CN106091722A - A kind of plant condenser moisturizing atomization system - Google Patents

A kind of plant condenser moisturizing atomization system Download PDF

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Publication number
CN106091722A
CN106091722A CN201610583450.7A CN201610583450A CN106091722A CN 106091722 A CN106091722 A CN 106091722A CN 201610583450 A CN201610583450 A CN 201610583450A CN 106091722 A CN106091722 A CN 106091722A
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China
Prior art keywords
condenser
layer
nozzle assembly
water
nozzle
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CN201610583450.7A
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CN106091722B (en
Inventor
郭清温
李本锋
卢海申
马建忠
王岩
郭永红
杨磊磊
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Datang Beijing Water Engineering Technology Co ltd
Datang Environment Industry Group Co Ltd
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Datang Beijing Energy Management Co Ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B9/00Auxiliary systems, arrangements, or devices
    • F28B9/04Auxiliary systems, arrangements, or devices for feeding, collecting, and storing cooling water or other cooling liquid

Abstract

A kind of plant condenser moisturizing atomization system, including pipeline, valve, atomising device, atomising device is arranged in condenser throat, if atomising device arranges dried layer nozzle assembly;Being provided with multiple atomizer on each layer of nozzle assembly, pipeline connects with power plant's Desalting Water System, utilizes water pump by the desalted water of certain pressure and flow velocity to be atomized water curtain mode, sprays from nozzle;Can meet a large amount of moisturizing demands during power plant's heat supply application, improve the heat exchange efficiency of moisturizing and turbine discharge, not affect the internal heat space making full use of condenser under the internal steam flow of condenser.

