JPH04345687A - Indirect heating rotary dryer for powder - Google Patents
Indirect heating rotary dryer for powderInfo
- Publication number
- JPH04345687A JPH04345687A JP11714991A JP11714991A JPH04345687A JP H04345687 A JPH04345687 A JP H04345687A JP 11714991 A JP11714991 A JP 11714991A JP 11714991 A JP11714991 A JP 11714991A JP H04345687 A JPH04345687 A JP H04345687A
- Authority
- JP
- Japan
- Prior art keywords
- heating
- powder
- rotary dryer
- support plates
- stress
- 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
Links
- 238000010438 heat treatment Methods 0.000 title claims abstract description 59
- 239000000843 powder Substances 0.000 title claims abstract description 16
- 238000005452 bending Methods 0.000 claims abstract description 13
- 239000008187 granular material Substances 0.000 claims description 14
- 239000002245 particle Substances 0.000 claims 1
- 238000003466 welding Methods 0.000 abstract description 9
- 230000006835 compression Effects 0.000 abstract description 2
- 238000007906 compression Methods 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 230000008719 thickening Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000003889 chemical engineering Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000003245 coal Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Coke Industry (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、粉粒体の間接加熱式回
転乾燥機に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an indirect heating type rotary dryer for powder and granular materials.
【0002】0002
【従来の技術】一般に、粉粒体の間接乾燥機として、水
蒸気を用いた多管束回転乾燥機が用いられている〔(社
)化学工学協会「化学工学便覧」昭41.05.20,
丸善(株), p.569 ;桐栄良三編「乾燥装置」
昭41.06.25,日刊工業新聞社,p.137 〕
。これらは、図2及び図3に示すように、回転円筒即ち
ドラム10の内側に同心円的に加熱管1を多数配設し、
回転ドラム10を回転させるとき内部の粉粒体14が回
転流動し、そのとき加熱管からの伝熱により粉粒体を乾
燥させるものである。粉粒体14は、図3の供給部11
より入り、排出部12より出てゆく。[Prior Art] Generally, a multi-tube bundle rotary dryer using steam is used as an indirect dryer for powder and granular materials [Chemical Engineering Society of Japan, "Chemical Engineering Handbook", May 20, 1972,
Maruzen Co., Ltd., p. 569 ; “Drying device” edited by Ryozo Kiri
June 25, 1972, Nikkan Kogyo Shimbun, p. 137]
. As shown in FIGS. 2 and 3, a large number of heating tubes 1 are arranged concentrically inside a rotating cylinder or drum 10.
When the rotary drum 10 is rotated, the granular material 14 inside rotates and flows, and at this time, the granular material is dried by heat transfer from the heating tube. The granular material 14 is supplied to the supply section 11 in FIG.
The liquid enters the tank and exits through the discharge section 12.
【0003】また、図3に示すように、加熱管1はその
長手方向を回転円筒の内周にリング状に立設された多数
の支持板13で支えられている。このため、加熱管1は
図2に示す粉粒体6の流動による力Fをうける“連続ば
り”に相当し、その曲げモーメント線図は、おおよそ図
4のようになり、支持板部で最大となる。Further, as shown in FIG. 3, the heating tube 1 is supported in its longitudinal direction by a number of support plates 13 that are erected in a ring shape on the inner periphery of a rotating cylinder. Therefore, the heating tube 1 corresponds to a "continuous burr" that is subjected to the force F due to the flow of the powder material 6 shown in Fig. 2, and its bending moment diagram is approximately as shown in Fig. 4, with the maximum at the support plate part. becomes.
【0004】0004
【発明が解決しようとする課題】従来の間接加熱式回転
乾燥機の加熱管では、特に最も中心側の加熱管1e(図
2に図示)が流動力の直撃をうけ、最大曲げモーメント
(すなわち曲げ応力)の生ずる支持点のところから破損
することがある。この対策として、加熱管1eの断面係
数を増加させる方法、即ち大径化及び又は、厚肉化があ
る。しかし、既設々備で大径化するということは、加熱
管の支持板の穴を大きくすることにつながり、これは施
工上及び支持板の強度上から現実的でない。そこで厚肉
化の方法がとられるわけであるが、一般に加熱管には高
強度で耐摩耗性,耐食性の良い、従って高価格の材料が
使用されるから、全長にわたり均一に厚肉化することは
経済的でない。また全長の厚肉化による重量増は改造時
のハンドリングに不便をきたすばかりでなく、ドラムの
回転負荷も増加させる。[Problems to be Solved by the Invention] In the heating tubes of the conventional indirect heating type rotary dryer, the heating tube 1e (shown in FIG. 2) located closest to the center is directly hit by the flow force, and the maximum bending moment (i.e., bending Failure may occur at the support point where stress is generated. As a countermeasure against this problem, there is a method of increasing the section modulus of the heating tube 1e, that is, increasing the diameter and/or thickening the tube. However, enlarging the diameter of the existing equipment means enlarging the hole in the support plate of the heating tube, which is not practical from the viewpoint of construction and the strength of the support plate. Therefore, the method of increasing the thickness is taken, but since materials with high strength, wear resistance, and corrosion resistance, and therefore high prices, are generally used for heating tubes, it is necessary to increase the thickness uniformly over the entire length. is not economical. Furthermore, the increased weight due to the thicker overall length not only causes inconvenience in handling during modification, but also increases the rotational load on the drum.
