JPS6249544B2 - - Google Patents
Info
- Publication number
- JPS6249544B2 JPS6249544B2 JP56028493A JP2849381A JPS6249544B2 JP S6249544 B2 JPS6249544 B2 JP S6249544B2 JP 56028493 A JP56028493 A JP 56028493A JP 2849381 A JP2849381 A JP 2849381A JP S6249544 B2 JPS6249544 B2 JP S6249544B2
- Authority
- JP
- Japan
- Prior art keywords
- corrosion
- closed circulation
- lithium bromide
- ruthenium chloride
- absorber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000010521 absorption reaction Methods 0.000 claims description 27
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims description 26
- 239000006096 absorbing agent Substances 0.000 claims description 16
- 239000000243 solution Substances 0.000 claims description 14
- 239000003507 refrigerant Substances 0.000 claims description 12
- 239000007864 aqueous solution Substances 0.000 claims description 11
- 239000003112 inhibitor Substances 0.000 claims description 11
- YBCAZPLXEGKKFM-UHFFFAOYSA-K ruthenium(iii) chloride Chemical compound [Cl-].[Cl-].[Cl-].[Ru+3] YBCAZPLXEGKKFM-UHFFFAOYSA-K 0.000 claims description 11
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 claims description 3
- 150000008044 alkali metal hydroxides Chemical class 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- 238000009833 condensation Methods 0.000 claims 1
- 239000012895 dilution Substances 0.000 claims 1
- 238000010790 dilution Methods 0.000 claims 1
- 230000007797 corrosion Effects 0.000 description 31
- 238000005260 corrosion Methods 0.000 description 31
- 239000007788 liquid Substances 0.000 description 21
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 10
- 230000000694 effects Effects 0.000 description 10
- 239000000463 material Substances 0.000 description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 8
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 8
- 229910052802 copper Inorganic materials 0.000 description 8
- 239000010949 copper Substances 0.000 description 8
- 239000000470 constituent Substances 0.000 description 5
- 229910052742 iron Inorganic materials 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 229910000975 Carbon steel Inorganic materials 0.000 description 3
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002250 absorbent Substances 0.000 description 3
- 230000002745 absorbent Effects 0.000 description 3
- 239000010962 carbon steel Substances 0.000 description 3
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical class [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000005057 refrigeration Methods 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000007865 diluting Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- MEFBJEMVZONFCJ-UHFFFAOYSA-N molybdate Chemical class [O-][Mo]([O-])(=O)=O MEFBJEMVZONFCJ-UHFFFAOYSA-N 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- 229910000640 Fe alloy Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- JQVALDCWTQRVQE-UHFFFAOYSA-N dilithium;dioxido(dioxo)chromium Chemical compound [Li+].[Li+].[O-][Cr]([O-])(=O)=O JQVALDCWTQRVQE-UHFFFAOYSA-N 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000003002 pH adjusting agent Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
本発明は吸収液を臭化リチウム水溶液とし、そ
の濃縮、冷媒希釈および熱交換の繰返しによつて
冷却を行なう密閉循環型吸収式冷凍機に関する。
密閉循環型吸収式冷凍機は冷媒に水を、また吸
収液として臭化リチウムの濃厚水溶液を用いてい
る。第1図にその原理系統図を示すように、この
冷凍機は再生器1、凝縮器2、蒸発器3、吸収器
4およびこれらの間に吸収液6,6a,6bおよ
び冷媒7を循環させるポンプ類8と、熱交換器5
