CN208012083U - Without the pressure intensive fume hot-water boiler of clean fuel - Google Patents

Without the pressure intensive fume hot-water boiler of clean fuel Download PDF

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Publication number
CN208012083U
CN208012083U CN201820456347.0U CN201820456347U CN208012083U CN 208012083 U CN208012083 U CN 208012083U CN 201820456347 U CN201820456347 U CN 201820456347U CN 208012083 U CN208012083 U CN 208012083U
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CN
China
Prior art keywords
heat
heat room
heat exchanging
room
chamber
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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
CN201820456347.0U
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Chinese (zh)
Inventor
岳公华
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Shandong Elly Leung Energy Group Co Ltd
Original Assignee
Shandong Elly Leung Energy Group Co Ltd
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Publication date
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Priority to CN201820456347.0U priority Critical patent/CN208012083U/en
Application granted granted Critical
Publication of CN208012083U publication Critical patent/CN208012083U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model is related to a kind of without the pressure intensive fume hot-water boiler of clean fuel, including combustion chamber and the Heat Room I, Heat Room II and Heat Room III that set gradually and be respectively equipped with heat exchanging water pipe, the shell of the Heat Room I, Heat Room II and Heat Room III and the heat exchanging water pipe of respectively inside form heat exchanging chamber, Heat Room I, the heat exchanging chamber of Heat Room II and Heat Room III, heat exchanging water pipe are sequentially communicated respectively, and the heat exchanging chamber of Heat Room III, heat exchanging water pipe are respectively communicated with air inducing dust pelletizing system, water source.The utility model is by being arranged three Heat Rooms, increase the lateral flow length of flow, it ensure that the abundant of heat exchange, the mode of communicating of heat exchanging water pipe and heat exchanging chamber keeps heat exchange more abundant, improves the utilization rate of heat, the setting of complete machine modularization, make equipment that there is mobility, and facilitates installation and transport, the environment such as coal mine, oil field can use in the wild, meet worker's demand.

