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Patent 2669134 Summary

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Claims and Abstract availability

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(12) Patent Application: (11) CA 2669134
(54) English Title: WASTE OIL BURNING SYSTEM
(54) French Title: SYSTEME DE COMBUSTION D'HUILE USAGEE
Status: Deemed Abandoned and Beyond the Period of Reinstatement - Pending Response to Notice of Disregarded Communication
Bibliographic Data
(51) International Patent Classification (IPC):
  • F23D 11/38 (2006.01)
  • F23G 05/12 (2006.01)
  • F23G 07/05 (2006.01)
(72) Inventors :
  • MASIN, RADEK (United States of America)
(73) Owners :
  • RADEK MASIN
(71) Applicants :
  • RADEK MASIN (United States of America)
(74) Agent: SMART & BIGGAR LP
(74) Associate agent:
(45) Issued:
(86) PCT Filing Date: 2008-01-28
(87) Open to Public Inspection: 2008-08-07
Availability of licence: N/A
Dedicated to the Public: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): Yes
(86) PCT Filing Number: PCT/US2008/001065
(87) International Publication Number: US2008001065
(85) National Entry: 2009-05-08

(30) Application Priority Data:
Application No. Country/Territory Date
11/700,290 (United States of America) 2007-01-31

Abstracts

English Abstract

A waste oil burning system having a burner and a heat exchanger for preheating atomizing air before the atomizing air is supplied to the nozzle. The burner includes a fuel conduit for supplying waste oil to the burner and an air supply line for supplying atomizing air to the burner. The burner has a nozzle which atomizes the waste oil by mixing the waste oil with the air from the air supply line. The nozzle sprays the atomized waste oil into a combustion zone where the atomized waste oil is combusted. The heat exchanger is positioned in the combustion zone, so that energy produced from the combustion of the waste oil preheats the air supplied through the air supply line before the air is mixed with the waste oil.


French Abstract

L'invention concerne un système de combustion d'huile usagée comportant un brûleur et un échangeur de chaleur pour préchauffer l'air atomisant avant que l'air atomisant ne soit fourni à la buse. Le brûleur comprend une conduite de carburant pour fournir l'huile usagée au brûleur et une ligne d'alimentation en air pour fournir l'air atomisant au brûleur. Le brûleur possède une buse qui atomise l'huile usagée en mélangeant l'huile usagée avec l'air à partir de la ligne d'alimentation en air. La buse pulvérise l'huile usagée atomisée dans une zone de combustion où l'huile usagée atomisée est brûlée. L'échangeur de chaleur est placé dans la zone de combustion, de sorte que l'énergie produite par la combustion de l'huile usagée préchauffe l'air fourni par la ligne d'alimentation en air avant que l'air ne soit mélangé avec l'huile usagée.

Claims

Note: Claims are shown in the official language in which they were submitted.


CLAIMS
Having described my invention, I claim:
1. A waste oil burning system, comprising:
a. a burner, including
i. a fuel conduit, configured to supply said waste oil to said burner;
ii. an air supply line, configured to supply air to said burner;
iii. a nozzle, configured to atomize said waste oil by mixing said waste oil
with said air from said air supply line, wherein said nozzle is configured to
spray said atomized waste oil into a combustion zone where said waste oil
is combusted; and
b. a heat exchanger positioned in said combustion zone, said heat exchanger
configured to preheat said air supplied through said air supply line with heat
produced from the combustion of said waste oil before said air is mixed with
said
waste oil.
2. The waste oil burning system of claim 1, wherein said air passing through
said air
supply line is preheated to at least 200 degrees Fahrenheit before said air is
mixed
with said waste oil.
3. The waste oil burning system of claim 1, wherein said nozzle is an external
mix
nozzle.

