CN208332681U - A kind of vertical bottom mixed in series and parallel combusts oily gas organic heat carrier boiler - Google Patents

A kind of vertical bottom mixed in series and parallel combusts oily gas organic heat carrier boiler Download PDF

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Publication number
CN208332681U
CN208332681U CN201820772648.4U CN201820772648U CN208332681U CN 208332681 U CN208332681 U CN 208332681U CN 201820772648 U CN201820772648 U CN 201820772648U CN 208332681 U CN208332681 U CN 208332681U
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China
Prior art keywords
coil pipe
boiler
ring coil
inner ring
outer ring
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CN201820772648.4U
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Inventor
胡海琴
张亚健
彭乐荣
袁巍巍
聂驰
陈银洁
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WUXI XINENG BOILER CO Ltd
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WUXI XINENG BOILER CO Ltd
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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The utility model relates to a kind of boiler of organic heat carrier, specifically a kind of vertical bottom mixed in series and parallel combusts oily gas organic heat carrier boiler, belongs to boiler plant technical field.It includes boiler barrel, inner ring coil pipe, centre circle coil pipe and outer ring coil pipe are successively arranged inside burner hearth from inside to outside, the input end of centre circle coil pipe and outer ring coil pipe stretches out boiler barrel upwards and connects import header jointly, and the outlet end of centre circle coil pipe and outer ring coil pipe extends downwardly boiler barrel and connects intermediate mixing header jointly;Inner ring coil pipe input end extends downwardly boiler barrel and connects intermediate mixing header, and boiler barrel and connection outlet header are stretched out in inner ring coil outlets end upwards.The utility model mixes in intermediate mixing header in advance due to entering the medium of inner ring coil pipe, keeps the medium temperature into inner ring coil pipe consistent, so that Coil outlet temperature be made to be consistent, ensure that the safe operation of boiler.

