GB2294232A - Methd and materials for the manufacture of moulds and refractory articles - Google Patents
Methd and materials for the manufacture of moulds and refractory articles Download PDFInfo
- Publication number
- GB2294232A GB2294232A GB9520669A GB9520669A GB2294232A GB 2294232 A GB2294232 A GB 2294232A GB 9520669 A GB9520669 A GB 9520669A GB 9520669 A GB9520669 A GB 9520669A GB 2294232 A GB2294232 A GB 2294232A
- Authority
- GB
- United Kingdom
- Prior art keywords
- phosphate
- magnesia
- phosphates
- mould
- slurry
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
- C04B35/6303—Inorganic additives
- C04B35/6306—Binders based on phosphoric acids or phosphates
- C04B35/6313—Alkali metal or alkaline earth metal phosphates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22C—FOUNDRY MOULDING
- B22C1/00—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22C—FOUNDRY MOULDING
- B22C1/00—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds
- B22C1/02—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by additives for special purposes, e.g. indicators, breakdown additives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22C—FOUNDRY MOULDING
- B22C1/00—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds
- B22C1/16—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents
- B22C1/18—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents of inorganic agents
- B22C1/185—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents of inorganic agents containing phosphates, phosphoric acids or its derivatives
Abstract
Moulds, especially for the casting of metals, and other articles, are made by forming a settable slurry of a refractory aggregate, one or more phosphates and fusible fibres and forming the mould by allowing the slurry to set in a mould. The fibres may be melted out from the formed product to enhance the porosity thereof. A castable magnesia system is also disclosed which comprises a short chain sodium, potassium or calcium phosphate or an equivalent phosphate.
Description
IMPROVEMENTS IN 5ER{KE2E AND MOULD MAKING
The Shaw process of Precision Casting metals into ceramic moulds is described variously but particularly in U.K.
Patents Nos. 716,394 and also 741,381. It should be noted that the continued success of this process for making large castings such as die castings continues 40 years on. Patent 716,394 using ethyl silicate as the binder is substantially unchanged. The key to its success is the principle of rapid ignition and microcrazing the ceramic to create dimensional stability and subsequent permeability.
With increasing need to meet requirements of health and safety the use of volatile substances to create microcrazing becomes more difficult. In addition the cost of these volatiles is not significant in the cost of the process.
Patent 741,381 describes an alternative which has not proved so popular - largely we believe because of the need to heat to achieve the desired microcrazing.
A further difficulty is encountered in the need in many modern steels or high melting point alloys to avoid the presence of silica.
The nw process in accordance with the invention addresses each of the problems and sets out to provide a process that avoids the use of a volatile, a process that avoids ignition the use of high temperature heating in order to generate stable and permeable mould and a process that avoids the need for a silicate binder.
The process of the present invention uses a neutral ph liquid phosphate mixture essentially monosodium phosphate with the small addition of one or a combination of the following:- dipotassium phosphate, tetra potassium phosphate and dicalcium phosphate.
These additions move the ph to a figure of between 6 and 7 when used in conjunction with basic ceramics and encourages more mobile slurries for a given quantity of fluid. The solution preferred has been typically a 40% solution wgt with water of 3 parts of monosodium phosphate and 2 parts of dipotassium phosphate.
This mixture gives an effective strong gel within the parameters of the Shaw process - 2 minutes to about 20 minutes with a fast build up of ceramic mould strength.
Suitable moulds can however be made using di sodium phosphate dipotassium phosphate or non calcium phosphate solutions individually or in mixtures. Equally solutions of the preferred mixture can be diluted in many instances. More concentrated solution mixtures are envisaged but the solubility limit has to be born in mind.
The preferred solution above could typically range from a 30% solution to a 50% solution and the ratio of monosodium phosphate to dipotassium phosphate can be between 9 : 1 to 1 : 2 to create an effective gel.
A further feature of the invention envisages the use of the phosphate mixture as a powder to the ceramic grogs.
Typically the addition of 3 - 7% by wgt. This mixture of grog and binder would be typically mixed with 120 160 ccs of water per Kg. of grog.
The slurry is made from a grog typically natural crushed magnesite or of sintered or of fused magnesite in mesh sizings
60% -1+h mesh
30% -200 mesh
10% -325 mesh fused magnesia or sintered
magnesia
For extra strong moulds as described in 741,381 the addition of
extra monosodium phosphate - 1-2%
extra dicalcium phosphate - 1-2% may be added to the grogs as a powder or the mould can be strengthened as described by Shaw Process using phosphoric acid solution. The mixture is then in accordance with a preferred feature of the invention mixed with polypropylene fibres typically 1-2% by wgt and typically 60 to 125 microns diameter 3 - 6 mm long.
