FIELD OF THE INVENTION
[0001] This invention refers to exothermic sleeves for obtaining mini-deadheads applicable
in the obtaining of cast pieces, especially in ductile iron, and to the procedure
for its production by blowing and curing.
BACKGROUND OF THE INVENTION
[0002] The production of cast metallic pieces comprises the pouring of the molten metal
into a mould, the solidification of the metal by cooling and the de-moulding or extraction
of the piece formed by means of the removal or destruction of the mould.
[0003] The moulds can be metallic or they can be formed by aggregates of different materials
(ceramics, graphite and, mainly, sand). These moulds need to have some sprues or runners
for communication between the internal cavity and the exterior, through which the
molten metal is poured in the moulding or casting phase. Due to the contraction of
the metal during the cooling process, some overflows have to be foreseen in the mould
which are filled with reserve molten metal with the object of forming a deadhead intended
to offset the contractions or cavities in the metal. The purpose of the deadhead is
to feed the piece when the melt contracts in this, for which reason the metal has
to remain in the deadhead in a liquid state for a longer period of time than the piece.
For this reason, the deadheads are usually covered with some sleeves, consisting of
insulating and/or exothermic materials, which slow the cooling of the metal contained
in the deadheads in order to guarantee the fluidity thereof when cavity voids are
produced in the cast metal.
[0004] The use of exothermic sleeves around the deadheads allows contraction problems to
be reduced and the quality of the cast pieces to be improved, which allows smaller
deadheads (mini-deadheads) to be employed which improve production and reduce the
contact surface of the deadhead with the cast piece, the elimination of which costs
money.
[0005] Exothermic sleeves are known based on fibres manufactured in a wet process starting
with a fibrous refractory material combined with a mixture of materials capable of
producing an exothermic reaction constituted by an oxidizable metal, in which aluminium
is habitually the most used, an oxidizing agent and a fusing agent or initiator of
the exothermic reaction which, habitually, is a fluorinated compound. The oxidizable
metal, when mixed with the oxidizing agent and the fusing agent and exposed to extreme
heat, is oxidized liberating heat in proportion to the advancing reaction.
[0006] Exothermic sleeves are also known based on sand, highly appreciated in ductile iron
foundries. The composition of these high-density sand-based sleeves contains a greater
quantity of aluminium very high so that the amount of heat produced is very high.
This heat is necessary to raise the temperature of the sand-based sleeve before favourably
influencing the temperature of the metal in the deadhead.
[0007] In 1997 a fibre-free sleeve technology was introduced, furnishing a new alternative
to the exothermic sleeves. The patent application
WO-A1-97/00172 discloses a procedure for blowing and cold box curing to manufacture dimensionally
accurate, exothermic and/or insulating sleeves, based on a mixture blowable into a
mould, said mixture consisting of microspheres of aluminium silicate with an alumina
content of less than 38% by weight, a binding agent for cold box curing and, optionally,
some non-fibrous loads. A typical composition for the production of exothermic sleeves
comprises hollow microspheres with an alumina content of less than 38% by weight,
aluminium powder, iron oxide and cryolite as fluorinated flux.
[0008] At the present time sleeves exist in the foundry industry for obtaining the so-called
mini-deadheads, the function of which is also to feed liquid metal to the piece while
the latter contracts during solidification.
[0009] The fundamental difference with the conventional exothermic sleeves is that the latter
maintain the metal liquid for a longer time, whereby the volume of metal necessary,
this is, the mini-deadhead, is smaller for a same feeding operation.
[0010] This result is achieved by increasing the exothermic load of the sleeve, but this
increased exothermicity gives rise to undesired collateral problems, such as:
- 1. The excess of residual aluminium in the deadhead, which is later recast, gives
rise to problems with pores in the molten pieces.
The defect known as "fish-eye" is a surface flaw in the cast piece, originated by
the accumulation of materials produced in the recovery of contaminated sand, fundamentally
by the aluminium which is found in high proportions in exothermic sleeves.
This defect can be overcome by the use of, for example, hollow microspheres of aluminium
silicate with a low content of alumina, such as that described in WO-A-97/00172.
