JPS61280354A - Absorption refrigerator - Google Patents

Absorption refrigerator

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Publication number
JPS61280354A
JPS61280354A JP9978885A JP9978885A JPS61280354A JP S61280354 A JPS61280354 A JP S61280354A JP 9978885 A JP9978885 A JP 9978885A JP 9978885 A JP9978885 A JP 9978885A JP S61280354 A JPS61280354 A JP S61280354A
Authority
JP
Japan
Prior art keywords
absorption liquid
absorption
generator
flow rate
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.)
Granted
Application number
JP9978885A
Other languages
Japanese (ja)
Other versions
JPH0635904B2 (en
Inventor
雅裕 古川
舘下 繁則
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP60099788A priority Critical patent/JPH0635904B2/en
Publication of JPS61280354A publication Critical patent/JPS61280354A/en
Publication of JPH0635904B2 publication Critical patent/JPH0635904B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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)産業上の利用分野 本発明は、吸収液流1°を調節する装置の備えられた吸
収冷凍機、吸収ヒートポンプ、吸収冷温水機なと(以下
、この種の吸収冷凍機という)の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Industrial Application Field The present invention is applicable to absorption refrigerators, absorption heat pumps, absorption chiller/heaters, etc. (hereinafter referred to as such types) equipped with a device for adjusting the flow rate of absorption liquid by 1°. (absorption refrigerator).

(ロ)従来の技術 この種の吸収冷凍機の従来の技術には、負荷の変化に対
応して変化する物理量例えば冷水温度を作動信号として
吸収液用ポンプの回転速度を制御することにより吸収液
fMil!:を調節するもの(例えば特公昭43−26
664号公報)や吸収液の流量制御弁の開度を調節する
もの(例えば特公昭55−27267号公報、特公昭5
7−27375号公報)などがある。
(B) Conventional technology The conventional technology for this type of absorption chiller involves controlling the rotational speed of an absorbent pump using a physical quantity that changes in response to a change in load, such as the chilled water temperature, as an operating signal. fMil! : A device that adjusts the
664) and those that adjust the opening degree of the absorption liquid flow rate control valve (for example, Japanese Patent Publication No. 55-27267, Japanese Patent Publication No. 55-27267,
7-27375).

ヒj 発明が解決しようとする問題点 上記のような従来のこの種の吸収冷凍機(以下、従来機
という)においては、負荷が徐々に変化してこれに対応
する物理量〔例えば冷水温度〕の変化もゆるやかで吸収
液の流量を少しずつ増減させる場合〔朝方から夕方にか
けて変化する気温により徐々に負荷が変化し、これに応
じて吸収液流量を変化させるような場合〕には適切な吸
収液の循埋置制御が可能であるものの、そうでない場合
〔例えば冷房に必要な部屋数が増減することによって負
荷が急変し、各部屋へ冷水を送るポンプの発停台数の増
減により従来機への冷水流量が大きく増減して冷水温度
が急変するような場合〕には負荷の急変直後の発生器内
の圧力や温度など従来機の内部の状態が急に変わらない
ので、吸収液の流量制御が実際に調節すべき吸収液流量
の範囲を越えて行なわれやすい。そのため、従来機にお
いては、負荷の急変初期での吸収液の循環量制御が必ず
しも適切に行なわれず、発生器内の吸収液面の過度の上
昇や低下あるいは吸収液用ポンプのキャビテーションな
どを負荷の急変直後に引き起こしやす<、シばしば保護
装置が働いて運転が止められる問題点を有していた。
Hj Problems to be Solved by the Invention In the above-mentioned conventional absorption chillers of this type (hereinafter referred to as conventional machines), the load changes gradually and the corresponding physical quantity [for example, chilled water temperature] changes. If the change is gradual and the flow rate of the absorbent is to be increased or decreased little by little (when the load changes gradually due to temperature changes from morning to evening, and the flow rate of the absorbent is changed accordingly), select the appropriate absorbent. Circulation control is possible, but this is not the case [for example, the load changes suddenly due to an increase or decrease in the number of rooms required for cooling, and the number of pumps that supply cold water to each room increases or decreases, causing problems compared to conventional models. In cases where the chilled water flow rate increases or decreases significantly and the chilled water temperature changes suddenly], the internal conditions of conventional machines, such as the pressure and temperature inside the generator, do not suddenly change immediately after a sudden change in load, so absorption liquid flow rate control is necessary. This is likely to be done beyond the range of the absorption liquid flow rate that should actually be adjusted. For this reason, in conventional machines, the circulation amount of absorption liquid is not always properly controlled at the beginning of a sudden change in load, and the load may cause problems such as an excessive rise or fall of the absorption liquid level in the generator or cavitation of the absorption liquid pump. The problem was that it was easy to cause immediately after a sudden change, and that the protective device was often activated and the operation was stopped.

