JP3569131B2 - Granulation drying equipment - Google Patents

Granulation drying equipment Download PDF

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Publication number
JP3569131B2
JP3569131B2 JP21766198A JP21766198A JP3569131B2 JP 3569131 B2 JP3569131 B2 JP 3569131B2 JP 21766198 A JP21766198 A JP 21766198A JP 21766198 A JP21766198 A JP 21766198A JP 3569131 B2 JP3569131 B2 JP 3569131B2
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Japan
Prior art keywords
chamber
granulation
soil
drying
rotating
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.)
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JP21766198A
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Japanese (ja)
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JP2000042396A (en
Inventor
滋 佐野
正俊 西田
嘉秀 竹本
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.)
Kurimoto Ltd
Shinko Pantec Co Ltd
Original Assignee
Kurimoto Ltd
Kobelco Eco Solutions Co Ltd
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  • Glanulating (AREA)
  • Drying Of Solid Materials (AREA)
  • Treatment Of Sludge (AREA)

Description

【0001】
【発明の属する技術分野】
この発明は、スラッジ等の造粒乾燥装置に関するものである。
【0002】
【従来の技術】
多量に排出される上水スラッジ等の各種スラッジは、乾燥されて廃棄処理されるものの他に、造粒乾燥されて農園芸用土等に再利用されるものがある。これらの再利用されるスラッジは、まず天日等で乾燥されたのち、混練工程、造粒工程および乾燥工程を経て粒状の農園芸用土等になる。
【0003】
上述した農園芸用土等の製造工程では、設備費用の低減や原料搬送の合理化を目的として、前記造粒と乾燥の両工程を一体の装置で行う場合があり、この種の装置としては、実開平6−56693号公報に開示された造粒乾燥装置がある。この造粒乾燥装置は、図6に示すように、ホッパ41から投入されるスラッジを供給するスクリューフィーダ42と、円筒状の回転ドライヤ43と、この回転ドライヤ43の入口端に継足された造粒筒44と、回転ドライヤ43の出口端に設けられた乾燥粒状土の取出室45と、スラッジから蒸発した蒸気を排気する排気室46とで構成されている。
【0004】
前記造粒筒44には、その内周面に近接してスクレーパ47が設けられ、造粒筒44の内周面に付着するスラッジを掻き落とすようになっている。前記スクリューフィーダ42から供給されるスラッジは、造粒筒44内を転動する間に角がとれて丸みを帯び、粒状土となって前記回転ドライヤ43に送り込まれる。
【0005】
前記回転ドライヤ43の外周部には、加熱ガス用のジャケット48が設けられ、前記造粒筒44から送り込まれる粒状土が乾燥される。この乾燥された粒状土は、前記取出室45の下端に設けられた取出口49から排出される。
【0006】
なお、この装置では、前記取出室45に設けられた供給口50からガスを供給し、粒状土が乾燥する際に発生する蒸気を造粒筒44内へ導き、冷たいスラッジとの接触で結露させることにより、バインダとして作用させたり、スラッジの水分を調整したりすることができるとしている。供給されたガスは前記排気室46の排出口51から装置外に排出される。
【0007】
【発明が解決しようとする課題】
上述した従来の造粒乾燥装置は、造粒筒内での転動のみでスラッジを粒状化しているため、粒状土の大きさがまちまちとなり、極端に大きな粒状土が混じる問題がある。例えば、農園芸用の乾燥粒状土は、大きくても10mm以下の直径のものが要求され、この寸法を大幅に越える乾燥粒状土は、出荷前に除去する必要がある。
【0008】
そこで、この発明の課題は、所定の寸法以下で丸みを帯びた乾燥粒状土を供給できる造粒乾燥装置を提供することである。
【0009】
【課題を解決するための手段】
上記の課題を解決するために、この発明は、概ね水平に配置され、回転駆動される円筒状の乾燥室の原料供給端側に、同じく円筒状の造粒室が継足され、この造粒室に供給された原料を造粒乾燥して、前記乾燥室の排出端から排出する造粒乾燥装置において、前記造粒室に、原料を攪拌する回転羽根を設け、前記乾燥室と造粒室との境界に環状の仕切板を設けた構成を採用したのである。
【0010】
すなわち、造粒室と乾燥室との境界に環状の仕切板を設けて、混練工程から供給される塊状土を造粒室内に一定時間溜め、造粒室に設けた回転羽根で前記塊状土を所定の寸法以下の塊に細かく解砕し、これらの解砕された塊を転動させて角をとり、丸みを帯びた粒状土を前記仕切板からオーバーフローさせて乾燥室に送り込むようにしたのである。また、前記回転羽根は、塊状土を練り込んで柔らかくするため、滑らかな丸みを持った粒状土を形成できる効果も有する。
【0011】
【発明の実施の形態】
以下、図1乃至図5に基づき、この発明の実施形態を説明する。図1乃至図3は、造粒乾燥装置の全体図を示す。図1は正面図、図2は平面図、図3は側面図である。この造粒乾燥装置は、回転駆動される円筒状の乾燥室1と、この乾燥室1の入口端に継足された同じく円筒状の造粒室2と、この造粒室2に設けられた回転羽根3と、造粒室2に塊状の混練土を供給するホッパ4と、前記乾燥室1の出口端5に設けられた乾燥粒状土を排出する出口フード6とで基本的に構成されている。
【0012】
前記乾燥室1と造粒室2は両端が開口する一体の回転胴7で形成され、回転胴7の内周の乾燥室1と造粒室2の境界には環状の仕切板8が設けられ、回転胴7の外周にはスプロケット9と2つのタイヤ10が取り付けられている。回転胴7は、架台11上に軸受12を介して取り付けられた2対のローラ13で、前記各タイヤ10部を支持され、減速機付きモータ14の回転軸に取り付けられたスプロケット15と前記スプロケット9に巻き掛けられたチェーン16で回転駆動されるようになっている。
【0013】
前記乾燥室1には、内周壁に近接して複数の加熱チューブ17が軸方向に通されている。これらの加熱チューブ17は、前記出口フード6に取り付けられたロータリージョイント18を介して蒸気配管19に接続され、蒸気配管19から供給される蒸気で乾燥室1を加熱するものであり、間接加熱方式のため高い熱効率を確保することができる。なお、蒸気配管19にはドレン管20も取り付けられている。
【0014】
前記回転胴7の造粒室2側には入口フード21が設けられ、回転胴7の両端はこの入口フード21と前記出口フード6の中に開口している。入口フード21には、後述するガス供給口22と掃除用の原料取出口23も設けられている。
【0015】
前記回転羽根3は、フランジ24と締付けボルトナット25で回転軸26に接続され、他の形態の回転羽根と交換できるようになっている。回転軸26は前記入口フード21を通して外部に取り出され、架台11上に取り付けられた2つの軸受27に支持されて、カップリング28でモータ29の回転軸に接続されている。
