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Sommaire du brevet 2424368 

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Disponibilité de l'Abrégé et des Revendications

L'apparition de différences dans le texte et l'image des Revendications et de l'Abrégé dépend du moment auquel le document est publié. Les textes des Revendications et de l'Abrégé sont affichés :

  • lorsque la demande peut être examinée par le public;
  • lorsque le brevet est émis (délivrance).
(12) Demande de brevet: (11) CA 2424368
(54) Titre français: PROCEDE ET DISPOSITIF POUR CONTROLER LA TEMPERATURE DE L'ACIER A LA SURFACE DU BAIN D'UNE INSTALLATION DE COULEE CONTINUE JUSQU'A LA PERCEE DE FOUR
(54) Titre anglais: METHOD AND DEVICE FOR CONTROLLING THE TEMPERATURE OF STEEL BETWEEN THE MENISCUS OF A CONTINUOUS CASTING MACHINE AND THE TAPPING OF THE FURNACE
Statut: Réputée abandonnée et au-delà du délai pour le rétablissement - en attente de la réponse à l’avis de communication rejetée
Données bibliographiques
(51) Classification internationale des brevets (CIB):
  • B22D 11/18 (2006.01)
  • B22D 11/16 (2006.01)
  • B22D 11/20 (2006.01)
(72) Inventeurs :
  • PLESCHIUTSCHNIGG, FRITZ-PETER (Allemagne)
  • PARSCHAT, LOTHAR (Allemagne)
  • SCHWENCKE, ECKART (Allemagne)
  • WOSCH, ERWIN (Allemagne)
  • ROLLINGER, BERNT (Allemagne)
  • FELDHAUS, STEPHAN (Allemagne)
(73) Titulaires :
  • SMS DEMAG AKTIENGESELLSCHAFT
(71) Demandeurs :
  • SMS DEMAG AKTIENGESELLSCHAFT (Allemagne)
(74) Agent: RICHES, MCKENZIE & HERBERT LLP
(74) Co-agent:
(45) Délivré:
(86) Date de dépôt PCT: 2001-10-31
(87) Mise à la disponibilité du public: 2003-03-28
Licence disponible: S.O.
Cédé au domaine public: S.O.
(25) Langue des documents déposés: Anglais

Traité de coopération en matière de brevets (PCT): Oui
(86) Numéro de la demande PCT: PCT/EP2001/012594
(87) Numéro de publication internationale PCT: EP2001012594
(85) Entrée nationale: 2003-03-28

(30) Données de priorité de la demande:
Numéro de la demande Pays / territoire Date
100 54 760.5 (Allemagne) 2000-11-04
101 52 201.0 (Allemagne) 2001-10-23

Abrégés

Abrégé français

L'invention concerne un procédé pour contrôler la température de l'acier à la surface du bain d'une coquille de coulée continue (1) dans le domaine de la métallurgie secondaire (4) dans son ensemble, avec une étape de processus déterminante pour la température finale (4.1) tel qu'un four-poche, jusqu'à la percée de four (5) au cours d'un processus de production d'acier. Ce procédé est caractérisé en ce que la température de l'acier à la surface du bain est contrôlée sur la base de T¿ML? = T¿li? + X ·C (X = 5 - 15·C) et respectée en tenant compte de la détermination d'une saute de température (9) entre la surface du bain dans la coquille (1) et un distributeur (3) en relation avec la vitesse de coulée (6) pour un format de barre prédéterminé, de l'historique de la poche (7) en termes de périodes, comme p. ex. "poche pleine", "poche vide", et de l'état de la poche, comme p. ex. son revêtement, son vieillissement, ainsi que d'une saute de température de l'acier entre le distributeur (3) et la dernière température de four-poche (LF-ex).