Description

A kind of vertical bottom mixed in series and parallel combusts oily gas organic heat carrier boiler
Technical field
The utility model relates to a kind of boiler of organic heat carrier, specifically a kind of vertical bottom mixed in series and parallel is combusted Oily gas organic heat carrier boiler belongs to boiler plant technical field.
Background technique
Currently, the heating surface that the vertical bottom of LS type combusts oily gas organic heat carrier boiler is by two layers of disk pipe or three layers of circle Coil pipe is nested together composition, in innermost coil pipe inner ring coil pipe, intermediate coil pipe centre circle coil pipe, the coil pipe in outside Outer ring coil pipe, every layer of coil pipe are made of the spiral coil of one or more coil pipe parallel connection, walk organic heat carrier inside coil pipe, and two Flue gas is walked in gap between layer coil pipe, and boiler heat absorption is divided into radiant heat and advection heat, and radiations heat energy accounts for 60%, and convection heat accounts for 40%, inner ring coil pipe absorbs whole radiations heat energy and a part of advection heat, 70% about always to recept the caloric, and centre circle and outer ring absorb Remaining advection heat.
Inside and outside coil pipe has two ways in parallel or series under normal circumstances, when using parallel connection, organic heat carrier by into Mouth header enters inside and outside three circles coil pipe simultaneously, then mixes in outlet header, the medium flow field that such structure passes through every root canal Amount is determined by the length of single cell, since the caloric receptivity of every circle coil pipe is different, is generally difficult to allow in every root canal Caloric receptivity is consistent, results in the Coil outlet temperature in every circle inconsistent in this way, and it is easy to appear lists if arrangement is unreasonable The sub- overtemperature of root canal, to damage boiler.When using series connection, organic heat carrier enters outer ring coil pipe by import header, by outer ring Coil pipe enters centre circle coil pipe, then enters inner ring coil pipe by centre circle coil pipe, finally enters outlet header, is arranged so every root canal Caloric receptivity is uniform, but since the length of single cell is that three circle coil pipes are added, the medium resistance of boiler under normal circumstances Power is bigger.The very big portion's wind consumption of the power consumption of circulating pump is uneconomical on boiler body.In addition the medium in such boiler is walked One N word shape, can not be by the mediator depletion in furnace in repair and maintenance boiler.Sometimes due to the characteristic by medium is influenced blowing out Otherwise mediator depletion can be solidified after medium cooling, be not available after causing by Shi Bixu.In addition the second of this two kinds of structures Flue gas and medium in convection section are downstream heat transfers, and heat transfer effect is poor, influence the thermal efficiency of boiler.
Summary of the invention
In place of the purpose of this utility model is to overcome above-mentioned deficiency, to provide a kind of vertical bottom burning mixed in series and parallel Fuel-firing gas-firing boiler of organic heat carrier, by the way that outer ring and centre circle coil pipe is in parallel, centre by an intermediate mixing header again with Inner ring series connection, solves the problems, such as parallel-connection structure boiler export coil temperature deviation, makes to obtain every coil pipe into outlet header Temperature is the same, by adjusting flue gas trend and medium flow direction, the flue gas of the second convection section and medium is made to become counterflow heat exchange, improved Boiler obtains the thermal efficiency, while it is big with resistance to solve the problems, such as that cascaded structure can not be emptied.
According to technical solution provided by the utility model, a kind of organic heat load of vertical bottom burning fuel-firing gas-firing mixed in series and parallel Body boiler includes boiler barrel, burner hearth is equipped in boiler barrel, it is characterized in that: being successively arranged inner ring disk inside burner hearth from inside to outside Pipe, centre circle coil pipe and outer ring coil pipe, centre circle coil pipe and outer ring coil pipe are arranged in parallel, the input end of centre circle coil pipe and outer ring coil pipe to Upper stretching boiler barrel simultaneously connects import header jointly, and the outlet end of centre circle coil pipe and outer ring coil pipe extends downwardly boiler barrel simultaneously It is common to connect intermediate mixing header;Inner ring coil pipe is arranged in series with centre circle coil pipe, outer ring coil pipe, and inner ring coil pipe input end is stretched downwards Boiler barrel and intermediate mixing header is connected out, boiler barrel and connection outlet header are stretched out in inner ring coil outlets end upwards;It is interior The first convection current exhaust gases passes, outer ring coil pipe and boiler drum are formed between circle coil pipe and centre circle coil pipe, centre circle coil pipe and outer ring coil pipe The second convection current exhaust gases passes are formed between body sidewall.
Further, intermediate mixing header is equipped with mediator depletion mouth.
Further, boiler barrel bottom centre is equipped with burner, and the burning spout of burner protrudes into burner hearth.
Compared with the prior art the utility model has the advantage that
The utility model structure is simple, compact, reasonable, and the medium due to entering inner ring coil pipe mentions in intermediate mixing header Preceding mixing keeps the medium temperature into inner ring coil pipe consistent, so that Coil outlet temperature be made to be consistent, ensure that the peace of boiler Row for the national games;Two the first convection current exhaust gases passes are in parallel to be reduced a flue gas backhaul, reduces boiler smoke collateral resistance downwards, Reduce the power consumption of air blower;Meanwhile second convection current exhaust gases passes flue gas and media for heat exchange become counterflow heat exchange, improve boiler The thermal efficiency;Third, medium can be drained by the evacuation port of intermediate mixing header in Boiler Furnace, be blowing out and maintenance provider Just;4th, the resistance of boiler body is reduced, circulating pump effective power consumption is improved.
Detailed description of the invention
Fig. 1 is the utility model main view.
Description of symbols: 1- boiler barrel, 2- burner hearth, 3- burner, 4- import header, the centre 5- mixing header, 6- Outlet header, the outer ring 7- coil pipe, 8- centre circle coil pipe, 9- inner ring coil pipe, the first convection current of 10- exhaust gases passes, 11- the second convection current flue gas Channel, 12- mediator depletion mouth.
Specific embodiment
The utility model will be further described in conjunction with the embodiment in attached drawing below:
As shown in Figure 1, the utility model mainly includes boiler barrel 1, burner hearth 2 is equipped in boiler barrel 1.Inside burner hearth 2 It is successively arranged inner ring coil pipe 9, centre circle coil pipe 8 and outer ring coil pipe 7 from inside to outside, centre circle coil pipe 8 and outer ring coil pipe 7 are arranged in parallel, The input end of centre circle coil pipe 8 and outer ring coil pipe 7 stretches out boiler barrel 1 upwards and connects import header 4,8 He of centre circle coil pipe jointly The outlet end of outer ring coil pipe 7 extends downwardly boiler barrel 1 and connects intermediate mixing header 5 jointly.
Inner ring coil pipe 9 is arranged in series with centre circle coil pipe 8, outer ring coil pipe 7, and 9 input end of inner ring coil pipe extends downwardly boiler drum Body 1 simultaneously connects intermediate mixing header 5, and boiler barrel 1 and connection outlet header 6 are stretched out in 9 outlet end of inner ring coil pipe upwards.
The first convection current exhaust gases passes 10 are formed between inner ring coil pipe 9 and centre circle coil pipe 8, centre circle coil pipe 8 and outer ring coil pipe 7, The second convection current exhaust gases passes 11 are formed between 1 side wall of outer ring coil pipe 7 and boiler barrel.
The medium of boiler of organic heat carrier is entered from the import header for being located at 1 top of boiler barrel by parallel way simultaneously Outer ring coil pipe and centre circle coil pipe, medium flow from top to bottom, are uniformly mixed in intermediate mixing header, and medium is by centre mixing collection Case enters inner ring coil pipe, and medium flows to outlet header from bottom to top.
1 bottom centre of boiler barrel is equipped with burner 3, and the burning spout of burner 3 protrudes into burner hearth 2, and fuel is from burning Burning forms high-temperature flue gas and flows up in the penetrating burner hearth 2 of device 3, and flue gas flows downward through the first convection current exhaust gases passes 10 and inner ring With the media for heat exchange in centre circle coil pipe, flue gas, which flow to furnace bottom, turns back and flows up upwards through the second convection current exhaust gases passes 11 and outer ring Medium reverse flow heat exchange in coil pipe.
The intermediate mixing header 5 is equipped with mediator depletion mouth 12, can drain intermediate mixing by mediator depletion mouth 12 Medium in header 5.
The utility model has the advantages that: the medium due to entering inner ring coil pipe mixes in advance in intermediate mixing header, makes Medium temperature into inner ring coil pipe is consistent, so that Coil outlet temperature be made to be consistent, ensure that the safe operation of boiler.Two A first convection current exhaust gases passes are in parallel downwards, reduce a flue gas backhaul, reduce boiler smoke collateral resistance, reduce air blast The power consumption of machine, meanwhile, the second convection current exhaust gases passes flue gas and media for heat exchange become counterflow heat exchange, the thermal efficiency of boiler is improved, Third, medium can be drained by the evacuation port of intermediate mixing header in Boiler Furnace, be provided conveniently for blowing out and maintenance.4th, The resistance of boiler body is reduced, circulating pump effective power consumption is improved.

Claims (3)

1. the vertical bottom that one kind mixes in series and parallel combusts oily gas organic heat carrier boiler, including boiler barrel (1), boiler barrel (1) burner hearth (2) are equipped in, it is characterized in that: being successively arranged inner ring coil pipe (9), centre circle coil pipe (8) from inside to outside inside burner hearth (2) With outer ring coil pipe (7), centre circle coil pipe (8) and outer ring coil pipe (7) are arranged in parallel, the import of centre circle coil pipe (8) and outer ring coil pipe (7) Boiler barrel (1) and connection import header (4) jointly are stretched out in end upwards, the outlet end of centre circle coil pipe (8) and outer ring coil pipe (7) to Lower stretching boiler barrel (1) simultaneously connects intermediate mixing header (5) jointly;Inner ring coil pipe (9) and centre circle coil pipe (8), outer ring coil pipe (7) it is arranged in series, inner ring coil pipe (9) input end extends downwardly boiler barrel (1) and connects intermediate mixing header (5), inner ring disk Boiler barrel (1) and connection outlet header (6) are stretched out in pipe (9) outlet end upwards;Inner ring coil pipe (9) and centre circle coil pipe (8), centre circle The first convection current exhaust gases passes (10), outer ring coil pipe (7) and boiler barrel (1) side wall are formed between coil pipe (8) and outer ring coil pipe (7) Between form the second convection current exhaust gases passes (11).
2. the vertical bottom that one kind as described in claim 1 mixes in series and parallel combusts oily gas organic heat carrier boiler, feature Be: the intermediate mixing header (5) is equipped with mediator depletion mouth (12).
3. the vertical bottom that one kind as described in claim 1 mixes in series and parallel combusts oily gas organic heat carrier boiler, feature Be: boiler barrel (1) bottom centre is equipped with burner (3), and the burning spout of burner (3) protrudes into burner hearth (2).
CN201820772648.4U 2018-05-22 2018-05-22 A kind of vertical bottom mixed in series and parallel combusts oily gas organic heat carrier boiler Active CN208332681U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820772648.4U CN208332681U (en) 2018-05-22 2018-05-22 A kind of vertical bottom mixed in series and parallel combusts oily gas organic heat carrier boiler

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Application Number Priority Date Filing Date Title
CN201820772648.4U CN208332681U (en) 2018-05-22 2018-05-22 A kind of vertical bottom mixed in series and parallel combusts oily gas organic heat carrier boiler

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108613384A (en) * 2018-05-22 2018-10-02 无锡锡能锅炉有限公司 A kind of vertical bottom of connection in series-parallel mixing combusts oily gas organic heat carrier boiler

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108613384A (en) * 2018-05-22 2018-10-02 无锡锡能锅炉有限公司 A kind of vertical bottom of connection in series-parallel mixing combusts oily gas organic heat carrier boiler

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