- 2. Degradation of the nodules in the area of contact of the sleeve with the piece
which results in the rejection of pieces through non-compliance with the specifications
for nodulation required by the client.
This second problem is originated by the excess of fluorine proceeding from the fluorinated
materials which are habitually used as initiating charge in the exothermic reaction.
To avoid this problem, either the sleeve is not put in contact with the piece, which
makes it necessary to use more metal, or an intermediate, fluoride-free biscuit is
used, stuck to the mouth of the sleeve and having an equivalent central hole, which
prevents contact of the actual sleeve with the piece. This biscuit, its production
and securing to the sleeve, signify a substantial additional expense.
[0011] Patent
ES-A-2 155 001 discloses an exothermic casting sleeve which has openings at both ends, both openings
having a cylindrical shape. The sleeve comprises insulating refractory material in
the form of hollow microspheres of aluminium silicate, at least one of Al, Mg, Si
as an oxidizable metal, a salt of an alkaline or earth alkaline as an oxidizing agent,
a binding agent for curing and a curing catalyst.
SUMMARY OF THE INVENTION
[0012] The invention arises from the challenge of furnishing a sleeve for obtaining mini-deadheads
which does not require the use of a fluoride-free biscuit, nor of any other element
to avoid contact of the sleeve with the piece and which, moreover, produces in the
deadhead a notch to facilitate its later separation from the cast piece and all this
based on a blowable mixture, without fluorine, capable of producing an exothermic
reaction for the provision of the heat required.
[0013] As defined in claim 1 the procedure for the production by blowing and cold box curing
of an exothermic sleeve for foundry moulds comprises the following steps:
- (A) introducing, by blowing, in a cold box curing mould in the space defined between
the mould and two cores, which are in line with each other and touch each other, a
mixture for the production of an exothermic sleeve, thereby obtaining an uncured sleeve,
open at both its ends, the respective lengths of the two cores and the configuration
of their ends touching each other being such that the opening of the mouth of the
uncured sleeve has an internal double chamfer, whilst the other opening is normally
flat,
- (B) bringing the uncured sleeve prepared in (A) into contact with a cold box curing
catalyst for curing said uncured sleeve;
- (C) leaving the sleeve resulting from (B) in the mould to be cured;
- (D) removing the cured sleeve from the mould; and
- (E) locating a plug in the orifice of the base of the cured sleeve opposite the mouth
of the sleeve.
[0014] Herein the mixture for the production of the exothermic sleeve comprises:
- a. a fluoride-free composition for the production of sleeves which comprises:
a.1) an insulating/refractory material
a.2) an exothermic mixture based on an oxidizable metal, an oxidizing agent capable
of producing an exothermic reaction and magnesium as initiator element of the reaction;
- b. a binding agent for cold box curing
[0015] Hollow microspheres of aluminium silicate are basically used as insulating material.
Mixtures of these aluminium silicate spheres with sand can also be used, when it is
necessary to improve the mechanical properties of the sleeve, to the detriment of
the insulating properties.
[0016] As oxidizable metals aluminium, silicon and others can be used. Preferably aluminium
in a combination of fine and coarse powder.
[0017] As oxidizing agents, nitrates, chlorates, permanganates and metallic oxides such
as iron and magnesium oxide can be used and, of course, combinations of these compounds.
[0018] As initiator of the exothermic reaction, magnesium is used.
[0019] Once this mixture is blown into the mould, the sleeve extracted and cured, the orifice
opposite the mouth is closed with a plug which can be made of plastic, wood, sawdust,
sand, etc. and even of the same material as the sleeve.
[0020] The use of these sleeves allows the manufacture of high quality pieces, without degradation
of the graphite nodules in the deadhead-piece contact zone, at reduced cost, comparatively
less than that of other conventional procedures which deliver pieces of similar quality
based on contact between the deadhead and the piece through an intermediate biscuit.