Abrégé anglais


The invention relates to a method, which is used in the area of secondary
metallurgy (4) in its entirety with a final temperature-determining process
step (4.1) such as a ladle furnace, for controlling the temperature of steel
from the surface of the bath of a continuous casting ingot mold (1) up to the
furnace tap (5) of a steel producing process. According to the invention, the
temperature of the steel in the surface of the bath is controlled based on the
equation TML = TLI + X ~C (X = 5 - 15 ~C) and while respecting the same such
that a jump in temperature (9) between the surface of the bath in the ingot
mold (1) and a distributor (3) is detected according to the pouring rate (6)
for a predetermined billet size. In addition, the ladle history (7) with
regard to the time intervals, such as ladle full , ladle empty and ladle
state, such as ladle bricking up and ladle age is detected as well as a jump
in the temperature of steel between the distributor (3) and the last ladle
furnace temperature (LF-ex).

Revendications

Note : Les revendications sont présentées dans la langue officielle dans laquelle elles ont été soumises.


CLAIMS
1. Method for controlling the temperature of the steel in a
steel production process between the meniscus of a continuous
casting mold (1) and the tapping of the furnace (5) and thus over
the entire course of secondary metallurgical processing (4) with
a final temperature-determining process stage (4.1) such as a
ladle furnace, characterized in that
.cndot. the temperature of the steel at the meniscus of T ML = T li +
X°C (X = 5-15°C) is controlled and maintained under
consideration of the fact that there is a discontinuity (9)
in the temperature between the meniscus in the mold (1) and
a tundish (3) as a function of the casting speed (6) for a
strand of predetermined format; and in that
.cndot. the ladle history (7), comprising the time periods "ladle
full" and "ladle empty"; the ladle conditions such as the
ladle lining and the age of the ladle; and the
discontinuity in the temperature of the steel between the
tundish (3) and the last ladle furnace temperature (LF-ex)
is recorded.
2. Method according to Claim 1, characterized in that the
ladle history (7) is recorded in a time-differentiated manner by
an individual ladle identification system (8), which is installed
in the ladle cycle.
3. Method according to Claim 1 or Claim 2, characterized in
that the natural radiation of the ladle skin, which is relatively
hot in comparison with the ambient temperature, is used as a

means of detecting the individual ladles.
4. Method according to one of Claims 1-3, characterized in
that the ladle identification system (8) differentiates at least
between the "ladle full" time, the "ladle empty" time, and the
"ladle with new lining" time.
5. Method according to one of Claims 1-4, characterized in
that the history of the tundish is differentiated with respect to
the tundish preheating temperature, the tundish lining, the
tundish drying time, and the tundish service life data to allow
for the more accurate determination of temperature
discontinuities between the meniscus and the tundish and between
the tundish and the ladle furnace (LF-ex).
6. Device for controlling the temperature of the steel in a
steel production process between the meniscus of a continuous
casting mold (1) and the tapping of the furnace (5) and thus over
the entire course of secondary metallurgical processing (4) with
a final temperature-determining process stage (4.1) such as a
ladle furnace, especially for implementing the method according
to Claim 1, characterized in that measuring means (1.2 or 4.3)
are provided for detecting the temperature of the steel at the
meniscus of the mold (1) in a temperature window (2.1) of TML = Tai
+ X°C (X = 5-15°C) or for detecting the temperature of the steel
in the tundish (3) from TT-ideal = T°li + 10°C (10.1) or TT-real
- T°li + 10°C ~ 5°C (10.2) as a function of the casting
speed (6),
measuring means (3.n) also being provided for detecting the
tundish preheating time (3.2.2) and the tundish preheating
16

temperature (3.2.1); in that a ladle identification system (8)
provided inside the ladle cycle (7.4) or the ladle turnover
(7.4.1) records the ladle history (7), where the measuring means
are connected to a computer (4.4), which uses the measurement
values to determine on-line the temperature discontinuities (9
and 4.1.1) between the meniscus (2) and the tundish (3) and
between the tundish (3) and the ladle furnace (4.1),
respectively.
7. Device according to Claim 6, characterized in that the
ladle identification system (8) works with a coded metal plate
(8.1.1) and makes use of the natural radiation of the ladle,
where the metal plate is mounted a certain distance away from the
outside surface of the ladle (4.3) and conveys the time and
position data of each individual ladle (8.1) (ladle as individual
entity) to at least one radiation-measuring device (8.1.2)
installed in the ladle cycle (7.4.1).
8. Device according to Claim 6 or Claim 7, characterized in
that the ladle detection system (8) is designed to detect at
least the "ladle full" time (7.1), the "ladle empty" time (7.2),
and the "ladle with a new lining" time.
17

Description

Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.