本発明は、このような問題点に鑑み、負荷の急変直後に
おける吸収液流量制御の補償が可能であり、負荷の急変
直後における保護装置の作動を防いで運転を安全に続け
ることが可能なこの種の吸収冷凍機の提供を目的とした
ものである。
In view of these problems, the present invention is capable of compensating the absorption liquid flow rate control immediately after a sudden change in load, and is capable of safely continuing operation by preventing the activation of a protection device immediately after a sudden change in load. The purpose is to provide a seed absorption refrigerator.

に)問題点を解決するための手段 本発明は、上記の問題点を解決する手段として、吸収液
の流量制御弁の開度または吸収液用ポンプの吐出量を調
節する制御装置により増減される吸収液流量の影響で変
化する物理量(発生器内の吸収液位や圧力など)を検知
しつつ流量制御弁の開度または吸収液ポンプの吐出量を
補正する調整装置をこの種の吸収冷凍機に備える構成と
したものである。
B) Means for Solving the Problems The present invention, as a means for solving the above-mentioned problems, provides a control device that adjusts the opening degree of the absorption liquid flow rate control valve or the discharge amount of the absorption liquid pump. This type of absorption chiller is equipped with an adjustment device that corrects the opening degree of the flow control valve or the discharge amount of the absorption liquid pump while detecting physical quantities (absorption liquid level and pressure in the generator, etc.) that change due to the influence of the absorption liquid flow rate. The structure is designed to prepare for the future.

(ホ)作用 本発明の吸収冷凍機においては、その作用〔働き〕とし
て、例えば負荷が急変して上記制御装置により吸収液用
ポンプの吐出量が大きく増減された際に発生器での吸収
液の出入量に不均衡を生じても、調整装置によりポンプ
の吐出量の増減度合いを補償して発生器での吸収液の出
入量をほぼバランスさせることが可能である。
(E) Function In the absorption refrigerator of the present invention, the function is that, for example, when the load suddenly changes and the discharge amount of the absorption liquid pump is greatly increased or decreased by the control device, the absorption liquid in the generator is Even if an imbalance occurs in the amount of absorption liquid in and out of the generator, it is possible to substantially balance the amount of absorption liquid in and out of the generator by compensating for the degree of increase/decrease in the discharge amount of the pump using the adjustment device.

したがって、本発明の吸収冷凍機においては、発生器内
の吸収液面の過度の上昇や低下などを防止でき、運転を
安全に継続することができる。
Therefore, in the absorption refrigerating machine of the present invention, it is possible to prevent the absorption liquid level in the generator from rising or falling excessively, and operation can be continued safely.

(へ)実施例 図面は本発明によるこの種の吸収冷凍機の一実施例を示
した概略構成説明図であり、+11は高温発生器、(2
)は低温発生器、(3)は凝縮器、(4)は蒸発器、(
5)は吸収器、(6)、(7)は低温、高温溶液熱交換
器、 ゛(P8)は冷媒液用ポンプ、(P、)は吐出量
可変の吸収液用ポンプで、これら機器は冷媒の流れる管
(8)、(9)、冷媒液の流下する管0眠冷媒液の還流
する管01)、(Iり、吸収液の送られる管a机側、吸
収液の流れる管(1飄(16L tJη、α枠により接
続されて冷媒〔水〕と吸収液〔臭化リチウム水溶液〕の
循環路を構成している。なお、alは管(8)と吸収器
(5)とを接続した冷暖切替弁(V、)付きの冷媒蒸気
用管路であり、翰は管Q51と吸収器(5)下部とを接
続した冷暖切替弁(V、)付きの吸収液用管路である。
(v) Embodiment The drawing is a schematic configuration explanatory diagram showing one embodiment of this type of absorption refrigerator according to the present invention, +11 is a high temperature generator, (2
) is a low temperature generator, (3) is a condenser, (4) is an evaporator, (
5) is an absorber, (6) and (7) are low-temperature and high-temperature solution heat exchangers, ゛(P8) is a pump for refrigerant liquid, and (P,) is a pump for absorbent liquid with variable discharge rate. Pipe (8), (9) through which the refrigerant flows, pipe (01) through which the refrigerant liquid flows, pipe (1) through which the refrigerant liquid flows, pipe (1) through which the absorption liquid flows, pipe (1) through which the absorption liquid flows, The pipe (16L tJη, connected by the α frame constitutes a circulation path for the refrigerant [water] and the absorption liquid [lithium bromide aqueous solution].Al connects the pipe (8) and the absorber (5). This is a refrigerant vapor pipe line with a heating/cooling switching valve (V,), and the pipe line is an absorbing liquid pipe line with a heating/cooling switching valve (V,) that connects the pipe Q51 and the lower part of the absorber (5).

(21)は高温発生器(1)の燃焼加熱室、(22,(
221・・・は燃焼ガスの流れる管、(ハ)は低温発生
器(2)の加熱器、(財)、C!唱言それぞれ凝縮器(
3)、吸収器(5)の冷却器であり、弼は蒸発器(4)
の熱交換器である。(2′?)(ハ)は熱交換器(ホ)
と負荷側の熱交換ユニット〔図示せず〕と結んだ冷水ま
たは温水の流れる管路であり、翰、(至)、01)は冷
却器(ハ)、C24)を直列に結んだ冷却水の流れる管
路である。また、04は燃焼加熱室01)へ燃料を供給
するための管路で、この管路には燃料調節弁(■、)が
備えである。
(21) is the combustion heating chamber of the high temperature generator (1), (22, (
221... is the pipe through which the combustion gas flows, (c) is the heater of the low temperature generator (2), (Foundation), C! Each chant is a condenser (
3) is the cooler for the absorber (5), and the bottom is the evaporator (4)
It is a heat exchanger. (2'?) (C) is a heat exchanger (E)
A pipe line through which cold water or hot water flows, which is connected to a heat exchange unit (not shown) on the load side. It is a flowing conduit. Further, 04 is a conduit for supplying fuel to the combustion heating chamber 01), and this conduit is equipped with a fuel control valve (■,).

(Sty )は管路(ハ)に備えた温度検出器で、これ
と第1調節器(C+)と吐出量可変の吸収液用ポンプ(
PA)とで負荷に対する吸収液流量の制御装置が従来の
ものと同様に構成されている。また、この制御装置はポ
ンプ(P、)の代りに流量制御弁(■、)を用いても良
い。
(Sty) is a temperature detector installed in the pipe line (C), this, the first regulator (C+), and the absorption liquid pump with variable discharge amount (Sty).
PA) and a control device for controlling the absorption liquid flow rate with respect to the load is constructed in the same manner as the conventional one. Further, this control device may use a flow control valve (■,) instead of the pump (P,).

なお、温度検出器(Stw)と第1v/4節器と燃料調
節弁(■、)とで負荷に対する加熱量制御装置が構成さ
れている。
Note that the temperature detector (Stw), the 1st v/4 node, and the fuel control valve (■,) constitute a heating amount control device for the load.

また、(Sta)は高温発生器fll内の吸収液の温度
を感知する検出器、(St)は高温発生器(1)の器壁
温度を感知する検出器、(Str)は高温発生器(1)
内の冷媒蒸気の温度を感知する検出器、(5tp)は高
温発生器(1)内圧を感知する検出器であり、(81)
は高温発生器(1)内の吸収液位を感知する検用益であ
る。かつまた、これら検出器のいずれかと第2調節器(
C8)と吸収液用ポンプ(P、)もしくは流量制御弁(
V、)とで吸収液流量の調整装置が構成されている。そ
して、吸収液流量の調整装置は前記制御装置により調節
された吸収液の流量を補正するようになっている。
Further, (Sta) is a detector that senses the temperature of the absorption liquid in the high temperature generator fll, (St) is a detector that senses the wall temperature of the high temperature generator (1), and (Str) is a detector that senses the temperature of the wall of the high temperature generator (1). 1)
A detector for sensing the temperature of the refrigerant vapor in the high temperature generator (1), (5tp) is a detector for sensing the internal pressure of the high temperature generator (1), (81)
is a test signal that senses the absorption liquid level in the high temperature generator (1). and also a second regulator (
C8) and absorption liquid pump (P,) or flow control valve (
V, ) constitute an absorption liquid flow rate adjustment device. The absorption liquid flow rate adjustment device corrects the absorption liquid flow rate adjusted by the control device.

