GB2215714A - Tubular reactor for the high-temperature decomposition of bauxite - Google Patents

Tubular reactor for the high-temperature decomposition of bauxite Download PDF

Info

Publication number
GB2215714A
GB2215714A GB8821233A GB8821233A GB2215714A GB 2215714 A GB2215714 A GB 2215714A GB 8821233 A GB8821233 A GB 8821233A GB 8821233 A GB8821233 A GB 8821233A GB 2215714 A GB2215714 A GB 2215714A
Authority
GB
United Kingdom
Prior art keywords
tubular reactor
tube
expansion joint
reactor
inner tube
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.)
Withdrawn
Application number
GB8821233A
Other versions
GB8821233D0 (en
Inventor
Ipl-Ing Hans-Georg Kaltenberg
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.)
Vereinigte Aluminium Werke AG
Original Assignee
Vereinigte Aluminium Werke 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.)
Filing date
Publication date
Application filed by Vereinigte Aluminium Werke AG filed Critical Vereinigte Aluminium Werke AG
Publication of GB8821233D0 publication Critical patent/GB8821233D0/en
Publication of GB2215714A publication Critical patent/GB2215714A/en
Withdrawn legal-status Critical Current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
    • B01J19/0053Details of the reactor
    • B01J19/0073Sealings
    • 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
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/2415Tubular reactors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16LPIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
    • F16L59/00Thermal insulation in general
    • F16L59/14Arrangements for the insulation of pipes or pipe systems
    • F16L59/16Arrangements specially adapted to local requirements at flanges, junctions, valves or the like
    • F16L59/21Arrangements specially adapted to local requirements at flanges, junctions, valves or the like adapted for expansion-compensation devices
    • 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
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00074Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00094Jackets

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

A tubular reactor for high temperature decomposition of beauxite containing bohmite and diaspore comprises a decomposition portion a sojourn portion with a jacket tube 1 and a separate inner tube 2 in which the tubes are fixed to each other at one end by connected to each other at the other end in a way 3 which permits relative movement, and a cooling portion. <IMAGE>

Description

TUBULAR REACTOR FOR THE HIGH-TEMPERATURE DECOMPOSITION OF BAUXITE CONTAINING BOHMITE AND DIASPORE The invention relates to a tubular reactor, particularly for the high-temperature decomposition of bauxite containing bohmite and diaspore, with a decomposition portion, a sojourn portion and a cooling portion.
A tubular reactor of this kind is known from the Germany patent specification DE-AS 19 37 392 (VAW). This reactor can be used for decomposing all minerals and ores of the kind which contain components soluble in certain reagents, particularly bauxite in aqueous sodium hydroxide.
In the operation of reactors of this kind there is a tendency for incrustations to build up on the inner walls of the tubes, which interfere with the reaction by forming a rough surface. This reduces the effective internal cross-sectional area of the tube, increasing the velocity of flow of the suspension. In extreme cases the flow cross-section is reduced so greatly that further economic operation of the process becomes impossible.
The intention in the present invention is to improve a tubular reactor of this kind, particularly for decomposing bauxite containing bohmite and diaspore, in such a way that the process can be operated reliably even when there is a strong tendency for incrustations to form, and at temperatures between 200 and 3000C.
The problem is solved, according to the invention, by the characteristics in the claims. The reactor of the invention comprises, in its sojourn portion, a jacket tube 1 containing a separate inner tube 2, the two tubes being welded together at one end but connected to each other in a mobile manner at the other end.
Although the reactor is primarily intended for decomposing, at high temperatures, bauxite containing bohmite and diaspore, it can also be used, in principle, for decomposing other wet, acid, alkaline or neutral minerals or ores of the kind which contain components which are soluble in appropriate reagents.
The invention will now be described in greater detail with the help of an example. Figure 1 shows a portion of the sojourn region of the reactor. Figure 2 shows, drawn to a larger scale, a longitudinal section of the downstream end of this portion of the reactor.
In Figure 1 a section of tube A in the sojourn region of the reactor tends to acquire an incrustation. The section A is connected at each end to connections B and C by flanges 6 and 7 and comprises an outer jacket-tube I containing a separate inner tube 2. At its downstream end the inner tube 2 has an expansion joint 3 which makes contact with the connection B. At their upstream ends both the outer 1 and inner 2 tubes are welded to a V-flange.
For maintenance operations the section A can quickly be separated from the two flanges 6 and 7 and replaced by a new section A. The old section A is freed from incrustations as follows. The inner tube 2 is extracted from the jacket-tube l and replaced by a new inner tube 2. The old jacket-tube 1 is then ready for use once more.
Figure 2 shows the downstream end of the inner tube 2 with its expansion joint 3. This is a corrugated bellows structure with a total conjugation height H of 20 to 25 mm and a constriction height d of 15 mm projecting inwards of the inner wall of the inner tube 2. The expansion joint 3 is welded to the downstream end of the inner tube 2 at 9 and welded to the jacket tube 1 at 8.
It will be observed that by this invention the inner tube 2 carries the incrustations. The expansion joint 3 allows the inner tube 2 to expand relative to the jacket-tube 1 even up to quite high temperatures. To give the expansion joint 3 the longest possible operational life between overhauls the build-up of incrustations on its inner surface must be restrained. This is best done by ensuring that the bellows projects exactly the right distance inwards into the interior of the inner tube 2. Correct dimensioning of the expansion-joint bellows, as specified in the present invention.
ensures optimal functioning of the reactor.

