CN1573259A - Three functions absorption type refrigerating apparatus - Google Patents
Three functions absorption type refrigerating apparatus Download PDFInfo
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- CN1573259A CN1573259A CNA2004100465927A CN200410046592A CN1573259A CN 1573259 A CN1573259 A CN 1573259A CN A2004100465927 A CNA2004100465927 A CN A2004100465927A CN 200410046592 A CN200410046592 A CN 200410046592A CN 1573259 A CN1573259 A CN 1573259A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract
To make simplified, reduced in cost and improvable in reliability the dilute solution supply flow quantity control such as the control of the revolution speed of a solution pump to prevent fluctuation of a liquid level in a high-temperature re-generator or the like. This triple effect absorption refrigerating device is provided with a condenser 3, an absorber 2, an evaporator 1, three re-generators 4, 5 and 6 of high-temperature, middle-temperature and low-temperature, and three solution heat exchangers 7, 8 and 9, and it is constituted so that absorbed liquid from the absorber 2 is supplied to, at least, the high-temperature re-generator 4 and the middle-temperature re-generator 5 through a solution pump 26, and refrigerant steam generated in the high-temperature side re-generators 4 and 5 is led into the low-temperature side re-generators 5 and 6 in order, and used as a heating source of the low-temperature side re-generators 5 and 6. The dilute solution inlet of the middle-temperature re-generator 5 is provided with a dilute solution flow-in quantity control means to separately control a liquid level of the middle-temperature re-generator 5 from a liquid level of the high-temperature re-generator 4.
Description
Technical field
The present invention relates to a kind of triple function absorption type refrigerating units with the different successively high temperature of operating temperature from high temperature to low temperature, middle temperature, 3 generators of low temperature.
Background technology
Generally, absorption type refrigerating unit is an inscape with condenser, evaporimeter, absorber, generator, solution heat exchanger, be connected these each inscapes with refrigerant piping by the solution pipe arrangement and make its periodic duty successively, constitute absorption freezing circulation.
In this absorption type refrigerating unit, will heat to concentrate at above-mentioned generator in the weak solution that above-mentioned absorber generates and make it be regenerated as absorption liquid (concentrated solution), and make it be back to above-mentioned absorber.On the other hand, make at above-mentioned generator the refrigerant vapour that the weak solution heating concentrates generation is formed liquid refrigerant in above-mentioned condenser condenses, make this liquid refrigerant simultaneously in above-mentioned evaporator evaporation.Make herein the refrigerant vapour that produces be absorbed by concentrated solution and generate weak solution at above-mentioned absorber once more.And,, realize the cycle period of above-mentioned absorbent solution and cold-producing medium by this process repeatedly.
And, the heat of evaporation of the cold-producing medium in above-mentioned evaporimeter can be waited Cooling and Heat Source and the effectively utilization that needs as refrigeration.
On the other hand, in this absorption type refrigerating unit, as a method that improves its energy-efficient performance, for example, the high temperature that the operating temperature of setting from high temperature to low temperature is different successively, middle temperature, 3 generators of low temperature, the refrigerant vapour that will generate by the heating of the high temperature side generator of at high temperature working imports the low temperature side generator of working at low temperatures successively, used as the heating source of low temperature side generator.On the other hand, at weak solution pipe arrangement midway from above-mentioned absorber to above-mentioned high temperature side generator, corresponding low temperature, middle temperature, 3 solution heat exchangers of high temperature of being provided with above-mentioned each generator,
By the low temperature absorption liquid (weak solution) of the effective heating of these 3 solution heat exchangers from above-mentioned absorber.
According to this structure, the absorption liquid (weak solution) that can utilize the temperature of the refrigerant vapour that is back to the absorber side will finish after the absorption concentrates by stages and with the good thermal efficiency, so can effectively be reduced in the needed heat that adds of each generator, realize energy-conservation.And, improve cycle efficieny, improve COP.
; the absorption type refrigerating unit that has many generators as mentioned above; from the multistage utilize the cycle characteristics of heat to consider; be the HTHP system eventually; interior pressure (saturation temperature of solution) particularly in order to improve high-temperature generator; liquid level sensor is set so that the steam of high-temperature generator does not pass the solution pipe arrangement in high-temperature generator outlet, and regulates the influx of supplying with high-temperature generator or discharge can regulate liquid level.Recently, frequency that regulate to supply with the driving power of the solution pump mode of controlling influx increases.
