JPH03241277A - Method and apparatus for defrosting using liquid refrigerant pump for dry vaporizer - Google Patents

Method and apparatus for defrosting using liquid refrigerant pump for dry vaporizer

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Publication number
JPH03241277A
JPH03241277A JP3573390A JP3573390A JPH03241277A JP H03241277 A JPH03241277 A JP H03241277A JP 3573390 A JP3573390 A JP 3573390A JP 3573390 A JP3573390 A JP 3573390A JP H03241277 A JPH03241277 A JP H03241277A
Authority
JP
Japan
Prior art keywords
liquid refrigerant
defrosting
liquid
pipe
hot
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
JP3573390A
Other languages
Japanese (ja)
Inventor
Atsuyoshi Mantani
淳致 萬谷
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP3573390A priority Critical patent/JPH03241277A/en
Publication of JPH03241277A publication Critical patent/JPH03241277A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To improve defrosting efficiency by forming a defrosting liquid refrigerant circulation piping between a liquid refrigerant heating coil and a dry vaporizer and providing in an intake pipe an automatic open/close valve which closes during defrosting operation. CONSTITUTION:Part of liquid refrigerant in a liquid reservoir 9 is made to pass through a liquid refrigerant heating coil 10 to be hot liquid refrigerant, and let it flow into a vaporizer 12, in which sensible heat of the hot liquid refrigerant defrosts the vaporizer 12. Successively, the liquid refrigerant having radiated defrosting heat is taken out of the vaporizer 12 by a liquid refrigerant pump 5, and then made to pass again through the liquid refrigerant heating coil 10 to be hot liquid refrigerant, which is circulated by the liquid refrigerant pump 5 between inside of the vaporizer 12 and the liquid refrigerant heating coil 10 until defrosting operation is finished. At this time, an automatic open/ close valve 1 provided in an intake pipe closes for preventing the liquid refriger ant which has defrosted from being taken in by a compressor. Thus, a vaporizer of high defrosting efficiency can be obtained.

Description

【発明の詳細な説明】 10発明の目的 (産業上の利用分野) 本発明は、乾式蒸発器を用いた冷凍、冷蔵庫及び冷凍、
冷蔵オープンショーケースの、除霜時の庫内温度の上昇
を極力低く抑え、常に庫内温度を適温に、かつ一定に保
持させる様に除霜を短時間に終らせる除霜方法及び除霜
装置に関する。
Detailed Description of the Invention 10 Objects of the Invention (Industrial Application Field) The present invention relates to refrigeration, refrigerators and refrigeration using a dry evaporator,
A defrosting method and defrosting device for a refrigerated open showcase that minimizes the rise in internal temperature during defrosting and keeps the internal temperature at an appropriate and constant level in a short time. Regarding.

(従来の技術) 従来満液式蒸発器に於ては、液冷媒ポンプを用いて除霜
する方法及び該除霜装置はあるが、乾式蒸発器の除霜に
は液冷媒ポンプを用いた除霜方法及び装置はない。従来
、乾式蒸発器(以下蒸発器と略称する)の除霜を行うに
は、ホットガスを用いて除霜する方法及び装置があり、
各種の装置が市販されている。
(Prior art) Conventionally, there is a defrosting method using a liquid refrigerant pump and a defrosting device for a flooded evaporator, but there is a defrosting method using a liquid refrigerant pump for defrosting a dry type evaporator. There is no frost method and equipment. Conventionally, there are methods and devices for defrosting dry evaporators (hereinafter referred to as evaporators) using hot gas.
Various devices are commercially available.

又、液冷媒を用いて除霜する装置もある。There are also devices that defrost using liquid refrigerant.

閉 (例えば特會昭63−290380号公報参照) (発明が解決しようとする課題) 従来のホットガスを蒸発器内に放出させ除霜を行う方法
では、ホットガスが凝縮液化して蒸発器内に多く滞留す
る問題点がある。凝縮液冷媒が蒸発器内に滞留すると、
除霜時に圧縮機の吸引作用により一部が再蒸発し蒸発潜
熱を吸収して冷却作用を行い、除霜を阻害するため除霜
時間が長くかかり、従ってホットガス除霜熱が蒸発器か
ら庫内に拡散し、庫内温度を上昇させ、保管商品の変色
や劣化を促進させている。又凝縮液冷媒が圧縮機に吸引
され、液冷媒の状態で圧縮機内に戻り液ハンマー現象を
起し、圧縮機を破損させることがある。圧縮機に吸引さ
れた低温の凝縮液冷媒は、そのま・の状態で圧縮機が吸
引してもホットガスの再発生を行うことは困難なため、
各種のホットガス再発生装置を用いて対処している。ホ
ットガス再発生装置には、単純ホットガス式、順次ホッ
トガス式、ホットガス蓄熱再蒸発式などが多く用いられ
ており、単純ホットガス式はもっとも簡単で経済的な装
置であるが、圧縮機よりm王立遠距離にあったり、複数
台あったり、また、大型の蒸発器等に用いると、冷凍サ
イクル内の冷媒が蒸発器内に寝込んでしまい(滞留する
こと)ホットガスを再発生させることが出来ないことも
ある。又液バツクを起しやすく、圧縮機破損の危険が大
きい。順次式ホットガス式は複数の蒸発器を用い、交互
に除霜と冷却を行える利点があって、庫内適温を保持す
る利点があるが、低温域の庫内の蒸発器の除霜に用いる
と、除霜時間が長くなり、又多くの自動開閉弁と制御装
置を必要とする。ホットガス蓄熱再蒸発装置を用いて除
霜を行うと、冬季など外気温度が低い季節に圧縮機が低
負荷運転を行い、運転稼働時間が少いと蓄熱量が不足し
、ホットガスの再発生を行うことが困難なため、電熱ヒ
ーター等の外部加熱を必要とし、省エネルギー的ではな
い。従来の液冷媒を除霜に用いる方法では、吐出ガス温
度を上げることによって液冷媒温度の上昇を計っている
が、冬季などの低外気温季には通常の受液器内の液冷媒
温度は望む程の高温が得られないので、中温域(約0℃
乃至一5℃程度の庫内温度)の庫内の蒸発器の除霜には
用いられるが、低温成約(−5℃乃至それ以下の庫内温
度)の庫内の蒸発器の除霜には不適当で、使用上の制約
があり、多くの自動開閉弁と複雑な制御装置が必要であ
る。本発明は、上述の様な従来のホットガス除霜と、液
冷媒除霜との諸問題点を除去するために開発されたもの
であって、簡単で確実にしかも消費電力を少く、故障も
少く、保守も容易で更に除霜を短時間で終らせ、除霜時
の庫内温度の上昇を極力抑え、保管商品の品質劣化を極
力遅らせることの出来る乾式蒸発器の除霜方法及び除霜
装置を提供することを目的とする。
(For example, see Japanese Patent Application Publication No. 63-290380.) (Problems to be Solved by the Invention) In the conventional method of defrosting by discharging hot gas into the evaporator, the hot gas condenses and liquefies and There are many problems that remain. When the condensate refrigerant remains in the evaporator,
During defrosting, a portion of the gas re-evaporates due to the suction action of the compressor, absorbs latent heat of vaporization, and performs a cooling action, which inhibits defrosting and takes a long time to defrost.Therefore, the hot gas defrosting heat is transferred from the evaporator to the storage room. It spreads inside the warehouse, raising the temperature inside the warehouse and accelerating discoloration and deterioration of stored products. Further, the condensed liquid refrigerant is sucked into the compressor and returns to the compressor in the form of liquid refrigerant, causing a liquid hammer phenomenon, which may damage the compressor. It is difficult to regenerate hot gas even if the compressor draws the low-temperature condensate refrigerant in its original state.
We are dealing with this problem using various hot gas regeneration devices. Many types of hot gas regeneration equipment are used, such as a simple hot gas type, sequential hot gas type, and hot gas heat storage reevaporation type.The simple hot gas type is the simplest and most economical type, but the compressor If the evaporator is located far away, has multiple units, or is used in a large evaporator, the refrigerant in the refrigeration cycle may stay in the evaporator and regenerate hot gas. Sometimes it is not possible. Also, it tends to cause liquid back-up, and there is a high risk of compressor damage. Sequential hot gas type uses multiple evaporators and has the advantage of being able to perform defrosting and cooling alternately, which has the advantage of maintaining an appropriate temperature inside the refrigerator, but it is used to defrost the evaporators inside the refrigerator in the low temperature range. This increases the defrosting time and requires many automatic on-off valves and control devices. When defrosting is performed using a hot gas heat storage re-evaporation device, the compressor operates at a low load during seasons such as winter when the outside temperature is low, and if the operation time is short, the amount of heat storage becomes insufficient and hot gas is not generated again. Since it is difficult to perform this method, external heating such as an electric heater is required, which is not energy-saving. In the conventional method of using liquid refrigerant for defrosting, the temperature of the liquid refrigerant is increased by increasing the temperature of the discharged gas. Since the desired high temperature cannot be obtained, the medium temperature range (approximately 0℃
It is used to defrost the evaporator inside the refrigerator (internal temperature of -5℃ to 15℃), but it is used to defrost the evaporator in the refrigerator with low temperature (interior temperature of -5℃ or lower). It is unsuitable, has limitations in use, and requires many automatic on-off valves and complex control equipment. The present invention was developed in order to eliminate the problems of conventional hot gas defrosting and liquid refrigerant defrosting as described above, and is simple and reliable, consumes less power, and is less likely to malfunction. A defrosting method and defrosting method for a dry evaporator that is easy to maintain, completes defrosting in a short time, minimizes the rise in internal temperature during defrosting, and delays quality deterioration of stored products as much as possible. The purpose is to provide equipment.

ロ 発明の構成 (課題を解決するための手段) 本発明の請求項第−及び第二に係る蒸発器の除霜方法及
び除霜装置は、除霜に際し、ホットガスを用いずに、受
液器内の一部の液冷媒を液冷媒加熱コイル内を通過させ
てホット液冷媒となし、蒸発器内に流入させ、ホット液
冷媒の顕熱を用いて蒸発器の除霜を行う。
B. Structure of the Invention (Means for Solving the Problems) The evaporator defrosting method and defrosting device according to the first and second claims of the present invention are capable of defrosting a liquid receiving liquid without using hot gas. A part of the liquid refrigerant in the container is passed through a liquid refrigerant heating coil to become hot liquid refrigerant, which is then flowed into the evaporator, and the evaporator is defrosted using the sensible heat of the hot liquid refrigerant.

続いて除霜熱放出後の除霜清液冷媒を液冷媒ポンプを用
いて蒸発器外に吸引し、再び液冷媒加熱コイル内を通過
させてホット液冷媒となし、除霜終了時まで、蒸発器内
と液冷媒加熱コイル間を液冷媒ポンプを用いて循環させ
、吸入管に設けた自動開閉弁を閉じて、除霜清液冷媒を
圧縮機に吸引させない構成となっている。本発明の請求
項第三及び第四に係る蒸発器の除霜方法及び除霜装置は
、ホットガスを除霜に用い、除霜に際し、吸入管に設け
た自動開閉弁を閉じ、受液器内の一部の液冷媒を液冷媒
加熱コイル内を通過させ、ホット液冷媒とし、気液分離
器の入口側管の吸入管の一部に、ホット液冷媒噴霧室を
設け、吸入管内に噴霧させ、ホットガス再発生用冷媒と
して用いる。蒸発器内に流入したホットガスの器内から
吸引し、上述の受液器内より供給された液冷媒と合流さ
せ、液冷媒加熱コイルを通過させてホット液冷媒とし、
ホット液冷媒噴霧室内に噴霧する構成となっている。
Next, the defrosted clean liquid refrigerant after releasing the defrosting heat is sucked out of the evaporator using a liquid refrigerant pump, and passed through the liquid refrigerant heating coil again to become hot liquid refrigerant, where it evaporates until the end of defrosting. A liquid refrigerant pump is used to circulate the liquid refrigerant between the inside of the container and the liquid refrigerant heating coil, and an automatic opening/closing valve provided in the suction pipe is closed to prevent the defrosting liquid refrigerant from being sucked into the compressor. The evaporator defrosting method and defrosting device according to the third and fourth claims of the present invention use hot gas for defrosting, close an automatic opening/closing valve provided in the suction pipe, and A part of the liquid refrigerant is passed through a liquid refrigerant heating coil to become hot liquid refrigerant, and a hot liquid refrigerant spray chamber is installed in a part of the suction pipe of the inlet side pipe of the gas-liquid separator to spray it into the suction pipe. It is used as a refrigerant for hot gas regeneration. The hot gas that has flowed into the evaporator is sucked from the inside of the container, combined with the liquid refrigerant supplied from the liquid receiver described above, and passed through a liquid refrigerant heating coil to become hot liquid refrigerant.
The hot liquid refrigerant is sprayed into the spray chamber.

(作用) 本発明の請求項第−及び第二の除霜方法及び除霜装置を
用いて除霜を行うと、吸入管の自動開閉弁(以下吸入弁
と略称する。)を閉じて受液器から供給された液冷媒を
加熱してホット液冷媒となし、蒸発器内と液冷媒加熱コ
イル間を循環し、除霜終了後には再び受液器内に戻され
るため、圧縮機は除霜清液冷媒を吸引しないので、液ハ
ンマーによる圧縮機の破損はおこらず、又除霜清液冷媒
を再蒸発させる必要はない。請求項第三及び第四の発明
の除霜方法及び除霜装置を用いて除霜を行うと、ホット
ガスを用いているため、速かに除霜が行われ、液冷媒ポ
ンプで凝縮液冷媒を蒸発器内に滞留させることなく外に
移送させるので除霜は早く終了し、吸入弁を閉じて除霜
を行うので圧縮機は凝縮液冷媒を吸引しない。従って、
液ハンマーによる圧縮機の破損はおこらず、ホット液冷
媒を小型のホット液冷媒噴霧室内に噴霧させることで、
ホットガスを再発生させることが出来るので、大型のホ
ットガス蓄熱再蒸発装置がなくてもホットガスを再発生
させることが出来る。
(Function) When defrosting is performed using the defrosting method and defrosting device according to the first and second claims of the present invention, the automatic opening/closing valve of the suction pipe (hereinafter abbreviated as suction valve) is closed to receive liquid. The compressor heats the liquid refrigerant supplied from the container to become hot liquid refrigerant, circulates it between the evaporator and the liquid refrigerant heating coil, and returns to the receiver after defrosting. Since fresh liquid refrigerant is not sucked, the compressor is not damaged by liquid hammer, and there is no need to reevaporate the defrosting fresh liquid refrigerant. When defrosting is performed using the defrosting method and defrosting device of the third and fourth inventions, since hot gas is used, defrosting is quickly performed, and the condensed liquid refrigerant is removed by the liquid refrigerant pump. Since the refrigerant is transferred outside without being retained in the evaporator, defrosting ends quickly, and since defrosting is performed with the suction valve closed, the compressor does not suck in condensed refrigerant. Therefore,
The compressor will not be damaged by the liquid hammer, and by spraying the hot liquid refrigerant into a small hot liquid refrigerant spray chamber,
Since hot gas can be regenerated, hot gas can be regenerated even without a large hot gas heat storage and reevaporation device.

(実施例) 以下本発明の一実施例を図面に基づいて説明する。第一
図は、請求項第−及び第二の発明の乾式蒸発器の液冷媒
ポンプを用いた除霜方法及び装置に係る構成を示してい
る。冷却運転中は吸入弁(1)と液弁(2)が開いであ
るため圧縮機(8)は運転している。除霜制御装置(7
)の除霜作動により、液弁(2)が閉鎖し、膨張弁(2
1)への液冷媒の供給が停止する。次いで吸入弁(1)
が閉鎖し圧縮機(8)は停止する。除霜用液冷媒循環弁
(6)が開き、次いで受液器(9)の出口側の液管(2
4)の一部を分岐して設けた受液器液供給管(25)中
に設けた受液器液供給弁(3)を、一定時間内のみ開か
せ、受液器(9)内の一部の液冷媒を、除霜に必要な除
霜用循環液冷媒量を供給した後に閉鎖させる。
(Example) An example of the present invention will be described below based on the drawings. FIG. 1 shows the configuration of a defrosting method and apparatus using a liquid refrigerant pump for a dry evaporator according to the first and second aspects of the invention. During the cooling operation, the suction valve (1) and the liquid valve (2) are open, so the compressor (8) is operating. Defrost control device (7
), the liquid valve (2) closes and the expansion valve (2) closes.
1) The supply of liquid refrigerant to 1) is stopped. Then the suction valve (1)
is closed and the compressor (8) is stopped. The defrosting liquid refrigerant circulation valve (6) opens, and then the liquid pipe (2) on the outlet side of the liquid receiver (9) opens.
The liquid receiver liquid supply valve (3) installed in the liquid receiver liquid supply pipe (25), which is provided by branching off a part of 4), is opened only for a certain period of time, and the liquid in the liquid receiver (9) is A part of the liquid refrigerant is closed after the amount of circulating liquid refrigerant for defrosting required for defrosting is supplied.

