METHOD FOR PRODUCING HOT-ROLLED SEAMLESS PIPES HAVING THICKENED ENDS
20170216896 · 2017-08-03
Assignee
Inventors
Cpc classification
B21B2271/02
PERFORMING OPERATIONS; TRANSPORTING
B21B27/024
PERFORMING OPERATIONS; TRANSPORTING
B21B23/00
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
A method for producing hot-rolled, seamless pipes having at least one wall thickening which can be arranged at any positions over the length of the pipe, wherein by means of a multiple-stand mandrel bar rolling mill, the rolls roll a hollow shell on a mandrel bar as an inner tool to a required nominal wall thickness and produce at specified positions over the length of the pipe a required wall thickening on the outer side of the pipe by opening the rolls in the rolling stands. The thickened wall is produced and finish-rolled by two rolling stands that are consecutive as seen in the rolling direction, in which the deviations of the finished contour of the thickening from an ideal circular cross-section are minimised, wherein the rolling stands located upstream are likewise opened as to avoid any contact of the rolls of these rolling stands with the previously produced thickening.
Claims
1. A method for producing hot-rolled, seamless pipes having at least one wall thickening which can be arranged at any positions over the length of the pipe, comprising rolling with rolls of a multiple-stand mandrel bar rolling mill having at least three rolling stands and at least two rolls per stand a hollow shell on a mandrel bar as an inner tool to a required nominal wall thickness and producing at specified positions over the length of the pipe a required wall thickening on the outer side of the pipe in comparison with the nominal wall thickness by opening the rolls in the rolling stands, wherein the thickened wall is produced and finish-rolled only by means of the two rolling stands, which are consecutive as seen in the rolling direction, at the specified positions, in which the deviations of the finished contour of the thickening from an ideal circular cross-section, which are produced by the roll contours when the rolls are being opened, are minimised, wherein the rolling stands located upstream thereof as seen in the rolling direction are likewise opened for a required wall thickness stepping of the rolling stands and all of the subsequent rolling stands are opened at least to such an extent as to avoid any contact of the rolls of these rolling stands with the previously produced thickening and thus any subsequent reduction of the produced wall thickening.
2. The method as claimed in claim 1, further comprising determining the two rolling stands which roll the wall thickening by test rolling procedures, wherein initially a pipe which does not have thickenings is rolled with the selected mandrel bar and in further test rolling procedures pipes which have wall thickenings are rolled with the same mandrel bar and the deviations of the finished contour of the produced wall thickening from the ideal circular cross-section are measured for the rolling parameters selected for this purpose and subsequently the two rolling stands which produce the smallest geometrical deviation in the finished contour from the ideal circular cross-section are selected.
3. The method as claimed in claim 1, further comprising establishing the two rolling stands which roll the wall thickening by means of a calculated evaluation parameter BWV,i, wherein the rolling stand having the smallest geometric deviation from an ideal circular cross-section in numerical terms and thus the smallest evaluation parameter BWV,i is selected as the first stand for finish-rolling of the wall thickening and the rolling stand arranged upstream thereof as seen in the rolling direction is selected as the second stand, wherein the evaluation parameter BWV,i is defined as follows:
BWV,i=|ev,i−1+ev,i| for i=2 to i-max where i=sequential number of the stand, starting with 1 and ascending in the rolling direction i-max=sequential number of the last stand wherein ev,i=centre point displacement of the groove base radius R1,i in comparison with the rolling axis (+=above rolling centre, −=below rolling centre during rolling of the thickened wall s-V) where
ev,i=eR,i+A,i, wherein eR,i=the centre point displacement of the groove base radius R1,i in comparison with the rolling axis (+=above rolling centre, −=below rolling centre) during rolling of the nominal pipe wall thickness s-R and A,i=theoretical opening dimension of stand i, in order to roll the thickened wall s-V in the groove base, where
A,i=s-V−s,i, wherein s,i=wall thickness in the groove base of stand i.