11
4. The waste oil burning system of claim 1, further comprising a starter fuel
supply line,
said starter fuel supply line configured to supply a starter fuel to said fuel
conduit so
that said starter fuel mixes with said waste oil.
5. The waste oil burning system of claim 2, wherein said nozzle is an external
mix
nozzle.
6. The waste oil burning system of claim 2, further comprising a starter fuel
supply line,
said starter fuel supply line configured to supply a starter fuel to said fuel
conduit so
that said starter fuel mixes with said waste oil.
7. The waste oil burning system of claim 1, wherein said waste oil burning
system is
configured to supply a starter fuel to said nozzle for a defined period of
time, said
designed period of time corresponding to a length of time for which said
starter fuel
must be burned until said air passing through said heat exchanger is preheated
to a
temperature of at least 200 degrees Fahrenheit.
8. The waste oil burning system of claim 1, further comprising a temperature
sensor
configured to sense the temperature of said air before said air is mixed with
said
waste oil, wherein said waste oil burning system is configured to supply a
starter fuel
to said nozzle until said air passing through said heat exchanger is preheated
to a
temperature of at least 200 degrees Fahrenheit.

12
9. A method of combusting waste oil, comprising the steps of:
a. providing a burner, said burner including:
i. a fuel conduit, configured to supply said waste oil to said burner;
ii. an air supply line, configured to supply air to said burner;
iii. a nozzle, configured to atomize said waste oil by mixing said waste oil
from said fuel conduit with said air from said air supply line, wherein said
nozzle is configured to spray said atomized waste oil into a combustion
zone where said waste oil is combusted;
b. supplying waste oil to said fuel conduit;
c. supplying air through said air supply line to said nozzle;
d. mixing said air and said waste oil at said nozzle;
e. combusting said air and said waste oil in a combustion zone; and
f. preheating said air to at least 200 degrees Fahrenheit prior to mixing said
air with
said waste oil.
10. The method of claim 9, wherein said nozzle is an external mix nozzle.
11. The method of claim 9, further comprising the step of supplying a starter
fuel to said
nozzle for a defined period of time, said designed period of time
corresponding to a
length of time for which said starter fuel must be burned until said air
supplied to said
nozzle is preheated to a temperature of at least 200 degrees Fahrenheit.

13
12. The method of claim 9, further comprising the steps of:
a. sensing said temperature of said air prior to mixing said air with said
waste oil,
and
b. supplying a starter fuel to said nozzle until said air supplied to said
nozzle is
preheated to a temperature of at least 200 degrees Fahrenheit.

Description

Note: Descriptions are shown in the official language in which they were submitted.


CA 02669134 2009-05-08
WO 2008/094487 PCT/US2008/001065
1
Patent Application of
Radek Masin
for
TITLE: WASTE OIL BURNING SYSTEM
CROSS-REFERENCES TO RELATED APPLICATIONS
Not Applicable
STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR
DEVELOPMENT
Not Applicable

CA 02669134 2009-05-08
WO 2008/094487 PCT/US2008/001065
2
BACKGROUND OF THE INVENTION
1. Background - Field of the Invention.
This invention relates to the field of waste oil burning systems. More
specifically, the
present invention comprises a waste oil burning system having a preheated
atomizing air feed.
2. Background - Prior Art
Combustion is one of the preferred methods of disposing of waste oils such as
used
engine oils, cooking oils, cutting oils, gear oils, hydraulic oils, and other
difficult to burn liquids,
such as glycerin and antifreeze. Waste oils do not burn cleanly or efficiently
if the oil is not
properly atomized. To improve efficiency, many facilities that burn waste oil
preheat the oil.
Preheating the oil lowers the viscosity of the oil so that it may be more
readily atomized when
mixed with air (such as when sprayed through an atomizing nozzle).
There are many disadvantages to preheating waste oils, however. First, the
energy to
preheat waste oils can be costly. Also, even the most controlled preheating
processes can cause
acceleration of chemical reactions within the waste oils which result in
formation of deposits on
heating surfaces. The fouling of the heating surfaces results in heating
inefficiencies, requiring
the preheater to be regularly cleaned and maintained. Furthermore, some of the
deposits may
break free of the heating surface only to foul other parts of the burner,
including the nozzle and
combustion chamber.
Accordingly, it would be desirable to have a waste oil burning system which is
not costly
to operate and avoids the problems associated with the preheating of waste
oils.
SUMMARY

CA 02669134 2009-05-08
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3
The present invention comprises a waste oil burning system having a burner and
a heat
exchanger for preheating atomizing air before the atomizing air is supplied to
the nozzle. The
burner includes a fuel conduit for supplying waste oil to the burner and an
air supply line for
supplying atomizing air to the burner. The burner has a nozzle which atomizes
the waste oil by
mixing the waste oil with the air from the air supply line. The nozzle sprays
the atomized waste
oil into a combustion zone where the atomized waste oil is burned. An air-to-
liquid type heat
exchanger is positioned in the combustion zone, so that energy produced from
the combustion of
the waste oil preheats the air supplied through the air supply line before the
air is mixed with the
waste oil.
DRAWINGS
FIG. 1 is a schematic, showing the present invention.
FIG. 2 is a schematic, showing the present invention.
FIG. 3 is a schematic, showing the present invention.
REFERENCE NUMERALS IN THE DRAWINGS
storage vessel
12 waste oil pump
14 waste oil supply line
16 burner
18 storage vessel

CA 02669134 2009-05-08
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4
20 fuel pump
22 fuel supply line
24 combustion zone
26 air supply line
28 air compressor
30 fuel conduit
32 nozzle
34 heat exchanger
36 flame
38 waste oil burning system
40 waste oil solenoid
42 fuel solenoid
44 fuel solenoid
46 switch
48 timer
50 switch
52 timer
DETAILED DESCRIPTION
The present invention, waste oil burning system (38) is illustrated in FIG. 1.
Waste oil
burning system (38) may be used to burn various waste oils, including most No.
4 specification
oils. No. 4 specification oils generally include heavy distillate and blends
of distillate and

CA 02669134 2009-05-08
WO 2008/094487 PCT/US2008/001065
residual fuel oils, typically having a carbon chain length of 12 to 70 atoms.
Storage vessel (10)
is provided for storing waste oils before they are burned. Waste oil pump (12)
is used to provide
a continuous supply of waste oil to burner (16) through waste oil supply line
(14). Although a
centrifugal pump is illustrated, the reader should note that any pump may be
used that is suitable
for transporting the waste oil at a controlled rate.
Air compressor (28) is provided to provide a continuous supply of atomizing
air to burner
(16) through air supply line (26). Air supply line (26) transports the
atomizing air through
combustion zone (24) where energy produced during the combustion of the waste
oils preheats
the atomizing air. A heat exchanger for preheating the air is positioned in
combustion zone (24)
and fluidly connected to air supply line (26). Heat exchangers of various
designs may be
employed for such a purpose. In the preferred embodiment, the heat exchanger
includes a
conduit or manifold which is heated by the energy produced during the
combustion of the waste
oils. As the atomizing air passes through the heat exchanger, the air is
heated.
During start-up, a starter fuel feed is mixed with the waste oil feed for a
period of time
until the heat exchanger reaches the designed operating temperature. Storage
vessel (18) is
provided to maintain a supply of starter fuel sufficient to facilitate the
combustion of the waste
oil while the heat exchanger is brought to operational temperature. Fuel pump
(20) supplies
burner (16) with a continuous feed of starter fuel during start-up through
fuel supply line (22).
As illustrated in FIG. 2, burner (16) includes nozzle (32) which is configured
to atomize
the waste oil by mixing the waste oil with the air from air supply line (26).
Nozzle (32) is
configured to spray the atomized waste oil into combustion zone (24) where the
waste oil is
combusted, as indicated by flame (36). Nozzle (32) is preferably an external
mix nozzle, but an