CA 02424368 2003-03-28
METHOD AND DEVICE FOR CONTROLLING THE TEMPERATURE OF STEEL
BETWEEN THE MENISCUS OF A CONTINUOUS CASTING MACHINE
AND THE TAPPING OF THE FURNACE
The invention pertains to a method and a device for
controlling the temperature of the steel in a steel production
process between the meniscus of a continuous casting mold and the
tapping of the furnace and thus over the entire course of
secondary metallurgical processing with a final temperature-
determining process stage such as a ladle furnace.
For the successful casting of strands in any type of
continuous casting machine with or without oscillation and
preferably for strands of steel, the temperature of the steel at
the meniscus is an essential factor in determining the quality of
the steel (both surface quality and internal quality) and also
the reliability of the casting operation.
Controlling the temperature of the steel at the meniscus of
the continuous casting mold is especially important when the
casting speeds are increased to 10 or 12 m/min. There are also
many other important factors, however, which are important for
obtaining the desired casting result, which will be discussed
below.
The invention is based on the task of creating a method and
a device which make it possible, regardless of these numerous
factors, to plan and to control on-line the change in temperature

CA 02424368 2003-03-28
of the melt between the temperature of the steel at the meniscus
and the furnace tap.
An unexpected solution which lies outside standard technical
understanding is described in the claims.
Figures 1-4 present the invention by way of example and in
highly schematic fashion:
-- Figure 1 shows the process and production chain extending
between the furnace tap and the meniscus in the continuous
casting mold;
-- Figure 2 shows the change in the temperature campaign or
the temperature curve of the steel over the course of processing
in the processing chain, starting from the meniscus in the mold
and proceeding via the ladle furnace to the furnace tap; and
-- Figure 3 shows an example of a melt plan in the form of
the two Figures 3a and 3b.
It is assumed, as illustrated in Figure 1, that, depending
on:
~ the casting speed,
~ the casting width,
~ the casting thickness,
~ the casting format (round, profiled, etc.),
~ the casting output,
~ the tundish design,
~ the degree to which the tundish is filled,
~ the lining of the tundish,
~ the technology of the tundish, and
2

CA 02424368 2003-03-28
~ the condition of the ladle,
regardless of whether casting is carried out with
~ exposed casting steel and oil lubrication or with
~ an immersed outlet nozzle/immersion tube and casting flux,
the temperature of the steel at the meniscus (2) in the mold (1)
must be controlled and kept constant. In all casting situations,
this steel temperature (2.1) at the meniscus of the melt in the
mold (2) must be:
TML = T1; + X°C (X = 5-15°C) , Tli - f (grade of steel)
(2.1)
at a defined point which is symmetric to the shape of the mold.
In addition, it should be mentioned here that this condition
of a controlled meniscus temperature (2.1) can be applied to any
grade of steel.
To ensure the casting condition (2.1) regardless of the
possible casting situation, exact data are collected concerning
the temperature losses of the steel, starting from the meniscus
(2) and proceeding via the tundish (3), the secondary metallurgy
(4) with the ladle furnace (4.1) and, for example, a vacuum
treatment station (4.2), all the way to the tapping (5) of a
basic oxygen converter (BOF)(5.1), for example, or of an electric
furnace (EAF)(5.2).
The loss of temperature which the steel experiences over the
course of the processing and production chain is strongly
affected by the times and temperatures of the steel and of the
3

