JPH0774342B2 - Method for detecting abnormal coal supply in coal gasifier - Google Patents

Method for detecting abnormal coal supply in coal gasifier

Info

Publication number
JPH0774342B2
JPH0774342B2 JP19377591A JP19377591A JPH0774342B2 JP H0774342 B2 JPH0774342 B2 JP H0774342B2 JP 19377591 A JP19377591 A JP 19377591A JP 19377591 A JP19377591 A JP 19377591A JP H0774342 B2 JPH0774342 B2 JP H0774342B2
Authority
JP
Japan
Prior art keywords
coal
gas
supply
hopper
pressure
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.)
Expired - Fee Related
Application number
JP19377591A
Other languages
Japanese (ja)
Other versions
JPH0532977A (en
Inventor
俊之 上田
栄次 木田
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 Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP19377591A priority Critical patent/JPH0774342B2/en
Publication of JPH0532977A publication Critical patent/JPH0532977A/en
Publication of JPH0774342B2 publication Critical patent/JPH0774342B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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、石炭の供給に係り、特
に、石炭ガス化炉に供給される石炭供給量の異常を検知
し、安定運転を維持するのに公的な石炭ガス化装置の石
炭供給異常検知方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the supply of coal, and more particularly, to a coal gasification apparatus that is public in order to detect abnormalities in the amount of coal supplied to a coal gasification furnace and maintain stable operation. The present invention relates to a coal supply abnormality detection method.

【0002】[0002]

【従来の技術】従来の石炭ガス化装置においては、特開
昭57−47748号公報等が知られているが、図5に
示すように、常圧ホッパ2に貯留された石炭は、定期的
に仕切弁20を開にすることにより、ロックホッパ3に
投入される。この時、ロックホッパ3内のガスを放出弁
22を開にして放出することにより、ロックホッパ3の
圧力を常圧ホッパ2と同一に保つ。常圧ホッパ2からの
石炭の供給が終了すると、仕切弁20及び放出弁22を
閉じ、加圧弁23を開にして、高圧ガスをロックホッパ
3に供給し、ロックホッパ3の圧力を上昇させる。ロッ
クホッパ3の圧力が供給ホッパ4の圧力と同一になる
と、加圧弁23を閉じる。供給ホッパ4内の石炭量はロ
ードセル5で検知し、石炭量がある一定値以下になると
均圧弁24と仕切弁21とを開け、供給ホッパ4に石炭
を供給する。石炭の供給が終了すると、均圧弁24と仕
切弁21とを閉じ、周期的にこれらの操作を繰り返す。
2. Description of the Related Art As a conventional coal gasifier, Japanese Patent Application Laid-Open No. 57-47748 is known, but as shown in FIG. 5, coal stored in the atmospheric hopper 2 is periodically charged. By opening the sluice valve 20, the lock hopper 3 is charged. At this time, the pressure in the lock hopper 3 is kept the same as that in the normal pressure hopper 2 by releasing the gas in the lock hopper 3 by opening the release valve 22. When the supply of coal from the normal pressure hopper 2 is completed, the sluice valve 20 and the discharge valve 22 are closed and the pressurizing valve 23 is opened to supply the high pressure gas to the lock hopper 3 to increase the pressure of the lock hopper 3. When the pressure of the lock hopper 3 becomes the same as the pressure of the supply hopper 4, the pressurizing valve 23 is closed. The amount of coal in the supply hopper 4 is detected by the load cell 5, and when the amount of coal falls below a certain value, the pressure equalizing valve 24 and the sluice valve 21 are opened to supply coal to the supply hopper 4. When the supply of coal is completed, the pressure equalizing valve 24 and the sluice valve 21 are closed, and these operations are periodically repeated.

【0003】供給ホッパ4に、石炭ガス化炉12への石
炭の安定供給のため、圧力を石炭ガス化炉12より高い
圧力に保つように、高圧の圧力調整用ガス7を供給す
る。圧力の調整は圧力計と圧力調整弁9とにより行う。
石炭ガス化炉12への石炭供給量を一定に保つため、ロ
ードセル5により常時、供給ホッパ4の重量を測定し、
その重量の経時変化から石炭供給量を演算し、石炭供給
量に応じてロータリフィーダ6の回転数を制御する。
In order to stably supply coal to the coal gasification furnace 12, a high pressure pressure adjusting gas 7 is supplied to the supply hopper 4 so as to maintain the pressure higher than that of the coal gasification furnace 12. The pressure is adjusted by the pressure gauge and the pressure adjusting valve 9.
In order to keep the amount of coal supplied to the coal gasifier 12 constant, the weight of the supply hopper 4 is constantly measured by the load cell 5,
The coal supply amount is calculated from the change over time of the weight, and the rotation speed of the rotary feeder 6 is controlled according to the coal supply amount.