But, utilize the liquid level of the signal detection high-temperature generator of liquid level sensor like this, adjust the supply frequency of solution pump rotary drive unit, can prevent that by regulating the influx of supplying with high-temperature generator steam from passing, but because liquid level is sharply change, so cause frequency variation to become big, it is big that the change of the pump head of solution pump (pumphead) (lift) becomes, and the influx that causes warm generator in the supply is change simultaneously also, therefore in the level control of warm generator become unstable easily.And, because changing freezing output, the flow of solution circulation also changes, have cold water temperature and produce problems such as change.
Therefore, following triple function absorption type refrigerating unit is proposed, refrigerant vapour export department at above-mentioned high-temperature generator is provided with pressure sensor, the concentrated solution export department of this high-temperature generator and above-mentioned in liquid level sensor is set in the concentrated solution outlet pathway of warm generator respectively, be output as the basis with above-mentioned pressure sensor, set from the basic rotary speed of absorber to the solution pump of high-temperature generator delivered solution.On the other hand, revise the rotary speed of the solution pump that sets, the liquid level of high temperature, middle each generator of temperature is maintained desired height (with reference to patent documentation 1) by the output that utilizes above-mentioned each liquid level sensor.
According to this structure, can utilize the fundamental quantity of recurrent state value (pressure, saturation temperature etc.) the setting solution internal circulating load of high-temperature generator to turn round, so can accomplish stable running, and owing to can maintain desired height to the liquid level of high temperature, each generator of low temperature, pass so can prevent the steam separately of high-temperature generator and middle temperature generator, can bring into play the efficient of heat exchanger to greatest extent.
In addition, triple function absorption type refrigerating units of following structure are also proposed, as mentioned above, in absorption type refrigerating unit, be provided with following 3 solution pumps: will supply with the weak solution pump of above-mentioned cryogenerator by the weak solution that absorption liquid absorption refrigeration agent is obtained with low temperature, middle temperature, 3 generators of high temperature; Will above-mentioned cryogenerator weak solution is heated the intermediate solution that concentrates and obtain supply with above-mentioned in the intermediate solution pump of warm generator; To in above-mentioned, heat the concentrated solution pump that the concentrated solution that concentrates and obtain is supplied with above-mentioned high-temperature generator to middle solution by warm generator, utilize above-mentioned intermediate solution pump only will the solution amount of the requirement ratio of the intermediate solution that above-mentioned cryogenerator obtains supply with above-mentioned in warm generator, and make remaining intermediate solution return absorber, and, utilize the solution amount of the requirement ratio that above-mentioned concentrated solution pump only will the concentrated solution that warm generator obtains in above-mentioned to supply with above-mentioned high-temperature generator, and make remaining concentrated solution return absorber, and, detect the high-temperature generator pressure inside, temperature and liquid capacity, make the rotating speed of the pump of absorption liquid circulation according to this testing result adjustment, thereby control absorption liquid internal circulating load (with reference to patent documentation 2).
According to this structure, can reduce the ratio of the absorption liquid that makes the high-temperature generator circulation, raise the efficiency easily.In addition, even load has under the situation of change, also can under stable status, carry out the liquid capacity control of high-temperature generator.
But, the structure of above-mentioned patent documentation 1, according to the pressure of high-temperature generator side and high-temperature generator side and in the rotating speed of output control solution pump of each liquid level sensor of warm generator side, only according to the rotating speed that with the pressure of high-temperature generator is the solution pump of parameter carry out high-temperature generator and in the control of two liquid levels of warm generator, so be difficult to accomplish stable control, can not corresponding rapid load change.And, since be according in the rotating speed of output calibration solution pump of warm generator side liquid level control the structure of the flow of warm generator in the supply, so the complex structure of control system and cost height.
On the other hand, the structure of above-mentioned patent documentation 2 needs 3 solution pumps, and controls these pumps when being equal to according to high-temperature generator pressure inside, temperature and liquid capacity, so the hardware and software structure is all complicated, and cost is very high
Summary of the invention
The objective of the invention is, a kind of triple function absorption type refrigerating unit is provided, its weak solution that constitutes the device of self-absorption is in the future supplied with high-temperature generator or high-temperature generator and middle temperature generator directly or indirectly at least, detect the liquid level of high-temperature generator and control weak solution supply flow rate (rotating speed of solution pump etc.), on the other hand, at the weak solution of middle temperature generator inlet weak solution influx control module is set also and controls the weak solution amount, can utilize the simple and stable control of low-cost configuration to supply with the liquid inventory of high-temperature generator thus, supply with the liquid inventory of high-temperature generator and middle temperature generator.
In order to reach this purpose, the present invention constitutes has the following apparatus that solves problem.