【0016】
前記回転羽根3は、図4(a)、(b)に示すように、回転胴7の下部に配置され、軸方向に一定間隔で、回転方向と垂直なパドル状の翼体30が4枚ずつ放射状に設けられている。これらの回転羽根3は、回転胴7の回転方向と逆方向に回転され、造粒室2の下部で転動する塊状の混練土31を解砕する。回転羽根3を回転胴7と逆方向に回転することにより、回転胴7と一緒に移動してくる混練土31を、その反対方向から効率よく解砕することができる。
【0017】
前記回転羽根3で解砕され、転動しながら丸みを帯びた粒状土は、仕切板8からオーバーフローして乾燥室1に送り込まれる。このとき、充分に造粒されていない混練土31は流動性が悪く、細かな混練土31は大きな混練土31の下にもぐり込むため、仕切板8をオーバーフローすることができず、充分に造粒された粒状土だけがオーバーフローする。このため、造粒室2の長さが短くても充分な造粒作用が行われる。また、回転羽根3の回転数を変更することにより、解砕の程度を調節して、製造される粒状土の大きさを変えることもできる。供給される混練土31の物性に応じて回転羽根3の回転数を変更し、混練土31の物性に左右されることなく一定の大きさの粒状土を得ることもできる。
【0018】
前記乾燥室1に送り込まれた粒状土は、乾燥室1内を転動しながら前記加熱チューブ17で加熱乾燥され、前記出口端5から出口フード6に送り出される。この出口フード6には、前記入口フード21のガス供給口22から供給されたガスを排出するガス排出口32が設けられており、このガスで粒状土から発生する蒸気を装置外へ排出するようになっている。このように乾燥された粒状土は、出口フード6の下部に設けられた取出口33より排出される。
【0019】
図5(a)、(b)は、別の形態の回転羽根34を示す。この回転羽根34は、軸方向に一定間隔で、回転方向と平行なブレード状の翼体35が4枚ずつ放射状に取り付けられている。この回転羽根34は混練土をシャーリングするため、硬質の混練土を解砕するのに適している。
【0020】
上述した実施形態では、塊状の混練土を解砕する回転羽根として、パドル状とブレード状のものを示したが、これらの中間的な機能を有するものとして、回転方向と傾斜する翼体を有するプロペラ状の回転羽根を採用することもできる。また、前記放射状に配置される翼体の枚数も任意に選定できる。
【0021】
【発明の効果】
以上のように、この発明の造粒乾燥装置は、造粒室と乾燥室との境界に環状の仕切板を設けて、混練工程から供給される塊状土を造粒室内に一定時間溜め、造粒室に設けた回転羽根で前記塊状土を所定の寸法以下の塊に細かく解砕し、これらの解砕された塊を転動させて角をとり、丸みを帯びた粒状土を仕切板からオーバーフローさせて乾燥室に送り込むようにしたので、所定の寸法以下に粒を揃えた乾燥粒状土を供給することができる。また、前記回転羽根は、塊状土を練り込んで柔らかくする作用も有するため、より滑らかな丸みを持った乾燥粒状土を供給することができる。
【図面の簡単な説明】
【図1】造粒乾燥装置の実施形態を示す一部切欠き正面図
【図2】図1の平面図
【図3】図2のIII −III 線に沿った縦断側面図
【図4】aは図1の要部拡大断面図、bはaのIV−IV線に沿った断面図
【図5】aは別の態様の回転羽根を示す正面図、bはその縦断側面図
【図6】従来の造粒乾燥装置を示す縦断面図
【符号の説明】
1 乾燥室
2 造粒室
3 回転羽根
4 ホッパ
5 出口端
6 出口フード
7 回転胴
8 仕切板
9 スプロケット
10 タイヤ
11 架台
12 軸受
13 ローラ
14 モータ
15 スプロケット
16 チェーン
17 加熱チューブ
18 ロータリージョイント
19 蒸気配管
20 ドレン管
21 入口フード
22 供給口
23 取出口
24 フランジ
25 ボルトナット
26 回転軸
27 軸受
28 カップリング
29 モータ
30 翼体
31 混練土
32 排出口
33 取出口
34 回転羽根
35 翼体
41 ホッパ
42 スクリューフィーダ
43 回転ドライヤ
44 造粒筒
45 取出室
46 排気室
47 スクレーパ
48 ジャケット
49 取出口
50 供給口
51 排出口
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to an apparatus for granulating and drying sludge and the like.
[0002]
[Prior art]
Various types of sludge such as water sludge discharged in a large amount are dried and discarded, and are also granulated and dried and reused as agricultural and horticultural soil. These reused sludges are first dried in the sun or the like, and then subjected to a kneading step, a granulating step, and a drying step to become granular agricultural and horticultural soil.
[0003]
In the above-mentioned production process of agricultural and horticultural soil, for the purpose of reducing equipment costs and rationalizing the transportation of raw materials, both the granulation and drying processes may be performed by an integrated device. There is a granulation drying apparatus disclosed in Japanese Unexamined Patent Publication No. 6-56693. As shown in FIG. 6, the granulating and drying apparatus includes a screw feeder 42 for supplying sludge supplied from a hopper 41, a cylindrical rotary dryer 43, and a granulator connected to an inlet end of the rotary dryer 43. It is composed of a granule cylinder 44, a dry granular soil extraction chamber 45 provided at the outlet end of the rotary dryer 43, and an exhaust chamber 46 for exhausting steam evaporated from sludge.
[0004]
The granulating cylinder 44 is provided with a scraper 47 close to the inner peripheral surface of the granulating cylinder 44 so as to scrape sludge attached to the inner peripheral surface of the granulating cylinder 44. The sludge supplied from the screw feeder 42 is rounded and rounded while rolling in the granulating cylinder 44, and is sent to the rotary dryer 43 as granular soil.
[0005]
A jacket 48 for a heating gas is provided on the outer periphery of the rotary dryer 43, and the granular soil fed from the granulating cylinder 44 is dried. The dried granular soil is discharged from a discharge port 49 provided at a lower end of the discharge chamber 45.
[0006]
In this apparatus, a gas is supplied from a supply port 50 provided in the extraction chamber 45, and steam generated when the granular soil is dried is guided into the granulation cylinder 44, where the vapor is condensed by contact with cold sludge. By doing so, it can be used as a binder or adjust the water content of sludge. The supplied gas is discharged out of the apparatus from the discharge port 51 of the exhaust chamber 46.
[0007]
[Problems to be solved by the invention]
In the above-mentioned conventional granulation drying apparatus, sludge is granulated only by rolling in a granulation cylinder, so that the size of the granular soil varies, and there is a problem that extremely large granular soil is mixed. For example, dry granular soil for agricultural and horticultural use is required to have a diameter of at most 10 mm or less, and dry granular soil greatly exceeding this size must be removed before shipment.
[0008]
Accordingly, an object of the present invention is to provide a granulating and drying apparatus capable of supplying a rounded dry granular soil having a predetermined size or less.
[0009]
[Means for Solving the Problems]
In order to solve the above-mentioned problem, the present invention is directed to a cylindrical drying chamber which is arranged substantially horizontally and is rotatably driven at the raw material supply end side of the cylindrical drying chamber. In a granulation drying apparatus for granulating and drying the raw material supplied to the chamber and discharging the raw material from the discharge end of the drying chamber, a rotary blade for stirring the raw material is provided in the granulating chamber, and the drying chamber and the granulating chamber Thus, a configuration was adopted in which an annular partition plate was provided at the boundary with.
[0010]
That is, an annular partition plate is provided at the boundary between the granulating chamber and the drying chamber, the massive soil supplied from the kneading step is stored in the granulating chamber for a certain period of time, and the massive soil is provided by the rotating blades provided in the granulating chamber. Since the crushed chunks were finely crushed into chunks having a predetermined size or less, the crushed chunks were rolled to take corners, and the rounded granular soil overflowed from the partition plate and sent to the drying chamber. is there. In addition, since the rotating blades knead and soften the massive soil, it has an effect of forming a granular soil having a smooth roundness.
[0011]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, an embodiment of the present invention will be described with reference to FIGS. 1 to 3 show general views of a granulating and drying apparatus. 1 is a front view, FIG. 2 is a plan view, and FIG. 3 is a side view. This granulation drying apparatus is provided in a cylindrical drying chamber 1 that is driven to rotate, a cylindrical granulation chamber 2 that is also connected to the inlet end of the drying chamber 1, and a granulation chamber 2. It is basically composed of a rotating blade 3, a hopper 4 for supplying a massive kneaded soil to the granulation chamber 2, and an outlet hood 6 provided at an outlet end 5 of the drying chamber 1 for discharging the dried granular soil. I have.
[0012]
The drying chamber 1 and the granulation chamber 2 are formed by an integral rotary drum 7 having both ends opened. An annular partition plate 8 is provided at the boundary between the drying chamber 1 and the granulation chamber 2 on the inner periphery of the rotary drum 7. A sprocket 9 and two tires 10 are mounted on the outer periphery of the rotating body 7. The rotating drum 7 has two pairs of rollers 13 mounted on a gantry 11 via bearings 12 and supports each of the tires 10, and a sprocket 15 and a sprocket 15 mounted on a rotating shaft of a motor 14 with a speed reducer. The chain 9 is driven to rotate by a chain 16 wound therearound.
[0013]
A plurality of heating tubes 17 are passed through the drying chamber 1 in the axial direction near the inner peripheral wall. These heating tubes 17 are connected to a steam pipe 19 via a rotary joint 18 attached to the outlet hood 6 and heat the drying chamber 1 with steam supplied from the steam pipe 19. Therefore, high thermal efficiency can be secured. In addition, a drain pipe 20 is also attached to the steam pipe 19.
[0014]
An inlet hood 21 is provided on the side of the granulation chamber 2 of the rotary drum 7, and both ends of the rotary drum 7 are opened into the inlet hood 21 and the outlet hood 6. The inlet hood 21 is also provided with a gas supply port 22 described later and a raw material outlet 23 for cleaning.
[0015]
The rotary blade 3 is connected to a rotary shaft 26 by a flange 24 and a tightening bolt / nut 25 so that the rotary blade 3 can be replaced with another type of rotary blade. The rotating shaft 26 is taken out to the outside through the inlet hood 21, supported by two bearings 27 mounted on the gantry 11, and connected to a rotating shaft of a motor 29 by a coupling 28.
[0016]
As shown in FIGS. 4 (a) and 4 (b), the rotating blades 3 are arranged at a lower portion of the rotating drum 7, and four paddle-shaped wings 30 are provided at regular intervals in the axial direction and perpendicular to the rotating direction. Each is provided radially. These rotary blades 3 are rotated in a direction opposite to the rotation direction of the rotary drum 7, and crush the massive kneaded soil 31 rolling at the lower part of the granulation chamber 2. By rotating the rotary blades 3 in the direction opposite to that of the rotary drum 7, the kneaded soil 31 moving together with the rotary drum 7 can be efficiently crushed from the opposite direction.
[0017]
The rounded granular soil that is crushed by the rotating blades 3 and tumbles while overflowing is overflowed from the partition plate 8 and sent into the drying chamber 1. At this time, the kneaded soil 31 that has not been sufficiently granulated has poor fluidity, and the fine kneaded soil 31 penetrates under the large kneaded soil 31, so that the partition plate 8 cannot overflow and the granulated soil 31 is not sufficiently granulated. Only the granular soil that has overflowed will overflow. Therefore, even if the length of the granulation chamber 2 is short, a sufficient granulation action is performed. Further, by changing the number of rotations of the rotary blades 3, the degree of crushing can be adjusted to change the size of the granular soil to be produced. By changing the rotation speed of the rotating blades 3 according to the physical properties of the kneaded soil 31 to be supplied, a granular soil of a certain size can be obtained without being affected by the physical properties of the kneaded soil 31.
[0018]
The granular soil fed into the drying chamber 1 is heated and dried by the heating tube 17 while rolling in the drying chamber 1, and sent out from the outlet end 5 to the outlet hood 6. The outlet hood 6 is provided with a gas outlet 32 for discharging the gas supplied from the gas supply port 22 of the inlet hood 21 so that the gas generated from the granular soil is discharged to the outside of the apparatus. It has become. The dried granular soil is discharged from an outlet 33 provided below the outlet hood 6.
[0019]
FIGS. 5A and 5B show another form of the rotating blade 34. The rotating blades 34 are provided with four blade-shaped blades 35 parallel to the rotating direction radially at regular intervals in the axial direction. Since the rotating blades 34 shear the kneaded soil, they are suitable for crushing hard kneaded soil.
[0020]
In the above-mentioned embodiment, paddle-shaped and blade-shaped blades are shown as rotary blades for crushing massive kneaded soil, but as a blade having an intermediate function between them, a blade body inclined with the rotation direction is provided. Propeller-shaped rotating blades can also be employed. Further, the number of wings arranged radially can be arbitrarily selected.
[0021]
【The invention's effect】
As described above, the granulation drying apparatus of the present invention provides an annular partition plate at the boundary between the granulation chamber and the drying chamber, and collects the bulk soil supplied from the kneading step in the granulation chamber for a certain period of time. The crushed mass is finely crushed into lumps having a predetermined size or less by rotating blades provided in the granulation chamber, and the crushed lumps are rolled to form a corner, and the rounded granular soil is separated from the partition plate. Since it overflows and is sent to the drying chamber, it is possible to supply a dry granular soil in which the grains are aligned to a predetermined size or less. In addition, since the rotating blades also have a function of kneading and softening the massive soil, it is possible to supply a dry granular soil having a smoother roundness.
[Brief description of the drawings]
1 is a partially cutaway front view showing an embodiment of a granulating and drying apparatus; FIG. 2 is a plan view of FIG. 1; FIG. 3 is a vertical side view taken along line III-III of FIG. 2; 1 is an enlarged sectional view of a main part of FIG. 1, b is a sectional view taken along line IV-IV of a. FIG. 5 is a front view showing a rotating blade of another embodiment, and b is a longitudinal side view thereof. Longitudinal sectional view showing a conventional granulation drying apparatus [Explanation of reference numerals]
REFERENCE SIGNS LIST 1 drying room 2 granulation room 3 rotating blades 4 hopper 5 outlet end 6 outlet hood 7 rotating drum 8 partition plate 9 sprocket 10 tire 11 gantry 12 bearing 13 roller 14 motor 15 sprocket 16 chain 17 heating tube 18 rotary joint 19 steam pipe 20 Drain pipe 21 Inlet hood 22 Supply port 23 Outlet port 24 Flange 25 Bolt and nut 26 Rotating shaft 27 Bearing 28 Coupling 29 Motor 30 Blade body 31 Kneaded soil 32 Discharge port 33 Removal port 34 Rotating blade 35 Blade body 41 Hopper 42 Screw feeder 43 Rotary dryer 44 Granulator 45 Extraction chamber 46 Exhaust chamber 47 Scraper 48 Jacket 49 Extraction port 50 Supply port 51 Discharge port

