CN105091398B - A kind of refrigerating output control methods of New Type of LiBr Absorption Chiller group - Google Patents
A kind of refrigerating output control methods of New Type of LiBr Absorption Chiller group Download PDFInfo
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- CN105091398B CN105091398B CN201510548332.8A CN201510548332A CN105091398B CN 105091398 B CN105091398 B CN 105091398B CN 201510548332 A CN201510548332 A CN 201510548332A CN 105091398 B CN105091398 B CN 105091398B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
- F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
- F25B15/06—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas the refrigerant being water vapour evaporated from a salt solution, e.g. lithium bromide
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B27/00—Machines, plants or systems, using particular sources of energy
- F25B27/002—Machines, plants or systems, using particular sources of energy using solar energy
- F25B27/007—Machines, plants or systems, using particular sources of energy using solar energy in sorption type systems
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B49/00—Arrangement or mounting of control or safety devices
- F25B49/04—Arrangement or mounting of control or safety devices for sorption type machines, plants or systems
- F25B49/043—Operating continuously
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/25—Control of valves
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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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
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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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
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Abstract
本发明公开了一种新型溴化锂吸收式制冷机组,包括发生器、冷凝器、蒸发器、吸收器、太阳能集热器循环供热系统、溶液热交换器、PLC控制系统、连接PLC控制系统的触摸屏显示器,所述太阳能集热器循环供热系统包括通过管路依次连接形成热水循环回路的太阳能集热器、热水电控调节阀、热水泵、发生器进口温度变送器、流量变送器、发生器出口温度变送器,所述热水电控调节阀、发生器进口温度变送器、流量变送器、发生器出口温度变送器均与PLC控制系统电路连接。本发明还提供了一种新型溴化锂吸收式制冷机组的制冷量调节方法。本发明有效地提高低温热源驱动下的溴化锂吸收式制冷机的制冷效率,降低制冷系统所需最低驱动热源温度。
The invention discloses a novel lithium bromide absorption refrigerating unit, comprising a generator, a condenser, an evaporator, an absorber, a solar heat collector cycle heating system, a solution heat exchanger, a PLC control system, and a touch screen connected to the PLC control system display, the solar heat collector cycle heating system includes a solar heat collector connected in turn to form a hot water circulation loop through pipelines, a hot water electric control valve, a hot water pump, a generator inlet temperature transmitter, a flow transmitter The generator, the generator outlet temperature transmitter, the hot water electric control valve, the generator inlet temperature transmitter, the flow transmitter, and the generator outlet temperature transmitter are all connected to the PLC control system circuit. The invention also provides a method for adjusting the cooling capacity of a novel lithium bromide absorption refrigeration unit. The invention effectively improves the refrigeration efficiency of the lithium bromide absorption refrigerator driven by the low-temperature heat source, and reduces the minimum driving heat source temperature required by the refrigeration system.
Description
技术领域technical field
本发明涉及机械制造及控制技术领域,尤其涉及一种新型溴化锂吸收式制冷机组及其制冷量调节方法。The invention relates to the technical field of mechanical manufacturing and control, in particular to a novel lithium bromide absorption refrigeration unit and a cooling capacity adjustment method thereof.
背景技术Background technique
溴化锂吸收式制冷机运行费用低,无运动部件,寿命长,无噪声,符合节能和环保的要求,有着广泛的应用前景。但是目前溴化锂吸收式制冷机由于技术能力发展水平限制,对于驱动热源的温度要求比较高,而目前的一般太阳能集热器只能提供低品质热源,无法达到其所需温度,效率相对较低,导致难以在市场上推广。机组控制系统的核心为能量调节系统,其主要目标是使外界所需要的热负荷同该溴化锂制冷机组的制冷量时刻匹配,体现在机组的冷媒水出口温度上,由于外界所需热负荷是存在波动的,所以对机组的制冷量要求也相应有所变化,能量调节系统需要根据驱动热源、溶液循环量的监测和调节,来经济稳定的满足系统的运行要求。The lithium bromide absorption refrigerator has low operating cost, no moving parts, long life, no noise, meets the requirements of energy saving and environmental protection, and has a wide application prospect. However, the current lithium bromide absorption refrigerator has a relatively high temperature requirement for the driving heat source due to the limitation of the technical ability development level, and the current general solar collector can only provide low-quality heat source, which cannot reach the required temperature, and the efficiency is relatively low. Difficult to promote in the market. The core of the unit control system is the energy regulation system. Its main goal is to match the heat load required by the outside world with the cooling capacity of the lithium bromide refrigeration unit at all times, which is reflected in the outlet temperature of the refrigerant water of the unit. Since the heat load required by the outside world exists Fluctuating, so the cooling capacity requirements of the unit also change accordingly. The energy regulation system needs to monitor and adjust the driving heat source and solution circulation volume to economically and stably meet the operating requirements of the system.