These fibres when melted away leave voids to achieve the desired porosity.
A very mobile slurry of this is prepared by adding the solution (available commercially as Clinochem 672 Bonding
Solution). Typically between 120 ccs liquid to 160 ccs liquid solution per kilo of magnesia mix. When mixed, possibly vacuumed (as described in various Shaw Process literature) the slurry is poured over a pattern in like manner to 716,394.
At 700F this slurry will set in approximately 2 minutes.
The setting time can be adjusted by reducing the fine magnesia fractions and substituting typically sintered or fused spinel in like size and proportions. This will increase the setting time or by substituting a less sintered fine magnesia in like quantity from the 200 or 300 mesh magnesia, typically magnesia (Lycal) by Redland
Magnesia in order to shorten the gel time. After gelling the mould is stripped. If the mould is then placed in an oven at 2000F or so (above boiling point of water and above melting point of polypropylene fibres) then surprisingly a stable mould permeable by virtue of discharged water and the voids left by the melted fibres is formed without further need for heating. That is not to say that the mould could not be heated to 500 - 6000C as described in 741,381 but it is not necessary except if further strength to the mould is required.
Magnesia moulds (basic ceramics) are substantially more resistant to metal mould reactions than alumina silicates. The removal of silicates reduces reactions further. Thus an economical mould can be made without recourse to the problems outlined.
The polypropylene fibres generate permeability and permit rapid drying of the mould. The use of water based binder removes the need for volatiles which are expensive and a problem in respect of health and safety. Other phosphates such as aluminium ortho phosphate, magnesium ortho phosphate, ammonium poly phosphates could be used as variously described for example in EPA 0,501 662 and
WO 94/21571. These binders however, do not remove satisfactorily the environmental problems even if they satisfy the technical problems.
It has further been found that very good moulds can be made for the process recently described as improvements of the above as follows.
The ceramic mixture Bauxite, Alumina or Zircon made with similar gramulometry and using polypropylene fibres may be mixed with 2-108 Magnesia active and finely divided [for gel control] and 1. Dry powdered Monosodium Phosphate 1-4% and then
adding as a liquid silica sol. 30-40% or 2. Premix into Monosodium Phosphate 50% w/v to Silica
sol. at 20-30% SiO2 and then using as a binder
liquid as described originally in Shaw ethyl
silicate mixtures or 3. Preparing a solution of 50% w/w Monosodium
Phosphate and mixing this solution 30-70% v/v with
30-40% Silica sol.
Slower setting times on even substantially basic ceramics such as fused or highly calcined Magnesia of the Alumina
Magnesia Spinels may be used if instead of Monosodium phosphate a Dipotassium phosphate is used but then in a similar manner to 1, 2 and 3 above.
The advantage of this additional process is that very strong moulds can be made by simply drying the mould at between 150-2500C. Naturally it is beneficial to fire up to 6500C as previously described but only if it is a requirement of the rest of the process parameters - for example wax removal.
There are no hazardous or smell generating ingredients in the chemical binders and as before the polypropylene fibres are removed at temperatures as low as 2000C.
This system is particularly suited to lower melting point metals such as copper, bronze and aluminium. The presence of Sodium or Potassium is less noticeable than the previous examples since Silica sol. is a partial replacement.
The disadvantage is however that the Silica, Na/K and
Magnesia form a low melting point eutectic. However the effect on lower melting point metals or alloys is reasonably insignificant.
It is well known that many phosphates can be used to make refractory cements, mortars and bricks as well as additives to improve castables all in the context of setting by a hydraulic reaction.
The most commonly used phosphates are aluminium ortho phosphates, sodium tripolyphosphate, sodium hexameta phosphate and phosphoric acids.
Aluminium ortho phosphate and phosphoric acid are used extensively for aluminous silicate castables as well as cements, rammables and pressed shapes. Sodium tripolyphosphate is used extensively as an addition to calcium aluminate cement castables for aluminas and aluminous silicates. Sodium hexameta phosphates are used for pressed brick including basic brick. In this specification cement is used to designate a hydraulically settable material.
The present invention is not concerned with hydraulic setting but with systems wherein a settable magnesium phosphate is formed by chemical reaction. The set magnesium phosphate is fired to yield magnesia.
