NO327793B1 - Fremgangsmate og apparat for a fordele en vaeske inn i en gasstrom. - Google Patents
Fremgangsmate og apparat for a fordele en vaeske inn i en gasstrom. Download PDFInfo
- Publication number
- NO327793B1 NO327793B1 NO20026200A NO20026200A NO327793B1 NO 327793 B1 NO327793 B1 NO 327793B1 NO 20026200 A NO20026200 A NO 20026200A NO 20026200 A NO20026200 A NO 20026200A NO 327793 B1 NO327793 B1 NO 327793B1
- Authority
- NO
- Norway
- Prior art keywords
- liquid
- gas
- gas stream
- contactor
- pipe
- Prior art date
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 150
- 238000000034 method Methods 0.000 title claims abstract description 58
- 239000007789 gas Substances 0.000 claims description 164
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 73
- 239000002904 solvent Substances 0.000 claims description 65
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 30
- 238000006243 chemical reaction Methods 0.000 claims description 24
- 238000002156 mixing Methods 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 17
- 239000003345 natural gas Substances 0.000 claims description 16
- 239000012071 phase Substances 0.000 claims description 16
- 239000007791 liquid phase Substances 0.000 claims description 13
- 239000003153 chemical reaction reagent Substances 0.000 claims description 10
- 238000004140 cleaning Methods 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 238000000926 separation method Methods 0.000 claims description 7
- 230000008859 change Effects 0.000 claims description 6
- 239000008240 homogeneous mixture Substances 0.000 claims description 5
- 230000018044 dehydration Effects 0.000 claims description 4
- 238000006297 dehydration reaction Methods 0.000 claims description 4
- 238000006392 deoxygenation reaction Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 230000001172 regenerating effect Effects 0.000 claims description 4
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 238000010924 continuous production Methods 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims description 2
- 238000007701 flash-distillation Methods 0.000 claims 1
- 238000010521 absorption reaction Methods 0.000 description 35
- 239000012530 fluid Substances 0.000 description 20
- 239000000126 substance Substances 0.000 description 14
- 239000002253 acid Substances 0.000 description 13
- 150000001412 amines Chemical class 0.000 description 13
- 230000009467 reduction Effects 0.000 description 11
- 230000008569 process Effects 0.000 description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 238000009826 distribution Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 8
- 239000010408 film Substances 0.000 description 7
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 6
- 241000196324 Embryophyta Species 0.000 description 6
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- CRVGTESFCCXCTH-UHFFFAOYSA-N methyl diethanolamine Chemical compound OCCN(C)CCO CRVGTESFCCXCTH-UHFFFAOYSA-N 0.000 description 5
- 239000013535 sea water Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 230000002378 acidificating effect Effects 0.000 description 4
- 230000002427 irreversible effect Effects 0.000 description 4
- 230000008929 regeneration Effects 0.000 description 4
- 238000011069 regeneration method Methods 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 238000012546 transfer Methods 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 230000001133 acceleration Effects 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000000567 combustion gas Substances 0.000 description 3