CA 02424368 2003-03-28
vessels with their refractory linings, specifically by the type
and condition of those linings (exposure time, wear, specific
heat transfer, etc.).
Thus, for example, the tundish (3) and the ladle (4.3) can
be considered heat exchangers, the specific thermal data of which
are determined by the type, age, or wear condition of their
linings.
It is also taken into consideration that, at the start of
casting, which is a non-steady-state phase of the process not yet
in heat flux equilibrium, the heat contents of the empty tundish
(3) and of the ladle (4.3), characterized by the heat-up time,
the heat-up temperature, and the ladle history (7), have a
significant effect on the temperature losses of the steel during
its holding time in the ladle, during the transfer from the ladle
to the tundish, and in the tundish itself.
In the case of a second ladle all the way to an n-th ladle
within a casting sequence, the tundish is in thermal equilibrium
with a constant heat loss, whereas the ladle, which can be
considered an "individual", continues to lose heat at various
rates.
In the past, these temperature losses along the route from
the tapping of the furnace (5) via the secondary metallurgy (4)
with the ladle furnace (4.1) as the interface to the tundish (3)
and finally to the area of the continuous casting machine (1.1)
have been estimated on the basis of practical experience and
taken qualitatively into account in the process.
4

CA 02424368 2003-03-28
For controlled casting, therefore, the starting point is the
desired steel temperature TML = T11 + X°C (2.1), and on this basis
the desired steel temperature in the tundish (3.1) is determined
for a planned casting speed and a planned casting format. The
tundish temperature (3.1) is adjusted appropriately on the basis
of the knowledge of the temperature loss (4.1.1) which occurs
between the ladle furnace and the tundish. A melt plan is shown
in Figure 3; it starts with the temperature of the steel at the
meniscus (2.1), expressed as the equivalent liquidus temperature
in the tundish T°li (3.1) with auxiliary temperatures of +5, 10,
15, 20°C (3.1.1), as a function of the casting speed (6) --
Figure 3a -- up to the delivery temperature from, for example,
the ladle furnace LF-ex (4.1) in the area of the secondary
metallurgy (4). The delivery temperature of the steel from the
ladle furnace is determined by the ladle history (7) with its two
essential factors:
~ the holding time of the steel in the ladle (7.1) between
the time it is tapped from the furnace and its delivery from the
ladle furnace for the start of casting, i.e., the "ladle full"
time, and
~ the period of the time when the ladle is not holding any
steel (7.2), i.e., the "ladle empty" time,
and by the tundish history (3.2) with its important factors:
~ the tundish preheating temperature (3.2.1),
~ the tundish preheating time (3.2.2), and
~ the tundish turnaround time (3.2.3) with its specific

CA 02424368 2003-03-28
preparation steps.
Figure 4 shows a suitable ladle identification system (8)
based on the encoding of the natural radiation of the ladle wall
by a perforated metal plate (8.1.1) and the detection of that
radiation by a radiation sensor (receiver) (8.1.2).
Figure 1 shows the entire process and production chain,
which extends between the tapping of the furnace (5) and the
continuous casting mold (1). So that the temperature of the
melt, starting from the desired temperature of the steel at the
meniscus (2.1), can be planned and controlled on-line, first for
the tundish and then for the ladle furnace LF-ex, it is necessary
to know:
~ the casting parameters, which here are:
~ the dependence of the temperature of the steel in the
tundish on the casting speed (6), described in the TT/VC system
(10) (see Figure 2), for a given casting output or holding time
of the steel in the tundish;
~ the history (3.2) of the tundish, comprising its
preheating temperature (3.2.1), preheating time (3.2.2), and the
tundish turnaround time (3.2.3) with the various possible
preparation steps such as relining, spraying, drying, etc.; and
~ the history of the ladle (7), comprising the holding time
of the steel in the ladle (7.1) and the remaining ladle time
(7.2), during which no steel is in the ladle, and the condition
(7.3) of the ladle, which is determined by:
-- the age of the ladle lining (wear) and
6

