JPH02192548A - Absorptive type freezer - Google Patents
Absorptive type freezerInfo
- Publication number
- JPH02192548A JPH02192548A JP974689A JP974689A JPH02192548A JP H02192548 A JPH02192548 A JP H02192548A JP 974689 A JP974689 A JP 974689A JP 974689 A JP974689 A JP 974689A JP H02192548 A JPH02192548 A JP H02192548A
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- liquid
- absorptive
- valve
- purifier
- 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
Links
- 239000007788 liquid Substances 0.000 claims abstract description 31
- 239000003507 refrigerant Substances 0.000 claims abstract description 4
- 239000007864 aqueous solution Substances 0.000 claims abstract description 3
- 238000010521 absorption reaction Methods 0.000 claims description 24
- 238000000746 purification Methods 0.000 claims description 5
- 229910001508 alkali metal halide Inorganic materials 0.000 claims description 2
- 150000008045 alkali metal halides Chemical class 0.000 claims description 2
- 150000002500 ions Chemical class 0.000 abstract description 12
- 239000000243 solution Substances 0.000 abstract description 9
- 229910021536 Zeolite Inorganic materials 0.000 abstract description 4
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 abstract description 4
- 239000010457 zeolite Substances 0.000 abstract description 4
- 239000000654 additive Substances 0.000 abstract description 3
- 229910052751 metal Inorganic materials 0.000 abstract description 3
- 239000002184 metal Substances 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 239000003795 chemical substances by application Substances 0.000 abstract 2
- 230000000996 additive effect Effects 0.000 abstract 1
- 239000010959 steel Substances 0.000 description 13
- 229910000831 Steel Inorganic materials 0.000 description 12
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 11
- 229910001431 copper ion Inorganic materials 0.000 description 11
- 239000000463 material Substances 0.000 description 10
- 230000007797 corrosion Effects 0.000 description 8
- 238000005260 corrosion Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- 238000011010 flushing procedure Methods 0.000 description 6
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 6
- 238000001816 cooling Methods 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 239000003463 adsorbent Substances 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 238000010828 elution Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 2
- 239000010962 carbon steel Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000001050 lubricating effect Effects 0.000 description 2
- 238000005461 lubrication Methods 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229910000851 Alloy steel Inorganic materials 0.000 description 1
- 229910000881 Cu alloy Inorganic materials 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 229940023913 cation exchange resins Drugs 0.000 description 1
- 239000011538 cleaning material Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- -1 zeolite Chemical compound 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は吸収式冷凍機における吸収液及び冷媒の浄化に
係り、特に溶存する有害イオンの除去に好適な吸収式冷
凍機に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to the purification of absorption liquid and refrigerant in an absorption refrigerator, and particularly relates to an absorption refrigerator suitable for removing dissolved harmful ions.
ハロゲン化アルカリ金属の水溶液は腐食性が強くこれを
吸収液とする吸収式冷凍機では鋼あるいは銅合金層の熱
交換器チューブが腐食し銅イオンを溶出させる。従来、
ポンプの軸受など摺動部品の冷却及び潤滑にポンプ移送
液体をフラッシング液として利用する実開昭61−15
1085号公報、実開昭62−176497号公報があ
る。これらはボンピングリングの回転、吐出圧と吸入圧
の差圧などによってフラッシング液を導入しており、ス
トレーナによって固形物の除去程度の処理を行なってい
る。Aqueous solutions of alkali metal halides are highly corrosive, and in absorption refrigerators that use them as absorption liquids, the heat exchanger tubes made of steel or copper alloy layers corrode and elute copper ions. Conventionally,
Utility Model No. 61-15 Utilizing the pump transfer liquid as a flushing liquid for cooling and lubricating sliding parts such as pump bearings
There are Japanese Utility Model Application No. 1085 and Japanese Utility Model Application No. 176497/1985. In these systems, flushing liquid is introduced by the rotation of a pumping ring, the differential pressure between discharge pressure and suction pressure, etc., and a strainer is used to remove solids.
上記従来技術はポンプの冷却及び潤滑においてフィルタ
ーによる固形物の除去装置を設けたものはあるが、溶存
イオンに対し考慮されておらず銅イオンなどの溶存イオ
ンは有害成分として金属部品の腐食あるいはそれにとも
なう金属鋼の摺動部への析出によるロック事故などの問
題があった。Although some of the above conventional technologies are equipped with filters to remove solids during pump cooling and lubrication, they do not take dissolved ions into consideration, and dissolved ions such as copper ions are harmful components that can corrode metal parts or cause damage. There were problems such as locking accidents due to precipitation of metal steel on sliding parts.
本発明の目的はポンプの冷却及び潤滑に使用されるフラ
ッシング液としての吸収液中に存在する有害イオンを除
去あるいは低減した吸収式冷凍機を提供することにある
。An object of the present invention is to provide an absorption refrigerator in which harmful ions present in an absorption liquid used as a flushing liquid used for pump cooling and lubrication are removed or reduced.
上記目的はポンプの冷却及び潤滑に使用するフラッシン
グ液である吸収液中に溶存する有害イオンを吸着材ある
いはイオン交換物質により捕捉し吸収液中より除去ある
いは低減させることによつて達成される。The above object is achieved by trapping harmful ions dissolved in the absorbing liquid, which is a flushing liquid used for cooling and lubricating the pump, with an adsorbent or ion exchange material, and removing or reducing them from the absorbing liquid.
機器構成材料の腐食によって吸収液あるいは冷媒中に溶
は込んだ銅イオンなどの有害イオンはその溶液を浄化材
として吸着材及び/あるいは陽イオン交換物質を充填し
たカートリッジ式浄化器を通すことによって除去あるい
は濃度が低減され腐食事故あるいは銅の析出によるポン
プのロック事故は防止できる。Toxic ions such as copper ions dissolved into the absorption liquid or refrigerant due to corrosion of equipment component materials are removed by passing the solution through a cartridge-type purifier filled with adsorbent and/or cation exchange material as a purifying material. Alternatively, the concentration can be reduced and corrosion accidents or pump lock accidents due to copper deposition can be prevented.
充填する浄化材としては活性炭、ゼオライトなどの吸着
材及び陽イオン交換樹脂があげられる。Examples of the purifying material to be filled include activated carbon, adsorbents such as zeolite, and cation exchange resins.
そしてこれらの浄化材は粒状のものが望ましい。These purifying materials are preferably in the form of granules.
次に浄化器の設置方法としては冷凍機の場合は配管系に
バイパス配管を設けこのバイパス配管に設置される。こ
れによって本機を停止することなく浄化器の交換作業も
容易となる。またポンプ移送液をフラッシング液とする
ポンプの場合にはポンプの吐出側からフラッシング液を
導入する配管に設置される。浄化材の粒径は浄化効率と
流れ抵抗(頭損)を考慮し4〜12程度とした。Next, as for how to install a purifier, in the case of a refrigerator, a bypass pipe is provided in the piping system and the purifier is installed in this bypass pipe. This makes it easy to replace the purifier without stopping the machine. Further, in the case of a pump that uses the pumping liquid as flushing liquid, the pump is installed in a pipe that introduces the flushing liquid from the discharge side of the pump. The particle size of the purification material was set to about 4 to 12 in consideration of purification efficiency and flow resistance (head loss).
次に吸収式冷凍機において使用される添加剤を加えた吸
収液である65%臭化リチウム溶液中での鉄鋼材料とし
ての5S41材の腐食量に及ぼす吸収液中の銅イオン濃
度の影響をみると第1図に示すように160℃、200
時間の試験結果より銅イオン濃度の増大は腐食量を増加
させるが、銅イオン濃度を110PP以下とすれば実用
上殆んど腐食量に影響をしないことは明らかである。ま
た金属鋼の析出も鉄鋼の腐食量に相当した析出量となる
ことから金属鋼の析出によるポンプのロック事故も鋼イ
オン濃度を110PP以下に抑制すれば防止あるいは長
時間運転できる。Next, we will examine the effect of the copper ion concentration in the absorption liquid on the amount of corrosion of 5S41 steel material in a 65% lithium bromide solution, which is an absorption liquid containing additives used in absorption refrigerators. and 160℃, 200℃ as shown in Figure 1.
