JP2019184220A - Treated material drying method and drying apparatus - Google Patents

Treated material drying method and drying apparatus Download PDF

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JP2019184220A
JP2019184220A JP2018128457A JP2018128457A JP2019184220A JP 2019184220 A JP2019184220 A JP 2019184220A JP 2018128457 A JP2018128457 A JP 2018128457A JP 2018128457 A JP2018128457 A JP 2018128457A JP 2019184220 A JP2019184220 A JP 2019184220A
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drying
processed
stirring
jacket
stirring blades
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JP7022021B2 (en
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洋 宮永
Hiroshi Miyanaga
洋 宮永
弘晃 岡本
Hiroaki Okamoto
弘晃 岡本
聖也 片又
Seiya Katamata
聖也 片又
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Pan Pacific Copper Co Ltd
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Abstract

To provide a method of drying a treated material and an apparatus for drying the same which allows a sludge treated material which contains copper or the like and has high moisture content and large bulk density.SOLUTION: A treated material inserted into a jacket 2 has moisture content of 30 - 70 mass %, cupper appearance quality of 5 - 50 mas %, and bulk density of .2 to 2.0 and is in a sludge state. The treated material is input into the jacket 2 at an input speed less than or equal to 1/3 of the rating, and is subjected to semi-drying until the treated material in the process of dry processing is hidden in height by an upper portion of a stirring blade 4to 4. After the semi-dried treated material is stored in the jacket 2 until the stirring blades 4to 4are hidden by the treated material, the treated material is input at an input speed of 80 - 100% of a rating input speed for drying. Thus, the treated material having the above properties can be dried in a desired state.SELECTED DRAWING: Figure 1

Description

本発明は、被処理物の乾燥方法及び乾燥装置に関し、さらに詳しくは、銅等を含有し、水分含有率が高く、嵩比重が大きいスラッジ状の被処理物であっても確実に乾燥することが可能な被処理物の乾燥方法及び乾燥装置に関する。   More specifically, the present invention relates to a drying method and a drying apparatus for a workpiece, and more specifically, a sludge-like workpiece that contains copper or the like, has a high moisture content, and has a large bulk specific gravity. The present invention relates to a drying method and a drying apparatus for an object to be processed.

下水汚泥、し尿汚泥、活性汚泥等は、水分が多く資源化や処分に際して問題となるため、乾燥を施して減量および資源化を図っている。また、森林保全のために間伐された間伐採(=林地残材)等は、そのままでは水分が多くバイオマス燃料等に利用することができないことから、木質チップ(木材チップ)とした後、乾燥が施される。このような汚泥や木質チップの乾燥には、例えば、バンド乾燥機、バンド流動乾燥機、箱型乾燥機、タコロータリー乾燥機、ウェッジ型スタイルドライヤー(「撹拌翼付乾燥機」ともいう。)等の乾燥機が用いられている。   Since sewage sludge, human waste sludge, activated sludge, etc. have a large amount of water and become a problem in resource recycling and disposal, they are dried to reduce and recycle resources. In addition, thinned trees (= forest residual materials) that have been thinned for forest conservation have a high water content and cannot be used as biomass fuel. Applied. For drying such sludge and wood chips, for example, a band dryer, a band fluidized dryer, a box-type dryer, an octopus rotary dryer, a wedge-type dryer (also referred to as a “dryer with a stirring blade”), and the like. The dryer is used.

各種の乾燥機のうち、ウェッジ型スタイルドライヤーは、複数のクサビ型の回転羽根であるウェッジ型撹拌翼(以下、単に「撹拌翼」という。)を備えており、この撹拌翼の内部に蒸気、温水、オイル等の熱媒体を供給すると共に、乾燥機本体のジャケット内にも蒸気、温水、オイル等の熱媒体を供給することにより乾燥を行う伝導伝熱型の乾燥機(伝導伝熱型乾燥装置)であり、処理物は回転羽根とジャケットからの熱伝導によって乾燥が行われる。このウェッジ型スタイルドライヤーは、1:熱効率が良く伝熱係数が高い、2:伝熱面積が大きいので設置面積が小さくて済む、3:風量が少ないために臭気ガスが少ない、4:連続処理が可能、5:撹拌効率が高く付着物が少ない、6:ランニングコストが低い、などの特徴を備えている。尚、伝導伝熱型乾燥装置に関しては、例えば、特許文献1,2がある。   Among various types of dryers, the wedge-type dryer has a wedge-type stirring blade (hereinafter simply referred to as “stirring blade”) that is a plurality of wedge-shaped rotary blades. Conductive heat transfer type dryer (conductive heat transfer type drying) that supplies heat medium such as hot water and oil and also supplies heat medium such as steam, hot water, and oil into the jacket of the dryer body. The processed product is dried by heat conduction from the rotating blades and the jacket. This wedge style dryer has 1: high thermal efficiency and high heat transfer coefficient, 2: large heat transfer area, small installation area, 3: low odor gas due to low air volume, 4: continuous processing Possible: 5: High stirring efficiency and few deposits, 6: Low running cost. In addition, there exists patent document 1, 2 regarding a conductive heat-transfer type drying apparatus, for example.

特許文献1に示す伝導伝熱型乾燥装置は、被処理物(樹脂を溶剤で溶かしたペースト状、ジェル状、液状等にしたもの)から溶剤と固形樹脂を回収する際の被処理物の乾燥を対象とし、一方、特許文献2に示す伝導伝熱型乾燥装置は、上下水汚泥のような粘着性の有る湿潤物質、その他粉体、粒体等の特に粘着性高い物質等を粉砕及び撹拌をしながら上述した熱媒体や触媒等を熱源として乾燥を行うものである。   The conductive heat transfer type drying apparatus shown in Patent Document 1 dries the object to be processed when the solvent and the solid resin are recovered from the object to be processed (a paste, gel, liquid or the like obtained by dissolving the resin with a solvent). On the other hand, the conductive heat transfer type drying apparatus shown in Patent Document 2 grinds and stirs wet materials with adhesive properties such as water and sewage sludge, and other particularly highly adhesive materials such as powders and granules. The drying is performed using the above-described heat medium or catalyst as a heat source.

特開2013−170754号公報JP 2013-170754 A 特開2014−9876号公報JP 2014-9876 A

本発明者らは、特許文献2に示すような伝導伝熱型乾燥装置を用いて銅等を含有し、水分含有率が高く、嵩比重が大きいスラッジ状の被処理物の乾燥を試みたが、期待したような結果は得られなかった。発明者らの検証によれば、上記スラッジ状の被処理物を投入して乾燥を開始すると撹拌翼に鋳付きが発生すると共に、鋳付きによって撹拌翼から被処理物への熱伝導が阻害されて乾燥速度が低下するという問題が生じた。また、乾燥速度が低下すると高水分(水分率30〜50%程度)の半乾燥品がジャケット内に増え、その結果、撹拌翼を駆動するモータに過負荷が生じるという問題が生じることも判明した。このような問題は、被処理物が汚泥、木質チップ、製紙スラッジ等ではなく、金属を含むスラッジ状の被処理物の特有の性状に影響するものであると推察される。したがって、特許文献1に示すような伝導伝熱型乾燥装置を用いた場合であっても本発明者が望む上記のようなスラッジ状の被処理物の乾燥は困難であると推察される。また、被処理物の粒子径が小さい(例えば、1〜100μm)場合には、乾燥後に飛散したり、落鉱が極めて多くなって搬送不良が生じるおそれがあるという問題があった。   The present inventors tried to dry a sludge-like object to be treated containing copper or the like, having a high moisture content and a large bulk specific gravity using a conductive heat transfer type drying apparatus as shown in Patent Document 2. The expected result was not obtained. According to the inventors' verification, when the sludge-like object to be treated is introduced and drying is started, casting occurs in the stirring blade, and the heat conduction from the stirring blade to the object is inhibited by casting. As a result, there was a problem that the drying rate was lowered. It was also found that when the drying speed decreases, semi-dried products with high moisture (water content of about 30 to 50%) increase in the jacket, resulting in a problem of overloading the motor that drives the stirring blades. . Such a problem is presumed that the object to be treated affects not the sludge, the woody chip, the papermaking sludge, or the like but the characteristic property of the sludge-like object to be treated containing metal. Therefore, even when a conductive heat transfer type drying apparatus as shown in Patent Document 1 is used, it is presumed that it is difficult to dry the sludge-like workpiece as described above, which the present inventor desires. Moreover, when the particle diameter of the to-be-processed object is small (for example, 1-100 micrometers), there existed a problem that it might be scattered after drying or there might be a lot of falling rocks and a conveyance defect might arise.

そこで、本発明は、かかる問題点に鑑みなされたもので、金属、例えば銅等を含有し、水分含有率が高く、また嵩比重が大きいスラッジ状の被処理物を効率的に、且つ、長期間安定的に乾燥することが可能な被処理物の乾燥方法及び乾燥装置を提供することを目的とする。   Therefore, the present invention has been made in view of such a problem, and efficiently and longly treats a sludge-like workpiece containing a metal such as copper, having a high moisture content and a large bulk specific gravity. It is an object of the present invention to provide a drying method and drying apparatus for a workpiece that can be stably dried for a period of time.

上記課題を解決するため請求項1に記載の本発明は、互いに平行に配置された少なくとも2本の回転軸を互いに反対方向へ回転可能に配置し、前記回転軸には所定の間隔を有して撹拌翼をそれぞれ複数配置すると共に、一方側の回転軸に取り付けられた撹拌翼と他方側に取り付けられた撹拌翼が交互に位置するように配置され、ジャケット及び前記撹拌翼に加熱された熱媒体を供給することにより被処理物を加熱乾燥する撹拌式乾燥装置によるスラッジ状の被処理物の乾燥方法において、スラッジ状の被処理物を定格の1/3以下の投入速度で前記撹拌式乾燥装置に投入し、前記撹拌式乾燥装置内で乾燥中の前記被処理物の高さ位置が前記撹拌翼の回転中心から上端までの長さの80%以上が隠れる高さとなるまで半乾燥を行う半乾燥工程と、前記半乾燥状態の前記被処理物が、前記撹拌翼が隠れる高さまで当該撹拌乾燥装置内に貯えられたら、前記被処理物を定格の80〜100%の投入速度で投入して乾燥を行う乾燥工程とを含み構成されたことを特徴とする。   In order to solve the above problems, the present invention according to claim 1 is arranged such that at least two rotating shafts arranged in parallel to each other are arranged to be rotatable in opposite directions to each other, and the rotating shaft has a predetermined interval. A plurality of stirring blades are arranged, and the stirring blades attached to the rotating shaft on one side and the stirring blades attached to the other side are alternately arranged, and the jacket and the heat heated by the stirring blades are arranged. In a method for drying a sludge-like object to be processed by a stirring-type drying device that heats and drys the object to be processed by supplying a medium, the agitation-type drying of the sludge-like object to be processed is performed at a rate of 1/3 or less of the rated speed. It puts into the apparatus and performs semi-drying until the height position of the object being dried in the stirring-type drying apparatus is such that 80% or more of the length from the rotation center to the upper end of the stirring blade is hidden. With semi-drying process When the workpiece in the semi-dried state is stored in the stirring and drying apparatus to a height at which the stirring blade is hidden, drying is performed by feeding the workpiece at a rate of 80 to 100% of the rated speed. And a process.

上記課題を解決するため請求項2に記載の本発明は、請求項1に記載の被処理物の乾燥方法において、前記被処理物の定格の投入速度が、3.0〜5.0wt/hであることを特徴とする。   In order to solve the above-mentioned problem, the present invention according to claim 2 is the method for drying an object to be processed according to claim 1, wherein the rated input speed of the object to be processed is 3.0 to 5.0 wt / h. It is characterized by being.

上記課題を解決するため請求項3に記載の本発明は、請求項1又は2に記載の被処理物の乾燥方法において、前記乾燥工程での乾燥は、内部に0.5〜0.6MPaの蒸気を導入することによって加熱された前記撹拌翼を15〜30rpmで回転させて行うことを特徴とする。   In order to solve the above problems, the present invention according to claim 3 is the method for drying an object to be processed according to claim 1 or 2, wherein the drying in the drying step is performed at 0.5 to 0.6 MPa inside. The stirring blade heated by introducing steam is rotated at 15 to 30 rpm.

上記課題を解決するため請求項4に記載の本発明は、請求項1から3のいずれか1項に記載の被処理物の乾燥方法において、前記撹拌式乾燥装置の内部に加熱エアを導入すると共に、当該撹拌式乾燥装置から排気される排ガスを集塵装置へ送る導管の少なくとも前記集塵装置の手前及び/又は前記集塵装置をスチームトレースによって保温することにより前記導管内部及び前記集塵装置の内部が露点温度以下とならないようにすることを特徴とする。   In order to solve the above-mentioned problem, the present invention described in claim 4 is the method for drying an object to be processed according to any one of claims 1 to 3, wherein heated air is introduced into the stirring-type drying apparatus. In addition, the inside of the conduit and the dust collector are kept warm by steam tracing at least before the dust collector and / or the dust collector that sends exhaust gas exhausted from the stirring-type drying device to the dust collector. It is characterized in that the inside of the inside does not fall below the dew point temperature.

上記課題を解決するため請求項5に記載の本発明は、請求項1から4のいずれか1項に記載の被処理物の乾燥方法において、乾燥が終了した前記被処理物を密閉系のコンベアによって搬送することを特徴とする。   In order to solve the above-mentioned problem, the present invention according to claim 5 is the method for drying an object to be processed according to any one of claims 1 to 4, wherein the object to be processed after the drying is closed in a closed conveyor. It is characterized by being conveyed by.

上記課題を解決するため請求項6に記載の本発明は、請求項1から5のいずれか1項に記載の被処理物の乾燥方法において、前記被処理物は、水分含量が30〜70質量%、銅品位が5〜50質量%、嵩比重1.2〜2.0であることを特徴とする。   In order to solve the above-mentioned problem, the present invention according to claim 6 is the method for drying an object to be processed according to any one of claims 1 to 5, wherein the object to be processed has a water content of 30 to 70 mass. %, The copper grade is 5 to 50% by mass, and the bulk specific gravity is 1.2 to 2.0.

上記課題を解決するため請求項7に記載の本発明は、請求項1から6のいずれか1項に記載の被処理物の乾燥方法において、前記被処理物の前記半乾燥工程では、当該被処理物の水分含量が20質量%以上、30質量%未満となるように半乾燥を行うことを特徴とする。   In order to solve the above-mentioned problem, the present invention described in claim 7 is the method for drying an object to be processed according to any one of claims 1 to 6, wherein in the semi-drying step of the object to be processed, the object to be processed is dried. Semi-drying is performed so that the moisture content of the processed product is 20% by mass or more and less than 30% by mass.

上記課題を解決するため請求項8に記載の本発明は、請求項1から7のいずれか1項に記載の被処理物の乾燥方法において、前記被処理物の粒子径が1〜100μmである場合には、前記乾燥工程では、当該被処理物の水分含量が15質量%以上、20質量%未満となるように乾燥を行うことを特徴とする。   In order to solve the above problems, the present invention according to claim 8 is the method for drying an object to be processed according to any one of claims 1 to 7, wherein the particle diameter of the object to be processed is 1 to 100 μm. In the case, in the drying step, drying is performed so that the moisture content of the object to be processed is 15% by mass or more and less than 20% by mass.

