CN208626639U - A kind of UTILIZATION OF VESIDUAL HEAT IN salt separator - Google Patents
A kind of UTILIZATION OF VESIDUAL HEAT IN salt separator Download PDFInfo
- Publication number
- CN208626639U CN208626639U CN201821292097.8U CN201821292097U CN208626639U CN 208626639 U CN208626639 U CN 208626639U CN 201821292097 U CN201821292097 U CN 201821292097U CN 208626639 U CN208626639 U CN 208626639U
- Authority
- CN
- China
- Prior art keywords
- salt water
- salt
- utilization
- jet chimney
- water reservoir
- 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.)
- Active
Links
Abstract
The utility model relates to salt water separating treatment technical field more particularly to a kind of UTILIZATION OF VESIDUAL HEAT IN salt separators, including salt water reservoir, jet chimney, brine pipeline, in which: salt water reservoir is the closed box with top cover, and its underpart is immersed in quenching salt tank；Jet chimney is arranged vertically at the top of salt water reservoir；Jet chimney it is top closed, bottom is connected to salt water reservoir, and the inner cavity of jet chimney forms steam accumulation chamber；The bottom of steam accumulation chamber is communicated with separation water outlet pipeline；Brine pipeline wraps up jet chimney arrangement, forming salt water cavity between brine pipeline and jet chimney；The bottom of salt water cavity is communicated with salt water inlet pipeline, and top is connected to by salt water outlet pipeline with salt water reservoir.On the one hand the UTILIZATION OF VESIDUAL HEAT IN salt separator of the utility model makes full use of quenching waste heat to realize salt water separation, on the other hand also achieve the continuous supply of saline solution in quenching salt tank, practical, and structure is simple, occupies little space.
Description
Technical field
The utility model relates to salt water separating treatment technical field more particularly to a kind of UTILIZATION OF VESIDUAL HEAT IN salt separators.
Background technique
There are three types of the cooling typical medias of workpiece quenching, i.e. water, oil and salt, when having Quench heating due to salt bath quenching
Between short, Temperature Distribution is good, copes with large-scale heat treatment condition, the advantages that oxidation and decarbonization is few, thus obtain more wide
General application.But after salt bath quenching, workpiece surface can take residual salt out of, can generate a large amount of brine waste after residual salt cleaning, directly
Run in put and will cause environmental pollution, and waste of resource, it is therefore desirable to which salt water separation is carried out to brine waste.
The method for realizing salt water separation industrial at present is usually electric heating evaporation, cooking process, gas heating cooking process
Deng, be required to expend a large amount of energy, as electric heating consume energy 1.3kwh/L, heated by natural gas consume energy 0.13m3/L.Although city
There are some equipment for carrying out salt water separation using quenching waste heat on face, but structure is complex, and occupied space is big, manufacturing cost
It is high.
Utility model content
The purpose of this utility model is to provide one kind can make full use of quenching waste heat and the simple UTILIZATION OF VESIDUAL HEAT IN salt of structure
Separator.
To achieve the goals above, the utility model provides a kind of UTILIZATION OF VESIDUAL HEAT IN salt separator, including salt water liquid storage
Slot, jet chimney, brine pipeline, in which: salt water reservoir is the closed box with top cover, and its underpart is immersed in quenching salt tank；
Jet chimney is arranged vertically at the top of salt water reservoir；Jet chimney it is top closed, bottom is connected to salt water reservoir, steam
The inner cavity in steam pipe road forms steam accumulation chamber；The bottom of steam accumulation chamber is communicated with separation water outlet pipeline；Brine pipeline package
Jet chimney arrangement, forming salt water cavity between brine pipeline and jet chimney；The bottom of salt water cavity is communicated with salt water inlet pipeline,
Top is connected to by salt water outlet pipeline with salt water reservoir.
Further, steam discharge pipe is vertically arranged in steam accumulation chamber, steam accumulation chamber passes through with salt water reservoir
Steam discharge pipe connection.
Further, the choke device that the top of steam accumulation chamber is disposed with for reducing steam flow rate.
Further, choke device includes support rod and several gas barrier plates, in which: support rod is along steam accumulation chamber
Heart axis vertical arrangement；Several gas barrier plates are successively spaced stacking and are fixed on support rod.