BRIEF DESCRIPTION OF THE FIGURES
[0021]
Figure 1 illustrates the steps for the production of a sleeve by means of a conventional
procedure of blowing and cold box curing pertaining to the state of the art. In this
case, the mixture for the production of sleeves is blown into a mould (3) with the
collaboration of a core (2) [Figure 1A]; next, the sleeve (1) is cured and de-moulded
leaving the void intended for the deadhead (4) [Figure 1B]; and, finally, an intermediate
biscuit (5) is applied which has an orifice (6) for the melt to pass [Figure 1C].
Figure 2 illustrates the steps for production of an exothermic sleeve according to
the procedure of blowing and cold box curing disclosed by the present invention.
DETAILED DESCRIPTION OF THE INVENTION
[0022] As can be appreciated in Figure 2, contrary to the conventional procedures pertaining
to the state of the art (see Figure 1), in the procedure disclosed by this invention,
the fluoride-free mixture for the production of exothermic sleeves is blown inside
a mould, in the space defined between the mould (3) and the cores (2,2') [Figure 2A].
The cores (2,2') as well as allowing the subsequent extraction of the sleeve, produce
a double chamfer (8) in the mouth thereof. When the sleeve (1) is cured, it is de-moulded
leaving the void intended for the deadhead (4) [Figure 2B]; and, finally, a plug (9)
is located in an open end of the sleeve (1) for the purpose of preventing sand or
of any other undesirable element from entering inside the cavity intended for the
deadhead during the casting operation [Figure 2C].
[0023] The double chamfer (8) of the sleeve, will produce in the deadhead a rut or slot
equivalent in form which defines and facilitates the cutting line for the separation
of the deadhead from the piece.
[0024] The insulating/refractory material (a.1) present in the fluoride-free composition
for the production of sleeves is a material which basically comprises hollow microspheres
of aluminium silicate, although it could also contain a certain quantity of sand,
on the assumption that, by sacrificing insulating capacity, it is desired to improve
the mechanical properties of the sleeve.
[0025] In general, the quantity of insulating/refractory material (a.1) will be between
30 and 70% by weight with respect to the total of the fluoride-free composition.
[0026] The exothermic material (a.2) present in the fluoride-free composition for the production
of sleeves comprises an oxidizable metal and an oxidizing agent capable of producing
an exothermic reaction, wherein said exothermic material might comprise:
- (i) magnesium as initiator element of the exothermic reaction, together with one or
more oxidizable metals, preferably a mixture of powdered and granulated aluminium.
- (ii) an oxidizing agent capable of reacting with the oxidizable metal and producing
an exothermic reaction at the pouring temperature of the metal, said oxidizing agent
being selected from the group formed by (a) salts of alkaline metals or alkaline earths,
for example, nitrates, chlorates and permanganates of alkaline metals or alkaline
earths; (b) metallic oxides, for example, iron and manganese oxides, preferably iron
oxide; and (c) mixtures of (a) and (b). Said exothermic material (a.2) is in non-fibrous
form, to be capable of being blown.
[0027] A property of the composition for the production of the exothermic sleeves according
to the present invention resides in that said composition comes without the inorganic
fluorinated flux habitually utilized as initiators of the exothermic reaction. Magnesium
is used in place thereof, which reacts at a lower temperature whereby the exothermic
reaction produced between the oxidizable metal and the oxidizing agent begins earlier.
[0028] The reaction between the oxidizable metal and the oxidizing agent is an exothermic
reaction which produces heat thereby enhancing the heating properties of the exothermic
sleeves. Thus, the loss of temperature is reduced of the molten material in the sprue,
which is kept hotter and liquid for a longer time.
[0029] Depending on the level of exothermic properties it is desired to attain in the sleeve,
the quantity of oxidizable metal present in the exothermic material (a.2) will be
between 20 and 30% by weight with respect to the total of the fluoride-free composition
for the production of the sleeve.
[0030] The procedure disclosed by this invention allows exothermic sleeves to be obtained
with the desired balance of insulating and exothermic properties merely by using the
quantities of insulating material (a.1) and of material exothermic (a.2) present in
component A in the appropriate ratios by weight.