EPA 0,501,662 designated PS cites an instance where a reactive ammonium phosphate can be used in a practical manner for a range of magnesia - alumina spinels. It is recognised that the evolution of NH4 is sometimes limiting.
My WO 94/21571 designated P450 cites similarly a mixture of aluminium and magnesium phosphate can be used in a practical manner for magnesia - alumina spinels.
This Patent Application concerns castables and it concerns castables that are cement free and essentially very rich magnesia - magnesia alumina spinels.
Whilst sodium hexameta phosphates and potassium phosphates in generality are cited as suitable as binders for magnesia rich refractories as already mentioned above, these citations have not been made in the context of a gellable bonding systems.
The present invention envisages short chain molecules of sodium phosphate, potassium phosphate and calcium phosphate reacting to form gels that are usable in castables of very high magnesia content.
This is contrary to the generally recognised uses of these phosphates in ceramics and refr.--tcries. Moreover these phosphates used individually whilst gelling and forming solid green shapes in the presence of magnesias form relatively weak pieces with no great inherent strength, except perhaps by adding unacceptably high amounts of phosphates - 10% or more x wgt.
What I have found is that: 1. The short chain mono sodium phosphate [an acidic phosphate ph 4.5] when combined with a short chain potassium phosphate, dipotassium phosphate [a basic phosphate ph 9] will form a gel with magnesia in a controlled manner and further build up quickly a green strength comparable to aluminium phosphates or say cements based on calcium aluminate.
2. The short chain monosodium phosphate has a similar effect with hexameta phosphate [also basic ph 7.5] which is surprising since hexameta phosphate normally is very slow reacting with basic magnesia refractories and too slow for practical purposes.
3. The short chain monosodium phosphate has a similar effect with calcium phosphate [which is surprising since dicalcium phosphate is insoluble with water and thus has a negligible reaction with magnesia]. It is worth noting that the best result appears to be a combination of an acidic soluble phosphate with a basic phosphate. Thus 4. The short chain mono sodium phosphate will have a similar effect in presence of the poly ammonium phosphates. However, if a polyammonium phosphate is acceptable within a system our co-pending Patent [P8] offers a solution.
A preferred mixture is:
A. Monosodium phosphate 3 parts x wgt.
Dipotassium phosphate 2 parts x wgt.
giving a resultant ph of approximately neutral 7.
The converse is:
B. Monopotassium phosphate 3 parts [acid ph 4.5]
Sodium hexameta phosphate 3 parts basic ph 7.5] giving a mixed ph of approximately 7. This mixture is however much slower to build up strength after gellation and tests have shown it not as effective as A.
The other preferred mixture is:
C. Monosodium phosphate 3 parts
Dicalcium phosphate 2 parts to again give a mixed ph of approximately 7.
Monocalcium phosphate it is found reacts quickly with basic mixtures of magnesia. It like the other mono compounds cited above is acid. It was found that a mixture of it with dicalcium phosphate was not as effective as A, B, C, probably for the reason that monocalcium phosphate has only a limited solubility in water. The selection of phosphate is governed to a notable extent upon the solubility of the phosphate concerned. Clearly an insoluble or only slightly soluble phosphate not only takes longer to disperse or dissolve in water and thus react with magnesia but then results in a much weaker green strength.
Our preferred mixture for maximum general performance that is to say: a) a controlled setting time within the acceptable
limits of time, 10 mins to 2 hours.
b) good green strength and maximum fired strength for
given phosphate content c) good strength build up after initial set so that a
castable can be readily stripped from its mould d) lacking any hazardous or offensive by-products on
heating is
D. Monosodium phosphate 3 parts
Dipotassium phosphate 1 part
Dicalcium phosphate 1 part though this is not intended as restrictive.
If the presence of calcium is undesirable in the ultimate refractory then mixtures A or B would be preferred.
By way of example the following is cited as a mixture for the manufacture of a refractory castable.
Aggregates as follows are all mixed together properly
Magnesite dead burnt or pericluse -5+3 mesh 35 parts x wgt.
-3+1 20 -1 20
Fused magnesia (pericluse) -200 15
Sintered Magnesia -200 5
Fused Magnesia -300 5 to which are mixed
Monosodium phosphate 3
Dipotassium phosphate 1
Dicalcium phosphate 1
Water is added - between 4-88 by wgt. to form a slurry which ' can be cast into a mould and vibrated to consolidate and left and allowed to set. This mixture, depending upon the temperature and the fineness of the -200 and -300 mesh magnesia will set typically at 180C in about 20 minutes.
