GB2355674A - High-pressure multi-cell reactor - Google Patents
High-pressure multi-cell reactor Download PDFInfo
- Publication number
- GB2355674A GB2355674A GB9925046A GB9925046A GB2355674A GB 2355674 A GB2355674 A GB 2355674A GB 9925046 A GB9925046 A GB 9925046A GB 9925046 A GB9925046 A GB 9925046A GB 2355674 A GB2355674 A GB 2355674A
- Authority
- GB
- United Kingdom
- Prior art keywords
- cell
- vessels
- reactor
- upper plate
- pressure
- 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.)
- Granted
Links
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000011022 operating instruction Methods 0.000 claims description 3
- 238000007654 immersion Methods 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 claims 1
- 239000011521 glass Substances 0.000 claims 1
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 230000037431 insertion Effects 0.000 claims 1
- 238000003780 insertion Methods 0.000 claims 1
- 239000004810 polytetrafluoroethylene Substances 0.000 claims 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims 1
- 239000000523 sample Substances 0.000 claims 1
- 238000005070 sampling Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- 238000012360 testing method Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 3
- 239000012530 fluid Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000000429 assembly Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000013102 re-test Methods 0.000 description 1
- 230000003252 repetitive effect Effects 0.000 description 1
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
- B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
- B01J3/03—Pressure vessels, or vacuum vessels, having closure members or seals specially adapted therefor
-
- 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
- B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
- B01J3/002—Component parts of these vessels not mentioned in B01J3/004, B01J3/006, B01J3/02 - B01J3/08; Measures taken in conjunction with the process to be carried out, e.g. safety measures
-
- 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
- B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
- B01J3/04—Pressure vessels, e.g. autoclaves
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
A multi-cell reactor for parallel reactions comprises an annular array of reactor vessels mounted into a carousel having upper and lower plates. The upper plate seals to each vessel by an O-ring and is held in place, when sealed, by a rotary ring having keyhole slots which engage, on rotation, with undercut portions at the top of an annular array of retaining posts. The upper plate has a high-pressure gas connection to each cell, fed from a common manifold. Jacking posts having threaded upper ends are used, in conjunction with wing nuts, to press the upper plate initially against the vessels, before the locking plate is rotated, the wing nuts being thereafter released. The locking plate and pressure supply are mechanically interlocked to prevent wrong operation. The reactor is of a sized to fit on a conventional laboratory magnetic stirrer.
Description
2355674 Hi%!h Pressure Multi - Cell Reactor
Description Drawiniz No. A3.SO0049
Many researchers and chemists require to carry out parallel reactions on a new material or product. Frequently this involves pressurisation of a small (typlicallv 5 to 50ml of fluid) sample with a variety of gases and stirring of the liquid.
In the past this work has been carried out in high pressure reactors where a single sample has been placed in an autoclave and sealed prior to being reacted. Frequently the vessel would require the use of special tools or spanners and the use of leak detection fluids to ensure the vessel is satisfactorily sealed. Parallel reactions were carried out in other reactors or remat tests were made in the same reactor. In addition to the time factor involved with repetitive testing, this procedure introduced the difficulty of always accurately reproducing the same test conditions.
The new Multi-cell reactor overcomes these problems by incorporating a number of vessels (typically 10 but may be more), and testing samples in these simultaneously under identical temperature and pressure conditions.
The cells or vessels are set into a fixed carousel comprising an upper and lower plate. All vessels are attached to the lower plate, and all covers are attached to the upper plate. (As shown in drawing).
A single manifold is provided on top of the assembly with a distribution pipe to each cover vessel. The manifold also has a aas inlet valve, gas outlet valve, pressure gauge and a pressure relief valve, all as shown in section A - A of the drawing.