Further, gas barrier plate is umbrella gas barrier plate, and open end is towards the bottom of steam accumulation chamber.
Further, along support rod, circumferential size gradually becomes smaller several gas barrier plates from bottom to top.
Further, the bottom of salt water reservoir be disposed with vertically it is several connection salt water reservoirs and quenching salt tank it is thermally conductive
Heat exchanger tube.
Further, the top of salt water reservoir has outwardly extending flank, and flank relies on quenching salt tank groove body
And it is bolted.
A kind of UTILIZATION OF VESIDUAL HEAT IN salt separator of the utility model, has the advantages that
1, the UTILIZATION OF VESIDUAL HEAT IN salt separator of the utility model, salt water reservoir lower part are immersed in quenching salt tank, can be led to
It crosses quenching waste heat and salt water separation is realized to salt water heating in salt water reservoir, so that thermal energy is made full use of, without providing additional energy
Source while energy saving, greatly reduces salt water separation costs.
2, the UTILIZATION OF VESIDUAL HEAT IN salt separator of the utility model, brine pipeline wraps up jet chimney arrangement, solidifying by steam
The salt water that the thermal energy of poly- release is intracavitary to salt water preheats, so that making full use of for thermal energy be furthermore achieved.
3, the whole vertical structure arrangement of the UTILIZATION OF VESIDUAL HEAT IN salt separator of the utility model, it is compact-sized, can directly it pacify
On quenching salt tank groove body, area occupied is few, and relatively existing cyclone separator arrangement is simpler.
Detailed description of the invention
Illustrate the utility model embodiment or technical solution in the prior art in order to clearer, it below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it is clear that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it can also be obtained according to these attached drawings other attached drawings.
Fig. 1 is the overall structure diagram of the UTILIZATION OF VESIDUAL HEAT IN salt separator of the utility model；
In figure: 1- salt water reservoir, 11- flank, 2- jet chimney, 21- steam accumulation chamber, 22- separation water outlet pipeline,
23- steam discharge pipe, 24- choke device, 241- support rod, 242- gas barrier plate, 25- condensed water gather chamber, 3- brine pipeline,
31- salt water cavity, 32- salt water inlet pipeline, 33- salt water outlet pipeline, 4- quenching salt tank, the thermally conductive heat exchanger tube of 5-；
Specific embodiment
Below in conjunction with the attached drawing in the utility model, to the technical scheme in the embodiment of the utility model carry out it is clear,
Complete description, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole implementation
Example.Based on the embodiments of the present invention, those skilled in the art is without making creative work
All other embodiment obtained, belongs to the protection scope of the utility model.
As shown in Figure 1, a kind of UTILIZATION OF VESIDUAL HEAT IN salt separator of the utility model embodiment, including salt water reservoir 1, steaming
Steam pipe road 2, brine pipeline 3, in which: salt water reservoir 1 is the closed box with top cover, and its underpart is immersed in quenching salt tank 4；It steams
Steam pipe road 2 is arranged vertically at the top of salt water reservoir 1；Jet chimney 2 it is top closed, bottom is connected to salt water reservoir 1,
The inner cavity of jet chimney 2 forms steam accumulation chamber 21；The bottom of steam accumulation chamber 21 is communicated with separation water outlet pipeline 22；Salt water
Pipeline 3 wraps up jet chimney 2 and arranges, forming salt water cavity 31 between brine pipeline 3 and jet chimney 2；The bottom of salt water cavity 31 connects
It is connected with salt water inlet pipeline 32, top is connected to by salt water outlet pipeline with salt water reservoir 1.
