JPS60191844A - Washing device in carrier vehicle for dangerous granular material - Google Patents

Washing device in carrier vehicle for dangerous granular material

Info

Publication number
JPS60191844A
JPS60191844A JP4837784A JP4837784A JPS60191844A JP S60191844 A JPS60191844 A JP S60191844A JP 4837784 A JP4837784 A JP 4837784A JP 4837784 A JP4837784 A JP 4837784A JP S60191844 A JPS60191844 A JP S60191844A
Authority
JP
Japan
Prior art keywords
water
exhaust gas
switching valve
tank
cooler
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.)
Granted
Application number
JP4837784A
Other languages
Japanese (ja)
Other versions
JPH0329601B2 (en
Inventor
Eiji Fujita
永治 藤田
Koichi Mizuta
水田 引一
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.)
Shinmaywa Industries Ltd
Original Assignee
Shin Meiva Industry 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 Shin Meiva Industry Ltd filed Critical Shin Meiva Industry Ltd
Priority to JP4837784A priority Critical patent/JPS60191844A/en
Publication of JPS60191844A publication Critical patent/JPS60191844A/en
Publication of JPH0329601B2 publication Critical patent/JPH0329601B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Cyclones (AREA)
  • Cleaning In General (AREA)
  • Air Transport Of Granular Materials (AREA)

Abstract

PURPOSE:To facilitate washing for a purifying device for a cooler, by providng a selector valve in the intermediate part of an introduction pipe communicating between a water tank in a water scrubber and the purifying device, and as well by enabling eithr one of exhaust gas and high temperature water to be selectively fed to the downstream side of the selector valve. CONSTITUTION:When pulverized coal is discharged from a pulverized coal storage tank 2, exhaust gas from an engine 5 is introduced from an introduction pipe 7 into a discharge section 4 through a primary air supply pipe 8 by way of an water scrubber 10, a cooler 13, a cyclone 14 and a heater 15 after tank 2 is tilted by means of a dump cylinder 3 and therefore, pulverized coal is mixed into exhaust gas and then is discharged to the outside. If accumulation of carbon, oil mist, etc. is progressed in a purifying device during the above-mentioned discharging step and the washing of the purifying device is required, high temperature water in a water tank 12 in the water scrubber 10 is introduced from a pipe line 30 with the use of the pressure of exhaust gas so that the high temperature water flows through the cooler 13, the cyclone 14 and the heater 15 in the mentioned order to dissolve adhered substances, and then the water and the substances are discharged through a selector valve 21.

Description

【発明の詳細な説明】 (利用分野) この発明は微粉炭などの危険性粉粒体をエンジン排気ガ
スを利用して圧送する危険性粉粒体運搬車の洗浄装置に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Application) The present invention relates to a cleaning device for a hazardous powder transport vehicle that uses engine exhaust gas to pump hazardous powder and granular materials such as pulverized coal.

(従来技術) 従来、粉じん爆発をさけるためエンジンの排気ガスを利
用して危険性粉粒体の圧送作業を行う運搬車が知られて
いる。 その際、排気カスr−PK含有する黒鉛などの
ダストはウォータスクラバーで取り除くようにしている
か、ウォータスクラバーに捕集されないカーボンやオイ
ルミストがタープやヒータ等の装置内に付着し排出性能
を低下させることになる。 これを除くため定期的に清
掃を行っているが、その都度装置を分解しなければなら
ないなど清掃に多大な労力を必要とする欠点かあった。
(Prior Art) Conventionally, transport vehicles have been known that use engine exhaust gas to pump hazardous powder and granular materials in order to avoid dust explosions. At that time, dust such as graphite containing exhaust residue r-PK should be removed with a water scrubber, or carbon and oil mist that is not collected by the water scrubber may adhere to the inside of equipment such as tarps and heaters, reducing exhaust performance. It turns out. Although cleaning is carried out regularly to eliminate this problem, the device has to be disassembled each time, which has the drawback of requiring a great deal of effort for cleaning.

(目 的) 本発明はか−る問題を解決するためのもので、旧ヒ &
 J/ +t 署h ル 凍ム 喪is rtt y 
帥 I÷ イー Jり1 偏 イh Iハ 1− 、シ
 − 協 ρ七により、簡単に浄化装置内に付着してい
るカーボンやオイルミスト等を洗浄できる危険性粉粒体
運搬車の洗浄装置を提供するものである。
(Purpose) The present invention is intended to solve the above problems, and
J/ +t sign h le freeze mourning is rtt y
A cleaning device for dangerous powder and granular material carriers that can easily clean carbon, oil mist, etc. adhering to the inside of the purification device using the following formula: It provides:

(構 成) ウォータスクラバーのウォータタンクからクーラなどの
浄化装置に通じる導入管の途中に、切換弁を設け、その
下流側に排気ガスもしくはウォータタンクよりの高温水
を選択的に供給可能VC!成したものである。
(Configuration) A switching valve is installed in the middle of the introduction pipe leading from the water tank of the water scrubber to a purification device such as a cooler, and exhaust gas or high temperature water from the water tank can be selectively supplied to the downstream side of the VC! It was completed.

(実施例) 以下本尭明の実施例を図面により説明する。(Example) Examples of the present invention will be described below with reference to the drawings.

■は粉粒体運搬車で、車体1上にはマンホールを有する
粉粒体収容タンク2が搭載され、該粉粒体収容タンク2
の前部と車体1間にはダンプシリンダ6が介装されてい
る。
2 is a powder/granular material transport vehicle, and a powder/granular material storage tank 2 having a manhole is mounted on the vehicle body 1.
A dump cylinder 6 is interposed between the front part of the vehicle and the vehicle body 1.

4は前記粉粒体収容タンク2の後端下部に形成された吐
出部であって、該吐出部には特にキャンパスは設けられ
ていない。 5は前記粉粒体運搬車Vのエンジンで、こ
のエンジン5の排気管6の途中には、後述する排気ガス
洗浄装置10が介装された導入管7の一端が連結され、
この導入管7の他端は一次空気供給管8及び二次空気供
給管9を介して前記吐出部4に連結されている。
Reference numeral 4 denotes a discharge section formed at the lower rear end of the powder storage tank 2, and no campus is provided in the discharge section. Reference numeral 5 designates the engine of the powder transport vehicle V, and an exhaust pipe 6 of the engine 5 is connected to one end of an introduction pipe 7 in which an exhaust gas cleaning device 10, which will be described later, is interposed.
The other end of the introduction pipe 7 is connected to the discharge section 4 via a primary air supply pipe 8 and a secondary air supply pipe 9.

そして、前記供給管8,9の途中には切換弁19.20
とチェ、り弁22,23が介装されている。
In the middle of the supply pipes 8 and 9, there are switching valves 19 and 20.
In addition, valves 22 and 23 are interposed.

24は背圧空気供給管で、一端を前記導入管7に、他端
を粉粒体収容タンク2の上部に連結され、その途中゛に
は切換弁25及びチェック弁26かそれぞれ介装されて
いる。
24 is a back pressure air supply pipe, one end of which is connected to the introduction pipe 7, the other end of which is connected to the upper part of the powder storage tank 2, and a switching valve 25 and a check valve 26 are interposed between the pipes. There is.

前記排気ガス浄化装置10はウオータスクラノく−11
,クーラ16.サイクレン14.ヒータ15を順に接続
してなり、ウォータスクラバー11は、導入されたエン
ジン排気ガスをウォータタンク12内の水に接触させて
、その排気ガス中の不純物を取り除くことができるよう
になっている他、ウォータタンク12内にはヒータ15
としての熱交換器が設置されている。
The exhaust gas purification device 10 is a water purification device 11.
, Cooler 16. Cyclen 14. The water scrubber 11 is configured by connecting the heaters 15 in sequence, and the water scrubber 11 is capable of removing impurities in the exhaust gas by bringing the introduced engine exhaust gas into contact with the water in the water tank 12. A heater 15 is installed in the water tank 12.
A heat exchanger is installed.

28は粉粒体収容タンク2に排気ガスを供給する圧送位
置と、前記浄化装置10を洗浄する洗浄位tiltとに
選択可能な切換弁で、該切換弁28が圧送位置にあると
き、ウォータタンク12上部より排気ガスを配管27.
29を通してクーラ16に1また洗浄位16にあるとき
、ウォータタンク12底部より高温水を配管30.29
を通してクーラ16にそれぞれ導くようになっている。
Reference numeral 28 denotes a switching valve that can be selected between a pressure feeding position for supplying exhaust gas to the powder storage tank 2 and a cleaning position tilt for cleaning the purification device 10. When the switching valve 28 is in the pressure feeding position, the water tank 12 Exhaust gas is piped from the top 27.
29 to the cooler 16, and when it is in the cleaning position 16, high temperature water is piped from the bottom of the water tank 12 through piping 30.29.
They are each guided to the cooler 16 through them.

続されている他、導入tZ先部にも切換弁21が介装さ
れている。
In addition, a switching valve 21 is also interposed at the tip of the introduction tZ.

(動作の説明) 次に本発明の作用について説明すると、粉粒体収容タン
ク2より微粉炭を排出する場合においては、ダンプシリ
ンダ6を伸長して、粉粒体収容タンク2を傾倒し、しか
る後に切換弁19,20を開き、一方切換弁21を閉じ
てエンジン5よりの排気ガスを排気管6.導入管7.−
次柴気供給管8を介して吐出部4内へ流入させ、微粉炭
を排気ガス内に混入させて外部に排出する。 この時導
l縛7ハカ山W I→mtし松若1n すかh東台譬−
タスクラバー10.クーラ16.サイクロン14及びヒ
ータ15が順次介装されているため、まずエンジン排気
ガス中に含まれる粗粒ダストはウォータスクラバー10
により除失される。 そして、排気ガスはウォータスク
ラバー10にて降温された後、さらにクーラ13により
冷却される結果、微粒ダストを核として結露し、サイク
ロン14にて水分と微粒ダストが除失される。 その後
ヒータ15にて昇温されるため、クーラ16より流出し
て自然突冷によって過飽和状態となっている排気ガス中
の水分はヒータ15にて蒸発される。
(Explanation of operation) Next, to explain the operation of the present invention, when discharging pulverized coal from the granular material storage tank 2, the dump cylinder 6 is extended, the granular material storage tank 2 is tilted, and the pulverized coal is Afterwards, the switching valves 19 and 20 are opened, while the switching valve 21 is closed to direct the exhaust gas from the engine 5 to the exhaust pipe 6. Introductory tube7. −
Next, the pulverized coal is caused to flow into the discharge part 4 through the air supply pipe 8, and the pulverized coal is mixed into the exhaust gas and discharged to the outside. At this time, the guide 7 Hakayama W I→mt Matsuwaka 1n Sukah Todai Parable-
Task Lover 10. Cooler 16. Since the cyclone 14 and the heater 15 are installed in sequence, the coarse dust contained in the engine exhaust gas is first removed by the water scrubber 10.
It is deleted by. Then, the temperature of the exhaust gas is lowered by the water scrubber 10 and then further cooled by the cooler 13, resulting in dew condensation with the fine dust as a core, and the moisture and the fine dust are removed by the cyclone 14. Thereafter, the temperature is raised by the heater 15, so that the moisture in the exhaust gas that has flowed out from the cooler 16 and has become supersaturated due to natural sudden cooling is evaporated by the heater 15.

なお、粉粒体数名タンク2内の圧か低下した場合は切換
弁25を開いて排気ガスを粉粒体収容タンク2内へ流入
させ、粉粒体収容タンク2内のタンク圧の低下を防止で
きる。
In addition, if the pressure inside the powder/granular material tank 2 drops, the switching valve 25 is opened to allow exhaust gas to flow into the powder/granular material storage tank 2 to prevent the tank pressure in the powder/granular material storage tank 2 from decreasing. It can be prevented.

このように、繰り返し圧送作業を行っているうちに、ウ
ォータスクラバー11やサイクロン14で捕集できなか
ったカーボンやオイルミストか前記浄化装vt、10内
に除々に堆積する。
As described above, while the pressure-feeding operation is repeated, carbon and oil mist that cannot be collected by the water scrubber 11 or the cyclone 14 gradually accumulates in the purification device vt, 10.

この結果、浄化装置10内を洗浄する必要かある場合は
、まず切換弁21を[開」にし、それから切換弁19,
21.]、25および17.18を「閉」にする。 次
に切換弁28を洗浄側に切換えた後、エンジン5を始動
させればよい。 その結果、排気ガスが前記ウォータス
クラバー11のウォータタンク12内に吐出され、その
吐出圧によりウォータタンク12内の高温水が、配管6
υ。
As a result, if it is necessary to clean the inside of the purification device 10, first open the switching valve 21, then open the switching valve 19,
21. ], 25 and 17.18 are "closed". Next, after switching the switching valve 28 to the cleaning side, the engine 5 may be started. As a result, the exhaust gas is discharged into the water tank 12 of the water scrubber 11, and the discharge pressure causes the high temperature water in the water tank 12 to flow into the pipe 6.
υ.

切換弁2B、配営ン9を介して、前記クーラ16゜サイ
クロン14.ヒータ15の浄化装置10内に流れ、付着
しているカーボンやオイルミスト等のダストを溶解して
切換弁21から排出される。
The cooler 16° cyclone 14. It flows into the purification device 10 of the heater 15, dissolves adhering dust such as carbon and oil mist, and is discharged from the switching valve 21.

ウォータタンク12の1%温水が全て切換弁21から放
出されたら、エンジン5を停止させ、切換弁17.18
を「開」にしてウォータスクラバー11及びサイクロン
14の残水を抜くことにより洗浄作業は終了する。
When all of the 1% hot water in the water tank 12 is discharged from the switching valve 21, the engine 5 is stopped and the switching valves 17 and 18 are released.
The cleaning work is completed by opening the water scrubber 11 and draining the remaining water from the cyclone 14.

(効 果) 以上のように本開明によれば、浄化装置に切換弁と配管
を追加し、前記切換弁を洗浄位置に切換えるだけの簡単
な操作で浄化装置uを洗浄することが可能となり、浄化
装置をいちいち分解する必要かない。
(Effects) As described above, according to the present invention, it becomes possible to clean the purification device u with a simple operation of adding a switching valve and piping to the purification device and switching the switching valve to the cleaning position. There is no need to disassemble the purification device one by one.

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

第1図は本発明の一実施例を示す構成図である。 2・・・・粉粒体収容タンク、4・・・・吐出部、5・
・・・エンジン、6・・・・排気管、7・・・・導入管
、11・・・・ウォータスクラバー、16・・・・クー
ラ、15・・・・ヒータ、28・・・・切換弁。 」願人 新明和工業株式会社
FIG. 1 is a block diagram showing an embodiment of the present invention. 2... Powder storage tank, 4... Discharge section, 5...
... Engine, 6 ... Exhaust pipe, 7 ... Inlet pipe, 11 ... Water scrubber, 16 ... Cooler, 15 ... Heater, 28 ... Switching valve . ” Applicant ShinMaywa Industries Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 粉粒体収容タンクの吐出部に導入管の一端を連結し、該
導入管の他端をエンジンからの排気管に連結するととも
に、前記導入管の途中に少なくともウォータスクラバー
及びヒータを有する排気ガス浄化装・置を介装してなる
危険性粉粒体の運搬車において、前記ウォータスクラバ
ーの下流側に、粉粒体収容タンクに排気ガスを供給する
圧送位置と、前記浄化装置を洗浄する洗浄位置とに選択
可能な切換弁を配設し、該切換弁か圧送位置にあるとき
、前記ウォータスクラバーのウォータタンク上部に配設
した配管を介して排気ガスを下流側に圧送せしめ、また
前記切換弁か洗浄位置にあるとき、切換弁からウォータ
タンクの底部へ配設した配管を介してウォータタンク内
の高温水を下流側へ導くように構成した危険性粉粒体運
搬車の洗浄
An exhaust gas purification system in which one end of an introduction pipe is connected to a discharge part of a powder storage tank, the other end of the introduction pipe is connected to an exhaust pipe from an engine, and at least a water scrubber and a heater are provided in the middle of the introduction pipe. In a vehicle for transporting hazardous powder and granular materials, which is equipped with equipment, downstream of the water scrubber, there is a pressure feeding position for supplying exhaust gas to the powder storage tank, and a cleaning position for cleaning the purification device. A selectable switching valve is disposed in the switching valve, and when the switching valve is in a pressure-feeding position, the exhaust gas is forced downstream through a pipe provided at the upper part of the water tank of the water scrubber, and the switching valve Cleaning of hazardous powder and granular material carriers configured to guide high-temperature water in the water tank downstream from the switching valve through piping installed at the bottom of the water tank when the vehicle is in the cleaning position.
JP4837784A 1984-03-13 1984-03-13 Washing device in carrier vehicle for dangerous granular material Granted JPS60191844A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4837784A JPS60191844A (en) 1984-03-13 1984-03-13 Washing device in carrier vehicle for dangerous granular material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4837784A JPS60191844A (en) 1984-03-13 1984-03-13 Washing device in carrier vehicle for dangerous granular material

Publications (2)

Publication Number Publication Date
JPS60191844A true JPS60191844A (en) 1985-09-30
JPH0329601B2 JPH0329601B2 (en) 1991-04-24

Family

ID=12801629

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4837784A Granted JPS60191844A (en) 1984-03-13 1984-03-13 Washing device in carrier vehicle for dangerous granular material

Country Status (1)

Country Link
JP (1) JPS60191844A (en)

Also Published As

Publication number Publication date
JPH0329601B2 (en) 1991-04-24

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