US3880143A - Combination fume oxidizer and asphalt heater - Google Patents
Combination fume oxidizer and asphalt heater Download PDFInfo
- Publication number
- US3880143A US3880143A US334257A US33425773A US3880143A US 3880143 A US3880143 A US 3880143A US 334257 A US334257 A US 334257A US 33425773 A US33425773 A US 33425773A US 3880143 A US3880143 A US 3880143A
- Authority
- US
- United States
- Prior art keywords
- fumes
- asphalt
- fume
- heating chamber
- odorous
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
- F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
Definitions
- ABSTRACT A combined fume oxidizer and asphalt heater which substantially reduces fumes normally associated with the production of asphalt roofing materials. These fumes are utilized to heat additional asphalt and are substantially combusted. A method is described wherein the fumes from an asphalt shingle saturation machine are directed through a burner of the gas or oil type and the combined streams of burned gases are utilized to heat asphalt material.
- the heat of combustion is controlled by a thermocouple and the temperature in the heating chamber by by-passing a portion of the combined combusted streams away from the heating chamber and into an exhaust duct to which the other portion of the combusted gases is directed after heating the asphalt material.
- a damper control means directs the portions of the combusted gases to the heating chamber or through the by-pass ducts depending upon the temperature desired in the heating cham her for heating the asphalt material.
- This invention relates to a burner and a method of substantially reducing fumes and odorous materials. More particularly, it relates to a method and apparatus for utilizing an odorous effluent stream from an asphalt shingle saturation apparatus in a manner to have it serve as a fuel source while at the same time regulating the heat of combustion of the combined fume and usual fuel gas stream by by-passing the heating chamber with a portion of the combined streams when temperature conditions indicate.
- the manufacture of asphalt shingles inherently includes the application of hot vaporous asphalt material to an underlying base of felt material which results in fumes being exhausted to the surrounding atmosphere. This is an undesired situation in that such fumes can pollute the atmosphere and their heat value is lost.
- a fluid combustible material such as vaporized asphalt is directed toward a combustion zone containing burner elements for the asphalt heater.
- the combustible material is burned with an additional fuel stream and a portion of the combusted gases are directed toward the heating elements for additional asphalt.
- another portion of the combusted gases is directed away from the heating elements and out through an exhaust duct or stack to the atmosphere where the first stream of gases which heated the asphalt is also directed.
- the apparatus for accomplishing the method of this invention includes a burner element through which the odorous asphalt stream is directed and a heating chamber which also contains a by-pass duct leading to an exhaust or outlet stack to which also is attached an intermediate duct from the heating chamber. Dampers are provided in the by-pass duct as well as in the intermediate or stack duct leading from the heating chamber for controlling the temperature within the heating chamber.
- An induction type fan is utilized downstream of the burner and the heating chamber to exert a pulling force on the by-pass stream as well as the stream heating the asphalt material to draw it through the burner and the heating chamber and to cause it to flow outwardly into the atmosphere through the exhaust duct.
- the method and apparatus of the invention is efficient enough so as to reach a temperature of I600F while affording an excess of one-half second retention time in the combustion chamber so as to burn all of the odorous asphalt material and thereby meet the most stringent air anti-pollution code requirements BRIEF DESCRIPTION OF THE DRAWINGS A better understanding of the present process and the apparatus for accomplishing it will be afforded by reference to the drawing wherein:
- FIG. I is a view in side elevation of the combined fume oxidizer and asphalt heater for effecting the process of this invention.
- FIG. 2 is a front end view of the combined fume oxidizer taken along line 2-2 of FIG. 1.
- FIG. 3 is a view in side elevation of an alternative embodiment of a combined fume oxidizer and asphalt heater.
- FIG. 4 is an end view in elevation showing the back of fume oxidizer and asphalt heater shown in FIG. 3.
- FIG. 5 is a partial view in elevation of the damper sys tem shown in the FIG. 3 embodiment but with the damper in another position.