Description

A kind of plant condenser moisturizing atomization system
Technical field
The present invention relates to water chiller field, thermal power plant, particularly relate to a kind of condenser water replenishing atomization system and side Method.
Background technology
Power plant runs and there is steam in production process and condense the loss of water, loses, for supplementing these, the power plant caused Working medium reduces, and can supplement demineralized water in boiler, steam turbine equipment and therrmodynamic system thereof.Supplementary water generally has two ways to enter Therrmodynamic system: one is to enter oxygen-eliminating device, one is to enter condenser.
In existing water supplement technology, it is to make to supplement water to realize atomization at condenser throat, makes the chemistry filled water (20 of low temperature ~25 DEG C) in condenser throat, realize mixed heat transfer, part turbine discharge with the turbine discharge (more than 35 DEG C) of high temperature Condense in advance at condenser throat, so that the vapour amount that steam turbine enters Cooling Tubes of Condenser region reduces, so, at cooling tube In the case of inner cooling water amount, water temperature are constant, favourable to the vacuum improving condenser.But find in actual motion, existing dress Putting when moisturizing, owing to current are to spray water aperture ejection along several rows on condenser throat filling pipe, these apertures are along mending Length of pipe direction arranges, and hole diameter is 3mm~5mm, and under the effect of supplementing water pressure, moisturizing sprays with column.Column Current effluxvelocity fast, jet length is remote, and heat exchange area is less, so that the moisturizing of low temperature and high temperature steam discharge are at condenser Throat cannot obtain sufficient mixed heat transfer, it is impossible to makes turbine discharge farthest be condensed in throat.
In steam turbine heat supply application, a kind of is for steam to the technical process of factory steam unit.Now steam no longer returns To power plant.So, power plant's power set are just with greater need for a large amount of moisturizings, and otherwise, the water in Steam Power Equipment can be fewer and feweri, nothing Method is run.Generally, this strand of rate of water make-up is bigger.And use current water supplement technology, due to design rate of water make-up Normal power generation operation conditions corresponding to system, it is impossible to when meeting as heat supply offer application, corresponding to substantial amounts of system water supplement The actual demand of amount.
Summary of the invention
It is an object of the invention to provide the internal heat space of a kind of Appropriate application condenser, improve heat exchange efficiency, real The condenser water replenishing system that now a large amount of moisturizings access.
To achieve these goals, the technical scheme is that a kind of plant condenser moisturizing atomization system, including pipe Road, valve, atomising device, atomising device is arranged in condenser throat;The desalted water come from small pump, utilizes pipeline from condensing Access outside device throat, be connected with condenser water replenishing atomization system;When unit moisturizing, open valve, start water pump, desalted water Sequentially passing through pipeline, valve, atomising device, the desalted water being atomized into water smoke is sprayed onto condenser throat, is mixed into steam turbine row In vapour, enter bank of condenser pipes with Turbine Steam stream;It is characterized in that: if atomising device arranges dried layer nozzle assembly;Each Being provided with multiple atomizer on layer nozzle assembly, pipeline connects with power plant Desalting Water System, utilize water pump by certain pressure and The desalted water of flow velocity, to be atomized water curtain mode, sprays from nozzle.
The present invention uses and moisturizing accesses the injection of multilamellar atomized spray, it is achieved that condenser during heat supply application is mended in a large number Water, had both achieved sufficient rate of water make-up, had also improved condenser internal heat efficiency.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention
Fig. 2 is monolayer pipeline jointing construction schematic diagram
Fig. 3 is water curtain density terraced distribution schematic diagram
Fig. 4 is improved structure one schematic diagram of the present invention
Fig. 5 is improved structure two schematic diagram of the present invention
Detailed description of the invention
The invention will be further described below in conjunction with the accompanying drawings, it will be appreciated that content described herein is merely to illustrate With the explanation present invention, it is not intended to limit the present invention.
Plant condenser moisturizing atomization system, generally includes pipeline, valve, instrument, atomising device etc..Condenser water replenishing mist Change system is arranged in condenser throat.The desalted water come from small pump, accesses, with condenser water replenishing outside condenser throat Atomization system connects.When unit needs moisturizing, opening valve, start water pump, desalted water sequentially passes through pipeline, valve, atomization Device, the desalted water being atomized into water smoke is sprayed onto condenser throat, is mixed in turbine discharge, enters solidifying with Turbine Steam stream Vapour device is restrained.Moisturizing is atomized into water smoke, substantially reduces water droplet and washes away tube bank, and turbine discharge can also be played by moisturizing Cooling effect.
For producing the condenser of design, moisturizing atomization system can be condenser this body structure of product;For having made Condenser in, if carried out construction steam turbine heating steam project, needs a large amount of moisturizing, can be with construction reformation condenser larynx Portion, sets up moisturizing atomization system in throat.The design of moisturizing atomization system is core.Moisturizing atomization system is to be become by Multilayer Density The atomizer group changed realizes, and can effectively utilize condenser inner space, does not affect the steam discharge steam flow entered within condenser, Effectively realize big flow moisturizing and internal heat process.
Such as the condenser water replenishing apparatus structure schematic diagram in Fig. 1.
The atomising device arranged at condenser throat includes several layers of nozzle sets.The saturated vapor of about more than 30 DEG C is from steam turbine Enter condenser throat.The desalted water come from small pump, accesses outside condenser throat, with condenser water replenishing atomization system even Connect.When unit needs moisturizing, opening valve, start water pump, desalted water sequentially passes through pipeline, valve, atomising device, is atomized The desalted water becoming water smoke is sprayed onto condenser throat, is mixed in turbine discharge, enters bank of condenser pipes with Turbine Steam stream.
Atomising device is mainly arranged in condenser throat, is made up of N+1 layer pipeline, and N shell pipeline (nozzle sets) runs, and N >= 2,1 layers standby, and pipeline is installed nozzle, and pipeline connects with Desalting Water System, utilizes water pump by certain pressure and the desalination of flow velocity Water, to be atomized water curtain mode, sprays from nozzle one by one.
Preferably, desirable 2 layers of N, 2 layers of nozzle assembly are used for running, and 1 layer of nozzle assembly is standby.
Each layer of nozzle assembly has similar structure, is made up of given shape pipeline, and circular or rectangle, with condenser larynx The cross sectional shape in portion matches.Here citing circular configuration illustrates, the pipeline structure of each layer as in figure 2 it is shown, use in Two orthogonal main lines constitute single layer structure body, and connect multi-layer annular pipe, certain to set spacing installation on ring pipe The nozzle of quantity.One main line of the superiors for being passed through cooling water from outside.Two main line crossover sites are used for connecting many The vertical connecting tube of interlayer.Each layer nozzle assembly, is made up of pipeline and atomizer.Nozzle is arranged on pipeline.
The water curtain that every layer of nozzle assembly is formed has certain density, for each layer water curtain density, both can be identical, Can also differ, as optional upper layer density is high, lower layer density reduces step by step, is adapted to carry out in heat transfer process with steam discharge From top to bottom change thermal change demand.
The water curtain that same layer nozzle assembly is formed, its density both can be evenly arranged, it is also possible to is to divide in step Cloth.As it is shown on figure 3, the water curtain density of internal whole heat exchange cutting plane can use terraced distribution, it is positioned at the turbine discharge at center Flow velocity is maximum, needs to arrange water curtain density accordingly maximum, along reducing the most step by step, arranges internal edge steam turbine Steam flow speed is minimum, needs to arrange water curtain density accordingly minimum.Can need to arrange 3-5 level terraced distribution according to operating mode.
Water curtain density can use terraced distribution can use multiple specific implementation.
Mode one, its radial dimension of multilamellar nozzle sets becomes larger to lower floor from upper strata, as it is shown in figure 1, what multilamellar was arranged The different nozzle assembly of radial dimension can realize water curtain density terraced distribution on whole heat exchange cutting plane;
Mode two, in order to realize parts production standard, as shown in Figure 4, all can make each layer in multilamellar nozzle sets It is made the nozzle sets of normal structure and the size with 2-3 sublayer, each calibrating nozzle group carries out layering and arranges, multiple Sublayer can use radial dimension variation pattern, can realize water curtain density terraced distribution on whole heat exchange cutting plane;
Mode three, makes further for convenient and install, multilamellar nozzle sets can be designed to identical normal size, Each layer constitute adjusts its quantity installing nozzle sets on pipeline, will constitute pipeline distribution 3-5 level concentric circular interval, position On the pipeline that concentric circular in center is interval, unit length top nozzle quantity is most, is positioned on the pipeline in concentric circular interval at edge Unit length top nozzle minimum number, reduces quantity from center to edge step.
Preferably, if as it is shown in figure 5, when the arrangement space of condenser throat is inadequate, also can be further by 1-3 layer The intermediate space of both sides tube bank in nozzle assembly layout entrance condenser main body.It is arranged on the nozzle assembly within condenser and larynx The nozzle assembly in portion has structure and the size of the plane differed, and is adapted to the spatial form within condenser, and not shadow Steam discharge within Xianging and interbank heat exchange.
As in figure 2 it is shown, include multiple ring pipe (nozzle assembly corresponding to circular) or grid at every layer of nozzle assembly Type pipe (corresponding to the nozzle assembly of rectangle, not shown in figure).Ring-like or the grid type pipeline chi that each layer nozzle assembly is used Very little, both can be identical, it is also possible to differ, be adjusted according to installed nozzle quantity.Every layer of nozzle assembly It is provided with adjustment switch valve between pipeline, connected relation can be regulated by adjusting switch valve, both can be connection, it is possible to Being disconnected.
Each annular of nozzle assembly or grid type pipe, be passed through shower water from outside.To set in annular or grid type pipe Determining deviation installs a number of nozzle.Nozzle selects spiral nozzle, is fixed on water-supply-pipe in the way of screw thread, flange or welding Lu Shang, material selection 316L, precision casting process.Spray angle select 60 degree, 90 degree, 120 degree, 150 degree, 170 degree, hollow or Solid-cone is sprayed.
The cone of the taper water curtain of spiral nozzle ejection is high, end circular diameter is all corresponding with hydraulic pressure and flow velocity, therefore, and each spray Circular diameter (size) at the bottom of the water curtain of mouth can be considered it is known that the sectional area of throat is also known.Each layer can be calculated accordingly The quantity of the spiral nozzle arranged.Arranging enough nozzle sets on pipeline, supplementary desalted water is to be atomized water curtain mode, from one Individual nozzle sprays, and forms atomization water curtain skirt layer.
Nozzle is installed on each layer nozzle assembly pipeline, both can be quantity to be installed in unit length formed uniform, it is possible to To be change.Installed nozzle total quantity on each layer nozzle assembly pipeline, both can be identical, it is also possible to be to differ 's.
Nozzle material it is installed on each layer nozzle assembly pipeline and fixing pattern is installed, both can be identical, it is also possible to be Differ.
Last it is noted that the foregoing is only the explanation of the present invention, it is not limited to the present invention, although to this Bright being described in detail, for a person skilled in the art, it still can be to aforementioned described technical scheme Modify, or wherein portion of techniques feature is carried out equivalent.All within the spirit and principles in the present invention, made Any modification, equivalent substitution and improvement etc., should be included within the scope of the present invention.

Claims (10)

1. a plant condenser moisturizing atomization system, including pipeline, valve, atomising device, atomising device is arranged on condenser In throat;The desalted water come from small pump, utilizes pipeline to access outside condenser throat, with condenser water replenishing atomization system even Connect;When unit moisturizing, opening valve, start water pump, desalted water sequentially passes through pipeline, valve, atomising device, is atomized into water The desalted water of mist is sprayed onto condenser throat, is mixed in turbine discharge, enters bank of condenser pipes with Turbine Steam stream;Its feature It is: if atomising device arranges dried layer nozzle assembly;Being provided with multiple atomizer on each layer of nozzle assembly, pipeline is with electricity Factory's Desalting Water System connects, and utilizes water pump by the desalted water of certain pressure and flow velocity to be atomized water curtain mode, sprays from nozzle.
Plant condenser moisturizing atomization system the most according to claim 1, it is characterised in that atomising device includes that N+1 layer sprays Nozzle assembly, N shell nozzle assembly is used for running, and 1 layer of nozzle assembly is standby, N >=2.
Plant condenser moisturizing atomization system the most according to claim 1, it is characterised in that if dried layer nozzle assembly is formed Water curtain, each layer water curtain density, reduce step by step to lower floor from upper strata.
Plant condenser moisturizing atomization system the most according to claim 1, it is characterised in that same layer nozzle assembly is formed Water curtain density use terraced distribution, be positioned at centrally disposed water curtain density maximum, along reducing the most step by step, at edge It is minimum that water curtain density is set.
Plant condenser moisturizing atomization system the most according to claim 1, it is characterised in that the nozzle assembly being positioned at lower floor sets Put in bank of condenser pipes middle part, there is structure and the size of the plane differed with the nozzle assembly being positioned at upper strata.
Plant condenser moisturizing atomization system the most according to claim 4, it is characterised in that every layer of nozzle assembly includes multiple Annular or grid type pipe, the pipeline structure of same layer nozzle assembly is the planar structure of uneven terraced distribution.
Plant condenser moisturizing atomization system the most according to claim 4, it is characterised in that each layer has multiple sublayer knot Structure, the plurality of sublayer structure, there is the physical dimension reducing change step by step.
Plant condenser moisturizing atomization system the most according to claim 1, it is characterised in that the pipeline of every layer of nozzle assembly it Between be provided with adjustment switch valve, regulate, by adjusting switch valve, the relation that is interconnected between each layer.
Plant condenser moisturizing atomization system the most according to claim 4, it is characterised in that every layer of nozzle assembly includes multiple Annular or grid type pipe, to set the spacing a number of nozzle of installation in annular or grid type pipe, be positioned at the pipeline at center Upper unit length top nozzle quantity is most, is positioned at unit length top nozzle minimum number on the pipeline at edge, from center to edge Step reduces quantity.
Plant condenser moisturizing atomization system the most according to claim 1, it is characterised in that on each layer nozzle assembly pipeline Nozzle quantity, nozzle model, nozzle material and installation approach are installed differ.
CN201610583450.7A 2016-07-15 2016-07-15 Water supplementing and atomizing system for condenser of power plant Active CN106091722B (en)

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CN106731614A (en) * 2017-01-14 2017-05-31 河北宏龙环保科技有限公司 A kind of method and apparatus of flue gas desulfurization and denitrification
CN107084627A (en) * 2017-05-08 2017-08-22 华电电力科学研究院 Large-scale counter-flow cooling tower preventing freeze in winter water dispensing apparatus
CN114705077A (en) * 2022-03-22 2022-07-05 中海石油气电集团有限责任公司 Refrigerant uniform distribution system of LNG (liquefied Natural gas) coiled tube heat exchanger

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Publication number Priority date Publication date Assignee Title
CN106731614A (en) * 2017-01-14 2017-05-31 河北宏龙环保科技有限公司 A kind of method and apparatus of flue gas desulfurization and denitrification
CN107084627A (en) * 2017-05-08 2017-08-22 华电电力科学研究院 Large-scale counter-flow cooling tower preventing freeze in winter water dispensing apparatus
CN107084627B (en) * 2017-05-08 2023-01-06 华电电力科学研究院有限公司 Winter anti-freezing water distribution device for large-scale countercurrent cooling tower
CN114705077A (en) * 2022-03-22 2022-07-05 中海石油气电集团有限责任公司 Refrigerant uniform distribution system of LNG (liquefied Natural gas) coiled tube heat exchanger

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