GB1267077A - - Google Patents

Info

Publication number
GB1267077A
GB1267077A GB1267077DA GB1267077A GB 1267077 A GB1267077 A GB 1267077A GB 1267077D A GB1267077D A GB 1267077DA GB 1267077 A GB1267077 A GB 1267077A
Authority
GB
United Kingdom
Prior art keywords
plates
stirring system
stirring
series
reaction mixture
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
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 filed Critical
Publication of GB1267077A publication Critical patent/GB1267077A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • B01J19/20Stationary reactors having moving elements inside in the form of helices, e.g. screw reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/07Stirrers characterised by their mounting on the shaft
    • B01F27/072Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis
    • B01F27/0724Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis directly mounted on the rotating axis
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • C08G63/785Preparation processes characterised by the apparatus used
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/18Details relating to the spatial orientation of the reactor
    • B01J2219/182Details relating to the spatial orientation of the reactor horizontal

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Polyesters Or Polycarbonates (AREA)

Abstract

1,267,077. Polymerisation apparatus; mixing apparatus. SOC. RHODIACETA. 23 May, 1969 [27 May, 1968], No. 26593/69. Headings B1C and B1X. [Also in Division C3] Apparatus suitable for continuously carrying out reactions in which the viscosity of the reaction mixture changes as the reaction proceeds and in which the reaction mixture and product are in the liquid phase, e.g. polycondensation, comprises a hollow shell reactor 1 with degassing orifices 4 through with the reaction mixture is continually passed from inlet 2 to outlet 3. The reactor has a substantially horizontal axis 6 about which a stirring system 7 rotates, the stirring system consisting of at least one series A, B, C or D of flat circular sector stirring plates 8 normal to the axis spaced from one another both linearly along and angularly around the axis, the plates being arranged in sets of one or more plates in each plane normal to the axisthe linear spacing and angular spacing of the plates being inter-related and related to the average viscosity and average density of the reaction medium at a designated point. The stirring system preferably comprises several stirring series A, B, C and D in each of which the distance between plates increases and the angular spacing remains constant, this latter increasing from one series to the next. The stirring system has a coefficient of obstruction which vanes from one end of the stirring system to the other, being 0.1-0.5 at the feed end and 0.01-0.1 at the outlet end. A speed of rotation of between 1 and 10 rev./minute is generally used and scraper strips 9 may be fitted to the circumference of the plates.
GB1267077D 1968-05-27 1969-05-23 Expired GB1267077A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR153065 1968-05-27

Publications (1)

Publication Number Publication Date
GB1267077A true GB1267077A (en) 1972-03-15

Family

ID=8650629

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1267077D Expired GB1267077A (en) 1968-05-27 1969-05-23

Country Status (10)

Country Link
JP (1) JPS4925436B1 (en)
AT (1) AT300372B (en)
BE (1) BE733657A (en)
CH (1) CH518998A (en)
DE (1) DE1926987A1 (en)
ES (1) ES367710A1 (en)
FR (1) FR1578999A (en)
GB (1) GB1267077A (en)
LU (1) LU58718A1 (en)
NL (1) NL6907626A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1017260C2 (en) * 2001-02-01 2002-08-02 Dsm Nv Continuous production of thermoplastic polyesters, includes a polycondensation step in which the partial pressure of the volatile reaction products is higher at the start of polycondensation than at the end
WO2011062600A1 (en) * 2009-11-19 2011-05-26 E. I. Du Pont De Nemours And Company Polycondensation with a kneader reactor

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3807703A (en) * 1972-10-12 1974-04-30 Usm Corp Mixer-emulsators
CN101220140B (en) * 2007-12-24 2010-08-25 中昊晨光化工研究院 Reaction device for interesterification and polycondensation reaction

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1017260C2 (en) * 2001-02-01 2002-08-02 Dsm Nv Continuous production of thermoplastic polyesters, includes a polycondensation step in which the partial pressure of the volatile reaction products is higher at the start of polycondensation than at the end
WO2011062600A1 (en) * 2009-11-19 2011-05-26 E. I. Du Pont De Nemours And Company Polycondensation with a kneader reactor

Also Published As

Publication number Publication date
BE733657A (en) 1969-11-27
FR1578999A (en) 1969-08-22
CH518998A (en) 1972-02-15
AT300372B (en) 1972-07-25
JPS4925436B1 (en) 1974-06-29
NL6907626A (en) 1969-12-01
DE1926987A1 (en) 1969-12-04
LU58718A1 (en) 1970-01-14
ES367710A1 (en) 1971-04-16

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PLNP Patent lapsed through nonpayment of renewal fees