CN201844390U - Water spray desuperheater - Google Patents

Water spray desuperheater Download PDF

Info

Publication number
CN201844390U
CN201844390U CN2010205887485U CN201020588748U CN201844390U CN 201844390 U CN201844390 U CN 201844390U CN 2010205887485 U CN2010205887485 U CN 2010205887485U CN 201020588748 U CN201020588748 U CN 201020588748U CN 201844390 U CN201844390 U CN 201844390U
Authority
CN
China
Prior art keywords
venturi tube
cooling water
inner chamber
desuperheater
tube
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 - Lifetime
Application number
CN2010205887485U
Other languages
Chinese (zh)
Inventor
赵树平
李军
程栾庆
杨平
陈崇柱
彭延生
韩学义
张鹏
彭民
张贞元
曹茂永
王毅
范迪
程学珍
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.)
FEICHENG MINING INDUSTRY GROUP Co Ltd
FEICHENG BAIZHUANG COAL MINE Co Ltd
Shandong University of Science and Technology
Original Assignee
FEICHENG MINING INDUSTRY GROUP Co Ltd
FEICHENG BAIZHUANG COAL MINE Co Ltd
Shandong University of Science and Technology
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
Publication date
Application filed by FEICHENG MINING INDUSTRY GROUP Co Ltd, FEICHENG BAIZHUANG COAL MINE Co Ltd, Shandong University of Science and Technology filed Critical FEICHENG MINING INDUSTRY GROUP Co Ltd
Priority to CN2010205887485U priority Critical patent/CN201844390U/en
Application granted granted Critical
Publication of CN201844390U publication Critical patent/CN201844390U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Abstract

The utility model relates to a water spray desuperheater, which belongs to the field of boiler equipment and comprises a tubular desuperheater header and the like. An inner sleeve is sheathed with the inner chamber of the desuperheater header; a primary Venturi tube and a secondary Venturi tube are arranged in the inner chamber of the inner sleeve; the flaring section of the primary Venturi tube enters into the inner chamber of the throat of the secondary Venturi tube from the left end of the secondary Venturi tube; a cooling water tube vertically passes through the desuperheater header and the inner sleeve; the lower end of the cooling water tube is connected with the upper end of the throat of the primary Venturi tube; the inner chamber of the cooling water tube is communicated with the inner chamber of the primary Venturi tube; the lower end of a centrifugal nozzle extends into the inner chamber of the primary Venturi tube after passing through the cooling water tube; and the spray direction of a spray orifice at the lower end of the centrifugal nozzle is over against the secondary Venturi tube. According to the utility model, the problems of small atomization range and poor heat exchange effect of desuperheating water are solved through combining the centrifugal nozzle with the primary Venturi tube and the secondary Venturi tube; and the water spray desuperheater has a simple processing technology and can effectively atomize the desuperheating water on a large scale, thereby effectively improving the heat exchange performance of the desuperheater.

Description

Direct-contact desuperheater
Technical field
The utility model relates to a kind of boiler plant, refers to a kind of direct-contact desuperheater especially.
Background technology
Attemperator is to be used for the visual plant of steam regulation temperature, in the thermal power plant, boiler produces a large amount of superheated steams, if do not equip attemperator, with regard to being difficult to the temperature of boiler export steam is controlled in the scope that needs, the boiler turbine relevant device is damaged because of overtemperature or cause a serious accident, when vapor (steam) temperature can not satisfy the steam turbine requirement, just must carry out desuperheat to superheated steam by attemperator.
Attemperator mainly contains two kinds of contactless and direct contact types, because the contactless heat exchange efficiency that exists is low, volume is big, shortcomings such as waste cooling water, the at present employing realized the direct contact type attemperator of lowering the temperature more by spraying water, the direct contact type attemperator directly contacts with superheated steam by cooling water lowers the temperature, it is spray desuperheating, existing as shown in Figure 1 attemperator structural representation, it is by the desuperheat water pipe 1 ' of horizontal placement, cooling water pipe 2 ' the one that is positioned over the first order Venturi tube 3 ' of desuperheat water pipe 1 ' inner chamber and vertically places constitutes, cooling water pipe 2 ' vertically passes desuperheat water pipe 1 ' and first order Venturi tube 3 ', desuperheat water pipe 1 ' is from right to left successively by superheated steam entrance point 4 ', the second level Venturi tube 5 ' and the superheated steam port of export 6 ' constitute, the flared section 32 ' of first order Venturi tube 3 ' left part is arranged at the flared section 52 ' of second level Venturi tube 5 ' inner chamber and the aditus laryngis place between the reducing section 51 ', the reducing section 31 ' of first order Venturi tube 3 ' right part is arranged at the inner chamber of superheated steam entrance point 4 ', the inner chamber of first order Venturi tube 3 ' and second level Venturi tube 5 ' communicates, offer a circle groove 7 ' and an apopore 8 ' on the aditus laryngis below tube wall of the reducing section 31 ' of first order Venturi tube 3 ' and flared section 32 ' junction, groove 7 ' communicates with the inner chamber of cooling water pipe 2 ', this attemperator adopts the two-stage Venturi tube, cooling water flows into the inner chamber of first order Venturi tube 3 ' behind groove 7 ' on the first order Venturi tube 3 ' and apopore 8 ' from cooling water pipe 2 ', after superheated steam enters first order Venturi tube 3 ', air-flow from the coarse to fine, gas flow rate is accelerated, make gas form a negative pressuren zone in the below of the aditus laryngis of this first order Venturi tube 3 ', cooling water apopore 8 ' is in this negative pressuren zone, negative pressure produces certain swabbing action to cooling water, make cooling water flow into first order Venturi tube 3 ' inner chamber at first order Venturi tube 3 ' aditus laryngis below negative pressuren zone, cooling water is carried out the atomizing first time, and mix with the superheated steam of coming in from right-hand member superheated steam entrance point 4 ', the mixed vapour that comes out from first order Venturi tube 3 ', directly enter the aditus laryngis of second level Venturi tube 5 ', the mixed vapour that utilizes the high-speed gas of second level Venturi tube 5 ' aditus laryngis that first order Venturi tube 3 ' is come out carries out the atomizing second time, mixes the back once more with superheated steam and flows out attemperator from the superheated steam port of export 6 '.
The shortcoming of this structure is that manufacturing process complicated and pressure and flow that must guarantee to flow to the superheated steam of attemperator are enough stablized, if superheated steam pressure and flow hour, the two-stage Venturi tube can not form enough suction forces, the attemperator cooling effect is poor, this attemperator temperature lowering effect is relevant with load variations, when being superheated steam pressure and instability of flow, the jet atomization weak effect of Venturi tube, cooled vapor (steam) temperature of attemperator and pressure are also unstable.
The utility model content
The purpose of this utility model is to provide a kind of direct-contact desuperheater, the heat exchange property that its manufacturing process is simple, the desuperheating water that can efficiently atomize on a large scale also effectively improves attemperator.
To achieve these goals, technical solution of the present utility model is: a kind of direct-contact desuperheater, attemperator header comprising tubulose, inner sleeve, first, the secondary Venturi tube, cooling water pipe and L shaped rotarytype injector, described inner sleeve is socketed on attemperator header inner chamber, described first, the secondary Venturi tube is arranged at the inner chamber of inner sleeve, the flared section right-hand member of described first order Venturi tube right part enters the aditus laryngis inner chamber of second level Venturi tube from the left end of second level Venturi tube, described cooling water pipe vertically passes the upper wall and the inner sleeve of attemperator header, aditus laryngis place vertical connection of upper end of described cooling water pipe lower end and described first order Venturi tube, the inner chamber of described cooling water pipe communicates with the inner chamber of described first order Venturi tube, the inner chamber that stretches into first order Venturi tube behind the cooling water pipe is passed in described rotarytype injector lower end, and spraying to of the spray orifice of described rotarytype injector lower end faces second level Venturi tube.
The utility model direct-contact desuperheater, wherein said cooling water pipe and first order Venturi tube are fixed together by welding or being spirally connected.
After adopting such scheme, the utility model direct-contact desuperheater combines by rotarytype injector and two-stage Venturi tube, make Venturi effect strengthen the jeting effect of nozzle, and nozzle ejection has been strengthened Venturi effect, their actings in conjunction, the range of cooling water has extended, improved the mixability of cooling water and superheated vapour, desuperheating water has on a large scale efficiently atomized, thereby strengthened the heat exchange efficiency of attemperator, and owing to this attemperator is formed by connecting by each independent parts, and each several part is simple in structure so processing technology is simple.
Description of drawings
Fig. 1 is the structural representation of existing attemperator;
Fig. 2 is the structural representation of the utility model direct-contact desuperheater.
Below in conjunction with accompanying drawing, the utility model is described further by embodiment.
The specific embodiment
See also shown in Figure 2ly, the utility model direct-contact desuperheater comprises attemperator header 1, inner sleeve 2, first order Venturi tube 3, second level Venturi tube 4, cooling water pipe 5 and the L shaped rotarytype injector 6 of tubulose;
Inner sleeve 2 is socketed on the inner chamber of attemperator header 1, first order Venturi tube 3 and second level Venturi tube 4 are placed on the inner chamber of inner sleeve 2, first order Venturi tube 3 is made of the reducing section 31 of left part and the flared section 32 of right part, second level Venturi tube 4 is made of the reducing section 41 of left part and the flared section 42 of right part, and the right-hand member of the flared section 32 of first order Venturi tube 3 right parts extend into the aditus laryngis inner chamber of second level Venturi tube 4 from the left end of second level Venturi tube 4;
Cooling water pipe 5 vertically passes the upper wall and the inner sleeve 2 of attemperator header 1, the lower end of cooling water pipe 5 is weldingly fixed on the upper end, aditus laryngis place of first order Venturi tube 3, the inner chamber of cooling water pipe 5 communicates with the inner chamber of first order Venturi tube 3, the inner chamber that stretches into first order Venturi tube 3 behind the cooling water pipe 5 is passed in rotarytype injector 6 lower ends, and spraying to of the spray orifice 7 of rotarytype injector 6 lower ends faces second level Venturi tube 4.
During the work of the utility model direct-contact desuperheater, superheated steam enters first order Venturi tube 3 backs along with flow velocity rises, its pressure can reduce, first order Venturi tube 3 is blown into high velocity air, aditus laryngis district in first order Venturi tube 3 can form low pressure, lower relatively back near the air pressure spray orifice 7 of the rotarytype injector 6 of overfire air stream, this low pressure produces a suction force on spray orifice 7, this suction force has been strengthened the jet-action of spray orifice 7, and quickened speed air flow in the first order Venturi tube 3, and the superheated steam outside the pulling first order Venturi tube 3, the flared section 32 that can be covered with first order Venturi tube 3 from cooling water pipe 5 inflows through the jet face of the cooling water of rotarytype injector 6, make cooling water and superheated steam after flared section 32 places are fully mixed, pressure raises, the air velocity at second level Venturi tube 4 aditus laryngis places is accelerated, utilize combination rotarytype injector 6 and first order Venturi tube 3 and second level Venturi tube 4, make Venturi effect strengthen the jeting effect of nozzle, the nozzle ejection effect has increased reducing section 31 and the reducing section 41 of second level Venturi tube 4 and the pressure reduction in aditus laryngis district of first order Venturi tube 3 again, strengthened Venturi effect, extended the again range of cooling water of rotarytype injector 6 ejections of Venturi effect, improved the mixability of cooling water and superheated vapour, cooling water reaches superfine atomizing effect, thereby has improved the heat exchange efficiency of attemperator; Rotarytype injector 6 combines with first order Venturi tube 3 and second level Venturi tube 4, has fabulous water spray effect, steam regulation temperature, and this attemperator on a large scale is formed by connecting by each independent parts, and each several part is simple in structure so the simple cost of processing technology is low; This structure is subjected to the influence of steam flow and pressure little, even steam flow and pressure transient, attemperator also can steady operation, has improved the ability that steam load changes significantly that adapts to; The volume of L shaped rotarytype injector is little, can reduce the impulsive force of superheated steam to spray orifice, improves its service life.
The above embodiment is described preferred implementation of the present utility model; be not that scope of the present utility model is limited; under the prerequisite that does not break away from the utility model design spirit; various distortion and improvement that the common engineers and technicians in this area make the technical solution of the utility model all should fall in the definite protection domain of claims of the present utility model.

Claims (2)

1. direct-contact desuperheater, it is characterized in that: the attemperator header (1) that comprises tubulose, inner sleeve (2), first, secondary Venturi tube (3,4), cooling water pipe (5) and L shaped rotarytype injector (6), described inner sleeve (2) is socketed on attemperator header (1) inner chamber, described first, secondary Venturi tube (3,4) be arranged at the inner chamber of inner sleeve (2), flared section (32) right-hand member of described first order Venturi tube (3) right part enters the aditus laryngis inner chamber of second level Venturi tube (4) from the left end of second level Venturi tube (4), described cooling water pipe (5) vertically passes the upper wall and the inner sleeve (2) of attemperator header (1), aditus laryngis place vertical connection of upper end of described cooling water pipe (5) lower end and described first order Venturi tube (3), the inner chamber of described cooling water pipe (5) communicates with the inner chamber of described first order Venturi tube (3), the inner chamber that stretches into first order Venturi tube (3) behind the cooling water pipe (5) is passed in described rotarytype injector (6) lower end, and spraying to of the spray orifice (7) of described rotarytype injector (6) lower end faces second level Venturi tube (4).
2. direct-contact desuperheater as claimed in claim 1 is characterized in that: described cooling water pipe (5) is fixed together by welding or being spirally connected with first order Venturi tube (3).
CN2010205887485U 2010-11-02 2010-11-02 Water spray desuperheater Expired - Lifetime CN201844390U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010205887485U CN201844390U (en) 2010-11-02 2010-11-02 Water spray desuperheater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010205887485U CN201844390U (en) 2010-11-02 2010-11-02 Water spray desuperheater

Publications (1)

Publication Number Publication Date
CN201844390U true CN201844390U (en) 2011-05-25

Family

ID=44039279

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010205887485U Expired - Lifetime CN201844390U (en) 2010-11-02 2010-11-02 Water spray desuperheater

Country Status (1)

Country Link
CN (1) CN201844390U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101979918A (en) * 2010-11-02 2011-02-23 肥城白庄煤矿有限公司 Spray desuperheater
CN104949103A (en) * 2014-03-28 2015-09-30 斗山重工业株式会社 Water spray type desuperheater and desuperheating method
CN110332517A (en) * 2019-07-17 2019-10-15 无锡职业技术学院 A kind of nozzle of steam assisted atomization
CN110849045A (en) * 2019-10-17 2020-02-28 合肥美的电冰箱有限公司 Refrigeration device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101979918A (en) * 2010-11-02 2011-02-23 肥城白庄煤矿有限公司 Spray desuperheater
CN104949103A (en) * 2014-03-28 2015-09-30 斗山重工业株式会社 Water spray type desuperheater and desuperheating method
CN104949103B (en) * 2014-03-28 2017-09-19 斗山重工业株式会社 Water spray formula overheat cooling device and method
CN110332517A (en) * 2019-07-17 2019-10-15 无锡职业技术学院 A kind of nozzle of steam assisted atomization
CN110332517B (en) * 2019-07-17 2023-02-14 无锡职业技术学院 Steam-assisted atomizing nozzle
CN110849045A (en) * 2019-10-17 2020-02-28 合肥美的电冰箱有限公司 Refrigeration device

Similar Documents

Publication Publication Date Title
CN101979918B (en) Spray desuperheater
CN201844390U (en) Water spray desuperheater
CN201382403Y (en) Desuperheater
CN103016423A (en) Novel changeable-jet-nozzle-position steam ejector
CN106224949B (en) A kind of non-coaxial horizontal bias low NOx DC coal burner
CN204404351U (en) A kind of for the mixed water heat-exchanger rig in heating system
CN104534105B (en) Integral type exhaust steam desuperheat booster
CN201326587Y (en) Vacuumizing device for smelting
CN202403262U (en) Preheating injection steam desuperheater for desuperheater water
CN202010598U (en) Steam atomization type porous nozzle apparatus
CN202451477U (en) Jetting type heat pump without receiving chamber
CN109653807B (en) Steam compensating device
CN203628624U (en) Throat structure of spray type desuperheater
CN202885584U (en) Condenser for turboset
CN208487710U (en) A kind of air cooling tubes condenser spray humidification cooling system of combination deflector
CN206071886U (en) For the pressure charging temperature reduction device and vacuum pump system of vacuum pump
CN201982148U (en) Vacuum steam heating and pressurizing recovery device for steam turbine
CN206609306U (en) Vaccum-pumping equipment
CN209909907U (en) Gas combustion nozzle
CN205635673U (en) Converter coal gas clarification plant that once removes dust
CN203203021U (en) Steam water-pumping type steam desuperheater
CN109611165A (en) A kind of application method of the new vapour source of heat exchangers for district heating
CN204897951U (en) Blast furnace stokehold dust removing facility
CN104197737A (en) Energy-saving cooling device for direct air cooling system
CN212998475U (en) Condenser deaerating plant and system with injection type nozzle

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20110525

Effective date of abandoning: 20120606