Triple function absorption type refrigerating units according to claim 1 have: condenser 3; Absorber 2 and evaporimeter 1; High temperature, middle temperature, 3 generators of low temperature 4,5,6; With 3 solution heat exchangers 7,8,9, to supply with above-mentioned high-temperature generator 4 and middle temperature generator 5 at least by solution pump 26 from the weak solution of above-mentioned absorber 2, to import low temperature side generator 5,6 successively at the refrigerant vapour that above-mentioned high temperature side generator 4,5 produces simultaneously, be used as the heating source of each generator 5,6 of this low temperature side.And, the weak solution of warm generator 5 inlet in above-mentioned, be provided with detect above-mentioned in the liquid level position of warm generator 5 and control supply with above-mentioned in the weak solution influx control module of weak solution influx of warm generator 5, make it possible to independent control above-mentioned in the liquid level position of warm generator 5 and the liquid level position of above-mentioned high-temperature generator 4.
According to this structure, the liquid level position of warm generator 5 and the liquid level position of high-temperature generator 4 irrespectively kept certain during the weak solution influx control module of warm generator 5 sides made in the utilization, so only control the liquid level of high-temperature generator 4 sides gets final product according to the rotating speed of solution pump 26, the structure of control device is become simply, improve reliability.
Triple function absorption type refrigerating units according to claim 2 are in the described structure of claim 1, and weak solution influx control module is by constituting with the lower part: the level detection sensor of the liquid level position of warm generator 5 in the detection; According to the influx of the weak solution of warm generator 5 in the detection signal adjusting supply of this level detection sensor, so that the liquid level position of middle temperature generator 5 reaches certain motor-driven valve.
According to this structure, utilize the level detection sensor of the liquid level position of warm generator 5 in detecting, and motor-driven valve, this motor-driven valve is regulated the influx of the weak solution of warm generator 5 in the supply according to the detection signal of this level detection sensor, so that the liquid level position of middle temperature generator 5 reaches necessarily, the liquid level position of the liquid level of warm generator 5 and high-temperature generator 4 irrespectively keeps certain in making.
Triple function absorption type refrigerating units according to claim 3 have: condenser 3; Absorber 2 and evaporimeter 1; High temperature, middle temperature, 3 generators of low temperature 4,5,6; With 3 solution heat exchangers 7,8,9, to supply with above-mentioned high-temperature generator 4 and middle temperature generator 5 at least by solution pump 26 from the weak solution of above-mentioned absorber 2, to import low temperature side generator 5,6 successively at the refrigerant vapour that above-mentioned high temperature side generator 4,5 produces simultaneously, be used as the heating source of each generator 5,6 of this low temperature side.And, the weak solution of warm generator 5 inlet is provided with liquid level position control ball-cock assembly FV in above-mentioned, control above-mentioned in the liquid level position of warm generator 5, outlet side at above-mentioned high-temperature generator 4 is provided with level detection sensor LS1, LS2 simultaneously, control the driving rotating speed of above-mentioned solution pump 26, so that the liquid level position of above-mentioned high-temperature generator 4 keeps certain.
According to this structure, the weak solution of warm generator 5 inlet is provided with ball-cock assembly FV in above-mentioned, utilize this ball-cock assembly FV make in the liquid level of warm generator 5 and the liquid level position of above-mentioned high-temperature generator 4 irrespectively keep certain, so only control the liquid level of high-temperature generator 4 gets final product according to the rotating speed of solution pump 26, the structure of control device is become simply, improve reliability.
Triple function absorption type refrigerating units according to claim 4 are in the described structure of claim 3, temperature sensor TS with the temperature that detects high-temperature generator 4, set basic rotating speed according to the detected temperatures of this temperature sensor TS to the solution pump 26 of high-temperature generator 4 delivered solution, carrying out rotating speed according to the output of the liquid level sensor LS1, the LS2 that are located at high-temperature generator 4 outlet sides proofreaies and correct, if liquid level position height then reduce rotating speed is if liquid level position is low then improve rotating speed.
According to this structure, can turn round according to the basic value that the recurrent state value of high-temperature generator is set the solution internal circulating load, accomplish steady running.And, can easy corresponding load change.
Triple function absorption type refrigerating units according to claim 5 are in claim 1,2,3 or 4 described structures, and the weak solution of the device of self-absorption in the future 2 is supplied with high-temperature generator 4 and middle temperature generator 5 side by side.
At least supply with the supply method of high-temperature generator 4 and middle temperature generator 5 as the weak solution of self-absorption in future device 2, can consider various endless form, as one of them mode, can adopt from absorber 2 directly to high-temperature generator 4 and warm generator 5 supply with the supply modes of weak solutions side by side.
Triple function absorption type refrigerating units according to claim 6 are in claim 1,2,3 or 4 described structures, and the weak solution of the device of self-absorption in the future 2 is supplied with high-temperature generator 4 and middle temperature generator 5 side by side by cryogenerator 6.
