JP2014105930A - Heat source system - Google Patents

Heat source system Download PDF

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JP2014105930A
JP2014105930A JP2012259779A JP2012259779A JP2014105930A JP 2014105930 A JP2014105930 A JP 2014105930A JP 2012259779 A JP2012259779 A JP 2012259779A JP 2012259779 A JP2012259779 A JP 2012259779A JP 2014105930 A JP2014105930 A JP 2014105930A
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cooling water
cooling
water inlet
water
cold water
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JP5913066B2 (en
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Michiaki Yamaguchi
倫明 山口
Taneya Yamashita
植也 山下
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Sanki Engineering Co Ltd
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Sanki Engineering Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To automatically change a cooling water temperature set value in the case that a cooling water inlet temperature set value of a water-cooling refrigerator can be lowered depending on a surrounding atmospheric condition or an air conditioning load or in the case that the cooling water inlet temperature must be increased.SOLUTION: This system comprises: a water-cooling refrigerator using a capacity compression type rotary compressor; a cooling water circulation passage having a cooling water going-side passage having a cooling water pump and a cooling water inlet thermometer, a cooling water returning-side passage and a bypass passage having a cooling water bypass valve arranged between the passages; a cooling tower communicated with the cooling water circulation passage; a cold water circulation passage provided with a cold water going-side passage for a load side and a cold water returning-side passage from a load side and having a cold water pump and a cold water inlet thermometer arranged on a cold water returning-side passage; and an instruction adjustor for outputting an instruction for changing a degree of opening of a cooling water bypass valve in such a way that a cooling water inlet temperature may become a cold water inlet temperature+Tα°C on the basis of a cooling water inlet temperature measured by the cooling water inlet thermometer and a cold water inlet temperature measured by the cold water inlet thermometer.

Description

本発明は、容積圧縮型回転式圧縮機を備えた、凝縮器が水冷方式である水冷冷凍機を用いる水を冷凍する熱源システムに関する。   The present invention relates to a heat source system for freezing water using a water-cooled refrigerator having a volumetric compression rotary compressor and having a water-cooled condenser.

工場やオフィスビル等における、内部発熱、建屋負荷及び外気負荷等の熱負荷があり、それを生産工程上冷却したり、保健空調として冷却したりすることが要求される種々の設備で、生産機器や空調設備等に備わる水−水熱交換器や空気−水熱交換器に対し、冷熱を伴った熱媒体(冷水)を循環供給する熱源システムとして、冷却塔等で大気と熱交換して凝縮器で熱を捨てる、凝縮器が水冷方式である水冷冷凍機を用いる熱源システムが一般に多く用いられている。
その一例を図10に示す。
水冷冷凍機1は、低温・低圧のフロンガスやアンモニアガス、水等の冷媒ガスを、高温・高圧のガスにし、冷凍サイクル内を循環させる働きをするもので、圧縮機2、凝縮器3、絞り装置(膨張弁やキャピラリ等)4、蒸発器5を備え、冷凍サイクルを構成する。
Production equipment in various facilities that have heat loads such as internal heat generation, building loads, and outside air loads in factories and office buildings, etc. that are required to be cooled during the production process or as health air conditioning As a heat source system that circulates and supplies a heat medium (cold water) with cold heat to water-water heat exchangers and air-water heat exchangers installed in air conditioning equipment, etc., heat is condensed with the air in a cooling tower etc. In general, a heat source system using a water-cooled refrigerator in which heat is thrown away by a condenser and a condenser is a water-cooling system is widely used.
An example is shown in FIG.
The water-cooled refrigerator 1 serves to circulate the refrigerant gas such as low-temperature / low-pressure chlorofluorocarbon gas, ammonia gas, water, etc. in the refrigeration cycle using a high-temperature / high-pressure refrigerant gas. The apparatus (expansion valve, capillary, etc.) 4 and the evaporator 5 are provided, and a refrigerating cycle is comprised.

凝縮器3には、冷却塔6からの冷却水を循環する冷却水循環通路7が配置されている。冷却水循環通路7は、冷却塔6からの往き側通路7aと冷却塔6への還り側通路7bとを備え、往き側通路7aには、冷却水ポンプ8と冷却水入口温度計9とが配置されている。往き側通路7aと還り側通路7bとは、水冷冷凍機1の近傍において流量調整弁12が配置された通路11により接続されている。
冷却水入口温度計9は、測定した冷却水入口温度の計測値を指示調節器(TIC)10へ入力し、指示調節器(TIC)10には、水冷冷凍機1の凝縮器3へ導入しても問題ない冷却水温が設定され、冷却水入口温度の計測値と当該問題ない冷却水温設定値との偏差に応じて、流量調整弁12の電動アクチュエータ12aを、冷却水温設定値より計測値が大で偏差が大きければ流量調整弁12を閉鎖し、冷却水温設定値が計測値より大きいものの偏差が小さくなってくれば流量調整弁12を開放する方向へ動作させるよう制御する。これにより、冷却水入口温度が前記問題ない冷却水温設定値を下回らないように制御する。
A cooling water circulation passage 7 for circulating the cooling water from the cooling tower 6 is disposed in the condenser 3. The cooling water circulation passage 7 includes an outward passage 7a from the cooling tower 6 and a return passage 7b to the cooling tower 6. A cooling water pump 8 and a cooling water inlet thermometer 9 are disposed in the outward passage 7a. Has been. The forward side passage 7a and the return side passage 7b are connected by a passage 11 in which a flow rate adjusting valve 12 is arranged in the vicinity of the water-cooled refrigerator 1.
The cooling water inlet thermometer 9 inputs a measured value of the measured cooling water inlet temperature to the indication controller (TIC) 10, and introduces the measured value of the cooling water inlet temperature into the condenser 3 of the water-cooled refrigerator 1. Even if the cooling water temperature that does not have any problem is set, the measured value of the electric actuator 12a of the flow rate adjusting valve 12 is determined from the cooling water temperature setting value according to the deviation between the measured value of the cooling water inlet temperature and the cooling water temperature setting value that has no problem. If the deviation is large and the deviation is large, the flow rate adjustment valve 12 is closed, and if the deviation of the cooling water temperature set value larger than the measured value becomes small, the flow rate adjustment valve 12 is controlled to open. Thereby, it controls so that a cooling water inlet temperature may not fall below the cooling water temperature setting value which does not have the said problem.

また、蒸発器5には、負荷側へ冷水を循環する冷水循環通路13が接続されている。冷却水循環通路13は、負荷側への往き側通路13aと負荷側からの還り側通路13bとを備えている。
図10に示す熱源システムでは、水冷冷凍機1は、低温・低圧の冷媒ガスを圧縮機2で高温・高圧のガスにし、凝縮器3で冷却塔6からの冷却水で熱を放出して高圧冷媒液とし、絞り装置(膨張弁等)4で減圧させて低圧冷媒液とした後、蒸発器5で負荷側からの還り冷水の熱を奪い低圧冷媒ガスとして圧縮機2に戻す冷凍サイクル内を循環させる。
ここで、圧縮機の形式は、容積圧縮型、エゼクタ型、遠心型(ターボ)の3種類が知られている。容積圧縮型と遠心型(ターボ)とが現在広く使用されており、エゼクタ型は工業用のごく一部にしか使用されていない。
The evaporator 5 is connected with a cold water circulation passage 13 for circulating cold water to the load side. The cooling water circulation passage 13 includes an outward passage 13a to the load side and a return passage 13b from the load side.
In the heat source system shown in FIG. 10, the water-cooled refrigerator 1 converts a low-temperature / low-pressure refrigerant gas into a high-temperature / high-pressure gas by the compressor 2 and releases heat from the cooling water from the cooling tower 6 by the condenser 3. After the refrigerant liquid is decompressed by the expansion device (expansion valve or the like) 4 to form a low-pressure refrigerant liquid, the evaporator 5 takes the heat of the return cold water from the load side and returns it to the compressor 2 as the low-pressure refrigerant gas. Circulate.
Here, three types of compressors are known: a volume compression type, an ejector type, and a centrifugal type (turbo). The volume compression type and the centrifugal type (turbo) are currently widely used, and the ejector type is used only for a small portion of industrial use.

容積圧縮型は、ケーシングとそれに内接する可動部材等との間に生じる密閉空間の変化によって冷媒ガスを吸入側から吐出側に圧縮する形式で、往復動式と回転式とがある。
往復動式は、ピストンの往復運動によりシリンダー内でガスを圧縮するもので、全密閉型、半密閉型、開放型がある。
回転式は、ロータリー型、スクロール型、スクリュー型がある。
遠心型(ターボ)は、羽根車の回転運動によって冷媒ガスにエネルギーを与えて圧縮する。
The volume compression type is a type in which refrigerant gas is compressed from the suction side to the discharge side by a change in a sealed space generated between the casing and a movable member inscribed in the casing, and there are a reciprocating type and a rotary type.
The reciprocating type compresses the gas in the cylinder by the reciprocating motion of the piston, and includes a fully sealed type, a semi-sealed type, and an open type.
The rotary type includes a rotary type, a scroll type, and a screw type.
The centrifugal type (turbo) imparts energy to the refrigerant gas and compresses it by the rotational movement of the impeller.

ところで、容積圧縮型回転式の圧縮機は、圧縮ガスの漏れを防ぐため、可動部の隙間を潤滑油でシールする構造を採用し、潤滑油を冷媒の差圧を利用して重要なロータの軸受部等に給油循環する。そのため、冷媒の圧縮機での差圧があまりに少ないと、つまり圧縮機が仕事をしないような前後圧のつかない状況では、潤滑油を重要な箇所に給油循環でき難くなり、軸の焼き付き等が生じる問題がある。
これに対し、容積圧縮型往復動式及び遠心型(ターボ)の圧縮機は、オイルポンプが内蔵され、オイルポンプの駆動に圧縮機駆動力の一部が利用されて潤滑油が必要な各所に給油循環が担保されているため、冷媒の圧力差が少ない場合でも潤滑油の循環が行われるという利点がある。これは、ターボ圧縮機の容量制御のホットガスバイパス機構や、往復動圧縮機のコンロッド部分の圧力差不存在による強制潤滑油循環等を利用しないと各種制御できないからでもあった。
By the way, the volume compression type rotary compressor employs a structure in which the gap between the movable parts is sealed with lubricating oil in order to prevent the leakage of compressed gas, and the lubricating oil is used for an important rotor by utilizing the differential pressure of the refrigerant. Oil is circulated through the bearings. Therefore, if the refrigerant differential pressure is too small, that is, in a situation where the compressor does not work and there is no front-rear pressure, it becomes difficult to lubricate and circulate the lubricating oil to important locations, causing seizure of the shaft, etc. There are problems that arise.
In contrast, volumetric compression type reciprocating and centrifugal (turbo) compressors have built-in oil pumps, and some parts of the compressor driving force are used to drive the oil pumps, which require lubricating oil. Since the oil supply circulation is secured, there is an advantage that the lubricating oil is circulated even when the refrigerant pressure difference is small. This is because various controls cannot be performed without using a hot gas bypass mechanism for controlling the capacity of the turbo compressor or forced lubricating oil circulation due to the absence of a pressure difference in the connecting rod portion of the reciprocating compressor.

