WO2013120375A1 - Method of controlling a heat pump system with two-stage enthalpy increase - Google Patents

Method of controlling a heat pump system with two-stage enthalpy increase Download PDF

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Publication number
WO2013120375A1
WO2013120375A1 PCT/CN2012/086191 CN2012086191W WO2013120375A1 WO 2013120375 A1 WO2013120375 A1 WO 2013120375A1 CN 2012086191 W CN2012086191 W CN 2012086191W WO 2013120375 A1 WO2013120375 A1 WO 2013120375A1
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WO
WIPO (PCT)
Prior art keywords
heat pump
pump system
stage heat
preset
controlling
Prior art date
Application number
PCT/CN2012/086191
Other languages
French (fr)
Chinese (zh)
Inventor
郑晓峰
魏会军
Original Assignee
国家节能环保制冷设备工程技术研究中心
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Application filed by 国家节能环保制冷设备工程技术研究中心 filed Critical 国家节能环保制冷设备工程技术研究中心
Publication of WO2013120375A1 publication Critical patent/WO2013120375A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • F25B1/10Compression machines, plants or systems with non-reversible cycle with multi-stage compression
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/30Expansion means; Dispositions thereof
    • F25B41/39Dispositions with two or more expansion means arranged in series, i.e. multi-stage expansion, on a refrigerant line leading to the same evaporator
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/13Economisers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/23Separators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2509Economiser valves

Definitions

  • the present invention relates to the field of compressors, and in particular to a two-stage heat pump system control method.
  • BACKGROUND OF THE INVENTION At present, the heat pump products are better promoted by the national energy efficiency improvement, and the energy-saving performance is better than before.
  • the emergence of frequency conversion technology has a significant improvement over the fixed-speed heat pump, such as rapid cooling, temperature rise, and stable control of the ambient temperature after startup. Technology can avoid frequent shutdowns and starts, and has a good advantage for energy saving and compressor reliability.
  • the variable frequency heat pump has made significant progress in energy saving and comfort compared to the fixed speed heat pump, there are still some shortcomings in some extremely extreme weather conditions.
  • the two-stage enthalpy system can overcome the above shortcomings by supplementing the gas. However, if the system is operated at any time, the performance will decrease under some conditions.
  • the present invention is directed to a method for controlling a two-stage heat pump system that improves energy efficiency.
  • the invention provides a two-stage heat pump system control method, comprising the following steps: detecting environmental parameters and/or system parameters of a two-stage heat pump system; and detecting environmental parameters and/or system parameters satisfying preset conditions At the same time, the two-stage heat pump system is controlled to close the boosting line.
  • the environmental parameters of the two-stage heat pump system include an ambient temperature; when the detected environmental parameters and/or system parameters meet the preset conditions, controlling the two-stage heat pump system to close the boosting pipeline includes: When the ambient temperature of the heat pump system is less than or equal to the preset temperature T1, the two-stage heat pump system is shut down to increase the temperature; when the two-stage heat pump system is in the heating cycle, When the detected ambient temperature is greater than or equal to the heating preset temperature T2, the two-stage heat pump system is controlled to close the boosting pipeline.
  • the range of the cooling preset temperature T1 is 16 ° C ⁇ T1 ⁇ 30 ° C; the range of the heating preset temperature T2 is 0 ° C ⁇ T2 ⁇ 20 ° C.
  • the system parameters of the two-stage heat pump system include the operating frequency of the two-stage booster compressor; and when the detected environmental parameters and/or system parameters meet the preset conditions, the control of the two-stage heat pump system is closed.
  • the pipeline includes: When the two-stage heat pump system is running a heating cycle or a refrigeration cycle, when the detected operating frequency is less than or equal to the preset frequency, the two-stage heat pump system is controlled to close the boosting pipeline.
  • the system parameters of the two-stage heat pump system include exhaust pressure and suction pressure; when the detected environmental parameters and/or system parameters meet the preset conditions, the two-stage heat pump system is controlled to close the boosting pipeline.
  • the method includes: controlling the two-stage heat pump system to close the boosting pipeline when the ratio of the exhaust pressure to the suction pressure is less than or equal to the preset system pressure ratio.
  • the system parameters of the two-stage heat pump system include the evaporation temperature and the condensation temperature of the outdoor unit; when the detected environmental parameters and/or system parameters meet the preset conditions, the two-stage heat pump system is controlled to close the tube.
  • the road includes: When the two-stage heat pump system runs the refrigeration cycle, the detected condensation temperature is less than or equal to 40 ° C, or the detected evaporation temperature is greater than or equal to 10 ° C, and the control two-stage heat pump system is closed. When the two-stage heat pump system is running and heating cycle, when the detected evaporation temperature is greater than or equal to o°c, the two-stage heat pump system is controlled to close the boosting pipeline.
  • the feedback adjustment system enhances the pipeline by detecting the system parameter or the environmental parameter and the preset condition, and when the preset preset condition is met, the heat pump system turns off the booster tube.
  • FIG. 1 is a schematic diagram of a refrigeration cycle of a heat pump air conditioning system of a two-stage heat pump system according to the present invention
  • FIG. 2 is a heat cycle of a heat pump air conditioning system or a heat pump water heater system of a two-stage heat pump system according to the present invention
  • schematic diagram is a schematic view showing a COP (energy efficiency ratio) of a two-stage heat pump system according to the present invention at different frequencies of opening and closing of a booster tube;
  • the method for controlling a two-stage heat pump system comprises the steps of: detecting environmental parameters and/or system parameters of a two-stage heat pump system; and when the detected environmental parameters and/or system parameters satisfy a preset condition, Control the two-stage heat pump system to close the enhanced pipeline. According to the actual operating efficiency characteristics of the two-stage heat pumping system, the invention adjusts the system to increase the pipeline through the actual working system parameters and environmental parameters.
  • the heat pump system is maintained at a higher energy efficiency ratio by controlling the boosting line of the two-stage boosting system to be closed at the energy efficiency inflection point.
  • the environmental parameters of the two-stage heat pump system mainly include the external environment temperature.
  • the control two-stage heat pump system is turned off.
  • the two-stage heat pump system is running and heating cycle, when the detected ambient temperature is greater than or equal to the heating preset temperature T2, the two-stage heat pump system is controlled to close the boosting pipeline.
  • the preset temperature T1 of the cooling range is 16 ⁇ 30°C.
