CN205759826U - A kind of spray-type separator - Google Patents
A kind of spray-type separator Download PDFInfo
- Publication number
- CN205759826U CN205759826U CN201620498299.2U CN201620498299U CN205759826U CN 205759826 U CN205759826 U CN 205759826U CN 201620498299 U CN201620498299 U CN 201620498299U CN 205759826 U CN205759826 U CN 205759826U
- Authority
- CN
- China
- Prior art keywords
- separation chamber
- head
- chamber
- matter transfer
- spray
- 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
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model discloses a kind of spray-type separator, comprising: separation chamber and crystallisation chamber, the bottom of separation chamber is provided with the first conical head, the bottom of the first conical head is connected on the ellipse head at crystallisation chamber top, the bottom of crystallisation chamber is provided with the second conical head, the bottom of the second conical head is connected on crystallize lower limb cylinder, separation chamber is provided with Matter Transfer import, Matter Transfer import is arranged on the top half of separation chamber and the ellipse head near top, separation chamber, Matter Transfer import connects bumped head, bumped head is arranged on inside described separation chamber, first conical head is provided with charging aperture；Crystallisation chamber is provided with Matter Transfer outlet, and Matter Transfer outlet and Matter Transfer import are in the same side；The bottom of crystallize lower limb cylinder is provided with discharging opening.Import is arranged on the top of device, it is possible to effectively reduce the height that separator is overall, save the space of device, provide further relative savings the cost of device.
Description
Technical field
This utility model relates to evaporation crystallization equipment field, is specifically related to a kind of spray-type separator.
Background technology
Oslo type crystallizer is also called grading type crystallizer, it be mainly characterized in that degree of supersaturation produces
Region and crystal growth district be separately positioned at the two of crystallizer, crystal fluidize in circulating mother liquor stream and hangs
Floating, provide a good condition for crystal growth.The operation principle of Oslo vacuum cooling crystallizer: knot
Brilliant device is made up of with crystallisation chamber two parts vaporizer, and the device body of crystallisation chamber often has certain tapering, and top is relatively
Bigger sectional area is arranged at bottom.Mother solution feed liquid dense with heat delivers to high-order vaporizer with circulating pump after mixing,
Solution boils, cooling in vaporizer and produce degree of supersaturation, then by central downtake flow to crystallization
The bottom of room, then flow up.Crystal suspension becomes the fluid bed of grading, grain in this liquid stream
Spending bigger crystal and be enriched in bottom, the solution maximum with the degree of supersaturation flowed out in downspout contacts,
To look bigger.In crystallisation chamber, liquid flow velocity upwards is gradually lowered, wherein the granularity of suspended crystal
The least, supersaturated solution, when being upward through crystal suspension bed, progressively releases its degree of supersaturation.
When solution arrives the top layer of crystallisation chamber, the most no longer containing crystal grain, the mother solution as clarification is crystallizing
The top overflow of room enters circulation line.Feed pipe is positioned on the suction line of circulating pump, and mother solution is in circulation
In pipeline, feed liquid dense with heat mixes the most again, subsequently into producing oversaturated region---vaporizer.
The crystallizer of this mode of operation belongs to mother liquid circulation, and its advantage is in circulation fluid substantially
Without crystal grain, thus avoid impeller and intercrystalline Crystallisation phenomenon, add the grain of crystallisation chamber
Degree grading, the crystal making this crystallizer produce is big and uniform.Such crystallizer has two kinds
Design, open type and closed type, their difference is that the crystallisation chamber of open type is come round with air, vaporization
Room is positioned at the top of crystallisation chamber, has enough height；The vaporizer of closed type is then completely in crystallisation chamber
Under identical vacuum, device in same container, its aspect ratio open type low.
On the whole, in evaporated crystallization device, separator typically uses two separators being vertically connected with
Tube structure, the material inlet of existing frequently-used separator is arranged on the lower part of cylinder, in whole evaporation
When crystal system is installed, the height that equipment needs separator overall is higher, and the space that device takies is relatively big,
And needing to be equipped with the highest pipeline, installation cost is the most of a relatively high.
Summary of the invention
The purpose of this utility model is the problem above overcoming prior art to exist, it is provided that a kind of spray-type
Separator, separator of the present utility model is also with double-decker, on the basis of not affecting separation efficiency,
Effectively reduce the height of whole device, save the space of separator, provide further relative savings cost.
