WO2023147719A1 - 一种冷轧退火炉保护气供气及循环利用方法 - Google Patents

一种冷轧退火炉保护气供气及循环利用方法 Download PDF

Info

Publication number
WO2023147719A1
WO2023147719A1 PCT/CN2022/112386 CN2022112386W WO2023147719A1 WO 2023147719 A1 WO2023147719 A1 WO 2023147719A1 CN 2022112386 W CN2022112386 W CN 2022112386W WO 2023147719 A1 WO2023147719 A1 WO 2023147719A1
Authority
WO
WIPO (PCT)
Prior art keywords
protective gas
annealing furnace
gas
rolling annealing
pressure
Prior art date
Application number
PCT/CN2022/112386
Other languages
English (en)
French (fr)
Inventor
胡学羽
夏朝晖
潘宏
吴炳成
刘孝清
王龙锋
施万玲
Original Assignee
中冶南方工程技术有限公司
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 中冶南方工程技术有限公司 filed Critical 中冶南方工程技术有限公司
Publication of WO2023147719A1 publication Critical patent/WO2023147719A1/zh

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/74—Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/26—Methods of annealing
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D9/00—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D9/00—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
    • C21D9/0006—Details, accessories not peculiar to any of the following furnaces
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • F27D17/008—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases cleaning gases
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00—Technologies related to metal processing
    • Y02P10/20—Recycling

