CN208843776U - Ion exchange pot is used in deionized water purification - Google Patents
Ion exchange pot is used in deionized water purification Download PDFInfo
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- CN208843776U CN208843776U CN201821551049.6U CN201821551049U CN208843776U CN 208843776 U CN208843776 U CN 208843776U CN 201821551049 U CN201821551049 U CN 201821551049U CN 208843776 U CN208843776 U CN 208843776U
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Abstract
The utility model relates to the separation and extraction technology fields of active ingredient of natural product, more particularly to being a kind of deionized water purification ion exchange pot, including tank ontology, liquid distributor and ion exchange column group are provided in tank ontology, the inlet tube and exhaust pipe across tank ontology are connected on liquid distributor, it is located at ion exchange column group over top at the top of liquid distributor, ion exchange column group is centered around liquid distributor surrounding, and by being connected in the middle part of connecting tube and liquid distributor periphery, the liquid outlet of ion exchange column group is connected to drain pipe.It solves existing ion exchange column and carries out separation and Extraction in use, inputting extraction liquor to be separated in ion exchange column by inlet tube, exist unevenly, the problem of increasing air-teturning mixed phenomenon, reduce separative efficiency when being entered due to liquor.
Description
Technical field
The utility model relates to the separation and extraction technology fields of active ingredient of natural product, and in particular to be that deionized water mentions
It is pure to use ion exchange pot.
Background technique
Ion exchange column is a kind of column pressure vessel for carrying out ion-exchange reactions, i.e., it is a certain proportion of sun,
Anion exchange resin is mixed loaded in ion exchange column, is swapped, is taken off to the ion in the liquid for flowing through exchanger resin
It removes.Ion exchange column is widely used in the fields such as chemical industry, food, wastewater treatment.Existing ion exchange column in use, by into
Extraction liquor to be separated is inputted in ion exchange column and carries out separation and Extraction by liquid pipe, there is uneven, increasing when entering due to liquor
Big air-teturning mixed phenomenon, reduces separative efficiency.
Utility model content
The utility model is directed to existing ion exchange column in use, extraction liquor to be separated is inputted ion by inlet tube
Separation and Extraction is carried out in exchange column, is existed unevenly when being entered due to liquor, is increased air-teturning mixed phenomenon, reduce separative efficiency
Problem provides a kind of deionized water purification ion exchange pot.
The utility model solves above-mentioned technical problem, the technical solution adopted is that, ion exchange pot is used in deionized water purification
Including tank ontology, it is provided with liquid distributor and ion exchange column group in tank ontology, the feed liquor across tank ontology is connected on liquid distributor
Pipe and exhaust pipe, liquid distributor top are located at ion exchange column group over top, and ion exchange column group is centered around liquid distributor surrounding, and
By being connected in the middle part of connecting tube and liquid distributor periphery, the liquid outlet of ion exchange column group is connected to drain pipe.
The purpose designed in this way is, by the way that liquid distributor is arranged in ion exchange pot, can will enter out of inlet tube
Liquid distribution it is uniform, reduce that local liquid speed is excessive, and liquid is accumulated in liquid distributor squeezes the air in liquid distributor from exhaust pipe
Extrude, final liquid from be drained into the communicating pipe of liquid distributor periphery ion exchange column group carry out ion exchange, solve it is existing from
Sub- exchange column carries out separation and Extraction in use, inputting extraction liquor to be separated in ion exchange column by inlet tube, due to liquid
Exist unevenly, the problem of increasing air-teturning mixed phenomenon, reduce separative efficiency when agent enters.
Further, ion exchange column group includes strong cationic resin exchange column, weak cationic resin exchange column, Qiang Yinli
Sub- resin-column and weakly anionic resin exchange column, the inlet of strong cationic resin exchange column by the first upper connector with
The liquid outlet of connection in the middle part of liquid distributor periphery, strong cationic resin exchange column is handed over by the first lower connector and weak cationic resin
Change the inlet connection of column.The liquid outlet of weak cationic resin exchange column is exchanged by the second upper connector with strong anionic resin
The inlet of column is connected to.The liquid outlet of strong anionic resin exchange column passes through the second lower connector and weakly anionic resin exchange column
Inlet connection.The liquid outlet of weakly anionic resin exchange column is connected to drain pipe.
The purpose designed in this way is that existing ion exchange column is lower to the utilization rate of resin, although strong and weak resin due to
The difference of density can accomplish to be layered substantially, but accomplish that layering is then more difficult completely, if the intersection in two kinds of resins has on a small quantity
Resin mutually mix, to operational effect, there is no big influences；If mixed rouge range is big, the weak type tree being mixed into strong type resin layer
Rouge cannot play exchange interaction, and the strong type resin being mixed into Weak Type Resin cannot regenerate, and be greatly reduced operational effect, to object
The clean-up effect of material or water is poor.