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 3
- 238000005187 foaming Methods 0.000 description 3
- 238000011068 loading method Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000005864 Sulphur Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 230000002000 scavenging effect Effects 0.000 description 2
- FYADHXFMURLYQI-UHFFFAOYSA-N 1,2,4-triazine Chemical compound C1=CN=NC=N1 FYADHXFMURLYQI-UHFFFAOYSA-N 0.000 description 1
- 102100032373 Coiled-coil domain-containing protein 85B Human genes 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 240000006829 Ficus sundaica Species 0.000 description 1
- 101000868814 Homo sapiens Coiled-coil domain-containing protein 85B Proteins 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- LVTYICIALWPMFW-UHFFFAOYSA-N diisopropanolamine Chemical compound CC(O)CNCC(C)O LVTYICIALWPMFW-UHFFFAOYSA-N 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005511 kinetic theory Methods 0.000 description 1
- 230000004807 localization Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 230000036316 preload Effects 0.000 description 1
- 239000002516 radical scavenger Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1456—Removing acid components
- B01D53/1462—Removing mixtures of hydrogen sulfide and carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/21—Mixing gases with liquids by introducing liquids into gaseous media
- B01F23/213—Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
- B01F25/3124—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
- B01F25/31242—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow the main flow being injected in the central area of the venturi, creating an aspiration in the circumferential part of the conduit
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/314—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/314—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
- B01F25/3142—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction
- B01F25/31423—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction with a plurality of perforations in the circumferential direction only and covering the whole circumference
- B01F25/314231—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction with a plurality of perforations in the circumferential direction only and covering the whole circumference the perforations being a complete cut-out in the circumferential direction covering the whole diameter of the tube, i.e. having two consecutive tubes placed consecutively, the additional component being introduced between them
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Gas Separation By Absorption (AREA)
- Treating Waste Gases (AREA)
- Sampling And Sample Adjustment (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Accessories For Mixers (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GBGB0015997.0A GB0015997D0 (en) | 2000-06-29 | 2000-06-29 | Method for mixing fluids |
| PCT/GB2001/002913 WO2002000334A1 (en) | 2000-06-29 | 2001-06-29 | Method for mixing fluids |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| NO20026200L NO20026200L (no) | 2002-12-23 |
| NO20026200D0 NO20026200D0 (no) | 2002-12-23 |
| NO327793B1 true NO327793B1 (no) | 2009-09-28 |
Family
ID=9894690