【0004】また、供給ホッパ4内に貯留される石炭の
固着防止用に供給ホッパ4の底部より流動化用ガス8を
供給し、この流動化用ガス8を石炭の流動化媒体として
使用する。従って、供給ホッパ4には、圧力調整用ガス
7と流動化用ガス8とが供給されるが、一般に、供給ホ
ッパ内で粉体が固着し石炭ブリッジを形成して、供給ホ
ッパからの排出が良好に行われなくなる現象は良く知ら
れている。
A fluidizing gas 8 is supplied from the bottom of the supply hopper 4 to prevent the coal stored in the supply hopper 4 from sticking, and the fluidizing gas 8 is used as a coal fluidizing medium. Therefore, the pressure adjusting gas 7 and the fluidizing gas 8 are supplied to the supply hopper 4, but in general, powder adheres in the supply hopper to form a coal bridge, and the discharge from the supply hopper occurs. The phenomenon of poor performance is well known.

【0005】噴流層式の石炭ガス化炉では、このような
石炭が供給されない状態が長く続くと、石炭ガス化炉内
の温度が低下して、スラグの温度が溶融点より低くなる
ため徐々に固化し、ガス化部のスラグタップを徐々に閉
そくしてしまい、石炭ガス化炉の運転を停止することに
もなりかねない。このため、石炭ガス化炉には、通常、
ガス化部の温度低下を生じた際に強制的に炉内温度を、
スラグが溶融状態を保つのに必要な温度まで上昇させる
昇温バーナ13が設置されている。しかしながら、ガス
化部の温度は千数百℃を超えるため、直接の温度測定は
困難であり、通常は石炭ガス化炉を出るガスの温度によ
りガス化部の温度を推測する。このため、昇温バーナ1
3の運転開始までには時間遅れを生じることになる。ま
た、昇温バーナ13を常時運転しておくことは不経済的
でもあり、ガス化部の温度を必要以上に上昇させること
にもなる。
In a spouted bed type coal gasification furnace, if such a state where coal is not supplied continues for a long time, the temperature in the coal gasification furnace lowers and the temperature of the slag becomes lower than the melting point. It may solidify and gradually block the slag tap in the gasification section, which may stop the operation of the coal gasification furnace. For this reason, coal gasifiers usually have
When the temperature of the gasification section drops, the temperature inside the furnace is forced to
A heating burner 13 is installed to raise the temperature to the temperature required to keep the slag molten. However, since the temperature of the gasification section exceeds one thousand and several hundred degrees Celsius, it is difficult to directly measure the temperature, and the temperature of the gasification section is usually estimated from the temperature of the gas leaving the coal gasification furnace. Therefore, the heating burner 1
There will be a time delay before the start of operation in No. 3. In addition, it is uneconomical to keep the temperature-raising burner 13 constantly operating, and the temperature of the gasification section is raised more than necessary.

【0006】従って、石炭ガス化炉の安定運転のため、
より早くガス化部の温度低下を察知すること、言い換え
れば、石炭供給量の低下をより早く検知することが重要
である。
Therefore, for stable operation of the coal gasifier,
It is important to detect the temperature decrease in the gasification section earlier, in other words, to detect the decrease in coal supply rate earlier.

【0007】従来の石炭供給異常検知方法においては、
石炭供給量の低下は、ロードセル5の測定値の経時変化
が小さくなること、また、石炭搬送配管11内の石炭搬
送ガス10の差圧が小さくなることにより検知されるも
のの、ロードセル5では供給ホッパ4の重量も含めた石
炭重量を測定すること、供給ホッパ4の圧力変動により
測定値が変動する可能性が大きいこと、並びに、重量の
変化幅が非常に少ないこと、また、石炭搬送配管11の
差圧については、脈動等があってこれらの検知結果で昇
温バーナ13の運転を制御することは、十分信頼性を有
しているとは言えない。
In the conventional coal supply abnormality detection method,
The decrease in the coal supply amount is detected by a decrease in the measured value of the load cell 5 over time, and a decrease in the differential pressure of the coal carrier gas 10 in the coal carrier pipe 11, but in the load cell 5, the supply hopper is detected. No. 4, the weight of coal is measured, the measured value is likely to fluctuate due to the pressure fluctuation of the supply hopper 4, and the variation width of the weight is very small, and the coal transfer pipe 11 has Regarding the differential pressure, there is pulsation and the like, and it cannot be said that it is sufficiently reliable to control the operation of the temperature rising burner 13 based on these detection results.