By setting strong cationic resin exchange column, weak cationic resin exchange column, strong anion for ion exchange column
Resin-column and weakly anionic resin exchange column, the resin of the interior filling respective electrode intensity of each cylinder make equipment operation stream
It is fast high, it can be improved ion-exchanging efficiency and effect, shorten runing time, reduce operating cost.
Further, the inlet of strong cationic resin exchange column and strong anionic resin exchange column is respectively positioned on the top of cylinder
Portion, liquid outlet are respectively positioned on the bottom of cylinder, the equal position of the inlet of weak cationic resin exchange column and weakly anionic resin exchange column
In the bottom of cylinder, liquid outlet is respectively positioned on the top of cylinder.
The purpose designed in this way is, by by strong cationic resin exchange column and strong anionic resin exchange column inlet
And liquid outlet, it is shifted to install with the inlet and liquid outlet of weak cationic resin exchange column and weakly anionic resin exchange column, just
In liquid to be separated in ion exchange column stay long enough, promoted separation and Extraction effect.
Optionally, it is provided with two groups of drainage units in ion exchange column group, and is located at the top of ion exchange column group
And lower part, multiple groups separative unit is provided between two groups of drainage units, and be located at the drainage unit on ion exchange column group top with
There is upper plenum between at the top of ion exchange column group, drainage unit and ion exchange column group bottom positioned at ion exchange column group lower part
Between have lower cavity.
Optionally, every group of separative unit is made of separation partition and separating pipe, and separation partition is regular hexagon, and separating pipe is inserted
Enter to separate in partition.
Optionally, every group of drainage unit is regular hexagon, and drainage unit is covered on separative unit, is arranged on drainage unit
There is conduction hole, conduction hole is adapted with separating pipe.
The purpose designed in this way is, forms separation partition by regular hexagon by being arranged in ion exchange column group, just
In setting separation resin etc. in Rapid Combination and installation, separating pipe for separating the material of liquor.
Meanwhile drainage unit is set above separative unit, it is easy to implement liquor and is uniformly distributed, enable from conduction hole
In middle inflow separating pipe.
Moreover cavity is directly set in drainage unit and ion exchange column group, facilitate access for drainage unit or single from drainage
The liquid of member discharge can be uniformly distributed, and provide a temporarily providing room.
Optionally, the first water pump is set on inlet tube, the second water pump is provided on drain pipe.
The purpose designed in this way is, by the first water pump of setting and the second water pump, can be improved liquid in ion exchange
Flowing velocity in tank applies suitable power and increases separating effect.
The beneficial effects of the utility model include at least following one；
1, can be uniform by the liquid distribution entered out of inlet tube by the way that liquid distributor is arranged in ion exchange pot, drop
Low part liquid speed is excessive, and liquid is accumulated in liquid distributor squeezes out the air in liquid distributor from exhaust pipe, and final liquid is from cloth
The ion exchange column group that is drained into communicating pipe of liquid device periphery carries out ion exchange.
2, existing ion exchange column is solved in use, extraction liquor to be separated is inputted ion exchange column by inlet tube
Middle carry out separation and Extraction is existed unevenly, the problem of increasing air-teturning mixed phenomenon, reduce separative efficiency when being entered due to liquor.
3, entire deionized water purification ion exchange pot separation and Extraction improved efficiency about 25%.
Detailed description of the invention
Fig. 1 is deionized water purification ion exchange pot structural schematic diagram；
Fig. 2 is deionized water purification ion exchange pot overlooking structure diagram；
Fig. 3 is deionized water purification ion exchange pot present invention looks up structural representation；
Fig. 4 is ion exchange column structural schematic diagram；
Fig. 5 is separative unit structural schematic diagram；
Fig. 6 is drainage unit structural schematic diagram；
In the figure, it is marked as 1 be tank ontology, 2 be inlet tube, 3 be drain pipe, 4 be exhaust pipe, 5 be ion exchange column group,
501 it is strong cationic resin exchange column, 502 be weak cationic resin exchange column, 503 be strong anionic resin exchange column, 504 is
Weakly anionic resin exchange column, 6 be liquid distributor, 7 be upper connector, 701 be the first upper connector, 702 be the second upper connector,
8 it is lower connector, 801 be the first lower connector, 802 be the second lower connector, 9 be upper plenum, 10 be lower cavity, 11 is first
Water pump, 12 be the second water pump, 13 be separative unit, 14 be separation partition, 15 be separating pipe, 16 be drainage unit, 17 be drainage
Hole.
Specific embodiment
It is clear in order to enable the purpose of this utility model, technical solution and advantage to be more clear, below in conjunction with attached drawing and
The present invention will be further described in detail for embodiment.It should be appreciated that specific embodiment described herein is only used to
It explains the utility model, is not used to limit the utility model protection content.