(■、)とで加熱量調整装置が構成されており、これに
より加熱量制御装置で調節された燃料の量を補正するよ
うになっている。
(■,) constitute a heating amount adjusting device, which corrects the amount of fuel adjusted by the heating amount controlling device.

次に、このように構成された吸収冷凍機〔以下、本機と
いう〕の動作例を従来のこの種の吸収冷凍機と比較しつ
つ説明する。
Next, an example of the operation of the absorption refrigerating machine configured as described above (hereinafter referred to as the present machine) will be explained while comparing it with a conventional absorption refrigerating machine of this type.

今、例えば冷房されていた部屋数が10室〔全負荷〕か
ら2室〔20%負荷〕に減った際、吸収液流量の制御装
置と加熱量制御装置とにより吸収器(5)から高温発生
器(1)への吸収液流量と高温発生器fl)の加熱量が
115に急減される。すなわち、本機においては、従来
のこの種の吸収冷凍機〔以下、従来機という〕と同様、
温度検出器(Stvr)の信号で第1調節器(CI)を
介して吸収液用ポンプ(P、)の吐出量もしくは流量制
御弁(V、)の開度と燃料制御弁(■、)の開度が電に
減じられる。
Now, for example, when the number of rooms being cooled is reduced from 10 (full load) to 2 (20% load), high temperature is generated from the absorber (5) by the absorption liquid flow rate control device and heating amount control device. The absorption liquid flow rate to the vessel (1) and the heating amount of the high temperature generator fl) are sharply reduced to 115. In other words, this machine, like the conventional absorption refrigerator of this type [hereinafter referred to as the conventional machine],
The discharge amount of the absorption liquid pump (P,) or the opening degree of the flow control valve (V,) and the fuel control valve (■,) are controlled by the signal from the temperature sensor (Stvr) via the first regulator (CI). The opening is reduced to electric.

しかし、この際、高温発生器(1)の保有熱によりその
温度、内圧は速やかに低下せず、高温発生器fil、低
温発生器(2)間の圧力差も急に変わらず、高温発生器
(1)からの吸収液の流出量が直ちに減らないので、こ
の発生器における吸収液の出入量が一時的にアンバラン
スとなる。そのため、従来機においては、高温発生器m
内の液面が一時的に低くなり過ぎて空焚に近い状態とな
り、保護装置〔図示せず〕が働いて高温発生器(1)の
加熱が断たれ、運転が止められてしまう。これに対し、
本機においては、検出器(S+)の信号で第2調節器(
C3)を介して吸収液用ポンプ(P、)の吐出量もしく
は流量制御弁(■、)の開度が増大調整されるので、負
荷の急減時における高温発生器(1)の液面の一時的な
過度の低下が防止される。すなわち、前記の制御装置に
よる吸収液の流量の減らし過ぎを調整装置により補正す
るようになっている。したがって、本機においては、負
荷が急減した際にも、その運転を安全に継続することが
できる。また、負荷の急減時に、高温発生器(1)の液
面が一時的に低下してや〜空焚き気味になった場合、こ
の発生器内の吸収液や冷媒の温度、蒸気圧あるいはこの
発生器の器壁温度などが過度に上昇することになるので
、検出器(Sl)の信号に代えて検出器(Sta )、
 (St)、(8tp)、(Str)のいずれかの信号
で吸収液流量を補正するようにしても良い。
However, at this time, the temperature and internal pressure of the high-temperature generator (1) do not drop quickly due to the heat retained in the high-temperature generator (1), and the pressure difference between the high-temperature generator fil and the low-temperature generator (2) does not suddenly change. Since the amount of absorption liquid flowing out from (1) does not immediately decrease, the amount of absorption liquid flowing in and out of this generator becomes temporarily unbalanced. Therefore, in conventional machines, the high temperature generator m
The liquid level inside the reactor becomes too low temporarily, resulting in a state close to dry firing, and a protection device (not shown) is activated to cut off the heating of the high temperature generator (1), stopping operation. On the other hand,
In this machine, the signal from the detector (S+) is used to control the second regulator (
C3), the discharge amount of the absorption liquid pump (P,) or the opening degree of the flow rate control valve (■,) is increased and adjusted, so that the liquid level of the high temperature generator (1) temporarily decreases when the load suddenly decreases. This prevents excessive deterioration. That is, the adjustment device corrects an excessive reduction in the flow rate of the absorption liquid caused by the control device. Therefore, this machine can safely continue its operation even when the load suddenly decreases. In addition, if the liquid level in the high-temperature generator (1) temporarily drops when the load suddenly decreases, and it starts to run dry, the temperature and vapor pressure of the absorbing liquid and refrigerant in this generator, or the Since the temperature of the chamber wall etc. will rise excessively, the detector (Sta), instead of the signal of the detector (Sl),
The absorption liquid flow rate may be corrected using any one of the signals (St), (8tp), and (Str).

逆に、負荷が急増した際、従来機においては高温発生器
il+の液面の一時的な過度の上昇や吸収器(5)の液
面の一時的な過度の低下などを引き起こすために保護装
置が働いてその運転が止められてしまうことになるが、
本機においては調整装置により吸収器(5)から高温発
生器(1)への吸収液流量の増し過ぎを補正して高温発
生器(1)での液の出入量がほぼバランスするように吸
収液の循環量を調整するためにその運転を安全に継続す
ることができる。
On the other hand, when the load suddenly increases, in conventional machines, protective devices are installed to prevent a temporary excessive rise in the liquid level in the high temperature generator il+ or a temporary excessive drop in the liquid level in the absorber (5). will be activated and the driving will be stopped,
In this machine, the adjustment device compensates for an excessive increase in the flow rate of absorption liquid from the absorber (5) to the high temperature generator (1), so that the amount of liquid in and out of the high temperature generator (1) is almost balanced. The operation can be continued safely in order to adjust the amount of liquid circulation.

なお、本機においては、負荷が急変した際に前記制御装
置により調節された吸収液流量の影響で高温発生器(1
)内の圧力、温度あるいは液位などの物理量の変化が一
時的に過大となった場合、加熱量調整装置Kよって燃料
制御弁(■、)の開度が補正され、高温発生器(1)の
加熱量が、一時的な過不足を生じないように、補償され
る。
In addition, in this machine, when the load suddenly changes, the high temperature generator (1
) If the change in physical quantities such as pressure, temperature or liquid level in ) becomes temporarily excessive, the opening degree of the fuel control valve (■, ) is corrected by the heating amount adjustment device K, and the high temperature generator (1) The amount of heating is compensated so that there is no temporary excess or deficiency.

(ト)発明の効果 以上のとおり、本発明のこの種の吸収冷凍機においては
、負荷が急変した際に従来の制御装置で調節された吸収
液流量の影響により発生器内の圧力、温度、液位などの
物理量の変化が一時的に過大となっても、吸収液流量の
調整装置によって発生器への吸収液の送り量が補正され
て発生器での液の出入量がバランスするように吸収液の
循環量が調整されるので、その運転が安全に継続される
実用的効果を有する。
(G) Effects of the Invention As described above, in this type of absorption refrigerator of the present invention, when the load suddenly changes, the pressure and temperature inside the generator change due to the influence of the absorption liquid flow rate adjusted by the conventional control device. Even if changes in physical quantities such as liquid level become temporarily excessive, the absorption liquid flow rate adjustment device corrects the amount of absorption liquid sent to the generator, so that the amount of liquid in and out of the generator is balanced. Since the circulation amount of the absorption liquid is adjusted, this has the practical effect of safely continuing the operation.

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

図面は本発明によるこの種の吸収冷凍機の一実施例を示
した概略構成説明図である。 (1)・・・高温発生器、 (2)・・・低温発生器、
 (3)・・・凝縮器、 (4)・・・蒸発器、 (5
)・・・吸収器、 (P、)・・・吸収液用ポンプ、 
 (CI)、(C宜)、(Cs)・”第1、第2、第3
調節器、  (Stw)・・・温度検出器、(Si)、
(Sta)、(Sip)、(Sir)、(Sl) ・・
・検出器、(■、)・・・流量制御弁、  (V、)・
・・燃料制御弁。
The drawing is a schematic structural diagram showing an embodiment of this type of absorption refrigerator according to the present invention. (1)...High temperature generator, (2)...Low temperature generator,
(3)... Condenser, (4)... Evaporator, (5
)...Absorber, (P,)...Absorbing liquid pump,
(CI), (C Y), (Cs)・”1st, 2nd, 3rd
Controller, (Stw)...Temperature detector, (Si),
(Sta), (Sip), (Sir), (Sl)...
・Detector, (■,)...Flow control valve, (V,)・
...Fuel control valve.

Claims (4)

【特許請求の範囲】[Claims] (1)吸収器と発生器間の吸収液の流路に設けた流量制
御弁の開度または吸収液用ポンプの吐出量を調節する制
御装置の備えられた吸収冷凍機において、その制御装置
で調節される吸収液流量に影響して変化する物理量を検
知しつつ流量制御弁の開度または吸収液用ポンプの吐出
量を補正する吸収液流量の調整装置が備えられているこ
とを特徴とした吸収冷凍機。
(1) In an absorption refrigerator equipped with a control device that adjusts the opening degree of a flow rate control valve provided in the absorption liquid flow path between the absorber and the generator or the discharge amount of the absorption liquid pump, the control device It is characterized by being equipped with an absorption liquid flow rate adjustment device that corrects the opening degree of the flow rate control valve or the discharge amount of the absorption liquid pump while detecting a physical quantity that changes depending on the flow rate of the absorption liquid to be adjusted. Absorption refrigerator.
(2)前記物理量が発生器内の吸収液位である特許請求
の範囲第1項に記載の吸収冷凍機。
(2) The absorption refrigerator according to claim 1, wherein the physical quantity is an absorption liquid level in the generator.
(3)前記物理量が発生器内の圧力である特許請求の範
囲第1項に記載の吸収冷凍機。
(3) The absorption refrigerator according to claim 1, wherein the physical quantity is pressure within the generator.
(4)前記物理量が発生器における温度である特許請求
の範囲第1項に記載の吸収冷凍機。
(4) The absorption refrigerator according to claim 1, wherein the physical quantity is a temperature in a generator.
JP60099788A 1985-05-10 1985-05-10 Absorption refrigerator Expired - Lifetime JPH0635904B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60099788A JPH0635904B2 (en) 1985-05-10 1985-05-10 Absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60099788A JPH0635904B2 (en) 1985-05-10 1985-05-10 Absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS61280354A true JPS61280354A (en) 1986-12-10
JPH0635904B2 JPH0635904B2 (en) 1994-05-11

Family

ID=14256666

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60099788A Expired - Lifetime JPH0635904B2 (en) 1985-05-10 1985-05-10 Absorption refrigerator

Country Status (1)

Country Link
JP (1) JPH0635904B2 (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4919447A (en) * 1972-06-14 1974-02-20
JPS513575A (en) * 1974-06-27 1976-01-13 Mitsubishi Electric Corp Handotainitaisuru kinzokudenkyokuno keiseihoho
JPS599035A (en) * 1982-07-09 1984-01-18 Furukawa Electric Co Ltd:The Extrusion method and apparatus for molding suppressing eccentricity in thickness

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4919447A (en) * 1972-06-14 1974-02-20
JPS513575A (en) * 1974-06-27 1976-01-13 Mitsubishi Electric Corp Handotainitaisuru kinzokudenkyokuno keiseihoho
JPS599035A (en) * 1982-07-09 1984-01-18 Furukawa Electric Co Ltd:The Extrusion method and apparatus for molding suppressing eccentricity in thickness

Also Published As

Publication number Publication date
JPH0635904B2 (en) 1994-05-11

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