ES2315667T3 - Dispositivo para la separacion de una corriente de entrada de dos fases con la relacion vapor/liquido deseada. - Google Patents
Dispositivo para la separacion de una corriente de entrada de dos fases con la relacion vapor/liquido deseada. Download PDFInfo
- Publication number
- ES2315667T3 ES2315667T3 ES04738943T ES04738943T ES2315667T3 ES 2315667 T3 ES2315667 T3 ES 2315667T3 ES 04738943 T ES04738943 T ES 04738943T ES 04738943 T ES04738943 T ES 04738943T ES 2315667 T3 ES2315667 T3 ES 2315667T3
- Authority
- ES
- Spain
- Prior art keywords
- phase
- liquid
- flow
- separator
- current
- 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.)
- Expired - Lifetime
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 247
- 238000000926 separation method Methods 0.000 title claims abstract description 78
- 239000012530 fluid Substances 0.000 claims abstract description 34
- 239000000203 mixture Substances 0.000 claims abstract description 15
- 238000004891 communication Methods 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 38
- 239000000126 substance Substances 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 238000009434 installation Methods 0.000 claims description 11
- 238000002156 mixing Methods 0.000 claims description 4
- 238000012545 processing Methods 0.000 claims description 3
- 230000003197 catalytic effect Effects 0.000 claims description 2
- 230000016507 interphase Effects 0.000 claims 2
- 239000012071 phase Substances 0.000 abstract description 106
- 239000007791 liquid phase Substances 0.000 abstract description 18
- 239000012808 vapor phase Substances 0.000 abstract description 12
- 230000008569 process Effects 0.000 description 32
- 238000011144 upstream manufacturing Methods 0.000 description 21
- 238000009826 distribution Methods 0.000 description 19
- 239000003054 catalyst Substances 0.000 description 16
- 238000013461 design Methods 0.000 description 14
- 230000003068 static effect Effects 0.000 description 13
- 238000004519 manufacturing process Methods 0.000 description 9
- 229930195733 hydrocarbon Natural products 0.000 description 8
- 150000002430 hydrocarbons Chemical class 0.000 description 8
- 238000012546 transfer Methods 0.000 description 8
- 230000005514 two-phase flow Effects 0.000 description 8
- 238000005191 phase separation Methods 0.000 description 7
- 239000004215 Carbon black (E152) Substances 0.000 description 6
- 238000005057 refrigeration Methods 0.000 description 6
- 230000035939 shock Effects 0.000 description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 5
- 229910052739 hydrogen Inorganic materials 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000000571 coke Substances 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000009834 vaporization Methods 0.000 description 4
- 230000008016 vaporization Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 238000009827 uniform distribution Methods 0.000 description 3
- 238000004517 catalytic hydrocracking Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000013021 overheating Methods 0.000 description 2
- 230000002028 premature Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000009533 lab test Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 230000026676 system process Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D1/00—Pipe-line systems
- F17D1/005—Pipe-line systems for a two-phase gas-liquid flow
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DKPA200300946 | 2003-06-24 | ||
| DK200300946 | 2003-06-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2315667T3 true ES2315667T3 (es) | 2009-04-01 |
Family
ID=33522197
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES04738943T Expired - Lifetime ES2315667T3 (es) | 2003-06-24 | 2004-06-24 | Dispositivo para la separacion de una corriente de entrada de dos fases con la relacion vapor/liquido deseada. |
Country Status (8)
| Country | Link |
|---|---|
| EP (1) | EP1651904B1 (zh) |
| JP (1) | JP4722840B2 (zh) |
| CN (1) | CN100561036C (zh) |
| AT (1) | ATE405790T1 (zh) |
| DE (1) | DE602004015999D1 (zh) |
| EA (1) | EA007546B1 (zh) |
| ES (1) | ES2315667T3 (zh) |
| WO (1) | WO2004113788A1 (zh) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| MX2010012015A (es) * | 2008-05-06 | 2010-12-01 | Fluor Tech Corp | Metodos y aparatos para separar un flujo de fases multiples. |
| US8500884B2 (en) * | 2010-09-27 | 2013-08-06 | Uop Llc | Vessel and process pertaining to an impermeable impingement plate |
| NO333218B1 (no) * | 2011-01-27 | 2013-04-15 | Fmc Kongsberg Subsea As | Manifold for bruk i et stromningssystem |
| NL2011856C2 (en) * | 2013-11-28 | 2014-09-25 | Avantium Technologies B V | Reactor system for high throughput applications. |
| CN105546347A (zh) * | 2015-12-11 | 2016-05-04 | 大连交通大学 | 一种液体汽化和输送装置 |
| JP7328486B2 (ja) * | 2019-02-21 | 2023-08-17 | 株式会社トリケミカル研究所 | 溶存ガス除去方法および溶存ガス除去装置 |
| CN110711546B (zh) * | 2019-11-15 | 2024-09-13 | 南通好唯智能制造科技有限公司 | 微通道反应器用分流系统、分流器及其制造方法 |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5331825B1 (zh) * | 1969-07-22 | 1978-09-05 | ||
| US4293025A (en) * | 1973-09-20 | 1981-10-06 | Atlantic Richfield Company | Method and apparatus for the distribution of liquid-vapor mixture |
| US4396063A (en) | 1981-11-16 | 1983-08-02 | Mobil Oil Corporation | Process and system for providing multiple streams of wet steam having substantially equal quality for recovering heavy oil |
| JPS58142483U (ja) | 1982-03-20 | 1983-09-26 | 住友金属工業株式会社 | 分流器 |
| US4528919A (en) | 1982-12-30 | 1985-07-16 | Union Oil Company Of California | Multi-phase fluid flow divider |
| US4574837A (en) | 1983-09-29 | 1986-03-11 | Exxon Production Research Co. | Method and apparatus for splitting two-phase gas-liquid flows having a known flow profile |
| US4516986A (en) | 1984-03-29 | 1985-05-14 | Shell Oil Company | Two-phase flow splitter |
| EP0172336A1 (de) * | 1984-08-24 | 1986-02-26 | GebràDer Sulzer Aktiengesellschaft | Vorrichtung zum gleichmässigen Verteilen eines Zwei-Phasengemisches |
| JPH0612165B2 (ja) * | 1985-09-06 | 1994-02-16 | 三菱重工業株式会社 | 気液二相流体分配器 |
| US4800921A (en) | 1986-06-20 | 1989-01-31 | Exxon Production Research Company | Method and apparatus for dividing a single stream of liquid and vapor into multiple streams having similar vapor to liquid rations |
| US4824614A (en) | 1987-04-09 | 1989-04-25 | Santa Fe Energy Company | Device for uniformly distributing a two-phase fluid |
| US5254292A (en) * | 1989-02-02 | 1993-10-19 | Institut Francais Du Petrole | Device for regulating and reducing the fluctuations in a polyphasic flow, and its use |
| JPH03129271A (ja) * | 1989-10-13 | 1991-06-03 | Mitsubishi Electric Corp | 混相流体分配器 |
| US5810032A (en) | 1995-03-22 | 1998-09-22 | Chevron U.S.A. Inc. | Method and apparatus for controlling the distribution of two-phase fluids flowing through impacting pipe tees |
-
2004
- 2004-06-24 WO PCT/DK2004/000446 patent/WO2004113788A1/en active IP Right Grant
- 2004-06-24 JP JP2006515729A patent/JP4722840B2/ja not_active Expired - Lifetime
- 2004-06-24 DE DE602004015999T patent/DE602004015999D1/de not_active Expired - Lifetime
- 2004-06-24 CN CNB2004800178329A patent/CN100561036C/zh not_active Expired - Lifetime
- 2004-06-24 ES ES04738943T patent/ES2315667T3/es not_active Expired - Lifetime
- 2004-06-24 EP EP04738943A patent/EP1651904B1/en not_active Expired - Lifetime
- 2004-06-24 EA EA200600090A patent/EA007546B1/ru unknown
- 2004-06-24 AT AT04738943T patent/ATE405790T1/de not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| EA200600090A1 (ru) | 2006-06-30 |
| DE602004015999D1 (de) | 2008-10-02 |
| WO2004113788A1 (en) | 2004-12-29 |
| CN100561036C (zh) | 2009-11-18 |
| EP1651904A1 (en) | 2006-05-03 |
| JP4722840B2 (ja) | 2011-07-13 |
| JP2007533419A (ja) | 2007-11-22 |
| ATE405790T1 (de) | 2008-09-15 |
| CN1813155A (zh) | 2006-08-02 |
| EA007546B1 (ru) | 2006-10-27 |
| EP1651904B1 (en) | 2008-08-20 |
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