Attached to the lower plate is a series of retaining posts each with a shoulder near to the top. The upper plate has corresponding holes for the posts to pass through. On top of the upper plate is a locking ring, which has a series of keyhole slots arranged to align with the retaining posts. The shouldered part of the posts will just pass through the larger portion of the keyhole slots, and when in position the ring is rotated thereby locating the smaller part of the keyhole under the shoulder and preventing removal of the retaining post. With the locking ring in the locked position the posts secure the upper and lower plates and therefore the covers, containing the pressure inside the vessels. The locking ring is operated by means of an Operating arm as shown in section C-C of the drawing.
To prevent accidental unlocking of the unit when charged with pressure a mechanical interlock is provided between the locking valve, connected to the manifold, and an operating arm fixed to the locking ring (see section C-C of the drawing). The handle on the locking valve and the operating arm interface in such a way that:- a) With the locking valve in the 'vent' or open position, the unit can be locked or unlocked. b) With the locking valve in the 'closed' position, the unit remains in the locked or operating position. c) When the operating lever is in the open position the cells cannot be pressurised.
U the vessel / cover Joints are sealed by an '0' ring in a piston / cylinder arrangement see -,ection A-A of the drawing. This closure requires only an active (closing) force to bring the two parts together. The closing (and removing) force is sufficiently low to be applied by intep i - nuts. (See section C-C of the drawini I I ral wing g, and the operating instructions) The unit is designed for low viscosity media where aggressive stirring is not essential.
The u it is desi I I I I ru 1 gned to fit on a commercially available sing e position hot plate / stirrer with a small spin bar in each vessel.
High Pressure Multi - Cell Reactor Operating Instructions See Drawinz A3. S00050 The multi - cell reactor consists of two sub-assemblies, the top 'half consisting of principally the upper plate., locking ring, manifold, distribution tubes, covers, wing nuts and interlock valve.
The lower'half includes the lower plate, vessels, retaining posts andjacking posts.
1. To complete the assembly of the unit, the top 'half is aligned above the lower half as shown on the drawine so that the wina nuts are aliened vertically above the Jacking posts. The top 'half is then lowered carefully onto the lower 'half so that the covers fit into the respective vessels, and the retaining posts pass through the respective holes in the upper plate and locking ring. (The top 'half may be rotated horizontally through 180' before locating with the lower 'half, i.e. either wing nut can be aligned with either jacking post).
2. With the top 'half sitting loosely on the lower 'half, the wing nuts are turned clockwise (finger-tight) to engage the Jacking: posts. This action simultaneously locates the covers in the respective vessels and the '0' rings in position. (Total time up to this point is about 15 seconds).
At this stage both the locking valve and the locking ring are in the open or vent positions.
4. The operating arm is then rotated clockwise to the stop position causing the locking ring, to engage the retaininLy posts. To transfer the full load onto the retaining posts the wing nuts are turned anticlockwise to take up the slack. Finally the locking valve is rotated clockwise to the stop or locked position. The multi-cell is now ready for charging, pressurising and heating.
5. Heating / cooling may be by partial immersion in a liquid bath, or by electrical band heaters on individual vessels.
6. On completion of the reaction, the pressure is removed through the gas outlet valve and the unit cooled if necessary. The reactor can then be opened.
7. This is done by 1) turning the locking valve anti-clockv4'se to the open position ii) moving the operating arm to the open position iii) removing the wing nuts by turning them anti-clockwise iv) lifting the top 'half free of the lower 'half.
8. The samples may then be removed from the unit, and the unit cleaned, if necessary, before reloading and re-testing.
3 r High Pressure Multi - Cell Reactor
Claims (8)
1. The Baskerville High Pressure Multi - Cell Reactor incorporates a number of vessels (up to 10 or more) into a single unit with simultaneously rapid closure (approximately 15 seconds) of all the vessels without the use of spanners or tools. See operating instructions.
2. The multi - cell reactor is designed to operate at above ambient temperature and pressure. Heating can be ap lied by immersion in a water or oil bath. or p I - I alternatively by electrical band heaters on individual vessels.
