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Steam heat pump for heat fluid regenerative flash evaporation circulation

A thermal fluid and flash evaporation technology, applied in heat pumps, superheaters, lighting and heating equipment, etc., can solve the problems of difficult energy saving, technical economy, loss of decompression potential energy, etc., to avoid investment and power consumption, reduce operating costs, The effect of reducing the initial investment

Pending Publication Date: 2022-07-22
侴雨宏
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] To sum up, in the existing waste heat and pressure recovery technology: although the heat exchanger recovers the waste heat of the hot fluid, it does not directly generate water vapor; although the steam generator generates water vapor, it must be driven by primary energy; the high-pressure water vapor in the pipe network At the end of the user, in order to increase the latent heat of condensation heating by about 10%, it is necessary to lose decompression potential energy and desuperheating sensible heat as a cost; although the water vapor compressor can compress low-pressure water vapor to generate high-pressure water vapor, it needs high-grade electric energy to drive ; so it is difficult to independently realize the economy of energy-saving technology

Method used

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  • Steam heat pump for heat fluid regenerative flash evaporation circulation
  • Steam heat pump for heat fluid regenerative flash evaporation circulation
  • Steam heat pump for heat fluid regenerative flash evaporation circulation

Examples

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Embodiment Construction

[0027] The example of the hot fluid regenerative flash cycle steam heat pump proposed by the present invention is attached image 3It is described as follows: it consists of a papermaking black lye 1 with an average flow of 418t / h and a temperature of 117 / 105°C; a shell-and-tube thermal fluid regenerator 2 with a heat output of 5.824MW; a 304 stainless steel thermal fluid inlet with a diameter of 400mm 2-1; 304 stainless steel thermal fluid outlet 2-2 with a diameter of 400mm; softened water inlet 2-3 of a carbon steel regenerator with a diameter of 400mm; softened water outlet of a carbon steel regenerator with a diameter of 400mm 2-4; average flow rate 418t / h and demineralized water 3 at a temperature of 112 / 100°C; volume 3m 3 / Carbon steel softening water tank 4 with wall thickness of 5mm; circulating water pump 5 with flow rate of 418t / h, lift of 7mH20 and electric power of 10.29kW; interface diameter of 400mm / length of 800mm / wall thickness of 3mm carbon steel water ...

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Abstract

The system integrates energy-saving technologies such as a heat exchanger, heating throttling flash evaporation water supplementing circulation and a jet type heat pump to achieve systematicness and economy of the energy-saving technologies, the heat exchanger recovers heat fluid waste heat to replace a primary energy source to drive the heating throttling flash evaporation water supplementing circulation, low-pressure saturated water vapor is directly generated, and the heat-fluid heat-regeneration flash evaporation circulation steam heat pump is used for heat recovery of the heat-fluid heat-regeneration flash evaporation water supplementing circulation. The pressure reduction potential energy and the temperature reduction sensible heat of the high-pressure water vapor of the pipe network are recycled by the jet type heat pump, so that the low-pressure saturated water vapor is injected and mixed, and medium-pressure water vapor is generated; and meanwhile, investment and power consumption of a water vapor compressor are avoided, so that the initial investment of the energy-saving system is reduced exponentially, and the operation cost of the energy-saving system is reduced exponentially.

Description

(1) Technical field [0001] The invention relates to a method of recovering the waste heat of 100-900°C hot fluid by a heat exchanger to drive a heating and throttling flash evaporation water replenishment cycle, so as to continuously flash to generate 90-120°C saturated water vapor, and then the water vapor at a gauge pressure of 5-16 barg passes through the water vapor. The thermal compression jet heat pump ejects, mixes and diffuses to generate water vapor with a gauge pressure of 1 to 6 barg. (2) Background technology [0002] Current status of energy-saving technologies for recovering waste heat and pressure in the industrial energy-saving market: [0003] 1. The heat exchanger recovers the waste heat of the hot fluid: the heat exchanger recovers the latent heat of condensation and or the sensible heat of cooling of the high-temperature gaseous thermal fluids such as boiler flue gas, generator flue gas, engine flue gas, rectification tower top gas, and aldehyde gas. , c...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F25B30/02F25B40/06F25B41/40
CPCF25B30/02F25B40/06F25B41/40
Inventor 侴雨宏魏蔚其他发明人请求不公开姓名
Owner 侴雨宏
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