4. The method as claimed in claim 3, wherein in order to roll the nominal pipe wall thickness s-R at the exit of the mandrel bar rolling mill, the mandrel bar diameter DSTist is selected such that the deviations from an ideal circular cross-section, which are produced by the roll contours, with the nominal pipe wall thickness s-R of the last rolling stand are minimised and the mandrel bar diameter DSTist is established by a calculated evaluation parameter BWR for rolling the nominal pipe wall thickness which is defined as follows as a value:
BWR=|eR,i-max-1+eR,i-max| for i-max where i-max=sequential number of the last stand
5. The method as claimed in claim 1, further comprising extracting the mandrel bar from the pipe after rolling in the mandrel bar rolling mill and subsequently urging the wall thickenings on the outer side of the pipe to the inner side of the pipe by subsequent rolling so as to produce a pipe having a constant outer diameter over the entire length.
6. The method as claimed in claim 5, wherein the wall thickenings are urged completely to the inner side of the pipe by a mandrel bar extracting mill, which is located downstream of the mandrel bar rolling mill, or a stretch-reducing mill.
7. The method as claimed in claim 6, further comprising subsequently urging in part the wall thickenings from the inner side of the pipe to the outer side of the pipe by a calibrating press.
8. The method as claimed in claim 7, wherein the produced wall thickenings extend in the longitudinal direction of the pipe over a length of at least 300 mm.
9. The method as claimed in claim 1, wherein the produced wall thickenings extend in the longitudinal direction of the pipe over a length of at least 300 mm.
10. The method as claimed in claim 2, further comprising extracting the mandrel bar from the pipe after rolling in the mandrel bar rolling mill and subsequently urging the wall thickenings on the outer side of the pipe to the inner side of the pipe by subsequent rolling so as to produce a pipe having a constant outer diameter over the entire length.
11. The method as claimed in claim 10, wherein the wall thickenings are urged completely to the inner side of the pipe by a mandrel bar extracting mill, which is located downstream of the mandrel bar rolling mill, or a stretch-reducing mill.
12. The method as claimed in claim 11, further comprising subsequently urging in part the wall thickenings from the inner side of the pipe to the outer side of the pipe by a calibrating press.
13. The method as claimed in claim 3, further comprising extracting the mandrel bar from the pipe after rolling in the mandrel bar rolling mill and subsequently urging the wall thickenings on the outer side of the pipe to the inner side of the pipe by subsequent rolling so as to produce a pipe having a constant outer diameter over the entire length.
14. The method as claimed in claim 13, wherein the wall thickenings are urged completely to the inner side of the pipe by a mandrel bar extracting mill, which is located downstream of the mandrel bar rolling mill, or a stretch-reducing mill.
15. The method as claimed in claim 14, further comprising subsequently urging in part the wall thickenings from the inner side of the pipe to the outer side of the pipe by a calibrating press.
16. The method as claimed in claim 4, further comprising extracting the mandrel bar from the pipe after rolling in the mandrel bar rolling mill and subsequently urging the wall thickenings on the outer side of the pipe to the inner side of the pipe by subsequent rolling so as to produce a pipe having a constant outer diameter over the entire length.
17. The method as claimed in claim 16, wherein the wall thickenings are urged completely to the inner side of the pipe by a mandrel bar extracting mill, which is located downstream of the mandrel bar rolling mill, or a stretch-reducing mill.
18. The method as claimed in claim 17, further comprising subsequently urging in part the wall thickenings from the inner side of the pipe to the outer side of the pipe by a calibrating press.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0035]
[0036]
[0037]
[0038]
[0039]
[0040]
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0041]
[0042] When the rolls are being opened (see
[0043] If the roll 3 is closed (see
[0044] A roll gap which is smaller in the flank compared to the roll groove is critical as the circumferential speed of the roll increases from the groove base to the flank. In combination with the roll gap which becomes smaller towards the flank, this can result in the material on the flank being pulled thin which in an extreme case can produce holes.
[0045] In order to ensure that these deviations remain under control, the roll pass design is composed typically of two circular arcs.
[0046] Therefore, an exact circle is formed for a central displacement of e=0. However, in practice the angle alpha is selected to be slightly larger than half of the angle beta. However, this addition Delta alpha should not be greater than 5% of the angle beta.
[0047] The zero position of the rolls which is designated is the position at which the central displacement e corresponds to the desired value specified by the roll pass designer.
