ES451790A1 - Un procedimiento mejorado para la separacion de parafinas normales a partir de una corriente de alimentacion. - Google Patents

Un procedimiento mejorado para la separacion de parafinas normales a partir de una corriente de alimentacion.

Info

Publication number
ES451790A1
ES451790A1 ES451790A ES451790A ES451790A1 ES 451790 A1 ES451790 A1 ES 451790A1 ES 451790 A ES451790 A ES 451790A ES 451790 A ES451790 A ES 451790A ES 451790 A1 ES451790 A1 ES 451790A1
Authority
ES
Spain
Prior art keywords
adsorbent
adsorbed
normal paraffins
contaminant
desorbent material
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
Application number
ES451790A
Other languages
English (en)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
VOP Inc
Original Assignee
VOP Inc
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 VOP Inc filed Critical VOP Inc
Publication of ES451790A1 publication Critical patent/ES451790A1/es
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G25/00Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
    • C10G25/02Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with ion-exchange material
    • C10G25/03Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with ion-exchange material with crystalline alumino-silicates, e.g. molecular sieves
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/12Purification; Separation; Use of additives by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers
    • C07C7/13Purification; Separation; Use of additives by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers by molecular-sieve technique

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

Un procedimiento mejorado para la separación de parafinas normales a partir de una corriente de alimentación que contiene una mezcla de parafinas normales e isoparafinas junto con hidrocarburos aromáticos, procedimiento que emplea un adsorbente que comprende una zeolita selectiva con respecto a la forma y que comprende las etapas de: (a) poner en contacto dicho adsorbente con dicha alimentación en condiciones de adsorción para efectuar la adsorción selectiva de las parafinas normales y de una porción de los hidrocarburos aromáticos por el adsorbente; (b) retirar una corriente de refinado que comprende las isoparafinas adsorbidas menos selectivamente de dicho adsorbente; (c) poner en contacto dicho adsorbente con un material desorbente en condiciones de desorción para efectuar la desorción de las parafinas normales de dicho adsorbente; (d) separar de dicho adsorbente una corriente de extracto que comprende parafinas normales; y, (e) hacer pasar al menos una porción de dicha corriente de extracto a un medio de separación y separar en éste, en condiciones de separación, las parafinas normales del material desorbente, cuya mejora comprende utilizar una operación de desorción en dos etapas, que comprende las etapas de: (i) poner en contacto en primeras condiciones de desorción dicho adsorbente con un primer material desorbente para efectuar la desorción de dichos hidrocarburos aromáticos de la alimentación; (ii) retirar una primera corriente de extracto que comprende dichos hidrocarburos aromáticos de la alimentación y dicho primer material desorbente de dicho adsorbente; (iii) poner en contacto en segundas condiciones de desorción dicho adsorbente con un segundo material desorbente para efectuar la desorción de las parafinas normales; (iv) retirar una segunda corriente de extracto que comprende parafinas normales y segundo material desorbente de dicho adsorbente; y (v) hacer pasar al menos una porción de dicha segunda corriente de extracto a un medio de separación y separar en éste, en condiciones de separación, las parafinas normales de dicho segundo material desorbente.
ES451790A 1975-09-24 1976-09-23 Un procedimiento mejorado para la separacion de parafinas normales a partir de una corriente de alimentacion. Expired ES451790A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US05/616,470 US4036745A (en) 1975-09-24 1975-09-24 Process for separating normal and isoparaffins

Publications (1)

Publication Number Publication Date
ES451790A1 true ES451790A1 (es) 1978-01-01

Family

ID=24469602

Family Applications (1)

Application Number Title Priority Date Filing Date
ES451790A Expired ES451790A1 (es) 1975-09-24 1976-09-23 Un procedimiento mejorado para la separacion de parafinas normales a partir de una corriente de alimentacion.

Country Status (33)

Country Link
US (1) US4036745A (es)
JP (1) JPS5283302A (es)
AR (1) AR216637A1 (es)
AU (1) AU502492B2 (es)
BR (1) BR7606346A (es)
CA (1) CA1081130A (es)
CH (1) CH625776A5 (es)
CS (1) CS191988B2 (es)
DD (1) DD127426A5 (es)
DE (1) DE2640365C3 (es)
EG (1) EG12618A (es)
ES (1) ES451790A1 (es)
FR (1) FR2325624A1 (es)
GB (1) GB1551285A (es)
GR (1) GR61273B (es)
HU (1) HU179328B (es)
IE (1) IE44026B1 (es)
IL (1) IL50395A (es)
IN (1) IN145637B (es)
IT (1) IT1070834B (es)
MX (1) MX143794A (es)
NL (1) NL186151C (es)
NO (1) NO148594C (es)
OA (1) OA05442A (es)
PH (1) PH15196A (es)
PL (1) PL106066B1 (es)
PT (1) PT65561B (es)
RO (1) RO70262A (es)
SE (1) SE425386B (es)
SU (1) SU686611A3 (es)
TR (1) TR19040A (es)
YU (1) YU39125B (es)
ZA (1) ZA765227B (es)

Families Citing this family (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4184943A (en) * 1978-12-21 1980-01-22 Uop Inc. Fractionation in an adsorptive hydrocarbon separation process
JPS62296Y2 (es) * 1979-06-28 1987-01-07
JPS5614583A (en) * 1979-07-17 1981-02-12 Nippon Petrochem Co Ltd Separating normal paraffin
US4648961A (en) * 1982-09-29 1987-03-10 Chevron Research Company Method of producing high aromatic yields through aromatics removal and recycle of remaining material
GB8526812D0 (en) * 1985-10-31 1985-12-04 Shell Int Research Separating branch-from unbranched hydrocarbons
US5132486A (en) * 1990-10-09 1992-07-21 Wylie Engineering & Construction, Inc. Adsorption-desorption separation process for the separation of low and high octane components in virgin naphthas
WO1993002154A1 (en) * 1991-07-25 1993-02-04 Exxon Chemical Patents, Inc. Adsorption process for liquid separation
FR2751641B1 (fr) * 1996-07-26 1998-09-11 Inst Francais Du Petrole Procede de separation isoalcanes/n-alcanes par adsorption en phase gazeuse utilisant une modulation de pression et quatre adsorbeurs
FR2781860B1 (fr) * 1998-07-31 2000-09-01 Inst Francais Du Petrole Systeme de mise en communication alternee d'au moins quatre fluides et son application dans un procede de separation en lit mobile simule
US6069289A (en) * 1998-08-31 2000-05-30 Uop Llc Process for separating and recovering multimethyl-branched alkanes
US6483002B1 (en) 2000-09-26 2002-11-19 Uop Llc Integrated fractional distillation for adsorptive separation process
US6348637B1 (en) 2000-09-26 2002-02-19 Uop Llc Multifunction fractionation column for adsorptive separation processes
US6395951B1 (en) 2000-09-26 2002-05-28 Uop Llc Adsorptive separation product recovery by fractional distillation
US6407305B1 (en) 2000-09-27 2002-06-18 Uop Llc Adsorptive separation process for recovery of two paraffin products
US6395950B1 (en) 2000-11-10 2002-05-28 Uop Llc Isomerization with adsorptive separation and dividing wall fractional distillation
EP1334079A2 (en) 2000-11-16 2003-08-13 Uop Llc Adsorptive separation process for recovery of para-xylene
KR100645660B1 (ko) * 2001-11-09 2006-11-13 에스케이 주식회사 탄화수소 유분으로부터 노말파라핀을 분리하는 공정 및분리된 유분의 활용
US20050101814A1 (en) * 2003-11-07 2005-05-12 Foley Timothy D. Ring opening for increased olefin production
FR2930174B1 (fr) * 2008-04-17 2010-04-30 Inst Francais Du Petrole Dispositif perfectionne de separation en lit mobile simule
US7728187B2 (en) * 2008-06-30 2010-06-01 Uop Llc Adsorbent and process for the separation of meta-xylene from aromatic hydrocarbons
US20100116711A1 (en) * 2008-11-12 2010-05-13 Kellogg Brown & Root Llc Systems and Methods for Producing N-Paraffins From Low Value Feedstocks
FR2952646B1 (fr) * 2009-11-13 2012-09-28 Inst Francais Du Petrole Procede de production de carburants kerosene et diesel de haute qualite et de coproduction d'hydrogene a partir de coupes saturees legeres
PE20130491A1 (es) 2009-12-30 2013-05-02 Basf Pharma Callanish Ltd Proceso simulado de separacion cromatografica de lecho movil para la purificacion de acidos grasos poliinsaturados
US20120302813A1 (en) * 2011-05-27 2012-11-29 Uop Llc Processes and apparatuses for producing a substantially linear paraffin product
GB201111589D0 (en) 2011-07-06 2011-08-24 Equateq Ltd New modified process
GB201111601D0 (en) 2011-07-06 2011-08-24 Equateq Ltd New process
GB201111591D0 (en) 2011-07-06 2011-08-24 Equateq Ltd Further new process
GB201111594D0 (en) 2011-07-06 2011-08-24 Equateq Ltd New improved process
GB201111595D0 (en) 2011-07-06 2011-08-24 Equateq Ltd Improved process
US9085499B2 (en) * 2011-11-09 2015-07-21 Uop Llc Energy efficiency in adsorptive separation
GB201300354D0 (en) 2013-01-09 2013-02-20 Basf Pharma Callanish Ltd Multi-step separation process
US8802880B1 (en) 2013-05-07 2014-08-12 Group Novasep Chromatographic process for the production of highly purified polyunsaturated fatty acids
US9428711B2 (en) 2013-05-07 2016-08-30 Groupe Novasep Chromatographic process for the production of highly purified polyunsaturated fatty acids
EP2883860B1 (fr) 2013-12-11 2016-08-24 Novasep Process Procédé chromatographique de production d'acides gras polyinsaturés
US10975031B2 (en) 2014-01-07 2021-04-13 Novasep Process Method for purifying aromatic amino acids
US9902912B2 (en) * 2014-01-29 2018-02-27 Uop Llc Hydrotreating coker kerosene with a separate trim reactor
US9816038B2 (en) * 2014-06-12 2017-11-14 Uop Llc Kerosene hydrotreating with a separate high pressure trim reactor

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL293774A (es) * 1962-06-08
US3274099A (en) * 1963-02-19 1966-09-20 Universal Oil Prod Co Continuous solid-fluid contacting process
US3378486A (en) * 1965-12-28 1968-04-16 Exxon Research Engineering Co Purification of normal paraffins
US3715409A (en) * 1971-03-08 1973-02-06 Universal Oil Prod Co Hydrocarbon separation
US3723302A (en) * 1971-04-30 1973-03-27 Universal Oil Prod Co Process for separating olefins from saturated hydrocarbons
US3753896A (en) * 1971-05-20 1973-08-21 Texaco Trinidad N-paraffin adsorption with a 20 to 55% overcharge
US3696107A (en) * 1971-05-27 1972-10-03 Richard W Neuzil Improved hydrocarbon separation process

Also Published As

Publication number Publication date
PL106066B1 (pl) 1979-11-30
SE7610541L (sv) 1977-03-25
NO148594C (no) 1983-11-09
YU39125B (en) 1984-06-30
PT65561B (en) 1978-03-28
MX143794A (es) 1981-07-16
AU1738776A (en) 1978-03-09
IL50395A (en) 1979-07-25
PH15196A (en) 1982-09-17
IL50395A0 (en) 1976-10-31
OA05442A (fr) 1981-03-31
IE44026B1 (en) 1981-07-29
DD127426A5 (es) 1977-09-21
DE2640365A1 (de) 1977-03-31
GB1551285A (en) 1979-08-30
EG12618A (en) 1979-06-30
CS191988B2 (en) 1979-07-31
FR2325624A1 (fr) 1977-04-22
DE2640365C3 (de) 1982-01-28
BR7606346A (pt) 1977-06-07
FR2325624B1 (es) 1979-09-28
NL7609951A (nl) 1977-03-28
CH625776A5 (es) 1981-10-15
IT1070834B (it) 1985-04-02
HU179328B (en) 1982-09-28
ZA765227B (en) 1977-08-31
IE44026L (en) 1977-03-24
GR61273B (en) 1978-10-17
PT65561A (en) 1976-10-01
DE2640365B2 (de) 1981-02-12
NL186151B (nl) 1990-05-01
IN145637B (es) 1985-01-05
TR19040A (tr) 1978-03-20
CA1081130A (en) 1980-07-08
SU686611A3 (ru) 1979-09-15
JPS5283302A (en) 1977-07-12
AR216637A1 (es) 1980-01-15
US4036745A (en) 1977-07-19
AU502492B2 (en) 1979-07-26
NL186151C (nl) 1990-10-01
SE425386B (sv) 1982-09-27
NO763224L (no) 1977-03-25
RO70262A (ro) 1982-04-12
YU231276A (en) 1982-05-31
NO148594B (no) 1983-08-01
JPS5634569B2 (es) 1981-08-11

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Legal Events

Date Code Title Description
FD1A Patent lapsed

Effective date: 19981001