Definitions

  • the invention belongs to the technical field of metallurgical cold rolling production, and in particular relates to a protective gas supply and recycling method for a cold rolling annealing furnace.
  • the cold rolling annealing furnaces of iron and steel metallurgical enterprises use high-purity hydrogen and high-purity nitrogen as protective gas, and the used protective gas is discharged as waste gas.
  • Metallurgical enterprises have invested more in the construction and operation of high-purity shielding gas production facilities, especially hydrogen production facilities, and the hydrogen production process will also produce some solid waste pollution; some types of annealing furnaces use high hydrogen content in the shielding gas, Discharging as waste gas is undoubtedly a great waste of resources.
  • the present invention aims to provide a protective gas supply and recycling method for a cold rolling annealing furnace to solve the above problems. For this reason, the concrete technical scheme that the present invention adopts is as follows:
  • a protective gas supply and recycling method for a cold-rolled annealing furnace which may include the following steps:
  • the gas storage tanks include nitrogen balloon tanks and hydrogen balloon tanks, and the gas is transported through corresponding tube bundle trailers respectively.
  • S2 is realized by controlling the pressure regulating valve and the flow regulating valve on the corresponding gas distribution branch pipe through the electronic control unit.
  • S3 is realized through the electronic control unit interlocking the electromagnetic switch valve on the pressure control main pipe of the shielding gas storage tank. Specifically, when the pressure of the shielding gas storage tank rises to the first set value, the electromagnetic switch valve is closed, and when the shielding gas The pressure of the storage tank drops to the second set value, and the electromagnetic switching valve opens.
  • the specific process of S5 is as follows: after the waste protective gas is recovered through the recovery buffer tank, it is pressurized by a pressurized fan and then enters the purification system for treatment to remove various impurities in it, and then transported to the protective gas storage tank through pipelines .
  • step: S6 In case of emergency, release all the gas in the protective gas circulation unit.
  • the present invention adopts the above-mentioned technical scheme, and has the beneficial effects that: the present invention combines the existing mature technology and proceeds from engineering reality to solve the whole system problem from the supply of component raw gas to the recovery and recycling of protective gas, reducing the waste The energy consumption and production cost of stove production have good application prospects.
  • Fig. 1 is the process flow chart of cold rolling annealing furnace protective gas supply and recycling system of the present invention
  • Fig. 2 is a flow chart of the protective gas supply and recycling method for the cold rolling annealing furnace of the present invention.
  • the terms “installation”, “installation”, “connection”, and “connection” should be understood in a broad sense, for example, it can be a fixed connection, It can also be a detachable connection or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediary, and it can be the internal communication of two components.
  • installation can be a fixed connection, It can also be a detachable connection or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediary, and it can be the internal communication of two components.
  • a protective gas supply and recycling system for a cold rolling annealing furnace may include a gas storage unit 1, a gas distribution unit 2, an electronic control unit 3 and a protective gas circulation unit 4, wherein the gas storage unit 1 mainly Used to supply and store raw material gases (for example, nitrogen and hydrogen) required by the system.
  • the gas storage unit 1 mainly Used to supply and store raw material gases (for example, nitrogen and hydrogen) required by the system.
  • External air is supplied to the gas storage unit, and the main facility of the gas storage unit 1 is a high-pressure spherical tank (ie, a nitrogen balloon tank 11 and a hydrogen balloon tank 12). Nitrogen and hydrogen are supplied externally, and can be transported in various ways (pipeline transportation, tank truck transportation, etc.), and the use of tube bundle trucks in Figure 1 is only for illustration.
  • the raw material (high-purity) nitrogen and hydrogen supplied by the tube bundle car are transported to the gas storage unit 11.
  • the gas supply is intermittent (periodical) gas supply, which can be manually controlled. When it reaches the gas storage tank (nitrogen balloon tank 11 and hydrogen Spherical tank 12) When the pressure is set, the external air supply stops.
  • the gas distribution unit 2 is mainly used to provide different proportions of nitrogen-hydrogen mixed gas (ie, protective gas) required by users of the cold rolling annealing furnace.
  • the main facilities of the gas distribution unit 2 are nitrogen and hydrogen pipeline facilities, including a flow regulating valve 21, a pressure regulating valve 22, a flow meter 23, a pressure gauge 24, and the like.
  • Nitrogen-hydrogen mixed gas is deployed according to user requirements, and check valves are installed in each branch to prevent gas backflow.
  • An electromagnetic switching valve 25 is installed on the mixing main pipe, and its action is interlocked with the rear downstream gas pressure (for example, the pressure of the protective gas storage tank 40 ) signal.