For realizing above-mentioned technical purpose, reaching above-mentioned technique effect, this utility model passes through techniques below side
Case realizes:
A kind of spray-type separator, comprising: separation chamber and be arranged on the crystallisation chamber of bottom, described separation chamber,
The bottom of described separation chamber is provided with the first conical head, and the bottom of described first conical head is connected to described
On the ellipse head at crystallisation chamber top, the bottom of described crystallisation chamber is provided with the second conical head, and described second
The bottom of conical head is connected on crystallize lower limb cylinder,
Described separation chamber is provided with Matter Transfer import, and described Matter Transfer import is arranged on described separation chamber
Top half and ellipse head near described separation chamber top, described Matter Transfer import connects punching
Press seal head, described bumped head is arranged on inside described separation chamber, by described bumped head at described point
Spraying material from chamber interior, described first conical head is provided with charging aperture；
Described crystallisation chamber is provided with Matter Transfer outlet, the outlet of described Matter Transfer and described Matter Transfer import
In the same side；
Described crystallize lower limb cylinder is provided with magma loop exit, and the bottom of described crystallize lower limb cylinder is provided with discharging
Mouthful.
In a preferred embodiment of the present utility model, farther including, the top of described separation chamber is ellipse
Circle end socket, is provided with indirect steam outlet at the top of described ellipse head.
In a preferred embodiment of the present utility model, farther include, also include wire mesh demister, institute
State wire mesh demister to be arranged between described separation chamber and described ellipse head.
In a preferred embodiment of the present utility model, farther include, described separation chamber and crystallisation chamber it
Between be provided with gas connection pipe, the through described separation chamber, one end of described gas connection pipe, described gas connect
The through described crystallisation chamber of the other end of pipe.
In a preferred embodiment of the present utility model, farther include, described separation chamber and crystallisation chamber it
Between be provided with interface of the level gauge, described interface of the level gauge is used for connecting liquidometer roof-mounted magnetic flap level gauge.
In a preferred embodiment of the present utility model, farther include, described separation chamber is additionally provided with people
Hole, described manhole enters in described separation chamber for maintainer.
In a preferred embodiment of the present utility model, farther include, by Er Shizhi bottom described manhole
Seat supports, hanging support is fixed on the barrel of described separation chamber.
The beneficial effects of the utility model are:
Separator in this utility model mainly includes separation chamber and crystallisation chamber, and the bottom of separation chamber is provided with
One conical head, the bottom of the first conical head is connected on the ellipse head at crystallisation chamber top, crystallisation chamber
Bottom be provided with the second conical head, the bottom of the second conical head is connected on crystallize lower limb cylinder, separate
Room is provided with Matter Transfer import, and Matter Transfer import is arranged on the top half of described separation chamber and close
The ellipse head at top, separation chamber, is arranged on the top of device by import, it is possible to effectively reduce separator whole
The height of body, saves the space of device, provide further relative savings the cost of device.
Described above is only the general introduction of technical solutions of the utility model, in order to better understand this practicality
Novel technological means, and can being practiced according to the content of description, below with of the present utility model relatively
Good embodiment and coordinate accompanying drawing describe in detail as after.Detailed description of the invention of the present utility model is by following enforcement
Example and accompanying drawing thereof are shown in detail in.
Accompanying drawing explanation
In order to be illustrated more clearly that the technical scheme in this utility model embodiment technology, below will be to enforcement
In the description of example technology, the required accompanying drawing used is briefly described, it should be apparent that, in describing below
Accompanying drawing is only embodiments more of the present utility model, for those of ordinary skill in the art, not
On the premise of paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model；
Wherein, 10-separation chamber, 20-crystallisation chamber, 30-crystallize lower limb cylinder, 100-the first conical head, 200-
Second conical head, 101-Matter Transfer import, 102-charging aperture, 103-indirect steam exports, 104-
Wire mesh demister, 105-bumped head, 106-manhole, 107-hanging support, 108-interface of the level gauge,
201-Matter Transfer exports, 202-gas connection pipe, 301-magma loop exit, 302-discharging opening.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, to the technology in this utility model embodiment
Scheme is clearly and completely described, it is clear that described embodiment is only this utility model one
Divide embodiment rather than whole embodiments.Based on the embodiment in this utility model, this area is common
The every other embodiment that technical staff is obtained under not making creative work premise, broadly falls into this
The scope of utility model protection.
Embodiment
With reference to shown in Fig. 1, present embodiment discloses a kind of spray-type separator, it mainly includes two parts:
Separation chamber 10 and crystallisation chamber 20, above-mentioned crystallisation chamber 20 is arranged on bottom, above-mentioned separation chamber 10, above-mentioned separation
The top of room 10 and crystallisation chamber 20 is ellipse head, and the bottom of above-mentioned separation chamber 10 is provided with the first taper
End socket 100, the bottom of above-mentioned first conical head 100 is connected to the oval envelope at above-mentioned crystallisation chamber top 20
On head, the bottom of above-mentioned crystallisation chamber 20 is provided with the second conical head 200, above-mentioned second conical head 200
Bottom be connected on crystallize lower limb cylinder 30, the cross-sectional area and above-mentioned second of above-mentioned crystallize lower limb cylinder 30
Conical head 200 smallest cross-section area is consistent.