- the method of this invention comprises the steps of directing a fluid stream of odorous and smoke forming combustible material such as the effluent from an asphalt shingle saturation apparatus through a combustion zone.
- An additional fuel stream such as natural gas or oil, is also directed to the combustion zone.
- the combined streams form a second zone of hot gases which are utilized to heat a material such as additional asphalt in a third zone.
- a portion of said combusted gases are directed away from the third zone and through a by-pass zone to an exhaust zone.
- the remaining portions of gases in the third heating zone are directed into the exhaust zone for recombination with combusted gases originally directed away from the third zone.
- the streams of vaporized asphalt and fuel are drawn through various zones by a negative pressure and exhausted by a positive pressure.
- the stream of combusted gases which are diverted away from the third heating zone. and those which are not, are recombined in a common zone prior to being exhausted.
- the vaporized asphalt stream is di rected through the combustion zone at an average rate of at least 20 feet per second with a retention time in the combustion zone of a minimum of one-half second, to effect a desired temperature of approximately I400TF in the combustion zone and a temperature in the range of 490530F for the heated asphalt.
- FIG. I One apparatus for best carrying out the method of this invention is the combined fume oxidizer and asphalt heater generally 10 as shown in FIG. I which includes a heating chamber 11 having a multiplicity of coiled pipes 12, an inlet 13 and an outlet (not shown) for flowing liquids such as asphalt into and out of the chamber for heating purposes.
- the heating chamber 11 with the coiled pipes 12 is of the standard type used in the asphalt shingle producing industry and is constructed of a refractory with an outer steel plate housing.
- Adjacent the heating chamber 11 is a burner canopy 15 which houses a burner element H5 in the form of a flame grid.
- Burner element or grid 16 is positioned in an intake duct 17 through which will be passed odorous and fume producing fluid combustible materials such as vaporized asphalt. Disposed upstream of the grid 16 is a natural gas line 18 communicating with grid 16 for purposes of combusting the fumes and heating a fluid material such as asphalt in pipes 12.
- a thermocouple 14 through standard proportional motor control 23 positions a fuel valve 24 in line 18 to control the fire box temperature.
- a draft control system consisting of controller 19 and pressure sensor line 27 is located at the top of canopy for sensing the pressure in chamber 11 and commands actuator 59 to position damper 22.
- Dampers 20, 21 and 22 are pivotally positioned in the normal manner in three separate ducts or conduits as follows: damper is located in by-pass duct 25 which is in communication with the back of chamber 11 and below coiled pipes 12; damper 21 is located in intermediate or stack duct 26 which is in communication with the top of heating chamber 11 and above the heating coils or pipes 12; damper 22 is operatively disposed in common duct or conduit 28.
- An induction type blower fan is connected to common duct 28 at one end which is the negative pressure side and to an upright exhaust or blower duct 32 at the other end of blower 30 which is the positive pressure side.
- Damper 22 is controlled by a standard actuator 59 by means of linkage 60 and 61. Dampers 20 and 21 are operated by a common air flow actuator 63 with a pivotal arm 64. A connecting link 65 interconnects with a double pivot arm clevis type connection 67 to which is attached another link 69 which in turn is secured to arm 70 on damper 21. Actuator 63 is commanded by thermocouple and controller 29 which senses the temperature of the leaving fluid in pipes 12.
- blower 30 is driven by two motors 33 and 34 with motor 33 being of larger horsepower than motor 34 and having a larger sheave 35 than sheave 36.
- Suitable Vbelts 38 and 39 drive the common sheave 40 independently on blower drive shaft 42 which is supported be hearing members 43 on support block 45.
- an exhaust duct 46 from a standard asphalt saturator is in fluid tight communication with the upstream end of intake conduit 17.
- a condensate well and heavy particle trap 47 is provided opposite the connection with fume intake conduit 17.
- a steam snuff line connection 49, drain 50 and clean out door 52 are provided in and for trap 47.
- a flame retardant screen 48 is located across intake duct 17 just downstream of the communication with fume exhaust duct 46.
