CN206355612U - One kind injection flash distillation circulation enrichment facility - Google Patents
One kind injection flash distillation circulation enrichment facility Download PDFInfo
- Publication number
- CN206355612U CN206355612U CN201621380038.7U CN201621380038U CN206355612U CN 206355612 U CN206355612 U CN 206355612U CN 201621380038 U CN201621380038 U CN 201621380038U CN 206355612 U CN206355612 U CN 206355612U
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- CN
- China
- Prior art keywords
- tank body
- flash distillation
- vacuum pump
- enrichment facility
- pump system
- 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 - Fee Related
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- Fertilizers (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A kind of injection flash distillation circulation enrichment facility disclosed in the utility model, including a tank body, the upper end capping of tank body offer a steam (vapor) outlet, and its lower end back cover offers a sewage draining exit；One is vertically arranged in the serpentine heating pipe in the middle part of tank body；At least two recycling ejector of the circumferentially-spaced outside for being arranged in tank body；One liquid distributor, liquid distributor includes feed tube and cloth liquid disk, and cloth liquid disk is arranged in tank body and positioned at the top of serpentine heating pipe, and the outlet end of feed tube is connected after passing through the upper end capping of tank body with the inlet of cloth liquid disk；One is arranged on the equal vapour device in the capping of the upper end of tank body；One vacuum pump system, the entrance point of vacuum pump system is connected by steam fairlead with equal vapour device；One cooler, the cooling import of cooler is connected with the port of export of vacuum pump system.Injection flash distillation of the present utility model circulates enrichment facility than being concentrated in vacuo quickly by film heating merely, and concentration speed is high, and device volume is small, low cost, it is adaptable to which water soluble organic fertilizer concentrates working process.
Description
Technical field
The utility model is related to evaporation concentration equipment technical field, more particularly to a kind of injection flash distillation circulation enrichment facility.
Background technology
Production water soluble organic fertilizer needs to be concentrated by evaporation into after finite concentration, and water-soluble liquid fertilizer or spray-dried system is made
Into the solid fertilizer of water solubility, unit is such as concentrated by evaporation using traditional film vacuum and carries out concentration processing, exist charging less, efficiency it is low,
Equipment volume is big, complex operation, high cost problem.Therefore, applicant carried out beneficial exploration and trial, have found solution
The method of above mentioned problem, technical scheme described below is produced under this background.
Utility model content
The purpose of this utility model is：One kind is provided suitable for water soluble organic fertilizer concentrates working process, charging is big, imitate
The injection flash distillation circulation enrichment facility that rate is high, equipment volume is small, simple to operate, equipment manufacturing cost is low.
The technical problem that the utility model is solved can be realized using following technical scheme：
One kind injection flash distillation circulation enrichment facility, including：
One tank body, the upper end capping of the tank body offers a steam (vapor) outlet, and its lower end back cover offers a sewage draining exit；
One is vertically arranged in the serpentine heating pipe in the middle part of the tank body；
At least two recycling ejector of the circumferentially-spaced outside for being arranged in the tank body, each recycling ejector includes
One injector head, a circulating pump and first, second connecting tube, the injector head are arranged on the side wall of the tank body and its nozzle
Through the tank body side wall and stretch into the tank body, the nozzle of these injector heads is circumferentially-spaced to be arranged in the snakelike heating
Around pipe, the discharging opening of the circulating pump is connected by first connecting tube with the injector head, its charging aperture with it is described
One end connection of second connecting tube, the other end of second connecting tube passes through the side wall of the tank body and stretches into the tank body
Bottom；
One liquid distributor, the liquid distributor include feed tube and cloth liquid disk, the cloth liquid disk be arranged on the tank body in and
Positioned at the top of the serpentine heating pipe, the outlet end of the feed tube through after the upper end capping of the tank body with the cloth liquid
The inlet connection of disk；
One is arranged on the equal vapour device in the capping of the upper end of the tank body, steam inlet and the tank body of the equal vapour device
Steam (vapor) outlet is connected；
One vacuum pump system, the entrance point of the vacuum pump system is gone out by the steam of steam fairlead and the equal vapour device
Mouth connection；
One cooler, the cooling import of the cooler is connected with the port of export of vacuum pump system, its coolant outlet with it is dense
Contracting liquid collecting device is connected；And
One blowoff valve pipe, the blowdown import of the blowoff valve pipe is connected with the sewage draining exit of the tank body, the blowoff valve pipe
On one first stop valve is installed.
In a preferred embodiment of the present utility model, divide in first, second connecting tube of each recycling ejector
Second, third stop valve is not installed.
In a preferred embodiment of the present utility model, the portion outside the tank body is located in the feed tube of the liquid distributor
One the 4th stop valve is installed on point.
In a preferred embodiment of the present utility model, the vacuum pump system is water-ring vacuum pump system.
In a preferred embodiment of the present utility model, the cooler is water-cooled cooler.
In a preferred embodiment of the present utility model, circumferential uniform intervals on the bottom surface of the lower end back cover of the tank body
It is provided with some supporting legs for being used to support the tank body.
As a result of technical scheme as above, the beneficial effects of the utility model are：Injection of the present utility model is dodged
Steam circulation enrichment facility to inject liquid on serpentine heating pipe under the impetus of circulating pump, moment flashes to steam, then
Water vapour is quickly guided to cooler by the negative pressure produced by vacuum pump system, and water vapour is cooled into concentrate through cooler.This
The injection flash distillation circulation enrichment facility of utility model is quicker than leaning on film heating to be concentrated in vacuo merely, and concentration speed is high, apparatus body
Small, the low cost of product, it is adaptable to which water soluble organic fertilizer concentrates working process.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
Or the accompanying drawing used required in description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, is not paying the premise of creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model.
Embodiment
In order that technological means, creation characteristic, reached purpose and effect that the utility model is realized are easy to understand, under
Face combines and is specifically illustrating, and the utility model is expanded on further.
Referring to Fig. 1, what is provided in figure is that a kind of injection flash distillation circulates enrichment facility, including tank body 100, serpentine heating pipe
200th, three recycling ejector 300, liquid distributor 400, equal vapour device 500, vacuum pump system 600, cooler 700 and blowoff valve pipe
800。
The upper end capping of tank body 100 offers a steam (vapor) outlet 110, and its lower end back cover offers a sewage draining exit 120, tank body
Circumferential uniform intervals are provided with some supporting legs 130 on the bottom surface of 100 lower end back cover, and tank body 100 is supported by some supporting legs 130
On the ground.
Serpentine heating pipe 200 is vertically arranged in the middle part of tank body 100, and it is interior by heating medium, so as to produce a large amount of
Heat.
The circumferentially-spaced outside for being arranged in tank body 100 of three recycling ejector 300, certainly, the number of recycling ejector 300
Amount is not limited to the quantity in the present embodiment, and it can be designed at least two according to design requirement.Each recycling ejector
300 include an injector head 310, a circulating pump 320 and connecting tube 330,340, and injector head 310 is arranged on the side wall of tank body 100
Upper and its nozzle 311 passes through the side wall of tank body 100 and stretched into tank body 100, and the nozzle 311 of these injector heads 310 is circumferentially-spaced
It is arranged in around serpentine heating pipe 200, the discharging opening 321 of circulating pump 320 is connected by connecting tube 330 with injector head 310, its
Charging aperture 322 is connected with one end of connecting tube 340, and the other end of the second 340 pipes of connection passes through the side wall of tank body 100 and stretches into tank
Stop valve 331,341 is separately installed with the bottom of body 100, connecting tube 330,340.
Liquid distributor 400 includes feed tube 410 and cloth liquid disk 420, and cloth liquid disk 420 is arranged in tank body 100 and positioned at snake
The surface of shape heating tube 200, the outlet end of feed tube 410 is through the feed liquor after the upper end capping of tank body 100 with cloth liquid disk 420
Mouth connection.A stop valve 411 is installed on the part that the feed tube 410 of liquid distributor 400 is located at outside tank body 100, to control feed liquor
The opening and closing of pipe 410 and cloth flow quantity.
Equal vapour device 500 is arranged in the capping of the upper end of tank body 100, steam inlet 510 and the tank body 100 of equal vapour device 500
Steam (vapor) outlet 110 is connected.
The entrance point 610 of vacuum pump system 600 is connected by the steam (vapor) outlet 520 of steam fairlead 900 and equal vapour device 500
Connect, in the present embodiment, vacuum pump system 600 is water-ring vacuum pump system.
The cooling import 710 of cooler 700 is connected with the port of export 620 of vacuum pump system 600, its coolant outlet 720 with
Concentrate collecting device is connected, in the present embodiment, and cooler 700 is water-cooled cooler.
The blowdown import 810 of blowoff valve pipe 800 is connected with the sewage draining exit of the tank body, the waste of blowoff valve pipe 800
820 are connected with outside sewage collecting equipment, a stop valve 830 are provided with blowoff valve pipe 800, with control of sewage disposal valve pipe 800
Opening and closing and blowdown flow.
General principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry is it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply illustrate principle of the present utility model, on the premise of the utility model spirit and scope are not departed from, the utility model is also
Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed the utility model.The utility model
Claimed scope is by appended claims and its equivalent thereof.
Claims (6)
1. one kind injection flash distillation circulation enrichment facility, it is characterised in that including：
One tank body, the upper end capping of the tank body offers a steam (vapor) outlet, and its lower end back cover offers a sewage draining exit；
One is vertically arranged in the serpentine heating pipe in the middle part of the tank body；
At least two recycling ejector of the circumferentially-spaced outside for being arranged in the tank body, each recycling ejector includes a spray
Head, a circulating pump and first, second connecting tube are penetrated, the injector head is arranged on the side wall of the tank body and its nozzle is passed through
The side wall of the tank body is simultaneously stretched into the tank body, and the nozzle of these injector heads is circumferentially-spaced to be arranged in the serpentine heating pipe
Around, the discharging opening of the circulating pump is connected by first connecting tube with the injector head, its charging aperture and described second
One end connection of connecting tube, the other end of second connecting tube passes through the side wall of the tank body and stretches into the bottom of the tank body
Portion；
One liquid distributor, the liquid distributor includes feed tube and cloth liquid disk, and the cloth liquid disk is arranged in the tank body and is located at
The top of the serpentine heating pipe, the outlet end of the feed tube through after the upper end capping of the tank body with the cloth liquid disk
Inlet is connected；
One is arranged on the equal vapour device in the capping of the upper end of the tank body, the steam inlet of the equal vapour device and the steam of the tank body
Outlet；
One vacuum pump system, the entrance point of the vacuum pump system is connected by the steam (vapor) outlet of steam fairlead and the equal vapour device
Connect；
One cooler, the cooling import of the cooler is connected with the port of export of vacuum pump system, its coolant outlet and concentrate
Collecting device is connected；And
One blowoff valve pipe, the blowdown import of the blowoff valve pipe is connected with the sewage draining exit of the tank body, the blowoff valve Guan Shangan
Equipped with one first stop valve.
2. injection flash distillation circulation enrichment facility as claimed in claim 1, it is characterised in that the of each recycling ejector
First, it is separately installed with second, third stop valve in the second connecting tube.
3. injection flash distillation circulation enrichment facility as claimed in claim 1, it is characterised in that in the feed tube position of the liquid distributor
In being provided with one the 4th stop valve on the part outside the tank body.
4. injection flash distillation circulation enrichment facility as claimed in claim 1, it is characterised in that the vacuum pump system is liquid-ring type
Vacuum pump system.
5. injection flash distillation circulation enrichment facility as claimed in claim 1, it is characterised in that the cooler cools down for water-cooled
Device.
6. injection flash distillation circulation enrichment facility as claimed in claim 1, it is characterised in that the bottom of the lower end back cover of the tank body
Circumferential uniform intervals are provided with some supporting legs for being used to support the tank body on face.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621380038.7U CN206355612U (en) | 2016-12-15 | 2016-12-15 | One kind injection flash distillation circulation enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621380038.7U CN206355612U (en) | 2016-12-15 | 2016-12-15 | One kind injection flash distillation circulation enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206355612U true CN206355612U (en) | 2017-07-28 |
Family
ID=59374314
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621380038.7U Expired - Fee Related CN206355612U (en) | 2016-12-15 | 2016-12-15 | One kind injection flash distillation circulation enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206355612U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106512452A (en) * | 2016-12-15 | 2017-03-22 | 宁波宝硕美机械设备工程有限公司 | Ejection and flash evaporation circulated concentration device |
-
2016
- 2016-12-15 CN CN201621380038.7U patent/CN206355612U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106512452A (en) * | 2016-12-15 | 2017-03-22 | 宁波宝硕美机械设备工程有限公司 | Ejection and flash evaporation circulated concentration device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170825 Address after: Zhenning Zhenhai District Jiaochuan streets Road 315200 Zhejiang city of Ningbo province No. 123 Patentee after: NINGBO BAOLINONG ENVIRONMENT TECHNOLOGY Co.,Ltd. Address before: 315192 Zhejiang city of Ningbo province Yinzhou District South Road No. 1288 Patentee before: NINGBO BAOSHUOMEI MACHINERY EQUIPMENT ENGINEERING CO.,LTD. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170728 Termination date: 20211215 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |