JPH05187772A - Dried material dropping port of multi-stage drying machine positioned apart from gas passage - Google Patents

Dried material dropping port of multi-stage drying machine positioned apart from gas passage

Info

Publication number
JPH05187772A
JPH05187772A JP7024891A JP7024891A JPH05187772A JP H05187772 A JPH05187772 A JP H05187772A JP 7024891 A JP7024891 A JP 7024891A JP 7024891 A JP7024891 A JP 7024891A JP H05187772 A JPH05187772 A JP H05187772A
Authority
JP
Japan
Prior art keywords
dried
rake
scraper
gas
items
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
JP7024891A
Other languages
Japanese (ja)
Inventor
Masakumi Hiroe
正九三 廣江
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP7024891A priority Critical patent/JPH05187772A/en
Publication of JPH05187772A publication Critical patent/JPH05187772A/en
Pending legal-status Critical Current

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  • Drying Of Solid Materials (AREA)

Abstract

PURPOSE:To reduce occurrence of power dusts caused by dropping of dried item by a method wherein a scraper is mounted under utilization of a rotary shaft of a rake to a dried crop dropping port and the dried item is transported and dropped at a part not acting as a passage for thermal medium gas. CONSTITUTION:Some dried items are pushed against a bank 4 with the upper stage rake 1 rotating an arrow direction 13 and piled up there, thereafter they are decayed down after the rake 1 is passed. The decayed down dried items are scraped by a scraper 3 toward an outlet port 6 and pulled toward a dropping port 8. At an inlet port 7, the scraper 3 oppositely pushes back the dried items into the drying surface, i.e., a rotating range of the rake 1. In addition, a shoot 9 may prevent occurrence of powder dusts as the dried items are dropped. In this way, the scraper 3 is mounted at the dropping port 8 for the dried items under utilization of a rotary shaft 10 of the rake 1. Then, the dried items are transported to the part not acting as the passage for the thermal medium gas and dropped there, thereby the occurrence of powder dusts accompanied by the dropping of the dried items is reduced.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、多段乾燥機内部の粉
塵発生を大幅に減少させる事を目的とするものである。
乾燥物と熱媒体ガスが、段と段を移動する通路は通常同
じ口を利用している。又構造上ガスの通過する口の面積
は他の通路に比較して小さくなりがちで、ガスの流速は
早くなり、この流れの中を落下する乾燥物が粉塵となっ
てガス中に混入する量は当然多くなる。この欠点を無く
するため、ガスの通路から乾燥物の落ち口を隔離して粉
塵発生の原因を取り除こうとするものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention aims to significantly reduce dust generation inside a multi-stage dryer.
The passages for the dry matter and the heat carrier gas to move between the steps usually use the same port. Also, the area of the mouth through which gas passes tends to be smaller than other passages due to the structure, the flow velocity of gas becomes faster, and the dry matter falling in this flow becomes dust and mixes in the gas. Will naturally increase. In order to eliminate this defect, it is intended to remove the cause of dust generation by isolating the dry matter outlet from the gas passage.

【0002】[0002]

【従来の技術】熱媒体ガスと直接接触して乾燥物を乾か
す乾燥機は、機種を問わず一般に高温の入り口ガスによ
る乾燥物の変質を防ぐ目的で乾燥物と熱媒体ガスが並行
流となっている場合が多い。高温の燃焼ガスを利用する
乾燥機に於いては殆ど此の方式を取っている。従って、
乾燥機出口に近くなれば乾燥度の進んだ乾燥物が熱媒体
ガスに接触する度合いは益々多くなる。この為、熱媒体
ガスに乾燥物が多量に粉塵として混入する事は、ガスに
乾燥物が直接接触する乾燥機では宿命として見過ごされ
ている。しかし、多軸多段乾燥機(昭和62年実願第6
2−03119)は、平面上で乾燥物を攪拌して乾燥す
る構造で、乾燥面で乾燥物が飛散してガスに混入する粉
塵の量は、ガス流に浮遊して落下する落ち口の発生粉塵
量に比べ遥かに少ない。下水汚泥の例で見ると、乾燥面
で発生する粉塵は殆ど完全に乾燥した部分においても熱
媒体ガス1立方米当たり0.5グラム程度である。一方
乾燥物がガス流の中を落下する落ち口では、1立方米当
たり10グラムを超える量の粉塵が発生する事がある。
発生する粉塵の量は、乾燥物の性状や乾燥の度合いで異
なるが、殆どの場合ガス系に集塵機を使用しないでは運
転出来なかった。特に、ガスを再加熱して循環利用する
システムでは粉塵が系全体に及ぼす影響は大きく、装置
の各機器を汚し連続運転時間を左右する大きな要因とな
っている。
2. Description of the Related Art In general, a dryer for drying a dried product by directly contacting it with a heat carrier gas is a parallel flow of the dried product and the heat carrier gas for the purpose of preventing alteration of the dried product by a high temperature inlet gas. There are many cases. This method is mostly used in the dryer that uses high-temperature combustion gas. Therefore,
The closer to the dryer outlet, the more dry the dried product comes into contact with the heat carrier gas. Therefore, a large amount of dry matter mixed in the heat medium gas as dust is overlooked as a fate in a dryer in which the dry matter is in direct contact with the gas. However, multi-axis multi-stage dryer (Shown in 1987, actual application No. 6
2-03119) has a structure in which a dried product is agitated and dried on a flat surface, and the amount of dust scattered on the drying surface and mixed in gas is generated by a falling port that floats in the gas flow and falls. Much less than the amount of dust. In the example of sewage sludge, the dust generated on the dry surface is about 0.5 g per cubic meter of heat carrier gas even in the almost completely dried portion. On the other hand, at the outlet where the dried product falls in the gas flow, dust of an amount exceeding 10 grams per cubic rice may be generated.
The amount of dust generated varies depending on the properties of the dried product and the degree of drying, but in most cases it could not be operated without using a dust collector in the gas system. In particular, in a system in which gas is reheated and circulated and used, dust has a great influence on the entire system, and each device of the apparatus is contaminated, which is a major factor affecting continuous operation time.

【0003】[0003]

【発明が解決しようとする課題】粉塵が熱媒体ガスに一
旦混入すると集塵機(通常サイクロン形式)でも70〜
80%程度しか除去する事は出来ない。もし、乾燥機で
の発生粉塵がガス1立方米当たり0.5グラム程度に少
なくなれば多くの場合集塵機を必要としなくなるし、集
塵機を付ければ更にガス系が清浄に保たれ、装置の各機
器は汚れることなく長時間の連続運転に耐える。
Once dust is mixed in the heat carrier gas, even a dust collector (usually a cyclone type) has 70 to 70%.
Only about 80% can be removed. If the amount of dust generated in the dryer is reduced to about 0.5 grams per cubic meter of gas, a dust collector will not be necessary in most cases, and if a dust collector is attached, the gas system will be kept clean and each device of the equipment will be kept clean. Withstands long-term continuous operation without becoming dirty.

【0004】[0004]

【課題を解決するための手段】この発明を図面について
説明する。図1は、この発明を採用しようとする多段乾
燥機の落ち口付近の立体図である。(1)は上の段のレ
ーキである。乾燥物は(13)の矢印方向に回転する
(1)のレーキで(4)の堰に押しつけられて盛り上が
り、レーキの通過したあとに崩れ落ちる。これを(3)
のスクレーパが(6)の口にかき寄せて、落ち口(8)
に引っ張っていく。又(7)の口では反対にスクレーパ
が乾燥物を乾燥面即ちレーキの回転圏内に押し戻す。
(9)は乾燥物の落下に伴う粉塵の拡散を防ぐシュート
である。図2は落ち口付近の平面図である。(1)のレ
ーキは矢印(13)の方向(3)のスクレーパは矢印
(11)の方向に互いに干渉しないよう回転する。図3
は、スクレーパ部分の立面図である。(3)のスクレー
パは下の段のレーキ(2)の上に乗り(10)のレーキ
駆動軸でレーキと一緒に回される。図4は、この発明を
適用した乾燥段の立体図である。この例は5個のレーキ
を2列に並べ両方の対角の位置をガス通路としている。
乾燥物はレーキで(4)の堰に押しつけられて盛り上が
り、レーキの回転した後に崩れる。これを(3)のスク
レーパが(6)の落ち口側は運び(8)の口から下の段
に落下する。これは自然落下であるから湿った乾燥物が
ある段には、シュート(9)を取りつけない方が落ち口
が詰まる懸念がない。(9)のシュートは乾燥物が落下
によって粉塵を巻き上げる程度に乾燥した段に取りつけ
る。仮に(9)のシュートが無くても乾燥物はガスの通
路を落下しないから、多少乾燥が進んだ粒子が混入して
いもガスに持ち去られて粉塵となる度合いは少ない。
The present invention will be described with reference to the drawings. FIG. 1 is a three-dimensional view of the vicinity of the outlet of a multi-stage dryer to which the present invention is applied. (1) is the upper rake. The dried product is pressed by the weir of (4) by the rake of (1) which rotates in the direction of the arrow of (13), rises, and collapses after the rake has passed. This (3)
Scraper scrapes up to the mouth of (6) and falls (8)
I will pull it to. At the mouth of (7), on the contrary, the scraper pushes the dried material back to the drying surface, that is, the rake rotating area.
(9) is a chute that prevents dust from diffusing when the dried product falls. FIG. 2 is a plan view near the outlet. The rake of (1) rotates in the direction of arrow (13) and the scrapers of (3) in the direction of arrow (11) so as not to interfere with each other. Figure 3
[Fig. 4] is an elevation view of a scraper portion. The scraper of (3) rides on the lower rake (2) and is rotated with the rake on the rake drive shaft of (10). FIG. 4 is a three-dimensional view of a drying stage to which the present invention is applied. In this example, five rakes are arranged in two rows and both diagonal positions are gas passages.
The dried product is pressed against the weir of (4) by the rake, rises, and collapses after the rake rotates. The scraper of (3) carries the falling side of (6) and drops from the mouth of (8) to the lower stage. Since this is a free fall, there is no concern that the outlet will be clogged if the chute (9) is not attached to the stage where there is a wet dry matter. The chute of (9) is attached to a dry stage where the dried product falls to wind up dust. Even if the chute of (9) is not provided, the dried product does not fall through the gas passage, so that even if particles that have been dried to some extent are mixed, they are hardly carried away by the gas and become dust.

【0005】[0005]

【発明の効果】この発明を適用する多段乾燥機の運転経
験から、熱媒体ガスの粉塵濃度が大きく変動することが
分かっていた。即ち、乾燥物の供給を止めて運転してい
る時は、乾燥機内部の乾燥度が各段共に進んでいるにも
かかわらず、ガスに含まれる粉塵濃度は大幅に減少す
る。反対に乾燥物の供給負荷が増大すると、ガスの粉塵
濃度は増大する。これはガスに含まれる粉塵の大部分が
乾燥物の落下部分で発生していることを示している。実
験は試験機(乾燥面積35平方米・乾燥能力500キロ
グラム/時)で乾燥の進んだ下部の2段(約1/3の面
積)にこの発明を適用した。試験運転では粉塵濃度が、
ガス1立方米当たり0.6〜0.8グラムで適用前の3
〜8グラムを大きく下回った。
From the operational experience of the multi-stage dryer to which the present invention is applied, it has been known that the dust concentration of the heat carrier gas fluctuates greatly. That is, when the operation is performed with the supply of the dry matter stopped, the dust concentration contained in the gas is greatly reduced even though the dryness inside the dryer is advanced at each stage. On the contrary, when the supply load of the dry matter increases, the dust concentration of the gas increases. This indicates that most of the dust contained in the gas is generated in the falling part of the dry matter. In the experiment, the present invention was applied to the lower two stages (about 1/3 of the area) where the drying proceeded with a tester (drying area: 35 square meters, drying capacity: 500 kg / hour). In the test run, the dust concentration was
0.6 to 0.8 grams per cubic meter of gas and 3 before application
Well below 8 grams.

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

【図1】ガス通路(乾燥物落ち口)付近の立体図であ
る。
FIG. 1 is a three-dimensional view near a gas passage (dried material outlet).

【図2】ガス通路付近の平面図である。矢印はレーキ、
スクレーパ、の回転及びガスの流れる方向を示す。
FIG. 2 is a plan view of the vicinity of a gas passage. The arrow is the rake,
The rotation of the scraper and the direction of gas flow are shown.

【図3】スクレーパ取付け部分の立面図である。スクレ
ーパは下の段のレーキの上に乗り、このレーキ軸と同じ
軸で回される。
FIG. 3 is an elevation view of a scraper mounting portion. The scraper rides on the lower rake and is rotated on the same axis as this rake.

【図4】この発明を適用した乾燥段の立体図である。FIG. 4 is a three-dimensional view of a drying stage to which the present invention is applied.

【符号の説明】[Explanation of symbols]

1・はスクレーパと同じ段のレーキ 2・はスクレー
パを乗せた下の段のレーキ 3・はスクレーパ 4
・はガス通路に面して上の段にある乾燥物落下防止の堰
5・はガスの通路 6・は乾燥物の通路で落ち口
側、即ちスクレーパ出口側 7・はスクレーパ入り口
側 8・は乾燥物落ち口 9・は乾燥物の落下口シ
ュート 10・はレーキ駆動軸 11・はスクレー
パの回転方向 12・はガスの流れる方向 13・
はレーキの回転方向
1. ・ Rake on the same level as the scraper 2 ・ Rake on the lower level with the scraper 3 ・ Scraper 4
• is a weir in the upper stage facing the gas passage for preventing dry matter from falling 5 · is a passage for gas 6 · is a passage for dry matter on the outlet side, that is, the scraper outlet side 7 · is the scraper inlet side 8 · Dry matter outlet 9 · Dry matter outlet chute 10 · Rake drive shaft 11 · Scraper rotation direction 12 · Gas flow direction 13 ·
Is the direction of rotation of the rake

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 多軸多段乾燥機(昭和62年実願第62
−031198)に関し、乾燥物が下の段に落下する落
ち口にレーキの回転軸を利用したスクレーパを設置し、
乾燥物を熱媒体ガスの通路でない部分に運び落下ささ
て、乾燥物落下に伴う粉塵の発生を減少させる事を特徴
とする多軸多段燥機の乾燥物落ち口
1. A multi-screw multi-stage dryer (Actual application No. 62 of 1987)
-031198), a scraper using a rake rotating shaft is installed at the outlet where the dried product falls to the lower stage.
A dry matter outlet of a multi-axis multi-stage dryer characterized in that the dried matter is carried to a portion which is not a passage of the heat carrier gas and dropped to reduce the generation of dust when the dried matter falls.
JP7024891A 1991-01-16 1991-01-16 Dried material dropping port of multi-stage drying machine positioned apart from gas passage Pending JPH05187772A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7024891A JPH05187772A (en) 1991-01-16 1991-01-16 Dried material dropping port of multi-stage drying machine positioned apart from gas passage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7024891A JPH05187772A (en) 1991-01-16 1991-01-16 Dried material dropping port of multi-stage drying machine positioned apart from gas passage

Publications (1)

Publication Number Publication Date
JPH05187772A true JPH05187772A (en) 1993-07-27

Family

ID=13426071

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7024891A Pending JPH05187772A (en) 1991-01-16 1991-01-16 Dried material dropping port of multi-stage drying machine positioned apart from gas passage

Country Status (1)

Country Link
JP (1) JPH05187772A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102345972A (en) * 2010-07-29 2012-02-08 绿色科技有限公司 Drying machine
KR101524567B1 (en) * 2015-01-02 2015-06-01 주식회사 한국테크놀로지 Apparatus for Dust-Shelter by Transferring of Falling Coal in System for Drying Coal
WO2016108360A1 (en) * 2015-01-02 2016-07-07 주식회사 한국테크놀로지 Dust reduction apparatus depending on supply of falling coal in coal drying apparatus using reheat steam

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102345972A (en) * 2010-07-29 2012-02-08 绿色科技有限公司 Drying machine
KR101524567B1 (en) * 2015-01-02 2015-06-01 주식회사 한국테크놀로지 Apparatus for Dust-Shelter by Transferring of Falling Coal in System for Drying Coal
WO2016108360A1 (en) * 2015-01-02 2016-07-07 주식회사 한국테크놀로지 Dust reduction apparatus depending on supply of falling coal in coal drying apparatus using reheat steam

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