JPH0423585B2 - - Google Patents

Info

Publication number
JPH0423585B2
JPH0423585B2 JP21344186A JP21344186A JPH0423585B2 JP H0423585 B2 JPH0423585 B2 JP H0423585B2 JP 21344186 A JP21344186 A JP 21344186A JP 21344186 A JP21344186 A JP 21344186A JP H0423585 B2 JPH0423585 B2 JP H0423585B2
Authority
JP
Japan
Prior art keywords
sieve
cwm
water
cleaning
coarse
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.)
Expired
Application number
JP21344186A
Other languages
Japanese (ja)
Other versions
JPS6369550A (en
Inventor
Tatsuo Hagiwara
Yoshio Kuwamura
Shunkai Fujimoto
Yasutomo Tomura
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP21344186A priority Critical patent/JPS6369550A/en
Publication of JPS6369550A publication Critical patent/JPS6369550A/en
Publication of JPH0423585B2 publication Critical patent/JPH0423585B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、高濃度石炭・水スラリー中の粗粒子
の分離に用いられる振動篩の洗浄方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for cleaning a vibrating sieve used for separating coarse particles in a highly concentrated coal/water slurry.

[従来の技術] 高濃度の石炭・水スラリー(以下、「CWM」
と記す。)は、微粉砕した石炭と水とに若干の添
加剤を加えた石炭濃度60重量%以上の混合物で、
直接燃焼可能な燃料であり、その燃焼性、輸送性
及び貯蔵性などを満足させるため、150μm以上の
粗粒子の含有率を低減させることが求められてお
り、湿式ボールミルなどで調製される高濃度
CWM中から粗粒子を除去するには、通常、振動
篩を用いた湿式篩分け方法がとられている。
[Conventional technology] Highly concentrated coal/water slurry (hereinafter referred to as “CWM”)
It is written as ) is a mixture of finely ground coal and water with a coal concentration of 60% by weight or more, with some additives added.
It is a fuel that can be directly combusted, and in order to satisfy its flammability, transportability, and storage properties, it is required to reduce the content of coarse particles of 150 μm or more.
To remove coarse particles from CWM, a wet sieving method using a vibrating sieve is usually used.

上記湿式篩分け方法は、高濃度CWMを傾斜し
た振動篩の上端部に供給し、篩面に直角方向の面
内において振幅の小さい高速度の振動を与えるこ
とにより、高濃度CWMが跳躍やすべりを繰り返
されつつ篩面を下降する間に篩分けされ、篩上産
物である高濃度粗粒CWMと篩下産物である所望
の高濃度微粒CWMとに分離され高濃度粗粒
CWMが振動篩の下端部から排出されるものであ
る。
The wet sieving method described above supplies high-concentration CWM to the upper end of an inclined vibrating sieve and applies high-velocity vibration with small amplitude in a plane perpendicular to the sieve surface, thereby preventing the high-concentration CWM from jumping or sliding. The process is repeated while moving down the sieve surface, and the high concentration coarse particles are separated into high-concentration coarse CWM, which is a product on the sieve, and desired high-concentration fine CWM, which is a product under the sieve.
CWM is discharged from the bottom end of the vibrating sieve.

しかしながら、上記湿式篩分け方法では、篩の
目開きが微小であるため、高粘度を呈する高濃度
CWMが篩面上を移動する際に、篩面に付着し、
その進展に伴つて篩目の開口を減少させ、ついに
は開口を閉塞させてしまい、高濃度CWM中から
の粗粒子の分離が不可能となつてしまうので、従
来、洗浄水を多数の散水ノズルにより定期的に又
は必要に応じて篩面の上方から篩面全面に及んで
同時に噴射して篩目を洗浄する方法が行われてい
る。
However, in the above-mentioned wet sieving method, the opening of the sieve is minute, so high concentrations that exhibit high viscosity are
When CWM moves on the sieve surface, it attaches to the sieve surface,
As this progresses, the openings of the sieve meshes decrease and eventually become blocked, making it impossible to separate coarse particles from the highly concentrated CWM. Therefore, a method of cleaning the sieve meshes is carried out by simultaneously spraying from above the sieve surface to the entire sieve surface periodically or as needed.