The footprint is sufficiently small that 10 vessels (of 20 mm bore and 95mm deep) will sit on a single position magnetic stirrer typically of 140mm. diameter.
4. Each cell designed to take removable glass or PTFE liners.
5. Common gas supply line allows for a single gas inlet connection.
6. Alternative smaller cell sizes can be retro-fitted.
7. Options are available for cell sampling or catalyst injection at low pressure.
8. Options are available for insertion of a temp, probe into each cell.
4
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB9925046A GB2355674B (en) | 1999-10-25 | 1999-10-25 | High pressure multi-cell reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB9925046A GB2355674B (en) | 1999-10-25 | 1999-10-25 | High pressure multi-cell reactor |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| GB9925046D0 GB9925046D0 (en) | 1999-12-22 |
| GB2355674A true GB2355674A (en) | 2001-05-02 |
| GB2355674B GB2355674B (en) | 2003-09-17 |
Family
ID=10863214
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB9925046A Expired - Fee Related GB2355674B (en) | 1999-10-25 | 1999-10-25 | High pressure multi-cell reactor |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB2355674B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6767514B2 (en) * | 2001-03-05 | 2004-07-27 | Baskerville Reactors And Autoclaves Limited | Test apparatus |
| WO2022184909A1 (en) | 2021-03-04 | 2022-09-09 | Hte Gmbh The High Throughput Experimentation Company | Apparatus for analyzing reaction systems |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3356346A (en) * | 1966-01-03 | 1967-12-05 | Landsberger Kurt | Test tube stirring support |
| US4183897A (en) * | 1970-02-23 | 1980-01-15 | Costruzioni Meccaniche G. Mazzoni S.P.A. | Apparatus for admixing liquid and gaseous chemical reactants with uniform pressure in a plurality of reaction tubes |
| GB2142826A (en) * | 1983-05-06 | 1985-01-30 | Boc Group Plc | Autoclaves |
| DE19543401A1 (en) * | 1995-11-21 | 1997-05-22 | Mikrowellen Systeme Mws Gmbh | Microwave heating with several test vessel stations turning on rotor |
| WO1998020965A1 (en) * | 1996-11-13 | 1998-05-22 | Doebelin Werner | Reaction chamber system for chemical synthesis or related applications |
| WO1998057181A1 (en) * | 1997-06-10 | 1998-12-17 | Pharmacopeia, Inc. | Methods and apparatus for universal fluid exchange |
-
1999
- 1999-10-25 GB GB9925046A patent/GB2355674B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3356346A (en) * | 1966-01-03 | 1967-12-05 | Landsberger Kurt | Test tube stirring support |
| US4183897A (en) * | 1970-02-23 | 1980-01-15 | Costruzioni Meccaniche G. Mazzoni S.P.A. | Apparatus for admixing liquid and gaseous chemical reactants with uniform pressure in a plurality of reaction tubes |
| GB2142826A (en) * | 1983-05-06 | 1985-01-30 | Boc Group Plc | Autoclaves |
| DE19543401A1 (en) * | 1995-11-21 | 1997-05-22 | Mikrowellen Systeme Mws Gmbh | Microwave heating with several test vessel stations turning on rotor |
| WO1998020965A1 (en) * | 1996-11-13 | 1998-05-22 | Doebelin Werner | Reaction chamber system for chemical synthesis or related applications |
| WO1998057181A1 (en) * | 1997-06-10 | 1998-12-17 | Pharmacopeia, Inc. | Methods and apparatus for universal fluid exchange |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6767514B2 (en) * | 2001-03-05 | 2004-07-27 | Baskerville Reactors And Autoclaves Limited | Test apparatus |
| WO2022184909A1 (en) | 2021-03-04 | 2022-09-09 | Hte Gmbh The High Throughput Experimentation Company | Apparatus for analyzing reaction systems |
Also Published As
| Publication number | Publication date |
|---|---|
| GB2355674B (en) | 2003-09-17 |
| GB9925046D0 (en) | 1999-12-22 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 20161025 |