AU646906B2 - Formation of densified material - Google Patents
Formation of densified materialInfo
- Publication number
- AU646906B2 AU646906B2 AU88495/91A AU8849591A AU646906B2 AU 646906 B2 AU646906 B2 AU 646906B2 AU 88495/91 A AU88495/91 A AU 88495/91A AU 8849591 A AU8849591 A AU 8849591A AU 646906 B2 AU646906 B2 AU 646906B2
- Authority
- AU
- Australia
- Prior art keywords
- furnace
- column
- canister
- processing elements
- spacer
- 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.)
- Ceased
Links
- 239000000463 material Substances 0.000 title claims description 8
- 230000015572 biosynthetic process Effects 0.000 title description 4
- 125000006850 spacer group Chemical group 0.000 claims description 35
- 238000000034 method Methods 0.000 claims description 29
- 238000007906 compression Methods 0.000 claims description 10
- 230000006835 compression Effects 0.000 claims description 9
- 239000007787 solid Substances 0.000 claims description 8
- 230000003213 activating effect Effects 0.000 claims description 2
- 230000004323 axial length Effects 0.000 claims description 2
- 238000006467 substitution reaction Methods 0.000 claims description 2
- 239000011236 particulate material Substances 0.000 claims 1
- 239000002775 capsule Substances 0.000 description 22
- 238000000280 densification Methods 0.000 description 8
- 239000011435 rock Substances 0.000 description 5
- 239000002927 high level radioactive waste Substances 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000007731 hot pressing Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 230000002285 radioactive effect Effects 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Catalysts (AREA)
Description
FORMATION OF DENSIFIED MATERIAL
The present invention relates to the formation of densified material and more particularly is concerned with producing blocks of densified material formed from particulate solid material. The invention will be exemplified with particular reference to the problem of a system for providing a synthetic rock structure in which high level radioactive waste is to be immobilised in a manner suitable for safe long term storage. The present applicants through their prior published patent specifications have disclosed systems for immobilising high level radioactive waste. Synthetic rock precursor material is impregnated with liquid high level radioactive waste, and a pourable granulated solid " is formed. This solid is then poured into a suitable container which, after closure, can undergo a pressure process at elevated temperature in order to produce a uniform densified block of synthetic rock which has extraordinarily high leach resistance. Such processes must be conducted in active cells which are very expensive to build and the process must be operated with remote manipulators. Commercial factors dictate that the process must be capable of being operated for a large number of years with just simple maintenance by remote manipulators. Exceedingly high reliability is required. Thus there has been a longstanding need to conceive of and develop elegant engineering solutions aimed at providing the highest possible through-put of processed material in the smallest volume of active cell space.
The present invention is directed to providing new and useful alternatives to previous proposals. It will be appreciated that although the invention has particular application to processing nuclear waste into synthetic rock form, the process arrangements may be equally valuable for other purposes such as the formation of sophisticated ceramic materials of non-radioactive
character. For machining into components of different types, there is a need to be able to produce efficiently cylindrical blocks of ceramic and embodiments of the invention can be useful in this field. According to a first aspect of the present invention, there is provided a method of forming a densified block of material from a particulate solid, the method comprising (a) arranging a vertically extending tubular furnace with open ends for providing an entry and a discharge for processing elements to be passed in a stream through the furnace, the processing elements comprising canisters and spacer elements, pressure means being provided to be - selectively operable to exert a compressive force only along the axis of the furnace and onto the stream of processing elements, (b) supplying the particulate solid in the canisters, each canister being of generally cylindrical form and a clearance fit in the furnace, each canister having axial end walls and a bellows-like convoluted side wall extending between the end walls, each canister being formed to retain the solid and to compress axially with no substantial radial expansion in the process, (c) supplying spacer elements to co-operate with the supplying of canisters whereby the stream is formed as a vertical column extending through the furnace, each spacer element being a rigid, refractory, cylindrical element dimensioned to move along the tubular furnace during the process and having end walls each shaped to engage with an axial end wall of a canister for controlling the location of the canister so as to be spaced from the wall of the furnace and for controlling uniaxial compression of the canisters, (d) operating the pressure means to compress the column and after sufficient residual time to displace a processing element through the discharge end of the furnace, (e) removing the applied pressure from time to time and either or both (i) removing a processing element from the discharge end and (ii) inserting a new processing element at the entry end of the furnace, and (f)
activating holding means to support the column of processing elements to enable substitution of the lowermost processing element in the column.
The invention in another aspect extends to an 5 apparatus for practising the above described method and also to product resulting from use of the method or apparatus.
In one apparatus aspect of the invention, there is provided a tubular furnace for semi-continuous operation
10 and arranged to be mounted vertically when in use and having ends providing an inlet and a discharge for cylindrical processing elements which are to be subject to uniaxial pressure along the axis of the furnace while being maintained at elevated temperature, the apparatus
15. comprising selectively operable pressure means for exerting uniaxial pressure on a column of processing elements located in and extending through the furnace and holding means for holding the column of processing elements in the furnace while the pressure means is 0 deactivated and a further processing element below the column may be manipulated with respect to the column. Where the apparatus is adapted for upward advance of processing elements, a new element is inserted when the holding means is activated. 5 Embodiments of the invention can operate with the processing elements being moved downwardly from an upper inward end to a lower discharge end or, more preferably, in the opposite upward direction.
In one embodiment, the processing elements in the 0 column comprise an alternating stream of spacer elements and canisters. However, depending upon the particular shape and dimensions of the apparatus and the canisters, it may be possible for the spacers to be inserted only periodically in the column and two or more adjacent 5 canisters might be useable.
A preferred embodiment is one which the spacer elements have ends which have a flat central region surrounded by an annular collar whereby each canister is
centralised. Preferably the canister has a curved junction between each flat end wall and the convolutions in the side wall and the spacer has a corresponding curve in the junction between the annular collar and the flat central region.
The spacer elements preferably are cylindrical and have an axial length in a preferred embodiment of the same order of magnitude as the diameter. The spacer elements can be a sliding fit or a close clearance fit within the tabular furnace.
In a typical embodiment, the tubular furnace will have a diameter in the range of 100 to 200mm.
Preferably, the pressure means comprises hydraulic rams arranged above and below the furnace and adapte ' to co-operate to maintain equal forces on the column. Advantageously, the apparatus includes sensing means such that any difference in the forces applied is indicative of one or more of the processing elements jamming in the furnace tube and rectification action is then required. The holding means is preferably a simple mechanical clamp and the apparatus preferably has an automatic control system to co-ordinate all operations and to provide controlled progressive displacement of the processing elements through the tubular furnace. An embodiment of the invention will now be described with reference to the accompanying drawings, of which:-
Figure 1 is a schematic part-sectional vertical elevation of an embodiment of the invention when operating; Figure 2 is a sectional view on an enlarged scale of the discharge upper end of the apparatus; and
Figure 3 is a similar sectional view on an enlarged scale of the lower feed end of the apparatus.
Referring to the drawings, Figure 1 depicts a continuous hot pressing apparatus 1 comprising a furnace 2 with a lower feed end 3 and an upper discharge end 4. Capsules 10 and spacers 11 enter the furnace at the feed end 3 and exit the furnace at discharge end 4. The
furnace comprises a densification tube 5 aligned with an upper hydraulic ram 12 and a lower hydraulic ram 13.
Figures 2 and 3 show the capsules 10 and spacers 11 in more detail. Each capsule comprises axial end walls 20 and a bellows-like convoluted side wall 21. The spacers have ends which have a flat central region 24 surrounded by an annular collar 25. Each capsule has a curved junction 26 between each axial end wall 20 and convoluted side wall 21, each spacer has a corresponding curve 27 in the junction between the flat central region 24 and the annular collar 25.
Figure 3 also shows the densification tube 5 in greater detail. A guide tube 23 is attached to the lower end of the densification tube 5, and a column clamp 22 extends through the wall of guide tube 23.
The continuous hot pressing apparatus l of Figure 1 further comprises a control panel 35 for remote operation of the system.
The upper ram 12 is connected through a load cell 41 to a variable speed drive 40. Temperature in the upper ram is regulated by the flow of cooling water 42. Similarly, temperature in the lower ram 13 is regulated by the flow of cooling water 34. The lower ram is driven by hydraulic power unit 32, pressure generated by the hydraulic unit being monitored by pressure gauge 31. A slide 33 braces the lower ram 13 preventing any lateral movement in the lower ram.
In operation, densification tube 5 is filled with an alternate arrangement of capsules and spacers. An uncompressed capsule 10 is fed in at the feed end 3 and a densified capsule 14 is removed after compression from the discharge end 4.
At the end of a compression cycle, the lowermost spacer in the densification tube is clamped. The upper ram is then retracted and a spacer and densified capsule are removed from the discharge end. The upper ram is then lowered to contact the next uppermost capsule. The lower ram is retracted and a further spacer and capsule
are loaded thereon. It is necessary that a spacer is loaded between the capsule and upper surface of the lower ram because the lowermost element to be subsequently clamped in the densification tube should be a spacer in this preferred embodiment.
The hydraulic power unit 32 is then activated, and the lower ram is driven upwardly until the capsule thereon contacts the lowermost clamped spacer. The column clamp 22 is then released and the lower ram is driven upwardly and, as the compression process proceeds, the lower ram gradually moves partially into the guide tube (as depicted in Figure 3) while the upper ram is retracting. The pressure between the upper and lower ram is equalized and maintained at a pre-specified pressure. The control system operates gradually to raise the upper ram so that the stream of capsules and spacers moves gradually to an end portion at the end of the cycle in
' which the uppermost capsule and spacer are above the tube
5. The lowermost spacer is then clamped, and the upper ram is retracted, sufficiently such that the uppermost densified capsule and spacer element can be removed from the discharge end. The upper ram is then extended downwardly by the variable speed drive 40 until it contacts the uppermost capsule. The lower ram is retracted and re-loaded with a spacer and capsule. The process cycle is then repeated.
The construction of each spacer and capsule is such that during compression any radial expansion of the capsule is minimised by virtue of the annular collar 25 in the spacer which centres the capsule by interacting with curved junction 26 in the capsule. This construction prevents the capsule from bellowing outwards during compression thereby blocking the densification tube.
The speed and throughput of compression is controlled by the hydraulic pressure employed and the speed of retraction of the upper ram. The speed of retraction of
the upper ram is in turn controlled by the variable speed drive. The load cell monitors the pressure in the upper ram and the process is operated such that the pressure in the upper ram and lower ram are substantially equal. Any large differential in pressure between the upper and lower rams (for example where there is significantly larger pressure in the lower ram) indicates that there has been a blockage or jamming in the compression column. The furnace is operated at elevated temperatures, the temperature being pre-determined by the degree of densification required (eg for the compression of synthetic rock) . The furnace temperature is controlled to be hottest towards the centre of the column, so that less costly heat resistant steels can be used in the upper and lower rams. Accordingly the upper and lower rams are cooled by a suitable cooling medium, a water circuit in this case.
The process can be completely automated and operated continuously.
Claims (16)
1. A method of forming a densified block of material from a particulate solid, the method comprising (a) arranging a vertically extending tubular furnace with open ends for providing an entry and a discharge for processing elements to be passed in a stream through the furnace, the processing elements comprising canisters and spacer elements, pressure means being provided to be selectively operable to exert a compressive force only along the axis of the furnace and onto the stream of processing elements, (b) supplying the particulate solid in the canisters, each canister being of generally cylindrical form and a clearance fit in the furnace, each canister having axial end walls' and a bellows-like convoluted side wall extending between the end walls, each canister being formed to retain the solid and to compress axially with no substantial radial expansion in
•the process, (c) supplying spacer elements to co-operate with the supplying of canisters whereby the stream is formed as a vertical column extending through the furnace, each spacer element being a rigid, refractory, cylindrical element dimensioned to move along the tubular furnace during the process and having end walls each shaped to engage with an axial end wall of a canister for controlling the location of the canister so as to be spaced from the wall of the furnace and for controlling uniaxial compression of the canisters, (d) operating the pressure means to compress the column and after sufficient residual time to displace a processing element " through the discharge end of the furnace, (e) removing the applied pressure from time to time and either or both (i) removing a processing element from the discharge end and (ii) inserting a new processing element at the entry end of the furnace, and (f) activating holding means to support the column of processing elements to enable substitution of the lowermost processing element in the column.
2. A method as claimed in claim 1 wherein the processing elements are moved upwardly.
3. A method as claimed in claim 1 or claim 2 wherein the processing elements in the column comprise an alternating stream of spacer elements and canisters.
4. A method as claimed in any one of the preceding claims wherein each canister is of generally cylindrical form, has axial end walls and a bellows-like convoluted side wall extending between the end walls.
5. A method as claimed in any one of the preceding claims, and wherein the spacer elements have ends which have a flat central region surrounded by an annular collar whereby each canister is centralised.
6. A method as claimed in any one of the preceding Claims in which each canister has a curved junction between each axial end wall and a convoluted side wall.
7. A method as claimed in claim 6 in which each spacer element has a corresponding curve in the junction between the annular collar and the flat central region.
8. A method as claimed in any one of the preceding claims in which each spacer element has an axial length of the same order of magnitude as its diameter.
9. A method as claimed in any one of the preceding claims wherein the spacer elements are a sliding fit or a close clearance fit within the furnace tube.
10. A method as claimed in any one of the preceding claims wherein the furnace is tubular and has a diameter in the range of 100 to 200 mm.
11. A method as claimed in any one of the preceding claims wherein the pressure means comprises hydraulic rams arranged above and below the furnace and are operated to co-operate to maintain equal forces on the column.
12. A method as claimed in claim 11 and including using sensing means to monitor any difference in the forces applied to the respective rams for indicating if one or more of the processing elements is jamming in the furnace.
