JP2001221399A - Gas supplying method - Google Patents

Gas supplying method

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Publication number
JP2001221399A
JP2001221399A JP2000028143A JP2000028143A JP2001221399A JP 2001221399 A JP2001221399 A JP 2001221399A JP 2000028143 A JP2000028143 A JP 2000028143A JP 2000028143 A JP2000028143 A JP 2000028143A JP 2001221399 A JP2001221399 A JP 2001221399A
Authority
JP
Japan
Prior art keywords
pressure
pressure gas
low
gas holder
holder
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.)
Pending
Application number
JP2000028143A
Other languages
Japanese (ja)
Inventor
Toshihiko Kukutsu
寿彦 久々津
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP2000028143A priority Critical patent/JP2001221399A/en
Publication of JP2001221399A publication Critical patent/JP2001221399A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a gas supplying method for supplying boosted gas through a high-pressure gas holder and a low-pressure gas holder. SOLUTION: A flow control valve for gas is provided on the inlet side of a low-pressure gas holder. When pressure of the low-pressure gas holder is less than a lower limit set value, the flow control valve is opened to fill gas. When pressure of the low-pressure gas holder is more than pressure of a high- pressure gas holder and also when pressure of the low-pressure gas holder is not less than the lower limit set value, the flow control valve is opened to supply gas of the low-pressure gas holder to the high-pressure gas holder. When pressure of the low-pressure gas holder is not more than pressure of high-pressure gas holder and also when pressure of the low-pressure gas holder is not less than the lower limit set value, the flow control valve is closed to feed gas to only a low-pressure gas using facility.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は高圧ガス使用設備用
の高圧ガスホルダと低圧ガス使用設備用の低圧ガスホル
ダを介してそれぞれの設備にガスの供給を行うガス供給
ラインにおけるガス供給方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas supply method in a gas supply line for supplying gas to each equipment via a high-pressure gas holder for high-pressure gas equipment and a low-pressure gas holder for low-pressure gas equipment.

【0002】[0002]

【従来の技術】一貫製鉄所においては、種々のガスが利
用されているが、例えば、多量の酸素ガスが高炉、転炉
等での生産に使用されている。一貫製鉄所において使用
される酸素ガスの供給ラインの例を図1に模式的に示
す。
2. Description of the Related Art In an integrated steel mill, various gases are used. For example, a large amount of oxygen gas is used for production in a blast furnace, a converter and the like. FIG. 1 schematically shows an example of an oxygen gas supply line used in an integrated steelworks.

【0003】大気中から取り込んだ空気は、空気圧縮機
1で圧縮を行い、水洗冷却塔2で冷却した後、モリキュ
ラシーブス吸着器3で分子ふるいにかけ、コールドボッ
クス4内の精留塔で精留して最終的に酸素を分離する。
そして、酸素圧縮機5で昇圧(圧縮)して所要の圧力の
圧縮酸素ガスを得る。ここで得られた圧縮酸素ガスは、
供給先の使用圧力に応じて、高圧と低圧の2つのホルダ
(ガスタンク)に供給されて貯蔵される。
The air taken in from the atmosphere is compressed by an air compressor 1, cooled in a washing cooling tower 2, passed through a molecular sieve in a molecular sieve adsorber 3, and purified in a rectifying tower in a cold box 4. To finally separate oxygen.
Then, the pressure is increased (compressed) by the oxygen compressor 5 to obtain a compressed oxygen gas having a required pressure. The compressed oxygen gas obtained here is
In accordance with the working pressure of the supply destination, it is supplied to and stored in two holders (gas tanks) of high pressure and low pressure.

【0004】高炉に代表される低圧ガス使用設備12に対
しては、低圧ガスホルダ9から酸素ガスが供給され、転
炉に代表される高圧ガス使用設備13に対しては、高圧ガ
スホルダ7から酸素ガスが供給される。そして、これら
低圧ガスホルダ9と高圧ガスホルダ7で上述の圧縮され
た酸素が各ガス使用設備において必要な圧力に調整され
る。ここで、低圧ガスホルダ9の入側部には流量調節弁
8が付設されている。なお、6は酸素放散弁である。シ
ーケンス制御装置11には、圧力計10a 、10b で計測され
た低圧ガスホルダ9と高圧ガスホルダ7の圧力値が入力
され、それらの圧力値を基にして流量調節弁8と酸素放
散弁6の制御が行われる。
An oxygen gas is supplied from a low-pressure gas holder 9 to a low-pressure gas facility 12 represented by a blast furnace, and an oxygen gas is supplied from a high-pressure gas holder 7 to a high-pressure gas facility 13 represented by a converter. Is supplied. Then, the above-described compressed oxygen is adjusted by the low-pressure gas holder 9 and the high-pressure gas holder 7 to a pressure required in each gas use facility. Here, a flow control valve 8 is attached to the entry side of the low-pressure gas holder 9. Reference numeral 6 denotes an oxygen release valve. The sequence controller 11 receives the pressure values of the low-pressure gas holder 9 and the high-pressure gas holder 7 measured by the pressure gauges 10a and 10b, and controls the flow control valve 8 and the oxygen release valve 6 based on the pressure values. Done.

