JPH0523501A - Solution concentrator - Google Patents

Solution concentrator

Info

Publication number
JPH0523501A
JPH0523501A JP3204962A JP20496291A JPH0523501A JP H0523501 A JPH0523501 A JP H0523501A JP 3204962 A JP3204962 A JP 3204962A JP 20496291 A JP20496291 A JP 20496291A JP H0523501 A JPH0523501 A JP H0523501A
Authority
JP
Japan
Prior art keywords
solution
absorbing
concentrating
concentrated
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.)
Pending
Application number
JP3204962A
Other languages
Japanese (ja)
Inventor
Katsutoshi Shimoyama
勝利 下山
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 Electric Co Ltd
Original Assignee
Nissin Electric 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 Electric Co Ltd filed Critical Nissin Electric Co Ltd
Priority to JP3204962A priority Critical patent/JPH0523501A/en
Publication of JPH0523501A publication Critical patent/JPH0523501A/en
Pending legal-status Critical Current

Links

Landscapes

  • Gas Separation By Absorption (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE:To concentrate a solution to be concentrated without heating the solution and damaging the same by heat. CONSTITUTION:A solution concentrator is equipped with a concn. means 10 evaporating a solution 14 to be concentrated under vacuum to concentrate the same, an absorbing means 11 letting an absorbing solution 25 absorb the steam generated by the concn. means and a regenerating means 12 concentrating the diluted absorbing solution 31 of the absorbing means 11 to supply the conc. absorbing solution to the absorbing means 11.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、濃縮すべき溶液を加熱
せず、真空中で濃縮するようにした溶液濃縮装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solution concentrating device for concentrating a solution to be concentrated in a vacuum without heating it.

【0002】[0002]

【従来の技術】従来の溶液濃縮装置は、図3に示すよう
に、第1容器1内の水2をボイラなどの熱源で加熱し、
その水蒸気3をパイプ4により第2容器5に導入する。
一方、濃縮すべき溶液6は、第3容器7を介して第2容
器5に導入し、第2容器5において、パイプ4の水蒸気
3の潜熱により加熱され、溶液6の水蒸気8がパイプ9
により第3容器7に導入され、当初の溶液6を加熱す
る。即ち、溶液6は第3容器7でまず加熱され、第2容
器5で濃縮される。
2. Description of the Related Art A conventional solution concentrator, as shown in FIG. 3, heats water 2 in a first container 1 with a heat source such as a boiler,
The steam 3 is introduced into the second container 5 through the pipe 4.
On the other hand, the solution 6 to be concentrated is introduced into the second container 5 via the third container 7, and is heated by the latent heat of the steam 3 in the pipe 4 in the second container 5, so that the steam 8 in the solution 6 is converted into the pipe 9.
Is introduced into the third container 7 and the original solution 6 is heated. That is, the solution 6 is first heated in the third container 7 and then concentrated in the second container 5.

【0003】[0003]

【発明が解決しようとする課題】従来の前記装置の場
合、濃縮すべき溶液6が加熱されるため、熱に弱い溶
液、例えばある種の抗生物質,ある種のビタミン,高タ
ンパク液,バクテリヤ及び酵母などの微生物液,各種果
汁類,血液製剤等の薬品類,食品類などには適用し難い
という問題点がある。さらに、低温加熱で濃縮する場合
は、濃縮,即ち蒸発効率が極めて悪いという問題点があ
る。
In the case of the above-mentioned conventional apparatus, since the solution 6 to be concentrated is heated, a heat-sensitive solution such as certain antibiotics, certain vitamins, high protein solutions, bacteria and There is a problem that it is difficult to apply to microbial liquids such as yeast, various fruit juices, chemicals such as blood products, and foods. Further, in the case of concentrating by low temperature heating, there is a problem that concentration, that is, evaporation efficiency is extremely poor.

【0004】本発明は、前記の点に留意し、濃縮すべき
溶液を加熱することなく濃縮する溶液濃縮装置を提供す
ることを目的とする。
In view of the above points, the present invention has an object to provide a solution concentrating device for concentrating a solution to be concentrated without heating.