【0008】[0008]

【発明が解決しようとする課題】従来の石炭ガス化装置
の石炭供給異常検知装置にあっては、石炭供給量の低下
を石炭搬送管内の差圧で検出していたが、供給ホッパの
圧力変動により測定値が変動する。また石炭ガス化炉の
温度低下をその排出ガス温度により測定していたが、昇
温バーナの運転に時間遅れを生じる等の問題点があっ
た。
In the conventional coal supply abnormality detecting device of the coal gasifier, the decrease in the coal supply amount is detected by the differential pressure in the coal conveying pipe, but the pressure fluctuation of the supply hopper is detected. Causes the measured value to fluctuate. Further, although the temperature decrease of the coal gasification furnace was measured by the temperature of the exhaust gas, there was a problem that the operation of the temperature raising burner was delayed.

【0009】本発明の目的は、昇温バーナの運転制御の
信頼性を向上するため、石炭ガス化炉への石炭供給量の
低下を早期に検知できる石炭ガス化装置の石炭供給異常
検知方法を提供することにある。
An object of the present invention is to provide a method for detecting abnormal coal supply in a coal gasifier which can detect early a decrease in the amount of coal supplied to a coal gasification furnace in order to improve the reliability of operation control of a temperature rising burner. To provide.

【0010】[0010]

【課題を解決するための手段】前記の目的を達成するた
め、本発明に係る石炭ガス化装置の石炭供給異常検知方
法は、ロックホッパに石炭を投入したのち加圧ガスを導
入して昇圧し、供給ホッパに圧力調整用ガス及び流動化
用ガスを導入して圧力調整を行うとともに投入された石
炭の流動化を行い、供給ホッパから搬出されかつ石炭供
給ガスにより石炭ガス化炉に供給される石炭の供給量を
検知する石炭ガス化装置の石炭供給異常検知方法におい
て、石炭供給ガスと異なる組成の圧力調整用ガス及び流
動化用ガスを用い、石炭供給ガス中の圧力調整用ガス及
び流動化用ガスの成分の濃度を検出し、その濃度増加に
より供給量の低下を検知する構成とする。
In order to achieve the above-mentioned object, a method for detecting abnormal coal supply of a coal gasifier according to the present invention comprises introducing coal into a lock hopper and then introducing pressurized gas to boost the pressure. , Introducing pressure adjusting gas and fluidizing gas into the supply hopper to adjust the pressure and fluidizing the input coal, carried out from the supply hopper and supplied to the coal gasifier by the coal supply gas. In a coal supply abnormality detection method for a coal gasifier that detects a coal supply amount, a pressure adjusting gas and a fluidizing gas having a composition different from that of the coal supplying gas are used, and the pressure adjusting gas and the fluidizing gas in the coal supplying gas are used. The concentration of the component of the working gas is detected, and the decrease in the supply amount is detected by the increase in the concentration.

【0011】そして石炭供給ガスに、石炭ガス化炉で生
成された生成ガスの一部を用い、ロックホッパの加圧ガ
ス、供給ホッパの圧力調整用ガス及び流動化用ガスに生
成ガスから分離された二酸化炭素の一部を用いる構成で
ある。
Then, a part of the produced gas produced in the coal gasification furnace is used as the coal supply gas, and is separated from the produced gas into the pressurized gas of the lock hopper, the pressure adjusting gas of the supply hopper and the fluidizing gas. It is also configured to use a part of carbon dioxide.

【0012】[0012]

【作用】本発明の石炭ガス化装置の石炭供給異常検知方
法によれば、石炭がロックホッパを経由して供給ホッパ
から石炭ガス化炉に安定して供給されている場合は、供
給ホッパが粉体シールされ石炭搬送配管への圧力調整用
ガス及び流動化用ガスの流出が少ないが、供給ホッパ内
で石炭ブリッジが形成し始めるとそれらのガスの流出が
多くなる。従って供給ホッパへ供給する圧力調整用ガス
及び流動化用ガスの組成を石炭供給ガスの組成と変える
ことにより、石炭搬送配管内の石炭供給ガス中の圧力調
整用及び流動化用ガスの成分の濃度を検出し、その濃度
増加から石炭供給量の低下を早期に検知することによ
り、石炭ガス化炉に挿着した昇温バーナの運転が開始さ
れる。
According to the method for detecting abnormal coal supply of the coal gasifier of the present invention, when the coal is stably supplied from the supply hopper to the coal gasification furnace via the lock hopper, the supply hopper is powdered. There is little outflow of the pressure adjusting gas and the fluidizing gas into the coal-conveying pipe that is body-sealed, but the outflow of these gases increases when the coal bridge begins to form in the supply hopper. Therefore, by changing the composition of the pressure adjusting gas and the fluidizing gas supplied to the supply hopper with the composition of the coal supplying gas, the concentrations of the components of the pressure adjusting and fluidizing gas in the coal supplying gas in the coal conveying pipe are changed. Is detected and the decrease in the coal supply amount is detected early from the increase in the concentration, the operation of the temperature rising burner inserted in the coal gasification furnace is started.

【0013】[0013]

【実施例】本発明の一実施例を図1を参照しながら説明
する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to FIG.

【0014】一例として図1に示す石炭ガス化装置によ
り水素を製造するプラントのように、ロックホッパ3に
常圧ホッパ2より仕切弁20を経由して石炭を投入した
のち、加圧ガスを加圧弁23より導入して昇圧し、供給
ホッパ4に圧力調整用ガス7及び流動化用ガス8を導入
して圧力調整を行うとともに、投入された石炭の流動化
を行い、供給ホッパ4から搬出されかつ石炭供給ガス1
0により石炭ガス化炉12に供給される石炭の供給を検
知する石炭ガス化装置の石炭供給異常検知方法であっ
て、石炭供給ガス10と異なる組成の圧力調整用ガス7
及び流動化用ガス8を用い、石炭供給ガス10中の圧力
調整用ガス7及び流動化用ガス8の成分の濃度を検出
し、その濃度増加により石炭の供給の低下を検知する構
成である。
As an example, as in the plant for producing hydrogen by the coal gasifier shown in FIG. 1, coal is charged into the lock hopper 3 from the atmospheric hopper 2 through the sluice valve 20, and then pressurized gas is added. It is introduced from the pressure valve 23 to increase the pressure, and the pressure adjusting gas 7 and the fluidizing gas 8 are introduced into the supply hopper 4 to adjust the pressure, and the coal fed is fluidized and discharged from the supply hopper 4. And coal supply gas 1
A method for detecting an abnormal coal supply of a coal gasifier for detecting the supply of coal supplied to a coal gasification furnace 12 according to 0, which comprises a pressure adjusting gas 7 having a composition different from that of the coal supply gas 10.
And the fluidizing gas 8 are used to detect the concentrations of the components of the pressure adjusting gas 7 and the fluidizing gas 8 in the coal supply gas 10, and the decrease in the coal supply is detected by the increase in the concentration.

【0015】石炭ガス化炉12で生成したガスは、冷却
されて脱硫装置15に導かれ、ガス中のH2S,COS
等の硫黄化合物が除去される。脱硫された生成ガスは、
一部をコンプレッサ18により昇圧し、石炭ガス化炉1
2への石炭供給ガス10として使用する。残りの生成ガ
スはCO変成装置30に導かれ、生成ガス中の一酸化炭
素が水素と二酸化炭素とに変成される。更に生成ガスは
脱炭酸装置31に導かれ、ここで二酸化炭素が除去さ
れ、製品水素ガス19を得る。脱炭酸装置31で分離除
去された二酸化炭素16は、一部をコンプレッサ17で
昇圧し、石炭供給用のロックホッパ3の加圧ガス並びに
供給ホッパ4の圧力調整用ガス7及び石炭の流動化用ガ
ス8として使用する。また石炭搬送配管11内の二酸化
炭素濃度を濃度計14により測定する。
The gas produced in the coal gasification furnace 12 is cooled and guided to the desulfurization device 15, where H 2 S and COS contained in the gas.
And other sulfur compounds are removed. The desulfurized product gas is
A part of the pressure is boosted by the compressor 18, and the coal gasifier 1
Used as coal feed gas 10 The remaining product gas is guided to the CO conversion device 30, and carbon monoxide in the product gas is converted into hydrogen and carbon dioxide. Further, the produced gas is guided to a decarbonation device 31, where carbon dioxide is removed, and a product hydrogen gas 19 is obtained. A part of the carbon dioxide 16 separated and removed by the decarbonator 31 is pressurized by the compressor 17, and the pressurized gas of the lock hopper 3 for coal supply, the pressure adjusting gas 7 of the supply hopper 4 and the fluidization of coal are used. Used as gas 8. Further, the carbon dioxide concentration in the coal transport pipe 11 is measured by the densitometer 14.

【0016】次に本発明の動作を図1〜図4を参照しな
がら説明する。
Next, the operation of the present invention will be described with reference to FIGS.

【0017】供給ホッパから石炭が安定して供給されて
いる場合は図2に示すように、ロータリフィーダ6は粉
体でシールされるため、供給ホッパ4へ供給される圧力
調整用及び流動化用ガス7、8は、石炭搬送配管11内
へ流出することはほとんどない。
When coal is stably supplied from the supply hopper, the rotary feeder 6 is sealed with powder as shown in FIG. 2, so that the pressure is supplied to the supply hopper 4 for fluidization and fluidization. The gases 7 and 8 rarely flow into the coal transport pipe 11.

【0018】一方、供給ホッパ4内で石炭ブリッジを形
成し始めると、ロータリフィーダ6を通り排出される石
炭は少なくなるとともに、供給ホッパ4へ供給される圧
力調整用及び流動化用ガス7、8がロータリフィーダ6
を通過し、石炭搬送配管11へ流出する量が多くなり、
完全に石炭ブリッジを形成すると、図3及び図4に示さ
れるように、圧力調整用及び流動化用ガス7、8のみが
ロータリフィーダ6を通過することとなる。この場合、
それぞれのガス7、8のロータリフィーダ6の通過量は
石炭供給ガス10の量の約半分にもなる。
On the other hand, when the coal bridge is started to be formed in the supply hopper 4, the amount of coal discharged through the rotary feeder 6 decreases and the pressure adjusting and fluidizing gas 7, 8 supplied to the supply hopper 4 is reduced. Is the rotary feeder 6
And the amount flowing out to the coal transport pipe 11 increases,
When the coal bridge is completely formed, only the pressure adjusting and fluidizing gases 7 and 8 pass through the rotary feeder 6, as shown in FIGS. 3 and 4. in this case,
The amount of each gas 7 and 8 passing through the rotary feeder 6 is about half the amount of the coal supply gas 10.

【0019】噴流層式の石炭ガス化炉で生成するガスに
は、石炭の性状によっても異なるが、通常、約5%以下
の二酸化炭素を含んでおり、その値は脱硫装置15を経
ても、増えることはない。従って、石炭供給ガス10に
含まれる二酸化炭素は、多くても5%となる。一方、脱
炭酸装置15により分離除去される二酸化炭素16の濃
度は通常90%以上である。
The gas produced in the spouted bed type coal gasification furnace contains carbon dioxide of about 5% or less, though it varies depending on the properties of the coal. It does not increase. Therefore, the carbon dioxide contained in the coal supply gas 10 is 5% at most. On the other hand, the concentration of carbon dioxide 16 separated and removed by the carbon dioxide removal device 15 is usually 90% or more.

【0020】従って、石炭が安定して石炭ガス化炉12
に供給されている場合、石炭搬送配管11内の二酸化炭
素は5%以下であるが、供給ホッパ4で石炭ブリッジを
形成し始めると、石炭搬送配管11内の二酸化炭素濃度
が上昇を始め、完全に石炭ブリッジを形成してしまう
と、その濃度は、約40%まで上昇する。
Therefore, the coal is stabilized and the coal gasifier 12
Carbon dioxide in the coal transport pipe 11 is 5% or less, the carbon dioxide concentration in the coal transport pipe 11 starts to rise and starts to form a coal bridge in the supply hopper 4. When coal bridges are formed, the concentration rises to about 40%.