A particular example of a castable readily available from
Clinochem Limited is as follows:
Clinochem cement Free Basic Castable having a chemistry:
MgO 80%
Al203 13%
CaO 0.9% p205 3.85%
Fe203 0.05%
Na20 1.35%
K20 0.90% This being a magnesia - magnesia spinel mixture gives physical properties as
Bulk density 2.75 gm/cc
% Porosity 19%
Cold Crush mpa 45
Cold MOR mpa 10
RUL @ 1500 less than 3%
Refractoriness greater than Cone 38 [Seger]
Thermal Shock greater than 100
The results are obtained on cast bricks 8 x 4 x 2", cast after mixing with 65 ccs H20 per kilogram of castable in a high sheer mixer and vibration cast for 3 minutes. The setting time of the castable to strip being 90 minutes.
The binder system consisted of an addition of 7% of preferred mixture D.
The following phosphates all to differing extents can be induced to form a gel in presence of magnesia. Thus enabling them to be used as non-cement castable.
Sodium Phosphates Monosodium phosphate Di sodium phosphate
Trisodium phosphate
Tetrasodium phosphate
Sodium Hexameta phosphate
Potassium phosphates Mono potassium phosphate MKP Di potassium phosphate DKP
Tri potassium phosphate TKP
Poly potassium phosphate TKPP
Calcium phosphates Mono calcium phosphate
Di calcium phosphate
This is despite them having widely differing solubility from nil to 100% and ph values acid and base.
The reaction in every case one has to presume is the formation of insoluble magnesium phosphate.
Short simple molecular structures work fastest to form a gel. The use of Calgon [sodium hexameta phosphate] is cited in many places as being a suitable binder for ref ractories to be pressed or as a heat setting or a setting cement with many refractory materials including basic materials such as magnesite. No mention is made of its ability to be used as a castable system which sets in presence of magnesia. This could be because in practice it takes several days to set. However, the use of monosodium phosphate has not to my knowledge noted anywhere. This being the shortest chain of the sodium phosphates reacts the fastest to set in presence of magnesia.
In the presence of a magnesia body typically
Magnesia Sintered -3+1 mesh 55% x wgt
Sintered -1 20% x wgt
Sintered -200 20% x wgt
Fused -325 5% x wgt will set and form a hard refractory within 1 - 2 minutes at 700F. If fused -200 mesh is used it will set in about 5 - 10 minutes at 700F.
That calcium phosphates are effective is even more surprising because: a) one would not expect calcium to pass its phosphate atoms to magnesium since magnesium is lower on the periodic table.
b) Mono calcium phosphate has only limited solubility in water and dicalcium is not soluble at all in water.
Mono potassium phosphate reacts in a close approximation to monosodium phosphate in presence of magnesia as does mono calcium phosphate. Trisodium phosphate has been proposed as an additive and binder for cement castables.
It is not cited as a binder in the absence of cement.
The binder in these instances appears always to refer to the effect of phosphate as an intermediate binder for calcium aluminate when heated above 6500C, not as a means of making a green shape.
What is also surprising is that the combination of sodium hexameta phosphate with aluminium tripoly phosphate results in not only a gel which is harder than sodium hexameta phosphate but that in presence of magnesia the two combined set in about 2 hours at 600F and are very hard in 4-5 hours at that temperature.
Sodium hexameta phosphate is very slow to react with magnesia - on its own several days. It has a ph of 7 and is very soluble in water or phosphoric acid and on its own has a negligible reaction with magnesia.
It is further surprising that potassium tetra polyphosphate behaves in a similar manner to the above in conjunction with aluminium tripolyphosphate.
The preferred mixture is using the sodium phosphate in a ratio of approximately 3 sodium to 1 aluminium.
However, this is not intended to be restrictive since different refractory applications could easily find expedient to change the ratio.
I have discovered that by combining one or more of these unlikely phosphates a result can b'e obtained which generates castable gels over a wide range of temperatures and over a wide range of magnesia content giving results that compare favourably with calcium aluminate cements at one end of the spectrum to a water based binder that compares very favourably with ethyl silicate at the other.
Claims (6)
1. A method of manufacturing moulds which comprises the steps of mixing a settable slurry of one or more phosphates and a suitable refractory aggregate and incorporating fibres into the slurry which, when melted after setting define stabilising voids.
2. A method as claimed in claim 1 wherein the slurry is based on a substantially neutral solution containing principally monosodium phosphate.
3. A method as claimed in either claim 1 or claim 2 wherein the fibres are of polypropylene.
4. A method of making a refractory object which uses a magnesia/phosphate setting system wherein the phosphate is a short chain sodium potassium, or calcium or equivalent phosphate.
