PL196111B1 - Urządzenie wewnętrzne do rozdzielania mieszaniny zawierającej co najmniej jedną fazę gazową i fazę ciekłą - Google Patents
Urządzenie wewnętrzne do rozdzielania mieszaniny zawierającej co najmniej jedną fazę gazową i fazę ciekłąInfo
- Publication number
- PL196111B1 PL196111B1 PL354888A PL35488802A PL196111B1 PL 196111 B1 PL196111 B1 PL 196111B1 PL 354888 A PL354888 A PL 354888A PL 35488802 A PL35488802 A PL 35488802A PL 196111 B1 PL196111 B1 PL 196111B1
- Authority
- PL
- Poland
- Prior art keywords
- liquid
- separator
- fraction
- chamber
- recirculation
- Prior art date
Links
- 238000000926 separation method Methods 0.000 title claims abstract description 24
- 239000007791 liquid phase Substances 0.000 title claims abstract description 22
- 239000000203 mixture Substances 0.000 title claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 106
- 239000007789 gas Substances 0.000 claims abstract description 59
- 239000002245 particle Substances 0.000 claims abstract description 19
- 239000007787 solid Substances 0.000 claims abstract description 17
- 210000003918 fraction a Anatomy 0.000 claims abstract description 12
- 210000002196 fr. b Anatomy 0.000 claims abstract description 10
- 230000005484 gravity Effects 0.000 claims abstract description 3
- 238000009835 boiling Methods 0.000 claims description 19
- 239000012071 phase Substances 0.000 claims description 14
- 229930195733 hydrocarbon Natural products 0.000 claims description 13
- 150000002430 hydrocarbons Chemical class 0.000 claims description 13
- 230000003197 catalytic effect Effects 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 11
- 239000007790 solid phase Substances 0.000 claims description 8
- 239000004215 Carbon black (E152) Substances 0.000 claims description 7
- 239000001257 hydrogen Substances 0.000 claims description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims description 6
- 230000008569 process Effects 0.000 claims description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 5
- 230000001939 inductive effect Effects 0.000 claims 1
- 239000007792 gaseous phase Substances 0.000 abstract description 6
- 238000007599 discharging Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 14
- 239000003054 catalyst Substances 0.000 description 10
- 238000011144 upstream manufacturing Methods 0.000 description 5
- 239000012263 liquid product Substances 0.000 description 4
- 230000001174 ascending effect Effects 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- 239000010779 crude oil Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 238000009530 blood pressure measurement Methods 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000001627 detrimental effect Effects 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000012295 chemical reaction liquid Substances 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000016507 interphase Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Classifications
-
- 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
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/22—Separation of effluents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0042—Degasification of liquids modifying the liquid flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0065—Separating solid material from the gas/liquid stream by impingement against stationary members
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1872—Details of the fluidised bed reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
- B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00283—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
-
- 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
- C10G2300/4081—Recycling aspects
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Centrifugal Separators (AREA)
