JP2014065619A - Oxygen gas supply system - Google Patents

Oxygen gas supply system Download PDF

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JP2014065619A
JP2014065619A JP2012210271A JP2012210271A JP2014065619A JP 2014065619 A JP2014065619 A JP 2014065619A JP 2012210271 A JP2012210271 A JP 2012210271A JP 2012210271 A JP2012210271 A JP 2012210271A JP 2014065619 A JP2014065619 A JP 2014065619A
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oxygen gas
oxygen
amount
gas supply
supply system
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JP6031914B2 (en
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Masayuki Komuro
正之 小室
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JFE Steel Corp
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Abstract

PROBLEM TO BE SOLVED: To provide an oxygen gas supply system with which oxygen gas is suitably supplied corresponding to the oxygen gas usage status of a demander as the oxygen gas supply system for a case in which one intermittently using oxygen gas such as a steel converter is included in demanders.SOLUTION: In an oxygen gas supply system, an oxygen gas generation amount in an oxygen gas generation apparatus 1 and a liquid oxygen storage amount and a liquid oxygen vaporization amount in an oxygen gas liquefaction and storage apparatus 5 are adjusted by using oxygen usage information consisting of a raw material charge signal synchronizing with raw material charge and a blow start signal synchronizing with start of blowing in a steel converter 11 operated according to a series of steps.

Description

本発明は、製鉄所等において使用される酸素ガスの供給システムに関する。   The present invention relates to an oxygen gas supply system used in steelworks or the like.

製鉄所等において、断続的な操業を行う転炉あるいはそれに類似する炉(例えば、シャフト炉)を使用先(需要先)に含む場合の酸素ガスの使用量(需要量)は、転炉等の稼働状況(操業状況)によるため大きく変動する。   The amount of oxygen gas used (demand) when a converter (such as a shaft furnace) that performs intermittent operation or a similar furnace (for example, a shaft furnace) is included in the user (demand) at a steelworks, etc. Fluctuates greatly due to operating conditions (operational conditions).

この酸素ガスの使用量(需要量)の変動は、酸素ガス発生装置(原料空気圧縮機、空気分離機)から供給される酸素ガスを一時的に貯蔵する酸素ガスホルダによって吸収され、空気分離機からの酸素ガスの供給量は平滑化される。   The fluctuation in the amount of oxygen gas used (demand amount) is absorbed by the oxygen gas holder that temporarily stores the oxygen gas supplied from the oxygen gas generator (raw material air compressor, air separator). The supply amount of oxygen gas is smoothed.

したがって、例えば転炉の吹錬が実施されて酸素ガスを使用する際には、酸素ガスホルダ内の酸素ガス量が減少して酸素ガスホルダ内の圧力は低下し、逆に転炉の吹錬が実施されていないときは、酸素ガスホルダ内の酸素ガス量が増加して酸素ガスホルダ内の圧力は上昇する。   Therefore, for example, when the converter is blown and oxygen gas is used, the amount of oxygen gas in the oxygen gas holder decreases, the pressure in the oxygen gas holder decreases, and conversely, the converter is blown. If not, the amount of oxygen gas in the oxygen gas holder increases and the pressure in the oxygen gas holder rises.

ただし、酸素ガスホルダの圧力管理値には上限値があるため、例えば転炉の吹錬が実施されていないときには、一時的に空気分離機での酸素ガスの発生量を減少させて、酸素ガスホルダの圧力上昇を抑制させる。   However, since the pressure control value of the oxygen gas holder has an upper limit value, for example, when the converter is not blown, the amount of oxygen gas generated in the air separator is temporarily reduced, and the oxygen gas holder Suppresses pressure rise.

一方、使用先(需要先)において必要となる酸素ガス圧力の下限値があるため、例えば転炉の吹錬が実施されているときには、一時的に空気分離機での酸素ガスの発生量を増加させて、酸素ガスの圧力低下を抑制させる。ただし、空気分離機での酸素ガスの発生量増加だけでは酸素ガスの圧力低下を抑制できない場合は、別途貯蔵されている液体酸素の気化により酸素ガス供給量の不足分を補充する。   On the other hand, since there is a lower limit of the oxygen gas pressure required at the user (demand), for example, when the converter is being blown, the amount of oxygen gas generated in the air separator is temporarily increased. Thus, the pressure drop of the oxygen gas is suppressed. However, when the pressure drop of oxygen gas cannot be suppressed only by increasing the amount of oxygen gas generated in the air separator, the shortage of oxygen gas supply is replenished by vaporizing liquid oxygen stored separately.

