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JPH074212B2 - How to use heat in the beer manufacturing process - Google Patents
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JPH074212B2 - How to use heat in the beer manufacturing process - Google Patents

How to use heat in the beer manufacturing process

Info

Publication number
JPH074212B2
JPH074212B2 JP62203497A JP20349787A JPH074212B2 JP H074212 B2 JPH074212 B2 JP H074212B2 JP 62203497 A JP62203497 A JP 62203497A JP 20349787 A JP20349787 A JP 20349787A JP H074212 B2 JPH074212 B2 JP H074212B2
Authority
JP
Japan
Prior art keywords
steam
heat
water
beer
boiler
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 - Fee Related
Application number
JP62203497A
Other languages
Japanese (ja)
Other versions
JPS6447367A (en
Inventor
省三 片山
悟 山本
千太郎 三浦
潔 古嶋
潤二 松田
茂 坂下
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.)
Mayekawa Manufacturing Co
Tokyo Gas Co Ltd
Original Assignee
Mayekawa Manufacturing Co
Tokyo Gas 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 Mayekawa Manufacturing Co, Tokyo Gas Co Ltd filed Critical Mayekawa Manufacturing Co
Priority to JP62203497A priority Critical patent/JPH074212B2/en
Publication of JPS6447367A publication Critical patent/JPS6447367A/en
Publication of JPH074212B2 publication Critical patent/JPH074212B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は、ビールの製造を行う各種工程の熱源として蒸
気を利用するようにしたビール製造工程における熱利用
方法に係り、特に各種工程に必要な熱源である蒸気、温
水、冷水を、ボイラーより発生した蒸気を用いて作成し
熱エネルギーの有効利用を図ったビール製造工程におけ
る熱利用方法に関する。
TECHNICAL FIELD The present invention relates to a heat utilization method in a beer production process in which steam is used as a heat source in various processes for producing beer, and is particularly required for various processes. The present invention relates to a heat utilization method in a beer manufacturing process in which steam, hot water, and cold water, which are various heat sources, are created by using steam generated from a boiler to effectively utilize heat energy.

「従来の技術」 ビールの製造工程を図面に基づいて概略的に説明する
に、麦芽粉砕機22により粉砕された麦芽は、糖化槽1及
び糖化釜2内で50℃前後の温水を加えて麦汁とし、該麦
芽中のでんぷんを酵素の働きにより糖分に変えた後、該
麦汁を75℃前後に加熱しその後濾過槽3で清澄な麦汁に
濾過し、煮沸釜4に供給する。
"Prior Art" To schematically explain the manufacturing process of beer based on the drawings, malt crushed by a malt crusher 22 is added to the saccharification tank 1 and the saccharification kettle 2 by adding warm water of about 50 ° C This is used as a broth, and the starch in the malt is converted into sugar by the action of an enzyme. The wort is heated to about 75 ° C. and then filtered into clear wort in the filtration tank 3 and supplied to the boiling kettle 4.

煮沸釜4では、前記麦汁にホップを添加しながら蒸気を
利用して煮沸(100℃)する事により、タンパク質の凝
固とともにホップ香味の抽出を図る。そしてこのように
して得られた麦汁を熱凝固物分離槽12内で、熱凝固物を
分離した後、該麦汁を冷水にて冷却して麦汁が形成出来
る。かかる釜及び槽の操作においては、毎回温水による
洗浄を行う。
In the boiling kettle 4, boiling of hops to the wort is carried out (100 ° C.) using steam to coagulate protein and extract hop flavor. Then, the wort thus obtained is separated from the heat-coagulated product in the heat-coagulated product separation tank 12, and then the wort can be cooled with cold water to form wort. In such operation of the pot and tank, washing with warm water is performed every time.

従ってかかるビール製造ラインにおいては、前記加熱、
冷却、洗浄等に多量の蒸気、冷水、温水を使用するが、
従来の製造工程においては、蒸気ボイラーで、冷水は冷
凍機で、又温水は前記ボイラーよりの蒸気の一部を熱源
として用いて製造されているが、このように夫々個別に
前記冷水や温水を製造する方法ではボイラー燃焼用エネ
ルギーと冷凍機駆動用電源又は燃料を必要とし運転コス
トが大になるという問題を有す。
Therefore, in such a beer production line, the heating,
A large amount of steam, cold water or hot water is used for cooling and cleaning,
In the conventional manufacturing process, a steam boiler, cold water is a refrigerator, and hot water is manufactured by using a part of the steam from the boiler as a heat source. The manufacturing method requires energy for boiler combustion and a power source or fuel for driving the refrigerator, which causes a problem of high operating cost.

この為従来では、煮沸釜4より排出される蒸気を圧縮機
にて吸引、圧縮して麦汁加熱に再使用するとともに、前
記煮沸釜4のドレンから熱を回収し温水を製造する技術
(第1従来技術)や、煮沸釜4より排出される蒸気を利
用して温水を作り、該温水を濾過槽等の洗浄用温水に利
用するとともに該温水の一部を利用して吸収式冷凍機を
駆動して冷水を作る技術(第2従来技術)が存在する。
For this reason, conventionally, a technique of sucking and compressing the steam discharged from the boiling pot 4 with a compressor to reuse it for heating wort, and recovering heat from the drain of the boiling pot 4 to produce hot water (No. 1) 1 prior art) or steam discharged from the boiling pot 4 is used to make hot water, which is used as hot water for washing a filter tank or the like, and at the same time, an absorption refrigerator is used as a part of the hot water. There is a technique (second conventional technique) of driving to produce cold water.

「発明が解決しようとする問題点」 しかしながら前記従来技術はいずれも煮沸釜より排出さ
れる蒸気やドレンという部分的な熱利用である為に、必
ずしも満足する量の温水を得る事が出来ず、やはりボイ
ラーの燃焼コストの低減は微小である。
"Problems to be solved by the invention" However, since the above-mentioned conventional techniques are all partial heat utilization of steam and drain discharged from the boiling pot, it is not always possible to obtain a sufficient amount of hot water, Again, the reduction in boiler combustion costs is insignificant.

而も前記第1従来技術においては、冷水製造用の冷凍機
の動力には何等考慮していない為に、冷凍機の動力コス
トは低減し得ない。
In the first prior art, however, the power cost of the refrigerator cannot be reduced because no consideration is given to the power of the refrigerator for producing cold water.

かかる欠点を解消する為に、前記第2従来技術において
は、前記温水の一部を利用して吸収式冷凍機を駆動する
技術が開示されているが、吸収式冷凍機においては冷却
能力の3倍程度の冷却水負荷が必要である為に、煮沸釜
より排出される蒸気を利用して得られた温水のほとんど
全部を使用しなければ所望の冷水が得られない場合があ
り、やはり必要とする温水は、ボイラーよりの蒸気を利
用して製造しなければならず、必ずしも効率的な熱エネ
ルギの利用とは言えない。
In order to solve such a drawback, the second conventional technique discloses a technique of driving an absorption refrigerator using a part of the hot water, but the absorption refrigerator has a cooling capacity of 3%. Since it is necessary to double the cooling water load, the desired cold water may not be obtained unless almost all of the hot water obtained using the steam discharged from the boiling pot is used. The hot water to be used must be produced by using the steam from the boiler, which is not necessarily an efficient use of heat energy.

本発明はかかる従来技術の欠点に鑑み、ボイラーの燃焼
コストの大幅低減を図るとともに冷水製造用の冷凍機運
転コストを低減しつつ、ビール製造工程で発生する熱エ
ネルギーを効率的利用を図った熱利用方法を提供する事
を目的とする。
In view of the drawbacks of the prior art, the present invention aims to significantly reduce the combustion cost of the boiler and reduce the operation cost of the refrigerator for producing cold water, while efficiently utilizing the heat energy generated in the beer production process. The purpose is to provide usage methods.

「問題点を解決する為の手段」 本発明はかかる技術的課題を達成する為に、 ボイラー11より供給される蒸気により駆動する膨張機
14にヒートポンプ用圧縮機15を連結して蒸発器19と凝縮
器17を含むヒートポンプシステム23を構成した点、 前記ヒートポンプシステム23の蒸発器19と凝縮器17に
夫々原水を通して冷水と温水を得るようにした点、 前記冷水を仕込工程終了時における麦汁の冷却に、一
方前記温水を所定温度まで加熱した後仕込水又は洗浄水
等に利用させる点、 を必須構成要件とするビール製造工程における熱利用方
法を提案する。
"Means for Solving Problems" In order to achieve the technical problem, the present invention is an expander driven by steam supplied from a boiler 11.
A heat pump compressor 15 is connected to 14 to form a heat pump system 23 including an evaporator 19 and a condenser 17, so that cold water and hot water can be obtained by passing raw water through the evaporator 19 and the condenser 17 of the heat pump system 23, respectively. The point that the cold water is used for cooling wort at the end of the charging step, while the hot water is heated to a predetermined temperature and then used for charging water or washing water, etc. Suggest usage.

「作用」 かかる技術手段によれば、ボイラー11より供給される蒸
気によりヒートポンプシステム23を駆動させ、該ヒート
ポンプシステム23により麦汁冷却用の冷水を得るように
構成した為に、当然に冷凍機駆動用の電力が不要にな
り、電力コストの大幅低減が図れる。
[Operation] According to the technical means, since the heat pump system 23 is driven by the steam supplied from the boiler 11 and the cold water for cooling the wort is obtained by the heat pump system 23, the refrigerator is driven naturally. Electric power for use becomes unnecessary, and the electric power cost can be greatly reduced.

又前記ヒートポンプシステム23においては冷水ととも
に、温水も併せて製造出来る為に、該温水を他の排熱エ
ネルギーを利用して所定温度まで加温した後、温水タン
クに供し、仕込水及び洗浄水として利用する事により、
従来の蒸気による温水製造に比較してボイラー11の蒸気
製造コストを大幅に低減させる事が出来る。
Further, in the heat pump system 23, since hot water can be produced together with cold water, the hot water is heated to a predetermined temperature by using other waste heat energy, and then supplied to a hot water tank to be used as a feed water and a wash water. By using
The steam production cost of the boiler 11 can be significantly reduced as compared with the conventional hot water production using steam.

又、前記ヒートポンプシステム23を駆動させる膨張機14
を背圧型にすることにより排出蒸気圧力を高めて、ビー
ル仕込み工程の加熱に利用することが出来、その分前記
ボイラー11の燃焼コストが一層低減する。
In addition, the expander 14 that drives the heat pump system 23
By making the back pressure type, the exhaust steam pressure can be increased and used for heating in the beer charging process, and the combustion cost of the boiler 11 can be further reduced by that amount.

更に、ビーム煮沸釜4より発生する蒸気を圧縮機5によ
り圧縮し、再利用を図るように構成したシステムにおい
て、前記圧縮機5へ回転力を付与するガスタービン又は
内燃機関(以下ガスタービン等という)の排熱を熱源と
して、前記ボイラー11を運転するように構成する事によ
り、前記ボイラー11の燃焼コストの低減が一層大にな
る。
Furthermore, in a system configured so that the steam generated from the beam boiling pot 4 is compressed by the compressor 5 to be reused, a gas turbine or an internal combustion engine (hereinafter referred to as a gas turbine or the like) that applies a rotational force to the compressor 5 By configuring the boiler 11 to operate by using the exhaust heat of 1) as a heat source, the combustion cost of the boiler 11 can be further reduced.

「実施例」 以下、図面を参照して本発明の好適な実施例を例示的に
詳しく説明する。ただしこの実施例に記載されている構
成部品の寸法、材質、形状、その相対配置などは特に特
定的な記載がない限りは、この発明の範囲をそれのみに
限定する趣旨ではなく、単なる説明例に過ぎない。
[Embodiment] Hereinafter, a preferred embodiment of the present invention will be exemplarily described in detail with reference to the drawings. However, unless otherwise specified, the dimensions, materials, shapes, relative positions, etc. of the components described in this embodiment are not intended to limit the scope of the present invention thereto, but merely illustrative examples. Nothing more than.

図面は本発明の実施例にビール仕込み工程を示し、該工
程は、麦芽粉砕機22、糖化工程24、濾過槽3、煮沸釜
4、熱凝固物分離槽12を有する事は前述した通りで、該
各種装置及び工程に供給する蒸気、温水及び冷水の製造
手順について説明する。
The drawings show a beer charging step in the embodiment of the present invention, which has a malt grinder 22, a saccharification step 24, a filtration tank 3, a boiling pot 4, and a thermal coagulation product separation tank 12 as described above, A procedure for producing steam, hot water, and cold water supplied to the various devices and processes will be described.

同図において、10は燃料ガスにより駆動するガスタービ
ン等で、その出力軸側に、誘導電動機として機能する発
電機8、クラッチ手段7を有する変速機6、及び圧縮機
5が直列に連結され、煮沸釜4より発生する蒸気を圧縮
機5に導入し、該圧縮機5で圧縮した後再び煮沸釜4に
導入し、該煮沸釜の加熱に供した後、熱交換器18に導
き、該熱交換器18で後記するヒートポンプシステム23の
凝縮器17により加温された中温水を加温した後排出され
る。
In the figure, 10 is a gas turbine or the like driven by fuel gas, and a generator 8 functioning as an induction motor, a transmission 6 having a clutch means 7, and a compressor 5 are connected in series on the output shaft side thereof. The steam generated from the boiling kettle 4 is introduced into the compressor 5, compressed by the compressor 5 and then introduced into the boiling kettle 4 again, and after being heated by the boiling kettle, it is introduced into the heat exchanger 18 and the heat The medium temperature water heated by the condenser 17 of the heat pump system 23, which will be described later, is heated by the exchanger 18 and then discharged.

又、前記煮沸釜4で麦汁の煮沸が行われていない時は、
クラッチ手段7により発電機8と圧縮機5間の連結を解
き、ガスタービン等10の駆動力を利用して発電機8のみ
を回転させ、該発電機8より得られた電力を、前記ビー
ル製造工程における工場内各種装置に利用される。
When the wort is not being boiled in the boiling pot 4,
The clutch means 7 releases the connection between the generator 8 and the compressor 5, and only the generator 8 is rotated by using the driving force of the gas turbine 10 or the like, and the electric power obtained from the generator 8 is supplied to the beer production machine. It is used for various devices in the factory in the process.

一方、前記ガスタービン等10の駆動中に得られた排ガス
はボイラー11の熱源として利用され、該ボイラー11によ
って得られた蒸気を、糖化工程24の加熱源として利用す
るとともに、その一部を膨張機14に導き、該膨張機14の
駆動源として利用する。
On the other hand, the exhaust gas obtained while driving the gas turbine 10 or the like is used as a heat source of the boiler 11, the steam obtained by the boiler 11 is used as a heating source of the saccharification step 24, and part of it is expanded. It is led to the machine 14 and used as a drive source of the expander 14.

前記膨張機14は圧縮機15に連結され、凝縮器17及び蒸発
器19とともにヒートポンプシステム23を構成する。
The expander 14 is connected to the compressor 15, and constitutes a heat pump system 23 together with the condenser 17 and the evaporator 19.

そして前記ヒートポンプシステム23においては、例えば
井戸等より20℃の原水20を前記蒸発器19と凝縮器17に導
く事により、先ず蒸発器19に導かれた原水20は、5℃前
後に冷却されて前記仕込み工程最終時における麦汁の冷
却に利用されて該冷却工程中で90℃前後に加温されて糖
化工程24に用いる温水21として利用される。
In the heat pump system 23, for example, by introducing raw water 20 at 20 ° C. from a well or the like to the evaporator 19 and the condenser 17, the raw water 20 first introduced to the evaporator 19 is cooled to around 5 ° C. It is used for cooling the wort at the end of the charging step, is heated to about 90 ° C. in the cooling step, and is used as hot water 21 used in the saccharification step 24.

一方凝縮器17側に導かれた原水20は、該凝縮の為の冷却
水に使用されて38℃前後にまで加熱された後、ヒートポ
ンプ駆動用膨張機の復水器16に導かれ65℃前後の温水を
得る。更にその後、煮沸釜4よりの蒸気ドレンによって
加熱され、85℃〜90℃の温水21を得る。
On the other hand, the raw water 20 guided to the condenser 17 side is used as cooling water for the condensation and heated up to around 38 ° C, and then guided to the condenser 16 of the expander for driving the heat pump to around 65 ° C. Get hot water. After that, it is heated by the steam drain from the boiling pot 4 to obtain the hot water 21 at 85 ° C to 90 ° C.

そしてかかる85℃〜90℃に昇温された温水21は、糖化工
程24の仕込水として、更には濾過槽等の洗浄用温水とし
て夫々利用される。
Then, the hot water 21 heated to 85 ° C. to 90 ° C. is used as charging water for the saccharification step 24 and further as hot water for cleaning the filtration tank and the like.

かかる実施例によれば、従来廃棄されていたヒートポン
プシステム23の凝縮熱を最終的に85℃〜90℃まで加熱
し、有効利用する事ができるとともに、該ヒートポンプ
システム23の駆動は温水21製造の為の蒸気で行なわれる
ので、ヒートポンプシステム23の駆動電力が節約され、
本発明の効果を円滑に達成し得る。
According to this embodiment, the heat of condensation of the heat pump system 23, which has been conventionally discarded, can be finally heated to 85 ° C. to 90 ° C. and can be effectively used, and the heat pump system 23 can be driven by the hot water 21 manufacturing process. Since it is carried out with steam for the purpose of saving the driving power of the heat pump system 23,
The effect of the present invention can be achieved smoothly.

尚、前記製造ラインにおいて、温水の使用が少ない場合
には、前記膨張器14を背圧型にして減圧弁の変わりとし
て用いこれを通過した蒸気を、糖化工程24の加熱を行う
低圧蒸気ライン等に供給するよう構成してもよい。
In the production line, when the amount of hot water used is small, the expander 14 is replaced with a back pressure type and the steam passing therethrough is used as a low pressure steam line for heating the saccharification process 24. It may be configured to supply.

「発明の効果」 以上記載した如く本発明によれば、蒸気製造コストの大
幅低減を可能ならしめるとともに、冷水製造用冷凍機の
駆動用電力若しくは、燃料を不要にし、ビール製造工程
で発生する熱エネルギーの効率的利用を図る事が出来る
等の種々の著効を有する。
[Advantages of the Invention] As described above, according to the present invention, it is possible to significantly reduce the steam production cost, and to eliminate the use of electric power or fuel for driving a chiller for producing cold water and heat generated in the beer production process. It has various remarkable effects such as efficient use of energy.

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

図面は本発明の実施例に係るビール製造ラインの概略構
成を示す工程図である。
The drawings are process diagrams showing a schematic configuration of a beer production line according to an embodiment of the present invention.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 三浦 千太郎 東京都杉並区今川1丁目7番25号 (72)発明者 古嶋 潔 東京都文京区西片2丁目16番14号 (72)発明者 松田 潤二 千葉県習志野市藤崎2丁目6番2−303号 (72)発明者 坂下 茂 東京都練馬区高松3丁目18番10号 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Sentaro Miura 1-7-25 Imagawa, Suginami-ku, Tokyo (72) Inventor Kiyoshi Furushima 2-16-14 Nishikata, Bunkyo-ku, Tokyo (72) Inventor Junji Matsuda Chiba Prefecture Narashino City 2-6 2-303 (72) Inventor Shigeru Sakashita 3-18-10 Takamatsu, Nerima-ku, Tokyo

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】ビールの製造を行う各種工程の熱源として
ボイラーより発生する蒸気を利用するようにしたビール
製造工程における熱利用方法において、 前記ボイラーより供給される蒸気により駆動する膨張機
に圧縮機を連結して、蒸発器及び膨張器を含むヒートポ
ンプシステムを構成し、該ヒートポンプシステムの蒸発
器と凝縮器に夫々原水を通して冷水と温水を得るととも
に、該冷水を麦汁仕込工程最終時における麦汁液の冷却
に、一方前記温水を所定温度まで加熱した後仕込水又は
洗浄水等として利用させた事を特徴とするビール製造工
程における熱利用方法
1. A method for utilizing heat in a beer manufacturing process, wherein steam generated from a boiler is used as a heat source in various processes for manufacturing beer, wherein an expander driven by steam supplied from the boiler is used as a compressor. To form a heat pump system including an evaporator and an expander, cold water and hot water are obtained by passing raw water through an evaporator and a condenser of the heat pump system, respectively, and the cold water is a wort liquid at the final stage of the wort charging step. The method for utilizing heat in the beer manufacturing process, characterized in that the hot water is heated to a predetermined temperature and then used as charging water or washing water
【請求項2】前記膨張機より排出する蒸気を、麦汁仕込
工程の加熱に利用することを特徴とする特許請求の範囲
第1項記載のビール製造工程における熱利用方法
2. A method for utilizing heat in a beer manufacturing process according to claim 1, wherein the steam discharged from the expander is used for heating in the wort charging process.
【請求項3】ビール煮沸釜より発生する蒸気を圧縮機に
より圧縮して蒸気の再利用を図るとともに、前記圧縮機
へ回転力を付与するガスタービン又は内燃機関の排ガス
を熱源として、前記ボイラーを加熱するようにした特許
請求の範囲第1項項記載のビール製造工程における熱利
用方法
3. The boiler is provided with a compressor, which compresses steam generated from a beer boiling pot to reuse the steam, and uses exhaust gas from a gas turbine or an internal combustion engine, which imparts rotational force to the compressor, as a heat source. A method for utilizing heat in the beer production process according to claim 1, wherein the method is for heating.
JP62203497A 1987-08-18 1987-08-18 How to use heat in the beer manufacturing process Expired - Fee Related JPH074212B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62203497A JPH074212B2 (en) 1987-08-18 1987-08-18 How to use heat in the beer manufacturing process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62203497A JPH074212B2 (en) 1987-08-18 1987-08-18 How to use heat in the beer manufacturing process

Publications (2)

Publication Number Publication Date
JPS6447367A JPS6447367A (en) 1989-02-21
JPH074212B2 true JPH074212B2 (en) 1995-01-25

Family

ID=16475136

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62203497A Expired - Fee Related JPH074212B2 (en) 1987-08-18 1987-08-18 How to use heat in the beer manufacturing process

Country Status (1)

Country Link
JP (1) JPH074212B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007333336A (en) * 2006-06-16 2007-12-27 Hitachi Ltd Energy supply system, energy supply method, and energy supply system remodeling method

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004008174A (en) * 2002-06-11 2004-01-15 Asahi Breweries Ltd Manufacturing equipment and method of using waste heat
JP5305099B2 (en) * 2009-04-02 2013-10-02 三浦工業株式会社 Water cooling equipment
CN109185849A (en) * 2018-07-01 2019-01-11 广东省能源研究会 Malt digesting apparatus steam utilization system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
HEAT RECOVERY SYSTEMS=1983 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007333336A (en) * 2006-06-16 2007-12-27 Hitachi Ltd Energy supply system, energy supply method, and energy supply system remodeling method

Also Published As

Publication number Publication date
JPS6447367A (en) 1989-02-21

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