JPS5820202A - Purification apparatus by pulverization - Google Patents

Purification apparatus by pulverization

Info

Publication number
JPS5820202A
JPS5820202A JP12025281A JP12025281A JPS5820202A JP S5820202 A JPS5820202 A JP S5820202A JP 12025281 A JP12025281 A JP 12025281A JP 12025281 A JP12025281 A JP 12025281A JP S5820202 A JPS5820202 A JP S5820202A
Authority
JP
Japan
Prior art keywords
pipe
solvent
hollow container
purified
waste liquid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP12025281A
Other languages
Japanese (ja)
Inventor
Seiichi Sakuma
佐久間 清一
Tadashi Fujii
藤井 唯士
Tomoyuki Yamaguchi
山口 友行
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.)
Ricoh Co Ltd
Original Assignee
Ricoh Co 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 Ricoh Co Ltd filed Critical Ricoh Co Ltd
Priority to JP12025281A priority Critical patent/JPS5820202A/en
Publication of JPS5820202A publication Critical patent/JPS5820202A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To continuously carry out the supply purification, drying, grinding of a stock material and the taking-out of purified pulverized product, by successively carrying out the charge of a solvent, the stirring thereof, the supply of a stock solution, the discharge of the solvent, the grinding of a purified solid substance and the discharge of the ground purified substance. CONSTITUTION:A stock solution is quantitatively supplied from a pipe 6 by a fixed delivery pump 7 while a solvent poured into a hollow container 1 by a pressurizing apparatus 11 is stirred by a shaft 3' and a propeller 3. On the other hand, the waste liquid sump 13 is evacutaed by a vacuum pump 14 to store a waste liquid in said sump 13 and the pressure reduction of the waste liquid sump 13 is subsequently stopped. In the next stage, while pressure is reduced by the pump 14, a purified solid substance is ground by rotating the shaft 3' and the propeller 3 and, at the same time, the obtained purified powder is dried while air is sent from an air sending pipe 8. After the reduced pressure of the waste liquid sump 13 is restored, the powdery purified substance is taken out from a pipe 9. At last, a solvent is again poured from a pipe 10, after the propeller 3 is rotated, and the solvent is discharged to wash the hollow container 1.

Description

【発明の詳細な説明】 本発明は、粉体を精製する粉体化精製装置に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a powder refining device for refining powder.

従来、粉体を精製する方法として、ソッ゛クスレー抽出
方法が知られている。この方法は、濾過フィルタを設け
−た容器に原料粉体を入れ、これを最下方連通管に接続
し、この最下方連通管の注液孔より下方に一方の孔を設
け、最下方連通管の上方に他方の孔を設けた蒸気上昇通
路を接続し、この蒸気上昇通路の上方の孔よりも上方に
冷却部を有し、蒸気上昇通路の下方の孔よりも下方に液
部を設けた装置において、液部を加熱して蒸発した液体
を蒸気上昇通路より冷却部に導びき、この冷却部で冷却
し、この冷却された液体で粉体を洗浄してから連通管か
ら排出するもので、高純度の洗浄液で繰り返し粉体の精
製を行なっている。
Conventionally, the Soxhlet extraction method has been known as a method for refining powder. In this method, raw material powder is placed in a container equipped with a filtration filter, connected to the lowest communicating pipe, one hole is provided below the liquid injection hole in the lowest communicating pipe, and the raw material powder is placed in a container equipped with a filtration filter. A steam rising passage with another hole provided above is connected, a cooling part is provided above the hole above the steam rising passage, and a liquid part is provided below the hole below the steam rising passage. In the device, the liquid part is heated and the evaporated liquid is led to the cooling part through the vapor rise passage, cooled in this cooling part, and the powder is washed with this cooled liquid before being discharged from the communication pipe. The powder is repeatedly purified using a high-purity cleaning solution.

しかしながら、この方法はバッチ方式であるため、粉体
の供給、取出し及び装置の組立て準備を1回の精製ごと
にiなう必要があり、従って、この方法で・は、1つの
装置で原料供給から排液工程までの精製を一環して得る
ことはできず、更に攪拌工程がないために1.一定洗浄
液量当りの精製効率が悪いという欠点があり、精製のバ
ラツキが大きいという欠点があった。
However, since this method is a batch method, it is necessary to perform powder supply, removal, and equipment assembly preparation for each refining process. It is not possible to obtain the purification process from 1. to the drainage process in one step, and there is no stirring process. This method has the drawbacks of poor purification efficiency per fixed amount of cleaning liquid and large variations in purification.

本発明は、上記従来例の欠点を解消するために、中空容
器に濾過フィルタ赤設けられ、濾過フィルタの上部に回
転翼が設けられ、濾過フィルタの上部の、中空容器の側
壁に開閉手段を有する第1.°第、2の管と、晶フィル
タの上部に接して中空容器の側壁に設けられた第3の管
と、濾過フィルタの下部の中空容器の側壁に設けられた
開閉手段を有する第4の管と、中空容器の下部に設けら
れた第5の管とからなり、第2の管に接続された定容量
ポンプで溶液化された粉体化原料が定容量供給され、回
転繭は中空容器の最上部の孔を通るシャツ ′トに接続
され、シャフトをモータで回転することにより粉体化原
料が攪拌され、また精製固形分が粉砕され、第1の管か
ら気体が送風されて精製粉体の乾燥及びこの精製粉体の
取り、出しを行ない、第4の管に加圧ポンプが接続され
て粉体化原料を精製する溶剤が供給され、第5の管に接
続された真空ポンプで精製後の排液を除去することを特
徴−とじ、その目的は精−ごとに装置の組立準備を必要
とせず、原料の供給、″精製、乾燥、粉砕、精製を提供
するものである。以下、図面により実施例を詳細に説明
する。
In order to eliminate the drawbacks of the above-mentioned conventional examples, the present invention provides a hollow container with a filtration filter, a rotating blade on the upper part of the filtration filter, and an opening/closing means on the side wall of the hollow container on the upper part of the filtration filter. 1st. ° A second pipe, a third pipe provided on the side wall of the hollow container in contact with the upper part of the crystal filter, and a fourth pipe having an opening/closing means provided on the side wall of the hollow container below the filtration filter. and a fifth pipe installed at the bottom of the hollow container. A fixed volume pump connected to the second pipe supplies a fixed volume of the solutionized powdered raw material, and the rotating cocoon is rotated through the hollow container. The shaft is connected to the shirt shaft passing through the hole at the top, and by rotating the shaft with a motor, the powdered raw material is stirred, the refined solid content is crushed, and gas is blown through the first pipe to form the refined powder. A pressure pump is connected to the fourth pipe to supply a solvent for refining the powdered raw material, and a vacuum pump connected to the fifth pipe performs purification. The purpose is to provide raw material supply, purification, drying, pulverization, and refining without requiring assembly and preparation of equipment for each refinement.Hereinafter, Examples will be explained in detail with reference to the drawings.

第1図は、本発明の一実施例の粉体化精製装置の概略構
成図を示したもので、1は中空容器、2は中空容器lの
内部を上下に分割するフィルタ取1付部1′に装着され
た濾過フィルタ、3は中空容器1の頂部に設けられたシ
ャフト挿入孔4か゛ら挿入されたシャフト3′の先端に
取り付けられたプロペラ、5はシャフト3′の他端に取
り付けられたモータ、6は中空容器1の上部側壁に設け
られ、定容量ボンプマが接続され、開閉手段6′を持つ
第1の管、8は中空容器iの上9部側壁に設けられ、開
閉手段8′を持つ第2の管、9は濾過フィルタ2の上部
に接して設けられ、開閉手段9′を持つ第3の管、10
は濾過フィルタ2の下部の中空容”器1の側壁に設けら
れ、加圧装置11が接続され、開閉手段10′を持つ第
4の管、12は中空容器1の下部に設けられ、廃液溜め
13、真空ポンプ14が接続され、開閉手段12′を持
つ第5の管であり、中空容器1は使用する溶剤により腐
食やその他の反応あるいは膨潤等の化学的ま°たけ物理
的改質を起こさず、原料溶液供給から廃液、粉体取出し
工程までの操作による条件変化に対して、充分な物理的
強度を持ち得る材料で、密着シール性が良く、気液漏れ
の生じ難い材料から・作られる。これらの材料としては
、例えば各種ガラス、ステンレス、銅、黄銅等の金属、
テフロン内装金属のような複合材料等が使用1できる。
FIG. 1 shows a schematic configuration diagram of a pulverization and purification apparatus according to an embodiment of the present invention, in which 1 is a hollow container, and 2 is a filter mounting part 1 that divides the inside of the hollow container L into upper and lower parts. 3 is a propeller attached to the tip of a shaft 3' inserted through a shaft insertion hole 4 provided at the top of the hollow container 1, and 5 is attached to the other end of the shaft 3'. A motor 6 is provided on the upper side wall of the hollow container 1, to which a constant volume pumper is connected, and a first tube 8 is provided on the upper 9 side wall of the hollow container i, and a first tube 8 is provided with an opening/closing means 6'. A second pipe 9 having an opening/closing means 9' is provided in contact with the upper part of the filter 2, and a third pipe 10 having an opening/closing means 9'.
is provided on the side wall of the hollow container 1 at the bottom of the filtration filter 2, is connected to a pressurizing device 11, and has an opening/closing means 10'; 12 is provided at the bottom of the hollow container 1, and is a waste liquid reservoir 13. A fifth pipe to which a vacuum pump 14 is connected and has an opening/closing means 12', and the hollow container 1 is not subject to chemical or physical modification such as corrosion, other reactions, or swelling due to the solvent used. First, it is made from a material that has sufficient physical strength to withstand changes in operating conditions from raw material solution supply to waste liquid and powder removal processes, has good sealing properties, and is resistant to gas and liquid leakage. These materials include various types of glass, stainless steel, copper, brass, and other metals,
Composite materials such as Teflon-lined metal can be used.

また加圧装置11は溶媒供給量が少なく、定速供給をす
る場合には、定容量ポンプでも使山することができ、通
常は高圧ガスやコしプレツサが使用される。更に、廃液
溜め13と真空ポンプ14の間にコールドトラップを使
用することが望ましく、このコールドトラップの冷却は
電気冷却(フレオンガスの液化から気化またはベルチェ
効果の利用)が使用されるが、ドライアイスや液体窒氷
などの冷却媒体を使用してもよい。
Further, when the pressurizing device 11 supplies a small amount of solvent and supplies the solvent at a constant rate, a constant volume pump can also be used, and a high pressure gas or pressurizer is usually used. Furthermore, it is desirable to use a cold trap between the waste liquid reservoir 13 and the vacuum pump 14, and electric cooling (from liquefaction to vaporization of Freon gas or utilization of the Beltier effect) is used to cool this cold trap, but dry ice or A cooling medium such as liquid nitrogen ice may also be used.

以上のように構成された本実施例の粉体化精製装置の操
作を説明する。まず、粉体取出部である第3の管9の開
閉手段9′及び廃液部である第5の管12の開閉手段1
2′を閉じ、溶媒状入部である第4の管10の開一手段
10′を開き、加圧装置11で中空容器1に溶媒を注入
する。この溶媒の注入後、開閉手段10′を閉じる。次
に、モータ5給部である第6の管6より定量供給し、供
給後、開閉手段♂を閉じる。その後、第5の管12の開
閉手段12′を開き、真空ポンプ14で減圧し、廃液溜
め13に廃液を貯える。廃液後、真空ポンプ14と廃液
溜め13の接続部を開放し、廃液溜めの減圧を止めて、
開閉手段12′を閉じる。
The operation of the powder refining apparatus of this embodiment configured as described above will be explained. First, the opening/closing means 9' of the third pipe 9 which is a powder extraction part and the opening/closing means 1 of the fifth pipe 12 which is a waste liquid part.
2' is closed, the opening means 10' of the fourth pipe 10 serving as the solvent inlet is opened, and the solvent is injected into the hollow container 1 using the pressurizing device 11. After injecting this solvent, the opening/closing means 10' is closed. Next, a fixed amount is supplied from the sixth pipe 6 which is the supply part of the motor 5, and after the supply, the opening/closing means ♂ is closed. Thereafter, the opening/closing means 12' of the fifth pipe 12 is opened, the pressure is reduced by the vacuum pump 14, and the waste liquid is stored in the waste liquid reservoir 13. After draining the liquid, open the connection between the vacuum pump 14 and the waste liquid reservoir 13, stop depressurizing the waste liquid reservoir, and
Close the opening/closing means 12'.

このように溶媒の門人、溶媒の攪拌、溶媒の廃液°?操
作を繰り返す2とに1り精製粉体を洗浄する。
Thus solvent pupil, solvent stirring, solvent effluent °? The refined powder is washed every second time the operation is repeated.

12′を開き、真空ポンプ14で減圧しながら、モータ
5によりシャ、フト3′、プロペラ3を回転して精製固
形物を粉砕する。同時に送風管である第2゛の管8の開
閉手段8′を開き、送風しながら精製粉体を乾燥する。
12' is opened, and while the pressure is reduced by the vacuum pump 14, the shaft, the shaft 3', and the propeller 3 are rotated by the motor 5 to crush the purified solids. At the same time, the opening/closing means 8' of the second pipe 8, which is a blowing pipe, is opened to dry the refined powder while blowing air.

次に、真空ボ″ンプ14の接続部の開閉手段1〆を閉じ
、廃液溜め13の開酌手段1:3′を開いて減圧を開放
し、廃液部である第5の管12の開閉手段12′を閉じ
る。そして、粉体取出し部である第3の管9の開閉手段
dを開き、粉体化精製物を取り出し、第2の管8、第3
の管9の開閉手段s/ 、 91を閉じる。最後に、再
び溶媒をi4の管10から注入し、プロペラ3を回転し
た後、溶媒を廃山して中空容器を洗浄する。
Next, the opening/closing means 1 of the connection part of the vacuum pump 14 is closed, the opening/closing means 1:3' of the waste liquid reservoir 13 is opened to release the reduced pressure, and the opening/closing means of the fifth pipe 12 which is the waste liquid part is opened. 12' is closed.Then, the opening/closing means d of the third tube 9, which is the powder extraction section, is opened, and the powdered purified product is taken out.
The opening/closing means s/, 91 of the tube 9 is closed. Finally, the solvent is again injected from the pipe 10 of i4, the propeller 3 is rotated, and then the solvent is discarded and the hollow container is washed.

なお、粉体取出部□である第3の管9に、第2図に示し
たように粉体貯蔵部15及び真空ポンプ16を接続し、
第3の管9の開閉手段9′を開いた時に、真空ポンプ1
6の開閉手段16′を開いて粉体を取出し、粉体取出後
に真空ポンプ16の開閉手段16′を閉じ、粉体貯門部
15の開閉手段15!を開くようにすればよい。また乾
燥時に送風管である第その管8から送られる気体は乾燥
速度を向上させるために加熱し、また粉体の酸化等の反
応を防止す為ために、02やCO,、を除いたN2  
など不活性気体の使用が望ましい。更に、粉体化精製物
気体は、粉体の、酸脅反応 を含む熱反応を防止するために、加熱されない不活性気
体の送風が望ましい。゛また第2図に示した真空ポンプ
16と粉体貯蔵部15の間に多孔質のフィル゛りを介在
させ、真空ポンプ16への粉体の混入を防止する。  
         1前述の真空ポンプ14と廃液溜め
130間に設けられたコールドトラップに、更に自由に
開閉できる2つの孔を設け、1つを加圧装置、1つを溶
媒貯蔵部に接続し、廃液溜め13に加熱装置を設け、廃
液溜め13の第5の管12の開閉手段12′、減圧開放
部13′を閉、じ、真空ポンプ14で、減圧しながら廃
液溜め13を加熱し、コールドトラップの接続部を閉じ
、しかる後゛、減圧開放部13′を、開き、常圧に戻っ
た時、減圧開放部13′を閉じる。
In addition, the powder storage section 15 and the vacuum pump 16 are connected to the third pipe 9, which is the powder extraction section □, as shown in FIG.
When the opening/closing means 9' of the third pipe 9 is opened, the vacuum pump 1
The opening/closing means 16' of the vacuum pump 16 is opened to take out the powder, and after taking out the powder, the opening/closing means 16' of the vacuum pump 16 is closed, and the opening/closing means 15 of the powder storage section 15 is opened. All you have to do is open it. In addition, during drying, the gas sent from the second tube 8, which is a blower tube, is heated to improve the drying speed, and in order to prevent reactions such as oxidation of the powder, the gas is heated to increase the drying rate.
It is preferable to use an inert gas such as Furthermore, it is desirable to blow an unheated inert gas to the powdered purified product gas in order to prevent thermal reactions of the powder, including acid threat reactions. Furthermore, a porous film is interposed between the vacuum pump 16 and the powder storage section 15 shown in FIG. 2 to prevent powder from entering the vacuum pump 16.
1 The cold trap provided between the vacuum pump 14 and the waste liquid reservoir 130 is further provided with two holes that can be opened and closed freely, one is connected to a pressurizing device, the other is connected to a solvent storage part, and the waste liquid reservoir 13 is connected to the cold trap. The opening/closing means 12' of the fifth pipe 12 of the waste liquid reservoir 13 and the vacuum release part 13' are closed, and the waste liquid reservoir 13 is heated while being depressurized by the vacuum pump 14, and the cold trap is connected. Then, the reduced pressure opening section 13' is opened, and when the pressure returns to normal pressure, the reduced pressure opening section 13' is closed.

次に、コールドトラップに貯蔵された溶媒を溶媒貯蔵部
に送入する。以上の操作により、溶媒の繰り返し使用も
可能である。
Next, the solvent stored in the cold trap is delivered to the solvent storage section. Through the above operations, the solvent can be used repeatedly.

以上説明したように、本発明によれば、溶媒の注入、溶
媒の攪拌、原料溶液の供給、溶媒の廃山、精製固形物の
粉砕、粉体化精製物の取出しを順次行なうことにより、
精製された粉体を効率良く、−mした操作で行なうこと
ができ、7また溶媒の注入、溶媒の攪拌、溶媒の廃山の
みを轡り返すことにより、より精製された粉体を取り出
すことかで゛きる。
As explained above, according to the present invention, by sequentially performing the injection of the solvent, stirring the solvent, supplying the raw material solution, discarding the solvent, pulverizing the purified solid, and taking out the powdered purified product,
Purified powder can be efficiently processed by -m operation, and more refined powder can be taken out by injecting the solvent, stirring the solvent, and turning over only the waste pile of solvent. I can ride it.

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

第1図は、本発明の一実施例の粉体化精製装置の概略構
成図、第2図は、第1図の一部の他の実施例の構成図で
ある。′ 1・・・中空容器、2・・・フィルタ、3・・・プロペ
ラ、3′・・・シャフト、4−・・シャフト挿入孔、5
・・・モータ、6・・・第1の管、ツ・・・定容量ポン
プ、8・・・第2の管、9・・・第3の管、10・・・
第4の管、11・・・加圧装置、12・・・第5の管、
6’、 8’、 9’、 10’、 l 2’・・・開
閉手段、13・・・廃液溜め、14・・・真空ポンプ、
15・・・粉体貯蔵部、“16・・・真空ポンプ。 特許出願人  株式会社 リ コ −
FIG. 1 is a schematic diagram of a pulverizing and refining apparatus according to one embodiment of the present invention, and FIG. 2 is a diagram of another embodiment of a part of FIG. 1. ' 1...Hollow container, 2...Filter, 3...Propeller, 3'...Shaft, 4-...Shaft insertion hole, 5
...Motor, 6..First pipe, 2..Constant displacement pump, 8..Second pipe, 9..Third pipe, 10..
4th pipe, 11...pressure device, 12...5th pipe,
6', 8', 9', 10', l2'... Opening/closing means, 13... Waste liquid reservoir, 14... Vacuum pump,
15...Powder storage section, "16...Vacuum pump. Patent applicant Rico Co., Ltd. -

Claims (1)

【特許請求の範囲】[Claims] 中空容器の中間部近傍に設けられた濾過フィルタと、該
濾過フィルタの上部に設けられた攪拌翼と、前記中空容
器の上部側壁に設けられた開閉手段を有する第1の管と
、該第1の管に対向した前記中空容器の側壁に設けられ
た開部手段を有する第2の管と、前記済過フィルタの上
部に接して前記中空容器の側壁に設けられた第3の管と
、該第3の管に対向した前記中空容器の側壁の前記濾過
フィルタの下部に設けられた開閉手段を有する第4の管
と、前記中空容器の最下部に設け、られた開閉手段を有
する第5の管とを備えた粉体化精製装置において、前記
第1の管に定容量ポンプが接続され、粉体化原料を溶液
で定容量供給し、前記回転翼は前記中空容器の最上部の
孔を通るシャフトに接続され、該シャフトをモータで回
転することにより前゛記溶液を攪拌し、精製固形分を粉
砕し、前記第2の管から気体が送風されて精製粉体の乾
燥及び第3の管から該精製粉体の取り出しを行ない、前
記第4の管に加圧ポンプが接続され、前記粉体化原料を
精製する溶剤を供給し、前記第5の管に真空ポンプが接
続され、精製後の排液を除去することを特徴とする粉体
化精製装置。
a first tube having an opening/closing means provided on an upper side wall of the hollow container; a second pipe having an opening means provided on a side wall of the hollow container opposite to the pipe; a third pipe provided on a side wall of the hollow container in contact with an upper part of the filter; a fourth pipe having an opening/closing means provided at a lower part of the filtration filter on the side wall of the hollow container opposite to the third pipe; and a fifth pipe having an opening/closing means provided at the lowest part of the hollow container. In the pulverization and purification apparatus, a constant volume pump is connected to the first pipe to supply a constant volume of the powdered raw material as a solution, and the rotary blade is configured to fill the hole at the top of the hollow container. By rotating the shaft with a motor, the solution is stirred and the purified solids are pulverized, and gas is blown from the second pipe to dry the purified powder and dry the purified powder. The purified powder is taken out from the pipe, a pressure pump is connected to the fourth pipe to supply a solvent for refining the powdered raw material, and a vacuum pump is connected to the fifth pipe to perform the refining process. A pulverization purification device characterized by removing the subsequent waste liquid.
JP12025281A 1981-07-31 1981-07-31 Purification apparatus by pulverization Pending JPS5820202A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12025281A JPS5820202A (en) 1981-07-31 1981-07-31 Purification apparatus by pulverization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12025281A JPS5820202A (en) 1981-07-31 1981-07-31 Purification apparatus by pulverization

Publications (1)

Publication Number Publication Date
JPS5820202A true JPS5820202A (en) 1983-02-05

Family

ID=14781588

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12025281A Pending JPS5820202A (en) 1981-07-31 1981-07-31 Purification apparatus by pulverization

Country Status (1)

Country Link
JP (1) JPS5820202A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63315139A (en) * 1987-06-19 1988-12-22 Mitsubishi Heavy Ind Ltd Apparatus for mixing treatment
CN110314406A (en) * 2019-07-11 2019-10-11 青岛润达生物科技有限公司 A kind of plant extracts separator of observable record
CN111714924A (en) * 2020-06-12 2020-09-29 漳州职业技术学院 Grape seed procyanidin extraction device and preparation method of anti-fatigue additive

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63315139A (en) * 1987-06-19 1988-12-22 Mitsubishi Heavy Ind Ltd Apparatus for mixing treatment
CN110314406A (en) * 2019-07-11 2019-10-11 青岛润达生物科技有限公司 A kind of plant extracts separator of observable record
CN111714924A (en) * 2020-06-12 2020-09-29 漳州职业技术学院 Grape seed procyanidin extraction device and preparation method of anti-fatigue additive

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