このような酸素ガスの供給システムにおいては、空気分離機での酸素ガスの発生量の減少が間に合わない場合、酸素ガスホルダの圧力が上限値に達し、余剰酸素ガスの大気放散となる。一方、空気分離機での酸素ガスの発生量の増加が間に合わない場合や、酸素ガスの使用量が多い場合は、液体酸素の補充量が増加する。   In such an oxygen gas supply system, when the decrease in the amount of oxygen gas generated in the air separator is not in time, the pressure of the oxygen gas holder reaches the upper limit value, and excess oxygen gas is released into the atmosphere. On the other hand, when the increase in the amount of oxygen gas generated in the air separator is not in time, or when the amount of oxygen gas used is large, the replenishment amount of liquid oxygen increases.

こうした酸素ガスの使用量(需要量)に応じた酸素ガスの供給量の調整方法として、酸素ガス需要量予測値と酸素ガス発生量予測値に基づき、酸素ガスホルダ圧力を予測し表示する方法(特許文献1)や、余剰酸素ガスを原料空気圧縮機の出側で原料空気に混入させ、余剰酸素ガスの放散を抑制する方法(特許文献2)がとられている。   As a method of adjusting the supply amount of oxygen gas according to the amount of oxygen gas used (demand amount), a method for predicting and displaying the oxygen gas holder pressure based on the predicted oxygen gas demand amount and the predicted oxygen gas generation amount (patent) Document 1) and a method of suppressing surplus oxygen gas emission by mixing surplus oxygen gas into the material air on the outlet side of the material air compressor (Patent Document 2).

特開2006−2958号公報JP 2006-2958 A 特開平5−34061号公報JP-A-5-34061

しかしながら、特許文献1のような方法では、転炉等の操業状態によっては、酸素ガス使用量予測値と実際の酸素ガス使用量にずれが生じて、吹錬スケジュールに基づいた酸素ガスホルダ圧力予測値と実際の酸素ガスホルダ圧力推移が乖離し、その乖離による酸素ガスの大気放散や液体酸素の気化供給量が発生するという問題点があった。   However, in the method as disclosed in Patent Document 1, depending on the operation state of the converter or the like, there is a difference between the predicted oxygen gas usage amount and the actual oxygen gas usage amount, and the predicted oxygen gas holder pressure value based on the blowing schedule. There is a problem that the actual oxygen gas holder pressure change deviates from that, and oxygen gas is released into the atmosphere and the vaporized supply amount of liquid oxygen is generated due to the difference.

また、特許文献2のような方法では、原料空気の吸入流量と余剰酸素ガス混入流量の合計流量を急激に変化させることができないため、抑制できる酸素ガスの大気放散量には限界があった。   Further, in the method as disclosed in Patent Document 2, since the total flow rate of the raw material intake flow rate and the surplus oxygen gas mixed flow rate cannot be changed rapidly, there is a limit in the amount of atmospheric oxygen gas that can be suppressed.

本発明は、上記のような事情に鑑みてなされたものであり、転炉等のように断続的に酸素ガスを使用する需要先に含む場合の酸素ガス供給システムとして、需要先の酸素ガス使用状況に応じて適切に酸素ガスを供給することができる酸素ガス供給システムを提供することを目的とするものである。   This invention is made | formed in view of the above situations, and uses oxygen gas of a customer as an oxygen gas supply system in the case of including in the customer who uses oxygen gas intermittently like a converter etc. An object of the present invention is to provide an oxygen gas supply system that can supply oxygen gas appropriately according to the situation.

上記課題を解決するために、本発明は以下の特徴を有する。   In order to solve the above problems, the present invention has the following features.

[1]断続的に酸素ガスを使用する需要先を含む場合の酸素ガス供給システムであって、酸素ガス発生装置と、酸素ガス発生装置からの酸素ガスを一時的に貯蔵する酸素ガスホルダと、酸素ガス発生装置からの酸素ガスを液化して貯蔵し、酸素ガスの供給量が不足すると液化した酸素を気化して補充する酸素ガス液化貯蔵装置と、需要先の酸素使用情報に基づいて需要先への酸素ガス供給量を制御する酸素ガス供給制御装置とを備えていることを特徴とする酸素ガス供給システム。   [1] An oxygen gas supply system in the case of including a customer who uses oxygen gas intermittently, an oxygen gas generator, an oxygen gas holder for temporarily storing oxygen gas from the oxygen gas generator, oxygen Oxygen gas from the gas generator liquefied and stored, oxygen gas liquefied storage device that vaporizes and replenishes the liquefied oxygen when the supply amount of oxygen gas is insufficient, and to the customer based on the oxygen usage information of the customer An oxygen gas supply system comprising: an oxygen gas supply control device that controls an oxygen gas supply amount of the gas.

[2]酸素ガス供給制御装置は、需要先の酸素使用情報に基づいて、酸素ガス発生装置からの酸素ガスの発生量を増減させることを特徴とする前記[1]に記載の酸素ガス供給システム。   [2] The oxygen gas supply system according to [1], wherein the oxygen gas supply control device increases or decreases the amount of oxygen gas generated from the oxygen gas generator based on oxygen usage information of a demand destination. .

[3]酸素ガス供給制御装置は、需要先の酸素使用情報に基づいて、酸素ガス液化貯蔵装置の液体酸素の貯蔵量と気化量を増減して、酸素ガス供給量の変動を平準化することを特徴とする前記[1]または[2]に記載の酸素ガス供給システム。   [3] The oxygen gas supply control device increases or decreases the storage amount and vaporization amount of liquid oxygen in the oxygen gas liquefaction storage device based on the oxygen usage information of the demand destination, and leveles the fluctuation of the oxygen gas supply amount. The oxygen gas supply system according to [1] or [2], wherein

[4]断続的に酸素ガスを使用する需要先が転炉であることを特徴とする前記[1]〜[3]のいずれかに記載の酸素ガス供給システム。   [4] The oxygen gas supply system according to any one of [1] to [3], wherein a demand destination that intermittently uses oxygen gas is a converter.

[5]需要先の酸素使用情報として、一連の工程に従って稼動される転炉における原料装入信号と吹錬開始信号からなる酸素使用情報を用いることを特徴とする前記[4]に記載の酸素ガス供給システム。   [5] The oxygen usage information according to [4], wherein oxygen usage information including a raw material charging signal and a blowing start signal in a converter operated in accordance with a series of processes is used as the oxygen usage information of a customer. Gas supply system.

[6]原料装入信号として、転炉における防爆シャッターの動作信号を用いることを特徴とする前記[5]に記載の酸素ガス供給システム。   [6] The oxygen gas supply system according to [5], wherein an operation signal of an explosion-proof shutter in a converter is used as a raw material charging signal.

本発明においては、需要先の酸素使用情報に基づいて需要先への酸素ガス供給量を制御するようにしたので、需要先の酸素ガス使用状況に応じて適切に酸素ガスを供給することができる。   In the present invention, since the oxygen gas supply amount to the customer is controlled based on the oxygen usage information of the customer, the oxygen gas can be appropriately supplied according to the oxygen gas usage situation of the customer. .

本発明の一実施形態における酸素ガス供給システムを示す図である。It is a figure which shows the oxygen gas supply system in one Embodiment of this invention. 本発明の一実施形態における酸素ガス圧力の変化等を示す図である。It is a figure which shows the change of the oxygen gas pressure, etc. in one Embodiment of this invention. 本発明の一実施形態における酸素ガス発生量と酸素液化量・気化量の変化を示す図である。It is a figure which shows the change of oxygen gas generation amount and oxygen liquefaction amount, and vaporization amount in one Embodiment of this invention.

本発明の一実施形態を図面に基づいて説明する。   An embodiment of the present invention will be described with reference to the drawings.

図1は、本発明の一実施形態における酸素ガス供給システムを示す図である。   FIG. 1 is a diagram showing an oxygen gas supply system according to an embodiment of the present invention.

図1に示すように、この実施形態における酸素ガス供給システムは、酸素ガスの需要先10として、断続的に酸素ガスを使用する転炉11(No.1転炉、No.2転炉)と連続的に酸素ガスを使用する高炉12を有しており、酸素ガス発生装置1と、酸素ガス発生装置1からの酸素ガスを一時的に貯蔵する酸素ガスホルダ4と、酸素ガス発生装置1からの酸素ガスを液化して貯蔵し、酸素ガスの供給量が不足すると液化した酸素を気化して補充する酸素ガス液化貯蔵装置5と、需要先の酸素使用情報に基づいて需要先への酸素ガス供給量を制御する酸素ガス供給制御装置(図示せず)とを備えている。   As shown in FIG. 1, the oxygen gas supply system in this embodiment includes a converter 11 (No. 1 converter, No. 2 converter) that uses oxygen gas intermittently as a demand destination 10 for oxygen gas. A blast furnace 12 that continuously uses oxygen gas is provided. The oxygen gas generator 1, the oxygen gas holder 4 that temporarily stores the oxygen gas from the oxygen gas generator 1, and the oxygen gas generator 1 Oxygen gas liquefied and stored, oxygen gas liquefied storage device 5 that vaporizes and replenishes liquefied oxygen when the supply amount of oxygen gas is insufficient, and supply of oxygen gas to customers based on oxygen usage information of customers And an oxygen gas supply control device (not shown) for controlling the amount.

なお、酸素ガス発生装置1は、原料空気圧縮機2と空気分離機3を備えている。また、酸素ガス液化貯蔵装置5は、酸素ガスを液化する酸素液化装置6と、液化した液体酸素の液体酸素貯蔵槽7と、圧送ポンプ8と、液体酸素を気化する酸素気化装置9を備えている。   The oxygen gas generator 1 includes a raw material air compressor 2 and an air separator 3. The oxygen gas liquefaction storage device 5 includes an oxygen liquefaction device 6 for liquefying oxygen gas, a liquid oxygen storage tank 7 for liquefied liquid oxygen, a pumping pump 8, and an oxygen vaporization device 9 for vaporizing liquid oxygen. Yes.

そして、図2(a)に酸素ガスホルダ4の圧力の時間的推移、図2(b)に転炉11(No.1転炉、No.2転炉)での吹錬スケジュール、図2(c)に酸素ガス発生装置1(空気分離機3)での酸素ガス発生量の時間的推移、図2(d)に酸素ガス液化貯蔵装置5での酸素液化量・気化量の時間的推移を示し、図3(a)に1回の吹錬における一連の作業工程(原料装入、吹錬開始、吹錬(酸素使用中))、図3(b)に1回の吹錬における空気分離機3での酸素ガス発生量の時間的推移、図3(c)に1回の吹錬における酸素ガス液化貯蔵装置5での酸素液化量の時間的推移を示している。ちなみに、図2(a)において、破線はこの実施形態による酸素ガス供給制御を行わなかった場合であり、実線はこの実施形態による酸素ガス供給制御を行なった場合である。   2 (a) shows the temporal transition of the pressure of the oxygen gas holder 4, FIG. 2 (b) shows the blowing schedule in the converter 11 (No. 1 converter, No. 2 converter), FIG. 2 (c). ) Shows the time transition of the oxygen gas generation amount in the oxygen gas generator 1 (air separator 3), and FIG. Fig. 3 (a) shows a series of work steps in one blowing (raw material charging, start of blowing, blowing (in use of oxygen)), Fig. 3 (b) shows an air separator in one blowing. 3 shows the time transition of the oxygen gas generation amount in FIG. 3, and FIG. 3 (c) shows the time transition of the oxygen liquefaction amount in the oxygen gas liquefaction storage device 5 in one blowing. Incidentally, in FIG. 2A, the broken line indicates the case where the oxygen gas supply control according to this embodiment is not performed, and the solid line indicates the case where the oxygen gas supply control according to this embodiment is performed.

このような図2、図3に示すように、この酸素ガス供給システムでは、一連の工程に従って稼動される転炉11での、原料装入と同期した原料装入信号と吹錬開始と同期した吹錬開始信号からなる酸素使用情報を用いて、酸素ガス発生装置1の酸素ガス発生量や酸素ガス液化貯蔵装置5での液体酸素貯蔵量・気化量を調整するようにしている。   As shown in FIGS. 2 and 3, in this oxygen gas supply system, in the converter 11 operated according to a series of processes, the raw material charging signal synchronized with the raw material charging and the start of blowing are synchronized. The oxygen use information formed from the blowing start signal is used to adjust the oxygen gas generation amount of the oxygen gas generator 1 and the liquid oxygen storage amount / vaporization amount of the oxygen gas liquefaction storage device 5.

すなわち、原料装入に応じて操作される防爆シャッターの動作信号を原料装入信号とし、その原料装入信号(酸素使用開始予告信号)に基づいて、酸素ガス発生装置1の酸素ガス発生量と酸素ガス液化貯蔵装置5での液体酸素貯蔵量を増加するように調整することで、吹錬前の酸素ガスホルダ4の圧力レベルの上昇を抑制することができる。その結果、酸素ガスホルダ4の圧力レベルが上限値に達することによる酸素ガスの放散を低減させることができる。   That is, the operation signal of the explosion-proof shutter operated according to the raw material charging is used as the raw material charging signal, and the oxygen gas generation amount of the oxygen gas generator 1 is determined based on the raw material charging signal (oxygen use start notice signal). By adjusting so that the amount of liquid oxygen stored in the oxygen gas liquefaction storage device 5 is increased, an increase in the pressure level of the oxygen gas holder 4 before blowing can be suppressed. As a result, the diffusion of oxygen gas due to the pressure level of the oxygen gas holder 4 reaching the upper limit value can be reduced.

そして、その後の吹錬開始信号に基づいて、酸素ガス発生装置1の酸素ガス発生量を増加した値に保持するようにしているので、酸素ガス供給量調整の遅れによる吹錬中の酸素ガス圧力の低下を抑制することができる。その結果、液体酸素による補充量を減少させることができる。   Since the oxygen gas generation amount of the oxygen gas generator 1 is maintained at an increased value based on the subsequent blowing start signal, the oxygen gas pressure during blowing due to the delay in adjusting the oxygen gas supply amount Can be suppressed. As a result, the replenishment amount with liquid oxygen can be reduced.

詳説すれば、図3に示すように、吹錬開始前の原料装入情報(酸素使用開始予告情報)に基づいて、空気分離機3からの酸素発生量の増加を開始させる。また、そのときの酸素ガスホルダ4の圧力レベルの上昇に応じて、酸素ガス液化貯蔵装置5を稼動させて酸素液化量を増加させることにより、酸素ガス発生量増加に伴う酸素ガスホルダ4の圧力の上昇速度を抑制する。その後、吹錬開始情報と同時に酸素液化を停止し、需要先への酸素供給量を増加させ、吹錬実施時の酸素ガス圧力の低下を抑制させる。   More specifically, as shown in FIG. 3, an increase in the amount of oxygen generated from the air separator 3 is started based on the raw material charging information (oxygen use start notice information) before the start of blowing. Further, by increasing the oxygen liquefaction amount by operating the oxygen gas liquefaction storage device 5 in response to an increase in the pressure level of the oxygen gas holder 4 at that time, the pressure of the oxygen gas holder 4 increases with the increase in the amount of oxygen gas generated. Suppress the speed. Thereafter, oxygen liquefaction is stopped simultaneously with the blowing start information, the amount of oxygen supplied to the customer is increased, and a decrease in oxygen gas pressure during the blowing is suppressed.

このように、空気分離機3からの酸素発生量や酸素ガス液化貯蔵装置5での酸素液化量の増減により、吹錬の実施時と未実施時における酸素ガス圧力レベルを管理値内にすることで、圧力上限値を超過することによる酸素放散量と圧力下限値を下回ることによる酸素気化量の削減が可能となる。   As described above, the oxygen gas pressure level when the blowing is performed and when it is not performed is set within the control value by increasing or decreasing the oxygen generation amount from the air separator 3 or the oxygen liquefaction amount in the oxygen gas liquefaction storage device 5. Thus, it is possible to reduce the amount of oxygen diffused by exceeding the pressure upper limit and the amount of oxygen vaporization by falling below the pressure lower limit.

このようにして、この実施形態では、転炉工場11における一連の操業工程において、原料装入に応じて操作される防爆シャッターの動作信号に基づいて酸素使用開始情報を作成することで、吹錬スケジュールと実際の吹錬との間のずれによる酸素ガスの供給量調整をなくすとともに、酸素使用開始までの裕度を確保することにより、吹錬開始までに酸素ガス発生装置1からの酸素ガス供給量を増加し、吹錬中(酸素使用中)の酸素ガス圧力の低下を抑制する。   Thus, in this embodiment, in a series of operation processes in the converter plant 11, the oxygen use start information is created based on the operation signal of the explosion-proof shutter operated in accordance with the raw material charging, so that the blowing is performed. Oxygen gas supply from the oxygen gas generator 1 before the start of blowing by eliminating the adjustment of the supply amount of oxygen gas due to the difference between the schedule and the actual blowing and ensuring the allowance until the start of oxygen use Increase the amount to suppress the decrease in oxygen gas pressure during blowing (using oxygen).