供給された除霜用循環液冷媒は、受液器液供給管(25
)の先端に設けた三分岐部(26)に接続した除霜用液
冷媒循環管(11)中に設けた除霜用液冷媒循環弁(6
)を通り液冷媒加熱コイル(10)内を通過中に加熱さ
れ、ホット液冷媒となり、除霜用液冷媒循環管(11)
を通り、膨張弁(21)の出口側管で蒸発器(12)の
入口側管に分岐接続したホット液冷媒流入管(13)か
ら蒸発器(12)内に流入する。流入したホット液冷媒
は顕熱を放出し蒸発器(12)の除霜を行いつつ流下し
、低温の除霜清液冷媒となり、蒸発器出口管(27)を
分岐し接続した除霜済液冷媒取出管(20)から、管中
に設けた除霜清液弁(4)を通り、液冷媒ポンプ(5)
の運転によって吸引され、液冷媒ポンプ(5)の出口側
管が接続されている三分岐部(26)を通り除霜用液冷
媒循環管(11)を通り液冷媒加熱コイル(10)内に
入り、加熱されホット液冷媒となり、蒸発器(12)と
液冷媒加熱コイル(10)間を液冷媒ポンプ(5)の運
転により、除霜用液冷媒循環管(11)内を除霜終了時
まで循環して除霜を行う。除霜終了は、除霜制御装置(
7)または除霜終了温度調節器(18)の何れかの作動
によって行い、先ず受液器液供給管(25)を分岐して
設けた受液器液戻し管(28)の管中に設けた受液器液
戻し弁(19)が開き、除霜用液冷媒循環弁(6)が閉
鎖し、蒸発器(12)内へのホット液冷媒の供給が停止
し、蒸発器(12)内の除霜清液冷媒は受液器液戻し弁
(19)を通り受液器(9)内に戻される。除霜済液弁
(4)と液冷媒ポンプ(5)が閉鎖し、吸入弁(1)と
液弁(2)が開き、膨張弁(21)に液冷媒が供給され
て圧縮機(8)が運転して冷却運転となる。各管中の必
要な個所にそれぞれ逆止弁(22)を設ける。ホット液
冷媒の液温度の設定は、圧縮機(8)が冷却運転中の吐
出ガス温度を蓄熱するホットガス蓄熱タンク(15)内
の蓄熱液温を検出する蓄熱温度調節器(16)により、
吐出管(33)と凝縮器(14)間中に設けたホットガ
スバイパス弁(17)を開閉させて調節する。ホットガ
ス蓄熱タンク(15)内に内蔵されている液冷媒加熱コ
イル(10)内を通過する液冷媒の温度はこれにより定
まる。第二図は、本発明の請求項第三及び第四の発明の
乾式蒸発器の液冷媒ポンプを用いた除霜方法及び除霜装
置に係る構成を示している。冷却運転中は吸入管(23
)中に設けた吸入弁(1)と液管(24)中に設けた液
弁(2)が開き圧縮機(8)は運転している。
The supplied circulating liquid refrigerant for defrosting is transferred to the receiver liquid supply pipe (25
) A liquid refrigerant circulation valve for defrosting (6) provided in a liquid refrigerant circulation pipe for defrosting (11) connected to a three-branch part (26) provided at the tip of the liquid refrigerant circulation valve for defrosting (11)
), it is heated while passing through the liquid refrigerant heating coil (10), becomes hot liquid refrigerant, and becomes a liquid refrigerant circulation pipe for defrosting (11).
The hot liquid refrigerant flows into the evaporator (12) through the hot liquid refrigerant inlet pipe (13) which is branched and connected to the inlet pipe of the evaporator (12) at the outlet pipe of the expansion valve (21). The inflowing hot liquid refrigerant emits sensible heat and flows down while defrosting the evaporator (12), becoming a low-temperature defrosted clear liquid refrigerant, and the defrosted liquid refrigerant is branched and connected to the evaporator outlet pipe (27). From the refrigerant extraction pipe (20), it passes through the defrost liquid valve (4) installed in the pipe, and then the liquid refrigerant pump (5)
The liquid refrigerant is sucked by the operation of the liquid refrigerant, passes through the three-branch part (26) to which the outlet side pipe of the liquid refrigerant pump (5) is connected, passes through the defrosting liquid refrigerant circulation pipe (11), and enters the liquid refrigerant heating coil (10). The liquid refrigerant is heated and becomes a hot liquid refrigerant, and the liquid refrigerant pump (5) is operated between the evaporator (12) and the liquid refrigerant heating coil (10), and the liquid refrigerant circulates in the defrosting liquid refrigerant circulation pipe (11) at the end of defrosting. defrost by circulating until When defrosting is finished, the defrost control device (
7) or by the operation of the defrosting end temperature regulator (18). The receiver liquid return valve (19) opens, the defrosting liquid refrigerant circulation valve (6) closes, and the supply of hot liquid refrigerant to the evaporator (12) is stopped. The defrosting fresh liquid refrigerant is returned into the receiver (9) through the receiver liquid return valve (19). The defrosted liquid valve (4) and the liquid refrigerant pump (5) close, the suction valve (1) and the liquid valve (2) open, and the liquid refrigerant is supplied to the expansion valve (21) and the compressor (8). is operated and cooling operation is started. Check valves (22) are provided at necessary locations in each pipe. The liquid temperature of the hot liquid refrigerant is set by a heat storage temperature controller (16) that detects the heat storage liquid temperature in the hot gas heat storage tank (15) that stores the discharge gas temperature during cooling operation of the compressor (8).
The hot gas bypass valve (17) provided between the discharge pipe (33) and the condenser (14) is adjusted by opening and closing. This determines the temperature of the liquid refrigerant passing through the liquid refrigerant heating coil (10) built in the hot gas heat storage tank (15). FIG. 2 shows the configuration of a defrosting method and a defrosting device using a liquid refrigerant pump for a dry evaporator according to the third and fourth aspects of the present invention. During cooling operation, the suction pipe (23
) and the liquid valve (2) provided in the liquid pipe (24) are open and the compressor (8) is operating.