以上の理由から、容積圧縮型回転式の圧縮機2は、凝縮器3の冷却水入口温度に下限温度が存在(例えば、冷水入口温度+1.0℃)するため、水冷冷凍機1の凝縮器3へ冷却塔6で大気と熱交換した冷却水を導入するにあたり、大気温度が季節のみでなく1日の時間によっても大きく変動することを鑑みて、指示調節器(TIC)10の、水冷冷凍機1の凝縮器3へ導入しても問題ない冷却水温設定値は、冷水温度の還り温度である冷水入口温度が設備の状況で20数℃になっても良いよう、冷却水側が変動しても良いように、余裕を持った固定値(例えば、27℃)で運用している。
よって、指示調節器(TIC)10の設定温度は余裕を持った固定値となり、水冷冷凍機1側で規定されている冷却水下限温度よりも実際は高温で冷却水が運用されていることが多い。
For the above reasons, the volume compression type rotary compressor 2 has a lower limit temperature in the cooling water inlet temperature of the condenser 3 (for example, cold water inlet temperature + 1.0 ° C.). In view of the fact that the air temperature greatly fluctuates not only in the season but also in the time of the day when introducing the cooling water heat-exchanged with the atmosphere in the cooling tower 6 to the water cooling tower 3, the water-cooled refrigeration of the indication controller (TIC) 10 The cooling water temperature set value that can be safely introduced into the condenser 3 of the machine 1 is such that the cooling water side fluctuates so that the cooling water inlet temperature, which is the return temperature of the cooling water temperature, may be 20 ° C. or more in the equipment situation. In order to improve the operation, a fixed value with a margin (for example, 27 ° C.) is used.
Accordingly, the set temperature of the instruction controller (TIC) 10 is a fixed value with a margin, and the cooling water is often operated at a temperature actually higher than the cooling water lower limit temperature defined on the water-cooled refrigerator 1 side. .

しかし、最近の省エネルギーに対する世間の喫緊の要請により、中間期〜冬期の外気湿球温度低下に伴う冷却塔6の冷却水温度低下によって、水冷冷凍機1の凝縮圧低下が図れることを最大限利用するため、冷凍機メーカでは、冷凍機の凝縮器へ導入できる冷却水の下限温度をますます低下させてきており(例えば、20℃や18℃までも)、この温度に近い余裕を持った固定値に年中設定することで、設備費をかけずに冷凍機の成績係数(運転効率)COPを向上させられることは広く知られている(例えば、非特許文献1参照。)。
また、水冷冷凍機側の条件を満たしつつ冷却塔の能力を有効活用するために、水冷冷凍機から導出された冷却水を再び水冷冷凍機に流入させる循環管と、循環管を流れる冷却水を流動させる循環ポンプとを備え、冷却塔から導出される冷却水の温度が水冷冷凍機に導入可能な下限温度よりも低い場合、水冷冷凍機が求める下限流量以上の冷却水を循環管及び水冷冷凍機に循環させつつ下限温度よりも低い冷却水を必要な流量に絞って循環管に流入させ、冷却水ポンプの動両区を低減させて省エネルギーを図る熱源システムが提案されている(例えば、特許文献1参照)。
However, due to the recent urgent demand for energy conservation, the maximum use of the reduction in the condensation pressure of the water-cooled refrigerator 1 due to the decrease in the cooling water temperature of the cooling tower 6 due to the decrease in the temperature of the outside air wet bulb during the intermediate period to winter Therefore, chiller manufacturers are increasingly lowering the lower limit temperature of cooling water that can be introduced into the condenser of the chiller (for example, up to 20 ° C and 18 ° C), and fixing with a margin close to this temperature. It is widely known that the coefficient of performance (operating efficiency) COP of a refrigerator can be improved without setting equipment costs by setting the value throughout the year (for example, see Non-Patent Document 1).
Also, in order to effectively utilize the capacity of the cooling tower while satisfying the conditions on the water-cooled refrigerator side, a circulation pipe for introducing the cooling water derived from the water-cooled refrigerator again into the water-cooled refrigerator, and a cooling water flowing through the circulation pipe are provided. When the temperature of the cooling water led out from the cooling tower is lower than the lower limit temperature that can be introduced into the water-cooled refrigerator, the circulating pipe and the water-cooled refrigerator A heat source system has been proposed in which cooling water lower than the lower limit temperature is squeezed to a required flow rate while being circulated through the machine and allowed to flow into a circulation pipe to reduce both the moving zones of the cooling water pump and save energy (for example, patents) Reference 1).

特開2010−85072号公報JP 2010-85072 A

「空調自動制御と省エネルギー」(発行日平成23年4月10日、発行所株式会社オーム社)第60頁〜第62頁"Air-conditioning automatic control and energy saving" (Issue date: April 10, 2011, Issuer Ohm Co., Ltd.) pp. 60-62

容積圧縮型回転式の圧縮機2を備えた水冷冷凍機1について、遠心式圧縮機を備えた水冷冷凍機のように外気の湿球温度等に応じて冷却水入口温度を自動で設定変更する考え方を採用すれば省エネルギーに貢献できるとする考え方は従来から想定されていた。
しかし、容積圧縮型回転式の圧縮機2は、圧縮ガスの漏れを防ぐため、可動部の隙間を潤滑油でシールする構造を採用し、潤滑油を冷媒の差圧を利用して重要なロータの軸受部等に給油循環する。そのため、冷媒の圧縮機での差圧があまりに少ないと、つまり圧縮機が仕事をしないような前後圧のつかない状況では、潤滑油を重要な箇所に給油循環でき難くなり、軸の焼き付き等が生じ、冷凍サイクルの状態維持に重大な問題が生じることとなる。このため、冷却塔側から送られてくる冷却水入口の実際温度と、水冷冷凍機の凝縮器へ導入できる冷却水下限温度とが近づくと、水冷冷凍機1の制御として備わる高圧側異常低圧として安全回路が動作し、水冷冷凍機1がエラー停止することとなる。水冷冷凍機1は破壊を免れるが熱源システムとしては機能を果たせなくなり、負荷側で重大な不具合が生じてしまう。
About the water-cooled refrigerator 1 provided with the volume compression type rotary compressor 2, the cooling water inlet temperature is automatically changed according to the wet bulb temperature of the outside air as in the water-cooled refrigerator provided with the centrifugal compressor. Conventionally, it has been assumed that the idea can contribute to energy saving.
However, the volume compression type rotary compressor 2 employs a structure in which the gap between the movable parts is sealed with lubricating oil to prevent leakage of compressed gas, and the lubricating oil is used as an important rotor by utilizing the differential pressure of the refrigerant. Oil is circulated through the bearings of the machine. Therefore, if the refrigerant differential pressure is too small, that is, in a situation where the compressor does not work and there is no front-rear pressure, it becomes difficult to lubricate and circulate the lubricating oil to important locations, causing seizure of the shaft, etc. This will cause serious problems in maintaining the state of the refrigeration cycle. For this reason, when the actual temperature of the cooling water inlet sent from the cooling tower side approaches the cooling water lower limit temperature that can be introduced into the condenser of the water-cooled refrigerator, the high-pressure side abnormal low pressure provided as the control of the water-cooled refrigerator 1 The safety circuit operates and the water-cooled refrigerator 1 is stopped due to an error. Although the water-cooled refrigerator 1 can be prevented from being destroyed, it cannot function as a heat source system, and a serious problem occurs on the load side.

以上の理由から、容積圧縮型回転式の圧縮機2は、凝縮器3の冷却水入口温度に下限温度が存在(例えば、冷水入口温度+1.0℃)するため、水冷冷凍機1の凝縮器3へ冷却塔6で大気と熱交換した冷却水を導入するにあたり、大気温度が季節で大きく変動することを鑑みて、前記の指示調節器(TIC)10の、水冷冷凍機1の凝縮器3へ導入しても問題ない冷却水温設定値は、冷却水側が変動しても良いように、余裕を持った固定値(例えば、27℃)で運用している。
また、水冷冷凍機1の凝縮圧低下が図れることを最大限利用するため、冷凍機メーカでは、冷凍機の凝縮器へ導入できる冷却水の下限温度をますます低下させてきてはいるものの(例えば、20℃や18℃までも)、余裕を持った固定値の余裕代は変えようがなく、少し固定値の値が下がるだけである。
このように、容積圧縮型回転式の圧縮機2を備えた水冷冷凍機1の冷却水入口温度は、年中固定値としていて、冬期等冷却水温度が充分凝縮器の冷却水入口下限温度を下回るまで低下する時期でも、冷却水温を余裕を見た固定値までわざわざ昇温させて導入するような設定となっていた。
For the above reasons, the volume compression type rotary compressor 2 has a lower limit temperature in the cooling water inlet temperature of the condenser 3 (for example, cold water inlet temperature + 1.0 ° C.). In consideration of the fact that the atmospheric temperature fluctuates greatly in the season when the cooling water exchanged with the atmosphere in the cooling tower 6 is introduced into the condenser 3, the condenser 3 of the water-cooled refrigerator 1 of the indication controller (TIC) 10 described above. The cooling water temperature setting value that is not a problem even if it is introduced into the system is operated at a fixed value (for example, 27 ° C.) with a margin so that the cooling water side may fluctuate.
Moreover, in order to make the best use of the ability to reduce the condensation pressure of the water-cooled refrigerator 1, the refrigerator manufacturer has been lowering the lower limit temperature of the cooling water that can be introduced into the condenser of the refrigerator (for example, Even 20 ° C and 18 ° C), the margin of the fixed value with a margin cannot be changed, and the value of the fixed value is slightly lowered.
Thus, the cooling water inlet temperature of the water-cooled refrigerator 1 equipped with the volume compression type rotary compressor 2 is set to a fixed value throughout the year, and the cooling water temperature such as in winter is sufficiently low. Even at the time when the temperature drops to below, the cooling water temperature was set to a fixed value with a margin and introduced.

そのため、容積圧縮型回転式の圧縮機2を備えた水冷冷凍機1は、冷却水入口温度設定値を外気条件や空調負荷が低温となって熱負荷も冷却水温も低くなる冬期においては、例えば工務担当者等が、余裕を持った固定値の余裕代を削るため、外気条件や冷水の還り温度等を見ながら手動で冷却水の入口温度設定値を変更していたが、逐一観察して水冷冷凍機1をエラー停止しないようにしなければならず、とても手間がかかる危険性の高い運用が求められた。
特に、中間期〜冬期にかけ、冷却水温度を1℃でも低くすると、冷凍機の成績係数(運転効率)COPは大きく改善できるのに、容積圧縮型回転式の圧縮機2を備えた水冷冷凍機1では、普通は余裕を持った固定値で運用され、中途半端な高効率運転となっていた。
For this reason, the water-cooled refrigerator 1 having the volumetric compression rotary compressor 2 has a cooling water inlet temperature set value in the winter season when the outdoor air condition and the air conditioning load are low, and the heat load and the cooling water temperature are low. Engineers etc. manually changed the cooling water inlet temperature setting value while looking at the outside air conditions and the return temperature of the cold water, etc., in order to reduce the margin of the fixed value with a margin. The water-cooled refrigerator 1 must be kept from error-stopping, and operation with a high risk of being troublesome is required.
In particular, when the cooling water temperature is lowered even at 1 ° C. from the middle period to the winter period, the coefficient of performance (operating efficiency) COP of the refrigerator can be greatly improved, but the water-cooled refrigerator equipped with the volume compression type rotary compressor 2 In No. 1, it was normally operated at a fixed value with a margin, and it was a halfway high-efficiency operation.

冷凍機の成績係数(運転効率:入力(圧縮仕事)に対する出力(冷凍効果)の比)COPは、図11に示す冷凍機の性能線図から明らかなように、またモリエ線図からも明らかなように、冷却水入口温度が低いほど、凝縮圧が低くてすむので、圧縮仕事が小さくて済み、冷凍機の成績係数COPが高効率となり、冷却水入口温度が高いほど、凝縮圧が高くなる必要があり圧縮仕事を多く要求するので、冷凍機の成績係数COPが低効率となることはよく知られている。
なお、容積圧縮型往復動式及び遠心型(ターボ)の圧縮機は、オイルポンプが内臓されているため、冷媒の圧力差が少ない場合でも潤滑油の循環が行われる。従って、容積圧縮型回転式の圧縮機のように、潤滑油を循環させることができ難くなるという問題は起こらない。
The coefficient of performance (operation efficiency: ratio of output (refrigeration effect) to input (compression work)) COP of the refrigerator is apparent from the performance diagram of the refrigerator shown in FIG. 11 and also from the Mollier diagram. Thus, the lower the cooling water inlet temperature, the lower the condensing pressure, so the compression work can be reduced, the coefficient of performance COP of the refrigerator becomes high efficiency, and the higher the cooling water inlet temperature, the higher the condensing pressure. It is well known that the coefficient of performance COP of the refrigerator is low in efficiency because it requires a lot of compression work.
In addition, since the volume compression type reciprocating type and centrifugal type (turbo) compressors have an oil pump, the lubricating oil is circulated even when the pressure difference of the refrigerant is small. Therefore, the problem that it becomes difficult to circulate the lubricating oil does not occur unlike the volumetric compression type rotary compressor.

本発明は斯かる従来の問題点を解決するために為されたもので、水冷冷凍機の冷却水入口温度設定値を外気条件や空調負荷によっては、低くできる場合や冷却水入口温度を高くしなければならない場合に自動で冷却水温度設定値を変更することが可能な熱源システムを提供することにある。   The present invention has been made to solve such a conventional problem, and the cooling water inlet temperature setting value of the water-cooled refrigerator can be lowered depending on the outside air condition or the air conditioning load, or the cooling water inlet temperature is increased. An object of the present invention is to provide a heat source system capable of automatically changing the set value of the cooling water temperature when it has to be.

請求項1に係る発明は、容積圧縮型回転式の圧縮機、水冷方式の凝縮器、絞り装置及び蒸発器を備え冷凍サイクルを構成する水冷冷凍機と、大気と冷却水とを熱交換する冷却塔と、前記冷却塔に一端を接続し冷却水ポンプ及び冷却水入口温度計の順に配置し、他端を前記凝縮器に接続する冷却水往き側通路と、前記凝縮器に一端を接続し他端を前記冷却塔に接続する冷却水還り側通路と、前記冷却水往き側通路の前記冷却水ポンプ吸込み側と前記冷却水還り側通路との間を冷却水バイパス弁を介して接続するバイパス通路とを有する冷却水循環通路と、負荷側への冷水往き側通路と前記負荷側からの冷水還り側通路とを有し、前記冷水還り側通路に冷水ポンプ及び冷水入口温度計を配置し、前記蒸発器に連絡する冷水循環通路と、前記冷却水入口温度計の冷却水入口温度計測値に基づいて設定冷却水入口温度との偏差を演算し、該偏差に応じた前記冷却水バイパス弁の開度出力をする冷却水バイパス制御回路を有する指示調節器を備え、前記指示調節器には、前記設定冷却水入口温度を、前記冷水入口温度計の計測値に基づいて、前記冷水入口温度計測値+Tα℃となる値として前記冷却水バイパス制御回路の設定値として出力するカスケード回路を備えることを特徴とする。   The invention according to claim 1 is a cooling system that exchanges heat between a water-cooled refrigerator that includes a volume compression rotary compressor, a water-cooled condenser, a throttling device, and an evaporator, and that constitutes a refrigeration cycle, and the atmosphere and cooling water. A tower, one end connected to the cooling tower, a cooling water pump and a cooling water inlet thermometer are arranged in this order, and the other end is connected to the condenser, and one end is connected to the condenser. A cooling water return side passage connecting an end to the cooling tower, and a bypass passage connecting the cooling water pump suction side of the cooling water going side passage and the cooling water return side passage via a cooling water bypass valve A cooling water circulation passage having a cooling water return side passage to the load side and a cooling water return side passage from the load side, a cooling water pump and a cold water inlet thermometer being disposed in the cooling water return side passage, and the evaporation Cold water circulation passage communicating with the vessel, and the cooling water An instruction adjustment having a cooling water bypass control circuit that calculates a deviation from the set cooling water inlet temperature based on a measured value of the cooling water inlet temperature of the mouth thermometer and outputs an opening degree of the cooling water bypass valve according to the deviation The indicator regulator is configured such that the set cooling water inlet temperature is set to a value that becomes the cold water inlet temperature measurement value + Tα ° C. based on the measurement value of the cold water inlet thermometer. A cascade circuit for outputting as a set value is provided.

請求項2に係る発明は、請求項1記載の熱源システムにおいて、前記冷水循環通路には、前記冷水還り側通路の前記冷水ポンプ吸い込み側に還りヘッダと、前記冷水往き側通路に往きヘッダと、前記還りヘッダと前記往きヘッダの間にヘッダ間バイパス管とを備え、負荷側の熱負荷が小さくなると前記ヘッダ間バイパス管を冷水が流れることを特徴とする。
請求項3に係る発明は、請求項1又は2記載の熱源システムにおいて、前記容積圧縮型回転式の圧縮機は、ロータリー型圧縮機、スクロール型圧縮機又はスクリュー型圧縮機であることを特徴とする。
請求項4に係る発明は、請求項1乃至3の何れか記載の熱源システムにおいて、前記負荷は、高温冷水を要求する空調設備又は生産機器冷却用の熱源設備であって、冷水の還り温度が前記水冷冷凍機の冷却水入口下限温度を上回ること場合があることを特徴とする。
請求項5に係る発明は、請求項4記載の熱源システムにおいて、前記空調設備は、データセンターの空調設備であることを特徴とする。
The invention according to claim 2 is the heat source system according to claim 1, wherein the cold water circulation passage includes a return header on the cold water pump suction side of the cold water return side passage, a forward header on the cold water return side passage, An inter-header bypass pipe is provided between the return header and the forward header, and cold water flows through the inter-header bypass pipe when a thermal load on the load side becomes small.
The invention according to claim 3 is the heat source system according to claim 1 or 2, wherein the volume compression type rotary compressor is a rotary type compressor, a scroll type compressor or a screw type compressor. To do.
The invention according to claim 4 is the heat source system according to any one of claims 1 to 3, wherein the load is an air conditioning facility that requires high-temperature cold water or a heat source facility for cooling production equipment, and the return temperature of the cold water is It may exceed the cooling water inlet lower limit temperature of the water-cooled refrigerator.
The invention according to claim 5 is the heat source system according to claim 4, wherein the air conditioning equipment is an air conditioning equipment of a data center.

本発明によれば、凝縮器を水冷形式とした水冷冷凍機に対し、季節によって低くなる大気温度に応じて低温にできる冷却水の温度を最大限利用可能となるよう、最大限凝縮圧を低下させて運用できるので、高効率運転を維持できる。
また、水冷冷凍機の冷水還り温度が上昇した場合にも監視をしながら手動で冷却水入口温度を変更する必要がないので、運転管理が容易になる。
According to the present invention, for a water-cooled refrigerator having a water-cooled condenser, the maximum condensing pressure is lowered so that the temperature of the cooling water that can be lowered according to the atmospheric temperature, which becomes lower depending on the season, can be used as much as possible. Because it can be operated, high-efficiency operation can be maintained.
In addition, since it is not necessary to manually change the cooling water inlet temperature while monitoring even when the cold water return temperature of the water-cooled refrigerator increases, the operation management becomes easy.

本発明の一実施形態に係る熱源システムを示す概略図である。It is the schematic which shows the heat source system which concerns on one Embodiment of this invention. 図1の熱源システムに用いられる冷却水入口温度計(TCDS)、冷水入口温度計(TCR)及び指示調節器(TIC)の関係を示す説明図である。Figure 1 of the heat source system to the cooling water inlet thermometer used (T CDS), is an explanatory diagram showing a relationship between the cold water inlet temperature thermometer (T CR) and instruction controller (TIC). Tα=1.0℃の場合の冷却水入口温度設定値と冷水還り温度との関係を示す図である。It is a figure which shows the relationship between the cooling water inlet temperature setting value in case of T (alpha) = 1.0 degreeC, and cold water return temperature. 冷却水バイパス弁(MV)の開度と冷却水入口温度との関係の概念を示す図である。It is a figure which shows the concept of the relationship between the opening degree of a cooling water bypass valve (MV), and cooling water inlet temperature. 本実施形態に係る熱源システムを二次側冷水ポンプの制御が変流量制御の場合における定格運転時の状態を示す図である。It is a figure which shows the state at the time of rated operation in case the control of a secondary side chilled water pump is variable flow control in the heat source system which concerns on this embodiment. 図5の負荷が減少し、負荷率50%時の状態を示す図である。FIG. 6 is a diagram showing a state when the load of FIG. 5 is reduced and the load factor is 50%. 図5の負荷が減少し、負荷率37.5%時の状態を示す図である。FIG. 6 is a diagram showing a state when the load of FIG. 5 decreases and the load factor is 37.5%. 本実施形態に係る熱源システムを二次側冷水ポンプの制御が定流量制御の場合における定格運転時の状態を示す図である。It is a figure which shows the state at the time of rated operation in case the control of a secondary side chilled water pump is constant flow control in the heat source system which concerns on this embodiment. 図8の負荷が減少し、負荷率50%時の状態を示す図である。It is a figure which shows the state when the load of FIG. 8 reduces and the load factor is 50%. 従来の熱源システムを示す概略図である。It is the schematic which shows the conventional heat source system. 冷却水入口温度違いによる、冷凍機の成績係数の負荷率に応じた変化を示す一例を示す図である。It is a figure which shows an example which shows the change according to the load factor of the coefficient of performance of a refrigerator by the difference in cooling water inlet temperature.

以下、本発明を図面に示す実施形態に基づいて説明する。
図1は、本実施形態に係る熱源システムを示す。
本実施形態に係る熱源システムは、容積圧縮型回転式の圧縮機を備えた水冷冷凍機として水冷スクリューチラー50を用いた場合について説明する。
本実施形態では、水冷スクリューチラーの冷却水入口温度下限値16℃、冷水往還温度設定13℃−20℃(Δt=7℃)で、冷水還り温度が一般の事務所ビル等と比較して高温の設備を成立させることを目的としている。
Hereinafter, the present invention will be described based on embodiments shown in the drawings.
FIG. 1 shows a heat source system according to this embodiment.
The heat source system according to the present embodiment will be described with respect to a case in which a water-cooled screw chiller 50 is used as a water-cooled refrigerator having a volumetric compression type rotary compressor.
In this embodiment, the cooling water inlet temperature lower limit value of the water cooling screw chiller is 16 ° C., the cooling water return temperature setting is 13 ° C.-20 ° C. (Δt = 7 ° C.), and the cooling water return temperature is higher than that of general office buildings. The purpose is to establish the facilities.

水冷スクリューチラー50は、低温・低圧の冷媒ガスを高温・高圧のガスにし、冷凍サイクル内を循環させる働きをするもので、スクリュー型圧縮機51、凝縮器52、絞り装置(膨張弁等)53、蒸発器54を備え、冷凍サイクルを構成する。
凝縮器52には、冷却塔60からの冷却水を循環する冷却水循環通路61が配置されている。冷却水循環通路61は、冷却塔60からの冷却水往き側通路61aと冷却塔への冷却水還り側通路61bとを備え、冷却水往き側通路61aには、冷却塔60を一端に接続し冷却水ポンプ62及び水冷スクリューチラー冷却水入口温度を計測する冷却水入口温度計(TCDS)63とが順に配置され、他端に凝縮器52が接続されるよう配置されている。冷却水往き側通路61aと冷却水還り側通路61bとは、水冷スクリューチラー50の近傍において、冷却水往き側通路61aの冷却水ポンプ62吸込み側と冷却水還り側通路61bの間をバイパス通路64により接続されている。
The water-cooled screw chiller 50 functions to circulate the refrigeration cycle by converting the low-temperature / low-pressure refrigerant gas into a high-temperature / high-pressure gas. The screw-type compressor 51, the condenser 52, the expansion device (expansion valve, etc.) 53 The evaporator 54 is provided to constitute a refrigeration cycle.
A cooling water circulation passage 61 that circulates the cooling water from the cooling tower 60 is disposed in the condenser 52. The cooling water circulation passage 61 includes a cooling water forward side passage 61a from the cooling tower 60 and a cooling water return side passage 61b to the cooling tower, and the cooling water forward side passage 61a is connected to the cooling tower 60 at one end for cooling. A water pump 62 and a cooling water inlet thermometer (TCDS) 63 for measuring the water cooling screw chiller cooling water inlet temperature are sequentially arranged, and the condenser 52 is connected to the other end. The cooling water return side passage 61a and the cooling water return side passage 61b are, in the vicinity of the water cooling screw chiller 50, a bypass passage 64 between the cooling water pump 62 suction side and the cooling water return side passage 61b of the cooling water return side passage 61a. Connected by.

バイパス通路64には、二方弁から成る冷却水バイパス弁(MV)65が配置されている。冷却水バイパス弁(MV)65は、外部からの入力信号に応じて弁体の開閉を比例制御できるものであり、その弁体の開閉を例えば、古くから有るモジュトロールモータや最近ではステッピングモータ等の電動アクチュエータ65aにより外部からの制御信号に応じて動作させる構造になっている。
冷却塔60は、上部に開口60bを設け、下部に塔底水槽60cを設けたケーシング60aと、ケーシング60aの開口60bに設けた送風機60dと、送風機60dの下方のケーシング60aに設けた冷却水還り側通路61bに接続する散水器60eと、散水器60eの下方側のケーシング60a内に配置した充填物60fと、充填物60fの下方側のケーシング60aに設けた外気取り入れ用のルーバ60gとを備えている。
A cooling water bypass valve (MV) 65 comprising a two-way valve is disposed in the bypass passage 64. The cooling water bypass valve (MV) 65 can proportionally control the opening and closing of the valve body in accordance with an input signal from the outside. The opening and closing of the valve body is, for example, an old modular roll motor or recently a stepping motor or the like. The electric actuator 65a is operated in accordance with a control signal from the outside.
The cooling tower 60 has an opening 60b in the upper part, a casing 60a in which a tower bottom water tank 60c is provided in the lower part, a blower 60d provided in the opening 60b of the casing 60a, and a cooling water return provided in the casing 60a below the blower 60d. A sprinkler 60e connected to the side passage 61b, a filling 60f disposed in a casing 60a below the sprinkler 60e, and a louver 60g for taking in outside air provided in the casing 60a below the filling 60f. ing.

また、蒸発器54には、負荷側へ冷水を循環する冷水循環通路70が接続されている。冷水循環通路70は、負荷側への冷水往き側通路70aと負荷側からの冷水還り側通路70bとを備えている。冷水還り側通路70bには、冷水ポンプ(CP)71と水冷スクリューチラー冷水入口温度を計測する冷水入口温度計(TCR)72とが配置されている。
冷却水入口温度計(TCDS)63は、計測した水冷スクリューチラー冷却水入口温度を冷却水入口温度計測値として、冷水入口温度計(TCR)72は、計測した水冷スクリューチラー冷水入口温度を冷水入口温度計測値として、それぞれ出力信号を指示調節器(TIC)80に送る。
The evaporator 54 is connected to a cold water circulation passage 70 for circulating cold water to the load side. The chilled water circulation passage 70 includes a chilled water outgoing side passage 70a to the load side and a chilled water return side passage 70b from the load side. A chilled water pump (CP) 71 and a chilled water inlet thermometer (TCR) 72 for measuring the chilled water inlet temperature are disposed in the chilled water return side passage 70b.
The cooling water inlet thermometer (TCDS) 63 uses the measured water cooling screw chiller cooling water inlet temperature as a measured value of the cooling water inlet temperature, and the cooling water inlet thermometer (TCR) 72 uses the measured water cooling screw chiller cooling water inlet temperature as the chilled water inlet. Each output signal is sent to an indicating controller (TIC) 80 as a temperature measurement value.

指示調節器(TIC)80は、水冷スクリューチラー50の冷却水入口温度を、冷却水バイパス制御回路(調節部82)に入力されて設定される冷却水入口温度設定値と、冷却水入口温度計63の冷却水入口温度計測値との偏差を演算し、該偏差に応じた冷却水バイパス弁(MV)65の開度出力を冷却水バイパス弁(MV)65の電動アクチュエータ65aに指令として出力し、冷却水バイパス弁(MV)65の開度を調整し、常に冷却水入口温度設定値に近づけるように制御する。
指示調節器(TIC)80では、さらに、水冷スクリューチラー50の冷水入口温度として冷水入口温度計(TCR)72の冷水入口温度計測値がカスケード回路(演算部)81に入力され、カスケード回路(演算部)81では、冷水入口温度計測値に基づいて冷水入口温度計測値+Tα℃となる値を演算し、これを冷却水入口温度設定値として、冷却水バイパス制御回路(調節部)82の設定入力部へ出力し続ける。
The instruction controller (TIC) 80 includes a cooling water inlet temperature setting value that is set by inputting the cooling water inlet temperature of the water cooling screw chiller 50 to the cooling water bypass control circuit (control unit 82), and a cooling water inlet thermometer. 63 is calculated as a command to the electric actuator 65a of the cooling water bypass valve (MV) 65, and an opening degree output of the cooling water bypass valve (MV) 65 corresponding to the deviation is calculated. Then, the opening degree of the cooling water bypass valve (MV) 65 is adjusted and controlled so as to always approach the cooling water inlet temperature set value.
In the indication controller (TIC) 80, the measured value of the chilled water inlet temperature of the chilled water inlet thermometer (TCR) 72 is input to the cascade circuit (calculation unit) 81 as the chilled water inlet temperature of the water cooled screw chiller 50, and the cascade circuit (calculated value) is calculated. Part) 81 calculates a value that becomes the measured value of the chilled water inlet temperature + Tα ° C. based on the measured value of the chilled water inlet temperature, and uses this value as the cooling water inlet temperature setting value to set the input of the cooling water bypass control circuit (regulator) 82 Continue to output to the section.

つまり、指示調節器(TIC)80は、図2に示すように、冷水入口温度計(TCR)72が計測する水冷スクリューチラー冷水入口温度を、カスケード回路(演算部)81に入力し、カスケード回路(演算部)81に格納されている式TCDS]SP=TCR]PV+Tαに基づいて演算する。
式TCDS]SP=TCR]PV+Tα)に基づく演算値として、冷却水バイパス制御回路(調節部)82に冷却水入口温度設定値として出力し、冷却水バイパス制御回路(調節部)82では、カスケード回路(演算部)81から入力された冷却水入口温度設定値と、冷却水入口温度計63の冷却水入口温度計測値との偏差を演算し、該偏差に応じた冷却水バイパス弁(MV)65の開度出力を冷却水バイパス弁(MV)65の電動アクチュエータ65aに指令として出力し、冷却水バイパス弁(MV)65の開度を調整制御する。
式中、TCDS]SP:冷却水入口温度設定値、SPは設定の意味、TCR]PV:冷水入口温度計測値 PVは現状値の意味、Tα:設定差(制御系の分解能や時定数により決まる値)を表す。
That is, as shown in FIG. 2, the instruction controller (TIC) 80 inputs the water-cooled screw chiller cold water inlet temperature measured by the cold water inlet thermometer (TCR) 72 to the cascade circuit (calculation unit) 81, and the cascade circuit (Calculation unit) Calculate based on the expression TCDS] SP = TCR] PV + Tα stored in 81.
Formula TCDS] SP = TCR] PV + Tα) is output as a cooling water inlet temperature setting value to the cooling water bypass control circuit (regulation unit) 82 as a calculated value, and the cooling water bypass control circuit (regulation unit) 82 has a cascade circuit (Calculation unit) A deviation between the coolant inlet temperature set value input from 81 and the coolant inlet temperature measured value of the coolant inlet thermometer 63 is calculated, and a coolant bypass valve (MV) 65 corresponding to the deviation is calculated. Is output as a command to the electric actuator 65a of the cooling water bypass valve (MV) 65, and the opening degree of the cooling water bypass valve (MV) 65 is adjusted and controlled.
TCDS] SP: Cooling water inlet temperature set value, SP means setting, TCR] PV: Cooling water inlet temperature measured value PV means current value, Tα: Setting difference (determined by control system resolution and time constant Value).

図3は、Tα=1.0℃の場合の冷却水入口温度設定値を示す。
ここでは、カスケード回路(演算部)81に格納されている式TCDS]SP=TCR]PV+Tαに冷水入口温度計(TCR)72が計測した水冷スクリューチラー冷水入口温度20℃がある時点で入力された場合、水冷スクリューチラー冷却水入口温度の設定値を20℃+1.0℃=21℃として逐一カスケード回路から冷却水バイパス弁制御回路へ設定変更を行う、冷却水入口温度カスケード制御を行っていることを示している。
図3では、左側に水平になった線分があるが、水冷スクリューチラーの冷却水下限温度が設定下限値として与えられることを示し、冷水還り温度が15℃以下の場合は設定下限値16℃であるよう保つことの例を示す。また、右側に水平になった線分があるが、関東地方での夏ピークの外気湿球温度条件27℃であり、この時冷却塔の入口冷却水温34℃〜出口水温29℃の外気冷却ができることなどから、冷却水入口温度の設定上限値を35℃としている例を示している。
FIG. 3 shows the cooling water inlet temperature set value when Tα = 1.0 ° C.
Here, the formula TCDS] SP = TCR] PV + Tα stored in the cascade circuit (arithmetic unit) 81 is inputted at a time when the water-cooled screw chiller cold water inlet temperature measured by the cold water inlet thermometer (TCR) 72 is 20 ° C. In this case, the setting value of the water cooling screw chiller cooling water inlet temperature is set to 20 ° C. + 1.0 ° C. = 21 ° C., and the setting is changed from the cascade circuit to the cooling water bypass valve control circuit, and the cooling water inlet temperature cascade control is performed. Is shown.
In FIG. 3, although there is a horizontal line segment on the left side, it shows that the cooling water lower limit temperature of the water-cooled screw chiller is given as the setting lower limit value, and when the cold water return temperature is 15 ° C. or less, the setting lower limit value 16 ° C. Here is an example of how to keep it. Also, there is a horizontal line on the right side, but the summer peak outdoor air wet bulb temperature condition is 27 ° C in the Kanto region. At this time, the outside air cooling of the cooling tower at the inlet cooling water temperature of 34 ° C to the outlet water temperature of 29 ° C is performed. In view of this, an example is shown in which the upper limit value of the cooling water inlet temperature is set to 35 ° C.

図4は、冷却水バイパス弁(MV)65の開度を概念として示している。
この図では横軸を冷却水入口温度として取っていて、実際冷却水入口温度との図4のような関係を取るのだが、冷却水バイパス弁(MV)開度は、冷却水入口温度設定値と冷却水入口温度測定値との偏差の量に応じて0〜100%の開度を取る。冷却水入口温度設定値−冷却水入口温度測定値を偏差とすると、偏差0の場合、図4の傾きと縦軸0%との交点となり、偏差がマイナスの場合、その交点から右側の開度出力となる。偏差がプラスに大きくなっていくに従い、傾きを左に動いていく。このような相関で、冷却水バイパス弁制御回路から電動アクチュエータ65aへ冷却水バイパス弁(MV)65の開度信号を出力している。
FIG. 4 shows the opening degree of the cooling water bypass valve (MV) 65 as a concept.
In this figure, the horizontal axis is taken as the cooling water inlet temperature, and the relationship with the actual cooling water inlet temperature is as shown in FIG. 4, but the cooling water bypass valve (MV) opening degree is the cooling water inlet temperature setting value. And an opening of 0 to 100% depending on the amount of deviation between the measured value of the cooling water inlet temperature. If the deviation of cooling water inlet temperature set value-cooling water inlet temperature measurement value is zero, the deviation is zero, which is the intersection of the slope of Fig. 4 and the vertical axis of 0%. Output. As the deviation increases to a plus, the slope moves to the left. With such a correlation, an opening degree signal of the coolant bypass valve (MV) 65 is output from the coolant bypass valve control circuit to the electric actuator 65a.

図11に示す水冷スクリューチラー性能線図から明らかなように、水冷スクリューチラー冷水入口温度が低いほど、冷凍機の成績係数(運転効率)COPが高効率となり、水冷スクリューチラー冷水入口温度が高いほど、冷凍機の成績係数(運転効率)COPが低効率となることを示している。
すなわち、水冷スクリューチラー50の性能を高めるためには、水冷スクリューチラー冷水入口温度を低くして運転することが望ましいことを示している。
As is clear from the performance chart of the water-cooled screw chiller shown in FIG. 11, the lower the water-cooled screw chiller cold water inlet temperature, the higher the coefficient of performance (operating efficiency) COP of the refrigerator, and the higher the water-cooled screw chiller cold water inlet temperature. The performance coefficient (operating efficiency) COP of the refrigerator is low.
That is, in order to improve the performance of the water-cooled screw chiller 50, it is indicated that it is desirable to operate with the water-cooled screw chiller cold water inlet temperature lowered.

以上のように、本実施形態によれば、水冷スクリューチラー50の冷却水入口温度を水冷スクリューチラー50の冷水入口温度+Tα℃(例えば1.0℃)となるように冷却水バイパス弁(MV)65の開度を自動変更し、常に水冷スクリューチラー50の冷却水下限温度で運用させ、省エネルギーを図ることができる。
特に、データセンターや設備冷却水用のシステムにて冷水往き温度が一般空調用(例えば、5℃−12℃)と比較して、高温(例えば、13℃−20℃)の場合等に大きな省エネルギー効果が得られる。
As described above, according to the present embodiment, the cooling water inlet valve (MV) so that the cooling water inlet temperature of the water cooling screw chiller 50 becomes the cooling water inlet temperature of the water cooling screw chiller 50 + Tα ° C. (for example, 1.0 ° C.). The opening degree of 65 is automatically changed and always operated at the cooling water lower limit temperature of the water-cooled screw chiller 50, so that energy saving can be achieved.
In particular, when the temperature of the chilled water in a data center or equipment cooling water system is higher than that for general air conditioning (for example, 5 ° C to 12 ° C), the energy saving is large. An effect is obtained.

また、水冷スクリューチラー50の冷水還り温度が上昇した場合も自動で冷却水入口温度設定値を変更するため、冷却水入口温度を高めに(安全側)に設定しておく必要がなくなる。
また、構成機器は、冷却水入口温度計(TCDS)63、冷水入口温度計(TCR)72、指示調節器(TIC)80及び二方弁から成る冷却水バイパス弁(MV)65であるから、安価で且つ複雑な制御プログラムを必要としない。
Further, since the cooling water inlet temperature set value is automatically changed even when the cold water return temperature of the water cooling screw chiller 50 rises, it is not necessary to set the cooling water inlet temperature higher (safe side).
In addition, since the component devices are a cooling water inlet thermometer (TCDS) 63, a cooling water inlet thermometer (TCR) 72, an instruction regulator (TIC) 80, and a cooling water bypass valve (MV) 65 including a two-way valve, An inexpensive and complicated control program is not required.

次に、図5〜図7に基づいて、本実施形態に係る熱源システムを二次側冷水ポンプの制御が変流量制御の場合について説明する。
本例では、図1に示す熱源システムの冷却水循環通路70の熱負荷側の構成を、チラー定格800RTの生産機器や空調設備等の熱負荷91に対し、冷水冷水往き側通路70aに変流量制御の二次側冷水ポンプ90を配置している。
図5は、定格運転時の状態を示す図である。
例えば、定格運転時には、生産機器や空調設備等の熱負荷91が800RT、水冷スクリューチラー50が800RTとして運転される。そして、冷水冷水往き側通路70aに13℃の冷水が水冷スクリューチラー50から送り出され、変流量制御の二次側冷水ポンプ90から13℃の冷水が生産機器や空調設備等の熱負荷91に供給され、生産機器や空調設備等の熱負荷91から20℃の5,760L/minの冷水が冷水ポンプ(CP)71によって水冷スクリューチラー50に還される運転を行う。
Next, the case where the control of the secondary chilled water pump is the variable flow rate control in the heat source system according to the present embodiment will be described based on FIGS.
In this example, the heat flow side configuration of the cooling water circulation passage 70 of the heat source system shown in FIG. 1 is controlled to change the flow rate to the cold water / cold water going-side passage 70a with respect to the heat load 91 of a chiller rated 800RT production equipment or air conditioning equipment. The secondary side cold water pump 90 is arranged.
FIG. 5 is a diagram illustrating a state during rated operation.
For example, during rated operation, the heat load 91 such as production equipment and air conditioning equipment is operated as 800 RT, and the water-cooled screw chiller 50 is operated as 800 RT. Then, 13 ° C. chilled water is sent out from the water cooling screw chiller 50 to the chilled water chilled water going-side passage 70a, and the 13 ° C. chilled water is supplied from the secondary side chilled water pump 90 of variable flow rate control to the heat load 91 such as production equipment or air conditioning equipment. Then, an operation is performed in which 5,760 L / min of chilled water at 20 ° C. is returned to the water-cooled screw chiller 50 by a chilled water pump (CP) 71 from a heat load 91 such as production equipment or air conditioning equipment.

この運転では、冷水入口温度計(TCR)72から水冷スクリューチラー冷水入口温度計測値が20℃であることを、例えば電流値4〜20mAに割り付けて指示調節計(TIC)80に入力し、カスケード回路(演算部)81では入力された信号を温度値に置き換え、カスケード回路(演算部)81に格納されている式TCDS]SP=TCR]PV+Tαに冷水入口温度計(TCR)72が計測した水冷スクリューチラー冷水入口温度20℃を代入して、水冷スクリューチラー冷却水入口温度の設定値を20℃+1.0℃=21℃と演算した結果を、冷却水バイパス制御回路(調節部)82に出力し、冷却水バイパス制御回路(調節部)82では、その冷却水入口温度設定値21℃と、冷却水入口温度計(TCDS)63からの冷却水入口温度計測値との偏差を演算し、偏差量に応じて冷却水バイパス弁(MV)65の電動アクチュエータ65aを制御して弁体の開度を調節する。凝縮器52での冷却水温度差は5℃で運転されるので、水冷スクリューチラー50からの冷却水出口温度は26℃となる。   In this operation, from the chilled water inlet thermometer (TCR) 72, the measured value of the water cooled screw chiller chilled water inlet temperature is 20 ° C., for example, assigned to a current value of 4 to 20 mA and input to the indicating controller (TIC) 80, and cascaded. The circuit (arithmetic unit) 81 replaces the input signal with a temperature value, and the water cooling measured by the cold water inlet thermometer (TCR) 72 in the formula TCDS] SP = TCR] PV + Tα stored in the cascade circuit (arithmetic unit) 81 Substitute the screw chiller cold water inlet temperature 20 ° C, and output the calculated value of the water cooled screw chiller cooling water inlet temperature 20 ° C + 1.0 ° C = 21 ° C to the cooling water bypass control circuit (control unit) 82 In the cooling water bypass control circuit (control unit) 82, the cooling water inlet temperature set value 21 ° C. and the cooling water inlet temperature from the cooling water inlet thermometer (TCDS) 63 It calculates a deviation between the temperature measured value, and controls the electric actuator 65a of the cooling water bypass valve (MV) 65 for adjusting the opening of the valve body in accordance with the deviation amount. Since the cooling water temperature difference in the condenser 52 is operated at 5 ° C., the cooling water outlet temperature from the water-cooled screw chiller 50 is 26 ° C.

図6は、負荷が減少し、負荷率50%時の状態を示す図である。
ここで、負荷が減少し、負荷率50%になると、生産機器や空調設備等の熱負荷91が400RT、水冷スクリューチラー50が400RTとして運転される。そして、冷水冷水往き側通路70aに13℃の冷水が水冷スクリューチラー50から送り出され、変流量制御の二次側冷水ポンプ90から13℃の冷水が生産機器や空調設備等の熱負荷91に供給され、生産機器や空調設備等の熱負荷91から20℃の2,880L/minの冷水が冷水ポンプ(CP)71によって水冷スクリューチラー50に還される運転を行う。
FIG. 6 is a diagram illustrating a state in which the load decreases and the load factor is 50%.
Here, when the load decreases and the load factor reaches 50%, the heat load 91 such as the production equipment and the air conditioning equipment is operated as 400 RT, and the water-cooled screw chiller 50 is operated as 400 RT. Then, 13 ° C. chilled water is sent out from the water cooling screw chiller 50 to the chilled water chilled water going-side passage 70a, and the 13 ° C. chilled water is supplied from the secondary side chilled water pump 90 of variable flow rate control to the heat load 91 such as production equipment or air conditioning equipment. Then, an operation is performed in which 2,880 L / min of chilled water at 20 ° C. is returned to the water-cooled screw chiller 50 by a chilled water pump (CP) 71 from a heat load 91 such as production equipment or air conditioning equipment.

この運転では、冷水入口温度計(TCR)72が測定した水冷スクリューチラー冷水入口温度は20℃であるから、水冷スクリューチラー冷却水入口温度の設定値は定格運転時と同じく21℃である。
図7は、負荷が減少し、負荷率37.5%時の状態を示す図である。
さらに、負荷が減少し、負荷率37.5%になると、生産機器や空調設備等の熱負荷91が300RT、水冷スクリューチラー50が300RTとして運転される。そして、冷水往き側通路70aに13℃の冷水が水冷スクリューチラー50から送り出され、変流量制御の二次側冷水ポンプ90から13℃の冷水が生産機器や空調設備等の熱負荷91に供給され、生産機器や空調設備等の熱負荷91から20℃の2,160L/minの冷水が2次側冷水ポンプ90の搬送力により還りヘッダまで還される。
In this operation, since the water-cooled screw chiller cold water inlet temperature measured by the cold water inlet thermometer (TCR) 72 is 20 ° C., the set value of the water-cooled screw chiller cooling water inlet temperature is 21 ° C. as in the rated operation.
FIG. 7 is a diagram illustrating a state in which the load decreases and the load factor is 37.5%.
Further, when the load decreases and the load factor becomes 37.5%, the heat load 91 such as the production equipment and the air conditioning equipment is operated as 300 RT, and the water-cooled screw chiller 50 is operated as 300 RT. Then, 13 ° C. cold water is sent from the water-cooled screw chiller 50 to the cold water going-side passage 70a, and 13 ° C. cold water is supplied from the secondary-side cold water pump 90 with variable flow rate control to a heat load 91 such as production equipment or air conditioning equipment. Then, 2,160 L / min of chilled water at 20 ° C. is returned to the header by the conveying force of the secondary chilled water pump 90 from the heat load 91 of the production equipment or air conditioning equipment.

一般的に、冷凍機の蒸発器を流れる冷水は変流量対応冷凍機でも下限流量は定格流量の50%とする例が多いので、37.5%の負荷に応じた37.5%の熱負荷91からの還水量よりも冷凍機を流す流量が多いこととなり、ヘッダ間バイパスを流れる流量が50%−37.5%=12.5%発生する。これにより、ヘッダ間バイパス管92を介して13℃の720L/minの冷水が、生産機器や空調設備等の熱負荷91から20℃の2,160L/minの冷水と還りヘッダで合流し、還りヘッダでの混合温度は18.3℃になり、つまり水冷スクリューチラー冷水入口温度は18.3℃に低下し、2,880L/minの冷水が、冷水ポンプ(CP)71により水冷スクリューチラー50に還される。
そこで、冷水入口温度計(TCR)72から水冷スクリューチラー冷水入口温度計測値が18.3℃であると指示調節計(TIC)80に入力し、カスケード回路(演算部)81では、カスケード回路(演算部)81に格納されている式TCDS]SP=TCR]PV+Tαに冷水入口温度計(TCR)72が計測した水冷スクリューチラー冷水入口温度18.3℃を代入して、水冷スクリューチラー冷却水入口温度の設定値を18.3℃+1.0℃=19.3℃と演算した結果を、冷却水バイパス制御回路(調節部)82に出力し、冷却水バイパス制御回路(調節部)82では、その冷却水入口温度設定値19.3℃と、冷却水入口温度計(TCDS)63からの冷却水入口温度計測値との偏差を演算し、偏差量に応じて冷却水バイパス弁(MV)65の電動アクチュエータ65aを制御して弁体の開度を調節する。凝縮器52での冷却水温度差は5℃で運転されるので、水冷スクリューチラー50からの冷却水出口温度は24.3℃となる。
Generally, the cold water flowing through the evaporator of the refrigerator is a variable flow rate compatible refrigerator, so the lower limit flow rate is often 50% of the rated flow rate, so the heat load of 37.5% corresponding to the load of 37.5% The flow rate of flowing through the refrigerator is greater than the amount of return water from 91, and the flow rate of flowing through the bypass between headers is 50% -37.5% = 12.5%. As a result, 720 L / min chilled water at 13 ° C. is merged with 2,160 L / min chilled water at 20 ° C. from the heat load 91 such as production equipment and air conditioning equipment through the return header 92 through the header bypass pipe 92. The mixing temperature at the header is 18.3 ° C., that is, the water-cooled screw chiller cold water inlet temperature is lowered to 18.3 ° C., and 2,880 L / min of cold water is supplied to the water-cooled screw chiller 50 by the cold water pump (CP) 71. It will be returned.
Therefore, when the measured value of the temperature of the water-cooled screw chiller chilled water inlet from the chilled water inlet thermometer (TCR) 72 is 18.3 ° C., it is input to the indicating controller (TIC) 80, and the cascade circuit (arithmetic unit) 81 Substituting the water-cooled screw chiller cold water inlet temperature 18.3 ° C. measured by the cold water inlet thermometer (TCR) 72 into the formula TCDS] SP = TCR] PV + Tα stored in the computing unit 81), the water-cooled screw chiller cooling water inlet The result of calculating the temperature set value as 18.3 ° C. + 1.0 ° C. = 19.3 ° C. is output to the cooling water bypass control circuit (adjusting unit) 82, and in the cooling water bypass control circuit (adjusting unit) 82, The deviation between the cooling water inlet temperature setting value 19.3 ° C. and the cooling water inlet temperature measurement value from the cooling water inlet thermometer (TCDS) 63 is calculated, and the cooling water bypass valve is calculated according to the deviation amount. By controlling the electric actuator 65a of MV) 65 for adjusting the opening of the valve body. Since the cooling water temperature difference in the condenser 52 is operated at 5 ° C., the cooling water outlet temperature from the water-cooled screw chiller 50 is 24.3 ° C.

このように、水冷スクリューチラー50の冷水入口温度が低下すると、水冷スクリューチラー50の冷却水入口温度を低くすることができる。
次に、図8、図9に基づいて本実施形態に係る熱源システムを二次側冷水ポンプの制御が定流量制御の場合について説明する。
本例では、図1に示す熱源システムの冷却水循環通路70の負荷側の構成を、チラー定格800RTの生産機器や空調設備等の熱負荷94に対し、冷水冷水往き側通路70aに定流量制御の二次側冷水ポンプ93を配置している。
Thus, when the cold water inlet temperature of the water cooling screw chiller 50 falls, the cooling water inlet temperature of the water cooling screw chiller 50 can be lowered.
Next, the case where the control of the secondary side chilled water pump is the constant flow control in the heat source system according to the present embodiment will be described based on FIGS.
In this example, the configuration of the load side of the cooling water circulation passage 70 of the heat source system shown in FIG. 1 is controlled by the constant flow rate control in the cold water chilled water going-side passage 70a with respect to the heat load 94 of production equipment or air conditioning equipment having a chiller rating of 800RT. A secondary side cold water pump 93 is disposed.

図8は、定格運転時の状態を示す図である。
例えば、定格運転時には、生産機器や空調設備等の熱負荷94が800RT、水冷スクリューチラー50が800RTとして運転される。そして、冷水冷水往き側通路70aに13℃の冷水が水冷スクリューチラー50から送り出され、定流量制御の二次側冷水ポンプ93から13℃の冷水が生産機器や空調設備等の熱負荷94に供給され、生産機器や空調設備等の熱負荷94から20℃の5,760L/minの冷水が冷水ポンプ(CP)71によって水冷スクリューチラー50に還される運転を行う。
FIG. 8 is a diagram illustrating a state during rated operation.
For example, during rated operation, the heat load 94 of the production equipment or air conditioning equipment is operated at 800 RT, and the water-cooled screw chiller 50 is operated at 800 RT. Then, 13 ° C. chilled water is sent out from the water cooling screw chiller 50 to the chilled water chilled water going-side passage 70a, and 13 ° C. chilled water is supplied to the heat load 94 such as production equipment or air conditioning equipment from the secondary-side chilled water pump 93 of constant flow control. Then, an operation is performed in which 5,760 L / min of chilled water at 20 ° C. is returned to the water-cooled screw chiller 50 by a chilled water pump (CP) 71 from a heat load 94 such as production equipment or air conditioning equipment.

この運転では、冷水入口温度計(TCR)72から水冷スクリューチラー冷水入口温度計測値が20℃であると指示調節計(TIC)80に入力し、カスケード回路(演算部)81では、カスケード回路(演算部)81に格納されている式TCDS]SP=TCR]PV+Tαに冷水入口温度計(TCR)72が計測した水冷スクリューチラー冷水入口温度20℃を代入して、水冷スクリューチラー冷却水入口温度の設定値を20℃+1.0℃=21℃と演算した結果を、冷却水バイパス制御回路(調節部)82に出力し、冷却水バイパス制御回路(調節部)82では、その冷却水入口温度設定値21℃と、冷却水入口温度計(TCDS)63からの冷却水入口温度計測値との偏差を演算し、偏差量に応じて冷却水バイパス弁(MV)65の電動アクチュエータ65aを制御して弁体の開度を調節する。凝縮器52での冷却水温度差は5℃で運転されるので、水冷スクリューチラー50からの冷却水出口温度は26℃となる   In this operation, the chilled water inlet thermometer (TCR) 72 inputs the measured value of the water-cooled screw chiller chilled water inlet temperature to 20 ° C. to the indicating controller (TIC) 80, and the cascade circuit (arithmetic unit) 81 Substituting the water-cooled screw chiller cold water inlet temperature 20 ° C. measured by the cold water inlet thermometer (TCR) 72 into the formula TCDS] SP = TCR] PV + Tα stored in the calculation unit 81), the water cooling screw chiller cooling water inlet temperature The result of calculating the set value as 20 ° C. + 1.0 ° C. = 21 ° C. is output to the cooling water bypass control circuit (control unit) 82, and the cooling water bypass control circuit (control unit) 82 sets the cooling water inlet temperature. The deviation between the value 21 ° C. and the measured value of the cooling water inlet temperature from the cooling water inlet thermometer (TCDS) 63 is calculated, and the cooling water bypass valve (MV) 65 of the cooling water bypass valve (MV) 65 is calculated according to the deviation amount. By controlling the dynamic actuator 65a adjusts the opening degree of the valve body. Since the cooling water temperature difference in the condenser 52 is operated at 5 ° C., the cooling water outlet temperature from the water-cooled screw chiller 50 is 26 ° C.

図9は、負荷が減少し、負荷率50%時の状態を示す図である。
ここで、負荷が減少し、負荷率50%になると、生産機器や空調設備等の熱負荷94が400RT、水冷スクリューチラー50が400RTとして運転される。そして、冷水冷水往き側通路70aに13℃の冷水が水冷スクリューチラー50から送り出され、定流量の二次側冷水ポンプ93から13℃の冷水が生産機器や空調設備等の熱負荷に供給され、生産機器や空調設備等の熱負荷から16.5℃の5,760L/minの冷水が2次側冷水ポンプ90の搬送力により還りヘッダまで還される運転を行う。
FIG. 9 is a diagram illustrating a state in which the load decreases and the load factor is 50%.
Here, when the load decreases and the load factor reaches 50%, the heat load 94 such as the production equipment and the air conditioning equipment is operated as 400 RT, and the water-cooled screw chiller 50 is operated as 400 RT. Then, 13 ° C. chilled water is sent out from the water-cooled screw chiller 50 to the chilled water chilled water going-side passage 70a, and 13 ° C. chilled water is supplied from a constant-flow secondary-side chilled water pump 93 to a heat load such as production equipment or air conditioning equipment, An operation is performed in which 5,760 L / min of chilled water at 16.5 ° C. is returned to the header by the conveying force of the secondary chilled water pump 90 from the heat load of the production equipment or air conditioning equipment.

そこで、冷水入口温度計(TCR)72から水冷スクリューチラー冷水入口温度計測値が16.5℃であると指示調節計(TIC)80に入力し、カスケード回路(演算部)81では、カスケード回路(演算部)81に格納されている式TCDS]SP=TCR]PV+Tαに冷水入口温度計(TCR)72が計測した水冷スクリューチラー冷水入口温度16.5℃を代入して、水冷スクリューチラー冷却水入口温度の設定値を16.5℃+1.0℃=17.5℃と演算した結果を、冷却水バイパス制御回路(調節部)82に出力し、冷却水バイパス制御回路(調節部)82では、その冷却水入口温度設定値19.3℃と、冷却水入口温度計(TCDS)63からの冷却水入口温度計測値との偏差を演算し、偏差量に応じて冷却水バイパス弁(MV)65の電動アクチュエータ65aを制御して弁体の開度を調節する。凝縮器52での冷却水温度差は5℃で運転されるので、水冷スクリューチラー50からの冷却水出口温度は22.5℃となる。   Therefore, when the measured value of the water-cooled screw chiller chilled water inlet temperature is 16.5 ° C. from the chilled water inlet thermometer (TCR) 72, it is input to the indicating controller (TIC) 80, and the cascade circuit (arithmetic unit) 81 Substituting the water-cooled screw chiller cold water inlet temperature 16.5 ° C. measured by the cold water inlet thermometer (TCR) 72 into the formula TCDS] SP = TCR] PV + Tα stored in the computing unit 81), the water-cooled screw chiller cooling water inlet The result of calculating the temperature set value as 16.5 ° C. + 1.0 ° C. = 17.5 ° C. is output to the cooling water bypass control circuit (adjusting unit) 82, and in the cooling water bypass control circuit (adjusting unit) 82, The deviation between the cooling water inlet temperature setting value 19.3 ° C. and the cooling water inlet temperature measurement value from the cooling water inlet thermometer (TCDS) 63 is calculated, and the cooling water bypass valve is calculated according to the deviation amount. By controlling the electric actuator 65a of MV) 65 for adjusting the opening of the valve body. Since the cooling water temperature difference in the condenser 52 is operated at 5 ° C., the cooling water outlet temperature from the water-cooled screw chiller 50 is 22.5 ° C.

還りヘッダから水冷スクリューチラー50までは冷水ポンプ(CP)71の揚程で搬送するのだが、現実的には熱負荷が小さくなっても定格流量を二次側冷水ポンプ93及び冷水ポンプ(CP)71でずっと流し続けるのは得策ではなく、流量で複数に分割した二次側冷水ポンプ93及び冷水ポンプ(CP)71を台数制御することが多い。その場合、ヘッダ間バイパス管95を往きヘッダから還りヘッダへ一部の流量が流れる時期が発生し、その場合、還りヘッダで、冷水往き温度のままの冷水と、負荷側から昇温して還ってきた還り冷水の混合による還り冷水温度の低下はまま起きる。   From the return header to the water-cooled screw chiller 50, it is conveyed by the head of the chilled water pump (CP) 71. Actually, the rated flow rate is reduced even if the heat load is reduced, and the secondary chilled water pump 93 and the chilled water pump (CP) 71 are used. It is not a good idea to continue the flow at all times. In many cases, the number of secondary side cold water pumps 93 and cold water pumps (CP) 71 divided into a plurality of flow rates is controlled. In that case, there is a time when a part of the flow rate flows from the forward header to the return header through the inter-header bypass pipe 95. In this case, the return header raises the cold water at the chilled water temperature and returns from the load side by raising the temperature. The drop in the temperature of the return cold water due to the mixing of the return cold water still occurs.

このように、負荷減少によって、水冷スクリューチラー50の冷水入口温度は低下するため、水冷スクリューチラー50の冷却水入口温度を低くすることができる。
この水冷スクリューチラー50は、圧縮機インバータ制御のターボ冷凍機よりも小さい定格容量の汎用装置が市販されており、その圧縮機の特性から冷凍能力の部分負荷運転を、例えば25%程度までとても絞り込める。なおかつ、運転停止後の起動時間が例えば10分弱で定格温度まで冷水を冷凍できるなど、起動が速いという優れた特徴を有する。このため、夏期以外の中間期や冬期に冷房負荷がある熱負荷を有する熱源システムにおいて、中間期から冬期にかけて、冷水還り温度よりも低い湿球温度となる外気の冷熱を有効利用するため、大型の冷却塔での、冷凍サイクルを用いない外気によるフリークーリング熱源を併用する熱源システムが最近多用されてきているが、この熱源システムの冷水温度補償の冷凍サイクルを用いた補完熱源に最適なのが、水冷スクリューチラー50なのである。このように、水冷スクリューチラー50は、中間期から冬期にかけて、熱負荷へ循環させる熱媒体(冷水)の温度差の殆どの部分を、冷却塔による外気との熱交換で賄える時間が多いのだが、僅かに足りない冷水往き設定温度までの僅かな冷凍を、小さい装置容量で、さらに絞り運転に柔軟で、かつ停止起動に追従性の良い冷凍機である、という意味である。
Thus, since the cold water inlet temperature of the water-cooled screw chiller 50 is lowered due to the load reduction, the cooling water inlet temperature of the water-cooled screw chiller 50 can be lowered.
This water-cooled screw chiller 50 is commercially available as a general-purpose device with a smaller rated capacity than a compressor-inverter-controlled turbo chiller. Due to the characteristics of the compressor, the partial load operation of the refrigeration capacity is greatly reduced to, for example, about 25%. I can put it in. In addition, it has an excellent feature that the start-up is fast, for example, the start-up time after the operation is stopped is less than 10 minutes, and cold water can be frozen to the rated temperature. For this reason, in a heat source system having a heat load that has a cooling load in the intermediate period and winter season other than the summer season, the cold air of the wet air temperature that is lower than the cold water return temperature is effectively used from the intermediate season to the winter season. Recently, a heat source system that uses a free cooling heat source by outside air that does not use a refrigeration cycle has been widely used, but the most suitable heat source system is a complementary heat source that uses a chilled water temperature compensated refrigeration cycle. It is a water-cooled screw chiller 50. As described above, the water-cooled screw chiller 50 has much time to cover most of the temperature difference of the heat medium (cold water) circulated to the heat load from the intermediate period to the winter by heat exchange with the outside air by the cooling tower. This means that a slight refrigeration up to the set temperature of the slightly cold water going back is a refrigerator that has a small device capacity, is flexible in throttle operation, and has good follow-up performance in stopping and starting.

なお、上記実施形態では、水冷スクリューチラー50について説明したが、本発明はこれに限らず、容積圧縮型回転式の圧縮機、即ち、ロータリー型、スクロール型、スクリュー型の圧縮機を備える冷凍機であれば良い。
また、上記実施形態では、開放型の冷却塔60を用いた場合について説明したが、本発明はこれに限らず、例えば、密閉型の冷却塔であっても良い。
In the above embodiment, the water-cooled screw chiller 50 has been described. However, the present invention is not limited to this, and a volume compression type rotary compressor, that is, a refrigerator having a rotary type, scroll type, screw type compressor. If it is good.
Moreover, although the said embodiment demonstrated the case where the open type cooling tower 60 was used, this invention is not limited to this, For example, a closed type cooling tower may be sufficient.

50 水冷スクリューチラー
51 スクリュー型圧縮機
52 凝縮器
53 絞り装置(膨張弁等)
54 蒸発器
60 冷却塔
61 冷却水循環通路
61a 冷却水往き側通路
61b 冷却水還り側通路
62 冷却水ポンプ
63 冷却水入口温度計(TCDS
64 バイパス通路
65 冷却水バイパス弁(MV)
65a 電動アクチュエータ
70 冷水循環通路
70a 冷水往き側通路
70b 冷水還り側通路
71 冷水ポンプ(CP)
72 冷水入口温度計(TCR
80 指示調節器(TIC)
81 カスケード回路(演算部)
82 冷却水バイパス制御回路(調節部)
50 Water-cooled screw chiller 51 Screw type compressor 52 Condenser 53 Throttle device (expansion valve, etc.)
54 Evaporator 60 Cooling Tower 61 Cooling Water Circulation Passage 61a Cooling Water Outward Passage 61b Cooling Water Return Side Passage 62 Cooling Water Pump 63 Cooling Water Inlet Thermometer (T CDS )
64 Bypass passage 65 Cooling water bypass valve (MV)
65a Electric actuator 70 Chilled water circulation passage 70a Chilled water outgoing side passage 70b Chilled water return side passage 71 Chilled water pump (CP)
72 Cold water inlet thermometer (T CR )
80 Indicator controller (TIC)
81 Cascade circuit (calculation unit)
82 Cooling water bypass control circuit (regulator)

Claims (5)

容積圧縮型回転式の圧縮機、水冷方式の凝縮器、絞り装置及び蒸発器を備え冷凍サイクルを構成する水冷冷凍機と、
大気と冷却水とを熱交換する冷却塔と、
前記冷却塔に一端を接続し冷却水ポンプ及び冷却水入口温度計の順に配置し、他端を前記凝縮器に接続する冷却水往き側通路と、前記凝縮器に一端を接続し他端を前記冷却塔に接続する冷却水還り側通路と、前記冷却水往き側通路の前記冷却水ポンプ吸込み側と前記冷却水還り側通路との間を冷却水バイパス弁を介して接続するバイパス通路とを有する冷却水循環通路と、
負荷側への冷水往き側通路と前記負荷側からの冷水還り側通路とを有し、前記冷水還り側通路に冷水ポンプ及び冷水入口温度計を配置し、前記蒸発器に連絡する冷水循環通路と、
前記冷却水入口温度計の冷却水入口温度計測値に基づいて設定冷却水入口温度との偏差を演算し、該偏差に応じた前記冷却水バイパス弁の開度出力をする冷却水バイパス制御回路を有する指示調節器を
備え、
前記指示調節器には、前記設定冷却水入口温度を、前記冷水入口温度計の計測値に基づいて、前記冷水入口温度計測値+Tα℃となる値として前記冷却水バイパス制御回路の設定値として出力するカスケード回路を備える
ことを特徴とする熱源システム。
A water-cooled refrigerator comprising a volumetric compression type rotary compressor, a water-cooled condenser, a throttling device and an evaporator, and constituting a refrigeration cycle;
A cooling tower for exchanging heat between the atmosphere and cooling water;
One end is connected to the cooling tower and arranged in the order of a cooling water pump and a cooling water inlet thermometer, the other end is connected to the condenser, and the other end is connected to the condenser and the other end is connected to the condenser. A cooling water return side passage connected to the cooling tower, and a bypass passage connecting the cooling water pump suction side of the cooling water outgoing side passage and the cooling water return side passage via a cooling water bypass valve. A cooling water circulation passage,
A cold water return passage from the load side and a cold water return passage from the load side, a cold water pump and a cold water inlet thermometer are arranged in the cold water return passage, and a cold water circulation passage communicating with the evaporator ,
A cooling water bypass control circuit that calculates a deviation from a set cooling water inlet temperature based on a measured value of the cooling water inlet temperature of the cooling water inlet thermometer and outputs an opening degree of the cooling water bypass valve according to the deviation. With an indicating regulator having
Based on the measured value of the cold water inlet thermometer, the set regulator water temperature is output as a set value of the cooling water bypass control circuit to the instruction controller as a value that becomes the measured value of the cold water inlet temperature + Tα ° C. A heat source system comprising a cascade circuit.
請求項1記載の熱源システムにおいて、
前記冷水循環通路には、前記冷水還り側通路の前記冷水ポンプ吸い込み側に還りヘッダと、前記冷水往き側通路に往きヘッダと、前記還りヘッダと前記往きヘッダとの間にヘッダ間バイパス管とを備え、負荷側の熱負荷が小さくなると前記ヘッダ間バイパス管を冷水が流れる
ことを特徴とする熱源システム。
The heat source system according to claim 1,
The cold water circulation passage includes a return header on the cold water pump suction side of the cold water return side passage, a forward header on the cold water forward side passage, and an inter-header bypass pipe between the return header and the forward header. A heat source system, wherein cold water flows through the inter-header bypass pipe when the load-side heat load is reduced.
請求項1又は2記載の熱源システムにおいて、
前記容積圧縮型回転式の圧縮機は、ロータリー型圧縮機、スクロール型圧縮機又はスクリュー型圧縮機である
ことを特徴とする熱源システム。
The heat source system according to claim 1 or 2,
The volumetric compression type rotary compressor is a rotary type compressor, a scroll type compressor, or a screw type compressor.
請求項1乃至3の何れか記載の熱源システムにおいて、
前記負荷は、高温冷水を要求する空調設備又は生産機器冷却用の熱源設備であって、冷水の還り温度が前記水冷冷凍機の冷却水入口下限温度を上回る場合がある
ことを特徴とする熱源システム。
The heat source system according to any one of claims 1 to 3,
The load is a heat source facility for cooling air-conditioning equipment or production equipment that requires high-temperature cold water, and the return temperature of the cold water may exceed the cooling water inlet lower limit temperature of the water-cooled refrigerator. .
請求項4記載の熱源システムにおいて、
前記空調設備は、データセンターの空調設備である
ことを特徴とする熱源システム。
The heat source system according to claim 4, wherein
The heat source system, wherein the air conditioning equipment is a data center air conditioning equipment.
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JP2018015727A (en) * 2016-07-28 2018-02-01 トヨタ紡織株式会社 Sediment removal device and coolant circulation system including the same
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