JPH04338102A - Method for enriching combustible gas with hydrogen - Google Patents

Method for enriching combustible gas with hydrogen

Info

Publication number
JPH04338102A
JPH04338102A JP10587691A JP10587691A JPH04338102A JP H04338102 A JPH04338102 A JP H04338102A JP 10587691 A JP10587691 A JP 10587691A JP 10587691 A JP10587691 A JP 10587691A JP H04338102 A JPH04338102 A JP H04338102A
Authority
JP
Japan
Prior art keywords
melting
furnace
combustible gas
amount
gas
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.)
Withdrawn
Application number
JP10587691A
Other languages
Japanese (ja)
Inventor
Kimiaki Otawa
大多和 公昭
Hiroaki Kaneda
金田 博晶
Masayasu Sakai
正康 坂井
Masahiro Tokuda
徳田 雅寛
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP10587691A priority Critical patent/JPH04338102A/en
Publication of JPH04338102A publication Critical patent/JPH04338102A/en
Withdrawn legal-status Critical Current

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  • Industrial Gases (AREA)

Abstract

PURPOSE:To enrich the combustible gas generated in melting iron with hydrogen to obtain a gas appropriate for methanol synthesis without hindering the operation of melting iron. CONSTITUTION:An org. fuel and reduced iron are supplied to a melting and gasifying furnace to produce molten iron and a combustible gas. In this case, the content of the fixed carbon in coal as the fuel to be added to the furnace is controlled to 0.3ton per ton of the product pig iron. The amt. of an oxygen- contg. gas to be blown into the furnace is adjusted so that the molten iron in the furnace is controlled to a specified temp. The amt. of hydrogen to be blown into the furnace is adjusted so that the ratio of the number of mols of the total carbon in the combustible gas generated from the furnace to that of the total oxygen is specified.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は溶解ガス化炉で発生する
可燃性ガスの水素富化方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for hydrogen enriching combustible gas generated in a melting gasifier.

【0002】0002

【従来の技術】銑鉄の製造はその大半を高炉法に頼って
いるが、周知の如く高炉法では高品質の原料炭および鉄
鉱石が必要であるため、今後の原料事情悪化に備えてそ
の代替法として溶融製銑法が注目されてきている。溶融
製銑法は、低品位炭や低品質の鉄鉱石が使用でき、かつ
高炉法で必要とされるコークス製造及び鉄鉱石焼結など
を必要としない画期的な製銑法であるが、製銑時に発生
する可燃性ガスが膨大となり、その有効利用が製銑の経
済性を左右している。このため、揮発分の多い一般炭の
使用制限は勿論、石炭供給量等の操業条件設定に制約を
設けざるを得ないなどの不都合が生じている。
[Prior Art] Most of the production of pig iron relies on the blast furnace method, but as is well known, the blast furnace method requires high-quality coking coal and iron ore, so it is possible to replace it in preparation for future deterioration of the raw material situation. As a method, the molten ironmaking method is attracting attention. The molten ironmaking method is an innovative ironmaking method that allows the use of low-grade coal and low-quality iron ore, and does not require coke production or iron ore sintering, which are required in the blast furnace method. A huge amount of flammable gas is generated during iron making, and its effective use determines the economic efficiency of iron making. For this reason, there are inconveniences such as not only restrictions on the use of steam coal with a high volatile content but also restrictions on the setting of operating conditions such as coal supply amount.

【0003】一方、地球温暖化の元凶とされる炭酸ガス
の発生抑制の観点から、炭酸ガスの除去および炭素含有
量の少ないクリーンエネルギの出現が社会的ニーズとな
ってきている。本発明はこのような背景のもと、溶融製
銑法による製銑時に発生する可燃性ガスから、クリーン
エネルギであるメタノールを効率的に製造できれば、前
記製銑および炭酸ガスの問題に対する社会的要請に応じ
られるとの観点でなされたものである。
On the other hand, from the viewpoint of suppressing the generation of carbon dioxide gas, which is considered to be the cause of global warming, the removal of carbon dioxide gas and the emergence of clean energy with low carbon content have become social needs. Against this background, the present invention aims to meet the social demands for solving the problem of iron making and carbon dioxide gas by efficiently producing methanol, which is a clean energy source, from flammable gas generated during iron making using the molten iron making method. This was done with the aim of meeting the needs of the public.

【0004】周知の通り、メタノールを合成するための
原料ガスの成分は水素(H2 )、一酸化炭素(CO)
、炭酸ガス(CO2 )であり、その組成は、H2 /
(3CO2 +2CO)=1の条件を満たす必要がある
。すなわち、原料ガス中の水素含量を多くする必要があ
るが、製銑で発生するガスは、その発生源が石炭である
ため、水素の含量が少ない。
As is well known, the raw material gas components for methanol synthesis are hydrogen (H2) and carbon monoxide (CO).
, carbon dioxide gas (CO2), whose composition is H2/
It is necessary to satisfy the condition of (3CO2 +2CO)=1. That is, although it is necessary to increase the hydrogen content in the raw material gas, the gas generated during iron making has a low hydrogen content because its source is coal.

【0005】水素含量が少ないガスをメタノール原料ガ
スとするためには、COをH2 に転換するいわゆるC
Oシフト反応操作が必要であり、水素含量が少なければ
少ないほどその転換量を多くしなければならず、それに
ともなってメタノールの取得量が少なくなる。従って、
製銑操作に支障をきたさない範囲内においては、溶融製
銑工程で水素富化の可燃性ガスを発生させるのが得策で
ある。
[0005] In order to use a gas with a low hydrogen content as a raw material gas for methanol, it is necessary to convert CO into H2.
O-shift reaction operation is necessary, and the lower the hydrogen content, the greater the amount of conversion must be, and the less methanol can be obtained. Therefore,
It is advisable to generate hydrogen-enriched combustible gas during the melt ironmaking process, within a range that does not interfere with the ironmaking operation.

【0006】水素富化の手段としては、石炭のガス化操
作等で水蒸気を吹込むことが公知となっており、また溶
融製銑操作においても、特開昭58−171510号公
報で生成ガスの温度制御を目的に水蒸気を吹込み、その
結果として水素富化が図れることが紹介されている。
[0006] As a means of hydrogen enrichment, it is known to inject steam in coal gasification operations, and also in molten pig iron making operations, Japanese Patent Laid-Open No. 171510/1983 discloses the method of injecting steam into the produced gas. It is introduced that water vapor can be injected for the purpose of temperature control, and hydrogen enrichment can be achieved as a result.

【0007】[0007]

【発明が解決しようとする課題】溶融製銑操作において
は、その操作を行う溶解ガス化炉で発生する可燃性ガス
を、鉄鉱石の還元ガスとして使用する都合上、同ガスに
還元ポテンシヤル(可燃性ガス中のCO+H2 の濃度
)を持たす必要があり、また溶解ガス化炉内に溶融製銑
に必要な炭素分を所定量保有しておく必要があることか
ら、単に可燃性ガスの水素富化を図る目的、あるいは温
度制御を目的としてのみ、水蒸気を吹込むことはできな
い。
[Problems to be Solved by the Invention] In molten iron making operations, the flammable gas generated in the melting and gasifying furnace that performs the operation is used as reducing gas for iron ore, so it is difficult to reduce the reduction potential (flammable gas) to the gas. It is necessary to have a certain amount of carbon (CO + H2 concentration in the combustible gas), and it is also necessary to have a certain amount of carbon necessary for molten pig iron production in the melting and gasifying furnace. Steam cannot be blown solely for the purpose of achieving temperature control or for the purpose of temperature control.

【0008】周知の通り、溶融製銑操作は、溶解ガス化
炉内に石炭等の燃料を添加し、これを酸素で部分燃焼さ
せて一酸化炭素(CO)及び水素(H2 )を主成分と
する可燃性ガスを発生させるとともに、ガス化炉に還元
鉄を投入して溶融製銑を製造するとともに、ガス化炉で
発生可燃性ガスで鉄鉱石を還元し、還元鉄を製造する操
作である。
[0008] As is well known, in the melting ironmaking operation, fuel such as coal is added to a melting and gasifying furnace, and this is partially combusted with oxygen to produce carbon monoxide (CO) and hydrogen (H2) as the main components. This is an operation in which flammable gas is generated and reduced iron is introduced into a gasifier to produce molten pig iron, and iron ore is reduced with the flammable gas generated in the gasifier to produce reduced iron. .

【0009】すなわち、酸素によって燃料中の炭素も消
費され、それにともなって溶解ガス化炉内温度も上昇す
る。この温度上昇を制御するため水蒸気を吹込むと、炭
素分との水成反応でH2 とCOを発生させることにな
るが、炭素も消費されることになる。従って、水蒸気の
過剰吹込みがあると、必要以上に炭素分を消費すること
になり、溶融製銑に必要な炭素分の保有が不可能となる
ばかりでなく、溶解ガス化炉内の温度保持上、燃料の燃
焼量を増やすことにもなり、また酸素の浪費にもつなが
る結果となる。
That is, carbon in the fuel is also consumed by oxygen, and the temperature inside the melting and gasifying furnace increases accordingly. If water vapor is injected to control this temperature rise, H2 and CO will be generated through a hydrochemical reaction with carbon, but carbon will also be consumed. Therefore, if there is excessive injection of steam, carbon content will be consumed more than necessary, which will not only make it impossible to retain the carbon content necessary for molten iron making, but also make it difficult to maintain the temperature in the melting and gasifying furnace. Moreover, this results in an increase in the amount of fuel burned, and also leads to a waste of oxygen.

【0010】また、溶融製銑操作で発生する可燃性ガス
をメタノールの合成原料として使用する場合は、水素富
化に加えて、組成が安定していることが重要である。組
成変動があるとCOシフト操作等の原料調整工程への負
荷変動のみならず、その結果として前述したメタノール
合成用原料ガスの組成条件が変動することになり、好ま
しくないが、温度制御を目途に水蒸気を吹込んだ場合、
ガス組成が変動することは容易に理解できよう。
[0010] Furthermore, when the flammable gas generated in the molten pig iron making operation is used as a raw material for methanol synthesis, it is important that the composition is stable in addition to hydrogen enrichment. If there is a change in composition, it will not only change the load on the raw material adjustment process such as CO shift operation, but also change the composition conditions of the raw material gas for methanol synthesis as mentioned above, which is not preferable, but it can be used for temperature control. When steam is blown into the
It is easy to understand that the gas composition varies.

【0011】加えて、製銑操作と併行してメタノール合
成を行う場合、プラントのフレキシビリテイを確認する
上から、メタノール合成側の要求に応じて溶融製銑操作
に支障をきたすことなく溶解ガス化炉での発生ガス量が
調節できなければならない。すなわち、溶解ガス化炉へ
の燃料供給量を増減する必要があるが、従来の方法では
このような状況への対応は全く不可能である。
In addition, when methanol synthesis is performed in parallel with ironmaking operations, it is necessary to confirm the flexibility of the plant, and in accordance with the requirements of the methanol synthesis side, dissolved gas can be synthesized without interfering with the molten ironmaking operation. It is necessary to be able to adjust the amount of gas generated in the chemical furnace. That is, it is necessary to increase or decrease the amount of fuel supplied to the melting and gasifying furnace, but it is completely impossible to deal with such a situation using conventional methods.

【0012】本発明は、溶融製銑で発生する可燃性ガス
からメタノールを製造して製銑の経済性向上及び炭酸ガ
スの排出抑制を可能にするため、溶融製銑で発生する可
燃性ガスを、溶融製銑操作に支障をきたすことなく、メ
タノール合成に適した水素富化とし、かつ安定して製造
できる方法を提供することを目的とするものである。す
なわち本発明は、溶融製銑の安定操作に必要な可燃性ガ
スの還元ポテンシヤルの保持、溶解ガス化炉内に所定量
の炭素分(コークス)の保持および溶解ガス化炉内温度
の適正維持を図りつつ、 (イ)水蒸気を吸込んで可燃性ガスを水素富化とすると
ともに可燃性ガスの組成変動を最小限とする。 (2)溶解ガス化炉への酸素吹込み量を必要最小限とす
る。 (3)溶解ガス化炉への燃料供給量を増減して、可燃性
ガスの発生量が増減できる。
[0012] The present invention produces methanol from the flammable gas generated in molten pig iron making, thereby improving the economic efficiency of pig iron making and suppressing carbon dioxide emissions. It is an object of the present invention to provide a method for enriching hydrogen suitable for methanol synthesis and stably producing it without hindrance to molten pig iron making operations. That is, the present invention maintains the reduction potential of combustible gas necessary for stable operation of molten pig iron, maintains a predetermined amount of carbon (coke) in the melting gasifier, and maintains an appropriate temperature inside the melting gasifier. (a) Enrich the flammable gas with hydrogen by inhaling water vapor and minimize compositional fluctuations in the flammable gas. (2) Minimize the amount of oxygen blown into the melting and gasifying furnace. (3) The amount of combustible gas generated can be increased or decreased by increasing or decreasing the amount of fuel supplied to the melting gasifier.

【0013】溶解ガス化炉で発生する可燃性ガスの水素
富化方法を提供することを目的とするものである。
[0013] It is an object of the present invention to provide a method for enriching combustible gas with hydrogen generated in a melting gasifier.

【0014】[0014]

【課題を解決するための手段】溶解ガス化炉に石炭(コ
ークスを含む)または石炭と他の有機物燃料(以下総称
して燃料という)を添加し、該燃料を酸素により部分燃
焼ガス化して一酸化炭素および水素を主成分とする可燃
性ガスを発生させるとともに、溶解ガス化炉に還元鉄(
1部還元された状態を含む)を添加して溶融製銑を製造
し、また溶解ガス化炉で発生する前記可燃性ガスの1部
または全量でもって鉄鉱石を還元して前記還元鉄を製造
する方法において、 (1)溶解ガス化炉に添加される燃料中の石炭の固定炭
素分の量が製品銑鉄1tonあたり0.3ton以上に
なるように燃料を添加する。 (2)溶解ガス化炉の溶銑温度が所定の温度になるよう
に、溶解ガス化炉内に吹込む酸素含有ガス量を調節する
。 (3)溶解ガス化炉から発生する可燃性ガス中の全炭素
成分(CO,CO2)のモル数に対する全酸素成分(C
O,CO2 ,H2 O)のモル数の比(以下O2 /
C比という)が、所定の値になるように、溶解ガス化炉
内に吹込む水蒸気量を調節する。
[Means for solving the problem] Coal (including coke) or coal and other organic fuels (hereinafter collectively referred to as fuel) is added to a melting gasifier, and the fuel is partially combusted and gasified with oxygen. In addition to generating flammable gas mainly composed of carbon oxide and hydrogen, reduced iron (
(including a partially reduced state) to produce molten pig iron, and reduce iron ore with part or all of the flammable gas generated in the melting and gasifying furnace to produce the reduced iron. In the method, (1) Fuel is added so that the fixed carbon content of coal in the fuel added to the melting-gasifier becomes 0.3 ton or more per 1 ton of product pig iron. (2) Adjust the amount of oxygen-containing gas blown into the melting and gasifying furnace so that the temperature of the hot metal in the melting and gasifying furnace becomes a predetermined temperature. (3) The total oxygen component (C
The ratio of the number of moles of O, CO2, H2 O) (hereinafter referred to as O2 /
The amount of steam blown into the melting and gasifying furnace is adjusted so that the C ratio) becomes a predetermined value.

【0015】[0015]

【作用】溶融製銑操作の安定化のためには、前述した如
く、(1)溶解ガス化炉内温度の適正維持、(2)溶解
ガス化炉内に炭素分が保持されていること、(3)溶解
ガス化炉で発生する可燃性ガスが、鉄鉱石還元に必要な
還元ポテンシヤルを保持していることが必要である。
[Function] In order to stabilize the molten pig iron making operation, as mentioned above, (1) maintaining the temperature in the melting and gasifying furnace at an appropriate level, (2) maintaining carbon content in the melting and gasifying furnace, (3) It is necessary that the combustible gas generated in the melting gasification furnace maintains the reduction potential necessary for iron ore reduction.

【0016】まず、溶解ガス化炉内温度の適正維持であ
るが、該ガス化炉に燃料が供給されている状態で溶解ガ
ス化炉内温度と連動している溶銑温度を検出して、その
温度が所定の値になるように酸素含有ガスの吹込み量を
調節した場合、その吹込み量が溶解ガス化炉の温度維持
に必要最小限の酸素含有ガス吹込み量となる。また、溶
解ガス化炉に供給される燃料の組成は、実質上一定組成
であり、溶解ガス化炉内温度が一定に保持されている場
合、該ガス化炉で発生する可燃性ガスの還元ポテンシヤ
ルは、該ガスのO2 /C比によって決まり、また溶解
ガス化炉内でガス化される炭素分の量もこのO2 /C
比によって決まる。従って、可燃性ガスの還元ポテンシ
ヤルを損わずかつ溶解ガス化炉内に炭素分が保有される
状態のO2 /C比を選定し、その値が一定になるよう
に水蒸気を吹込むと、その吹込み量が溶融製銑操作に支
障をきたさない上での水蒸気の最大吹込み量となり、可
燃性ガス中の水素含量が最大となる。また、ガス中のO
2 /C比を一定に保つことで、ガス組成の変動が小さ
くなることは、容易に理解できよう。
First, to properly maintain the temperature inside the melting and gasifying furnace, the hot metal temperature, which is linked to the temperature inside the melting and gasifying furnace, is detected while fuel is being supplied to the gasifying furnace. When the amount of oxygen-containing gas blown is adjusted so that the temperature becomes a predetermined value, the amount of blown oxygen-containing gas becomes the minimum amount necessary to maintain the temperature of the melting and gasifying furnace. In addition, the composition of the fuel supplied to the melting gasifier is substantially constant, and if the temperature inside the melting gasifier is kept constant, the reduction potential of the combustible gas generated in the gasifier is is determined by the O2 /C ratio of the gas, and the amount of carbon gasified in the melting-gasifier also depends on this O2 /C ratio.
Determined by ratio. Therefore, by selecting an O2/C ratio that does not impair the reduction potential of combustible gas and retaining carbon content in the melting gasifier, and injecting steam so that the value remains constant, the This amount is the maximum amount of steam that can be blown in without causing any trouble to the molten pig iron making operation, and the hydrogen content in the combustible gas is maximized. Also, O in the gas
It is easy to understand that by keeping the 2 /C ratio constant, fluctuations in gas composition are reduced.

【0017】次に燃料供給量増減への対応性であるが、
溶解ガス化炉が定常常態で操業されている時、可燃性ガ
スの発生量を多くするなどの目的で、溶解ガス化炉への
燃料供給量を増やしたとすると、燃料の熱分解熱で溶解
ガス化炉内温度が降温し、溶銑温度が低下してくる。溶
銑温度が低下すれば、設定温度維持のため酸素含有ガス
の吹込み量が増加していくとともに、その条件変動に応
じた水蒸気の吹込み量が調節されていき、結果として燃
料供給量の増加分に応じた最適の酸素含有ガスおよび水
蒸気の吹込み量が設定される。
Next, regarding the response to changes in fuel supply amount,
When the melting gasifier is operated in a steady state, if the amount of fuel supplied to the melting gasifier is increased for the purpose of increasing the amount of combustible gas generated, the melted gas will increase due to the heat of thermal decomposition of the fuel. The temperature inside the heat treatment furnace decreases, and the temperature of the hot metal decreases. As the hot metal temperature decreases, the amount of oxygen-containing gas blown increases to maintain the set temperature, and the amount of steam blown is adjusted in response to changes in conditions, resulting in an increase in the amount of fuel supplied. The optimal amount of oxygen-containing gas and water vapor to be blown is set according to the time.

【0018】すなわち、溶銑温度が所定値になるように
、溶解ガス化炉への酸素含有ガス吹込み量を調節すると
ともに、該ガス化炉から発生する可燃性ガスのO2 /
C比が所定値になるように水蒸気を吹込む本発明の方法
をとれば、溶融製銑操作に支障をきたすことなく、酸素
含有ガスの吹込み量を必要最小限に、可燃性ガスの組成
変動を最小限に、可燃性ガス中の水素含量を最大にでき
るとともに、燃料供給量の増減、すなわち可燃性ガス発
生量の増減が容易となる。
That is, the amount of oxygen-containing gas blown into the melting and gasifying furnace is adjusted so that the temperature of the hot metal reaches a predetermined value, and the O2 /
By using the method of the present invention in which steam is injected so that the C ratio becomes a predetermined value, the composition of the combustible gas can be adjusted to the minimum necessary amount of oxygen-containing gas without interfering with the molten pig iron making operation. The hydrogen content in the combustible gas can be maximized while minimizing fluctuations, and the amount of fuel supplied, that is, the amount of combustible gas generated, can be easily increased or decreased.

【0019】[0019]

【実施例】次に実施例に基づき本発明を詳細に説明する
。図1は本発明の実施態様を示す系統図であり、図にお
いて、1は溶解ガス化炉を示し、2は溶解ガス化炉へ供
給する還元鉄を製造するための予備還元炉を示す。予備
還元炉で製造された還元鉄(1部還元を含む)の溶解ガ
ス化炉への供給は導管3から行い、溶解ガス化炉への燃
料の供給は導管4から行い、酸素含有ガスの吹込みは導
管5から行い、水蒸気の吹込みは導管6から行われる。 また溶解ガス化炉には、必要に応じ石灰石等の造滓剤を
、燃料とともに導管4または別途設けた装入口(図示な
し)から装入され、滓の塩基度、流動性、脱硫効果等が
調節される。
EXAMPLES Next, the present invention will be explained in detail based on examples. FIG. 1 is a system diagram showing an embodiment of the present invention. In the diagram, 1 indicates a melting and gasifying furnace, and 2 indicates a preliminary reduction furnace for producing reduced iron to be supplied to the melting and gasifying furnace. Reduced iron (including partial reduction) produced in the preliminary reduction furnace is supplied to the melting and gasifying furnace through conduit 3, fuel is supplied to the melting and gasifying furnace through conduit 4, and oxygen-containing gas is blown into the melting and gasifying furnace. The filling is carried out through conduit 5, and the injection of water vapor is carried out through conduit 6. In addition, a sludge-forming agent such as limestone is charged into the melting and gasifying furnace as necessary together with fuel through a conduit 4 or a charging port (not shown) provided separately, to improve the basicity, fluidity, desulfurization effect, etc. of the slag. adjusted.

【0020】溶解ガス化炉で製銑された溶銑は、スラグ
とともに導管7から取り出される。溶解ガス化炉で発生
する可燃性ガスは、導管8から固気分離器9に導入され
、固形分を分離した後、導管10から予備還元炉に吹込
まれ、分離した固形分は導管12から溶解ガス化炉に還
元される。予備還元炉に吹込まれる可燃性ガス量は予備
還元炉の操業条件によって適当に選定することができ、
余剰ガスがある場合は導管11からメタノール合成用原
料粗ガスとして取りだされる。
Hot metal produced in the melting and gasifying furnace is taken out from the conduit 7 together with slag. The combustible gas generated in the melting gasification furnace is introduced into the solid-gas separator 9 through a conduit 8, and after separating the solid content, it is blown into the preliminary reduction furnace through the conduit 10, and the separated solid content is dissolved through the conduit 12. It is reduced to the gasifier. The amount of combustible gas blown into the pre-reduction furnace can be appropriately selected depending on the operating conditions of the pre-reduction furnace.
If there is surplus gas, it is taken out from the conduit 11 as crude raw material gas for methanol synthesis.