Embodiment 1
As shown in Figure 1, deionized water purification ion exchange pot, including tank ontology 1, are wherein provided with cloth in tank ontology 1
Liquid device 6 and ion exchange column group 5 are connected with inlet tube 2 and exhaust pipe 4 across tank ontology 1,6 top of liquid distributor on liquid distributor 6
Positioned at 5 over top of ion exchange column group, ion exchange column group 5 is centered around 6 surrounding of liquid distributor, and passes through connecting tube and liquid distributor
Connection, the liquid outlet of ion exchange column group 5 are connected to drain pipe 3 in the middle part of 6 peripheries.
The purpose designed in this way is, liquid distributor is arranged in ion exchange pot, the liquid that can will enter out of inlet tube
Body is evenly distributed, and the local liquid speed of reduction is excessive, and liquid is accumulated in liquid distributor squeezes out the air in liquid distributor from exhaust pipe,
Final liquid carries out ion exchange from ion exchange column group is drained into the communicating pipe of liquid distributor periphery.Solves existing ion exchange
Column carries out separation and Extraction in use, inputting extraction liquor to be separated in ion exchange column by inlet tube, since liquor enters
When exist it is uneven, the problem of increasing air-teturning mixed phenomenon, reduce separative efficiency.
Embodiment 2
Based on embodiment 1, as shown in Figures 2 and 3, ion exchange column group 5 includes strong cationic resin exchange column 501, weak
Cation exchange resin column 502, strong anionic resin exchange column 503 and weakly anionic resin exchange column 504, strong cationic resin
The inlet of exchange column 501 in the middle part of the first upper connector 701 and 6 periphery of liquid distributor by being connected to, strong cationic resin exchange column
501 liquid outlet is connected to by the first lower connector 801 with the inlet of weak cationic resin exchange column 502.Weak cation tree
The liquid outlet of Ester exchange column 502 is connected to by the second upper connector 702 with the inlet of strong anionic resin exchange column 503.By force
The inlet that the liquid outlet of resin anion (R.A.) exchange column 503 passes through the second lower connector 802 and weakly anionic resin exchange column 504
Connection.The liquid outlet of weakly anionic resin exchange column 504 is connected to drain pipe 3.
In use, setting strong cationic resin exchange column, weak cationic resin exchange column, Qiang Yinli for ion exchange column
Sub- resin-column and weakly anionic resin exchange column, the resin of the interior filling respective electrode intensity of each cylinder, run equipment
Flow velocity is high, can be improved ion-exchanging efficiency and effect, shortens runing time, reduces operating cost.It solves existing ion to hand over
It is lower to the utilization rate of resin to change column, although strong and weak resin since the difference of density can accomplish to be layered substantially, will be accomplished completely
Layering is then more difficult, if the intersection in two kinds of resins has a small amount of resin mutually to mix, to operational effect, there is no big influences；
If mixed rouge range is big, the Weak Type Resin being mixed into strong type resin layer cannot play exchange interaction, be mixed into strong in Weak Type Resin
Type resin cannot regenerate, and be greatly reduced operational effect, the problem poor to the clean-up effect of material or water.
Embodiment 3
Based on embodiment 2, the equal position of the inlet of strong cationic resin exchange column 501 and strong anionic resin exchange column 503
In the top of cylinder, liquid outlet is respectively positioned on the bottom of cylinder, weak cationic resin exchange column 502 and weakly anionic resin exchange column
504 inlet is respectively positioned on the bottom of cylinder, and liquid outlet is respectively positioned on the top of cylinder.
In use, by strong cationic resin exchange column and strong anionic resin exchange column inlet and liquid outlet, with weak sun
The inlet and liquid outlet of ion exchange resin exchange column and weakly anionic resin exchange column shift to install, convenient for liquid to be separated from
Stay long enough in sub- exchange column promotes separation and Extraction effect.
Embodiment 4
Based on one of embodiment 1 to embodiment 3, two groups of drainage units 16 are provided in ion exchange column group 5, and position respectively
It is provided with multiple groups separative unit 13 between the upper and lower part of ion exchange column group 5, two groups of drainage units 16, and is located at ion
There is upper plenum 9 between 5 top of drainage unit 16 and ion exchange column group on 5 top of exchange column group, is located under ion exchange column group 5
There is lower cavity 10 between 5 bottom of drainage unit 16 and ion exchange column group in portion.Every group of separative unit 13 is by 14 He of separation partition
Separating pipe 15 forms, and separation partition 14 is regular hexagon, and the insertion of separating pipe 15 separates in partition 14.Every group of drainage unit 16 is positive
Hexagon, drainage unit 16 are covered on separative unit 13, are provided with conduction hole 17 on drainage unit 16, conduction hole 17 with separate
Pipe 15 is adapted.5 top of ion exchange column group is connect with upper connector 7, and lower part is connect with lower connector 8.