The cold box curing binding agents which can be used in the mixture for the production
of sleeves according to the sleeve manufacturing procedure disclosed by this invention
are known. In principle, any cold box curing binding agent can be used which is capable
of maintaining the fluoride-free composition for the production of sleeves in the
form of a sleeve and polymerise in presence of a curing catalyst. By way of example,
use can be made of phenol resins, phenol-urethane resins, epoxy acrylic resins, alkaline
phenol resins, resins of silicates, etc. activated by an appropriate catalyst in the
gaseous phase. In a particular embodiment, this cold box curing binding agent is selected
from among the epoxy acrylic resins activated by SO
2 (gas) and the phenol-urethane resins activated by amine (gas) known as cold box curing
binding agents EXACTCAST® (Ashland).
[0031] The necessary quantity of cold box curing binding agent is the effective quantity
to maintain the form of the sleeve and to permit its effective curing, that is, a
quantity such as allows a sleeve to be produced which can be handled after the curing
process. By way of example, the quantity of cold box curing binding agent will be
between 1 and 10% with respect to the total of the composition for the production
of the sleeve.
[0032] The catalyst for cold box curing is applied in gas form and is made to pass through
the sleeve until the latter reaches a manageable consistency. The catalyst in the
gaseous phase can be an amine, carbon dioxide, methyl formate, sulphur dioxide, etc.
depending on the cold box curing binder utilized.
[0033] Operating appropriately and selecting the components of the composition for the production
of sleeves, exothermic sleeves can be obtained with both internal and external dimensional
accuracy, which can be coupled easily to the moulding assembly in the foundry after
being manufactured with no need to carry out additional manipulations.
[0034] The exothermic sleeve obtainable according to the procedure disclosed by this invention
constitutes an additional aspect of the present invention.
As can be appreciated in Figure 2, the sleeve (1) provided by this invention comprises:
- (i) a body which surrounds the void intended to contain the deadhead (4) and which
has a double chamfer (8) on the mouth thereof, and
- (ii) a plug (9) in the base opposite the mouth.
[0035] The double chamfer (8) present in the sleeve provided by this invention is due to
the combined action of 2 cores (2,2') during the blowing of the mixture. The double
chamfer (8) will define in the deadhead a rut or slot which facilitates the separation
of the same from the cast piece.
[0036] Due to the manufacturing procedure of the sleeve provided by this invention, which
comprises the combined action of 2 cores, 2 open ends are produced. One of said ends
contains a double chamfer (8) whilst the other open end is closed with a plug (9)
for the purpose of preventing sand or any other undesirable element from passing into
the interior of the sleeve during the mounting of the same on the mould and, of course,
during the casting operation. Thus, said plug (9) has no structural purpose nor does
it intervene in the formation or action of the deadhead, and, for this reason, the
material used in the production of the plug can be practically any material, advantageously,
a cheap material, such as plastic, wood, sawdust, paper, sand, etc., or even the actual
material constituting the sleeve.
[0037] By way of comparison a table is provided below of blowable mixtures for obtaining
exothermic sleeves with fluorinated and fluoride-free flux, according to the invention,
for the same exothermal capacity.
COST OF THE MIXTURES FOR THE SAME DEGREE DE EXOTHERMICITY
| |
MINI-DEADHEADS WITH FLUORINE |
MINI-DEADHEADS WITHOUT FLUORINE |
MINI-DEADHEADS MADE OF SAND |
| % |
% |
% |
| Microspheres |
56.0% |
54.0% |
|
| Microspheres Aluminium, fine |
22.0% |
22.0% |
22.0% |
| Aluminium, coarse |
6.0% |
6.0% |
6.0% |
| Fe3O4-Magnetite |
4.0% |
4.0% |
4.0% |
| Cryolite |
4.0% |
|
4.0% |
| KNO3-Potassium nitrate |
8.0% |
10.0% |
8.0% |
| Magnesium |
|
4.0% |
|
| Sand 60/70 |
|
|
56.0% |
| COST PER KILOGRAM OF MIXTURE |
100.0% |
100.0% |
100.0% |
1. A procedure for the production by blowing and cold box curing of an exothermic sleeve
for foundry moulds which comprises:
(A) introducing, by blowing, in a cold box curing mould in the space defined between
the mould and two cores, which are in line with each other and touch each other, a
mixture for the production of an exothermic sleeve, thereby obtaining an uncured sleeve,
open at both its ends, the respective lengths of the two cores and the configuration
of their ends touching each other being such that the opening of the mouth of the
uncured sleeve has an internal double chamfer, whilst the other opening is normally
flat, in which said mixture for the production of exothermic sleeves comprises:
a. a fluoride-free composition for the production of sleeves which comprises:
a.1) an insulating/refractory material
a.2) an exothermic mixture based on an oxidizable metal, an oxidizing agent capable
of producing an exothermic reaction and magnesium as initiator element of the reaction;
b. a binding agent for cold box curing;
(B) bringing the uncured sleeve prepared in (A) into contact with a cold box curing
catalyst for curing said uncured sleeve;
(C) leaving the sleeve resulting from (B) in the mould to be cured;
(D) removing the cured sleeve from the mould; and
(E) locating a plug in the orifice of the base of the cured sleeve opposite the mouth
of the sleeve.
2. Procedure according to claim 1, wherein said insulating material with refractory properties
(a.1) is aluminium silicate in the form of hollow microspheres.
3. Procedure according to claim 1, wherein said oxidizable metal is aluminium, preferably
a mixture of fine and coarse powder of this metal.
4. Procedure according to claim 1, wherein said oxidizing agent is selected from the
group formed by salts of alkaline metals or alkaline earths, metallic oxides, and
mixtures thereof.
5. Procedure according to claims 1 and 4, in which said oxidizing agent is selected of
the group formed by nitrates, chlorates and permanganates of alkaline metals or alkaline
earths, iron oxide, manganese oxide, and mixtures thereof.
6. Procedure according to claim 1, wherein said exothermic material (a.2) is in non-fibrous
form, that is, in blowable form.
7. Procedure according to claim 1, wherein said cold box curing binding agent is selected
from the group formed by phenol resins, phenol-urethane resins, acrylic epoxy resins,
alkaline phenol resins and resins of silicates.
8. Procedure according to claim 12, wherein said cold box curing binding agent is selected
from the group formed by acrylic epoxy resins activated by SO2 (gas) and phenol-urethane resins activated by amine (gas).
9. Procedure according to claim 1, wherein, in stage (B), the uncured sleeve prepared
in stage (A) is put in contact with a catalyst in the gaseous phase suitable for curing
said sleeve.
10. Procedure according to claim 1, wherein said catalyst for curing the uncured sleeve
is a catalyst in the gaseous phase selected from among a gaseous amine to activate
phenol-urethane resins; SO2 (gas) to activate acrylic epoxy resins; CO2 (gas) or methyl formate (gas) to activate alkaline phenol resins; and CO2 (gas) to activate sodium silicate resins.
11. Sleeve made according to the method of claim 1, characterised in that when moulded, de-moulded and cured, it has a mouth for the entrance of the melt which
has to form the deadhead provided with an internal peripheral chamfer, which will
produce in the deadhead a rut or slot of equivalent geometry, whilst the orifice opposite
the mouth is closed with a plug of plastic, wood, sawdust, sand or even of the actual
material which constitutes the sleeve.
1. Verfahren zur Herstellung einer exothermen Hülse für Gießformen durch Blasen und Cold-Box-Härten
umfassend:
A) Einführen durch Blasen, in eine Form zum Cold-Box-Härten / in den Raum, welcher
zwischen der Form und zwei Kernen definiert wird, welche zueinander ausgerichtet sind
und einander berühren, einer Mischung zur Herstellung einer exothermen Hülse, wodurch
eine ungehärtete Hülse erhalten wird, die an beiden Enden offen ist, wobei die jeweiligen
Längen der zwei Kerne und der Aufbau der Enden, welche einander berühren, solchermaßen
ist, dass die Öffnung des Mundstückes bzw. der Mündung der ungehärteten Hülse eine
innere doppelte Fase aufweist, während die andere Öffnung normal flach ist, wobei
die Mischung zur Herstellung der exothermen Hülse umfasst:
a. eine fluoridfreie Zusammensetzung zur Herstellung von Hülsen, welche umfasst:
a.1) ein isolierendes/feuerfestes Material
a.2) eine exotherme Mischung, basierend auf einem oxidierbaren Metall, einem Oxidationsmittel,
welches geeignet ist, eine exotherme Reaktion zu erzeugen, und Magnesium als Initiatorelement
der Reaktion.
b. ein Bindemittel für das Cold-Box-Härten;
B) in Kontakt bringen der ungehärteten Hülse, welche in (A) hergestellt wurde, mit
einem Cold-Box-Härtungskatalysator, zum Härten der ungehärteten Hülse;
C) Lassen der Hülse, welche aus (B) resultiert, in der Form, um gehärtet zu werden;
D) Entfernen der gehärteten Hülse aus der Form; und
E) Anordnen einen Stöpsels in der Öffnung der Basis bzw. Grundfläche der gehärteten
Hülse, welche dem Mundstück bzw. der Mündung der Hülse gegenüberliegt.
2. Verfahren nach Anspruch 1, wobei das isolierende Material mit feuerfesten Eigenschaften
(a.1) ein Aluminiumsilikat in der Form von hohlen Mikrokugeln ist.
3. Verfahren nach Anspruch 1, wobei das oxidierbare Metall Aluminium vorzugsweise eine
Mischung aus feinem und groben Pulver dieses Metalls ist.
4. Verfahren nach Anspruch 1, wobei das Oxidationsmittel gewählt wird aus der Gruppe,
gebildet durch Salze von Alkalimetallen oder Erdalkalimetallen, metallischen Oxiden
und deren Mischungen.
5. Verfahren nach Anspruch 1 und 4, wobei das Oxidationsmittel gewählt ist aus der Gruppe
gebildet durch Nitrate, Chlorate und Permanganate von Alkalimetallen oder Erdalkalimetallen,
Eisenoxid, Manganoxid und Mischungen dieser.
6. Verfahren nach Anspruch 1, wobei das exotherme Material (a.2) in nicht faserförmiger
Form vorliegt, d.h. in blasbarer Form.
7. Verfahren nach Anspruch 1, wobei das Bindemittel für das Cold-Box-Härten gewählt wird
aus der Gruppe, gebildet durch Phenolharze, Phenolurethanharze, Acryl-Epoxidharze,
alkalische Phenolharze und Harze von Silikaten.
8. Verfahren nach Anspruch 12, wobei das Bindemittel für das Cold-Box-Härten gewählt
wird aus der Gruppe gebildet durch Acryl-Epoxidharze, aktiviert durch SO2 (Gas) und Phenol-Urethanharze, aktiviert durch Amin (Gas).
9. Verfahren nach Anspruch 1, wobei in Stufe (B), die in Stufe (A) hergestellte ungehärtete
Hülse mit einem Katalysator in gasförmiger Phase in Kontakt gebracht wird, welcher
geeignet ist, die Hülse zu härten.
10. Verfahren nach Anspruch 1, wobei der Katalysator zum Härten der ungehärteten Hülse
ein Katalysator in der gasförmigen Phase ist, gewählt unter einem gasförmigen Amin
zur Aktivierung von Phenol-Urethanharzen; SO2 (Gas) zur Aktivierung von Acryl-Epoxidharzen; CO2 (Gas) oder Methylformat (Gas), um alkalische Phenolharze zu aktivieren; und CO2 (Gas), um Natriumsilikatharze zu aktivieren.
11. Hülse, hergestellt nach dem Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass, wenn sie geformt, entformt und gehärtet wurde, sie ein Mundstück bzw. eine Mündung
zum Eingang der Schmelze aufweist, welche(s) den Gießkopf bildet, und mit einer inneren
Umfangsfase versehen ist, welche in dem Gießkopf eine Furche oder einen Schlitz mit
äquivalenter Geometrie bildet, während die Öffnung, welche dem Mundstück gegenüberliegt,
mit einem Stopfen aus Plastik, Holz, Sägemehl, Sand oder sogar mit dem tatsächlichen
Material, welches die Hülse bildet, verschlossen ist.