  • the boosting pipeline When the ambient temperature is in the range of 16 ⁇ 30°C, according to the actual load of the system, the boosting pipeline is closed. , to ensure that the system operates in the range of higher energy efficiency; when adjusting the system heating cycle, the heating preset temperature T2 ranges from 0 °C to 20 °C, when the ambient temperature is in the range of 0t ⁇ 20°C, according to the actual system In the case of load, the pipeline is closed and the system is operated in a range with high energy efficiency.
  • the system parameters of the two-stage heat pump system include the operating frequency of the two-stage booster compressor.
  • curve S1 represents the energy efficiency ratio of the system opening and increasing at different frequencies
  • curve S2 represents the energy efficiency ratio of the system closing and increasing at different frequencies. It can be seen from the figure that S1 and S2 are at the frequency F. The time intersects, that is, the frequency F is the inflection point frequency. It can be seen from the figure that when the operating frequency of the system is lower than the inflection point frequency, the energy efficiency of the system shutdown is higher than that of the opening enhancement.
  • Table 1 Energy-efficiency ratios of the system for increasing and closing the boost at different frequencies Frequency CO
  • the frequency of the open enthalpy is 30 Hz
  • the energy efficiency ratio (COP) is 3.175
  • the calculated SEER season energy efficiency ratio
  • the frequency 31Hz COP is 3.497
  • the calculated SEER is 3.39. That is to say, at the low frequency, the energy efficiency ratio of the system is higher than that of the open operation.
  • the preset frequency F of the two-stage heat pump system is 10 50Hz.
  • the cooling environment temperature is higher than 30 ° C
  • the operating frequency is higher than 50 Hz
  • the heating environment temperature is lower than 0 ° C
  • the operating frequency is higher than 50 Hz
  • the system parameters of the two-stage heat pump system include the exhaust pressure and the suction pressure; when the ratio of the exhaust pressure to the suction pressure is less than or equal to the preset system pressure ratio, the two-stage heat pump system is controlled to close the boosting pipeline.
  • the curve S3 represents the energy efficiency ratio of the system opening and increasing in different system pressure ratios (the ratio of the exhaust pressure to the suction pressure)
  • the curve S4 represents the energy efficiency ratio of the system closing and increasing the ratio at different system pressure ratios.
  • the curve S3 and the curve S4 intersect when the system pressure ratio is N, that is, the preset system pressure ratio is N. It can be seen from the figure that when the system pressure ratio of the system is lower than the inflection point N, the energy efficiency of the system shutdown is higher than that of the opening enhancement. According to the actual load and environment, the preset system pressure ratio N ranges from 2.0 ⁇ N ⁇ 3.0.
  • the ratio of the system's exhaust pressure to the suction pressure is less than or equal to N, the system closes the boost line.
  • the ratio of exhaust pressure to suction pressure is greater than N, the system boost line is opened. When the system is increased, the pressure in the system flasher is Pm.
  • Embodiment 1 The two-stage heat pump system shown in FIGS.
  • the heat pump system further includes a flasher 5, the flasher 5 is connected to the outdoor heat exchanger 3 and the indoor heat exchanger 4 through a pipe, and the pipe is provided with throttle valves 7a, 7b to control the flow rate of the refrigerant entering the flasher 5, thereby controlling the flash The pressure inside the steamer 5.
  • the flasher 5 is connected to the compressor through a reinforced pipe, and the switch on the reinforced pipe is provided with a solenoid valve 6 to control the reinforced pipe.
  • the heat pump system is provided with a sensor for detecting the operating frequency of the system and a temperature sensor for detecting the ambient temperature, and the opening or closing of the enhanced pipeline section is controlled by the frequency value of the system operation and the ambient temperature value of the outdoor unit.
  • the preset ambient temperature of the heat pump system is 25 °C.
  • the solenoid valve 6 closes the boosting pipeline;
  • the preset frequency of the heat pump system is preset. 35HZ, when the operating frequency of the system is less than or equal to 35Hz, the solenoid valve 6 closes the boosting pipeline.
  • the solenoid valve opens the boosting line.
  • the preset ambient temperature of the heat pump system is 10 °C
  • the solenoid valve 6 closes the boosting pipeline.
  • the preset frequency of the heat pump system is preset to 35 Hz.
  • the solenoid valve 6 closes the reinforced pipeline. Only when the ambient temperature is less than 10 ° C and the operating frequency is greater than 35 Hz, the solenoid valve opens the boosting line.
  • Embodiment 2 In the two-stage heat pump system, the opening or closing of the reinforcing pipeline section is controlled by the frequency value of the system operation and the evaporation temperature and the condensation temperature value of the outdoor unit. Under refrigeration conditions, the heat pump system preset condensing temperature is 40 ° C, the evaporation temperature is 10 ° C, when the condensing temperature is lower than 40 ° C, or the evaporation temperature is higher than 10 ° C, the solenoid valve 6 closes the reinforced pipeline.
  • the preset frequency of the heat pump system is 35HZ.
  • the solenoid valve 6 closes the boosting pipeline, only when the condensation temperature is higher than 40 °C and the evaporation temperature is lower than 10 °C, and the operation
  • the solenoid valve opens the booster pipeline; under the heating condition, when the evaporation temperature is higher than 0°C, the solenoid valve 6 closes the booster pipeline, and when the running frequency is less than or equal to 35Hz, the solenoid valve is powered off.
  • the system closes the booster pipeline.
  • the solenoid valve is energized and the system boosting pipeline is opened. Table 2: Energy efficiency ratio of the system for opening and closing enthalpy at condensing and evaporating temperatures
  • Embodiment 3 In the two-stage heat pump system, the preset frequency of the heat pump system is 35HZ. When the operating frequency of the system is less than or equal to 35Hz, the solenoid valve 6 closes the boosting pipeline to make the heat pump system operate in energy efficiency.
  • the efficiency of the system is much higher than that of the operation.
  • the pressure in the system flasher is the intermediate pressure Pm.
  • the opening degree of the condenser outlet throttle valves 7a, 7b is feedback-adjusted, so that the Pm is controlled at 0.8 ⁇ 1.0 ⁇ . ⁇ . If the system closes the booster solenoid valve, the intermediate pressure is not adjusted.
  • the above-mentioned embodiments of the present invention achieve the following technical effects:
  • the two-stage increase The heat pump system has been increasing and the energy efficiency change will occur. That is, the energy efficiency ratio of the heat pump system is less than the energy efficiency ratio of the non-increased heat.
  • the present invention compares the system parameters or the environmental parameters with the preset conditions, and the feedback adjustment system enhances the pipeline. When the preset preset conditions are met, the heat pump system closes the boosting pipeline, so that the heat pump system operates at a higher energy efficiency ratio, thereby increasing heating or cooling capacity and reducing energy consumption.