【0005】圧縮酸素ガス量は、常に使用設備の稼動に
合わせて最適となるように制御が行われ生産されてお
り、例えば、使用設備のいずれかが停止する際には、そ
の状況に合わせ、精留塔の稼動基数を削減する等して、
電力消費のコストがミニマムとなるように調節を行う。
ただし、精留塔は、塔内の精留板上での液と蒸気の平衡
バランスを厳密に管理しながら空気の分離を行う装置で
あり、精留塔内の液・蒸気バランスを安定させるために
は最低でも3時間程度を必要とする。そのため、使用設
備側の短時間停止(例えば、30分から180 分程度)のた
めに精留塔を一時停止したり、負荷変更を行ったりする
ことは実際上不可能である。
[0005] The amount of compressed oxygen gas is controlled and produced so as to always be optimal in accordance with the operation of the equipment to be used. By reducing the number of operating rectification towers,
Make adjustments to minimize the cost of power consumption.
However, the rectification tower is a device that separates air while strictly controlling the equilibrium balance between liquid and vapor on the rectification plate in the tower. Requires at least about 3 hours. For this reason, it is practically impossible to temporarily stop the rectification tower or change the load due to a short stop (for example, about 30 to 180 minutes) on the equipment side.

【0006】また、精留した酸素ガスを酸素圧縮機5で
圧縮し、所要のガス圧として供給を行うが、精留した酸
素ガスは連続的に発生するのに対し、ガス使用設備側で
は、転炉に代表されるように、非連続的な操業が行われ
るのが通常である。そのため、工場の操業停止時や負荷
変更時のバッファを確保し、安定的な供給を行うため、
ガス供給ライン上にガスホルダを設けるのである。
[0006] The rectified oxygen gas is compressed by the oxygen compressor 5 and supplied at a required gas pressure. Usually, discontinuous operation is performed, as represented by a converter. Therefore, in order to secure a buffer at the time of factory shutdown or load change and to provide a stable supply,
The gas holder is provided on the gas supply line.

【0007】このガスホルダとしては、既に説明したよ
うに、ガス使用設備に対応して低圧ガスホルダ9と高圧
ガスホルダ7の2通りのタイプを設ける。転炉等の高圧
ガス使用設備13側に設ける高圧ガスホルダ7は、例え
ば、上限設定値2.16MPa、下限設定値1.57MPaの高圧領
域での運用が行われ、酸素圧縮機5から圧縮酸素ガス
が、通常、連続的に供給され、ホルダ圧は常に高圧状態
とされる。
As described above, two types of gas holders, a low-pressure gas holder 9 and a high-pressure gas holder 7, are provided corresponding to the gas use equipment. The high-pressure gas holder 7 provided on the side of the high-pressure gas use equipment 13 such as a converter is operated in a high-pressure region of, for example, an upper limit set value of 2.16 MPa and a lower limit set value of 1.57 MPa. Usually, it is supplied continuously, and the holder pressure is always in a high pressure state.

【0008】一方、高炉等の低圧ガス使用設備12側に設
ける低圧ガスホルダ9には、その入口側に流量調節弁8
が配置されている。そして、その運用は、ホルダ圧が下
限設定値を下回るような緊急時を除いた通常状態では流
量調節弁8を閉とし、低圧ガスホルダ9に貯蔵したガス
を低圧ガス使用設備12側にのみ供給するようにし、圧力
を常に低圧側に下げるような操業を行う。低圧ガスホル
ダ9は、例えば、上限設定値1.86MPa、下限設定値0.98
MPaの範囲での運用が行われる。なお、ガスホルダその
ものの規格は、通常、低圧ガスホルダも高圧ガスホルダ
も同一仕様であり、規格上の耐圧である最上限設定値
は、いずれも2.35MPa程度とされる。
On the other hand, a low pressure gas holder 9 provided on the low pressure gas use equipment 12 side such as a blast furnace has a flow control valve 8 at its inlet side.
Is arranged. Then, the operation is such that the flow control valve 8 is closed in a normal state except for an emergency in which the holder pressure is lower than the lower limit set value, and the gas stored in the low-pressure gas holder 9 is supplied only to the low-pressure gas use facility 12 side. So that the pressure is constantly reduced to the low pressure side. The low-pressure gas holder 9 has, for example, an upper limit set value of 1.86 MPa and a lower limit set value of 0.98
Operation is performed in the range of MPa. Note that the specifications of the gas holder itself are usually the same for both the low-pressure gas holder and the high-pressure gas holder, and the upper limit set value, which is the withstand pressure in the standard, is about 2.35 MPa.

【0009】ここで、高圧ガスホルダ7が満杯となり、
最上限設定値以上となった場合、低圧ガスホルダ9を高
圧ガスホルダ7のバックアップとして用い、流量調節弁
8を開として高圧ガスホルダ内の余剰ガスの回収を行
う。これを放散回収とよぶ。そして、低圧ガスホルダ9
と高圧ガスホルダ7のいずれもが満杯となったときには
酸素放散弁6から大気放散を行う。
Here, the high pressure gas holder 7 becomes full,
When the pressure is equal to or greater than the upper limit set value, the low pressure gas holder 9 is used as a backup for the high pressure gas holder 7 and the flow control valve 8 is opened to collect the excess gas in the high pressure gas holder. This is called radiation collection. And the low pressure gas holder 9
When both the high pressure gas holder 7 and the high pressure gas holder 7 are full, the oxygen is released from the oxygen release valve 6 to the atmosphere.

【0010】低圧ガスホルダ9は、高圧ガスホルダ7と
比較して圧力運用幅が広いことを特徴とする。つまり、
圧縮性ガスの貯蔵可能容量は(圧力幅ΔP×ガスホルダ
容積V)で決まることから、最上限設定値までの圧力幅
の広い低圧ガスホルダ9の方が高圧ガスホルダ7に比
べ、より多量のガスを貯蔵することができる。一貫製鉄
所において従来から行われてきた酸素ガス供給方法を、
図4に基づき説明する。
The low pressure gas holder 9 is characterized in that the pressure operation width is wider than that of the high pressure gas holder 7. That is,
Since the storable capacity of the compressible gas is determined by (pressure width ΔP × gas holder volume V), the low-pressure gas holder 9 having a wide pressure width up to the upper limit set value stores a larger amount of gas than the high-pressure gas holder 7. can do. The oxygen gas supply method that has been used in integrated steelworks
A description will be given based on FIG.

【0011】図4(a)は、高圧ガス使用設備である転
炉、溶融還元炉、脱炭炉等での操業のトレンド、すなわ
ち、酸素消費のトレンドを示すグラフである。図4
(a)の縦軸は、それぞれの炉での酸素消費量を示す。
なお、低圧ガス使用設備である高炉は、常時ほぼ一定量
の酸素ガスを消費する。図4(b)は、上記操業状態に
おける高圧ガスホルダと低圧ガスホルダのホルダ圧力の
トレンドを示す。ここで、ガスホルダの耐圧上限は、い
ずれのホルダも2.35MPaである。また、高圧ガスホルダ
圧下限は1.57MPaと、低圧ガスホルダ圧下限は0.69MPa
と規定される。
FIG. 4A is a graph showing a trend of operation in a converter, a smelting reduction furnace, a decarburization furnace, etc., which are high-pressure gas-using facilities, that is, a trend of oxygen consumption. FIG.
The vertical axis of (a) indicates the oxygen consumption in each furnace.
The blast furnace, which is a facility using low-pressure gas, always consumes a substantially constant amount of oxygen gas. FIG. 4B shows the trend of the holder pressure of the high-pressure gas holder and the low-pressure gas holder in the above-mentioned operation state. Here, the upper limit of the pressure resistance of each gas holder is 2.35 MPa. The lower limit of the high pressure gas holder pressure is 1.57MPa, and the lower limit of the low pressure gas holder pressure is 0.69MPa.
Is defined.

【0012】高圧ガスホルダ圧は、転炉等の操業に応じ
て大きく変動し、操業負荷が軽くなると耐圧上限にまで
上昇する。ここで、高圧ガスホルダ圧が耐圧上限となる
と、低圧ガスホルダ入側の流量調節弁が開とされ、低圧
ガスホルダへの放散回収が行われる。そして、高圧ガス
ホルダと低圧ガスホルダの両方が満杯となると、酸素放
散弁が開とされ、大気放散が行われるのである。
The high-pressure gas holder pressure fluctuates greatly depending on the operation of the converter and the like, and rises to the upper limit of the pressure resistance when the operation load is reduced. Here, when the high-pressure gas holder pressure reaches the upper limit of the pressure resistance, the flow control valve on the low-pressure gas holder inlet side is opened, and the radiation collection to the low-pressure gas holder is performed. Then, when both the high-pressure gas holder and the low-pressure gas holder are full, the oxygen release valve is opened, and atmospheric release is performed.

【0013】[0013]

【発明が解決しようとする課題】しかしながら、上記従
来のガス供給方法では、図4(b)に(*)で示すよう
に、低圧ガスホルダ圧の方が高圧ガスホルダ圧よりも高
くなってしまう場合が多々発生するという問題がある。
このような状態は、活用されない余分のガスが低圧ガス
ホルダに貯蔵されていることであり、ガス供給ライン全
体としてのガス貯蔵能力に大きな無駄が生じていること
になる。
However, in the above-mentioned conventional gas supply method, as shown by (*) in FIG. 4B, the low-pressure gas holder pressure may be higher than the high-pressure gas holder pressure. There is a problem that it often occurs.
Such a state is that excess gas that is not used is stored in the low-pressure gas holder, and a large waste is generated in the gas storage capacity of the entire gas supply line.

【0014】本発明は、ガス貯蔵能力にこのような無駄
を生じさせることなく、ガス供給ラインにおけるガス貯
蔵能力の最適化を実現することを目的とする。
An object of the present invention is to realize optimization of gas storage capacity in a gas supply line without causing such waste in gas storage capacity.

【0015】[0015]

【課題を解決するための手段】本発明は、昇圧したガス
を、高圧ガスホルダを介して高圧ガス使用設備に供給
し、かつ、ガス入側にガスの流量を調節する流量調節弁
を有する低圧ガスホルダを介して低圧ガス使用設備に供
給するガス供給方法であって、前記の低圧ガスホルダの
圧力と高圧ガスホルダの圧力の関係が、(低圧ガスホル
ダの圧力)>(高圧ガスホルダの圧力)であり、かつ、
低圧ガスホルダの圧力が下限設定値以上であるときは、
前記流量調節弁を開として、低圧ガスホルダのガスを高
圧ガスホルダにも送給し、(低圧ガスホルダの圧力)≦
(高圧ガスホルダの圧力)であり、かつ、低圧ガスホル
ダの圧力が下限設定値以上であるときは、前記流量調節
弁を閉として、低圧ガスホルダのガスを低圧ガス使用設
備にのみ送給するようにしたことを特徴とするガス供給
方法によって上記課題を解決したのである。
SUMMARY OF THE INVENTION The present invention provides a low-pressure gas holder having a flow control valve for supplying a pressurized gas to a high-pressure gas-using facility via a high-pressure gas holder and controlling a flow rate of the gas at a gas inlet side. A gas supply method for supplying to the low-pressure gas-using equipment via the above, wherein the relationship between the pressure of the low-pressure gas holder and the pressure of the high-pressure gas holder is (low-pressure gas holder pressure)> (high-pressure gas holder pressure), and
When the pressure of the low-pressure gas holder is higher than the lower limit set value,
By opening the flow control valve, the gas in the low-pressure gas holder is also supplied to the high-pressure gas holder, and (pressure of the low-pressure gas holder) ≦
(Pressure of the high-pressure gas holder) and when the pressure of the low-pressure gas holder is equal to or higher than the lower limit set value, the flow rate control valve is closed, and the gas of the low-pressure gas holder is supplied only to the equipment using the low-pressure gas. The above problem has been solved by a gas supply method characterized by the above.

【0016】[0016]

【発明の実施の形態】本発明のガス供給方法の好適な実
施の形態を表1に基づき説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the gas supply method of the present invention will be described with reference to Table 1.

【0017】[0017]

【表1】 [Table 1]

【0018】表1は、図1に示した一貫製鉄所における
酸素ガス供給ラインにおいて適用される本発明のガス供
給方法をマトリックス化して示した表である。表の横方
向には低圧ガスホルダの圧力をとり、縦方向には高圧ガ
スホルダの圧力をとって層別を行っている。ここで、HH
は最上限設定値(ガスホルダ耐圧上限)、PHは上限設定
値、PLは下限設定値を示す。表中には、それらの具体的
な数値例をMPa単位で併記している。
Table 1 shows a matrix of the gas supply method of the present invention applied to the oxygen gas supply line in the integrated steelworks shown in FIG. In the table, stratification is performed by taking the pressure of the low-pressure gas holder in the horizontal direction and taking the pressure of the high-pressure gas holder in the vertical direction. Where HH
Indicates the upper limit set value (gas holder withstand pressure upper limit), PH indicates the upper limit set value, and PL indicates the lower limit set value. In the table, specific numerical examples thereof are also described in units of MPa.

【0019】高圧ガスホルダ圧力現在値(PV)がPH以
上、つまり、2.16MPa以上の場合、流量調節弁は常に開
とされ、無条件で低圧ガスホルダへの放散回収が行われ
る。ただし、表には示していないが、高圧ガスホルダ圧
力現在値(PV)と低圧ガスホルダ圧力現在値(PV)のい
ずれもがHH以上、つまり、2.35MPa以上となった場合に
は、大気放散が行われることになる。なお、本発明には
直接関係しないが、高圧ガスホルダ圧力現在値(PV)が
PH以上であってもHH未満(2.35MPa未満)の場合には、
ゆっくりと放散が行われ、高圧ガスホルダ圧力現在値
(PV)がHH以上ではそれ以上に圧力が上がらないように
一気に放散が行われる。
When the current high-pressure gas holder pressure (PV) is equal to or higher than PH, that is, equal to or higher than 2.16 MPa, the flow control valve is always opened, and the radiation is recovered unconditionally to the low-pressure gas holder. However, although not shown in the table, if both the high-pressure gas holder pressure current value (PV) and low-pressure gas holder pressure current value (PV) are HH or more, that is, 2.35 MPa or more, atmospheric emission is performed. Will be Although not directly related to the present invention, the present high pressure gas holder pressure (PV) is
In the case of less than HH (less than 2.35 MPa) even if it is PH or more,
Dissipation is performed slowly, and when the high-pressure gas holder pressure current value (PV) is higher than HH, the radiation is performed at once so that the pressure does not rise any more.

【0020】次に、高圧ガスホルダ圧力現在値(PV)が
PH未満PL以上の場合は、低圧ガスホルダ圧と高圧ガスホ
ルダ圧の大小比較を行い、(低圧ガスホルダ圧)>(高
圧ガスホルダ圧)の場合には、流量調節弁を開として低
圧ガスホルダから高圧ガスホルダと低圧ガス使用設備の
両方にガスの送給を行うようにする。なお、表には示し
ていないが、低圧ガスホルダ圧がHH以上の場合も流量調
整弁を開とする。一方、(低圧ガスホルダ圧)≦(高圧
ガスホルダ圧)の場合は、流量調節弁を閉として低圧ガ
スホルダからは低圧ガス使用設備のみにガスの送給を行
うようにする。ただし、低圧ガスホルダ圧がPL未満、す
なわち、0.69MPa未満の場合には、流量調節弁を開と
し、緊急バックアップとして低圧ガスホルダへの酸素ガ
スの導入、貯蔵を行う。
Next, the current value of the high pressure gas holder pressure (PV) is
If the pressure is less than PH and not less than PL, the magnitudes of the low pressure gas holder pressure and the high pressure gas holder pressure are compared. If (low pressure gas holder pressure)> (high pressure gas holder pressure), the flow control valve is opened and the low pressure gas holder is moved from the high pressure gas holder to the low pressure gas holder. Supply gas to both gas-using facilities. Although not shown in the table, the flow regulating valve is also opened when the low-pressure gas holder pressure is higher than HH. On the other hand, when (low-pressure gas holder pressure) ≦ (high-pressure gas holder pressure), the flow control valve is closed, and gas is supplied from the low-pressure gas holder only to the equipment using low-pressure gas. However, when the low-pressure gas holder pressure is less than PL, that is, less than 0.69 MPa, the flow control valve is opened, and oxygen gas is introduced into the low-pressure gas holder and stored as an emergency backup.

【0021】高圧ガスホルダ圧力現在値(PV)がPL未満
の場合は、酸素圧縮機からの圧縮酸素を供給するととも
に、低圧ガスホルダ圧と高圧ガスホルダ圧の大小の比較
を行い、(低圧ガスホルダ圧)>(高圧ガスホルダ圧)
の場合には、流量調節弁を開として、低圧ガスホルダか
ら高圧ガスホルダと低圧ガス使用設備の両方にガスの供
給を行うようにする。なお、表には示していないが、低
圧ガスホルダ圧がHH以上の場合も流量調整弁を開とす
る。一方、(低圧ガスホルダ圧)≦(高圧ガスホルダ
圧)の場合は、流量調節弁を閉として低圧ガスホルダか
らは低圧ガス使用設備のみにガスの送給を行うようにす
る。ただし、低圧ガスホルダ圧がPL未満、すなわち、0.
69MPa未満の場合には、流量調節弁を開とし、緊急バッ
クアップとして低圧ガスホルダへの酸素ガスの導入、貯
蔵を行う。
When the high-pressure gas holder pressure current value (PV) is less than PL, compressed oxygen is supplied from the oxygen compressor, and the low-pressure gas holder pressure and the high-pressure gas holder pressure are compared, and (low-pressure gas holder pressure)> (High pressure gas holder pressure)
In this case, the flow control valve is opened to supply the gas from the low-pressure gas holder to both the high-pressure gas holder and the low-pressure gas using equipment. Although not shown in the table, the flow regulating valve is also opened when the low-pressure gas holder pressure is higher than HH. On the other hand, when (low-pressure gas holder pressure) ≦ (high-pressure gas holder pressure), the flow control valve is closed, and gas is supplied from the low-pressure gas holder only to the equipment using low-pressure gas. However, the low pressure gas holder pressure is less than PL, that is, 0.
If the pressure is lower than 69 MPa, the flow control valve is opened, and oxygen gas is introduced into the low-pressure gas holder and stored as an emergency backup.

【0022】すなわち、本発明のガス供給方法では、低
圧ガスホルダの圧力がその下限設定値未満のときは、ガ
スの流量調節弁を開として低圧ガスホルダへのガスの充
填を行い、低圧ガスホルダの圧力(低圧ガスホルダ圧)
と高圧ガスホルダの圧力(高圧ガスホルダ圧)の関係
が、(低圧ガスホルダ圧)>(高圧ガスホルダ圧)であ
り、かつ、低圧ガスホルダの圧力が下限設定値以上であ
るとき、前記流量調節弁を開とし、低圧ガスホルダのガ
スを高圧ガスホルダにも供給するようにし、高圧ガスホ
ルダと低圧ガス使用設備の両方にガスを送給し、(低圧
ガスホルダ圧)≦(高圧ガスホルダ圧)であり、かつ、
低圧ガスホルダ圧が下限設定値以上であるときは、前記
流量調節弁を閉とし、ガスを低圧ガス使用設備にのみ送
給するようにしたことを特徴とする。
That is, in the gas supply method of the present invention, when the pressure of the low-pressure gas holder is less than the lower limit set value, the gas flow control valve is opened to fill the low-pressure gas holder with the gas, and the pressure of the low-pressure gas holder is reduced. Low pressure gas holder pressure)
When the relationship between the pressure of the high-pressure gas holder and the pressure of the high-pressure gas holder (high-pressure gas holder pressure) is (low-pressure gas holder pressure)> (high-pressure gas holder pressure) and the pressure of the low-pressure gas holder is equal to or higher than the lower limit set value, the flow control valve is opened. The gas in the low-pressure gas holder is also supplied to the high-pressure gas holder, and the gas is supplied to both the high-pressure gas holder and the equipment using the low-pressure gas, (low-pressure gas holder pressure) ≦ (high-pressure gas holder pressure), and
When the low-pressure gas holder pressure is equal to or higher than the lower limit set value, the flow control valve is closed, and the gas is supplied only to the equipment using the low-pressure gas.

【0023】[0023]

【実施例】図1に示す一貫製鉄所における酸素供給ライ
ンに、本発明のガス供給方法を適用した。なお、図中に
は表示していないが、酸素圧縮機の出口近傍に逆止弁を
設けている。すなわち、低圧ガスホルダの圧力がその下
限設定値未満のときは、ガスの流量調節弁を開としてガ
スの充填を行い、低圧ガスホルダの圧力(低圧ガスホル
ダ圧)と高圧ガスホルダの圧力(高圧ガスホルダ圧)の
関係が、(低圧ガスホルダ圧)>(高圧ガスホルダ圧)
であり、かつ、低圧ガスホルダ圧が下限設定値以上であ
るとき、前記流量調節弁を開とし、低圧ガスホルダのガ
スを高圧ガスホルダにも供給するようにし、高圧ガス使
用設備と低圧ガス使用設備の両方にガスを送給し、(低
圧ガスホルダ圧)≦(高圧ガスホルダ圧)であり、か
つ、低圧ガスホルダ圧が下限設定値以上であるときは、
前記流量調節弁を閉とし、ガスを低圧ガス使用設備にの
み送給するようにした。
EXAMPLE The gas supply method of the present invention was applied to an oxygen supply line in an integrated steelworks shown in FIG. Although not shown in the figure, a check valve is provided near the outlet of the oxygen compressor. That is, when the pressure of the low pressure gas holder is less than the lower limit set value, the gas flow control valve is opened to fill the gas, and the pressure of the low pressure gas holder (low pressure gas holder pressure) and the pressure of the high pressure gas holder (high pressure gas holder pressure) are reduced. The relationship is (low pressure gas holder pressure)> (high pressure gas holder pressure)
And, when the low-pressure gas holder pressure is equal to or higher than the lower limit set value, the flow control valve is opened, so that the gas in the low-pressure gas holder is also supplied to the high-pressure gas holder, and both the high-pressure gas using equipment and the low-pressure gas using equipment are used. When the gas is supplied to (low pressure gas holder pressure) ≦ (high pressure gas holder pressure) and the low pressure gas holder pressure is equal to or higher than the lower limit set value,
The flow control valve was closed, and gas was supplied only to equipment using low-pressure gas.

【0024】なお、その際の高圧ガスホルダ圧と低圧ガ
スホルダ圧のトレンド例を図2に示す。図2は、従来の
ガス供給方法としてすでに説明した図4に対応して記載
している。図2から明らかなように、本発明によって、
従来では問題となっていた低圧ガスホルダ圧の方が高圧
ガスホルダ圧よりも高くなってしまう現象がほぼ解消さ
れていることがわかる。
FIG. 2 shows a trend example of the high-pressure gas holder pressure and the low-pressure gas holder pressure at that time. FIG. 2 corresponds to FIG. 4 already described as a conventional gas supply method. As is apparent from FIG. 2, according to the present invention,
It can be seen that the problem that the low-pressure gas holder pressure, which has conventionally been a problem, becomes higher than the high-pressure gas holder pressure has been almost eliminated.

【0025】次に、図3に基づき、酸素ガス供給ライン
における幾つかの具体的な供給状態の例を挙げ、酸素ガ
ス供給をどのように行っているかを説明する。図3は、
図2(b)で示すトレンドにおいてa、b、cの矢印で
示す各時点での酸素ガス供給状態を説明する模式図であ
る。このa、b、cは、図3における(a)、(b)、
(c)に対応させている。
Next, based on FIG. 3, some specific examples of supply states in the oxygen gas supply line will be described to explain how the oxygen gas is supplied. FIG.
FIG. 3 is a schematic diagram illustrating an oxygen gas supply state at each time point indicated by arrows a, b, and c in the trend illustrated in FIG. These a, b, and c are (a), (b),
(C).

【0026】図3(a)のピーク吹錬中では、流量調節
弁8が開とされ、高圧ガス使用設備(転炉、溶融還元
炉、脱炭炉)13での酸素ガス不足分を低圧ガスホルダ9
から払い出すようにする。図3(b)のピーク吹錬終了
後では、流量調節弁8を閉とし、高圧ガスホルダ7のみ
に酸素ガスを供給する。
During the peak blowing shown in FIG. 3A, the flow control valve 8 is opened, and the oxygen gas shortage in the high pressure gas use equipment (converter, smelting reduction furnace, decarburization furnace) 13 is reduced by a low pressure gas holder. 9
To pay out from. After the peak blowing in FIG. 3B, the flow control valve 8 is closed, and oxygen gas is supplied only to the high-pressure gas holder 7.

【0027】また、図3(c)の吹錬の切れ間では、高
圧ガスホルダ7の圧力が上限となった時点で流量調節弁
8を開とし、低圧ガスホルダ9に酸素ガスの放散回収を
行うようにする。一方、従来例のガス供給方法について
は、従来の技術として図4に基づいて説明したとおりで
ある。
In the period of blowing shown in FIG. 3C, when the pressure of the high-pressure gas holder 7 reaches the upper limit, the flow rate control valve 8 is opened, and the low-pressure gas holder 9 is allowed to diffuse and collect oxygen gas. I do. On the other hand, a conventional gas supply method is as described with reference to FIG. 4 as a conventional technique.

【0028】本発明例においては、従来例よりも酸素ガ
スを大気放散した割合が約2.5 %削減することができ
た。そして、その結果、本発明例では酸素プラントの消
費電力を従来例から約795KWH/Hr削減することができ
た。なお、高圧ガスホルダには、高圧ガス使用設備のみ
を接続した例を示したが、低圧ガス使用設備も接続され
ていてもよい。
In the example of the present invention, the rate of oxygen gas emission to the atmosphere was reduced by about 2.5% as compared with the conventional example. As a result, in the example of the present invention, the power consumption of the oxygen plant was reduced by about 795 kWh / hr from the conventional example. In addition, although the example which connected only the high pressure gas using equipment to the high pressure gas holder was shown, the low pressure gas using equipment may also be connected.

【0029】また、低圧ガスホルダには、複数の低圧ガ
ス使用設備が接続されていてもよい。
Further, the low-pressure gas holder may be connected to a plurality of facilities using low-pressure gas.

【0030】[0030]

【発明の効果】本発明によって、従来ピーク使用時にお
いて逼迫していた高圧側のガスバランスを緩和すること
が可能となり、また、低圧ガスホルダ圧を下限近くまで
下げての運用が可能となった。その結果、低圧ガスホル
ダの能力を十分に発揮させることができるようになり、
圧力運用幅を広げた操業が可能となり、大気中への無用
のガス放散を大幅に削減できるようになり、ひいては、
酸素プラントの消費電力を大幅に削減することができる
ようになった。
According to the present invention, the gas balance on the high pressure side which has been tight in the past during peak use can be alleviated, and the low pressure gas holder pressure can be reduced to near the lower limit. As a result, the ability of the low-pressure gas holder can be fully exhibited,
Operation with a wider range of pressure operation is possible, and unnecessary gas emission to the atmosphere can be significantly reduced, and as a result,
The power consumption of the oxygen plant can be greatly reduced.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明を適用するのに好適なガス供給ラインの
一例を示す模式図である。
FIG. 1 is a schematic diagram showing an example of a gas supply line suitable for applying the present invention.

【図2】本発明を適用した場合の高圧ガスホルダと低圧
ガスホルダのそれぞれのホルダ圧の推移を示すグラフで
ある。
FIG. 2 is a graph showing changes in the holder pressure of a high-pressure gas holder and a low-pressure gas holder when the present invention is applied.

【図3】本発明を適用した場合の各状態におけるガス供
給ラインのガスの流れを説明するための模式図である。
FIG. 3 is a schematic diagram for explaining a gas flow in a gas supply line in each state when the present invention is applied.

【図4】従来の高圧ガスホルダと低圧ガスホルダのそれ
ぞれのホルダ圧の推移を示すグラフである。
FIG. 4 is a graph showing changes in the respective holder pressures of a conventional high-pressure gas holder and a low-pressure gas holder.

【符号の説明】[Explanation of symbols]

1 空気圧縮機 2 水洗冷却塔 3 モリキュラシーブス吸着器 4 コールドボックス(精留塔、主熱交換器等) 5 酸素圧縮機 6 酸素放散弁 7 高圧ガスホルダ 8 流量調節弁 9 低圧ガスホルダ 10a 、10b 圧力計 11 シーケンス制御装置 12 高炉(低圧ガス使用設備) 13 転炉(高圧ガス使用設備) DESCRIPTION OF SYMBOLS 1 Air compressor 2 Rinsing cooling tower 3 Molecular sieves adsorber 4 Cold box (rectification tower, main heat exchanger, etc.) 5 Oxygen compressor 6 Oxygen dissipating valve 7 High pressure gas holder 8 Flow control valve 9 Low pressure gas holder 10a, 10b Pressure Total 11 Sequence controller 12 Blast furnace (Low pressure gas equipment) 13 Converter (High pressure gas equipment)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 昇圧したガスを、高圧ガスホルダを介し
て高圧ガス使用設備に供給し、かつ、ガス入側にガスの
流量を調節する流量調節弁を有する低圧ガスホルダを介
して低圧ガス使用設備に供給するガス供給方法であっ
て、前記の低圧ガスホルダの圧力と高圧ガスホルダの圧
力の関係が、(低圧ガスホルダの圧力)>(高圧ガスホ
ルダの圧力)であり、かつ、低圧ガスホルダの圧力が下
限設定値以上であるときは、前記流量調節弁を開とし
て、低圧ガスホルダのガスを高圧ガスホルダにも送給
し、(低圧ガスホルダの圧力)≦(高圧ガスホルダの圧
力)であり、かつ、低圧ガスホルダの圧力が下限設定値
以上であるときは、前記流量調節弁を閉として、低圧ガ
スホルダのガスを低圧ガス使用設備にのみ送給するよう
にしたことを特徴とするガス供給方法。
The pressurized gas is supplied to a high-pressure gas-using facility via a high-pressure gas holder, and is supplied to a low-pressure gas-using facility via a low-pressure gas holder having a flow control valve for adjusting a gas flow rate on a gas inlet side. In the gas supply method, the relationship between the pressure of the low-pressure gas holder and the pressure of the high-pressure gas holder is (low-pressure gas holder pressure)> (high-pressure gas holder pressure), and the low-pressure gas holder pressure is a lower limit set value. When the above is the case, the flow control valve is opened, the gas in the low-pressure gas holder is also supplied to the high-pressure gas holder, and (pressure of the low-pressure gas holder) ≦ (pressure of the high-pressure gas holder), and the pressure of the low-pressure gas holder is When the gas flow rate is equal to or higher than the lower limit value, the flow rate control valve is closed so that the gas in the low-pressure gas holder is supplied only to the low-pressure gas use facility. Supply method.
JP2000028143A 2000-02-04 2000-02-04 Gas supplying method Pending JP2001221399A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000028143A JP2001221399A (en) 2000-02-04 2000-02-04 Gas supplying method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000028143A JP2001221399A (en) 2000-02-04 2000-02-04 Gas supplying method

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2010118191A Division JP5012955B2 (en) 2010-05-24 2010-05-24 Gas supply method

Publications (1)

Publication Number Publication Date
JP2001221399A true JP2001221399A (en) 2001-08-17

Family

ID=18553598

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000028143A Pending JP2001221399A (en) 2000-02-04 2000-02-04 Gas supplying method

Country Status (1)

Country Link
JP (1) JP2001221399A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111947031A (en) * 2019-05-15 2020-11-17 宝山钢铁股份有限公司 Wiggins type gas chamber operation system and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111947031A (en) * 2019-05-15 2020-11-17 宝山钢铁股份有限公司 Wiggins type gas chamber operation system and method
CN111947031B (en) * 2019-05-15 2022-03-18 宝山钢铁股份有限公司 Wiggins type gas chamber operation system and method

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