JPH0226917Y2 - - Google Patents
Info
- Publication number
- JPH0226917Y2 JPH0226917Y2 JP1982037188U JP3718882U JPH0226917Y2 JP H0226917 Y2 JPH0226917 Y2 JP H0226917Y2 JP 1982037188 U JP1982037188 U JP 1982037188U JP 3718882 U JP3718882 U JP 3718882U JP H0226917 Y2 JPH0226917 Y2 JP H0226917Y2
- Authority
- JP
- Japan
- Prior art keywords
- gasifier
- gas
- bag filter
- valve
- temperature
- 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
Links
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は、高純度の酸素でコークスをガス化す
るガス化器を含む一酸化炭素ガス発生装置に関す
る。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a carbon monoxide gas generator including a gasifier that gasifies coke with high-purity oxygen.
高純度の酸素でコークスをガス化するガス化器
は特公昭47−11331号公報から公知である。この
ようなガス化器において生成される一酸化炭素ガ
スは高温で、灰分やコークス微粉等の固体粒子を
含んでいるので、このガスを冷却すると共に、固
体粒子を分離する必要がある。
A gasifier for gasifying coke with high purity oxygen is known from Japanese Patent Publication No. 11331/1983. Since the carbon monoxide gas produced in such a gasifier is at a high temperature and contains solid particles such as ash and fine coke, it is necessary to cool this gas and separate the solid particles.
このためガス化器の後に廃熱ボイラまたはバツ
グフイルタを接続して、固体粒子を含有する生成
ガスを冷却し、さらに廃熱ボイラの後に静電集塵
機を接続して、ガスから固体粒子を分離すること
も公知である(特開昭56−86991号または昭53−
120703号公報)。 For this purpose, a waste heat boiler or bag filter is connected after the gasifier to cool the produced gas containing solid particles, and an electrostatic precipitator is connected after the waste heat boiler to separate the solid particles from the gas. is also publicly known (JP-A-56-86991 or 1983-
Publication No. 120703).
しかしながら廃熱ボイラは、それ自体および付
属する制御装置のため、熱の回収により得られる
利益を上回る費用を要し、また静電集塵機は高電
圧電源等を必要とするので、経済上の点から実際
に採用することは困難である。さらにバツグフイ
ルタは、高温のガスにより焼損するおそれがあ
り、金属繊維からなる高価なバツグフイルタを使
用せねばならない。 However, waste heat boilers themselves and their associated control equipment require costs that exceed the benefits obtained from heat recovery, and electrostatic precipitators require high-voltage power supplies, etc., so they are not economically viable. It is difficult to actually adopt it. Furthermore, there is a risk that the bag filter may be burned out by the high temperature gas, and an expensive bag filter made of metal fiber must be used.
本考案の課題は、ガス化器の生成ガスの冷却お
よび固体粒子分離をもつと簡単かつ安価に行なう
ことである。
The object of the invention is to provide simple and inexpensive cooling of the gas produced by a gasifier and separation of solid particles.
このため本考案によれば、ガス化器を出る生成
ガス中に含まれる固体粒子を分離するバツグフイ
ルタが設けられ、ガス化器とバツグフイルタとを
接続するガス導管の少なくとも一部を包囲して冷
却水を供給される水冷ジヤケツトが設けられ、さ
らに温度調節器により制御されて水冷ジヤケツト
内を通る冷却水の流量を制御する冷却水制御弁
と、生成ガスの特定値以上の温度においてガス化
器とバツグフイルタとの接続を断つ緊急遮断弁
と、この緊急遮断弁より上流側に設けられて緊急
遮断弁の閉じる際開いて生成ガスを外部へ放出す
る放出弁とが設けられる。
For this reason, according to the present invention, a bag filter is provided to separate solid particles contained in the produced gas exiting the gasifier, and a bag filter is provided that surrounds at least a part of the gas conduit connecting the gasifier and the bag filter to provide cooling water. A water-cooled jacket is provided, which is further controlled by a temperature controller to control the flow rate of cooling water passing through the water-cooled jacket, and a cooling water control valve that controls the flow rate of cooling water through the water-cooled jacket, and a gasifier and a bag filter at a temperature above a certain value of the produced gas. An emergency shutoff valve is provided to disconnect the emergency shutoff valve, and a release valve is provided upstream of the emergency shutoff valve and opens when the emergency shutoff valve is closed to release generated gas to the outside.
こうして本考案によれば、ガス化器とバツグフ
イルタとを接続するためいずれにせよ存在してい
る導管を水冷ジヤケツトで包囲するだけなので、
冷却装置の構造が簡単であるにもかかわらず、冷
却水の流量を制御する冷却水制御弁により、ガス
を所望の温度に冷却できる。万一ガスの温度が異
常に高くなつても、緊急遮断弁を閉じ、放出弁を
開いて、この異常高温のガスがバツグフイルタへ
達しないようにできるので、バツフイルタ用炉布
として安価な化学繊維布を使用しても、その焼損
が確実に防止されるという利点がある。
Thus, according to the invention, it is only necessary to surround the conduit, which is present anyway, for connecting the gasifier and the bag filter with a water-cooled jacket.
Although the structure of the cooling device is simple, the gas can be cooled to a desired temperature by a cooling water control valve that controls the flow rate of cooling water. Even if the gas temperature becomes abnormally high, the emergency shutoff valve can be closed and the release valve can be opened to prevent this abnormally high temperature gas from reaching the baggage filter. There is an advantage that burnout can be reliably prevented even if a
本考案の実施例を図について説明すると、入口
および出口にロツク弁11をもつ供給タンク1か
らガス化器2の上部へ供給されるコークスaは、
ガス化器2内に固定床を形成し、ガス化器2の底
部から供給される高純度の酸素ガスbによりガス
化される。このガス化反応はコークスによる過剰
な炭素存在下で進行するので、反応式C+1/2O2
→COにより純度の高い一酸化炭素ガスが生成さ
れる。ガス化器2の反応域における温度は1400℃
〜1700℃で、局部的には2500℃の高温度に達する
ため、コークス中の鉄、珪素、アルミニウム、マ
グネシウム、ナトリウムなどの酸化物から成る灰
分の一部は蒸発し、1000℃以下になると凝縮また
は固化して、ガスと共にガス化器2の上部から出
て行く。生成ガスは温度100℃〜250℃であり、ガ
ス化器内部の状態によつて異なるが正常状態で
120℃程度、異常時には250℃程度に上昇する。生
成ガスはガス化器2の上部に接続される導管3を
経て、除塵器4および6へ入り、ここでガスに同
伴されている灰分を除去された後、清浄な一酸化
炭素ガスcとして遮断弁14を経て次の工程の精
製装置へ送られる。除塵器4および6として公知
のバツグフイルタが用いられ、バツグフイルタ4
で大部分の灰分gがガスから除かれ、ロツクホツ
パ5を経て排出される。バツグフイルタ4の布
の表面に多量の灰分が堆積すると流れ抵抗が大き
くなるので、ガス弁7を介して図示されていない
精製装置の後の清浄な一酸化炭素ガスeがバツグ
フイルタ4内へ吹込まれて、布表面に堆積した
灰分を払い落とす。ガス化器2とバツグフイルタ
4とを接続する導管3は一部分を水冷ジヤケツト
8により包囲され、このジヤケツト8と導管3と
の間の環状空間に冷却水fが流されて、導管3を
通るガスを冷却することができるようになつてい
る。過大な量の冷却水が流れないようにするた
め、図示されてない温度調節器により冷却水制御
弁15の開度を自動的に調節する。導管3の内面
は、ガス中の灰分が付着しないように、アルミニ
ウムを溶射して壁面を緻密かつ平滑にされてい
る。
To explain an embodiment of the present invention with reference to the drawings, coke a is supplied to the upper part of the gasifier 2 from a supply tank 1 having a lock valve 11 at the inlet and outlet.
A fixed bed is formed in the gasifier 2 and gasified by high-purity oxygen gas b supplied from the bottom of the gasifier 2. Since this gasification reaction proceeds in the presence of excess carbon due to coke, highly pure carbon monoxide gas is produced according to the reaction formula C+1/2O 2 →CO. The temperature in the reaction zone of gasifier 2 is 1400℃
~1700℃, locally reaching high temperatures of 2500℃, so some of the ash in the coke, which consists of oxides of iron, silicon, aluminum, magnesium, sodium, etc., evaporates, and when the temperature drops below 1000℃, it condenses. Or it solidifies and leaves from the upper part of the gasifier 2 together with the gas. The temperature of the generated gas is between 100℃ and 250℃, which varies depending on the internal conditions of the gasifier, but under normal conditions.
The temperature rises to about 120℃, and in abnormal situations it rises to about 250℃. The generated gas passes through a conduit 3 connected to the upper part of the gasifier 2 and enters dust removers 4 and 6, where the ash entrained in the gas is removed and then shut off as clean carbon monoxide gas c. It passes through the valve 14 and is sent to the refiner for the next step. Known bug filters are used as the dust removers 4 and 6, and the bug filter 4
Most of the ash g is removed from the gas and discharged via the lock hopper 5. If a large amount of ash accumulates on the cloth surface of the bag filter 4, the flow resistance increases, so clean carbon monoxide gas e from the purification device (not shown) is blown into the bag filter 4 through the gas valve 7. , brush off the ash that has accumulated on the surface of the cloth. A portion of the conduit 3 connecting the gasifier 2 and the bag filter 4 is surrounded by a water cooling jacket 8, and cooling water f is flowed into the annular space between the jacket 8 and the conduit 3 to cool the gas passing through the conduit 3. It is now possible to cool down. In order to prevent an excessive amount of cooling water from flowing, the opening degree of the cooling water control valve 15 is automatically adjusted by a temperature regulator (not shown). The inner surface of the conduit 3 is thermally sprayed with aluminum to make the wall surface dense and smooth so that ash in the gas does not adhere to it.
前述したようにガス化器2を出るガスの温度は
通常120℃程度であるが、異常時には250℃に達す
ることがある。ガスの温度が異常に高くなると、
水冷ジヤケツト8内を流れる水の冷却能力を越え
て温度の高いガスがバツグフイルタ4へ入り、
布を焼損する恐れがある。これを避けるために、
図示されていない温度警報スイツチでガスの異常
高温を検知し、導管3にある緊急遮断弁12を閉
じて、ガス化器2とバツグフイルタ4との接続を
断つと共に、放出弁13を開いて高温のガスdを
一時的に放出する。 As mentioned above, the temperature of the gas exiting the gasifier 2 is normally about 120°C, but in abnormal circumstances it can reach 250°C. When the gas temperature becomes abnormally high,
Gas whose temperature exceeds the cooling capacity of the water flowing inside the water cooling jacket 8 enters the bag filter 4,
There is a risk of burning the cloth. To avoid this,
A temperature alarm switch (not shown) detects an abnormally high temperature of the gas, closes the emergency shutoff valve 12 in the conduit 3, disconnects the gasifier 2 and baggage filter 4, and opens the discharge valve 13 to prevent the high temperature. Temporarily releases gas d.
図面は本考案による装置全体概略構成図であ
る。
2……ガス化器、3……導管、4,6……バツ
グフイルタ、8……水冷ジヤケツト、a……コー
クス、b……高純度酸素、f……冷却水。
The drawing is a schematic diagram of the entire apparatus according to the present invention. 2... Gasifier, 3... Conduit, 4, 6... Bag filter, 8... Water cooling jacket, a... Coke, b... High purity oxygen, f... Cooling water.
Claims (1)
2と、ガス化器を出る生成ガス中に含まれる固体
粒子を分離するバツグフイルタ4と、ガス化器2
とバツグフイルタ4とを接続するガス導管3の少
なくとも一部を包囲して冷却水を供給される水冷
ジヤケツト8と、温度調節器により制御されて水
冷ジヤケツト8内を通る冷却水の流量を制御する
冷却水制御弁15と、生成ガスの特定値以上の温
度においてガス化器2とバツグフイルタ4との接
続を断つ緊急遮断弁12と、この緊急遮断弁12
より上流側に設けられて緊急遮断弁12の閉じる
際開いて生成ガスを外部へ放出する放出弁13と
から成ることを特徴とする一酸化炭素ガス発生装
置。 A gasifier 2 that gasifies coke with high-purity oxygen, a bag filter 4 that separates solid particles contained in the generated gas exiting the gasifier, and a gasifier 2
a water-cooled jacket 8 that surrounds at least a portion of the gas conduit 3 connecting the bag filter 4 and the bag filter 4 and is supplied with cooling water; a water control valve 15; an emergency shutoff valve 12 that disconnects the gasifier 2 and the bag filter 4 when the temperature of the generated gas exceeds a specific value;
A carbon monoxide gas generator characterized by comprising a release valve 13 which is provided on the upstream side and opens when the emergency shutoff valve 12 closes to release generated gas to the outside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3718882U JPS58140156U (en) | 1982-03-18 | 1982-03-18 | carbon monoxide gas generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3718882U JPS58140156U (en) | 1982-03-18 | 1982-03-18 | carbon monoxide gas generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58140156U JPS58140156U (en) | 1983-09-21 |
| JPH0226917Y2 true JPH0226917Y2 (en) | 1990-07-20 |
Family
ID=30048586
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3718882U Granted JPS58140156U (en) | 1982-03-18 | 1982-03-18 | carbon monoxide gas generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58140156U (en) |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4296087A (en) * | 1978-10-02 | 1981-10-20 | Phillips Petroleum Company | Method for producing carbon black |
| DE2947222C2 (en) * | 1979-11-23 | 1987-05-07 | Carbon Gas Technologie GmbH, 4030 Ratingen | Device for gasification of solid, dusty to lumpy carbonaceous fuels and their use |
| JPS5686990A (en) * | 1979-12-17 | 1981-07-15 | Showa Denko Kk | Heating of material |
-
1982
- 1982-03-18 JP JP3718882U patent/JPS58140156U/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58140156U (en) | 1983-09-21 |
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