CN1046450C - Guide system for continuously cast metal - Google Patents

Abstract

The invention relates to a process and a continuous casting facility for the production of thin slabs, preferably of steel with a predetermined congealing thickness of (for example) 50 mm. In the said process, an optimal casting surface and internal quality, with minimal and predetermined congealing thickness and plant capacity, and thus minimal complexity of rolling material, is achieved by the optimal combination of such elements as the following: rolling of cast metal in the area of the casting guide (segment 0), cambered ingot mould with a cross-sectional area which increases from inlet to outlet, hydraulically driven lifting platform, casting powder and supply thereof, immersion discharge with specific flow cross section. Qualitative adjustment of these process and system parameters results in satisfactory supply of casting slag and circulation in the meniscus by comparison with a standard 200 mm thick slab. The conditions from the basin top to the meniscus have a direct effect on the superficial and interior quality of the casting and the reliability of the casting process.

Description

Produce the continuous casting facility and the method for rectangular thin plate base

The present invention relates to a kind of continuous casting facility and method of producing sheet billet.

By the prior art flat submersed nozzle of DE3709188A1 known applications for example.In addition, hydraulically powered lifting platform is habitually practised, its allow in addition in casting process by departing from sinusoidal vibration, change and select best hoisting depth, frequency and the shape of shaking of vibration.By the known molten condition rolling of for example DE3818077A1, in process of setting, reduce to pour into a mould thickness by it, with the strand internal soundness that is improved.

The conclusion that the evaluation prior art draws is, need solve many-sided problem in order to produce thin strand, and, too many from the influential total number of variable of whole continuous casting facility, so that the knowledge of normal expert is not nearly enough far away, and can not make excessive demands them, should may find a scheme the more or less useful scheme from numerous, it can bring gratifying result under the situation of the least possibleization expense.

The objective of the invention is, propose a kind of method and a kind of continuous casting facility, they can reach the thickness of thin strand regulation like this, promptly, in slag supply and the slab thickness optimum condition aspect reducing, in crystallizer and in guiding device frame, when molten condition rolling, reached.

For achieving the above object, press one aspect of the present invention, a kind of method of producing sheet billet is provided, it comprises the following steps:

-in the rectangle crystallizer of a vibration, carry out the cast of metal bath by means of a submersed nozzle, and observe the condition that is used for submersed nozzle and crystallizer $\frac{F_{\mathrm{ST}}}{F_{\mathrm{TA}}}\≤50$

F wherein _ST=solidify the strand cross section of slab,

F _TA=submersed nozzle outlet cross section,

-on metal bath, infeed covering slag, and, observe condition according to vibration height, the vibration shape and frequency that crystallizer moves

h _Slag〉=h _{Casting blank outer cover}

Wherein

h _{Casting blank outer cover}=casting blank outer cover is higher than the height of bath surface,

h _Slag=slag height,

-in the multi roll frame, directly below crystallizer, reduce the strand cross section by a plurality of steps, so that when reducing slab thickness continuously, form forced convection abreast for liquid strand is inner still, this convection current is corresponding to the effect of magnetic stirrer, at this moment, still be issued to the final thickness of strand for the situation of liquid core at the end of multi roll frame, and

-under still existing the situation of two-phase section, strand inside solidifies when reaching final thickness in multi roll frame exit.

Press another aspect of the present invention, a kind of continuous casting facility is provided: it

-submersed nozzle arranged, 1/50 of the strand cross section of its cross section 〉=solidify slab, its inserts in rectangle crystallizer, and crystallizer can freely be adjusted frequency with one, hoisting depth is connected with the vibrating device of the shape of shaking,

-there is a covering slag to infeed device; it links to each other with vibrating device with control device by measurement, and can infeed covering slag in the following manner according to vibration height, vibration mode and vibration frequency, promptly; abide by slag height 〉=casting blank outer cover and be higher than the height of bath surface, and

-a multi roll frame after pull-out direction is located at the rectangle crystallizer is arranged, it has a hydraulic means, can infinitely change the spacing of two opposed rollers by means of this device.

The present invention of explanation as an example below accompanying drawing is represented with example.

Wherein:

Fig. 1 is illustrated in the pouring condition in the crystallizer;

When Fig. 2 surface quality keeps identical with cast productivity ratio, with respect to thick 200 millimeters * wide 1000 millimeters slab, the relation of technical expense and slab thickness;

When Fig. 3 .1-3.3 surface quality keeps identical with slab thickness, with respect to thick 200 millimeters * wide 1000 millimeters slab, the relation of technical expense and poring rate;

Fig. 4 is with respect to thick 200 millimeters * wide 100 millimeters slab, the hydraulic characteristic of steel in crystallizer and the relation of slab thickness;

Fig. 5 continuous casting facility.

The test of carrying out in the scope of drawing up by the present invention shows that slab surface quality and slag guiding are in close relations.To this falcate metal bath surface, that is slag height (h _Slag) and the casting blank outer cover (h that the time in the molten bath, shows in crystallizer height ratio speed _{Casting blank outer cover}) coefficient having a great responsibility (Fig. 1).

Draw, lubricated and avoid blemish (the direct covering slag particle that exists is mainly with the form of oxide) under casting billet surface for the best, must satisfy following criterion

h _Slag〉=h _{Casting blank outer cover}(1)

Slag height h _SlagMain relevant with the thickness of crystallizer entrance cross-section, and casting blank outer cover height h _{Casting blank outer cover}Then main relevant with the hoisting depth of oscillation mould.

If consider h _SlagSize and the relation of it and crystallizer entrance cross-section thickness, relational expression is then arranged

It also can be described as the technological difficulties that must bring in the system, unexpectedly draws following result:

Be under 2.736 tons/minute the situation in predetermined cast productivity ratio, 200 millimeters slabs and 50 millimeters slabs that people will use always are made comparisons, and with its substitution relational expression (2), equal 1 for 200 millimeters slabs, and rise to 16.62 for 50 millimeters these values of slab, this situation as seen from Figure 2.That is to say, relational expression (2) and slab thickness be reduced to inverse ratio, this relation is followed an exponential curve.

If keep the cast fixed thickness to observe the variation of relational expression when improving poring rate, then as among Fig. 3 at a kind of 75/100 and 125 millimeter crystallizer represented, people can determine that this is a straight line with rising of less slope.

For relational expression (1) big influence is arranged because metal flows into the turbulent flow that crystallizer causes, and this turbulent flow often proceeds to bath surface and can cause fluctuation, in this case, crest can rise from the slag liquid level, thereby can cause interrupting lubricated.In addition, this turbulent flow and output and relevant at the thickness and the width of submersed nozzle outlet cross-section crystallizer.As the tolerance of turbulent flow, define by hydraulic characteristic, and can be expressed as following expression formula as the merchant of output and thickness

With respect to the slab of 200 millimeters thick, but the value of hydraulic characteristic Fig. 4 for example.Represent among the figure that bigger crystallizer thickness has obviously favourable hydraulic characteristic.

Relevant for turbulent flow, the following relationship formula is also significant $\frac{F_{\mathrm{ST}}}{F_{\mathrm{TA}}}\≤50------\left(4\right)$

In the formula: F _TA=submersed nozzle outlet cross-sectional area,

F _ST=solidify the strand cross section of slab.

In addition, the electromagnetic braking in the crystallizer zone has obviously reduced the turbulent flow in mould inner metal liquid face district.

By the above with by the pass that measures empirical tests be, for example be reduced to 50 millimeters from 100 millimeters during slab thickness in being chosen in crystallizer, difficulty is very big observing aspect the relational expression (1).In other words, except the difficulty aspect the metal conveying, may discharge enough protections hardly on small crystallizer entrance cross-section, slag is with lubricated established very huge casting billet surface, and adjusts relational expression (4) in addition.Otherwise, in crystallizer and thereby the slab thickness in horizontal inner metal liquid face when for example being 75 millimeters, just can improve poring rate need not to strengthen especially under the situation of expense.This causes drawing unexpected solution, promptly, keeping from crystallizer in the sheet billet pouring area is that constant is nonsensical to solidifying end (liquid core) slab thickness, and very simply be technically, the slab thickness of input milling train reduces by means of a molten condition rolling operation and reaches, multi roll frame (the 0th section) for example is designed to the clamp section for this reason, had proved already that it was favourable doing like this.