- To supply air for combustion when fumes are not being incinerated an air door 53 is disposed above intake duct 17 which is moved to a fully opened position by means of standard motor actuator 56 with the usual linkage 57 controls door 53. When fumes are being combusted air door 53 will be completely closed.
- by-pass duct 125 rather than the stack duct 26, is extended in a U- shaped manner up the back of chamber 111, across the top of chamber 111, over blower 130 and down along the front portion of chamber 111 where it joins common and intermediate or stack duct 126 in a T- junction.
- exhaust duct 132 is relatively short and extends a short distance from blower 130 in a horizontal direction.
- the general method of conducting combusted fuel and fumes through heating chamber 111 is the same.
- fumes from an asphalt saturation machine will be introduced by suitable controls into exhaust duct 46 of the saturation machine. These fumes will flow through flame retardant screen 48 and along duct 17 across burner element 16 whereupon the combined streams of fumes and natural gas will become combusted in a first combustion zone immediately downstream of burner element 16. They will move away as indicated by the arrows from burner element 16 where the combusted substances will form a second zone of hot gases below the area of the coiled pipes 12 and indicated at 31. In the combustion of asphalt fumes to which this invention is particularly directed, it is desired to have a temperature of 1400F in this area.
- thermocouple 29 When asphalt is to be heated to a temperature of approximately 5 10F thermocouple 29 in the asphalt tubes and controller actuator 63 position dampers 20 and 21 accordingly. It should be understood that the temperature of the asphalt in pipes 12 is controlled independently of the fire box. When the asphalt temperature reaches 490F the actuator 63 will be activated by thermocouple 29 and gradually open the by-pass damper 20 by moving pivot arm 64 downwardly and through double pivot arm 67 will cause the stack damper 21 in intermediate or stack duct 26 to close. These dampers will assume a 50% open or close position substantially as shown in FIG. 1 which will be in approximately the 50% full open or close position. This is effected by means of the interconnecting linkage such as connecting link 65, double clevis arm 67, link 69 and arm 70 on damper 21.
- dampers will divert a portion of some of the hot gases away from the third zone in the area of the coiled pipes 12 containing the asphalt to be heated and will divert it through the by-pass duct 25.
- the bypass damper 20 would be fully opened and the damper 21 in the stack duct would be fully closed.
- the dampers would operate in a reverse manner through actuator 63.
- the fire box 31 would be maintained at its setting of 1400F by its own thermal control system comprising thermocouple 14 proportional motor control 23 and valve 24.
- Damper 22 in common duct 28 serves to maintain a preset negative pressure in the fire box 31 utilizing the vacuum sensing line 27, controller 19, actuator 59 and linkages 60 and 61.
- the heating chamber volume is approximately 330 cubic feet.
- the flow of fumes into fume or exhaust duct from the saturator 46 should be approximately 1 1,400 cubic feet per minute with a duct velocity on the average of 38 feet per second.
- the velocity of the fumes in the fire box 31 immediately downstream of the burner is approximately 20.2 feet per second with a retention time in this area of 0.503 second which exceeds most pollution code requirements.
- damper 121 in stack duct 126 and damper 120 in by-pass duct 125 in unit 110 as shown in FIG. 3 will indicate the maximum amount of combusted fumes and fuel gas which will pass through heating chamber 111 and across coiled pipes 1 12.
- actuator 163 When a lower asphalt temperature is desired actuator 163 will be actuated which will cause double clevis arm 167 to move in a clockwise manner thereby closing damper 121 and opening damper to divert a portion of the combined combusted fuel and fumes around coils 112 and out of the heating chamber through by-pass duct 125.
- Both streams of combusted fuel and fumes whether passing through the heating chamber 111 or the by-pass duct 125 will be recombined in common duct 128 after which they will be passed through blower 130 and out through outlet duct 132 to the atmosphere.
- the operating conditions concerning flow of the fluid streams, retention times, et cetera, for unit 110 are approximately the same as that described for the previous unit 10.
- all of the duct work is fabricated from three foot internal diameter pipe having a 37 inch outside diameter.
- it is fabricated from stainless steel. This would include the exhaust ducts 46, 146 or inlet duct for the fumes, intake ducts 17, 117, as well as by-pass ducts 25 and 125, intermediate duct or stack ducts 26, 126, common ducts 28, 128 and exhaust ducts 32 and 132.
- a two motor system as described by motors 33, 34 and 133 and 134 which are of high and low speeds, respectively, provide an initial high flow rate through the heating chambers 11 and 111 and after the flow rate is achieved, the low speed motors can be utilized.
- Natural gas is indicated as the preferred fluid fuel in conjunction with burner grid 16.
- other fluid fuels could be utilized in its place such as fuel oil, pulverized coal, propane and electricity, all with suitable burner, electrode or resistance elements.
- a combined fume oxidizer and asphalt heater comprising: means defining a heating chamber; fluid conduit means disposed in said heating chamber for flowing fluids into and out of said chamber for heating said fluids; a burner element for combusting fluid fuels in fluid communication with said chamber; means to supply fluid fuel to said burner element; an intake duct in communication with said burner element; an exhaust duct open at one end with the atmosphere and at the other end with said heating chamber; a by-pass duct in fluid communication with said chamber and said exhaust duct; means to supply with force combustible flowable fumes to said intake duct for combustion by said burner element and means to regulate the flow of said combusted fumes through said by-pass duct and said heating chamber.
- the combined fume oxidizer and asphalt heater as defined in claim 1 further including an exhaust outlet duct in communication with an asphalt shingle saturating machine which conveys combustible fumes, said outlet duct secured in fluid communication with said intake duct.
- heating chamber includes U-shaped tubular members for conveying asphalt through the heating chamber.
- the combined fume oxidizer and asphalt heater as defined in claim 6 further including an intermediate conduit disposed between said heating chamber and said draft fan and including dampers in said intermediate conduit and said by-pass conduits and means to regulate said dampers including temperature. sensing means operatively connected to said fluid conduit means.
- the combined fume oxidizer and asphalt heater as defined in claim 7 further including a common conduit in communication with said by-pass conduit and said intermediate conduit and secured in fluid communication with said draft fan at the upstream side of said fan with said exhaust duct connected to the downstream side.
- a method of combusting odorous and fume forming combustible fumes present in a fluid state while utilizing and controlling the heat of combustion comprising: directing a fluid to be heated through a conduit in a heating chamber, directing said fluid combustible fumes toward a first combustion zone, burning a fluid fuel in said combustion zone to substantially combust said combustible fumes and form a second zone of hot gases; directing a portion of said gases in said second zone toward the heating chamber for heating said fluid and directing another portion of said gases in said second zone away from said heating chamber.
- the method of combusting odorous and fume forming combustible fumes as defined in claim 11 further including the step of directing said gases from said heating chamber and the gases directed away from the heating chamber into a common exhaust zone.
- the method of combusting odorous and fume forming combustible fumes as defined in claim 11 including passing the fluid fuel and the odorous or smoke forming combustible fumes through a flame grid prior to the combustion zone.
Abstract
Description
Claims (18)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US334257A US3880143A (en) | 1973-02-21 | 1973-02-21 | Combination fume oxidizer and asphalt heater |
CA181,728A CA981546A (en) | 1973-02-21 | 1973-09-24 | Combination fume oxidizer and asphalt heater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US334257A US3880143A (en) | 1973-02-21 | 1973-02-21 | Combination fume oxidizer and asphalt heater |
Publications (1)
Publication Number | Publication Date |
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US3880143A true US3880143A (en) | 1975-04-29 |
Family
ID=23306362
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US334257A Expired - Lifetime US3880143A (en) | 1973-02-21 | 1973-02-21 | Combination fume oxidizer and asphalt heater |
Country Status (2)
Country | Link |
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US (1) | US3880143A (en) |
CA (1) | CA981546A (en) |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4477250A (en) * | 1983-03-07 | 1984-10-16 | Mechtron International Corporation | Asphalt recycle plant and method |
US5090813A (en) * | 1990-07-23 | 1992-02-25 | Cedarapids, Inc. | Dual drum recycle asphalt drying and mixing method and apparatus |
US5174650A (en) * | 1990-07-23 | 1992-12-29 | Cedarapids, Inc. | Dual drum recycle asphalt drying and mixing method and apparatus |
US5176445A (en) * | 1990-08-10 | 1993-01-05 | Astec Industries, Inc. | Apparatus for decontaminating soils |
US5556197A (en) * | 1994-11-04 | 1996-09-17 | Gentec Equipment Company | Asphalt plant for both continuous and batch operation |
US5558029A (en) * | 1994-12-14 | 1996-09-24 | Barnstead/Thermlyne Corporation | Ashing furnace and method |
US5873919A (en) * | 1995-06-07 | 1999-02-23 | Simon Roofing & Sheet Metal Corp. | System for removal of noxious fumes |
US6000935A (en) * | 1997-02-21 | 1999-12-14 | Troxler Electronic Laboratories, Inc | Adjustable apparatus for pyrolysis of a composite material and method of calibration therefor |
US6033629A (en) * | 1998-03-18 | 2000-03-07 | Barnstead/Thermolyne Corporation | Ashing furnace |
US6065469A (en) * | 1999-01-08 | 2000-05-23 | Cleasby Manufacturing Company, Inc. | Emission control system for asphalt kettle |
US6109826A (en) * | 1999-06-03 | 2000-08-29 | Cimline, Inc. | Melter and applicator for applying filling material to paved surfaces |
US6146007A (en) * | 1998-03-20 | 2000-11-14 | Cedarapids Inc. | Asphalt plant having centralized media burner and low fugitive emissions |
US6534020B1 (en) * | 1997-07-09 | 2003-03-18 | Garlock Equipment Co. | Fume recovery methods |
CN104930523A (en) * | 2015-06-30 | 2015-09-23 | 天津海泰环保科技发展有限公司 | Processing method and processing device for pitch flue gas |
Citations (4)
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US2750680A (en) * | 1952-08-02 | 1956-06-19 | Oxy Catalyst Inc | Method for treating materials |
US2795054A (en) * | 1954-10-07 | 1957-06-11 | Oxy Catalyst Inc | Method and apparatus for heat recovery from drying oven effluents |
US3706445A (en) * | 1971-09-30 | 1972-12-19 | Granco Equipment | Fume incinerator |
US3787171A (en) * | 1972-06-15 | 1974-01-29 | Hunter Eng Co | Closed loop, inert atmosphere, paint line oven heat source |
-
1973
- 1973-02-21 US US334257A patent/US3880143A/en not_active Expired - Lifetime
- 1973-09-24 CA CA181,728A patent/CA981546A/en not_active Expired
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2750680A (en) * | 1952-08-02 | 1956-06-19 | Oxy Catalyst Inc | Method for treating materials |
US2795054A (en) * | 1954-10-07 | 1957-06-11 | Oxy Catalyst Inc | Method and apparatus for heat recovery from drying oven effluents |
US3706445A (en) * | 1971-09-30 | 1972-12-19 | Granco Equipment | Fume incinerator |
US3787171A (en) * | 1972-06-15 | 1974-01-29 | Hunter Eng Co | Closed loop, inert atmosphere, paint line oven heat source |
Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1985005439A1 (en) * | 1983-03-07 | 1985-12-05 | Mechtron International Corp. | Asphalt recycle plant |
US4477250A (en) * | 1983-03-07 | 1984-10-16 | Mechtron International Corporation | Asphalt recycle plant and method |
US5090813A (en) * | 1990-07-23 | 1992-02-25 | Cedarapids, Inc. | Dual drum recycle asphalt drying and mixing method and apparatus |
US5174650A (en) * | 1990-07-23 | 1992-12-29 | Cedarapids, Inc. | Dual drum recycle asphalt drying and mixing method and apparatus |
US5176445A (en) * | 1990-08-10 | 1993-01-05 | Astec Industries, Inc. | Apparatus for decontaminating soils |
US5607231A (en) * | 1994-11-04 | 1997-03-04 | Gentec Equipment Company | Method for operating an asphalt plant for both continuous and batch operation |
US5556197A (en) * | 1994-11-04 | 1996-09-17 | Gentec Equipment Company | Asphalt plant for both continuous and batch operation |
US5943969A (en) * | 1994-12-14 | 1999-08-31 | Barnstead/Thermolyne Corporation | Ashing furnace and method |
US5799596A (en) * | 1994-12-14 | 1998-09-01 | Barnstead/Thermolyne Corporation | Ashing furnace and method |
US5558029A (en) * | 1994-12-14 | 1996-09-24 | Barnstead/Thermlyne Corporation | Ashing furnace and method |
US5873919A (en) * | 1995-06-07 | 1999-02-23 | Simon Roofing & Sheet Metal Corp. | System for removal of noxious fumes |
US6000935A (en) * | 1997-02-21 | 1999-12-14 | Troxler Electronic Laboratories, Inc | Adjustable apparatus for pyrolysis of a composite material and method of calibration therefor |
US20030099581A1 (en) * | 1997-07-09 | 2003-05-29 | Byrne Brian T. | Fume recovery apparatus and methods |
US6534020B1 (en) * | 1997-07-09 | 2003-03-18 | Garlock Equipment Co. | Fume recovery methods |
US6709637B2 (en) | 1997-07-09 | 2004-03-23 | Garlock Equipment Co. | Fume recovery apparatus and methods |
US6033629A (en) * | 1998-03-18 | 2000-03-07 | Barnstead/Thermolyne Corporation | Ashing furnace |
US6146007A (en) * | 1998-03-20 | 2000-11-14 | Cedarapids Inc. | Asphalt plant having centralized media burner and low fugitive emissions |
US6634780B1 (en) | 1998-03-20 | 2003-10-21 | Cedarapids Inc. | Asphalt plant having centralized media burner and low fugitive emissions |
US6065469A (en) * | 1999-01-08 | 2000-05-23 | Cleasby Manufacturing Company, Inc. | Emission control system for asphalt kettle |
US6109826A (en) * | 1999-06-03 | 2000-08-29 | Cimline, Inc. | Melter and applicator for applying filling material to paved surfaces |
CN104930523A (en) * | 2015-06-30 | 2015-09-23 | 天津海泰环保科技发展有限公司 | Processing method and processing device for pitch flue gas |
Also Published As
Publication number | Publication date |
---|---|
CA981546A (en) | 1976-01-13 |
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Owner name: UIPE PRODUCTS, INC., A NEVADA CORPORATION Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:U.I.P., ENGINEERED PRODUCTS CORP., A CORP. OF IL;REEL/FRAME:004950/0018 Effective date: 19880801 Owner name: UIPE PRODUCTS, INC.,STATELESS Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:U.I.P., ENGINEERED PRODUCTS CORP., A CORP. OF IL;REEL/FRAME:004950/0018 Effective date: 19880801 |
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Owner name: CONTINENTAL BANK N.A. Free format text: SECURITY INTEREST;ASSIGNOR:UIPE PRODUCTS, INC., A NEVADA CORP.;REEL/FRAME:005602/0230 Effective date: 19910208 Owner name: ROBOTRAC, INC., A CORP. OF ILLINOIS, ILLINOIS Free format text: SECURITY INTEREST;ASSIGNOR:UIPE PRODUCTS, INC., A CORP. OF ILLINOIS;REEL/FRAME:005597/0934 Effective date: 19910208 |
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Owner name: UIPE PRODUCTS, INC., ILLINOIS Free format text: RELEASE OF SECURITY INTEREST & ASSIGNMENT;ASSIGNOR:CONTINENTAL BANK N.A.;REEL/FRAME:006772/0257 Effective date: 19930930 |