【0021】予備還元炉に吹込まれる可燃性ガスは、炉
頂部付近から供給される鉄鉱石を還元した後、導管13
からメタノール合成用原料粗ガスとして取りだされる。 溶銑温度は温度検出器(イ)で検出され、該温度が所定
値になるよう調節計(ハ)で、酸素含有ガスの吹込み量
調節弁(ニ)の開度が調節される。また(ロ)は制御用
マイクロプロセツサーを示し、燃料・鉄鉱石・造滓剤の
組成および供給量などの溶解ガス化炉の操業条件から算
出される酸素含有ガス吹込み量の情報を、温度検出器(
イ)の情報の支援情報として使用する場合に採用され、
溶解ガス化炉の操業条件をひんぱんに変更するような場
合は有用である。
The combustible gas blown into the preliminary reduction furnace reduces the iron ore supplied from near the top of the furnace, and then passes through the conduit 13.
It is extracted as raw material gas for methanol synthesis. The temperature of the hot metal is detected by a temperature detector (a), and the opening degree of the oxygen-containing gas injection amount control valve (d) is adjusted by a controller (c) so that the temperature becomes a predetermined value. In addition, (b) shows a control microprocessor, which outputs information on the amount of oxygen-containing gas injected, which is calculated from the operating conditions of the melting and gasifier, such as the composition and supply amount of fuel, iron ore, and slag-forming agent. Temperature detector (
b) is adopted when the information is used as supporting information,
This is useful when the operating conditions of the melting gasifier are frequently changed.

【0022】溶銑温度すなわち温度調節の設定値は、1
400℃〜1700℃(好ましくは1450℃〜160
0℃)の範囲から選定される。また溶銑温度の検出器と
しては、接触タイプとしてはタングステンレニユウ熱電
対が適当であり、また非接触タイプとしては赤外線温度
計が採用できる。酸素含有ガスは、なるべく酸素純度の
高いものが好ましく、純度95容量%以上のものが適当
である。窒素などの不純物の含量が高いとメタノール合
成時に支障をきたす。
[0022] The hot metal temperature, that is, the setting value for temperature control is 1
400°C to 1700°C (preferably 1450°C to 160°C
0°C). As the hot metal temperature detector, a contact type tungsten thermocouple is suitable, and an infrared thermometer is suitable as a non-contact type. The oxygen-containing gas preferably has as high an oxygen purity as possible, and suitably has a purity of 95% by volume or more. High content of impurities such as nitrogen causes problems during methanol synthesis.

【0023】溶解ガス化炉で発生する可燃性ガスの組成
分析は、オンライン分析計(a)で行われ、導管10か
ら少量の可燃性ガスを略一定速度で抜出しつつ分析され
る。分析計としてはある程度の精度があれば分析時間の
短いのがよく、例えば質量分析と高速ガスクロマトグラ
フを併用する方式の分析計などが使用できる。分析値は
、制御用マイクロプロセツサー(b)で処理され、可燃
性ガスのO2 /C比(実用上は、可燃性ガス中の成分
の容量割合を使用して、〔CO2 +1/2(H2 O
+CO)〕/(CO+CO2+CH4 )が所定の値に
なるように、調節計(c)で、水蒸気の吹込み量調節弁
(d)の開度が調節される。
The composition analysis of the combustible gas generated in the melting gasification furnace is carried out using an on-line analyzer (a), and the analysis is performed while a small amount of combustible gas is extracted from the conduit 10 at a substantially constant rate. As long as the analyzer has a certain degree of accuracy, it is best to have a short analysis time; for example, an analyzer that uses mass spectrometry and high-speed gas chromatography in combination can be used. The analysis value is processed by the control microprocessor (b), and the O2 /C ratio of the combustible gas (in practice, using the volume ratio of the components in the combustible gas, it is calculated as [CO2 + 1/2 ( H2O
+CO)]/(CO+CO2+CH4) is a predetermined value, the controller (c) adjusts the opening degree of the water vapor injection amount control valve (d).

【0024】O2 /C比は、0.2〜0.7の範囲か
ら選定されるが、設定値の選定にあたっては、オンライ
ン分析計等で分析される可燃性ガス中の(H2 O+C
O2 )濃度、製品銑鉄中の炭素分濃度および燃料の組
成・供給量などの情報をもとに選定され、制御用プロセ
ツサー(b)でこれらの情報を処理し、調節計(c)の
O2 /C比の設定値を自動的に調節することも可能で
ある。
[0024] The O2/C ratio is selected from the range of 0.2 to 0.7, but when selecting the set value, the (H2 O + C
The control processor (b) processes this information, and the controller (c) controls the O2/ It is also possible to automatically adjust the set value of the C ratio.

【0025】予備還元炉に供給される可燃性ガスの温度
の調節が必要な場合は、導管11から抜出される可燃性
ガスを冷却した後、その1部を循環させるなどの公知の
手段が採用できる。予備還元炉に供給される可燃性ガス
中のCOおよびH2 は、鉄鉱石を還元してそれぞれC
O2 およびH2 Oとなり、導管13から抜出される
ガス中のCO2 およびH2 O濃度が高くなるが、こ
れらのCO2 およびH2 Oを除去することでメタノ
ール合成用原料に利用できる。また、鉄鉱石の還元にお
けるCOとH2 の消費率は略同じであり、水素富化さ
れた可燃性ガスが予備還元炉において、メタノール合成
用原料としての品位を損うものではない。
If it is necessary to adjust the temperature of the flammable gas supplied to the pre-reduction furnace, known means such as cooling the combustible gas extracted from the conduit 11 and then circulating a part of it may be adopted. can. CO and H2 in the combustible gas supplied to the pre-reduction furnace reduce iron ore and convert into carbon, respectively.
The gas becomes O2 and H2O, and the concentration of CO2 and H2O in the gas extracted from the conduit 13 increases, but by removing these CO2 and H2O, it can be used as a raw material for methanol synthesis. Furthermore, the consumption rates of CO and H2 in the reduction of iron ore are approximately the same, and the hydrogen-enriched combustible gas does not impair its quality as a raw material for methanol synthesis in the preliminary reduction furnace.