上記課題を解決するため請求項9に記載の本発明は、互いに平行に配置された少なくとも2本の回転軸を互いに反対方向へ回転可能に配置し、前記回転軸には所定の間隔を有して撹拌翼をそれぞれ複数配置すると共に、一方側の回転軸に取り付けられた撹拌翼と他方側に取り付けられた撹拌翼が交互に位置するように配置され、ジャケット及び前記撹拌翼に加熱された熱媒体を供給することにより被処理物を加熱乾燥する撹拌式乾燥装置において、前記ジャケットに配置された堰板の上端を前記撹拌翼の回転中心から上端までの長さの80%以上の高さとなるように形成されると共に、乾燥後の前記被処理物を前記堰板からオーバーフローさせることにより排出可能に構成されたことを特徴とする。   In order to solve the above problem, the present invention according to claim 9 is arranged such that at least two rotating shafts arranged in parallel to each other are rotatably arranged in opposite directions, and the rotating shafts have a predetermined interval. A plurality of stirring blades are arranged, and the stirring blades attached to the rotating shaft on one side and the stirring blades attached to the other side are alternately arranged, and the jacket and the heat heated by the stirring blades are arranged. In the stirring-type drying apparatus that heats and drys an object to be processed by supplying a medium, the upper end of the weir plate arranged in the jacket has a height of 80% or more of the length from the rotation center to the upper end of the stirring blade. In addition, it is characterized in that it can be discharged by overflowing the object to be processed after drying from the weir plate.

上記課題を解決するため請求項10に記載の本発明は、請求項9に記載の撹拌式乾燥装置において、前記撹拌装置の内部に加熱エアを導入する加熱エア供給手段と、前記撹拌装置から排気される排ガスを集塵装置へ送る導管と、前記集塵装置の内部の温度が露点温度以下にならないように前記導管の少なくとも前記集塵装置の手前及び/又は前記集塵装置に設けられたスチームトレースとを備えていることを特徴とする。   In order to solve the above-mentioned problem, the present invention described in claim 10 is the stirring-type drying apparatus according to claim 9, wherein a heating air supply means for introducing heated air into the stirring apparatus, and an exhaust from the stirring apparatus. A conduit for sending the exhaust gas to the dust collector, and steam provided at least before the dust collector and / or in the dust collector so that the temperature inside the dust collector does not fall below the dew point temperature And a trace.

上記課題を解決するため請求項11に記載の本発明は、請求項9又は10に記載の被処理物の乾燥装置において、乾燥が終了した前記被処理物を搬送する搬送手段が密閉式であることを特徴とする。   In order to solve the above-mentioned problem, the present invention according to claim 11 is the drying apparatus for the object to be processed according to claim 9 or 10, wherein the conveying means for conveying the object to be processed after drying is hermetically sealed. It is characterized by that.

本発明に係る被処理物の乾燥方法によれば、水分含量が30〜70質量%、銅品位が5〜50質量%、嵩比重1.2〜2.0であるスラッジ状の被処理物を定格の投入速度の1/3以下の投入速度で半乾燥を行った後、定格の投入速度の80〜100%の投入速度で投入して乾燥を行うこととしたので、乾燥装置(ジャケット)内が空の状態から乾燥を開始する段階、及びその後の定格運転の段階に至る間において、撹拌翼への鋳付きが防止されると共に駆動機構の過負荷の発生を防止することができるという効果がある。   According to the method for drying an object to be processed according to the present invention, a sludge-like object to be processed having a water content of 30 to 70% by mass, a copper quality of 5 to 50% by mass, and a bulk specific gravity of 1.2 to 2.0. After semi-drying at a feed rate of 1/3 or less of the rated feed rate, it was decided to feed and dry at a feed rate of 80-100% of the rated feed rate. During the stage of starting drying from the empty state and the subsequent stage of rated operation, it is possible to prevent the stirrer blade from sticking and to prevent the drive mechanism from being overloaded. is there.

また、本発明に係る被処理物の乾燥装置によれば、堰板の上端を少なくとも撹拌翼の回転中心から上端までの長さの80%以上より高い位置に設けることとしたので、撹拌翼への鋳付きが防止され全ての撹拌翼によって乾燥及び撹拌・解砕を効率的に行うことができるという効果があると共に、駆動機構の過負荷を防止することができるという効果がある。   Further, according to the apparatus for drying an object to be processed according to the present invention, since the upper end of the weir plate is provided at a position higher than at least 80% of the length from the rotation center to the upper end of the stirring blade, This has the effect of preventing the casting from being prevented and drying and stirring and crushing can be efficiently performed by all the stirring blades, and can prevent the drive mechanism from being overloaded.

また、本発明に係る被処理物の乾燥方法及び乾燥装置によれば、集塵装置の内部が露点温度以下とならないように撹拌式乾燥装置の内部に加熱エアを導入すると共に、排ガスを集塵装置へ送る導管の少なくとも集塵装置の手前及び/又は集塵装置をスチームトレースによって保温することとしたので集塵装置の濾布の水濡れによって操業が不可能となるのを防止することができるという効果がある。   Moreover, according to the drying method and drying apparatus of the to-be-processed object which concerns on this invention, while introducing heated air into the inside of a stirring type drying device so that the inside of a dust collector may not become below a dew point temperature, it collects exhaust gas. It is possible to prevent the operation from being impossible due to the wetness of the filter cloth of the dust collector because the dust collector is kept warm by steam tracing at least before the dust collector of the conduit to the device. There is an effect.

本発明に係る被処理物の乾燥装置の一実施形態における内部構成を示す平面断面図である。It is a plane sectional view showing an internal configuration in one embodiment of a drying apparatus of a processed object concerning the present invention. 図1に示す乾燥装置のB−B断面図である。It is BB sectional drawing of the drying apparatus shown in FIG. 撹拌翼の側面図である。It is a side view of a stirring blade. 図1に示すA部の詳細を示す拡大図である。It is an enlarged view which shows the detail of the A section shown in FIG. 各撹拌翼の取り付け角度を示す説明図である。It is explanatory drawing which shows the attachment angle of each stirring blade. 入口側から5枚目までの各撹拌翼の取付角度を示す説明図である。It is explanatory drawing which shows the attachment angle of each stirring blade from an entrance side to the 5th sheet. 本発明に係る被処理物の乾燥方法の一実施形態を示すフローチャートである。It is a flowchart which shows one Embodiment of the drying method of the to-be-processed object which concerns on this invention.

[被処理物の乾燥装置の構成]
以下、本発明に係る被処理物の乾燥方法及び乾燥装置について、好ましい一実施形態に基づいて詳細に説明する。図1は本発明に係る被処理物の乾燥装置の一実施形態における内部構成を示す平面断面図、図2は図1に示す乾燥装置のB−B断面図、図3は撹拌翼の側面図である。本発明に係る被処理物の乾燥装置(以下、単に「乾燥装置」という。)1は、概略として、水平に配置された横長のジャケット(又はケーシング)2と、このジャケット2の内部を貫通するように並列に配置された2つの回転軸3a,3bと、回転軸3a,3bのそれぞれに所定間隔に取り付けられた複数(本実施形態では、回転軸3a側に22基、回転軸3b側に23基)の撹拌翼(ウェッジ)4(4−1〜4−45)と、回転軸3a,3bの駆動源である駆動機構5a,5bと、ジャケット2の後端(図1では右側端)の内側に配設された堰板6と、ジャケット2を支持する支持部材7を備えて構成されている。
[Configuration of Drying Device for Processing Object]
Hereinafter, a drying method and a drying apparatus for an object to be processed according to the present invention will be described in detail based on a preferred embodiment. FIG. 1 is a plan sectional view showing an internal configuration of an embodiment of a drying apparatus for an object to be treated according to the present invention, FIG. 2 is a sectional view taken along line BB of the drying apparatus shown in FIG. 1, and FIG. It is. A processing object drying apparatus (hereinafter simply referred to as a “drying apparatus”) 1 according to the present invention generally includes a horizontally long jacket (or casing) 2 that is horizontally disposed and an inside of the jacket 2. Two rotation shafts 3a and 3b arranged in parallel, and a plurality of rotation shafts 3a and 3b attached to each of the rotation shafts 3a and 3b (in this embodiment, 22 on the rotation shaft 3a side and on the rotation shaft 3b side). 23) stirring blades (wedges) 4 ( 4-1 to 4-45 ), driving mechanisms 5a and 5b which are driving sources of the rotating shafts 3a and 3b, and the rear end of the jacket 2 (right end in FIG. 1) And a support member 7 that supports the jacket 2.

ジャケット2は、例えば金属製であり、図3に示すように、下部側が撹拌翼4−1〜4−22及び撹拌翼4−23〜4−45の形状に即して断面が円弧状をした略W字形状に形成されると共に、その内部は密封構造とされている。そして、図2に示すように、ジャケット2の一端側(図2では左側)の上部には被処理物の投入口2aが設けられ、他端側(図2では右側)には堰板6が配置されると共に、堰板6の上部に排出口2eが設けられている。そして、堰板6の上部高さ位置は撹拌翼4の高さ位置よりも高い位置とされている。これにより、操業の初めに全ての撹拌翼4−1〜4−45の上部が隠れる高さとなるまでジャケット2内に半乾燥状態の被処理物を保持させることで、投入口2aから投入された新たな被処理物が撹拌翼4の表面に直接接触するのを防止して、撹拌翼4の表面で鋳付きが成長するのを防止したものである。尚、堰板6の上部高さ位置は、被処理物を撹拌翼4−1〜4−45の回転中心から上端までの長さの80%以上、好ましくは95%以上の高さ、さらに好ましくは上端の高さまで満たすことができる高さを確保できれば撹拌翼4の表面の鋳付きの成長を防止することは可能である。また、ジャケット2は二重構造とされていると共に、ジャケット2の両側面にはそれぞれ加熱蒸気供給口2f,2fが複数設けられ、加熱蒸気供給口2f,2fから加熱蒸気をジャケット2の空洞内に供給することによりジャケット2内の被処理物の加熱乾燥を促進する。そして、ジャケット2の底部には複数(図2では3つ)のドレン排出口2c,2cが取り付けられており、加熱蒸気供給口2f,2fから供給された加熱蒸気が冷却された後のドレンを排水するようになっている。さらに、排出口2eの近傍には加熱エア供給口2bが設けられると共に、ジャケット2の上部の途中位置にはジャケット2内に導入された加熱エアと被処理物を乾燥させる際に発生する蒸気を図示しない集塵装置へ導くための排気ダクト2d(図2参照)が接続されている。そして、排気ダクト2dと図示しない集塵装置とは図示しない導管によって連結されており、導管の少なくとも集塵装置の手前及び集塵装置にはいわゆるスチームトレースが設けられている。被処理物を乾燥させる際に発生する蒸気によって乾燥装置内部や図示しない集塵装置が結露するのを防止するためである。尚、スチームトレースは導管の少なくとも集塵装置の手前又は集塵装置のいずれか一方に設けることもできる。スチームトレースによって図示しない集塵装置内の温度が露点温度以下に低下するのを防止する。集塵装置内の温度が露点温度以下になると結露によって集塵装置の濾布が濡れてしまい、濾布による圧損が急上昇して操業不可になるからである。 Jacket 2 is for example made of metal, as shown in FIG. 3, section in line with the shape of the lower side agitating blade 4 -1 to 4 -22 and stirring blade 4 -23 -4 -45 has an arcuate While being formed in a substantially W shape, the inside is made into the sealing structure. As shown in FIG. 2, a workpiece inlet 2 a is provided at the upper portion of one end side (left side in FIG. 2) of the jacket 2, and a weir plate 6 is provided on the other end side (right side in FIG. 2). At the same time, a discharge port 2 e is provided on the top of the barrier plate 6. The upper height position of the weir plate 6 is higher than the height position of the stirring blade 4. Thereby, the semi-dried object to be treated is held in the jacket 2 until the upper part of all the stirring blades 4-1 to 4-45 is hidden at the beginning of the operation, so that the material is charged from the charging port 2a. The new object to be treated is prevented from coming into direct contact with the surface of the stirring blade 4 to prevent the casting from growing on the surface of the stirring blade 4. The upper height position of the weir plate 6 is 80% or more, preferably 95% or more of the length from the rotation center to the upper end of the stirring blades 4-1 to 4-45 , more preferably 95% or more. If the height which can be filled up to the height of the upper end can be secured, it is possible to prevent the growth of the surface of the stirring blade 4 from being cast. Further, the jacket 2 has a double structure, and a plurality of heating steam supply ports 2f and 2f are provided on both side surfaces of the jacket 2, and the heating steam is supplied from the heating steam supply ports 2f and 2f into the cavity of the jacket 2. To heat the drying of the object to be processed in the jacket 2. A plurality (three in FIG. 2) of drain discharge ports 2c and 2c are attached to the bottom of the jacket 2, and the drain after the heating steam supplied from the heating steam supply ports 2f and 2f is cooled is removed. It is designed to drain. Further, a heating air supply port 2b is provided in the vicinity of the discharge port 2e, and heating air introduced into the jacket 2 and steam generated when drying the object to be processed are disposed at an intermediate position on the jacket 2. An exhaust duct 2d (see FIG. 2) for leading to a dust collector (not shown) is connected. The exhaust duct 2d and a dust collector (not shown) are connected by a conduit (not shown), and a so-called steam trace is provided at least before the dust collector and in the dust collector. This is to prevent the inside of the drying device and a dust collector (not shown) from condensing due to the steam generated when the workpiece is dried. Note that the steam trace can be provided at least before the dust collector of the conduit or on either the dust collector. Steam trace prevents the temperature in the dust collector (not shown) from dropping below the dew point temperature. This is because when the temperature in the dust collector becomes equal to or lower than the dew point, the filter cloth of the dust collector becomes wet due to dew condensation, and the pressure loss due to the filter cloth rises rapidly and the operation becomes impossible.

回転軸3a,3bは、内部が中空状とされてその内部に蒸気供給口2g,2gを介して加熱蒸気(例えば、0.5〜0.6MPaの加熱蒸気)が導入可能に形成されており、回転軸3a,3b内に導入された加熱蒸気はさらに、後述するように、撹拌翼4−1〜4−45の内部に導入されるようになっている。被処理物が加熱蒸気によって加熱された回転軸3a,3b及び撹拌翼4−1〜4−45と接触することにより被処理物の乾燥が行われる。尚、蒸気供給口2g,2gは、内部に複数の流路を備えたロータリージョイントによって形成されており、回転軸3a,3b及び撹拌翼4−1〜4−45に導入された加熱蒸気が熱交換されることにより生じた水分は再び蒸気供給口2g,2gを介して排水される。乾燥された被処理物は、堰板6の上部に設けられた排出口2eからオーバーフローするようにして排出され、排出シュート2h(図2参照)を介して密閉式の搬送装置、例えば、フローコンベアによって搬出されるように構成されている。その理由は、解砕・乾燥された乾燥品の粒子径が1〜100μmと極めて細かい場合にはベルトコンベア等の開放系のコンベアによる搬送では乾燥品が飛散したり、落鉱が極めて多くなって搬送不良が生じるおそれがあるからである。 The rotary shafts 3a and 3b are formed in a hollow shape so that heating steam (for example, heating steam of 0.5 to 0.6 MPa) can be introduced into the rotation shafts via the steam supply ports 2g and 2g. The heating steam introduced into the rotary shafts 3a and 3b is further introduced into the stirring blades 4-1 to 4-45 as will be described later. The workpiece is dried by contacting the workpieces with the rotating shafts 3a and 3b and the stirring blades 4-1 to 4-45 heated by the heating steam. The steam supply ports 2g and 2g are formed by rotary joints having a plurality of flow paths therein, and the heated steam introduced into the rotating shafts 3a and 3b and the stirring blades 4 -1 to 4-45 is heated. The water generated by the exchange is drained again through the steam supply ports 2g and 2g. The dried object to be processed is discharged so as to overflow from a discharge port 2e provided at the upper portion of the dam plate 6, and is sealed through a discharge chute 2h (see FIG. 2), for example, a flow conveyor. It is comprised so that it may be carried out by. The reason for this is that when the particle size of the crushed and dried product is as fine as 1 to 100 μm, the dried product scatters or the amount of ore falling is extremely high when transported by an open conveyor such as a belt conveyor. This is because a conveyance failure may occur.

