stream of hot combustion gases for a time sufficient to remove oil
from the turnings, mixing vaporized oil with air, burning the
air-vaporized oil mixture to form hot combustion gases
recirculating sufficient hot combustion gases to effect removal of
oil from the turnings and venting any excess combustion gases.
Although a number of significant advances are made by the apparatus
and method of this invention, it should be noted that the practice
of this invention provides minimal heat losses to the atmosphere
since the heat of combustion from oil removed from the turnings is
used to generate hot combustion gases needed to remove additional
quantities of oil from the turnings. In addition, reduced
quantities of additional fuel, e.g., secondary combustion gases,
are required in the apparatus of this invention because the oil
itself acts as a fuel.
It should also be noted that the invention provides: (1) suspension
of the turnings in a stream of hot gases for a vastly improved oil
removal efficiency, (2) high throughput rates, (3) automatic
adjustment for excessive quantities of oil contained on the
turnings by means of an afterburner which burns excess oil vapor
rather than overheating the entire apparatus, (4) reduced
likelihood of oxidation occurring on the turnings since the
turnings are not subjected to a direct flame in an oxygen
environment, (5) relatively smoke-free reclamation of the turnings
because oil and other combustibles are burned to carbon dioxide and
water, and (6) a concentric tube arrangement in the dryer which
permits the turnings to be heated by conduction during an initial
pass of the hot combustion gases and by convection and radiation
during a subsequent pass.
BRIEF DESCRIPTION OF THE DRAWINGS
This invention will be more readily understood by reference to the
accompanying drawings in which:
FIG. 1 is a block diagram of the oil removal process of this
invention schematically representing the various steps involved in
the process;
FIG. 2 is a side elevational view of the dryer end of the oil
removal apparatus of this invention;
FIG. 3 is a side elevational view of the combustion chamber end of
the oil removal apparatus of this invention;
FIG. 4 is a top elevational view of a portion of the combustion
chamber end of the oil removal apparatus illustrated in FIG. 3;
and
FIG. 5 is a cross-sectional view taken through line 5--5 in FIG. 2
illustrating the internal baffle arrangement of the rotatable dryer
used to suspend oily turnings in a stream of hot combustion
gases.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
The steps performed in the oil removal process of this invention
are diagrammatically represented in FIG. 1. Basically, the process
is self-sustaining in the sense that oil removed from the turnings
furnishes enough fuel to sustain additional vaporization of oil
from the turnings. The removed oil is burned to essentially
invisible products, such as carbon dioxide and water, to minimize
potential air pollution hazards. In addition, the actual removal of
oil from the turnings is uniquely effected by means of vaporization
rather than burning with the consequent advantage that undesirable
oxidation of the turnings is markedly reduced.
Briefly, therefore, the steps involved in the process include the
suspension of oily turnings within a rotary dryer so that hot
combustion gases can come in intimate contact with the turnings,
mixing oil vaporized from the turnings with air and then burning
the air-oil mixture to form additional hot combustion gases to
effect the removal of oil from the turnings.
More specifically, however, as shown in FIG. 1, the oil removal
process of this invention is initiated by first transferring
metallic oily turnings into a suitable assembly for suspending the
oily turnings in a stream of hot combustion gases. As shown in FIG.
1, one suitable apparatus for carrying out the suspension of
turnings in a stream of hot combustion gases is a rotary dryer
which, by means of rotation and a unique internal baffle
arrangement, maintains the turnings in a suspended state and in
intimate contact with a stream of hot combustion gases.
As the turnings are held in contact with the hot combustion gases,
vaporization of the oils contained on the turnings occurs. Then the
oil vaporized from the turnings is removed from the turnings
suspension apparatus, e.g., rotary dryer, and mixed with a quantity
of air sufficient to support combustion of the vaporized oil.
This air-vaporized oil mixture is then transmitted by means of a
blower; or the like, to a combustion chamber where combustion or
burning of the vaporized oil takes place. Since the oils
contaminating the turnings are typically hydrocarbon compositions,
combustion in the presence of air tends to create a stream of hot
combustion gases composed primarily of carbon dioxide and water. It
should be particularly noted that since combustion of the oil
removed from the turnings occurs outside the presence of the
turnings the likelihood of oxidizing the turnings is significantly
diminished.