[発明が解決しようとする問題点] しかしながら、上記従来の洗浄方法によれば、
多量の洗浄水を使用する割には洗浄効果があがら
ない問題がある。
[Problems to be Solved by the Invention] However, according to the above conventional cleaning method,
There is a problem that the cleaning effect is not improved even though a large amount of cleaning water is used.

これは、篩面上の上部において希釈洗浄された
粗粒CWMの流下が、その下方で噴射される洗浄
水によつて妨げられるためと考えられる。
This is thought to be because the flow of the coarse CWM diluted and washed above the sieve surface is blocked by the washing water sprayed below.

そこで、本発明は、比較的少量の洗浄水により
大きな洗浄効果をあげ得るようにした高濃度
CWM用振動篩の洗浄方法を提供しようとするも
のである。
Therefore, the present invention has developed a high-concentration solution that can achieve a large cleaning effect with a relatively small amount of cleaning water.
The present invention attempts to provide a method for cleaning a vibrating screen for CWM.

[問題点を解決するための手段] 前記問題点を解決するため、本発明は、高濃度
CWMの湿式篩分けにより目詰まりした振動篩の
篩目を水洗浄するに際し、篩面の上部から下部に
亘つて順次洗浄水を篩面の上方から局部的に噴射
して篩目を洗浄する方法である。
[Means for Solving the Problems] In order to solve the above problems, the present invention provides high concentration
A method of cleaning the sieve mesh of a vibrating sieve that has become clogged due to CWM wet sieving by spraying cleaning water locally from above the sieve surface sequentially from the top to the bottom of the sieve surface. It is.

[作 用] 上記手段によれば、篩面の上部から下部に亘つ
て順次局部的に噴射される洗浄水により洗浄希釈
された粗粒CWMは、その洗浄部分より下部の篩
面上に付着した高濃度粗粒CWM上を流下して篩
面上の下端部から機外に落下排出され、篩目が上
部から下部に向つて順次洗浄される。
[Function] According to the above means, the coarse CWM that has been washed and diluted by the washing water that is sequentially locally sprayed from the top to the bottom of the sieve surface adheres to the sieve surface below the washed part. It flows down over the highly concentrated coarse grain CWM and is discharged from the lower end of the sieve surface to the outside of the machine, and the sieve mesh is washed sequentially from the top to the bottom.

[実施例] 以下、本発明の一実施例を図面に基づいて説明
する。
[Example] Hereinafter, an example of the present invention will be described based on the drawings.

第1図、第2図は本発明の実施に供した粗粒分
離装置の概略構成を示す側面図、正面図である。
FIG. 1 and FIG. 2 are a side view and a front view showing a schematic configuration of a coarse particle separator used for carrying out the present invention.

図において1は傾斜した振動篩で、振動篩1
は、方形の篩枠2と、篩枠2内に張設された目開
き0.5〜0.8mmの篩網(篩面)3と、篩網3を小振
幅、高振動数で振動させる発振機4とからなり、
発振器4は、取付台5を介して篩枠2の中間上部
に取り付けられると共に、伝達子6を介して篩網
3と連結されている。
In the figure, 1 is a tilted vibrating sieve, vibrating sieve 1
The sieve frame 2 includes a rectangular sieve frame 2, a sieve screen (sieve surface) 3 with a mesh opening of 0.5 to 0.8 mm stretched inside the sieve frame 2, and an oscillator 4 that vibrates the sieve screen 3 at a small amplitude and high frequency. It consists of
The oscillator 4 is attached to the middle upper part of the sieve frame 2 via a mounting base 5 and is connected to the sieve screen 3 via a transmitter 6.

振動篩1の上端部(第1図においては右端部)
の上方には、図示しない湿式ボールミルなどから
供給される高濃度CWMを篩網3の幅方向(第2
図おける左右方向)に均等に供給する供給樋7が
配設されている。又、振動篩1の上方には、篩網
3の幅方向に延在する複数(第1図においては4
本)の給水管8a,8b,8c,8dが、振動篩
1の傾斜に沿い上下方向に適宜に離隔して配設さ
れており、それぞれの給水管8a,8b,8c,
8dには、洗浄水を噴射する複数の散水ノズル9
a,9b,9c,9dが取り付けられている。な
お、各散水ノズル9a,9b,9c,9dは、図
おいて2点鎖線で示す散水時のフルコーンが篩面
3上で互いに重畳するように設けられている。そ
して、各給水管8a,8b,8c,8dは、タイ
マー10a,10b,10c,10dによつて
入・切される電磁弁11a,11b,11c,1
1dを介して、加圧水源(図示せず)と接続した
ヘツダ12と接続されている。
Upper end of vibrating sieve 1 (right end in Figure 1)
Above the sieve screen 3, high-concentration CWM supplied from a wet ball mill or the like is placed in the width direction of the sieve screen 3 (second
A supply gutter 7 is disposed to supply water evenly in the left-right direction in the figure. Further, above the vibrating sieve 1, a plurality of (in FIG. 1, four
The water supply pipes 8a, 8b, 8c, and 8d are arranged at appropriate distances in the vertical direction along the inclination of the vibrating sieve 1, and the water supply pipes 8a, 8b, 8c, and
At 8d, a plurality of water nozzles 9 that spray cleaning water are provided.
a, 9b, 9c, and 9d are attached. The water spray nozzles 9a, 9b, 9c, and 9d are provided so that their full cones during water spraying, indicated by two-dot chain lines in the figure, overlap each other on the sieve surface 3. Each water supply pipe 8a, 8b, 8c, 8d is connected to a solenoid valve 11a, 11b, 11c, 1 which is turned on/off by a timer 10a, 10b, 10c, 10d.
1d to a header 12 which is connected to a source of pressurized water (not shown).

一方、振動篩1の下方には、篩下産物である高
濃度微粒CWMを貯留タンク13に案内するガイ
ドホツパー14が配設されており、ガイドホツパ
ー14内の上部には、混入防止板15が配置され
ている。混入防止板15は、篩目の水洗浄時に篩
網3を通る希釈CWMが貯留タンク13内の高濃
度微粒CWMと混入するのを防止するもので、上
端縁を軸16により枢支され、かつその裏面とベ
ース17との間に介装した油圧シリンダー18の
ピストンロツド18aの伸縮により第1図におい
て実線で示す位置と2点鎖線で示す位置とに揺動
可能に設けられている。
On the other hand, a guide hopper 14 is disposed below the vibrating sieve 1 to guide high-concentration particulate CWM, which is a product under the sieve, to a storage tank 13, and a contamination prevention plate 15 is disposed above the guide hopper 14. ing. The mixing prevention plate 15 prevents the diluted CWM passing through the sieve screen 3 from mixing with the high-concentration fine CWM in the storage tank 13 during water washing of the sieve mesh, and has an upper edge pivotally supported by a shaft 16. The piston rod 18a of the hydraulic cylinder 18 interposed between the back surface and the base 17 expands and contracts to be able to swing between the position shown by the solid line and the position shown by the two-dot chain line in FIG.

又、振動篩1の下端部側方には、スクリユーコ
ンベヤ19を装入した樋20が配設されており、
樋20の端部には高濃度粗粒CWMと洗浄CWN
(水洗浄時の篩上産物と篩下産物とが混合したも
の)とを粗粒回収タンク21と排水ピツト22と
に切り換えて案内する切換ホツパー23が配設さ
れている。切換ホツパー23には、高濃度粗粒
CWM排出口23aと洗浄CWM排出口23bと
が設けられており、この切換ホツパー23内に
は、両排出口23a,23bを開閉切り換えする
切換板24が、第1図において実線で示す位置と
2点鎖線で示す位置とに揺動可能に設けられてい
る。
Further, on the side of the lower end of the vibrating screen 1, a gutter 20 into which a screw conveyor 19 is inserted is arranged.
High concentration coarse grain CWM and cleaning CWN are placed at the end of the gutter 20.
A switching hopper 23 is provided to switch and guide the sieved product (a mixture of the sieved product and the sieved product during water washing) to the coarse particle collection tank 21 and the drainage pit 22. The switching hopper 23 contains highly concentrated coarse particles.
A CWM discharge port 23a and a cleaning CWM discharge port 23b are provided, and within this switching hopper 23, a switching plate 24 for switching the opening and closing of both discharge ports 23a and 23b is located at the position shown by the solid line in FIG. It is provided so as to be able to swing to the position shown by the dotted chain line.

なお、排水ピツト22に排水された洗浄CWM
は、ポンプ26を介して廃水タンク(図示せず)
に送られるものである。又、第2図において25
は振動篩1の篩枠2とガイドホツパー14の上端
部との間に介装したベローズである。
In addition, the cleaning CWM drained into the drain pit 22
is connected to a wastewater tank (not shown) via pump 26.
It is sent to. Also, in Figure 2, 25
is a bellows interposed between the sieve frame 2 of the vibrating sieve 1 and the upper end of the guide hopper 14.

上記構成の粗粒分離装置においては、混入防止
板15及び切換板24をそれぞれ2点鎖線で示す
位置に揺動させると共に、供給樋7から高濃度
CWMを振動篩1に供給すると、高濃度CWMは、
跳躍やすべりを繰り返されつつ篩面3を下降する
間に篩分けされ、篩上産物である高濃度粗粒
CWMと篩下産物である高濃度微粒CWMとに分
離される。高濃度粗粒CWMは、振動篩1の篩枠
2の下端部に設けられた排出口2aから樋20内
に落下し、スクリユーコンベヤ19により運ばれ
て切換ホツパー23内に落下すると共に、その高
濃度粗粒CWM排出口23aを経て粗粒回収タン
ク21内に貯留される一方、高濃度微粒CWM
は、ガイドホツパー14を経て貯留タンク13に
貯留される。
In the coarse particle separator having the above configuration, the contamination prevention plate 15 and the switching plate 24 are swung to the positions shown by the two-dot chain lines, and the high concentration
When CWM is supplied to the vibrating sieve 1, the high concentration CWM is
Highly concentrated coarse grains, which are sieved products, are sieved while descending the sieve surface 3 while repeating jumping and sliding.
It is separated into CWM and highly concentrated fine CWM, which is a subsieve product. The highly concentrated coarse grain CWM falls into the gutter 20 from the discharge port 2a provided at the lower end of the sieve frame 2 of the vibrating sieve 1, is carried by the screw conveyor 19, falls into the switching hopper 23, and then While the high concentration coarse particle CWM is stored in the coarse particle collection tank 21 through the high concentration coarse particle CWM discharge port 23a, the high concentration fine particle CWM
is stored in the storage tank 13 via the guide hopper 14.

しかして、上記湿式篩分けにより振動篩1の篩
網3が目詰まりした場合には、供給樋7からの高
濃度CWMの供給を停止し、かつ混入防止板15
及び切換板24を実線で示す位置に揺動する。つ
いで、タイマー10aにより電磁弁11aを作動
させ、ヘツダ12から最上段の給水管8aに洗浄
水を送水し、給水管8aの各散水ノズル9aから
洗浄水を所要時間(例えば約15秒)噴出させる。
ついで、最上段の給水管8aの各散水ノズル9a
からの散水を停止し、タイマー10bにより電磁
弁11bを作動させ、第2段の給水管8bの各散
水ノズル9bから洗浄水を同様の時間噴出させて
停止する。以下、同様に第3段及び最下段の給水
管8c,8dの各散水ノズル9c,9dから順次
同様の時間洗浄水を噴出させる。上記洗浄は、発
振機4を作動させ、篩網3を振動させた状態で行
う。
If the sieve screen 3 of the vibrating sieve 1 becomes clogged due to the wet sieving, the supply of high concentration CWM from the supply gutter 7 is stopped, and the contamination prevention plate 15
Then, the switching plate 24 is swung to the position shown by the solid line. Next, the solenoid valve 11a is activated by the timer 10a, and the cleaning water is sent from the header 12 to the uppermost water supply pipe 8a, and the cleaning water is spouted from each water spray nozzle 9a of the water supply pipe 8a for the required time (for example, about 15 seconds). .
Next, each water nozzle 9a of the uppermost water supply pipe 8a
The solenoid valve 11b is activated by the timer 10b, and the cleaning water is spouted from each water nozzle 9b of the second stage water supply pipe 8b for the same period of time, and then stopped. Thereafter, cleaning water is sequentially spouted for the same period of time from the water spray nozzles 9c and 9d of the third and lowest water supply pipes 8c and 8d. The above cleaning is performed while the oscillator 4 is activated and the sieve screen 3 is vibrated.