发明内容Contents of the invention
有鉴于此,本发明的主要目的在于提供一种新型溴化锂吸收式制冷机组及其制冷量调节方法,用以有效地提高低温热源驱动下的溴化锂吸收式制冷机的制冷效率,降低制冷系统所需最低驱动热源温度,促进其市场推广化。In view of this, the main purpose of the present invention is to provide a novel lithium bromide absorption refrigerating unit and its cooling capacity adjustment method, in order to effectively improve the refrigerating efficiency of the lithium bromide absorption refrigerating machine driven by a low-temperature heat source, and reduce the refrigeration system. The lowest driving heat source temperature promotes its market promotion.
本发明提供的新型溴化锂吸收式制冷机组是通过如下技术方案实现的:The novel lithium bromide absorption refrigerating unit provided by the invention is realized through the following technical solutions:
一种新型溴化锂吸收式制冷机组,包括设置在高压腔体内的发生器和冷凝器、设置在低压腔体内的蒸发器和吸收器、为发生器提供热水的太阳能集热器循环供热系统、溶液热交换器、PLC控制系统、连接PLC控制系统的触摸屏显示器,所述蒸发器用于与目标冷媒水换热,所述太阳能集热器循环供热系统包括通过管路依次连接形成热水循环回路的太阳能集热器、热水电控调节阀、热水泵、发生器进口温度变送器、流量变送器、发生器出口温度变送器,所述热水电控调节阀、发生器进口温度变送器、流量变送器、发生器出口温度变送器均与PLC控制系统电路连接;A new type of lithium bromide absorption refrigerating unit, including a generator and a condenser arranged in a high-pressure chamber, an evaporator and an absorber arranged in a low-pressure chamber, a solar collector circulation heating system that provides hot water for the generator, Solution heat exchanger, PLC control system, touch screen display connected to the PLC control system, the evaporator is used to exchange heat with the target refrigerant water, and the solar heat collector circulation heating system includes a hot water circulation loop formed by sequentially connecting pipelines The solar collector, hot water electric control valve, hot water pump, generator inlet temperature transmitter, flow transmitter, generator outlet temperature transmitter, the hot water electric control valve, generator inlet temperature The transmitter, flow transmitter, and generator outlet temperature transmitter are all connected to the PLC control system circuit;
所述溶液热交换器与吸收器之间通过管道设置有将溴化锂稀溶液经溶液热交换器泵送至发生器的溶液泵,所述溶液泵通过变频器与PLC控制系统电路连接;A solution pump is arranged between the solution heat exchanger and the absorber to pump the lithium bromide dilute solution to the generator through the solution heat exchanger, and the solution pump is connected to the PLC control system circuit through a frequency converter;
所述蒸发器的目标冷媒水入口管道上设置有蒸发器进口温度变送器,所述蒸发器的目标冷媒水出口管道上设置有蒸发器出口温度变送器。The target refrigerant water inlet pipe of the evaporator is provided with an evaporator inlet temperature transmitter, and the target refrigerant water outlet pipe of the evaporator is provided with an evaporator outlet temperature transmitter.
进一步地,还包括超声强化装置,所述超声强化装置的换能器直接安装于所在高压腔体底部,超声波强化装置用超声空化效应,强化发生器内溴化锂-水溶液的传质传热过程;Further, it also includes an ultrasonic strengthening device, the transducer of the ultrasonic strengthening device is directly installed at the bottom of the high-pressure chamber, and the ultrasonic strengthening device uses the ultrasonic cavitation effect to strengthen the mass transfer and heat transfer process of the lithium bromide-water solution in the generator;
进一步地,所述超声强化装置产生频率为20kHz以上,工作功率为100w以上。Further, the frequency of the ultrasonic intensifier is above 20kHz, and the working power is above 100w.
进一步地,所述换能器的数量≥1个,当数量超过1个时,相邻换能器之间的安装位置间隔相等且不小于100mm,具体可根据机组规模和高压腔体结构及其底部面积而适当调整,安装方式可以为高强度胶水,机械安装,磁性吸附。Further, the number of transducers is ≥ 1. When the number exceeds 1, the installation positions between adjacent transducers are equal and not less than 100mm. Specifically, it can be determined according to the scale of the unit and the structure of the high-pressure chamber and its The bottom area can be properly adjusted, and the installation method can be high-strength glue, mechanical installation, and magnetic adsorption.
进一步地,所述热水电控调节阀与PLC控制系统之间采用闭环控制系统,以提高对热水电控调节阀的调节精度。Further, a closed-loop control system is adopted between the hot water electric control valve and the PLC control system to improve the adjustment accuracy of the hot water electric control valve.
本发明提供的新型溴化锂吸收式制冷机组的制冷量调节方法通过如下方案实现的:The refrigerating capacity adjustment method of the novel lithium bromide absorption refrigerating unit provided by the present invention is realized by the following scheme:
一种如所述新型溴化锂吸收式制冷机组的制冷量调节方法,包括步骤:A method for adjusting the cooling capacity of the novel lithium bromide absorption refrigerating unit, comprising the steps of:
1)PLC控制系统将蒸发器出口温度变送器实时获取的所述蒸发器的目标冷媒水出口的实际温度Tr与通过触摸屏显示器设定的设定温度Ts进行比较;1) The PLC control system compares the actual temperature Tr of the target refrigerant water outlet of the evaporator acquired by the evaporator outlet temperature transmitter in real time with the set temperature Ts set by the touch screen display;
2)若1℃≤|Tr‐Ts|<5℃时,PLC控制系统首先采用循环液变频调速模式,即调用PID算法调整变频器频率,使变频器作用于与其连接的溶液泵,通过溶液泵控制机组溴化锂稀溶液的循环流速,进而调节制冷量,直到|Tr‐Ts|﹤1℃。2) If 1°C≤|Tr‐Ts|<5°C, the PLC control system first adopts the circulating fluid frequency conversion speed regulation mode, that is, calls the PID algorithm to adjust the frequency of the frequency converter, so that the frequency converter acts on the solution pump connected to it, and passes through the solution The pump controls the circulating flow rate of the lithium bromide dilute solution of the unit, and then adjusts the cooling capacity until |Tr‐Ts|﹤1℃.
进一步地,若|Tr‐Ts|≥5℃时,还包括步骤:Further, if |Tr‐Ts|≥5℃, further steps:
3)检查热水电控调节阀(6)和变频器的工作状态,判断机组工作状态和热水电控调节阀(6)静止时间,以保证不会调节过度和避免频繁操作热水电控调节阀;3) Check the working status of the hot water electric control valve (6) and the inverter, and judge the working status of the unit and the static time of the hot water electric control valve (6), so as to ensure that there will be no excessive adjustment and avoid frequent operation of the hot water electric control valve. regulating valve;
4)若机组未处于全负荷工作状态且热水电控调节阀(6)静止已达3分钟,则同时启动调节热水供给量模式,即PLC控制系统产生信号,所述信号使得热水电控调节阀(6)开度增加或减少5%,通过对制冷量调节方法进行优化,即采用循环液变频调速技术与热水供给量调节模式智能结合的方式,综合调节目标冷媒水出口温度,提高调解效率和精度;4) If the unit is not in full-load working condition and the hot water electric control valve (6) has been static for 3 minutes, then start the mode of adjusting the hot water supply at the same time, that is, the PLC control system generates a signal, and the signal makes the hot water electricity Control the opening of the control valve (6) to increase or decrease by 5%. By optimizing the cooling capacity adjustment method, that is, the intelligent combination of circulating fluid frequency conversion speed regulation technology and hot water supply adjustment mode is used to comprehensively adjust the target refrigerant water outlet temperature. , improve mediation efficiency and accuracy;
5)热水电控调节阀(6)开度到位后静止3分钟,接着PLC控制系统将蒸发器出口温度变送器(1)实时获取的所述蒸发器(13)的目标冷媒水出口的实际温度Tr与通过触摸屏显示器设定的设定温度Ts进行比较,若|Tr‐Ts|﹤1℃时,则完成制冷量调节,否则,则返回步骤3)。5) After the opening of the hot water electric control valve (6) is in place, stand still for 3 minutes, and then the PLC control system will obtain the temperature of the target refrigerant water outlet of the evaporator (13) obtained in real time by the evaporator outlet temperature transmitter (1). The actual temperature Tr is compared with the set temperature Ts set through the touch screen display, if |Tr‐Ts|<1°C, the cooling capacity adjustment is completed, otherwise, return to step 3).
进一步地,当实际温度Tr高于设定温度Ts时,如果变频器频率跟热水电控调节阀开度已达上限,则机组维持当前工作状态;当实际温度Tr低于设定温度Ts时,如果变频器频率跟热水电控调节阀开度已达下限,则PLC控制系统启动黄色报警信号,同时机组停机,停止制冷进行稀释,起到保护系统以免发生结晶及其他故障的作用。Furthermore, when the actual temperature Tr is higher than the set temperature Ts, if the inverter frequency and the opening of the hot water electric control valve have reached the upper limit, the unit will maintain the current working state; when the actual temperature Tr is lower than the set temperature Ts , if the frequency of the frequency converter and the opening of the hot water electric control valve have reached the lower limit, the PLC control system will start a yellow alarm signal, and at the same time the unit will stop, stop cooling for dilution, and protect the system from crystallization and other failures.
进一步地,所述PLC控制系统产生信号控制热水电控调节阀开度时,热水电控调节阀通过闭环控制系统及时将当前开度反馈回PLC控制系统,所述PLC控制系统根据反馈数据判断并确保热水电控调节阀到达目标开度时停止,形成闭环控制,以提高对热水电控调节阀的调节精度。Further, when the PLC control system generates a signal to control the opening of the hot water electric control valve, the hot water electric control valve will timely feed back the current opening to the PLC control system through the closed-loop control system, and the PLC control system will Judging and ensuring that the hot water electric control valve stops when it reaches the target opening, forming a closed-loop control to improve the adjustment accuracy of the hot water electric control valve.
相比现有技术,本发明具如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
本发明提出的新型溴化锂吸收式制冷机组及其制冷量调节方法,组成结构上,溴化锂机组在一般基础上,加装了超声波强化装置,利用超声空化效应,强化发生器内溴化锂-水溶液的传质传热过程;制冷量调节方法上,通过对制冷量调节方式进行优化,采用循环液变频调速技术与热水供给量调节模式智能结合,综合调节目标冷媒水出口温度。这种新型溴化锂吸收式制冷机组,有效地提高低温热源驱动下的溴化锂吸收式制冷机的制冷效率,降低制冷机组所需的最低驱动热源温度,更有效经济的实现制冷量调节目标,且不会破坏系统稳定运行特性。该调节方法适用于低温热水驱动的太阳能吸收式制冷系统,从而增强太阳能空调的制冷效果,促进其市场推广。The new lithium bromide absorption refrigeration unit and its cooling capacity adjustment method proposed by the present invention, in terms of composition and structure, the lithium bromide unit is equipped with an ultrasonic strengthening device on a general basis, and the ultrasonic cavitation effect is used to strengthen the transmission of lithium bromide-water solution in the generator. Mass and heat transfer process; in terms of the cooling capacity adjustment method, by optimizing the cooling capacity adjustment method, the circulating fluid frequency conversion speed regulation technology is intelligently combined with the hot water supply adjustment mode to comprehensively adjust the target refrigerant water outlet temperature. This new type of lithium bromide absorption refrigeration unit can effectively improve the refrigeration efficiency of the lithium bromide absorption refrigeration unit driven by a low-temperature heat source, reduce the minimum driving heat source temperature required by the refrigeration unit, and achieve the goal of cooling capacity adjustment more effectively and economically. Destroy the stable operation characteristics of the system. The adjustment method is applicable to a solar absorption refrigeration system driven by low-temperature hot water, thereby enhancing the cooling effect of the solar air conditioner and promoting its market promotion.
附图说明:Description of drawings:
图1是本发明实施例的新型溴化锂制冷机组的结构示意图。Fig. 1 is the structural representation of the novel lithium bromide refrigerating unit of the embodiment of the present invention.
图2是本发明实施例的新型溴化锂制冷机组超声波强化装置的换能器安装侧视示意图。Fig. 2 is a schematic side view of the installation of the transducer of the ultrasonic strengthening device of the novel lithium bromide refrigeration unit according to the embodiment of the present invention.
图3是本发明实施例的新型溴化锂制冷机组超声波强化装置的换能器安装立体示意图。Fig. 3 is a three-dimensional schematic diagram of the installation of the transducer of the ultrasonic strengthening device of the novel lithium bromide refrigeration unit according to the embodiment of the present invention.
图4是本发明实施例的新型溴化锂吸收式制冷机组制冷量调节方法总体方案图。Fig. 4 is an overall scheme diagram of a cooling capacity adjustment method of a novel lithium bromide absorption refrigeration unit according to an embodiment of the present invention.
图5是本本发明实施例的新型溴化锂吸收式制冷机组制冷量调节方法的详细流程图。Fig. 5 is a detailed flowchart of the cooling capacity adjustment method of the novel lithium bromide absorption refrigerating unit according to the embodiment of the present invention.
附图标记包括:1‐蒸发器出口温度变送器;2‐蒸发器进口温度变送器;3‐超声强化装置;4‐发生器出口温度变送器;5‐太阳能集热器;6‐热水电控调节阀;7‐热水泵;8‐发生器进口温度变送器;9‐流量变送器;10‐发生器;11‐高压腔体;12‐冷凝器;13‐蒸发器;14‐吸收器;15‐低压腔体;16‐溶液泵;17‐溶液热交换器;18‐换能器。Reference signs include: 1-evaporator outlet temperature transmitter; 2-evaporator inlet temperature transmitter; 3-ultrasonic strengthening device; 4-generator outlet temperature transmitter; 5-solar collector; 6- Hot water electric control valve; 7‐hot water pump; 8‐generator inlet temperature transmitter; 9‐flow transmitter; 10‐generator; 11‐high pressure cavity; 12‐condenser; 13‐evaporator; 14‐absorber; 15‐low pressure chamber; 16‐solution pump; 17‐solution heat exchanger; 18‐transducer.
具体实施方式detailed description
为了更好地理解本发明,下面结合附图和实施例对本发明的具体实施方法作进一步的说明,但本发明要求保护的范围不局限于此。In order to better understand the present invention, the specific implementation methods of the present invention will be further described below in conjunction with the accompanying drawings and examples, but the protection scope of the present invention is not limited thereto.