回転軸3a,3bはそれぞれ両端側が軸受けによって回転可能に軸支されている。そして、図6に示すように、回転軸3aは時計方向に回転し、回転軸3bは反時計方向に回転するようになっている。すなわち、回転軸3a,3bは駆動機構5a,5bによって互いに逆方向で、且つ、同一速度で回転するように駆動されようになっている。そして、図1に示すように、本実施形態では各回転軸3a,3bにそれぞれ取り付けられて2列に配置された撹拌翼4−1〜4−45は回転軸3a側が22基(4−1〜4−22)で、回転軸3b側が23基(4−23〜4−45)となっている。平面方向から見ると、撹拌翼4−1〜4−22と撹拌翼4−23〜4−45とがジャケット2の中央側で一部が交互に千鳥状に重なるようにして配置されている。 The rotary shafts 3a and 3b are pivotally supported at both ends by bearings. As shown in FIG. 6, the rotating shaft 3a rotates in the clockwise direction, and the rotating shaft 3b rotates in the counterclockwise direction. That is, the rotating shafts 3a and 3b are driven to rotate in opposite directions and at the same speed by the driving mechanisms 5a and 5b. As shown in FIG. 1, in this embodiment, the stirring blades 4 -1 to 4-45 attached to the respective rotary shafts 3a and 3b and arranged in two rows have 22 rotary shafts 3a (4 -1). ˜4 −22 ), and the rotating shaft 3 b side is 23 (4 −23 to 4-45 ). When viewed from the plane direction, the stirring blades 4-1 to 4-22 and the stirring blades 4-23 to 4-45 are arranged so as to partially overlap each other alternately at the center side of the jacket 2.

撹拌翼4−1〜4−45は、それぞれ同一の形状とされ、円盤状の2箇所の一部に切欠8,8によって扇形に形成された一対の翼片4a,4b及び翼片4c,4dを備えて形成されている。翼片4a〜4dは、内部が中空構造とされ、回転軸3a,3bに導入された加熱蒸気が内部に導入されて加熱されるようになっている。また、翼片4a〜4dは、図5に示すように、回転方向側端部を厚く、回転方向逆側端部を薄くしたテーパー状とされており被処理物の解砕及び撹拌力を増加できる形状とされている。また、図3に示すように、撹拌翼4−1〜4−22は、回転軸3a側においては翼片4a,4bの2枚を同一円周上に対向配置されており、同様に、撹拌翼4−23〜4−45は、回転軸3b側においては翼片4c,4dの2枚を同一円周上に対向配置させた構成になっている。そして、撹拌翼4−1〜4−45の翼片4a〜4dは切欠部8の設けられた位置が軸方向から見て所定枚数(本実施形態では4枚)において重ならないように異なる位置に配置されている。 The stirring blades 4 -1 to 4 -45 have the same shape, and a pair of blade pieces 4 a and 4 b and blade pieces 4 c and 4 d formed in a disk shape by notches 8 and 8 in two portions of the disk shape. It is formed with. The wing pieces 4a to 4d have a hollow structure inside, and the heating steam introduced into the rotary shafts 3a and 3b is introduced into the inside and heated. Further, as shown in FIG. 5, the blade pieces 4a to 4d have a tapered shape in which the rotation direction side end portion is thick and the rotation direction opposite side end portion is thinned, thereby increasing the crushing and stirring force of the workpiece. It can be shaped. Further, as shown in FIG. 3, the stirring blades 4 -1 to 4-22 are arranged so that two blade pieces 4a and 4b are opposed to each other on the same circumference on the rotating shaft 3a side. Each of the blades 4-23 to 4-45 has a configuration in which two blade pieces 4c and 4d are arranged opposite to each other on the same circumference on the rotating shaft 3b side. The wing 4a~4d impellers 4 -1 to 4 -45 to different positions so that the position provided with the cutout portion 8 does not overlap the predetermined number as viewed from the axial direction (four in this embodiment) Has been placed.

切欠部8を形成する外縁部には補助翼20が取り付けられている。補助翼20は、被処理物を乾燥した乾燥物が固まらないように解砕すると共に、被処理物を出口側へ送り出したり入口側へ戻したりして被処理物をジャケット2内に所定時間保持して乾燥を促進するために設けられている。補助翼20は金属製の板部材を90°に折り曲げた略L字状の補助翼片20a,20aを2個一対として翼片4a〜4dに形成した切欠部8における回転方向の後端側の縁部の外周部の位置外周端縁部に設けられた補助翼取付座12に図示しないボルト及びロックナットによって固定することによって取り付けられている。そして、補助翼20は翼片4a〜4dの板面に対して各々所定の傾斜角度θで取り付けられている。   An auxiliary wing 20 is attached to the outer edge portion forming the notch portion 8. The auxiliary blade 20 crushes the processed material so that the dried product does not harden, and sends the processed material to the outlet side or returns it to the inlet side to hold the processed material in the jacket 2 for a predetermined time. And provided to promote drying. The auxiliary wing 20 is a rear end side in the rotational direction of the notch 8 formed in the wing pieces 4a to 4d as a pair of substantially L-shaped auxiliary wing pieces 20a and 20a formed by bending a metal plate member at 90 °. The outer peripheral portion of the edge portion is attached to the auxiliary wing mounting seat 12 provided at the outer peripheral edge by being fixed by bolts and lock nuts (not shown). And the auxiliary wing | blade 20 is each attached with the predetermined inclination | tilt angle (theta) with respect to the plate | board surface of blade piece 4a-4d.

翼片4a〜4dの回転軸3a,3bへの取り付け角度は、本実施形態の場合、図6に示すようになっている。図6では回転軸3aに撹拌翼4−1〜4−5の5枚目まで、そして、回転軸3bに撹拌翼4−23〜4−27の5枚目までの各翼片4a〜4dの取付角度を示している。そして、回転軸3a側においては、撹拌翼4−1〜4−4の翼片4a〜4dが水平位置(9時の位置)から半時計方向へ15°、60°、105°、150°というように角度をずらして取り付けられ、撹拌翼4−5〜4−22は撹拌翼4−1〜4−4の取り付けの繰り返しとなる。また、回転軸3b側においては、撹拌翼4−23〜4−26の翼片4c,4dが12時の位置から時計方向へ15°、60°、105°、150°というように角度をずらして取り付けられ、撹拌翼4−27〜4−45は撹拌翼4−23〜4−26の取り付けの繰り返しとなる。このように、補助翼20の取り付け方向がそれぞれ相違するので被処理物の破砕や撹拌が十分に行われると共に、被処理物を投入口2a側から排出口2eへ送り出すと共に反対側へ戻す動きを与える撹拌翼4の作用がさらに補助される。尚、送り補助翼20は、被乾燥物の粘着性の度合等に応じて適宜、最適な大きさ、形状及び傾斜角等のものを選定することができる。 In the case of this embodiment, the attachment angles of the blade pieces 4a to 4d to the rotary shafts 3a and 3b are as shown in FIG. Until 5 th of the stirring blade 4 -1 to 4 -5 to the rotary shaft 3a in FIG. 6, and, for each wing 4a~4d to 5th stirring blade 4 -23 -4 -27 to the rotary shaft 3b The mounting angle is shown. Then, in the rotary shaft 3a side, stirring blade 4 -1 15 ° from -4 -4 wing 4a~4d horizontal position (9 o'clock) the counterclockwise direction, 60 °, 105 °, that 150 ° shifting the angle attached to, stirring blade 4 -5 to 4 -22 is the repetition of the attachment of the stirring blade 4 -1 to 4 -4. On the rotating shaft 3b side, the blade pieces 4c and 4d of the stirring blades 4-23 to 4-26 are shifted in the clockwise direction from the 12 o'clock position to 15 °, 60 °, 105 °, and 150 °. The agitating blades 4-27 to 4-45 are repeatedly attached to the agitating blades 4-23 to 4-26 . As described above, since the attachment directions of the auxiliary blades 20 are different from each other, the workpiece is sufficiently crushed and stirred, and the workpiece is sent from the inlet 2a side to the outlet 2e and returned to the opposite side. The action of the stirring blade 4 to be applied is further assisted. The auxiliary feeding blade 20 can be appropriately selected in accordance with the degree of adhesiveness of the material to be dried and the like, as appropriate, with an optimal size, shape, inclination angle, and the like.

駆動機構5a,5bは、回転軸3a,3bのそれぞれに対応して同一構成のものが配置されている。ここで、回転軸3a側の駆動機構5aの構成について説明すると、図2に示すように、駆動源であるモータ5a−1と、モータ5a−1の回転数を調整する減速装置5a−2と、減速装置5a−2の回転出力を回転軸3aに伝達する伝達部材5a−3とを備えて構成されている。 The drive mechanisms 5a and 5b have the same configuration corresponding to the rotation shafts 3a and 3b, respectively. Here, the configuration of the drive mechanism 5a on the rotary shaft 3a side will be described. As shown in FIG. 2, a motor 5a- 1 that is a drive source, and a speed reducer 5a- 2 that adjusts the number of rotations of the motor 5a- 1. The transmission member 5a- 3 that transmits the rotational output of the speed reducer 5a- 2 to the rotary shaft 3a is provided.

堰板6は、ジャケット2内に供給された被処理物をせき止め、被処理物が撹拌翼4−1〜4−45の回転中心から上端までの長さの80%以上、好ましくは95%以上の高さ、さらに好ましくは上端の高さ(図2のYレベルを越える高さ)まで満たされるように保持するための部材である。被処理物を撹拌翼4−1〜4−45の回転中心から上端までの長さの少なくとも80%以上の高さまで保持できれば、撹拌翼4−1〜4−45への鋳付き防止及び駆動機構5a,5bの過負荷の発生を防止することができる。堰板6の寸法・形状は図3に示すジャケット2の内部形状相当であるが、本実施形態では上端の高さは少なくとも撹拌翼4−1〜4−45が投入された被処理物によって隠れる高さ以上とされ、撹拌翼4−1〜4−45の上部高さよりも上方とされている。尚、堰板6の使用材料は、撹拌翼4−1〜4−45によって乾燥品の押し出し圧に耐えられるもの、例えば鉄系等の金属を用いることができる。 The weir plate 6 dams the workpiece supplied into the jacket 2, and the workpiece is 80% or more, preferably 95% or more of the length from the rotation center to the upper end of the stirring blades 4-1 to 4-45. And more preferably a member for holding it so as to be filled up to the height of the upper end (height exceeding the Y level in FIG. 2). If you are holding an object to be processed until stirring blade 4 -1 to 4 -45 from the rotation center to the upper end of a length of at least 80% of the height, casting with preventing and drive mechanism for the stirring blade 4 -1 to 4 -45 Occurrence of overloads 5a and 5b can be prevented. The dimensions and shape of the weir plate 6 are equivalent to the internal shape of the jacket 2 shown in FIG. 3, but in this embodiment, the height of the upper end is hidden by the workpiece to which at least the stirring blades 4-1 to 4-45 are put. The height is set to be higher than the upper height of the stirring blades 4-1 to 4-45 . The material used for the weir plate 6 may be a material that can withstand the extrusion pressure of the dried product by the stirring blades 4-1 to 4-45 , for example, an iron-based metal.

支持部材7は、ジャケット2を所定の高さに維持するための構造体であり、所望の強度を有する鋼管、形鋼等を組み合わせて構築されている。   The support member 7 is a structure for maintaining the jacket 2 at a predetermined height, and is constructed by combining a steel pipe, a shape steel, and the like having a desired strength.

[被処理物の乾燥装置の動作及び乾燥方法]
次に、上述した乾燥装置1の動作及び乾燥方法について説明する。図7は本発明に係る被処理物の乾燥方法の一実施形態を示すフローチャートである。本実施形態における被処理物の性状は、例えば、水分含量が30〜70質量%、銅品位が5〜50質量%、嵩比重が1.2〜2.0、粒子径が1〜100μmのスラッジ状の物である。このような性状の被処理物は、例えば特許文献2に示すような従来の伝導伝熱型乾燥装置では十分に乾燥を行うことができなかったものだからである。もちろん、本実施形態における乾燥装置1による乾燥の対象となる被処理物はこのような性状に限定されるものではない。
[Operation and drying method of drying apparatus for processing object]
Next, operation | movement of the drying apparatus 1 mentioned above and the drying method are demonstrated. FIG. 7 is a flowchart showing an embodiment of a method for drying an object to be processed according to the present invention. The properties of the object to be treated in the present embodiment are, for example, sludge having a water content of 30 to 70% by mass, a copper grade of 5 to 50% by mass, a bulk specific gravity of 1.2 to 2.0, and a particle size of 1 to 100 μm. It is a shape. This is because the object to be treated having such properties cannot be sufficiently dried by a conventional conductive heat transfer type drying apparatus as shown in Patent Document 2, for example. Of course, the workpiece to be dried by the drying apparatus 1 in the present embodiment is not limited to such properties.

初めに、回転軸3a,3bを介して加熱蒸気を撹拌翼4−1〜4−45内に導入すると共に、駆動機構5a,5bを駆動して撹拌翼4−1〜4−45を所定速度(例えば、15〜30rpm)で回転駆動させ、投入口2aから被処理物をジャケット2内に投入する(ステップS1:投入工程)。このときの被処理物の投入速度は定格(例えば、3.0wt/h)の1/3以下である。定格の1/3の速度より早い投入速度で投入すると、被処理物が撹拌翼4−1〜4−45に鋳付いてしまい、撹拌翼4−1〜4−45から離れなくなり、乾燥効率が著しく低下すると共に鋳付きの除去のために数日後に長期操業停止が必要となるからである。尚、ジャケット2内には、排ガス中に多量の水分が含まれるため、排ガス処理設備や排気ダクト2dの結露防止のために蒸気圧0.5〜0.6MPaの蒸気で熱交換された加熱エアを導入することでジャケット2内部が露点温度以下とならないようにしている。また、排気ダクト2dから図示しない導管を介して連結された図示しない集塵装置にはスチームトレースが設けられ、少なくとも集塵装置内を80℃以上に維持しているので集塵装置の濾布が結露によって濡れて圧損が急上昇して操業不可となるのを防止している。 First, heating steam is introduced into the stirring blades 4-1 to 4-45 through the rotating shafts 3a and 3b, and the driving mechanisms 5a and 5b are driven to move the stirring blades 4-1 to 4-45 at a predetermined speed. (For example, 15 to 30 rpm), the workpiece is introduced into the jacket 2 from the introduction port 2a (step S1: introduction step). The input speed of the object to be processed at this time is 1/3 or less of the rating (for example, 3.0 wt / h). When turning at a faster input rate than the rate of 1/3 of the rated, the treatment object is will be attached cast to stirring blade 4 -1 to 4 -45, no longer separated from the stirring blade 4 -1 to 4 -45, drying efficiency This is because it is remarkably lowered and a long-term operation stop is required after several days for removing the casting. Since the jacket 2 contains a large amount of moisture in the exhaust gas, the heated air is heat-exchanged with steam having a vapor pressure of 0.5 to 0.6 MPa in order to prevent dew condensation in the exhaust gas treatment facility and the exhaust duct 2d. Is introduced so that the inside of the jacket 2 does not fall below the dew point temperature. Also, a dust collector (not shown) connected from the exhaust duct 2d via a conduit (not shown) is provided with a steam trace, and at least the inside of the dust collector is maintained at 80 ° C. or higher. It prevents wet operation due to condensation and pressure loss soaring that it becomes impossible to operate.

