JPS62288800A - Dust removing apparatus for natural steam - Google Patents

Dust removing apparatus for natural steam

Info

Publication number
JPS62288800A
JPS62288800A JP12715486A JP12715486A JPS62288800A JP S62288800 A JPS62288800 A JP S62288800A JP 12715486 A JP12715486 A JP 12715486A JP 12715486 A JP12715486 A JP 12715486A JP S62288800 A JPS62288800 A JP S62288800A
Authority
JP
Japan
Prior art keywords
steam
mist
dust
pipe
conduit
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.)
Pending
Application number
JP12715486A
Other languages
Japanese (ja)
Inventor
Kazuo Shiroo
城尾 和男
Yoichiro Yokote
横手 洋一郎
Seiji Nakayama
中山 清司
Makoto Kiyono
清野 良
Keizaburo Tokura
都倉 敬三郎
Tetsuo Tabata
田畑 鉄夫
Masanobu Akiyama
秋山 雅信
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP12715486A priority Critical patent/JPS62288800A/en
Publication of JPS62288800A publication Critical patent/JPS62288800A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To remove the dust with high efficiency by utilizing a condensed steam for producing a mist in a conduit and catching micro particle dust by means of said mist. CONSTITUTION:Natural steam taken from a steam well 1 is cooled through a cooler 3 arranged in the way of a conduit 2 and a portion thereof is condensed into water which is fed with high speed through the conduit together with the steam. When passing through a projection 4 provided in the downstream, said water is fed with a higher speed because the diameter of the conduit 2 is restricted near the projection 4 and dispersed in mist into the conduit. Consequently, the dust contained in the steam is caught onto the surface of the mist drip. Furthermore, the mist is separated from the steam through a mist separator 5 thereby only a clean steam is fed through the conduit 2 to a turbine 6.

Description

【発明の詳細な説明】 3、発明の詳細な説明 〔産業上の利用分野〕 本発明は、天然蒸気形地熱発電プラント等において天然
蒸気中のダストを除去するための装置に関する。
Detailed Description of the Invention 3. Detailed Description of the Invention [Field of Industrial Application] The present invention relates to an apparatus for removing dust from natural steam in a natural steam type geothermal power generation plant or the like.

〔従来の技術〕[Conventional technology]

地熱発電プラントは、地熱井の特性により徨々の形式の
ものが実用化されているが、その中で、地上設備が簡単
で低コストの発電を行なうことができる方式として、地
下の天然蒸気を利用する方式がよく知られている。
Many types of geothermal power generation plants have been put into practical use depending on the characteristics of geothermal wells, but among them, underground natural steam is used as a method that uses simple above-ground equipment and can generate power at low cost. The method used is well known.

この天然蒸気形地熱発電プラントは、地下の蒸気井から
取出す高温・高圧の天然蒸気そのものを発電用蒸気とし
て用いるものであるが、地下から噴出する蒸気中には土
砂、シリカ、硫化物等の微粒ダストが多量に含まれてお
り、この微粒ダストはタービン羽根やシュラウド面等に
スケーリングを生じさせタービン出力低下の原因となる
ため、このような天然蒸気をそのまま直接タービンに送
り込むことはできない。
This natural steam type geothermal power generation plant uses high-temperature, high-pressure natural steam extracted from an underground steam well as the steam for power generation. Such natural steam cannot be directly fed into the turbine as it is because it contains a large amount of dust, and this fine dust causes scaling on the surfaces of turbine blades and shrouds, causing a reduction in turbine output.

このため従来では、第4図に示すように、蒸気井(7)
から取出される蒸気を蒸気管路(8)を介してサイクロ
ンセパレータや慣性力セパレータ等の乾式のセパレータ
(9)に送り込んで蒸気に含有されているダストを分離
し除去し、しかる後タービンαOへ送り込むという方法
を採っていた。
For this reason, conventionally, as shown in Figure 4, the steam well (7)
The steam taken out from the steam pipe (8) is sent to a dry separator (9) such as a cyclone separator or an inertia separator to separate and remove dust contained in the steam, and then to the turbine αO. The method was to send them in.

しかし、このような乾式セパレータでは、捕集可能なダ
ストの粒子径が、遠心力を利用するサイクロンセパレー
タで20〜30μ以上、慣性力を利用する慣性力セパレ
ータでも10μ以上であり、捕集効率も60〜70憾糧
度と低い。したがって、このような乾式セパレータを通
過した蒸気中には依然大量の微粒ダストが残存し、これ
らがタービンのスケーリングを発生させ、タービン出力
を低下させる原因となる。このようなダストの影響によ
る出力低下は、成る発電所では約104/月にも及んで
いる。
However, with such dry separators, the particle size of the dust that can be collected is 20 to 30 μ or more for a cyclone separator that uses centrifugal force, and 10 μ or more for an inertial force separator that uses inertial force, and the collection efficiency is also low. Low level of 60-70. Therefore, a large amount of fine dust still remains in the steam that has passed through such a dry separator, which causes scaling of the turbine and reduces the turbine output. The reduction in output due to the influence of dust extends to about 104 times per month at the power plants.

このような乾式セパレータに対し、数μ〜数10μの微
粒ダストを適切に除去することができる方式として湿式
スクラバ一方式が知られており、この方式を天然蒸気の
集塵に適用することが考えられる。この方式はダストを
含む流体中に水を流入し、この水に微粒ダストを捕集さ
せ、ダストを水とともに流体から分離除去するもので、
95繋以上の捕集効率が期待できる。
In contrast to such a dry separator, a one-type wet scrubber is known as a method that can appropriately remove fine dust from several microns to several tens of microns, and it is considered that this method can be applied to dust collection from natural steam. It will be done. In this method, water flows into a fluid containing dust, the water collects fine dust, and the dust is separated and removed from the fluid along with the water.
A collection efficiency of 95 or more can be expected.

〔発明が解決しようとする問題〕[Problem that the invention seeks to solve]

しかし、この湿式スクラバーを天然蒸気形地熱発電プラ
ントに適用した場合、注入水(こ溶存している酸素によ
り設備の腐食が急速に進行するという大きな問題がある
However, when this wet scrubber is applied to a natural steam type geothermal power generation plant, there is a major problem in that the equipment is rapidly corroded by the dissolved oxygen in the injected water.

すなわち、加熱流体中に酸素の混入があつ。That is, oxygen may be mixed into the heated fluid.

た場合、多くの地熱プラントで報告されているように、
炭素鋼で構成された管路設備においては酸素混入がない
場合に較べて全面腐食が10倍以上も加速さね7、設備
の寿命を極端に縮めることになる。これは注入水に溶存
している酸素が天然蒸気に含まれている硫化水ぶを酸化
して硫黄や硫酸を生じさせ、これらが配管等の内面を洗
う結果、表面を4覆している硫化第1鉄が洗落され、腐
食が8行することによるものである。また酸素混入は局
部的な電池形成により部分腐食を引き起こす原因ともな
り、また管がステンレス鋼である場合には、酸素と塩素
イオンとの反応により生じる塩酸等により孔食の原因と
もなる。
As has been reported in many geothermal plants,
In pipe equipment made of carbon steel, general corrosion accelerates more than ten times as much as in the case where there is no oxygen contamination7, resulting in an extremely shortened service life of the equipment. This is because the oxygen dissolved in the injected water oxidizes the sulfide water contained in the natural steam to produce sulfur and sulfuric acid, which wash the inside surfaces of pipes, etc. This is due to the fact that 1 iron is washed away and 8 lines of corrosion occur. In addition, oxygen contamination can cause partial corrosion due to local battery formation, and if the tube is made of stainless steel, it can also cause pitting corrosion due to hydrochloric acid generated by the reaction between oxygen and chlorine ions.

したがって、湿式スクラバーを地熱発電プラントに適用
しようとした場合、注入水に溶存する酸素を除去する必
要があるが、このためには付帯設備として高性能の脱気
器が必要となり、却って設備を大型化・複雑化させてし
まう。
Therefore, when trying to apply a wet scrubber to a geothermal power plant, it is necessary to remove oxygen dissolved in the injected water, but this requires a high-performance deaerator as ancillary equipment, which would actually require large equipment. It makes things complicated and complex.

本発明は以上述べたような従来の問題点に鑑みなされた
ものであり、湿式スクラバーのような管路設備の腐食と
いう問題を生じさせることなく、簡単な設備で蒸・気中
の微粒ダストを効率的に除去することができる装置の提
供をその目的とする。
The present invention was developed in view of the conventional problems described above, and it is possible to remove fine dust from steam and air using simple equipment without causing the problem of corrosion of pipe equipment such as wet scrubbers. The purpose is to provide a device that can remove the waste efficiently.

〔問題を解決するための手段〕[Means to solve the problem]

このため本発明の装置は、蒸気管路の途中に管内を流れ
る蒸気の一部を1疑縮させるための冷却部を設け、その
下流の管内部に、パα伍を狭め蒸気の流速を高めること
により凝縮水をミストとして分散させるための突起部を
設け、さらにその下流の蒸気管路に蒸気とダストを捕集
したミストとを分離するためのミストセパレータを設け
たことをその特徴とする。
For this reason, the device of the present invention is provided with a cooling section in the middle of the steam pipe line for condensing a part of the steam flowing inside the pipe, and inside the pipe downstream thereof, narrows the gap and increases the flow velocity of the steam. The feature is that a protrusion is provided to disperse the condensed water as mist, and a mist separator is further provided in the steam pipe downstream of the protrusion to separate the steam and the mist that collects dust.

〔作 用〕[For production]

蒸気井等から取出される天然蒸気は蒸気管路の途中に設
けらねた冷却部において冷却され、一部が凝縮して水と
なる。この凝縮水は蒸気により大きな流速で管内を搬送
さね1、冷却部下流側に設けられている突起部により更
に流速を増大され、これにより管内にミスト状1こ分散
する。蒸気中のダストはこのミストの欣滴表面で捕集さ
れる。そして、このダストを含むミストは下流側に設け
られているミストセパレータで蒸気から分離除去され、
この結果、79浄な蒸気のみがタービンlこ供給される
Natural steam taken out from a steam well or the like is cooled in a cooling section installed in the middle of a steam pipe, and a portion of it condenses to become water. This condensed water is conveyed through the tube at a high flow rate by the steam, and the flow rate is further increased by a protrusion provided downstream of the cooling section, thereby dispersing it in the form of a mist inside the tube. Dust in the steam is collected on the surface of the droplets of this mist. The mist containing this dust is then separated and removed from the steam by a mist separator installed on the downstream side.
As a result, only 79 clean steam is supplied to the turbine.

〔実施例〕〔Example〕

以下、本考案の一実施例を第1図ないし第3図に基づき
説明する。
An embodiment of the present invention will be described below with reference to FIGS. 1 to 3.

図において、(1)は蒸気井、(6)はタービン、(2
)はこの蒸気井から取出した天然蒸気をタービン(6)
に供、@するための管路である。
In the figure, (1) is a steam well, (6) is a turbine, and (2) is a steam well.
) is the turbine (6) that uses the natural steam extracted from this steam well.
It is a conduit for serving and @.

前記管路(2)の途中には冷却器(3)が設けられてい
る。該冷却器(3)は管路(2)内の蒸気を冷却し、そ
の一部を凝縮させるためのもので、冷却水等の冷却用流
体により管路(2)内の蒸気を冷却する構造となってい
る。なお、本実施例では冷却部として冷却器を利用して
いるが、蒸気を自然放熱させ寥気を凝縮させる構造とす
ることもできる。すなわち、一般に管路(2)は蒸気の
高温性を維持するために配管に保温材等を巻付けて保温
されているが、生産井蒸気産出量に余裕がある場合は、
W路(2)のある区間に亘って該保温材等を取外して、
この部分を冷却部として構成し、管路(21からの放熱
を促すことによって凝縮水を得るようにすることもでき
る。
A cooler (3) is provided in the middle of the pipe (2). The cooler (3) is for cooling the steam in the pipe (2) and condensing a part of it, and has a structure in which the steam in the pipe (2) is cooled by cooling fluid such as cooling water. It becomes. Although a cooler is used as the cooling unit in this embodiment, a structure may also be used in which steam naturally radiates heat and the residual air is condensed. In other words, the pipe (2) is generally kept warm by wrapping a heat insulating material around the pipe to maintain the high temperature of the steam, but if there is sufficient steam output from the production well,
Remove the heat insulation material, etc. over a certain section of W road (2),
It is also possible to construct this part as a cooling part and obtain condensed water by promoting heat radiation from the pipe (21).

前記冷却器の下流の管内面には突起部(4)が設けられ
ている。該突起部(4)は、管径を狭め蒸気の流速を高
めることにより、蒸気中の凝縮水を管内でミスト状(A
)に分散させるためのもので、本実施例では管内周に沿
って設けられた環状の板状体lこより構成されている。
A protrusion (4) is provided on the inner surface of the tube downstream of the cooler. The protrusion (4) narrows the pipe diameter and increases the flow rate of steam, thereby converting condensed water in the steam into a mist (A) inside the pipe.
), and in this embodiment, it is composed of an annular plate-shaped body provided along the inner periphery of the tube.

この板状体は蒸気の流れを円滑にするため管路下流方向
に一定の傾斜ルもって設けられてい−る。
This plate-shaped body is provided with a certain slope in the downstream direction of the pipe in order to smooth the flow of steam.

前記突起部(4)の更に下流側の管路(2)にはミスト
セパレータ(5)が設けられている。該ミストセパレー
タ(5)はダストを捕集したミストを蒸気から分離除去
するためのものである。このミストセパレータとしては
、例えば従来知られているような邪魔板にミストを衝突
させドレンとして蒸気から分離除去する構造のもの等、
適宜な構造のものを用いることができる。
A mist separator (5) is provided in the conduit (2) further downstream of the projection (4). The mist separator (5) is for separating and removing the mist that has collected dust from the steam. Examples of this mist separator include a structure that collides mist with a conventionally known baffle plate and separates it from steam as a drain.
A material having an appropriate structure can be used.

次に、本実施列の作用を説明すると、蒸気井(1)から
取出された天然蒸気は管路(2)途中の冷却器(3)に
より冷却され、その一部が凝縮して水となり、蒸気とと
もに高流速で管内を送られる。この凝、縮水は前記冷却
器(3)の下流に設けられた突起部(4)を通過する際
、この部分の管内1が狭められているため流速が更に高
められ、管内でミスト状に分散する。このような凝縮水
のミスト化により、蒸気に含まれているダストはミスト
の液滴表面で捕集される。そしてこのようJこダストを
4甫集したミストはミストセパレータ(5)において蒸
気から分離除去され、清浄な蒸気のみが管路(2)を介
してタービン(6)に供給される。なお、前記冷却器(
3)で回収する蒸気の熱量は多目的利用施設の熱源とし
て利用することにより、エネルギーの唸金利用率の向上
が図られる。
Next, to explain the operation of this embodiment, the natural steam taken out from the steam well (1) is cooled by the cooler (3) in the middle of the pipe (2), and a part of it condenses and becomes water. It is sent through the pipe at a high flow rate along with steam. When this condensed water passes through the protrusion (4) provided downstream of the cooler (3), the flow rate is further increased because the pipe 1 in this part is narrowed, and it is dispersed in the form of a mist within the pipe. do. By turning the condensed water into a mist, dust contained in the steam is collected on the surface of the mist droplets. Then, the mist that has collected four pieces of dust is separated and removed from the steam in the mist separator (5), and only clean steam is supplied to the turbine (6) via the pipe (2). Note that the cooler (
By using the heat of the steam recovered in step 3) as a heat source for multi-purpose facilities, the energy utilization rate can be improved.

以上のような本発明の寝覚では、蒸気中のダストはミス
トの液滴表面で捕集され、ミストセパレータでの分離効
率が上昇するため、乾き度99.994 以上の清浄な
蒸気を得ることができる。
In the device of the present invention as described above, the dust in the steam is collected on the surface of the mist droplets, and the separation efficiency at the mist separator increases, so that clean steam with a dryness level of 99.994 or higher can be obtained. Can be done.

また、本発明では、冷却部による冷却により蒸気の保有
エネルギーが低下せしめられるとともに、蒸気の一部を
凝縮してミスト形成用の水を得る際に蒸気量が減少させ
られるため、タービンにおいて利用可能な蒸気の保有エ
ネルギーが減少することとなるが、ミストセパレータに
おいて分離されるミストの量に見合うだけの蒸気を増産
することによってタービンの定格蒸気量は確保すること
ができる。
In addition, in the present invention, the energy retained in the steam is reduced by cooling by the cooling section, and the amount of steam is reduced when a part of the steam is condensed to obtain water for mist formation, so that it can be used in a turbine. Although the retained energy of the steam will decrease, the rated steam amount of the turbine can be secured by increasing the steam production to match the amount of mist separated by the mist separator.

〔発明の効果〕〔Effect of the invention〕

以上述べた本発明によれば、外部から水を注入すること
なく、蒸気の凝縮水を利用して管路内でミストを生じさ
せ、このミストにより蒸気中の微粒ダストを適切に捕集
することができ、このため従来の湿式スクラバーのよう
な注入水の溶存酸素による管路設備の腐食という問題を
生じさせることなく、しかも高い捕集効率で蒸気中の微
粒ダストを除去することができ、このためダストJこよ
るスケーリングの発生を抑え、タービンを長期間安定し
て運転することが可能となる。
According to the present invention described above, a mist is generated in a pipe by using condensed water of steam without injecting water from the outside, and fine dust in the steam can be appropriately collected by this mist. As a result, it is possible to remove fine dust from steam with high collection efficiency without causing the problem of corrosion of pipe equipment due to dissolved oxygen in the injected water, which is the case with conventional wet scrubbers. Therefore, it is possible to suppress the occurrence of scaling caused by dust J, and to operate the turbine stably for a long period of time.

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

第1図ないし第3図は本発明の一実施例を示すもので、
第1図は全体説明図、第2図は突起部配役部の縦断面図
、第3図は同じく横断面図である。第4図は従来の天然
蒸気形地熱発電プラントにおける乾式ダスト除去装置の
全体説明図である。 図において、(2)は蒸気管路、(3)は冷却器、(4
)は突起部、(5ンはミストセパレータを各示す。
1 to 3 show an embodiment of the present invention,
FIG. 1 is an overall explanatory diagram, FIG. 2 is a longitudinal cross-sectional view of the protruding part, and FIG. 3 is a cross-sectional view. FIG. 4 is an overall explanatory diagram of a dry dust removal device in a conventional natural steam type geothermal power generation plant. In the figure, (2) is the steam pipe, (3) is the cooler, and (4
) indicates a protrusion, and (5) indicates a mist separator.

Claims (1)

【特許請求の範囲】 蒸気管路の途中に管内を流れる蒸気の一 部を凝縮させるための冷却部を設け、その 下流の管内部に、管径を狭め蒸気の流速を 高めることにより凝縮水をミストとして分 散させるための突起部を設け、さらにその 下流の蒸気管路に蒸気とダストを捕集した ミストとを分離するためのミストセパレー タを設けてなる天然蒸気のダスト除去装置。[Claims] A portion of steam flowing through a steam pipe A cooling section is provided to condense the Inside the downstream pipe, the pipe diameter is narrowed to reduce the steam flow rate. By raising the temperature, condensed water is separated as mist. Protrusions are provided for dispersion, and Steam and dust were collected in the downstream steam line. Mist separator to separate from mist A natural steam dust removal device equipped with a
JP12715486A 1986-06-03 1986-06-03 Dust removing apparatus for natural steam Pending JPS62288800A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12715486A JPS62288800A (en) 1986-06-03 1986-06-03 Dust removing apparatus for natural steam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12715486A JPS62288800A (en) 1986-06-03 1986-06-03 Dust removing apparatus for natural steam

Publications (1)

Publication Number Publication Date
JPS62288800A true JPS62288800A (en) 1987-12-15

Family

ID=14952965

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12715486A Pending JPS62288800A (en) 1986-06-03 1986-06-03 Dust removing apparatus for natural steam

Country Status (1)

Country Link
JP (1) JPS62288800A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5223875A (en) * 1990-09-06 1993-06-29 Canon Kabushiki Kaisha Automatic tracking camera system

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5910301A (en) * 1982-07-07 1984-01-19 Toshiba Corp Remover of scale from terrestrial heat steam

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5910301A (en) * 1982-07-07 1984-01-19 Toshiba Corp Remover of scale from terrestrial heat steam

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5223875A (en) * 1990-09-06 1993-06-29 Canon Kabushiki Kaisha Automatic tracking camera system

Similar Documents

Publication Publication Date Title
RU2290446C2 (en) Method of recuperation of energy from hot gas
JP2012162716A (en) Energy recovery in syngas applications
KR101609815B1 (en) Biomass syngas purification process under negative pressure for producing oil and system configuration thereof
US4344920A (en) Air pollution control system
JP4664093B2 (en) Heat recovery device and chlorine bypass facility
JPH0661414B2 (en) Steam turbine equipment
KR20150060723A (en) Method for recovering process wastewater from a steam power plant
JPS62288800A (en) Dust removing apparatus for natural steam
JP5213126B2 (en) Chlorine bypass system
US4930316A (en) Geothermal plant noncondensable gas removal and heat recovery system and method
CN101402882A (en) Purification apparatus and method for biomass gas
US3739549A (en) Rhenium extraction process
JP2008209106A (en) Gravitational settling bed for removal of particulate impurities in nuclear steam generator
JP2777061B2 (en) Device for preventing erosion damage of steam turbine blades by solid particles
CN110559779A (en) dry processing system for roasting flue gas by rare earth concentrate concentrated sulfuric acid method
CN206965404U (en) A kind of high-efficient wet-type cleaning dust device
US4548162A (en) Slagging heat recovery unit with potassium seed recovery
US3212856A (en) Apparatus for collecting fume from recovery unit gases
CN214300018U (en) System for retrieve phenol oil in blue charcoal production
CN104745237B (en) A kind of process for being pyrolyzed high-temperature oil gas dedusting oil recovery
CN104667682B (en) A kind of high-temperature forming machine treating apparatus for exhaust gas of oil smoke and technique
CN110559778A (en) Dry-wet combined treatment system for roasting flue gas by rare earth concentrate concentrated sulfuric acid method
CN217154212U (en) Coal-electricity production waste gas purification treatment device with waste heat recycling function
CN215480760U (en) High-temperature gas purification and recovery equipment
CN210261642U (en) Four-phase separation device for biomass carbonization