实施例一Embodiment one
如图1所示,本实施例在一台以85℃热水驱动的设计制冷量为10KW的小型太阳能溴化锂吸收式制冷机的一般结构基础上,加装了超声波强化装置,利用超声空化效应,强化发生器内溴化锂‐水溶液的传质传热过程,具体如下:As shown in Figure 1, this embodiment is based on the general structure of a small solar lithium bromide absorption refrigerator with a design cooling capacity of 10KW driven by 85°C hot water, and an ultrasonic strengthening device is added to utilize the ultrasonic cavitation effect , to strengthen the mass transfer and heat transfer process of lithium bromide-aqueous solution in the generator, as follows:
一种新型溴化锂吸收式制冷机组,包括设置在高压腔体11内的发生器10和冷凝器12、设置在低压腔体15内的蒸发器13和吸收器14、为发生器10提供热水的太阳能集热器循环供热系统、溶液热交换器17、PLC控制系统、连接PLC控制系统的触摸屏显示器,所述蒸发器13用于与目标冷媒水换热,所述太阳能集热器循环供热系统包括通过管路依次连接形成热水循环回路的太阳能集热器5、热水电控调节阀6、热水泵7、发生器进口温度变送器8、流量变送器9、发生器出口温度变送器4,所述热水电控调节阀6、发生器进口温度变送器8、流量变送器9、发生器出口温度变送器4均与PLC控制系统电路连接,同时所述热水电控调节阀6与PLC控制系统之间采用闭环控制系统,以提高对热水电控调节阀的调节精度;A new lithium bromide absorption refrigerating unit, including a generator 10 and a condenser 12 arranged in a high-pressure chamber 11, an evaporator 13 and an absorber 14 arranged in a low-pressure chamber 15, and a device for providing hot water to the generator 10 Solar heat collector circulation heating system, solution heat exchanger 17, PLC control system, touch screen display connected to the PLC control system, the evaporator 13 is used for heat exchange with target refrigerant water, and the solar heat collector circulation heat supply The system includes a solar collector 5 connected in turn to form a hot water circulation loop through pipelines, a hot water electric control valve 6, a hot water pump 7, a generator inlet temperature transmitter 8, a flow transmitter 9, and a generator outlet temperature transmitter. The transmitter 4, the hot water electric control valve 6, the generator inlet temperature transmitter 8, the flow transmitter 9, and the generator outlet temperature transmitter 4 are all connected to the PLC control system circuit. A closed-loop control system is adopted between the water electric control valve 6 and the PLC control system to improve the adjustment accuracy of the hot water electric control valve;
所述溶液热交换器17与吸收器14之间通过管道设置有将溴化锂稀溶液经溶液热交换器17泵送至发生器10的溶液泵16,所述溶液泵16通过变频器与PLC控制系统电路连接;A solution pump 16 is arranged between the solution heat exchanger 17 and the absorber 14 to pump the lithium bromide dilute solution to the generator 10 through the solution heat exchanger 17, and the solution pump 16 is controlled by a frequency converter and a PLC. circuit connection;
所述蒸发器13的目标冷媒水入口管道上设置有蒸发器进口温度变送器2,所述蒸发器13的目标冷媒水出口管道上设置有蒸发器出口温度变送器1。An evaporator inlet temperature transmitter 2 is arranged on the target refrigerant water inlet pipe of the evaporator 13 , and an evaporator outlet temperature transmitter 1 is arranged on the target refrigerant water outlet pipe of the evaporator 13 .
具体来说,本实施例还包括超声强化装置3,所述超声强化装置3的换能器18直接安装于所在高压腔体11底部,超声波强化装置用超声空化效应,强化发生器内溴化锂-水溶液的传质传热过程;所示超声强化装置产生频率采用25kHz,工作功率采用500w,采用5个换能器18,直接安装于发生器10所在高压腔体底部,不同换能器18之间安装位置间隔为250mm,安装方式采用磁性吸附(见如2和图3)。该超声强化装置的工作方式为随机组启停,机组制冷期间持续运行。Specifically, this embodiment also includes an ultrasonic strengthening device 3, the transducer 18 of the ultrasonic strengthening device 3 is directly installed at the bottom of the high-pressure chamber 11, and the ultrasonic strengthening device uses the ultrasonic cavitation effect to strengthen the lithium bromide- The mass transfer and heat transfer process of the aqueous solution; the ultrasonic intensification device shown has a generating frequency of 25kHz, a working power of 500w, and 5 transducers 18, which are directly installed at the bottom of the high-pressure chamber where the generator 10 is located, between different transducers 18 The installation position interval is 250mm, and the installation method adopts magnetic adsorption (see eg 2 and Figure 3). The working mode of the ultrasonic strengthening device is to start and stop in random groups, and the unit continues to run during the cooling period.