【0021】すなわち、石炭搬送配管11内の二酸化炭
素を濃度計14で連続的に測定し、その濃度変化をみて
石炭ブリッジ等による石炭供給量の低下、並びに、それ
がもたらすガス化部の温度の低下を正確かつ迅速に察知
することが可能となる。この濃度の上昇変化を検知する
ことにより、石炭ガス化炉12の昇温バーナ13を、自
動的あるいは運転員の判断により運転する。と同時に、
供給ホッパ4の石炭ブリッジをバイブレータ又はハンマ
リングのような機械的操作により崩壊する。この操作を
石炭安定供給時に行うことは、かえって石炭を押し固め
ることになり逆効果であり、この操作は、石炭ブリッジ
が形成し始める初期に行うのが効果的である。石炭供給
ガス10中の二酸化炭素の濃度上昇を検知することによ
り、この機械的操作も、迅速に行うことができる。
That is, the carbon dioxide in the coal conveying pipe 11 is continuously measured by the densitometer 14, and the change in the concentration is observed to decrease the coal supply amount due to a coal bridge or the like, and the temperature of the gasification section caused by the decrease. It becomes possible to detect the decrease accurately and quickly. By detecting this increase in the concentration, the temperature rising burner 13 of the coal gasification furnace 12 is operated automatically or at the operator's discretion. At the same time
The coal bridge of the feed hopper 4 is collapsed by a mechanical operation such as a vibrator or hammering. Performing this operation at the time of stable coal supply has the opposite effect because it compacts the coal rather, and it is effective to perform this operation at the initial stage when the coal bridge begins to form. By detecting the increase in the concentration of carbon dioxide in the coal supply gas 10, this mechanical operation can be performed quickly.

【0022】本発明の他の効果は、石炭供給ガス10に
生成ガスを、供給ホッパ4のそれぞれのガス7、8に生
成ガスから分離される二酸化炭素を用いることにより、
供給ホッパ4が石炭ブリッジを形成した場合でも、石炭
供給ガス中、すなわち、生成ガス中に、通常は生成ガス
中に含まれないガス、あるいは、生成ガスから分離する
ことが困難な窒素等のガスが混入しないこと、また石炭
ガス化装置系以外からのガスの導入を不要とする、さら
にロックホッパの放出ガスが二酸化炭素であるため、こ
のまま、大気に放出できる、等の効果が挙げられる。
Another advantage of the present invention is that by using the produced gas for the coal feed gas 10 and the carbon dioxide separated from the produced gas for the respective gases 7, 8 of the feed hopper 4,
Even when the supply hopper 4 forms a coal bridge, in the coal supply gas, that is, in the produced gas, a gas that is not normally contained in the produced gas, or a gas such as nitrogen that is difficult to separate from the produced gas. Is not mixed, the introduction of gas from other than the coal gasifier system is not necessary, and further, since the gas released from the lock hopper is carbon dioxide, it can be released to the atmosphere as it is.

【0023】本発明の他の実施例として、石炭ガス化装
置の生成ガスから水素を製造するプロセスの例を示した
が、石炭ガス化装置の生成ガスから合成ガスを製造する
プロセス、又は燃料電池により発電を行うプロセス等で
も、プロセス内で分離除去される二酸化炭素を、供給ホ
ッパに供給することにより同様の効果が得られる。
As another embodiment of the present invention, an example of the process for producing hydrogen from the product gas of the coal gasifier is shown, but the process of producing the syngas from the product gas of the coal gasifier or the fuel cell. In the process of generating power by means of the above, the same effect can be obtained by supplying the carbon dioxide separated and removed in the process to the supply hopper.

【0024】[0024]

【発明の効果】本発明の石炭ガス化装置の石炭供給異常
検知方法によれば、石炭供給量の低下が石炭供給ガスの
濃度を検出することにより、早期に検知することができ
るため石炭ガス化炉の安定運転を長期にわたって維持す
ることができる。
According to the method for detecting abnormal coal supply of the coal gasifier of the present invention, the decrease in the amount of supplied coal can be detected at an early stage by detecting the concentration of the coal supplied gas. The stable operation of the furnace can be maintained for a long period of time.

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

【図1】本発明の一実施例を示す構成図である。FIG. 1 is a configuration diagram showing an embodiment of the present invention.

【図2】本発明の動作を説明する図である。FIG. 2 is a diagram for explaining the operation of the present invention.

【図3】本発明の動作を説明する図である。FIG. 3 is a diagram for explaining the operation of the present invention.

【図4】本発明の動作を説明する図である。FIG. 4 is a diagram illustrating the operation of the present invention.

【図5】従来の技術を示す図である。FIG. 5 is a diagram showing a conventional technique.

【符号の説明】 3 ロックホッパ 4 供給ホッパ 7 圧力調整用ガス 8 流動化用ガス 10 石炭搬送ガス 11 石炭搬送配管 12 石炭ガス化炉[Explanation of reference numerals] 3 lock hopper 4 supply hopper 7 pressure adjusting gas 8 fluidizing gas 10 coal carrier gas 11 coal carrier pipe 12 coal gasifier

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ロックホッパに石炭を投入したのち加圧
ガスを導入して昇圧し、供給ホッパに圧力調整用ガス及
び流動化用ガスを導入して圧力調整を行うとともに投入
された前記石炭の流動化を行い、前記供給ホッパから搬
出されかつ石炭供給ガスにより石炭ガス化炉に供給され
る前記石炭の供給量を検知する石炭ガス化装置の石炭供
給異常検知方法において、前記石炭供給ガスと異なる組
成の前記圧力調整用ガス及び前記流動化用ガスを用い、
前記石炭供給ガス中の該圧力調整用ガス及び該流動化用
ガスの成分の濃度を検出し、その濃度増加により前記供
給量の低下を検知することを特徴とする石炭ガス化装置
の石炭供給異常検知方法。
1. A coal hopper is charged into a lock hopper, a pressurized gas is then introduced to increase the pressure, and a pressure adjusting gas and a fluidizing gas are introduced into a supply hopper to adjust the pressure and to charge the coal. In a coal supply abnormality detection method of a coal gasifier that fluidizes and detects the supply amount of the coal that is carried out from the supply hopper and supplied to the coal gasification furnace by the coal supply gas, different from the coal supply gas. Using the pressure adjusting gas and the fluidizing gas of the composition,
Coal supply abnormality of a coal gasifier characterized by detecting the concentrations of the components of the pressure adjusting gas and the fluidizing gas in the coal supply gas, and detecting the decrease in the supply amount by increasing the concentration. Detection method.
【請求項2】 石炭供給ガスに、石炭ガス化炉で生成さ
れた生成ガスの一部を用い、ロックホッパの加圧ガス、
供給ホッパの圧力調整用ガス及び流動化用ガスに前記生
成ガスから分離された二酸化炭素の一部を用いることを
特徴とする請求項1記載の石炭ガス化装置の石炭供給異
常検知方法。
2. A part of the produced gas produced in the coal gasification furnace is used as the coal supply gas, and the pressurized gas of the lock hopper is used,
2. The method for detecting abnormal coal supply in a coal gasifier according to claim 1, wherein a part of carbon dioxide separated from the generated gas is used as a pressure adjusting gas and a fluidizing gas of a supply hopper.
JP19377591A 1991-08-02 1991-08-02 Method for detecting abnormal coal supply in coal gasifier Expired - Fee Related JPH0774342B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19377591A JPH0774342B2 (en) 1991-08-02 1991-08-02 Method for detecting abnormal coal supply in coal gasifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19377591A JPH0774342B2 (en) 1991-08-02 1991-08-02 Method for detecting abnormal coal supply in coal gasifier

Publications (2)

Publication Number Publication Date
JPH0532977A JPH0532977A (en) 1993-02-09
JPH0774342B2 true JPH0774342B2 (en) 1995-08-09

Family

ID=16313600

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19377591A Expired - Fee Related JPH0774342B2 (en) 1991-08-02 1991-08-02 Method for detecting abnormal coal supply in coal gasifier

Country Status (1)

Country Link
JP (1) JPH0774342B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014136789A (en) * 2013-01-18 2014-07-28 Mitsubishi Heavy Ind Ltd Powder fuel feed hopper and powder fuel feeding method

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100450901C (en) * 2005-07-11 2009-01-14 西安热工研究院有限公司 Dry coal pressure closed phase conveyer with several discharge branches
KR101353783B1 (en) * 2011-12-27 2014-01-22 주식회사 포스코 Method for Coal Gasifying and Apparatus Therefor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014136789A (en) * 2013-01-18 2014-07-28 Mitsubishi Heavy Ind Ltd Powder fuel feed hopper and powder fuel feeding method

Also Published As

Publication number Publication date
JPH0532977A (en) 1993-02-09

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