CA 02424368 2003-03-28
-- the type of ladle lining.
This history of the ladle (7) thus consists of:
~ the "ladle full" time, i.e., the time between the start of
the tap and the delivery from the ladle furnace with a maximum
duration until the start of casting of, for example, 25 minutes
(7.1);
~ the "ladle empty" time (7.2), and
~ the ladle condition (7.3),
where the
~ "ladle full" time (7.1) and
~ "ladle empty" time (7.2)
constitute the standard ladle cycle time (7.4).
During the "ladle empty" time (7.2), the ladle passes
through various treatments such as cleaning (7.2.1) and the
preparation of the slide valve for the next use (7.2.2). In
addition, the ladle can also be taken out of the ladle cycle so
that it can be heated on a heating stand (7.5) during long empty
periods or placed on a ladle lining stand (7.6) so that it can be
given a new lining.
To record all the numerous factors which act on the ladle
and thus ultimately determine the temperature loss (4.1.1)
between the ladle furnace and the tundish, the ladle
identification system (8) is installed in the ladle cycle (7.4)
at the locations relevant to the determination of the ladle
history (7). The detection system works preferably by means of
the encoding of the ladle radiation (8.1) and is based on the
7

CA 02424368 2003-03-28
natural radiation of the ladle. A measuring system of this type
can record the movement and the differentiated time sequences in
the "ladle full" (7.1) and "ladle empty" (7.2) phases, so that
the temperature losses (4.1.1) between the LF and the tundish can
be put into functional relationships with each other on-line on
the basis of the data thus acquired.
A procedure similar to that for the ladle is also
appropriate in the area of tundish management (3.2), where
special attention should be paid to the start of casting of a
casting sequence consisting of several ladles. Here the history
of the tundish (3.2) is superimposed additionally on the
temperature loss (4.1.1) between the LF (4.1) and the tundish
(3); this history consists of:
~ the preheating temperature of the tundish (3.2.1),
~ the tundish preheating time (3.2.2),
~ the tundish turnaround time (3.2.3),
~ the tundish drying time and temperature (3.2.4), and
~ the tundish lining (3.2.5).
Figure 2 shows the change in the temperature of the melt as
it travels from the electric furnace (5.2) or BOF (4.1) via the
ladle furnace LF-ex (4.1) to the meniscus (2) in the mold (1).
The desired temperature of the steel at the meniscus (2.1) is the
basis on which the temperatures in the tundish and in the ladle
furnace LF-ex (4.1) are planned.
The discontinuity in temperature between the meniscus and
the tundish (9), i.e., the decrease in the temperature of the
8

CA 02424368 2003-03-28
steel between the tundish and the meniscus, is determined
essentially by the casting speed (6) and the casting output, that
is, the solidification thickness and casting width.
The discontinuity in the temperature between the tundish and
the ladle furnace (4.1.1), however, is determined essentially by
the ladle history (7) and the tundish history (3.2).
Figure 3 is divided into parts 3a and 3b. Figure 3a shows
the tundish temperature (3.1) TT versus the casting speed (6) VC
for the equivalent liquidus temperature of the steel (3.1.1) in
the tundish T°~i with the auxiliary temperatures (3.1.1.1') T°li
+
5, 10, 15, 20°C.
If it is planned to cast at a rate of, for example, 5 m/min,
then a tundish temperature (10) of 1,560°C is obtained, which is
to be considered the ideal steel temperature (10.1)
TT = Tli + 10°C (VC = 5 m/min)
in the tundish for a grade with Tli = 1,530°C
To arrive at the ideal temperature (10.1) of, for example,
1,560°C, the discontinuity in the temperature (4.1.1) of the
steel between the tundish and the ladle furnace LF-ex (4.1) is
determined as shown in Figure 3b.
Here the temperature loss (4.1.1) is shown versus the time
factor "steel in the ladle (7.1)" for the start of casting in the
case of
~ a tundish preheating temperature of 1,100°C (3.2.1.1),
9