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO20026200A NO327793B1 (no) | 2000-06-29 | 2002-12-23 | Fremgangsmate og apparat for a fordele en vaeske inn i en gasstrom. |
Country Status (15)
| Country | Link |
|---|---|
| US (1) | US7128276B2 (da) |
| EP (1) | EP1294473B1 (da) |
| CN (1) | CN1302838C (da) |
| AT (1) | ATE317722T1 (da) |
| AU (2) | AU2001269265B2 (da) |
| BR (1) | BR0112060B1 (da) |
| CA (1) | CA2411417C (da) |
| DE (1) | DE60117265T2 (da) |
| DK (1) | DK1294473T3 (da) |
| ES (1) | ES2258538T3 (da) |
| GB (1) | GB0015997D0 (da) |
| NO (1) | NO327793B1 (da) |
| RU (1) | RU2247595C2 (da) |
| WO (1) | WO2002000334A1 (da) |
| ZA (1) | ZA200209844B (da) |
Families Citing this family (61)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NO20044181L (no) * | 2004-10-01 | 2006-04-03 | Propure As | Injection mixer |
| EA012104B1 (ru) * | 2004-10-01 | 2009-08-28 | Пропуре Ас | Инжекционный смеситель для множества текучих сред |
| NO343579B1 (no) * | 2004-10-01 | 2019-04-08 | Propure As | Injeksjonsblander |
| US20090038701A1 (en) | 2006-01-17 | 2009-02-12 | Baxter International Inc. | Device, system and method for mixing |
| RU2392061C2 (ru) * | 2007-09-19 | 2010-06-20 | Сергей Викторович Надмитов | Способ селективно-рециркуляционного распыления жидкости и устройство для его осуществления (варианты) |
| KR101506654B1 (ko) * | 2007-12-20 | 2015-03-27 | 레이브 엔.피., 인크. | 노즐용 유체 분사 조립체 |
| US20090261021A1 (en) * | 2008-04-16 | 2009-10-22 | Bower David J | Oil sands processing |
| CA2736222A1 (en) * | 2008-10-14 | 2010-04-22 | Exxonmobil Upstream Research Company | Removal of acid gases from a gas stream |
| MX2011010404A (es) | 2009-04-20 | 2011-10-24 | Exxonmobil Upstream Res Co | Sistema criogenico para remocion de gases acidos de una corriente de gas de hidrocarburo y metodo para remover gases acidos. |
| FR2947185B1 (fr) | 2009-06-26 | 2011-07-01 | Total Sa | Procede de traitement de gaz acides |
| MY161120A (en) | 2009-09-09 | 2017-04-14 | Exxonmobil Upstream Res Co | Cryogenic system for removing acid gases from a hydrocarbon gas stream |
| MX2012003246A (es) * | 2009-09-18 | 2012-04-10 | Fluor Tech Corp | Configuraciones de alta remocion de co2 de alta presion y metodos. |
| CA2777760C (en) * | 2009-11-02 | 2017-06-27 | Exxonmobil Upstream Research Company | Cryogenic system for removing acid gases from a hydrocarbon gas stream, with removal of hydrogen sulfide |
| WO2011090553A1 (en) | 2010-01-22 | 2011-07-28 | Exxonmobil Upstream Research Company | Removal of acid gases from a gas stream, with co2 capture and sequestration |
| US20110217218A1 (en) * | 2010-03-02 | 2011-09-08 | Exxonmobil Research And Engineering Company | Systems and Methods for Acid Gas Removal |
| US8336319B2 (en) * | 2010-06-04 | 2012-12-25 | Tesla Motors, Inc. | Thermal management system with dual mode coolant loops |
| CN103052856B (zh) | 2010-07-30 | 2016-03-30 | 埃克森美孚上游研究公司 | 使用并流分离装置从烃气流中去除酸性气体的低温系统 |
| US8899557B2 (en) | 2011-03-16 | 2014-12-02 | Exxonmobil Upstream Research Company | In-line device for gas-liquid contacting, and gas processing facility employing co-current contactors |
| FR2977168B1 (fr) * | 2011-06-29 | 2015-07-24 | IFP Energies Nouvelles | Procede de desacidification d'un gaz avec plusieurs etapes de mise en contact a co-courant avec une solution absorbante |
| US20190277416A1 (en) * | 2012-02-20 | 2019-09-12 | Nyloncraft Incorporated | High mass flow check valve aspirator |
| WO2013142100A1 (en) | 2012-03-21 | 2013-09-26 | Exxonmobil Upstream Research Company | Separating carbon dioxide and ethane from a mixed stream |