から構成され、各部分は各々次のように作動す
る。
(A) 蒸発器3
蒸発器3の蒸発器管束の管内には冷水12が通
じており、管外には冷媒7が散布され、その蒸発
の潜熱によつて冷水から熱を奪う。
(B) 吸収器4
臭化リチウム水溶液は同じ温度の水よりも蒸気
圧が著しく低く、かなり低い温度において発生す
る水蒸気を吸収できる。吸収器4では蒸発器3で
蒸発した冷媒は吸収器の管束の外面に散布された
臭化リチウム水溶液(吸収液)6に吸収され、こ
の時発生する吸収熱は管内を通る冷却水13によ
り冷却される。
(C) 再生器1a,1b
吸収器4で冷媒を吸収した希溶液6bは濃度が
低下し、吸収力が弱くなる。そこで溶液循環ポン
プ8により、一部は高温再生器1aに送られ、高
温蒸気11等によつて加熱され、冷媒蒸気10が
蒸発分離し、溶液は濃縮され濃溶液6aは吸収器
4に戻る。さらに吸収器4から出た希溶液6bの
一部は溶液循環ポンプ8により低温再生器1bに
送られ、高温再生器1aで発生した冷媒蒸気10
により加熱濃縮され、濃溶液6aは吸収器4に戻
る。
(D) 凝縮器2
再生器1で分離された冷媒蒸気10は凝縮器2
で管内を流れる冷却水9によつて冷却され、凝縮
液化し、蒸発器3に戻る。
(E) 熱交換器5
吸収器4から再生器1に向かう低温の希薄溶液
6bを再生器1から吸収器4に向かう高温の濃溶
液6によつて予熱し、再生器加熱量を減少させ
る。
(F) ポンプ8
ポンプ8に濃溶液6a、希薄溶液6bおよび冷
媒7を循環させる。
吸収器4、再生器1およびポンプ8が圧縮式冷
凍機の圧縮機と同じ機能をする。吸収液6,6a
および6bは、冷凍機運転中に熱交換器5を介し
て再生器1と吸収器4の間を循環する。吸収液の
濃度が高い程、一般に冷凍効率も高まる故、吸収
液を濃縮するために、再生器1はより高温に保持
する必要がある。
一方、臭化リチウム水溶液が高温、高濃度であ
る程、その冷凍機構成材料である鋼や銅に対する
腐食性は増大する。したがつて、吸収液には腐食
防止のためのインヒビタの添加が不可欠である。
ところで、これまで実用されているインヒビタ
としてはそのほとんどがクロム酸塩であり、一部
モリブデン酸塩等の使用例もあるが、低温におけ
る溶解性が乏しいため、極く一部に限られてい
る。上記インヒビタはいずれも酸化剤であり、鉄
表面に緻密な保護膜を形成することによつて腐食
を抑制するものであつた。しかし、数種類に及ぶ
冷凍機構成材料の全てについて、完全な防食をす
ることは困難であつた。すなわち、前記のような
インヒビタは、銅系材料には防食効果を示さない
ばかりでなく、かえつて腐食を促進することさえ
あつた。さらに、その際溶出した銅イオンが鉄の
表面に析出し、両金属の電位差により鉄が腐食さ
れ易くなるという欠点もあつた。
また、銅系材料に防食効果を示す有機系インヒ
ビタは、冷凍運転中に160℃以上に達する高温に
ある再生器等において、安定性に問題を生ずるう
えに、腐食の最も激しい該再生器の鉄系材料に対
しては防食効果が乏しいという欠点があつた。
本発明の目的は臭化リチウム水溶液に対する耐
食性の優れた密閉循環型吸収式冷凍機を提供する
ことにある。
また他の目的は耐食性にすぐれ、かつ冷却効率
の高い密閉循環型吸収式冷凍機を提供することに
ある。
このような目的を達成するために、本発明は、
再生器、凝縮器、蒸発器、吸収器および熱交換器
を順次結合して構成したクローズド循環系内に封
入された臭化リチウム水溶液の凝縮、冷媒希釈お
よび熱交換の繰返しによつて寒冷を得る密閉循環
型吸収式冷凍機において、前記臭化リチウム水溶
液にインヒビタとして実質的に機能するに十分な
量の塩化ルテニウムを含むようにしたものであ
る。
本発明において、塩化ルテニウムは鉄または鉄
合金から成る部材に対し、吸収液中で加水分解
し、その加水分解生成物が皮膜を形成し、これが
腐食を抑制すると考えられる。
本発明は、一重効用密閉循環型吸収式冷凍機に
対しても有効であるが、とりわけ二重効用密閉循
環型吸収式冷凍機に有効である。これは、前記イ
ンヒビタがモリブデン酸塩インヒビタ等に比較し
溶解性に優れているため、吸収液が低温状態にな
つても析出、沈澱する心配がないためである。
本発明における塩化ルテニウムの量すなわち、
濃度は、構成材料の腐食を防止するに十分な濃度
とするが、実用的には2×10-4mol/l以上であ
れば良い。しかしながら、濃度が高くなりすぎる
と液中の沈澱物量が増加することから好ましくは
2×10-4mol/l〜5×10-2mol/lの範囲内で
ある。本発明において、吸収液にはpH調整剤と
してLiOH,NaOH,KOH等のアルカリ剤の併用
が好ましく、これによつて塩化ルテニウムの効果
をさらに顕著にする。また、吸収液には、吸収器
の熱効率を高めるために、オクチルアルコールの
ような界面活性剤を加えることができ、これによ
つて塩化ルテニウムの防食効果が何ら損われるこ
とはない。
本発明は、ガス、灯油、重油等の燃焼ガスある
いは蒸気等、その熱源の種類によつて構成材料の
種類および比率が若干異なるが、本発明はそれら
全ての機種にその効果を発揮する。しかも、本発
明の吸収液は、クロム酸塩等を用いた吸収液と比
較して、公害上の心配もない。
次に実施例を記して具体的に説明する。
〔実施例 1〕
塩化ルテニウムを所定量溶解した水溶液に臭化
リチウムを62重量%および水酸化リチウムを0.2
重量%添加して吸収液を調整した。
この吸収液を用い、炭素鋼(SS―41)につい
て、160℃、200時間腐食試験した。なお腐食試験
は吸収液を脱気後行なつた。その時の腐食量を第
2図に示す。比較例として従来用いられているク
ロム酸リチウムインヒビタを含む吸収液による試
験結果の腐食量は炭素鋼で500mg/dm2である。
従来例では、鋭く深い孔食が発生して、腐食量が
ばらつくので、試片10個の平均値を採用した。一
方、実施例では、試験片は均一な薄い黒色の皮膜
で覆われていた。
第2図から明らかなように、実施例における腐
食量は20〜30mg/dm2であり、従来例に比して大
幅に軽減されており、その効果が顕著である。
〔実施例 2〕
塩化ルテニウムを8×10-4mol/l溶解した水
溶液に臭化リチウムを62重量%および水酸化リチ
ウムを0.2重量%添加し、さらにこの水溶液にn
―オクチルアルコールを25mol/l添加して吸収
液を調整した。
この吸収液を用い、炭素鋼(SS―41)、無酸素
銅(OFCuP)、70/30キユプロニツケル(銅70
%、ニツケル30%の合金)(CNTF―3)につい
て、それぞれ160℃で0〜1000時間腐食試験をし
た。その時の腐食量を第3図に示す。この第3図
において符号14は軟鋼の腐食量、15は無酸素
銅の腐食量および16は70/30キユプロニツケル
の腐食量を示す。腐食量はいずれの材料も時間が
経つにしたがつて飽和する傾向があり、しかも、
その時間変化が極めて小さく、安定した防食効果
を示すことが明らかである。なお、試験後の軟
鋼、無酸素銅、70/30キユプロニツケルの腐食形
態は全面腐食型であり、従来インヒビタ(クロム
酸塩)等で見られる孔食等の異常腐食は全く認め
られなかつた。
以上の各実施例から明らかなように、本発明に
よれば吸収式冷凍機の構成材料を極めて効果的に
防食でき、しかも長時間安定した防食性能を維持
でき、冷却効果の向上を図れる等の優れた効果が
得られることがわかる。
