WO1995012103A1 - Purge feeding means and method - Google Patents

Purge feeding means and method Download PDF

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Publication number
WO1995012103A1
WO1995012103A1 PCT/US1994/012312 US9412312W WO9512103A1 WO 1995012103 A1 WO1995012103 A1 WO 1995012103A1 US 9412312 W US9412312 W US 9412312W WO 9512103 A1 WO9512103 A1 WO 9512103A1
Authority
WO
WIPO (PCT)
Prior art keywords
chamber
solid material
interlocking solid
rotatable
rotated
Prior art date
Application number
PCT/US1994/012312
Other languages
French (fr)
Inventor
Vahan Avetisian
Constantin Bugescu
Craig Joseph Gastagnoli
Suk-Bae Cha
Original Assignee
Texaco Development Corporation
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to AU80932/94A priority Critical patent/AU678639B2/en
Priority to DK94932068T priority patent/DK0725920T3/en
Priority to US08/637,692 priority patent/US5720854A/en
Priority to BR9407915A priority patent/BR9407915A/en
Priority to DE69410284T priority patent/DE69410284T2/en
Priority to PL94314137A priority patent/PL314137A1/en
Application filed by Texaco Development Corporation filed Critical Texaco Development Corporation
Priority to SK543-96A priority patent/SK54396A3/en
Priority to EP94932068A priority patent/EP0725920B1/en
Publication of WO1995012103A1 publication Critical patent/WO1995012103A1/en
Priority to BG100523A priority patent/BG100523A/en
Priority to NO961619A priority patent/NO961619L/en
Priority to FI961807A priority patent/FI961807A0/en

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D88/00—Large containers
    • B65D88/54—Large containers characterised by means facilitating filling or emptying
    • B65D88/64—Large containers characterised by means facilitating filling or emptying preventing bridge formation
    • B65D88/68—Large containers characterised by means facilitating filling or emptying preventing bridge formation using rotating devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B33/00—Discharging devices; Coke guides
    • C10B33/02—Extracting coke with built-in devices, e.g. gears, screws

Definitions

  • the present invention relates to means and method for feeding interlocking solid material to process apparatus and, more particularly, to means and method for feeding shredded tires to a tire liquefaction process apparatus.
  • the present invention is a purge chamber which includes a chamber for holding interlocking solid material.
  • An entrance port apparatus passes the interlocking solid material into the chamber where it is purged by a purging gas.
  • An exit port apparatus passes the solid interlocking solid material from the chamber.
  • moving apparatus which moved the interlocking solid material from the chamber through the exit port apparatus.
  • yet another apparatus which prevent the binding of the interlocking solid material.
  • Fig. 1 is a graphical representation of apparatus, constructed in accordance with the present invention, for the purge feeding of interlocking solid material to process apparatus.
  • Fig. 2 is a isometric view of the chamber shown in Fig. 1.
  • interlocking solid material refers to solid substances that, because of their shape and/or composition, have a strong tendency to knit together like entangled yarn. While the primary example of the present invention is related to discharging shredded tire pieces, other applications, such as woodchips, reinforce plastics and scrap may also be applicable.
