CN205425453U - Normal pressure hot water boiler heat transfer system - Google Patents

Normal pressure hot water boiler heat transfer system Download PDF

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Publication number
CN205425453U
CN205425453U CN201620177619.4U CN201620177619U CN205425453U CN 205425453 U CN205425453 U CN 205425453U CN 201620177619 U CN201620177619 U CN 201620177619U CN 205425453 U CN205425453 U CN 205425453U
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CN
China
Prior art keywords
heat
flue gas
heat exchange
heat transfer
smoke chamber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201620177619.4U
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Chinese (zh)
Inventor
胡成良
贾印丰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Liaoning Jimei Biomass Heating Co Ltd
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Liaoning Jimei Biomass Heating Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
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Priority to CN201620177619.4U priority Critical patent/CN205425453U/en
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Publication of CN205425453U publication Critical patent/CN205425453U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model belongs to the technical field of the boiler and specifically relates to a normal pressure hot water boiler heat transfer system, include to set up in inside heat transfer room and the flue gas chamber of furnace body heat transfer room upside is equipped with water inlet and delivery port, flue gas chamber sets up in heat transfer room below heat transfer room lower extreme be equipped with a plurality of protrusions stretch into to flue gas chamber's heat transfer fin, the inside water flow region that is of heat transfer fin, the outside flue gas flow region that is of heat transfer fin. The utility model discloses heat energy utilization efficiency has greatly been improved, resources are saved, mitigate contamination simultaneously.

Description

A kind of normal-pressure hot-water boiler heat-exchange system
Technical field
This utility model relates to field of boilers, specifically a kind of normal-pressure hot-water boiler heat-exchange system.
Background technology
Normal-pressure hot-water boiler is also unpressurized hot water boiler, belong to the category of domestic life boiler, normal-pressure hot-water boiler is that a kind of top is provided with atmosphere entry, boiler body and is in the unpressurized hot water boiler of normal pressure running status all the time, its main feature is exactly boiler not pressure-bearing, there is no potential safety hazard, it is mainly used in producing hot water for warm, it it is relatively common boiler, although normal-pressure hot-water boiler of the prior art can meet normal heating requirement, but it is low to be because its heat exchange efficiency, easily wastes resource and cause severe contamination.
Utility model content
The purpose of this utility model is to provide a kind of normal-pressure hot-water boiler heat-exchange system, drastically increases utilization efficiency of heat energy, economizes on resources, simultaneously pollution abatement.
The purpose of this utility model is achieved through the following technical solutions:
A kind of normal-pressure hot-water boiler heat-exchange system, including the Heat Room and the smoke chamber that are arranged at furnace interior, water inlet and outlet it is provided with on the upside of described Heat Room, described smoke chamber is arranged at below Heat Room, it is provided with multiple protrusion in described Heat Room lower end and stretches to the heat exchange fin of described smoke chamber, described heat exchange fin is internal is water flow region, and described heat exchange fin is outside is flow of flue gas region.
Being provided with multi-stage heat exchanger pipeline in described Heat Room, heat exchanging pipes at different levels head and the tail communicate.
Described heat exchange fin is one-level heat exchange, is provided with secondary heat exchange pipeline and three grades of heat exchanging pipes in described Heat Room, and flue gas is turned back after being exported by smoke chamber in entrance secondary heat exchange pipeline, then three grades of heat exchanging pipes of entrance of turning back.
It is provided with the first dividing plate on the upside of the flue gas outfan of described smoke chamber, the flue gas input of described secondary heat exchange pipeline and the flue gas outfan of three grades of heat exchanging pipes are separated by described first dividing plate, being provided with second partition on the upside of the flue gas input of described smoke chamber, the flue gas outfan of described secondary heat exchange pipeline is separated by described second partition with the flue gas input of described smoke chamber.
Described first dividing plate and second partition inner filling water.
Advantage of the present utility model with good effect is:
1, one-level heat exchange of the present utility model uses the welded heat exchange fin of U-shaped docking, it is internal is water flow region, outside is flow of flue gas region, this considerably increases heat exchange area, cold water quickly can be heated, with conventional hot water boiler ratio, one-level heat exchanging part heat exchange area is its 5.12 times, and one-level heat exchange efficiency arrives 78.5%.
2, two grades and three grades of heat exchange employing lengthening heat exchanger tubes of the present utility model, as much as possible reclaim heat, make whole efficiency reach 96.4%. and achieve heat energy utilization maximization, economize on resources, simultaneously pollution abatement.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model,
Fig. 2 is the schematic diagram of heat exchanging pipes at different levels in Fig. 1,
Fig. 3 is the side view of heat exchanging pipes at different levels in Fig. 2.
Wherein, 1 is heat exchange fin, and 2 is smoke chamber, and 3 is secondary heat exchange pipeline, and 4 is three grades of heat exchanging pipes, and 5 is Heat Room, and 6 is water flow region, and 7 is flow of flue gas region, and 8 is the first dividing plate, and 9 is second partition.
Detailed description of the invention
The utility model is described in further detail below in conjunction with the accompanying drawings.
nullAs shown in Figures 1 to 3,This utility model includes Heat Room 5 and the smoke chamber 2 being arranged in body of heater,Smoke chamber 2 is arranged at below Heat Room 5,It is provided with water inlet and outlet on the upside of described Heat Room 5,It is provided with multiple protrusion in described Heat Room 5 lower end and stretches to the heat exchange fin 1 of described smoke chamber 2,As shown in Figure 3,The internal water flow region 6 for communicating with Heat Room 5 of described heat exchange fin 1,Described heat exchange fin 1 outside is the flow of flue gas region 7 in smoke chamber 2,The water heating in heat exchange fin 1 is given when flue gas flows in described smoke chamber 2,Multiple heat exchange fins 1 be arranged in parallel and arrange in flap-like,Thus considerably increase heat exchange area,It is thus possible to water is quickly heated,With conventional hot water boiler ratio,The heat exchange area of described heat exchange fin 1 is 5.12 times of conventional hot water boiler,In the present embodiment,Described heat exchange fin 1 is U-shaped docking Welding Structure,Described heat exchange fin 1 is one-level heat exchange of the present utility model.
It is additionally provided with multi-stage heat exchanger pipeline in described Heat Room 5, and heat exchanging pipe at different levels head and the tail communicate, in the present embodiment, two-stage heat exchanging pipe it is provided with altogether in described Heat Room 5, as shown in Figure 2, the first dividing plate 8 it is provided with on the upside of the flue gas outfan of described smoke chamber 2, and the flue gas input of secondary heat exchange pipeline 3 and the flue gas outfan of three grades of heat exchanging pipes 4 are separated by described first dividing plate 8, flue gas is i.e. turned back after being exported by described smoke chamber 2 and is entered in secondary heat exchange pipeline 3, it is provided with second partition 9 on the upside of the flue gas input of described smoke chamber 2, and the flue gas input of the flue gas outfan of described secondary heat exchange pipeline 3 with described smoke chamber 2 is separated by described second partition 9, flue gas is i.e. turned back after being exported by secondary heat exchange pipeline 3 and is entered in three grades of heat exchanging pipes 4.Described secondary heat exchange pipeline 3 and three grades of heat exchanging pipes 4 all include the heat exchanger tube of multiple circle, and heat exchanger tube extended length is to reclaim heat as much as possible.Described first dividing plate 8 and second partition 9 inside communicate full water to meet every cigarette requirement with Heat Room 5.
Operation principle of the present utility model is:
One-level heat exchange of the present utility model uses the welded heat exchange fin of U-shaped docking 1, substantially increases heat exchange area, can quickly be heated by cold water, and with conventional hot water boiler ratio, one-level heat exchanging part heat exchange area is its 5.12 times, and one-level heat exchange efficiency arrives 78.5%;Two grades and three grades of heat exchange employing lengthening heat exchanger tubes, as much as possible reclaim heat, make whole efficiency reach 96.4%. and achieve heat energy utilization maximization, economize on resources, simultaneously pollution abatement.

Claims (5)

1. a normal-pressure hot-water boiler heat-exchange system, including the Heat Room and the smoke chamber that are arranged at furnace interior, water inlet and outlet it is provided with on the upside of described Heat Room, it is characterized in that: described smoke chamber (2) is arranged at Heat Room (5) lower section, it is provided with multiple protrusion in described Heat Room (5) lower end and stretches to the heat exchange fin (1) of described smoke chamber (2), described heat exchange fin (1) is internal is water flow region (6), and described heat exchange fin (1) is outside is flow of flue gas region (7).
Normal-pressure hot-water boiler heat-exchange system the most according to claim 1, it is characterised in that: being provided with multi-stage heat exchanger pipeline in described Heat Room (5), heat exchanging pipes at different levels head and the tail communicate.
Normal-pressure hot-water boiler heat-exchange system the most according to claim 2, it is characterized in that: described heat exchange fin (1) is one-level heat exchange, secondary heat exchange pipeline (3) and three grades of heat exchanging pipes (4) it are provided with in described Heat Room (5), flue gas is turned back in entrance secondary heat exchange pipeline (3) after being exported by smoke chamber (2), then three grades of heat exchanging pipes (4) of entrance of turning back.
Normal-pressure hot-water boiler heat-exchange system the most according to claim 3, it is characterized in that: on the upside of the flue gas outfan of described smoke chamber (2), be provided with the first dividing plate (8), the flue gas input of described secondary heat exchange pipeline (3) and the flue gas outfan of three grades of heat exchanging pipes (4) are separated by described first dividing plate (8), second partition (9) it is provided with on the upside of the flue gas input of described smoke chamber (2), the flue gas outfan of described secondary heat exchange pipeline (3) is separated by described second partition (9) with the flue gas input of described smoke chamber (2).
Normal-pressure hot-water boiler heat-exchange system the most according to claim 4, it is characterised in that: described first dividing plate (8) and second partition (9) inner filling water.
CN201620177619.4U 2016-03-08 2016-03-08 Normal pressure hot water boiler heat transfer system Expired - Fee Related CN205425453U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620177619.4U CN205425453U (en) 2016-03-08 2016-03-08 Normal pressure hot water boiler heat transfer system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620177619.4U CN205425453U (en) 2016-03-08 2016-03-08 Normal pressure hot water boiler heat transfer system

Publications (1)

Publication Number Publication Date
CN205425453U true CN205425453U (en) 2016-08-03

Family

ID=56534181

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620177619.4U Expired - Fee Related CN205425453U (en) 2016-03-08 2016-03-08 Normal pressure hot water boiler heat transfer system

Country Status (1)

Country Link
CN (1) CN205425453U (en)

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C14 Grant of patent or utility model
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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160803

Termination date: 20200308

CF01 Termination of patent right due to non-payment of annual fee