13. Apparatus for densifying particulate material in canisters adapted to be uniaxially compressed without substantial radial expansion, the apparatus comprising a tubular furnace for semi-continuous operation and arranged to be mounted vertically when in use and having ends providing an inlet and a discharge for cylindrical processing elements which are to be subject to uniaxial pressure along the axis of the furnace while being maintained at elevated temperature, the apparatus comprising selectively operable pressure means for exerting uniaxial pressure on a column of processing elements located in and extending through the furnace and holding means for holding the column of processing elements in the furnace while the pressure means " is deactivated and a further processing element below the column may be manipulated with respect to the column.
14. Apparatus as claimed in claim 13 wherein the holding means is a mechanical clamp.
15. Apparatus as claimed in claim 13 or claim 14 including an automatic control system to co-ordinate all operations.
16. Apparatus substantially as herein described with reference to Figures 1 to 3 of the accompanying drawings.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU88495/91A AU646906B2 (en) | 1990-10-18 | 1991-10-18 | Formation of densified material |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AUPK285890 | 1990-10-18 | ||
| AUPK2858 | 1990-10-18 | ||
| AU88495/91A AU646906B2 (en) | 1990-10-18 | 1991-10-18 | Formation of densified material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| AU8849591A AU8849591A (en) | 1992-05-20 |
| AU646906B2 true AU646906B2 (en) | 1994-03-10 |
Family
ID=25641068
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU88495/91A Ceased AU646906B2 (en) | 1990-10-18 | 1991-10-18 | Formation of densified material |
Country Status (1)
| Country | Link |
|---|---|
| AU (1) | AU646906B2 (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0230732A1 (en) * | 1985-11-29 | 1987-08-05 | Australian Nuclear Science And Technology Organisation | Formation of ceramics |
| US4834917A (en) * | 1986-06-25 | 1989-05-30 | Australian Nuclear Science & Technology Organization | Encapsulation of waste materials |
| US4929394A (en) * | 1988-02-01 | 1990-05-29 | Kabushiki Kaisha Kobe Seiko Sho | Process for compacting radioactive metal wastes |
-
1991
- 1991-10-18 AU AU88495/91A patent/AU646906B2/en not_active Ceased
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0230732A1 (en) * | 1985-11-29 | 1987-08-05 | Australian Nuclear Science And Technology Organisation | Formation of ceramics |
| US4834917A (en) * | 1986-06-25 | 1989-05-30 | Australian Nuclear Science & Technology Organization | Encapsulation of waste materials |
| US4929394A (en) * | 1988-02-01 | 1990-05-29 | Kabushiki Kaisha Kobe Seiko Sho | Process for compacting radioactive metal wastes |
Also Published As
| Publication number | Publication date |
|---|---|
| AU8849591A (en) | 1992-05-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA1270073A (en) | Encapsulation of waste material | |
| US3555597A (en) | Apparatus for hot pressing refractory materials | |
| US2968551A (en) | Method of sintering compacts | |
| AU646906B2 (en) | Formation of densified material | |
| US5414208A (en) | Formation of densified material | |
| KR101576707B1 (en) | Compressive rod assembly for molten metal containment structure | |
| EP0230732B1 (en) | Formation of ceramics | |
| DE3886549T2 (en) | LOW TEMPERATURE. | |
| EP4392996A1 (en) | Remote sublimination apparatus | |
| EP0102246B1 (en) | Containment and densification of particulate material | |
| JP3839846B2 (en) | Vertical catalytic reactor | |
| CA2537659A1 (en) | Separation system, method and apparatus | |
| US3295844A (en) | Sintering furnace | |
| US5205980A (en) | Sublimer assembly | |
| CN120890273B (en) | A sintering furnace for reaction sintering silicon carbide processing with monitoring function | |
| DE3641253C1 (en) | Process and furnace for sintering high temperature ceramics | |
| US6199277B1 (en) | Bake carbon flue straightener | |
| EP0230740A2 (en) | Container heating or sintering arrangements and methods | |
| WO1991020087A1 (en) | Capsule hot pressing | |
| IL22391A (en) | Process and apparatus for producing elongate rods | |
| CN2183545Y (en) | Cantilever atmosphere resistance furnace | |
| US3340270A (en) | Method of hot pressing metals and refractories | |
| EP0296855A2 (en) | A method of storing radioactive waste material | |
| Martin | Dimensional behavior of the experimental gas-cooled reactor fuel element at elevated temperatures | |
| CN2185415Y (en) | Cantilever type atmospheric resistance furnace |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MK14 | Patent ceased section 143(a) (annual fees not paid) or expired |