  • the gas distribution unit 2 outputs nitrogen-hydrogen mixed gas according to the user's requirements of the cold rolling annealing furnace.
  • the mixed flow value is set to be small.
  • the flow rate will be gradually increased after the system is in normal operation.
  • the flow rate value of the mixed gas stably output by the gas distribution unit 2 is greater than the actual demand of the user, and the remaining gas enters the protective gas storage tank 40 for storage.
  • the main function of the shielding gas circulation unit 4 is to realize the recovery, purification and recycling of the shielding gas, which includes a shielding gas storage tank 40, a pressure regulating facility 41, a recovery buffer tank 42, a pressurized fan 43 and a purification system 44, etc.
  • the type, volume and design pressure of the shielding gas storage tank 40 are determined according to actual needs. After the shielding gas storage tank 40 starts receiving gas, it has the ability to send gas downstream. When the protective gas flow rate from the upstream gas distribution unit 2 is greater than the demand of the downstream annealing furnace, a part of the gas enters the protective gas storage tank 40 for storage.
  • the outlet of the shielding gas storage tank 40 is equipped with 2-way pressure regulating facilities 41, the working system is one for use and one for standby, and its function is to provide low-pressure shielding gas that meets the requirements of the annealing furnace.
  • the pressure regulating facility 41 is composed of a pressure regulating valve and a pressure gauge, wherein the pressure regulating valve is arranged on the branch pipe, and the pressure gauge is arranged on the main pipeline connected to the cold rolling annealing furnace.
  • the waste protective gas used in the annealing furnace passes through the buffer tank 42, and then pressurized by the pressurized fan 43, and then enters the purification system 44 for treatment to remove various impurities (such as emulsion, water and oxygen, etc.), and then passes through
  • the pipeline is recovered to the protective gas storage tank 40 for recycling. That is, all technical parameters of the shielding gas at the outlet of the purification system 44 can meet the requirements for recycling.
  • the pressurizing blower 43 may be commercially available.
  • the outlet pipeline of the purification system 44 is provided with a cut-off valve and a one-way check valve. As the core facility of the recycling unit, the purification system 44 is a relatively mature complete set of equipment, which will not be repeated here.
  • the shielding gas circulation unit 4 is also provided with a release pipe and a release valve for releasing the exhaust gas of the shielding gas under emergency conditions, and the release valve is in a closed state under normal conditions.
  • the electronic control unit 3 is provided with an electrical control system and an instrument signal system.
  • the instrument signal system gathers the detection signals set by the whole system of the present invention, outputs the control signals after program analysis and comparison, and the electrical control system regulates and controls each regulating valve and solenoid valve set up in the whole system.
  • the electronic control unit 3 is a control system based on PLC, and its configuration and program can be designed and developed according to actual process requirements.
  • a cold rolling annealing furnace protective gas supply and recycling method of the present invention may include the following steps:
  • the pressures PN and PH are set for the raw gas storage tanks of the gas storage unit (ie, the nitrogen balloon tank 11 and the hydrogen balloon tank 12).
  • the gas supply pressure reaches the design value during the initial commissioning, the external gas transmission will stop.
  • the pressure values PN and PH of the storage tank of the gas storage unit are lower than the set values, the system will send out an alarm prompt.
  • the gas storage unit also needs to be replenished according to the gas loss of the downstream unit.
  • the gas distribution system adjusts the pressure of the raw gas from the gas storage unit, and the background program performs precise ratio feedback adjustment according to the parameters fed back by the flow detection signal.
  • the mixed nitrogen-hydrogen mixed gas meets the downstream pressure and component ratio requirements. Due to the adjustment of the working conditions, the annealing furnace user needs to change the ratio of nitrogen and hydrogen in the protective gas. It is necessary to analyze the ratio and total amount of nitrogen and hydrogen in the existing protective gas storage tank, and issue an action command to the nitrogen or hydrogen branch control valve of the gas distribution unit to make up for it separately. gas. Or in an emergency, all the gas in the protective gas circulation unit is released, and re-input according to the user's requirements.
  • waste protective gas used in the cold rolling annealing furnace is recovered by the buffer tank 42, and then pressurized by the pressurized fan 43, and then enters the purification system 44 for treatment to remove various impurities (such as emulsion, moisture and oxygen, etc.) ), and then recovered to the protective gas storage tank 40 through pipelines for recycling.
  • impurities such as emulsion, moisture and oxygen, etc.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Furnace Details (AREA)

Abstract

本发明涉及一种冷轧退火炉保护气供气及循环利用方法，其可包括以下步骤：S1.对保护气的各储气罐进行输气，使其达到预设压力；S2.通过电控单元根据冷轧退火炉的实际需求进行气体混合配比；S3.将混合配比后的保护气根据保护气压力补充至保护气储罐；S4.在保护气储罐出口设置1用1备的两路调压设施，以提供满足冷轧退火炉要求的低压保护气；S5.通过保护气循环单元将冷轧退火炉使用后的废保护气回收至保护气储罐。本发明结合现有成熟的工艺技术，从工程实际出发，解决了从组分原料气的供应到保护气回收循环利用的全系统问题，降低退火炉生产的能耗和生产成本，具有较好的应用前景。

Description

一种冷轧退火炉保护气供气及循环利用方法 技术领域
本发明属于冶金冷轧生产技术领域，具体地涉及一种冷轧退火炉保护气供气及循环利用方法。
背景技术
钢铁冶金企业冷轧退火炉采用高纯氢气、高纯氮气作为保护气，使用后的保护气作为废气排放。冶金企业在高纯保护气的制气设施尤其是制氢设施的建设及运行上投入较多，制氢过程也会产生一些固废污染；部分类型退火炉使用的保护气中氢气含量较高，作为废气排放无疑是对资源的极大浪费。
近年来随着国家节能环保政策要求的提高，行业内对保护气回收循环利用技术的研究也逐渐加强。本申请由此产生。
发明内容
本发明旨在提供一种冷轧退火炉保护气供气及循环利用方法，以解决上述问题。为此，本发明采用的具体技术方案如下：
一种冷轧退火炉保护气供气及循环利用方法，其可包括以下步骤：
S1.对保护气的各储气罐进行输气，使其达到预设压力；
S2.通过电控单元根据冷轧退火炉的实际需求进行气体混合配比；
S3.将混合配比后的保护气根据保护气储罐压力补充至保护气储罐；
S4.在保护气储罐出口设置1用1备的两路调压设施，以提供满足冷轧退火炉要求的低压保护气；
S5.通过保护气循环单元将冷轧退火炉使用后的废保护气回收至保护气储 罐。
进一步地，在S1中，储气罐包括氮气球罐和氢气球罐，分别通过相应管束拖车输气。
进一步地，S2通过电控单元控制相应配气支管上的压力调节阀和流量调节阀实现。
进一步地，S3通过电控单元联锁保护气储罐压力控制主管上的电磁开关阀实现，具体地，当保护气储罐压力升至第一设定值，电磁开关阀关闭，以及当保护气储罐压力降至第二设定值，电磁开关阀打开。
进一步地，S5的具体过程为：将废保护气通过回收缓冲罐回收后，再经加压风机加压后进入净化系统处理，脱除其中的各种杂质，再通过管道输送至保护气储罐。
进一步地，还包括步骤：S6.在紧急情况下，将保护气循环单元中的气体全部放散。
本发明采用上述技术方案，具有的有益效果是：本发明结合现有成熟的工艺技术，从工程实际出发，解决了从组分原料气的供应到保护气回收循环利用的全系统问题，降低退火炉生产的能耗和生产成本，具有较好的应用前景。
附图说明
为进一步说明各实施例，本发明提供有附图。这些附图为本发明揭露内容的一部分，其主要用以说明实施例，并可配合说明书的相关描述来解释实施例的运作原理。配合参考这些内容，本领域普通技术人员应能理解其他可能的实施方式以及本发明的优点。图中的组件并未按比例绘制，而类似的组件符号通常用来表示类似的组件。
图1是本发明的冷轧退火炉保护气供气及循环利用系统的工艺流程图；
图2是本发明的冷轧退火炉保护气供气及循环利用方法的流程图。
具体实施方式
需要说明的是，下述实施方案中所述实验方法，如无特殊说明，均为常规方法，所述试剂和材料，如无特殊说明，均可从商业途径获得；在本申请的描述中，术语“横向”、“纵向”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系，仅是为了便于描述本发明和简化描述，并不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作，因此不能理解为对本发明的限制。
此外，术语“水平”、“竖直”、“悬垂”等术语并不表示要求部件绝对水平或悬垂，而是可以稍微倾斜。如“水平”仅仅是指其方向相对“竖直”而言更加水平，并不是表示该结构一定要完全水平，而是可以稍微倾斜。
在本申请的描述中，还需要说明的是，除非另有明确的规定和限定，术语“设置”、“安装”、“相连”、“连接”应做广义理解，例如，可以是固定连接，也可以是可拆卸连接，或一体地连接；可以是机械连接，也可以是电连接；可以是直接相连，也可以通过中间媒介间接相连，可以是两个元件内部的连通。对于本领域的普通技术人员而言，可以具体情况理解上述术语在本申请中的具体含义。
现结合附图和具体实施方式对本发明进一步说明。
如图1所示，一种冷轧退火炉保护气供气及循环利用系统可包括储气单元1、配气单元2、电控单元3和保护气循环单元4，其中，储气单元1主要用于提供 及存储系统所需的原料气体(例如，氮气和氢气)。外部供气至储气单元，储气单元1的主要设施为高压球罐(即，氮气球罐11和氢气球罐12)。氮气和氢气由外部供应，可采用多种方式(管道输送、槽车运输等)，图1中采用管束车仅为示意。由管束车供应的原料(高纯)氮气和氢气输送至储气单元11，该供气为间断性(周期性)供气，可采用人工控制，当达到储气罐(氮气球罐11和氢气球罐12)设定压力时，外部供气停止。
配气单元2主要用于提供冷轧退火炉用户所需的不同比例的氮氢混合气(即，保护气)。配气单元2的主要设施为氮氢管线设施，包括流量调节阀21、压力调节阀22、流量计23、压力计24等。根据用户要求进行调配氮氢混合气，各支路装有止回阀，以防止气体回流。混合总管上装有电磁开关阀25，其动作与后下游气体压力(例如，保护气储罐40的压力)信号联锁。配气单元2按冷轧退火炉用户要求输出氮氢混合气，初始时由于可能存在的混合误差，设定混合流量值较小。当输出氮氢混合气比例稳定，系统正常运行后逐渐加大流量。配气单元2稳定输出的混合气流量值大于用户实际需求，剩余部分气体进入保护气储罐40储存。
保护气循环单元4主要功能为实现保护气回收净化及循环利用，其包括保护气储罐40、调压设施41、回收缓冲罐42、加压风机43及净化系统44等。保护气储罐40的型式、容积及设计压力根据实际需要确定。保护气储罐40受气开始后，即具备往下游送气能力。当来自上游配气单元2的保护气流量大于下游退火炉需求，一部分气体进入保护气储罐40储存。保护气储罐40的出口设有2路调压设施41，工作制度为1用1备，其功能在于提供满足退火炉要求的低压保护气。调压设施41由压力调节阀和压力计组成，其中，压力调节阀设置在支管上，压力计设置在连接至冷轧退火炉的总管线上。经退火炉使用后的废 保护气经缓冲罐42、再经加压风机43加压后进入净化系统44处理，脱除其中的各种杂质(例如，乳化液、水分和氧气等)，再通过管道回收至保护气储罐40进行循环利用。即，净化系统44出口的保护气的各项技术参数均能满足再循环使用的要求。加压风机43可以是市场上可购得的。优选地，净化系统44的出口管线上设有切断阀门及单向止回阀。作为循环利用单元的核心设施，净化系统44为较为成熟的成套设备，这里不再赘述。
此外，保护气循环单元4还设有放散管和放散阀，用于紧急工况下的保护气废气放散，正常工况下该放散阀处于关闭状态。
电控单元3设有电气控制系统及仪表信号系统。仪表信号系统将本发明全系统所设的检测信号集中，经程序分析比对后输出控制信号，电气控制系统对全系统所设各调节阀、电磁阀等进行调节控制。电控单元3为基于PLC的控制系统，其配置和程序可根据实际工艺要求设计开发。
如图2所示，基于图1所示的冷轧退火炉保护气供气及循环利用系统，本发明的一种冷轧退火炉保护气供气及循环利用方法可包括以下步骤：
S1.对保护气的各储气罐进行输气，使其达到预设压力。具体地，根据用户(冷轧退火炉)消耗需求，对储气单元的原料气储罐(即，氮气球罐11和氢气球罐12)设定压力P N、P H。初始投运时供气压力达到设计值时，外部输气停止。当储气单元储罐的压力值P N、P H低于设定值时，系统发出报警提示，此时储气单元也需根据下游单元气体损失进行补充。
S2.通过电控单元根据冷轧退火炉的实际需求进行气体混合配比。具体地，根据下游工序要求的设计压力值，配气系统对来自储气单元的原料气进行压力调节，根据流量检测信号反馈的参数，后台程序进行精准配比反馈调节。混合后的氮氢混合气体满足下游压力及组分比例要求。退火炉用户由于工况调整， 对保护气氮氢比例需求变化，需对现有保护气储罐中氮氢比例及总量进行分析，对配气单元氮气或氢气支管调节阀发出动作指令单独补气。或紧急情况下，保护气循环单元气体全部放散，按照用户要求重新输入。
S3.将混合配比后的保护气根据保护气储罐压力补充至保护气储罐。随着配气单元2持续输出混合氮氢保护气的进行，保护气储罐40内气体逐渐增多，储气罐40的压力也不断升高。当达到第一设定值P NH-1时，配气单元2的电磁开关阀25关闭，配气单元2停止供气，循环单元具备独立运行条件开始工作。在保护气循环利用过程中，系统存在不可避免的气体泄漏。经过一段时间运行，保护气储罐40内压力不断降低。当储气压力降至第二设定值P NH-2时，配气单元2的电磁开关阀25打开，保护气储罐40接受上游补气。当储气压力达到P NH-1时，电磁阀再次关闭。此过程在循环利用过程中周期性出现。
S4.在保护气储罐出口设置1用1备的两路调压设施，以提供满足冷轧退火炉要求的低压保护气。通过保护气储罐40和调压设施41，使整个保护气系统的压力保持稳定。
S5.通过保护气循环单元将冷轧退火炉使用后的废保护气回收至保护气储罐。具体地，经退火炉使用后的废保护气经缓冲罐42回收、再经加压风机43加压后进入净化系统44处理，脱除其中的各种杂质(例如，乳化液、水分和氧气等)，再通过管道回收至保护气储罐40进行循环利用。
S6.在紧急情况下，将保护气循环单元中的气体全部放散，以确保系统安全。
尽管结合优选实施方案具体展示和介绍了本发明，但所属领域的技术人员应该明白，在不脱离所附权利要求书所限定的本发明的精神和范围内，在形式上和细节上可以对本发明做出各种变化，均为本发明的保护范围。