A kind of continuous casting facility as an example as seen from Figure 5, it includes whole feature of the present invention.

Symbol table

1 Q _{Covering slag}

2 powder T_li, powder/slag phase boundary

3 h _{Casting blank outer cover}, casting blank outer cover/bath surface height

4 h _Slag, the slag height

5 powder, the powder height

6 submersed nozzles

7 sedimentary deposits

Oxide flow in 8 slags

9 Vg=poring rates

10 Q _Slag=slag consumption

11 air

12 crystallizations circle, the liquid/solid steel

13 casting blank outer covers

14 vibrations (hoisting depth, frequency, shape is shaken)

15 copper coins

16 distributors

For example 250 * 45 millimeters of 17 submersed nozzles, external dimensions, for example 220 * 15 millimeters of inside dimensions

18 best protection slags

19 75 * 800-1600 millimeter, the slab specification in horizontal inner metal liquid face (falcate metal bath surface)

20 15 * 220 millimeters, flow cross section-submersed nozzle

21 fluid pressure type crystallizer transmission devices

22 F _ST/ F _TA≤ 50 F _ST=submersed nozzle outlet cross section

F _TA=solidify the strand cross section of slab

23 75 * 800-1600 millimeter, the slab specification in the crystallizer exit

24 hinges or hydraulic cylinder or analog

25 the 0th sections, for example be designed to clamp

26 hydraulic cylinders or analog

27 50 millimeters, the slab thickness after the molten condition rolling process

28 have the 1st of hydraulic regulating device or analog ... the n section

29 Vg _Maximum6 meters/minute

30 50 millimeters, the slab thickness of casting metal guiding device end.

Claims (4)

1. a method of producing sheet billet comprises the following steps:

-in the rectangle crystallizer of a vibration, carry out the cast of metal bath by means of a submersed nozzle, and observe the condition that is used for submersed nozzle and crystallizer $\frac{F_{\mathrm{ST}}}{F_{\mathrm{TA}}}\≤50$

F wherein _ST=solidify the strand cross section of slab,

F _TA=submersed nozzle outlet cross section,

-on metal bath, infeed covering slag, and, observe condition according to vibration height, the vibration shape and frequency that crystallizer moves

h _Slag〉=h _{Casting blank outer cover}

Wherein

h _{Casting blank outer cover}=casting blank outer cover is higher than the height (3) of bath surface,

h _Slag=slag height (4),

-in the multi roll frame, directly below crystallizer, reduce the strand cross section by a plurality of steps, so that when reducing slab thickness continuously, form forced convection abreast for liquid strand is inner still, this convection current is corresponding to the effect of magnetic stirrer, at this moment, still be issued to the final thickness of strand for the situation of liquid core at the end of multi roll frame, and

-under still existing the situation of two-phase section, strand inside solidifies when reaching final thickness in multi roll frame exit.

2. according to the described method of claim 1, it is characterized by: even in casting process, frequency, hoisting depth and the vibration mode of crystallizer motion can freely be selected.

3. implement continuous casting facility according to the described method of one of all claims in prostatitis:

-submersed nozzle, its cross section (F arranged _TAStrand cross section (the F of) 〉=solidify slab _ST) 1/50, its inserts in rectangle crystallizer, crystallizer can freely be adjusted frequency with one, hoisting depth is connected with the vibrating device of the shape of shaking,

-there is a covering slag to infeed device, it links to each other with vibrating device with control device by measurement, and can infeed covering slag in the following manner according to vibration height, vibration mode and vibration frequency,, abides by slag height (h that is _Slag) 〉=casting blank outer cover is higher than the height (h of bath surface _{Casting blank outer cover}), and

-a multi roll frame (25) after pull-out direction is located at the rectangle crystallizer is arranged, it has a hydraulic means (24,25), can infinitely change the spacing of two opposed rollers by means of this device.

4. according to the described continuous casting facility of claim 3, it is characterized by: the spacing of two adjacent rollers is chosen as, and is still obtaining a kind of stirring action for liquid strand is inner when predetermined slab thickness reduces.

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