JPS5826975A - Method and device for supplying refrigerant to evaporator of refrigerator - Google Patents

Method and device for supplying refrigerant to evaporator of refrigerator

Info

Publication number
JPS5826975A
JPS5826975A JP12445981A JP12445981A JPS5826975A JP S5826975 A JPS5826975 A JP S5826975A JP 12445981 A JP12445981 A JP 12445981A JP 12445981 A JP12445981 A JP 12445981A JP S5826975 A JPS5826975 A JP S5826975A
Authority
JP
Japan
Prior art keywords
refrigerant
evaporator
header
coil
pressure
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
JP12445981A
Other languages
Japanese (ja)
Inventor
村山 豪
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.)
Nissin Kogyo Co Ltd
Original Assignee
Nissin Kogyo 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 Nissin Kogyo Co Ltd filed Critical Nissin Kogyo Co Ltd
Priority to JP12445981A priority Critical patent/JPS5826975A/en
Publication of JPS5826975A publication Critical patent/JPS5826975A/en
Pending legal-status Critical Current

Links

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】 本発明は冷媒液が蒸発器コイル内を上方から蒸発しなが
ら自重で下降する方式の冷凍装置に於いて、各蒸発器コ
イルへの冷媒の供給を均等に而も圧力−損失なく分配す
る冷凍装置の蒸発器への冷媒供給方法並びに其の装置に
係るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a refrigeration system in which the refrigerant liquid evaporates from above inside the evaporator coil and descends under its own weight. - A method and apparatus for supplying refrigerant to an evaporator of a refrigeration system without loss.

一般に冷凍装置に於いては蒸発器への冷媒の供給が各コ
イル均等であること、またその際に蒸発器内での冷媒の
圧力損失が可及的小なることが理想とされている。
In general, in a refrigeration system, it is ideal that refrigerant be supplied to the evaporator evenly to each coil, and that the pressure loss of the refrigerant within the evaporator be as small as possible.

然るに従来の蒸発器への冷媒供給は下部のヘッダーよシ
冷媒を供給するボトムフィード式、」二部のヘッダーよ
り冷媒を供給するトップフィード式又はデイヌトリビュ
ー′グーによる供給等が行々われている。
However, the conventional methods of supplying refrigerant to the evaporator include a bottom-feed system that supplies refrigerant through a lower header, a top-feed system that supplies refrigerant through a two-part header, and a system that supplies refrigerant through a double header. There is.

ところがボトムフィード式ではコイル内を冷媒液が蒸発
しながら上昇するので、ヘッダ一部には冷媒液柱分の圧
力が掛かり、各コイルへの冷媒の分配は該液柱圧によっ
である程度均等になるが、該液柱正分だけの圧力損失が
生じるという欠点がある。またトップフィード式ではコ
イル内を冷媒液が蒸発しながら自重で下降するので、冷
媒の圧力損失は全くなく、むしろ場合によってはコイル
部よシヘツダ一部の方が圧力が低いマイナスの圧力損失
になったシする。ところが各コイルへの冷媒の供給を均
等にするためには、上部のヘッダーの据え付けに当シ各
ヘッダーを完全に水平位置にある様据え付けることは現
実には極めて困難であり、通り易いコイルへの流量は多
くなるため、夫々のヘッダーよシ各コイルへの冷媒の均
等な供給が不可能となる。
However, in the bottom feed type, the refrigerant liquid rises inside the coil while evaporating, so the pressure of the refrigerant liquid column is applied to a part of the header, and the refrigerant is distributed to each coil evenly to some extent depending on the liquid column pressure. However, there is a drawback that a pressure loss corresponding to the amount of the liquid column occurs. In addition, in the top-feed type, the refrigerant liquid evaporates inside the coil and descends under its own weight, so there is no pressure loss of the refrigerant at all.In fact, in some cases, there may be a negative pressure loss where the pressure is lower in the coil part than in the head part. Tashi. However, in order to equalize the supply of refrigerant to each coil, it is extremely difficult to install the upper header so that each header is in a completely horizontal position, and it is difficult to install the header in a completely horizontal position. Since the flow rate increases, it becomes impossible to uniformly supply refrigerant to each header and each coil.

このため従来は第6図に示す如く上部ヘッダー内のコイ
ル基端部に細孔16を設けて該ヘッダー内に僅かに圧力
が掛かるようにして均等分配を行なっている。しかしこ
の場合、コイル内には圧力損失はないが、ヘッダーを含
めた蒸発器としての圧力損失は大きくなるという欠点が
ある。更にディストリビュータ−による供給ではディス
トリビュータ−17内部の圧力降下によシ冷媒液を多数
の細管18に均等に分配し、該細管18を各コイル基端
部に連結するため、大きな圧力損失となり、またディス
トリビュータ−の製作精度によ多分配の均等性が左右さ
れる等といった大なる欠点を存し、現在乾式蒸発器のみ
で使用されているに過ぎ々い。
For this reason, conventionally, as shown in FIG. 6, a fine hole 16 is provided at the base end of the coil in the upper header to apply a slight pressure inside the header to achieve even distribution. However, in this case, although there is no pressure loss within the coil, there is a drawback that the pressure loss in the evaporator including the header becomes large. Furthermore, when supplying by a distributor, the refrigerant liquid is evenly distributed to a large number of thin tubes 18 due to the pressure drop inside the distributor 17, and the thin tubes 18 are connected to the base end of each coil, resulting in a large pressure loss. It has major drawbacks such as the fact that the uniformity of distribution depends on the manufacturing precision of -, and is currently used only in dry evaporators.

以上詳述した如〈従来の冷媒供給は冷媒を均等に供給す
ることを主眼とし、成る程度の圧力損失は容認されてい
て、低温冷却を目的とする蒸発器への冷媒の供給方法並
びに装置として充分なものとはいえなかった。即ち冷媒
の蒸発圧力はその温度に於ける飽和圧力であり、温度が
低い程圧力も低く、従って微少な圧力損失でも温度が低
い場合、その冷却効率への影響は極めて大きくなる。例
えば冷媒としてフロン22を使用して一55℃に冷却し
たい場合を考えると、冷媒蒸発温度は一62℃で通常充
分であるが、もし蒸発器に0.182¥j(フロン22
液柱88σ)の圧力損失があれば、圧縮機の吸入ガス体
積は1.6倍となシ、これに圧縮機の効率を加えると略
2倍の大きさの圧縮機を使用しなければ冷却できないこ
とになる。
As detailed above, conventional refrigerant supply focuses on supplying refrigerant evenly, and a certain amount of pressure loss is accepted, and the method and device for supplying refrigerant to an evaporator for low-temperature cooling are It could not be said to be sufficient. That is, the evaporation pressure of the refrigerant is the saturation pressure at that temperature, and the lower the temperature, the lower the pressure.Therefore, even a small pressure loss will have an extremely large effect on cooling efficiency when the temperature is low. For example, if we want to use Freon 22 as a refrigerant to cool the temperature to -55°C, the refrigerant evaporation temperature is usually sufficient at -62°C, but if we use 0.182 yen (Freon 22) in the evaporator,
If there is a pressure loss of 88σ in the liquid column, the suction gas volume of the compressor will be 1.6 times, and if you add the efficiency of the compressor to this, it will not be possible to cool it unless you use a compressor that is approximately twice the size. It turns out you can't do it.

然るに本発明に於いては、前記のトップフィード式の装
置を利用し、水平に設備した上部ヘッダーのパイプ下面
に各冷却コイルの基端を貫通挿嵌し、該冷却コイルの基
端に開口した冷媒液出口に竪型の冷媒流入間隙を穿設し
、ヘッダー内に挿嵌する冷却コイルの太さと該コイル基
部の高さ及び前記間隙の巾と高さとを夫々互いに等しく
したから、冷媒液入口よりヘッダー内に入った冷媒液は
各冷却コイル基端の冷媒液出口にまで溜まシ、オーバー
フローする形で各コイル基端に供給されて行き、均等な
分配が可能となる。またヘッダーに多少の水平度の狂い
があっても、竪型の冷媒流入間隙より冷媒がコイル内に
供給されるので、大きな不均等とはならないものである
。而も本発明に於いては冷媒液に圧力を掛けたシまた圧
力が掛かることもないから、蒸発器に於ける冷媒の圧力
損失もないものである。
However, in the present invention, the above-mentioned top feed type device is used, and the base end of each cooling coil is inserted through the lower surface of the pipe of the upper header installed horizontally, and an opening is formed at the base end of the cooling coil. A vertical refrigerant inlet gap is formed at the refrigerant liquid outlet, and the thickness of the cooling coil inserted into the header, the height of the coil base, and the width and height of the gap are made equal to each other, so that the refrigerant liquid inlet The refrigerant liquid that has entered the header accumulates up to the refrigerant liquid outlet at the base end of each cooling coil, and is then supplied to the base end of each coil in the form of overflow, making it possible to distribute it evenly. Furthermore, even if there is some leveling error in the header, the refrigerant is supplied into the coil through the vertical refrigerant inlet gap, so there is no major unevenness. Furthermore, in the present invention, no pressure is applied to the refrigerant liquid, so there is no pressure loss of the refrigerant in the evaporator.

今、ここに本発明実施の一例を示した添付図面について
詳説する。1は冷凍装置の蒸発器2の上部ヘッダーであ
シ、8は該ヘッダー1のパイプ側面中央部に付設した冷
媒液入口で、該冷媒液人口8よりヘッダー1内に低圧受
液器8よりの冷媒液を液ポンプ9で供給するものである
Reference will now be made in detail to the accompanying drawings, which illustrate one example of carrying out the invention. 1 is the upper header of the evaporator 2 of the refrigeration system, and 8 is the refrigerant liquid inlet attached to the central part of the pipe side of the header 1. The refrigerant liquid is supplied by a liquid pump 9.

4は第2図に示す如く該ヘッダー1のパイプ下面より基
端部の立上がシ部5を多数貫通挿嵌した冷却コイルで、
夫々同一径のパイプを使用し、各冷却コイ/I/4の立
上がり部5のヘッダー1内への挿嵌高さを第3図に示す
如く各冷却コイル4で等しくするものである。6は該冷
却コイル4の基端部上面(立上がり部5先端)に開口し
た冷媒液出口で、7,7は各冷却コイ)L/4の該開口
端より立上がシ部5に穿設した竪型の冷媒流入間隙で、
各冷媒液出口6の太さ、該間隙7゜7の巾及び高さは各
冷却コイ/I/4で等しくするものである。10は蒸発
器2の下部ヘッダーで、各コイ/V 4内を蒸発しなが
ら自重で下降してきた冷媒ガスと冷媒液との混合物を冷
媒ガス出口11よシ前記低圧受液器8に導くよう設備す
るものである。12は該低圧受液器8よりの冷媒ガスを
圧縮し、高圧の冷媒ガスを凝縮器18に供給する冷媒圧
縮機である。14は該凝縮器によシ液化された高圧の冷
媒液を収容する受液器である。15は該受液器14と低
圧受液器i間に介在せしめた膨張弁で、高圧の冷媒液を
低圧の冷媒液に変換するものである。
4 is a cooling coil whose proximal end rises from the lower surface of the pipe of the header 1 and is inserted through a number of holes 5, as shown in FIG.
Pipes of the same diameter are used, and the insertion height of the rising portion 5 of each cooling coil/I/4 into the header 1 is made equal for each cooling coil 4 as shown in FIG. Reference numeral 6 denotes a refrigerant liquid outlet opened at the upper surface of the proximal end of the cooling coil 4 (the tip of the rising part 5), and 7, 7 is a refrigerant liquid outlet opened at the upper surface of the proximal end of the cooling coil 4 (the tip of the rising part 5). In the vertical refrigerant inflow gap,
The thickness of each refrigerant liquid outlet 6 and the width and height of the gap 7.7 are made equal for each cooling coil/I/4. Reference numeral 10 denotes a lower header of the evaporator 2, which is equipped to guide the mixture of refrigerant gas and refrigerant liquid that has descended under its own weight while evaporating inside each coil/V 4 through the refrigerant gas outlet 11 to the low-pressure liquid receiver 8. It is something to do. A refrigerant compressor 12 compresses the refrigerant gas from the low-pressure receiver 8 and supplies high-pressure refrigerant gas to the condenser 18. Reference numeral 14 denotes a liquid receiver for storing the high-pressure refrigerant liquid liquefied by the condenser. Reference numeral 15 denotes an expansion valve interposed between the liquid receiver 14 and the low-pressure liquid receiver i, which converts high-pressure refrigerant liquid into low-pressure refrigerant liquid.

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

添付図面は本発明実施の一例を示したもので、第1図は
トップフィード式を利用した本発明装置のサイクル系統
図、第2図は蒸発器の上部ヘッダーと冷却コイルとの接
合部の要部縦断面図、第3図は第2図A −A線要部断
面図、第4図ははボトムフィード式の蒸発器の要部斜視
図、第6図はトップフィード式の上部ヘッダーと冷却コ
イルの接合部を示す要部断面図、第7図はディストリビ
ュータ−による供給の概略を示す要部斜視図である。 1・・・上部ヘッダー、2・・・蒸発器、8・・・冷媒
液入 口、4・・・冷却コイル、5・・・立上がり部、
6・・・冷媒液出口、7・・・流入間隙、8・・・低圧
受液器、9・・・液ポンプ、10・・・下部ヘッダー、
11・・・冷媒ガス出口、12・・・冷媒圧縮機、13
・・・凝縮器、14・・・受液器、15・・・膨張弁、
16・・・細孔、17・・・ディストリビュータ−11
8・・・細管。 出・・願 人  日新興業株式会社 wJ l 図 第2図    第3図 m− 躬5図 躬6図 b 第7図
The attached drawings show an example of the implementation of the present invention. Figure 1 is a cycle diagram of the apparatus of the present invention using the top feed type, and Figure 2 shows the main points of the joint between the upper header of the evaporator and the cooling coil. Figure 3 is a cross-sectional view of the main part taken along the line A-A in Figure 2, Figure 4 is a perspective view of the main part of a bottom-feed type evaporator, and Figure 6 is a top-feed type upper header and cooling. FIG. 7 is a cross-sectional view of a main part showing a joint part of the coil, and a perspective view of a main part showing an outline of supply by a distributor. 1... Upper header, 2... Evaporator, 8... Refrigerant liquid inlet, 4... Cooling coil, 5... Rising part,
6... Refrigerant liquid outlet, 7... Inflow gap, 8... Low pressure liquid receiver, 9... Liquid pump, 10... Lower header,
11... Refrigerant gas outlet, 12... Refrigerant compressor, 13
...Condenser, 14...Liquid receiver, 15...Expansion valve,
16... Pore, 17... Distributor-11
8...tubule. Applicant: Nichishin Gyogyo Co., Ltd. wJ l Figure 2 Figure 3 m- Figure 5 Figure 6 b Figure 7

Claims (1)

【特許請求の範囲】 1冷媒液が上方より蒸発しながら自重にて下降するに当
り、ヘッダーより冷却用者コイルへの冷媒の配分条件を
均等とすることを特徴とする冷凍装置の蒸発器への冷媒
供給方法。 2冷媒液入口を稍々上位に存するヘッダーパイプを水平
に設備し、該ヘッダーパイプの下面を貫通して冷却コイ
ルの基端を挿嵌し、該基端上面に冷媒液出口を開口する
と共に該開口端より流入間隙を穿設し、同一ヘッダーパ
イプよυ出発する冷却コイルの開口の太さと高さとを各
コイル相互等しくすると共に、前記間隙の太さと高さと
を各冷却コイル相互等しくすることを特徴とする冷凍装
置の蒸発器への冷媒供給装置。
[Scope of Claims] 1. An evaporator for a refrigeration system characterized by equalizing refrigerant distribution conditions from a header to a cooling coil as the refrigerant liquid evaporates from above and descends under its own weight. refrigerant supply method. 2. A header pipe with a refrigerant liquid inlet located slightly above the header pipe is installed horizontally, the base end of the cooling coil is inserted through the bottom surface of the header pipe, and a refrigerant liquid outlet is opened on the top surface of the base end. An inflow gap is bored from the open end, and the thickness and height of the opening of the cooling coils starting from the same header pipe are made equal to each other, and the thickness and height of the gap is made equal to each cooling coil. A refrigerant supply device to an evaporator of a refrigeration system.
JP12445981A 1981-08-07 1981-08-07 Method and device for supplying refrigerant to evaporator of refrigerator Pending JPS5826975A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12445981A JPS5826975A (en) 1981-08-07 1981-08-07 Method and device for supplying refrigerant to evaporator of refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12445981A JPS5826975A (en) 1981-08-07 1981-08-07 Method and device for supplying refrigerant to evaporator of refrigerator

Publications (1)

Publication Number Publication Date
JPS5826975A true JPS5826975A (en) 1983-02-17

Family

ID=14886038

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12445981A Pending JPS5826975A (en) 1981-08-07 1981-08-07 Method and device for supplying refrigerant to evaporator of refrigerator

Country Status (1)

Country Link
JP (1) JPS5826975A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6064639A (en) * 1983-09-19 1985-04-13 伊藤 恭司 Crushing of building aggregate material
JPS6053343U (en) * 1983-09-19 1985-04-15 伊藤 恭司 Construction aggregate grinding equipment
JPS6171846A (en) * 1984-09-17 1986-04-12 川崎重工業株式会社 Regulator for grind grain form
JPS62279849A (en) * 1986-05-27 1987-12-04 川崎重工業株式会社 Jaw crsher
JPS63187078A (en) * 1987-01-28 1988-08-02 株式会社 渡辺製作所 Evaporator and manufacture thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6064639A (en) * 1983-09-19 1985-04-13 伊藤 恭司 Crushing of building aggregate material
JPS6053343U (en) * 1983-09-19 1985-04-15 伊藤 恭司 Construction aggregate grinding equipment
JPS6171846A (en) * 1984-09-17 1986-04-12 川崎重工業株式会社 Regulator for grind grain form
JPS62279849A (en) * 1986-05-27 1987-12-04 川崎重工業株式会社 Jaw crsher
JPS63187078A (en) * 1987-01-28 1988-08-02 株式会社 渡辺製作所 Evaporator and manufacture thereof

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