Claims (6)

  1. 一种冷轧退火炉保护气供气及循环利用方法，其特征在于，包括以下步骤：
    S1.对保护气的各储气罐进行输气，使其达到预设压力；
    S2.通过电控单元根据冷轧退火炉的实际需求进行气体混合配比；
    S3.将混合配比后的保护气根据保护气储罐压力补充至保护气储罐；
    S4.在保护气储罐出口设置1用1备的两路调压设施，以提供满足冷轧退火炉要求的低压保护气；
    S5.通过保护气循环单元将冷轧退火炉使用后的废保护气回收至保护气储罐。
  2. 如权利要求1所述的冷轧退火炉保护气供气及循环利用方法，其特征在于，在S1中，储气罐包括氮气球罐和氢气球罐，分别通过相应管束拖车输气。
  3. 如权利要求1所述的冷轧退火炉保护气供气及循环利用方法，其特征在于，S2通过电控单元控制相应配气支管上的压力调节阀和流量调节阀实现。
  4. 如权利要求1所述的冷轧退火炉保护气供气及循环利用方法，其特征在于，S3通过电控单元联锁保护气储罐压力控制主管上的电磁开关阀实现，具体地，当保护气储罐压力升至第一设定值，电磁开关阀关闭，以及当保护气储罐压力降至第二设定值，电磁开关阀打开。
  5. 如权利要求1所述的冷轧退火炉保护气供气及循环利用方法，其特征在于，S5的具体过程为：将废保护气通过回收缓冲罐回收后，再经加压风机加压后进入净化系统处理，脱除其中的各种杂质，再通过管道输送至保护气储罐。
  6. 如权利要求1所述的冷轧退火炉保护气供气及循环利用方法，其特征在于，还包括步骤：S6.在紧急情况下，将保护气循环单元中的气体全部放散。
PCT/CN2022/112386 2022-02-07 2022-08-15 一种冷轧退火炉保护气供气及循环利用方法 WO2023147719A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202210115750.8A CN114540598A (zh) 2022-02-07 2022-02-07 一种冷轧退火炉保护气供气及循环利用方法
CN202210115750.8 2022-02-07

Publications (1)

Publication Number Publication Date
WO2023147719A1 true WO2023147719A1 (zh) 2023-08-10

Family

ID=81673853

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2022/112386 WO2023147719A1 (zh) 2022-02-07 2022-08-15 一种冷轧退火炉保护气供气及循环利用方法

Country Status (2)

Country Link
CN (1) CN114540598A (zh)
WO (1) WO2023147719A1 (zh)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114540598A (zh) * 2022-02-07 2022-05-27 中冶南方工程技术有限公司 一种冷轧退火炉保护气供气及循环利用方法

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06306454A (ja) * 1993-04-21 1994-11-01 Sumitomo Metal Ind Ltd 熱処理炉雰囲気ガスの再利用方法
US20040134348A1 (en) * 2003-01-13 2004-07-15 Ati Properties, Inc. (A Delaware Corporation) Hydrogen reclamation apparatus and method
CN101956061A (zh) * 2010-07-27 2011-01-26 苏州品源气体设备有限公司 钟罩式光亮退火炉保护气回收循环利用工艺及其装置
CN110699526A (zh) * 2019-10-18 2020-01-17 甘肃酒钢集团宏兴钢铁股份有限公司 热镀锌立式退火炉上下炉压检测氮气联锁控制系统操作方法
CN110819772A (zh) * 2019-10-28 2020-02-21 鞍钢股份有限公司 一种连续退火炉氮氢保护气控制方法
CN111589299A (zh) * 2020-05-14 2020-08-28 中冶南方工程技术有限公司 一种轧钢退火炉的氮氢保护气分离系统及方法
CN112941287A (zh) * 2021-01-26 2021-06-11 中冶南方工程技术有限公司 冷轧退火炉废氢回收利用系统及冷轧退火炉氢气供应系统
CN114540598A (zh) * 2022-02-07 2022-05-27 中冶南方工程技术有限公司 一种冷轧退火炉保护气供气及循环利用方法