After the hot combustion gases have been generated in the
combustion chamber, the gases are passed through the turnings
suspension apparatus to effect the removal of oil contained on the
turnings by vaporization. Preferably, the hot gases are first
passed through the turnings suspension apparatus in a direction
counter to the flow of the turnings without coming in contact with
the oily turnings. In this way, the oily turnings are first
preheated by means of conduction, the hot gases transferring heat
through a centrally disposed conduit, or the like. Next, the hot
combustion gases make a second pass through the turnings suspension
apparatus, this time in contact with and in the same flow direction
of the oily turnings. During this second pass, sufficient heat is
transferred to the oily trunings by convection and radiation to
cause the vaporization and ultimate removal of oil contained on the
turnings.
In addition, during continuous operation of the oil removal
process, a portion of the hot combustion gases generated in the
combustion chamber are vented to an exhaust stack, as shown in FIG.
1, after making an initial pass through the turnings suspension
apparatus.
It is contemplated that sufficient quantities of oil will be
removed from the turnings to provide the complete fuel requirements
for the process. However, in some instances, excessive amounts of
oil may be contained on the turnings while, in other instances,
insufficient amounts of oil may be present on the turnings. In
either event, the process, shown generally in FIG. 1, can readily
adapt to such changing situations.
More specifically, when excessive amounts of oil are contained on
the turnings, a portion of the vaporized oil removed from the
turnings suspension apparatus are diverted from the combustion
chamber and, instead, are burned in an afterburner, or the like,
and vented to an exhaust stack. In the case where insufficient
amounts of oil are contained on the turnings or where an initial
startup of the process takes place, a stream of secondary
combustion gases is provided to maintain sufficient quantities of
hot gases to effect the vaporization of oil from the turnings. By
automatically controlling the quantity of vaporized oil diverted
from the combustion chamber and the quantity of secondary
combustion gases provided to the combustion chamber, the oil
removal process of this invention can be efficiently operated to
provide a sufficient, but not excessive, quantity of hot combustion
gases for use in removing oil from the turnings.
One embodiment of the oil removal apparatus of this invention is
illustrated in FIGS. 2, 3, and 4 and generally comprises a
rotatable dryer 11 designed to suspend oily turnings in a stream of
hot combustion gases, a combustion chamber 12 which provides hot
combustion gases to the dryer, a blower 13 used to circulate gases
through the apparatus, a natural gas burner 14 to generate
secondary combustion gases and an afterburner oriented in a
parallel flow arrangement with the combustion chamber.
More specifically, dryer 11 is rotatably mounted on a series of
cradles or pillars 20. These pillars 20, in turn, are disposed
along the length of the dryer 11 to permit the dryer to be inclined
at some predetermined angle sufficient to allow oily turnings to
move forward in the direction of combustion chamber 12. The
assembly used to rotate dryer 11 includes a gear ring 21 secured to
the outer circumference of the dryer which is driven by means of
gear motor assembly 22.
Steel tires 32, mounted on trunnion rollers 33, are disposed along
the length of dryer 11. These tires are not driven by gear motor
assembly 22 but rather merely serve to sustain the rotational
effect of dryer 11 caused by gear ring 21 and gear motor assembly
22.
The upper inclined inlet end 23 of dryer 11 is adapted to receive
oily turnings transferred by conveyor 24. As the turnings move
along conveyor 24, they fall by gravity flow through vertical chute
25 into dryer 11.
Externally, dryer 11 is provided with a relatively thick layer of
insulation 34 sufficient to maintain the outer surfaces of the
dryer 11 at temperatures of about 250.degree. F. or less.
Internally, dryer 11 is provided with an outer shell 16, normally
in the shape of a cylinder, and inner conduit 17 which is
concentrically disposed within the outer shell and is adapted to
receive hot combustion gases discharging from combustion chamber
12.
As shown in FIG. 5, a plurality of baffles or lifters 30 are spaced
about the inside surface of outer shell 16. These baffles are
designed both to suspend oily turnings within the annular space 18
formed between inner conduit 17 and outer shell 16 and to transfer
turnings along the length of the annular space as the dryer is
rotated. Fins 19 are disposed along the outer surface of inner
conduit 17 to improve the conductive heat transfer capability of
conduit 17 and to allow heat to be transferred to the oil turnings
by conduction through conduit 17 as well as by convection and
radiation from hot combustion gases passing through annular space
18. Support bars 35 and 36 are provided to support conduit 17
within outer shell 16 of dryer 11. In practice, hot combustion
gases at temperatures of about 1,200.degree. F. are discharged from
combustion chamber 12 within and along the length of inner conduit
17 until they reach the upper inlet end 23 of the dryer. This first
pass of hot gases through dryer 11 is in a flow direction counter
to that of the oily turnings. Then the hot combustion gases make a
second pass within and along annular space 18 of dryer 11 in the
same flow direction as the turnings. As the hot gases pass through
annular space 18, the combined action of rotating dryer 11 and
baffles 30 tend to suspend the oily turnings in the hot gases for a
time sufficient to permit oil contained on the turnings to be
vaporized as the oily turnings pass through the dryer.