| DE102012209342A1 (de) * | 2012-06-04 | 2013-12-05 | Siemens Aktiengesellschaft | Verfahren zum Anpassen der Geometrie einer Dispergierdüse |
| AU2013375230B2 (en) | 2013-01-25 | 2016-02-18 | Exxonmobil Upstream Research Company | Contacting a gas stream with a liquid stream |
| FI20135295L (fi) * | 2013-03-26 | 2014-09-27 | Aalto Korkeakoulusäätiö | SCR-järjestelmä dieselmoottoreiden pakokaasujen jälkikäsittelyä varten sekä vastaava SCR-tekniikkaa hyödyntävä menetelmä |
| AR096132A1 (es) * | 2013-05-09 | 2015-12-09 | Exxonmobil Upstream Res Co | Separar dióxido de carbono y sulfuro de hidrógeno de un flujo de gas natural con sistemas de co-corriente en contacto |
| AR096078A1 (es) | 2013-05-09 | 2015-12-02 | Exxonmobil Upstream Res Co | Separación de impurezas de una corriente de gas usando un sistema de contacto en equicorriente orientado verticalmente |
| CA2925406C (en) | 2013-12-06 | 2017-11-21 | Exxonmobil Upstream Research Company | Method and system of modifying a liquid level during start-up operations |
| MX363766B (es) | 2013-12-06 | 2019-04-02 | Exxonmobil Upstream Res Co | Metodo y dispositivo para separar hidrocarburos y contaminantes con un mecanismo de calentamiento para desestabilizar y/o prevenir la adhesion de solidos. |
| AU2014357667B2 (en) | 2013-12-06 | 2017-10-05 | Exxonmobil Upstream Research Company | Method and system for separating a feed stream with a feed stream distribution mechanism |
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| AU2014357663B2 (en) | 2013-12-06 | 2016-12-22 | Exxonmobil Upstream Research Company | Method and device for separating hydrocarbons and contaminants with a spray assembly |
| AU2014357665B2 (en) | 2013-12-06 | 2017-06-22 | Exxonmobil Upstream Research Company | Method and device for separating a feed stream using radiation detectors |
| WO2015084495A2 (en) | 2013-12-06 | 2015-06-11 | Exxonmobil Upstream Research Company | Method and system of maintaining a liquid level in a distillation tower |
| US9562719B2 (en) | 2013-12-06 | 2017-02-07 | Exxonmobil Upstream Research Company | Method of removing solids by modifying a liquid level in a distillation tower |
| SG11201704529RA (en) | 2015-01-09 | 2017-07-28 | Exxonmobil Upstream Res Co | Separating impurities from a fluid steam using multiple co-current contactors |
| AU2016220515B2 (en) | 2015-02-17 | 2019-02-28 | Exxonmobil Upstream Research Company | Inner surface features for co-current contactors |
| AU2016223296B2 (en) | 2015-02-27 | 2018-11-08 | Exxonmobil Upstream Research Company | Reducing refrigeration and dehydration load for a feed stream entering a cryogenic distillation process |
| EP3268119A1 (en) | 2015-03-13 | 2018-01-17 | ExxonMobil Upstream Research Company | Coalescer for co-current contactors |
| US9630125B2 (en) * | 2015-06-08 | 2017-04-25 | Shimadzu Corporation | Gas-blowing liquid sample infusing device and infusion container used for the same |
| US10365037B2 (en) | 2015-09-18 | 2019-07-30 | Exxonmobil Upstream Research Company | Heating component to reduce solidification in a cryogenic distillation system |
| MY187623A (en) | 2015-09-24 | 2021-10-04 | Exxonmobil Upstream Res Co | Treatment plant for hydrocarbon gas having variable contaminant levels |
| US20170239612A1 (en) * | 2016-02-19 | 2017-08-24 | Suhas P. Mondkar | Cold Solvent Gas Treating System |
| CA3024545C (en) | 2016-03-30 | 2020-08-25 | Exxonmobile Upstream Research Company | Self-sourced reservoir fluid for enhanced oil recovery |
| RU2644604C1 (ru) * | 2016-10-31 | 2018-02-13 | Марат Минасхатович Ризванов | Сопло для создания реактивной газовой и жидкостной струи для сместителей |
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| IL255268B (en) * | 2017-10-26 | 2019-01-31 | Izun Pharmaceuticals Corp | Smoke capture system and method |
| PL3765801T3 (pl) * | 2018-03-13 | 2022-04-04 | Thorsteinn I. VIGLUNDSSON | Sposób i urządzenie do wytwarzania mokrego śniegu |
| WO2020005552A1 (en) | 2018-06-29 | 2020-01-02 | Exxonmobil Upstream Research Company | Hybrid tray for introducing a low co2 feed stream into a distillation tower |
| WO2020005553A1 (en) | 2018-06-29 | 2020-01-02 | Exxonmobil Upstream Research Company (Emhc-N1.4A.607) | Mixing and heat integration of melt tray liquids in a cryogenic distillation tower |
| CN109201364B (zh) * | 2018-09-13 | 2020-10-27 | 宁波工程学院 | 一种提高喷涂均匀性的喷涂装置 |
| US11833481B2 (en) | 2018-10-05 | 2023-12-05 | Produced Water Absorbents Inc. | Multi-channel, variable-flow mixers and related methods |
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| US11331636B2 (en) | 2020-07-29 | 2022-05-17 | Saudi Arabian Oil Company | Multi-opening chemical injection device |
| US11813580B2 (en) * | 2020-09-02 | 2023-11-14 | Nov Canada Ulc | Static mixer suitable for additive manufacturing |
| US12005407B2 (en) | 2021-01-22 | 2024-06-11 | Saudi Arabian Oil Company | Chemical injection and mixing device |
| CN112944213A (zh) * | 2021-03-17 | 2021-06-11 | 重庆渝微电子技术研究院有限公司 | 一种动态气液配气系统及方法 |
| CN112933866B (zh) * | 2021-03-22 | 2022-07-22 | 哈尔滨工程大学 | 一种可用于有害气体净化处理的气液两相引射器 |
Family Cites Families (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB769821A (en) | 1954-06-05 | 1957-03-13 | Svenska Flaektfabriken Ab | Method and device for supplying, spraying and mixing a liquid in a gaseous medium flowing in a channel |
| NL132863C (da) * | 1968-07-26 | |||
| US4019983A (en) * | 1974-10-10 | 1977-04-26 | Houdaille Industries, Inc. | Disinfection system and method |
| DE2634496C2 (de) * | 1976-07-31 | 1985-10-17 | Bayer Ag, 5090 Leverkusen | Injektor zur Begasung einer Flüssigkeit |
| US4405563A (en) * | 1980-11-26 | 1983-09-20 | Irwin Fox | Scavenging natural gas streams with slurry apparatus |
| JPS5887102A (ja) * | 1981-11-19 | 1983-05-24 | Kanegafuchi Chem Ind Co Ltd | 凝固ラテツクスの製造方法および装置 |
| DE3325741C1 (de) * | 1983-07-16 | 1985-02-21 | Lechler Gmbh & Co Kg, 7012 Fellbach | Zylindrischer Einsatz fuer eine Zweistoff-Zerstaeubungsduese |
| US4668498A (en) * | 1985-09-27 | 1987-05-26 | Davis James A | Supersonic singlet delta oxygen aerosol generator |
| JPS6388026A (ja) | 1986-10-01 | 1988-04-19 | Mitsubishi Rayon Eng Co Ltd | 気液混合装置 |
| SU1761241A1 (ru) * | 1987-02-25 | 1992-09-15 | Одесский Политехнический Институт | Устройство дл получени водотопливных эмульсий |
| SU1457971A1 (ru) | 1987-07-09 | 1989-02-15 | Производственно-Техническое Предприятие Треста "Укрэнергочермет" | Устройство дл очистки отход щих газов |
| SU1599069A1 (ru) * | 1988-12-12 | 1990-10-15 | Рубежанский филиал Днепропетровского химико-технологического института им.Ф.Э.Дзержинского | Тепломассообменный аппарат Вентури |
| US4932213A (en) * | 1989-02-10 | 1990-06-12 | Amoco Corporation | Method of treating natural gas to remove ethane and higher hydrocarbons |