[0048] The minimum size of the factor C where R2=C×R1 for calculating the flank radius R2 from the base radius R1 is likewise deduced from geometric considerations. Even when the roll is being opened to the maximum intended extent, there should be no decrease in the wall thickness arriving at the flank, instead there should even be an air gap. Therefore, e.g. in the case of a three-roll mandrel bar rolling mill C-values greater than 2 are typical.
[0049]
[0050] In order to overcome the described problems which occur when opening the rolls for the purpose of producing wall thickenings, the geometries of the wall thickenings which are produced with the individual stands and the deviation thereof from an ideal circular cross-section are evaluated in accordance with the invention. Starting from the wall thicknesses in the groove base, at the exit of all of the stands it is established at which stands does the wall thickening fall short of the required wall thickening during rolling of the pipe.
[0051] The two stands which produce the smallest geometric deviations from a circle are then used for rolling the wall thickenings. The settings of the rolls of the remaining stands and the rolls of the stand which is first to fall short of the required wall thickening are then opened in a controlled manner. In accordance with the invention, this opening procedure must satisfy the following two criteria.
[0052] Criterion 1: the two selected stands finish-roll the desired thickened wall thickness in the groove base. They are opened accordingly. All remaining stands located upstream are likewise opened so as to produce a suitable wall thickness stepping per stand for the purpose of rolling the thickening. In this connection, the term “suitable” means that the decreases in wall thickness in the stands which are required for rolling the thickened wall are relatively similar to when the nominal pipe wall thickness is being rolled. All subsequent stands are opened to such an extent as to reliably avoid any contact of the rolls with the pipe at the location of the thickening and thus any subsequent reduction in the wall thickening produced.
[0053] Criterion 2: The stands responsible for finish-rolling of the wall thickening are determined by the evaluation parameter BWV,i. The smaller the evaluation parameter BWV,i, the more the final contour of the thickened pipe part to be achieved corresponds to an exact circular ring.
[0054] The following examples explain the selection of the stands for finish-rolling of the desired wall thickening.
Example 1
[0055] A mandrel bar rolling mill comprising 5 stands and 3 rolls per stand is used for elongation and rolling the wall thickening.
[0056] The following applies:
i=sequential number of the stand, starting with 1 and ascending in the rolling direction
i-max=sequential number of the last stand
number of stands=5
s-R=pipe wall thickness at the exit of the mandrel bar rolling mill
s-V=thickened wall
[0057] The following also applies for each stand i:
s,i=wall thickness in the groove base of stand i
e,i=eccentric displacement of the centre point of the groove base radius R1 to the zero position of the rolls in the stand i. The zero position of the rolls is the position which the roll pass designer has specified for establishing the groove contours, i.e. the specified groove contour and actual contour are identical when the rolls are in the zero position in the stand.
DSTideal=ideal mandrel bar diameter with which the pipe wall s-R is rolled when the roll position is in the zero position.
DSTist=mandrel bar diameter used for rolling of s-R
A-ges.=identical setting dimension for all roll positions, so that the pipe wall thickness s-R can be rolled with the actual mandrel bar diameter,
+=rolls are opened with respect to the zero position.
−=rolls are closed with respect to the zero position.
[0058] The opening and closing dimensions are defined as radial distances.
A-ges.=½×(DSTist−DSTideal)
eR,i=actual centre point displacement of the groove base radius R1,i in comparison with the rolling axis (+=above rolling centre, −=below rolling centre during rolling of the pipe wall s-R)
[0059] A,i—theoretical opening dimension of stand i, in order to roll the thickened wall in the groove base
A,i=s-V−s,i
ev,i=centre point displacement of the groove base radius R1,i in comparison with the rolling axis (+=above rolling centre, −=below rolling centre during rolling of the thickened wall s-V)
ev,i=eR,i+A,i
BWR=evaluation parameter for rolling the nominal pipe wall thickness in the form of an absolute value
BWR=|eR,i-max−1+eR,i-max| for i-max=5
BWV,i=evaluation parameter for rolling the thickened wall s-V in the form of an absolute value
BWV,i=|ev,i−1+ev,i| for i=2 to i-max (5)
MIN BWV,i=smallest value from the evaluation parameters BWV,i determined for all from the second stand with the respective sequential numbers i.
