RU2005104559A - CURVE TUBE SEPARATOR - Google Patents

CURVE TUBE SEPARATOR Download PDF

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Publication number
RU2005104559A
RU2005104559A RU2005104559/15A RU2005104559A RU2005104559A RU 2005104559 A RU2005104559 A RU 2005104559A RU 2005104559/15 A RU2005104559/15 A RU 2005104559/15A RU 2005104559 A RU2005104559 A RU 2005104559A RU 2005104559 A RU2005104559 A RU 2005104559A
Authority
RU
Russia
Prior art keywords
gas
solid particles
cylindrical body
separator
vortex tube
Prior art date
Application number
RU2005104559/15A
Other languages
Russian (ru)
Other versions
RU2326717C2 (en
Inventor
Томас Шон ДЕВИЦ (US)
Томас Шон ДЕВИЦ
Хюбертус Вилхелмус Албертус ДРИС (NL)
Хюбертус Вилхелмус Албертус ДРИС
Андреас ЭККЕР (NL)
Андреас ЭККЕР
Ян КАТЕР (NL)
Ян КАТЕР
Ричард Эддисон СЭНБОРН (US)
Ричард Эддисон СЭНБОРН
Алекс Кристиан ХОФФМАН (NO)
Алекс Кристиан ХОФФМАН
Вейминг ПЕНГ (NO)
Вейминг ПЕНГ
Original Assignee
Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL)
Шелл Интернэшнл Рисерч Маатсхаппий Б.В.
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
Application filed by Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL), Шелл Интернэшнл Рисерч Маатсхаппий Б.В. filed Critical Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL)
Publication of RU2005104559A publication Critical patent/RU2005104559A/en
Application granted granted Critical
Publication of RU2326717C2 publication Critical patent/RU2326717C2/en

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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
    • B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B04C5/181—Bulkheads or central bodies in the discharge opening
    • 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
    • B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
    • B04C3/04—Multiple arrangement thereof
    • 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
    • B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
    • B04C3/06—Construction of inlets or outlets to the vortex chamber
    • 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
    • B04C5/08—Vortex chamber constructions
    • B04C5/103—Bodies or members, e.g. bulkheads, guides, in the vortex chamber
    • 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
    • B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
    • B04C5/13—Construction of the overflow ducting, e.g. diffusing or spiral exits formed as a vortex finder and extending into the vortex chamber; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow
    • 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
    • B04C5/24—Multiple arrangement thereof
    • B04C5/28—Multiple arrangement thereof for parallel flow

Landscapes

  • Cyclones (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

Swirl tube separator for separating solids from a gas-solid containing feed comprising a tubular housing, an inlet for introducing a gas-solids mixture at one end of said housing, a solids outlet opening at the opposite end of said housing, and a co-axial positioned tubular gas outlet conduit placed at an end of said housing, wherein along the axis of the tubular housing a vortex extender pin is present.

Claims (9)

1. Сепаратор с вихревой трубой для отделения твердых частиц от подаваемого вещества, содержащего газ и твердые частицы, включающий цилиндрический корпус, осевой впуск для введения смеси газа и твердых частиц на одном конце упомянутого корпуса, причем упомянутый осевой впуск для введения смеси газа и твердых частиц оснащен придающими завихрение средствами, выпускное отверстие для твердых частиц на противоположном конце упомянутого корпуса и расположенную коаксиально цилиндрическую выпускную трубу для газа, установленную на конце упомянутого корпуса, причем вдоль оси цилиндрического корпуса установлен вихреудлиняющий шток.1. A separator with a vortex tube for separating solid particles from a feed substance containing gas and solid particles, comprising a cylindrical body, an axial inlet for introducing a mixture of gas and solid particles at one end of the said housing, said axial inlet for introducing a mixture of gas and solid particles equipped with swirl-giving means, an outlet for solids at the opposite end of said housing and a coaxially arranged cylindrical gas outlet pipe mounted at the end of said casing, and along the axis of the cylindrical casing is installed eddy extension rod. 2. Сепаратор с вихревой трубой по п.1, в котором шток проходит, по меньшей мере, вдоль 20% оси цилиндрического корпуса, причем упомянутая ось проходит от впускного отверстия выпускной трубы для газа до конца цилиндрического корпуса, противоположного упомянутой выпускной трубе для газа.2. The vortex tube separator according to claim 1, wherein the rod extends along at least 20% of the axis of the cylindrical body, said axis extending from the inlet of the gas outlet pipe to the end of the cylindrical body opposite the said gas outlet pipe. 3. Сепаратор с вихревой трубой по п.2, в котором шток проходит на расстояние от 30 до 100% оси цилиндрического корпуса.3. The separator with a vortex tube according to claim 2, in which the rod extends from 30 to 100% of the axis of the cylindrical body. 4. Сепаратор с вихревой трубой по п.3, в котором шток проходит на расстояние 100% вдоль оси цилиндрического корпуса.4. The separator with a vortex tube according to claim 3, in which the rod extends to a distance of 100% along the axis of the cylindrical body. 5. Сепаратор с вихревой трубой по любому из пп.1-4, в котором шток проходит изнутри выпускной трубы для газа в цилиндрический корпус, и в котором шток крепится внутри выпускной трубы для газа с помощью опорных средств, причем упомянутые опорные средства являются придающими завихрение средствами, которые расположены так, что они замедляют вихревое движение газа, выпускаемого через выпускную трубу для газа.5. The separator with a vortex tube according to any one of claims 1 to 4, in which the rod extends from the inside of the exhaust pipe for gas into a cylindrical body, and in which the rod is mounted inside the exhaust pipe for gas using support means, said support means being a swirl means that are arranged so that they slow down the swirling movement of the gas discharged through the gas outlet pipe. 6. Сепаратор с вихревой трубой по любому из пп.1-4, в котором впуск для введения смеси газа и твердых частиц и выпускная труба для газа расположены на одном конце цилиндрического корпуса, а выпускное отверстие для твердых частиц расположено на противоположном конце упомянутого корпуса.6. The vortex tube separator according to any one of claims 1 to 4, in which the inlet for introducing a mixture of gas and solid particles and the exhaust pipe for gas are located at one end of the cylindrical body, and the outlet for solid particles is located on the opposite end of the said body. 7. Сепаратор с вихревой трубой по любому из пп.1-4, в котором впуск для введения смеси газа и твердых частиц расположен на одном конце цилиндрического корпуса, а выпускное отверстие для твердых частиц и выпускная труба для газа расположены на противоположном конце упомянутого корпуса так, что выпускное отверстие для твердых частиц расположено в пространстве между выпускной трубой для газа и стенкой корпуса.7. The vortex tube separator according to any one of claims 1 to 4, wherein the inlet for introducing the mixture of gas and solid particles is located at one end of the cylindrical body, and the outlet for solid particles and the exhaust pipe for gas are located on the opposite end of said body that the outlet for solid particles is located in the space between the outlet pipe for gas and the wall of the housing. 8. Многокомпонентный сепаратор, оснащенный совокупностью параллельно работающих сепараторов с вихревыми трубами по любому из пп.1-7.8. A multi-component separator equipped with a set of parallel-working separators with vortex tubes according to any one of claims 1 to 7. 9. Способ отделения твердых частиц от газообразной смеси, несущей твердые частицы, имеющей содержание твердых частиц между 100 и 500 мг/Нм3, для получения потока газа, содержащего менее 50 мг твердых частиц на Нм3, в сепараторе с вихревой трубой по любому из пп.1-7 или в многокомпонентном сепараторе по п.8.9. A method of separating solid particles from a gaseous mixture carrying solid particles having a solids content of between 100 and 500 mg / Nm 3 to produce a gas stream containing less than 50 mg of solid particles per Nm 3 in a vortex tube separator according to any one of claims 1-7 or in a multi-component separator according to claim 8.
RU2005104559/15A 2002-07-19 2003-07-17 Vortex tube separator RU2326717C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP02077964.1 2002-07-19
EP02077964 2002-07-19