Preferably dryer 11 is rotated at a rate within the range of 1.25
to 2.50 revolutions per minute. At this rotation rate, the oily
turnings are suspended in the hot gases for a sufficient time to
permit complete vaporization of oil.
Vaporized oil discharging from the outlet end 24 of dryer 11 is
mixed with sufficient air to support combustion in combustion
chamber 12. Air is drawn into the blower 13 through bleed air
damper 31. The air-vaporized oil mixture then passes through blower
13 which is driven by motor assembly 28 and then into combustion
chamber 12 where combustion of the air-oil mixture takes place.
As shown in FIG. 4, blower 13 is interconnected through inlet duct
26 and the outlet end 24 of dryer 11 which narrows somewhat at 27
to accommodate the inlet of blower 13. As such blower 13 receives
vaporized oil emitted from the dryer 11, air drawn through bleed
air damper 31 discharges through outlet duct 44 to combustion
chamber 12 or through gate valve 42 to afterburner 15. The purpose
of natural gas burner 14 is to provide secondary combustion gases
during the startup of the overall oil removal apparatus. In
addition, when insufficient vaporized oil is discharged from dryer
11, burner 14 acts to supplement hot combustion gases generated in
combustion chamber 12 from the combustion of the air-vaporized oil
mixture for use in removing oil from the turnings moving through
dryer 11.
After the oil removal apparatus of this invention has been properly
heated by means of natural gas burner 14, the heat of combustion
(and hot combustion gases) produced by the burning of vaporized oil
removed from the turnings permits a reduction in the amount of heat
(and secondary combustion gases) required from burner 14. A control
assembly is, therefore, provided to balance the quantity of
secondary combustion gases generated in burner 14 with the quantity
of vaporized oil discharging from the outlet of dryer 11 so that
the temperature and amount of combined combustion gases emitted
from combustion chamber 12 is maintained at some predetermined
level. Ideally, this temperature level is maintained sufficiently
high to allow the discharge of a stream of hot combustion gases to
dryer 11 capable of vaporizing oil from the oily turnings.
When oily turnings processed in the apparatus of this invention
contain an excessive amount of oil, heat generated in the
combustion chamber 12 may exceed that required for efficient oil
removal in the dryer 11. Accordingly, a control assembly which
includes thermocouple 41 located near the inlet of blower 13
automatically turns down burner 14, lights a gas flame in
afterburner 15, and opens motor operated blast gate valve 42 in
front of the combustion chamber to divert a portion of the
air-vaporized oil mixture into the afterburner. Excess
air-vaporized oil mixture diverted to afterburner 15 is completely
burned to carbon dioxide and water vapor and allowed to vent
through stack 43. Gate valve 42 then opens and closes as required
to reduce the quantity of combustion gases generated in combustion
chamber 12.
Combustion chamber 12 can be constructed from various refractory
materials sufficiently to withstand a temperature in excess of
1,200.degree. F. A burner 14 housed outside the combustion chamber
12 is used to burn the air-vaporized oil mixture to carbon dioxide
and water vapor which comprise the essential ingredients of the hot
combustion gases used to vaporize oil from oily turnings. During
continuous operation of the oil removing apparatus, a portion of
combustion gases are vented through main stack 45 as shown in FIG.
2 while the remaining portion circulates through dryer 11. After
oil has been removed from the turnings, they are removed from the
outlet end 24 of dryer 11 by means of apron conveyors 46 and 47
which receive turnings dropping through opening 38 in dryer 11.
Accordingly, as dryer 11 is rotated, turnings pass opening 38 while
vaporized oil removed from the turnings pass directly into the
inlet end of blower 13.
It should be understood that the various modifications of the
apparatus and invention discussed herein can be constructed without
departing from the spirit and scope of the invention.
* * * * *