GB1493489A - Process for the recovery of high purity paraxylene - Google Patents

Process for the recovery of high purity paraxylene

Info

Publication number
GB1493489A
GB1493489A GB10118/75A GB1011875A GB1493489A GB 1493489 A GB1493489 A GB 1493489A GB 10118/75 A GB10118/75 A GB 10118/75A GB 1011875 A GB1011875 A GB 1011875A GB 1493489 A GB1493489 A GB 1493489A
Authority
GB
United Kingdom
Prior art keywords
xylene
cake
zone
separating
mother liquor
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
GB10118/75A
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.)
Standard Oil Co
Original Assignee
Standard Oil Co
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 Standard Oil Co filed Critical Standard Oil Co
Publication of GB1493489A publication Critical patent/GB1493489A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D11/00Solvent extraction
    • B01D11/02Solvent extraction of solids
    • B01D11/0269Solid material in other moving receptacles
    • B01D11/0273Solid material in other moving receptacles in rotating drums
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D11/00Solvent extraction
    • B01D11/02Solvent extraction of solids
    • B01D11/028Flow sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D9/00Crystallisation
    • B01D9/0004Crystallisation cooling by heat exchange
    • B01D9/0013Crystallisation cooling by heat exchange by indirect heat exchange
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D9/00Crystallisation
    • B01D9/004Fractional crystallisation; Fractionating or rectifying columns
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D9/00Crystallisation
    • B01D9/0059General arrangements of crystallisation plant, e.g. flow sheets
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/14Purification; Separation; Use of additives by crystallisation; Purification or separation of the crystals

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

1493489 Purification of para-xylene by crystallisation STANDARD OIL CO 11 March 1975 [11 March 1974] 10118/75 Heading B1G A process for separating para-xylene having a purity in excess of 99% from a liquid mixture of xylenes and C 8 aromatics comprises cooling the mixture to a temperature just above the p-xylene eutetic to form a slurry and separating a substantial portion of mother liquor from the slurry to form a porous p-xylene cake having entrained mother liquor therein, washing the cake with from 0.4- 1.2 parts by wt, of wash liquid per part of cake, the wash liquid comprising a major portion of a C 5 -C 8 hydrocarbon and a minor portion of dissolved p-xylene, and separating a substantial portion of the wash liquid from the washed cake to recover the product of p-xylene. It is preferred to carry out the process using a continuous feed multiple zone centrifugal separator unit as shown in Fig. 2 in a first zone of which solid-liquid separation is effected whereby a substantial portion of the mother liquor is extracted and discarded. The p-xylene filter cake passes to a second zone where it is washed, preferably with hexane containing 5-30 parts of p-xylene at a temperature of about 70‹F. The wash liquor effluent is distilled to recover a mixture of xylene iximers for recycle and hexane for revise. The washed cake is dried in a third zone of the separator and passed to a melt tank and a fractionation tower to remove hexane and so yields high purity pxylene product.
GB10118/75A 1974-03-11 1975-03-11 Process for the recovery of high purity paraxylene Expired GB1493489A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US44990974A 1974-03-11 1974-03-11

Publications (1)

Publication Number Publication Date
GB1493489A true GB1493489A (en) 1977-11-30

Family

ID=23785971

Family Applications (1)

Application Number Title Priority Date Filing Date
GB10118/75A Expired GB1493489A (en) 1974-03-11 1975-03-11 Process for the recovery of high purity paraxylene

Country Status (11)

Country Link
JP (1) JPS50126624A (en)
BE (1) BE826553A (en)
BR (1) BR7501394A (en)
DD (1) DD117669A5 (en)
DE (1) DE2509182A1 (en)
ES (1) ES435492A1 (en)
FR (1) FR2263994A1 (en)
GB (1) GB1493489A (en)
IT (1) IT1029989B (en)
NL (1) NL7502812A (en)
TR (1) TR18478A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0084895A2 (en) * 1982-01-11 1983-08-03 Nederlandse Organisatie voor toegepast-natuurwetenschappelijk onderzoek TNO A process for the continuous partial crystallization and the separation of a liquid mixture and a device for carrying out this process
CN102372591A (en) * 2010-08-23 2012-03-14 中国石油化工股份有限公司 Crystallization method for p-xylene production
CN102372590A (en) * 2010-08-23 2012-03-14 中国石油化工股份有限公司 Crystallization method for preparing para-xylene from xylol
EP2686096A1 (en) * 2011-03-18 2014-01-22 GTC Technology US LLC Energy recovery from mother liquid in paraxylene crystallization process
CN103772127A (en) * 2012-10-25 2014-05-07 中国石油化工股份有限公司 Method for producing p-xylene
CN103880582A (en) * 2012-12-19 2014-06-25 中国石油化工股份有限公司 Multistage crystallization method for p-xylene
CN112679305A (en) * 2019-10-18 2021-04-20 中国石油化工股份有限公司 Method for producing p-xylene

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5498822A (en) * 1994-04-04 1996-03-12 Mobil Oil Corporation Single temperature stage crystallization of paraxylene

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0084895A2 (en) * 1982-01-11 1983-08-03 Nederlandse Organisatie voor toegepast-natuurwetenschappelijk onderzoek TNO A process for the continuous partial crystallization and the separation of a liquid mixture and a device for carrying out this process
EP0084895A3 (en) * 1982-01-11 1983-08-10 Nederlandse Centrale Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek A process for the continuous partial crystallization and the separation of a liquid mixture and a device for carrying out this process
CN102372591B (en) * 2010-08-23 2014-03-26 中国石油化工股份有限公司 Crystallization method for p-xylene production
CN102372590A (en) * 2010-08-23 2012-03-14 中国石油化工股份有限公司 Crystallization method for preparing para-xylene from xylol
CN102372591A (en) * 2010-08-23 2012-03-14 中国石油化工股份有限公司 Crystallization method for p-xylene production
CN102372590B (en) * 2010-08-23 2014-03-26 中国石油化工股份有限公司 Crystallization method for preparing para-xylene from xylol
EP2686096A1 (en) * 2011-03-18 2014-01-22 GTC Technology US LLC Energy recovery from mother liquid in paraxylene crystallization process
CN103596670A (en) * 2011-03-18 2014-02-19 Gtc科技美国有限责任公司 Energy recovery from mother liquid in paraxylene crystallization process
EP2686096A4 (en) * 2011-03-18 2014-09-10 Gtc Technology Us Llc Energy recovery from mother liquid in paraxylene crystallization process
CN103772127A (en) * 2012-10-25 2014-05-07 中国石油化工股份有限公司 Method for producing p-xylene
CN103772127B (en) * 2012-10-25 2015-07-08 中国石油化工股份有限公司 Method for producing p-xylene
CN103880582A (en) * 2012-12-19 2014-06-25 中国石油化工股份有限公司 Multistage crystallization method for p-xylene
CN103880582B (en) * 2012-12-19 2015-08-12 中国石油化工股份有限公司 P-Xylol multistage crystallization method
CN112679305A (en) * 2019-10-18 2021-04-20 中国石油化工股份有限公司 Method for producing p-xylene
CN112679305B (en) * 2019-10-18 2022-10-11 中国石油化工股份有限公司 Method for producing p-xylene

Also Published As

Publication number Publication date
BR7501394A (en) 1975-12-09
BE826553A (en) 1975-09-11
NL7502812A (en) 1975-09-15
ES435492A1 (en) 1977-01-01
IT1029989B (en) 1979-03-20
DE2509182A1 (en) 1975-10-02
DD117669A5 (en) 1976-01-20
JPS50126624A (en) 1975-10-04
FR2263994A1 (en) 1975-10-10
TR18478A (en) 1977-02-24

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee