JP4540772B2 - Steam heating device - Google Patents

Steam heating device Download PDF

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Publication number
JP4540772B2
JP4540772B2 JP29338099A JP29338099A JP4540772B2 JP 4540772 B2 JP4540772 B2 JP 4540772B2 JP 29338099 A JP29338099 A JP 29338099A JP 29338099 A JP29338099 A JP 29338099A JP 4540772 B2 JP4540772 B2 JP 4540772B2
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Japan
Prior art keywords
condensate
steam
recovery device
heating
pressure
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Expired - Fee Related
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JP29338099A
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Japanese (ja)
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JP2001113183A (en
Inventor
高之 森井
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Tlv Co Ltd
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Tlv Co Ltd
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Priority to JP29338099A priority Critical patent/JP4540772B2/en
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Description

【0001】
【発明の属する技術分野】
本発明は熱交換器内に収容した被加熱物を加熱用の蒸気で加熱するものに関し、特にその加熱温度が100度C前後程度の比較的低温の場合に適した蒸気加熱装置に関する。
【0002】
【従来の技術】
従来の蒸気加熱装置としては例えば特開平9−250887号公報に示されているようなものが用いられていた。これは、反応釜1に加熱部としてのジャケット部2を形成して加熱用の蒸気供給管3を接続し、加熱により生じた復水を加熱部から排出する復水回収装置16を接続すると共に、加熱部の入口側に蒸気供給管3と連通した蒸気エゼクタ6を配置して当該蒸気エゼクタ6の出口側をジャケット部2と接続し、蒸気エゼクタ6の吸引室7を復水回収装置16と接続したものであり、ジャケット部2に復水を滞留することがなく、100度C程度の比較的低温の蒸気によって被加熱物を加熱することができるものである。
【0003】
【発明が解決しようとする課題】
上記従来のものでは、加熱部の温度が変動してしまい、被加熱物に加熱ムラを生じてしまう問題があった。これは、復水回収装置が蒸気エゼクタと連通している場合に、加熱部の温度又は圧力状態、あるいは被加熱物の温度に関わらず、蒸気エゼクタで発生するほぼ一定の吸引力で復水回収装置、更には連通した加熱部を吸引するために、加熱部の蒸気圧力即ち蒸気温度が、加熱部や被加熱物の温度変動に追随することができずに、加熱ムラを生じてしまうのである。
【0004】
従って本発明の課題は、蒸気エゼクタへの吸引量を適宜コントロールすることにより、加熱部の温度変動を防止して、被加熱物に加熱温度ムラを生じることのない蒸気加熱装置を得ることである。
【0005】
【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講じた本発明の手段は、熱交換器に加熱部を形成して加熱用の蒸気供給管を接続し、当該蒸気供給管に蒸気エゼクタを取り付けて、当該蒸気エゼクタの吸引室と、加熱により生じた復水を加熱部から排出する復水回収装置を、接続し、当該復水回収装置が、蒸気エゼクタの吸引室と復水回収装置の排気口とが管路で接続され、ジャケット部の下部と復水回収装置の復水流入口とが管路で接続され、当該管路にはジャケット部から復水回収装置側への流体の通過のみを許容する逆止弁が取り付けられ、復水流出口には逆止弁を介して復水回収管が接続され、復水回収装置の上部には圧送流体流入口と圧送流体排気口が設けられ、圧送流体流入口が管路を介して高圧の蒸気供給管と接続され、復水流入口から流入してきた復水が内部に溜りその水位が上昇すると装置内部のフロートが上昇して所定高さに達し、圧送流体流入口に取り付けた圧送弁を開弁すると共に排気口に取り付けた排気弁を閉弁し、それによって蒸気供給管から高圧の蒸気が復水回収装置の内部に供給されることにより、溜まっていた復水を復水流出口から復水回収管へ圧送するものであり、他方で復水が圧送されるに連れて、内部のフロートが降下して、所定の液位まで低下すると圧送流体流入口の圧送弁を閉弁すると共に排気口に取り付けた排気弁が開弁して、反応釜のジャケット部から復水が復水回収装置内に流下してくるものにおいて、蒸気エゼクタの吸引室と復水回収装置との間に制御弁を配置し、蒸気供給管から供給される蒸気の圧力を検出する蒸気圧力検出手段を取り付けて、当該蒸気圧力検出手段からの検出信号値に応じて上記制御弁を開閉制御し、蒸気エゼクタへの吸引量をコントロールするものである。