At least supply with the supply method of high-temperature generator 4 and middle temperature generator 5 as the weak solution of self-absorption in future device 2, can consider various endless form, wherein can adopt the weak solution of self-absorption device 2 in the future to supply with the supply mode of high-temperature generator 4 and middle temperature generator 5 indirectly side by side by cryogenerator 6.
As mentioned above, according to triple function absorption type refrigerating units of the present invention, can form simple and low-cost configuration, and can suitably control the liquid inventory of supplying with high-temperature generator or supply with high-temperature generator respectively and the liquid inventory of middle temperature generator, when even load change is arranged, also can guarantee stable behavior in service, keep certain refrigerating capacity.
Description of drawings
Fig. 1 is the summary construction diagram of structure of triple function absorption type refrigerating units of expression embodiments of the present invention 1.
Fig. 2 is the summary construction diagram of major part of other topology examples (the 1st example) in expression absorption cycle of being suitable for triple function absorption type refrigerating units of the present invention.
Fig. 3 is the summary construction diagram of major part of other topology examples (the 2nd example) in expression absorption cycle of being suitable for triple function absorption type refrigerating units of the present invention.
Fig. 4 is the summary construction diagram of major part of other topology examples (the 3rd example) in expression absorption cycle of being suitable for triple function absorption type refrigerating units of the present invention.
Fig. 5 is the summary construction diagram of major part of other topology examples (the 4th example) in expression absorption cycle of being suitable for triple function absorption type refrigerating units of the present invention.
Symbol description
1 evaporimeter; 2 absorbers; 3 condensers; 4 high-temperature generators; Warm generator in 5; 6 cryogenerators; 7 cryogenic fluid heat exchangers; Warm solution heat exchanger in 8; 9 high-temperature solution heat exchangers; The rotary drive unit of 10 solution pumps; 16 control panels; 17 fuel gas open and close control valves; 19 air blasts; 26 solution pumps; 26a the 1st solution pump; 26b the 2nd solution pump; 38 gas-liquid separators; 41 containers; 43 gas burners as heating source; FS level detection sensor; F1, F2 the 1st, the 2nd level detection electrode bar; The TS temperature detection sensor.
The specific embodiment
＜embodiment 1 〉
Below, the structure of triple function absorption type refrigerating units of embodiments of the present invention 1 is described with reference to Fig. 1.
The absorption type refrigerating unit that this embodiment relates to constitutes triple function absorption type refrigerating units, for example be cold-producing medium, be absorption liquid with lithium bromide (LiBr) with water, be used to refrigerant vapour from the high-temperature generator side this absorption liquid (weak solution) after with absorption and effectively concentrate in three stages, can effectively reduce the needed heat that adds of high-temperature generator.In following example, at least 1 condenser, at least 1 absorber and at least 1 evaporimeter relatively, connect 3 the different successively generators of operating temperature that make high temperature, middle temperature, low temperature by stages, constitute the cycle period (absorption freezing cycle) of cold-producing medium and absorption liquid.
The basic structure and the effect of this absorption type refrigerating unit at first, are described according to Fig. 1.Evaporimeter 1 has: the heat exchanger 12 by the liquid that is cooled (making water) We in container 11; With the cold-producing medium disperser 13 of decentralized system cryogen (water) R4 on this heat exchanger 12, cooling flows into and the liquid that is cooled (making water) We by the heat exchanger 12 in this evaporimeter 1 from the liquid pipe arrangement 14 of being cooled.In addition, though omit diagram, the unevaporated liquid refrigerant R4 above-mentioned evaporimeter 1 bottom in is by the refrigerant piping of regulation, is drawn into cold-producing medium disperser 13 sides of upper side successively via the refrigerated medium pump of stipulating, is dispersed on the above-mentioned heat exchanger 12.
Supply with cooling water Wa from cooling water pipe 24 to heat exchange department 22, remove the absorption heat that in above-mentioned absorber 2, produces.And this cooling water Wa also supplies with the heat exchange department 32 of condenser 3 sides described later from this heat exchange department 22, with removing condensation heat (omitting the diagram connecting portion).