The present invention relates to a closed circulation type absorption refrigerator which uses a lithium bromide aqueous solution as an absorption liquid and performs cooling by repeatedly concentrating the liquid, diluting the refrigerant, and exchanging heat. Closed circulation absorption refrigerators use water as the refrigerant and a concentrated aqueous solution of lithium bromide as the absorption liquid. As shown in the principle diagram in Fig. 1, this refrigerator has a regenerator 1, a condenser 2, an evaporator 3, an absorber 4, and circulates absorption liquid 6, 6a, 6b and refrigerant 7 between them. Pumps 8 and heat exchanger 5
Each part operates as follows. (A) Evaporator 3 Cold water 12 flows through the tubes of the evaporator tube bundle of the evaporator 3, and refrigerant 7 is spread outside the tubes, and the latent heat of evaporation removes heat from the cold water. (B) Absorber 4 Lithium bromide aqueous solution has significantly lower vapor pressure than water at the same temperature, and can absorb water vapor generated at considerably lower temperatures. In the absorber 4, the refrigerant evaporated in the evaporator 3 is absorbed by a lithium bromide aqueous solution (absorbing liquid) 6 sprinkled on the outer surface of the tube bundle of the absorber, and the absorbed heat generated at this time is cooled by cooling water 13 passing through the tubes. be done. (C) Regenerators 1a, 1b The concentration of the dilute solution 6b that has absorbed the refrigerant in the absorber 4 decreases, and its absorption capacity becomes weaker. A part of the solution is sent to the high-temperature regenerator 1a by the solution circulation pump 8, heated by high-temperature steam 11, etc., the refrigerant vapor 10 is evaporated and separated, the solution is concentrated, and the concentrated solution 6a is returned to the absorber 4. Further, a part of the dilute solution 6b discharged from the absorber 4 is sent to the low temperature regenerator 1b by the solution circulation pump 8, and the refrigerant vapor 10 generated in the high temperature regenerator 1a is
The concentrated solution 6a is concentrated by heating and returned to the absorber 4. (D) Condenser 2 The refrigerant vapor 10 separated in the regenerator 1 is transferred to the condenser 2.
It is cooled by the cooling water 9 flowing through the pipe, condenses and liquefies, and returns to the evaporator 3. (E) Heat exchanger 5 The low-temperature dilute solution 6b heading from the absorber 4 to the regenerator 1 is preheated by the high-temperature concentrated solution 6 heading from the regenerator 1 to the absorber 4, thereby reducing the regenerator heating amount. (F) Pump 8 The pump 8 circulates the concentrated solution 6a, dilute solution 6b, and refrigerant 7. The absorber 4, the regenerator 1 and the pump 8 have the same function as the compressor of a compression refrigerator. Absorption liquid 6, 6a
and 6b circulate between the regenerator 1 and the absorber 4 via the heat exchanger 5 during refrigerator operation. Generally, the higher the concentration of the absorption liquid, the higher the refrigeration efficiency, so the regenerator 1 needs to be maintained at a higher temperature in order to concentrate the absorption liquid. On the other hand, the higher the temperature and concentration of the lithium bromide aqueous solution, the more corrosive it becomes to steel and copper, which are the constituent materials of the refrigerator. Therefore, it is essential to add an inhibitor to the absorption liquid to prevent corrosion. By the way, most of the inhibitors that have been put into practical use so far have been chromate salts, and although there have been some examples of the use of molybdate salts, their use is limited to only a few due to their poor solubility at low temperatures. . All of the above inhibitors are oxidizing agents and suppress corrosion by forming a dense protective film on the iron surface. However, it has been difficult to provide complete corrosion protection for all of the several types of refrigerator constituent materials. That is, the above-mentioned inhibitors not only have no anticorrosive effect on copper-based materials, but also sometimes even promote corrosion. Another drawback was that the copper ions eluted at that time precipitated on the surface of the iron, making the iron more susceptible to corrosion due to the potential difference between the two metals. In addition, organic inhibitors that have a corrosion-preventing effect on copper-based materials not only cause stability problems in regenerators, etc., which are exposed to high temperatures of 160°C or higher during refrigeration operation, but also cause problems with the corrosion of the most severely corroded iron in the regenerator. The drawback was that it had a poor anticorrosive effect on other types of materials. An object of the present invention is to provide a closed circulation absorption refrigerator that has excellent corrosion resistance against aqueous lithium bromide solutions. Another object of the present invention is to provide a closed circulation absorption refrigerator which has excellent corrosion resistance and high cooling efficiency. In order to achieve such an objective, the present invention
Refrigeration is obtained by repeatedly condensing a lithium bromide aqueous solution, diluting the refrigerant, and exchanging heat sealed in a closed circulation system consisting of a regenerator, condenser, evaporator, absorber, and heat exchanger. In the closed circulation type absorption refrigerator, the lithium bromide aqueous solution contains a sufficient amount of ruthenium chloride to substantially function as an inhibitor. In the present invention, ruthenium chloride hydrolyzes a member made of iron or an iron alloy in an absorption liquid, and the hydrolysis product forms a film, which is thought to suppress corrosion. Although the present invention is effective for single-effect closed circulation absorption refrigerators, it is particularly effective for double-effect closed circulation absorption refrigerators. This is because the inhibitor has superior solubility compared to molybdate inhibitors and the like, so there is no fear of precipitation or precipitation even when the absorbing liquid is at a low temperature. The amount of ruthenium chloride in the present invention, namely:
The concentration should be sufficient to prevent corrosion of the constituent materials, but practically it is sufficient if it is 2×10 −4 mol/l or more. However, if the concentration becomes too high, the amount of precipitates in the liquid will increase, so it is preferably within the range of 2×10 −4 mol/l to 5×10 −2 mol/l. In the present invention, it is preferable to use an alkaline agent such as LiOH, NaOH, or KOH as a pH adjuster in the absorption liquid in combination, thereby making the effect of ruthenium chloride even more pronounced. Also, a surfactant such as octyl alcohol can be added to the absorption liquid to increase the thermal efficiency of the absorber, without any loss in the anticorrosion effect of ruthenium chloride. Although the types and proportions of the constituent materials of the present invention differ slightly depending on the type of heat source such as combustion gas or steam such as gas, kerosene, and heavy oil, the present invention exerts its effects on all such models. Furthermore, the absorbent liquid of the present invention has no pollution concerns compared to absorbent liquids using chromate or the like. Next, examples will be described in detail. [Example 1] 62% by weight of lithium bromide and 0.2% of lithium hydroxide were added to an aqueous solution in which a predetermined amount of ruthenium chloride was dissolved.
An absorption liquid was prepared by adding % by weight. Using this absorption liquid, a corrosion test was conducted on carbon steel (SS-41) at 160°C for 200 hours. The corrosion test was conducted after the absorbent was degassed. Figure 2 shows the amount of corrosion at that time. As a comparative example, the amount of corrosion in carbon steel was 500 mg/dm 2 as a result of a test using an absorbing liquid containing a lithium chromate inhibitor, which has been conventionally used.
In the conventional example, sharp and deep pitting corrosion occurs and the amount of corrosion varies, so the average value of 10 specimens was used. On the other hand, in the example, the test piece was covered with a uniform thin black film. As is clear from FIG. 2, the amount of corrosion in the example was 20 to 30 mg/dm 2 , which was significantly reduced compared to the conventional example, and the effect was remarkable. [Example 2] 62% by weight of lithium bromide and 0.2% by weight of lithium hydroxide were added to an aqueous solution in which ruthenium chloride was dissolved at 8×10 -4 mol/l, and further n
- The absorption liquid was prepared by adding 25 mol/l of octyl alcohol. Using this absorption liquid, carbon steel (SS-41), oxygen-free copper (OFCuP), 70/30 Cypronickel (copper 70
%, Nickel 30% alloy) (CNTF-3) were subjected to corrosion tests at 160°C for 0 to 1000 hours. Figure 3 shows the amount of corrosion at that time. In FIG. 3, reference numeral 14 indicates the amount of corrosion of mild steel, 15 indicates the amount of corrosion of oxygen-free copper, and 16 indicates the amount of corrosion of 70/30 Cypronickel. The amount of corrosion tends to reach saturation over time for all materials, and
It is clear that the change over time is extremely small and that it exhibits a stable anticorrosive effect. The corrosion pattern of mild steel, oxygen-free copper, and 70/30 cupronite after the test was a general corrosion type, and no abnormal corrosion such as pitting corrosion, which is seen with conventional inhibitors (chromate), was observed. As is clear from the above examples, according to the present invention, the constituent materials of an absorption chiller can be extremely effectively protected from corrosion, and moreover, stable corrosion protection performance can be maintained for a long period of time, and the cooling effect can be improved. It can be seen that excellent effects can be obtained.