TABLE-US-00001 TABLE 1 Basic configuration of a 5-stand mandrel bar rolling mill and Examples 1 and 2 for rolling of thickenings Variant Basis Example 1 Example 2 s-R 10 10 10 s-V 11 11 DSTist DSTideal DSTideal DSTideal-2 A-ges 0 0 −1 Stand i s, i e, i eR, i A, i BWR ev, i BWV, i eR, i A, i BWR ev, i BWV, i 1 18.5 −3.0 −3.0 −7.5 −10.5 −4.0 −7.5 −11.5 2 14.0 −1.0 −1.0 −3.0 −4.0 14.5 −2.0 −3.0 −5.0 16.5 3 11.0 0.0 0.0 0.0 0.0 4.0 −1.0 0.0 −1.0 6.0 4 10.0 0.0 0.0 1.0 1.0 1.0 −1.0 1.0 0.0 1.0 5 10.0 0.0 0.0 1.0 0.0 1.0 2.0 −1.0 1.0 2.0 0.0 0.0 All dimensions in mm
TABLE-US-00002 TABLE 2 Basic configuration of a 5-stand mandrel bar rolling mill and Examples 3 and 4 for rolling of thickenings Variant Basis Example 3 Example 4 s-R 10 10 10 s-V 13 18 DSTist DSTideal DSTideal-2 DSTideal-3 A-ges 0 −1 −1.5 Stand i s, i e, i eR, i A, i BWR ev, i BWV, i eR, i A, i BWR ev, i BWV, i 1 18.5 −3.0 −4.0 −5.5 −9.5 −4.5 −0.5 −5.0 2 14.0 −1.0 −2.0 −1.0 −3.0 12.5 −2.5 4.0 1.5 3.5 3 11.0 0.0 −1.0 2.0 1.0 2.0 −1.5 7.0 5.5 7.0 4 10.0 0.0 −1.0 3.0 2.0 3.0 −1.5 8.0 6.5 12.0 5 10.0 0.0 −1.0 3.0 2.0 2.0 4.0 −1.5 8.0 3.0 6.5 13.0 All dimensions in mm
[0060] The starting position designated in Tables 1 and 2 as the basis shows the roll positions in the zero position, the mandrel bar used corresponds to the ideal mandrel bar for rolling a nominal pipe wall thickness of 10 mm at the exit of the mandrel bar rolling mill.
[0061] In Example 1 of Table 1, the thickened wall to be produced is 11 mm. Therefore, a wall thickening of 1 mm is to be produced. Since the mandrel bar used corresponds to the ideal mandrel bar, the roll setting in total (A-ges) is equal to zero and the centre point displacements eR,i are identical to the values for the zero position of the rolls. In order to roll a wall thickness of 11 mm, the rolls must be opened by 1 mm with respect to the nominal pipe wall thickness of 10 mm.
[0062] Stand 4 with a value of 1.0 has the numerically smallest value for the evaluation parameter MIN BWV,i, i.e. when the thickening is being rolled by stand 4, the smallest deviations from an ideal circular ring occur. Since stand 4 has the smallest value MIN BWV,i the thickening is finish-rolled with the stand 3 located upstream thereof in the rolling direction and the already determined stand 4, since the stand 4 produces, in terms of a finishing stand, a pipe with the smallest geometric deviations from an ideal circular ring.
[0063] Therefore, only the first 4 stands are required for producing the wall thickening, wherein the stands 3 and 4 finish-roll said wall thickness of 11 mm. Stand 5 is then only still required for rolling the nominal pipe wall thickness of 10 mm.
Example 2
[0064] In Example 2 of Table 1, in the case of a nominal pipe wall thickness of likewise 10 mm and a required wall thickening of 1 mm, rolling is performed with a mandrel bar which is 2 mm smaller in diameter, i.e. DSTideal minus 2 mm. In this case, a 0.0 is shown to be the most favourable evaluation MIN BWV,i for stand 5. Therefore, in this variant all 5 stands are required for rolling the thickening, wherein the last two stands, i.e. stands 4 and 5, finish-roll the thickening of 11 mm wall thickness.