Specifically, as shown in Figure 1, salt water reservoir 1 is a closing groove body with top cover, for accommodating salt to be separated
Water；In addition, enclosed groove body is also for the collection for realizing the vapor generated after salt water separation；The shape of salt water reservoir 1,
Structure size and material, those skilled in the art can be determines according to actual conditions；It should be there are above salt water in salt water reservoir 1
Certain space, for gathering vapor；Oil-quenching tank is immersed in the lower part of salt water reservoir 1, thus using quenching waste heat to salt
Salt water in water reservoir 1 is heated, to realize that UTILIZATION OF VESIDUAL HEAT IN carries out salt water separation, energy saving, the vapor of generation
Gather on the top of salt water reservoir 1；Certainly, according to the actual needs, the lower part of salt water reservoir 1 can connect high salt concentration
Liquid discharge line, for the high concentration saline solution generated after salt water separation to be discharged.Jet chimney 2 runs through the top cover of salt water reservoir 1
It is connected to salt water reservoir 1, the vapor for being collected at 1 top of salt water reservoir is continually drained the steam accumulation chamber of jet chimney 2
21, and be constantly condensed into jet chimney 2 after water droplet flow to the lower section of jet chimney 2, not through separation water outlet pipeline 22
Disconnected discharge.Brine pipeline 3 wraps up jet chimney 2, so that the heat that vapor gathers release in steam accumulation chamber 21 can be to salt
Salt water in water cavity 31 is preheated, to further utilize thermal energy；Salt water in salt water cavity 31 is by salt water inlet pipeline 32
It is continuing to supply, various control valves can be set according to the actual situation on salt water inlet pipeline 32；The top of salt water cavity 31 connects
There is salt water outlet pipeline, to realize that the salt water in salt water cavity 31 after preheating is continuing to supply into salt water reservoir 1；In addition, salt water
Inlet pipeline 32 is located at the bottom of salt water cavity 31, and salt water outlet pipeline is located at the top of salt water cavity 31, to realize salt water cavity 31
Interior salt water flow to salt water reservoir 1 through salt water outlet pipeline in a manner of overflow, is increased in salt water cavity 31 to the maximum extent
The preheating time of salt water, heat energy utilization are more abundant.
The UTILIZATION OF VESIDUAL HEAT IN salt separator of the utility model, 1 lower part of salt water reservoir are immersed in quenching salt tank 4, can be led to
It crosses quenching waste heat and salt water separation is realized to salt water heating in salt water reservoir 1, so that thermal energy is made full use of, without providing additional energy
Source while energy saving, greatly reduces salt water separation costs；Brine pipeline 3 wraps up jet chimney 2 and arranges, passes through steam
The thermal energy of cohesion release preheats the salt water in salt water cavity 31, so that making full use of for thermal energy be furthermore achieved；In addition,
The whole vertical structure of UTILIZATION OF VESIDUAL HEAT IN salt separator is arranged, compact-sized, can be directly mounted on 4 groove body of quenching salt tank,
Area occupied is few, and relatively existing cyclone separator arrangement is simpler.
Further, as shown in Figure 1, being vertically arranged with steam discharge pipe 23 in steam accumulation chamber 21, steam accumulation chamber 21
It is connected to salt water reservoir 1 by steam discharge pipe 23.
Specifically, the length of steam discharge pipe 23 is unsuitable too long, the setting of steam discharge pipe 23 is mainly used for arranging in steam
It puts formation condensed water between pipe 23 and jet chimney 2 and gathers chamber 25, is i.e. Water vapor condensation gathers chamber 25 in condensed water at after water droplet
It is discharged after inside gathering through separation water outlet pipeline 22, partial condensation water is avoided to again flow into salt water reservoir 1；Certainly, this field
Technical staff can also design other structures and condensed water is avoided to blow back into salt water reservoir 1.
Further, the choke device 24 that the top of steam accumulation chamber 21 is disposed with for reducing steam flow rate, for blocking
Intercept water steam, accelerates vapor condensation rate.
Specifically, as shown in Figure 1, choke device 24 includes support rod 241 and several gas barrier plates 242, in which: support rod
241 arrange vertically along the central axis of steam accumulation chamber 21；Several gas barrier plates 242 are successively spaced stacking and are fixed on support rod 241
On.Preferably, gas barrier plate 242 is umbrella gas barrier plate, and open end is towards the bottom of steam accumulation chamber 21, and several gas barrier plates
242 along support rod 241, circumferential size gradually becomes smaller from bottom to top, i.e., in the increase gas barrier plate 242 of height and jet chimney 2
The distance between wall becomes larger, and can constantly significantly alter airflow direction in this way, and air-flow is avoided only to become upwards simply
In perpendicular flow, to enhance interception/barriering effect of gas barrier plate 242.
Further, as shown in Figure 1, the top of salt water reservoir 1 has outwardly extending flank 11, flank 11 is relied on
It on quenching salt tank groove body and is bolted, to realize UTILIZATION OF VESIDUAL HEAT IN salt separator consolidating above quenching salt tank 4
Dingan County's dress, and whole device is located at 4 top of quenching salt tank, saves space.
In some embodiments of the UTILIZATION OF VESIDUAL HEAT IN salt separator of the utility model, as shown in Figure 1, salt water reservoir 1
Bottom be disposed with vertically it is several connection salt water reservoirs 1 and quenching salt tank 4 thermally conductive heat exchanger tubes 5.
Specifically, thermally conductive heat exchanger tube 5 is disposed with more through 1 bottom surface of salt water reservoir vertically, thermally conductive 5 lower end of heat exchanger tube is excellent
Choosing extends to the bottom of quenching salt tank 4, but should ensure that, there are certain gap between 4 bottom surface of quenching salt tank, upper end extends
To 1/3 to 2/3 height of salt water reservoir 1, guarantee that salt water reservoir 1 can store part salt water and top has vapor
The space gathered.
Salt water in salt water cavity 31 after preheating instills salt water reservoir 1 through the continuous overflow of salt water outlet pipeline, with salt water
The raising of salt water horizontal plane in reservoir 1, when salt water level face, height reaches thermally conductive 5 upper end level height of heat exchanger tube, salt water
Salt water in reservoir 1 will be along the constantly diffusion downwards of thermally conductive heat exchanger tube 5；As salt water constantly expands downwards in thermally conductive heat exchanger tube 5
It dissipates, is wrapped up due to being quenched high temperature saline solution in salt bath 4 outside thermally conductive heat exchanger tube 5, to promote salt water in thermally conductive heat exchanger tube 5
Constantly separation, vapor are equally collected at 1 top of salt water reservoir and are continually drained the steam accumulation chamber 21 of jet chimney 2, and
The high concentration saline solution generated after thermally conductive 5 inner salt water of heat exchanger tube separation is then continuing to supply into quenching salt tank 4, i.e., thermally conductive heat exchanger tube 5
On the one hand setting realizes accelerates salt water separation, on the other hand realizes saline solution in quenching salt tank 4 and feeds.
The UTILIZATION OF VESIDUAL HEAT IN salt water cyclone separator arrangement of the utility model is simple, occupies little space, and on the one hand makes full use of quenching
Waste heat realizes salt water separation, on the other hand also achieves the continuous supply of saline solution in quenching salt tank 4, practical.
The utility model is further described by specific embodiment above, it should be understood that, have here
The description of body, should not be construed as the restriction to the spirit and scope of the utility model, and one of ordinary skilled in the art is readding
The various modifications made after reader specification to above-described embodiment belong to the range that the utility model is protected.
Claims (8)
1. a kind of UTILIZATION OF VESIDUAL HEAT IN salt separator, which is characterized in that including salt water reservoir, jet chimney, brine pipeline,
In:
The salt water reservoir is the closed box with top cover, and its underpart is immersed in quenching salt tank；
The jet chimney is arranged vertically at the top of the salt water reservoir；The jet chimney it is top closed, bottom with
The salt water reservoir connection, the inner cavity of the jet chimney form steam accumulation chamber；The bottom of the steam accumulation chamber is connected to
There is separation water outlet pipeline；
The brine pipeline wraps up the jet chimney arrangement, forms salt water between the brine pipeline and the jet chimney
Chamber；The bottom of the salt water cavity is communicated with salt water inlet pipeline, and top is connected by salt water outlet pipeline and the salt water reservoir
It is logical.
2. UTILIZATION OF VESIDUAL HEAT IN salt separator according to claim 1, which is characterized in that set vertically in the steam accumulation chamber
It is equipped with steam discharge pipe, the steam accumulation chamber is connected to the salt water reservoir by the steam discharge pipe.
3. UTILIZATION OF VESIDUAL HEAT IN salt separator according to claim 1, which is characterized in that the top cloth of the steam accumulation chamber
It is equipped with the choke device for reducing steam flow rate.
4. UTILIZATION OF VESIDUAL HEAT IN salt separator according to claim 3, which is characterized in that the choke device includes support rod
And several gas barrier plates, in which:
The support rod is arranged vertically along the central axis of the steam accumulation chamber；
Several gas barrier plates are successively spaced stacking and are fixed on the support rod.
5. UTILIZATION OF VESIDUAL HEAT IN salt separator according to claim 4, which is characterized in that the gas barrier plate is umbrella choke
Piece, open end is towards the bottom of the steam accumulation chamber.
6. UTILIZATION OF VESIDUAL HEAT IN salt separator according to claim 4, which is characterized in that several gas barrier plates are along the branch
Circumferential size gradually becomes smaller strut from bottom to top.
7. UTILIZATION OF VESIDUAL HEAT IN salt separator according to claim 1, which is characterized in that the bottom of the salt water reservoir is perpendicular
Directly it is disposed with the thermally conductive heat exchanger tube of several connection the salt water reservoirs and the quenching salt tank.
8. UTILIZATION OF VESIDUAL HEAT IN salt separator according to claim 1, which is characterized in that the top of the salt water reservoir has
There is outwardly extending flank, the flank is relied on quenching salt tank groove body and is bolted.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821292097.8U CN208626639U (en) | 2018-08-10 | 2018-08-10 | A kind of UTILIZATION OF VESIDUAL HEAT IN salt separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821292097.8U CN208626639U (en) | 2018-08-10 | 2018-08-10 | A kind of UTILIZATION OF VESIDUAL HEAT IN salt separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208626639U true CN208626639U (en) | 2019-03-22 |
Family
ID=65741423
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821292097.8U Active CN208626639U (en) | 2018-08-10 | 2018-08-10 | A kind of UTILIZATION OF VESIDUAL HEAT IN salt separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208626639U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108721925A (en) * | 2018-08-10 | 2018-11-02 | 亚捷科技（唐山）股份有限公司 | A kind of UTILIZATION OF VESIDUAL HEAT IN salt separator |
-
2018
- 2018-08-10 CN CN201821292097.8U patent/CN208626639U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108721925A (en) * | 2018-08-10 | 2018-11-02 | 亚捷科技（唐山）股份有限公司 | A kind of UTILIZATION OF VESIDUAL HEAT IN salt separator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206673403U (en) | A kind of industrial generation of electricity by new energy box-type substation | |
| CN103194265A (en) | Thermal cycle continuous comprehensive method employing pyrolysis gasification of coal gangue | |
| CN103205278A (en) | Thermal-cycle continuous pyrolysis-gasification comprehensive device for coal gangues | |
| CN105152253B (en) | A kind of solar energy sea water desalination apparatus | |
| CN208626639U (en) | A kind of UTILIZATION OF VESIDUAL HEAT IN salt separator | |
| CN203494188U (en) | Double-effect concentrator | |
| CN108721925A (en) | A kind of UTILIZATION OF VESIDUAL HEAT IN salt separator | |
| CN102876443B (en) | Unit for removing water from used mineral oil | |
| CN206553479U (en) | A kind of new raw gas purifying cooling device | |
| CN205909251U (en) | Highly -effective steam generator | |
| CN203229497U (en) | Thermal cycle continuous coal gangue pyrolysis gasification comprehensive device | |
| CN210268273U (en) | Steam-water preheating device | |
| CN204185459U (en) | For the Distallation systm of white liquor distilling | |
| CN103242908A (en) | Continuous thermal cycle coal gangue pyrolysis gasification humidifying and tail gas purifying device | |
| CN206488515U (en) | A kind of reheater for absorption heat pump | |
| CN207570372U (en) | A kind of environmental-protection energy-saving device | |
| CN206494918U (en) | A kind of animal oil molecular distillation deodorization tank | |
| CN203155037U (en) | Tail gas mist purifier for use after humidification and dehydration of charged coal gangue hot waste gas | |
| CN207238264U (en) | One kind condensation reheat-type wet static dedusting system | |
| CN202297191U (en) | Natural condensation type solar pure water production and water heating device | |
| CN206085447U (en) | Drip proof pinnacle steaming chamber | |
| CN206145652U (en) | Steam chest structure | |
| CN106753779A (en) | A kind of deodorant tank of animal oil molecular distillation | |
| CN208365504U (en) | Fuel vapor normal-pressure boiler | |
| CN205843134U (en) | A kind of vaporizer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |