JPH04203769A - Absorption type cold water of hot water device - Google Patents
Absorption type cold water of hot water deviceInfo
- Publication number
- JPH04203769A JPH04203769A JP32926790A JP32926790A JPH04203769A JP H04203769 A JPH04203769 A JP H04203769A JP 32926790 A JP32926790 A JP 32926790A JP 32926790 A JP32926790 A JP 32926790A JP H04203769 A JPH04203769 A JP H04203769A
- Authority
- JP
- Japan
- Prior art keywords
- solution
- absorption device
- absorber
- regenerator
- refrigerant
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 238000010521 absorption reaction Methods 0.000 title claims abstract description 17
- 239000003507 refrigerant Substances 0.000 claims abstract description 17
- 239000006096 absorbing agent Substances 0.000 claims description 19
- 239000000243 solution Substances 0.000 abstract description 35
- 239000000498 cooling water Substances 0.000 abstract description 14
- 238000010790 dilution Methods 0.000 abstract description 5
- 239000012895 dilution Substances 0.000 abstract description 5
- 239000007788 liquid Substances 0.000 abstract description 5
- 230000008030 elimination Effects 0.000 abstract 1
- 238000003379 elimination reaction Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 238000001816 cooling Methods 0.000 description 5
- 230000007423 decrease Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000009977 dual effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
- F25B29/006—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、吸収式冷温水ユニットに係り、安定した冷房
運転を継続できる制御機構を備えた、吸収式冷温水ユニ
ットに関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an absorption type cold/hot water unit, and more particularly, to an absorption type cold/hot water unit that is equipped with a control mechanism that can continue stable cooling operation.
吸収式冷温水ユニットに通水される冷却水の温度には、
冷温水ユニット機内の冷媒保有量等との関連により、下
限がある。そのため1通常冷温水ユニットを通過した冷
却水は一部が冷却塔に、−部は冷却塔を経由せずに、再
び、冷温水ユニットに戻ると云った様に、バイパス制御
する事により冷却水温の下がりすぎを防止している。The temperature of the cooling water passed through the absorption type chilled/hot water unit is as follows:
There is a lower limit depending on the amount of refrigerant held in the cold/hot water unit. Therefore, by bypass control, the cooling water temperature can be adjusted by controlling the cooling water such that part of the cooling water that has passed through the normal cold/hot water unit goes to the cooling tower, and the other part returns to the cold/hot water unit without passing through the cooling tower. This prevents the temperature from dropping too low.
(ガス吸収冷温水機 ハンドブンク 日本冷凍空調工業
会 平成元年6月改訂第二版)
〔発明が解決しようとする課題〕
従来の技術によると、通常運転時の冷却水温制御は可能
であるが、冬期の立上げ時等に冷却水温が外気により適
冷状態にある時は、温度制御が不能となり、冷温水ユニ
ットに許容される下限水温を下廻り、冷温水ユニット機
内冷媒不足等の運転支障に至る事があった。(Gas absorption chiller/heater handbunk, Japan Refrigeration and Air Conditioning Industry Association, revised 2nd edition, June 1989) [Problem to be solved by the invention] According to the conventional technology, it is possible to control the cooling water temperature during normal operation; When the cooling water temperature is properly cooled by the outside air, such as during startup in winter, temperature control becomes impossible and the water temperature drops below the minimum allowable temperature for the chilled/hot water unit, leading to operational problems such as a lack of refrigerant in the chilled/hot water unit. Something happened.
本発明の目的は、この問題を冷温水ユニット内の装置に
より解決することにある。The object of the present invention is to solve this problem by means of a device within a hot and cold water unit.
上記目的を達成するために、本発明は高温及び低温再生
器から環流する濃溶液の一部又は全量を吸収器の伝熱管
にて撒布せずに吸収器又は吸収器と溶液ポンプを連結す
る管に合流し、溶液ポンプで再び再生器へ送る機構を備
えたものである。In order to achieve the above object, the present invention provides an absorber or a pipe connecting an absorber and a solution pump without distributing part or all of the concentrated solution recirculating from a high-temperature and low-temperature regenerator through a heat transfer tube of the absorber. The system is equipped with a mechanism for sending the liquid to the regenerator again using a solution pump.
再生器から環流する濃溶液の一部又は全量を吸収器伝熱
管に撒布せずに再び再生器に送る事によって、吸収器で
の溶液と冷却水の熱伝達が阻害される。それによって溶
液の過剰稀釈を防ぐ事ができるから、機内の冷媒液量を
維持する事ができる。By sending part or all of the concentrated solution flowing back from the regenerator to the regenerator without distributing it to the absorber heat transfer tubes, heat transfer between the solution and the cooling water in the absorber is inhibited. This prevents excessive dilution of the solution, allowing the amount of refrigerant in the machine to be maintained.
以下、本発明の一実施例を第1図および第2図により説
明する。第1図は、本発明の一実施例に係る吸収式冷温
水ユニットの動作系を示す系統図、第2図は二重効用吸
収式冷温水ユニットの系統図である。An embodiment of the present invention will be described below with reference to FIGS. 1 and 2. FIG. 1 is a system diagram showing an operating system of an absorption type cold/hot water unit according to an embodiment of the present invention, and FIG. 2 is a system diagram of a dual effect absorption type cold/hot water unit.
まず、第2図により二重効用吸収式冷凍機の冷凍サイク
ルを説明する。First, the refrigeration cycle of a dual-effect absorption refrigerator will be explained with reference to FIG.
蒸発器1内は約百分の一気圧に保たれている。The inside of the evaporator 1 is maintained at about 1/100th of an atmospheric pressure.
冷媒である水は、冷媒ポンプ2により蒸発器1へ送られ
、冷水が流通する伝熱管3の上に撒布され冷水の熱を奪
って蒸発する。これにより冷却作用が発生する。蒸発し
た冷媒蒸気は、伝熱管4内を通る冷却水による冷却によ
って低圧に保たれた吸収器5へ流れ込み、ここで溶液ポ
ンプ6により撒布された臭化リチウム水溶液により吸収
され、臭化リチウム水溶液は薄くなる。この稀溶液は溶
液ポンプ6により溶液熱交換器7を経て、一部は高温再
生器8へ、残りは低温再生器9へ、それぞれ、送り込ま
れる。この稀溶液は、高温再生器8では、直接、熱源(
ボイラ)により加熱されて蒸気と濃溶液に分離され、ま
た、低温再生器9では高温再生器8で発生した蒸気によ
り加熱されて蒸気と濃溶液に分離される。Water, which is a refrigerant, is sent to the evaporator 1 by a refrigerant pump 2, and is spread over heat transfer tubes 3 through which the cold water flows, absorbing heat from the cold water and evaporating. This produces a cooling effect. The evaporated refrigerant vapor flows into the absorber 5 kept at low pressure by cooling with cooling water passing through the heat transfer tube 4, where it is absorbed by the lithium bromide aqueous solution sprayed by the solution pump 6, and the lithium bromide aqueous solution is Become thin. This diluted solution is sent by a solution pump 6 through a solution heat exchanger 7, a portion of which is sent to a high temperature regenerator 8, and the remainder to a low temperature regenerator 9. This dilute solution is directly supplied to the heat source (
In the low-temperature regenerator 9, it is heated by the steam generated in the high-temperature regenerator 8 and is separated into steam and a concentrated solution.
このようにして濃縮された溶液は、再び、溶液熱交換器
7を経て吸収器5に導かれる。低温再生器9で溶液を加
熱し凝縮したドレンは、凝縮器10に導かれる。また、
低温再生器9で発生した蒸気は凝縮器1oで凝縮する。The solution thus concentrated is again led to the absorber 5 via the solution heat exchanger 7. Drainage obtained by heating and condensing the solution in the low-temperature regenerator 9 is led to the condenser 10. Also,
The steam generated in the low temperature regenerator 9 is condensed in the condenser 1o.
このようにしてできた凝縮冷媒は、蒸発器1へ導かれ、
サイクルを一巡する。The condensed refrigerant thus produced is led to the evaporator 1,
Complete the cycle.
次に、第1図を参照して本実施例の吸収式冷温水ユニッ
トの構成および作用を説明する。Next, the structure and operation of the absorption type cold/hot water unit of this embodiment will be explained with reference to FIG.
溶縮された溶液は溶液熱交換器7を経て吸収器5に導か
れるが、途中、三方弁11により、一部又は全量が吸収
器伝熱管4に撒布される事なく吸収器5、又は、破線で
示す様に、吸収器5と濃液ポンプ6を連結する管に導か
れ、再び、溶液ポンプ6により再生器へ導かれる。゛三
方弁11は、制御装置12により能動的に制御され、そ
の動作は、冷媒液面計13の減少、冷媒温度計14.冷
水温度計15.冷却水温度計16の低下のいずれが、又
は、組合わせ演算結果により撒布溶液量が減する様に動
作する。The melted solution is guided to the absorber 5 via the solution heat exchanger 7, but on the way, a three-way valve 11 prevents part or all of the amount from being spread to the absorber heat exchanger tube 4, and the solution is transferred to the absorber 5 or As shown by the broken line, the solution is guided to a pipe connecting the absorber 5 and the concentrated solution pump 6, and is again guided to the regenerator by the solution pump 6. ``The three-way valve 11 is actively controlled by the control device 12, and its operation is controlled by the decrease of the refrigerant level gauge 13, the decrease of the refrigerant temperature gauge 14. Cold water thermometer 15. It operates so that the amount of solution to be sprayed decreases depending on whether the cooling water thermometer 16 decreases or the result of a combination of calculations.
これによって、濃溶液と冷却水の熱交換が阻害されるた
め、溶液の過剰稀釈が防止され、従って、機内冷媒液が
無くなる事が防止されるため、安定した運転を継続する
事ができる。This inhibits heat exchange between the concentrated solution and the cooling water, thereby preventing excessive dilution of the solution, thereby preventing the in-machine refrigerant liquid from running out, allowing stable operation to continue.
本発明によれば、冷却水温が低く制御不能な時でも吸収
器熱伝達を制御する事で過剰稀釈による機内冷媒不足を
防止できるので、安定した運転を継続することができる
。According to the present invention, even when the cooling water temperature is low and uncontrollable, by controlling absorber heat transfer, a shortage of refrigerant in the machine due to excessive dilution can be prevented, so stable operation can be continued.
第1図は本発明の一実施例の系統図、第2図は従来の系
統図である。
1・・蒸発器、2・・・冷媒ポンプ、5・・・吸収器。
′lJ1図FIG. 1 is a system diagram of an embodiment of the present invention, and FIG. 2 is a conventional system diagram. 1... Evaporator, 2... Refrigerant pump, 5... Absorber. 'lJ1 figure
Claims (1)
溶液ポンプ、冷媒ポンプとこれらを作動的に結合する配
管系からなる吸収式冷温水ユニットに於いて、 前記高温及び低温再生器から前記吸収器に環流する溶液
の一部、又は、全量を、前記吸収器の伝熱管に撒布せず
に、前記吸収器又は前記吸収器と前記溶液ポンプを連結
する管に合流し、前記溶液ポンプにより、再び、再生器
へ送る機構をもつことを特徴とする吸収式冷温水ユニッ
ト。[Claims] 1. Evaporator, absorber, high and low temperature regenerator, heat exchanger,
In an absorption type cold/hot water unit consisting of a solution pump, a refrigerant pump, and a piping system that operatively connects these, part or all of the solution flowing back from the high temperature and low temperature regenerators to the absorber is The absorption characterized by having a mechanism in which the absorber does not spread to the heat transfer tube of the absorber, but flows into the absorber or a tube connecting the absorber and the solution pump, and is sent to the regenerator again by the solution pump. Type cold/hot water unit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32926790A JPH04203769A (en) | 1990-11-30 | 1990-11-30 | Absorption type cold water of hot water device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32926790A JPH04203769A (en) | 1990-11-30 | 1990-11-30 | Absorption type cold water of hot water device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04203769A true JPH04203769A (en) | 1992-07-24 |
Family
ID=18219541
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32926790A Pending JPH04203769A (en) | 1990-11-30 | 1990-11-30 | Absorption type cold water of hot water device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04203769A (en) |
-
1990
- 1990-11-30 JP JP32926790A patent/JPH04203769A/en active Pending
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