第1図は本発明の一実施例に成る密閉循環型吸
収式冷凍機の原理系統図、第2図は塩化ルテニウ
ムの濃度と腐食量の関係を示すグラフ、第3図は
軟鋼、無酸素銅および70/30キユプロニツケルに
ついて時間と腐食量の関係を示すグラフである。
1a…高温再生器、1b…低温再生器、2…凝
縮器、3…蒸発器、4…吸収器、5…熱交換器。
Figure 1 is a diagram of the principle of a closed circulation absorption refrigerator according to an embodiment of the present invention, Figure 2 is a graph showing the relationship between the concentration of ruthenium chloride and the amount of corrosion, and Figure 3 is a diagram of mild steel and oxygen-free copper. It is a graph showing the relationship between time and corrosion amount for 70/30 Cypronickel. 1a...High temperature regenerator, 1b...Low temperature regenerator, 2...Condenser, 3...Evaporator, 4...Absorber, 5...Heat exchanger.
Claims (1)
換器を順次結合して構成したクローズド循環系内
に封入された臭化リチウム水溶液の凝縮、冷媒希
釈および熱交換の繰返しによつて寒冷を得る密閉
循環型吸収式冷凍機において、前記臭化リチウム
水溶液にインヒビタとして実質的に機能するに十
分な量の塩化ルテニウムを含むことを特徴とする
密閉循環型吸収式冷凍機。 2 塩化ルテニウムの濃度は1×10-4mol/l〜
5×10-2mol/lである特許請求の範囲第1項記
載の密閉循環型吸収式冷凍機。 3 臭化リチウム水溶液に塩化ルテニウム、アル
カリ金属の水酸化物およびオクチルアルコールを
含有せしめた特許請求の範囲第1項記載の密閉循
環型吸収式冷凍機。[Claims] 1. Condensation of an aqueous lithium bromide solution, refrigerant dilution, and heat exchange sealed in a closed circulation system configured by sequentially combining a regenerator, a condenser, an evaporator, an absorber, and a heat exchanger. A closed circulation type absorption refrigerating machine that repeatedly obtains cold air, wherein the lithium bromide aqueous solution contains a sufficient amount of ruthenium chloride to substantially function as an inhibitor. . 2 The concentration of ruthenium chloride is 1×10 -4 mol/l ~
5×10 -2 mol/l. The closed circulation absorption refrigerator according to claim 1. 3. The closed circulation absorption refrigerator according to claim 1, wherein the lithium bromide aqueous solution contains ruthenium chloride, an alkali metal hydroxide, and octyl alcohol.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56028493A JPS57144858A (en) | 1981-03-02 | 1981-03-02 | Closed circulation type absorption refrigerating machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56028493A JPS57144858A (en) | 1981-03-02 | 1981-03-02 | Closed circulation type absorption refrigerating machine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57144858A JPS57144858A (en) | 1982-09-07 |
| JPS6249544B2 true JPS6249544B2 (en) | 1987-10-20 |
Family
ID=12250190
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56028493A Granted JPS57144858A (en) | 1981-03-02 | 1981-03-02 | Closed circulation type absorption refrigerating machine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57144858A (en) |
-
1981
- 1981-03-02 JP JP56028493A patent/JPS57144858A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57144858A (en) | 1982-09-07 |
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