JPH09329370A - Adsorption refrigerator - Google Patents

Adsorption refrigerator

Info

Publication number
JPH09329370A
JPH09329370A JP8146075A JP14607596A JPH09329370A JP H09329370 A JPH09329370 A JP H09329370A JP 8146075 A JP8146075 A JP 8146075A JP 14607596 A JP14607596 A JP 14607596A JP H09329370 A JPH09329370 A JP H09329370A
Authority
JP
Japan
Prior art keywords
adsorption
adsorbent
tube
fin
heat
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.)
Withdrawn
Application number
JP8146075A
Other languages
Japanese (ja)
Inventor
Shuichi Adachi
秀一 安達
Toshiaki Takeuchi
稔朗 竹内
Yoshio Miyairi
嘉夫 宮入
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP8146075A priority Critical patent/JPH09329370A/en
Publication of JPH09329370A publication Critical patent/JPH09329370A/en
Withdrawn legal-status Critical Current

Links

Classifications

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

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

PROBLEM TO BE SOLVED: To accelerate and improve the heat transmission speed of an adsorption element by a method wherein a metallic yarn is mixed in an adsorbent fixed at the adsorption element. SOLUTION: A tube 3 through which a heating medium (hot water) or a refrigerant (cooling water) on the heat source side flows is extended through the vacuum vessel of an adsorption type refrigerating device. A fin 4 is spirally and integrally formed in the tube 3. Further, adsorption elements 6 are fixed between the adjoining fins 4. An adsorbent 11 and a metallic yarn 12 integrally molded by a bonding agent 13 are used as the adsorption element 6. When the metallic yarn 12 makes contact with the outer periphery of a tube 3 and the side of the fin 4, thermal conductivity is improved. Or, instead of the metallic yarn 12, a strip-form metallic piece 14, such as an aluminum foil having high thermal conductivity, having a given length may be used.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、吸着剤を用いて熱
交換を行なう吸着式冷凍装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an adsorption type refrigeration system for exchanging heat with an adsorbent.

【0002】[0002]

【従来の技術】図3の(a)は、従来のこの種の吸着式
冷凍装置の構成を示す図であり、図3の(b)はその構
成要素であるチューブを示す断面図である。これらの構
成は、実開昭63−142659号公報に開示されてい
る。
2. Description of the Related Art FIG. 3 (a) is a diagram showing the structure of a conventional adsorption type refrigerating apparatus of this type, and FIG. 3 (b) is a sectional view showing a tube which is a component thereof. These configurations are disclosed in Japanese Utility Model Application Laid-Open No. Sho 63-142659.

【0003】図3の(a)および(b)に示す吸着式冷
凍装置は、所要量の水等の冷媒を封入した真空容器の胴
体51の内部空間53に、熱源側熱媒を通過させる第1
のフィンチューブ52,52と、利用側熱媒を通過させ
る第2のフィンチューブ54,54とを収設している。
第1のフィンチューブ52においては、伝熱管56の外
面に直交する複数のフィン57が配設されている。また
第2のフィンチューブ54においては、伝熱管61の外
面にワイヤーフィン62が螺旋状に配設されている。
In the adsorption type refrigerating apparatus shown in FIGS. 3A and 3B, a heat source side heating medium is passed through an internal space 53 of a body 51 of a vacuum container in which a required amount of refrigerant such as water is sealed. 1
The fin tubes 52, 52 and the second fin tubes 54, 54 for allowing the heat medium on the use side to pass therethrough are housed.
In the first fin tube 52, a plurality of fins 57 that are orthogonal to the outer surface of the heat transfer tube 56 are arranged. In the second fin tube 54, the wire fins 62 are spirally arranged on the outer surface of the heat transfer tube 61.

【0004】フィン57の表面には、天然ゼオライト・
活性炭・活性アルミナあるいはシリカゲルの如き吸着剤
58が、この吸着剤58より熱伝導率の高いバインダー
59例えばスミセラム(商品名)などの耐熱性無機質接
着剤を用いて各フィン57の間隙の約3分の1程度の薄
い層状に接着されている。これらの固体状態の吸着剤5
8の層の間に、フィン57の先端から伝熱管56の外周
面に至る冷媒蒸気通路としての偏平な空隙60が形成さ
れている。
On the surface of the fin 57, natural zeolite
An adsorbent 58 such as activated carbon, activated alumina or silica gel is used as a binder 59 having a higher thermal conductivity than the adsorbent 58, for example, a heat-resistant inorganic adhesive such as Sumiceram (trade name) is used for about 3 minutes of space between the fins 57. No. 1 is bonded in a thin layer. These solid-state adsorbents 5
Between the eight layers, a flat void 60 is formed as a refrigerant vapor passage extending from the tips of the fins 57 to the outer peripheral surface of the heat transfer tube 56.

【0005】胴体51の底部は、胴体底面511を温水
または冷却水に通過させて、加熱または冷却するタンク
63が一体的に備えられているとともに、タンク63の
下方位置において、中間に真空バルブ64を備えた配管
65を介して、常時真空を保持し得る所定容量の冷媒貯
蔵タンク66に接続されている。
The bottom of the body 51 is integrally provided with a tank 63 which heats or cools the bottom surface 511 of the body by passing it through hot water or cooling water. A vacuum valve 64 is provided in the middle of the tank 63 below the tank 63. It is connected to a refrigerant storage tank 66 having a predetermined capacity capable of constantly maintaining a vacuum via a pipe 65 provided with.

【0006】また、前記吸着剤の熱伝導率を向上させる
ために、吸着剤58自体に銅粉などの熱伝導率の高い物
質を予め混入して固化し、これをフィン57に固着した
り、予め銅粉を混入したバインダー59を用いて粒状吸
着剤58をフィン57に接着する方法も提供されてい
る。さらに、フィン57に固着される吸着剤58の形態
として、図4の(a)〜(d)に示すものがある。図4
の(a)〜(d)において図3の(b)と同一な部分に
は同一符号を付してある。
Further, in order to improve the thermal conductivity of the adsorbent, a substance having a high thermal conductivity such as copper powder is previously mixed into the adsorbent 58 itself and solidified, and this is fixed to the fin 57, There is also provided a method of adhering the granular adsorbent 58 to the fins 57 using a binder 59 in which copper powder is mixed in advance. Further, as a form of the adsorbent 58 fixed to the fin 57, there are the forms shown in FIGS. 4 (a) to 4 (d). FIG.
3A to 3D, the same parts as those in FIG. 3B are denoted by the same reference numerals.

【0007】次に、上記のような構成をなす吸着式冷凍
装置の作用を述べる。まず脱着運転時において、第1の
フィンチューブ52に熱源側熱媒(例えば60〜80℃
の熱水)を供給し吸着剤58を加熱脱着するとともに、
第2のフィンチューブ54にクーリングタワー等で生成
した30〜32℃の冷却水を供給する。すると、吸着剤
58の加熱脱着により吐き出された冷媒蒸気が第2のフ
ィンチューブ54の表面で冷却されて凝縮し、液状の冷
媒がフィン62および伝熱管61の対向間隙に液膜状態
で多量に保持される。すなわち、第1のフィンチューブ
52においては吸着剤58がフィン57に直接固着さ
れ、吸着剤58の粒子がフィン57の表面と面接触し、
この部分での熱伝達率が高くなっているため、加熱速度
が大きく脱着工程時間が大幅に短縮される。
Next, the operation of the adsorption type refrigerating apparatus having the above structure will be described. First, during the desorption operation, the heat source side heat medium (for example, 60 to 80 ° C.) is added to the first fin tube 52.
Hot water) to heat and desorb the adsorbent 58,
Cooling water of 30 to 32 ° C. generated by a cooling tower or the like is supplied to the second fin tubes 54. Then, the refrigerant vapor discharged by the heat desorption of the adsorbent 58 is cooled and condensed on the surface of the second fin tube 54, and a large amount of liquid refrigerant is formed in the opposed gap between the fin 62 and the heat transfer tube 61 in a liquid film state. Retained. That is, in the first fin tube 52, the adsorbent 58 is directly fixed to the fin 57, and the particles of the adsorbent 58 make surface contact with the surface of the fin 57,
Since the heat transfer coefficient in this portion is high, the heating rate is high and the desorption process time is greatly shortened.

【0008】次に、吸着運転時の作用を述べる。まず、
第1のフィンチューブ52に冷却水(30〜32℃)を
供給し、吸着剤58を冷却し胴体51内の冷媒蒸気を吸
着させる。すると、第2のフィンチューブ54の表面で
は、フィン62に保持された冷媒が盛んに蒸発し、フィ
ンチューブ54から気化熱を奪い第2のフィンチューブ
54内を通過する利用側熱媒体は、その入口温度12℃
から出口温度7℃程度まで冷却される。
Next, the operation during the adsorption operation will be described. First,
Cooling water (30 to 32 ° C.) is supplied to the first fin tube 52 to cool the adsorbent 58 and adsorb the refrigerant vapor in the body 51. Then, on the surface of the second fin tube 54, the refrigerant held by the fins 62 evaporates vigorously, deprives the fin tube 54 of heat of vaporization, and the utilization side heat medium passing through the second fin tube 54 is Inlet temperature 12 ° C
To the outlet temperature of about 7 ° C.

【0009】なお、運転条件(温度条件)の変化により
胴体51内部の冷媒封入量が過多になった場合は、第2
のフィンチューブ54内への冷媒供給を遮断したまま第
1のフィンチューブ52に熱源側熱媒を供給する。そし
て吸着剤58を加熱脱着しながら、タンク63に冷却水
を供給すると、胴体51内の冷媒はそのほとんどが胴体
51の底面511で凝縮するので、このとき真空バルブ
64を開放すると冷媒液は重力により冷媒貯蔵タンク6
5に回収される。
If the amount of refrigerant charged in the body 51 becomes excessive due to a change in operating conditions (temperature conditions), the second
The heat source side heat medium is supplied to the first fin tube 52 while the supply of the refrigerant into the fin tube 54 is shut off. When cooling water is supplied to the tank 63 while heating and desorbing the adsorbent 58, most of the refrigerant in the body 51 is condensed on the bottom surface 511 of the body 51. Therefore, if the vacuum valve 64 is opened at this time, the refrigerant liquid is gravitational force. Refrigerant storage tank 6
Recovered in 5.

【0010】[0010]

【発明が解決しようとする課題】上述した従来の吸着式
冷凍装置は、フィンチューブのフィン表面に吸着剤を固
着したものであり、両者間の熱伝導率を高める手段とし
て提供されたものである。吸着剤が真空容器胴体内の水
分を吸着した場合における吸着熱は、フィンを介してフ
ィンチューブ内の流体に吸収させるが、銅粉などが混入
された吸着剤は該銅粉などがそれぞれ分離した状態であ
る。そのため、該銅粉を混入しない場合より熱伝導は良
くなるが、該銅粉を大量に混入しないと熱伝導が向上し
ないという欠点がある。また、混入量を多くし過ぎると
吸着剤の量が少くなり、吸着量が少なくなるという問題
がある。本発明の目的は、吸着エレメントにおける熱伝
導速度を加速向上させることで、被吸着剤の脱着・吸着
を促進する吸着式冷凍装置を提供することにある。
The above-mentioned conventional adsorption type refrigerating apparatus is one in which an adsorbent is fixed to the fin surface of a fin tube and is provided as a means for increasing the thermal conductivity between the two. . The heat of adsorption when the adsorbent adsorbs the water in the vacuum container body is absorbed by the fluid in the fin tube through the fins, but the copper powder is separated from the adsorbent mixed with copper powder. It is in a state. Therefore, the heat conduction is better than when the copper powder is not mixed, but there is a disadvantage that the heat conduction is not improved unless the copper powder is mixed in a large amount. Further, if the mixing amount is too large, the amount of the adsorbent becomes small, and the amount of adsorption becomes small. An object of the present invention is to provide an adsorption type refrigerating apparatus which accelerates desorption / adsorption of an adsorbent by increasing the heat conduction rate in the adsorption element.

【0011】[0011]

【課題を解決するための手段】上記課題を解決し目的を
達成するために、本発明の吸着式冷凍装置は以下の如く
構成されている。 (1)本発明の吸着式冷凍装置は、内部に熱媒体を流す
チューブの表面にフィンを設け前記チューブおよび前記
フィンの表面に吸着剤を固着した吸着エレメントを有す
る吸着式冷凍装置において、前記吸着エレメントに固着
された前記吸着剤内に金属糸を混入している。 (2)本発明の吸着式冷凍装置は、内部に熱媒体を流す
チューブの表面にフィンを設け前記チューブおよび前記
フィンの表面に固体状態の吸着剤を固着した吸着エレメ
ントを有する吸着式冷凍装置において、前記吸着エレメ
ントに固着された前記吸着剤内に短冊状の金属薄片を混
入している。 (3)本発明の吸着式冷凍装置は上記(1)または
(2)に記載の装置であって、かつ前記金属糸または前
記金属薄片を前記チューブおよび前記フィンの表面に接
触させている。
In order to solve the above problems and achieve the object, the adsorption type refrigerating apparatus of the present invention is constructed as follows. (1) The adsorption refrigeration apparatus of the present invention is the adsorption refrigeration apparatus having a fin provided on a surface of a tube through which a heat medium flows inside, and an adsorption element having an adsorbent adhered to the surface of the tube and the fin. A metal thread is mixed in the adsorbent fixed to the element. (2) The adsorption refrigeration apparatus of the present invention is an adsorption refrigeration apparatus having a fin on the surface of a tube through which a heat medium flows and an adsorption element having a solid adsorbent adhered to the surface of the tube and the fin. Strip-shaped metal flakes are mixed in the adsorbent fixed to the adsorption element. (3) The adsorption type refrigeration apparatus of the present invention is the apparatus described in (1) or (2) above, wherein the metal thread or the metal flakes are brought into contact with the surfaces of the tubes and the fins.

【0012】上記手段を講じた結果、それぞれ次のよう
な作用が生じる。 (1)本発明の吸着式冷凍装置によれば、前記吸着エレ
メントに固着された前記吸着剤内に金属糸を混入してい
るので、前記吸着エレメント内の温度が早く均一になる
とともに、その熱伝導速度が加速向上することで、前記
吸着エレメントにおける被吸着剤の脱着・吸着を促進さ
せ、熱交換器における蒸発・凝縮を効果的に行なうこと
ができる。 (2)本発明の吸着式冷凍装置によれば、前記吸着エレ
メントに固着された前記吸着剤内に短冊状の金属薄片を
混入しているので、前記吸着エレメント内の温度が早く
均一になるとともに、その熱伝導速度(熱移動)が加速
向上することで、前記吸着エレメントにおける被吸着剤
の脱着・吸着を促進させ、熱交換器における蒸発・凝縮
を効果的に行なうことができる。 (3)本発明の吸着式冷凍装置によれば、前記金属糸ま
たは前記金属薄片を前記チューブおよび前記フィンの表
面に接触させているので、前記チューブ、前記フィン、
および前記吸着エレメントの前記金属糸または前記金属
片を介して前記吸着剤を冷却することにより、当該吸着
式冷凍装置を構成する真空容器内の被吸着剤が前記吸着
エレメントの吸着剤に吸着される。したがって、前記真
空容器内の被吸着剤の濃度は低くなり、前記真空容器の
下部にあり前記熱交換器に接する被吸着剤は蒸発するこ
とになり、そのとき発生する水蒸気がその周囲から気化
熱を奪う。よって、前記熱交換器の冷水はさらに冷却さ
れ、その冷却された低温の冷水を利用することが可能に
なる。
As a result of taking the above-described measures, the following effects are produced. (1) According to the adsorption type refrigeration apparatus of the present invention, since the metal thread is mixed in the adsorbent fixed to the adsorption element, the temperature in the adsorption element becomes fast and uniform, and Since the conduction speed is accelerated and improved, desorption and adsorption of the adsorbent in the adsorption element can be promoted, and evaporation and condensation in the heat exchanger can be effectively performed. (2) According to the adsorption refrigeration apparatus of the present invention, since strip-shaped thin metal flakes are mixed in the adsorbent fixed to the adsorption element, the temperature in the adsorption element becomes fast and uniform. Since the heat conduction speed (heat transfer) is accelerated and improved, desorption / adsorption of the adsorbent in the adsorption element can be promoted, and evaporation / condensation in the heat exchanger can be effectively performed. (3) According to the adsorption type refrigeration apparatus of the present invention, since the metal thread or the metal flakes are brought into contact with the surfaces of the tube and the fin, the tube, the fin,
And by cooling the adsorbent through the metal thread or the metal piece of the adsorption element, the adsorbent in the vacuum container constituting the adsorption refrigeration apparatus is adsorbed by the adsorbent of the adsorption element. . Therefore, the concentration of the adsorbent in the vacuum container becomes low, the adsorbent in the lower part of the vacuum container in contact with the heat exchanger is evaporated, and the water vapor generated at that time evaporates from its surroundings. Take away. Therefore, the cold water of the heat exchanger is further cooled, and the cooled low-temperature cold water can be used.

【0013】[0013]

【発明の実施の形態】図1は、本発明の実施の形態に係
る吸着式冷凍装置の構成を示す図である。図1におい
て、吸着式冷凍装置1の真空容器2には、熱源側の熱媒
(温水)または冷媒(冷却水)が流通するチューブ3が
貫挿されている。このチューブ3にはフィン4がスパイ
ラル状に一体成形されて設けられており、このフィン4
の各間隙には吸着エレメント6が固着されている。真空
容器2内の下部には被吸着剤である水が充填されてお
り、さらに蒸発・凝縮の機能を備えた熱交換器7が設け
られ、冷水が入出するよう配管接続されている。
1 is a diagram showing the configuration of an adsorption type refrigerating apparatus according to an embodiment of the present invention. In FIG. 1, a tube 3 through which a heat medium (warm water) or a refrigerant (cooling water) on the heat source side flows is inserted into a vacuum container 2 of an adsorption type refrigeration apparatus 1. The fins 4 are integrally formed on the tube 3 in a spiral shape.
An adsorption element 6 is fixed to each of the gaps. The lower part of the vacuum container 2 is filled with water as an adsorbent, and a heat exchanger 7 having a function of evaporation / condensation is further provided, and is connected by piping so that cold water can flow in and out.

【0014】図1ではフィン4が一体成形されて設けら
れているが、ロウ(蝋)付け等で固着されるようにして
もよい。さらに、その形状はスパイラル状に限らず、輪
形状のものを等間隔で取り付けてもよい。また被吸着剤
として水を用いたが、その他の吸着剤に吸着されるもの
でもよい。しかし、取扱いの容易さから水であることが
好ましい。
Although the fin 4 is integrally formed in FIG. 1, it may be fixed by brazing. Furthermore, the shape is not limited to a spiral shape, and a ring-shaped shape may be attached at equal intervals. Although water is used as the adsorbent, it may be adsorbed by other adsorbents. However, water is preferable because it is easy to handle.

【0015】図2の(a)は、吸着エレメント6の構成
を示す図である。図2の(a)において、チューブ3の
外周とフィン4の間隙側面に固設される吸着エレメント
6は、吸着剤11と金属糸12が結合剤(接着剤)13
によって一体形成されたものである。吸着剤11にはシ
リカゲル・アルミナゲル・活性炭等が用いられている。
FIG. 2A is a diagram showing the structure of the adsorption element 6. In FIG. 2A, in the adsorption element 6 fixedly provided on the outer circumferential surface of the tube 3 and the side surface of the gap between the fins 4, the adsorbent 11 and the metal thread 12 are bonded together (adhesive) 13
It is integrally formed by. As the adsorbent 11, silica gel, alumina gel, activated carbon, or the like is used.

【0016】本実施の形態では、金属糸12として安価
で熱伝導性の良い所定の長さを有する銅やアルミ材を用
いている。金属糸12は吸着エレメント6の吸着剤11
と結合剤13の内にできるだけ均一に混入し、場合によ
っては金属糸12同士が接するか、または金属糸12が
チューブ3の外周およびフィン4の側面に接することで
熱伝導性を高めている。また結合剤13には、エチレン
系酢酸ビニル樹脂・フェノール樹脂などを用い、金属糸
12に代え熱伝導性の良いアルミ箔など所定の長さを有
する短冊状の金属片14を用いることも可能である。
In this embodiment, the metal thread 12 is made of copper or aluminum having a predetermined length which is inexpensive and has good thermal conductivity. The metal thread 12 is the adsorbent 11 of the adsorption element 6.
And the binder 13 are mixed into the binder 13 as evenly as possible, and in some cases, the metal threads 12 are in contact with each other, or the metal threads 12 are in contact with the outer circumference of the tube 3 and the side surfaces of the fins 4 to enhance heat conductivity. It is also possible to use ethylene vinyl acetate resin, phenol resin, or the like as the binder 13, and to replace the metal thread 12 with a strip-shaped metal piece 14 having a predetermined length, such as an aluminum foil having good thermal conductivity. is there.

【0017】図2の(b)および(c)は、吸着エレメ
ント6がチューブ3およびフィン4に固着した状態を示
す断面図である。吸着エレメント6がチューブ3および
フィン4に固着する形状を図2の(b)および(c)に
示すようにすることで、被吸着剤(水)の脱着効果が上
がる。以上の吸着エレメント6の構成において、吸着式
冷凍装置1の運転における脱着工程では、チューブ3内
に熱源側の熱媒である流体(温水等)を流すことによ
り、吸着剤11の再生が行なわれる。すなわち、チュー
ブ3内に温水等を流すことにより、チューブ3とフィン
4および吸着剤エレメント6の金属糸12または金属片
14を介し吸着剤11が加熱され、吸着剤11に吸着保
持された被吸着剤(水)が脱着され、熱交換器7におい
て冷却水により冷され凝縮される。
2B and 2C are sectional views showing a state in which the adsorption element 6 is fixed to the tube 3 and the fin 4. By making the shape in which the adsorption element 6 is fixed to the tube 3 and the fin 4 as shown in FIGS. 2B and 2C, the adsorbing effect of the adsorbent (water) is improved. In the structure of the adsorption element 6 described above, in the desorption process in the operation of the adsorption refrigeration system 1, the adsorbent 11 is regenerated by flowing a fluid (hot water or the like) that is a heat medium on the heat source side into the tube 3. . That is, by flowing hot water or the like into the tube 3, the adsorbent 11 is heated through the tube 3, the fins 4, and the metal threads 12 or the metal pieces 14 of the adsorbent element 6, and the adsorbent 11 adsorbed and held by the adsorbent 11 is adsorbed and held. The agent (water) is desorbed, cooled in the heat exchanger 7 by cooling water and condensed.

【0018】また、運転時の吸着工程においては、吸着
剤11は真空容器2内の被吸着剤(水蒸気)の吸着を行
なう。そのときに発生する吸着熱は、予めチューブ3内
に冷却源熱媒体である流体(冷却水等)を流すことによ
り取り除かれる。すなわち、チューブ3とフィン4およ
び吸着エレメント6の金属糸12または金属片14を介
して吸着剤11を冷却することにより、吸着式冷凍装置
1を構成する真空容器内2の被吸着剤(水蒸気)は、吸
着エレメント6の吸着剤11に吸着される。
In the adsorption step during operation, the adsorbent 11 adsorbs the adsorbent (water vapor) in the vacuum container 2. The heat of adsorption generated at that time is removed by flowing a fluid (cooling water or the like) as a cooling source heat medium into the tube 3 in advance. That is, by cooling the adsorbent 11 through the tubes 3, the fins 4 and the metal threads 12 or the metal pieces 14 of the adsorption element 6, the adsorbed material (steam) in the vacuum container 2 constituting the adsorption refrigeration apparatus 1 is cooled. Are adsorbed by the adsorbent 11 of the adsorption element 6.

【0019】したがって、真空容器2内の被吸着剤(水
蒸気)の濃度は低くなり、これにより真空容器2の下部
にあり熱交換器7に接する被吸着剤(水)は蒸発するこ
とになり、そのとき発生する水蒸気がその周囲から気化
熱を奪う。よって、熱交換器7の冷水はさらに冷却さ
れ、その冷却された低温の冷水を利用することができ
る。このような装置を二式用意し交互に利用すること
で、常に温水を利用して冷水を得ることができる。
Therefore, the concentration of the adsorbent (water vapor) in the vacuum container 2 becomes low, so that the adsorbent (water) in the lower part of the vacuum container 2 in contact with the heat exchanger 7 evaporates, The steam generated at that time removes the heat of vaporization from its surroundings. Therefore, the cold water in the heat exchanger 7 is further cooled, and the cooled low-temperature cold water can be used. By preparing two sets of such devices and alternately using them, cold water can always be obtained by using hot water.

【0020】なお、吸着剤11と結合剤13からなる吸
着エレメント6に金属糸12または金属片14を混入す
ることで、吸着剤11と結合剤13の結合体間の補強が
なされ、吸着剤11と結合剤13が負荷を受けても壊れ
にくくなる。したがって、熱ストレスに対しても抗力を
増す。ここで熱伝導および強度に対しては、金属糸12
を混入した場合の方が金属片14を混入した場合より
も、混入する金属量が同程度であるとすれればその効果
は優れている。しかし金属片14が充分薄いものであれ
ば、実用に際しては充分な効果を奏する。
By mixing the metal thread 12 or the metal piece 14 into the adsorbing element 6 composed of the adsorbent 11 and the binder 13, the adsorbent 11 and the binder 13 are reinforced with each other by the admixture. Therefore, the binder 13 is less likely to be broken even if it receives a load. Therefore, the resistance to heat stress is increased. Here, for heat conduction and strength, the metal thread 12
If the mixed amount of the metal is approximately the same as the mixed amount of the metal piece 14, the effect is excellent. However, if the metal piece 14 is sufficiently thin, sufficient effects can be obtained in practical use.

【0021】つまり金属粉を用いた場合、その金属粉の
周りのごく一部のみ熱伝導率が高くなり、その金属部に
熱が通り温度が均一化される。しかしながらこの場合、
金属粉と金属粉との間は分断されており熱が伝わりにく
いため、金属粉の量を多くしなければならない。しかし
金属糸や金属片であれば、その長さ方向に熱が伝わりや
すく、その表面全域が均一な温度になるので、吸着エレ
メント6の熱伝達が非常に良くなる。
That is, when the metal powder is used, the thermal conductivity is increased only in a small part around the metal powder, and heat is passed through the metal part to make the temperature uniform. However, in this case,
Since the metal powder and the metal powder are separated from each other and heat is hard to be transmitted, the amount of the metal powder has to be increased. However, in the case of a metal thread or a metal piece, heat is easily transferred in the length direction, and the entire surface thereof has a uniform temperature, so that the heat transfer of the adsorption element 6 is very good.

【0022】なお、本発明は上記実施の形態のみに限定
されず、要旨を変更しない範囲で適時変形して実施でき
る。 (実施の形態のまとめ)実施の形態に示された吸着式冷
凍装置1は、所定量の被吸着剤(水)が封入された真空
容器2の胴体内に、吸着剤11に被吸着剤を吸着させる
ときに発生する吸着熱を除去するための流体および被吸
着剤を吸着剤11から脱着するために加熱流体を通すチ
ューブ3、このチューブ3と吸着剤11との間の熱伝達
を容易にするためにチューブ3に設けたフィン4、およ
びチューブ3とフィン4に吸着剤11を固着させるとと
もに、吸着剤11同士を接合させる結合剤(接着剤)1
3からなり、吸着剤11と結合剤13により形成される
吸着エレメント6に金属糸12または短冊状の薄い金属
片14を混入して結合している。
The present invention is not limited to the above-mentioned embodiments, and can be modified and implemented as appropriate without departing from the scope of the invention. (Summary of Embodiments) In the adsorption type refrigeration system 1 shown in the embodiment, the adsorbent 11 is placed in the body of the vacuum container 2 in which a predetermined amount of adsorbent (water) is enclosed. A tube 3 through which a fluid for removing heat of adsorption generated during adsorption and a heating fluid for desorbing the adsorbent from the adsorbent 11 are passed, and heat transfer between the tube 3 and the adsorbent 11 is facilitated. For adhering the adsorbent 11 to the tube 3 and the fins 4 and for joining the adsorbents 11 to each other.
3, the metal thread 12 or the strip-shaped thin metal piece 14 is mixed and bonded to the adsorption element 6 formed by the adsorbent 11 and the binder 13.

【0023】吸着式冷凍装置1の熱源体の流体を供給す
るチューブ3に配設されたフィン4の間隙において、吸
着剤11に金属糸12または金属片14を混入して結合
剤(接着剤)13で形成された吸着エレメント6を固着
することにより、チューブ3内を流通する熱媒体の熱は
吸着剤11と結合剤13同士および混入された金属糸1
2または金属片14を介して、吸着エレメント6の占有
体積内の吸着剤11に確実に熱伝達される。また吸着剤
11の温度が吸着熱により上がった場合、吸着剤11と
結合剤13同士および混入された金属糸12または金属
片14を介してチューブ3内を流れる冷却水に伝達され
る。
In the gap between the fins 4 arranged in the tube 3 for supplying the fluid of the heat source of the adsorption type refrigerating apparatus 1, the adsorbent 11 is mixed with the metal thread 12 or the metal piece 14 to form a binder (adhesive). By fixing the adsorption element 6 formed of 13, the heat of the heat medium flowing in the tube 3 is absorbed by the adsorbent 11 and the binder 13 and the mixed metal thread 1
The heat is reliably transferred to the adsorbent 11 in the volume occupied by the adsorption element 6 via the metal piece 2 or the metal piece 14. When the temperature of the adsorbent 11 rises due to the heat of adsorption, it is transferred to the cooling water flowing in the tube 3 through the adsorbent 11 and the binder 13 and the mixed metal thread 12 or metal piece 14.

【0024】つまり、金属糸12または金属片14を混
入することにより吸着エレメント6内の温度が早く均一
になるとともに、その熱伝導速度(熱移動)を加速向上
させることで、吸着エレメント6における被吸着剤の脱
着・吸着を促進させ、熱交換器7における蒸発・凝縮を
効果的に行なうことができる。すなわち、金属粉を用い
る場合よりはるかに少量の金属片14または金属糸12
を混入することで、熱伝導が良くなり効率の向上が図れ
るとともに、金属粉では得られにくい吸着エレメント6
の強度も向上し、吸着エレメント6の耐久性も向上す
る。
That is, by mixing the metal thread 12 or the metal piece 14, the temperature in the adsorption element 6 becomes faster and uniform, and the heat conduction speed (heat transfer) thereof is accelerated and improved. The desorption / adsorption of the adsorbent can be promoted, and the evaporation / condensation in the heat exchanger 7 can be effectively performed. That is, a much smaller amount of metal pieces 14 or metal threads 12 than when metal powder is used.
By mixing in, the heat conduction is improved and the efficiency is improved, and the adsorption element 6 that is difficult to obtain with metal powder
The strength of the suction element 6 is also improved, and the durability of the adsorption element 6 is also improved.

【0025】[0025]

【発明の効果】本発明によれば、吸着エレメントにおけ
る熱伝導速度を加速向上させることで、被吸着剤の脱着
・吸着を促進する吸着式冷凍装置を提供できる。
According to the present invention, it is possible to provide an adsorption type refrigerating apparatus which accelerates desorption / adsorption of an adsorbent by accelerating and improving the heat conduction rate in the adsorption element.

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

【図1】本発明の実施の形態に係る吸着式冷凍装置の構
成を示す図。
FIG. 1 is a diagram showing a configuration of an adsorption type refrigerating apparatus according to an embodiment of the present invention.

【図2】本発明の実施の形態に係る図であり、(a)は
吸着エレメントの構成を示す図、(b)および(c)は
吸着エレメントがチューブおよびフィンに固着した状態
を示す断面図。
2A and 2B are diagrams according to an embodiment of the present invention, in which FIG. 2A is a diagram showing a structure of an adsorption element, and FIGS. 2B and 2C are sectional views showing a state in which the adsorption element is fixed to a tube and fins. .

【図3】従来例に係る図であり、(a)は吸着式冷凍装
置の構成を示す図、(b)はチューブを示す断面図。
3A and 3B are diagrams related to a conventional example, FIG. 3A is a diagram showing a configuration of an adsorption type refrigerating apparatus, and FIG. 3B is a sectional view showing a tube.

【図4】従来例に係るチューブを示す断面図。FIG. 4 is a sectional view showing a tube according to a conventional example.

【符号の説明】[Explanation of symbols]

1…吸着式冷凍装置 2…真空容器 3…チューブ 4…フィン 6…吸着エレメント 7…熱交換器 11…吸着剤 12…金属糸 13…結合剤(接着剤) 14…金属片 51…胴体 511…胴体底面 52…第1のフィンチューブ 53…内部空間 54…第2のフィンチューブ 56…伝熱管 57…フィン 58…吸着剤 59…バインダー 60…空隙 61…伝熱管 62…ワイヤーフィン 63…タンク 64…真空バルブ 65…配管 66…冷媒貯蔵タンク DESCRIPTION OF SYMBOLS 1 ... Adsorption type | formula freezer 2 ... Vacuum container 3 ... Tube 4 ... Fin 6 ... Adsorption element 7 ... Heat exchanger 11 ... Adsorbent 12 ... Metal thread 13 ... Binder (adhesive) 14 ... Metal piece 51 ... Body 511 ... Body bottom surface 52 ... First fin tube 53 ... Internal space 54 ... Second fin tube 56 ... Heat transfer tube 57 ... Fin 58 ... Adsorbent 59 ... Binder 60 ... Void 61 ... Heat transfer tube 62 ... Wire fin 63 ... Tank 64 ... Vacuum valve 65 ... Piping 66 ... Refrigerant storage tank

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】内部に熱媒体を流すチューブの表面にフィ
ンを設け前記チューブおよび前記フィンの表面に吸着剤
を固着した吸着エレメントを有する吸着式冷凍装置にお
いて、 前記吸着エレメントに固着された前記吸着剤内に金属糸
を混入したことを特徴とする吸着式冷凍装置。
1. An adsorption type refrigeration apparatus having a fin on the surface of a tube through which a heat medium flows inside, and an adsorption element having an adsorbent adhered to the surface of the tube and the fin, wherein the adsorption adhered to the adsorption element An adsorption type refrigerating device characterized in that a metal thread is mixed in the agent.
【請求項2】内部に熱媒体を流すチューブの表面にフィ
ンを設け前記チューブおよび前記フィンの表面に固体状
態の吸着剤を固着した吸着エレメントを有する吸着式冷
凍装置において、 前記吸着エレメントに固着された前記吸着剤内に短冊状
の金属薄片を混入したことを特徴とする吸着式冷凍装
置。
2. An adsorption type refrigeration apparatus having an adsorption element in which a fin is provided on the surface of a tube through which a heat medium flows, and a solid state adsorbent is adhered to the surface of the tube and the fin, the adsorption refrigeration apparatus being fixed to the adsorption element. An adsorbing type refrigerating apparatus, wherein strip-shaped metal flakes are mixed in the adsorbent.
【請求項3】前記金属糸または前記金属薄片を前記チュ
ーブおよび前記フィンの表面に接触させたことを特徴と
する請求項1または2に記載の吸着式冷凍装置。
3. The adsorption type refrigerating apparatus according to claim 1, wherein the metal thread or the metal thin piece is brought into contact with the surfaces of the tube and the fin.
JP8146075A 1996-06-07 1996-06-07 Adsorption refrigerator Withdrawn JPH09329370A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8146075A JPH09329370A (en) 1996-06-07 1996-06-07 Adsorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8146075A JPH09329370A (en) 1996-06-07 1996-06-07 Adsorption refrigerator

Publications (1)

Publication Number Publication Date
JPH09329370A true JPH09329370A (en) 1997-12-22

Family

ID=15399546

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8146075A Withdrawn JPH09329370A (en) 1996-06-07 1996-06-07 Adsorption refrigerator

Country Status (1)

Country Link
JP (1) JPH09329370A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010530953A (en) * 2007-06-22 2010-09-16 アドバンスド テクノロジー マテリアルズ,インコーポレイテッド Components of a solar adsorption refrigeration system and methods for making such components

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010530953A (en) * 2007-06-22 2010-09-16 アドバンスド テクノロジー マテリアルズ,インコーポレイテッド Components of a solar adsorption refrigeration system and methods for making such components
US9132412B2 (en) 2007-06-22 2015-09-15 Entegris, Inc. Component for solar adsorption refrigeration system and method of making such component

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