Description

Without the pressure intensive fume hot-water boiler of clean fuel
Technical field
The utility model is related to boiler plant field more particularly to it is a kind of without pressure the intensive fume hot-water pot of clean fuel Stove.
Background technology
In daily life, boiler is the important equipment for obtaining hot water, either common plunge bath, boiling water room or winter The heating of heating all be unable to do without the use of boiler.But at present used in boiler heat exchange when it is less efficient, energy consumption compared with Greatly, the environmental requirement being increasingly stringenter can not be adapted to.
Invention content
The utility model in view of the deficiencies of the prior art, provide it is a kind of without pressure the intensive fume hot-water boiler of clean fuel, lead to Being oppositely arranged for overfire air and flow, greatly improved heat exchange efficiency.
The utility model is achieved by the following technical solution, and is provided a kind of without the pressure intensive fume hot-water pot of clean fuel Stove, including combustion chamber and the Heat Room I, Heat Room II and Heat Room III that set gradually and be respectively equipped with heat exchanging water pipe, it is described to change The shell in hot cell I, Heat Room II and Heat Room III and the heat exchanging water pipe of respectively inside form heat exchanging chamber, Heat Room I, Heat Room II It is sequentially communicated respectively with the heat exchanging chamber of Heat Room III, heat exchanging water pipe, the heat exchanging chamber of Heat Room III, heat exchanging water pipe are respectively communicated with air inducing Dust pelletizing system, water source;
The combustion chamber includes the water trapping layer surrounded by inner casing and shell, and inclination is threaded through on the inner casing and both ends Several fire grate pipes being connected to respectively with the water trapping layer, the fire grate pipe are mutually parallel and are located at sustained height, the water trapping layer It is connected to water tank, the inner casing, water trapping layer are connected to the heat exchanging chamber of Heat Room I, heat exchanging water pipe respectively.
The hot gas that combustion chamber generates in this programme is opposite with water (flow) direction, using the hot gas of lower temperature to entering heat-exchanging water The water of pipe preheats, and with water (flow) direction, heating temperature steps up, and heat exchange efficiency is made to be largely increased;Meanwhile passing through setting Three Heat Rooms extend flow lateral flow length, further ensure heat transfer effect;By the way that air inducing dust pelletizing system is arranged, It ensure that the clean cleaning of discharge gas;Fire grate pipe is set in combustion chamber, not only acts as fire grate effect, inside also has flow logical It crosses, heat exchange is more abundant.
As an optimization, further include thermal-insulating body, the combustion chamber, Heat Room I, Heat Room II, Heat Room III and air inducing remove Dirt system is fixed on the thermal-insulating body inner chassis.By the way that thermal-insulating body is arranged, heat insulation effect is on the one hand played, heat is reduced On the other hand amount loss makes each section form a module, is easily installed and transports, solving field construction scene can not make The problem of using.
As an optimization, the outer surface of the heat exchanging water pipe is equipped with the helical form recess for inwardly squeezing and being formed, the recess Inner surface forms protrusion inside heat exchanging water pipe.By this prioritization scheme, the heat exchange area inside and outside heat exchanging water pipe is increased, Improve heat exchange efficiency.
As an optimization, heat exchanging water pipe's upper and lower ends in the Heat Room I, Heat Room II and Heat Room III have been respectively communicated with The collection chamber of collection chamber, III lower part of Heat Room is connected to water source, and the collection chamber on top is connected to the collection chamber on II top of Heat Room, changes The collection chamber of II lower part of hot cell is connected to the collection chamber of I lower part of Heat Room, and collection chamber and the water trapping layer on I top of Heat Room connect It is logical.By be arranged collection chamber, not only facilitated between adjacent heat exchange room heat exchanging water pipe connection, but also make each heat exchanging water pipe water into Row is mutually mixed, and makes heat exchange evenly;It is heat exchanging chamber between upper and lower collection chamber, the hot gas in heat exchanging chamber is simultaneously in collection chamber Water is heated, and heat exchange efficiency is further increased.
As an optimization, the heat exchanging chamber top of the Heat Room III respectively with the heat exchanging chamber top of Heat Room II and air inducing dedusting System connectivity, the heat exchanging chamber lower part of Heat Room II are connected to the heat exchanging chamber lower part of Heat Room I, the heat exchanging chamber top of Heat Room I with The inner casing connection.The mode of communicating of this prioritization scheme can make hot wind fully circulate in each Heat Room heat exchanging chamber, avoid flowing Logical dead angle.
As an optimization, the collection chamber bottom surface on III top of the Heat Room is equipped with the wind shield extended downwardly, the wind shield The collection chamber top surface of lower edge and lower part is equipped with ventilating duct.By the way that wind shield is arranged, make the heat for entering heat exchanging chamber in Heat Room III Wind is folded up again after flowing downward, and air inducing dust pelletizing system is entered back into after so that hot wind is fully exchanged heat with the water in heat exchanger tube, is improved The utilization rate of hot wind.
The beneficial effects of the utility model are:By the way that three Heat Rooms are arranged, the lateral flow length of flow is increased, is protected The abundant of heat exchange is demonstrate,proved, the mode of communicating of heat exchanging water pipe and heat exchanging chamber keeps heat exchange more abundant, improves the utilization rate of heat, complete machine Modularization is arranged, and so that equipment is had mobility, and facilitate installation and transport, the environment such as coal mine, oil field can make in the wild With meeting worker's demand.
Description of the drawings
FIG. 1 is a schematic structural view of the utility model;
Fig. 2 is A direction views in Fig. 1;
As shown in the figure:
1, combustion chamber, 2, Heat Room I, 3, Heat Room II, 4, Heat Room III, 5, air inducing dust pelletizing system, 6, heat exchanging chamber, 7, change Hot-water line, 8, collection chamber, 9, wind shield, 10, thermal-insulating body, 11, shell, 12, inner casing, 13, fire grate pipe, 14, water trapping layer.
Specific implementation mode
In order to clarify the technical characteristics of the invention, below by specific implementation mode, this programme is illustrated.
It is a kind of without the pressure intensive fume hot-water boiler of clean fuel, including thermal-insulating body 10, combustion chamber 1, air inducing as shown in Figure 1 Dust pelletizing system 5, and the Heat Room I 2, Heat Room II 3 and Heat Room III 4 of heat exchanging water pipe 7 are set gradually and are respectively equipped with, it burns Room 1, Heat Room I 2, Heat Room II 3, Heat Room III 4 and air inducing dust pelletizing system 5 are fixed in 10 inner chassis of the thermal-insulating body On, the shell of Heat Room I, Heat Room II and Heat Room III and the heat exchanging water pipe of respectively inside form heat exchanging chamber 6, and Heat Room I changes The heat exchanging chamber of hot cell II and Heat Room III, heat exchanging water pipe are sequentially communicated respectively, and the heat exchanging chamber of Heat Room III, heat exchanging water pipe connect respectively Logical air inducing dust pelletizing system 5, water source.Air inducing dust pelletizing system includes air-introduced machine and deduster, ensures combustion chamber by the way that air-introduced machine is arranged Interior hot wind passes through each heat exchanging chamber, using deduster by the hot gas purification after heat exchange, the gas of discharge is avoided to make environment At pollution.
Combustion chamber 1 includes inner casing 12 and shell 11, and inner casing 12 and shell 11 surround water trapping layer 14, are tilted on inner casing 12 Several fire grate pipes 13 that both ends are connected to water trapping layer 14 respectively are equipped with, the fire grate pipe 13 is mutually parallel and is located at same height Degree, is arranged in fire grate shape, support is provided for fuel, make full combustion of fuel, have flow to pass through in fire grate pipe, improves heat exchange effect Rate.Water trapping layer 14 is connected to water tank, and the inner casing, water trapping layer are connected to the heat exchanging chamber of Heat Room I, heat exchanging water pipe respectively, water source Water successively after Heat Room III, Heat Room II, Heat Room I and water trapping layer enter water tank, in case other use, Ke Yitong Enter caliduct, for bathing or can also drink.
Heat exchanging water pipe's upper and lower ends in Heat Room I, Heat Room II and Heat Room III have been respectively communicated with collection chamber 8, heat exchange The collection chamber of III 4 lower part of room is connected to water source, and the collection chamber on top is connected to the collection chamber on II top of Heat Room, II lower part of Heat Room Collection chamber be connected to the collection chamber of I lower part of Heat Room, the collection chamber on I top of Heat Room is connected to the water trapping layer.Heat Room III heat exchanging chamber top is connected to the heat exchanging chamber top of Heat Room II and air inducing dust pelletizing system respectively, under the heat exchanging chamber of Heat Room II Portion is connected to the heat exchanging chamber lower part of Heat Room I, and the heat exchanging chamber top of Heat Room I is connected to the inner casing.
Be additionally provided with the wind shield 9 extended downwardly in the collection chamber bottom surface on III top of Heat Room, 9 lower edge of the wind shield with The collection chamber top surface of lower part is equipped with ventilating duct.
In order to improve heat exchange area, 7 outer surface of heat exchanging water pipe in the present embodiment is equipped with the helical form for inwardly squeezing and being formed Recess, the inner surface of the recess form protrusion inside heat exchanging water pipe.
In use, the indoor hot gas that burns passes through each heat exchanging chamber successively under the action of air-introduced machine, the water at water source along with Successively by each indoor heat exchanging water pipe of heat exchange, heating temperature gradually rises, and takes full advantage of hot gas heat in the direction of hot wind contrary Amount, improves heat exchange efficiency, reduces energy consumption.By installing concentratedly each section in incubator, alloing this boiler more preferable Heat preservation, reduce thermal loss, and convenience in transport.
Certainly, above description is also not limited to the example above, and technical characteristic of the utility model without description can lead to It crosses or realizes that details are not described herein using the prior art;Above example and attached drawing are merely to illustrate the technology of the utility model Scheme is not limitations of the present invention, and the utility model is described in detail with reference to preferred embodiment, this Field it is to be appreciated by one skilled in the art that those skilled in the art institute in the essential scope of the utility model The variations, modifications, additions or substitutions made without departure from the objective of the utility model, want by the right that should also belong to the utility model Seek protection domain.