CA 02424368 2003-03-28
~ a tundish preheating temperature of 1,200°C (3.2.1.2),
and also for a 2nd and an n-th ladle (3.2.1.3) of a sequence.
The figure makes it clear how the temperature losses change
as a function of the holding time of the steel in the ladle (7.1)
and the tundish preheating temperature (3.2.1), both for the
first ladle of a sequence and for all the subsequent ladles.
These temperature losses also depend on the remaining part of the
ladle history (7) and can be determined by means of the on-line
method described here.
Figure 4 shows the ladle identification system (8), which
works with a perforated metal plate (8.1.1) to encode the natural
radiation (8.1). The encoded radiation is then detected by one
or more radiation sensors (8.1) located at strategic points in
the ladle cycle (7.4).
These descriptive process-related and device-related
features lead to controlled casting, which is characterized by:
~ good, maximized product quality,
~ high casting reliability with
~ high casting speeds and thus
~ high productivity.

CA 02424368 2003-03-28
List of Reference Numbers
1 Continuous Casting Mold
1.1 continuous casting machine
1.2 measuring means
2 Meniscus in the Mold
2.1 planned temperature window of steel at the meniscus,
TML = Tl~ + x°C (x = 5-15°C)
3 Tundish
3.1 temperature of the steel in the tundish, TT
3.1.1 equivalent liquidus temperature in the tundish, T°~i
3.1.1.1 auxiliary temperatures T°1~ + 5, 10, 15, 20°C
3.2 tundish history, tundish management
3.2.1 tundish preheating temperature
3.2.1.1 tundish preheating temperature of 1,100°C
3.2.1.2 tundish preheating temperature of 1,200°C
3.2.1.3 2nd to n-th ladle of a sequence
3.2.2 tundish preheating time
3.2.2.1 tundish preheating stand
3.2.3 tundish turnaround time
3.2.4 tundish drying time and temperature
3.2.5 tundish brick lining
3.2.6 tundish spray lining
3.n measuring means
11

CA 02424368 2003-03-28
4. Secondary Metallurcty
4.1 final temperature-determining process stage
such as a ladle furnace, LF-ex
4.1.1 temperature loss or jump between ladle furnace and
tundish
4.2 vacuum treatment stand
4.3 ladle
4.4 computer
Tappincr from Furnace to Ladle
5.1. converter, BOF
5.1.1 oxygen lance
5.2 electric furnace
6 Castinct Speed, VC in m/min
7 Ladle History
7.1 holding time of the eel in the ladle from the tapping
st
of the furnace t o the delivery of the ladle furnace
(LF-ex) or until the opening" of the ladle (start
" of
casting), "ladle full" time
7.2. time during whic h the ladle contains no steel, "ladle
empty" time
7.2.1 cleaning of the ladle,bottom, nozzle bricks, slide
valve
7.2.2 preparation of the slide valve, inspection, packing the
12

CA 02424368 2003-03-28
slide valve sand, etc.
7.3 ladle condition, age and type of lining
7.4 ladle cycle time
7.4.1 ladle cycle, ladle turnaround
7.5 ladle heating status
7.6. ladle brick lining status, new spray lining
8 Ladle Identification System
8.1 individual ladle with encoded radiation system, based
on the natural radiation of the ladle body, individual
ladle
8.1.1 coded metal plate
8.1.2. radiation sensor
9 Temperature Jump
steel at the meniscus/steel in the tundish or
temperature loss of the steel between the tundish and
the meniscus, function of the casting speed (VC) (6),
tundish design, etc.
Distributor Temperature, TT in °C
10.1 ideal target temperature TT-ideal = T°1~ (3.1.1) + 10°C
10.1.1 ideal target temperature TT-ideal = T°li (3.1.1) + 10°C
for VC = 5 mlmin
10.2 real temperature window TT-real = T°1~ (3.1.1) + 10°C ~
13

CA 02424368 2003-03-28
5°C
10.2.1 real temperature window TT-real = T°li (3.1.1) + 10°C ~
5°C for VC = m/min
11 Rolling Mill
14

Dessin représentatif
Une figure unique qui représente un dessin illustrant l'invention.
États administratifs

2024-08-01 : Dans le cadre de la transition vers les Brevets de nouvelle génération (BNG), la base de données sur les brevets canadiens (BDBC) contient désormais un Historique d'événement plus détaillé, qui reproduit le Journal des événements de notre nouvelle solution interne.

