FIELD: metallurgy.
SUBSTANCE: crystalliser with core is transferred at rate of 0.75-0.95 of optimal calculated rate of building-up. When level of metal coincides with beginning of crystalliser broadening, rate is increased to 1.5-2.0 of calculated rate of building-up, facilitating higher position of level sensor relative to liquid metal within the range of 1.0-2.0 of height of broadening zone of crystalliser. There is maintained a cycle of the crystalliser motion with the core before beginning of withdrawal of a shrinkage cavity. Process of withdrawal of a consumable electrode and crystalliser beyond the slag bath is completed in 1.3-1.8 of time required for reaching a calculated mode of melting.
EFFECT: increased reliability of melting hollow ingot and facilitation of melted metal quality.
2 dwg
Title | Year | Author | Number |
---|---|---|---|
PROCEDURE FOR ELECTRIC-SLAG REMELTING | 2009 |
|
RU2424335C1 |
ELECTROSLAG MELTING PLANT AND METHOD OF ITS CONTROL | 2011 |
|
RU2486264C2 |
METHOD FOR ELECTROSLAG REMELTING | 2011 |
|
RU2487182C1 |
ELECTROSLAG MELTING PLANT FOR LARGE HOLLOW AND SOLID INGOTS | 2011 |
|
RU2456355C1 |
ELECTROSLAG REMELTING METHOD AND DEVICE FOR ITS IMPLEMENTATION | 2009 |
|
RU2448173C2 |
ELECTROSLAG REMELTING METHOD | 2011 |
|
RU2479649C1 |
ELECTROSLAG FURNACE | 2009 |
|
RU2424336C2 |
METHOD FOR CONTROL OVER LIQUID METAL OR SLAG BATH LEVEL IN MOULD AND DEVICE TO THIS END | 2011 |
|
RU2456118C1 |
ELECTROSLAG SURFACING METHOD FOR BILLET AND DEVICE FOR IMPLEMENTATION THEREOF | 2019 |
|
RU2730360C1 |
ELECTROSLAG REMELTING METHOD, AND DEVICE FOR ITS IMPLEMENTATION | 2012 |
|
RU2497959C1 |
Authors
Dates
2011-07-20—Published
2009-09-17—Filed