【0005】[0005]

【課題を解決するための手段】前記課題を解決するため
に、本発明の溶液濃縮装置は、濃縮すべき溶液を真空中
で蒸発して濃縮する濃縮手段と、この濃縮手段により発
生する水蒸気を吸収液に吸収する吸収手段と、この吸収
手段の希釈吸収液を濃縮し,吸収手段に供給する再生手
段とを備えたものである。
In order to solve the above-mentioned problems, the solution concentrating device of the present invention comprises a concentrating means for evaporating and concentrating a solution to be concentrated in a vacuum, and steam generated by the concentrating means. The absorption means for absorbing the absorption liquid and the regeneration means for concentrating the diluted absorption liquid of the absorption means and supplying it to the absorption means are provided.

【0006】また、再生手段により発生する水蒸気を圧
縮して高温の水蒸気を形成する圧縮手段と、この圧縮手
段による高温の水蒸気の潜熱を再生手段の吸収液に給熱
する再生熱交換器を備えたものである。
Further, there are provided compression means for compressing the steam generated by the regeneration means to form high temperature steam, and a regeneration heat exchanger for supplying latent heat of the high temperature steam by the compression means to the absorption liquid of the regeneration means. It is a thing.

【0007】[0007]

【作用】前記のように構成された本発明の溶液濃縮装置
は、濃縮手段により濃縮すべき溶液を真空中で蒸発させ
て濃縮するため、溶液が加熱されず、溶液を熱で損なう
ことがなく、かつ、溶液が酸化変質する恐れもない。そ
の上、溶液からの水蒸気を吸収手段の吸収液に吸収し、
その希釈吸収液が再生手段により濃縮されて再び吸収手
段に供給されるため、吸収液の補充を必要としない。
In the solution concentrating apparatus of the present invention configured as described above, the solution to be concentrated is evaporated and concentrated in a vacuum by the concentrating means, so that the solution is not heated and the solution is not damaged by heat. Moreover, there is no fear that the solution will be oxidatively deteriorated. Furthermore, the water vapor from the solution is absorbed by the absorbing liquid of the absorbing means,
Since the diluted absorbing solution is concentrated by the regenerating means and supplied again to the absorbing means, it is not necessary to replenish the absorbing solution.

【0008】また、圧縮手段により、再生手段の水蒸気
が圧縮されて高温の水蒸気となり、その高温の水蒸気の
潜熱が再生熱交換器により再生手段の吸収液に給熱され
るため、再生手段における熱エネルギが節減され、運転
効率が向上する。
Further, the compression means compresses the steam of the regenerating means into high temperature steam, and the latent heat of the high temperature steam is supplied to the absorbing liquid of the regenerating means by the regenerating heat exchanger, so that the thermal energy in the regenerating means is increased. Is saved and operating efficiency is improved.

【0009】[0009]

【実施例】実施例について図1及び図2を参照して説明
する。 (実施例1)まず、実施例1を示した図1において、濃
縮手段10,吸収手段11,再生手段12及び凝縮手段
13の系全体は真空状態であり、濃縮すべき溶液14が
ポンプ15,パイプ16,流量調整弁17を経て濃縮手
段10の散水器18から濃縮手段10内に散水される。
このとき、濃縮手段10内が真空状態のため、水滴は6
℃以上の温度があれば沸騰して蒸発し、溶液14が濃縮
され、ポンプ19,流量調整弁20,パイプ21を経て
濃縮された溶液22となる。
EXAMPLES Examples will be described with reference to FIGS. 1 and 2. (Embodiment 1) First, in FIG. 1 showing Embodiment 1, the entire system of the concentrating means 10, the absorbing means 11, the regenerating means 12 and the condensing means 13 is in a vacuum state, and the solution 14 to be concentrated is pumped by a pump 15, Water is sprayed into the concentrating means 10 from the water sprinkler 18 of the concentrating means 10 through the pipe 16 and the flow rate adjusting valve 17.
At this time, since the inside of the concentrating means 10 is in a vacuum state, 6
If there is a temperature of ℃ or more, it will boil and evaporate, and the solution 14 will be concentrated and become a concentrated solution 22 via the pump 19, the flow rate adjusting valve 20, and the pipe 21.

【0010】一方、濃縮すべき溶液14は、濃縮手段1
0における沸騰蒸発により気化熱をうばわれ温度が低下
するので、給熱管23により給熱し、常温から数十℃の
範囲に維持し、運転効率をより高めることが望ましい。
On the other hand, the solution 14 to be concentrated is the concentration means 1
Since the heat of vaporization is dissipated by the boiling evaporation at 0, and the temperature is lowered, it is desirable to supply heat by the heat supply pipe 23 and maintain it in the range from room temperature to several tens of degrees Celsius to further improve the operation efficiency.

【0011】また、濃縮手段10で発生した水蒸気をそ
のまま放置すると、蒸気圧が高くなり、蒸発効率が低下
する。そこで、水蒸気を通路24を通って吸収手段11
に導入し、吸収手段11において、高濃度のLiBr溶
液などの吸収液25を、ポンプ26,パイプ27,流量
調整弁28を経て散水器29から散水し、水蒸気を吸収
液25に吸収させ、常に低圧状態を維持し、濃縮手段1
0における濃縮すべき溶液14の蒸発及び吸収手段11
における水蒸気の吸収を継続する。
If the water vapor generated in the concentrating means 10 is left as it is, the vapor pressure increases and the evaporation efficiency decreases. Then, the water vapor passes through the passage 24 and the absorbing means 11
In the absorbing means 11, the absorbing solution 25 such as a high-concentration LiBr solution is sprinkled from the sprinkler 29 through the pump 26, the pipe 27, and the flow rate adjusting valve 28 so that the absorbing solution 25 absorbs water vapor, Maintaining a low pressure state, concentrating means 1
Means for evaporating and absorbing solution 14 to be concentrated at 0
To continue to absorb water vapor.

【0012】このとき吸収液25は、通常水分の吸収に
より吸収発熱が生じるため、吸収液自体の温度が上昇
し、吸収効率が低下する。そこで、冷却水が流通する吸
熱パイプ30により吸熱し、吸収手段11における温度
の上昇を防止する。
At this time, since the absorbing liquid 25 normally generates absorption heat by absorbing water, the temperature of the absorbing liquid itself rises and the absorption efficiency decreases. Therefore, heat is absorbed by the heat absorbing pipe 30 through which the cooling water flows, and the temperature rise in the absorbing means 11 is prevented.

【0013】つぎに、水蒸気を吸収し濃度の低下した希
釈吸収液31は、ポンプ32,パイプ33,流量調整弁
34及び熱交換器35を経て再生手段12に流入し、加
熱用バーナ36により加熱され、吸収した水蒸気を放出
し、濃縮された吸収液25となり、熱交換器35,パイ
プ27,流量調整弁28を経て散水器29から濃縮吸収
液25が散水される。なお、再生手段12における加熱
手段はバーナ36に限定されるものではない。
Next, the diluted absorbing solution 31 which has absorbed water vapor and has a reduced concentration flows into the regenerating means 12 through the pump 32, the pipe 33, the flow rate adjusting valve 34 and the heat exchanger 35, and is heated by the heating burner 36. Then, the absorbed water vapor is released to become the concentrated absorbing liquid 25, and the concentrated absorbing liquid 25 is sprayed from the water sprinkler 29 through the heat exchanger 35, the pipe 27, and the flow rate adjusting valve 28. The heating means in the regeneration means 12 is not limited to the burner 36.

【0014】そして、再生手段12において放出された
水蒸気は、通路37を通って凝縮手段13に流入する。
一方、吸収手段11の吸熱パイプ30はパイプ38を介
して凝縮手段13内の伝熱管39に接続されており、伝
熱管39内の冷却水により水蒸気が冷却されて冷却液と
なる。
Then, the water vapor released in the regenerating means 12 flows into the condensing means 13 through the passage 37.
On the other hand, the heat absorbing pipe 30 of the absorbing means 11 is connected to the heat transfer pipe 39 in the condensing means 13 via the pipe 38, and the cooling water in the heat transfer pipe 39 cools the steam to become a cooling liquid.