CA 02669134 2009-05-08
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6
internal mix nozzle may also be used. Those that are skilled in the art know
that the term
"external mix nozzle" describes a class of nozzles in which air is mixed with
a liquid after the
liquid exits a discharge orifice. In external mix nozzles, the nozzle opening
is generally coaxial
with the liquid discharge orifice. A pressurized air stream is typically
directed on the
discharging liquid stream so that the two components mix while passing through
the nozzle
opening.
Nozzle (32) has fuel conduit (30) which transports waste oil through nozzle
(32). The
waste oil mixes with the atomizing air as it exits fuel conduit (30). Nozzle
(32) sprays the waste
oil and air mixture into combustion zone (24) where the waste oil combusts.
Waste oil supply
line (14) and fuel supply line (22) both feed into fuel conduit (30). As
mentioned previously,
fuel supply line (22) supplies starter fuel during start-up. Once heat
exchanger (34) reaches
operational temperature, only waste oil is combusted.
In the preferred embodiment, air supply line (26) feeds air to burner (16),
then through
combustion zone (24), then back to burner (16) where the air is discharged
from air supply line
(26) into nozzle (32). Those that are skilled in the art will know that the
various materials and
designs may be used for heat exchanger (34). In addition, the dimensions of
heat exchanger (34)
and the distance of heat exchanger (34) from flame (36) may all be adjusted so
that the atomizing
air enters nozzle (32) at the appropriate temperature. In the preferred
embodiment, the atomizing
air is heated to a temperature of at least 200 degrees Fahrenheit prior to
entering nozzle (32). As
illustrated in FIG. 2, heat exchanger (34) may simply be a continuation of air
supply line (26)
which passes through combustion zone (24).
EXAMPLE

CA 02669134 2009-05-08
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7
Through experimentation it has been determined that waste oils having a flow
rate of
approximately 2.5 gallons per hour may be cleanly and efficiently combusted
when mixed with
atomizing air having a flow rate of 0.3 cubic feet per minute at a pressure of
7 psi and a
temperature of 250 degrees Fahrenheit. In the referenced experiment, an
external mix aspiration
nozzle was used to mix the waste oil with the atomizing air. The waste oil was
not preheated
prior to being mixed with the atomizing air.
For start-up, a combustion enhancer was mixed with the waste oil for improved
atomization and ignition. Also, atomizing air was provided at a flow rate of
0.8 cubic feet per
minute until the atomizing air reached a temperature of 250 degrees
Fahrenheit.
A control system for controlling the starter fuel and waste oil is illustrated
in FIG. 3. The
flow rate of waste oil through waste oil supply line (14) is controlled by
waste oil solenoid (40).
Two solenoids, fuel solenoid (42) and fuel solenoid (44), are arranged in
parallel to control the
flow rate of starter fuel through fuel supply line (22). Fuel solenoid (42) is
controlled by switch
(46) and fuel solenoid (44) is controlled by switch (50). Both switch (46) and
switch (50) have
three operating modes - "timed," "off," and "continuous."
During start-up, switch (50) may be adjusted to the "timed" mode so that fuel
solenoid
(44) opens and starter fuel is supplied for a period of time. Switch (50) is
electronically
connected with timer (52). Timer (52) is preferably adjustable so that the
timing period may be
changed as necessary. The period of time which fuel solenoid (44) is in the
opened position may
be experimentally determined to meet the requirements of the particular heat
exchanger and flow
rate of waste oil that is to be combusted. By the time fuel solenoid (44)
closes, the atomizing air
is hot enough to keep the burning process going without the aid of the starter
fuel.