Publications (2)

Publication Number Publication Date
RU2005104559A true RU2005104559A (en) 2005-08-10
RU2326717C2 RU2326717C2 (en) 2008-06-20

Family

ID=30470294

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2005104559/15A RU2326717C2 (en) 2002-07-19 2003-07-17 Vortex tube separator

Country Status (13)

Country Link
EP (1) EP1534437B1 (en)
JP (1) JP2006515533A (en)
CN (1) CN100415381C (en)
AT (1) ATE372831T1 (en)
AU (1) AU2003256582B2 (en)
BR (1) BR0312777A (en)
CA (1) CA2498522A1 (en)
DE (1) DE60316306T2 (en)
ES (1) ES2293034T3 (en)
MX (1) MXPA05000719A (en)
PT (1) PT1534437E (en)
RU (1) RU2326717C2 (en)
WO (1) WO2004009244A2 (en)

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CN100408195C (en) * 2006-04-03 2008-08-06 西安交通大学 Cyclone separator having stable vortex pipe
WO2008020051A1 (en) 2006-08-18 2008-02-21 Shell Internationale Research Maatschappij B.V. Process to separate particles from a particles-containing gas stream
CN101678370B (en) 2007-06-01 2012-12-26 国际壳牌研究有限公司 Gas-solids separator
CN105073221B (en) * 2013-01-09 2017-06-09 Fmc分离系统公司 Gas desander
RU2708597C2 (en) * 2015-03-03 2019-12-09 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Improved separators with vortex tubes
CN109351491A (en) * 2018-10-30 2019-02-19 湖南天际智慧材料科技有限公司 A kind of turbine separates and collects the device of nanometer powder and is made from it powder manufacturing apparatus
CN109550318B (en) * 2018-12-03 2023-11-17 中国石油大学(北京) Gas-liquid separator and separation method thereof
IL294428A (en) * 2019-12-31 2022-09-01 Ravands Controls LLP Cyclone filter
CN112371358B (en) * 2020-09-14 2021-06-11 东北石油大学 Outflow direction and multiphase product adjustable cyclone separation device
KR102508627B1 (en) * 2021-07-19 2023-03-09 한국해양대학교 산학협력단 Variable geometry hydrocyclone for contaminated water treatment with multiple inlets and vortex induction device
EP4268967A1 (en) * 2022-04-29 2023-11-01 ESTA Apparatebau GmbH & Co. KG Cyclone separator for separating solids from a process stream

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Also Published As

Publication number Publication date
AU2003256582A1 (en) 2004-02-09
DE60316306D1 (en) 2007-10-25
CN100415381C (en) 2008-09-03
AU2003256582B2 (en) 2006-10-19
JP2006515533A (en) 2006-06-01
MXPA05000719A (en) 2005-04-08
ATE372831T1 (en) 2007-09-15
BR0312777A (en) 2005-05-03
WO2004009244A2 (en) 2004-01-29
PT1534437E (en) 2007-12-18
CN1668380A (en) 2005-09-14
WO2004009244A3 (en) 2004-06-10
EP1534437B1 (en) 2007-09-12
EP1534437A2 (en) 2005-06-01
RU2326717C2 (en) 2008-06-20
CA2498522A1 (en) 2004-01-29
DE60316306T2 (en) 2008-06-12
ES2293034T3 (en) 2008-03-16

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Effective date: 20081209

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Effective date: 20121129