Claims (1)

概ね水平に配置され、回転駆動される円筒状の乾燥室の原料供給端側に、同じく円筒状の造粒室が継足され、この造粒室に供給された原料を造粒乾燥して、前記乾燥室の排出端から排出する造粒乾燥装置において、前記造粒室に、原料を攪拌する回転羽根を設け、前記乾燥室と造粒室との境界に環状の仕切板を設けたことを特徴とする造粒乾燥装置。A generally cylindrical granulation chamber is added to the raw material supply end side of the cylindrical drying chamber that is arranged substantially horizontally and is driven to rotate, and the raw material supplied to the granulation chamber is granulated and dried. In the granulation drying apparatus discharged from the discharge end of the drying chamber, a rotating blade for stirring the raw material is provided in the granulation chamber, and an annular partition plate is provided at a boundary between the drying chamber and the granulation chamber. Granulation and drying equipment.
JP21766198A 1998-07-31 1998-07-31 Granulation drying equipment Expired - Lifetime JP3569131B2 (en)

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JP21766198A JP3569131B2 (en) 1998-07-31 1998-07-31 Granulation drying equipment

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Application Number Priority Date Filing Date Title
JP21766198A JP3569131B2 (en) 1998-07-31 1998-07-31 Granulation drying equipment

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JP3569131B2 true JP3569131B2 (en) 2004-09-22

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Publication number Priority date Publication date Assignee Title
JP2002361065A (en) * 2001-06-05 2002-12-17 Taiheiyo Kiko Kk Apparatus for treating powder and granular material or the like
JP6003463B2 (en) * 2012-09-24 2016-10-05 Jsr株式会社 Method for producing solid fuel
CN108059319A (en) * 2017-12-07 2018-05-22 洪作娟 Bio-fertilizer dewatered drying system
CN108112790A (en) * 2018-02-12 2018-06-05 费军 A kind of automation feed processing granulation device
CN109607724B (en) * 2019-02-21 2021-11-09 新疆德安环保科技股份有限公司 Integrated flocculation and precipitation device
CN113758183B (en) * 2021-09-03 2022-12-13 泉州市交发泓盛材料科技有限责任公司 Aggregate drying roller and drying method for dry-mixed mortar production line

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