Method and device for reaction control

Abstract

A method for controlling surface reactions on a steel strip running through a furnace includes, successively, a first section, a second section, and a third section separated by a sealing element, an atmosphere in the second and third sections being oxidizing and reducing respectively, the method including: heating, in the first section, the steel strip to between 600 and 750° C., while causing the atmosphere therein to be slightly oxidizing and to include: an H.sub.2 content inferior to 2%; an O.sub.2 content inferior to 0.1%; an H.sub.2O or CO.sub.2, or H.sub.2O+CO.sub.2 content superior to 0.03%; a controlled dew point ranging from −50 to −15° C.; and a controlled concentration of CO+CO.sub.2 maintained below 2%. All percentages are expressed in terms of volume.

Claims

1. A method for controlling surface reactions on a steel strip running through a furnace comprising, successively, a first section, a second section, and a third section separated by a sealing element, an atmosphere in the second and third sections being oxidizing and reducing respectively, the method comprising: heating, in the first section, the steel strip to between 600 and 750° C., the first section comprising a resistance heater, an inductive heater, or a radiant tube heater, while causing the atmosphere therein to be slightly oxidizing and to include: an H.sub.2 content inferior to 2%; an O.sub.2 content inferior to 0.1%; an H.sub.2O or CO.sub.2, or H.sub.2O+CO.sub.2 content superior to 0.03%; a controlled dew point ranging from −50 to −15° C.; and a controlled concentration of CO+CO.sub.2 maintained below 2%, wherein all percentages are expressed in terms of volume; and wherein the atmosphere in the second section comprises a concentration of oxygen of between 0.1 and 5% by volume.

2. The method according to claim 1, wherein the dew point in the first section ranges from −30 to −15° C.

3. The method according to claim 1, wherein the strip is heated in the first section to between 650 and 750° C.

4. The method according to claim 1, wherein, in the second section, a mixture of oxygen and nitrogen is injected on each side of the strip with a concentration of oxygen in the mixture being comprised of between 0.1 and 5% in volume.

5. The method according to claim 1, wherein, in the second section, the temperature of the strip is maintained between 500 and 700° C.

6. The method according to claim 1, wherein a residence time of the strip in the second section is between 1 and 10 seconds.

7. The method according to claim 1, wherein, in the third section, the strip is heated up to a temperature of between 750 and 870° C.

8. The method according to claim 1, wherein, in the third section, the concentration of H.sub.2 is adjusted between 3% and 30% in volume.

9. The method according to claim 1, wherein, in the third section, the dew point is controlled to be between −50 and −5° C.

10. The method according to claim 1, wherein the H.sub.2O or CO.sub.2, or H.sub.2O+CO.sub.2 content is superior to 0.035%.

11. The method according to claim 3, wherein the strip is heated in the first section to between 650 and 700° C.

12. The method according to claim 4, wherein the mixture is comprised of between 0.5 and 2% in volume.

13. The method according to claim 8, wherein the concentration of H.sub.2 is adjusted between 5 and 20% in volume.

14. The method according to claim 9, wherein, in the third section, the dew point is controlled to be between −20 and −10° C.

15. The method according to claim 1, wherein the atmosphere in the second section comprises a concentration of oxygen of between 0.5 and 2% by volume.

16. The method according to claim 1, wherein the atmosphere in the second section comprises a concentration of oxygen of between 0.5 and 5% by volume.

17. The method according to claim 1, wherein, in the second section, a mixture of oxygen and an inert gas is injected on each side of the strip with a concentration of oxygen in the mixture being comprised of between 0.1 and 5% in volume.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The present invention will be described in even greater detail below based on the exemplary figures. The invention is not limited to the exemplary embodiments. Other features and advantages of various embodiments of the present invention will become apparent by reading the following detailed description with reference to the attached drawings which illustrate the following:

(2) FIG. 1 schematically represents an annealing furnace comprising three separated sections according to the invention. The incoming and outgoing flows through the different sections are also schematically represented.

(3) FIG. 2 represents according to the invention the control means for regulating the parameters of the atmosphere in the second section i.e. in the oxidation section.

DETAILED DESCRIPTION

(4) The present invention relates to a method for controlling the surface reactions on a steel strip running through a furnace comprising successively a first section, a second section and a third section, the atmosphere in the second and third sections being oxidizing and reducing respectively, wherein in the first section, the atmosphere is oxidizing to potentially form an iron oxide layer, said atmosphere having a H.sub.2 content inferior to 2%, a O.sub.2 content inferior to 0.1% and a H.sub.2O or CO.sub.2, or H.sub.2O+CO.sub.2 content superior to 0.03% and, preferably, superior to 0.035%, the percentages being expressed in volume.

(5) According to particular preferred embodiments, the method according to the invention further discloses at least one or a suitable combination of the following features: the dew point in the first section is controlled and ranges from −50 to −15° C. and, preferably, from −30 to −15° C.; the strip is heated in the first section between 600 and 750° C., preferably between 650 and 750° C. and, more preferably, between 650 and 700° C.; the concentration of CO+CO2 is controlled in the first section and maintained below 2% in volume; in the second section, a mixture of an oxidant medium and an inert gas is injected, said oxidant medium being oxygen and the concentration of oxygen in the mixture being comprised between 0.1 and 5% and preferably between 0.5 and 2% in volume; the mixture is injected with a flow ranging from 50 to 300 Nm3/h for each side of the strip; in the second section, the temperature of the strip is maintained between 500 and 700° C.; the residence time of the strip in the second section is comprised between 1 and 10 seconds; in the third section, the strip is heated up to a temperature comprises between 750 and 870° C.; in the third section, the concentration of H2 is adjusted between 3% and 30%, and preferably between 5 and 20% in volume; and in the third section, the dew point is controlled to be between −50 and −5° C. and, preferably, between −20 and −10° C.

(6) The present invention also relates to a furnace for carrying out the method as described above, said furnace comprising a first section, a second section and a third section located respectively in distinct casings, each section being provided with control means, wherein the first section is provided with means for controlling the dew point, the H2 content and the CO content.

(7) According to a particular embodiment, the first section of the furnace comprises a resistance heating, an inductive heating or a radiant tube heater.

(8) The invention aims to provide a method with process parameters adjusted to get an optimized wettability for alloyed steels. To this end, a furnace has been specifically developed. This furnace has different sections each located in a distinct casing comprising means to carefully control the atmosphere. The furnace is dedicated to anneal steel sheets to be coated by a liquid metal comprising Zn, Al or a combination of those two in various proportions with addition of Mg and Si in proportion higher than 0.1%. The furnace according to the invention can also be used in a continuous annealing line without hot-dip galvanizing facilities.

(9) As shown in FIG. 1, this furnace comprises three well-defined sections which are separated by efficient sealing devices. Well-defined means that each section is located in a casing having its own heat insulation, heating components if required and control means, the latter being means for controlling the dew point, the hydrogen content, the oxygen content, the carbon monoxide content and the temperature.

(10) The first section is a classical heating section comprising heating elements and rolls. It is designed with a technology well-known for the skilled person. In this section, it is essential to have an atmosphere slighting oxidizing to limit the risk of external oxidation of the alloying elements and potentially to start forming a Fe oxide in some cases. To this end, the H.sub.2 content is below 2%, the O.sub.2 level is below 0.1% but the H.sub.2O or CO.sub.2 content or the sum H.sub.2O and CO.sub.2 (H.sub.2O+CO.sub.2) is superior to 0.03% and preferably superior to 0.035% to obtain this atmosphere slightly oxidizing. The atmosphere is controlled in terms of H.sub.2, dew point and CO, the rest being inert gas. It is controlled with a H.sub.2 content below 2% as indicated above, a dew point between −50 and −15° C. and, preferably, between −30 and −15° C. Those target values are adjusted by injecting a mixture H.sub.2+N.sub.2 with a given proportion of hydrogen and by an eventual injection of steam if required. The sum CO and CO.sub.2 (CO+CO.sub.2) is maintained below 2% to avoid a combustion in the section. The strip is heated to a temperature between 600 and 750° C., preferably between 650 and 750° C., and more preferably between 650 and 700° C., said temperatures being measured by pyrometers.

(11) In the second section, a mixture of O.sub.2 and N.sub.2 is injected to form a controlled iron oxide layer on the surface of the steel sheet. The concentration of O.sub.2 ranges from 0.1 to 5% but, preferably, between 0.5 and 2%. This section can have various shapes like U shape which imposes to use one or 2 turn down roll(s), or to be straight without any rolls. The length of this chamber is calculated to have a residence time of the strip between 1 and 10 sec. This chamber can comprise heating elements if required but it is heat insulated. The oxidant medium which is mainly based on oxygen but can also comprise C02, can be injected in this chamber by specific devices as described in document EP 15162341. This atmosphere is injected on each side separately. It can be either fresh or recirculated, cold or heated. Preferably, the injected flow is recirculated by a fan. The reacted atmosphere from the chamber is sucked by a fan, the oxidant content is adjusted by a device adding some air according to the oxidant content desired. The temperature of this inert gas+oxidant mixture is adjusted preferably in the range of 500 and 700° C. by a heating element and is finally injected with a defined flow on each side of the strip. The volume injected depends on the chamber size but is typically superior to 50 Nm.sup.3/h and preferably between 100 and 300 Nm.sup.3/h per side for a 2 meter wide chamber. An example of means for controlling the atmosphere parameters in the second section is given in FIG. 2. To minimize the escape of the oxidant in the first and third parts of the furnace, the sealing system is preferably composed of two pairs of rolls with injection of and extraction of the atmosphere between the two pairs. Since this section has its own full casing, it is easy to install devices on each side of the strip to measure the oxide thickness on the running sheet. The control means can further comprise a scanning system to check if the oxide thickness is uniform.

(12) The third section of the furnace is similar to the first one and has the objective of heating the strip to the desired temperature, preferably between 750 and 870° C. The atmosphere in this section is composed of a gas able to reduce the iron oxide formed in the second chamber. The classical practice is to use H.sub.2 mixed with an inert gas. The concentration of H.sub.2 is adjustable between 3 and 30%, preferably between 5 and 20%, depending on the aimed reduction kinetics. The dew point in this section is controlled between −50 and −5° C. with a preferred range of −20 to −10° C. when high strength steels are processed. The control of the incoming and outgoing flows of inert+H.sub.2 gas in this section is based on the measurements of the pressure, H.sub.2 content and dew point in each section as well as the opening of the various valves to let escape the atmosphere and promote an eventual dilution. Finally, the atmosphere of this section is separated from the fourth section of the furnace which is the cooling section by dampers or similar like pair of rolls or baffle plate, to limit the exchange of this atmosphere with those of the next sections.

(13) While the invention has been illustrated and described in detail in the drawings and foregoing description, such illustration and description are to be considered illustrative or exemplary and not restrictive. It will be understood that changes and modifications may be made by those of ordinary skill within the scope of the following claims. In particular, the present invention covers further embodiments with any combination of features from different embodiments described above and below.

(14) The terms used in the claims should be construed to have the broadest reasonable interpretation consistent with the foregoing description. For example, the use of the article “a” or “the” in introducing an element should not be interpreted as being exclusive of a plurality of elements. Likewise, the recitation of “or” should be interpreted as being inclusive, such that the recitation of “A or B” is not exclusive of “A and B,” unless it is clear from the context or the foregoing description that only one of A and B is intended.

(15) While the invention has been illustrated and described in detail in the drawings and foregoing description, such illustration and description are to be considered illustrative or exemplary and not restrictive. It will be understood that changes and modifications may be made by those of ordinary skill within the scope of the following claims. In particular, the present invention covers further embodiments with any combination of features from different embodiments described above and below. Additionally, statements made herein characterizing the invention refer to an embodiment of the invention and not necessarily all embodiments.

(16) The terms used in the claims should be construed to have the broadest reasonable interpretation consistent with the foregoing description. For example, the use of the article “a” or “the” in introducing an element should not be interpreted as being exclusive of a plurality of elements. Likewise, the recitation of “or” should be interpreted as being inclusive, such that the recitation of “A or B” is not exclusive of “A and B,” unless it is clear from the context or the foregoing description that only one of A and B is intended. Further, the recitation of “at least one of A, B and C” should be interpreted as one or more of a group of elements consisting of A, B and C, and should not be interpreted as requiring at least one of each of the listed elements A, B and C, regardless of whether A, B and C are related as categories or otherwise. Moreover, the recitation of “A, B and/or C” or “at least one of A, B or C” should be interpreted as including any singular entity from the listed elements, e.g., A, any subset from the listed elements, e.g., A and B, or the entire list of elements A, B and C.

REFERENCE SYMBOLS

(17) (1) Annealing furnace (2) First section (3) Second section (4) Third section (5) Strip or sheet (6) Sealing roll