ジャケット2内に投入された被処理物は、回転している撹拌翼4−1〜4−45及び補助翼20によって順次撹拌されながら後段へ移動し、その過程で乾燥処理が行われる。この過程では、乾燥中の被処理物の高さ位置が攪拌翼4−1〜4−45の回転中心から上端までの長さの80%以上、好ましくは95%以上の高さとなるまで、さらに好ましくは撹拌翼4−1〜4−45の上端が隠れる高さとなるまで半乾燥を行う(ステップS2:半乾燥工程)。半乾燥工程では被処理物の水分含量が20質量%以上、30質量%未満となるように被処理物の乾燥を行う。半乾燥を行うのは撹拌翼4−1〜4−45への鋳付き防止及び駆動機構5a,5bの過負荷の発生を防止するためである。尚、半乾燥状態となった被処理物を半乾燥品という。このような半乾燥工程を継続することによりジャケット2内には半乾燥品が堆積し、最終的に撹拌翼4−1〜4−45の上端が隠れるレベルに到達するまで半乾燥を行う(ステップS3:蓄積工程)。 The object to be processed put into the jacket 2 moves to the subsequent stage while being sequentially stirred by the rotating stirring blades 4-1 to 4-45 and the auxiliary blade 20, and a drying process is performed in the process. In this process, the height position of the workpiece to be dried is 80% or more of the length from the rotation center to the upper end of the stirring blades 4 -1 to 4-45 , preferably 95% or more. Preferably, semi-drying is performed until the stirring blades 4-1 to 4-45 have a height at which the upper ends are hidden (step S2: semi-drying step). In the semi-drying step, the object to be processed is dried so that the water content of the object to be processed is 20% by mass or more and less than 30% by mass. Perform semi-dry is to prevent the stirring blade 4 -1 to 4 cast with prevention and drive mechanism 5a to -45, the occurrence of 5b overload. In addition, the to-be-processed object which became a semi-dry state is called a semi-dry product. By continuing such a semi-drying process, a semi-dry product is accumulated in the jacket 2 and finally semi-drying is performed until reaching a level at which the upper ends of the stirring blades 4-1 to 4-45 are hidden (step). S3: Accumulation step).

半乾燥品が撹拌翼4−1〜4−45が隠れる高さまでジャケット2内に貯えられたら被処理物の投入速度を定格の投入速度(例えば、3.0wt/h)の80〜100%の投入速度で定格操業に移行する(ステップS4:乾燥工程)。乾燥工程では、被処理物の水分含量が15質量%以上、20質量%未満となるように乾燥を行う。被処理物の水分含量が15%未満となるような完全乾燥を行うと被処理物の粒度が細かい場合には乾燥品貯留鉱区やその後の運搬などの際に酷い発塵を生じることで作業環境の悪化を招いたり、設備寿命を著しく短くする等の不具合を招くおそれがあるからである。そのため、水分含量が20質量%以上、30質量%未満の半乾燥品の状態で一旦ジャケット2内に保持し、その後乾燥工程によって被処理物の水分含量が15質量%以上、20質量%未満となるように乾燥を行う。ここで、乾燥状態となった被処理物を乾燥品という。尚、粒度が細かくなく、乾燥後の飛散等の問題がない場合には、水分含量を15質量%以下となるまで乾燥してもよい。乾燥工程において撹拌翼4−1〜4−45の回転によって解砕されて乾燥された乾燥品は、堰板6をオーバーフローして排出口2eから排出シュート2hへ落下しジャケット2の外へ排出され(ステップS5:排出工程)、さらに密閉式のフローコンベアによって所定の場所へ運ばれる。 When the semi-dried product is stored in the jacket 2 to such a height that the stirring blades 4-1 to 4-45 are hidden, the charging speed of the workpiece is set to 80 to 100% of the rated charging speed (for example, 3.0 wt / h). The operation shifts to the rated operation at the charging speed (step S4: drying process). In the drying step, drying is performed so that the water content of the object to be processed is 15% by mass or more and less than 20% by mass. When complete drying is performed so that the moisture content of the object to be processed is less than 15%, if the particle size of the object to be processed is fine, severe dust generation will occur during the dry product storage or subsequent transportation, etc. This is because there is a risk of inconveniences such as deterioration of the equipment life and remarkably shortening of the equipment life. Therefore, the moisture content is temporarily held in the jacket 2 in a semi-dried product having a moisture content of 20% by mass or more and less than 30% by mass, and then the moisture content of the object to be processed is 15% by mass or more and less than 20% by mass by a drying process. Dry so as to be. Here, an object to be processed that has been dried is referred to as a dried product. If the particle size is not fine and there is no problem such as scattering after drying, drying may be performed until the water content is 15% by mass or less. Was dried and crushed by rotating the stirring blades 4 -1 to 4 -45 in the drying process drying product, overflows a weir plate 6 falls from the discharge port 2e to the discharge chute 2h is discharged to the outside of the jacket 2 (Step S5: Discharge process) Further, it is carried to a predetermined place by a sealed flow conveyor.

以上のように、本発明の好ましい実施形態について詳述したが、本発明は係る特定の実施形態に限定されるものではなく、特許請求の範囲に記載された本発明の要旨の範囲内において、種々の変形・変更が可能であることはいうまでもない。例えば、本発明に係る乾燥装置は、含銅スラッジ以外の被処理物にも幅広く展開可能である。また、乾燥品排出設備や集塵装置ダスト搬送設備は粒子径の観点から搬送不良を極度に起こしやすい被処理物に対応可能な仕様としているため、より幅広い被処理物の取り扱いにも対応可能である。   As described above, the preferred embodiment of the present invention has been described in detail. However, the present invention is not limited to the specific embodiment, and within the scope of the gist of the present invention described in the claims, Needless to say, various modifications and changes are possible. For example, the drying apparatus according to the present invention can be widely applied to objects to be processed other than copper-containing sludge. In addition, the dry product discharge facility and dust collector dust transport facility are designed to handle workpieces that are extremely susceptible to poor transport from the viewpoint of particle size, so they can handle a wider range of workpieces. is there.

1 乾燥装置
2 ジャケット
2a 投入口
2b 加熱エア供給口
2c ドレン排出口
2d 排気ダクト
2e 排出口
2f 加熱蒸気供給口
2g 蒸気供給口
2h 排出シュート
3a,3b 回転軸
−1〜4−45 撹拌翼
4a〜4d 撹拌翼
5 駆動機構
5a モータ
5b 減速装置
5c 伝達部材
6 堰板
7 支持部材
8 切欠部
9 送り羽根
10 戻り羽根
11 ボルト孔
12 補助翼取付座
20 補助翼
20a 補助翼片
DESCRIPTION OF SYMBOLS 1 Drying apparatus 2 Jacket 2a Input port 2b Heating air supply port 2c Drain discharge port 2d Exhaust duct 2e Discharge port 2f Heating steam supply port 2g Steam supply port 2h Discharge chute 3a, 3b Rotating shaft 4 -1 to 4-45 Stirring blade 4a -4d Stirring blade 5 Drive mechanism 5a Motor 5b Deceleration device 5c Transmission member 6 Dam plate 7 Support member 8 Notch 9 Feed blade 10 Return blade 11 Bolt hole 12 Auxiliary blade mounting seat 20 Auxiliary blade 20a Auxiliary blade piece

Claims (11)

互いに平行に配置された少なくとも2本の回転軸を互いに反対方向へ回転可能に配置し、前記回転軸には所定の間隔を有して撹拌翼をそれぞれ複数配置すると共に、一方側の回転軸に取り付けられた撹拌翼と他方側に取り付けられた撹拌翼が交互に位置するように配置され、ジャケット及び前記撹拌翼に加熱された熱媒体を供給することにより被処理物を加熱乾燥する撹拌式乾燥装置によるスラッジ状の被処理物の乾燥方法において、
スラッジ状の被処理物を定格の1/3以下の投入速度で前記撹拌式乾燥装置に投入し、前記撹拌式乾燥装置内で乾燥中の前記被処理物の高さ位置が前記撹拌翼の回転中心から上端までの長さの80%以上が隠れる高さとなるまで半乾燥を行う半乾燥工程と、
前記半乾燥状態の前記被処理物が、前記撹拌翼が隠れる高さまで当該撹拌乾燥装置内に貯えられたら、前記被処理物を定格の80〜100%の投入速度で投入して乾燥を行う乾燥工程と、
を含み構成されたことを特徴とする被処理物の乾燥方法。
At least two rotating shafts arranged in parallel to each other are arranged so as to be rotatable in opposite directions to each other, and a plurality of stirring blades are arranged on the rotating shaft with a predetermined interval. Stirring-type drying in which the stirring blades attached and the stirring blades attached to the other side are alternately arranged, and the workpiece is heated and dried by supplying a heated heat medium to the jacket and the stirring blades In the method for drying the sludge-like workpiece by the apparatus,
A sludge-like object to be treated is introduced into the stirring type drying device at an input speed of 1/3 or less of the rated value, and the height position of the object to be treated in the stirring type drying device is rotated by the stirring blade. A semi-drying step of semi-drying until 80% or more of the length from the center to the upper end is hidden,
When the workpiece in the semi-dried state is stored in the stirring and drying apparatus to a height at which the stirring blade is hidden, drying is performed by feeding the workpiece at a rate of 80 to 100% of the rated speed. Process,
A method for drying an object to be processed, comprising:
請求項1に記載の被処理物の乾燥方法において、
前記被処理物の定格の投入速度が、3.0〜5.0wt/hであることを特徴とする被処理物の乾燥方法。
In the drying method of the to-be-processed object of Claim 1,
The method for drying an object to be processed is characterized in that the rated input speed of the object to be processed is 3.0 to 5.0 wt / h.
請求項1又は2に記載の被処理物の乾燥方法において、
前記乾燥工程での乾燥は、内部に0.5〜0.6MPaの蒸気を導入することによって加熱された前記撹拌翼を15〜30rpmで回転させて行うことを特徴とする被処理物の乾燥方法。
In the drying method of the to-be-processed object of Claim 1 or 2,
The drying in the drying step is performed by rotating the stirring blade heated by introducing steam of 0.5 to 0.6 MPa into the interior at 15 to 30 rpm. .
請求項1から3のいずれか1項に記載の被処理物の乾燥方法において、
前記撹拌式乾燥装置の内部に加熱エアを導入すると共に、当該撹拌式乾燥装置から排気される排ガスを集塵装置へ送る導管の少なくとも前記集塵装置の手前及び/又は前記集塵装置をスチームトレースによって保温することにより前記導管内部及び前記集塵装置の内部が露点温度以下とならないようにすることを特徴とする被処理物の乾燥方法。
In the drying method of the to-be-processed object of any one of Claim 1 to 3,
The heated air is introduced into the agitation-type drying device and the exhaust gas exhausted from the agitation-type drying device is sent to the dust collection device at least before the dust collection device and / or the steam collection device. The method of drying an object to be treated is characterized in that the inside of the conduit and the inside of the dust collector are kept at a dew point temperature or lower by keeping the temperature at a low temperature.
請求項1から4のいずれか1項に記載の被処理物の乾燥方法において、
乾燥が終了した前記被処理物を密閉系のコンベアによって搬送することを特徴とする被処理物の乾燥方法。
In the drying method of the to-be-processed object of any one of Claim 1 to 4,
A method for drying an object to be processed, wherein the object to be processed after drying is conveyed by a closed conveyor.
請求項1から5のいずれか1項に記載の被処理物の乾燥方法において、
前記被処理物は、水分含量が30〜70質量%、銅品位が5〜50質量%、嵩比重1.2〜2.0であることを特徴とする被処理物の乾燥方法。
In the drying method of the to-be-processed object of any one of Claim 1 to 5,
The said processed material is 30-70 mass% of water contents, 5-50 mass% of copper grades, and bulk specific gravity 1.2-2.0, The drying method of the processed material characterized by the above-mentioned.
請求項1から6のいずれか1項に記載の被処理物の乾燥方法において、
前記被処理物の前記半乾燥工程では、当該被処理物の水分含量が20質量%以上、30質量%未満となるように半乾燥を行うことを特徴とする被処理物の乾燥方法。
In the drying method of the to-be-processed object of any one of Claim 1 to 6,
In the said semi-drying process of the said to-be-processed object, the semi-drying is performed so that the moisture content of the said to-be-processed object may be 20 mass% or more and less than 30 mass%, The drying method of the to-be-processed object characterized by the above-mentioned.
請求項1から7のいずれか1項に記載の被処理物の乾燥方法において、
前記被処理物の粒子径が1〜100μmである場合には、前記乾燥工程では、当該被処理物の水分含量が15質量%以上、20質量%未満となるように乾燥を行うことを特徴とする被処理物の乾燥方法。
In the drying method of the to-be-processed object of any one of Claim 1 to 7,
When the particle size of the object to be treated is 1 to 100 μm, the drying step is performed such that the moisture content of the object to be treated is 15% by mass or more and less than 20% by mass. A method for drying an object to be processed.
互いに平行に配置された少なくとも2本の回転軸を互いに反対方向へ回転可能に配置し、前記回転軸には所定の間隔を有して撹拌翼をそれぞれ複数配置すると共に、一方側の回転軸に取り付けられた撹拌翼と他方側に取り付けられた撹拌翼が交互に位置するように配置され、ジャケット及び前記撹拌翼に加熱された熱媒体を供給することにより被処理物を加熱乾燥する撹拌式乾燥装置において、
前記ジャケットに配置された堰板の上端を前記撹拌翼の回転中心から上端までの長さの80%以上の高さとなるように形成されると共に、乾燥後の前記被処理物を前記堰板からオーバーフローさせることにより排出可能に構成されたことを特徴とする撹拌式乾燥装置。
At least two rotating shafts arranged in parallel to each other are arranged so as to be rotatable in opposite directions to each other, and a plurality of stirring blades are arranged on the rotating shaft with a predetermined interval. Stirring-type drying in which the stirring blades attached and the stirring blades attached to the other side are alternately arranged, and the workpiece is heated and dried by supplying a heated heat medium to the jacket and the stirring blades In the device
The upper end of the weir plate arranged on the jacket is formed to be 80% or more of the length from the rotation center to the upper end of the stirring blade, and the processed material after drying is removed from the weir plate. A stirrer type drying apparatus characterized in that it can be discharged by overflowing.
請求項9に記載の撹拌式乾燥装置において、
前記撹拌装置の内部に加熱エアを導入する加熱エア供給手段と、
前記撹拌装置から排気される排ガスを集塵装置へ送る導管と、
前記集塵装置の内部の温度が露点温度以下にならないように前記導管の少なくとも前記集塵装置の手前及び/又は前記集塵装置に設けられたスチームトレースと、
を備えていることを特徴とする被処理物の乾燥装置。
The stirring-type drying apparatus according to claim 9,
Heating air supply means for introducing heated air into the stirring device;
A conduit for sending exhaust gas exhausted from the stirring device to a dust collector;
A steam trace provided at least before the dust collector and / or in the dust collector so that the temperature inside the dust collector does not become a dew point temperature or less;
An apparatus for drying an object to be processed, comprising:
請求項9又は10に記載の被処理物の乾燥装置において、
乾燥が終了した前記被処理物を搬送する搬送手段が密閉式であることを特徴とする被処理物の乾燥装置。
In the drying apparatus of the to-be-processed object of Claim 9 or 10,
An apparatus for drying an object to be processed, wherein a conveying means for conveying the object to be processed after drying is hermetically sealed.
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