除霜制御装置(7)の除霜作動により、液弁(2)が閉
鎖し、膨張弁(21)への液冷媒の供給が停止する。次
いで吸入弁(1)が閉鎖し、蒸発器(12)から冷媒を
圧縮機(8)が直接に吸引しない。受液器(9)の出口
側の液管(24)の一部を分岐して設けた受液器液供給
管(25)中の受液器液供給弁(3)を開き、受液器(
9)内の一部の液冷媒を供給液量調節弁(29)により
流入量を調節して三分岐部(26)に接続した吸入放出
管(30)を通り、液冷媒加熱コイル(10)内を通り
加熱されてホット液冷媒となり、気液分離器(31)の
入口側の吸入管(23)中に設けたホット液冷媒噴霧室
(32)内に噴霧させ、高温低圧ガスとし、圧縮機(8
)が引続き運転して、吸引してホットガスを発生させる
。ホットガスは圧縮機(8)の吐出管(33)を分岐し
て設けたホットガス管(34)中に設けたホットガス弁
(35)を通り、膨張弁(21)の出口管で、蒸発器(
12)の入口管を分岐して接続したホットガス流入管(
36)から蒸発器(12)内に流入する。流入したホッ
トガスは、凝縮潜熱を放出して除霜を行い、凝縮液冷媒
となり蒸発器出口管(27)を分岐し接続した除霜済液
冷媒取出管(20)から除霜済液弁(4)を通り、液冷
媒ポンプ(5)の運転により吸引され、液冷媒ポンプ(
5)の出口管の接続されている三分岐部(26)を通り
、吸入放出管(30)中の噴霧液量調節弁(37)を通
り、液冷媒加熱コイル(10)内で加熱されホット液冷
媒となり、ホット液冷媒噴霧室(32)内に噴霧され、
除霜終了まで繰返してこの行程を行い除霜を行う。受液
器(9)から供給された液冷媒と、除霜済の凝縮液冷媒
が、液冷媒ポンプ(5)により吸引されて吐出され、三
分岐部(26)で合流し、噴霧液量調節弁(37)の調
節により除霜済の凝縮液冷媒の戻り量が多い場合は、三
分岐部(26)より受液器(9)内に戻り、不足の場合
は受液器(9)内から供給される。除霜終了は、除霜制
御装置(7)又は除霜終了温度調節器(18)の何れか
の作動によって行い、ホットガス弁(35)と受液器液
供給弁(3)を閉鎖し、ホットガスと液冷媒の供給を停
止させ、蒸発器(12)内の除霜済の凝縮液冷媒を全部
ホット液冷媒噴霧室(32)内に噴霧した後に、除霜済
液弁(4)を閉鎖し、液冷媒ポンプ(5)の運転を停止
し、液弁(2)を開き、膨張弁(21)に液冷媒を供給
し、吸入弁(1)を開き冷媒を圧縮機(8)に吸引させ
て冷却運転となる。各管中の必要な個所にそれぞれ逆止
弁(22)を設ける。ホット液冷媒の液温度の設定は、
圧縮機(8)が冷却運転中の吐出ガスの熱を蓄熱するホ
ットガス蓄熱タンク(15)内の蓄熱温度を検出する蓄
熱温度調節器(16)により、吐出管(33)と凝縮器
(14)間中に設けたホットガスバイパス弁(17)を
開閉させて調節する。ホットガス蓄熱タンク(15)内
に内蔵されている液冷媒加熱コイル(10)内を通過す
る液冷媒の温度はこれにより定まる。
Due to the defrosting operation of the defrosting control device (7), the liquid valve (2) closes and the supply of liquid refrigerant to the expansion valve (21) is stopped. The suction valve (1) is then closed and the compressor (8) no longer draws refrigerant directly from the evaporator (12). Open the receiver liquid supply valve (3) in the receiver liquid supply pipe (25) provided by branching off a part of the liquid pipe (24) on the outlet side of the receiver (9), and open the receiver liquid supply valve (3). (
The inflow amount of some of the liquid refrigerant in 9) is adjusted by the supply liquid amount control valve (29), and the liquid refrigerant is passed through the suction and discharge pipe (30) connected to the three-branch portion (26), and then the liquid refrigerant is heated to the liquid refrigerant heating coil (10). The hot liquid refrigerant is heated and becomes a hot liquid refrigerant, and is sprayed into the hot liquid refrigerant spray chamber (32) provided in the suction pipe (23) on the inlet side of the gas-liquid separator (31) to become a high-temperature, low-pressure gas and compressed. machine (8
) continues to operate, sucking in and generating hot gas. The hot gas passes through a hot gas valve (35) installed in a hot gas pipe (34) branched from the discharge pipe (33) of the compressor (8), and is evaporated at the outlet pipe of the expansion valve (21). vessel(
12) Hot gas inflow pipe (
36) into the evaporator (12). The inflowing hot gas performs defrosting by releasing latent heat of condensation, becomes a condensed liquid refrigerant, and is transferred from the defrosted liquid refrigerant extraction pipe (20) connected to the evaporator outlet pipe (27) by branching off to the defrosted liquid valve ( 4), is sucked in by the operation of the liquid refrigerant pump (5), and is sucked in by the operation of the liquid refrigerant pump (5).
The liquid refrigerant passes through the three-branch part (26) connected to the outlet pipe of 5), passes through the spray liquid volume control valve (37) in the suction/discharge pipe (30), and is heated in the liquid refrigerant heating coil (10) to become hot. It becomes a liquid refrigerant and is sprayed into the hot liquid refrigerant spray chamber (32),
This process is repeated until defrosting is completed. The liquid refrigerant supplied from the liquid receiver (9) and the defrosted condensed liquid refrigerant are sucked and discharged by the liquid refrigerant pump (5), and are combined at the three-branch portion (26) to adjust the amount of sprayed liquid. If there is a large amount of defrosted condensate refrigerant returned by adjusting the valve (37), it will return to the liquid receiver (9) from the three-branch part (26), and if there is a shortage, it will return to the liquid receiver (9). Supplied from. The defrosting is completed by operating either the defrosting control device (7) or the defrosting end temperature regulator (18), closing the hot gas valve (35) and receiver liquid supply valve (3), After stopping the supply of hot gas and liquid refrigerant and spraying all of the defrosted condensed liquid refrigerant in the evaporator (12) into the hot liquid refrigerant spray chamber (32), the defrosted liquid valve (4) is opened. The liquid refrigerant pump (5) is closed, the liquid refrigerant pump (5) is stopped, the liquid valve (2) is opened, the liquid refrigerant is supplied to the expansion valve (21), and the suction valve (1) is opened to supply the refrigerant to the compressor (8). It is sucked into cooling operation. Check valves (22) are provided at necessary locations in each pipe. To set the liquid temperature of hot liquid refrigerant,
The discharge pipe (33) and the condenser (14) are controlled by the heat storage temperature controller (16) that detects the heat storage temperature in the hot gas heat storage tank (15) that stores the heat of discharged gas during cooling operation of the compressor (8). ) Adjust by opening and closing the hot gas bypass valve (17) provided in between. This determines the temperature of the liquid refrigerant passing through the liquid refrigerant heating coil (10) built in the hot gas heat storage tank (15).