From the time test results, it is clear that an increase in the copper ion concentration increases the amount of corrosion, but if the copper ion concentration is set to 110 PP or less, it has practically no effect on the amount of corrosion. Further, since the amount of precipitation of metallic steel corresponds to the amount of corrosion of steel, locking accidents of the pump due to precipitation of metallic steel can be prevented or operated for a long time by suppressing the steel ion concentration to 110 PP or less.
次に300RT吸収式冷凍機の吸収液中に溶存する鋼イ
オン濃度の分析結果の1例をみると2ケ月間(10時間
/日運転として500時間)で約1000pp+aの溶
出量があり20PP!+/日の平均溶出量となっている
。たとえば見掛比重0.5゜200mu量のゼオライト
の浄化効率をみると52pP璽の含銅イオン吸収液1回
通過により吸収液中に溶存する銅イオンの約50%が除
去される第2図に示す実験結果から、鋼イオン溶出濃度
を50ppm/日としてみてもIQppm以下に抑制す
ることが可能である。Next, looking at an example of the analysis results of the concentration of steel ions dissolved in the absorption liquid of a 300RT absorption chiller, the elution amount is approximately 1000pp+a over 2 months (500 hours of 10 hours/day operation), which is 20PP! The average elution amount is +/day. For example, looking at the purification efficiency of zeolite with an apparent specific gravity of 0.5° and an amount of 200 mu, Figure 2 shows that approximately 50% of the copper ions dissolved in the absorption liquid are removed by passing a 52pP cup of copper-containing ion absorption liquid once. From the experimental results shown, even if the steel ion elution concentration is assumed to be 50 ppm/day, it is possible to suppress it to IQppm or less.
以下、本発明の実施例を図により説明する。 Embodiments of the present invention will be described below with reference to the drawings.
第3図は蒸気発生器モデルである。下部の蒸発器1を上
部の凝縮器2で構成され蒸発器1の下方から配管3及び
ポンプ4で蒸発器1内の溶液5は循環撹拌されている。Figure 3 is a steam generator model. It consists of a lower evaporator 1 and an upper condenser 2, and a solution 5 in the evaporator 1 is circulated and stirred from below the evaporator 1 by piping 3 and a pump 4.
凝縮器2で水冷され凝縮した凝縮水6は配管7に導入さ
れ、配管3内に吸入される。溶液5は60%臭化リチす
吸収液で酸化鋼を1.0%wt添加し他に若干の添加剤
を含む。Condensed water 6 that has been water-cooled and condensed in the condenser 2 is introduced into a pipe 7 and sucked into the pipe 3. Solution 5 is a 60% lithium bromide absorption liquid containing 1.0% wt of oxidized steel and some other additives.
なお缶内は当初I X 10−”ma+Hgの減圧状態
として蒸発器1内に溶液5を封入したもので缶体は気密
容器となっている。カートリッジ式浄化器8は浄化材9
としてゼオライトを充填してあり配管3に設けたバイパ
ス配管10に設置してあり、流量は配管3に設けたバル
ブ9とバイパス管10の浄化器8の前後に設けたバルブ
11及びバルブllaによって1m/sに調節される。The inside of the can is initially in a reduced pressure state of I x 10-"ma + Hg, and the solution 5 is sealed in the evaporator 1, and the can body is an airtight container. The cartridge type purifier 8 is equipped with a purifying material 9.
It is filled with zeolite and installed in the bypass pipe 10 provided in the pipe 3, and the flow rate is 1 m by the valve 9 provided in the pipe 3, the valve 11 provided before and after the purifier 8 of the bypass pipe 10, and the valve lla. /s.
構成材料は缶体は炭素鋼材、凝縮器2の熱交換チューブ
12は純銅チューブであり、蒸発器1の熱交換チューブ
13はボイラー用鋼管である。その他の配管3.7及び
10はいずれも配管用鋼管を使用した。試験では溶液温
度を100℃に加圧蒸気で加熱し配管3の凝縮水6の吸
入される直前での吸収液をバルブ14の部分から採取し
、銅イオン濃度の経時変化を調べた。その結果を第4図
に示す。当初鋼イオン濃度は時間の経過とともに増大す
るが浄化器を通しはじめた2時間以後は銅イオン濃度の
急速に低下し約30分でl0Pp11以下に減少し、そ
の後はloppm以下に保たれている。As for the constituent materials, the can body is made of carbon steel, the heat exchange tube 12 of the condenser 2 is a pure copper tube, and the heat exchange tube 13 of the evaporator 1 is a boiler steel tube. The other pipes 3, 7 and 10 were all made of steel pipes. In the test, the solution temperature was heated to 100° C. with pressurized steam, and the absorbed liquid was collected from the valve 14 immediately before the condensed water 6 was sucked into the pipe 3, and the change in copper ion concentration over time was investigated. The results are shown in FIG. Initially, the steel ion concentration increases with the passage of time, but after 2 hours after passing through the purifier, the copper ion concentration rapidly decreases to less than 10Pp11 in about 30 minutes, and thereafter remains below loppm.
なお前記カートリッジ浄化器8は処理量によってその大
きさは変るが、形状は第5図に示すような円筒形筒15
の中に浄化材9が充填され、両端に同形の綱17及び1
7a付M16及び16aがありバイパス配管10にユニ
オン部18及び18aで連結される。The size of the cartridge purifier 8 varies depending on the throughput, but the shape is a cylindrical tube 15 as shown in FIG.
A cleaning material 9 is filled in the inside, and ropes 17 and 1 of the same shape are attached to both ends.
M16 and 16a with 7a are connected to the bypass pipe 10 by union parts 18 and 18a.
本発明によれば吸収式冷凍機のポンプのロック事故、そ
の他機器の腐食による外気の漏洩事故等が防止され吸収
式冷凍機の信頼性の向上効果が大きい。According to the present invention, accidents such as locking of the pump of an absorption refrigerating machine and leakage of outside air due to corrosion of other equipment are prevented, and the reliability of the absorption refrigerating machine is greatly improved.
第1図は臭化リチウム溶液中での炭素鋼の腐食量と溶存
銅イオン濃度との関係を示す図、第2図は吸収液中に溶
存する銅イオンの本発明の浄化器による除去効果を示す
図、93図は蒸発器モデルによる吸収液の浄化例の系統
図、第4図は蒸発器モデルによる吸収液の浄化効果を示
す回、第5図はカートリッジ式浄化器の断面図である。Figure 1 shows the relationship between the amount of corrosion of carbon steel in a lithium bromide solution and the dissolved copper ion concentration, and Figure 2 shows the removal effect of the purifier of the present invention on copper ions dissolved in the absorption liquid. Figure 93 is a system diagram of an example of purifying an absorption liquid using an evaporator model, Figure 4 is a diagram showing the effect of purifying an absorption liquid using an evaporator model, and Figure 5 is a sectional view of a cartridge type purifier.
Claims (1)
収式冷凍機において、吸収液及び冷媒系配管に浄化機構
を設置することを特徴とする吸収式冷凍機。1. An absorption refrigerator that uses an aqueous solution of an alkali metal halide as an absorption liquid, and is characterized in that a purification mechanism is installed in the absorption liquid and refrigerant system piping.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP974689A JPH02192548A (en) | 1989-01-20 | 1989-01-20 | Absorptive type freezer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP974689A JPH02192548A (en) | 1989-01-20 | 1989-01-20 | Absorptive type freezer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02192548A true JPH02192548A (en) | 1990-07-30 |
Family
ID=11728872
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP974689A Pending JPH02192548A (en) | 1989-01-20 | 1989-01-20 | Absorptive type freezer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02192548A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007303689A (en) * | 2006-05-08 | 2007-11-22 | Hitachi Kyowa Engineering Co Ltd | Refrigerant purifying device and absorption type cooling and heating machine comprising the same |
KR100841655B1 (en) * | 2007-09-18 | 2008-06-26 | 주식회사신우이엔지 | Chiller heater with refining apparatus of absorption liquids |
-
1989
- 1989-01-20 JP JP974689A patent/JPH02192548A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007303689A (en) * | 2006-05-08 | 2007-11-22 | Hitachi Kyowa Engineering Co Ltd | Refrigerant purifying device and absorption type cooling and heating machine comprising the same |
KR100841655B1 (en) * | 2007-09-18 | 2008-06-26 | 주식회사신우이엔지 | Chiller heater with refining apparatus of absorption liquids |
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