GB1114477A

GB1114477A – Polycondensation reactor
– Google Patents

GB1114477A – Polycondensation reactor
– Google Patents
Polycondensation reactor

Info

Publication number
GB1114477A

GB1114477A
GB24146/66A
GB2414666A
GB1114477A
GB 1114477 A
GB1114477 A
GB 1114477A
GB 24146/66 A
GB24146/66 A
GB 24146/66A
GB 2414666 A
GB2414666 A
GB 2414666A
GB 1114477 A
GB1114477 A
GB 1114477A
Authority
GB
United Kingdom
Prior art keywords
consist
chambers
outlet
chamber
divided
Prior art date
1965-06-01
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
GB24146/66A
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.)

Vickers Zimmer AG

Original Assignee
Vickers Zimmer AG
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.)
1965-06-01
Filing date
1966-05-31
Publication date
1968-05-22

1966-05-31
Application filed by Vickers Zimmer AG
filed
Critical
Vickers Zimmer AG

1968-05-22
Publication of GB1114477A
publication
Critical
patent/GB1114477A/en

Status
Expired
legal-status
Critical
Current

Links

Espacenet

Global Dossier

Discuss

Classifications

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

B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus

B01J19/18—Stationary reactors having moving elements inside

B—PERFORMING OPERATIONS; TRANSPORTING

B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL

B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING

B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders

B01F27/05—Stirrers

B01F27/09—Stirrers characterised by the mounting of the stirrers with respect to the receptacle

B01F27/092—Stirrers characterised by the mounting of the stirrers with respect to the receptacle occupying substantially the whole interior space of the receptacle

B—PERFORMING OPERATIONS; TRANSPORTING

B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL

B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING

B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders

B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis

B01F27/625—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis the receptacle being divided into compartments, e.g. with porous divisions

B—PERFORMING OPERATIONS; TRANSPORTING

B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL

B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING

B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders

B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis

B01F27/72—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with helices or sections of helices

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

B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus

B01J19/18—Stationary reactors having moving elements inside

B01J19/20—Stationary reactors having moving elements inside in the form of helices, e.g. screw reactors

C—CHEMISTRY; METALLURGY

C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON

C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS

C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule

C08G63/78—Preparation processes

C08G63/785—Preparation processes characterised by the apparatus used

B—PERFORMING OPERATIONS; TRANSPORTING

B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL

B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING

B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application

B01F35/50—Mixing receptacles

B01F35/53—Mixing receptacles characterised by the configuration of the interior, e.g. baffles for facilitating the mixing of components

B01F35/531—Mixing receptacles characterised by the configuration of the interior, e.g. baffles for facilitating the mixing of components with baffles, plates or bars on the wall or the bottom

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

B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus

B01J2219/00049—Controlling or regulating processes

B01J2219/00051—Controlling the temperature

B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids

B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor

B01J2219/00094—Jackets

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

B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus

B01J2219/00049—Controlling or regulating processes

B01J2219/00162—Controlling or regulating processes controlling the pressure

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

B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus

B01J2219/00049—Controlling or regulating processes

B01J2219/00164—Controlling or regulating processes controlling the flow

B01J2219/00166—Controlling or regulating processes controlling the flow controlling the residence time inside the reactor vessel

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

B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus

B01J2219/18—Details relating to the spatial orientation of the reactor

B01J2219/182—Details relating to the spatial orientation of the reactor horizontal

Abstract

1,114,477. Polycondensation apparatus. VICKERS-ZIMMER PLANUNG UND BAU VON INDUSTRIEANLAGEN A.G. 31 May, 1966 [1 June, 1965], No. 24146/66. Heading B1X. A polycondensation reactor comprises a horizontally oriented cylindrical activated vessel 1 divided by partitions 5 into a plurality of reaction chambers, apertures in the dividers allowing for through flow of liquid and a rotatable shaft 3 carrying flights 7, 8 agitating the material while it moves from chamber to chamber from inlet 9 to outlet 10, the vapours forming being removed through outlet 11. The dividers 5 consist of baffle plates insulated by plates 5a to reduce heat transfer between chambers, and the jacket is divided into a plurality of sections for temperature control of the individual chambers. The flights may consist of two continuous helices extending through the vessel as shown in Fig. 1 or may consist of circular rings arranged in planes parallel to each other and inclined to the shaft (see Fig. 3 not shown).

GB24146/66A
1965-06-01
1966-05-31
Polycondensation reactor

Expired

GB1114477A
(en)

Applications Claiming Priority (1)

Application Number
Priority Date
Filing Date
Title

US46017465A

1965-06-01
1965-06-01

Publications (1)

Publication Number
Publication Date

GB1114477A
true

GB1114477A
(en)

1968-05-22

Family
ID=23827650
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

GB24146/66A
Expired

GB1114477A
(en)

1965-06-01
1966-05-31
Polycondensation reactor

Country Status (5)

Country
Link

US
(1)

US3440019A
(en)

AT
(1)

AT270230B
(en)

DE
(1)

DE1645630B2
(en)

GB
(1)

GB1114477A
(en)

NL
(1)

NL150819B
(en)

Families Citing this family (16)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US3617225A
(en)

*

1967-06-22
1971-11-02
Vickers Zimmer Ag
Polycondensation apparatus

US3728083A
(en)

*

1971-03-03
1973-04-17
Allied Chem
Polymer finisher

JPS5021514B2
(en)

*

1972-04-12
1975-07-23

US3987021A
(en)

*

1973-08-30
1976-10-19
Karl Fischer Apparate U. Rohrleitungsbau
Process utilizing a stirring reactor

DE3377579D1
(en)

*

1983-10-07
1988-09-08
Fischer Karl Ind Gmbh
Process for the continuous removal of residual monomers and the post-polymerisation of polyamide 6, and apparatus for carrying it out

US5599507A
(en)

*

1994-11-09
1997-02-04
Shaw; Gordon
Reactor apparatus for preparing a polymeric material

US6007782A
(en)

*

1996-09-11
1999-12-28
Arteva North America S.A.R.L.
Reactor with a flexurally rigid stirrer element

US5814282A
(en)

*

1997-01-15
1998-09-29
Lohe; Hans
High surface intermeshing profile reactor

ITTO20021124A1
(en)

*

2002-12-24
2004-06-25
Giuliano Cavaglia

REACTOR AND METHOD FOR POLYMERIZING THE POLYETHYLENE TEREPHALATE (PET) IN CONTINUOUS SOLID PHASE.

JP4177769B2
(en)

*

2004-02-04
2008-11-05
株式会社日立製作所

Polymer synthesizer

DE102005003731B4
(en)

2005-01-26
2006-10-05
Epc Industrial Engineering Gmbh

Reactor for the continuous and simultaneous production of various and variably viscous polyester products with control of the process progress via the hydraulic drive system (s)

EP2055730B1
(en)

*

2007-10-29
2013-02-27
Hitachi Plant Technologies, Ltd.
Polymer producing method and apparatus and polymer degassing method and apparatus

DE102008056411A1
(en)

2008-11-07
2010-05-20
Dürr Systems GmbH

Coating plant component, in particular bell cup, and corresponding manufacturing method

EP2428266B1
(en)

*

2010-09-10
2013-07-10
Princo Middle East FZE
Process for preparation of high viscosity polymeric materials

RU2761057C2
(en)

2017-07-12
2021-12-02
Арланксео Дойчланд Гмбх
Reactor and continuous polymerization method

CN110385098A
(en)

*

2019-08-02
2019-10-29
双龙集团有限公司
Horizontal-type high temperature kettle

Family Cites Families (4)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US2626856A
(en)

*

1948-06-22
1953-01-27
American Viscose Corp
Gas-solid extrusion reactor

US3118739A
(en)

*

1959-01-20
1964-01-21
Du Pont
Polymer finisher apparatus

US3377139A
(en)

*

1963-06-21
1968-04-09
Allied Chem
Apparatus for preparing low density urea-formaldehyde foams

US3343922A
(en)

*

1963-09-23
1967-09-26
Vickers Zimmer Ag
Chemical reactor

1965

1965-06-01
US
US460174A
patent/US3440019A/en
not_active
Expired – Lifetime

1966

1966-05-28
DE
DE1645630A
patent/DE1645630B2/en
active
Pending

1966-05-31
GB
GB24146/66A
patent/GB1114477A/en
not_active
Expired

1966-06-01
AT
AT517166A
patent/AT270230B/en
active

1966-06-01
NL
NL666607576A
patent/NL150819B/en
unknown

Also Published As

Publication number
Publication date

DE1645630A1
(en)

1971-02-11

NL150819B
(en)

1976-09-15

AT270230B
(en)

1969-04-25

DE1645630B2
(en)

1974-07-25

NL6607576A
(en)

1966-12-02

US3440019A
(en)

1969-04-22

Similar Documents

Publication
Publication Date
Title

GB1114477A
(en)

1968-05-22

Polycondensation reactor

US3263748A
(en)

1966-08-02

Conveyor heat exchanger

GB1239057A
(en)

1971-07-14

GB1208999A
(en)

1970-10-14

Apparatus for continuous treatment of viscous materials

GB1108626A
(en)

1968-04-03

Apparatus for continuous reactions

GB1432077A
(en)

1976-04-14

Autoclave

GB1089397A
(en)

1967-11-01

Apparatus comprising a stirred vessel for conducting processes

GB1524471A
(en)

1978-09-13

Method and apparatus for evaporating water from material

GB1055918A
(en)

1967-01-18

A method of polycondensing bis(2-hydroxyethyl)-terephthalate and apparatus for performing the same

GB1151908A
(en)

1969-05-14

Method and Apparatus for Cleaning Contaminated Gas.

ES314835A1
(en)

1966-04-01

Process of preparing aromatic polyamines by catalytic hydrogenation of aromatic polynitro compounds

GB1445856A
(en)

1976-08-11

Heat exchanger

GB988675A
(en)

1965-04-07

Improvements in or relating to vessels for processing fluent materials

GB1030678A
(en)

1966-05-25

Apparatus for the cooling or heating, by continuous air circulation, of granulated materials

GB1459122A
(en)

1976-12-22

Coating apparatus

ES426116A1
(en)

1976-11-16

Milling apparatus

GB1089994A
(en)

1967-11-08

Improvements in reaction vessels

ES469738A1
(en)

1979-01-01

Conditioning apparatus

US4075766A
(en)

1978-02-28

Apparatus for the treatment of divided solid material

GB1394098A
(en)

1975-05-14

Mixer

GB1182300A
(en)

1970-02-25

Heating-Element for Electric Cable Furnace for Heating a Flow of Gas or Liquid.

GB854371A
(en)

1960-11-16

Improvements in or relating to heat exchangers

DK157173B
(en)

1989-11-20

PROCEDURE AND APPARATUS FOR CONTINUOUS IMPLEMENTATION OF CHEMICAL OR PHYSICAL REACTIONS BETWEEN A FLOWING MEDIUM AND SOLIDS

GB1269600A
(en)

1972-04-06

Polymerization reactor

ES367710A1
(en)

1971-04-16

Improvements in the construction of devices for the policondensation of a prepolimero. (Machine-translation by Google Translate, not legally binding)

Download PDF in English

None