JPS6113551B2 - - Google Patents

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Publication number
JPS6113551B2
JPS6113551B2 JP272879A JP272879A JPS6113551B2 JP S6113551 B2 JPS6113551 B2 JP S6113551B2 JP 272879 A JP272879 A JP 272879A JP 272879 A JP272879 A JP 272879A JP S6113551 B2 JPS6113551 B2 JP S6113551B2
Authority
JP
Japan
Prior art keywords
solution
heating amount
detection device
danger
dilution
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
Application number
JP272879A
Other languages
Japanese (ja)
Other versions
JPS5595071A (en
Inventor
Osayuki Inoe
Toshio Matsubara
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP272879A priority Critical patent/JPS5595071A/en
Publication of JPS5595071A publication Critical patent/JPS5595071A/en
Publication of JPS6113551B2 publication Critical patent/JPS6113551B2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 本発明は吸収冷凍機に関するものである。[Detailed description of the invention] The present invention relates to an absorption refrigerator.

従来の吸収冷凍機の例を第1図に示せば、吸収
器A、蒸発器E、発生器G、凝縮器C、溶液熱交
換器X、溶液ポンプSP、冷媒ポンプRPが備えら
れている。これらの機器を接続して管路1,2,
3,4,5、散布管6、管路7,8、散布管9、
管路10、膨張弁11が設けられている。冷媒ポ
ンプRPの吐出側の管路8と溶液ポンプSPの吸込
側の管路1とは、稀釈弁SVを備えた稀釈回路1
3により接続されている。
An example of a conventional absorption refrigerator is shown in FIG. 1, which includes an absorber A, an evaporator E, a generator G, a condenser C, a solution heat exchanger X, a solution pump SP, and a refrigerant pump RP. Connect these devices and connect pipes 1, 2,
3, 4, 5, spray pipe 6, pipe lines 7, 8, spray pipe 9,
A conduit 10 and an expansion valve 11 are provided. A pipe line 8 on the discharge side of the refrigerant pump RP and a pipe line 1 on the suction side of the solution pump SP are a dilution circuit 1 equipped with a dilution valve SV.
Connected by 3.

14は加熱管であり、発生器G内の溶液を加熱
するために蒸気などの熱媒流体が導かれ、その熱
媒流体の流量は加熱量制御弁HVで制御され加熱
量の調節が行なわれる。15は冷水管であり、冷
水出口温度を温度検出器16にて検出し、その信
号により加熱量制御弁HVを調節するようになつ
ている。17,18は冷却水管である。
Reference numeral 14 denotes a heating pipe through which a heat medium fluid such as steam is guided to heat the solution in the generator G, and the flow rate of the heat medium fluid is controlled by a heating amount control valve HV to adjust the amount of heating. . Reference numeral 15 denotes a cold water pipe, and the cold water outlet temperature is detected by a temperature detector 16, and the heating amount control valve HV is adjusted based on the signal. 17 and 18 are cooling water pipes.

19はフロートスイツチであり蒸発器E内の冷
媒液面を検出することにより、溶液の濃度を間接
的に検出する濃度相当値検出装置として作用して
結晶危険度を検出し、その危険信号により稀釈弁
SVを操作するようになつている。
19 is a float switch which acts as a concentration equivalent value detection device that indirectly detects the concentration of the solution by detecting the refrigerant liquid level in the evaporator E, detects the danger level of crystals, and uses the danger signal to dilute the liquid. valve
It is now possible to operate SV.

このような従来例のものにおいては、運転時の
溶液の過濃縮を防止するために、フロートスイツ
チ19により溶液濃度を推定し、結晶が起こるお
それがあるような濃度に相当する液面高さを検出
した場合には、信号を発して通常は閉じている稀
釈弁SVを開いて冷媒液を溶液中に混入せしめて
溶液を稀釈し、過濃縮による結晶化を防止してい
る。
In such conventional systems, in order to prevent over-concentration of the solution during operation, the float switch 19 estimates the solution concentration and determines the liquid level height corresponding to the concentration that may cause crystallization. When detected, a signal is generated to open the normally closed dilution valve SV to mix refrigerant into the solution to dilute the solution and prevent crystallization due to overconcentration.