1. Procédé pour produire par soufflage et par durcissement en boîte froide d'un manchon
exothermique pour moules de fonderie, comprenant :
(A) l'introduction, par soufflage, dans un moule de durcissement en boîte froide dans
l'espace défini entre le moule et deux noyaux alignés l'un avec l'autre et qui se
touchent, d'un mélange pour la production d'un manchon exothermique, obtenant de cette
manière un manchon non durci, ouvert à ses deux extrémités, les longueurs respectives
des deux noyaux et la configuration de leurs extrémités qui se touchent étant telle
que l'ouverture de l'embouchure du manchon non durci a un double chanfrein interne
tandis que l'autre ouverture est normalement plate, et dont le mélange pour produire
des manchons exothermiques comprend :
a. une composition sans fluorures pour produire des manchons comprenant :
a.1) un matériau isolant/ réfractaire,
a.2) un mélange exothermique à base d'un métal oxydable, d'un agent oxydant capable
de produire une réaction exothermique, et de magnésium en tant qu'élément amorceur
de la réaction ;
b. un agent liant pour le durcissement en boîte froide ;
(B) la mise en contact du manchon non durci préparé en (A) en contact avec un catalyseur
de durcissement en boîte froide pour durcir le manchon non durci ;
(C) le séjour du manchon obtenu en (B) dans le moule à durcir ;
(D) le retrait du manchon durci à partir du moule ; et
(E) la mise en place d'un bouchon dans l'orifice de la base du manchon durci qui est
opposé à l'embouchure du manchon.
2. Procédé selon la revendication 1, selon lequel le matériau isolant ayant des propriétés
réfractaires (a.1) est le silicate d'aluminium sous la forme de microsphères creuses.
3. Procédé selon la revendication 1, dans lequel le métal oxydable est l'aluminium, de
préférence un mélange de poudres fine et grossière de ce métal.
4. Procédé selon la revendication 1, dans lequel l'agent oxydant est choisi dans le groupe
formé par des sels de métaux alcalins ou de terres alcalines, des oxydes métalliques
et des mélanges de ceux-ci.
5. Procédé selon les revendications 1 et 4, dans lequel l'agent oxydant est choisi dans
le groupe formé par les nitrates, les chlorates et les permanganates de métaux alcalins
ou de terres alcalines, l'oxyde de fer, l'oxyde de manganèse et des mélanges de ceux-ci.
6. Procédé selon la revendication 1, dans lequel le matériau exothermique (a.2) est sous
forme non fibreuse, c'est-à-dire, sous forme soufflable.
7. Procédé selon la revendication 1, dans lequel l'agent liant de durcissement en boîte
froide est choisi dans le groupe formé par les résines phénoliques, les résines phénol-uréthane,
les résines époxy-acryliques, les résines phénoliques alcalines et les résines de
silicates.
8. Procédé selon la revendication 12, dans lequel l'agent liant de durcissement en boîte
froide est choisi dans le groupe formé par des résines époxy-acryliques activées par
du SO2 (gaz) et des résines phénol-uréthane activées par une amine (gaz).
9. Procédé selon la revendication 1, dans lequel, à l'étape (B), le manchon non durci
préparé à l'étape (A) est mis en contact avec un catalyseur dans la phase gazeuse
adaptée pour durcir le manchon.
10. Procédé selon la revendication 1, dans lequel le catalyseur pour durcir le manchon
non durci est un catalyseur dans la phase gazeuse choisie parmi une amine gazeuse
pour activer les résines phénol-uréthane, le SO2 (gaz) pour activer les résines époxy-acryliques, le CO2 (gaz) ou le formiate de méthyle (gaz) pour activer les résines phénoliques alcalines
et le CO2 (gaz) pour activer les résines de silicate de sodium.
11. Manchon fabriqué selon le procédé de la revendication 1,
caractérisé en ce que
lorsqu'il est moulé, démoulé et durci, il présente une embouchure pour l'entrée de
la masse fondue qui doit former la masselotte, dotée d'un chanfrein périphérique interne,
ce qui va produire dans la masselotte une ornière ou une fente de géométrie équivalente,
tandis que l'orifice opposé à l'embouchure est fermé par un bouchon en plastique,
en bois, en sciure, en sable et même en matériau constituant précisément le manchon.