【0005】本発明は、以上のもろもろの問題点を一挙
に解決した粉粒体の間接加熱式回転乾燥機を提供するこ
とを目的とするものである。The object of the present invention is to provide an indirect heating type rotary dryer for powder and granular materials, which solves all of the above-mentioned problems at once.
【0006】[0006]
【課題を解決するための手段】本発明は、回転円筒の内
側に同心円的に加熱管を多列に配設し、かつ該加熱管を
該回転円筒の内周にリング状に立設した複数の支持板で
支持した粉粒体の間接加熱式回転乾燥機において、少な
くとも最内周列に配設した加熱管の1ヶ所以上の該支持
板部近傍のみにおいて、その肉厚を厚くしたことを特徴
とする粉粒体の間接加熱式回転乾燥機であり、望ましく
は加熱管の厚肉部とうす肉部とを曲げ応力がほぼ0にな
る位置で溶接したものであり、またさらに望ましくは厚
肉部からうす肉部へと連続的に肉厚が変化するテーパ管
部を溶接部の熱影響部より離したものである。[Means for Solving the Problems] The present invention provides a plurality of heating tubes arranged concentrically in multiple rows inside a rotating cylinder, and a plurality of heating tubes erected in a ring shape on the inner periphery of the rotating cylinder. In an indirect heating rotary dryer for powder and granular materials supported by a support plate, the wall thickness is increased at least in the vicinity of the support plate at one or more locations of the heating tubes arranged in the innermost row. This is an indirect heating type rotary dryer for powder and granular materials, preferably in which the thick and thin parts of the heating tube are welded at a position where the bending stress is approximately 0, and more preferably in the A tapered tube section whose wall thickness changes continuously from a thick section to a thin section is separated from the heat affected zone of the welded section.
【0007】[0007]
【作用】本発明によれば、少なくとも最内周側に位置す
る加熱管の1ヶ所以上の支持板部近傍の加熱管の外径を
変えることなく、他の部分より厚肉化したので、既設の
支持板を何ら改造することなく本発明を適用でき、そし
て粉粒体の流動力による最も大きな曲げモーメントの生
ずる回転ドラム最内周の加熱管に本発明を適用すれば、
支持板による加熱管の支持点での最大曲げ応力を低下さ
せることができ加熱管の寿命を延長できる。[Function] According to the present invention, the outer diameter of the heating tube near one or more support plate portions located at least on the innermost circumferential side is made thicker than other parts without changing the outer diameter of the heating tube. The present invention can be applied without any modification to the support plate of the rotating drum, and if the present invention is applied to the heating tube on the innermost circumference of the rotating drum, where the largest bending moment occurs due to the flow force of the powder or granular material,
The maximum bending stress at the point where the heating tube is supported by the support plate can be reduced, and the life of the heating tube can be extended.
【0008】また加熱管全体を厚肉管で構成する場合と
比べて材料費が安く、かつ回転ドラム重量増による回転
負荷の増加も少なくて済む。また外径が他の加熱管部と
同じで中央部に厚肉部、その両側に厚肉からうす肉へ連
続的に肉厚を変化させた勾配部(テーパ管部)、さらに
その両端にうす肉部を設けた管を、うす肉管と、例えば
計算での曲げ応力が0になる点で溶接することは、既設
の回転乾燥機への本発明の適用が容易に行えるとともに
、溶接部に加わる応力が実質的に小さくでき、溶接部か
らの破損を生ずることもないので望ましい。[0008] Furthermore, the material cost is lower than in the case where the entire heating tube is made of a thick-walled tube, and the increase in rotational load due to the increase in the weight of the rotating drum can be reduced. In addition, the outside diameter is the same as that of other heating tube sections, with a thick wall section in the center, a sloped section (tapered tube section) where the wall thickness changes continuously from thick wall to thin wall on both sides, and thin wall section at both ends. By welding a pipe with a fleshed part to a thin-walled pipe, for example, at a point where the calculated bending stress becomes 0, the present invention can be easily applied to an existing rotary dryer, and the welded part can be welded. This is desirable because the stress applied can be substantially reduced and no damage will occur from the weld.
【0009】またさらに、厚肉からうす肉へ連続的に肉
厚を変化させた勾配部(テーパ管部)を溶接熱影響部よ
り離すことは、テーパ管部における応力集中と溶接の影
響(残留応力等)による破損が防止できるので望ましい
。Furthermore, separating the sloped part (tapered pipe part) where the wall thickness changes continuously from thick to thin from the weld heat affected zone reduces stress concentration in the tapered pipe part and the effect of welding (residual This is desirable because it prevents damage caused by stress, etc.).
【0010】0010
【実施例】本発明の実施例を図面を用いて説明する。図
1(a) は、本発明の一実施例の要部断面図である。
この図において、13は加熱管を支持する支持板である
。この支持板13を中心として両側の合計l1 なる長
さの加熱管部1aをt2 なる肉厚にする。[Embodiment] An embodiment of the present invention will be explained with reference to the drawings. FIG. 1(a) is a sectional view of a main part of an embodiment of the present invention. In this figure, 13 is a support plate that supports the heating tube. The heating tube portion 1a having a total length of l1 on both sides of the supporting plate 13 is made to have a wall thickness of t2.
【0011】長さl1 はあとで述べる長さl5 より
短くし、具体的には、テーパ管部を溶接の熱影響部から
十分離した長さにすることが望ましい。l2 はこう配
部長さである。加熱管のうす肉部1bの肉厚をt1 と
すると、l2 は肉厚の差の3倍以上(l2 ≧3×(
t2 −t1 ))にすることが望ましい。また、図1
(b) は、該加熱管1の長手方向の曲げ応力σの分布
を示す。これより、曲げ応力σが+(引張)から−(圧
縮)に変化する途中で必ず0になる点Aが支持板13の
両側に存在するから、両A点間の長さ(=l5 )で厚
肉管1aを用意し、A点でうす肉管1bと溶接する。[0011] The length l1 is preferably shorter than the length l5, which will be described later, and specifically, it is desirable that the tapered pipe portion be sufficiently separated from the heat-affected zone of welding. l2 is the gradient length. If the thickness of the thin wall portion 1b of the heating tube is t1, then l2 is more than three times the difference in wall thickness (l2 ≧3×(
It is desirable to set it to t2 - t1 )). Also, Figure 1
(b) shows the distribution of bending stress σ in the longitudinal direction of the heating tube 1. From this, since there are points A on both sides of the support plate 13 where the bending stress σ always becomes 0 while changing from + (tension) to - (compression), the length between both points A (=l5) A thick-walled pipe 1a is prepared and welded to a thin-walled pipe 1b at point A.
【0012】図5にうす肉部の肉厚t1 を一定として
、厚肉部の肉厚t2 を種々変えた場合の加熱管下面の
軸方向応力分布σを比較して示した。支持点の軸方向応
力σはt2 を厚肉化することにより低下する。この時
、“応力が0の点”Aはほとんど変わらない。また図5
ではこう配を3×(t2 −t1 )としたが、こう配
部への応力集中もほとんどない。FIG. 5 shows a comparison of the axial stress distribution σ on the lower surface of the heating tube when the thickness t1 of the thin wall portion is constant and the thickness t2 of the thick wall portion is varied. The axial stress σ at the support point is reduced by increasing the thickness of t2. At this time, the "point where stress is 0" A remains almost unchanged. Also, Figure 5
In this case, the gradient was set to 3×(t2 - t1), but there is almost no stress concentration on the gradient part.
【0013】また、本発明の部分厚肉管と全長を厚肉管
にした場合との応力を比較すると図6のようになる。こ
れにより、全体のレベルはもとより最大応力(支持板の
ところ)にも両者の間にほとんど差がないことがわかる
。以上のように本発明では、支持板近くの加熱管部を厚
肉化し、他はうす肉管とし、その溶接点を応力が0とな
る点にもってきたから、溶接点からの破損を防止するこ
とができ、かつ、全体のわずかな重量増で、支持点の応
力を大幅に下げることができる。FIG. 6 shows a comparison of the stress between the partially thick-walled pipe of the present invention and the case where the entire length is made of a thick-walled pipe. This shows that there is almost no difference between the two in terms of the overall level as well as the maximum stress (at the support plate). As described above, in the present invention, the heating tube near the support plate is made thicker, the other parts are made thinner, and the welding point is brought to the point where the stress becomes 0, thereby preventing damage from the welding point. In addition, the stress at the supporting points can be significantly reduced with a slight increase in overall weight.
【0014】因みに、従来の直径 2.8m,長さ21
mの石炭の間接加熱式回転乾燥機において、最も中心側
の加熱管の外径65A,支持板のピッチを 3.0m,
加熱管の肉厚は一様にt1 = 2.5mmとし、一方
本発明実施例の加熱管として、材質は従来と変わらず、
うす肉部の肉厚t1 = 2.5mm,厚肉部の肉厚t
2 = 5.5mm, こう配部長さl2 =20mm
, 厚肉部長さl1 = 800mm,溶接点間長さl
5 = 950mm(計算により求めた値)としたもの
を用い、従来と全く同一条件で運転し、加熱管のひずみ
測定により支持点の応力を比較したところ、従来の48
%の応力値で大幅に応力が低下していることがわかった
。[0014] Incidentally, the conventional diameter is 2.8 m and the length is 21 m.
m indirect heating type rotary dryer for coal, the outer diameter of the heating tube closest to the center is 65A, the pitch of the support plates is 3.0m,
The thickness of the heating tube was uniformly t1 = 2.5 mm, while the material of the heating tube according to the embodiment of the present invention was the same as before.
Thickness of thin part t1 = 2.5mm, thickness of thick part t
2 = 5.5mm, gradient length l2 = 20mm
, thick wall length l1 = 800mm, length between welding points l
5 = 950mm (calculated value), operated under exactly the same conditions as before, and compared the stress at the support point by measuring strain on the heating tube.
It was found that the stress decreased significantly at a stress value of %.
【0015】また、溶接点の応力値は絶対値が0.32
kgf/mm2 であり、この程度の応力値は無視でき
る程度に小さい。本実施例では、図1の長さl1 ,l
2 ,l3 ,l4 ,l5 にそれぞれ上記の値を用
いたが、これらはその乾燥機の形状,寸法,粉粒体の供
給速度、回転ドラムの回転速度等から決定すればよい。
また最内側の加熱管についてのみ適用したが、その他の
位置の加熱管に適用してもよい。厚肉化するところは、
全ての支持板部でも良いし、特に粉粒体の流動が悪く、
たい積しやすい供給側の1ヶ所又は2ヶ所のみでも良い
。[0015] Furthermore, the absolute value of the stress value at the welding point is 0.32.
kgf/mm2, and this stress value is so small that it can be ignored. In this example, the lengths l1 and l in FIG.
The above values were used for 2, l3, l4, and l5, but these may be determined based on the shape and dimensions of the dryer, the supply rate of powder and granular material, the rotation speed of the rotating drum, etc. Further, although the present invention is applied only to the innermost heating tube, it may be applied to heating tubes at other positions. Where the wall becomes thicker,
All the support plate parts may be used, or if the flow of powder or granules is particularly poor,
It may be sufficient to have only one or two locations on the supply side where it is easy to accumulate.
【0016】[0016]
【発明の効果】本発明は加熱管の外径を変えることなく
支持板近くのみを厚肉化しかつ、加熱管の軸方向応力値
が0になるところに溶接点をもってきたから、以下のよ
うな効果を生ずる。
(1) 支持点での応力値を低下させることができ、加
熱管の破損がなくなった。[Effects of the Invention] The present invention thickens only the area near the support plate without changing the outer diameter of the heating tube, and the welding point is placed at a location where the stress value in the axial direction of the heating tube becomes 0. produce an effect. (1) It was possible to reduce the stress value at the support point, eliminating damage to the heating tube.
【0017】(2) 支持板の穴を大きくする必要がな
いため、既設の設備の改造に際し施工や支持板の強度上
の問題がない。
(3) 部分厚肉化のため重量増がわずかである。
(4) 重量増が小であり、全長厚肉に比べ比較的安価
である。
(5) 1本の重量増が小でハンドリングが容易である
。(2) Since there is no need to enlarge the holes in the support plate, there are no problems with construction or strength of the support plate when modifying existing equipment. (3) Weight increase is slight due to thickening of parts. (4) The weight increase is small, and it is relatively inexpensive compared to full-length thick-walled. (5) The weight increase per piece is small and handling is easy.
【0018】(6) 全体の重量増が小で回転ドラムの
回転負荷も小さい。(6) The overall weight increase is small and the rotational load on the rotating drum is small.
【図1】本発明の要部断面図と支持板近傍における加熱
管下面の軸方向応力分布図である。FIG. 1 is a sectional view of a main part of the present invention and an axial stress distribution diagram on the lower surface of a heating tube in the vicinity of a support plate.
【図2】回転ドラム断面図である。FIG. 2 is a sectional view of a rotating drum.
【図3】回転ドラム側面図である。FIG. 3 is a side view of the rotating drum.
【図4】加熱管に作用する曲げモーメント線図である。FIG. 4 is a bending moment diagram acting on the heating tube.
【図5】厚肉管の肉厚を変えた場合の軸方向応力比較図
である。FIG. 5 is a comparison diagram of axial stress when the wall thickness of a thick-walled pipe is changed.
【図6】部分厚肉化と全体厚肉化の場合の軸方向応力比
較図である。FIG. 6 is a comparison diagram of axial stress in the case of partial thickening and overall thickening.
1 加熱管 10 ドラム 11 供給部 12 排出部 13 支持板 14 粉粒体 1 Heating tube 10 Drum 11 Supply section 12 Discharge section 13 Support plate 14 Powder
Claims (3)
多列に配設し、かつ該加熱管を該回転円筒の内周にリン
グ状に立設した複数の支持板で支持した粉粒体の間接加
熱式回転乾燥機において、少なくとも最内周列に配設し
た加熱管の1ヶ所以上の該支持板部近傍のみにおいて、
その肉厚を厚くしたことを特徴とする粉粒体の間接加熱
式回転乾燥機。1. Powder particles in which heating tubes are arranged concentrically in multiple rows inside a rotating cylinder, and the heating tubes are supported by a plurality of support plates standing upright in a ring shape on the inner circumference of the rotating cylinder. In the indirect heating type rotary dryer for the body, only in the vicinity of one or more support plate portions of the heating tubes arranged at least in the innermost circumferential row,
An indirect heating type rotary dryer for powder and granular materials, which is characterized by its thick wall.
力がほぼ0になる位置で溶接したことを特徴とする粉粒
体の間接加熱式回転乾燥機。2. An indirect heating type rotary dryer for powder and granular material, characterized in that the thick walled portion and the thin walled portion of the heating tube are welded at a position where bending stress is approximately zero.
が変化するテーパ管部を溶接部の熱影響部より離したこ
とを特徴とする請求項2記載の粉粒体の間接加熱式回転
乾燥機。3. The joint of powder or granular material according to claim 2, characterized in that the tapered pipe portion whose wall thickness continuously changes from a thick wall portion to a thin wall portion is separated from a heat affected zone of a welded portion. Heated rotary dryer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3117149A JP2519849B2 (en) | 1991-05-22 | 1991-05-22 | Indirect heating rotary dryer for powder and granular material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3117149A JP2519849B2 (en) | 1991-05-22 | 1991-05-22 | Indirect heating rotary dryer for powder and granular material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04345687A true JPH04345687A (en) | 1992-12-01 |
JP2519849B2 JP2519849B2 (en) | 1996-07-31 |
Family
ID=14704678
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3117149A Expired - Lifetime JP2519849B2 (en) | 1991-05-22 | 1991-05-22 | Indirect heating rotary dryer for powder and granular material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2519849B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009243859A (en) * | 2008-03-31 | 2009-10-22 | Mitsui Eng & Shipbuild Co Ltd | Indirect heating pyrolysis device |
WO2015186666A1 (en) * | 2014-03-31 | 2015-12-10 | 月島機械株式会社 | Method for drying material being processed, and horizontal rotary dryer |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58127782A (en) * | 1982-01-26 | 1983-07-29 | Nippon Steel Corp | Rotary drier for fine coal for coke equipped with indirect heating tubes |
-
1991
- 1991-05-22 JP JP3117149A patent/JP2519849B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58127782A (en) * | 1982-01-26 | 1983-07-29 | Nippon Steel Corp | Rotary drier for fine coal for coke equipped with indirect heating tubes |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009243859A (en) * | 2008-03-31 | 2009-10-22 | Mitsui Eng & Shipbuild Co Ltd | Indirect heating pyrolysis device |
WO2015186666A1 (en) * | 2014-03-31 | 2015-12-10 | 月島機械株式会社 | Method for drying material being processed, and horizontal rotary dryer |
US9897376B2 (en) | 2014-03-31 | 2018-02-20 | Tsukishima Kikai Co., Ltd | Drying method for processing material and horizontal rotary dryer |
Also Published As
Publication number | Publication date |
---|---|
JP2519849B2 (en) | 1996-07-31 |
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