Claims (6)

1. a kind of without the pressure intensive fume hot-water boiler of clean fuel, it is characterised in that:Including combustion chamber(1)With set gradually and point It She You not heat exchanging water pipe(7)Heat Room I(2), Heat Room II(3)With Heat Room III(4), the Heat Room I, II and of Heat Room The shell of Heat Room III and the heat exchanging water pipe of respectively inside form heat exchanging chamber(6), Heat Room I, Heat Room II and Heat Room III Heat exchanging chamber, heat exchanging water pipe are sequentially communicated respectively, and the heat exchanging chamber of Heat Room III, heat exchanging water pipe are respectively communicated with air inducing dust pelletizing system(5), Water source;
The combustion chamber(1)Including by inner casing(12)And shell(11)The water trapping layer surrounded(14), and tilt be threaded through it is described Inner casing(12)Upper and both ends respectively with the water trapping layer(14)Several fire grate pipes of connection(13), the fire grate pipe(13)It is mutually flat Row and be located at sustained height, the water trapping layer is connected to water tank, the inner casing, water trapping layer respectively with the heat exchanging chamber of Heat Room I, change Hot-water line is connected to.
2. according to claim 1 without the pressure intensive fume hot-water boiler of clean fuel, it is characterised in that:It further include incubator Body(10), the combustion chamber(1), Heat Room I(2), Heat Room II(3), Heat Room III(4)With air inducing dust pelletizing system(5)It is affixed In the thermal-insulating body(10)On inner chassis.
3. according to claim 1 without the pressure intensive fume hot-water boiler of clean fuel, it is characterised in that:The heat exchanging water pipe (7)Outer surface be equipped with the helical form recess for inwardly squeezing and being formed, the inner surface of the recess forms convex inside heat exchanging water pipe It rises.
4. according to claim 1 without the pressure intensive fume hot-water boiler of clean fuel, it is characterised in that:The Heat Room I, Heat exchanging water pipe's upper and lower ends in Heat Room II and Heat Room III have been respectively communicated with collection chamber(8), Heat Room III(4)The remittance of lower part Collect chamber and be connected to water source, the collection chamber on top is connected to the collection chamber on II top of Heat Room, the collection chamber of II lower part of Heat Room with change The collection chamber of I lower part of hot cell is connected to, and the collection chamber on I top of Heat Room is connected to the water trapping layer.
5. according to claim 4 without the pressure intensive fume hot-water boiler of clean fuel, it is characterised in that:The Heat Room III Heat exchanging chamber top be connected to respectively with the heat exchanging chamber top of Heat Room II and air inducing dust pelletizing system, the heat exchanging chamber lower part of Heat Room II It is connected to the heat exchanging chamber lower part of Heat Room I, the heat exchanging chamber top of Heat Room I is connected to the inner casing.
6. according to claim 5 without the pressure intensive fume hot-water boiler of clean fuel, it is characterised in that:The Heat Room III The collection chamber bottom surface on top is equipped with the wind shield extended downwardly(9), the wind shield(9)The collection chamber top surface of lower edge and lower part Equipped with ventilating duct.
CN201820456347.0U 2018-04-03 2018-04-03 Without the pressure intensive fume hot-water boiler of clean fuel Expired - Fee Related CN208012083U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820456347.0U CN208012083U (en) 2018-04-03 2018-04-03 Without the pressure intensive fume hot-water boiler of clean fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820456347.0U CN208012083U (en) 2018-04-03 2018-04-03 Without the pressure intensive fume hot-water boiler of clean fuel

Publications (1)

Publication Number Publication Date
CN208012083U true CN208012083U (en) 2018-10-26

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Family Applications (1)

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Country Status (1)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113390186A (en) * 2021-07-16 2021-09-14 廊坊劲华锅炉有限公司 Integrated pressure-bearing condensing boiler
CN113390185A (en) * 2021-07-16 2021-09-14 廊坊劲华锅炉有限公司 Pressure-bearing condensing boiler

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113390186A (en) * 2021-07-16 2021-09-14 廊坊劲华锅炉有限公司 Integrated pressure-bearing condensing boiler
CN113390185A (en) * 2021-07-16 2021-09-14 廊坊劲华锅炉有限公司 Pressure-bearing condensing boiler
CN113390186B (en) * 2021-07-16 2022-06-17 廊坊劲华锅炉有限公司 Integrated pressure-bearing condensing boiler

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GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20181026

Termination date: 20210403

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