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Special energy-saving type boiler system matched with condensate water recovery system

A technology for recovering system and condensed water, applied in supplementary feed water, feed water heater, combustion method, etc., can solve the problems affecting the stable operation of the boiler system, gasification of economizers, and high exhaust temperature of boilers, so as to avoid gasification and reduce Condensate water temperature, the effect of reducing boiler exhaust gas temperature

Inactive Publication Date: 2019-03-26
焦武军
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, as the vast majority of users adopt closed systems (or open systems) to recover condensed water and use it directly in the boiler system, some problems have also been exposed
[0004] One is the gasification of the economizer, which affects the stable operation of the boiler system;
[0005] The second is that the exhaust gas temperature of the boiler is too high, and most users generally reach about 150°C
In this case, if the working pressure of the user's boiler is around 0.7MPa, gasification of the economizer will also occur

Method used

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  • Special energy-saving type boiler system matched with condensate water recovery system
  • Special energy-saving type boiler system matched with condensate water recovery system
  • Special energy-saving type boiler system matched with condensate water recovery system

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Example 1 as figure 1 shown

[0025] The economizer in the system is divided into the first-level economizer 1 and the second-level economizer 2. The low-temperature water source of the second-level economizer is provided by mixing the external low-temperature water source 4 and the condensed water 5 that has been desuperheated by the condensate water desuperheating device. The second-level energy-saving The drain from device 2 enters primary economizer 1.

[0026] The condensed water desuperheating device 3 uses condensed water 10 at 120-130°C to heat the cold air 7. Through heat exchange, the temperature of the condensed water at 120-130°C is reduced to about 100°C, and the temperature of the cold air is raised from 20°C to about 100°C . The cold air flow rate of the condensed water desuperheating device 3 is designed to match the air flow rate required by the combustion of the boiler. The generated hot air enters the heating part of the boiler for combustion suppo...

Embodiment 2

[0028] Example 2 as figure 2 shown

[0029] The economizers in the system are divided into first-level economizer 1 and second-level economizer 2. The low-temperature water source of the second-level economizer 2 is provided by an external low-temperature water source 4. The condensed water 5 desuperheated by the water desuperheating device is mixed and provided. The high-temperature water from the secondary economizer enters the open hot water tank 12. The open hot water tank 12 has a flow monitoring device, and the mixing ratio with the condensed water after the cooling treatment is adjusted through the data of the flow monitoring device.

[0030] The low-temperature water source of the secondary economizer is directly provided by the external low-temperature water source 4, so that the inlet water temperature of the secondary economizer is relatively lower, and the temperature of the flue gas 9 at the outlet of the economizer can be reduced to below 80°C. The open hot wa...

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Abstract

The invention provides a special energy-saving type boiler system matched with a condensate water recovery system. The special energy-saving type boiler system matched with the condensate water recovery system is characterized in that the special energy-saving type boiler system matched with the condensate water recovery system comprises a boiler, an energy saver and a condensate water temperaturereduction device; and boiler discharged smoke is discharged into the atmosphere after cooling by the energy saver, a low-temperature water source of the energy-saver is provided by an external low-temperature water source and condensate water with temperature reduction processed by the condensate water temperature reduction device, boiler feed water is supplied by high-temperature water heated bythe energy-saver, and cold air for boiler combustion enters a boiler furnace through heat exchange and warming of the condensate water temperature reduction device. The special energy-saving type boiler system matched with the condensate water recovery system has the technical effects that the gasification phenomenon of the energy-saver is avoided, the temperature of the boiler discharged smoke is reduced, the heat efficiency of the boiler system is improved, the cold air for the boiler combustion is directly used for the condensate water temperature reduction device and the condensate waterfor heat exchange, the temperature of the condensate water is reduced, and generated hot wind is more beneficial to the combustion of the boiler.

Description

technical field [0001] The invention relates to an energy-saving boiler system, in particular to a special energy-saving boiler system matched with a condensed water recovery system. Background technique [0002] With the rapid development of economy, people's awareness of energy saving and environmental protection is also increasing. In recent years, more and more enterprises have carried out condensate recovery work. From open system recovery to closed system recovery, the efficiency of condensate recovery and utilization is also getting higher and higher. [0003] However, as the vast majority of users adopt closed systems (or open systems) to recover condensed water and use it directly in boiler systems, some problems have also been exposed. [0004] One is the gasification of the economizer, which affects the stable operation of the boiler system; [0005] The second is that the exhaust gas temperature of the boiler is too high, and most users generally reach about 15...

Claims

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Application Information

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IPC IPC(8): F22D11/06F22D1/28F23L15/04F23J15/06
CPCF22D1/28F22D11/06F23J15/06F23L15/045Y02E20/34
Inventor 焦武军张亮臣罗自力陈德山王战钦周黎
Owner 焦武军
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