しかし、従来においては、稀釈弁SVを開いて
稀釈を行なつている場合でも加熱量制御弁HVの
開度を行なつている場合でも加熱量制御弁HVの
開度は、その時の冷水負荷に対応した開度のまま
となつている。一方、全負荷時には加熱量制御弁
HVは全開となつており、しかも一般に全負荷時
に過濃縮が生ずる可能性が大であり、この場合に
危険信号が発せられ稀釈が行なわれるが加熱量制
御弁HVは全開のままとなつている。
However, in the past, whether dilution was performed by opening the dilution valve SV or by changing the opening degree of the heating amount control valve HV, the opening degree of the heating amount control valve HV was determined based on the chilled water load at that time. It remains at the corresponding opening. On the other hand, at full load, the heating amount control valve
The HV is fully open, and there is generally a high possibility that overconcentration will occur at full load, in which case a danger signal will be issued and dilution will be performed, but the heating amount control valve HV remains fully open. .

このように稀釈を行なう必要がある場合には、
多くの場合加熱量制御弁HVは全開であり、ある
いはかなり開いた状態にあるので、稀釈回路13
にて溶液を稀釈する一方、発生器Gにて溶液を濃
縮する、という無駄があつた。また、稀釈弁SV
のサイズを決定する場合は、加熱量制御弁HVが
全開となり、100%負荷に相当する加熱媒体が発
生器Gに供給されている時に発生器Gで加熱分離
される冷媒量以上の冷媒量を、冷媒系統から溶液
系統に移動せしめるに十分なサイズでなければな
らず、稀釈弁SVが大型となる欠点があつた。
If it is necessary to dilute in this way,
In many cases, the heating amount control valve HV is fully open or considerably open, so the dilution circuit 13
There was a waste of diluting the solution in the generator G while concentrating the solution in the generator G. In addition, dilution valve SV
When determining the size of the refrigerant, determine the amount of refrigerant that is greater than or equal to the amount of refrigerant that is heated and separated by generator G when the heating amount control valve HV is fully open and heating medium equivalent to 100% load is supplied to generator G. However, the dilution valve SV had to be large enough to be transferred from the refrigerant system to the solution system, which resulted in a large dilution valve SV.

本発明は、結晶の発生する危険度を検出し、そ
の検出信号により稀釈回路を作動せしめて溶液の
稀釈を行なうと共に、発生器の加熱量調節機構を
操作して加熱量を減少せしめて所定の低加熱量に
なるよう制御することにより、従来のものの上記
の欠点を除き、稀釈作用時には溶液の濃縮作用も
低減せしめ、無駄なエネルギの消費を防ぎ、かつ
稀釈作用が短時間で効果的に行なわれ、かつ稀釈
弁を小型とすることができる吸収冷凍機を提供す
ることを目的とするものである。
The present invention detects the degree of risk of crystal formation, operates a dilution circuit based on the detection signal to dilute the solution, and operates the heating amount adjustment mechanism of the generator to reduce the heating amount to a predetermined level. By controlling the amount of heating to a low level, it eliminates the above-mentioned drawbacks of conventional products, and also reduces the concentration effect of the solution during dilution, prevents wasted energy consumption, and allows the dilution to be performed effectively in a short time. It is an object of the present invention to provide an absorption refrigerator in which the dilution valve can be made small.

本発明は、蒸発器、吸収器、発生器、凝縮器、
溶液熱交換器、前記発生器における加熱量調節機
構、冷媒ポンプ、溶液ポンプ及び機器間を接続す
る経路とにより溶液サイクルと冷媒サイクルとが
形成されている吸収冷凍機において、冷凍能力と
負荷量との相対関係に応じて前記加熱量調節機構
に容量制御信号を与えて制御する容量制御機構が
備えられ、前記冷媒サイクル中の冷媒液部と前記
溶液サイクル中の一部とを稀釈用制御弁を介して
接続する稀釈回路が備えられ、前記溶液サイクル
中の溶液の結晶危険度を検出する結晶危険度検出
装置が備えられ、該結晶危険度検出装置は、所定
の危険度を超える危険度を検出した場合に危険信
号を発し、該危険信号により前記稀釈用制御弁が
開かれて濃溶液が稀釈されると共に、前記危険信
号により前記加熱量調節機構が前記容量制御信号
に優先して制御されて加熱量が低減され、所定の
低加熱量となるよう構成されたことを特徴とする
吸収冷凍機である。
The present invention provides evaporators, absorbers, generators, condensers,
In an absorption refrigerator in which a solution cycle and a refrigerant cycle are formed by a solution heat exchanger, a heating amount adjustment mechanism in the generator, a refrigerant pump, a solution pump, and a path connecting the equipment, the refrigerating capacity and the load amount are A capacity control mechanism is provided for controlling the heating amount adjusting mechanism by giving a capacity control signal to the heating amount adjusting mechanism according to the relative relationship between the heating amount adjusting mechanism, and a dilution control valve for controlling the refrigerant liquid part in the refrigerant cycle and a part in the solution cycle. a dilution circuit connected through the solution cycle, and a crystallization risk detection device for detecting a crystallization risk of the solution during the solution cycle, the crystallization risk detection device detecting a risk exceeding a predetermined risk. a danger signal is issued, and the dilution control valve is opened by the danger signal to dilute the concentrated solution, and the heating amount adjustment mechanism is controlled by the danger signal in priority to the volume control signal. The absorption refrigerator is characterized in that the amount of heating is reduced to a predetermined low amount of heating.

本発明を実施例につき図面を用いて説明する。
第2図において、第1図と同一符号の部分は同一
のものを示す。しかして本実施例においては、正
常運転時における容量制御を行なうために、冷水
出口温度を温度検出器16にて温度を検出し、冷
凍能力と負荷量との相対関係を検知し、この相対
関係に応じて発信される容量制御信号により加熱
量調節機構としての加熱量制御弁HVが操作され
る容量制御機構が備えられているほかに、結晶の
危険度が大となつて稀釈を必要とする非常時に
は、結晶危険度検出装置としてのフロートスイツ
チ19の危険信号により、稀釈回路13を作動せ
しめると共に加熱量制御弁HVの開度を減少せし
めて加熱量を低減せしめるようになつている。
The present invention will be explained with reference to the drawings based on examples.
In FIG. 2, parts with the same reference numerals as in FIG. 1 indicate the same parts. However, in this embodiment, in order to perform capacity control during normal operation, the chilled water outlet temperature is detected by the temperature detector 16, the relative relationship between the refrigerating capacity and the load amount is detected, and this relative relationship is detected. In addition to being equipped with a capacity control mechanism in which the heating amount control valve HV is operated by a capacity control signal sent in response to the In an emergency, a danger signal from a float switch 19 serving as a crystal danger detection device activates the dilution circuit 13 and reduces the opening degree of the heating amount control valve HV to reduce the amount of heating.

即ち、フロートスイツチ19による蒸発器E内
の冷媒液面検出機構は、液面の高さにより溶液サ
イクル中の溶液濃度を間接的に検知する濃度相当
値検出装置であり、溶液が結晶を生ずる結晶危険
度を検出する結晶危険度検出装置として作用する
もので結晶危険度がある、所定危険度を超える場
合(即ち、濃度がある所定濃度を超える場合、即
ち蒸発器E内の冷媒液面がある、高さを超える場
合)に危険信号を発する。しかして、この危険信
号は温度検出器16からの容量制量信号に優先す
るように構成され、この危険信号を受けた場合加
熱量制御弁HVは、温度検出器16からの容量制
御信号の如何に拘らず、所定の小開度まで絞られ
所定の低加熱量を保つにとどまる。
That is, the refrigerant liquid level detection mechanism in the evaporator E using the float switch 19 is a concentration equivalent value detection device that indirectly detects the solution concentration during the solution cycle based on the height of the liquid level. This device acts as a crystal danger detection device to detect the crystal danger level, and when the crystal danger level exceeds a predetermined danger level (i.e., when the concentration exceeds a certain predetermined concentration, that is, when the refrigerant liquid level in the evaporator E is , the height is exceeded), a danger signal is issued. Therefore, this dangerous signal is configured to have priority over the capacity control signal from the temperature detector 16, and when this dangerous signal is received, the heating amount control valve HV controls the capacity control signal from the temperature detector 16. Regardless of the opening, the opening is narrowed down to a predetermined small opening and a predetermined low heating amount is maintained.

吸収冷凍機の運転中に溶液が過濃縮されると蒸
発器E内の液面が上昇してフロートスイツチ19
が作動し危険信号を発し、この危険信号により稀
釈弁SVが開いて稀釈が行なわれると同時に加熱
量制御弁HVが絞られて所定の小開度となり低加
熱量となるので、無駄なエネルギの消費を防ぎ、
また稀釈動作が短時間に確実に行なわれる。
If the solution becomes overconcentrated during operation of the absorption refrigerator, the liquid level in the evaporator E will rise and the float switch 19 will be activated.
is activated and issues a danger signal, and this danger signal opens the dilution valve SV to perform dilution. At the same time, the heating amount control valve HV is throttled to a predetermined small opening and a low heating amount, thereby saving wasted energy. prevent consumption,
Further, the dilution operation can be performed reliably in a short period of time.

稀釈作用により蒸発器E内の冷凍液面が所定の
高さまで下がつたことを別のフロートスイツチ
(図示せず)にて検出するか、又は稀釈後一定時
間経過した後にタイマーなどにより稀釈弁SVを
全閉とすると叫に加熱量制御弁HVの開度制限を
解除して、冷水負荷に関連する温度検出器16か
らの容量制御信号により加熱量制御弁HVを制御
する、通常の容量制御が行なわれる。
When the frozen liquid level in the evaporator E falls to a predetermined level due to the dilution action, it is detected by another float switch (not shown), or after a certain period of time has elapsed after dilution, the dilution valve SV is activated by a timer or the like. When fully closed, the opening limit of the heating amount control valve HV is canceled and the heating amount control valve HV is controlled by the capacity control signal from the temperature sensor 16 related to the chilled water load. It is done.

稀釈時における加熱量制御弁HVの所定の小開
度としては、開度ゼロ(全閉)を選んでもよい。
この場合には、発生器G内での加熱濃縮が全く行
なわれないまま稀釈回路13による稀釈のみが行
なわれ(溶液ポンプSP、冷媒ポンプRPなどはそ
のまま運転を続ける)、蒸発器E内の冷媒液面の
低下の検出、又はタイマーによる時間経過の検出
により、稀釈弁SVを閉じ、温度検出器16から
の容量制御信号により加熱量制御弁HVの制御を
行なう通常の運転状態に複帰せしめる。
Zero opening (fully closed) may be selected as the predetermined small opening of the heating amount control valve HV during dilution.
In this case, only dilution by the dilution circuit 13 is performed without heating and concentrating in the generator G (the solution pump SP, refrigerant pump RP, etc. continue to operate), and the refrigerant in the evaporator E is Upon detection of a decrease in the liquid level or detection of the passage of time by a timer, the dilution valve SV is closed and the normal operating state is returned to, in which the heating amount control valve HV is controlled by the capacity control signal from the temperature detector 16.

溶液濃度相当値としては、上述の如き蒸発器E
内の冷媒液面のほか、吸収器A内溶液面、発生器
G内溶液面などを単独又は組み合わせて検出して
もよく、また、濃度計により吸収器A、発生器
G、戻りの管路4,5内、溶液熱交換器X内など
のうち一箇所又は複数箇所の溶液の濃度を直接検
出してもよい。
As the solution concentration equivalent value, the evaporator E as described above is used.
In addition to the refrigerant liquid level in the absorber A, the solution level in the generator G, etc. may be detected singly or in combination.In addition, the concentration meter may be used to detect the absorber A, generator G, and return pipe. The concentration of the solution at one or more locations within the solution heat exchanger X, etc. may be directly detected.

溶液の結晶条件は濃度と温度との関係で決まる
ので、上述の実施例の如く濃度のみで危険度を検
知するようにすると、最悪又は最悪に近い低い温
度条件で危険濃度を決めることになるので高い温
度の場合には必要以上に稀釈が行なわれて冷凍能
力の低下を招く。これを防ぐために、溶液温度又
は溶液温度を推定することができる温度相当値を
検出し、その危険信号と濃度又は濃度相当値の検
出による危険信号とを組み合わせて、各種温度に
対して予め判明している危険濃度の値に設定し
て、段階的あるいは連続的に制御することもでき
る。溶液の温度検出としては吸収器A、発生器
G、管路4,5、溶液熱交換器Xなどの中の溶液
の温度の検出が行なわれ、温度相当値の検出とし
ては吸収器A、発生器G内の蒸気圧力の検出など
が行なわれる。これらの検出は単独又は併用して
もよい。
Since the crystallization conditions of a solution are determined by the relationship between concentration and temperature, if the degree of danger is detected only by concentration as in the above example, the dangerous concentration will be determined based on the worst or near worst low temperature conditions. If the temperature is high, dilution will occur more than necessary, resulting in a decrease in refrigerating capacity. In order to prevent this, we detect the solution temperature or a temperature equivalent value that can estimate the solution temperature, and combine that danger signal with the danger signal from the detection of the concentration or concentration equivalent value. It is also possible to control the concentration in stages or continuously by setting the dangerous concentration value. The temperature of the solution is detected in absorber A, generator G, pipes 4 and 5, solution heat exchanger X, etc., and the temperature equivalent value is detected in absorber A, generator The steam pressure inside the vessel G is detected. These detections may be performed alone or in combination.

発生器Gが直火式の場合は加熱量調節機構とし
ては、燃料の液体又は気体の流量制御弁が相当す
ることになる。
When the generator G is a direct-fired type, the heating amount adjustment mechanism corresponds to a flow control valve for liquid or gaseous fuel.

本発明は、蒸発器、吸収器、発生器、凝縮器、
溶液熱交換器、前記発生器における加熱量調節機
構、冷媒ポンプ、溶液ポンプ及び機器間を接続す
る経路とにより溶液サイクルと冷媒サイクルとが
形成されている吸収冷凍機において、冷凍能力と
負荷量との相対関係に応じて前記加熱量調節機構
に容量制御信号を与えて制御する容量制御機構が
備えられ、前記冷媒サイクル中の冷媒液部と前記
溶液サイクル中の一部とを稀釈用制御弁を介して
接続する稀釈回路が備えられ、前記溶液サイクル
中の溶液の結晶危険度を起える危険度を検出する
結晶危険度検出装置が備えられ、該結晶危険度検
出装置は、所定の危険度を検出した場合に危険信
号を発し、該危険信号により前記稀釈用制御弁が
開かれて濃溶液が稀釈されると共に、前記危険信
号により前記加熱量調節機構が前記容量制御信号
に優先して制御されて加熱量が低減され、所定の
低加熱量となるよう構成されたことにより、溶液
の結晶の危険が大となり、稀釈動作を行なうに当
たつて発生器における加熱濃縮を抑制して無駄な
エネルギの消費を防ぎ、稀釈動作を短時間に確実
に行なわしめ、かつ稀釈時に冷媒蒸気の発生が抑
制されるので蒸発器Eに戻る冷媒量も少なく、従
つて稀釈弁SVは小容量のもので済む利点を有す
る吸収冷凍機を提供することができ、実用上極め
て大なる効果を有するものである。
The present invention provides evaporators, absorbers, generators, condensers,
In an absorption refrigerator in which a solution cycle and a refrigerant cycle are formed by a solution heat exchanger, a heating amount adjustment mechanism in the generator, a refrigerant pump, a solution pump, and a path connecting the equipment, the refrigerating capacity and the load amount are A capacity control mechanism is provided for controlling the heating amount adjusting mechanism by giving a capacity control signal to the heating amount adjusting mechanism according to the relative relationship between the heating amount adjusting mechanism, and a dilution control valve for controlling the refrigerant liquid part in the refrigerant cycle and a part in the solution cycle. a dilution circuit connected through the solution cycle, and a crystallization risk detection device for detecting a risk of causing a crystallization risk of the solution during the solution cycle, the crystallization risk detection device detecting a predetermined risk of crystallization of the solution during the solution cycle. When detected, a danger signal is issued, and the dilution control valve is opened by the danger signal to dilute the concentrated solution, and the heating amount adjustment mechanism is controlled by the danger signal with priority over the capacity control signal. Since the amount of heating is reduced and the heating amount is reduced to a predetermined low amount, the danger of crystallization of the solution is increased, and heating concentration in the generator is suppressed during the dilution operation, resulting in wasted energy. Since the consumption of refrigerant is prevented, the dilution operation is performed reliably in a short period of time, and the generation of refrigerant vapor is suppressed during dilution, the amount of refrigerant returned to the evaporator E is small, so the dilution valve SV can be of small capacity. It is possible to provide an absorption refrigerating machine that has advantages, and has extremely large practical effects.