上記各段の給水管8a,8b,8c,8dのそ
れぞれの散水ノズル9a,9b,9c,9dから
の段階的な散水により、篩面上に付着した高濃度
粗粒CWMは、粘度が低下した粗粒CWM(篩上産
物)と濃度が低下した希釈CWM(篩下産物)と
なり、粗粒CWMは、その洗浄部分より下部の篩
面上に付着した高濃度粗粒CWM上を流下して排
出口2aから樋20内に落下する一方、希釈
CWMは、混入防止板15上を流下して同様に樋
20内に落下する。樋20内に落下した粗粒
CWMと希釈CWMは、洗浄CWMとなり、樋2
0の端部から切換ホツパー23内に落下すると共
に、切換板24により洗浄CWM排出口23bか
ら排水ピツト22内に排出され、ポンプ25によ
り廃水タンクに送られる。
Due to the stepwise water sprinkling from the water nozzles 9a, 9b, 9c, and 9d of the water supply pipes 8a, 8b, 8c, and 8d in the above-mentioned stages, the viscosity of the highly concentrated coarse particles CWM adhering to the sieve surface decreased. The resulting products are coarse CWM (upper sieve product) and diluted CWM (lower sieve product), and the coarse CWM flows down onto the highly concentrated coarse CWM that adheres to the sieve surface below the washed part and is discharged. While falling into the gutter 20 from the outlet 2a, the diluted
The CWM flows down on the mixing prevention plate 15 and similarly falls into the gutter 20. Coarse particles that fell into the gutter 20
CWM and diluted CWM become cleaning CWM and gutter 2
The water falls into the switching hopper 23 from the end of the cleaning CWM, and is discharged from the cleaning CWM outlet 23b into the drainage pit 22 by the switching plate 24, and is sent to the waste water tank by the pump 25.

したがつて、振動篩1の篩目は、比較的少量の
洗浄水で短時間に、上部から下部に向つて順次局
部的(段階的)に洗浄される。
Therefore, the sieve mesh of the vibrating sieve 1 is sequentially and locally (stepwise) washed from the top to the bottom in a short time with a relatively small amount of washing water.

なお、上記実施例においては、篩面の上部から
下部に亘つて順次洗浄水を篩面の上部から局部的
に噴射して篩目を洗浄するため、複数の散水ノズ
ル9a,9b,9c,9dを有する複数の給水管
8a,8b,8c,8dを篩面の上方に配置した
が、複数の散水ノズルを有する幅方向の単一の給
水管を篩面に沿つて上下動可能に設け、この給水
管を間欠的に移動して洗浄するようにしてもよ
い。
In the above embodiment, in order to locally spray washing water from the upper part of the sieve surface to the lower part of the sieve surface to clean the sieve meshes, a plurality of water spray nozzles 9a, 9b, 9c, 9d are used. Although a plurality of water supply pipes 8a, 8b, 8c, and 8d having water spray nozzles are arranged above the sieve surface, a single water supply pipe in the width direction having a plurality of water nozzles is provided so as to be movable up and down along the sieve surface. The water supply pipe may be moved and cleaned intermittently.