Separation partition is formed by regular hexagon in use, being arranged in ion exchange column group, is convenient for Rapid Combination and installation,
Setting separation resin etc. is for separating the material of liquor in separating pipe.Meanwhile drainage unit is set above separative unit, it is convenient for
It realizes that liquor is uniformly distributed, enables to flow into separating pipe from conduction hole.
Moreover cavity is directly set in drainage unit and ion exchange column group, facilitate access for drainage unit or single from drainage
The liquid of member discharge can be uniformly distributed, and provide a temporarily providing room.
Embodiment 5
Based on embodiment 1, the first water pump 11 is set on inlet tube 2, the second water pump 12 is provided on drain pipe 3.
In use, the first water pump of setting and the second water pump, can be improved liquid flowing velocity in ion exchange pot, apply
Suitable power increases separating effect.
Claims (7)
1. deionized water purification ion exchange pot, including tank ontology (1), it is characterised in that: be provided in the tank ontology (1)
Liquid distributor (6) and ion exchange column group (5) are connected with the inlet tube (2) across tank ontology (1) and row on the liquid distributor (6)
Tracheae (4), liquid distributor (6) top are located at ion exchange column group (5) over top, and the ion exchange column group (5) is centered around cloth
Liquid device (6) surrounding, and by being connected in the middle part of connecting tube and liquid distributor (6) periphery, the liquid outlet of ion exchange column group (5) and drain
Manage (3) connection.
2. deionized water purification ion exchange pot according to claim 1, it is characterised in that: the ion exchange column group
It (5) include strong cationic resin exchange column (501), weak cationic resin exchange column (502), strong anionic resin exchange column
(503) pass through on first with weakly anionic resin exchange column (504), the inlet of the strong cationic resin exchange column (501)
It is connected in the middle part of connecting tube (701) and liquid distributor (6) periphery, the liquid outlet of strong cationic resin exchange column (501) passes through under first
Connecting tube (801) is connected to the inlet of weak cationic resin exchange column (502)；
The liquid outlet of the weak cationic resin exchange column (502) is handed over by the second upper connector (702) and strong anionic resin
Change the inlet connection of column (503)；
The liquid outlet of the strong anionic resin exchange column (503) is handed over by the second lower connector (802) and weakly anionic resin
Change the inlet connection of column (504)；
The liquid outlet of the weakly anionic resin exchange column (504) is connected to drain pipe (3).
3. deionized water purification ion exchange pot according to claim 2, it is characterised in that: the strong cationic resin
The inlet of exchange column (501) and strong anionic resin exchange column (503) is respectively positioned on the top of cylinder, and liquid outlet is respectively positioned on cylinder
Bottom, the inlet of the weak cationic resin exchange column (502) and weakly anionic resin exchange column (504) is respectively positioned on cylinder
Bottom, liquid outlet is respectively positioned on the top of cylinder.
4. according to claim 1 to deionized water purification ion exchange pot described in one of 3, it is characterised in that: the ion
Two groups of drainage units (16) are provided in exchange column group (5), and are located at the upper and lower part of ion exchange column group (5), two
It is provided with multiple groups separative unit (13) between group drainage unit (16), and is located at the drainage unit on ion exchange column group (5) top
(16) there are upper plenum (9) between ion exchange column group (5) top, be located at the drainage unit of ion exchange column group (5) lower part
(16) there are lower cavity (10) between ion exchange column group (5) bottom.
5. deionized water purification ion exchange pot according to claim 4, it is characterised in that: separative unit described in every group
(13) it is made of separation partition (14) and separating pipe (15), separation partition (14) is regular hexagon, separating pipe (15) insertion separation
In partition (14).
6. deionized water purification ion exchange pot according to claim 5, it is characterised in that: drainage unit described in every group
It (16) is regular hexagon, drainage unit (16) is covered on separative unit (13), and drainage unit is provided with conduction hole on (16)
(17), conduction hole (17) is adapted with separating pipe (15).
7. deionized water purification ion exchange pot according to claim 1, it is characterised in that: on the inlet tube (2)
It is arranged the first water pump (11), is provided with the second water pump (12) on the drain pipe (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821551049.6U CN208843776U (en) | 2018-09-21 | 2018-09-21 | Ion exchange pot is used in deionized water purification |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821551049.6U CN208843776U (en) | 2018-09-21 | 2018-09-21 | Ion exchange pot is used in deionized water purification |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208843776U true CN208843776U (en) | 2019-05-10 |
Family
ID=66373561
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821551049.6U Active CN208843776U (en) | 2018-09-21 | 2018-09-21 | Ion exchange pot is used in deionized water purification |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208843776U (en) |
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2018
- 2018-09-21 CN CN201821551049.6U patent/CN208843776U/en active Active
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