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

第1図は従来例のフロー図、第2図は本発明の
実施例のフロー図を示す。 1…管路、2…管路、3…管路、4…管路、5
…管路、6…散布管、7…管路、8…管路、9…
散布管、10…管路、11…膨張弁、13…稀釈
回路、14…加熱管、15…冷水管、16…温度
検出器、17…冷却水管、18…冷却水管、19
…フロートスイツチ、A…吸収器、G…発生器、
C…凝縮器、E…蒸発器、X…溶液熱交換器、
SP…溶液ポンプ、RP…冷媒ポンプ、HV…加熱
量制御弁、SV…稀釈弁。
FIG. 1 shows a flowchart of a conventional example, and FIG. 2 shows a flowchart of an embodiment of the present invention. 1...Pipeline, 2...Pipeline, 3...Pipeline, 4...Pipeline, 5
...pipe line, 6...dispersion pipe, 7...pipe line, 8...pipe line, 9...
Spreading pipe, 10... Pipe line, 11... Expansion valve, 13... Dilution circuit, 14... Heating tube, 15... Cold water pipe, 16... Temperature detector, 17... Cooling water pipe, 18... Cooling water pipe, 19
...float switch, A...absorber, G...generator,
C... Condenser, E... Evaporator, X... Solution heat exchanger,
SP...solution pump, RP...refrigerant pump, HV...heating amount control valve, SV...dilution valve.

Claims (1)

【特許請求の範囲】 1 蒸発器、吸収器、発生器、凝縮器、溶液熱交
換器、前記発生器における加熱量調節機構、冷媒
ポンプ、溶液ポンプ及び機器間を接続する経路と
により溶液サイクルと冷媒サイクルとが形成され
ている吸収冷凍機において、冷凍能力と負荷量と
の相対関係に応じて前記加熱量調節機構に容量制
御信号を与えて制御する容量制御機構が備えら
れ、前記冷媒サイクル中の冷媒液部と前記溶液サ
イクル中の一部とを稀釈用制御弁を介して接続す
る稀釈回路が備えられ、前記溶液サイクル中の溶
液の結晶危険度を検出する結晶危険度検出装置が
備えられ、該結晶危険度検出装置は、所定の危険
度を超える危険度を検出した場合に危険信号を発
し、該危険信号により前記稀釈用制御弁が開かれ
て濃溶液が稀釈されると共に、前記危険信号によ
り前記加熱量調節機構が前記容量制御信号に優先
して制御されて加熱量が低減され、所定の低加熱
量となるよう構成されたことを特徴とする吸収冷
凍機。 2 前記加熱量調節機構が、前記発生器を加熱す
る加熱用熱媒流体の流量制御弁である特許請求の
範囲第1項記載の吸収冷凍機。 3 前記加熱量調節機構が、前記発生器内の溶液
の液面調節により伝熱面積を変化せしめて熱交換
量を調節する機構である特許請求の範囲第1項記
載の吸収冷凍機。 4 前記結晶危険度検出装置が、前記溶液サイク
ル中の溶液濃度を直接又は間接に検出する濃度相
当値検出装置である特許請求の範囲第1項記載の
吸収冷凍機。 5 前記結晶危険度検出装置が、前記溶液サイク
ル中の溶液を直接又は間接に検出する温度相当値
検出装置を併せ備え、検出された濃度相当値と温
度相当値との組合わせにより、前記危険信号を発
するよう構成されている特許請求の範囲第4項記
載の吸収冷凍機。 6 前記所定の低加熱量がゼロである特許請求の
範囲第1項記載の吸収冷凍機。 7 前記濃度相当値検出装置が、前記蒸発器内の
冷媒液面検出装置である特許請求の範囲第4項記
載の吸収冷凍機。
[Claims] 1. A solution cycle and a path connecting the evaporator, absorber, generator, condenser, solution heat exchanger, heating amount adjustment mechanism in the generator, refrigerant pump, solution pump, and equipment. An absorption refrigerator having a refrigerant cycle is provided with a capacity control mechanism that controls the heating amount adjusting mechanism by giving a capacity control signal to the heating amount adjusting mechanism according to the relative relationship between the refrigerating capacity and the load amount, and A dilution circuit is provided which connects the refrigerant liquid part of the refrigerant and a part of the solution cycle via a dilution control valve, and a crystal risk detection device is provided to detect the crystal risk of the solution in the solution cycle. , the crystal danger level detection device issues a danger signal when detecting a danger level exceeding a predetermined danger level, the danger signal opens the dilution control valve to dilute the concentrated solution, and the danger signal An absorption refrigerating machine characterized in that the heating amount adjusting mechanism is controlled by a signal with priority over the capacity control signal to reduce the heating amount to a predetermined low heating amount. 2. The absorption refrigerator according to claim 1, wherein the heating amount adjustment mechanism is a flow rate control valve for a heating heat medium fluid that heats the generator. 3. The absorption refrigerator according to claim 1, wherein the heating amount adjustment mechanism is a mechanism that adjusts the amount of heat exchange by changing the heat transfer area by adjusting the level of the solution in the generator. 4. The absorption refrigerator according to claim 1, wherein the crystal risk detection device is a concentration equivalent value detection device that directly or indirectly detects the solution concentration during the solution cycle. 5. The crystal danger detection device is also equipped with a temperature equivalent value detection device that directly or indirectly detects the solution during the solution cycle, and the danger signal is detected by the combination of the detected concentration equivalent value and temperature equivalent value. An absorption refrigerator according to claim 4, which is configured to emit. 6. The absorption refrigerator according to claim 1, wherein the predetermined low heating amount is zero. 7. The absorption refrigerator according to claim 4, wherein the concentration equivalent value detection device is a refrigerant liquid level detection device in the evaporator.
JP272879A 1979-01-12 1979-01-12 Absorption type refrigerating machine Granted JPS5595071A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP272879A JPS5595071A (en) 1979-01-12 1979-01-12 Absorption type refrigerating machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP272879A JPS5595071A (en) 1979-01-12 1979-01-12 Absorption type refrigerating machine

Publications (2)

Publication Number Publication Date
JPS5595071A JPS5595071A (en) 1980-07-18
JPS6113551B2 true JPS6113551B2 (en) 1986-04-14

Family

ID=11537365

Family Applications (1)

Application Number Title Priority Date Filing Date
JP272879A Granted JPS5595071A (en) 1979-01-12 1979-01-12 Absorption type refrigerating machine

Country Status (1)

Country Link
JP (1) JPS5595071A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59129359A (en) * 1983-01-17 1984-07-25 株式会社荏原製作所 Absorption refrigerator
JPS602858A (en) * 1983-06-20 1985-01-09 株式会社荏原製作所 Absorption refrigerator

Also Published As

Publication number Publication date
JPS5595071A (en) 1980-07-18

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