CN202501677U - Steam compression refrigeration device driven by organic Rankine cycle - Google Patents

Abstract

The utility model discloses a steam compression refrigeration device driven by organic Rankine cycle. An organic Rankine cycle system is formed by sequentially connecting a booster pump, a first evaporator, an expander, a first condenser and a first liquid storage tank from end to end; a steam compression refrigeration cycle system is formed by sequentially connecting a second condenser, a second liquid storage tank, a throttle valve, a second evaporator, a first valve and an open-type refrigeration compressor from end to end; the expander is connected with the open-type refrigeration compressor by a transmission device; and an outlet of the second evaporator, an electrodynamic-type refrigeration compressor and an inlet of the second condenser are sequentially connected. The utility model organically combines the organic Rankine cycle system and the steam compression refrigeration system so as to realize thermally driven refrigeration, having the advantages of ability of using low-grade heat sources such as geothermal energy, solar energy, biomass burning, industrial waste heat, engine exhaust waste heat and the like, compact structure of the system, wide application range in respects of refrigeration temperature and refrigeration amount, ability of getting high refrigeration efficiency, and the like.

Description

Vapor Compression Refrigeration Device Driven by Organic Rankine Cycle

technical field

The utility model relates to heat-driven refrigeration, in particular to a vapor compression refrigeration device driven by an organic Rankine cycle.

Background technique

Energy shortage and global warming are becoming more and more serious, threatening the survival and development of human beings, and have become the two most concerned issues in the world today. In China, in order to deal with these two major problems, it is actively implementing energy conservation and emission reduction strategies, which not only meet the development requirements of contemporary people, but also ensure that the survival and development rights of future generations will not be endangered in terms of resources and environment, and strive to achieve long-term sustainable development. develop. From a technical point of view, in order to cope with energy shortages and climate warming, scientists and technicians from various countries are constantly creating various emerging technologies and developing vigorously, such as: clean utilization technologies of fossil energy, various renewable energy sources (solar energy, wind energy, etc.) , biomass energy, tidal energy, etc.) utilization technology, nuclear fusion energy utilization technology, etc. In addition to the development of new energy sources, strengthening the recovery and utilization of low-grade heat is also an important way to achieve energy conservation and emission reduction. A large number of new solutions for power generation using low-temperature heat sources have been proposed, and among these solutions, the organic Rankine cycle system is the most widely used.

The so-called organic Rankine cycle is a Clausius-Rankine cycle that uses organic working fluid instead of water, including evaporation process from liquid to gaseous state, gaseous state expansion process, gaseous state to liquid state condensation process and liquid state pressurization process. Since the organic working fluid selected by the ORC system has a lower boiling point than water, relatively high efficiency can be achieved at a lower heat source temperature. The temperature of low-grade heat sources that can be used to drive the organic Rankine cycle system is generally close to 100°C to 300°C, including geothermal, solar energy, biomass combustion, industrial waste heat, engine exhaust waste heat, etc., and has flexible installations, which can be applied to small and medium scale (kW level) applications and other advantages. It can be seen that vigorously developing organic Rankine cycle technology and strengthening the utilization of low-grade heat sources is one of the effective ways to achieve energy saving and emission reduction.

Commercial organic Rankine cycle system products began to appear in the 1980s and showed rapid growth. According to statistics, as of 2009, the total installed capacity of organic Rankine cycle power generation in the world was about 1600MW, mainly MW-level devices. Due to the different temperatures of the driving heat source, the current power generation efficiency of the organic Rankine cycle system is in the range of about 6-17%. In addition to being used for power generation, the organic Rankine cycle is also used in combination with the reverse osmosis seawater desalination process to construct a solar heat collection-driven seawater desalination system. At present, the research focus of the United States, Germany, Italy, Belgium, Japan, etc. on the organic Rankine cycle is mainly on the research and development of high-performance, environmentally friendly organic working fluids suitable for low-temperature heat sources, high-efficiency expansion devices for kW-level small and medium-scale applications, and the exploration of organic Rankine cycles. The comprehensive low-grade heat source utilization technology combined with Ken cycle and other technologies can expand the application field of ORC.

