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ECSP13012731A - Método, sistema y aparato para la separación en el procesamiento de materias primas - Google Patents

Método, sistema y aparato para la separación en el procesamiento de materias primas

Info

Publication number
ECSP13012731A
ECSP13012731A ECSP13012731A ECSP13012731A EC SP13012731 A ECSP13012731 A EC SP13012731A EC SP13012731 A ECSP13012731 A EC SP13012731A EC SP13012731 A ECSP13012731 A EC SP13012731A
Authority
EC
Ecuador
Prior art keywords
tubular container
barrel
solids
separation
square tube
Prior art date
Application number
Other languages
English (en)
Inventor
Stephen K Pavel
Steven A Kalota
Original Assignee
Ivanhoe Energy Inc
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=45524995&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=ECSP13012731(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Ivanhoe Energy Inc filed Critical Ivanhoe Energy Inc
Publication of ECSP13012731A publication Critical patent/ECSP13012731A/es

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/02—Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
    • B04C5/04—Tangential inlets
    • 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
    • B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • 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
    • B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
    • B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B04C5/15—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations with swinging flaps or revolving sluices; Sluices; Check-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
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/16—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form
    • C10B49/20—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form in dispersed form
    • C10B49/22—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form in dispersed form according to the "fluidised bed" technique
    • 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
    • C10B55/02—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials
    • C10B55/04—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials
    • C10B55/08—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials in dispersed form
    • C10B55/10—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials in dispersed form according to the "fluidised bed" technique
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Fluid Mechanics (AREA)
  • Physics & Mathematics (AREA)
  • Combustion & Propulsion (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Cyclones (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Centrifugal Separators (AREA)

Abstract

Se divulga un método, sistema y aparato para la separación en el procesamiento de materias primas. De acuerdo con una realización, un aparato comprende un recipiente tubular que tiene una entrada de tubo cuadrado y una salida de vapor, donde la salida de vapor está ubicada en la parte superior del recipiente tubular, y donde la entrada de tubo cuadrado es tangencial a un diámetro interior del recipiente tubular; un barril ubicado debajo del recipiente tubular; y una válvula de cuchilla de doble aislamiento ubicada entre el recipiente tubular y el barril, donde una corriente de gas y sólidos entra al recipiente tubular a través de la entrada de tubo cuadrado, y donde el gas y los sólidos se separaran usando fuerza centrífuga, y donde el gas sale por la salida de vapor y los sólidos se recogen en el barril.
ECSP13012731 2010-12-30 2013-07-03 Método, sistema y aparato para la separación en el procesamiento de materias primas ECSP13012731A (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US201061428316P 2010-12-30 2010-12-30

Publications (1)

Publication Number Publication Date
ECSP13012731A true ECSP13012731A (es) 2013-10-31

Family

ID=45524995

Family Applications (1)

Application Number Title Priority Date Filing Date
ECSP13012731 ECSP13012731A (es) 2010-12-30 2013-07-03 Método, sistema y aparato para la separación en el procesamiento de materias primas

Country Status (12)

Country Link
US (2) US9162171B2 (es)
EP (1) EP2658631A2 (es)
JP (1) JP2014503353A (es)
CN (1) CN103429311A (es)
BR (1) BR112013016550A2 (es)
CA (1) CA2823209C (es)
CO (1) CO6761359A2 (es)
EA (1) EA201390989A1 (es)
EC (1) ECSP13012731A (es)
MX (1) MX2013007721A (es)
PE (1) PE20140205A1 (es)
WO (1) WO2012092613A2 (es)

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AU2011323198B2 (en) 2010-11-05 2015-06-18 Thermochem Recovery International, Inc. Solids circulation system and method for capture and conversion of reactive solids
CN103958398B (zh) 2011-09-27 2016-01-06 国际热化学恢复股份有限公司 合成气净化系统和方法
SE538725C2 (sv) 2014-06-26 2016-11-01 Valmet Oy Ångavskiljningsenhet och system för hydrolysförfarande innefattande en ångavskiljningsenhet
CN104785065A (zh) * 2015-05-13 2015-07-22 常州禹豪防水科技有限公司 沥青废气处理装置及其处理工艺
UY37068A (es) * 2016-01-06 2017-07-31 Oren Tech Llc Transportador con sistema integrado de recoleccion de polvo
WO2017142515A1 (en) 2016-02-16 2017-08-24 Thermochem Recovery International, Inc., Two-stage energy-integrated product gas generation system and method
EP3433340B1 (en) 2016-03-25 2022-06-29 ThermoChem Recovery International, Inc. Three-stage energy-integrated product gas generation system
US10364398B2 (en) 2016-08-30 2019-07-30 Thermochem Recovery International, Inc. Method of producing product gas from multiple carbonaceous feedstock streams mixed with a reduced-pressure mixing gas
US10329506B2 (en) * 2017-04-10 2019-06-25 Thermochem Recovery International, Inc. Gas-solids separation system having a partitioned solids transfer conduit
US10717102B2 (en) 2017-05-31 2020-07-21 Thermochem Recovery International, Inc. Pressure-based method and system for measuring the density and height of a fluidized bed
US9920926B1 (en) 2017-07-10 2018-03-20 Thermochem Recovery International, Inc. Pulse combustion heat exchanger system and method
US10099200B1 (en) 2017-10-24 2018-10-16 Thermochem Recovery International, Inc. Liquid fuel production system having parallel product gas generation
WO2020168062A1 (en) * 2019-02-15 2020-08-20 Exxonmobil Chemical Patents Inc. Coke and tar removal from a furnace effluent
US11555157B2 (en) 2020-03-10 2023-01-17 Thermochem Recovery International, Inc. System and method for liquid fuel production from carbonaceous materials using recycled conditioned syngas
US11466223B2 (en) 2020-09-04 2022-10-11 Thermochem Recovery International, Inc. Two-stage syngas production with separate char and product gas inputs into the second stage
CN114042355B (zh) * 2021-09-27 2023-03-21 浙江中烟工业有限责任公司 烟叶原料流化床干馏产物过滤系统及其旋风分离工艺
CN116839039B (zh) * 2023-06-26 2024-03-01 蓝途金汇(北京)环保科技有限公司 一种垃圾焚烧处理与能源利用模块化装配式设备

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Also Published As

Publication number Publication date
EP2658631A2 (en) 2013-11-06
PE20140205A1 (es) 2014-03-08
WO2012092613A3 (en) 2012-09-27
CA2823209A1 (en) 2012-07-05
CO6761359A2 (es) 2013-09-30
EA201390989A1 (ru) 2014-06-30
WO2012092613A2 (en) 2012-07-05
CN103429311A (zh) 2013-12-04
US20120167767A1 (en) 2012-07-05
JP2014503353A (ja) 2014-02-13
US9162171B2 (en) 2015-10-20
MX2013007721A (es) 2013-11-04
BR112013016550A2 (pt) 2016-09-27
US20160001304A1 (en) 2016-01-07
CA2823209C (en) 2016-07-19

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