Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS5927608B2 - Method for absorbing and removing SO↓2 gas using goethite and active iron oxide - Google Patents
[go: Go Back, main page]

JPS5927608B2 - Method for absorbing and removing SO↓2 gas using goethite and active iron oxide - Google Patents

Method for absorbing and removing SO↓2 gas using goethite and active iron oxide

Info

Publication number
JPS5927608B2
JPS5927608B2 JP48132428A JP13242873A JPS5927608B2 JP S5927608 B2 JPS5927608 B2 JP S5927608B2 JP 48132428 A JP48132428 A JP 48132428A JP 13242873 A JP13242873 A JP 13242873A JP S5927608 B2 JPS5927608 B2 JP S5927608B2
Authority
JP
Japan
Prior art keywords
gas
goethite
iron oxide
absorbing
water
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
Application number
JP48132428A
Other languages
Japanese (ja)
Other versions
JPS5081986A (en
Inventor
林平 鎌田
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.)
HOTSUKAIDO
Original Assignee
HOTSUKAIDO
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 HOTSUKAIDO filed Critical HOTSUKAIDO
Priority to JP48132428A priority Critical patent/JPS5927608B2/en
Publication of JPS5081986A publication Critical patent/JPS5081986A/ja
Publication of JPS5927608B2 publication Critical patent/JPS5927608B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Treating Waste Gases (AREA)

Description

【発明の詳細な説明】 本発明は火力発電所、製錬所、その他石炭や重油燃焼の
際に発生する有害なS02ガスを化学反応と吸着により
吸収除去する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for absorbing and removing harmful S02 gas generated during combustion of coal or heavy oil in thermal power plants, smelters, etc. by chemical reaction and adsorption.

以上に関して既に幾多の発明がなされ特許となっている
のでここでは近似する発明(特公昭43〜11648、
特公昭46−20688、特公昭48−2117)と比
較して本発明の特長を鮮明として本願を主張するもので
ある。
Since many inventions regarding the above have already been made and patented, here we will discuss similar inventions (Japanese Patent Publication No. 43-11648,
The purpose of this application is to clearly highlight the features of the present invention in comparison with Japanese Patent Publication No. 46-20688 and Japanese Patent Publication No. 48-2117).

吸収剤としている活性酸化鉄はつぎのようにして作る。The activated iron oxide used as an absorbent is made as follows.

第1図のととく11の三角フラスコに硫酸第1鉄の1/
4モル(69,51g)を水500m1に溶解しpH4
,0以下でとれを図のごとくホットプレートで加湿し6
0〜70℃に保ちながら空気を吹き込む。
Add 1/2 ferrous sulfate to the Erlenmeyer flask No. 11 shown in Figure 1.
Dissolve 4 mol (69.51 g) in 500 ml of water and adjust the pH to 4.
, Humidify with a hot plate as shown in the figure below 6.
Blow in air while keeping the temperature between 0 and 70°C.

(図のごとく水流ポンプを使って外気を吸引し溶液中に
導入する。
(As shown in the figure, use a water pump to suck in outside air and introduce it into the solution.

)かくして出来る沈澱を一夜放置し、ろ過水洗して真空
乾燥すればαFed・(αDができる。
) The resulting precipitate is left overnight, filtered, washed with water, and vacuum dried to yield αFed・(αD.

この時の反応式は2 FeSO4・7H20+H20+
202−〉Fe2O3・H20+2H2SO4+12
H20である。
The reaction formula at this time is 2 FeSO4・7H20+H20+
202-〉Fe2O3・H20+2H2SO4+12
It is H20.

これがゲーサイトで天然には針鉄鉱、褐鉄鉱などとして
産出する。
This is goethite, which is naturally produced as goethite and limonite.

この人工物と天然物とは電子顕微鏡によって見れば外観
は全く異なり人工物は針状で天然物は塊状である。
When viewed under an electron microscope, the artificial material and the natural material have completely different appearances, with the artificial material having a needle-like shape and the natural material having a block-like shape.

天然物は含有する不純物などの関係で一様な性質のもの
を得ることは困難であシ、したがって比較試験には適し
ない。
It is difficult to obtain natural products with uniform properties due to the impurities they contain, and therefore they are not suitable for comparative tests.

故に工業的にはできた沈澱のFe2O3・H20= 2
FeO・(OH)を回収し鉄くずと水を追加すれば、
連続して作ることができるので、この価格は鉄くずから
決められるものである。
Therefore, industrially produced precipitate Fe2O3・H20 = 2
If you collect FeO・(OH) and add iron scraps and water,
Since it can be made continuously, this price is determined from scrap iron.

このαFe2O3・H20養示差熱分析すれば326℃
に吸熱のピークがあり、ここで結晶水の放出がある。
If this αFe2O3・H20 differential heat analysis is performed, it will be 326℃.
There is an endothermic peak at which water of crystallization is released.

またX線回析によって検すればFe2O3・H2Oの結
晶は300℃付近でくずれ、以後600℃付近でヘマタ
イトの結晶を作るまでは明瞭な結晶性はなく、この間で
よくSO□ガスを吸収し反応してFe2(SO4)3を
作る。
Furthermore, when examined by X-ray diffraction, Fe2O3/H2O crystals collapse at around 300℃, and there is no clear crystallinity until hematite crystals are formed at around 600℃, during which time SO□ gas is well absorbed and reacts. to produce Fe2(SO4)3.

すなわち、この300〜600°Cの間において極めて
活性化されている。
That is, it is extremely activated between 300 and 600°C.

この活性化された酸化鉄の製法は第2図に示す。The method for producing this activated iron oxide is shown in FIG.

図中で2は電気炉で325°Cに保つ。In the figure, 2 is kept at 325°C in an electric furnace.

4は試料αFeO・(OH)で第1図の装置によシ作っ
たものである。
4 is a sample αFeO.(OH) prepared using the apparatus shown in FIG.

3は試料を入れている試験管で中間を図のごとく細くし
ている。
3 is the test tube containing the sample, with the middle part narrowed as shown in the figure.

1は真空ポンプに連結する肉厚ゴム管である。1 is a thick rubber tube connected to a vacuum pump.

真空ポンプで減圧し325°Cで1時間加熱した後断電
し放冷する。
After reducing the pressure with a vacuum pump and heating at 325°C for 1 hour, the power was cut off and the mixture was allowed to cool.

冷却後炉外に取り出し細くしである部分をバーナーで焼
き切る。
After cooling, take it out of the oven and burn off the thin part with a burner.

かくして活性酸化鉄をアンブール中に減圧封入し保存す
る。
Thus, the activated iron oxide is sealed and stored in an ambour under reduced pressure.

このアンブールの尖端を切って空気中にさらすならば活
姓酸化鉄は発熱し赤化し手で持つととはできない。
If you cut off the tip of this ambour and expose it to the air, the active iron oxide will heat up and turn red, making it impossible to hold it in your hand.

したがってこのもののX線回析や化学分析をその性質を
保持したまま行うことは困難である。
Therefore, it is difficult to perform X-ray diffraction or chemical analysis of this material while preserving its properties.

との興味ある物質は昭和49年11月29日に日本鉱業
会北海道支部大会に発表した。
The interesting substance was presented at the Hokkaido Branch Conference of the Japan Mining Association on November 29, 1971.

大気中で室温で強い発熱酸化をすることは、このものの
表面積が極めて多大であり空気中の酸素と接触酸化を行
うためと考えられる。
The strong exothermic oxidation in the air at room temperature is thought to be due to the extremely large surface area of this material, which causes catalytic oxidation with oxygen in the air.

また、その色は黒色でFe2O3・FeOと同様な感じ
であり微粒子活性のFe2O3・FeOが空気により2
Fe 20gに変化したものかも知れないが現段階で
は結論は出せない。
In addition, its color is black and it looks similar to Fe2O3/FeO, and the active particulate Fe2O3/FeO is oxidized by air.
It may have changed to 20g of Fe, but no conclusion can be drawn at this stage.

このような活性なものを純粋に保って吸収試験を行うこ
とはできないので減圧下でゆっくり酸化させて使用した
Since it is not possible to conduct an absorption test while keeping such an active substance pure, it was used after being slowly oxidized under reduced pressure.

この時に完全に同一のものを作ることが困難でゲーサイ
トと活性酸化鉄との吸収試験の比較を行ったが一部に矛
盾が見られた。
At this time, it was difficult to make completely identical products, so we compared absorption tests between goethite and active iron oxide, but some discrepancies were found.

それを第1表に示す。It is shown in Table 1.

上表によって明らかなように、脱硫に利用される混度帯
すなわち室温から350°Cの間において活性酸化鉄の
ほうがゲーサイトよりよい成績を示す。
As is clear from the above table, active iron oxide shows better performance than goethite in the mixing range used for desulfurization, that is, between room temperature and 350°C.

この吸収試験の方法は第3図に示す。試験の条件は、試
料3.0g、SO2ガス濃度約1.0%、通気量毎分1
00〜120m1.試料層の厚さ110朋、試料管の太
さ内径10mmである。
The method of this absorption test is shown in FIG. The test conditions were: sample 3.0g, SO2 gas concentration approximately 1.0%, air flow rate 1/min.
00-120m1. The thickness of the sample layer was 110 mm, and the inner diameter of the sample tube was 10 mm.

第1表でゲーサイトの欄に450°C1500℃を記入
したが、450℃では活性酸化鉄になっているはずで、
この試験はゲーサイトの吸収試験で段々昇温させたとき
のものである。
In Table 1, I entered 450°C and 1500°C in the goethite column, but at 450°C it should be active iron oxide.
This test is an absorption test of goethite when the temperature is gradually increased.

326°Cより高温ではゲーサイトは存在しないはずで
ある。
There should be no goethite present above 326°C.

以上の結果からゲーサイトのSO2ガス吸収は主として
表面付着であり、活性酸化鉄による吸収は付着と化学反
応と両方が行われているものである。
From the above results, SO2 gas absorption by goethite is mainly due to surface adhesion, and absorption by active iron oxide involves both adhesion and chemical reaction.

つぎに、前記の3特許と比較し一覧表として示すと第2
表の如くなる。
Next, when compared with the three patents mentioned above and shown as a list, the second
It will look like the table.

上表で特公昭46−20688、特公昭48−2117
、本発明ともにγFed(OH)からスタートしている
が、詳細な説明で述べているごとく製法が異なり本発明
がもつとも簡便である。
In the table above, special public service number 46-20688, special public service number 48-2117
Both of the present invention and the present invention start from γFed(OH), but as described in the detailed description, the manufacturing method is different and the present invention is simpler.

また、沈澱する時のpHが異なる故に性質が異なる。Furthermore, since the pH at the time of precipitation is different, the properties are different.

特に本発明の吸収剤はまだ特定出来ないがFe2O3・
FeOの可能性がある。
In particular, the absorbent of the present invention cannot be identified yet, but Fe2O3.
Possibly FeO.

