JPH07218024A - Absorption type chilled and warm water generator - Google Patents

Absorption type chilled and warm water generator

Info

Publication number
JPH07218024A
JPH07218024A JP6010275A JP1027594A JPH07218024A JP H07218024 A JPH07218024 A JP H07218024A JP 6010275 A JP6010275 A JP 6010275A JP 1027594 A JP1027594 A JP 1027594A JP H07218024 A JPH07218024 A JP H07218024A
Authority
JP
Japan
Prior art keywords
valve
liquid level
temperature regenerator
absorber
high temperature
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
JP6010275A
Other languages
Japanese (ja)
Inventor
Yoshikatsu Kishi
吉旦 岸
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP6010275A priority Critical patent/JPH07218024A/en
Publication of JPH07218024A publication Critical patent/JPH07218024A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To hold a supply amount and a return amount in balance by providing a control valve in series with a float valve in a solution distribution conduit, installing a bypass valve for bypassing them, switching the control vale by a liquid level of an absorber or a pressure of a high temperature regenerator, and supplying solution to the regenerator. CONSTITUTION:A dropped liquid level of an absorber 5 is detected by a liquid level switch 16, and a pressure of a high temperature regenerator 9 is detected by a pressure switch 17. When two conditions are satisfied, a control valve 13 provide din series with a float valve 15 in a solution distribution conduit is fully closed by an electric signal, and a control valve 14 is fully opened. A dropped liquid level of the absorber 5 is controlled by a flow rate regulating valve 18 as a bypass valve provided at a secondary side of the valve 14, a concentrated solution liquid level is raised, the valve 15 is fully closed, and dilute solution passed through a valve gap at the time of fully closing the valve 15 is supplied to the regenerator 9. Thus, at the time of starting and stopping a circulating malfunction due to a liquid level drop of the absorber 5 can be eliminated.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、吸収式冷温水機に係
り、特に、小形吸収式直焚冷温水発生機のオン−オフ制
御を行う冷温水発生機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption chiller / hot water generator, and more particularly to a chiller / hot water generator for performing on / off control of a small absorption type direct-fired chilled / hot water generator.

【0002】[0002]

【従来の技術】従来、高温再生器の給液量を制御する方
法は、給液配管系にフロート弁を設け、高温再生器の濃
溶液戻り量をフロートボックスに導き、そのボックス内
の液面レベルでフロートを浮動させ、供給量を制御する
フロート弁制御が一般的である。
2. Description of the Related Art Conventionally, a method of controlling the liquid supply amount of a high temperature regenerator is to install a float valve in the liquid supply piping system, guide the concentrated solution return amount of the high temperature regenerator to a float box, and Float valve control in which the float is floated at a level and the supply amount is controlled is common.

【0003】[0003]

【発明が解決しようとする課題】従来技術のフロート弁
制御は、小容量の冷温水発生機では、制御循環量が小さ
いため、弁の作動状態や、弁のリーフ量が、サイクルを
形成するうえで非常に重要な部分となる。このため、フ
ロート弁の製作精度,信頼性が冷温水発生機の信頼性を
決めることになる。
In the float valve control of the prior art, since the control circulation amount is small in the small capacity hot and cold water generator, the operating state of the valve and the leaf amount of the valve form a cycle. Is a very important part. Therefore, the manufacturing accuracy and reliability of the float valve determine the reliability of the cold / hot water generator.

【0004】しかし、フロート弁は、動作が不安定にな
ったり、作動しなくなる事が懸念される不具合要因を持
っている。特に、フロート弁の動作や、弁の加工精度に
よっては少量の循環量を制御する事が難しく、このため
小容量機ではフロート弁全閉時のリーク量が供給量−戻
り量の関係に大きな影響を与える。
However, the float valve has a defect factor that may cause unstable operation or may not operate. In particular, it is difficult to control a small amount of circulation depending on the operation of the float valve and the processing accuracy of the valve.Therefore, in a small capacity machine, the leak amount when the float valve is fully closed has a great effect on the relationship between the supply amount and the return amount. give.