本实施例提供的制冷机组利用太阳能集热器5将太阳能转化为热能进行水的加热,为机组的发生器10提供热水。当溴化锂制冷机工作时,工质吸收来自热水的热量,并产生制冷剂蒸汽,制冷剂蒸汽流动到冷凝器12中被冷却水吸收热量,凝结成液体,然后经过节流阀降压进入低压腔体15内被蒸发器13吸热蒸发,带走了外界冷媒水的热量,使其降温,降温后的外界冷媒水进入室内机中产生制冷效应。而蒸发产生的冷剂水蒸汽流动进入吸收器14,被溴化锂浓溶液吸收,溴化锂浓溶液吸收冷剂水蒸汽后变成溴化锂稀溶液,所述溴化锂稀溶液再经溶液泵16送入发生器10,如此利用水‐溴化锂工质对的质量分数变化来完成溶液循环,制取冷量。其中,为了提高机组的热效率,设有溶液热交换器17用于在溴化锂稀溶液进入发生器10前预热。The refrigerating unit provided in this embodiment utilizes the solar heat collector 5 to convert solar energy into thermal energy to heat water and provide hot water for the generator 10 of the unit. When the lithium bromide refrigerator is working, the working medium absorbs the heat from the hot water and generates refrigerant vapor. The refrigerant vapor flows into the condenser 12, is absorbed by the cooling water, condenses into a liquid, and then enters the low pressure through the throttle valve. The cavity 15 is absorbed and evaporated by the evaporator 13, which takes away the heat of the external refrigerant water to cool it down, and the cooled external refrigerant water enters the indoor unit to generate a cooling effect. The refrigerant water vapor produced by evaporation flows into the absorber 14 and is absorbed by the lithium bromide concentrated solution. After absorbing the refrigerant water vapor, the lithium bromide concentrated solution becomes a lithium bromide dilute solution, and the lithium bromide dilute solution is sent to the generator 10 through the solution pump 16. In this way, the change of the mass fraction of the water-lithium bromide working medium is used to complete the solution circulation and produce cooling capacity. Wherein, in order to improve the thermal efficiency of the unit, a solution heat exchanger 17 is provided for preheating before the lithium bromide dilute solution enters the generator 10 .
本实施例提供的制冷机组利用超声波强化装置产生超声空化效应,强化发生器10内溴化锂-水溶液的传质传热过程;而PLC控制系统能够根据蒸发器出口温度变送器1获取的实际温度与设定温度的差值自动调节变频器和热水电控调节阀6的开度,采用循环液变频调速模式与热水供给量调节模式智能结合,综合调节目标冷媒水出口温度,达到组合制冷、智能制冷的目的(见图4)。这种新型溴化锂吸收式制冷机组,能有效地提高低温热源驱动下的溴化锂吸收式制冷机的制冷效率,降低制冷机组所需的最低驱动热源温度,促进其市场推广化。The refrigerating unit provided in this embodiment utilizes an ultrasonic intensifier to generate an ultrasonic cavitation effect to strengthen the mass transfer and heat transfer process of the lithium bromide-water solution in the generator 10; and the PLC control system can obtain the actual temperature according to the evaporator outlet temperature transmitter 1 The difference with the set temperature automatically adjusts the opening of the frequency converter and the hot water electric control valve 6, adopts the intelligent combination of the circulating fluid frequency conversion speed regulation mode and the hot water supply adjustment mode, and comprehensively adjusts the target refrigerant water outlet temperature to achieve a combination The purpose of refrigeration and intelligent refrigeration (see Figure 4). This new lithium bromide absorption refrigeration unit can effectively improve the refrigeration efficiency of the lithium bromide absorption refrigeration unit driven by a low-temperature heat source, reduce the minimum driving heat source temperature required by the refrigeration unit, and promote its market promotion.
实施例二Embodiment two
如图5所示,一种如所述新型溴化锂吸收式制冷机组的制冷量调节方法,包括步骤:As shown in Figure 5, a kind of refrigeration capacity adjustment method as described novel lithium bromide absorption refrigerating unit, comprises steps:
1)PLC控制系统将蒸发器出口温度变送器1实时获取的所述蒸发器13的目标冷媒水出口的实际温度Tr与通过触摸屏显示器设定的设定温度Ts进行比较,所述设定温度Ts为用户根据外界环境而设定的冷媒水出口目标温度,该数值一般要结合机组设计的热力参数以及机组运行时的建筑热负荷而确定,本实施例默认为10℃;1) The PLC control system compares the actual temperature Tr of the target refrigerant water outlet of the evaporator 13 acquired by the evaporator outlet temperature transmitter 1 in real time with the set temperature Ts set by the touch screen display, the set temperature Ts is the target temperature of the refrigerant water outlet set by the user according to the external environment. This value is generally determined in conjunction with the thermal parameters of the unit design and the building heat load when the unit is running. In this embodiment, the default is 10°C;
2)若1℃≤|Tr‐Ts|<5℃时,PLC控制系统首先采用循环液变频调速模式,即调用PID算法调整变频器频率,即当5℃﹥Ts‐Tr≥1℃时,变频器进行PID调节减少频率;当5℃﹥Tr‐Ts≥1℃时,变频器进行PID调节增加频率;接着变频器作用于与其连接的溶液泵16,通过溶液泵16控制机组溴化锂稀溶液的循环流速,进而调节制冷量,直到|Tr‐Ts|﹤1℃。2) If 1°C≤|Tr‐Ts|<5°C, the PLC control system first adopts the circulating fluid frequency conversion speed regulation mode, that is, calls the PID algorithm to adjust the inverter frequency, that is, when 5°C﹥Ts‐Tr≥1°C, The inverter performs PID adjustment to reduce the frequency; when 5℃﹥Tr-Ts≥1℃, the inverter performs PID adjustment to increase the frequency; then the inverter acts on the solution pump 16 connected to it, and the solution pump 16 controls the concentration of the dilute lithium bromide solution of the unit. Circulate the flow rate, and then adjust the cooling capacity until |Tr‐Ts|﹤1℃.