Examples 3 and 4
[0065] Examples 3 and 4 of Table 2 show the situation for a thickened pipe wall of 13 or 18 mm with a nominal pipe wall thickness of likewise 10 mm. In this case, for a wall thickening to 13 mm (Example 3) only the first 3 stands are required, as the lowest BWV-value MIN BWV,i of 2.0 is achieved for stand 3. In Example 4 for a thickening of the pipe wall to 18 mm, stand 2 at 3.5 has the lowest BWV-value so that only the first two stands finish-roll the wall thickening.
[0066] It is also apparent from Table 2 that positive ev,i values cannot be avoided in all cases. Therefore, in theory ranges are also produced in which the target thickening cannot be achieved.
[0067] Since the contour of the rolls determines the outer contour of the pipe and the wall thickness is formed by the mandrel bar diameter, the absolute wall thickness deviations are always the same when the rolls are opened or closed. Therefore, when said rolls are opened by 1 mm, a wall thinning of about 0.13 mm is produced and when opened by 5 mm a wall is produced which is thinner by about 0.69 mm. When said rolls are closed by 1 mm, the maximum deviation is +0.14 mm. The relative values decrease more and more as the wall thickness increases. The illustration showing curves made up of straight line portions has only been selected for greater clarity.
[0068] Ultimately, the type of further processing and the method used for sizing the pipe ends determine the still tolerable wall thickness deviations.
[0069] In theory, the method described can be used to produce thickened walls which correspond at most to the hollow shell wall thickness. In the Examples in accordance with Table 1, the hollow shell wall thickness is 25 mm.
[0070] As described above, the mandrel bar diameter DSTist for achieving optimum roundness for rolling the nominal pipe wall thickness is established by means of a determined evaluation parameter BWR.
[0071] In Examples 1 and 2 of Table 1, with otherwise identical geometric specifications for the pipe to be rolled, the evaluation parameters BWR in Example 1 are calculated as 0.0 and in Example 2 as 2.0 by the formula BWR=|eR, imax-1+eR,imax| for i-max=5.
[0072] As described, the geometric deviations of the nominal pipe wall thickness from the ideal circular ring are smaller, the smaller the BWR value. In the present case, the mandrel bar diameter DSTideal in accordance with Example 1 would thus be selected.
[0073] However, the requirement of the wall thickness tolerances of the pipe, rolling technology aspects and the requirements of the wall thickness uniformity of the thickenings are to be weighed up against one another in order to establish the most suitable mandrel bar diameter and thus the BWR-value, and the BWV,i effective for the thickenings and thus the stands required for rolling the thickening.
[0074] Although a BWR-value of zero is theoretically the best, but due to the longitudinal tensile stresses in the flank region, negative eR,max and eR,imax-1 which lead to a BWR deviating from zero with simultaneous improvement of the BWV,i can represent the better solution. In practice, Example 2 with a mandrel bar diameter DSTist=DSTideal minus 2 mm with thin wall thicknesses where the longitudinal tension can be critical and thus delivers the better rolling results.
[0075] However, the mandrel bar must still be removed from the so-called continuous pipe, which is how the pipe is referred to after it has been rolled in the mandrel bar rolling mill. Typically, the pipe downstream of mandrel bar rolling mills having two rolls per stand is designated as the continuous pipe. However, in this case the term generally stands for a pipe which is rolled in mandrel bar rolling mills, irrespective of how many rolls are used per stand.
[0076] The mandrel bar can be removed from the continuous pipe by extracting it in the secondary flow via a chain after rolling. However, the common method is a so-called extracting mill which in the rolling line pulls the continuous pipe from the mandrel bar and advantageously can be used to displace the wall thickening located on the outer side of the pipe towards the inner side of the pipe.
[0077] For this purpose, three three-roll stands are generally used which at least reduce the diameter of the continuous pipe by about 2.5%. Removal of the pipe with the aid of the extracting mill commences as soon as the pipe head reaches the extracting mill. At this point in time, the rolling procedure in the mandrel bar rolling mill is not yet completed in most cases. The rolling procedure in the mandrel bar rolling mill ends at the latest when the mandrel bar head comes to a standstill just upstream of the extracting mill. Then, the extracting mill removes from the mandrel bar the remaining part of the pipe which is still located thereon.
[0078] The maximum values of the diameter reduction are about 4.5% in total across all three stands. If e.g. an 11 mm continuous pipe wall thickness is rolled and the thickening is intended to be 10 mm, this signifies an increase in the outer diameter reduction by 20 mm, which in the case of a 200 mm groove already constitutes 10%. Since the settings of the rolls of the extracting stands are generally not variable, it is necessary to adapt the roll pass design for larger wall thickenings. This has to be performed in such a manner that the minimum decrease for the filet part is effected only in at most two stands, preferably only in the last one. Therefore, the two front stands can each perform the additionally required diameter reduction which, however, should not exceed 4.5% per stand.
[0079] In a further variant, in order to extract the mandrel bar an extracting mill is not used and instead the mandrel bar is extracted by means of a sizing or stretch-reducing mill. In this case, extraction of the mandrel bar is simpler than in the case of the extracting mill, since depending on the thickening of the pipe ends, one or a plurality of additional stands merely have to be placed upstream of the stands required for reducing the filet parts. The pipe sections which have the nominal wall thickness are designated as the filet parts.
[0080] The diameter reduction in the extracting or stretch-reducing mill ensures that the thickenings are urged inwardly and the pipe externally has a constant outer diameter. This has the advantage that transportation of the pipes and also the heat treatment required in most cases can be performed without additional measures. However, it is likewise possible to distribute the wall thickening in any manner towards the outer side and inner side of the pipe.
[0081] When used in the production line for line or oil field pipes, the ends are then sized by means of a calibrating press or other suitable unit so as to produce a wall thickness progression of the pipe ends in accordance with the specifications. The forming required for this purpose and customer specification with regard to permitted deformations in the cold state and internal stresses can mean that the pipe ends must be preheated and/or also post-heated. Then, the further steps are conducted in order ultimately to produce the desired end product according to specification. The hydraulic pressure test which is prescribed in most cases is performed in each case depending on specification before or after sizing of the pipe ends.
[0082] Therefore, in order to produce thickened ends, the following procedure is adopted in accordance with the invention:
1. Specify the wall thickness progression at the pipe ends of the finished pipe and the tolerances to be observed prior to mechanical further processing, such as internal or external machining, threading or the like.
2. Specify the length range with the finished pipe wall, the filet part, and the tolerances to be observed.
3. Convert the wall thickness progression on the finished pipe into a wall thickness progression with a wall thickness increase towards the outside for the pipe in the run-out of the mandrel bar rolling mill, the continuous pipe, taking into account the stretching and change in wall thickness through the sizing or stretch-reducing mill and the extracting mill, if present, and the required crop cuts. The continuous pipe can optionally contain multiple lengths of the finished pipe.
4. Calculate the specifications for the roll setting of the individual stands to match the pre-calculated geometry progression of the continuous pipe in all of the stands, taking into account the introduced evaluation parameters BWV,i and BWR for determining the stands for finish-rolling of the desired thickening and the resulting geometry in the opened state as described above. Stands which are no longer required for rolling the thickening or the transition are opened to such an extent that in a reliable manner they no longer effect any wall deformation.
5. Calculate the cross-sections of the continuous pipe over the length with the associated surface areas at the exit of each stand.
6. Specify the desired exit speed of the continuous pipe downstream of the last stand. If the continuous pipe runs out at a constant speed, the roll rotational speeds of the extracting mill do not need to be regulated.
7. Calculate the roll settings over time for all stands in accordance with points 5 and 6.
8. Calculate the continuous pipe speeds over time at the run-out of each stand in accordance with point 7.
9. Calculate the roll rotational speeds over time for all stands.
10. Produce the adjustment specifications and data records required for controlling the mandrel bar rolling mill in order to control the roll settings and the roll rotational speeds.
11. Roll the hot-finished pipe in the sizing or stretch-reducing mill, in which all wall thickenings are now located on the inside as a result of the reduction in the outer diameter, and perform the required crop and partial cuts.
12. If required, temper the pipe and examine the mechanically-technological properties.
13. Perform non-destructive testing of the pipe according to specification.
14. Size the pipe ends, optionally with heating to avoid cold work hardening and internal stresses.
15. Perform the hydraulic pressure test and further steps to produce the end product according to specification.
LIST OF REFERENCE NUMERALS
[0083] 1 rolling axis [0084] 2 mandrel bar [0085] 3 roll