【0005】本発明の目的はフロート弁の全閉リーク量
の精度にたよらず常に一定の給液方式を行い、供給量と
戻り量のバランスを保ち、冷温水発生機の信頼性を向上
させる事にある。
An object of the present invention is to always perform a constant liquid supply method regardless of the accuracy of the fully closed leak amount of the float valve, maintain a balance between the supply amount and the return amount, and improve the reliability of the cold / hot water generator. It is in.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するた
め、本発明は高温再生器へ供給する臭化リチウム水溶液
(以下、単に溶液)配管路にフロート弁とシリーズに制
御弁を設け、これらをバイパスするバイパス弁を設置
し、吸収器の液面レベルや高温再生器の圧力等により、
それぞれの制御弁を開閉させる事で、溶液を高温再生器
へ供給される機構とする。
In order to achieve the above object, the present invention provides a float valve and a series control valve in a lithium bromide aqueous solution (hereinafter simply referred to as solution) pipe line to be supplied to a high temperature regenerator. Bypass valve is installed to bypass the liquid level of the absorber and the pressure of the high temperature regenerator.
By opening and closing each control valve, the solution is supplied to the high temperature regenerator.

【0007】[0007]

【作用】高温再生器への入熱量を制御する方式は、比例
式,四位置,三位置,オン−オフ制御と、種々あるが、
その制御信号は、一般に負荷により変化する冷温水温度
をセンサ等で検出し、その信号を温調計へ入力し、設定
した温度に対する偏差量を演算処理し、結果を出力信号
として高温再生器の入熱量を制御する制御機器へ出力し
入熱量を制御する。高温再生器では、その入熱により希
釈溶液が加熱され、希釈溶液中の冷媒を冷媒蒸気として
取り出し、溶液は濃縮され高温再生器中の溶液保有量が
減少する。このため、再び、希釈溶液が供給されるが、
濃縮された溶液は、希釈のため、吸収器へ戻るため、吸
収器へ戻る濃溶液量と、高温再生器へ供給する溶液の供
給量のバランスを保つ制御機構が必要である。
There are various methods for controlling the heat input to the high temperature regenerator, such as proportional expression, four-position, three-position and on-off control.
As for the control signal, the temperature of cold / hot water that generally changes depending on the load is detected by a sensor, etc., that signal is input to the temperature controller, the deviation amount for the set temperature is arithmetically processed, and the result is used as an output signal of the high temperature regenerator. The heat input is output to a control device that controls the heat input to control the heat input. In the high temperature regenerator, the diluted solution is heated by the heat input, the refrigerant in the diluted solution is taken out as a refrigerant vapor, the solution is concentrated, and the amount of solution retained in the high temperature regenerator is reduced. Therefore, the diluted solution is supplied again,
Since the concentrated solution returns to the absorber for dilution, a control mechanism for maintaining the balance between the amount of concentrated solution returning to the absorber and the amount of solution supplied to the high temperature regenerator is necessary.

【0008】溶液の供給と戻る液量のバランスは、高温
再生器から戻る液量を液面レベルにより検出し、その結
果供給側の給液制御弁と連動させ制御するフロート弁制
御により行っている。このフロート弁は、高温再生器の
器内と同一圧力室となるフロート室に収納されており、
給液は浮液循環ポンプの押し込み圧により高温再生器へ
供給され、戻り溶液は、高温再生器の圧力ヘッドと位置
ヘッド及び吸収器へ戻る液エゼクタの駆動力により吸収
器へ戻る。この給液と戻り液との関係は、吸収器と高温
再生器の圧力差が小さい程アンバランスとなる。
The balance between the supply of the solution and the amount of the returned liquid is carried out by the float valve control in which the amount of the liquid returned from the high temperature regenerator is detected by the liquid level and as a result, the liquid supply control valve on the supply side is interlocked with and controlled. . This float valve is housed in the float chamber, which is the same pressure chamber as the inside of the high temperature regenerator.
The feed liquid is supplied to the high temperature regenerator by the pushing pressure of the floating liquid circulation pump, and the return solution returns to the absorber by the driving force of the pressure head and the position head of the high temperature regenerator and the liquid ejector returning to the absorber. The relationship between the supply liquid and the return liquid becomes unbalanced as the pressure difference between the absorber and the high temperature regenerator becomes smaller.

【0009】本発明では、供給量と戻り量がアンバラン
スとなった場合、吸収器の液面が低下し、溶液循環ポン
プがキャビテーションに入り、不安定な運転となるた
め、吸収器の液面と、高温再生器の圧力を検出し、吸収
器の液面がポンプキャビテーション液面レベルに到達し
た場合又は、高温再生器圧力がある基準圧力以下となっ
た場合、フロート弁制御によらず供給量を一定に絞り、
ポンプのキャビテーションを防止する制御システムを作
る。
In the present invention, when the supply amount and the return amount are unbalanced, the liquid level of the absorber lowers, the solution circulation pump enters cavitation, and the operation becomes unstable. When the pressure of the high temperature regenerator is detected and the liquid level of the absorber reaches the pump cavitation level, or when the high temperature regenerator pressure falls below a certain reference pressure, the supply amount will not depend on the float valve control. To a constant
Create a control system to prevent pump cavitation.

【0010】[0010]

【実施例】以下、本発明の一実施例を図1,図2により
説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIGS.

【0011】図1は、本発明の直焚吸収式二重効用冷温
水発生器のサイクルについて説明する。
FIG. 1 illustrates a cycle of a direct-burning absorption double-effect cold / hot water generator of the present invention.

【0012】蒸発器1内は、約百分の一気圧に保たれて
おり、この中で冷媒2(水)は、冷媒ポンプ3により冷
水の熱を奪い蒸発して、冷却効果が生じる。蒸発した冷
媒蒸気は、冷却水により低圧に保たれ、吸収器5へ流れ
込み、ここで吸収器伝熱管6の上にスプレーされる溶液
により吸収され溶液は希釈される。この希釈溶液は、溶
液ポンプ7により熱交換器8を経て、一部は高温再生器
9へ、残りは低温再生器10へ、それぞれ送り込まれ、
高温再生器9では、直接、熱源11により、加熱されて
蒸気と濃溶液に分離される。
The inside of the evaporator 1 is maintained at about one-hundredth atmospheric pressure, in which the refrigerant 2 (water) takes heat of the cold water by the refrigerant pump 3 and evaporates, thereby producing a cooling effect. The evaporated refrigerant vapor is kept at a low pressure by the cooling water and flows into the absorber 5, where it is absorbed by the solution sprayed on the absorber heat transfer tube 6 and the solution is diluted. This diluted solution is sent to the high temperature regenerator 9 and the rest to the low temperature regenerator 10 through the heat exchanger 8 by the solution pump 7,
In the high temperature regenerator 9, it is directly heated by the heat source 11 and separated into vapor and concentrated solution.

【0013】一方、低温再生器10では、希釈溶液は高
温再生器9で発生した蒸気により、加熱されて蒸気と、
濃溶液に分離される。この様にして濃縮された溶液は、
再び熱交換器8を経て吸収器5内にスプレーされる。
On the other hand, in the low temperature regenerator 10, the diluted solution is heated by the steam generated in the high temperature regenerator 9 to form steam.
Separated into a concentrated solution. The solution thus concentrated is
It is sprayed again into the absorber 5 via the heat exchanger 8.

【0014】また、低温再生器10で溶液を加熱し、凝
縮したドレンは、凝縮器12へ導かれる。
Further, the drainage obtained by heating the solution in the low temperature regenerator 10 and condensing is introduced into the condenser 12.

【0015】一方、低温再生器10で発生した蒸気は、
凝縮器12で凝縮する。この様にして出来た凝縮冷媒
は、蒸発器へ導かれ、スプレーされてサイクルを一循す
る。
On the other hand, the steam generated in the low temperature regenerator 10 is
It is condensed in the condenser 12. The condensed refrigerant thus produced is guided to the evaporator, sprayed, and cycled once.

【0016】ここで、高温再生器9へ供給される溶液量
の制御方式について、図2により説明する。
The control method of the amount of solution supplied to the high temperature regenerator 9 will be described with reference to FIG.

【0017】図2は、本発明による高温再生器9への溶
液供給系統と、供給量を調節する制御弁13,14をコ
ントロールする機能について説明する。
FIG. 2 illustrates the function of controlling the solution supply system to the high temperature regenerator 9 and the control valves 13 and 14 for adjusting the supply amount according to the present invention.

【0018】高温再生器9へ供給される希釈溶液は、運
転中フロート弁15により高温再生器9から戻る濃溶液
のフロートボックス16の濃溶液液面レベルをフロート
弁15により検出制御される。
The diluted solution supplied to the high temperature regenerator 9 is controlled by the float valve 15 to detect the liquid level of the concentrated solution in the float box 16 of the concentrated solution returned from the high temperature regenerator 9 during operation.

【0019】濃溶液液面レベルが上昇し、フロート弁1
5が全閉となると、以後はフロート弁15の全閉時の弁
ギャップを通過する希釈溶液が、高温再生器9へ供給さ
れる。高温再生器9の圧力が高い場合は、供給側と戻り
側の溶液バランスは保たれ、吸収器5の液面は溶液ポン
プ7のキャビテーション液面以上に保たれるが、高温再
生器9の圧力が低い場合、戻り側の流路圧損との関係で
液が戻りにくくなり、吸収器5の液面が降下してくる。
この降下液面レベルを液面スイッチ16で検出し、更に
高温再生器9の圧力条件も必要のため、高温再生器9の
圧力を圧力スイッチ17により検出し、二つの条件が備
わった時に電気的信号により制御弁13を全閉にし、制
御弁14を全開とする。この結果、制御弁14の二次側
に設けられた流量調節弁18により、一定流量に絞ら
れ、給液量を制御し、吸収器5の降下液面を制御する。
The liquid level of the concentrated solution rises, and the float valve 1
When 5 is fully closed, the diluted solution that subsequently passes through the valve gap when the float valve 15 is fully closed is supplied to the high temperature regenerator 9. When the pressure of the high temperature regenerator 9 is high, the solution balance between the supply side and the return side is maintained and the liquid level of the absorber 5 is maintained above the cavitation liquid level of the solution pump 7. Is low, it becomes difficult for the liquid to return due to the pressure loss of the flow path on the return side, and the liquid level of the absorber 5 drops.
This falling liquid level is detected by the liquid level switch 16, and the pressure condition of the high temperature regenerator 9 is also necessary. Therefore, the pressure of the high temperature regenerator 9 is detected by the pressure switch 17, and when two conditions are provided, an electrical condition is set. The signal causes the control valve 13 to be fully closed and the control valve 14 to be fully open. As a result, the flow rate control valve 18 provided on the secondary side of the control valve 14 restricts the flow rate to a constant flow rate, controls the liquid supply amount, and controls the descending liquid level of the absorber 5.

【0020】[0020]

【発明の効果】本発明によれば、小形冷温水発生機の起
動時、及び、停止時の吸収器液面低下による循環不具合
が解消され、フロート弁の弁加工精度の緩和,最少循環
量の確保等、機器の運転上の信頼性が向上する。
EFFECTS OF THE INVENTION According to the present invention, the circulation problem due to the drop in the liquid level of the absorber at the time of starting and stopping the small cold / hot water generator is solved, the valve processing accuracy of the float valve is relaxed, and the minimum circulation amount is reduced. The operational reliability of the equipment, such as securing it, is improved.

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

【図1】冷温水発生機のサイクル循環の系統図。FIG. 1 is a system diagram of cycle circulation of a cold / hot water generator.

【図2】本発明の高温再生器の溶液供給制御機構の系統
図。
FIG. 2 is a system diagram of a solution supply control mechanism of the high temperature regenerator of the present invention.

【符号の説明】[Explanation of symbols]

5…吸収器、9…高温再生器、11…熱源、13…制御
弁、14…制御弁、15…フロート弁、16…液面スイ
ッチ、17…圧力スイッチ、18…流量調整弁、19…
バイパス配管。
5 ... Absorber, 9 ... High temperature regenerator, 11 ... Heat source, 13 ... Control valve, 14 ... Control valve, 15 ... Float valve, 16 ... Liquid level switch, 17 ... Pressure switch, 18 ... Flow control valve, 19 ...
Bypass piping.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】蒸発器,吸収器,凝縮器,低温および高温
再生器,熱交換器,これらを互いに作動させサイクルを
継続的に維持する冷媒ポンプ,溶液ポンプを含む吸収式
冷温水発生機において、前記高温再生器への臭化リチウ
ム水溶液の供給量を制御する方式に、前記高温再生器か
ら戻る前記臭化リチウム水溶液の液面により制御される
フロート式制御弁と、シリーズ及び並列に前記臭化リチ
ウム水溶液の供給配管路に弁と、前記弁の開閉指令を前
記吸収器の液面や前記高温再生器の圧力により前記臭化
リチウム水溶液の供給量を制御する制御機構とを設けて
なる事を特徴とする吸収式冷温水発生機。
1. An absorption-type cold / hot water generator including an evaporator, an absorber, a condenser, a low-temperature and high-temperature regenerator, a heat exchanger, a refrigerant pump for operating these components continuously to maintain a cycle, and a solution pump. , A method of controlling the supply amount of the lithium bromide aqueous solution to the high temperature regenerator, a float type control valve controlled by the liquid level of the lithium bromide aqueous solution returning from the high temperature regenerator, and the odor in series and in parallel. A valve is provided in the supply line of the lithium bromide aqueous solution, and a control mechanism for controlling the opening / closing command of the valve to control the supply amount of the lithium bromide aqueous solution by the liquid level of the absorber or the pressure of the high temperature regenerator. An absorption type cold / hot water generator characterized by.
JP6010275A 1994-02-01 1994-02-01 Absorption type chilled and warm water generator Pending JPH07218024A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6010275A JPH07218024A (en) 1994-02-01 1994-02-01 Absorption type chilled and warm water generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6010275A JPH07218024A (en) 1994-02-01 1994-02-01 Absorption type chilled and warm water generator

Publications (1)

Publication Number Publication Date
JPH07218024A true JPH07218024A (en) 1995-08-18

Family

ID=11745769

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6010275A Pending JPH07218024A (en) 1994-02-01 1994-02-01 Absorption type chilled and warm water generator

Country Status (1)

Country Link
JP (1) JPH07218024A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007263464A (en) * 2006-03-28 2007-10-11 Sanyo Electric Co Ltd Absorption cold/hot water supply apparatus
JP2016176604A (en) * 2015-03-18 2016-10-06 ジョンソンコントロールズ ヒタチ エア コンディショニング テクノロジー(ホンコン)リミテッド Absorption refrigeration machine and controlling method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007263464A (en) * 2006-03-28 2007-10-11 Sanyo Electric Co Ltd Absorption cold/hot water supply apparatus
JP2016176604A (en) * 2015-03-18 2016-10-06 ジョンソンコントロールズ ヒタチ エア コンディショニング テクノロジー(ホンコン)リミテッド Absorption refrigeration machine and controlling method thereof

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