Veuillez noter que les événements débutant par « Inactive : » se réfèrent à des événements qui ne sont plus utilisés dans notre nouvelle solution interne.

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Historique d'événement

Description Date
Inactive : CIB de MCD 2006-03-12
Demande non rétablie avant l'échéance 2005-10-31
Le délai pour l'annulation est expiré 2005-10-31
Réputée abandonnée - omission de répondre à un avis sur les taxes pour le maintien en état 2004-11-01
Lettre envoyée 2003-07-16
Inactive : Transfert individuel 2003-06-16
Inactive : Lettre de courtoisie - Preuve 2003-06-10
Inactive : IPRP reçu 2003-06-09
Inactive : Page couverture publiée 2003-06-05
Inactive : Notice - Entrée phase nat. - Pas de RE 2003-06-03
Demande reçue - PCT 2003-05-02
Exigences pour l'entrée dans la phase nationale - jugée conforme 2003-03-28
Demande publiée (accessible au public) 2003-03-28

Historique d'abandonnement

Date d'abandonnement Raison Date de rétablissement
2004-11-01

Taxes périodiques

Le dernier paiement a été reçu le 2003-03-28

Avis : Si le paiement en totalité n'a pas été reçu au plus tard à la date indiquée, une taxe supplémentaire peut être imposée, soit une des taxes suivantes :

  • taxe de rétablissement ;
  • taxe pour paiement en souffrance ; ou
  • taxe additionnelle pour le renversement d'une péremption réputée.

Les taxes sur les brevets sont ajustées au 1er janvier de chaque année. Les montants ci-dessus sont les montants actuels s'ils sont reçus au plus tard le 31 décembre de l'année en cours.
Veuillez vous référer à la page web des taxes sur les brevets de l'OPIC pour voir tous les montants actuels des taxes.

Historique des taxes

Type de taxes Anniversaire Échéance Date payée
Enregistrement d'un document 2003-03-28
TM (demande, 2e anniv.) - générale 02 2003-10-31 2003-03-28
Taxe nationale de base - générale 2003-03-28
Titulaires au dossier

Les titulaires actuels et antérieures au dossier sont affichés en ordre alphabétique.

Titulaires actuels au dossier
SMS DEMAG AKTIENGESELLSCHAFT
Titulaires antérieures au dossier
BERNT ROLLINGER
ECKART SCHWENCKE
ERWIN WOSCH
FRITZ-PETER PLESCHIUTSCHNIGG
LOTHAR PARSCHAT
STEPHAN FELDHAUS
Les propriétaires antérieurs qui ne figurent pas dans la liste des « Propriétaires au dossier » apparaîtront dans d'autres documents au dossier.
Documents

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Liste des documents de brevet publiés et non publiés sur la BDBC .

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({010=Tous les documents, 020=Au moment du dépôt, 030=Au moment de la mise à la disponibilité du public, 040=À la délivrance, 050=Examen, 060=Correspondance reçue, 070=Divers, 080=Correspondance envoyée, 090=Paiement})


Description du
Document 
Date
(aaaa-mm-jj) 
Nombre de pages   Taille de l'image (Ko) 
Abrégé 2003-03-27 2 105
Description 2003-03-27 14 438
Dessin représentatif 2003-03-27 1 30
Dessins 2003-03-27 5 105
Revendications 2003-03-27 3 110
Avis d'entree dans la phase nationale 2003-06-02 1 189
Courtoisie - Certificat d'enregistrement (document(s) connexe(s)) 2003-07-15 1 105
Courtoisie - Lettre d'abandon (taxe de maintien en état) 2004-12-28 1 175
PCT 2003-03-27 3 102
Correspondance 2003-06-02 1 26
PCT 2003-03-28 2 68
PCT 2003-03-28 2 80