On the other hand, the above-mentioned high temperature that this absorption type refrigerating unit uses, middle temperature, 3 generators 4 of low temperature, 5,6 will be divided into high temperature at the weak solution L5 after above-mentioned absorber 2 finishes absorption respectively, middle temperature, three stages of low temperature, and heat concentrated with the good thermal efficiency, successively as the concentrated solution L1～L3 (L1+L2+L3=L4) of high concentration, save the needed heat that adds of generator as much as possible, obtain energy-saving effect, this weak solution L5 passes through weak solution pipe arrangement 25 from above-mentioned absorber 2 according to diagram, 36, via solution pump 26 with converter (inverter) rotary drive unit 10, imported high-temperature generator 4 and the middle temperature generator 5 that has as the gas burner 43 of heating source side by side, and be generated as high temperature, middle temperature.In addition, as hereinafter described, at above-mentioned weak solution pipe arrangement 25,36 midway, with illustrated configuration relation be provided with the weak solution L5 in this weak solution pipe arrangement 25,36 by stages from low-temperature heat be high temperature low temperature, temperature, 3 solution heat exchangers of high temperature 7,8,9.
Promptly, in this embodiment, cryogenic fluid heat exchanger 7, high-temperature solution heat exchanger 9 are located at from the upstream and downstream of the weak solution pipe arrangement 25 of the inlet that exports to high-temperature generator 4 of absorber 2, and middle temperature solution heat exchanger 8 is located between these cryogenic fluid heat exchangers 7 and the high-temperature solution heat exchanger 9, and be provided in a side of be branched in warm generator 5 sides weak solution pipe arrangement 36 midway.In addition, the intake section of middle temperature generator 5 sides in this weak solution pipe arrangement 36, be provided with according to diagram and utilize ball float F to carry out floater controlled valve (the floating valve) FV of open and close controlling, this floater controlled valve FV by be located at above-mentioned in the liquid level position of ball float F in the container 51 of warm generator 5 change corresponding lifting action and carry out the mechanical type open and close controlling, so that with level control is the liquid level position of specified altitude, regulate the weak solution flow of supplying with in this container 51, its liquid level is remained on specified altitude.
Above-mentioned high-temperature generator 4 for example is made of full-liquid type fire-cylinder fire tube boiler, has not shown heat pipe and as the gas burner 43 in predetermined heating source, utilize its flame 43a to make the weak solution L5 that generates at above-mentioned absorber 2, heat concentrated at the heat transfer boiling in ducts.Generate the concentrated solution L1 of the 1st concentration (%) thus, generate simultaneously the 1st saturation temperature T1 (℃) refrigerant vapour R1.The concentrated solution L1 of the 1st concentration of the highest temperature that generates at this high-temperature generator 4 and the refrigerant vapour R1 of the 1st saturation temperature are imported in the gas-liquid separator 38 by passage 42.And, in this gas-liquid separator 38, be separated from each other, the concentrated solution L1 of the 1st concentration is by the absorption liquid disperser 23 of pyrosol pipe arrangement 27 supply absorbers 2, and the refrigerant vapour R1 of the 1st saturation temperature is imported into the middle temperature generator 5 of back by high temperature refrigerant steam pipe arrangement 28.In addition, symbol 19 is air blasts of gas burner 43 usefulness.
In have solution heating unit (heat pipe) 52 in the container 51 of warm generator 5.Solution heating unit (heat pipe) 52 be according to top described, the 1st saturation temperature T1 of the highest temperature that will generate at high-temperature generator 4 (℃) refrigerant vapour R1 import by high temperature refrigerant steam pipe arrangement 28, and as thermal source.In warm generator 5 utilize this solution heating unit 52, will concentrate by the heating that the weak solution from absorber 2 that above-mentioned cryogenic fluid heat exchanger 7, middle temperature solution heat exchanger 8 supplied with is carried out second stage.Generate the concentrated solution L2 of the 2nd concentration (%) thus, generate simultaneously the 2nd saturation temperature T2 (℃) refrigerant vapour R2.The concentrated solution L2 of above-mentioned the 2nd concentration that warm generator 5 generates in this is imported into the cryogenerator 6 of final stage by middle temperature solution pipe arrangement 30.
(the refrigerant vapour R2 of the 2nd saturation temperature T2 that will generate at middle temperature generator 5 imports by middle temperature refrigerant vapour pipe arrangement 29 to have solution heating unit (heat pipe) 62 in the container 61 of cryogenerator 6, and as thermal source), utilize this solution heating unit 62, the concentrated solution L2 of the 2nd concentration that will import from above-mentioned the 2nd generator 5 carries out the heating of phase III (final stage) and concentrates.Generate the concentrated solution L3 of the 3rd concentration (%) be higher than above-mentioned the 2nd concentration thus, generate simultaneously be lower than above-mentioned the 2nd temperature T 2 (℃) the 3rd saturation temperature T3 (℃) refrigerant vapour R3.
The concentrated solution L3 of the 3rd concentration that generates at this cryogenerator 6 is imported into above-mentioned absorber 2 once more by cryogenic fluid pipe arrangement 35, and disperses from above-mentioned absorption liquid disperser 23.