CA 02669134 2009-05-08
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8
Switch (46) controls fuel solenoid (42). Fuel solenoid (42) controls the flow
of starter
fuel through a second fuel line. Switch (46) is electronically connected to
timer (48). The
second fuel line may be opened when larger amounts of starter fuel are needed.
If the waste oil
is very poor, either switch (46) or switch (50), or the two combined, may be
turned to
"continuous" mode so that a constant supply of starter fuel is provided
throughout the burn time.
It is also possible to turn off the supply of waste oil completely and burn
only starter fuel until
the desired operating temperature is attained.
The feed of starter fuel to burner (16) may also be controlled with a solenoid
integrated
with a temperature sensor and controller. A temperature sensor may be
positioned in the air
supply line downstream of heat exchanger (34). The temperature sensor may be
configured to
sense the temperature of the air before the air is mixed with the waste oil.
When the temperature
is less than 200 degrees Fahrenheit, the controller may open the solenoid to
supply starter fuel to
burner (16). When the temperature sensor observes an air temperature of at
least 200 degrees
Fahrenheit, the controller may close the solenoid in the starter fuel supply
line, cutting off the
starter fuel feed to the nozzle. It should be noted that the temperature
sensor and controller may
use a different set point than 200 degrees Fahrenheit.
In addition, multiple set points may be used to control the flow rate of
starter fuel. This
may be accomplished by using a solenoid that may be opened to various
increments. For
example, the solenoid may be set to a partially open position when the air
reaches 200 degrees
Fahrenheit. The solenoid may then be moved to a completely closed position
when the air
reaches 250 degrees Fahrenheit. Obviously, even more set points on solenoid
positions may be
incorporated to minimize the use of starter fuel.

CA 02669134 2009-05-08
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9
The preceding description contains significant detail regarding the novel
aspects of the
present invention. It should not be construed, however, as limiting the scope
of the invention but
rather as providing illustrations of the preferred embodiments of the
invention. As an example,
combustion zone (24) may be an enclosed fire box or it may be completely
external to burner
(16). Thus, the scope of the invention should be fixed by the following
claims, rather than by
the examples given.

Representative Drawing
A single figure which represents the drawing illustrating the invention.
Administrative Status

2024-08-01:As part of the Next Generation Patents (NGP) transition, the Canadian Patents Database (CPD) now contains a more detailed Event History, which replicates the Event Log of our new back-office solution.

Please note that "Inactive:" events refers to events no longer in use in our new back-office solution.

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Event History

Description Date
Application Not Reinstated by Deadline 2013-01-28
Time Limit for Reversal Expired 2013-01-28
Deemed Abandoned - Failure to Respond to Maintenance Fee Notice 2012-01-30
Inactive: Cover page published 2009-08-28
Inactive: Inventor deleted 2009-08-26
Inactive: Notice - National entry - No RFE 2009-08-26
Inactive: IPC assigned 2009-07-08
Inactive: IPC assigned 2009-07-08
Application Received - PCT 2009-07-07
National Entry Requirements Determined Compliant 2009-05-08
Application Published (Open to Public Inspection) 2008-08-07

Abandonment History

Abandonment Date Reason Reinstatement Date
2012-01-30

Maintenance Fee

The last payment was received on 2010-10-22

Note : If the full payment has not been received on or before the date indicated, a further fee may be required which may be one of the following

  • the reinstatement fee;
  • the late payment fee; or
  • additional fee to reverse deemed expiry.

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Please refer to the CIPO Patent Fees web page to see all current fee amounts.

Fee History

Fee Type Anniversary Year Due Date Paid Date
Basic national fee - standard 2009-05-08
MF (application, 2nd anniv.) - standard 02 2010-01-28 2009-12-29
MF (application, 3rd anniv.) - standard 03 2011-01-28 2010-10-22
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
RADEK MASIN
Past Owners on Record
None
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Description 2009-05-07 9 271
Drawings 2009-05-07 3 25
Abstract 2009-05-07 1 53
Claims 2009-05-07 4 92
Representative drawing 2009-05-07 1 6
Notice of National Entry 2009-08-25 1 206
Reminder of maintenance fee due 2009-09-28 1 111
Courtesy - Abandonment Letter (Maintenance Fee) 2012-03-25 1 174
Reminder - Request for Examination 2012-09-30 1 118
PCT 2009-05-07 1 49
Fees 2009-12-28 1 34
Fees 2010-10-21 1 35