| US5273734A (en) * | 1990-01-12 | 1993-12-28 | The Texas A&M University System | Conversion of H2 to sulfur |
| JPH0448920A (ja) * | 1990-06-18 | 1992-02-18 | Inax Corp | エゼクタ及び浄化装置 |
| US5090619A (en) * | 1990-08-29 | 1992-02-25 | Pinnacle Innovations | Snow gun having optimized mixing of compressed air and water flows |
| US5238665A (en) * | 1991-06-10 | 1993-08-24 | Beco Engineering Company | Method for minimizing environmental release of toxic compounds in the incineration of wastes |
| DE9202828U1 (de) | 1992-03-04 | 1992-07-09 | Wopfner, Gaston M., 82515 Wolfratshausen | Einrichtung zum Belüften oder Imprägnieren einer Flüssigkeit |
| GB9405000D0 (en) * | 1994-03-15 | 1994-04-27 | Boc Group Plc | Gas dissolving |
| DE4446000C2 (de) | 1994-12-22 | 1997-11-20 | Hrch Huppmann Maschf Gmbh | Vorrichtung zum Mischen zweier strömender Fluide, insbesondere zum Belüften von Würze für die Bierherstellung |
| WO1999013966A1 (en) * | 1997-09-15 | 1999-03-25 | Den Norske Stats Oljeselskap A.S | Fluid separation system |
| RU2123617C1 (ru) * | 1997-12-04 | 1998-12-20 | Попов Сергей Анатольевич | Жидкостно-газовый струйный аппарат |
| JPH11276836A (ja) * | 1998-03-31 | 1999-10-12 | Chiyoda Engineering Kk | 湿式集塵装置 |
| FR2801648B1 (fr) * | 1999-11-30 | 2002-06-21 | Commissariat Energie Atomique | Injecteur a vapeur haute pression comportant un drain axial |
-
2000
- 2000-06-29 GB GBGB0015997.0A patent/GB0015997D0/en not_active Ceased
-
2001
- 2001-06-29 EP EP01947618A patent/EP1294473B1/en not_active Expired - Lifetime
- 2001-06-29 AU AU2001269265A patent/AU2001269265B2/en not_active Ceased
- 2001-06-29 CA CA2411417A patent/CA2411417C/en not_active Expired - Lifetime
- 2001-06-29 RU RU2003102445/15A patent/RU2247595C2/ru not_active IP Right Cessation
- 2001-06-29 WO PCT/GB2001/002913 patent/WO2002000334A1/en not_active Ceased
- 2001-06-29 DE DE60117265T patent/DE60117265T2/de not_active Expired - Lifetime
- 2001-06-29 AT AT01947618T patent/ATE317722T1/de not_active IP Right Cessation
- 2001-06-29 BR BRPI0112060-3A patent/BR0112060B1/pt not_active IP Right Cessation
- 2001-06-29 US US10/312,074 patent/US7128276B2/en not_active Expired - Lifetime
- 2001-06-29 ES ES01947618T patent/ES2258538T3/es not_active Expired - Lifetime
- 2001-06-29 DK DK01947618T patent/DK1294473T3/da active
- 2001-06-29 AU AU6926501A patent/AU6926501A/xx active Pending
- 2001-06-29 CN CNB018119085A patent/CN1302838C/zh not_active Expired - Fee Related
-
2002
- 2002-12-04 ZA ZA200209844A patent/ZA200209844B/en unknown
- 2002-12-23 NO NO20026200A patent/NO327793B1/no not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| EP1294473B1 (en) | 2006-02-15 |
| BR0112060A (pt) | 2003-06-17 |
| ATE317722T1 (de) | 2006-03-15 |
| WO2002000334A1 (en) | 2002-01-03 |
| GB0015997D0 (en) | 2000-08-23 |
| AU2001269265B2 (en) | 2005-11-17 |
| CA2411417A1 (en) | 2002-01-03 |
| NO20026200L (no) | 2002-12-23 |
| RU2247595C2 (ru) | 2005-03-10 |
| CA2411417C (en) | 2010-09-07 |
| ES2258538T3 (es) | 2006-09-01 |
| CN1438916A (zh) | 2003-08-27 |
| NO20026200D0 (no) | 2002-12-23 |
| ZA200209844B (en) | 2003-12-04 |
| DK1294473T3 (da) | 2006-06-12 |
| US20030155436A1 (en) | 2003-08-21 |
| AU6926501A (en) | 2002-01-08 |
| CN1302838C (zh) | 2007-03-07 |
| US7128276B2 (en) | 2006-10-31 |
| DE60117265T2 (de) | 2006-11-23 |
| BR0112060B1 (pt) | 2010-05-18 |
| DE60117265D1 (de) | 2006-04-20 |
| EP1294473A1 (en) | 2003-03-26 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MK1K | Patent expired |