本实施例中,若|Tr‐Ts|≥5℃时,还包括步骤:In this embodiment, if |Tr‐Ts|≥5°C, further steps are included:
3)检查热水电控调节阀6和变频器的工作状态,判断机组工作状态和热水电控调节阀6静止时间,以保证不会调节过度和避免频繁操作热水电控调节阀;3) Check the working status of the hot water electric control valve 6 and the frequency converter, judge the working status of the unit and the static time of the hot water electric control valve 6, so as to ensure that there will be no excessive adjustment and avoid frequent operation of the hot water electric control valve;
4)若机组未处于全负荷工作状态且热水电控调节阀6静止已达3分钟,则同时启动调节热水供给量模式,即PLC控制系统产生信号,所述信号使得热水电控调节阀6开度增加或减少5%,通过对制冷量调节方法进行优化,即采用循环液变频调速技术与热水供给量调节模式智能结合的方式,综合调节目标冷媒水出口温度,提高调解效率和精度;4) If the unit is not in full-load working condition and the hot water electric control regulating valve 6 has been static for 3 minutes, then start the hot water supply adjustment mode at the same time, that is, the PLC control system generates a signal, and the signal makes the hot water electric control adjust The opening of the valve 6 is increased or decreased by 5%. By optimizing the cooling capacity adjustment method, that is, the intelligent combination of circulating fluid frequency conversion speed regulation technology and hot water supply adjustment mode is used to comprehensively adjust the target refrigerant water outlet temperature and improve mediation efficiency. and precision;
5)热水电控调节阀6开度到位后静止3分钟,接着PLC控制系统将蒸发器出口温度变送器1实时获取的所述蒸发器13的目标冷媒水出口的实际温度Tr与通过触摸屏显示器设定的设定温度Ts进行比较,若|Tr‐Ts|﹤1℃时,则完成制冷量调节,否则,则返回步骤3),继续通过调节热水电控调节阀6开度,直到|Tr‐Ts|﹤1℃时,则完成制冷量调节。5) Stand still for 3 minutes after the opening of the hot water electric control valve 6 is in place, then the PLC control system compares the actual temperature Tr of the target refrigerant water outlet of the evaporator 13 obtained by the evaporator outlet temperature transmitter 1 in real time with the actual temperature Tr through the touch screen If |Tr‐Ts| is less than 1°C, the adjustment of the cooling capacity is completed; otherwise, return to step 3), and continue to adjust the opening degree of the hot water electric control valve 6 until When |Tr‐Ts|﹤1℃, the cooling capacity adjustment is completed.
本实施例中,当实际温度Tr高于设定温度Ts时,如果变频器频率跟热水电控调节阀6开度已达上限,则机组维持当前工作状态;当实际温度Tr低于设定温度Ts时,如果变频器频率跟热水电控调节阀6开度已达下限,则PLC控制系统启动黄色报警信号,同时机组停机,停止制冷进行稀释,起到保护系统以免发生结晶及其他故障的作用。In this embodiment, when the actual temperature Tr is higher than the set temperature Ts, if the frequency of the inverter and the opening of the hot water electric control valve 6 have reached the upper limit, the unit maintains the current working state; when the actual temperature Tr is lower than the set temperature When the temperature is Ts, if the frequency of the inverter and the opening of the hot water electric control valve 6 have reached the lower limit, the PLC control system will start a yellow alarm signal, and at the same time the unit will stop, stop cooling and dilute, to protect the system from crystallization and other failures role.
本实施例中,所述PLC控制系统产生信号控制热水电控调节阀6开度时,热水电控调节阀6通过闭环控制系统及时将当前开度反馈回PLC控制系统,所述PLC控制系统根据反馈数据判断并确保热水电控调节阀6到达目标开度时停止,形成闭环控制,以提高对热水电控调节阀的调节精度。In this embodiment, when the PLC control system generates a signal to control the opening of the hot water electric control valve 6, the hot water electric control valve 6 will timely feed back the current opening to the PLC control system through the closed-loop control system, and the PLC control According to the feedback data, the system judges and ensures that the hot water electric control valve 6 stops when it reaches the target opening, forming a closed-loop control to improve the adjustment accuracy of the hot water electric control valve.
本实施例提供过的制冷量调节方法,综合采用循环液变频调速模式和调节热水供给量模式,优化了制冷机组的运行核心部分,改善了溴化锂溶液的循环过程,由于循环液变频调速模式是改变变频器的工作频率来实现制冷量调节的,当频率下降到一定程度时,会导致溶液泵扬程变得过小而导致循环无法进行,受到一定的限制,而使用热水供给量调节模式时,当机组制冷量下降到50%及以下时,经济性明显下降,综合考虑以上两者的优缺点,组合使用两种模式,可更有效经济的实现制冷量调节目标,且不会破坏系统稳定运行特性。该调节方法适用于低温热水驱动的太阳能吸收式制冷系统,从而增强太阳能空调的制冷效果。The cooling capacity adjustment method provided in this embodiment comprehensively adopts the circulating fluid frequency conversion speed regulation mode and the hot water supply adjustment mode, optimizes the operation core part of the refrigeration unit, improves the circulation process of the lithium bromide solution, and because the circulating fluid frequency conversion speed regulation Mode is to change the working frequency of the inverter to adjust the cooling capacity. When the frequency drops to a certain level, the head of the solution pump will become too small and the cycle cannot be carried out, which is subject to certain restrictions. The use of hot water supply adjustment Mode, when the cooling capacity of the unit drops to 50% or below, the economy will drop significantly. Considering the advantages and disadvantages of the above two modes, the combined use of the two modes can achieve the cooling capacity adjustment target more effectively and economically without damaging the System stable operation characteristics. This adjustment method is suitable for solar absorption refrigeration systems driven by low-temperature hot water, thereby enhancing the cooling effect of solar air conditioners.
最后应当说明的是,本发明的上述实施例仅仅是为清楚地说明本发明所作的举例,而并非是对本发明的实施方式的限定。对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明权利要求的保护范围之内。Finally, it should be noted that the above-mentioned embodiments of the present invention are only examples for clearly illustrating the present invention, rather than limiting the implementation of the present invention. For those of ordinary skill in the art, other changes or changes in different forms can be made on the basis of the above description. It is not necessary and impossible to exhaustively list all the implementation manners here. All modifications, equivalent replacements and improvements made within the spirit and principles of the present invention shall be included within the protection scope of the claims of the present invention.
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| CN112413925A (en) * | 2019-08-23 | 2021-02-26 | 海南泰立来科技有限公司 | Low-temperature heat source refrigerating device |
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| CN114216287B (en) * | 2021-12-24 | 2023-05-12 | 北京华源泰盟节能设备有限公司 | Method and system for controlling heat source valve of absorption heat pump based on multiple PID |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4100755A (en) * | 1976-12-20 | 1978-07-18 | Carrier Corporation | Absorption refrigeration system utilizing solar energy |
| US4205529A (en) * | 1978-12-04 | 1980-06-03 | The United States Of America As Represented By The United States Department Of Energy | LiCl Dehumidifier LiBr absorption chiller hybrid air conditioning system with energy recovery |
| CN102384605A (en) * | 2011-10-25 | 2012-03-21 | 华南理工大学 | Ultrasonic-strengthened generator for absorption refrigerator |
| CN203501533U (en) * | 2013-08-27 | 2014-03-26 | 苏州新华软智能装备有限公司 | Ultrahigh-temperature absorption lithium bromide heat pump |
| CN203533960U (en) * | 2013-08-30 | 2014-04-09 | 广州科创节能科技服务有限公司 | Solar absorption refrigeration system |
| CN103954068A (en) * | 2014-04-17 | 2014-07-30 | 广东工业大学 | Absorption refrigerating machine with integrated solar assisted heat pump system |
| CN204285887U (en) * | 2014-10-31 | 2015-04-22 | 江西高信有机化工有限公司 | A kind of small capacity double thermal source lithium bromide refrigerator with filtering function |
| CN204987537U (en) * | 2015-08-29 | 2016-01-20 | 华南理工大学 | Novel lithium bromide absorbed refrigeration unit |
-
2015
- 2015-08-29 CN CN201510548332.8A patent/CN105091398B/en not_active Expired - Fee Related
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4100755A (en) * | 1976-12-20 | 1978-07-18 | Carrier Corporation | Absorption refrigeration system utilizing solar energy |
| US4205529A (en) * | 1978-12-04 | 1980-06-03 | The United States Of America As Represented By The United States Department Of Energy | LiCl Dehumidifier LiBr absorption chiller hybrid air conditioning system with energy recovery |
| CN102384605A (en) * | 2011-10-25 | 2012-03-21 | 华南理工大学 | Ultrasonic-strengthened generator for absorption refrigerator |
| CN203501533U (en) * | 2013-08-27 | 2014-03-26 | 苏州新华软智能装备有限公司 | Ultrahigh-temperature absorption lithium bromide heat pump |
| CN203533960U (en) * | 2013-08-30 | 2014-04-09 | 广州科创节能科技服务有限公司 | Solar absorption refrigeration system |
| CN103954068A (en) * | 2014-04-17 | 2014-07-30 | 广东工业大学 | Absorption refrigerating machine with integrated solar assisted heat pump system |
| CN204285887U (en) * | 2014-10-31 | 2015-04-22 | 江西高信有机化工有限公司 | A kind of small capacity double thermal source lithium bromide refrigerator with filtering function |
| CN204987537U (en) * | 2015-08-29 | 2016-01-20 | 华南理工大学 | Novel lithium bromide absorbed refrigeration unit |
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