In the general refrigeration temperature range, vapor compression refrigeration is the dominant refrigeration method, and has been widely used in refrigerators, air conditioners, cold storage and other fields. Vapor compression refrigeration generally mainly uses electric refrigeration compressors, which are driven by electric energy to achieve refrigeration. The vapor compression refrigeration system used in automotive air conditioners is rather special. It uses the mechanical power output by the engine to drive an open refrigeration compressor to achieve vapor compression refrigeration. In order to realize the utilization of low-grade heat sources, in the field of refrigeration, absorption refrigeration technology and adsorption refrigeration technology directly driven by heat energy have been developed, which have also been applied in air conditioners, refrigerators and other fields.

Contents of the invention

The purpose of the utility model is to overcome the deficiencies of the prior art and provide a vapor compression refrigeration device driven by an organic Rankine cycle.

The vapor compression refrigeration device driven by organic Rankine cycle includes a booster pump, a first evaporator, an expander, a first condenser, a first liquid storage tank, a transmission device, a second condenser, a second liquid storage tank, a section Flow valve, second evaporator, first valve, open refrigeration compressor, second valve, electric refrigeration compressor; booster pump, first evaporator, expander, first condenser, first liquid storage tank The organic Rankine cycle system is formed by connecting end to end; the second condenser, the second liquid storage tank, the throttle valve, the second evaporator, the first valve, and the open refrigeration compressor are connected end to end in order to form a vapor compression refrigeration cycle system The expander is connected with the open refrigeration compressor through the transmission device; the outlet of the second evaporator, the electric refrigeration compressor and the inlet of the second condenser are connected in sequence.

The utility model organically combines the organic Rankine cycle system and the vapor compression refrigeration system to realize heat-driven refrigeration, and has low-grade heat sources that can be used (such as: geothermal energy, solar energy, biomass combustion, industrial waste heat, engine exhaust waste heat, etc.) , the system is compact in structure, suitable for a wide range of cooling temperature and cooling capacity, and can obtain high cooling efficiency and other advantages.

Description of drawings

1 is a schematic diagram of a vapor compression refrigeration device driven by an organic Rankine cycle;

In the figure: booster pump 1, first evaporator 2, expander 3, first condenser 4, first liquid storage tank 5, transmission device 6, second condenser 7, second liquid storage tank 8, throttling Valve 9, second evaporator 10, first valve 11, open refrigeration compressor 12, second valve 13, electric refrigeration compressor 14.

Detailed ways

As shown in the figure, the vapor compression refrigeration device driven by organic Rankine cycle includes a booster pump 1, a first evaporator 2, an expander 3, a first condenser 4, a first liquid storage tank 5, a transmission device 6, a first Second condenser 7, second liquid storage tank 8, throttle valve 9, second evaporator 10, first valve 11, open refrigeration compressor 12, second valve 13, electric refrigeration compressor 14; booster pump 1. The first evaporator 2, the expander 3, the first condenser 4, and the first liquid storage tank 5 are sequentially connected end to end to form an organic Rankine cycle system; the second condenser 7, the second liquid storage tank 8, the throttling The valve 9, the second evaporator 10, the first valve 11, and the open refrigeration compressor 12 are sequentially connected end to end to form a vapor compression refrigeration cycle system; the expander 3 is connected to the open refrigeration compressor 12 through the transmission device 6; The outlet of the evaporator 10, the electric refrigeration compressor 14, and the inlet of the second condenser 7 are connected in sequence.

The vapor compression refrigeration method driven by the organic Rankine cycle is: use the organic Rankine cycle system to convert low-grade heat energy into mechanical work, and transfer the mechanical work output by the expander 3 of the organic Rankine cycle system to the vapor through the transmission device 6 The open-type refrigeration compressor 12 of the compression refrigeration cycle drives the vapor compression refrigeration cycle system, thereby realizing heat-driven vapor compression refrigeration; the second valve 13 and the electric refrigeration compressor 14 are formed with the first valve 11 and the open-type refrigeration compressor 12 Parallel structure, when the heat-driven vapor compression refrigeration cannot meet the cooling capacity required by the user, open the second valve 13 and the electric refrigeration compressor 14, and increase the refrigeration capacity of the vapor compression refrigeration system through the compressor driven by auxiliary electric energy, thereby realizing Stable cooling output to meet user needs.

In the vapor compression refrigeration device driven by the organic Rankine cycle, the organic Rankine cycle system can use R134a, R245fa, R123, n-pentane and silicone oil as working fluids. The vapor compression refrigeration system can use R22, R134a, R32, etc. as the working fluid.

Below in conjunction with accompanying drawing 1, the concrete operating process of the present utility model is further described:

When the organic Rankine cycle-driven vapor compression refrigeration device is in operation, the low-grade heat source of the first evaporator 2, the ambient cold source of the first condenser 4 and the second condenser 7, and the low-temperature heat source of the second evaporator 10 are connected. , open the first valve 11, close the second valve 13, and start the booster pump 1. The organic working medium of the organic Rankine cycle system absorbs the heat from the heat source in the first evaporator 2 and changes from a liquid state to a gaseous state; after that, the high-temperature and high-pressure gaseous organic working medium enters the expander 3 for expansion and is output in the form of shaft work Mechanical work; the gaseous organic working medium after expansion and cooling enters the first condenser 4, and after being condensed from a gaseous state to a liquid state by an ambient cold source, enters the first liquid storage tank 5; the low-pressure liquid organic working medium flowing out of the first liquid storage tank 5 The substance is boosted by the booster pump 1 into a high-pressure liquid working medium, and then sent to the first evaporator 2 for evaporation; this cycle repeats to complete the conversion of low-grade heat sources (such as: geothermal, solar energy, biomass combustion, industrial waste heat, Engine exhaust waste heat, etc.) is converted into mechanical work and output in the form of shaft work. The expander 3 transmits the shaft work to the open refrigeration compressor 12 of the vapor compression refrigeration system through the transmission device 6, and drives it to compress the low-temperature and low-pressure gaseous refrigerant into a high-temperature and high-pressure gas; the high-temperature and high-pressure gaseous refrigerant In the second condenser 7, it is condensed into a liquid state by the ambient cold source and enters the second liquid storage tank 8; the liquid refrigerant flowing out of the second liquid storage tank 8 expands and cools down through the throttle valve 9; after that, the gas-liquid two-phase refrigerant Enter the second evaporator 10 to cool the low-temperature heat source, absorb heat and evaporate into a gaseous state; the low-temperature and low-pressure gaseous refrigerant is sucked into the open refrigeration compressor 12 after passing through the first valve 11, and is compressed into a high-temperature and high-pressure gas; Reciprocating to complete vapor compression refrigeration.

When the heat supply from the heat source is insufficient or the cooling demand of the user increases, so that the above-mentioned heat-driven vapor compression refrigeration cannot meet the cooling capacity required by the user, the second valve 13 is opened to start the electric refrigeration compressor 14, and the compressor driven by auxiliary electric energy increases the cooling capacity. Large vapor compression refrigeration system refrigeration capacity to meet user needs. This is of great significance for the application of unstable and discontinuous low-grade heat sources (such as solar energy, etc.) and large changes in cooling demand, and can achieve the purpose of energy saving and emission reduction under the premise of ensuring user needs.

Claims (1)

1. A vapor compression refrigerating device driven by an Organic Rankine cycle is characterized in that it comprises a booster pump (1), a first evaporator (2), an expander (3), a first condenser (4), a second A liquid storage tank (5), a transmission device (6), a second condenser (7), a second liquid storage tank (8), a throttle valve (9), a second evaporator (10), a first valve ( 11), open refrigeration compressor (12), second valve (13), electric refrigeration compressor (14); booster pump (1), first evaporator (2), expander (3), second A condenser (4), the first liquid storage tank (5) are connected end to end in order to form an organic Rankine cycle system; the second condenser (7), the second liquid storage tank (8), the throttle valve (9), The second evaporator (10), the first valve (11), and the open refrigeration compressor (12) are sequentially connected end to end to form a vapor compression refrigeration cycle system; The machine (12) is connected; the outlet of the second evaporator (10), the electric refrigeration compressor (14), and the inlet of the second condenser (7) are connected in sequence.

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