Being provided with Matter Transfer import 101 in above-mentioned separation chamber 10, above-mentioned Matter Transfer import 101 is arranged
Top half in above-mentioned separation chamber 10 and the ellipse head near top, above-mentioned separation chamber 10, and,
Above-mentioned Matter Transfer import 101 connects has bumped head 105, above-mentioned bumped head 105 to be arranged on above-mentioned point
Internal, by above-mentioned bumped head 105 at above-mentioned separation chamber 10 internal spray material from room 10.
In the present embodiment, the charging aperture 102 of separator is arranged on above-mentioned first conical head 100.
Above-mentioned crystallisation chamber 20 is provided with Matter Transfer outlet 201, above-mentioned Matter Transfer outlet 201 and above-mentioned thing
Material circulation import 101 is in the same side, and above-mentioned Matter Transfer import 101 exports 201 with above-mentioned Matter Transfer
Complete Matter Transfer.
In the present embodiment, being provided with magma loop exit 301 on above-mentioned crystallize lower limb cylinder 30, above-mentioned magma follows
Ring outlet 301 is arranged on the side of above-mentioned crystallize lower limb cylinder 30, and, at above-mentioned crystallize lower limb cylinder 30
Bottom be provided with discharging opening 302.
Import is arranged on the top of device, it is possible to effectively reduce the height that separator is overall, save dress
The space put, provide further relative savings the cost of device.
The top of above-mentioned separation chamber 10 is ellipse head, and in evaporation and crystal process, steam is in whole system
Middle circulation, therefore, is provided with indirect steam outlet 103, by above-mentioned secondary at the top of above-mentioned ellipse head
The indirect steam produced in separator is discharged by steam (vapor) outlet 103.
In the separator, material has foam and produces, and for more preferable scumming, is also provided with silk screen and removes
Foam device 104, above-mentioned wire mesh demister 104 is arranged between above-mentioned separation chamber 10 and above-mentioned ellipse head.
In order to ensure the connectivity between above-mentioned separation chamber 10 and crystallisation chamber 20, above-mentioned separation chamber 10 with
Gas connection pipe 202 it is provided with, through above-mentioned point of one end of above-mentioned gas connecting tube 202 between crystallisation chamber 20
From room 10, the through above-mentioned crystallisation chamber 20 of the other end of above-mentioned gas connecting tube 202.
Meanwhile, interface of the level gauge 108, above-mentioned liquidometer it are provided with between above-mentioned separation chamber 10 and crystallisation chamber 20
Interface 108 is used for connecting liquidometer, and above-mentioned interface of the level gauge 108 is provided with some connected entrances, Qi Zhongyi
Individual connected entrance connects above-mentioned separation chamber 10, and a connected entrance connects above-mentioned crystallisation chamber 20, in addition it is also necessary to a company
Port connects liquidometer.
Being additionally provided with manhole 106 in above-mentioned separation chamber 10, above-mentioned manhole 106 enters above-mentioned point for maintainer
In room 10, above-mentioned people, supported by hanging support 107 bottom 106, hanging support 107 is fixed on above-mentioned
On the barrel of separation chamber 10.
Separator in the present embodiment mainly includes separation chamber and crystallisation chamber, and the bottom of separation chamber is provided with first
Conical head, the bottom of the first conical head is connected on the ellipse head at crystallisation chamber top, crystallisation chamber
Bottom is provided with the second conical head, and the bottom of the second conical head is connected on crystallize lower limb cylinder, separation chamber
Being provided with Matter Transfer import, Matter Transfer import is arranged on the top half of above-mentioned separation chamber and near dividing
From the ellipse head in ceiling portion, import is arranged on the top of device, it is possible to effectively reduce separator overall
Height, save the space of device, provide further relative savings the cost of device.
Described above to the disclosed embodiments, makes professional and technical personnel in the field be capable of or uses
This utility model.Multiple amendment to these embodiments will be aobvious for those skilled in the art
And be clear to, generic principles defined herein can be without departing from spirit or scope of the present utility model
In the case of, realize in other embodiments.Therefore, this utility model is not intended to be limited to institute herein
These embodiments shown, and it is to fit to consistent with principles disclosed herein and features of novelty the widest
Scope.
Claims (7)
1. a spray-type separator, comprising: separation chamber and the crystallization being arranged on bottom, described separation chamber
Room, the bottom of described separation chamber is provided with the first conical head, and the bottom of described first conical head is connected to
On the ellipse head at described crystallisation chamber top, the bottom of described crystallisation chamber is provided with the second conical head, described
The bottom of the second conical head is connected on crystallize lower limb cylinder, it is characterised in that
Described separation chamber is provided with Matter Transfer import, and described Matter Transfer import is arranged on described separation chamber
Top half and the ellipse head near top, described separation chamber, described Matter Transfer import connects punching press
End socket, described bumped head is arranged on inside described separation chamber, by described bumped head in described separation
Chamber interior sprays material, and described first conical head is provided with charging aperture；
Described crystallisation chamber is provided with Matter Transfer outlet, the outlet of described Matter Transfer and described Matter Transfer import
In the same side；
Described crystallize lower limb cylinder is provided with magma loop exit, and the bottom of described crystallize lower limb cylinder is provided with discharging
Mouthful.
Spray-type separator the most according to claim 1, it is characterised in that the top of described separation chamber
For ellipse head, it is provided with indirect steam outlet at the top of described ellipse head.
Spray-type separator the most according to claim 2, it is characterised in that also include wire mesh demister,
Described wire mesh demister is arranged between described separation chamber and described ellipse head.
Spray-type separator the most according to claim 1, it is characterised in that described separation chamber and crystallization
Gas connection pipe it is provided with between room, the through described separation chamber, one end of described gas connection pipe, described gas
The through described crystallisation chamber of the other end of connecting tube.
Spray-type separator the most according to claim 1, it is characterised in that described separation chamber and crystallization
Being provided with interface of the level gauge between room, described interface of the level gauge is used for connecting liquidometer.
Spray-type separator the most according to claim 1, it is characterised in that also set in described separation chamber
Having manhole, described manhole enters in described separation chamber for maintainer.
Spray-type separator the most according to claim 6, it is characterised in that by ear bottom described manhole
Formula seat supports, hanging support is fixed on the barrel of described separation chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620498299.2U CN205759826U (en) | 2016-05-27 | 2016-05-27 | A kind of spray-type separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620498299.2U CN205759826U (en) | 2016-05-27 | 2016-05-27 | A kind of spray-type separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205759826U true CN205759826U (en) | 2016-12-07 |
Family
ID=57408370
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620498299.2U Active CN205759826U (en) | 2016-05-27 | 2016-05-27 | A kind of spray-type separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205759826U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105817050A (en) * | 2016-05-27 | 2016-08-03 | 苏州乔发环保科技股份有限公司 | Spraying type separator |
-
2016
- 2016-05-27 CN CN201620498299.2U patent/CN205759826U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105817050A (en) * | 2016-05-27 | 2016-08-03 | 苏州乔发环保科技股份有限公司 | Spraying type separator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103071310B (en) | Evaporating crystallizer | |
| CN207270810U (en) | A kind of raw lacquer filter plant | |
| CN209138036U (en) | A kind of device for effectively separating | |
| CN104880118B (en) | A kind of cooling tower water distribution system, cooling tower and cooling tower decreasing water distribution method | |
| CN205759826U (en) | A kind of spray-type separator | |
| CN205115411U (en) | Natural gas second grade vapour and liquid separator | |
| CN206285519U (en) | A kind of rectifying tower with bulkhead with moveable bulkhead | |
| CN209261766U (en) | A kind of reciprocating compressor entrance gas-liquid separation device | |
| CN208667365U (en) | A kind of energy conservation solventing-out evaporated crystallization device | |
| CN208990284U (en) | A kind of material directly contacts cooling crystallizer with refrigerant | |
| CN105865247B (en) | A kind of disc type uniform fluid distribution device | |
| CN105817050A (en) | Spraying type separator | |
| CN207970486U (en) | A kind of crystallizer for MVR sewage disposal systems | |
| CN202410226U (en) | Continuous evaporation crystallization device | |
| CN205784020U (en) | Single process side's housing dry evaporator | |
| CN208031944U (en) | A kind of Despumation device and vapo(u)rization system | |
| CN107930175A (en) | A kind of crystallizer for MVR sewage disposal systems | |
| CN209214160U (en) | Drum type brake precooling evaporator | |
| CN208465593U (en) | A kind of packless new and effective mass transfer desulfurizing tower | |
| CN208293066U (en) | A kind of device improving hot-dip galvanized steel pipe coating uniformity | |
| CN206950960U (en) | A kind of tail gas absorbing system | |
| CN105087095A (en) | Gas-liquid separator for natural gas | |
| CN204939421U (en) | Gas-liquid separation flow-guiding structure | |
| CN110975318A (en) | Epichlorohydrin receiving device | |
| CN206709452U (en) | A kind of air-conditioning refrigerating liquid-dividing head |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |