CN206897149U - A kind of hypergravity takes off ammonium salt device - Google Patents
A kind of hypergravity takes off ammonium salt device Download PDFInfo
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- CN206897149U CN206897149U CN201720261797.XU CN201720261797U CN206897149U CN 206897149 U CN206897149 U CN 206897149U CN 201720261797 U CN201720261797 U CN 201720261797U CN 206897149 U CN206897149 U CN 206897149U
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Abstract
It the utility model is related to a kind of hypergravity and take off ammonium salt device, first hypergravity machine has been firstly introduced in stripping water treatment field, pre-treatment is carried out to sewage first with filter and membrane module, the alkali lye in alkali liquid tank and the sewage after filter, membrane module processing are carried out mixing and enters hypergravity machine by the fluid passage of the first hypergravity machine afterwards, pass through the hypergravity machine structure of uniqueness, removing of the alkali lye to Oil in Sewage Water class material and COD is realized, test indicate that the water stripping sewage after above-mentioned processing can be widely applied in de- ammonium salt processing；Afterwards, the utility model is also initiative must merge the sewage after above-mentioned processing effective removing that the release gas after being hydrogenated with adds alkali lye hydrogen sulfide and ammonium chloride in being realized under the second hypergravity machine acts on to release gas simultaneously, test indicate that, removal efficiency is up to 98%.
Description
Technical field
It the utility model is related to a kind of hypergravity and take off ammonium salt device, belong to technical field of chemistry.
Background technology
In the industrial production, it is a kind of very common pending tail gas to discharge gas, and its main source is that oil is through catalysis weight
Enter de- C towers after whole to be handled, the cooling gas after processing enters return tank separation and obtains C5 components and release gas.Releasing
In deflation, containing substantial amounts of ammonium chloride and hydrogen sulfide, these are all the important components for needing to be handled.
In the prior art, absorbent is made for the processing generally use water of ammonium salt in release gas, after ammonium chloride is dissolved in water
Ammonia and hydrogen chloride are resolved into, and these materials are serious to equipment corrosion, stainless steel corroded more serious.In addition, for
The processing of hydrogen sulfide in gas is discharged, then does nertralizer, sodium hydroxide and hydrogen sulfide reaction life usually using dilute NaOH solution
Into vulcanized sodium and water.
It is not thorough enough that the above method handles N removal in obtained release gas, poor effect.
So, there is provided suitably de- ammonium salt technique, is current urgent problem to be solved.
Utility model content
The utility model provides a kind of hypergravity and takes off ammonium salt device, it is intended to is realized using hypergravity to ammonium salt in release gas
Removing processing.
In order to solve the above technical problems, the utility model is achieved through the following technical solutions：
A kind of hypergravity takes off ammonium salt device, it is characterised in that
Reactor is provided with, the reactor is provided with release gas import and releases bleeder holes；
It is additionally provided with the alkali storage tank for storing alkali lye, and the first hypergravity machine；
First hypergravity machine has shell, and insertion shell is provided with power-actuated hollow on the axis of shell
Rotating shaft, sealable fluid inlet is provided with the rotating shaft, there is fluid passage in rotating shaft；It is and described outside rotating shaft
Rotating shaft is coaxially arranged and is connected with sleeve, so as to the shaping gas passage between the rotating shaft and the sleeve lining, on sleeve
It is provided with multiple stomatas and gas vent；The rotating shaft is extended towards the sleeve multiple rotating channels, logical in rotation
Raised or recessed helical duct is provided with road；The rotating channel penetrates the sleeve and set；
Coaxially it is arranged with the rotating shaft, sleeve and is connected with filling tube, in the filling tube internal shaping packing area；The rotation
Passage, the stomata connect with the packing area；
Gas feed, gas vent and fluid issuing are provided with shell, the gas feed, fluid issuing is equal and fills out
Expect area's connection；Release the gas feed connection of bleeder holes and the first hypergravity machine；
The lye export of alkali storage tank connects with the fluid inlet of the first hypergravity machine；
The holding vessel for storing water stripping sewage is additionally provided with, filtering is connected with the outlet of sewer of holding vessel
Device；
Membrane module is connected with the outlet of sewer of filter, the membrane module is made up of multi-level tubular membrane module, more
Level tubular membrane component has concentrated water outlet and treated water outlet；
It is additionally provided with the alkali liquid tank for storing demulsifier, and the second hypergravity machine；
Second hypergravity machine has shell, and insertion shell is provided with power-actuated hollow on the axis of shell
Rotating shaft, there is fluid passage in rotating shaft, sealable fluid inlet is provided with the rotating shaft；The fluid inlet simultaneously with
Concentrated water outlet, the lye export connection of alkali liquid tank；
Coaxially be arranged with the rotating shaft outside rotating shaft and be connected with sleeve, so as to the rotating shaft and the sleeve lining it
Between formed channel, the rotating shaft towards the sleeve be extended have multiple rotating channels, projection is provided with rotating channel
Or recessed helical duct；The rotating channel penetrates the sleeve and set；
Coaxially it is arranged with the rotating shaft, sleeve and is connected with filling tube, in the filling tube internal shaping packing area；The rotation
Passage connects with packing area；
Fluid issuing is provided with shell, the fluid issuing connects with packing area；
The fluid inlet connection of the fluid issuing and the first hypergravity machine of second hypergravity machine；
The fluid issuing of first hypergravity machine connects with the holding vessel of storage water stripping sewage.
The filter includes grade one filter and secondary filter, and the pore size filter of the grade one filter is less than
50um, the pore size filter of secondary filter are less than 5um.
The inlet diameter sum of multiple rotating channels is equal to or less than the internal diameter of hollow axle.
The packing area is provided with multiple filling layers；The rotating shaft and motor connection.
The lye export of alkali storage tank is connected with the fluid inlet of the first hypergravity machine by kinetic pump；Concentrated water export and
The fluid inlet of second hypergravity machine is connected by kinetic pump.
The rotating channel is each perpendicular to the rotating shaft and set.
The membrane module is PC6040 rolled films.
It is additionally provided with UF membrane cleaning device and cleaning and anti-cleaning is carried out to membrane module.
Above-mentioned technical proposal of the present utility model has advantages below compared with prior art：
1st, hypergravity described in the utility model takes off ammonium salt device, has been firstly introduced first in stripping water treatment field overweight
Power machine, pre-treatment is carried out to sewage first with filter and membrane module, afterwards by the alkali lye in alkali liquid tank and by filter, film
Sewage after component processing carries out mixing and enters hypergravity machine by the fluid passage of the first hypergravity machine, passes through the overweight of uniqueness
Power machine structure, and the rotating channel with helical duct connected with packing area shaped between hollow axle and sleeve, it is real
Having showed fluid, rotated passage realizes spinning into for fluid again after hollow axle, and is engraved in rotation in enter packing area one
Under the spin active force of active force, shearing force and fluid, circumferential speed increase, caused centrifugal force pushes fluid to outer rim,
The filler in the filled area of fluid cuts, is broken, scattered in this process, so as to form the liquid film of micron to nano grade, liquid
Drop and brin, boundary that is huge, quickly updating is produced, produce flowing contact in the filler in numerous bending ducts, realize
Sewage and alkali lye are sufficiently mixed in fluid, improve the sufficient degree of liquid liquid contact, it is achieved thereby that alkali lye is to Oil in Sewage Water class
The removing of material and COD, test indicate that the water stripping sewage after above-mentioned processing can be widely applied in de- ammonium salt processing；
The utility model is initiative to be hydrogenated with by the sewage after above-mentioned processing in the presence of mixed alkali liquor to reacted device
Release gas afterwards carries out hypergravity hybrid switching processing, and the concentrated water and release gas after processing are engraved in rotation in enter packing area one
Transfer to firmly, under the spin active force of shearing force and fluid, circumferential speed increase, caused centrifugal force pushes fluid to outer
Edge, the filler cutting in the filled area of fluid, broken, scattered in this process, so as to formed the liquid film of micron to nano grade,
Drop and brin, boundary that is huge, quickly updating is produced, flowing contact is produced in the filler in numerous bending ducts so that
Mass transport process and chemical reaction occur for gas-liquid, improve the sufficient degree of gas-liquid contact, realize to hydrogen sulfide and chlorination in release gas
Effective removing of ammonium, test indicate that, removal efficiency is up to 98%.
2nd, hypergravity described in the utility model takes off ammonium salt device, is further also provided with entering for multiple rotating channels
Mouth diameter sum is equal to or less than the internal diameter of hollow axle, so as to ensure the internal diameter of rotating channel in suitable section, protects
The roll rate and spin states of fluid are demonstrate,proved, so as to further improve in packing area in fluid fully connecing for two kinds of mixing liquids
Touch.
Brief description of the drawings
In order that content of the present utility model is more likely to be clearly understood, below according to specific implementation of the present utility model
Example and with reference to accompanying drawing, is described in further detail to the utility model, wherein
Fig. 1 is the structural representation that hypergravity described in the utility model takes off ammonium salt device；
Reference is expressed as in figure：1- reactors, 2- alkali storage tanks, the hypergravity machines of 3- first, 4- shells, 5- turn
Axle, 6- fluid passages, 7- fluid inlets, 8- fluid issuings, 9- gas feeds, 10- gas vents, 11- sleeves, 12- rotations are logical
Road, 13- filling tubes, 14- packing areas, 15- release bleeder holes, 16- holding vessels, 17- grade one filters, 18- secondary filters,
19- membrane modules, the outlet of 20- concentrated waters, 21- treated water outlets, 22- alkali liquid tanks, the hypergravity machines of 23- second.
Embodiment
Embodiment 1
Hypergravity described in the utility model takes off ammonium salt device, and it is provided with reactor 1, and the reactor 1, which is provided with, to be released
Deflation import and release bleeder holes 15；
It is additionally provided with the alkali storage tank 162 for storing alkali lye, and the first hypergravity machine 3；
First hypergravity machine 3 has shell 4, and insertion shell 4 is provided with power-actuated on the axis of shell 4
Hollow axle 5, sealable fluid inlet 7 is provided with the rotating shaft 5, there is fluid passage 6 in rotating shaft 5；Outside rotating shaft 5
Portion, sleeve 11 is connected with coaxial be arranged of the rotating shaft 5, so as to shape gas between the rotating shaft 5 and the inwall of the sleeve 11
Body passage, multiple stomatas and gas vent 10 are provided with sleeve 11；The rotating shaft 5 is extended towards the sleeve 11 to be had
Multiple rotating channels 12, are provided with raised or recessed helical duct in rotating channel 12；The rotating channel 12 penetrates
The sleeve 11 is set；
Filling tube 13 is connected with the rotating shaft 5, coaxial be arranged of sleeve 11, in the internal shaping packing area of filling tube 13
14；The rotating channel 12, the stomata connect with the packing area 14；
Gas feed 9, gas vent 10 and fluid issuing 8, the gas feed 9, fluid issuing are provided with shell 4
8 connect with packing area 14；The gas feed 9 for releasing the hypergravity machine 3 of bleeder holes 15 and first connects；
The fluid inlet 7 of the lye export of alkali storage tank 162 and the first hypergravity machine 3 connects；
The holding vessel 16 for storing water stripping sewage is additionally provided with, was connected with the outlet of sewer of holding vessel 16
Filter；
Membrane module 19 is connected with the outlet of sewer of filter, and the membrane module 19 is by 19 groups of multi-level tubular membrane module
Into multi-level tubular membrane module 19 has concentrated water outlet 20 and treated water outlet 21；Wherein for the selection of membrane module 19, preferably set
It is set to and is made up of multi-level tubular membrane module 19, multi-level tubular membrane module 19 has concentrated water outlet 20 and treated water outlet 21；Wherein,
Treated water outlet 21 can be discharged directly to construction works of sewage purification plant and carry out further subsequent treatment.
It is additionally provided with the alkali liquid tank 22 for storing demulsifier, and the second hypergravity machine；Wherein select suitable alkali lye
Purpose be to exchange to carry out contact with water stripping sewage to need the impurity that removes so as to remove.
Second hypergravity machine has shell 4, and insertion shell 4 is provided with power-actuated on the axis of shell 4
Hollow axle 5, there is fluid passage 6 in rotating shaft 5, sealable fluid inlet 7 is provided with the rotating shaft 5；The fluid
Lye export of the import 7 simultaneously with concentrated water outlet 20, alkali liquid tank 22 is connected；
Sleeve 11 is connected with coaxial be arranged of the rotating shaft 5 in the outside of rotating shaft 5, so as in the rotating shaft 5 and the sleeve
Formed channel between 11 inwalls, the rotating shaft 5 is extended towards the sleeve 11 multiple rotating channels 12, in rotating channel
Raised or recessed helical duct is provided with 12；The rotating channel 12 penetrates the sleeve 11 and set；
Filling tube 13 is connected with the rotating shaft 5, coaxial be arranged of sleeve 11, in the internal shaping packing area of filling tube 13
14；The rotating channel 12 connects with packing area 14；Wherein, the setting for packing area 14 according to Practical Project, it is necessary to carry out
Selection, filler can with integral-filled, can also paved in multi-layers, so as to which packing area 14 is arranged into multiple filling layers area 14, it is therefore an objective to
In order to ensure when hypergravity machine works, realized using rotation under the multiple filling layers effect of packing area 14 to two kinds of liquid
Be fully rotatable cutting.
Fluid issuing 8 is provided with shell 4, the fluid issuing 8 connects with packing area 14；
The fluid inlet 7 of the hypergravity machine 3 of fluid issuing 8 and first of second hypergravity machine connects；
The fluid issuing 8 of first hypergravity machine 3 and the holding vessel 16 of storage water stripping sewage connect.
As preferred embodiment, on the basis of above-described embodiment setting, the filter is preferably provided with by one-level
Filter 17 and secondary filter 18 form, and the pore size filter of the grade one filter 17 is less than 50um, secondary filter 18
Pore size filter is less than 5um.
As preferred embodiment, the inlet diameter sum of preferably multiple rotating channels 12 is equal to or less than middle idle running
The internal diameter of axle 5.Certainly, set different, it is necessary to according to processed material, the difference for the treatment of effect requirement in the engineering construction of reality
Inlet diameter and hollow axle 5 size relationship.Also, set it is preferred that multiple rotating channels 12 are each perpendicular to the rotating shaft 5,
So as to be more favorable for the flowing of fluid.
It is further preferred that on the basis of above-described embodiment, the fluid of the lye export of alkali liquid tank 22 and the second hypergravity machine 23
Import 7 is connected by kinetic pump, more smooth to realize that alkali lye enters in the second hypergravity machine 23 through fluid inlet 7.Same mesh
, also to select to set concentrated water outlet 20 to connect by kinetic pump with the fluid inlet 7 of the second hypergravity machine 23.
Hypergravity sewage-treatment plant described in the utility model, Electric Desalting Wastewater or water stripping sewage are contour at work
After concentration sewage first passes around grade one filter, secondary filter filtering, then by the further purification membrane of multistage membrane module progress
Processing, exported through concentrated water and discharge concentrated water, the concentrated water after discharge enters the fluid inlet of the first hypergravity machine by kinetic pump；With
This simultaneously, alkali lye in alkali liquid tank also enters the fluid inlet of hypergravity machine through kinetic pump.Concentrated water and alkali lye enter through fluid inlet
After entering, into the fluid passage of hollow axle, and the entrance of rotating channel is flowed to, rotated feeder connection enters rotation again
Turn in passage, under the drainage of the raised or recessed helical duct inside rotating channel, form the rotating flow of fluid
It is dynamic, and enter in this role in the packing area connected with passage, and the spin work of fluid is formed at a moment for entering packing area
Firmly flowed to spin.Demulsifier and concentrated water are engraved in the spin of rotating force, shearing force and fluid in enter packing area one
Under active force, circumferential speed increase, caused centrifugal force pushes fluid to outer rim, in this process in the filled area of fluid
Filler cutting, broken, scattered, so as to form the liquid film of micron to nano grade, drop and brin, produce huge, quick renewal
Boundary, produce flowing contact in the fillers in numerous bending ducts so that mass transport process and chemistry occur for concentrated water and alkali lye
Reaction, being sufficiently mixed for sewage and demulsifier in fluid is realized, improves the sufficient degree of liquid liquid contact so that demulsifier and dense
Water-In-Oil molecule in water is fully contacted, and the Water-In-Oil molecule in concentrated water is fully demulsified, and improves the ability of water-oil separating, from
And removing of the demulsifier to Oil in Sewage Water class material and COD is realized, it must successfully realize demulsification and de-oiling.Afterwards, fluid passes through
Fluid issuing leaves the second hypergravity machine, and in the presence of mixed alkali liquor, the release gas after being hydrogenated with to reacted device carries out overweight
The processing of power hybrid switching, concentrated water after processing and release gas enter packing area one be engraved in rotating force, shearing force and
Under the spin active force of fluid, circumferential speed increase, caused centrifugal force pushes fluid to outer rim, in this process fluid
Filler in filled area cuts, is broken, scattered, so as to form the liquid film of micron to nano grade, drop and brin, produces huge
Greatly, the boundary quickly updated, it is numerous bending ducts fillers in produce flowing contact so that gas-liquid occur mass transport process and
Chemical reaction, the sufficient degree of gas-liquid contact is improved, realize effective removing to hydrogen sulfide and ammonium chloride in release gas.
Embodiment 2
Hypergravity described in the utility model takes off ammonium salt device at work, and step is as follows：
(1) filtering and impurity removing processing is carried out at 40 DEG C to Electric Desalting Wastewater, filters out the miscellaneous particle of machine that particle diameter is more than 50um；
(2) cooling treatment is carried out to the sewage after removal of impurities, is 40 DEG C to its temperature；
(3) 0.3MPa is boosted to sewage after cooling, it is 40 DEG C to set temperature, into membrane module, the membrane module
Membrane material be high hydrophilic superoleophobic property film, water pass through film, oily to be separated in influent side enrichment method, profit；
(4) concentrated water and demulsifier of the enriched oil after UF membrane and impurity are under rotation status, into hypergravity machine stream
Body import, and packing area is spun into after rotating channel, in packing area, concentrated water and demulsifier are under the influence of centrifugal force
Liquid liquid mixing is carried out, realizes water-oil separating；
(5) gas is discharged under hydrogen environment, and temperature is 45 DEG C, and Hydrogen Vapor Pressure under conditions of being 0.5MPa be catalyzed instead
Should；
(6) water after step (4) separation, alkali lye and the gas after step (5) processing enter in hypergravity machine, are filling out
Expect to carry out gas-liquid exchange in area；
(7) fluid after step (6) processing, which enters, carries out circular treatment in step (1).
Embodiment 3
Hypergravity described in the utility model takes off ammonium salt device at work, and step is as follows：
(1) filtering and impurity removing processing is carried out at 50 DEG C to water stripping sewage, filters out the miscellaneous particle of machine that particle diameter is more than 50um；
(2) cooling treatment is carried out to the sewage after removal of impurities, is 50 DEG C to its temperature；
(3) 1.0MPa is boosted to sewage after cooling, it is 50 DEG C to set temperature, into membrane module, the membrane module
Membrane material be high hydrophilic superoleophobic property film, water pass through film, oily to be separated in influent side enrichment method, profit；
(4) concentrated water and demulsifier of the enriched oil after UF membrane and impurity are under rotation status, into hypergravity machine stream
Body import, and packing area is spun into after rotating channel, in packing area, concentrated water and demulsifier are under the influence of centrifugal force
Liquid liquid mixing is carried out, realizes water-oil separating；
(5) gas is discharged under hydrogen environment, and temperature is 60 DEG C, and Hydrogen Vapor Pressure under conditions of being 1.0MPa be catalyzed instead
Should；
(6) water after step (4) separation, alkali lye and the gas after step (5) processing enter in hypergravity machine, are filling out
Expect to carry out gas-liquid exchange in area；
(7) fluid after step (6) processing, which enters, carries out circular treatment in step (1).
Embodiment 4
Hypergravity described in the utility model takes off ammonium salt device at work, and step is as follows：
(1) filtering and impurity removing processing is carried out at 60 DEG C to Electric Desalting Wastewater, filters out the miscellaneous particle of machine that particle diameter is more than 50um；
(2) cooling treatment is carried out to the sewage after removal of impurities, is 60 DEG C to its temperature；
(3) 3.0MPa is boosted to sewage after cooling, it is 60 DEG C to set temperature, into membrane module, the membrane module
Membrane material be high hydrophilic superoleophobic property film, water pass through film, oily to be separated in influent side enrichment method, profit；
(4) concentrated water and demulsifier of the enriched oil after UF membrane and impurity are under rotation status, into hypergravity machine stream
Body import, and packing area is spun into after rotating channel, in packing area, concentrated water and demulsifier are under the influence of centrifugal force
Liquid liquid mixing is carried out, realizes water-oil separating；
(5) gas is discharged under hydrogen environment, and temperature is 60 DEG C, and Hydrogen Vapor Pressure under conditions of being 1.0MPa be catalyzed instead
Should；
(6) water after step (4) separation, alkali lye and the gas after step (5) processing enter in hypergravity machine, are filling out
Expect to carry out gas-liquid exchange in area；
(7) fluid after step (6) processing, which enters, carries out circular treatment in step (1).
Embodiment 5
Hypergravity described in the utility model takes off ammonium salt device at work, and step is as follows：
(1) secondary filtration removal of impurities processing is carried out at 60 DEG C to Electric Desalting Wastewater, filters out miscellaneous of the machine that particle diameter is more than 50um
Grain；
(2) cooling treatment is carried out to the sewage after removal of impurities, is 50 DEG C to its temperature；
(3) 3.0MPa is boosted to sewage after cooling, it is 60 DEG C to set temperature, into membrane module, the membrane module
Membrane material be high hydrophilic superoleophobic property film, water pass through film, oily to be separated in influent side enrichment method, profit；The step
In film process be made up of one-level membrane separation and two level membrane separation, the one-level membrane separation is more than for separation
50um material, two level membrane separation are used to separate the material more than 5um.
(4) concentrated water and demulsifier of the enriched oil after UF membrane and impurity are under rotation status, into hypergravity machine stream
Body import, and packing area is spun into after rotating channel, in packing area, concentrated water and demulsifier are under the influence of centrifugal force
Liquid liquid mixing is carried out, realizes water-oil separating；
(5) gas is discharged under hydrogen environment, and temperature is 70 DEG C, and Hydrogen Vapor Pressure under conditions of being 1.3MPa be catalyzed instead
Should；
(6) water after step (4) separation, alkali lye and the gas after step (5) processing enter in hypergravity machine, are filling out
Expect to carry out gas-liquid exchange in area；
(7) fluid after step (6) processing, which enters, carries out circular treatment in step (1).
In hypergravity sewage-treatment plant described in the utility model, the membrane module is PC6040 rolled films.Also set
It is equipped with UF membrane cleaning device and cleaning and anti-cleaning is carried out to membrane module.
Test case
The utility model is tested using the release gas of following composition：
After de- ammonium salt PROCESS FOR TREATMENT described in the utility model, test display is as a result as follows：
Although the utility model is elaborated by above-mentioned specific embodiment to it, this specialty is general
Logical technical staff should be understood that any form and details without departing from claims made on this basis
Change, belongs to the utility model scope of the claimed.
Claims (6)
1. a kind of hypergravity takes off ammonium salt device, it is characterised in that
Reactor is provided with, the reactor is provided with release gas import and releases bleeder holes；
It is additionally provided with the alkali storage tank for storing alkali lye, and the first hypergravity machine；
First hypergravity machine has shell, and shell is penetrated on the axis of shell and is provided with power-actuated middle idle running
Axle, sealable fluid inlet is provided with the rotating shaft, there is fluid passage in rotating shaft；Outside rotating shaft, with described turn
Axle is coaxially arranged and is connected with sleeve, so as to the shaping gas passage between the rotating shaft and the sleeve lining, is set on sleeve
It is equipped with multiple stomatas and gas vent；The rotating shaft is extended towards the sleeve multiple rotating channels, in rotating channel
Inside it is provided with raised or recessed helical duct；The rotating channel penetrates the sleeve and set；
Coaxially it is arranged with the rotating shaft, sleeve and is connected with filling tube, in the filling tube internal shaping packing area；The rotation is logical
Road, the stomata connect with the packing area；
It is provided with gas feed, gas vent and fluid issuing on shell, the gas feed, fluid issuing are and packing area
Connection；Release the gas feed connection of bleeder holes and the first hypergravity machine；
The lye export of alkali storage tank connects with the fluid inlet of the first hypergravity machine；
The holding vessel for storing air lift water sewage is additionally provided with, filter is connected with the outlet of sewer of holding vessel；
Membrane module is connected with the outlet of sewer of filter, the membrane module is made up of multi-level tubular membrane module, multiple valve
Formula membrane module has concentrated water outlet and treated water outlet；
It is additionally provided with the alkali liquid tank for storing demulsifier, and the second hypergravity machine；
Second hypergravity machine has shell, and shell is penetrated on the axis of shell and is provided with power-actuated middle idle running
Axle, there is fluid passage in rotating shaft, sealable fluid inlet is provided with the rotating shaft；The fluid inlet simultaneously with
Concentrated water outlet, the lye export connection of alkali liquid tank；
Coaxially be arranged with the rotating shaft outside rotating shaft and be connected with sleeve, so as between the rotating shaft and the sleeve lining into
Shape passage, the rotating shaft is extended towards the sleeve multiple rotating channels, be provided with rotating channel it is raised or
Recessed helical duct；The rotating channel penetrates the sleeve and set；
Coaxially it is arranged with the rotating shaft, sleeve and is connected with filling tube, in the filling tube internal shaping packing area；The rotating channel
Connected with packing area；
Fluid issuing is provided with shell, the fluid issuing connects with packing area；
The fluid inlet connection of the fluid issuing and the first hypergravity machine of second hypergravity machine；
The fluid issuing of first hypergravity machine connects with the holding vessel of storage air lift water sewage.
2. a kind of hypergravity according to claim 1 takes off ammonium salt device, it is characterised in that the filter includes one-level mistake
Filter and secondary filter, the pore size filter of the grade one filter are less than 50um, and the pore size filter of secondary filter is less than
5um。
3. a kind of hypergravity according to claim 1 or 2 takes off ammonium salt device, it is characterised in that multiple rotating channels
Inlet diameter sum be equal to or less than hollow axle internal diameter.
4. a kind of hypergravity according to claim 3 takes off ammonium salt device, it is characterised in that the packing area is provided with multilayer
Filler；The rotating shaft and motor connection.
5. a kind of hypergravity according to claim 1 or 2 or 4 takes off ammonium salt device, it is characterised in that the alkali of alkali storage tank
Liquid outlet is connected with the fluid inlet of the first hypergravity machine by kinetic pump；Concentrated water exports and the fluid inlet of the second hypergravity machine
Connected by kinetic pump.
6. a kind of hypergravity according to claim 1 or 2 or 4 takes off ammonium salt device, it is characterised in that the rotating channel is equal
Set perpendicular to the rotating shaft.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720261797.XU CN206897149U (en) | 2017-03-17 | 2017-03-17 | A kind of hypergravity takes off ammonium salt device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720261797.XU CN206897149U (en) | 2017-03-17 | 2017-03-17 | A kind of hypergravity takes off ammonium salt device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206897149U true CN206897149U (en) | 2018-01-19 |
Family
ID=61293848
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720261797.XU Withdrawn - After Issue CN206897149U (en) | 2017-03-17 | 2017-03-17 | A kind of hypergravity takes off ammonium salt device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106799122A (en) * | 2017-03-17 | 2017-06-06 | 北京沃尔福环保科技有限公司 | A kind of hypergravity takes off ammonium salt device and technique |
-
2017
- 2017-03-17 CN CN201720261797.XU patent/CN206897149U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106799122A (en) * | 2017-03-17 | 2017-06-06 | 北京沃尔福环保科技有限公司 | A kind of hypergravity takes off ammonium salt device and technique |
| CN106799122B (en) * | 2017-03-17 | 2023-08-01 | 北京沃尔福环保科技有限公司 | Supergravity ammonium salt removal device and process |
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