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100905113B1 (ko) * 2002-11-08 2009-06-30 주식회사 포스코 냉연공정에 이용되는 탈산 질소가스제어장치 및 제어방법
CN204193872U (zh) * 2014-11-14 2015-03-11 成都森乐化工科技有限公司 一种退火炉保护气的制备系统
CN104846159B (zh) * 2015-06-01 2017-05-10 苏州苏净保护气氛有限公司 一种具有保护气回收功能的连续退火炉
CN108690905B (zh) * 2017-04-07 2020-01-10 江油立航金属材料有限公司 不锈钢热处理保护气循环系统
CN108690904B (zh) * 2017-04-07 2020-01-10 江油立航金属材料有限公司 不锈钢热处理保护气循环利用方法
CN108546809A (zh) * 2018-06-29 2018-09-18 鞍钢集团工程技术有限公司 一种用于冷轧退火氮氢回收系统及方法

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06306454A (ja) * 1993-04-21 1994-11-01 Sumitomo Metal Ind Ltd 熱処理炉雰囲気ガスの再利用方法
US20040134348A1 (en) * 2003-01-13 2004-07-15 Ati Properties, Inc. (A Delaware Corporation) Hydrogen reclamation apparatus and method
CN101956061A (zh) * 2010-07-27 2011-01-26 苏州品源气体设备有限公司 钟罩式光亮退火炉保护气回收循环利用工艺及其装置
CN110699526A (zh) * 2019-10-18 2020-01-17 甘肃酒钢集团宏兴钢铁股份有限公司 热镀锌立式退火炉上下炉压检测氮气联锁控制系统操作方法
CN110819772A (zh) * 2019-10-28 2020-02-21 鞍钢股份有限公司 一种连续退火炉氮氢保护气控制方法
CN111589299A (zh) * 2020-05-14 2020-08-28 中冶南方工程技术有限公司 一种轧钢退火炉的氮氢保护气分离系统及方法
CN112941287A (zh) * 2021-01-26 2021-06-11 中冶南方工程技术有限公司 冷轧退火炉废氢回收利用系统及冷轧退火炉氢气供应系统
CN114540598A (zh) * 2022-02-07 2022-05-27 中冶南方工程技术有限公司 一种冷轧退火炉保护气供气及循环利用方法

Also Published As

Publication number Publication date
CN114540598A (zh) 2022-05-27

Similar Documents

Publication Publication Date Title
WO2023147719A1 (zh) 一种冷轧退火炉保护气供气及循环利用方法
CN109611686B (zh) 冶金空分供氧管网系统及其运行方法
CN113549717B (zh) 一种高炉喷吹欧冶炉煤气系统
KR20140066699A (ko) 유리 용융 장치 및 방법
CN115522003B (zh) 一种基于能质转换的富氢高炉炼铁系统及其生产控制方法
CN106406255B (zh) 氯化氢生产中送气工序的dcs控制方法
CN106444651B (zh) 氯化氢生产中制酸工序的dcs控制方法
CN206535212U (zh) 液氨蒸发系统
CN217103976U (zh) 一种冷轧退火炉保护气供气及循环利用系统
CN101482223A (zh) 一种配气装置及方法
CN215102208U (zh) 一种处理高浓度废水的催化湿式氧化系统
CN113639200A (zh) 一种化工厂高压氧气并入钢铁厂中压氧气管网的管路系统及方法
CN218951242U (zh) 一种电子玻璃锡槽保护气节能环保装置
CN109485277B (zh) 一种用于石灰窑的天然气煅烧设备及方法
CN202390455U (zh) 一种高炉富氧平衡装置
CN110645475A (zh) 一种高炉氧气输送系统及工作方法
CN202733435U (zh) 一种制氧供给炼钢系统氧气限速装置
CN220056907U (zh) 一种高炉鼓风机前富氧安全控制装置
CN218179674U (zh) 一种分解炉管路系统
CN218910416U (zh) 一种基于空分系统的供氧装置
CN217173771U (zh) 一种可在线切换喷吹气体的高炉喷煤喷吹系统
CN215672598U (zh) 一种化工尾气中氢气综合利用系统
CN216924412U (zh) 一种用于烧结机富氧点火的氧气输送系统
CN216638170U (zh) 一种利用压缩空气代替氮气进行热矿输送的装置
CN218001149U (zh) 一种氩气回收系统

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 22924647

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE