A kind of steam exhaust recovering device
Technical field
This utility model belongs to heat-exchange apparatus technical field, relates to a kind of for thermoelectricity or change
The equipment such as work oxygen-eliminating device, continuous blowdown flash tank, flash tank, drainer discharge exhaust steam (ES)
Carry out the device reclaimed.
Background technology
At present the known type steam exhaust recovering device product of this area be all by injection, mixing,
The phase process such as collection reclaim exhaust steam, a large amount of electric adjusting device of intermediate demand, generally also exist
Structure is complicated, investment is big, recovery usefulness is low, removal process energy consumption big, cost of investment cannot be returned
The defects such as receipts, affect the enthusiasm of environmental protection of enterprise investment, so that considerable enterprise can only leave
Arrange outside exhaust steam, cause the waste of this partial heat and water resource.
Utility model content
The purpose of this utility model is that the problem that there is prior art is solved, it is provided that one
Kind of compact conformation, cost of investment are low, it is high, stable to reclaim usefulness, Non-energy-consumption, can have
Exhaust steam total condensation is quickly become the steam exhaust recovering device of hot water by the space of limit.
The technical solution used for achieving the above object is such that being provided
Steam exhaust recovering device has about one two ends and has vent connection and hot water outlet pipe
Hollow upright cylinder, be disposed with from top to bottom in cylinder cold water distributor, spray district,
Packing layer, condensing zone and hydrothermal area, have and cold water distributor and solidifying on cylinder lateral wall
The cold water inlet of interface connection and exhaust steam import, be provided with one end band loudspeaker in the middle of condensing zone
The exhaust steam distributor of type diffusing opening, the other end of exhaust steam distributor is connected with exhaust steam import.
In above-mentioned steam exhaust recovering device, cold water distributor is arranged on cylinder lumen top by coiling
Circular water pipe is constituted, and one end of circular water pipe is connected with cold water inlet, in circular water pipe down tube
Be placed with multiple swirl nozzle on wall, described spray district for be positioned at circular water pipe and packing layer it
Between shell cavity region.
In above-mentioned steam exhaust recovering device, packing layer by the upper frame being welded in the middle part of cylinder lumen,
Underframe and the silk screen stainless steel helices being filled between upper and lower framework are constituted.
In above-mentioned steam exhaust recovering device, condensing zone is positioned at the lower zone of packing layer, at condensing zone
Centre is provided with the exhaust steam distributor of band trumpet type diffusing opening, and the trumpet type at exhaust steam distributor spreads
Mouthful diffusingsurface on have multiple aperture, to the region between hot water outlet pipe below condensing zone
For hydrothermal area.
Work process of the present utility model is such that opening cold water inlet and exhaust steam import,
Cold water passes to swirl nozzle through the circular water pipe of cold water distributor and is uniformly injected in spray district, and then
Fall to condensing zone through packing layer, exhaust steam import the exhaust steam entered is through the loudspeaker of exhaust steam distributor
Type diffusing opening is diffused in coagulation region, first carries out first order mass transfer heat exchange with cold water, condenses big portion
The water liquid after exhaust steam is divided to enter hydrothermal area;Rise to packing layer with the gas of fraction exhaust steam enter again
The mass transfer heat exchange of the row second level, absorbs the liquid after the most substantial amounts of exhaust steam and falls into condensing zone again and change
Heat, the third level carrying out exhaust steam and cold water in spray district again with the gas of more small part exhaust steam passes
Matter heat exchange, absorbs the liquid after last exhaust steam and falls into packing layer and condensing zone the most successively;So
Moving in circles, lower housing portion intracavity has condensed the water liquid of most exhaust steam and has formed hydrothermal area, heat
Water flows out from hot water outlet pipe, completes exhaust steam and reclaims whole process;Remaining non-condensing gas is then
Discharge through vent connection.
Compared with existing similar technique, this utility model have compact equipment, small investment,
The advantages such as stable, Non-energy-consumption, more energy efficient, more environmentally friendly, adaptive ability is strong, it can be
Exhaust steam total condensation is quickly become hot water by limited space, thus reclaims one and cut with recovery value
The heat of exhaust steam and condensation water, and incondensable gas can be arranged, be suitable to application.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of circular water pipe sections.
Fig. 3 is the structural representation of packing layer part.
In figure, the title of each number designation is respectively: 1-cylinder, 2-hydrothermal area, and 3-condenses
District, 4-exhaust steam import, 5-packing layer, 6-sprays district, 7-cold water distributor, and 8-arranges
Gas is taken over, and 9-cold water inlet, 10-exhaust steam distributor, 11-hot water outlet pipe, on 12-
End socket, 15-circle water pipe, 16-swirl nozzle, 17-(packing layer) upper frame, 18-fills out
Material, 19-(packing layer) underframe.
Detailed description of the invention
Seeing accompanying drawing, steam exhaust recovering device described in the utility model has a band upper cover
The cylinder 1 of the hollow upright of 12, in the upper end of cylinder 1, i.e. upper cover 12 center has one
The individual vent connection 8 for emptying incondensable gas, have in the lower end of cylinder 1 one for
Discharge the hot water outlet pipe 11 of hot water, be disposed with from top to bottom in the housing of cylinder 1
Cold water distributor 7, spray district 6, packing layer 5, condensing zone 3 and hydrothermal area 2, at cylinder 1
The top of sidewall has a cold water inlet 9 connected with cold water distributor 7, at cylinder 1
The bottom of sidewall has an exhaust steam import 4 being passed through condensing zone 3.
The top of cold water distributor 7 connects with upper cover 12, coiling be arranged in cylinder 1
The circular water pipe 15 on top, chamber is constituted (seeing Fig. 2), and one end of circular water pipe 15 is entered with cold water
Water pipe 9 connects, and is placed with multiple swirl nozzle 16, work on the lower tube wall of circular water pipe 15
By each outside shower water liquid of swirl nozzle 16 when making.
Spray district 6 is the one section of barrel chamber space being arranged under cold water distributor 7, and exhaust steam is empty at this
In with shower water liquid carry out third level mass transfer heat exchange.
Packing layer 5 is positioned under spray district 6, including one by upper frame 17, underframe 19
The framework comb group constituted, framework comb bond pads, in cylinder 1, is filled with silk screen in framework comb group
Stainless steel helices 18.Packing layer 5 is mainly used in carrying out the gas with fraction exhaust steam again
Second level mass transfer heat exchange.
Condensing zone 3 is the region below packing layer 5, is provided with an one end in the middle of condensing zone 3
With the exhaust steam distributor 10 of trumpet type diffusing opening, the other end of exhaust steam distributor 10 enters with exhaust steam
Mouth 4 connects, and exhaust steam distributor 10 is connected trumpet type diffusing opening, diffusion by exhaust steam steam inlet pipe road
Aperture is had on face.It is hot water to the region between hot water outlet pipe 11 below condensing zone 3
District 2, hydrothermal area 2 connects hot water outlet pipe 11.During work, exhaust steam import 4 enter cylinder
Exhaust steam after the trumpet type diffusing opening of exhaust steam distributor, be diffused in condensing zone, the exhaust steam diffused out
Carrying out first order mass transfer heat exchange with cold water, the water liquid after condensation major part exhaust steam enters hydrothermal area 2,
Finally flow out from hot water outlet pipe 11, complete exhaust steam and reclaim whole process.