CN108057725B - Control method of descaling system - Google Patents

Control method of descaling system Download PDF

Info

Publication number
CN108057725B
CN108057725B CN201711478455.4A CN201711478455A CN108057725B CN 108057725 B CN108057725 B CN 108057725B CN 201711478455 A CN201711478455 A CN 201711478455A CN 108057725 B CN108057725 B CN 108057725B
Authority
CN
China
Prior art keywords
descaling
frequency
30mpa
pump system
variable
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201711478455.4A
Other languages
Chinese (zh)
Other versions
CN108057725A (en
Inventor
金柏林
周孝廉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SUQIAN JINXIN STEEL ROLLING Co.,Ltd. OF NISCO
Original Assignee
Nanjing Iron and Steel Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nanjing Iron and Steel Co Ltd filed Critical Nanjing Iron and Steel Co Ltd
Priority to CN201711478455.4A priority Critical patent/CN108057725B/en
Publication of CN108057725A publication Critical patent/CN108057725A/en
Application granted granted Critical
Publication of CN108057725B publication Critical patent/CN108057725B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21BROLLING OF METAL
    • B21B45/00Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills
    • B21B45/04Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills for de-scaling, e.g. by brushing
    • B21B45/08Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills for de-scaling, e.g. by brushing hydraulically

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Control Of Positive-Displacement Pumps (AREA)

Abstract

The invention discloses a control method of a descaling system, and belongs to the technical field of steel smelting. By the control method of the descaling system, when the 30MPa variable-frequency descaling pump system is required to perform rough descaling and the 25MPa descaling pump system is required to perform system fine descaling, the electric valve is closed, and the descaling system can be divided into two sets of pressure systems to meet the use of a steel plate with high descaling requirement, so that the diversity of products and the high quality requirement of the surface of the products are ensured; when the 25MPa descaling pump system is only needed to perform fine descaling, the electric valve is opened, so that the 30MPa variable-frequency descaling pump system is communicated with the 25MPa descaling pump system, the 30MPa variable-frequency descaling pump provides 25MPa high-pressure descaling water through frequency conversion of a frequency converter, and the whole descaling system performs 25MPa pressure descaling to reduce energy consumption of field production.

