JPH10328542A - Method for dissolving quick line and device therefor - Google Patents

Method for dissolving quick line and device therefor

Info

Publication number
JPH10328542A
JPH10328542A JP15927297A JP15927297A JPH10328542A JP H10328542 A JPH10328542 A JP H10328542A JP 15927297 A JP15927297 A JP 15927297A JP 15927297 A JP15927297 A JP 15927297A JP H10328542 A JPH10328542 A JP H10328542A
Authority
JP
Japan
Prior art keywords
shaped member
lime
quicklime
solution
pipe
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Withdrawn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
JP15927297A
Other languages
Japanese (ja)
Inventor
Kiyoaki Mori
清明 森
Takaki Yoshimura
恭樹 吉村
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP15927297A priority Critical patent/JPH10328542A/en
Publication of JPH10328542A publication Critical patent/JPH10328542A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To inexpensively and efficiently neutralize a waste acid by preventing the generation of dust in the case of using quick lime inexpensive as a neutralize for waste acid treatment. SOLUTION: This quick lime dissolving device is provided with a helmet shaped member 7 receiving a granular quick lime discharged and falling down from a quick lime charging pipe 4, a funnel shaped member 8 provided to surround the helmet shaped member 7 and a liquid injection pipe 9 for injecting a solution inside of the funnel shaped member 8 in the tangential direction of the funnel shaped member 8. The solution injected to the funnel shaped member 8 from the liquid injection pipe 9 spirally flows and forms swirling flow and the quick lime falling down from the helmet shaped member 7 is rapidly involved in the swirling flow and dissolved without generating dust.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、製鉄所等で発生す
る酸廃液の中和処理に用いられる生石灰の溶解方法及び
その装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for dissolving lime used for neutralizing acid waste liquor generated in an ironworks.

【0002】[0002]

【従来の技術】酸洗廃液等の酸廃液の中和処理には、従
来は安全で取扱の容易な消石灰が主に用いられてきた
が、最近は中和処理コストを低減するために生石灰が用
いられるようになってきた。これら石灰は粉粒状のもの
を水に解かした石灰溶液の状態で用いられるが、生石灰
を水に解かす場合は、発熱による水蒸気の発生により生
石灰の粉塵が多量に発生し配管等を閉塞させるという問
題がある。
2. Description of the Related Art Slaked lime, which is safe and easy to handle, has been mainly used for neutralizing acid waste liquid such as pickling waste liquid. Recently, however, quick lime has been used to reduce the cost of neutralization treatment. It is being used. These limes are used in the form of a lime solution in which powdery and granular materials are dissolved in water.However, when quicklime is dissolved in water, a large amount of quicklime is generated due to the generation of steam due to heat generation, which blocks pipes and the like. There's a problem.

【0003】このような問題を解決するために、生石灰
を溶解槽に投入する投入管の周囲をカバーで覆う方法が
知られているが、カバー内で発生した粉塵がカバー内面
に付着するため、清掃に多大な労力を必要とする。ま
た、溶解を促進させるために溶解槽内を撹拌すると、溶
解不十分な生石灰は溶解槽内で団子状となってカバー外
に流出した後、崩れて粉塵となり、また粉塵を捕獲する
ためのバグフィルターは目詰まりしを生じ易く頻繁な交
換を必要とする。
[0003] In order to solve such a problem, a method of covering around a charging pipe for charging quicklime into a melting tank with a cover is known. However, dust generated in the cover adheres to the inner surface of the cover. Cleaning requires a lot of labor. Also, if the inside of the melting tank is agitated to promote the melting, the insufficiently dissolved quicklime will form a dumpling in the melting tank and flow out of the cover, then collapse and become dust, and a bug to capture the dust. Filters are prone to clogging and require frequent replacement.

【0004】粉塵の発生を抑制する方法として、例えば
特開昭64−30694号公報によれば、中和剤として
生石灰を60%以下、消石灰を23〜83%、炭酸カル
シウを7〜25%配合したものを用いる方法が知られて
いる。しかし、この方法では生石灰を100%使用する
ことはできない。
As a method for suppressing the generation of dust, for example, according to Japanese Patent Application Laid-Open No. Sho 64-30694, 60% or less of quicklime, 23 to 83% of slaked lime, and 7 to 25% of calcium carbonate are used as neutralizing agents. There is known a method of using the above. However, 100% of quicklime cannot be used in this method.

【0005】[0005]

【発明が解決しようとする課題】本発明は、廃酸処理用
の中和剤として廉価な生石灰を用いた場合の、粉塵発生
を防止することにより、廃酸中和処理を低コストで効率
よく行うことを目的とする。
DISCLOSURE OF THE INVENTION The present invention provides a low-cost and efficient waste acid neutralization treatment by preventing the generation of dust when inexpensive quicklime is used as a neutralizing agent for waste acid treatment. The purpose is to do.

【0006】[0006]

【課題を解決するための手段】前記課題を解決する本発
明の生石灰溶解方法は、粉粒状の生石灰粉を水に供給し
溶解させて石灰溶液とする方法において、渦状に流動す
る水または石灰溶液の旋回流を形成させ、該旋回流に前
記生石灰を供給することを特徴とする。
According to the present invention, there is provided a method for dissolving quicklime in a method for supplying and dissolving powdered quicklime powder in water to form a lime solution. Wherein the swirling flow is formed, and the quicklime is supplied to the swirling flow.

【0007】また、生石灰溶解装置は、生石灰投入管か
ら排出され落下する粉粒状の生石灰粉を受ける陣笠状部
材と、陣笠状部材を囲むように設けられた漏斗状部材
と、漏斗状部材の接線方向に向けて漏斗状部材の内側に
水または石灰溶液を注入する液注入管とを有することを
特徴とする。
[0007] The quicklime dissolving apparatus further comprises a chin-shape member for receiving powdery granulated lime powder discharged from the quick-lime charging pipe, falling, a funnel-like member provided to surround the chinshade-like member, and a tangent to the funnel-like member. A liquid injection pipe for injecting water or lime solution into the funnel-shaped member in the direction.

【0008】[0008]

【発明の実施の形態】本発明の方法及び装置を図面に示
す装置例を用いて詳細に説明する。図1において、粉粒
状の生石灰Cを収容する貯留タンク1の下端には生石灰
を切り出す切出フィーダ2が設けられており、切出フィ
ーダ2の出側には切出弁3を有する生石灰投入管4が設
けられている。貯留タンク1内の生石灰Cはモーター5
により回転するスクリュー6によって生石灰投入管4か
ら切り出すことができる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The method and apparatus of the present invention will be described in detail with reference to an apparatus example shown in the drawings. In FIG. 1, a cutout feeder 2 for cutting out quicklime is provided at a lower end of a storage tank 1 for accommodating powdered and granular quicklime C, and a quicklime feed pipe having a cutout valve 3 on an outlet side of the cutout feeder 2. 4 are provided. Quicklime C in the storage tank 1
Can be cut out from the quicklime input pipe 4 by the screw 6 rotating.

【0009】図2及び図3に拡大して示すように生石灰
投入管4の下端には、漏斗状部材8が設けられており、
漏斗状部材8に支持して陣笠状部材7が設けられてい
る。漏斗状部材8の上部には、水または石灰溶液を注入
する液注入管9が設けられており、液注入管9の液注入
口9aは、漏斗状部材8の内側に開口し、且つ漏斗状部
材8の接線方向に向けられている。液注入管9からは、
生石灰を溶解するための水または石灰溶液が漏斗状部材
8の接線方向から噴出し、漏斗状部材8の内周面に沿っ
て旋回することで漏斗状部材8の内周面上で渦状の旋回
流Wが形成される。
As shown in FIGS. 2 and 3 in an enlarged manner, a funnel-shaped member 8 is provided at a lower end of the quicklime input pipe 4.
The umbrella-shaped member 7 is provided so as to be supported by the funnel-shaped member 8. A liquid injection pipe 9 for injecting water or lime solution is provided at an upper part of the funnel-shaped member 8, and a liquid injection port 9a of the liquid injection pipe 9 is opened inside the funnel-shaped member 8 and has a funnel shape. It is oriented in the tangential direction of the member 8. From the liquid injection pipe 9,
Water or lime solution for dissolving quicklime is squirted from the tangential direction of the funnel-shaped member 8 and swirls along the inner peripheral surface of the funnel-shaped member 8, thereby making a spiral swirl on the inner peripheral surface of the funnel-shaped member 8. A stream W is formed.

【0010】生石灰投入管4から陣笠状部材7に落下し
た生石灰Cは、陣笠状部材7で均等分散されながらその
周縁から渦状の旋回流Wに落下することで、速やかに旋
回流Wに巻き込まれながら下方へ向かうため、石灰粉塵
の発生が抑制されて、図1に示す溶解槽10に送られ
る。溶解槽10は蓋11で覆われて撹拌機12及び液面
レベル計13が設けられており、溶解槽10内の石灰溶
液は撹拌され混和される。溶解槽の蓋11には槽内で発
生した石灰粉塵を吸引する排気ダクト14が設けられて
おり、排気ダクト14は石灰粉塵を捕獲回収するウエッ
トスクラバー15に接続されている。
The quicklime C that has fallen from the quicklime input pipe 4 to the garbage-like member 7 falls into the spiral vortex W from the periphery thereof while being uniformly dispersed by the garbage-like member 7, and is quickly caught in the whirlpool W. While moving downward, the generation of lime dust is suppressed and sent to the melting tank 10 shown in FIG. The dissolving tank 10 is covered with a lid 11 and provided with a stirrer 12 and a liquid level meter 13, and the lime solution in the dissolving tank 10 is stirred and mixed. The lid 11 of the melting tank is provided with an exhaust duct 14 for sucking lime dust generated in the tank, and the exhaust duct 14 is connected to a wet scrubber 15 for capturing and collecting lime dust.

【0011】ウエットスクラバー15には、多数段の多
孔板16、ミストセパレータ(エリミネータ)17、循
環ポンプ18を介して設けられた洗浄ノズル19、補給
水管20及び補給水弁21を有する洗浄ノズル22、排
気ファン23を内蔵する排気ダクト24が設けられてい
る。ウエットスクラバー15の下端には水または石灰溶
液を貯留する逆角錐状の循環液貯留タンク25が設けら
れており、循環液貯留タンク25内には循環ポンプ18
のサクション部、液温計26及び液面レベル計27が設
けられている。
The wet scrubber 15 includes a multistage perforated plate 16, a mist separator (eliminator) 17, a washing nozzle 19 provided via a circulation pump 18, a washing nozzle 22 having a makeup water pipe 20 and a makeup water valve 21, An exhaust duct 24 containing an exhaust fan 23 is provided. An inverted pyramid-shaped circulating liquid storage tank 25 for storing water or lime solution is provided at the lower end of the wet scrubber 15.
, A liquid temperature gauge 26 and a liquid level meter 27 are provided.

【0012】循環液貯留タンク25の下端には、弁2
8、29を有するサクション部が設けられており、該サ
クション部は図2及び図3に示す液注入管9に接続され
ている。ウエットスクラバー15と貯留タンク1との間
には、密閉弁30を有する排気管31が設けられてお
り、貯留タンク1で発生した石灰粉塵をウエットスクラ
バー15の下方に取り込むようになっている。排気管3
1と32の間にはサイクロン33及び貯留タンク1に接
続された粉塵排出弁34が設けられており、貯留タンク
1には、生石灰受入管46及び受入管の口栓47が設け
られている。
At the lower end of the circulating liquid storage tank 25, a valve 2 is provided.
A suction part having 8 and 29 is provided, and the suction part is connected to the liquid injection pipe 9 shown in FIGS. An exhaust pipe 31 having a sealing valve 30 is provided between the wet scrubber 15 and the storage tank 1 so that lime dust generated in the storage tank 1 is taken in below the wet scrubber 15. Exhaust pipe 3
A dust discharge valve 34 connected to the cyclone 33 and the storage tank 1 is provided between 1 and 32. The storage tank 1 is provided with a quicklime receiving pipe 46 and a plug 47 for the receiving pipe.

【0013】溶解槽10の上方には、石灰溶液の温度を
測定するための液温計測用タンク35が設けられてお
り、該タンクは3室に分割されている。ウエットスクラ
バー15側の第1室35aは下部が連通するセパレータ
36によって仕切られており、そのウエットスクラバー
側には溶解槽10の石灰溶液を汲み上げるための溶液汲
上管37がポンプ38を介して設けられており、反ウエ
ットスクラバー側には液温計39が設けられている。
Above the melting tank 10, a tank 35 for measuring the temperature of the lime solution is provided, and the tank is divided into three chambers. The first chamber 35a on the wet scrubber 15 side is partitioned by a separator 36 communicating with the lower part, and a solution pumping tube 37 for pumping the lime solution in the dissolving tank 10 is provided on the wet scrubber side via a pump 38. A liquid thermometer 39 is provided on the side opposite to the wet scrubber.

【0014】液温計測用タンクの第2室35bには弁4
0を有する溶液排出管41が溶解槽の蓋11に接続して
設けられており、第3室35cには石灰溶液を溶液貯留
槽43に排出する溶液排出管42が設けられている。溶
液貯留槽43には液面レベル計44及び撹拌機45が設
けられている。
A valve 4 is provided in the second chamber 35b of the liquid temperature measuring tank.
A solution discharge pipe 41 having 0 is provided to be connected to the lid 11 of the dissolution tank, and a solution discharge pipe 42 for discharging the lime solution to the solution storage tank 43 is provided in the third chamber 35c. The solution storage tank 43 is provided with a liquid level meter 44 and a stirrer 45.

【0015】次に、上述の装置における作動を主に図1
を用いて説明する。本装置を新規に使用する場合は、図
1に示す循環溶液貯留タンク25には補給水管20から
供給された水が満たされている。循環溶液貯留タンク2
5の弁28及び29を開にすると、循環溶液貯留タンク
25内の水が図2及び図3に示す液注入管9から漏斗状
部材8内に注入される。液注入管9は漏斗状部材8の接
線方向に設けられているため、液注入管9から吐き出さ
れた水は、漏斗状部材8の内周面に沿って流動して旋回
流Wを形成し、渦状となって溶解槽10に落下する。
Next, the operation of the above-described apparatus will be described mainly with reference to FIG.
This will be described with reference to FIG. When this apparatus is newly used, the circulating solution storage tank 25 shown in FIG. 1 is filled with water supplied from the makeup water pipe 20. Circulating solution storage tank 2
When the valves 28 and 29 of No. 5 are opened, the water in the circulating solution storage tank 25 is injected into the funnel-shaped member 8 from the liquid injection pipe 9 shown in FIGS. Since the liquid injection pipe 9 is provided in the tangential direction of the funnel-shaped member 8, the water discharged from the liquid injection pipe 9 flows along the inner peripheral surface of the funnel-shaped member 8 to form a swirling flow W. , And falls into the dissolving tank 10 in a vortex shape.

【0016】一方、図1に示す貯留タンク1内の粉状の
生石灰は、切出しフィーダ2によって切り出され、生石
灰投入管4から陣笠状部材7に落下し、図2及び図3に
示す陣笠状部材7の上面で円周方向均等に分散されて旋
回流Wに落下する。旋回流Wに均等分散して落下した生
石灰は、速やかに旋回流Wに巻き込まれるため、粉塵の
発生が抑制されて溶解槽10に流れ落ちると共に溶解槽
10での団子状化が防止される。
On the other hand, the powdery lime in the storage tank 1 shown in FIG. 1 is cut out by the cut-out feeder 2 and falls from the quick lime charging pipe 4 to the chin-shape member 7, and the gin-shape member shown in FIGS. 7 are uniformly distributed in the circumferential direction and fall into the swirling flow W. The quicklime that is uniformly dispersed and falls in the swirling flow W is immediately caught in the swirling flow W, so that the generation of dust is suppressed, and the quicklime flows down into the melting tank 10 and is prevented from forming a dumpling in the melting tank 10.

【0017】溶解槽10では水と生石灰との反応によっ
て石灰溶液は60℃近くまで上昇し(濃度8%のと
き)、石灰粉塵を含む水蒸気が発生する。この水蒸気
は、排気ファン23により排気ダクト14を通してウェ
ットスクラバー15の下方に吸引することで、溶解槽1
0で発生した粉塵が漏斗状部材8内に浸入することによ
る生石灰投入管4及び切出弁3の閉塞を防止する。
In the dissolving tank 10, the lime solution rises to near 60 ° C. (when the concentration is 8%) due to the reaction between water and quicklime, and steam containing lime dust is generated. This water vapor is sucked by the exhaust fan 23 below the wet scrubber 15 through the exhaust duct 14 so that
The dust generated at 0 is prevented from entering the funnel-shaped member 8 to block the quicklime input pipe 4 and the cutout valve 3.

【0018】ウェットスクラバー15においては、排気
ダクト14を通った粉塵が複数段の多孔板16に向かっ
て上昇する。循環溶液貯留タンク25の水は循環ポンプ
18によって汲み上げられ洗浄ノズル19から水膜状と
なって複数段の多孔板16に供給され、この水膜に粉塵
は捕獲され循環溶液貯留タンク25に落下する。
In the wet scrubber 15, the dust passing through the exhaust duct 14 rises toward the multi-stage perforated plate 16. The water in the circulating solution storage tank 25 is pumped up by the circulating pump 18 and is supplied from the washing nozzle 19 into a water film form to the perforated plates 16 in a plurality of stages. Dust is captured by the water film and falls into the circulating solution storage tank 25. .

【0019】多孔板16で発生する粉塵を含む飛沫は、
排気ファン23によって吸い上げられてミストセパレー
タ17で捕獲される。ミストセパレータ17で捕獲され
た粉塵は、洗浄ノズル22から噴出する補給水管20の
洗浄水によって洗い流される。粉塵の捕獲に伴って循環
溶液貯留タンク25の水は石灰溶液となり、弁28、2
9を通って液注入管9に供給される。
The droplets including dust generated in the perforated plate 16 are:
The air is sucked up by the exhaust fan 23 and captured by the mist separator 17. The dust captured by the mist separator 17 is washed away by the washing water of the makeup water pipe 20 ejected from the washing nozzle 22. With the capture of dust, the water in the circulating solution storage tank 25 becomes a lime solution,
The liquid is supplied to the liquid injection pipe 9 through the pipe 9.

【0020】循環液貯留タンク25における液面レベル
の制御は、液面レベル計27による検出値が所定の範囲
内となるように補給水弁21を制御して行い、溶解槽1
0における液面レベルの制御は、液面レベル計13によ
る検出値が所定の範囲内となるように弁40を調整する
ことによって行う。
The liquid level in the circulating liquid storage tank 25 is controlled by controlling the make-up water valve 21 so that the value detected by the liquid level meter 27 falls within a predetermined range.
The control of the liquid level at 0 is performed by adjusting the valve 40 so that the value detected by the liquid level meter 13 falls within a predetermined range.

【0021】石灰溶液の温度は濃度と比例関係にあるた
め、石灰溶液の温度を制御することで濃度を制御する。
溶解槽10の濃度の制御は、液温計39による液温に応
じてモータ5を制御することで行い、循環液貯留タンク
25の濃度の制御は、液温計26による液温に応じて補
給水弁21を制御することで行う。
Since the temperature of the lime solution is proportional to the concentration, the concentration is controlled by controlling the temperature of the lime solution.
The concentration of the dissolving tank 10 is controlled by controlling the motor 5 according to the liquid temperature measured by the liquid thermometer 39, and the concentration of the circulating liquid storage tank 25 is controlled according to the liquid temperature measured by the liquid thermometer 26. This is performed by controlling the water valve 21.

【0022】貯留タンク1に生石灰を受け入れるとき
は、粉塵排出弁34を開にしてサイクロン33により石
灰粉塵を捕獲し、貯留タンク1に回収する。排気管31
内の粉塵は、密閉弁30を開にして排気ファン24を作
動させウェットスクラバー15に引き入れる。生石灰切
り出し時以外は切出弁3は閉にし、生石灰受入れ時以外
は生石灰受入管46に口栓47を装着し、また、排気管
31の密閉弁30を閉じて貯留タンク1を密閉状態にす
る。
When the quicklime is to be received in the storage tank 1, the dust discharge valve 34 is opened and the lime dust is captured by the cyclone 33 and collected in the storage tank 1. Exhaust pipe 31
The dust inside is drawn into the wet scrubber 15 by opening the sealing valve 30 and activating the exhaust fan 24. The extraction valve 3 is closed except when the quick lime is cut out, and the stopper 47 is attached to the quick lime receiving pipe 46 except when the quick lime is received, and the sealing valve 30 of the exhaust pipe 31 is closed to keep the storage tank 1 in a closed state. .

【0023】[0023]

【発明の効果】本発明においては、粉粒状の生石灰を水
に供給し溶解させ石灰溶液とする方法において、渦状に
流動する旋回流を形成させ、この旋回流に生石灰を均等
分散させて供給するように構成したので、生石灰は 旋
回流に速やかに巻き込まれて溶解槽に供給される。その
結果、生石灰を水に供給したときに発生する石灰粉塵の
発生を抑制し、粉塵による配管等の閉塞や環境悪化を防
止できる。
According to the present invention, in a method of supplying and dissolving powdery and granular lime into water to form a lime solution, a swirling flow is formed, and the quicklime is uniformly dispersed and supplied to the swirling flow. With such a configuration, quicklime is immediately caught in the swirling flow and supplied to the melting tank. As a result, it is possible to suppress the generation of lime dust generated when quick lime is supplied to water, and to prevent clogging of pipes and the like due to the dust and deterioration of the environment.

【0024】また、溶解槽等で発生した石灰粉塵は、ウ
ェットスクラバーにおいて捕獲し、捕獲によって発生し
た石灰溶液は、生石灰の溶解に使用するように構成した
ので石灰粉塵を効率よく回収できる。さらには、石灰溶
液の温度(濃度)に応じて生石灰の供給量を調整するよ
うに構成したので、石灰溶液の過熱による粉塵の発生を
防止できる。
Further, the lime dust generated in the dissolving tank or the like is captured by a wet scrubber, and the lime solution generated by the capture is used for dissolving quick lime, so that the lime dust can be efficiently recovered. Further, since the supply amount of quicklime is adjusted according to the temperature (concentration) of the lime solution, it is possible to prevent dust from being generated due to overheating of the lime solution.

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

【図1】本発明の実施例に係る生石灰溶解装置の全体図
(フロー図)
FIG. 1 is an overall view (flow diagram) of a quicklime dissolving apparatus according to an embodiment of the present invention.

【図2】図1の部分拡大図(側断面図)FIG. 2 is a partially enlarged view (side sectional view) of FIG.

【図3】図2のX−X線切断の平断面図FIG. 3 is a cross-sectional plan view taken along line XX of FIG. 2;

【符号の説明】[Explanation of symbols]

1;生石灰貯留タンク 2;切出フィーダ
3;切出弁 4;生石灰投入管 5;モータ
6;スクリュー 7;陣笠状部材 8;漏斗状部材
9;液注入管 10;溶解槽 11;溶解槽の蓋
12;撹拌機 13;液面レベル計 14;排気ダクト
15;ウェットスクラバ 16;多孔板 17;ミストセパレータ
18;循環ポンプ 19;洗浄ノズル 20;補給水管
21;補給水弁 22;洗浄ノズル 23;排気ファン
24;排気ダクト 25;循環液貯留タンク 26;液温計
27;液面レベル計 28;弁 29;弁
30;密閉弁 31;排気管 32;排気管
33;サイクロン 34;粉塵排出弁 35;液温計測用タンク
36;セパレータ 37;溶液吸上管 38;ポンプ
39;液温計 40;弁 41;液排出管
42;液排出管 43;溶液貯留槽 44;液面レベル計
45;撹拌機 46;生石灰受入管 47;受入管の口栓
C;生石灰 W;旋回流
1; quicklime storage tank 2; cutting feeder
3; cut-off valve 4; quick lime inlet pipe 5; motor
6; Screw 7; Jin-shape member 8; Funnel-shaped member
9; liquid injection tube 10; dissolution tank 11; lid of dissolution tank
12; agitator 13; liquid level meter 14; exhaust duct
15; wet scrubber 16; perforated plate 17; mist separator
18; circulation pump 19; washing nozzle 20; makeup water pipe
21; makeup water valve 22; washing nozzle 23; exhaust fan
24; exhaust duct 25; circulating fluid storage tank 26; liquid thermometer
27; liquid level meter 28; valve 29; valve
30; sealing valve 31; exhaust pipe 32; exhaust pipe
33; cyclone 34; dust discharge valve 35; tank for measuring liquid temperature
36; separator 37; solution suction pipe 38; pump
39; liquid thermometer 40; valve 41; liquid discharge pipe
42; liquid discharge pipe 43; solution storage tank 44; liquid level meter
45; Stirrer 46; Quicklime receiving pipe 47; Plug of receiving pipe
C: quicklime W: swirling flow

フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 1/66 530 C02F 1/66 530A Continued on the front page (51) Int.Cl. 6 Identification code FI C02F 1/66 530 C02F 1/66 530A

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】粉粒状の生石灰粉を水に供給し溶解させて
石灰溶液とする方法において、渦状に流動する水または
石灰溶液の旋回流を形成させ、該旋回流に前記生石灰を
供給することを特徴とする生石灰溶解方法。
1. A method for supplying and dissolving powdery and granular lime powder in water to form a lime solution, wherein a swirling flow of water or lime solution flowing in a swirl is formed, and the quicklime is supplied to the swirling flow. A quicklime dissolving method characterized by the following.
【請求項2】生石灰投入管(4)から排出され落下する
粉粒状の生石灰を受ける陣笠状部材(7)と、陣笠状部
材(7)を囲むように設けられた漏斗状部材(8)と、
漏斗状部材(8)の接線方向に向けて漏斗状部材(8)
の内側に水または石灰溶液を注入する液注入管(9)と
を有することを特徴とする生石灰溶解装置。
2. A girder-shaped member (7) for receiving powdered granulated lime discharged from a quick-lime charging pipe (4) and a funnel-shaped member (8) provided so as to surround the girder-shaped member (7). ,
Funnel-shaped member (8) tangential to funnel-shaped member (8)
And a liquid injection pipe (9) for injecting water or lime solution into the inside of the device.
JP15927297A 1997-06-03 1997-06-03 Method for dissolving quick line and device therefor Withdrawn JPH10328542A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15927297A JPH10328542A (en) 1997-06-03 1997-06-03 Method for dissolving quick line and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15927297A JPH10328542A (en) 1997-06-03 1997-06-03 Method for dissolving quick line and device therefor

Publications (1)

Publication Number Publication Date
JPH10328542A true JPH10328542A (en) 1998-12-15

Family

ID=15690163

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15927297A Withdrawn JPH10328542A (en) 1997-06-03 1997-06-03 Method for dissolving quick line and device therefor

Country Status (1)

Country Link
JP (1) JPH10328542A (en)

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WO2017191851A1 (en) * 2016-05-06 2017-11-09 株式会社オーノギ Device for generating saturated solution of calcined calcium
JP2017202968A (en) * 2016-05-06 2017-11-16 株式会社オーノギ Calcined calcium saturated solution generating device
JP2019147104A (en) * 2018-02-27 2019-09-05 ニチラク機械株式会社 Revolution type melting method and revolution type melting device
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Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004076042A1 (en) * 2003-02-28 2004-09-10 Okutama Kogyo Co., Ltd. Mixing device and slurrying device
EP1604730A1 (en) * 2003-02-28 2005-12-14 Okutama Kogyo Co., Ltd. Mixing device and slurrying device
US7575364B2 (en) * 2003-02-28 2009-08-18 Okutama Kogyo Co., Ltd. Mixing device and slurrying device
EP1604730A4 (en) * 2003-02-28 2011-10-19 Okutama Kogyo Co Ltd Mixing device and slurrying device
JP2009160576A (en) * 2007-12-14 2009-07-23 Yasumasa Nishiyama Fine air bubble generator
JP2010158680A (en) * 2007-12-14 2010-07-22 Yasumasa Nishiyama Additional device for whirling type fine bubble generation apparatus
JP4636420B2 (en) * 2007-12-14 2011-02-23 康正 西山 Microbubble generator
JP4678617B2 (en) * 2007-12-14 2011-04-27 康正 西山 Additional device for swirling microbubble generator
JP2015157252A (en) * 2014-02-24 2015-09-03 シャープ株式会社 Mixture producing apparatus
JP2016121031A (en) * 2014-12-24 2016-07-07 株式会社トクヤマ Production method and production device of gypsum slurry
JP2016187799A (en) * 2015-03-30 2016-11-04 兵神装備株式会社 Powder blender and powder blending method
WO2017191851A1 (en) * 2016-05-06 2017-11-09 株式会社オーノギ Device for generating saturated solution of calcined calcium
JP2017202968A (en) * 2016-05-06 2017-11-16 株式会社オーノギ Calcined calcium saturated solution generating device
JP2019147104A (en) * 2018-02-27 2019-09-05 ニチラク機械株式会社 Revolution type melting method and revolution type melting device
WO2019167916A1 (en) * 2018-02-27 2019-09-06 ニチラク機械株式会社 Swirling-type dissolution method and swirling-type dissolution device
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