言い換えれば、この実施形態では、転炉工場11における防爆シャッター信号に基づく原料装入開始・終了や吹錬開始の操作信号を取り込み、その信号に基づき原料空気圧縮機2の吸入量を制御することにより、吹錬開始までの酸素発生量の増量や吹錬開始と同期した酸素ガスの供給量調整を行い、酸素ガスホルダ4の圧力上昇・低下の抑制を可能にしたものである。   In other words, in this embodiment, an operation signal for starting and ending raw material charging and starting blowing is acquired based on the explosion-proof shutter signal in the converter plant 11, and the intake amount of the raw material air compressor 2 is controlled based on the signal. Thus, an increase in the amount of oxygen generated until the start of blowing and adjustment of the supply amount of oxygen gas in synchronization with the start of blowing are performed, thereby making it possible to suppress the pressure rise and fall of the oxygen gas holder 4.

また、上記の原料空気圧縮機2の吸入量制御に加えて、液体酸素の貯蔵量制御を付加することにより、原料空気圧縮機2の吸入量制御で対応できない急激な酸素ガス需要量の変動を吸収し、酸素ガスホルダ4の圧力上昇の抑制を可能にしたものである。   Moreover, in addition to the intake air amount control of the raw material air compressor 2 described above, by adding the storage amount control of liquid oxygen, rapid fluctuations in oxygen gas demand that cannot be accommodated by the intake air amount control of the raw material air compressor 2 are achieved. It absorbs and the pressure rise of the oxygen gas holder 4 can be suppressed.

このようにして、この実施形態では、転炉11の原料装入情報や吹錬開始信号を取り込み、原料空気圧縮機2の吸入量制御として利用するようにしたので、実際の転炉11の稼動状態と同期した酸素ガスの供給量調整や吹錬開始までの酸素ガス発生量の増量が可能となった。また、余剰酸素ガスの液化貯蔵量制御を付加することにより、原料空気圧縮機2の吸入量制御で対応できない急激な酸素使用量の変動にも対応できる酸素ガスの供給量調整が可能となった。   In this way, in this embodiment, since the raw material charging information and the blowing start signal of the converter 11 are taken in and used as the intake amount control of the raw material air compressor 2, the actual operation of the converter 11 is performed. It became possible to adjust the supply amount of oxygen gas in synchronization with the state and increase the amount of oxygen gas generated until the start of blowing. Further, by adding liquefied storage amount control of surplus oxygen gas, it has become possible to adjust the supply amount of oxygen gas that can cope with rapid fluctuations in oxygen usage that cannot be handled by the intake air amount control of the raw air compressor 2. .

なお、上記の実施形態では、断続的に酸素ガスを使用する需要先として転炉を対象にしているが、転炉に類似する炉(例えば、シャフト炉)を対象にした場合でも同様に適用することができる。   In the above-described embodiment, the converter is targeted as a demand destination that uses oxygen gas intermittently, but the same applies to a furnace similar to the converter (for example, a shaft furnace). be able to.

1 酸素ガス発生装置
2 原料空気圧縮機
3 空気分離機
4 酸素ガスホルダ
5 酸素ガス液化貯蔵装置
6 酸素液化装置
7 液体酸素貯蔵槽
8 圧送ポンプ
9 酸素気化装置
10 酸素ガスの需要先
11 転炉
12 高炉
DESCRIPTION OF SYMBOLS 1 Oxygen gas generator 2 Raw material air compressor 3 Air separator 4 Oxygen gas holder 5 Oxygen gas liquefying storage device 6 Oxygen liquefying device 7 Liquid oxygen storage tank 8 Pressure pump 9 Oxygen vaporizer 10 Oxygen gas customer 11 Converter 12 Blast furnace

Claims (6)