Abstract

Disclosed is a method of controlling a heat pump system with two-stage enthalpy increase, comprising the following steps: detecting environmental parameters and/or system parameters of the heat pump system with two-stage enthalpy increase; and when the environmental parameters and/or system parameters detected meet preset conditions, controlling the heat pump system with two-stage enthalpy increase so that the enthalpy increase channel is closed. By comparing the system parameters or environmental parameters detected with preset conditions, the method of controlling the heat pump system with two-stage enthalpy increase, feedback regulates the enthalpy increase channel of the system and when preset conditions for the energy efficiency inflection point are met, the heat pump system closes the enthalpy increase channel, making the heat pump system work at a comparatively high energy efficiency ratio, thereby increasing the cooling or heating capacity, and reducing energy consumption.

Description

双级增焓热泵系统控制方法 技术领域 本发明涉及压缩机领域, 具体而言, 涉及一种双级增焓热泵系统控制方法。 背景技术 目前热泵产品在国家能效提升促进下,节能性能比以往更好了,变频技术的出现, 对启动后快速降温、升温, 环境温度的平稳控制都比定速热泵有了明显的进步, 而且, 技术可以避免频繁的停机和启动, 对节能和压缩机的可靠性都有较好的优势。 虽然变 频热泵在节能和舒适性上比定速热泵有了很明显的进步, 但是, 在一些恶劣极端的天 气条件下, 还是有一些不足。 例如: 高温制冷量、 超低温制热量等, 无法完全满足消 费者的需求。 双级增焓系统通过补气增焓能够克服以上缺点, 但是, 如果系统在任何时候都开 增焓运行, 则在有些条件下性能反而会降低。 发明内容 本发明旨在提供一种提高能效比的双级增焓热泵系统控制方法。 本发明提供了一种双级增焓热泵系统控制方法, 包括以下步骤: 检测双级增焓热 泵系统的环境参数和 /或系统参数; 当检测到的环境参数和 /或系统参数满足预设条件 时, 控制双级增焓热泵系统关闭增焓管路。 进一步地, 双级增焓热泵系统的环境参数包括环境温度; 当检测到的环境参数和 / 或系统参数满足预设条件时, 控制双级增焓热泵系统关闭增焓管路包括: 当双级增焓 热泵系统运行制冷循环时, 检测到的环境温度小于或者等于制冷预设温度 T1 时, 控 制双级增焓热泵系统关闭增焓管路; 当双级增焓热泵系统运行制热循环时, 检测到的 环境温度大于或等于制热预设温度 T2时, 控制双级增焓热泵系统关闭增焓管路。 进一步地, 制冷预设温度 T1 的范围为 16°C≤T1≤30°C ; 制热预设温度 T2的范围 为 0°C≤T2≤20°C。 进一步地, 制冷预设温度 T1=25 °C ; 制热预设温度 T2=10°C。 进一步地, 双级增焓热泵系统的系统参数包括双级增焓压缩机的运行频率; 当检 测到的环境参数和 /或系统参数满足预设条件时,控制双级增焓热泵系统关闭增焓管路 包括: 当双级增焓热泵系统运行制热循环或者制冷循环时, 检测到的运行频率小于或 等于预设频率时, 控制双级增焓热泵系统关闭增焓管路。 进一步地, 预设频率 F的范围为 10HZ≤F≤50HZ。 进一步地, 预设频率 F=35HZ。 进一步地, 双级增焓热泵系统的系统参数包括排气压力和吸气压力; 当检测到的 环境参数和 /或系统参数满足预设条件时, 控制双级增焓热泵系统关闭增焓管路包括: 当排气压力与吸气压力的比值小于或等于预设系统压比时, 控制双级增焓热泵系统关 闭增焓管路。 进一步地, 预设系统压比 N的范围为 1.5≤N≤3.0。 进一步地, 预设系统压比 N=2.2。 进一步地, 双级增焓热泵系统的系统参数包括室外机的蒸发温度和冷凝温度; 当 检测到的环境参数和 /或系统参数满足预设条件时,控制双级增焓热泵系统关闭增焓管 路包括: 当双级增焓热泵系统运行制冷循环时, 检测到的冷凝温度小于等于 40°C, 或 者检测到的蒸发温度大于或等于 10°C, 控制双级增焓热泵系统关闭增焓管路; 当双级 增焓热泵系统运行制热循环时, 检测到的蒸发温度大于或等于 o°c时, 控制双级增焓 热泵系统关闭增焓管路。 根据本发明的双级增焓热泵系统控制方法, 通过检测系统参数或者环境参数与预 设条件对比, 反馈调节系统增焓管路, 当满足预设的预设条件时, 热泵系统关闭增焓 管路, 使热泵系统工作在较高的能效比的状态下, 从而增加制热量, 减少能耗。 附图说明 构成本申请的一部分的附图用来提供对本发明的进一步理解, 本发明的示意性实 施例及其说明用于解释本发明, 并不构成对本发明的不当限定。 在附图中: 图 1是根据本发明的双级增焓热泵系统的热泵空调系统制冷循环示意图; 图 2是根据本发明的双级增焓热泵系统的热泵空调系统或热泵热水器系统制热循 环示意图; 图 3为根据本发明的双级增焓热泵系统在增焓管开启与关闭在不同频率下的 COP (能效比) 示意图; 以及 图 4为根据本发明的双级增焓热泵系统在增焓管开启与关闭在不同吸气压力与排 气压力比下的 COP示意图。 具体实施方式 下面将参考附图并结合实施例来详细说明本发明。 根据本发明的双级增焓热泵系统控制方法, 包括以下步骤: 检测双级增焓热泵系 统的环境参数和 /或系统参数; 当检测到的环境参数和 /或系统参数满足预设条件时,控 制双级增焓热泵系统关闭增焓管路。 本发明根据双级增焓热泵系统的实际运行效率特 点, 通过实际工作的系统参数和环境参数, 反馈调节系统增焓管路。 通过控制双级增 焓系统的增焓管路在能效拐点处关闭, 从而保持热泵系统以较高的能效比运行。 双级增焓热泵系统的环境参数主要包括外界环境温度, 当双级增焓热泵系统运行 制冷循环时, 检测到的环境温度小于或者等于制冷预设温度 T1 时, 控制双级增焓热 泵系统关闭增焓管路; 当双级增焓热泵系统运行制热循环时, 检测到的环境温度大于 或等于制热预设温度 T2时, 控制双级增焓热泵系统关闭增焓管路。 根据实际负载的不同情况, 热泵系统制冷循环时, 制冷预设温度 T1范围为 16〜 30°C, 当环境温度在 16〜30°C范围, 根据系统的实际负载情况, 对增焓管路关闭, 保 证系统在能效较高的范围段运行; 调系统制热循环时, 制热预设温度 T2范围为 0°C〜 20 °C , 当环境温度在 0t〜 20°C范围, 根据系统的实际负载情况, 对增焓管路关闭, 保证系统在能效高的范围段运行。 双级增焓热泵系统的系统参数包括双级增焓压缩机的运行频率, 当双级增焓热泵 系统运行制热循环或者制冷循环时, 检测到的运行频率小于或等于预设频率 F时, 控 制双级增焓热泵系统关闭增焓管路。 如图 3所示, 曲线 S1表示系统开启增焓在不同频率下的能效比, 曲线 S2表示系 统关闭增焓在不同频率下的能效比, 从图中可以看出, S1与 S2在频率为 F时相交, 即频率 F为拐点频率。 从图中可以看出, 当系统运行频率低于拐点频率时, 系统关闭 增焓的能效高于开启增焓的能效。 表 1 : 系统在不同频率下开启增焓和关闭增焓的能效比 频 CO BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the field of compressors, and in particular to a two-stage heat pump system control method. BACKGROUND OF THE INVENTION At present, the heat pump products are better promoted by the national energy efficiency improvement, and the energy-saving performance is better than before. The emergence of frequency conversion technology has a significant improvement over the fixed-speed heat pump, such as rapid cooling, temperature rise, and stable control of the ambient temperature after startup. Technology can avoid frequent shutdowns and starts, and has a good advantage for energy saving and compressor reliability. Although the variable frequency heat pump has made significant progress in energy saving and comfort compared to the fixed speed heat pump, there are still some shortcomings in some extremely extreme weather conditions. For example: high-temperature cooling capacity, ultra-low temperature heating, etc., can not fully meet the needs of consumers. The two-stage enthalpy system can overcome the above shortcomings by supplementing the gas. However, if the system is operated at any time, the performance will decrease under some conditions. SUMMARY OF THE INVENTION The present invention is directed to a method for controlling a two-stage heat pump system that improves energy efficiency. The invention provides a two-stage heat pump system control method, comprising the following steps: detecting environmental parameters and/or system parameters of a two-stage heat pump system; and detecting environmental parameters and/or system parameters satisfying preset conditions At the same time, the two-stage heat pump system is controlled to close the boosting line. Further, the environmental parameters of the two-stage heat