But in this embodiment, as mentioned above, high-temperature generator 4 adopts full-liquid type fire-cylinder fire tube boiler structures, across passage 42 gas-liquid separator 38 is set independently at the outlet side of its container (body) 41.Housing section at this gas-liquid separator 38 is provided with level detection sensor FS, and this level detection sensor FS is by constituting with the lower part: the 1st level detection electrode bar F1 in this high liquid level H position of the position probing corresponding with the high liquid level H of concentrated solution L1; Should hang down the 2nd level detection electrode bar F2 of liquid level L position in the position probing corresponding equally with the low liquid level L of concentrated solution L1; With common electrode rod Fc.Whether the liquid level that above-mentioned the 1st, the 2nd level detection electrode bar F1, the F2 of this level detection sensor FS detects respectively in the above-mentioned gas-liquid separator 38 surpasses high liquid level H position or is lower than liquid level L position, with the micro computer of this detection signal input control panel 16.
Like this, control panel 16 is according to this detection signal, for example when the liquid level of reality surpasses above-mentioned high liquid level H position (the 1st level detection electrode bar F1 exports H), reduce the rotating speed of the rotary drive unit 10 of above-mentioned solution pump 26, reduce the supply flow rate of the weak solution L5 that supplies with above-mentioned high-temperature generator 4 sides, and when the liquid level of reality is lower than above-mentioned low liquid level L position (the 2nd level detection electrode bar F2 exports H), improve the rotating speed of the rotary drive unit 10 of above-mentioned solution pump 26, the supply flow rate of the weak solution L5 of above-mentioned high-temperature generator 4 sides of increasing supply.Thus, the liquid level of reality is maintained proper height zone between above-mentioned high liquid level H position and the low liquid level L position, prevent to pass, keep stable operating condition at the steam of high-temperature generator 4.
In addition, during this situation, above-mentioned floater controlled valve FV is set, makes liquid level mechanically be remained on desired setting height in middle temperature generator 5 sides.Prevent passing of steam thus, keep stable operating condition.
Therefore, in this embodiment, only consider the liquid level of above-mentioned high-temperature generator 4 sides, the rotating speed control of carrying out solution pump 26 gets final product, and software, the hardware configuration of the revolution speed control device system of solution pump 26 are all simple, and cost is low, improve reliability.
And, in this embodiment, when this situation, the temperature detection sensor TS of its temperature of detection is set at the outlet side passage 42 of above-mentioned high-temperature generator 4, detection is from the temperature T of the concentrated solution L1 of high-temperature generator 4 and refrigerant vapour R1 ℃, and imports the micro computer of above-mentioned control panel 16.This micro computer according to detected from the temperature T of the concentrated solution L1 of high-temperature generator 4 and refrigerant vapour R1 ℃, set the basic rotational speed N o (the fundamental frequency f0 of TCU transfer control unit) of above-mentioned solution pump rotary drive unit 10, be benchmark and proofread and correct this basic rotational speed N o (No ± Δ N=fo ± Δ f) with it according to the output of above-mentioned the 1st, the 2nd level detection electrode bar F1, F2, thus, the final driving rotational speed N (supply frequency f) of decision and output solution pump rotary drive unit 10 drives solution pump 26 with suitable rotating speed rotation.
Therefore, according to this structure, only the basic value of setting the solution internal circulating load according to the recurrent state value of high-temperature generator 4 turns round, and realizes steady running.In addition, also easy corresponding load change.
As mentioned above, triple function absorption type refrigerating units according to present embodiment, can form simple and low-cost configuration, and can suitably control the liquid inventory of supply high-temperature generator 4 and the liquid inventory of middle temperature generator 5 simultaneously, when even both have load change, also can guarantee stable behavior in service, keep certain refrigerating capacity.
＜variation 〉
In addition, the floater controlled valve FV, the 1st of said structure, the 2nd level detection electrode bar F1, F2, solution pump rotary drive unit 10 etc. for example can carry out following distortion.
(1) floater controlled valve FV
In the floater controlled valve FV of warm generator 5 also can be arranged to, the each several part in the liquid level in the container 21 of middle temperature generator 5 or the 51a of export department of middle temperature generator 5 or inlet portion and the container is provided with the floating ball box of prescribed level respectively, regulates its liquid level.
(2) level detection sensor FS (the 1st, the 2nd level detection electrode bar F1, F2)
Level detection sensor FS may not be above-mentioned electrode bar structure.
(3) the solution pump rotary drive unit 10
The frequency of the conversion control device of this rotary drive unit 10 can be controlled by stages, also can continuous control.
＜embodiment 2 〉
In above-mentioned embodiment 1, mechanically be independent of the liquid level position control of middle temperature generator 5 sides outside the high-temperature generator 4 by ball-cock assembly FV, but, for example also can be by the level detection sensor by the liquid level position of this warm generator 5 of detection that is arranged in above-mentioned temperature generator 5 sides is set, supply with the weak solution influx control module that the motor-driven valve of the weak solution influx of this warm generator 5 constitutes with the adjusting of the weak solution inlet that is arranged in this warm generator 5, one side detect above-mentioned in the liquid level position of warm generator 5, the weak solution influx of warm generator 5 maintained certain altitude with this liquid level position thus during the suitable control supply of one side was above-mentioned.
According to this structure, can obtain the action effect identical with above-mentioned embodiment 1.
＜other embodiments 〉
In above-mentioned embodiment 1, for example shown in the flow chart of Fig. 1, in the device of following loop structure, be suitable for the present invention, the weak solution L5 of the device of self-absorption in the future 2 supplies with high-temperature generator 4 by cryogenic fluid heat exchanger 7 and high-temperature solution heat exchanger 9, and by warm generator 5 in cryogenic fluid heat exchanger 7 and middle temperature solution heat exchanger 8 arranged side by side the supplies.
But, be suitable for loop structure of the present invention and never be limited to loop structure shown in Figure 1, can be applicable to various loop structures in addition equally fully.
(1) the 1st example (with reference to Fig. 2)
In this example, the weak solution of the device of self-absorption in the future 2 is supplied with above-mentioned high-temperature generator 4, the middle temperature generator 5 in the above-mentioned embodiment side by side, supplies with cryogenerator 6 in addition side by side, and this structure will further improve heat recovery efficiency.
(2) the 2nd examples (with reference to Fig. 3)
Identical with the 1st example in this example, the weak solution of the device of self-absorption in the future 2 is supplied with high-temperature generator 4, middle temperature generator 5 side by side, supply with cryogenerator 6 in addition side by side, particularly, carry out on the basis of recuperation of heat at the middle temperature solution heat exchanger 8 of the weak solution that will supply with high-temperature generator 4, supply with high-temperature generator 4 by high-temperature solution heat exchanger 9 by middle temperature generator 5 sides.
(3) the 3rd examples (with reference to Fig. 4)
The structure of this example is, in the time of will supplying with cryogenerator 6, middle temperature generator 5, high-temperature generator 4 respectively from the weak solution of above-mentioned absorber 2, be provided with 2 group the 1st, the 2nd solution pump, at first supply with cryogenerator 6 for the time being by the 1st solution pump 26a, and then by warm generator 5 and high-temperature generator 4 in the 2nd solution pump 26b supply arranged side by side.
(4) the 4th examples (with reference to Fig. 5)
The structure of this example is, in the time of resembling above-mentioned embodiment, will supplying with high-temperature generator 4, middle temperature generator 5 side by side from the weak solution of above-mentioned absorber 2, make weak solution pipe arrangement 25 form branch in cryogenic fluid heat exchanger 7 fronts, when supplying with high-temperature generator 4,, only will not supply with absorber 2 from the concentrated solution of high-temperature generator 4 simultaneously by high-temperature solution heat exchanger 9 by cryogenic fluid heat exchanger 7 not by cryogenic fluid heat exchanger 7.
According to this structure, can increase heat exchange amount in high-temperature solution heat exchanger 9 parts.
Claims (6)
1. a triple function absorption type refrigerating unit has: condenser (3); Absorber (2) and evaporimeter (1); High temperature, middle temperature, 3 generators of low temperature (4,5,6); With 3 solution heat exchangers (7,8,9), to supply with above-mentioned high-temperature generator (4) and middle temperature generator (5) at least by solution pump (26) from the weak solution of above-mentioned absorber (2), to import low temperature side generator (5,6) successively at the refrigerant vapour that above-mentioned high temperature side generator (4,5) produces simultaneously, be used as the heating source of each generator (5,6) of this low temperature side, it is characterized in that
The weak solution of warm generator (5) inlet in above-mentioned, be provided with detect above-mentioned in the liquid level position of warm generator (5) and control supply with above-mentioned in the weak solution influx control module of weak solution influx of warm generator (5), independently control above-mentioned in the liquid level position of warm generator (5) and the liquid level position of above-mentioned high-temperature generator (4).
2. triple function absorption type refrigerating unit according to claim 1 is characterized in that, weak solution influx control module is by constituting with the lower part: the level detection sensor of the liquid level position of warm generator (5) in the detection; And motor-driven valve, the influx of the weak solution of warm generator (5) during its detection signal according to this level detection sensor is regulated and supplied with is so that the liquid level position of middle temperature generator (5) keeps certain.
3. a triple function absorption type refrigerating unit has: condenser (3); Absorber (2) and evaporimeter (1); High temperature, middle temperature, 3 generators of low temperature (4,5,6); With 3 solution heat exchangers (7,8,9), to supply with above-mentioned high-temperature generator (4) and middle temperature generator (5) at least by solution pump (26) from the weak solution of above-mentioned absorber (2), to import low temperature side generator (5,6) successively at the refrigerant vapour that above-mentioned high temperature side generator (4,5) produces simultaneously, be used as the heating source of each generator (5,6) of this low temperature side, it is characterized in that
The weak solution of warm generator (5) inlet is provided with liquid level position control ball-cock assembly (FV) in above-mentioned, control above-mentioned in the liquid level position of warm generator (5), outlet side at above-mentioned high-temperature generator (4) is provided with level detection sensor (LS1, LS2) simultaneously, control the driving rotating speed of above-mentioned solution pump (26), so that the liquid level position of above-mentioned high-temperature generator (4) keeps certain.
4. triple function absorption type refrigerating unit according to claim 3, it is characterized in that, temperature sensor (TS) with temperature of detection high-temperature generator (4), set basic rotating speed according to the detected temperatures of this temperature sensor (TS) to the solution pump (26) of high-temperature generator (4) delivered solution, carrying out rotating speed according to the output of the liquid level sensor that is located at high-temperature generator (4) outlet side (LS1, LS2) proofreaies and correct, if liquid level position height then reduce rotating speed is if liquid level position is low then improve rotating speed.
5. according to claim 1,2,3 or 4 described triple function absorption type refrigerating units, it is characterized in that the weak solution of self-absorption device (2) is supplied with high-temperature generator (4) and middle temperature generator (5) side by side in the future.
6. according to claim 1,2,3 or 4 described triple function absorption type refrigerating units, it is characterized in that the weak solution of self-absorption device (2) is supplied with high-temperature generator (4) and middle temperature generator (5) side by side by cryogenerator (6) in the future.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP169270/2003 | 2003-06-13 | ||
| JP2003169270A JP2005003312A (en) | 2003-06-13 | 2003-06-13 | Triple effect absorption refrigerating plant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1573259A true CN1573259A (en) | 2005-02-02 |
| CN100453925C CN100453925C (en) | 2009-01-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100465927A Expired - Fee Related CN100453925C (en) | 2003-06-13 | 2004-06-11 | Three functions absorption type refrigerating apparatus |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP2005003312A (en) |
| CN (1) | CN100453925C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104653427A (en) * | 2015-01-04 | 2015-05-27 | 上海理工大学 | Thermally driven liquid pressurizing device |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007232271A (en) * | 2006-03-01 | 2007-09-13 | Ebara Refrigeration Equipment & Systems Co Ltd | Triple effect absorption refrigerating machine |
| KR100732228B1 (en) | 2006-03-06 | 2007-06-27 | 학교법인 포항공과대학교 | Hybrid absorption chiller |
| JP2008064422A (en) * | 2006-09-11 | 2008-03-21 | Ebara Refrigeration Equipment & Systems Co Ltd | High temperature regenerator and absorption refrigerating machine |
| JP2011185511A (en) * | 2010-03-08 | 2011-09-22 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011220622A (en) * | 2010-04-12 | 2011-11-04 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011220623A (en) * | 2010-04-12 | 2011-11-04 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011226679A (en) * | 2010-04-16 | 2011-11-10 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP2011226678A (en) * | 2010-04-16 | 2011-11-10 | Kawasaki Thermal Engineering Co Ltd | Fluid heating device |
| JP6735978B2 (en) * | 2018-03-12 | 2020-08-05 | 国立研究開発法人産業技術総合研究所 | Gas production system and gas production method |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5724823A (en) * | 1996-10-10 | 1998-03-10 | Carrier Corporation | Absorption over-concentration control |
| JP3753356B2 (en) * | 1998-12-03 | 2006-03-08 | 荏原冷熱システム株式会社 | Triple effect absorption refrigerator |
| JP3554858B2 (en) * | 2000-10-23 | 2004-08-18 | 川重冷熱工業株式会社 | Absorption refrigerator |
-
2003
- 2003-06-13 JP JP2003169270A patent/JP2005003312A/en active Pending
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2004
- 2004-06-11 CN CNB2004100465927A patent/CN100453925C/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104653427A (en) * | 2015-01-04 | 2015-05-27 | 上海理工大学 | Thermally driven liquid pressurizing device |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2005003312A (en) | 2005-01-06 |
| CN100453925C (en) | 2009-01-21 |
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