【0006】
【発明の実施の形態】
通常の加熱用の飽和蒸気はその圧力と温度の関係が1対1で決まる。従って、蒸気の圧力をコントロールすることによって、蒸気温度も同時にコントロールすることができる。供給蒸気圧力値に応じて蒸気エゼクタの吸引室側の制御弁を開閉制御することにより、蒸気エゼクタの吸引量をコントロールすることができ、復水回収装置及びこの復水回収装置と連通した加熱部を所定の圧力状態即ち温度状態とすることができ、被加熱物の加熱温度ムラを防止することができる。
【0007】
【実施例】
本実施例においては熱交換器として反応釜1を用いた例を示す。反応釜1の外周に加熱部としてのジャケット部2を形成して蒸気供給管3を接続する。蒸気供給管3には、順次、開閉弁4と圧力調節弁5と蒸気エゼクタ6を接続する。蒸気エゼクタ6は内部にノズルを有する吸引室7とディフューザ9で形成する。
【0008】
蒸気エゼクタ6の吸引室7と、後述する下方の復水回収装置16の排気口21を管路8で接続する。管路8には制御弁10を設けて、蒸気供給管3に取り付けた圧力検出手段としての圧力センサ11と接続する。
【0009】
ジャケット部2の下部に管路12を接続して、復水回収装置16の復水流入口15と接続する。管路12にはジャケット部2から復水回収装置16側への流体の通過のみを許容する逆止弁14を取り付ける。
【0010】
復水回収装置16の復水流出口17には、逆止弁18を介して復水回収管19を接続する。逆止弁18は復水回収装置16から復水回収管19側のみへの流体の通過を許容するものである。
【0011】
復水回収装置16の上部に、圧送流体流入口20と排気口21を設けて、圧送流体流入口20を管路22を介して高圧の蒸気供給管3と接続する。
【0012】
復水回収装置16は従来技術のものと同一であり、復水流入口15から流入してきた復水が内部に溜りその水位が上昇すると図示しないフロートを上昇させ、所定高さに達するとフロートがスナップ移動して、圧送流体流入口20に取り付けた圧送弁を開弁すると共に、排気口21に取り付けた排気弁を閉弁して、蒸気供給管3から高圧の蒸気が復水回収装置16内部に供給されて、溜まっていた復水を復水流出口17から復水回収管19へ圧送するものである。
【0013】
復水回収装置16内の復水が圧送されるに連れて、図示しない内部のフロートが降下して、所定の液位まで低下するとフロートは上記とは反対方向にスナップ移動して、圧送流体流入口20の圧送弁を閉弁すると共に、排気口21に取り付けた排気弁が開弁して、反応釜1のジャケット部2から復水が復水回収装置16内に流下してくるものである。
【0014】
排気口21の排気弁が開弁した場合は、復水回収装置16と蒸気エゼクタ6が連通され、蒸気エゼクタ6の吸引力により復水回収装置16内が所定の減圧状態となるものである。
【0015】
図1において、蒸気供給管3から反応釜1のジャケット部2へ加熱用の蒸気を供給することにより、反応釜1内の図示しない被加熱物が加熱される。加熱蒸気温度は圧力調節弁5によって蒸気圧力を調節することにより、蒸気、正確には飽和蒸気、の圧力と温度は1対1の関係があるために、任意に調節することができる。加熱により熱を奪われた蒸気は凝縮して復水となる。
【0016】
復水は管路12と復水流入口15から復水回収装置16内へ流入する。この場合、圧送流体流入口20の圧送弁は閉弁しているが、排気口21の排気弁は開弁しておりエゼクタ6の吸引室7と接続している。このエゼクタ6の吸引力により復水回収装置16内を所定の減圧状態とすることによって、ジャケット部2で発生した復水は管路12を介して滞留することなく復水回収装置16内へ流下することができる。
【0017】
本実施例においては、蒸気供給管3に蒸気圧力センサ11を取り付けて、この検出圧力値に応じて制御弁10を開閉制御することによって、ジャケット部2の蒸気圧力即ち加熱温度をより精度良く維持して、反応釜1内の被加熱物を加熱ムラなく加熱することができる。
【0018】
本実施例においては、蒸気エゼクタ6の吸引室7を復水回収装置16の排気口21と連通した例を示したが、蒸気エゼクタ6の吸引室7と復水回収装置16との接続は、これに限られるものではなく、例えば復水排出装置16に排気口21や流入口20とは別個の連結口を設けて吸引室7と接続することもできるものである。
【0019】
【発明の効果】
上記のように本発明によれば、供給蒸気圧力値に応じて、蒸気エゼクタへの吸引量を適宜コントロールすることにより、加熱部の圧力変動即ち温度変動を防止して、被加熱物に加熱温度ムラを生じることのない蒸気加熱装置を得ることができる。
【図面の簡単な説明】
【図1】本発明の蒸気加熱装置の実施例を示す構成図。
【符号の説明】