【0015】(実施例2)実施例2を図2について説明
する。この実施例が実施例1と異なる点はつぎのとおり
である。再生手段12で発生した水蒸気の通路37に、
水蒸気を断熱圧縮して高温の水蒸気を形成する圧縮手段
40を設けるとともに、圧縮手段40により形成された
高温の水蒸気の潜熱を、再生手段12の吸収液25に給
熱する再生熱交換器41を設けた点である。この場合、
再生熱交換器41で高温の水蒸気を凝縮させることによ
り、再生手段12で発生した水蒸気よりも高い温度で潜
熱を回収することができる。
(Second Embodiment) A second embodiment will be described with reference to FIG. The difference between this embodiment and the first embodiment is as follows. In the passage 37 for water vapor generated in the regenerating means 12,
A regenerating heat exchanger 41 is provided which is provided with a compressing means 40 for adiabatically compressing the steam to form high-temperature steam, and which supplies the latent heat of the high-temperature steam formed by the compressing means 40 to the absorbing liquid 25 of the regenerating means 12. That is the point. in this case,
By condensing the high temperature steam in the regenerative heat exchanger 41, the latent heat can be recovered at a temperature higher than that of the steam generated in the regenerating means 12.

【0016】例えば、再生手段12において100℃=
1Kg/cm2 で蒸発した水蒸気を圧縮手段40により30
%圧縮し、1.3Kg/cm2 に昇圧することにより約12
5℃の水蒸気を得ることができ、再生手段12の100
℃の吸収液25に対して充分給熱することができる。な
お、圧縮手段40による昇圧圧力,即ち昇温温度は、必
要に応じて任意に設定する。
For example, in the reproducing means 12, 100 ° C. =
Water vapor evaporated at 1 kg / cm 2 is compressed by the compression means 40 to 30
About 12 by compressing and compressing to 1.3Kg / cm 2.
Water vapor of 5 ° C. can be obtained and 100 of the regeneration means 12 can be obtained.
Sufficient heat can be supplied to the absorbing liquid 25 at 0 ° C. The pressure boosted by the compression means 40, that is, the temperature rise is arbitrarily set as needed.

【0017】[0017]

【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載する効果を奏する。濃縮手段1
0により濃縮すべき溶液14を真空中で蒸発させて濃縮
するため、溶液14が加熱されず、溶液14を熱で損な
う心配がなく、かつ、溶液14の酸化変質を防止するこ
とができる。その上、溶液14からの水蒸気を吸収手段
11の吸収液25に吸収し、その希釈吸収液31が再生
手段12により濃縮されて再び吸収手段11に供給され
るため、吸収液25の補充を必要としない。
Since the present invention is configured as described above, it has the following effects. Concentration means 1
Since the solution 14 to be concentrated by 0 is evaporated and concentrated in a vacuum, the solution 14 is not heated, there is no concern that the solution 14 is damaged by heat, and the oxidative deterioration of the solution 14 can be prevented. In addition, since the water vapor from the solution 14 is absorbed by the absorbing liquid 25 of the absorbing means 11, and the diluted absorbing liquid 31 is concentrated by the regenerating means 12 and supplied to the absorbing means 11 again, it is necessary to replenish the absorbing liquid 25. Not.

【0018】また、圧縮手段40により、再生手段12
の水蒸気が圧縮されて高温の水蒸気となり、その高温の
水蒸気の潜熱が再生熱交換器41により再生手段12の
吸収液25に給熱されるため、再生手段12における加
熱用バーナなどの熱エネルギを節減することができ、運
転効率を向上することができる。
Further, the reproducing means 12 is constituted by the compression means 40.
Of the steam is compressed into high-temperature steam, and the latent heat of the high-temperature steam is supplied to the absorbing liquid 25 of the regenerating means 12 by the regenerative heat exchanger 41, so that the heat energy of the heating burner in the regenerating means 12 is saved. The operation efficiency can be improved.

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

【図1】本発明の実施例1の系統図である。FIG. 1 is a system diagram of a first embodiment of the present invention.

【図2】本発明の実施例2の系統図である。FIG. 2 is a system diagram of a second embodiment of the present invention.

【図3】従来例の系統図である。FIG. 3 is a system diagram of a conventional example.

【符号の説明】[Explanation of symbols]

10 濃縮手段 11 吸収手段 12 再生手段 14 濃縮すべき溶液 25 吸収液 31 希釈吸収液 40 圧縮手段 41 再生熱交換器 10 Concentration means 11 Absorption means 12 Playback means 14 Solution to be concentrated 25 absorption liquid 31 diluted absorbent 40 compression means 41 Regenerative heat exchanger

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 濃縮すべき溶液を真空中で蒸発して濃縮
する濃縮手段と、該濃縮手段により発生する水蒸気を吸
収液に吸収する吸収手段と、該吸収手段の希釈吸収液を
濃縮し,前記吸収手段に供給する再生手段とを備えた溶
液濃縮装置。
1. A concentrating means for evaporating and concentrating a solution to be concentrated in a vacuum, an absorbing means for absorbing water vapor generated by the concentrating means into an absorbing solution, and a concentrated absorbing solution for the absorbing means, A solution concentrating apparatus comprising: a regenerating unit that supplies the absorbing unit.
【請求項2】 再生手段により発生する水蒸気を圧縮し
て高温の水蒸気を形成する圧縮手段と、該圧縮手段によ
る高温の水蒸気の潜熱を前記再生手段の吸収液に給熱す
る再生熱交換器を備えた請求項1記載の溶液濃縮装置。
2. A compression means for compressing the steam generated by the regeneration means to form high temperature steam, and a regeneration heat exchanger for supplying the latent heat of the high temperature steam by the compression means to the absorption liquid of the regeneration means. The solution concentrating device according to claim 1, which is provided.
JP3204962A 1991-07-19 1991-07-19 Solution concentrator Pending JPH0523501A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3204962A JPH0523501A (en) 1991-07-19 1991-07-19 Solution concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3204962A JPH0523501A (en) 1991-07-19 1991-07-19 Solution concentrator

Publications (1)

Publication Number Publication Date
JPH0523501A true JPH0523501A (en) 1993-02-02

Family

ID=16499189

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3204962A Pending JPH0523501A (en) 1991-07-19 1991-07-19 Solution concentrator

Country Status (1)

Country Link
JP (1) JPH0523501A (en)

Similar Documents

Publication Publication Date Title
JP2004257705A (en) Concentration device using absorption heat pump
CA2225335A1 (en) Compression absorption heat pump
EP0354749A3 (en) Air-cooled absorption air-conditioner
JP2003056937A (en) Heat pump system
JP2858908B2 (en) Absorption air conditioner
JP3138094B2 (en) High-pressure absorption refrigerator
KR0137580Y1 (en) Liquid refrigerant chiller of absorption chiller, heater
JP2750783B2 (en) Exhaust heat recovery method in cogeneration system
JPS637081B2 (en)
KR970009811B1 (en) Absorption type water cooling/heating machine by ejector circulating type
JP3219529B2 (en) Absorption refrigerator
JPS61287402A (en) High vacuum evaporator
JPS58219371A (en) Double effect absorption type heat pump
JPS6145520B2 (en)
JPH05263610A (en) Power generation equipment
JPH0583831B2 (en)
JPS60235969A (en) Absorption heat pump
JPS6024903B2 (en) Multiple effect absorption refrigerator
JP2647487B2 (en) Solution heat exchange mechanism in absorption cycle
JP2639991B2 (en) Absorption refrigerator
JP2892519B2 (en) Absorption heat pump equipment
JPH0820141B2 (en) Absorption refrigerator
JPS59176550A (en) Single and double effect combination abroption type refrigerator
JPH0694972B2 (en) Absorption heat pump device
JPH0357385B2 (en)