pump system include an ambient temperature; when the detected environmental parameters and/or system parameters meet the preset conditions, controlling the two-stage heat pump system to close the boosting pipeline includes: When the ambient temperature of the heat pump system is less than or equal to the preset temperature T1, the two-stage heat pump system is shut down to increase the temperature; when the two-stage heat pump system is in the heating cycle, When the detected ambient temperature is greater than or equal to the heating preset temperature T2, the two-stage heat pump system is controlled to close the boosting pipeline. Further, the range of the cooling preset temperature T1 is 16 ° C ≤ T1 ≤ 30 ° C; the range of the heating preset temperature T2 is 0 ° C ≤ T2 ≤ 20 ° C. Further, the cooling preset temperature T1 = 25 ° C; the heating preset temperature T2 = 10 ° C. Further, the system parameters of the two-stage heat pump system include the operating frequency of the two-stage booster compressor; and when the detected environmental parameters and/or system parameters meet the preset conditions, the control of the two-stage heat pump system is closed. The pipeline includes: When the two-stage heat pump system is running a heating cycle or a refrigeration cycle, when the detected operating frequency is less than or equal to the preset frequency, the two-stage heat pump system is controlled to close the boosting pipeline. Further, the preset frequency F ranges from 10 Hz to F ≤ 50 Hz. Further, the preset frequency F=35HZ. Further, the system parameters of the two-stage heat pump system include exhaust pressure and suction pressure; when the detected environmental parameters and/or system parameters meet the preset conditions, the two-stage heat pump system is controlled to close the boosting pipeline. The method includes: controlling the two-stage heat pump system to close the boosting pipeline when the ratio of the exhaust pressure to the suction pressure is less than or equal to the preset system pressure ratio. Further, the preset system pressure ratio N ranges from 1.5 ≤ N ≤ 3.0. Further, the preset system pressure ratio is N=2.2. Further, the system parameters of the two-stage heat pump system include the evaporation temperature and the condensation temperature of the outdoor unit; when the detected environmental parameters and/or system parameters meet the preset conditions, the two-stage heat pump system is controlled to close the tube. The road includes: When the two-stage heat pump system runs the refrigeration cycle, the detected condensation temperature is less than or equal to 40 ° C, or the detected evaporation temperature is greater than or equal to 10 ° C, and the control two-stage heat pump system is closed. When the two-stage heat pump system is running and heating cycle, when the detected evaporation temperature is greater than or equal to o°c, the two-stage heat pump system is controlled to close the boosting pipeline. According to the control method of the two-stage heat pump system according to the present invention, the feedback adjustment system enhances the pipeline by detecting the system parameter or the environmental parameter and the preset condition, and when the preset preset condition is met, the heat pump system turns off the booster tube. Road, the heat pump system works in a higher energy efficiency ratio, thereby increasing heat production and reducing energy consumption. BRIEF DESCRIPTION OF THE DRAWINGS The accompanying drawings, which are incorporated in FIG. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram of a refrigeration cycle of a heat pump air conditioning system of a two-stage heat pump system according to the present invention; FIG. 2 is a heat cycle of a heat pump air conditioning system or a heat pump water heater system of a two-stage heat pump system according to the present invention; schematic diagram; 3 is a schematic view showing a COP (energy efficiency ratio) of a two-stage heat pump system according to the present invention at different frequencies of opening and closing of a booster tube; and FIG. 4 is a double-stage heat pumping system according to the present invention. Turn on and off the COP diagram at different suction pressure and exhaust pressure ratios. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail with reference to the accompanying drawings. The method for controlling a two-stage heat pump system according to the present invention comprises the steps of: detecting environmental parameters and/or system parameters of a two-stage heat pump system; and when the detected environmental parameters and/or system parameters satisfy a preset condition, Control the two-stage heat pump system to close the enhanced pipeline. According to the actual operating efficiency characteristics of the two-stage heat pumping system, the invention adjusts the system to increase the pipeline through the actual working system parameters and environmental parameters. The heat pump system is maintained at a higher energy efficiency ratio by controlling the boosting line of the two-stage boosting system to be closed at the energy efficiency inflection point. The environmental parameters of the two-stage heat pump system mainly include the external environment temperature. When the two-stage heat pump system runs the refrigeration cycle, when the detected ambient temperature is less than or equal to the cooling preset temperature T1, the control two-stage heat pump system is turned off. When the two-stage heat pump system is running and heating cycle, when the detected ambient temperature is greater than or equal to the heating preset temperature T2, the two-stage heat pump system is controlled to close the boosting pipeline. According to the actual load, when the heat pump system is in the refrigeration cycle, the preset temperature T1 of the cooling range is 16~30°C. When the ambient temperature is in the range of 16~30°C, according to the actual load of the system, the boosting pipeline is closed. , to ensure that the system operates in the range of higher energy efficiency; when adjusting the system heating cycle, the heating preset temperature T2 ranges from 0 °C to 20 °C, when the ambient temperature is in the range of 0t~20°C, according to the actual system In the case of load, the pipeline is closed and the system is operated in a range with high energy efficiency. The system parameters of the two-stage heat pump system include the operating frequency of the two-stage booster compressor. When the two-stage heat pump system is running a heating cycle or a refrigeration cycle, when the detected operating frequency is less than or equal to the preset frequency F, Control the two-stage heat pump system to close the enhanced pipeline. As shown in Fig. 3, curve S1 represents the energy efficiency ratio of the system opening and increasing at different frequencies, and curve S2 represents the energy efficiency ratio of the system closing and increasing at different frequencies. It can be seen from the figure that S1 and S2 are at the frequency F. The time intersects, that is, the frequency F is the inflection point frequency. It can be seen from the figure that when the operating frequency of the system is lower than the inflection point frequency, the energy efficiency of the system shutdown is higher than that of the opening enhancement. Table 1: Energy-efficiency ratios of the system for increasing and closing the boost at different frequencies Frequency CO
压缩机 能力 功率 备注  Compressor capacity power remarks
P 额定制冷 2590. 1005. 2.57 开增  P rated cooling 2590. 1005. 2.57 increase
61  61
里 9 9 6 焓  Lane 9 9 6 焓
QXAT-A0 3.17 开增  QXAT-A0 3.17 increase
30 415.3  30 415.3
75 5  75 5
中间制冷 焓  Intermediate refrigeration
里 3.49 关增  3.49 Guanzeng
31 369  31 369
7 焓 从表 1 的数据可以看出, 在中间制冷量测试中, 开增焓的频率为 30Hz, 能效比 ( COP)为 3.175,计算 SEER (季节能效比)为 3.215 ;而关闭增焓运行时,频率 31Hz COP为 3.497, 计算 SEER为 3.39。 即在低频下系统关增焓的能效比要高于开增焓运 行。 ο' 根据实际负载的不同情况, 双级增焓热泵系统的预设频率 F的范围为 10 50Hz 当热泵系统运行频率范围为 10 50Hz,根据系统的实际负载情况,可对增焓管路关闭, 保证系统在能效高的范围段运行。 一般地, 制冷环境温度高于 30°C, 运行频率高于 50Hz, 或者, 制热环境温度低于 0°C, 运行频率高于 50Hz, 系统均需要打开增焓运行。 双级增焓热泵系统的系统参数包括排气压力和吸气压力; 当排气压力与吸气压力 的比值小于或等于预设系统压比时, 控制双级增焓热泵系统关闭增焓管路。 如图 4所 示, 曲线 S3表示系统开启增焓在不同系统压比(排气压力与吸气压力的比值)下的能 效比, 曲线 S4表示系统关闭增焓在不同系统压比下的能效比, 从图 4中可以看出, 曲 线 S3与曲线 S4在系统压比为 N时相交, 即预设系统压比为 N。 从图中可以看出, 当 系统运行的系统压比低于拐点 N时, 系统关闭增焓的能效高于开启增焓的能效。 根据 实际负载和环境, 预设系统压比 N的范围为 2.0≤N≤3.0。 当系统的排气压力与吸气压 力的比值小于或者等于 N时, 系统关闭增焓管路。 当排气压力与吸气压力的比值大于 N时, 系统增焓管路打开。 当系统增焓管路打开运行时, 系统闪蒸器内的压力为 Pm 通过监测 Pm 的值来反馈调节冷凝器出口节流阀的开度, 使 Pm 控制在 0.8 l 0 /Pd PS (其中, Μ为排气压力, PS为吸气压力)。 本发明根据双级增焓系统的实际运行效率特点, 通过实际工作的负荷条件, 反馈 调节系统增焓管路。 通过控制双级增焓系统的增焓管路的打开或关闭, 保证系统处于 一个较高的能效比下运行。 下面结合本发明的具体实施例介绍本发明: 实施例 1 : 如图 1和图 2所示的双级增焓热泵系统包括: 双级增焓压缩机 1, 以及 通过管道和四通阀 2与压缩机 1相互连接的室外换热器 3和室内换热器 4。 热泵系统 还包括闪蒸器 5, 闪蒸器 5与室外换热器 3和室内换热器 4通过管道连通, 管道上设 置有节流阀 7a、 7b控制进入闪蒸器 5的冷媒的流量, 从而控制闪蒸器 5内部的压力。 闪蒸器 5与压缩机通过增焓管道连接, 增焓管道上设置有电磁阀 6控制增焓管道的开 关。 热泵系统中设置有检测系统运行频率的传感器和检测环境温度的温度传感器, 通 过系统运行的频率值和室外机所处的环境温度值控制增焓管路段的打开或者关闭。 如 图 1所示, 制冷条件下, 热泵系统预设的环境温度为 25 °C, 当环境温度小于等于 25 °C 时, 电磁阀 6关闭增焓管路; 热泵系统预设的预设频率为 35HZ, 当系统的运行频率小 于等于 35Hz时, 电磁阀 6关闭增焓管路。 只有当环境温度高于 25 °C且运行频率大于 35Hz时, 电磁阀才打开增焓管路。 如图 2所示, 制热条件下, 热泵系统预设的环境温 度为 10°C, 当环境温度大于等于 10°C时, 电磁阀 6关闭增焓管路。热泵系统预设的预 设频率为 35HZ, 当系统的运行频率小于等于 35Hz时, 电磁阀 6关闭增焓管路。 只有 当环境温度小于 10°C且运行频率大于 35Hz时, 电磁阀才打开增焓管路。 实施例 2: 在双级增焓热泵系统中, 通过系统运行的频率值和室外机的蒸发温度、 冷凝温度值控制增焓管路段的打开或者关闭。 制冷条件下, 热泵系统预设的冷凝温度 为 40°C, 蒸发温度为 10°C, 当冷凝温度低于 40°C, 或者蒸发温度高于 10°C, 电磁阀 6关闭增焓管路。热泵系统预设的预设频率为 35HZ,当系统的运行频率小于等于 35Hz 时, 电磁阀 6关闭增焓管路, 仅当冷凝温度高于 40°C而蒸发温度低于 10°C, 且运行频 率高于 35Hz时, 电磁阀打开增焓管路; 制热条件下, 当蒸发温度高于 0°C时, 电磁阀 6关闭增焓管路, 当运行频率小于等于 35Hz时, 电磁阀断电, 系统关闭增焓管路, 仅 当蒸发温度低于 0°C, 且运行频率高于 35 Hz时, 电磁阀通电, 系统增焓管路打开。 表 2: 系统对应冷凝和蒸发温度下开启增焓和关闭增焓的能效比 7 焓 From the data in Table 1, it can be seen that in the intermediate cooling capacity test, the frequency of the open enthalpy is 30 Hz, the energy efficiency ratio (COP) is 3.175, and the calculated SEER (season energy efficiency ratio) is 3.215; The frequency 31Hz COP is 3.497, and the calculated SEER is 3.39. That is to say, at the low frequency, the energy efficiency ratio of the system is higher than that of the open operation. ο' According to the actual load, the preset frequency F of the two-stage heat pump system is 10 50Hz. When the operating frequency range of the heat pump system is 10 50Hz, according to the actual load of the system, the boosting pipeline can be closed. Ensure that the system operates in a range of high energy efficiency. Generally, the cooling environment temperature is higher than 30 ° C, the operating frequency is higher than 50 Hz, or the heating environment temperature is lower than 0 ° C, the operating frequency is higher than 50 Hz, and the system needs to open the increased operation. The system parameters of the two-stage heat pump system include the exhaust pressure and the suction pressure; when the ratio of the exhaust pressure to the suction pressure is less than or equal to the preset system pressure ratio, the two-stage heat pump system is controlled to close the boosting pipeline. . As shown in Fig. 4, the curve S3 represents the energy efficiency ratio of the system opening and increasing in different system pressure ratios (the ratio of the exhaust pressure to the suction pressure), and the curve S4 represents the energy efficiency ratio of the system closing and increasing the ratio at different system pressure ratios. As can be seen from FIG. 4, the curve S3 and the curve S4 intersect when the system pressure ratio is N, that is, the preset system pressure ratio is N. It can be seen from the figure that when the system pressure ratio of the system is lower than the inflection point N, the energy efficiency of the system shutdown is higher than that of the opening enhancement. According to the actual load and environment, the preset system pressure ratio N ranges from 2.0 ≤ N ≤ 3.0. When the ratio of the system's exhaust pressure to the suction pressure is less than or equal to N, the system closes the boost line. When the ratio of exhaust pressure to suction pressure is greater than N, the system boost line is opened. When the system is increased, the pressure in the system flasher is Pm. By monitoring the value of Pm, feedback adjusts the opening of the condenser outlet throttle valve, so that Pm is controlled at 0.8 l 0 /Pd P S (where Μ is the exhaust pressure, P S is the suction pressure). According to the actual operating efficiency characteristics of the two-stage enthalpy system, the invention adjusts the system to increase the pipeline through the actual working load conditions. By controlling the opening or closing of the boosting line of the two-stage boosting system, the system is guaranteed to operate at a higher energy efficiency ratio. The invention is described below in connection with specific embodiments of the invention: Embodiment 1: The two-stage heat pump system shown in FIGS. 1 and 2 includes: a two-stage booster compressor 1, and an outdoor heat exchanger 3 interconnected with the compressor 1 through a pipe and a four-way valve 2; Indoor heat exchanger 4. The heat pump system further includes a flasher 5, the flasher 5 is connected to the outdoor heat exchanger 3 and the indoor heat exchanger 4 through a pipe, and the pipe is provided with throttle valves 7a, 7b to control the flow rate of the refrigerant entering the flasher 5, thereby controlling the flash The pressure inside the steamer 5. The flasher 5 is connected to the compressor through a reinforced pipe, and the switch on the reinforced pipe is provided with a solenoid valve 6 to control the reinforced pipe. The heat pump system is provided with a sensor for detecting the operating frequency of the system and a temperature sensor for detecting the ambient temperature, and the opening or closing of the enhanced pipeline section is controlled by the frequency value of the system operation and the ambient temperature value of the outdoor unit. As shown in Fig. 1, under the cooling condition, the preset ambient temperature of the heat pump system is 25 °C. When the ambient temperature is less than or equal to 25 °C, the solenoid valve 6 closes the boosting pipeline; the preset frequency of the heat pump system is preset. 35HZ, when the operating frequency of the system is less than or equal to 35Hz, the solenoid valve 6 closes the boosting pipeline. Only when the ambient temperature is higher than 25 °C and the operating frequency is greater than 35 Hz, the solenoid valve opens the boosting line. As shown in Fig. 2, under the heating condition, the preset ambient temperature of the heat pump system is 10 °C, and when the ambient temperature is greater than or equal to 10 °C, the solenoid valve 6 closes the boosting pipeline. The preset frequency of the heat pump system is preset to 35 Hz. When the operating frequency of the system is less than or equal to 35 Hz, the solenoid valve 6 closes the reinforced pipeline. Only when the ambient temperature is less than 10 ° C and the operating frequency is greater than 35 Hz, the solenoid valve opens the boosting line. Embodiment 2: In the two-stage heat pump system, the opening or closing of the reinforcing pipeline section is controlled by the frequency value of the system operation and the evaporation temperature and the condensation temperature value of the outdoor unit. Under refrigeration conditions, the heat pump system preset condensing temperature is 40 ° C, the evaporation temperature is 10 ° C, when the condensing temperature is lower than 40 ° C, or the evaporation temperature is higher than 10 ° C, the solenoid valve 6 closes the reinforced pipeline. The preset frequency of the heat pump system is 35HZ. When the operating frequency of the system is less than or equal to 35Hz, the solenoid valve 6 closes the boosting pipeline, only when the condensation temperature is higher than 40 °C and the evaporation temperature is lower than 10 °C, and the operation When the frequency is higher than 35Hz, the solenoid valve opens the booster pipeline; under the heating condition, when the evaporation temperature is higher than 0°C, the solenoid valve 6 closes the booster pipeline, and when the running frequency is less than or equal to 35Hz, the solenoid valve is powered off. The system closes the booster pipeline. When the evaporation temperature is lower than 0 °C and the operating frequency is higher than 35 Hz, the solenoid valve is energized and the system boosting pipeline is opened. Table 2: Energy efficiency ratio of the system for opening and closing enthalpy at condensing and evaporating temperatures
Figure imgf000007_0001
Figure imgf000007_0001
从表 2可以看出, 在冷凝温度为 38°C, 蒸发温度为 13 °C, 频率 31Hz的条件下, 开增焓的 COP为 3.189, 而关增焓的 COP则达到 3.497, 提高 0.31左右。 即在以上条 件下系统关增焓运行的效率远高于开增焓运行。 实施例 3 : 在双级增焓热泵系统中, 热泵系统预设的预设频率为 35HZ, 当系统的 运行频率小于等于 35Hz时, 电磁阀 6关闭增焓管路, 使热泵系统运行在能效比较高 的不增焓状态; 当系统的排气压力 Pd与吸气压力 Ps的比值小于等于 2.2时, 电磁阀 6 关闭增焓管路, 此时系统能效比高于开启增焓管路时的能效比。 当运行频率高于 35Hz 而且排气压力 Pd与吸气压力 Ps的比值大于 2.2时, 电磁阀打开增焓管路。 表 3 : 系统在低压力比下开启增焓和关闭增焓的能效比 It can be seen from Table 2 that under the conditions of condensing temperature of 38 ° C, evaporation temperature of 13 ° C and frequency of 31 Hz, the COP of open enthalpy is 3.189, while the COP of Guan Zeng 达到 is 3.497, which is increased by about 0.31. That is to say, under the above conditions, the efficiency of the system is much higher than that of the operation. Embodiment 3: In the two-stage heat pump system, the preset frequency of the heat pump system is 35HZ. When the operating frequency of the system is less than or equal to 35Hz, the solenoid valve 6 closes the boosting pipeline to make the heat pump system operate in energy efficiency. High non-increased state; When the ratio of the system's exhaust pressure Pd to the suction pressure Ps is less than or equal to 2.2, the solenoid valve 6 closes the boosting line, and the energy efficiency ratio of the system is higher than that when the boosting line is opened. ratio. When the operating frequency is higher than 35 Hz and the ratio of the exhaust pressure Pd to the suction pressure Ps is greater than 2.2, the solenoid valve opens the boosting line. Table 3: Energy efficiency ratio of the system to increase and decrease the growth at low pressure ratio
Figure imgf000008_0001
Figure imgf000008_0001
从表 3可以看出,在排气压力为 2.284MPa,吸气温度为 1.18MPa,压力比为 1.94, 频率 31Hz的条件下, 开增焓的 COP为 3.189, 而关增焓的 COP则达到 3.497, 提高 It can be seen from Table 3 that under the conditions of exhaust pressure of 2.284 MPa, suction temperature of 1.18 MPa, pressure ratio of 1.94, frequency of 31 Hz, the COP of open enthalpy is 3.189, and the COP of Guanzeng 达到 is 3.497. Increase
0.31左右。 即在以上条件下系统关增焓运行的效率远高于开增焓运行。 当系统增焓管路打开运行时, 系统闪蒸器内的压力为中间压力 Pm, 通过监测 Pm 的值来反馈调节冷凝器出口节流阀 7a、 7b的开度, 使 Pm控制在 0.8〜1.0^^。 如果系统关闭增焓电磁阀运行, 则不进行中间压力的调节。 从以上的描述中, 可以看出, 本发明上述的实施例实现了如下技术效果: 根据本发明的双级增焓热泵系统控制方法, 当系统参数或者环境参数满足预设条 件时, 双级增焓热泵系统一直增焓会出现能效变化, 即热泵系统增焓的能效比小于不 增焓的能效比, 本发明通过检测系统参数或者环境参数与预设条件对比, 反馈调节系 统增焓管路, 当满足预设的预设条件时, 热泵系统关闭增焓管路, 使热泵系统工作在 较高的能效比的状态下, 从而增加制热或者制冷量, 减少能耗。 以上所述仅为本发明的优选实施例而已, 并不用于限制本发明, 对于本领域的技 术人员来说, 本发明可以有各种更改和变化。 凡在本发明的精神和原则之内, 所作的 任何修改、 等同替换、 改进等, 均应包含在本发明的保护范围之内。 Around 0.31. That is to say, under the above conditions, the efficiency of the system is much higher than that of the operation. When the system is opened and the pipeline is opened, the pressure in the system flasher is the intermediate pressure Pm. By monitoring the value of Pm, the opening degree of the condenser outlet throttle valves 7a, 7b is feedback-adjusted, so that the Pm is controlled at 0.8~1.0^. ^. If the system closes the booster solenoid valve, the intermediate pressure is not adjusted. From the above description, it can be seen that the above-mentioned embodiments of the present invention achieve the following technical effects: According to the control method of the two-stage heat pump system according to the present invention, when the system parameters or environmental parameters meet the preset conditions, the two-stage increase The heat pump system has been increasing and the energy efficiency change will occur. That is, the energy efficiency ratio of the heat pump system is less than the energy efficiency ratio of the non-increased heat. The present invention compares the system parameters or the environmental parameters with the preset conditions, and the feedback adjustment system enhances the pipeline. When the preset preset conditions are met, the heat pump system closes the boosting pipeline, so that the heat pump system operates at a higher energy efficiency ratio, thereby increasing heating or cooling capacity and reducing energy consumption. The above description is only a preferred embodiment of the present invention, and is not intended to limit the present invention, and various modifications and changes can be made to the present invention. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and scope of the present invention are intended to be included within the scope of the present invention.

Claims

权 利 要 求 书 Claim
1. 一种双级增焓热泵系统控制方法, 其特征在于, 所述方法包括以下步骤: 检测双级增焓热泵系统的环境参数和 /或系统参数; A method for controlling a two-stage heat pump system, characterized in that the method comprises the steps of: detecting environmental parameters and/or system parameters of a two-stage heat pump system;
当检测到的所述环境参数和 /或所述系统参数满足预设条件时,控制所述双 级增焓热泵系统关闭增焓管路。  The dual-stage heat pump system is controlled to close the boosting pipeline when the detected environmental parameter and/or the system parameter meets a preset condition.
2. 根据权利要求 1所述的双级增焓热泵系统控制方法, 其特征在于, 2. The method of controlling a two-stage heat pump system according to claim 1, wherein:
所述双级增焓热泵系统的环境参数包括环境温度;  The environmental parameters of the two-stage heat pump system include an ambient temperature;
当检测到的所述环境参数和 /或所述系统参数满足预设条件时,控制双级增 焓热泵系统关闭增焓管路包括:  When the detected environmental parameter and/or the system parameter meet the preset condition, controlling the dual-stage heat pump system to close the boosting pipeline includes:
当所述双级增焓热泵系统运行制冷循环时, 检测到的所述环境温度小于或 者等于制冷预设温度 T1时, 控制所述双级增焓热泵系统关闭增焓管路;  When the two-stage heat pump system runs a refrigeration cycle, when the detected ambient temperature is less than or equal to the cooling preset temperature T1, the two-stage heat pump system is controlled to close the boosting pipeline;
当所述双级增焓热泵系统运行制热循环时, 检测到的所述环境温度大于或 等于制热预设温度 T2时, 控制所述双级增焓热泵系统关闭增焓管路。  When the two-stage heat pump system is in the heating cycle, when the detected ambient temperature is greater than or equal to the heating preset temperature T2, the two-stage heat pump system is controlled to close the boosting pipeline.
3. 根据权利要求 2所述的双级增焓热泵系统控制方法, 其特征在于, 3. The method of controlling a two-stage heat pump system according to claim 2, wherein
所述制冷预设温度 T1的范围为 16°C≤T1≤30°C ;  The cooling preset temperature T1 ranges from 16 ° C ≤ T1 ≤ 30 ° C;
所述制热预设温度 T2的范围为 0°C≤T2≤20°C。  The heating preset temperature T2 ranges from 0 °C ≤ T2 ≤ 20 °C.
4. 根据权利要求 3所述的双级增焓热泵系统控制方法, 其特征在于,  4. The method of controlling a two-stage heat pump system according to claim 3, wherein
所述制冷预设温度 T1=25 °C ;  The cooling preset temperature T1=25 °C;
所述制热预设温度 T2=10°C。  The heating preset temperature T2 = 10 °C.
5. 根据权利要求 1所述的双级增焓热泵系统控制方法, 其特征在于,  5. The method of controlling a two-stage heat pump system according to claim 1, wherein:
所述双级增焓热泵系统的系统参数包括双级增焓压缩机的运行频率; 当检测到的所述环境参数和 /或所述系统参数满足预设条件时,控制双级增 焓热泵系统关闭增焓管路包括:  The system parameters of the two-stage heat pump system include the operating frequency of the two-stage booster compressor; and when the detected environmental parameters and/or the system parameters meet the preset conditions, the two-stage heat pump system is controlled. Closing the booster pipeline includes:
当所述双级增焓热泵系统运行制热循环或者制冷循环时, 检测到的所述运 行频率小于或等于预设频率 F时, 控制所述双级增焓热泵系统关闭增焓管路。 When the two-stage heat pump system runs a heating cycle or a refrigeration cycle, when the detected operating frequency is less than or equal to the preset frequency F, the two-stage heat pump system is controlled to close the boosting pipeline.
6. 根据权利要求 5所述的双级增焓热泵系统控制方法, 其特征在于, 6. The method of controlling a two-stage heat pump system according to claim 5, wherein
所述预设频率 F的范围为 10HZ≤F≤50HZ。  The preset frequency F ranges from 10HZ ≤ F ≤ 50HZ.
7. 根据权利要求 6所述的双级增焓热泵系统控制方法, 其特征在于, 7. The method of controlling a two-stage heat pump system according to claim 6, wherein:
所述预设频率 F=35HZ。  The preset frequency F = 35HZ.
8. 根据权利要求 1所述的双级增焓热泵系统控制方法, 其特征在于, 8. The method of controlling a two-stage heat pump system according to claim 1, wherein:
所述双级增焓热泵系统的系统参数包括排气压力和吸气压力; 当检测到的所述环境参数和 /或所述系统参数满足预设条件时,控制双级增 焓热泵系统关闭增焓管路包括:  The system parameters of the two-stage heat pump system include exhaust pressure and suction pressure; when the detected environmental parameters and/or the system parameters meet preset conditions, controlling the two-stage heat pump system to increase The pipeline includes:
当所述排气压力与所述吸气压力的比值小于或等于预设系统压比时, 控制 所述双级增焓热泵系统关闭增焓管路。  When the ratio of the exhaust pressure to the suction pressure is less than or equal to a preset system pressure ratio, the two-stage heat pump system is controlled to close the boost line.
9. 根据权利要求 8所述的双级增焓热泵系统控制方法, 其特征在于, 9. The method of controlling a two-stage heat pump system according to claim 8, wherein:
所述预设系统压比 N的范围为 1.5≤N≤3.0。  The preset system pressure ratio N ranges from 1.5 ≤ N ≤ 3.0.
10. 根据权利要求 9所述的双级增焓热泵系统控制方法, 其特征在于, 10. The method of controlling a two-stage heat pump system according to claim 9, wherein:
所述预设系统压比 N=2.2。  The preset system pressure ratio is N=2.2.
11. 根据权利要求 1所述的双级增焓热泵系统控制方法, 其特征在于, 11. The method of controlling a two-stage heat pump system according to claim 1, wherein:
所述双级增焓热泵系统的系统参数包括室外机的蒸发温度和冷凝温度; 当检测到的所述环境参数和 /或所述系统参数满足预设条件时,控制双级增 焓热泵系统关闭增焓管路包括:  The system parameters of the two-stage heat pump system include an evaporation temperature and a condensation temperature of the outdoor unit; and when the detected environmental parameter and/or the system parameter meet the preset condition, the dual-stage heat pump system is controlled to be closed. Enhancement pipelines include:
当所述双级增焓热泵系统运行制冷循环时, 检测到的所述冷凝温度小于等 于 40°C,或者检测到的所述蒸发温度大于或等于 10°C,控制所述双级增焓热泵 系统关闭增焓管路;  When the two-stage heat pump system is operated in a refrigeration cycle, the detected condensation temperature is less than or equal to 40 ° C, or the detected evaporation temperature is greater than or equal to 10 ° C, and the two-stage heat pump is controlled. The system closes the boosting pipeline;
当所述双级增焓热泵系统运行制热循环时, 检测到的所述蒸发温度大于或 等于 0°C时, 控制所述双级增焓热泵系统关闭增焓管路。  When the two-stage heat pump system is in a heating cycle, when the detected evaporation temperature is greater than or equal to 0 ° C, the two-stage heat pump system is controlled to close the augmentation pipeline.
PCT/CN2012/086191 2012-02-14 2012-12-07 Method of controlling a heat pump system with two-stage enthalpy increase WO2013120375A1 (en)

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