ハ 発明の効果 本発明の請求項第−及び第二の除霜方法及び除霜装置は
、除霜用冷媒に加熱したホット液冷媒を用いている。ホ
ット液冷媒はホットガスに比して、熱容量が多く、熱伝
導率も高いのでホットガスより除霜効率は高い。又ホッ
ト液冷媒の温度は調節出来るが、ホットガスは調節が困
難である。中温域(約0℃乃至一5℃程度の庫内温度)
の冷蔵庫や冷蔵オープンケース内に保管する商品は主と
して、精肉、鮮魚、加工食品等であり、庫内温度の上昇
は最も恐れるところであり、変色や品質劣化を促進させ
る。故に庫内温度が、冷却中でも除霜中でも常に適温を
保持することが望まと除霜時間を調整すると、蒸発器(
12)は薄箱状態を維持するので、除霜時間は著しく短
縮され、従って蒸発器(12)がら除霜熱が庫内に拡散
するのが極力少くなり、庫内温度の適温保持に効果があ
り、この発明の除霜方法及び除霜装置は、特に庫内温度
が中温域の保管庫用蒸発器の除霜に適している。ホット
液冷媒の移送用配管は小口径管で済むので、除霜用液冷
媒循環管(11)の大部分を液管で、ホットガスに比し
て、配管の伸縮度合が少く、配管の破損や取付弁類の締
付ネジの温度変化によるゆるみも少なく、冷媒洩れの故
障が少ない。吸入弁を閉じて除霜を行うので、蒸発器内
の除霜清液冷媒を圧縮機が吸引しないから、液バンクは
起らず圧縮機の破損する危険はない。従って液バツク防
止機器も必要でない。ホットガスを再発生させる必要が
ないので、ホットガス再発生装置も不用である。
C. Effects of the Invention The defrosting method and defrosting device according to the first and second claims of the present invention use a heated hot liquid refrigerant as the defrosting refrigerant. Hot liquid refrigerant has a higher heat capacity and higher thermal conductivity than hot gas, so it has higher defrosting efficiency than hot gas. Also, while the temperature of hot liquid refrigerant can be controlled, it is difficult to control the temperature of hot gas. Medium temperature range (approximately 0℃ to 15℃ internal temperature)
The products stored in refrigerators and refrigerated open cases are mainly meat, fresh fish, processed foods, etc., and the greatest fear is an increase in internal temperature, which accelerates discoloration and quality deterioration. Therefore, it is desirable to maintain the temperature inside the refrigerator at an appropriate temperature during cooling and defrosting, and when adjusting the defrosting time, the evaporator (
12) maintains a thin box state, so the defrosting time is significantly shortened, and therefore, the diffusion of defrosting heat into the refrigerator from the evaporator (12) is minimized, which is effective in maintaining the temperature inside the refrigerator at an appropriate temperature. The defrosting method and defrosting device of the present invention are particularly suitable for defrosting an evaporator for storage where the internal temperature is in the medium temperature range. Since the piping for transferring the hot liquid refrigerant can be a small-diameter pipe, most of the liquid refrigerant circulation pipe (11) for defrosting is a liquid pipe, and compared to hot gas, the degree of expansion and contraction of the piping is less, and damage to the piping is reduced. There is also less loosening of the tightening screws of mounting valves and mounting valves due to temperature changes, and there are fewer failures due to refrigerant leaks. Since defrosting is performed by closing the suction valve, the compressor does not suck in the defrosted clean liquid refrigerant in the evaporator, so there is no risk of liquid bank formation and damage to the compressor. Therefore, there is no need for liquid back protection equipment. Since there is no need to regenerate hot gas, a hot gas regeneration device is also unnecessary.

蒸発器内に耐着したり滞留する冷凍機油も除霜時ごとに
、液冷媒ポンプで蒸発器外に移送させるので冷却運転時
の蒸発器の熱交換効率は向上する。除霜時は圧縮機を運
転休止させ、小馬力の液冷媒ポンプを運転して除霜を行
うので除霜用消費電力は少く、圧縮機の寿命も永くなる
。従来の液冷媒を用いて除霜を行う装置では、それ程温
度の高くない液冷媒を一方の蒸発器内に満液とし、他方
の蒸発器の膨張弁への供給量の液冷媒への移動だけの液
冷媒の蒸発器内移動速度だけであり、液冷媒の顕熱を利
用した除霜であるから、除霜時間が長くかかり除霜効率
は悪い。従って庫内温度が低温域の蒸発器の除霜には適
さない。本発明の除霜方法及び除霜装置では、除霜用ホ
ット液冷媒の温度を低温から高温に調節出来るので、低
い外気温の時、及び庫内温度が低温域の蒸発器の除霜に
使用可能で、又液冷媒ポンプで除霜用ホット液冷媒を蒸
発器内に急速に循環させるので、除霜時間は著しく短縮
され除霜効率は高い。厳冬季や酷寒地における庫内温度
が低温域の蒸発器の除霜には、ホットガス蓄熱を利用し
て液冷媒加熱コイルを加熱せずに、他の熱源、例えば石
油温水器等の熱源を用いると、如何なる庫内温度が低温
域の蒸発器に対しても、除霜が可能である。請求項第三
及び第四の発明に係る除霜方法及び除霜装置は、除霜に
ホットガスを用いているので、低温域(約−5℃以下)
の庫内温度の蒸発器の除霜に適している。従来のホット
ガス除霜において、ホットガスの除霜後の凝縮液冷媒が
蒸発器内に滞留し、除霜時間が長くかかったり、圧縮機
に液バツクしたり、母吸入冷媒を再蒸発装置で処理しな
ければならないと云う問題点は本発明の場合には有り得
ない。液冷媒ポンプで凝縮液冷媒を速かに蒸発器外へ移
送させるので、除霜時間は著しく短縮され、除霜中は吸
入弁を閉鎖させるので圧縮機は低温の凝縮液冷媒を直接
に吸引しないから、液バツクの問題は起らない。除霜時
間が短かいため、蒸発器から除霜熱が庫内に拡散する時
間が短かく、従って、庫内温度の上昇は最低に抑えられ
、保管商品の品質劣化は遅れる。凝縮液冷媒を加熱して
ホット液冷媒となし、吸入管中に設けたホット液冷媒噴
霧室に噴霧すると、ホット液冷媒は高温低圧ガス冷媒と
なり、従来の低温凝縮液冷媒を圧縮機が吸引し、ホット
ガス蓄熱再蒸発装置で加熱して高温低圧ガス冷媒にさせ
た行程と同じ効果があり、従って大型の高価な従来のホ
ットガス蓄熱再蒸発装置等は不必要である。蒸発器内に
耐着したり滞留する冷凍機油は、除霜時ごとに液冷媒ポ
ンプによってホット液冷媒噴霧室内に噴霧され圧縮機に
戻るので、冷凍機油返しの問題も起らず、冷却中の蒸発
器の熱交換効率も向上する。上述の請求項の第一から第
四の発明にかかる除霜方法及び除霜装置の構成は、何れ
も圧縮機1台と蒸発器1台の場合の除霜方法及び除霜装
置であるが、弁類を増加し制御装置を変更することによ
って複数の蒸発器を同時に冷却と除霜を行わせることが
出来る上、請求項第二の発明の除霜装置と、第四の発明
の除霜装置とを合体した乾式蒸発器のホット液冷媒とホ
ットガスとを両用した液冷媒ポンプを用いた除霜方法及
び除霜装置が得られる。請求項第一から第四の発明の除
霜方法及び除霜装置は、大型の装置を必要とせずに、経
済的に、除霜消費電力も少く、除霜が短時間で行われ、
従って庫内温度の上昇も少く、保管商品の品質劣化を抑
止する効果が得られた。
Since the refrigerating machine oil that adheres or remains in the evaporator is transferred to the outside of the evaporator by the liquid refrigerant pump every time defrosting is performed, the heat exchange efficiency of the evaporator during cooling operation is improved. During defrosting, the compressor is stopped and a small horsepower liquid refrigerant pump is operated to defrost, so the power consumption for defrosting is low and the life of the compressor is extended. In conventional defrosting equipment using liquid refrigerant, one evaporator is filled with liquid refrigerant whose temperature is not so high, and only the amount supplied to the expansion valve of the other evaporator is transferred to the liquid refrigerant. Since the moving speed of the liquid refrigerant in the evaporator is only 1, and the defrosting is performed using the sensible heat of the liquid refrigerant, the defrosting time is long and the defrosting efficiency is poor. Therefore, it is not suitable for defrosting an evaporator where the internal temperature is in the low temperature range. In the defrosting method and defrosting device of the present invention, the temperature of the hot liquid refrigerant for defrosting can be adjusted from low to high temperature, so it can be used when the outside temperature is low and for defrosting the evaporator when the internal temperature is in the low range. Since the hot liquid refrigerant for defrosting is rapidly circulated in the evaporator by the liquid refrigerant pump, the defrosting time is significantly shortened and the defrosting efficiency is high. To defrost an evaporator with a low internal temperature in severe winters or extremely cold regions, instead of using hot gas heat storage to heat the liquid refrigerant heating coil, use another heat source, such as an oil water heater, to defrost the evaporator. When used, it is possible to defrost any evaporator whose internal temperature is in the low range. Since the defrosting method and defrosting device according to the third and fourth inventions use hot gas for defrosting, the defrosting method and the defrosting device according to the third and fourth inventions use hot gas for defrosting.
Suitable for defrosting an evaporator with an internal temperature of . In conventional hot gas defrosting, the condensed refrigerant after hot gas defrost stays in the evaporator, resulting in long defrosting times, liquid backlog in the compressor, and reevaporation of the mother suction refrigerant. The problem of having to deal with it is not possible in the case of the present invention. Since the liquid refrigerant pump quickly transfers the condensed refrigerant to the outside of the evaporator, the defrosting time is significantly shortened, and the suction valve is closed during defrosting, so the compressor does not directly suck in the low-temperature condensed refrigerant. Therefore, there is no problem of liquid back up. Since the defrosting time is short, the time for the defrosting heat from the evaporator to diffuse into the refrigerator is short, so the rise in temperature inside the refrigerator is kept to a minimum and the deterioration of the quality of stored products is delayed. When the condensed liquid refrigerant is heated to become hot liquid refrigerant and sprayed into the hot liquid refrigerant spray chamber provided in the suction pipe, the hot liquid refrigerant becomes a high temperature and low pressure gas refrigerant, and the compressor sucks the conventional low temperature condensed liquid refrigerant. It has the same effect as the process of heating the hot gas refrigerant to a high-temperature, low-pressure gas refrigerant using a hot gas heat storage and reevaporation device, so there is no need for a large and expensive conventional hot gas heat storage and reevaporation device. Refrigerating machine oil that adheres or accumulates in the evaporator is sprayed into the hot liquid refrigerant spray chamber by the liquid refrigerant pump every time the defrost is performed and returned to the compressor, so there is no problem with refrigerating machine oil return, and during cooling. The heat exchange efficiency of the evaporator is also improved. The configurations of the defrosting method and defrosting device according to the first to fourth inventions of the above claims are all defrosting methods and defrosting devices in the case of one compressor and one evaporator, By increasing the number of valves and changing the control device, a plurality of evaporators can be cooled and defrosted simultaneously, and the defrosting device of the second invention and the defrosting device of the fourth invention A defrosting method and a defrosting device using a liquid refrigerant pump that uses both hot liquid refrigerant and hot gas in a dry evaporator can be obtained. The defrosting method and defrosting device of the first to fourth inventions do not require a large-sized device, are economical, have low defrosting power consumption, and defrost in a short time,
Therefore, the rise in temperature inside the warehouse was small, and the effect of suppressing quality deterioration of stored products was achieved.

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

第一図は、請求項第−及び第二の発明の乾式蒸発器の冷
媒液ポンプを用いた除霜方法及び除霜装置に係る構成図
、第二図は、請求項第三及び第四の発明の乾式蒸発器の
冷媒液ポンプを用いた除霜方法及び除霜装置に係る構成
図である。第一 第二図中において、点線矢印は液冷媒
の、−点矢印はホット液冷媒の、二点矢印は除霜清液冷
媒の、三点矢印はホットガスの、直線矢印は吸入ガス冷
媒の配管内の進行方向を示す。図において、l・・・吸
入弁、2・液弁、3・・受液器液供給弁、4・・除霜済
液弁、5・・・液冷媒ポンプ、6・除霜用液冷媒循環弁
、7・除霜制御装置、8 圧縮機、9受液器、10 液
冷媒加熱コイル、11トガス蓄熱タンク、16・・蓄熱
温度調節器、17 ・ホットガスバイパス弁、18・・
除霜終了温度調節器、19・・・受液器液戻し弁、20
・除霜清液冷媒取出し管、21・膨張弁、22・逆止弁
、23・吸入管、24・・液管、25・受液器液供給管
、26−・三分岐部、27蒸発器出ロ管、28 受液器
液戻し管、29 供給液量調節弁、30・・吸入放出管
、31・気液分離器、32 ホット液冷媒噴霧室、33
・吐出管、34・・ホットガス管、35ホツトガス弁、
 36 ホットガス流入管、 37 噴霧液量調節弁。
Fig. 1 is a block diagram of a defrosting method and defrosting device using a refrigerant liquid pump for a dry evaporator according to the second and second claims, and Fig. 2 is a block diagram of a defrosting device according to the third and fourth claims. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a configuration diagram of a defrosting method and a defrosting device using a refrigerant liquid pump of a dry evaporator of the invention. 1 In Figure 2, dotted arrows indicate liquid refrigerant, - dot arrows indicate hot liquid refrigerant, two-dot arrows indicate defrosting liquid refrigerant, three-dot arrows indicate hot gas, and straight arrows indicate suction gas refrigerant. Indicates the direction of movement within the pipe. In the figure, l...suction valve, 2. liquid valve, 3. liquid receiver liquid supply valve, 4.. defrosted liquid valve, 5.. liquid refrigerant pump, 6. liquid refrigerant circulation for defrosting. Valve, 7. Defrost control device, 8. Compressor, 9. Liquid receiver, 10. Liquid refrigerant heating coil, 11. Heat storage tank, 16.. Heat storage temperature controller, 17.. Hot gas bypass valve, 18..
Defrosting end temperature regulator, 19... Receiver liquid return valve, 20
・Defrosting liquid refrigerant extraction pipe, 21・Expansion valve, 22・Check valve, 23・Suction pipe, 24・Liquid pipe, 25・Liquid receiver liquid supply pipe, 26・・Three branch part, 27 Evaporator Outlet pipe, 28 Receiver liquid return pipe, 29 Supply liquid amount control valve, 30... Suction/discharge pipe, 31/ Gas-liquid separator, 32 Hot liquid refrigerant spray chamber, 33
・Discharge pipe, 34...Hot gas pipe, 35 Hot gas valve,
36 Hot gas inflow pipe, 37 Spray liquid amount control valve.

Claims (1)

【特許請求の範囲】 1、乾式蒸発器に、ホット液冷媒流入管と、除霜済液冷
媒取出管を設け、液冷媒ポンプを用いて液冷媒加熱コイ
ルと乾式蒸発器間に、ホット液冷媒の除霜用液冷媒循環
管路を構成させ、ホット液冷媒を循環させて除霜を行い
、吸入管に自動開閉弁を設け、除霜中は閉鎖させること
を特徴とする乾式蒸発器の液冷媒ポンプを用いた除霜方
法。 2、乾式蒸発器に、ホット液冷媒流入管と、除霜済液冷
媒取出管を設け、液冷媒ポンプを用いて液冷媒加熱コイ
ルと乾式蒸発器間に、ホット液冷媒の除霜用液冷媒循環
管路を構成させ、ホット液冷媒を循環させて除霜を行い
、吸入管に自動開閉弁を設け、除霜中は閉鎖させること
を特徴とする乾式蒸発器の液冷媒ポンプを用いた除霜装
置。 3、乾式蒸発器に、ホットガス流入管と、除霜済液冷媒
取出管を設け、液冷媒ポンプを用いて、除霜済液冷媒取
出管から、ホットガスの凝縮液冷媒を吸引し、液冷媒加
熱コイルを通過させて、ホット液冷媒とし、吸入管内に
噴霧放出させ、吸入管に自動開閉弁を設け、除霜中は閉
鎖させることを特徴とする乾式蒸発器の液冷媒ポンプを
用いた除霜方法。 4、乾式蒸発器に、ホットガス流入管と、除霜済液冷媒
取出管を設け、液冷媒ポンプを用いて、除霜済液冷媒取
出管から、ホットガスの凝縮液冷媒を吸引し、液冷媒加
熱コイルを通過させて、ホット液冷媒とし、吸入管内に
噴霧放出させ、、吸入管に自動開閉弁を設け、除霜中は
閉鎖させることを特徴とする乾式蒸発器の液冷媒ポンプ
を用いた除霜装置。
[Claims] 1. The dry evaporator is provided with a hot liquid refrigerant inlet pipe and a defrosted liquid refrigerant outlet pipe, and a liquid refrigerant pump is used to supply the hot liquid refrigerant between the liquid refrigerant heating coil and the dry evaporator. A liquid dry evaporator characterized by comprising a defrosting liquid refrigerant circulation pipe, performing defrosting by circulating hot liquid refrigerant, and providing an automatic opening/closing valve in the suction pipe, which is closed during defrosting. Defrosting method using a refrigerant pump. 2. A hot liquid refrigerant inflow pipe and a defrosted liquid refrigerant take-out pipe are installed in the dry evaporator, and a liquid refrigerant pump is used to supply the defrosting liquid refrigerant between the liquid refrigerant heating coil and the dry evaporator. A method of defrosting using a liquid refrigerant pump of a dry evaporator, which is characterized by configuring a circulation pipe, circulating hot liquid refrigerant to perform defrosting, and providing an automatic opening/closing valve in the suction pipe, which is closed during defrosting. frost device. 3. The dry evaporator is equipped with a hot gas inflow pipe and a defrosted liquid refrigerant take-out pipe, and a liquid refrigerant pump is used to suck the hot gas condensate refrigerant from the defrosted liquid refrigerant take-out pipe. A liquid refrigerant pump for a dry evaporator is used, which is characterized by passing the refrigerant through a heating coil to form a hot liquid refrigerant and spraying it into the suction pipe, and installing an automatic opening/closing valve in the suction pipe, which is closed during defrosting. Defrosting method. 4. The dry evaporator is equipped with a hot gas inflow pipe and a defrosted liquid refrigerant take-out pipe, and a liquid refrigerant pump is used to suck the hot gas condensate refrigerant from the defrosted liquid refrigerant take-out pipe. A liquid refrigerant pump for a dry evaporator is used, which is characterized by passing the refrigerant through a heating coil to form a hot liquid refrigerant and spraying it into the suction pipe.The suction pipe is equipped with an automatic opening/closing valve, which is closed during defrosting. Defrost equipment.
JP3573390A 1990-02-16 1990-02-16 Method and apparatus for defrosting using liquid refrigerant pump for dry vaporizer Pending JPH03241277A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3573390A JPH03241277A (en) 1990-02-16 1990-02-16 Method and apparatus for defrosting using liquid refrigerant pump for dry vaporizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3573390A JPH03241277A (en) 1990-02-16 1990-02-16 Method and apparatus for defrosting using liquid refrigerant pump for dry vaporizer

Publications (1)

Publication Number Publication Date
JPH03241277A true JPH03241277A (en) 1991-10-28

Family

ID=12450033

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3573390A Pending JPH03241277A (en) 1990-02-16 1990-02-16 Method and apparatus for defrosting using liquid refrigerant pump for dry vaporizer

Country Status (1)

Country Link
JP (1) JPH03241277A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6318107B1 (en) * 1999-06-15 2001-11-20 D. S. Inc. (Defrost Systems Inc.) Advanced defrost system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6318107B1 (en) * 1999-06-15 2001-11-20 D. S. Inc. (Defrost Systems Inc.) Advanced defrost system

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