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Non-azeotropic working medium dual-stage organic flash evaporation circulation system and heat energy recovery method thereof

A circulatory system and non-azeotropic technology, applied in steam recovery, mechanical equipment, steam engine devices, etc., to achieve effective utilization, improve temperature matching, and achieve high-efficiency utilization

Inactive Publication Date: 2020-01-14
YUNNAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to provide a non-azeotropic working medium two-stage organic flash cycle system and its heat energy recovery method in view of the above shortcomings, and to solve how to improve the temperature matching between the cycle and the cold source, and reduce the direct throttling of single-stage OFC The resulting exergy loss, improving system efficiency, and realizing the cascade efficient utilization of medium and low temperature heat energy, etc.

Method used

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  • Non-azeotropic working medium dual-stage organic flash evaporation circulation system and heat energy recovery method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0022] See attached figure 1 . A non-azeotropic working medium two-stage organic flash cycle system, including a condenser 1, a working medium pump 2, a heat exchanger 3, a first throttle valve 4, a high-pressure stage gas-liquid separator 5, and a high-pressure stage turbine 6 , high-pressure stage mixer 8, second throttle valve 7, low-pressure stage gas-liquid separator 9, low-pressure stage turbine 10, low-pressure stage mixer 12 and the third throttle valve 11; the thermal fluid side of the condenser 1 The outlet, the working medium pump 2 and the inlet of the cold fluid side of the heat exchanger 3 are sequentially connected through pipelines; the outlet of the cold fluid side of the heat exchanger 3, the first throttle valve 4 and the inlet of the high-pressure stage gas-liquid separator 5 Connect sequentially through pipelines; the steam outlet of the high-pressure stage gas-liquid separator 5 is connected with the inlet of the high-pressure stage turbine 6 through pip...

Embodiment 2

[0024] See attached figure 1 . A non-azeotropic working medium two-stage organic flash cycle system, including a condenser 1, a working medium pump 2, a heat exchanger 3, a first throttle valve 4, a high-pressure stage gas-liquid separator 5, and a high-pressure stage turbine 6 , high-pressure stage mixer 8, second throttle valve 7, low-pressure stage gas-liquid separator 9, low-pressure stage turbine 10, low-pressure stage mixer 12 and the third throttle valve 11; the thermal fluid side of the condenser 1 The outlet, the working medium pump 2 and the inlet of the cold fluid side of the heat exchanger 3 are sequentially connected through pipelines; the outlet of the cold fluid side of the heat exchanger 3, the first throttle valve 4 and the inlet of the high-pressure stage gas-liquid separator 5 Connect sequentially through pipelines; the steam outlet of the high-pressure stage gas-liquid separator 5 is connected with the inlet of the high-pressure stage turbine 6 through pip...

Embodiment 3

[0031] See attached figure 1 . A method for recovering heat energy of a non-azeotropic working medium two-stage organic flash cycle system, using the above-mentioned non-azeotropic working medium two-stage organic flash cycle system, including a waste heat absorption step, a heat energy utilization step and a working medium Cooling step; the step of absorbing waste heat is specifically: the working fluid comes out from the hot fluid side outlet of the condenser 1, and enters the cold fluid side inlet of the heat exchanger 3 after being pressurized by the working fluid pump 2, and the working fluid is in the heat exchanger 3 and The waste heat medium input from the hot fluid side inlet of the heat exchanger 3 and output from the hot fluid side outlet of the heat exchanger 3 is heat-exchanged; the heat energy utilization steps are as follows: the working fluid comes out from the cold fluid side outlet of the heat exchanger 3, passes through After throttling by the first throttl...

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Abstract

The invention discloses a non-azeotropic working medium dual-stage organic flash evaporation circulation system and a heat energy recovery method thereof, and belongs to the field of energy recovery.A working medium exchanges heat with a waste heat medium in a heat exchanger after being pressurized by a working medium pump, and enters a high-pressure-stage gas-liquid separator after being throttled by a first throttle valve; a saturated steam after high-pressure-stage flash evaporation enters a high-pressure-stage turbine to do work through expansion, and saturated liquid is throttled again through a second throttle valve to change into a gas-liquid mixture; the gas-liquid mixture and exhaust gas are mixed in a high-pressure-stage mixer, and then enter a low-pressure-stage gas-liquid separator together; saturated steam after the low-pressure-stage flash evaporation enters a low-pressure-stage turbine to do work through expansion, saturated liquid is throttled through a third throttledvalve to change to a gas-liquid mixture, and the gas-liquid mixture and the exhaust gas are mixed in a low-pressure-stage mixer; and the gas-liquid mixture and the exhaust gas are jointly cooled in acondenser. The temperature matching between the circulation and a cold source is improved, the exergy loss caused by single-stage OFC direct throttling is reduced, the system efficiency is improved,and the stepwise efficient use of medium and low temperature thermal energy is realized.

Description

technical field [0001] The invention belongs to the field of energy recovery, and in particular relates to a non-azeotropic working fluid two-stage organic flash cycle system and a heat energy recovery method thereof. Background technique [0002] With the development of society and economy, China's total energy consumption is increasing year by year. According to statistics, China's total energy consumption reached 464 million tons of standard coal in 2018, with an average annual growth rate of 2.2% in the past five years. It can be expected that under the background of China's economy maintaining medium-to-high speed growth, China's demand for energy will further increase. From the perspective of energy consumption structure, China's energy consumption is still dominated by coal, oil, and natural gas. Taking 2016 as an example, the total consumption of coal, oil, and natural gas accounted for about 86.7% of the total energy consumption in that year. On the one hand, the e...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F01K25/06F01K7/02F01K19/00
CPCF01K7/02F01K19/00F01K25/06
Inventor 葛众袁志鹏鄢银连相华江黄桂冬解志勇张军
Owner YUNNAN UNIV
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