JPS5944558A - Controller for absorption refrigerator - Google Patents

Controller for absorption refrigerator

Info

Publication number
JPS5944558A
JPS5944558A JP15446582A JP15446582A JPS5944558A JP S5944558 A JPS5944558 A JP S5944558A JP 15446582 A JP15446582 A JP 15446582A JP 15446582 A JP15446582 A JP 15446582A JP S5944558 A JPS5944558 A JP S5944558A
Authority
JP
Japan
Prior art keywords
refrigerant
cooling water
liquid
absorption
solution
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.)
Granted
Application number
JP15446582A
Other languages
Japanese (ja)
Other versions
JPH0379631B2 (en
Inventor
滋 坂田
吉井 一寛
雅裕 古川
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.)
Tokyo Sanyo Electric Co Ltd
Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
Sanyo Electric Co Ltd
Sanyo Denki 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 Tokyo Sanyo Electric Co Ltd, Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP15446582A priority Critical patent/JPS5944558A/en
Publication of JPS5944558A publication Critical patent/JPS5944558A/en
Publication of JPH0379631B2 publication Critical patent/JPH0379631B2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (イ)発明の技術分野 本発明は、吸収冷凍機の冷却水と吸収液並びに冷水と冷
媒液との熱交換量を調整する制御装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Technical Field of the Invention The present invention relates to a control device for adjusting the amount of heat exchange between cooling water and absorption liquid of an absorption refrigerator, as well as between cold water and refrigerant liquid.

(ロ)従来技術とその問題点 吸収冷凍機においては、外気温度が低下すると冷却水温
もその影響を受けて低下するために、吸収器の冷却水管
に散布される吸収液の温度が低くなる。その結果、吸収
液の飽和蒸気圧が降下して吸収液の吸収作用が促進され
、冷凍能力換言すれば吸収冷凍機の出力が向上する。し
か■−1外気温度が低下すると冷房負荷も減少するので
、吸収冷凍機の出力が過剰となって所謂冷え過ぎという
問題を生じる。逆に外気温が高くなって冷却水温が上昇
すると吸収作用が抑制され出力不足という問題を生じる
ことになる。
(B) Prior art and its problems In absorption refrigerators, when the outside air temperature falls, the cooling water temperature also falls under the influence of it, so the temperature of the absorption liquid sprayed into the cooling water pipes of the absorber becomes low. As a result, the saturated vapor pressure of the absorption liquid decreases, the absorption action of the absorption liquid is promoted, and the refrigerating capacity, in other words, the output of the absorption refrigerator is improved. However, (1) When the outside air temperature decreases, the cooling load also decreases, so the output of the absorption refrigerator becomes excessive, resulting in the problem of so-called overcooling. On the other hand, when the outside air temperature becomes high and the cooling water temperature rises, the absorption effect is suppressed, resulting in a problem of insufficient output.

また、冷却水温の低下が長時間にわたって続き、しかも
冷却水温の低下の程度が著しく大きい場合には、凝縮器
での冷媒液生成量よりも吸収器で吸収される冷媒量換言
すれば蒸発器での冷媒気化液の方が多くなるために、蒸
発器の冷媒液溜めの冷媒が著しく減少し、冷媒ポンプの
キャピテーシ目ンという弊害も生じる。
In addition, if the cooling water temperature continues to decrease for a long time and the degree of decrease in the cooling water temperature is extremely large, the amount of refrigerant absorbed by the absorber will be greater than the amount of refrigerant produced by the condenser. Since the amount of refrigerant vaporized liquid increases, the amount of refrigerant in the refrigerant reservoir of the evaporator decreases significantly, which also causes the problem of capacity loss of the refrigerant pump.

それ故、冷媒に吸収液を混入して蒸発器における冷媒の
気化作用を抑制する手段により 吸収冷凍機の冷凍能力
即ち出力を低下させることが、従来、行われているが、
斯る従来の手段においては冷却水温が再び一ヒ昇した際
に冷媒を元の状態に戻すことが困かICなために、冷却
水温の変化に対して吸収冷凍機の出力を適確に制御し得
ない欠点がある。
Therefore, it has been conventional practice to reduce the refrigerating capacity, or output, of an absorption refrigerator by mixing an absorption liquid into the refrigerant to suppress the vaporization of the refrigerant in the evaporator.
With such conventional means, it is difficult to return the refrigerant to its original state when the cooling water temperature rises once again.Since the IC is used, it is difficult to accurately control the output of the absorption chiller in response to changes in the cooling water temperature. There are some drawbacks that cannot be avoided.

(ハ)問題点を解決するための手段 本発明は、」1記問題点に鑑み、冷却水温の上昇又は低
下に対応して変化する物η1!館を検出し、この物理量
の変化に応じて吸収器の冷却水管への吸収液散布面積並
びに冷水管への冷媒液散布面請を拡大又は、縮少する制
御手段により、吸収液と冷却水並びに冷媒と冷水の熱交
換量を調節して吸収器における吸収液の吸収作用と蒸発
器におけろ気化作用とを調整し、吸収冷凍機の出力を適
確に制御するようにしたものである。
(c) Means for Solving the Problems In view of the problem described in item 1, the present invention provides an object η1! that changes in response to an increase or decrease in cooling water temperature. The absorption liquid, cooling water, and The amount of heat exchange between the refrigerant and the cold water is adjusted to adjust the absorption action of the absorption liquid in the absorber and the evaporation action in the evaporator, thereby accurately controlling the output of the absorption refrigerator.

に)実施例 図面は、本発明の一実施例である吸収冷凍機を示したも
ので、(1)は発生器、(2)は凝縮器、(3)は蒸発
器、(4)は吸収器及び(5)は溶液熱交換器で、これ
らは溶液ポンプ(6)を有する補液管(7)、濃液管(
8)、冷媒蒸気管(9)、冷媒液流下管θ0)、冷媒ポ
ンプ(11)を有する冷媒還流管02)で接続されてい
る。
2) Embodiment The drawing shows an absorption refrigerator that is an embodiment of the present invention, (1) is a generator, (2) is a condenser, (3) is an evaporator, and (4) is an absorption refrigerator. The container and (5) are solution heat exchangers, which include a liquid replacement pipe (7) with a solution pump (6), a concentrated liquid pipe (
8), a refrigerant vapor pipe (9), a refrigerant liquid flow down pipe θ0), and a refrigerant return pipe 02) having a refrigerant pump (11).

03)は蒸発器(3)に収納した冷水管、θ4)は凝縮
器(2)及び吸収器(4)に収納した冷却水管、(15
)は蒸発器(3)の下部に配設した冷媒液溜めである。
03) is a cold water pipe stored in the evaporator (3), θ4) is a cooling water pipe stored in the condenser (2) and absorber (4), (15)
) is a refrigerant reservoir located at the bottom of the evaporator (3).

(A)は冷却水管04)における冷却水の凝縮器(2)
出口側若しくは入口側に配設した冷却水湿度検出器、(
IJ1は冷媒液溜め05)の冷媒液位検出器、(qは発
生器(1)に配設した冷媒蒸気温度検出器、(IJは濃
液管(8)に配設した濃液温度検出器、(E)及び(F
’)は補液及び濃液の濃度検出器である。
(A) is the cooling water condenser (2) in the cooling water pipe 04)
Cooling water humidity detector installed on the outlet or inlet side, (
IJ1 is the refrigerant level detector in the refrigerant reservoir 05), (q is the refrigerant vapor temperature detector installed in the generator (1), (IJ is the concentrated liquid temperature detector installed in the concentrated liquid pipe (8)) , (E) and (F
') is a concentration detector for replacement fluid and concentrated solution.

ソシテ、06)、a7)ハ、夫々、冷媒分散器、θ8)
、ogIは、夫々、溶液分散器であり、該溶液分散器の
各々と濃液管(8)とは溶液分配管(2O)、01)を
介して接続されており、また、冷媒分散器(16)、α
力と冷媒還流管θ湯とは、各々、冷媒分配管(22)、
(23)を介して接続されている。更に溶液分配管(2
1)及び冷媒分配管(23)には、夫々、制御弁■及び
鵠)が備えである。
Socite, 06), a7) C, refrigerant distributor, θ8)
, ogI are solution dispersers, and each of the solution dispersers and the concentrated liquid pipe (8) are connected via a solution distribution pipe (2O), 01), and the refrigerant disperser ( 16), α
The power and refrigerant return pipe θ water are the refrigerant distribution pipe (22),
(23). Furthermore, a solution distribution pipe (2
1) and the refrigerant distribution pipe (23) are equipped with control valves (1) and (23), respectively.

(24)は冷媒還流管02)の冷媒ポンプθ1)吐出側
と冷媒液溜めθ5)とを接続した冷媒制御弁(3)付き
の冷媒バイパス管、(2阻ま補液管(力の溶液ポンプ(
6)吐出側と吸収器(4)の溶液溜め(26)とを接続
した溶液制御弁菌付きの溶液バイパス管である。
(24) is a refrigerant bypass pipe with a refrigerant control valve (3) that connects the refrigerant pump θ1) discharge side of the refrigerant return pipe 02) and the refrigerant reservoir θ5),
6) A solution bypass pipe with a solution control valve connecting the discharge side and the solution reservoir (26) of the absorber (4).

而して、外気温度が下がって吸収冷凍機へ供給される冷
却水温が低下し始めると前記冷却水湿度検出器囚の信号
により、前記制御弁(■及び尚の開度を絞り、史に冷却
水温が低下し続ければ全閉にする。このようにすること
により、冷媒分配管(23)から冷媒分散器α力へ導か
れる冷媒量と溶液分配管(21)から溶液分散器a■へ
導かれる濃液量が減少し、′  更に散布される冷媒液
と冷水管(I3+内を流れる冷水との熱交換面積及び散
布される濃液と冷却水管04)内を流れる冷却水との熱
交換面積が縮少する結果、吸収器(4)の吸収機能が低
下すると同時に蒸発器(3)の冷媒気化作用も抑制され
て外気温低下に伴なう冷房負荷の減少に対応して冷凍能
力が低下し、負荷に応じた出力制御が可能となる。又、
制御弁(ト)開度の減増に応じて前記溶液制御弁(至)
の開度も増れると共に制御弁W開度の減増に応じて前記
冷媒制御弁(3)の開度も増減されて冷媒液溜め0■か
ら冷媒分散器(16)、(17)へ送られる冷媒液量と
これら分散器Q61.07)から冷媒液溜めa■へ流下
する冷媒液量との均衡が保たれる。この均衡を保つため
に、溶液ポンプ(6)、冷媒ポンプ01)の回転数を制
御する等、吐出量制御可能のポンプを使用するようにし
ても良い。
When the outside air temperature drops and the temperature of the cooling water supplied to the absorption chiller begins to drop, a signal from the cooling water humidity detector reduces the opening of the control valve (■ and If the water temperature continues to drop, close it completely.By doing this, the amount of refrigerant guided from the refrigerant distribution pipe (23) to the refrigerant distributor α force and the amount of refrigerant introduced from the solution distribution pipe (21) to the solution distributor a The amount of concentrated liquid distributed decreases, and the area of heat exchange between the refrigerant liquid sprayed and the cold water flowing in the cold water pipe (I3+ and the heat exchange area between the concentrated liquid sprayed and the cooling water flowing in the cooling water pipe 04) increases. As a result, the absorption function of the absorber (4) decreases, and at the same time, the refrigerant vaporization effect of the evaporator (3) is also suppressed, and the refrigeration capacity decreases in response to the decrease in cooling load due to the decrease in outside temperature. This makes it possible to control the output according to the load.
The solution control valve (to) according to the decrease or increase in the opening degree of the control valve (g)
At the same time, the opening degree of the refrigerant control valve (3) is also increased or decreased in accordance with the decrease or increase in the opening degree of the control valve W, and the refrigerant is sent from the refrigerant reservoir 0 to the refrigerant distributors (16) and (17). A balance is maintained between the amount of refrigerant flowing down from these distributors Q61.07) to the refrigerant reservoir a. In order to maintain this balance, a pump whose discharge amount can be controlled may be used, such as by controlling the rotational speed of the solution pump (6) and the refrigerant pump 01).

尚、図においては、溶液分散器と溶液分配管並びに冷媒
分散器と冷媒分配管とを夫々2個ずつ配設した実施例を
示しているが、これらを多数設け、かつ多数の溶液分配
管と冷媒分配管の夫々に制御弁を備え、冷却水温の低下
の度合いにより各制御弁を段階的に閉じるようにしても
良い このようにすれば、濃液と冷却水並びに冷媒液と
冷水との熱交換面積をより高い精度で調整でき、出力制
御の正確性が向上する。
Although the figure shows an example in which two solution distributors and two solution distribution pipes, two refrigerant distributors and two refrigerant distribution pipes are provided, it is possible to install a large number of these and to connect a large number of solution distribution pipes. Each refrigerant distribution pipe may be provided with a control valve, and each control valve may be closed in stages depending on the degree of decrease in the cooling water temperature.In this way, the heat between the concentrated liquid and the cooling water, as well as between the refrigerant liquid and the cold water, can be closed. The exchange area can be adjusted with higher precision, improving the accuracy of output control.

向弁、冷却水温が低下すると、凝縮器(2)内圧力が低
くなって発生器(1)内圧が低下することと併せて吸収
器(/J)の吸収作用が促進されて補液濃度が降下する
ので、発生器(1)での吸収液の沸騰温度即ち冷媒蒸気
温度が低くなると共に濃液温度も低下し、また濃液濃度
も降下する。或いは又、冷却水温が低下すると吸収作用
が促進され冷媒液溜め(15)の冷媒液位も低下する。
When the cooling water temperature decreases, the pressure inside the condenser (2) decreases and the pressure inside the generator (1) decreases, and the absorption action of the absorber (/J) is promoted, causing the concentration of replacement fluid to drop. Therefore, the boiling temperature of the absorption liquid in the generator (1), that is, the refrigerant vapor temperature becomes lower, the concentrated liquid temperature also decreases, and the concentrated liquid concentration also decreases. Alternatively, when the cooling water temperature decreases, the absorption action is promoted and the refrigerant level in the refrigerant reservoir (15) also decreases.

このように、冷却水温の低下に伴なって変化する物理■
を検出しつつ+ii]記制御弁(■、尚の開度を制御し
ても良い。すなわち前記冷却水温度検出器(5)の代り
に冷媒液位検出器(B)、冷媒蒸気温度検出器fc)、
濃液温度検出器Q−))、補液濃反検出器(E)、濃液
濃度検出器W)のいずれを用いても良い。
In this way, the physics that change as the cooling water temperature decreases
The opening degree of the control valve (■) may also be controlled while detecting the above.In other words, instead of the cooling water temperature detector (5), a refrigerant level detector (B), a refrigerant vapor temperature detector fc),
Any of the concentrated liquid temperature detector Q-)), the replacement liquid concentration detector (E), and the concentrated liquid concentration detector W) may be used.

外気温低下に伴なう冷房負荷の減少に対して吸収冷凍機
の出力を低下せしめるには、冷却水温を直接検出する方
が制御の追従性の点で他の物理量を検出するよりも秀れ
ているが、他面において、冷媒液位を直接検出すること
によって冷媒ポンプ(II)のキャビテーションを確実
に防止できるという利点がある。
In order to reduce the output of an absorption chiller in response to a decrease in cooling load due to a drop in outside temperature, directly detecting the cooling water temperature is superior to detecting other physical quantities in terms of control followability. However, another advantage is that cavitation of the refrigerant pump (II) can be reliably prevented by directly detecting the refrigerant liquid level.

次に、外気温が再び上昇し始め冷却水温が高くなってく
ると、逆に制御弁(ト)及びWの開度を増加し、散布さ
れる濃液量及び冷却水管(]滲への濃液散布面積を拡大
すると共に散布される冷媒汲置及び冷水管03)への冷
媒液散布面積を拡大して負荷の増加に見合う冷凍能力即
ち出力に調整する。
Next, when the outside temperature starts to rise again and the cooling water temperature becomes high, the opening degree of the control valve (G) and W are increased to increase the amount of concentrated liquid sprayed and the concentration in the cooling water pipe ( ). The refrigerating capacity, ie, the output, is adjusted to match the increase in load by expanding the area where the liquid is sprayed and at the same time expanding the area where the refrigerant liquid is sprayed to the refrigerant pump and cold water pipe 03).

尚、本発明は一重効用吸収冷凍機に限らず、二重効用吸
収冷凍機にも適用できることは勿論のととξであり、か
つまた、二重効用吸収冷凍機に供給する冷却水温の変化
に対応して変化する物理量発 として高温発生器から低温掛生器へ流通する吸収液の温
度や濃度を検出して出力調整ずろことも可能である (ホ)発明の効果 以上のように、本発明制御装置は、冷却水温度変化に伴
なう物理量変化を検出しつつ冷水管への冷媒液散布面積
を調整すると同時に冷却水管への吸収液散布面積を調整
するようにしたものであるから、吸収器における吸収液
の冷媒吸収作用と蒸発器における冷媒気化作用とをバラ
ンス良く調節でき、負荷に見合う出力を安定的に得られ
、かつ冷媒ポンプのキャビテーシヨンを防市できる等実
用上有益な効果を奏するものである。
It should be noted that the present invention is of course applicable not only to single-effect absorption chillers but also to double-effect absorption chillers, and is also applicable to changes in the temperature of cooling water supplied to the double-effect absorption chillers. It is also possible to adjust the output by detecting the temperature and concentration of the absorbent flowing from the high-temperature generator to the low-temperature hanger as a correspondingly changing physical quantity. (E) Effects of the Invention As described above, the present invention The control device detects changes in physical quantities due to changes in cooling water temperature and adjusts the area of refrigerant sprayed onto the cooling water pipes, and at the same time adjusts the area of absorption liquid sprayed onto the cooling water pipes. The refrigerant absorption effect of the absorbing liquid in the evaporator and the refrigerant vaporization effect in the evaporator can be adjusted in a well-balanced manner, resulting in a stable output commensurate with the load, as well as practical benefits such as preventing cavitation in the refrigerant pump. It is something to play.

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

図面は、本発明の一実施例を/]′:、シた措成販路図
であろう (1)・−・発生器、 (2)・・・凝縮器、 (3)
・・・蒸発器、(4)・・・吸収器、(5)・・・溶液
熱交換器、 03)・・・除水管、(14)・・・冷却
水管、 (I5)・・・冷媒液溜め、 (旧、(17)
・・・冷媒分散器、 (ILθ9・・・溶液分散器、 
(加)、(2+1・・・溶液分配臂、 (2,り、(2
軒・・冷媒分配管、 c!4)・・・冷媒バイパス管、
 (25)・・・溶液バイパス管、 (5)・・・冷却
水温度検出器、 (I3)・・・冷媒液位検出器、 (
Q・・・冷媒蒸気温度検出器、 (至)・・・濃液温度
検出器、 (I→・・・稀酸濃度検出器、 (ト)・・
・濃液濃度検出器、 (V)、W・・・制御弁、 (X
)・・・冷媒制御弁、 0′)・・・溶、1に制御弁。
The drawings show an embodiment of the present invention. (1) Generator, (2) Condenser, (3)
... Evaporator, (4) ... Absorber, (5) ... Solution heat exchanger, 03) ... Water removal pipe, (14) ... Cooling water pipe, (I5) ... Refrigerant Liquid reservoir, (old, (17)
...refrigerant disperser, (ILθ9...solution disperser,
(Add), (2+1...Solution distribution arm, (2, Ri, (2
Eaves... Refrigerant distribution piping, c! 4)...refrigerant bypass pipe,
(25)...Solution bypass pipe, (5)...Cooling water temperature detector, (I3)...Refrigerant level detector, (
Q...Refrigerant vapor temperature detector, (To)...Concentrated liquid temperature detector, (I→...Dilute acid concentration detector, (G)...
・Concentrated liquid concentration detector, (V), W...control valve, (X
)...refrigerant control valve, 0')...melt, 1 control valve.

Claims (1)

【特許請求の範囲】[Claims] (1)発生器、凝縮器、蒸発器、吸収器及び溶液熱交換
器を配管接続して成る吸収冷凍機において、吸収器に収
納した冷却水管へ吸収液を散布する溶液分散器と蒸発器
に収納した冷水管へ冷媒液を散布する冷媒分散器とを複
数個設けると共に溶液分散器の夫々に吸収液を導く溶液
分配管と冷媒分散器の夫々に冷媒液を導く冷媒分配管と
を設け、冷却水温度の変化に対応して変化する物理量を
感知する検出器の信号により、吸収液が導かれる溶液分
散器と冷媒液が導かれる冷媒分散器の個数を制御する機
構を備え、冷却水管への吸収液散布面積と冷水管への冷
媒液散布面積とを調整するようにしたことを特徴とする
吸収冷凍機の制御装置。
(1) In an absorption chiller that consists of a generator, condenser, evaporator, absorber, and solution heat exchanger connected via piping, the solution disperser and evaporator that spray the absorption liquid to the cooling water pipes housed in the absorber A plurality of refrigerant distributors for dispersing refrigerant liquid to the stored cold water pipes are provided, and a solution distribution pipe for guiding the absorption liquid to each of the solution distributors and a refrigerant distribution pipe for guiding the refrigerant liquid to each of the refrigerant distributors are provided, Equipped with a mechanism that controls the number of solution distributors to which the absorption liquid is guided and the number of refrigerant distributors to which the refrigerant liquid is guided, based on signals from a detector that senses physical quantities that change in response to changes in the cooling water temperature, and is connected to the cooling water pipes. A control device for an absorption refrigerating machine, characterized in that the absorption liquid distribution area and the refrigerant liquid distribution area in the cold water pipes are adjusted.
JP15446582A 1982-09-03 1982-09-03 Controller for absorption refrigerator Granted JPS5944558A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15446582A JPS5944558A (en) 1982-09-03 1982-09-03 Controller for absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15446582A JPS5944558A (en) 1982-09-03 1982-09-03 Controller for absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS5944558A true JPS5944558A (en) 1984-03-13
JPH0379631B2 JPH0379631B2 (en) 1991-12-19

Family

ID=15584834

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15446582A Granted JPS5944558A (en) 1982-09-03 1982-09-03 Controller for absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS5944558A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01273965A (en) * 1988-04-25 1989-11-01 Mitsubishi Heavy Ind Ltd Absorption refrigerating machine
JPH02166361A (en) * 1988-12-20 1990-06-27 Sanyo Electric Co Ltd Absorption refrigerator
JPH0395364A (en) * 1989-09-08 1991-04-19 Hitachi Ltd Capacitor controller for absorption refrigerating machine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01273965A (en) * 1988-04-25 1989-11-01 Mitsubishi Heavy Ind Ltd Absorption refrigerating machine
JPH02166361A (en) * 1988-12-20 1990-06-27 Sanyo Electric Co Ltd Absorption refrigerator
JPH0395364A (en) * 1989-09-08 1991-04-19 Hitachi Ltd Capacitor controller for absorption refrigerating machine

Also Published As

Publication number Publication date
JPH0379631B2 (en) 1991-12-19

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