  • a chamber 3 with a top feed port 7 has support members 15 to give it greater strength.
  • hanger bars 22 which are used to support a material drive system including a drive motor 27.
  • a drive shaft 36, rotated by motor 27, is connected to a gear reducer 44.
  • Gear reducer 44 also provides a 90°F translation of the driving force to another drive shaft 52.
  • a bearing 56 mounted on a mounting plate 58 having being held in place by support members 65.
  • an exit port 72 At the bottom of chamber 3 is an exit port 72.
  • screw auger 80 Connected to drive shaft 52 is a screw auger 80.
  • screw auger 80 might have an 10-inch diameter centered over a 16-inch outlet port 72.
  • a pair of cylinders 88 Arranged on either side of screw auger 80 are a pair of cylinders 88 having a plurality of lugs 96 mounted in a predetermined manner thereon. i should be noted that the bottom of chamber 3 is curved so as not to create any dead space between the lugs 96 on cylinder 88 and the bottom of chamber 3.
  • Motor drive means for rotating cylinders 88 on axles 104 are not shown but their location would be obvious to one skilled in the art.
  • the rotations of cylinders 88 may be any one of a combination of three movements with both cylinders 88 being rotated clockwise, both cylinders 88 being rotated counterclockwise or having one cylinder being rotated clockwise and the other cylinder being rotated counterclockwise.
  • Cylinder 88 may be rotated at a rotational speed that may be from 1/lOth to 1/2 the speed of screw auger 80.
  • feed valve means 120 and discharge valve means 126 are simply conventional style gate valves that will allow the feed to enter chamber 3 and allow the feed material to exit chamber 3.
  • a source of nitrogen 135 which provides purging nitrogen to chamber 3 through a line 140 including a valve 148.
  • the system of the present invention contemplates batch feeding of a tire liquefaction processing apparatus by having the interlocking solid material, namely the shredded tires, enter through valve means 120 which is then closed.
  • discharge valve means 125 being closed prevents any of the shredded tires from entering the processing apparatus.
  • valve 148 With both valve means 120 and 125 closed, valve 148 is open to allow nitrogen to enter chamber 3 to purge the oxygen that has entered with the tires. After the oxygen level has dropped to a suitable level, valve 148 is closed, discharge valve 125 is opened, and motors 27 and motors not shown are energized causing the screw auger 80 to rotate driving the shredded tire material out of bin 3. However, as happens in many cases, the shredded tire will bind because of their interlocking nature. Screw auger 80 then has a tendency to tunnel through the bound material. When binding occurs, only the tire material within the range of screw auger 80 would be moved. It is at this junction that the operations of cylinders 88 by their motor drive means keep the tire material in motion so that the tire material is being fed to auger screw 80 and thus preventing the tunneling effect.
  • discharge valve means 125 Upon removal of the shredded tire material from bin 3, discharge valve means 125 maybe closed and the system shut down until the next batch is ready to be processed.

Abstract

The present invention includes a purge chamber which includes a chamber (3) holding the interlocking solid material. An entrance port apparatus (120) passes the interlocking solid material into the chamber (3) where it is purged by a purging gas (135). An exit port apparatus (65) passes the solid interlocking material from the chamber. Located within the chamber is other apparatus (80) which moved the interlocking solid material from the chamber through the exit port apparatus. Further, located within the chamber is yet other apparatus (88) which prevents the binding of the interlocking solid material.

Description

PURGE FEEDING MEANS AND METHOD
BACKGROUND OF THE INVENTION
Field of the Invention
The present invention relates to means and method for feeding interlocking solid material to process apparatus and, more particularly, to means and method for feeding shredded tires to a tire liquefaction process apparatus.
SUMMARY OF THE INVENTION
The present invention is a purge chamber which includes a chamber for holding interlocking solid material. An entrance port apparatus passes the interlocking solid material into the chamber where it is purged by a purging gas. An exit port apparatus passes the solid interlocking solid material from the chamber. Located within the chamber is moving apparatus which moved the interlocking solid material from the chamber through the exit port apparatus. Further, located within the chamber, is yet another apparatus which prevent the binding of the interlocking solid material.
The objectives and advantages of the invention will appear more fully hereinafter from a consideration of the detailed description which follows, taking together with the accompanying drawings, wherein one embodiment of the invention is illustrated by way of example. It is to be expressly understood, however, that the drawings are for illustration purposes and are not to be construed as defining the limits of the invention.
DESCRIPTION OF THE DRAWINGS
Fig. 1 is a graphical representation of apparatus, constructed in accordance with the present invention, for the purge feeding of interlocking solid material to process apparatus.
Fig. 2 is a isometric view of the chamber shown in Fig. 1.
DESCRIPTION OF THE INVENTION
Referring to Figs. 1 and 2, there is shown apparatus for the purging of interlocking solid materials in a sealed chamber. The phrase "interlocking solid material" refers to solid substances that, because of their shape and/or composition, have a strong tendency to knit together like entangled yarn. While the primary example of the present invention is related to discharging shredded tire pieces, other applications, such as woodchips, reinforce plastics and scrap may also be applicable.
In the discharging of shredded tire material to feed a tire liquefaction process, as described and disclosed in U.S.P. Application, Serial No. 08/053,727 filed April 27, 1993, the shredded tire material is contacted with oil at a temperature of 700°F. It is required, therefore, that the material be purged of oxygen prior to introduction into the liquefaction reactor. The present invention is for apparatus and method for doing that.
A chamber 3 with a top feed port 7 has support members 15 to give it greater strength. Located within chamber 3 are hanger bars 22 which are used to support a material drive system including a drive motor 27. A drive shaft 36, rotated by motor 27, is connected to a gear reducer 44. Gear reducer 44 also provides a 90°F translation of the driving force to another drive shaft 52. Associated with drive shaft 52 is a bearing 56 mounted on a mounting plate 58 having being held in place by support members 65. At the bottom of chamber 3 is an exit port 72.
Connected to drive shaft 52 is a screw auger 80. By way of example, screw auger 80 might have an 10-inch diameter centered over a 16-inch outlet port 72. Arranged on either side of screw auger 80 are a pair of cylinders 88 having a plurality of lugs 96 mounted in a predetermined manner thereon. i should be noted that the bottom of chamber 3 is curved so as not to create any dead space between the lugs 96 on cylinder 88 and the bottom of chamber 3. Motor drive means for rotating cylinders 88 on axles 104 are not shown but their location would be obvious to one skilled in the art. The rotations of cylinders 88 may be any one of a combination of three movements with both cylinders 88 being rotated clockwise, both cylinders 88 being rotated counterclockwise or having one cylinder being rotated clockwise and the other cylinder being rotated counterclockwise. Cylinder 88 may be rotated at a rotational speed that may be from 1/lOth to 1/2 the speed of screw auger 80.
Also shown in Fig. 1 is feed valve means 120 and discharge valve means 126. These are simply conventional style gate valves that will allow the feed to enter chamber 3 and allow the feed material to exit chamber 3. Also shown in a simplified box diagram format, is a source of nitrogen 135 which provides purging nitrogen to chamber 3 through a line 140 including a valve 148. As shown, the system of the present invention contemplates batch feeding of a tire liquefaction processing apparatus by having the interlocking solid material, namely the shredded tires, enter through valve means 120 which is then closed. In the meantime, discharge valve means 125 being closed prevents any of the shredded tires from entering the processing apparatus.
With both valve means 120 and 125 closed, valve 148 is open to allow nitrogen to enter chamber 3 to purge the oxygen that has entered with the tires. After the oxygen level has dropped to a suitable level, valve 148 is closed, discharge valve 125 is opened, and motors 27 and motors not shown are energized causing the screw auger 80 to rotate driving the shredded tire material out of bin 3. However, as happens in many cases, the shredded tire will bind because of their interlocking nature. Screw auger 80 then has a tendency to tunnel through the bound material. When binding occurs, only the tire material within the range of screw auger 80 would be moved. It is at this junction that the operations of cylinders 88 by their motor drive means keep the tire material in motion so that the tire material is being fed to auger screw 80 and thus preventing the tunneling effect.
Upon removal of the shredded tire material from bin 3, discharge valve means 125 maybe closed and the system shut down until the next batch is ready to be processed.

Claims

WHAT IS CLAIMED IS:
1. A purge chamber comprising: chamber means for holding interlocking solid material, entrance port means connected to the 5 chamber means for passing the interlocking solid material into the chamber means, purge means connected to the chamber means for providing a purging gas to the chamber means, exit port means connected to the chamber 0 means for passing the interlocking solid material from the chamber means, discharge means located in the chamber means for moving the interlocking solid material from the chamber means through the exit port means, and 5 prevent means, located within the chamber means for preventing the binding of the interlocking solid material.
2. A chamber as described in Claim 1 in which the discharge means includes: auger screw means for moving the interlocking solid material from within the chamber means into = the exit port means when rotated, and means for rotating the auger screw means.
3. A chamber as described in Claim 2 further comprising anti-binding means for preventing the interlocking solid material from binding around the auger screw means.
*
4. A chamber as described in Claim 3 in which the anti-binding means includes at least at two rotatable means, each rotatable means rotating around an axis substantially perpendicular to the longitudinal axis of the auger screw J means.
5. A chamber as described in Claim 4, in which the axis or rotation for each rotatable means is substantially parallel to the axis rotation for the other rotatable means.
6. A chamber as described in Claim 5 in which each rotatable means includes: a shaft, motor means connected to the shaft for rotating the shaft, a cylinder of a larger diameter affixed to and enclosing the shaft so that as the shaft rotates, the cylinder rotates too, and a plurality of lugs arranged on the cylinder for breaking up the interlocking solid material so as to prevent binding.
7. A chamber as described in Claim 6. in which the auger screw means is preferably being rotated at 20 revolutions per minute.
8. A chamber as described in Claim 7 in which each rotatable means is rotated at a frequency of 1/lθth to 1/2 the rotational speed of the auger screw means.
9. A system as described in Claim 8 in which each rotatable means is rotated in the same rotational direction.
10. A chamber as described in Claim 8 in which the rotatable means are rotated in opposite directions.
PCT/US1994/012312 1993-10-28 1994-10-27 Purge feeding means and method WO1995012103A1 (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
DK94932068T DK0725920T3 (en) 1993-10-28 1994-10-27 Cleaning chamber
US08/637,692 US5720854A (en) 1993-10-28 1994-10-27 Purge feeding means and method
BR9407915A BR9407915A (en) 1993-10-28 1994-10-27 Purge feeding device and method
DE69410284T DE69410284T2 (en) 1993-10-28 1994-10-27 Rinsing chamber
PL94314137A PL314137A1 (en) 1993-10-28 1994-10-27 Means for and method of purifying materials being feed to a processing equipment
AU80932/94A AU678639B2 (en) 1993-10-28 1994-10-27 Purge feeding means
SK543-96A SK54396A3 (en) 1993-10-28 1994-10-27 Purge feeding means and method
EP94932068A EP0725920B1 (en) 1993-10-28 1994-10-27 Purge chamber
BG100523A BG100523A (en) 1993-10-28 1996-04-19 Method and device for solid waste treatment
NO961619A NO961619L (en) 1993-10-28 1996-04-23 Flushing Chamber
FI961807A FI961807A0 (en) 1993-10-28 1996-04-26 Flush feed type and method

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/142,020 1993-10-28
US08/142,020 US5433018A (en) 1993-10-28 1993-10-28 Purge feeding means and method

Publications (1)

Publication Number Publication Date
WO1995012103A1 true WO1995012103A1 (en) 1995-05-04

Family

ID=22498234

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1994/012312 WO1995012103A1 (en) 1993-10-28 1994-10-27 Purge feeding means and method

Country Status (18)

Country Link
US (2) US5433018A (en)
EP (1) EP0725920B1 (en)
JP (1) JP2743218B2 (en)
CN (1) CN1047840C (en)
AU (1) AU678639B2 (en)
BG (1) BG100523A (en)
BR (1) BR9407915A (en)
CA (1) CA2175244A1 (en)
DE (1) DE69410284T2 (en)
DK (1) DK0725920T3 (en)
FI (1) FI961807A0 (en)
HU (1) HUT74214A (en)
NO (1) NO961619L (en)
NZ (1) NZ275342A (en)
PL (1) PL314137A1 (en)
SK (1) SK54396A3 (en)
TW (1) TW267130B (en)
WO (1) WO1995012103A1 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5433018A (en) * 1993-10-28 1995-07-18 Texaco Inc. Purge feeding means and method
AU2005257982B8 (en) * 2004-06-16 2011-03-10 Jack Arbiser Carbazole formulations for the treatment of psoriasis and angiogenesis
CN104650932A (en) * 2009-10-14 2015-05-27 瑞克莱姆股份有限公司 Pyrolysis process and products
DE102016121232A1 (en) * 2016-11-07 2018-05-09 Walter Geroldinger PROCESS FOR PROCESSES IN THE BULK BY MEASURING GASES
CN115231335B (en) * 2022-08-01 2023-05-26 赣州步莱铽新资源有限公司 Continuous rare earth waste quantitative discharging device

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US2351706A (en) * 1943-11-16 1944-06-20 Robinson Thomas Apparatus for treating plastic material in a controlled atmosphere
US3766664A (en) * 1972-08-08 1973-10-23 K Burgin Grain circulating system
US4499669A (en) * 1982-09-30 1985-02-19 Miller Hofft, Inc. Combination dryer and surge bin
US4652289A (en) * 1984-11-26 1987-03-24 Hydro-Quebec Purification of effluent gases
US4932785A (en) * 1988-06-21 1990-06-12 Bracegirdle P E Aggregate drying system with improved aggregate dryer and mass flow apparatus
US5074225A (en) * 1989-10-18 1991-12-24 Petrie A Stephen Mechanism for feeding solid materials
US5129995A (en) * 1990-02-01 1992-07-14 General Motors Corporation Pyrolysis process and apparatus

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US4235676A (en) * 1977-09-16 1980-11-25 Deco Industries, Inc. Apparatus for obtaining hydrocarbons from rubber tires and from industrial and residential waste
US4250158A (en) * 1978-02-15 1981-02-10 Intenco, Inc. Process for recovering carbon black and hydrocarbons from used tires
US4255129A (en) * 1979-07-11 1981-03-10 Thomas N. DePew Apparatus and method for processing organic materials into more useful states
US4474524A (en) * 1981-03-30 1984-10-02 Kabushiki Kaisha Kobe Seiko Sho System for discharging thermal decomposition residue containing carbon residue and steel wire balls
US4454427A (en) * 1981-11-10 1984-06-12 Leon Sosnowski Incinerator and fume separator system and apparatus
CA1225062A (en) * 1983-09-13 1987-08-04 Trevor R. Bridle Processes and apparatus for the conversion of sludges
US4686008A (en) * 1985-10-08 1987-08-11 Gibson Harry T Pyrolytic decomposition apparatus
US5037628A (en) * 1987-08-14 1991-08-06 American Tire Reclamation, Inc. Method for reclaiming carbonaceous material from a waste material
US4900401A (en) * 1988-06-20 1990-02-13 Horton Norman P Continuous pyrolysis system for tire shreds
US4889556A (en) * 1988-08-01 1989-12-26 Westinghouse Electric Corp. Method of recycling steel belted tires
US5157176A (en) * 1990-07-26 1992-10-20 Munger Joseph H Recycling process, apparatus and product produced by such process for producing a rubber extender/plasticizing agent from used automobile rubber tires
US5095040A (en) * 1991-02-11 1992-03-10 Ledford Charles D Process for conveying old rubber tires into oil and a useful residue
US5127588A (en) * 1991-02-11 1992-07-07 Tire Service Equipment Mfg. Co. Inc. Tire chipper
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US5464503A (en) * 1993-10-28 1995-11-07 Texaco Inc. Tire liquefying process reactor discharge system and method
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US5423950A (en) * 1993-10-28 1995-06-13 Texaco Inc. Method and reactor for producing tire oil

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2351706A (en) * 1943-11-16 1944-06-20 Robinson Thomas Apparatus for treating plastic material in a controlled atmosphere
US3766664A (en) * 1972-08-08 1973-10-23 K Burgin Grain circulating system
US4499669A (en) * 1982-09-30 1985-02-19 Miller Hofft, Inc. Combination dryer and surge bin
US4652289A (en) * 1984-11-26 1987-03-24 Hydro-Quebec Purification of effluent gases
US4932785A (en) * 1988-06-21 1990-06-12 Bracegirdle P E Aggregate drying system with improved aggregate dryer and mass flow apparatus
US5074225A (en) * 1989-10-18 1991-12-24 Petrie A Stephen Mechanism for feeding solid materials
US5129995A (en) * 1990-02-01 1992-07-14 General Motors Corporation Pyrolysis process and apparatus

Non-Patent Citations (1)

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Title
See also references of EP0725920A4 *

Also Published As

Publication number Publication date
DE69410284T2 (en) 1998-09-03
FI961807A (en) 1996-04-26
AU8093294A (en) 1995-05-22
BR9407915A (en) 1996-11-26
CN1047840C (en) 1999-12-29
AU678639B2 (en) 1997-06-05
NO961619D0 (en) 1996-04-23
NO961619L (en) 1996-04-23
JP2743218B2 (en) 1998-04-22
DE69410284D1 (en) 1998-06-18
TW267130B (en) 1996-01-01
PL314137A1 (en) 1996-08-19
SK54396A3 (en) 1998-07-08
BG100523A (en) 1997-04-30
HU9601110D0 (en) 1996-07-29
JPH09502673A (en) 1997-03-18
HUT74214A (en) 1996-11-28
DK0725920T3 (en) 1998-10-07
US5720854A (en) 1998-02-24
EP0725920B1 (en) 1998-05-13
EP0725920A1 (en) 1996-08-14
CA2175244A1 (en) 1995-05-04
US5433018A (en) 1995-07-18
CN1134188A (en) 1996-10-23
FI961807A0 (en) 1996-04-26
EP0725920A4 (en) 1996-10-30
NZ275342A (en) 1997-04-24

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