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

第1図はゲーサイトαFed(OH)の製造装置である
。 1は内容11の三角フラスコである。2は硫酸第一鉄F
eSO4・7H20の水溶液で、3は300Wのホット
プレートである。 4は生成されたゲーサイトである。 第2図はゲーサイトから活1生酸化鉄を製造する装置で
ある。 4はゲーサイト、2は電気炉、3は中間を加熱して細く
した試験管、1は真空ポンプへ連結する肉厚ゴム管であ
る。 第3図はSO2ガス吸収試験をする装置である。 1は内容約50Tnlのガラス管で、2はH2SO3溶
液である。 3はSO□ガスを貯蔵する風船で内容約11.257で
ある。 4は内容約207のガラス瓶で水道水の流入、流出によ
り風船中のガスを出したり入れたりする。 5は活栓付ガラス管である。6はゴム管を締めるゴム管
を締めるピンチコックである。 7は試料管で、8は試料、9はガラスフィルター、10
はニクロム線電気炉である。 11は500m1の三角フラスコ、12はKMn 04
の水溶液、13は300m1の三角フラスコで、14は
KMnO4の水溶液であり、15はいはい形流量計であ
る。 捷ず、4に水道水を充満させて3中の空気を追い出し、
つぎにH2SO3に連結するピンチコツクロを開け、つ
ぎに4中の水を左下に流出する。 この時空気が、H2SO3水中を通過しSO2を発生し
風船中に貯蔵する。 風船が一杯に膨張したならば水の排出をとめピンチコツ
クロを閉める(図の現状)。 つぎにゴム管を試料管に連結し水道水を毎分100〜1
20m1づつ4に流入させれば風船中のSO2ガスは1
00〜120m1/分の流量で試料中を通過する。 発生させ風船中に貯蔵したS02ガスの量は次のごとく
して決定する。 H2SO3水中のSO2は大体6〜7%程度のものであ
るが、それはH2SO3→H20十SO2の反応によっ
てSO2を生ずるが、残部は中性の水ではなく、空気に
よって酸化されたH2SO4を残留する。 まずH2S03水にH2O2を力口えて酸化しH2SO
4とし1/1ONNaOHにより滴定LJI度を決定す
る。 また、空気を吹き込んでS02が発生した後の残留液を
H2O2で完全にH2SO4とした後、1/10 N
NaOHで滴定し濃度を決定し、その差が発生したSO
2の量である。 かくして亜硫酸水の濃度を決め、その1rulからSO
。 ガスがどれだけ発生するかを決める。 それから112廐を発生するに必要な量を決め、1に入
れて空気を通せば風船の内容が11.251であるから
約1%の濃度のガスが風船中に貯蔵される。 試料を電気炉で所定の温度に予め加熱しておく。 そして風船中のS02ガスを通過させる。 試料を通過したS02ガスは、12のKMnO4溶液に
入る。 S02は還元性ガスであるからKMr+04溶液と当量
になった時に溶液の赤紫色が無色透明に変る。 この反応は鋭敏であるから明確に知り得る。14のKM
nO4溶液は予備的なもので、万一にもS02ガスが流
量計に来て外部に漏れることがないようにしている。
FIG. 1 shows an apparatus for manufacturing goethite αFed (OH). 1 is an Erlenmeyer flask with contents 11. 2 is ferrous sulfate F
It is an aqueous solution of eSO4.7H20, and 3 is a 300W hot plate. 4 is a generated game site. Figure 2 shows an apparatus for producing live iron oxide from goethite. 4 is goethite, 2 is an electric furnace, 3 is a test tube whose middle part is heated to make it thin, and 1 is a thick rubber tube connected to a vacuum pump. Figure 3 shows an apparatus for conducting SO2 gas absorption tests. 1 is a glass tube with a content of about 50 Tnl, and 2 is a H2SO3 solution. 3 is a balloon that stores SO□ gas and has a content of approximately 11.257. 4 is a glass bottle with a content of approximately 207 cm, and the gas in the balloon is released and added by the inflow and outflow of tap water. 5 is a glass tube with a stopcock. 6 is a pinch cock that tightens the rubber tube. 7 is a sample tube, 8 is a sample, 9 is a glass filter, 10
is a nichrome wire electric furnace. 11 is a 500m1 Erlenmeyer flask, 12 is KMn 04
13 is a 300 ml Erlenmeyer flask, 14 is an aqueous solution of KMnO4, and 15 is a crawler flowmeter. Without washing, fill 4 with tap water and expel the air in 3.
Next, open the pinch bottle connected to H2SO3, and then let the water in 4 flow out to the bottom left. At this time, air passes through the H2SO3 water and generates SO2, which is stored in the balloon. Once the balloon is fully inflated, stop draining the water and close the pinch cap (as shown in the diagram). Next, connect the rubber tube to the sample tube and pour tap water at 100 to 1
If 20ml of SO2 gas flows into 4 at a time, the amount of SO2 gas in the balloon will be 1.
It passes through the sample at a flow rate of 00 to 120 ml/min. The amount of S02 gas generated and stored in the balloon is determined as follows. SO2 in H2SO3 water is approximately 6 to 7%, which produces SO2 through the reaction of H2SO3→H20+SO2, but the remainder is not neutral water but remains H2SO4 oxidized by air. First, add H2O2 to H2S03 water and oxidize it to H2SO.
4 and 1/1 ON NaOH to determine the titration LJI degree. In addition, after blowing air and generating S02, the residual liquid was completely converted to H2SO4 with H2O2, and then 1/10 N
Titrate with NaOH to determine the concentration, and the difference occurs in SO
The amount is 2. In this way, the concentration of sulfite water is determined, and SO
. Determines how much gas is produced. Then, determine the amount necessary to generate 112 ml, put it in 1, and pass air through it.Since the content of the balloon is 11.25 ml, a concentration of about 1% gas will be stored in the balloon. The sample is preheated to a predetermined temperature in an electric furnace. Then, the S02 gas in the balloon is passed through. The S02 gas passing through the sample enters the KMnO4 solution at 12. Since S02 is a reducing gas, when it becomes equivalent to the KMr+04 solution, the reddish-purple color of the solution changes to colorless and transparent. This reaction is so sensitive that it can be clearly seen. 14 KM
The nO4 solution is a preliminary one to prevent S02 gas from reaching the flow meter and leaking outside.

Claims (1)

【特許請求の範囲】[Claims] 1 ゲーサイト(αFed(OH)またはαFe2O3
−H2O)を300〜400℃に加熱して結晶水を除去
して得た活性酸化鉄(Fe203であって、未だへマタ
イトの結晶を生じていない非晶質の状態にあるもの)を
S02含有ガスと接触させてSO□ガスを吸収除去する
方法。
1 Goethite (αFed(OH) or αFe2O3
-H2O) to 300 to 400°C to remove crystallization water and contains activated iron oxide (Fe203, which is in an amorphous state without forming hematite crystals) containing S02. A method of absorbing and removing SO□ gas by contacting it with gas.
JP48132428A 1973-11-25 1973-11-25 Method for absorbing and removing SO↓2 gas using goethite and active iron oxide Expired JPS5927608B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP48132428A JPS5927608B2 (en) 1973-11-25 1973-11-25 Method for absorbing and removing SO↓2 gas using goethite and active iron oxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP48132428A JPS5927608B2 (en) 1973-11-25 1973-11-25 Method for absorbing and removing SO↓2 gas using goethite and active iron oxide

Publications (2)

Publication Number Publication Date
JPS5081986A JPS5081986A (en) 1975-07-03
JPS5927608B2 true JPS5927608B2 (en) 1984-07-06

Family

ID=15081134

Family Applications (1)

Application Number Title Priority Date Filing Date
JP48132428A Expired JPS5927608B2 (en) 1973-11-25 1973-11-25 Method for absorbing and removing SO↓2 gas using goethite and active iron oxide

Country Status (1)

Country Link
JP (1) JPS5927608B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013053060A (en) * 2011-08-09 2013-03-21 Jfe Steel Corp Method for generating hydrogen gas
JP2016199439A (en) * 2015-04-13 2016-12-01 Jfeスチール株式会社 Hydrogen gas generation method

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5296966A (en) * 1976-02-12 1977-08-15 Hitachi Ltd Treatment of exhaust gas containing nitrogen oxides and sulfur oxides
JPS5317591A (en) * 1976-08-02 1978-02-17 Hitachi Ltd Treating method for exhaust gas containing sulfur oxides
CN103962090B (en) * 2013-01-29 2017-02-08 中国石油化工股份有限公司 Multi-metal solid desulfurizing agent and preparing method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013053060A (en) * 2011-08-09 2013-03-21 Jfe Steel Corp Method for generating hydrogen gas
JP2016199439A (en) * 2015-04-13 2016-12-01 Jfeスチール株式会社 Hydrogen gas generation method

Also Published As

Publication number Publication date
JPS5081986A (en) 1975-07-03

Similar Documents

Publication Publication Date Title
CN110404526B (en) La derived based on MOFs2O3Method for removing PPCPs and As (III) by using @ C activated persulfate
Liander The utilisation of natural gases for the ammonia process
Merrill et al. The Catalytic Oxidation of Carbon Monoxide at Ordinary Temperatures.
CN103495333A (en) Treatment technology for Claus tail gas containing sulfur dioxide, hydrogen sulfide and organic sulfur
ITMI950184A1 (en) MATERIAL WITH A LAYER STRUCTURE OF THE HYDROTHALCITE TYPE AND RELATED USES
JPS5927608B2 (en) Method for absorbing and removing SO↓2 gas using goethite and active iron oxide
Schuit et al. Activated adsorption of hydrogen on nickel catalysts
CN108620099A (en) Double cavity magnetic Fes3O4@mSiO2@BiOCl-Ag/AgBr composite material and preparation methods
CN109678137A (en) A kind of preparation method of hollow Nano carbon balls
CN114956078A (en) Porous carbon material and preparation method and application thereof
Maak et al. A simple method of inert gas purification
US1896916A (en) Method of making commercial hydrogen
CN110280213B (en) A nano-magnetic composite iron-copper oxide dearsenic adsorbent and its preparation method and application
CN109250763A (en) A kind of method of hydrogen sulfide methane reforming hydrogen manufacturing
CN106823769A (en) A kind of preparation method of ferric oxide desulfurizer
JPS5820729A (en) Preparation of manganese oxide
CN113603177B (en) Reconfigurable and regenerative azo dye adsorption method and application thereof
CN106475040A (en) A kind of facile syntheesis of additive Mn iron oxide and its application
CN118724089A (en) A NiO-Co3O4 composite material and its preparation method and application
Holmes et al. Vanadium Compounds as Catalysts for the Oxidation of Sulfur Dioxide1
CN113643599A (en) Catalytic oxidation experimental device and experimental method for ethanol
JPS5959248A (en) Ozone decomposing catalyst
US1912877A (en) Gas purification
US1316950A (en) Elektbisk kvaelstofaktieseliskab
US1370867A (en) Process of making oxids of nitrogen