断続的に酸素ガスを使用する需要先を含む場合の酸素ガス供給システムであって、酸素ガス発生装置と、酸素ガス発生装置からの酸素ガスを一時的に貯蔵する酸素ガスホルダと、酸素ガス発生装置からの酸素ガスを液化して貯蔵し、酸素ガスの供給量が不足すると液化した酸素を気化して補充する酸素ガス液化貯蔵装置と、需要先の酸素使用情報に基づいて需要先への酸素ガス供給量を制御する酸素ガス供給制御装置とを備えていることを特徴とする酸素ガス供給システム。   An oxygen gas supply system in the case of including a customer who uses oxygen gas intermittently, an oxygen gas generator, an oxygen gas holder for temporarily storing oxygen gas from the oxygen gas generator, and an oxygen gas generator Liquefied and stored oxygen gas from the storage, oxygen gas liquefied storage device to vaporize and replenish the liquefied oxygen when the oxygen gas supply amount is insufficient, and oxygen gas to the customer based on the oxygen usage information of the customer An oxygen gas supply system comprising an oxygen gas supply control device for controlling a supply amount. 酸素ガス供給制御装置は、需要先の酸素使用情報に基づいて、酸素ガス発生装置からの酸素ガスの発生量を増減させることを特徴とする請求項1に記載の酸素ガス供給システム。   2. The oxygen gas supply system according to claim 1, wherein the oxygen gas supply control device increases or decreases the amount of oxygen gas generated from the oxygen gas generator on the basis of the oxygen usage information of the customer. 酸素ガス供給制御装置は、需要先の酸素使用情報に基づいて、酸素ガス液化貯蔵装置の液体酸素の貯蔵量と気化量を増減して、酸素ガス供給量の変動を平準化することを特徴とする請求項1または2に記載の酸素ガス供給システム。   The oxygen gas supply control device is characterized by leveling fluctuations in the oxygen gas supply amount by increasing / decreasing the storage amount and vaporization amount of liquid oxygen in the oxygen gas liquefaction storage device based on the oxygen usage information of the customer. The oxygen gas supply system according to claim 1 or 2. 断続的に酸素ガスを使用する需要先が転炉であることを特徴とする請求項1〜3のいずれかに記載の酸素ガス供給システム。   The oxygen gas supply system according to any one of claims 1 to 3, wherein a demander that uses oxygen gas intermittently is a converter. 需要先の酸素使用情報として、一連の工程に従って稼動される転炉における原料装入信号と吹錬開始信号からなる酸素使用情報を用いることを特徴とする請求項4に記載の酸素ガス供給システム。   5. The oxygen gas supply system according to claim 4, wherein oxygen usage information including a raw material charging signal and a blowing start signal in a converter operated according to a series of steps is used as the oxygen usage information of a demand destination. 原料装入信号として、転炉における防爆シャッターの動作信号を用いることを特徴とする請求項5に記載の酸素ガス供給システム。   6. The oxygen gas supply system according to claim 5, wherein an operation signal of an explosion-proof shutter in the converter is used as the raw material charging signal.
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CN105274277A (en) * 2015-11-25 2016-01-27 中冶南方工程技术有限公司 Oxygen blowing control method for dry dedusting explosion suppression of converter
CN110527776A (en) * 2019-09-27 2019-12-03 山东钢铁股份有限公司 The unsuccessful processing method of piping and druming fire is opened in a kind of converter
CN111566425A (en) * 2017-12-26 2020-08-21 乔治洛德方法研究和开发液化空气有限公司 System and method for supplying a backup product in an air separation plant
CN111621615A (en) * 2020-06-10 2020-09-04 中冶沈勘秦皇岛工程设计研究总院有限公司 Device and method for shortening electric furnace steelmaking smelting period
JP7247394B1 (en) 2022-03-11 2023-03-28 大陽日酸株式会社 gas purifier

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105274277A (en) * 2015-11-25 2016-01-27 中冶南方工程技术有限公司 Oxygen blowing control method for dry dedusting explosion suppression of converter
CN105274277B (en) * 2015-11-25 2017-07-11 中冶南方工程技术有限公司 A kind of datonation-inhibition oxygen blast control method of converter dry dedusting
CN111566425A (en) * 2017-12-26 2020-08-21 乔治洛德方法研究和开发液化空气有限公司 System and method for supplying a backup product in an air separation plant
CN110527776A (en) * 2019-09-27 2019-12-03 山东钢铁股份有限公司 The unsuccessful processing method of piping and druming fire is opened in a kind of converter
CN111621615A (en) * 2020-06-10 2020-09-04 中冶沈勘秦皇岛工程设计研究总院有限公司 Device and method for shortening electric furnace steelmaking smelting period
JP7247394B1 (en) 2022-03-11 2023-03-28 大陽日酸株式会社 gas purifier
JP2023132479A (en) * 2022-03-11 2023-09-22 大陽日酸株式会社 Gas purifier

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