Description

Control method of descaling system
Technical Field
The invention relates to a control method of a descaling system, and belongs to the technical field of steel smelting.
Background
The high-pressure water descaling is to spray high-pressure water from a high-pressure pipeline system through a nozzle of a collecting pipe to strike on a high-temperature billet, rapidly cool the billet by the high-pressure water to generate temperature difference between the scale and the billet body, mechanically descale the cracked scale on the surface, and then shovel the scale on the surface of the billet by the striking force generated by the high-pressure water.
The high-pressure centrifugal descaling system is mainly used for plate strip production, and has the advantages of long rolling time, more descaling passes, more descaling points on a rolling line and large descaling water consumption.
Disclosure of Invention
The invention aims to solve the technical problem that aiming at the defects in the prior art, the invention provides the control method of the descaling system, which can be divided into two sets of pressure systems to meet the use requirement of a steel plate with high descaling requirement, so as to ensure the diversity of products and the high quality requirement of the surface of the products, can switch the mode sharing system mode to reduce the energy consumption of field production, and achieve the purpose of reducing the initial project investment and daily production cost.
The technical scheme for solving the technical problems is as follows: a control method of a descaling system comprises a 30MPa variable-frequency descaling pump system and a 25MPa descaling pump system which are connected through electric valves, and comprises the following steps:
filtering the descaling water by a self-cleaning filter for later use;
⑵ before the 30MPa variable frequency descaling pump system and the 25MPa descaling pump system are started, the injection valves and the minimum flow valves of the two systems are respectively closed, the outlet output valves of the 30MPa variable frequency descaling pump and the 25MPa descaling pump are opened, the lowest liquid level valve and the pneumatic gate valve in front of the lowest liquid level valve are opened, water is firstly added to the energy accumulators of the two systems, when the energy accumulators add water to a set liquid level, the water adding is stopped, the lowest liquid level valves of the two systems are closed, and the outlet output valve of the pump is closed;
⑶, manually starting the high-pressure air compressors of the 30MPa variable-frequency descaling pump system and the 25MPa descaling pump system respectively, and supplying air to the energy accumulators, so that the air supply of the high-pressure air compressors is stopped after the internal pressure of the energy accumulators of the two systems reaches the set pressure;
⑷ 30MPa variable-frequency descaling pump system and 25MPa descaling pump system, respectively fully exhausting gas, opening a minimum flow valve, respectively starting the 30MPa variable-frequency descaling pump and the 25MPa descaling pump, and enabling the whole system to enter an automatic operation state;
⑸ when the 30MPa variable-frequency descaling pump system is needed to perform rough descaling and the 25MPa descaling pump system is needed to perform system fine descaling, the electric valve is closed;
A. when the steel billet reaches the descaling box, the 30MPa variable-frequency descaling pump system automatically opens the injection valve, and the energy accumulator of the 30MPa variable-frequency descaling pump system supplies water to a descaling point; when the liquid level of an energy accumulator of the 30MPa variable-frequency descaling pump system is lowered to a set value, water is supplied to the energy accumulator of the 30MPa variable-frequency descaling pump system and the energy accumulator of the 30MPa variable-frequency descaling pump system for descaling at the same time, an injection valve is automatically closed after descaling, the 30MPa variable-frequency descaling pump supplies water to the energy accumulator, the 30MPa variable-frequency descaling pump operates at a reduced speed after the pressure set value of the energy accumulator of the 30MPa variable-frequency descaling pump system is reached, and at the moment, the 30MPa variable-frequency descaling pump does not output flow;
B. when the steel billet reaches the rolling mill, the 25MPa descaling pump system prevents the pipeline from vibrating, a pre-filling water valve of the 25MPa descaling pump system is opened and delays for a certain time, the pre-filling water valve is closed, the 25MPa descaling pump system is opened, and an energy accumulator of the 25MPa descaling pump system supplies water for the rolling mill to descale;
⑹ when only 25MPa descaling pump system is needed for fine descaling;
an electric valve between the 30MPa variable-frequency descaling pump system and the 25MPa descaling pump system is opened, so that the 30MPa variable-frequency descaling pump system is communicated with the 25MPa descaling pump system, the 30MPa variable-frequency descaling pump provides 25MPa high-pressure descaling water through frequency conversion of a frequency converter, and the whole descaling system performs 25MPa pressure descaling.
The improvement of the technical scheme is as follows: if the liquid level of the energy accumulator in the descaling system reaches the lowest set value, the high-pressure liquid level meter transmits a signal to the control system, the control system automatically closes the lowest liquid level valve to prevent high-pressure gas from flowing into the pipeline, and the lowest liquid level valve has the function of a one-way valve, namely, high-pressure water only can enter the energy accumulator; when the water level of an energy accumulator in the descaling system is recovered to a normal state, the lowest liquid level valve is recovered to the normal state; and if the liquid level of the energy accumulator reaches the highest set value and the pressure value reaches the lower limit of the specified range, the control system gives an alarm, and the air compressor is manually started to supplement air to the energy accumulator.
The invention has the beneficial effects that:
the descaling pump station in the control method of the descaling system is divided into two sets of systems of 30MPa and 25MPa, the two sets of systems can be operated independently or can share the 25MPa system after being communicated through a valve, and the two sets of systems can be divided into two sets of pressure systems to meet the use of a steel plate with high descaling requirement, so that the diversity of products and the high quality requirement of the surface of the products can be ensured; and the mode can be switched to share the system mode to reduce the energy consumption of field production, thereby achieving the purpose of reducing the cost and saving the annual total price of the electric charge by about 205 ten thousand yuan.
Detailed Description
Example 1
The descaling system of the embodiment comprises a 30MPa variable-frequency descaling pump system and a 25MPa descaling pump system which are connected through electric valves, and the control method of the descaling system comprises the following steps:
⑴ filtering the water for descaling by a self-cleaning filter for later use;
⑵ before the 30MPa variable frequency descaling pump system and the 25MPa descaling pump system are started, the injection valves and the minimum flow valves of the two systems are respectively closed, the outlet output valves of the 30MPa variable frequency descaling pump and the 25MPa descaling pump are opened, the lowest liquid level valve and the pneumatic gate valve in front of the lowest liquid level valve are opened, water is firstly added to the energy accumulators of the two systems, when the energy accumulators add water to a set liquid level, the water adding is stopped, the lowest liquid level valves of the two systems are closed, and the outlet output valve of the pump is closed;
⑶, manually starting the high-pressure air compressors of the 30MPa variable-frequency descaling pump system and the 25MPa descaling pump system respectively, and supplying air to the energy accumulators, so that the air supply of the high-pressure air compressors is stopped after the internal pressure of the energy accumulators of the two systems reaches the set pressure;
⑷ 30MPa variable-frequency descaling pump system and 25MPa descaling pump system, respectively fully exhausting gas, opening a minimum flow valve, respectively starting the 30MPa variable-frequency descaling pump and the 25MPa descaling pump, and enabling the whole system to enter an automatic operation state;
⑸ when the 30MPa variable-frequency descaling pump system is needed to perform rough descaling and the 25MPa descaling pump system is needed to perform system fine descaling, the electric valve is closed;
A. when the steel billet reaches the descaling box, the 30MPa variable-frequency descaling pump system automatically opens the injection valve, and the energy accumulator of the 30MPa variable-frequency descaling pump system supplies water to a descaling point; when the liquid level of an energy accumulator of the 30MPa variable-frequency descaling pump system is lowered to a set value, water is supplied to the energy accumulator of the 30MPa variable-frequency descaling pump system and the energy accumulator of the 30MPa variable-frequency descaling pump system for descaling at the same time, an injection valve is automatically closed after descaling, the 30MPa variable-frequency descaling pump supplies water to the energy accumulator, the 30MPa variable-frequency descaling pump operates at a reduced speed after the pressure set value of the energy accumulator of the 30MPa variable-frequency descaling pump system is reached, and at the moment, the 30MPa variable-frequency descaling pump does not output flow;
B. when the steel billet reaches the rolling mill, the 25MPa descaling pump system prevents the pipeline from vibrating, a pre-filling water valve of the 25MPa descaling pump system is opened and delays for a certain time, the pre-filling water valve is closed, the 25MPa descaling pump system is opened, and an energy accumulator of the 25MPa descaling pump system supplies water for the rolling mill to descale;
⑹ when only 25MPa descaling pump system is needed for fine descaling;
an electric valve between the 30MPa variable-frequency descaling pump system and the 25MPa descaling pump system is opened, so that the 30MPa variable-frequency descaling pump system is communicated with the 25MPa descaling pump system, the 30MPa variable-frequency descaling pump provides 25MPa high-pressure descaling water through frequency conversion of a frequency converter, and the whole descaling system performs 25MPa pressure descaling.
If the liquid level of an energy accumulator in the descaling system reaches a lowest set value, a high-pressure liquid level meter transmits a signal to a control system, the control system automatically closes a lowest liquid level valve to prevent high-pressure gas from entering a pipeline, and the lowest liquid level valve has the function of a one-way valve, namely, high-pressure water only can enter the energy accumulator; when the water level of an energy accumulator in the descaling system is recovered to a normal state, the lowest liquid level valve is recovered to the normal state; and if the liquid level of the energy accumulator reaches the highest set value and the pressure value reaches the lower limit of the specified range, the control system gives an alarm, and the air compressor is manually started to supplement air to the energy accumulator.
The descaling system of the embodiment has two kinds of descaling pressure selection, the first mode is that two systems of 25MPa and 30MPa coexist, an intermediate pipeline is separated by an electric valve, 25MPa is used for descaling of a rolling mill, and 30MPa is used for rough descaling, so that the use of a steel plate with high descaling requirement can be met; the second mode is that an electric valve between 25MPa and 30MPa systems is opened, a 30MPa variable-frequency descaling pump system reduces the frequency and the speed, the two systems are combined into a whole, the same pressure grade (25 MPa pressure is used), and the mode can save energy.
The predicted annual economic benefit can reach 205 ten thousand yuan: 1. the electricity cost is saved by 3 degrees/ton, calculated according to 0.57 yuan per degree of electricity and 120 ten thousand tons per year of output, and the annual total saved cost is 205 ten thousand yuan.
In addition to the above embodiments, the present invention may have other embodiments. All technical solutions formed by adopting equivalent substitutions or equivalent transformations fall within the protection scope of the claims of the present invention.

Claims (2)

1. A control method of a descaling system is characterized in that: the descaling system comprises a 30MPa variable-frequency descaling pump system and a 25MPa descaling pump system which are connected through electric valves, and the control method of the descaling system comprises the following steps:
⑴ filtering the water for descaling by a self-cleaning filter for later use;
⑵ before the 30MPa variable frequency descaling pump system and the 25MPa descaling pump system are started, the injection valves and the minimum flow valves of the two systems are respectively closed, the outlet output valves of the 30MPa variable frequency descaling pump and the 25MPa descaling pump are opened, the lowest liquid level valve and the pneumatic gate valve in front of the lowest liquid level valve are opened, water is firstly added to the energy accumulators of the two systems, when the energy accumulators add water to a set liquid level, the water adding is stopped, the lowest liquid level valves of the two systems are closed, and the outlet output valve of the pump is closed;
⑶, manually starting the high-pressure air compressors of the 30MPa variable-frequency descaling pump system and the 25MPa descaling pump system respectively, and supplying air to the energy accumulators, so that the air supply of the high-pressure air compressors is stopped after the internal pressure of the energy accumulators of the two systems reaches the set pressure;
⑷ 30MPa variable-frequency descaling pump system and 25MPa descaling pump system, respectively fully exhausting gas, opening a minimum flow valve, respectively starting the 30MPa variable-frequency descaling pump and the 25MPa descaling pump, and enabling the whole system to enter an automatic operation state;
⑸ when the 30MPa variable-frequency descaling pump system is needed to be used for rough descaling and the 25MPa descaling pump system is needed to be used for fine descaling, the electric valve is closed;
A. when the steel billet reaches the descaling box, the 30MPa variable-frequency descaling pump system automatically opens the injection valve, and the energy accumulator of the 30MPa variable-frequency descaling pump system supplies water to a descaling point; when the liquid level of an energy accumulator of the 30MPa variable-frequency descaling pump system is lowered to a set value, water is supplied to the energy accumulator of the 30MPa variable-frequency descaling pump system and the energy accumulator of the 30MPa variable-frequency descaling pump system for descaling at the same time, an injection valve is automatically closed after descaling, the 30MPa variable-frequency descaling pump supplies water to the energy accumulator, the 30MPa variable-frequency descaling pump operates at a reduced speed after the pressure set value of the energy accumulator of the 30MPa variable-frequency descaling pump system is reached, and at the moment, the 30MPa variable-frequency descaling pump does not output flow;
B. when the steel billet reaches the rolling mill, the 25MPa descaling pump system prevents the pipeline from vibrating, a pre-filling water valve of the 25MPa descaling pump system is opened and delays for a certain time, the pre-filling water valve is closed, the 25MPa descaling pump system is opened, and an energy accumulator of the 25MPa descaling pump system supplies water for the rolling mill to descale;
⑹ when only 25MPa descaling pump system is needed for fine descaling;
an electric valve between the 30MPa variable-frequency descaling pump system and the 25MPa descaling pump system is opened, so that the 30MPa variable-frequency descaling pump system is communicated with the 25MPa descaling pump system, the 30MPa variable-frequency descaling pump provides 25MPa high-pressure descaling water through frequency conversion of a frequency converter, and the whole descaling system performs 25MPa pressure descaling.
2. The control method of a descaling system according to claim 1, wherein: when the descaling system is used, if the liquid level of the energy accumulator in the descaling system reaches the lowest set value, the high-pressure liquid level meter transmits a signal to the control system, the control system automatically closes the lowest liquid level valve to prevent high-pressure gas from flowing into a pipeline, and the lowest liquid level valve has the function of a one-way valve, namely, high-pressure water only can enter the energy accumulator; when the water level of an energy accumulator in the descaling system is recovered to a normal state, the lowest liquid level valve is recovered to the normal state; and if the liquid level of the energy accumulator reaches the highest set value and the pressure value reaches the lower limit of the specified range, the control system gives an alarm, and the air compressor is manually started to supplement air to the energy accumulator.
CN201711478455.4A 2017-12-29 2017-12-29 Control method of descaling system Active CN108057725B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711478455.4A CN108057725B (en) 2017-12-29 2017-12-29 Control method of descaling system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711478455.4A CN108057725B (en) 2017-12-29 2017-12-29 Control method of descaling system

Publications (2)

Publication Number Publication Date
CN108057725A CN108057725A (en) 2018-05-22
CN108057725B true CN108057725B (en) 2020-03-27

Family

ID=62140887

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711478455.4A Active CN108057725B (en) 2017-12-29 2017-12-29 Control method of descaling system

Country Status (1)

Country Link
CN (1) CN108057725B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110747939A (en) * 2019-10-18 2020-02-04 南京钢铁股份有限公司 Method for overhauling valve of high-pressure water system

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0625383B1 (en) * 1993-05-17 1998-02-25 DANIELI & C. OFFICINE MECCANICHE S.p.A. Line to produce strip and/or sheet
JPH09271832A (en) * 1996-04-08 1997-10-21 Nippon Steel Corp Descaling method of hot rolled ferritic stainless steel plate
CN100411763C (en) * 2005-12-09 2008-08-20 广东韶钢松山股份有限公司 High-pressure water descaling system
CN101559439A (en) * 2009-05-26 2009-10-21 广州金关节能科技发展有限公司 Energy-saving control method for multi-section descaling and control device thereof
CN103302117B (en) * 2013-06-21 2015-09-09 上海宝钢节能环保技术有限公司 A kind of frequency-changing control system of single pump de-scaling and control method thereof
CN103909103A (en) * 2014-02-12 2014-07-09 上海宝菱电气控制设备有限公司 Slab descaling pump system and method
CN105834232A (en) * 2015-01-15 2016-08-10 宝钢不锈钢有限公司 High-pressure water descaling intelligent energy-saving system and control method thereof

Also Published As

Publication number Publication date
CN108057725A (en) 2018-05-22

Similar Documents

Publication Publication Date Title
CN101559439A (en) Energy-saving control method for multi-section descaling and control device thereof
CN108057725B (en) Control method of descaling system
CN203686580U (en) Nitrogen supplementing system
CN101601419A (en) A kind of high-pressure water descaling technology and device
CN107964576B (en) A kind of vacuum pump system and its working method for VOD refining furnace
CN103909103A (en) Slab descaling pump system and method
CN203594974U (en) Pressure stabilizing and reclaiming device for high-pressure nitrogen
CN101497086B (en) High-pressure water descaling system
CN105234195A (en) Energy-saving steel rolling phosphorous spraying device
CN210601032U (en) Novel liquefied natural gas unloading system capable of being started quickly
CN111412389A (en) High-pressure variable frequency pump energy-saving device and control method thereof
CN111020092A (en) Pressure-equalizing energy recovery system for blast furnace hot blast stove and use method thereof
CN204099314U (en) The automatic thickness hydraulic control system of high low pressure independence split
CN205477788U (en) Gas pressure regulating facility residual pressure utilizes system
CN111014702B (en) Energy-saving system for gas atomization powder making equipment
CN203955734U (en) Medium plate control cooling side spraying system
CN210411931U (en) Water-saving device for water purification and circulation
CN202431484U (en) Automatic drainage device for air compressors
CN111715711B (en) Efficient descaling control method for hot-rolled strip production line
CN105964710A (en) High pressure water descaling device and descaling method
CN202199606U (en) Precision rolling low-flow descaling device
CN216113353U (en) Supply system of hydrogen production and hydrogenation integrated hydrogenation station
CN215696859U (en) Self-opening and closing type high-pressure water pump and high-pressure water system for steel billet descaling
CN105327942B (en) A kind of bar mill roll cooling water pipe valve commutation eliminates vibrational system
CN212839354U (en) High-pressure water storage tank

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20201230

Address after: 223801 Suyu Economic Development Zone, Suqian City, Jiangsu Province

Patentee after: SUQIAN JINXIN STEEL ROLLING Co.,Ltd. OF NISCO

Address before: Liuhe District of Nanjing City, Jiangsu province 210035 xiejiadian

Patentee before: Nanjing Iron&Steel Co.,Ltd.