WO2001096495A1 - Deflecteur d'un four a coke a buse d'evacuation surelevee, et procede correspondant - Google Patents
Deflecteur d'un four a coke a buse d'evacuation surelevee, et procede correspondant Download PDFInfo
- Publication number
- WO2001096495A1 WO2001096495A1 PCT/US2001/040875 US0140875W WO0196495A1 WO 2001096495 A1 WO2001096495 A1 WO 2001096495A1 US 0140875 W US0140875 W US 0140875W WO 0196495 A1 WO0196495 A1 WO 0196495A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- coke drum
- aperture
- deflector
- solids
- drum
- 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.)
- Ceased
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
-
- 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
- C10B1/00—Retorts
- C10B1/02—Stationary retorts
- C10B1/04—Vertical retorts
-
- 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
- C10B27/00—Arrangements for withdrawal of the distillation gases
- C10B27/06—Conduit details, e.g. valves
-
- 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
- C10B55/00—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
Definitions
- the present invention relates to delayed coking. More particularly, the present
- invention relates to a deflector placed inside the top of a coke drum and below the overhead
- feedstock is introduced to
- Overhead vapors from the drum being filled return to a
- the coke drum or drums may be operating under higher than atmospheric
- the present invention provides a deflector in the top coke drum
- the deflector is placed below and spaced from the overhead vapor nozzle outlet
- An even further object of the present invention is to provide a deflector improvement
- Still another object of the present invention is to provide a new and improved
- delayed coking unit which is more efficient and of a durable and reliable construction.
- delayed coking unit which maximizes input into a coke drum without blowing coke, liquid
- Figure 1 is a schematic view of a delayed coking process to which the present invention may be applied.
- Figure 2 is a side elevation, partly in cross section, showing details of a coke drum and deflector constructed in accordance with the present invention.
- Figure 3 is a perspective view, partly in cross section, showing details of a coke drum and a conical deflector in accordance with an alternate embodiment of the present invention.
- FIG. 1 shows a simplified, typical coker unit where coker feed from line 10 passes
- Coke drums 14 and 16 are alternately filled and emptied. When a drum
- a recycle liquid such as coker gas oil or coker feedstock is feed into
- fractionator 20 via line 22.
- a wet gas overhead stream is removed from fractionator 20 via line 22.
- Overhead vapor outlet nozzle 38 is preferably
- outlet nozzle may range from between approximately 24 to 30 inches (61 to 76 cm).
- FIG. 1 is partially cut away for clarity.
- the invention includes the addition of
- deflector 40 placed generally below and spaced from aperture 36 in the coke drum 14 and
- Deflector 40 is generally removably attached by an attachment mechanism 42 to overhead vapor outlet nozzle 38.
- deflector 40 is preferably suspended 1 (one) to 10 (ten) feet below overhead
- attachment means are brackets, bolts, wires, hooks,
- deflector 40 is preferably a circular plate made from metal or
- the diameter of the plate will be slightly less than the diameter of the aperture.
- deflector 40 is a generally conically shaped
- deflector 44 as shown in Figure 3 where apex tip 46 of the cone points toward overhead
- the center point of the aperture is generally aligned with the apex
- the deflector might take the form of a pair of
- escaping vapors are forced to take a circuitous route.
- feed heated in the furnace is delivered to the drum and thermally decomposes.
- Vapors in the drum will rise toward the aperture. Liquid droplets and solid particles will rise toward the aperture. Liquid droplets and solid particles will rise toward the aperture. Liquid droplets and solid particles will rise toward the aperture. Liquid droplets and solid particles will rise toward the aperture. Liquid droplets and solid particles will rise toward the aperture. Liquid droplets and solid particles will rise toward the aperture. Liquid droplets and solid particles will rise toward the aperture. Liquid droplets and solid particles will rise toward the aperture.
- the deflector may be suspended from the overhead vapor outlet
- the present invention provides a coke drum for a delayed coking unit
- said coke drum comprises:
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Coke Industry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU2001265427A AU2001265427A1 (en) | 2000-06-13 | 2001-06-07 | Coke drum outlet overhead deflector plate apparatus and method |
| BR0106726-5A BR0106726A (pt) | 2000-06-13 | 2001-06-07 | Tambor de coque para unidade de coqueificação retardada e processo de reduzir o escapamento de sólidos e de lìquidos de hidrocarboneto pesados a partir de um tambor de coque |
| MXPA02001551A MXPA02001551A (es) | 2000-06-13 | 2001-06-07 | Aparato y metodo de placa deflectora aerea de salida para cilindro de coque. |
| JP2002510618A JP2004503658A (ja) | 2000-06-13 | 2001-06-07 | コーク・ドラム出口の天井デフレクタ装置および方法 |
| CA002382283A CA2382283A1 (fr) | 2000-06-13 | 2001-06-07 | Deflecteur d'un four a coke a buse d'evacuation surelevee, et procede correspondant |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US21143800P | 2000-06-13 | 2000-06-13 | |
| US60/211,438 | 2000-06-13 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2001096495A1 true WO2001096495A1 (fr) | 2001-12-20 |
| WO2001096495A8 WO2001096495A8 (fr) | 2002-03-07 |
Family
ID=22786925
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2001/040875 Ceased WO2001096495A1 (fr) | 2000-06-13 | 2001-06-07 | Deflecteur d'un four a coke a buse d'evacuation surelevee, et procede correspondant |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US20020117389A1 (fr) |
| JP (1) | JP2004503658A (fr) |
| CN (1) | CN1383447A (fr) |
| AU (1) | AU2001265427A1 (fr) |
| BR (1) | BR0106726A (fr) |
| CA (1) | CA2382283A1 (fr) |
| MX (1) | MXPA02001551A (fr) |
| MY (1) | MY133973A (fr) |
| WO (1) | WO2001096495A1 (fr) |
| ZA (1) | ZA200201088B (fr) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2364492A (en) * | 1941-05-31 | 1944-12-05 | Max B Miller & Co Inc | Method of coking and cracking petroleum residues or the like |
| DD154612A1 (de) * | 1980-11-21 | 1982-04-07 | Manfred Gross | Verfahren zur verkokung von kohlenwasserstoffen nach der blasentechnologie |
| WO1998001512A1 (fr) * | 1996-07-10 | 1998-01-15 | Citgo Petroleum Corporation | Procede de conception et de fabrication d'une cuve a coke differee |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3816084A (en) * | 1970-04-16 | 1974-06-11 | Exxon Research Engineering Co | Cokeless coker with recycle of coke from gasifier to heater |
| US4549934A (en) * | 1984-04-25 | 1985-10-29 | Conoco, Inc. | Flash zone draw tray for coker fractionator |
| US4621724A (en) * | 1984-09-13 | 1986-11-11 | Foster Wheeler Energy Corporation | Fractionator having reduced product vapor condensation in the flash zone |
| US4801402A (en) * | 1985-11-12 | 1989-01-31 | Texaco Inc. | Partial oxidation process |
| US4816136A (en) * | 1986-05-27 | 1989-03-28 | Exxon Research And Engineering Company | Low severity fluid coking |
| US5645711A (en) * | 1996-01-05 | 1997-07-08 | Conoco Inc. | Process for upgrading the flash zone gas oil stream from a delayed coker |
-
2001
- 2001-06-04 US US09/873,561 patent/US20020117389A1/en not_active Abandoned
- 2001-06-07 CN CN01801729A patent/CN1383447A/zh active Pending
- 2001-06-07 BR BR0106726-5A patent/BR0106726A/pt not_active IP Right Cessation
- 2001-06-07 JP JP2002510618A patent/JP2004503658A/ja active Pending
- 2001-06-07 WO PCT/US2001/040875 patent/WO2001096495A1/fr not_active Ceased
- 2001-06-07 CA CA002382283A patent/CA2382283A1/fr not_active Abandoned
- 2001-06-07 AU AU2001265427A patent/AU2001265427A1/en not_active Abandoned
- 2001-06-07 MX MXPA02001551A patent/MXPA02001551A/es unknown
- 2001-06-12 MY MYPI20012745 patent/MY133973A/en unknown
-
2002
- 2002-02-07 ZA ZA200201088A patent/ZA200201088B/en unknown
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2364492A (en) * | 1941-05-31 | 1944-12-05 | Max B Miller & Co Inc | Method of coking and cracking petroleum residues or the like |
| DD154612A1 (de) * | 1980-11-21 | 1982-04-07 | Manfred Gross | Verfahren zur verkokung von kohlenwasserstoffen nach der blasentechnologie |
| WO1998001512A1 (fr) * | 1996-07-10 | 1998-01-15 | Citgo Petroleum Corporation | Procede de conception et de fabrication d'une cuve a coke differee |
Also Published As
| Publication number | Publication date |
|---|---|
| ZA200201088B (en) | 2003-07-25 |
| CA2382283A1 (fr) | 2001-12-20 |
| US20020117389A1 (en) | 2002-08-29 |
| MXPA02001551A (es) | 2003-07-21 |
| BR0106726A (pt) | 2002-04-30 |
| WO2001096495A8 (fr) | 2002-03-07 |
| MY133973A (en) | 2007-11-30 |
| JP2004503658A (ja) | 2004-02-05 |
| CN1383447A (zh) | 2002-12-04 |
| AU2001265427A1 (en) | 2001-12-24 |
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