[発明の効果] 以上のように本発明によれば、篩面の上部から
下部に亘つて順次局部的に噴射される洗浄水によ
り洗浄希釈された粗粒CWMは、その洗浄部分よ
り下部の篩面上に付着した高濃度粗粒CWM上を
流下して篩面上の下端部から機外に落下排出さ
れ、篩目が上部から下部に向つて順次洗浄される
ので、従来のように粗粒CWMの流下が妨げられ
ることがなく、比較的少量の洗浄水で、しかも短
時間に篩目の洗浄を行うことができ、洗浄効果を
大幅に向上することができる。
[Effects of the Invention] As described above, according to the present invention, coarse CWM washed and diluted by washing water sequentially and locally sprayed from the upper part to the lower part of the sieve surface is removed from the sieve below the washing part. The highly concentrated coarse particles CWM that adheres to the surface flow down and are discharged from the lower end of the sieve surface to the outside of the machine, and the sieve mesh is washed sequentially from the top to the bottom, so coarse particles are The flow of CWM is not obstructed, and the sieve mesh can be cleaned in a short time with a relatively small amount of cleaning water, greatly improving the cleaning effect.

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

第1図、第2図はそれぞれ本発明の実施に供し
た粗粒分離装置の概略構成を示す側面図、正面図
である。 1…振動篩、3…篩網(篩目)、4…発振機、
6…伝達子、7…供給樋、8a,8b,8c,8
d…給水管、9a,9b,9c,9d…散水ノズ
ル、10a,10b,10c,10d…タイマ
ー、11a,11b,11c,11d…電磁弁、
12…ヘツダ。
FIG. 1 and FIG. 2 are a side view and a front view, respectively, showing the schematic configuration of a coarse particle separator used for carrying out the present invention. 1... Vibrating sieve, 3... Sieve mesh (sieve mesh), 4... Oscillator,
6...Transmitter, 7...Supply gutter, 8a, 8b, 8c, 8
d... Water supply pipe, 9a, 9b, 9c, 9d... Water nozzle, 10a, 10b, 10c, 10d... Timer, 11a, 11b, 11c, 11d... Solenoid valve,
12...Hetsuda.

Claims (1)

【特許請求の範囲】[Claims] 1 高濃度石炭・水スラリーの湿式篩分けにより
目詰まりした振動篩の篩目を水洗浄するに際し、
篩面の上部から下部に亘つて順次洗浄水を篩面の
上方から局部的に噴射して篩目を洗浄することを
特徴とする高濃度石炭・水スラリー用振動篩の洗
浄方法。
1. When cleaning the sieve mesh of a vibrating sieve that has become clogged due to wet sieving of highly concentrated coal/water slurry,
A method for cleaning a vibrating sieve for highly concentrated coal/water slurry, characterized in that washing water is sequentially locally sprayed from above the sieve surface to clean the sieve meshes from the top to the bottom of the sieve surface.
JP21344186A 1986-09-10 1986-09-10 Method for washing vibrating screen for concentrated coal-water slurry Granted JPS6369550A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21344186A JPS6369550A (en) 1986-09-10 1986-09-10 Method for washing vibrating screen for concentrated coal-water slurry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21344186A JPS6369550A (en) 1986-09-10 1986-09-10 Method for washing vibrating screen for concentrated coal-water slurry

Publications (2)

Publication Number Publication Date
JPS6369550A JPS6369550A (en) 1988-03-29
JPH0423585B2 true JPH0423585B2 (en) 1992-04-22

Family

ID=16639281

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21344186A Granted JPS6369550A (en) 1986-09-10 1986-09-10 Method for washing vibrating screen for concentrated coal-water slurry

Country Status (1)

Country Link
JP (1) JPS6369550A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100433754B1 (en) * 2001-10-29 2004-06-04 한국전력공사 Cleaning method of Contaminated Ion Exchange Resin
JP2008253962A (en) * 2007-04-09 2008-10-23 As One Corp Holding stand
CN106334666A (en) * 2016-09-20 2017-01-18 中交天津港航勘察设计研究院有限公司 Graded careful choosing method and device for sea sand
CN106423972A (en) * 2016-10-27 2017-02-22 南丹县联丰矿业有限公司 Ore washing system

Also Published As

Publication number Publication date
JPS6369550A (en) 1988-03-29

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