JPS58139922A - Transport apparatus for dangerous granular powder - Google Patents

Transport apparatus for dangerous granular powder

Info

Publication number
JPS58139922A
JPS58139922A JP57061341A JP6134182A JPS58139922A JP S58139922 A JPS58139922 A JP S58139922A JP 57061341 A JP57061341 A JP 57061341A JP 6134182 A JP6134182 A JP 6134182A JP S58139922 A JPS58139922 A JP S58139922A
Authority
JP
Japan
Prior art keywords
exhaust gas
tank
pulverized coal
granular powder
heater
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
JP57061341A
Other languages
Japanese (ja)
Inventor
Eiji Fujita
永治 藤田
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.)
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 JP57061341A priority Critical patent/JPS58139922A/en
Publication of JPS58139922A publication Critical patent/JPS58139922A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N5/00Exhaust or silencing apparatus combined or associated with devices profiting by exhaust energy
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Air Transport Of Granular Materials (AREA)

Abstract

PURPOSE:To smoothly transport dangerous granular powder such as pulverized coal by utilizing exhaust gas by removing dust, water and the like from exhaust gas from an engine, and then supplying the exhaust gas to a discharge portion of a granular powder storing tank. CONSTITUTION:In transporting dangerous granular powder such as pulverized coal, the pulverized coal is first thrown from a manhole 29 in a tank 2, and a cart V loaded with a tank on its car body 1 is moved to the destination. In case of discharging the pulverized coal from the tank 2, a damp cylinder 3 is expanded to incline the tank 2, and then opening and closing valves 24, 25 are opened, and an opening and closing valve 23 is closed, whereby exhaust gas from an engine 5 of the cart V flows through an exhaust pipe 6, a conduit pipe 7 and a primary air feed pipe 8 in a discharge portion 4 of the tank 2, and the pulverized coal is mixed in the exhaust gas to be discharged to the outside. At this time, the exhaust gas is improved in quality by a water scrubber 10, a cooler 20, a cyclon 30, a heater 31 and so on.

Description

【発明の詳細な説明】 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の輸送装置に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for transporting hazardous powder and granular materials such as pulverized coal using engine exhaust gas.

一般に粉じん爆発においては酸素濃度が低くなれば爆発
圧力や圧力上昇速度は小さくなり、遂には爆発性を失う
ようになる。 また浮遊炭じんの電気スパークによる発
大を防止するための限界酸素濃度は16%以下といわれ
ている。
In general, in a dust explosion, as the oxygen concentration decreases, the explosion pressure and pressure rise rate decrease, and eventually the substance loses its explosive properties. Furthermore, the critical oxygen concentration to prevent floating coal dust from escalating due to electric sparks is said to be 16% or less.

この意味から危険性粉粒体を圧送するには車両のエンジ
ン排気ガスを利用するのが有効である。
In this sense, it is effective to use vehicle engine exhaust gas to forcefully transport hazardous powder and granular materials.

しかしながら排気ガス中には黒鉛などのダストが含有さ
れており、これらのダスFを含有したままの状態で粉粒
体の圧送空気源に利用すると、微粉炭がダストによって
劣化し、品資が低下する恐れがある他、エアスライド用
キャンパスを用いて圧送する場合にはキャンパスが目詰
りを起して使用不能となり、頻繁にキャンパスを交換し
なければならないことになる。
However, the exhaust gas contains dust such as graphite, and if it is used as a compressed air source for granular materials while still containing dust F, the pulverized coal will deteriorate due to the dust, resulting in a decline in quality. In addition, when using an air slide canvas for pressure feeding, the canvas becomes clogged and becomes unusable, requiring frequent replacement of the canvas.

本瘍明は上記の点に鑑みてなされたもので、エンジン排
気ガス中より確実にダストを補集すると同時に、円滑な
圧送作業を行うことを目的とするものである。
The present invention was developed in view of the above points, and the purpose is to reliably collect dust from engine exhaust gas and at the same time perform smooth pumping work.

以下本発明の実施例な図面により説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be explained below with reference to the drawings.

■は粉粒体運搬車で、車体1上に粉粒体収容タンク2が
搭載され、該粉粒体収容タンク2の11都と車体1間に
はダンプシリンダ3が介装されている・ 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N4に連結されている
3 is a powder transport vehicle, in which a powder storage tank 2 is mounted on a vehicle body 1, and a dump cylinder 3 is interposed between the powder storage tank 2 and the vehicle body 1. is a discharge section formed at the lower part of the rear end of the powder storage tank 2, and the discharge section is not particularly provided with a canvas. Reference numeral 5 designates the engine of the powder transport vehicle V. One end of an inlet pipe 7 is connected to the middle of an exhaust pipe 6 of the engine 5, and the other end of the inlet pipe 7 is connected to a primary air supply pipe 8 and a secondary air supply pipe 8. It is connected to the discharge N4 via a supply pipe 9.

10はウォータスクラバーで、導入されたエンジン排気
ガスをウォータタンク11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ができるようになっ
ている。
Reference numeral 10 denotes a water scrubber, which brings the introduced engine exhaust gas into contact with water in the water tank 11 to remove impurities from the exhaust gas.

17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
開閉弁18及びチェック弁19がそれぞれ介装されてい
る。
17 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 an on-off valve 18 and a check valve 19 are interposed in the middle thereof. .

なお20は前記導入管7の途中に介装されたクーラー、
25,24.25.26は開閉弁、27゜28はチェッ
ク弁、29はマンホール、30はサイクロン、31はヒ
ーターである。
Note that 20 is a cooler interposed in the middle of the introduction pipe 7;
25, 24, 25, and 26 are on-off valves, 27 and 28 are check valves, 29 is a manhole, 30 is a cyclone, and 31 is a heater.

塾2図には前記ウォータスクラバー10とヒータタンク
11内にヒーター61としての熱交換器が設置されてお
り、ウォータタンク11内の水温(常時80〜85°C
)を利用したものである。
In the cram school 2, a heat exchanger as a heater 61 is installed in the water scrubber 10 and the heater tank 11, and the water temperature in the water tank 11 (always 80 to 85°C) is installed in the water scrubber 10 and the heater tank 11.
).

従って前記クーラー20、前記サイクロン60及び −
ヒーター61内 へ流入した排気ガス(約40°0)はヒーター61によ
り昇温(約80°O)されて前記吐出部4へ流入する。
Therefore, the cooler 20, the cyclone 60 and -
The exhaust gas that has flowed into the heater 61 (approximately 40° 0) is heated by the heater 61 (approximately 80° 0) and then flows into the discharge portion 4 .

次に本発明の作用について説明すると、まず微粉炭をマ
ンホール29より粉粒体収容タンク2内に投入した後、
目的地まで輸送する。 次に粉粒体収容タンク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、しかる後に開閉
弁24.25を開き、一方間閉弁26を閉してエンジン
5よりの排気ガスを排気管6、導入管7、−次空気供給
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。 この時導入管7の途
中にはウォータスクラバー10、クーラー20、サイク
ロン30及びヒーター61等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により除去される。 そして、排気
ガスはウォータスクラバー10にて降温(550’o−
>80°0)された後、さらにクーラー20により冷却
(80°0→40°a)される結果、微粒ダストを核と
して結露し、サイクロン60にて水分と微粒ダストが除
去される。 その後ヒーター61にて昇温(40°0→
80°O)されるため、クーラー20より流出して自然
空冷によって過飽和状態となっている排気ガス中の水分
はヒーター51にて蒸発される。 したがって、吐出部
4内壁がiVれて微粉炭が付着、凝固し、吐出部4が閉
塞する恐れがない。
Next, to explain the operation of the present invention, first, after putting pulverized coal into the granular material storage tank 2 through the manhole 29,
Transport to destination. Next, when discharging pulverized coal from the granular material storage tank 2, the dump cylinder 6 is extended and the granular material storage tank 2 is tilted, and then the on-off valves 24 and 25 are opened, and the valves are closed for a while. 26 is closed to allow exhaust gas from the engine 5 to flow into the discharge part 4 via the exhaust pipe 6, the introduction pipe 7, and the secondary air supply pipe 8, and the pulverized coal is mixed into the exhaust gas and discharged to the outside. do. At this time, since a water scrubber 10, a cooler 20, a cyclone 30, a heater 61, etc. are sequentially installed in the middle of the introduction pipe 7, the coarse dust contained in the engine exhaust gas is first removed by the water scrubber 10. . Then, the temperature of the exhaust gas is lowered by the water scrubber 10 (550'o-
>80°0), and then further cooled by the cooler 20 (from 80°0 to 40°a), resulting in dew condensation with the fine dust as a nucleus, and the moisture and fine dust are removed by the cyclone 60. After that, the temperature is raised using the heater 61 (40°0 →
80° O), the moisture in the exhaust gas flowing out from the cooler 20 and becoming supersaturated due to natural air cooling is evaporated by the heater 51. Therefore, there is no possibility that the inner wall of the discharge part 4 is exposed to IV and the pulverized coal adheres and solidifies, thereby clogging the discharge part 4.

なお粉粒体収容タンク2内の圧が低下した場合は開閉弁
18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。
Note that when the pressure inside the powder storage tank 2 decreases, the on-off valve 18 is opened to allow exhaust gas to flow into the powder storage tank 2, thereby preventing the tank pressure inside the powder storage tank 2 from decreasing. .

以上説明した様に本発明によれば微粉炭などの危険性粉
粒体の排出時においてエンジン排気ガス中のダストをウ
ォータスクラバーにより除去すると同時にエンジン排気
ガスを降温し、さらにクーラー20にて冷却して、水分
の絶対艦を低下させた後、ヒーターにて昇温させて、排
気ガス中の水分を蒸発させるため、吐出部内壁がメ寧れ
て閉本することがなく、圧送作業を円滑に行うことがで
きる。
As explained above, according to the present invention, when discharging dangerous powder particles such as pulverized coal, the dust in the engine exhaust gas is removed by the water scrubber, the temperature of the engine exhaust gas is lowered at the same time, and the engine exhaust gas is further cooled by the cooler 20. After lowering the absolute moisture content, the temperature is raised with a heater to evaporate the moisture in the exhaust gas, so the inner wall of the discharge part does not become clogged and close, and the pumping work can be carried out smoothly. It can be carried out.

【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411成図、第2図は
本発明のウォータスクラバー及びヒーターの具体的構成
図である。
FIG. 1 is a 411 diagram showing one embodiment of the present invention, and FIG. 2 is a specific configuration diagram of the water scrubber and heater of the present invention.

Claims (2)

【特許請求の範囲】[Claims] (1)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ウォータスクラバー、ク
ーラ及びヒーターを順次介装してなる危険性粉粒体の輸
送装置。
(1) Connect one end of the introduction pipe to the discharge part of the powder storage tank, connect the other end of the introduction pipe to the exhaust pipe from the engine, and install a water scrubber, cooler, and heater in the middle of the introduction pipe. A device for transporting hazardous powder and granular materials that is sequentially interposed.
(2)前記クーラ及びヒーターの間にサイクロンを配設
した番番特許請求の範囲第1項記載の危険性粉粒体の輸
送装置。
(2) The apparatus for transporting hazardous powder and granular materials according to claim 1, wherein a cyclone is disposed between the cooler and the heater.
JP57061341A 1982-04-12 1982-04-12 Transport apparatus for dangerous granular powder Pending JPS58139922A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57061341A JPS58139922A (en) 1982-04-12 1982-04-12 Transport apparatus for dangerous granular powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57061341A JPS58139922A (en) 1982-04-12 1982-04-12 Transport apparatus for dangerous granular powder

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP2167982A Division JPS58139830A (en) 1982-02-12 1982-02-12 Transporting device for dangerous powdered or granular material

Publications (1)

Publication Number Publication Date
JPS58139922A true JPS58139922A (en) 1983-08-19

Family

ID=13168326

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57061341A Pending JPS58139922A (en) 1982-04-12 1982-04-12 Transport apparatus for dangerous granular powder

Country Status (1)

Country Link
JP (1) JPS58139922A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4421427Y1 (en) * 1968-12-28 1969-09-10
JPS4834765A (en) * 1971-09-08 1973-05-22
JPS495314U (en) * 1972-04-18 1974-01-17
JPS49115978A (en) * 1973-03-10 1974-11-06

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4421427Y1 (en) * 1968-12-28 1969-09-10
JPS4834765A (en) * 1971-09-08 1973-05-22
JPS495314U (en) * 1972-04-18 1974-01-17
JPS49115978A (en) * 1973-03-10 1974-11-06

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