1 反応釜
2 ジャケット部
3 蒸気供給管
6 蒸気エゼクタ
7 吸引室
10 制御弁
11 圧力センサ
15 復水流入口
16 復水回収装置
17 復水流出口
20 圧送流体流入口
21 排気口
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an apparatus for heating an object to be heated contained in a heat exchanger with heating steam, and more particularly to a steam heating apparatus suitable for a case where the heating temperature is a relatively low temperature of about 100 degrees C.
[0002]
[Prior art]
As a conventional steam heating device, for example, a device as disclosed in JP-A-9-250887 has been used. This is because a jacket portion 2 as a heating portion is formed in the reaction kettle 1 and a steam supply pipe 3 for heating is connected, and a condensate recovery device 16 for discharging condensate generated by heating from the heating portion is connected. A steam ejector 6 communicating with the steam supply pipe 3 is arranged on the inlet side of the heating section, the outlet side of the steam ejector 6 is connected to the jacket section 2, and the suction chamber 7 of the steam ejector 6 is connected to the condensate recovery device 16. The condensate is not retained in the jacket portion 2 and can be heated by a relatively low temperature steam of about 100 degrees C.
[0003]
[Problems to be solved by the invention]
In the said conventional thing, the temperature of the heating part fluctuated and there existed a problem which produced a heating nonuniformity in a to-be-heated material. This is because when the condensate recovery device communicates with the steam ejector, the condensate recovery is performed with a substantially constant suction force generated by the steam ejector regardless of the temperature or pressure state of the heating part or the temperature of the object to be heated. In order to suck the apparatus and further the connected heating part, the steam pressure of the heating part, that is, the steam temperature, cannot follow the temperature fluctuations of the heating part and the object to be heated, resulting in heating unevenness. .
[0004]
Accordingly, an object of the present invention is to obtain a steam heating apparatus that prevents the temperature fluctuation of the heating part and does not cause uneven heating temperature in the heated object by appropriately controlling the suction amount to the steam ejector. .
[0005]
[Means for Solving the Problems]
The means of the present invention devised to solve the above-mentioned problem is that a heating unit is formed in a heat exchanger, a heating steam supply pipe is connected, a steam ejector is attached to the steam supply pipe, and the steam ejector A condensate recovery device that discharges the condensate generated by heating from the heating section, and the condensate recovery device is connected to the suction chamber of the steam ejector and the exhaust port of the condensate recovery device. Connected to the lower part of the jacket portion and the condensate inlet of the condensate recovery device by a pipe line, and the check valve allows only passage of fluid from the jacket part to the condensate recovery apparatus side in the pipe line A condensate recovery pipe is connected to the condensate outlet via a check valve, and a pumping fluid inlet and a pumping fluid outlet are provided in the upper part of the condensate recovery device. It is connected to the high-pressure steam supply pipe through a road, and flows from the condensate water inlet When the condensate accumulates inside and the water level rises, the float inside the device rises and reaches a predetermined height, opening the pressure feed valve attached to the pressure feed fluid inlet and closing the exhaust valve attached to the exhaust port. As a result, high-pressure steam is supplied from the steam supply pipe into the condensate recovery device, so that the accumulated condensate is pumped from the condensate outlet to the condensate recovery pipe. When the internal float is lowered and lowered to a predetermined liquid level, the pressure feed valve at the pressure feed fluid inlet is closed and the exhaust valve attached to the exhaust port is opened to open the reaction kettle. In the case where condensate flows down from the jacket part into the condensate recovery unit, a control valve is disposed between the suction chamber of the steam ejector and the condensate recovery unit, and the pressure of the steam supplied from the steam supply pipe A steam pressure detection means to detect , According to the detection signal values from the steam pressure detecting means controls the opening and closing of the said control valve is for controlling the amount of suction to the steam ejector.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
Normal steam saturated steam has a one-to-one relationship between pressure and temperature. Therefore, the steam temperature can be controlled simultaneously by controlling the steam pressure. The suction amount of the steam ejector can be controlled by controlling the opening and closing of the control valve on the suction chamber side of the steam ejector according to the supply steam pressure value, and the condensate recovery device and the heating unit communicating with the condensate recovery device Can be set to a predetermined pressure state, that is, a temperature state, and uneven heating temperature of the object to be heated can be prevented.
[0007]
【Example】
In this embodiment, an example in which the reaction kettle 1 is used as a heat exchanger will be shown. A jacket portion 2 as a heating portion is formed on the outer periphery of the reaction kettle 1 and a steam supply pipe 3 is connected thereto. The steam supply pipe 3 is connected with an on-off valve 4, a pressure control valve 5, and a steam ejector 6 in sequence. The steam ejector 6 is formed by a suction chamber 7 having a nozzle inside and a diffuser 9.
[0008]
A suction chamber 7 of the steam ejector 6 and an exhaust port 21 of a lower condensate recovery device 16 described later are connected by a pipe line 8. A control valve 10 is provided in the pipe line 8 and connected to a pressure sensor 11 as pressure detection means attached to the steam supply pipe 3.
[0009]
A pipe line 12 is connected to the lower part of the jacket part 2 and connected to the condensate inlet 15 of the condensate recovery device 16. A check valve 14 that allows only passage of fluid from the jacket portion 2 to the condensate recovery device 16 side is attached to the pipe line 12.
[0010]
A condensate recovery pipe 19 is connected to the condensate outlet 17 of the condensate recovery device 16 via a check valve 18. The check valve 18 allows passage of fluid from the condensate recovery device 16 only to the condensate recovery pipe 19 side.
[0011]
A pumping fluid inlet 20 and an exhaust port 21 are provided in the upper part of the condensate recovery device 16, and the pumping fluid inlet 20 is connected to the high-pressure steam supply pipe 3 through a pipe line 22.
[0012]
The condensate recovery device 16 is the same as that of the prior art, and when the condensate flowing in from the condensate inlet 15 accumulates inside and the water level rises, the float (not shown) rises, and when it reaches a predetermined height, the float snaps. It moves and opens the pressure feed valve attached to the pressure feed fluid inlet 20 and closes the exhaust valve attached to the exhaust port 21 so that the high-pressure steam from the steam supply pipe 3 enters the condensate recovery device 16. The condensate supplied and accumulated is pumped from the condensate outlet 17 to the condensate recovery pipe 19.
[0013]
As the condensate in the condensate recovery device 16 is pumped, the float inside (not shown) descends, and when it falls to a predetermined liquid level, the float snaps in the direction opposite to the above, and the pumping fluid flow The pressure feed valve at the inlet 20 is closed and the exhaust valve attached to the exhaust port 21 is opened, so that the condensate flows down from the jacket portion 2 of the reaction kettle 1 into the condensate recovery device 16. .
[0014]
When the exhaust valve of the exhaust port 21 is opened, the condensate recovery device 16 and the steam ejector 6 are communicated, and the condensate recovery device 16 is brought into a predetermined reduced pressure state by the suction force of the steam ejector 6.
[0015]
In FIG. 1, by supplying steam for heating from the steam supply pipe 3 to the jacket portion 2 of the reaction kettle 1, an object to be heated (not shown) in the reaction kettle 1 is heated. The heating steam temperature can be arbitrarily adjusted by adjusting the steam pressure by the pressure control valve 5, because the pressure and temperature of the steam, more precisely, the saturated steam has a one-to-one relationship. Steam deprived of heat by heating condenses into condensate.
[0016]
Condensate flows into the condensate recovery device 16 from the conduit 12 and the condensate inlet 15. In this case, the pumping valve of the pumping fluid inlet 20 is closed, but the exhaust valve of the exhaust port 21 is open and connected to the suction chamber 7 of the ejector 6. By bringing the condensate recovery device 16 into a predetermined pressure-reduced state by the suction force of the ejector 6, the condensate generated in the jacket portion 2 flows down into the condensate recovery device 16 without staying through the conduit 12. can do.
[0017]
In the present embodiment, the steam pressure sensor 11 is attached to the steam supply pipe 3 and the control valve 10 is controlled to open and close according to the detected pressure value, thereby maintaining the steam pressure, that is, the heating temperature of the jacket portion 2 with higher accuracy. Thus, the object to be heated in the reaction kettle 1 can be heated without heating unevenness.
[0018]
In the present embodiment, the example in which the suction chamber 7 of the steam ejector 6 is communicated with the exhaust port 21 of the condensate recovery device 16 is shown. However, the connection between the suction chamber 7 of the steam ejector 6 and the condensate recovery device 16 is as follows. For example, the condensate discharge device 16 may be connected to the suction chamber 7 by providing a connection port separate from the exhaust port 21 and the inflow port 20.
[0019]
【The invention's effect】
As described above, according to the present invention, by appropriately controlling the suction amount to the steam ejector according to the supply steam pressure value, the pressure fluctuation of the heating part, that is, the temperature fluctuation is prevented, and the heating temperature is applied to the object to be heated. A steam heating apparatus that does not cause unevenness can be obtained.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing an embodiment of a steam heating apparatus according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Reaction kettle 2 Jacket part 3 Steam supply pipe 6 Steam ejector 7 Suction chamber 10 Control valve 11 Pressure sensor 15 Condensate inlet 16 Condensate recovery device 17 Condensate outlet 20 Pressure feed fluid inlet 21 Exhaust outlet

Claims (1)

熱交換器に加熱部を形成して加熱用の蒸気供給管を接続し、当該蒸気供給管に蒸気エゼクタを取り付けて、当該蒸気エゼクタの吸引室と、加熱により生じた復水を加熱部から排出する復水回収装置を、接続し、当該復水回収装置が、蒸気エゼクタの吸引室と復水回収装置の排気口とが管路で接続され、 ジャケット部の下部と復水回収装置の復水流入口とが管路で接続され、当該管路にはジャケット部から復水回収装置側への流体の通過のみを許容する逆止弁が取り付けられ、復水流出口には逆止弁を介して復水回収管が接続され、復水回収装置の上部には圧送流体流入口と圧送流体排気口が設けられ、圧送流体流入口が管路を介して高圧の蒸気供給管と接続され、復水流入口から流入してきた復水が内部に溜りその水位が上昇すると装置内部のフロートが上昇して所定高さに達し、圧送流体流入口に取り付けた圧送弁を開弁すると共に排気口に取り付けた排気弁を閉弁し、それによって蒸気供給管から高圧の蒸気が復水回収装置の内部に供給されることにより、溜まっていた復水を復水流出口から復水回収管へ圧送するものであり、他方で復水が圧送されるに連れて、内部のフロートが降下して、所定の液位まで低下すると圧送流体流入口の圧送弁を閉弁すると共に排気口に取り付けた排気弁が開弁して、反応釜のジャケット部から復水が復水回収装置内に流下してくるものにおいて、蒸気エゼクタの吸引室と復水回収装置との間に制御弁を配置し、蒸気供給管から供給される蒸気の圧力を検出する蒸気圧力検出手段を取り付けて、当該蒸気圧力検出手段からの検出信号値に応じて上記制御弁を開閉制御し、蒸気エゼクタへの吸引量をコントロールすることを特徴とする蒸気加熱装置。A heating part is formed in the heat exchanger, a steam supply pipe for heating is connected, a steam ejector is attached to the steam supply pipe, and the suction chamber of the steam ejector and the condensate generated by heating are discharged from the heating part. The condensate recovery device is connected, and the condensate recovery device is connected by a pipe line to the suction chamber of the steam ejector and the exhaust port of the condensate recovery device. The inlet is connected by a pipe line, and a check valve that allows only passage of fluid from the jacket portion to the condensate recovery device side is attached to the pipe line, and the condensate outlet is connected via the check valve. water recovery pipe is connected, the upper part pumping fluid inlet and pumping fluid exhaust port is provided in the condensate recovery system is connected to a high-pressure steam supply pipe pumped fluid inlet via a conduit, condensate water inlet When the condensate flowing in from the inside accumulates and the water level rises, The float rises to a predetermined height and opens the pumping valve attached to the pumping fluid inlet and closes the exhaust valve attached to the exhaust port, so that high-pressure steam is condensed from the steam supply pipe. By supplying it to the inside of the recovery device, the condensate that has accumulated is pumped from the condensate outlet to the condensate recovery pipe. On the other hand, as the condensate is pumped, the internal float drops. When the liquid level drops to a predetermined level, the pumping valve at the pumping fluid inflow port is closed and the exhaust valve attached to the exhaust port is opened, so that the condensate flows into the condensate recovery unit from the jacket of the reaction kettle. In this case, a control valve is disposed between the suction chamber of the steam ejector and the condensate recovery device, and a steam pressure detecting means for detecting the pressure of the steam supplied from the steam supply pipe is attached to the steam pressure. According to the detection signal value from the detection means And it controls the opening and closing of the serial control valves, steam heating apparatus characterized by controlling the suction amount of the steam ejector.
JP29338099A 1999-10-15 1999-10-15 Steam heating device Expired - Fee Related JP4540772B2 (en)

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Publication number Priority date Publication date Assignee Title
JP2007218471A (en) * 2006-02-15 2007-08-30 Tlv Co Ltd Waste heat-recovering/pressure-reducing device for steam
KR101372680B1 (en) 2012-11-16 2014-03-11 김기열 Steam ejector for self controlling
JP6842302B2 (en) * 2017-01-05 2021-03-17 株式会社テイエルブイ Drain collection system
JP7372083B2 (en) * 2019-08-30 2023-10-31 株式会社カネカ Expanded particle manufacturing device and manufacturing method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03101830A (en) * 1989-09-14 1991-04-26 Tlv Co Ltd Steam heating and vaporization cooling device
JPH04369302A (en) * 1991-06-14 1992-12-22 Tlv Co Ltd Vacuum steam generating device
JPH09250887A (en) * 1996-03-15 1997-09-22 Tlv Co Ltd Steam heating device
JPH09250705A (en) * 1996-03-15 1997-09-22 Tlv Co Ltd Pressure reduction steam generating device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03101830A (en) * 1989-09-14 1991-04-26 Tlv Co Ltd Steam heating and vaporization cooling device
JPH04369302A (en) * 1991-06-14 1992-12-22 Tlv Co Ltd Vacuum steam generating device
JPH09250887A (en) * 1996-03-15 1997-09-22 Tlv Co Ltd Steam heating device
JPH09250705A (en) * 1996-03-15 1997-09-22 Tlv Co Ltd Pressure reduction steam generating device

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