【0026】溶融製銑法としては、周知の如く予備還元
炉に流動層方式を使用するなど色々な方法が提案されて
いるが、いずれの方法においても溶解ガス化炉の機能は
同じであり、本発明の方法はいずれの溶融製銑法におい
ても有用である。次に本発明の具体的な実験結果につい
て説明する。 使用鉄鉱石:全鉄濃度68重量%、供給量1.47t/
hr 使用燃料:一般炭、組成:C71.19重量%、H2 
4.69重量%、O2 7.62重量%、N2 1.4
0重量%、S  0.29重量%、灰分12.4重量%
、固有水分2.41重量%、供給量1.36t/hr使
用酸素含有ガス:純度98容量%以上予備還元炉の型式
:移動床式シヤフト炉上記条件で、従来法と本発明の方
法の比較実験を実施した。
Various methods have been proposed for the molten pig iron making process, such as using a fluidized bed method in the preliminary reduction furnace, as is well known, but the function of the melting and gasifying furnace is the same in all methods. The method of the present invention is useful in any hot melt ironmaking process. Next, specific experimental results of the present invention will be explained. Iron ore used: Total iron concentration 68% by weight, supply amount 1.47t/
hr Fuel used: Steam coal, composition: C71.19% by weight, H2
4.69% by weight, O2 7.62% by weight, N2 1.4
0% by weight, S 0.29% by weight, ash 12.4% by weight
, inherent moisture 2.41% by weight, supply rate 1.36t/hrOxygen-containing gas used: Purity 98% by volume or more Pre-reduction furnace type: Moving bed shaft furnace Comparison of the conventional method and the method of the present invention under the above conditions An experiment was conducted.

【0027】従来法の実験では、酸素含有ガスの吹込み
量を略一定とし、水蒸気の吹込みは溶解ガス化炉出口の
可燃性ガス温度が1000℃になるよう吹込んだ。また
、酸素含有ガスの吹込みは、溶銑温度が1500℃にな
るように調節して吹込み、水蒸気の吹込みは可燃性ガス
中のO2 /C比が0.55になるように吹込んだ。
In experiments using the conventional method, the amount of oxygen-containing gas blown was kept approximately constant, and water vapor was blown in so that the temperature of the flammable gas at the outlet of the melting gasifier reached 1000°C. In addition, the oxygen-containing gas was blown in so that the hot metal temperature was 1500°C, and the steam was blown in so that the O2/C ratio in the combustible gas was 0.55. .

【0028】実験結果を表1に示す。The experimental results are shown in Table 1.

【0029】[0029]

【表1】[Table 1]

【0030】上記実験結果から明らかのように、従来法
に比較して本発明の方法は酸素含有ガスの吹込み量を削
減できる上、格段に水素富化された可燃性ガスが得られ
る。導管11および13から得られる可燃性ガスを、C
Oシフト反応操作、精製操作等で調整し、メタノール合
成を行ったとすると、従来法でのメタノール取得量は約
0.7t/t銑鉄、本発明の方法では約0.9t/t銑
鉄とメタノール取得量が大巾に向上する。
As is clear from the above experimental results, compared to the conventional method, the method of the present invention can reduce the amount of oxygen-containing gas blown into the gas, and can also obtain a combustible gas that is significantly enriched in hydrogen. The flammable gas obtained from conduits 11 and 13 is
Assuming that methanol synthesis is performed by adjusting the O shift reaction operation, purification operation, etc., the amount of methanol obtained by the conventional method is about 0.7 t/t pig iron, and the amount of methanol obtained by the method of the present invention is about 0.9 t/t pig iron and methanol. The quantity will be greatly improved.

【0031】[0031]

【発明の効果】本発明による可燃性ガスの水素富化方法
は、溶解ガス化炉に石炭または石炭と他の有機物燃料を
添加し、該燃料を酸素により部分燃焼ガス化して一酸化
炭素および水素を主成分とする可燃性ガスを発生させる
とともに、溶解ガス化炉に還元鉄(1部還元された状態
を含む)を添加して溶融銑鉄を製造するとともに、溶解
ガス化炉で発生する可燃性ガスの一部または全量でもっ
て鉄鉱石を還元して還元鉄を製造する方法において、溶
解ガス化炉に添加する燃料中の石炭の固定炭素分の量が
、製品銑鉄1tonあたり0.3ton以上になるよう
にし、また溶解ガス化炉の溶銑温度が所定値になるよう
に、同溶解ガス化炉内に吹込まれる酸素含有ガス量を調
節し、溶解ガス化炉から発生する可燃性ガス中の全炭素
成分のモル数に対する全酸素成分のモル数の比が所定値
になるように同溶解ガス化炉内に吹込まれる水蒸気量を
調節することにより、次の効果を有する。
Effects of the Invention The method for enriching hydrogen in combustible gas according to the present invention involves adding coal or coal and other organic fuel to a melting gasifier, and partially combustion gasifying the fuel with oxygen to produce carbon monoxide and hydrogen. At the same time, molten pig iron is produced by producing flammable gas mainly composed of In a method for producing reduced iron by reducing iron ore with part or all of the gas, the amount of fixed carbon in the coal in the fuel added to the melting and gasifier is 0.3 tons or more per 1 ton of pig iron product. The amount of oxygen-containing gas injected into the melting and gasifying furnace is adjusted so that the temperature of the hot metal in the melting and gasifying furnace reaches a predetermined value. By adjusting the amount of water vapor blown into the melting and gasifying furnace so that the ratio of the number of moles of all oxygen components to the number of moles of all carbon components becomes a predetermined value, the following effects can be obtained.

【0032】溶融製銑で発生する可燃性ガスを、溶融製
銑操作には何等支障をきたすことなく、メタノール合成
に適するように水素富化することができ、製銑の経済性
を向上し、炭酸ガスの排出を抑制することが可能になる
[0032] The flammable gas generated in molten pig iron making can be enriched with hydrogen to make it suitable for methanol synthesis without causing any hindrance to the molten pig iron making operation, improving the economic efficiency of pig iron making, It becomes possible to suppress carbon dioxide emissions.

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

【図1】本発明の実施例の系統図である。FIG. 1 is a system diagram of an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1  溶解ガス化炉 2  予備還元炉 9  固気分離器 イ  温度検出器 a  オンライン分析計 ロ  制御用マイクロプロセツサー b  制御用マイクロプロセツサー ハ  調節計 c  調節計 ニ  調節計 d  調節計 1 Melting and gasification furnace 2 Preliminary reduction furnace 9 Solid-gas separator B Temperature detector a Online analyzer B Control microprocessor b Control microprocessor C Controller c Controller D Controller d Controller

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  溶解ガス化炉に石炭と他の有機物燃料
を添加し、前記燃料を酸素により部分燃焼ガス化して一
酸化炭素および水素を主成分とする可燃性ガスを発生さ
せるとともに、前記溶解ガス化炉に還元鉄を添加して溶
融銑鉄を製造するとともに、前記溶解ガス化炉で発生す
る可燃性ガスの一部または全量でもって鉄鉱石を還元し
て還元鉄を製造する方法において、前記溶解ガス化炉に
添加する燃料中の石炭の固定炭素分の量が、製品銑鉄1
tonあたり0.3ton以上になるようにし、また前
記溶解ガス化炉の溶銑温度が所定値になるように、同溶
解ガス化炉内に吹込まれる酸素含有ガス量を調節し、更
に前記溶解ガス化炉から発生する可燃性ガス中の全炭素
成分のモル数に対する全酸素成分のモル数の比が所定値
になるように同溶解ガス化炉内に吹込まれる水蒸気量を
調節することを特徴とする可燃性ガスの水素富化方法。
Claim 1: Coal and other organic fuels are added to a melting gasification furnace, and the fuel is partially combustion gasified with oxygen to generate a combustible gas containing carbon monoxide and hydrogen as main components, and the melting In the method of producing molten pig iron by adding reduced iron to a gasification furnace, and reducing iron ore with a part or all of the combustible gas generated in the melting and gasification furnace, the method includes: The amount of fixed carbon in the coal added to the melting and gasifying furnace is
The amount of oxygen-containing gas injected into the melting and gasifying furnace is adjusted so that the temperature of the hot metal in the melting and gasifying furnace reaches a predetermined value. It is characterized by adjusting the amount of steam blown into the melting gasifier so that the ratio of the number of moles of all oxygen components to the number of moles of all carbon components in the combustible gas generated from the combustible gas is adjusted to a predetermined value. A method for enriching combustible gas with hydrogen.
JP10587691A 1991-05-10 1991-05-10 Method for enriching combustible gas with hydrogen Withdrawn JPH04338102A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10587691A JPH04338102A (en) 1991-05-10 1991-05-10 Method for enriching combustible gas with hydrogen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10587691A JPH04338102A (en) 1991-05-10 1991-05-10 Method for enriching combustible gas with hydrogen

Publications (1)

Publication Number Publication Date
JPH04338102A true JPH04338102A (en) 1992-11-25

Family

ID=14419146

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10587691A Withdrawn JPH04338102A (en) 1991-05-10 1991-05-10 Method for enriching combustible gas with hydrogen

Country Status (1)

Country Link
JP (1) JPH04338102A (en)

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