Claims (7)

1. A tubular reactor, particularly for decomposing, at high temperatures, bauxite containing bohmite and diaspore, the reactor having a decomposition portion, a sojourn portion and a cooling portion, characterised in that the sojourn portion comprises a jacket-tube (1) containing a separate inner tube (2), the two tubes being fixed to each other at one end but mobile, relative to each other, at the other end.
2. A tubular reactor as claimed in Claim 1, characterised in that the gap between the tubes is 0.01 to 0.02 D wide, where D is the outer diameter of the jacket tube.
3. A tubular reactor as claimed in one of the above claims, characterised in that mobility between the outer and inner tubes is provided by an expansion joint (3) situated at the downstream ends of the tubes (1,2).
4. A tubular reactor as claimed in one of the above claims, characterised in that the expansion joint (3) is a corrugated bellows whose corrugation height (H) is 3 to 5% of the nominal diameter of the tubular reactor.
5. A tubular reactor as claimed in one of the above claims, characterised in that the expansion joint (3) projects inwards into the interior of the inner tube (2) by 2 to 10who of the nominal diameter.
6. A tubular reactor as claimed in one of the above claims, characterised in that in the sojourn region the reactor consists of several tubular sections connected together by flanges, the inner tube (2) of each section being connected at its downstream end in a mobile manner to the flange by an expansion joint (3), whereas at its upstream end the inner tube (2) is connected to the flange by a weld seam.
7. A tubular reactor as claimed in one of the above claims, characterised in that the length of the expansion joint (3) is between 0.5 and 1% of the length of the section of tube.
GB8821233A 1988-03-18 1988-09-09 Tubular reactor for the high-temperature decomposition of bauxite Withdrawn GB2215714A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE8803700U DE8803700U1 (en) 1988-03-18 1988-03-18

Publications (2)

Publication Number Publication Date
GB8821233D0 GB8821233D0 (en) 1988-10-12
GB2215714A true GB2215714A (en) 1989-09-27

Family

ID=6822029

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8821233A Withdrawn GB2215714A (en) 1988-03-18 1988-09-09 Tubular reactor for the high-temperature decomposition of bauxite

Country Status (12)

Country Link
JP (1) JPH01139829U (en)
AU (1) AU606431B2 (en)
DE (1) DE8803700U1 (en)
FR (1) FR2628755B3 (en)
GB (1) GB2215714A (en)
GR (1) GR880100420A (en)
HU (1) HU199709B (en)
IT (1) IT215002Z2 (en)
NL (1) NL8801660A (en)
PL (1) PL273532A1 (en)
RO (1) RO104156B1 (en)
SU (1) SU1708143A3 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001022017A1 (en) * 1999-09-23 2001-03-29 Outokumpu Oyj Apparatus for clearing dust accretions in connection with a smelting furnace

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB876597A (en) * 1954-02-17 1961-09-06 Dorr Oliver Inc Calcination of alumina
DE1937392A1 (en) * 1969-07-23 1972-03-02 Vaw Ver Aluminium Werke Ag Process for the wet digestion of minerals, ores or other substances
GB2127709A (en) * 1982-10-06 1984-04-18 Univ Edinburgh Manufacture of aluminium nitride

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1814796A (en) * 1930-04-23 1931-07-14 Dow Chemical Co Autoclave
US3018170A (en) * 1959-07-13 1962-01-23 Soloducha Nicolas Pressure leaching apparatus
US3744946A (en) * 1971-10-15 1973-07-10 Nat Standard Co Apparatus for fabricating continuous elongated components
DE3602603A1 (en) * 1986-01-29 1987-07-30 Franz Dr Ing Maly Self-compensating district-heating pipe with connecting element, designed as steel-jacket composite pipe
FR2632973B1 (en) * 1988-06-21 1993-01-15 Michelin & Cie METHODS AND DEVICES FOR OBTAINING A HOMOGENEOUS AUSTENITY STRUCTURE

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB876597A (en) * 1954-02-17 1961-09-06 Dorr Oliver Inc Calcination of alumina
DE1937392A1 (en) * 1969-07-23 1972-03-02 Vaw Ver Aluminium Werke Ag Process for the wet digestion of minerals, ores or other substances
GB2127709A (en) * 1982-10-06 1984-04-18 Univ Edinburgh Manufacture of aluminium nitride

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001022017A1 (en) * 1999-09-23 2001-03-29 Outokumpu Oyj Apparatus for clearing dust accretions in connection with a smelting furnace
US6689309B1 (en) 1999-09-23 2004-02-10 Outokumpu Oyj Apparatus for clearing dust accretions in connection with a smelting furnace

Also Published As

Publication number Publication date
AU606431B2 (en) 1991-02-07
JPH01139829U (en) 1989-09-25
SU1708143A3 (en) 1992-01-23
DE8803700U1 (en) 1989-07-13
FR2628755B3 (en) 1990-03-09
IT8853285V0 (en) 1988-07-08
GB8821233D0 (en) 1988-10-12
HUT49505A (en) 1989-10-30
NL8801660A (en) 1989-10-16
FR2628755A3 (en) 1989-09-22
IT215002Z2 (en) 1990-07-30
HU199709B (en) 1990-03-28
GR880100420A (en) 1990-01-19
RO104156B1 (en) 1993-12-15
PL273532A1 (en) 1989-10-02
AU1897388A (en) 1989-01-19

Similar Documents

Publication Publication Date Title
US4202672A (en) Apparatus for gasification of finely divided fuel
US4377894A (en) Method of lining inner wall surfaces of hollow articles
US5101892A (en) Heat exchanger
ES2079907T3 (en) A PROCEDURE AND A DEVICE FOR MANUFACTURING COMPOSITE TUBES WITH TUBULAR SLEEVE IN CONTINUOUS REGIME.
EP0506343A2 (en) Cyclone separator roof
EP0148453A2 (en) Flexible stabilizer for degraded heat exchanger tubing
GB2215714A (en) Tubular reactor for the high-temperature decomposition of bauxite
GB2150041A (en) Double pipe exothermic reactor
CA1177863A (en) Flange coupling
CN110345464A (en) A kind of nuclear power station steam generator flexible tubesheet structure
DE3560925D1 (en) Vertical tube heat exchange panel for recovery boilers, such as black liquor boilers or town refuse incinerators, and manufacturing processes
KR850004799A (en) Corrosion resistant steam generator
US5399321A (en) Tubular pressurized catalytic hydrocarbon converter
BR0308336A (en) Process for catalytic vapor phase oxidation
JPH03234314A (en) Manufacture of double tube
DE60000548D1 (en) corrugated pipe
CN215215107U (en) High-precision threaded stainless steel seamless steel tube
CN219194533U (en) Feeding structure of fluidized bed for producing fumed silica
CN218992742U (en) Composite external pressure compensator
CN218936395U (en) Novel cooling device for carbon black smoke
CN216692657U (en) Expansion device for nitric acid economizer
KR910008896B1 (en) Heat exchanger
SU1310067A1 (en) Mandrel for bending tubes
CN214842712U (en) Multi-point support spiral finned tube
CN220119917U (en) Stuffing box type double-tube-plate heat exchanger

Legal Events

Date Code Title Description
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)