ES483690A1 - Procedimiento para dividir un efluente producto de reaccion hidrocarbonoso en fase mixta - Google Patents
Procedimiento para dividir un efluente producto de reaccion hidrocarbonoso en fase mixtaInfo
- Publication number
- ES483690A1 ES483690A1 ES483690A ES483690A ES483690A1 ES 483690 A1 ES483690 A1 ES 483690A1 ES 483690 A ES483690 A ES 483690A ES 483690 A ES483690 A ES 483690A ES 483690 A1 ES483690 A1 ES 483690A1
- Authority
- ES
- Spain
- Prior art keywords
- separation zone
- phase
- product effluent
- separation
- mixed
- 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
Links
- 238000000926 separation method Methods 0.000 title abstract 10
- 239000007795 chemical reaction product Substances 0.000 title abstract 2
- 239000012071 phase Substances 0.000 abstract 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 2
- 229910052739 hydrogen Inorganic materials 0.000 abstract 2
- 239000001257 hydrogen Substances 0.000 abstract 2
- 239000007791 liquid phase Substances 0.000 abstract 2
- 238000004517 catalytic hydrocracking Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 239000000047 product Substances 0.000 abstract 1
- 239000012808 vapor phase Substances 0.000 abstract 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
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Procedimiento para dividir un efluente productos de reacción hidrocarbonoso en fase mixta, (1) resultando dicho efluente producto de la conversión de un material de carga de hidrocarburo que hierve por encima de una temperatura de 204, 4ºC, y (2) conteniendo hidrógeno a recircular a la zona de conversión, hidrocarburos normalmente líquidos e hidrocarburos normalmente vapor, el cual procedimiento de separación comprende las etapas en secuencia de: (1) dividir dicho efluente producto, en una primera zona de separación a sustancialmente la misma presión que dicho efluente, para proporcionar (i) una primera fase líquida, y (ii) una primera fase vapor; (b) enfriar dicha primera fase vapor hasta una temperatura comprendida entre 10ºC y 65,6ºC, y dividir la fase vapor enfriada, en una segunda zona de separación a sustancialmente la misma presión que dicha primera zona de separación, proporcionando (i) una segunda fase vapor rica en hidrógeno, y (ii) una segunda fase líquida que contiene metano; ©aumentar la temperatura de dicha segunda fase líquida, y dividir la fase líquida calentada, en una tercera zona de separación a una presión sustancialmente reducida, eligiéndose dichas temperatura y presión para proporcionar (i) una tercera fase líquida, y (ii) una tercera fase vapor que contiene al menos aproximadamente 70,0% del metano de dicha segunda fase líquida; y (d) mezclar al menos una porción de dicha tercera fase líquida con dicha primera fase vapor.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US05/938,182 US4159937A (en) | 1978-08-30 | 1978-08-30 | Mixed-phase reaction product effluent separation process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES483690A1 true ES483690A1 (es) | 1980-05-16 |
Family
ID=25471029
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES483690A Expired ES483690A1 (es) | 1978-08-30 | 1979-08-28 | Procedimiento para dividir un efluente producto de reaccion hidrocarbonoso en fase mixta |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US4159937A (es) |
| JP (1) | JPS585958B2 (es) |
| CA (1) | CA1127580A (es) |
| DE (1) | DE2934679C2 (es) |
| ES (1) | ES483690A1 (es) |
| FR (1) | FR2434859A1 (es) |
| GB (1) | GB2034745B (es) |
| IT (1) | IT1193498B (es) |
Families Citing this family (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4333820A (en) * | 1981-01-26 | 1982-06-08 | Uop Inc. | Recovery of normally gaseous hydrocarbons from net excess hydrogen in a catalytic reforming process |
| US4333818A (en) * | 1981-01-26 | 1982-06-08 | Uop Inc. | Separation of normally gaseous hydrocarbons from a catalytic reforming effluent and recovery of purified hydrogen |
| US4374726A (en) * | 1981-01-26 | 1983-02-22 | Uop Inc. | Separation of hydrogen from a catalytic reforming zone effluent stream |
| US4333817A (en) * | 1981-01-26 | 1982-06-08 | Uop Inc. | Separation of normally gaseous hydrocarbons from a catalytic reforming effluent and recovery of purified hydrogen |
| US4333819A (en) * | 1981-01-26 | 1982-06-08 | Uop Inc. | Separation and recovery of hydrogen and normally gaseous hydrocarbons from net excess hydrogen from a catalytic reforming process |
| US4469587A (en) * | 1983-09-02 | 1984-09-04 | Intevep, S.A. | Process for the conversion of asphaltenes and resins in the presence of steam, ammonia and hydrogen |
| US4457834A (en) * | 1983-10-24 | 1984-07-03 | Lummus Crest, Inc. | Recovery of hydrogen |
| US4673488A (en) * | 1985-08-26 | 1987-06-16 | Uop Inc. | Hydrocarbon-conversion process with fractionator overhead vapor recycle |
| GB8807807D0 (en) * | 1988-03-31 | 1988-05-05 | Shell Int Research | Process for separating hydroprocessed effluent streams |
| US5082551A (en) * | 1988-08-25 | 1992-01-21 | Chevron Research And Technology Company | Hydroconversion effluent separation process |
| US5178751A (en) * | 1991-11-27 | 1993-01-12 | Uop | Two-stage process for purifying a hydrogen gas and recovering liquifiable hydrocarbons from hydrocarbonaceous effluent streams |
| US5221463A (en) * | 1991-12-09 | 1993-06-22 | Exxon Research & Engineering Company | Fixed-bed/moving-bed two stage catalytic reforming with recycle of hydrogen-rich stream to both stages |
| US6497812B1 (en) | 1999-12-22 | 2002-12-24 | Chevron U.S.A. Inc. | Conversion of C1-C3 alkanes and fischer-tropsch products to normal alpha olefins and other liquid hydrocarbons |
| CN102099112B (zh) * | 2008-06-25 | 2013-11-20 | 国际壳牌研究有限公司 | 制备链烷烃的方法 |
| CN106147830B (zh) * | 2015-04-27 | 2017-11-10 | 中国石油天然气集团公司 | 加氢反应流出物的分离系统及分离方法 |
| US10711205B2 (en) * | 2017-06-22 | 2020-07-14 | Uop Llc | Process for recovering hydroprocessed effluent with improved hydrogen recovery |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3364134A (en) * | 1966-11-30 | 1968-01-16 | Universal Oil Prod Co | Black oil conversion and desulfurization process |
| US3375189A (en) * | 1966-11-30 | 1968-03-26 | Universal Oil Prod Co | Conversion of black oils to maximize gasoline production |
| US3371029A (en) * | 1966-11-30 | 1968-02-27 | Universal Oil Prod Co | Mixed-phase conversion product separation process |
| US3402122A (en) * | 1966-12-05 | 1968-09-17 | Universal Oil Prod Co | Preparation of an absorption medium for hydrocarbon recovery |
| US3371030A (en) * | 1966-12-30 | 1968-02-27 | Universal Oil Prod Co | Black oil conversion product separation process |
| US3723301A (en) * | 1971-12-01 | 1973-03-27 | Universal Oil Prod Co | Process for the recovery of heat from hydrocarbons and the separationthereof |
| US3801494A (en) * | 1972-09-15 | 1974-04-02 | Standard Oil Co | Combination hydrodesulfurization and reforming process |
-
1978
- 1978-08-30 US US05/938,182 patent/US4159937A/en not_active Expired - Lifetime
-
1979
- 1979-08-28 CA CA334,595A patent/CA1127580A/en not_active Expired
- 1979-08-28 FR FR7921545A patent/FR2434859A1/fr active Granted
- 1979-08-28 DE DE2934679A patent/DE2934679C2/de not_active Expired
- 1979-08-28 ES ES483690A patent/ES483690A1/es not_active Expired
- 1979-08-29 GB GB7929919A patent/GB2034745B/en not_active Expired
- 1979-08-30 JP JP54111035A patent/JPS585958B2/ja not_active Expired
- 1979-08-30 IT IT25393/79A patent/IT1193498B/it active
Also Published As
| Publication number | Publication date |
|---|---|
| GB2034745A (en) | 1980-06-11 |
| DE2934679A1 (de) | 1980-03-13 |
| US4159937A (en) | 1979-07-03 |
| IT7925393A0 (it) | 1979-08-30 |
| JPS585958B2 (ja) | 1983-02-02 |
| GB2034745B (en) | 1982-09-22 |
| JPS5569694A (en) | 1980-05-26 |
| IT1193498B (it) | 1988-07-08 |
| FR2434859B1 (es) | 1982-04-02 |
| FR2434859A1 (fr) | 1980-03-28 |
| CA1127580A (en) | 1982-07-13 |
| DE2934679C2 (de) | 1984-04-05 |
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