5. Methods as claimed in either claim 1 or claim 4 and substantially as described in the specification.
6. Objects produced by a method according to any preceding claim.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9420875A GB9420875D0 (en) | 1994-10-17 | 1994-10-17 | Improvements in mould making |
GB9420877A GB9420877D0 (en) | 1994-10-17 | 1994-10-17 | Improvements in refractories |
Publications (3)
Publication Number | Publication Date |
---|---|
GB9520669D0 GB9520669D0 (en) | 1995-12-13 |
GB2294232A true GB2294232A (en) | 1996-04-24 |
GB2294232B GB2294232B (en) | 1998-06-10 |
Family
ID=26305821
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9520669A Expired - Lifetime GB2294232B (en) | 1994-10-17 | 1995-10-10 | Improvements in refractory and mould making |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB2294232B (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0771601A1 (en) | 1995-10-31 | 1997-05-07 | Richard Dudley Shaw | Refractory pouring nozzle |
WO2001068291A2 (en) * | 2000-03-17 | 2001-09-20 | Daniel James Duffey | Investment casting mould |
US6450243B1 (en) | 2000-03-17 | 2002-09-17 | Richard Dudley Shaw | Investment casting |
US6991022B2 (en) | 2000-11-10 | 2006-01-31 | Buntrock Industries, Inc | Investment casting mold and method of manufacture |
US7004230B2 (en) | 2000-11-10 | 2006-02-28 | Buntrock Industries, Inc. | Investment casting shells and compositions including rice hull ash |
US7048034B2 (en) | 2000-11-10 | 2006-05-23 | Buntrock Industries, Inc. | Investment casting mold and method of manufacture |
US10981214B2 (en) | 2017-12-11 | 2021-04-20 | Richard D. Shaw | Investment casting compositions |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB644994A (en) * | 1946-01-30 | 1950-10-25 | Emerik Imre Valyi | Investment compositions for the production of refractory molds and method of preparation |
GB1402318A (en) * | 1972-03-10 | 1975-08-06 | Foseco Int | Refractory heat insulating materials |
GB1410634A (en) * | 1972-10-18 | 1975-10-22 | Ici Ltd | Mould preparation |
US4623014A (en) * | 1983-06-04 | 1986-11-18 | Giulini Chemie Gmbh | Process for the production of precision castings |
-
1995
- 1995-10-10 GB GB9520669A patent/GB2294232B/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB644994A (en) * | 1946-01-30 | 1950-10-25 | Emerik Imre Valyi | Investment compositions for the production of refractory molds and method of preparation |
GB1402318A (en) * | 1972-03-10 | 1975-08-06 | Foseco Int | Refractory heat insulating materials |
GB1410634A (en) * | 1972-10-18 | 1975-10-22 | Ici Ltd | Mould preparation |
US4623014A (en) * | 1983-06-04 | 1986-11-18 | Giulini Chemie Gmbh | Process for the production of precision castings |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0771601A1 (en) | 1995-10-31 | 1997-05-07 | Richard Dudley Shaw | Refractory pouring nozzle |
WO2001068291A2 (en) * | 2000-03-17 | 2001-09-20 | Daniel James Duffey | Investment casting mould |
WO2001068291A3 (en) * | 2000-03-17 | 2001-12-27 | Daniel James Duffey | Investment casting mould |
US6450243B1 (en) | 2000-03-17 | 2002-09-17 | Richard Dudley Shaw | Investment casting |
US6755237B2 (en) | 2000-03-17 | 2004-06-29 | Daniel James Duffey | Investment casting |
US6769475B2 (en) | 2000-03-17 | 2004-08-03 | Richard Dudley Shaw | Investment casting |
US6991022B2 (en) | 2000-11-10 | 2006-01-31 | Buntrock Industries, Inc | Investment casting mold and method of manufacture |
US7004230B2 (en) | 2000-11-10 | 2006-02-28 | Buntrock Industries, Inc. | Investment casting shells and compositions including rice hull ash |
US7048034B2 (en) | 2000-11-10 | 2006-05-23 | Buntrock Industries, Inc. | Investment casting mold and method of manufacture |
US10981214B2 (en) | 2017-12-11 | 2021-04-20 | Richard D. Shaw | Investment casting compositions |
Also Published As
Publication number | Publication date |
---|---|
GB9520669D0 (en) | 1995-12-13 |
GB2294232B (en) | 1998-06-10 |
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