JPS5829994B2 - Coal gasification method and device - Google Patents
Coal gasification method and deviceInfo
- Publication number
- JPS5829994B2 JPS5829994B2 JP3598378A JP3598378A JPS5829994B2 JP S5829994 B2 JPS5829994 B2 JP S5829994B2 JP 3598378 A JP3598378 A JP 3598378A JP 3598378 A JP3598378 A JP 3598378A JP S5829994 B2 JPS5829994 B2 JP S5829994B2
- Authority
- JP
- Japan
- Prior art keywords
- coal
- furnace
- gasification
- blowing pipe
- heat medium
- 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
- 239000003245 coal Substances 0.000 title claims description 24
- 238000002309 gasification Methods 0.000 title claims description 11
- 238000000034 method Methods 0.000 title claims description 6
- 238000007664 blowing Methods 0.000 claims description 19
- 239000007789 gas Substances 0.000 claims description 14
- 238000002347 injection Methods 0.000 claims description 5
- 239000007924 injection Substances 0.000 claims description 5
- 229910052582 BN Inorganic materials 0.000 claims description 4
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical group N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 230000001590 oxidative effect Effects 0.000 claims description 4
- 238000010793 Steam injection (oil industry) Methods 0.000 claims description 2
- 239000012159 carrier gas Substances 0.000 claims 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 34
- 229910052742 iron Inorganic materials 0.000 description 17
- 239000002893 slag Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 229910052799 carbon Inorganic materials 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 239000002245 particle Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 150000004767 nitrides Chemical class 0.000 description 2
- 239000011819 refractory material Substances 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 229910052581 Si3N4 Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000002802 bituminous coal Substances 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- PMHQVHHXPFUNSP-UHFFFAOYSA-M copper(1+);methylsulfanylmethane;bromide Chemical compound Br[Cu].CSC PMHQVHHXPFUNSP-UHFFFAOYSA-M 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Description
【発明の詳細な説明】
この発明は溶融熱媒体を貯留するガス化炉に、石炭粒お
よび水蒸気を送入してガス化するガス化装置の改良に関
する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a gasifier that gasifies coal grains and steam by feeding them into a gasifier that stores a molten heat medium.
溶融鉄などの高温溶融物質を熱媒体とし、これに吹込用
管を浸漬して石炭粒を水蒸気によって溶融鉄中に吹込ん
でガス化する方法は、炭種の如何に拘らず、効率よくガ
ス化でき、かつ脱塵脱硫作用を有するなど多くの利点を
有する方法がありながら、吹込用管の材料の耐久性の問
題から実用化がはばまれている。This method uses a high-temperature melting substance such as molten iron as a heat medium, immerses a blowing pipe in it, and blows coal grains into the molten iron with steam to gasify the coal particles. Regardless of the type of coal, it can be efficiently gasified. Although there are methods that have many advantages such as dust removal and desulfurization, their practical application has been hindered due to the durability of the material of the blowing tube.
事実、1500〜16008Cという高温で、炭素含有
率の高い還元性の溶融鉄に耐え同時に酸化カルシウム分
を多く含む腐蝕性の強い溶融スラグに対しても耐久性が
あり、かつ高温水蒸気にも反応せず侵されることがない
吹込管用耐火材料を既存の材料中に見出すことは殆んど
不可能といってよい。In fact, it can withstand reducing molten iron with a high carbon content at high temperatures of 1,500 to 16,008 C, and at the same time is durable against highly corrosive molten slag containing a large amount of calcium oxide, and does not react with high-temperature steam. It is almost impossible to find a refractory material for blowpipe in existing materials that will not be attacked.
この発明はこれを解決するためなされたものであって、
石炭粒吹込用管と水蒸気吹込用管とを分け、かつ石炭粒
吹込用管が水蒸気に曝されることがないよう取りつけ、
石炭粒の吹込はガス化によって生成した生成ガスを循環
使用して行ない、石炭粒吹込用管は高温還元性ふん囲気
に耐えると共に、耐高温溶融スラグおよび耐溶融鉄材で
作成した管を用い、水蒸気の吹込みは溶融鉄に浸漬せず
液面上から高流速で吹込むようにして前記不都合を避け
るようにしたものである。This invention was made to solve this problem,
The coal grain injection pipe and the steam injection pipe are separated, and the coal grain injection pipe is installed so that it is not exposed to steam,
Injection of coal particles is carried out by circulating the gas produced by gasification, and the pipe for blowing coal particles is made of high-temperature reducing atmosphere and is made of high-temperature molten slag and molten iron. The above-mentioned disadvantages are avoided by blowing the iron into the molten iron at a high flow rate from above the liquid surface without immersing it in the liquid.
以下図を参照しつつこの発明一実施例の詳細について述
べる。The details of one embodiment of this invention will be described below with reference to the drawings.
図示しない粉砕機で粉砕された石炭は酸化カルシウム(
石炭)を混合し、公知の送給装置1によって生成ガスと
共に吹込管2により炉F内の溶融鉄3中に送入される。The coal pulverized by a pulverizer (not shown) is calcium oxide (
Coal) is mixed and fed into the molten iron 3 in the furnace F through the blowing pipe 2 along with the produced gas by a known feeding device 1.
石炭粉吹込管2は1500〜16000Gの高温におい
ても炉F内の溶融スラグ4および溶融鉄3に耐えうるセ
ラミック材、例えば熱圧した窒化硼素で製作する。The coal powder injection pipe 2 is made of a ceramic material that can withstand the molten slag 4 and molten iron 3 in the furnace F even at high temperatures of 1,500 to 16,000 G, such as hot-pressed boron nitride.
一般に窒化硅素や窒化アルミニウムや窒化硼素など窒化
物系耐火物は還元ふん囲気中では極めて安定しているが
、酸化ふん囲気では弱く水蒸気や酸には加水分解する。In general, nitride-based refractories such as silicon nitride, aluminum nitride, and boron nitride are extremely stable in a reducing atmosphere, but are weakly hydrolyzed by water vapor and acids in an oxidizing atmosphere.
従って、図に示すように吹込管2が通る炉Fの差込み壁
F1にはスラグ4表面まで延長して、水蒸気吹込管5か
らの水蒸気が接触しないように構成する。Therefore, as shown in the figure, the insertion wall F1 of the furnace F through which the blowing pipe 2 passes is extended to the surface of the slag 4 so that the steam from the steam blowing pipe 5 does not come into contact with it.
即ち、前述したように水蒸気を除いては、この方式のガ
ス化炉内部は、溶融鉄、生成ガスとも還元ふん囲気であ
り、窒化硼素は溶融スラグにぬれないので水蒸気さえ避
断ずれば相当の耐久性がある。That is, as mentioned above, except for water vapor, the interior of this type of gasifier is a reducing atmosphere for both the molten iron and the produced gas, and boron nitride does not get wet with molten slag, so if only water vapor is avoided, a considerable amount of Durable.
かくて、溶融鉄3中に吹込まれた石炭粒は乾留熱分解し
て高熱量のガスを発生し、石炭中の固定炭素は溶融鉄3
中に溶解するが、炉F頂周囲に設けられた水蒸気吹込管
5から吹込まれる高流速水蒸気による水性ガス反応によ
って水性ガス化する。In this way, the coal particles injected into the molten iron 3 undergo carbonization pyrolysis to generate high-calorie gas, and the fixed carbon in the coal is released into the molten iron 3.
However, it is converted into water gas by a water gas reaction caused by high-flow steam blown in from the steam blowing pipe 5 installed around the top of the furnace F.
このようにして生成した約1000℃のガスは取出口F
2より取出され冷却器6に入りカーボン析出を防止する
ため急冷され、この工程で水分アンモニア、粉塵などが
除去され、次の廃熱ボイラー7でエンタルピーを回収さ
れ、次工程、すなわちガス精製装置8に送り込まれる。The gas of about 1000℃ generated in this way is extracted from the outlet F.
2 and enters a cooler 6 where it is rapidly cooled to prevent carbon precipitation. In this step, moisture ammonia and dust are removed. The enthalpy is recovered in the next waste heat boiler 7, and then it is sent to the next step, that is, the gas purification device 8. sent to.
実、験によれは、灰分14.1%、揮発分42.2%、
固定炭素37.5%、水分6.0%、硫黄分0.2%の
瀝青炭をガス化するとH255,2%、CO35,7%
、Co23.7%、CH4,2%、C2H40,7%、
C2H65ぞの粗ガス約1450 m”/ tを発生す
る。In fact, according to experiments, the ash content is 14.1%, the volatile content is 42.2%,
When bituminous coal with fixed carbon 37.5%, moisture 6.0%, and sulfur content 0.2% is gasified, H255.2% and CO35.7% are produced.
, Co23.7%, CH4,2%, C2H40,7%,
Approximately 1450 m"/t of crude gas of C2H65 is generated.
ガス組成からら知られるようにこのガスは還元ガスであ
る。As is known from the gas composition, this gas is a reducing gas.
ノ
ボイラー7の一部における気液分離器7aにおいて分離
された水は、冷却器6における冷媒となる。The water separated in the gas-liquid separator 7a in a part of the boiler 7 becomes a refrigerant in the cooler 6.
炉Fの側面には、スラグ取出手段F3が設けられ、炉F
内部とは連通孔9で連通され、溶融鉄3、スラグ4など
が流入するべくなされる。A slag removal means F3 is provided on the side of the furnace F.
It communicates with the inside through a communication hole 9, through which molten iron 3, slag 4, etc. can flow.
手段F3には、取出孔10と11とが上下に離でて設け
られ、比重の小なるスラグ4は上部取出孔10より、ま
た溶融鉄3は下部取出孔11より外部に取出され、石炭
中の鉄分の混入による増加した溶融鉄や、6岩中の灰分
によるスラグなどが外部に取出される。The means F3 is provided with take-out holes 10 and 11 which are vertically separated from each other, and the slag 4 having a small specific gravity is taken out from the upper take-out hole 10, and the molten iron 3 is taken out from the lower take-out hole 11. The increased amount of molten iron due to the iron content in the rock and slag due to the ash content in the six rocks are taken out.
12は燃焼炉であり、炉Fとは上下の通路13・14に
より連通される。12 is a combustion furnace, which is communicated with the furnace F through upper and lower passages 13 and 14.
この炉12内に空気を注入することにより、溶融鉄8内
の炭素が酸化燃焼し、炉F内の熱分解による熱量を供給
する。By injecting air into the furnace 12, the carbon in the molten iron 8 is oxidized and burned, supplying heat from thermal decomposition in the furnace F.
前述したガス化装置によれば、吹込管2は、窒化物系耐
火物によって構成され、さらに、吹込管2の外周は、炉
Fの炉壁の延長によってスラグ4内迄囲まれているため
、また水蒸気は別の吹込管5で炉F内に送入させるよう
にしたため、吹込管2は水蒸気には直接接触することな
くその寿命の長い特徴を有するものである。According to the above-mentioned gasifier, the blowing pipe 2 is made of a nitride-based refractory, and furthermore, the outer periphery of the blowing pipe 2 is surrounded by the extension of the furnace wall of the furnace F to the inside of the slag 4. Further, since the steam is introduced into the furnace F through a separate blowing pipe 5, the blowing pipe 2 does not come into direct contact with the water vapor and has a long lifespan.
図面はこの発明一実施例を示す側面図である。
1・・・・・・送給装置、2・・・・・・石炭吹込管、
3・・・・・・溶融鉄、5・・・・・・水蒸気吹込管、
F・・・・・・ガス化炉。The drawing is a side view showing one embodiment of this invention. 1... Feeding device, 2... Coal blowing pipe,
3... Molten iron, 5... Steam blowing pipe,
F...Gasifier.
Claims (1)
て送入してガス化する方法において、前記吹込管の内外
周を非酸化ふん囲気に保つべくしたことを特長とする、
前記ガス化方法。 2 前記吹込管の内外周を非酸化ふん囲気に保つのに、
生成ガスを石炭搬送ガスとし、かつ吹込管外周は炉内酸
化ふん囲気と絶縁してなる、特許請求の範囲第1項記載
のガス化方法。 3 溶融熱媒体を貯留するガス化炉に、還元ふん囲気に
おける耐高温性材で構成した石炭吹込管を、石炭送給装
置と前記ガス化炉の溶融熱媒体内とを連通して設け、さ
らにこの石炭吹込管の前記ガス化炉内の少なくとも前記
溶融熱媒体表面より上部は、前記ガス化炉の炉壁の延長
によってガス化炉内のふん囲気と絶縁され、別途水蒸気
吹込管を前記ガス化炉内のふん囲気内に開口させてなる
、石炭のガス化装置。 4 前記石炭送給装置における搬送ガスは、このガス化
炉における生成ガスとしてなる、特許請求の範囲第3項
記載の石炭のガス化装置。 5 前記吹込管の材料は窒化ホウ素とした、特許請求の
範囲第3項記載の石炭のガス化装置。[Claims] 1. A method for gasifying coal by feeding it into a furnace using a molten heat medium through a blowing pipe, characterized in that the inner and outer peripheries of the blowing pipe are kept in a non-oxidizing atmosphere. and
The gasification method. 2. To maintain a non-oxidizing atmosphere around the inner and outer peripheries of the blow pipe,
2. The gasification method according to claim 1, wherein the produced gas is a coal carrier gas, and the outer periphery of the blowing pipe is insulated from the oxidizing atmosphere in the furnace. 3. A coal blowing pipe made of a material resistant to high temperatures in a reducing atmosphere is provided in the gasifier that stores the molten heat medium so as to communicate between the coal feeding device and the molten heat medium of the gasifier, and At least the upper part of the coal injection pipe in the gasification furnace above the surface of the molten heat medium is insulated from the surrounding air in the gasification furnace by the extension of the furnace wall of the gasification furnace, and the steam injection pipe is separately connected to the gasification furnace. A coal gasifier that opens into the atmosphere inside the furnace. 4. The coal gasification device according to claim 3, wherein the carrier gas in the coal feeding device is produced gas in the gasification furnace. 5. The coal gasification apparatus according to claim 3, wherein the material of the blowing pipe is boron nitride.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3598378A JPS5829994B2 (en) | 1978-03-30 | 1978-03-30 | Coal gasification method and device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3598378A JPS5829994B2 (en) | 1978-03-30 | 1978-03-30 | Coal gasification method and device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54129004A JPS54129004A (en) | 1979-10-06 |
| JPS5829994B2 true JPS5829994B2 (en) | 1983-06-25 |
Family
ID=12457103
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3598378A Expired JPS5829994B2 (en) | 1978-03-30 | 1978-03-30 | Coal gasification method and device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5829994B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60243195A (en) * | 1984-04-27 | 1985-12-03 | Hitachi Ltd | Burner for gasifying coal |
-
1978
- 1978-03-30 JP JP3598378A patent/JPS5829994B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54129004A (en) | 1979-10-06 |
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