- Cyclones (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0109055A FR2826876B1 (fr) | 2001-07-06 | 2001-07-06 | Dispositif interne de separation d'un melange comprenant au moins une phase gazeuse et une phase liquide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| PL354888A1 PL354888A1 (en) | 2003-01-13 |
| PL196111B1 true PL196111B1 (pl) | 2007-12-31 |
Family
ID=8865254
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL354888A PL196111B1 (pl) | 2001-07-06 | 2002-07-04 | Urządzenie wewnętrzne do rozdzielania mieszaniny zawierającej co najmniej jedną fazę gazową i fazę ciekłą |
Country Status (8)
| Country | Link |
|---|---|
| EP (1) | EP1275425B1 (enExample) |
| JP (1) | JP4329313B2 (enExample) |
| BR (1) | BR0202586B1 (enExample) |
| CA (1) | CA2374894C (enExample) |
| FR (1) | FR2826876B1 (enExample) |
| MX (1) | MXPA02006728A (enExample) |
| PL (1) | PL196111B1 (enExample) |
| RU (1) | RU2301103C2 (enExample) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050075527A1 (en) * | 2003-02-26 | 2005-04-07 | Institut Francais Du Petrole | Method and processing equipment for hydrocarbons and for separation of the phases produced by said processing |
| CN104549063B (zh) * | 2013-10-12 | 2016-08-10 | 中国石油化工股份有限公司 | 一种沸腾床反应器 |
| CN105688450B (zh) * | 2016-03-31 | 2017-07-14 | 飞潮（无锡）过滤技术有限公司 | 一种气液固液固五相过滤分离器 |
| FR3058421B1 (fr) * | 2016-11-09 | 2020-07-24 | Ifp Energies Now | Nouveau dispositif de separation gaz liquide pour equiper les reacteurs en lit fluidise triphasique tels que ceux utilises dans le procede h-oil |
| CN107297186B (zh) * | 2017-07-24 | 2018-03-20 | 上海英保能源化工科技有限公司 | 一种沸腾床加氢反应系统和沸腾床加氢方法 |
| PL71191Y1 (pl) * | 2018-03-05 | 2020-01-31 | Electronic Components And Devices Marek Turzanski Spolka Jawna | Separator przepływu cieczy i powietrza |
| FR3094984B1 (fr) * | 2019-04-12 | 2024-08-16 | Ifp Energies Now | Reacteur triphasique avec coupelle de recycle de section decroissante et d’angle d’inclinaison variable |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4221653A (en) * | 1978-06-30 | 1980-09-09 | Hydrocarbon Research, Inc. | Catalytic hydrogenation process and apparatus with improved vapor liquid separation |
| JPS6051510A (ja) * | 1983-09-01 | 1985-03-23 | Mitsubishi Heavy Ind Ltd | 気液分離器 |
| US4886644A (en) * | 1987-12-02 | 1989-12-12 | Texaco Inc. | Liquid degaser in an ebullated bed process |
| US4971678A (en) * | 1988-06-27 | 1990-11-20 | Texaco Inc. | Liquid inventory control in an ebullated bed process |
| US5066467A (en) * | 1990-10-05 | 1991-11-19 | Texaco Inc. | Liquid degasser in an ebullated bed process |
| US5624642A (en) * | 1994-10-14 | 1997-04-29 | Amoco Corporation | Hydrocarbon processing apparatus |
-
2001
- 2001-07-06 FR FR0109055A patent/FR2826876B1/fr not_active Expired - Lifetime
-
2002
- 2002-03-05 EP EP20020290531 patent/EP1275425B1/fr not_active Expired - Lifetime
- 2002-03-06 CA CA2374894A patent/CA2374894C/fr not_active Expired - Lifetime
- 2002-07-04 PL PL354888A patent/PL196111B1/pl unknown
- 2002-07-05 RU RU2002118206/15A patent/RU2301103C2/ru active
- 2002-07-05 BR BR0202586A patent/BR0202586B1/pt not_active IP Right Cessation
- 2002-07-05 MX MXPA02006728 patent/MXPA02006728A/es active IP Right Grant
- 2002-07-08 JP JP2002198596A patent/JP4329313B2/ja not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| MXPA02006728A (es) | 2005-08-16 |
| BR0202586A (pt) | 2003-04-29 |
| JP4329313B2 (ja) | 2009-09-09 |
| PL354888A1 (en) | 2003-01-13 |
| EP1275425B1 (fr) | 2010-09-15 |
| FR2826876B1 (fr) | 2003-09-26 |
| CA2374894A1 (fr) | 2003-01-06 |
| EP1275425A1 (fr) | 2003-01-15 |
| RU2301103C2 (ru) | 2007-06-20 |
| CA2374894C (fr) | 2010-12-14 |
| JP2003112037A (ja) | 2003-04-15 |
| BR0202586B1 (pt) | 2012-04-17 |
| FR2826876A1 (fr) | 2003-01-10 |
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