CN208799971U - A kind of latex intensified is than turbid reagent process units - Google Patents
A kind of latex intensified is than turbid reagent process units Download PDFInfo
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- CN208799971U CN208799971U CN201821359635.0U CN201821359635U CN208799971U CN 208799971 U CN208799971 U CN 208799971U CN 201821359635 U CN201821359635 U CN 201821359635U CN 208799971 U CN208799971 U CN 208799971U
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Abstract
The utility model discloses a kind of latex intensifieds than turbid reagent process units, including ultrafiltration column and peristaltic pump one, peristaltic pump one is connected by conduit with the inlet tube of ultrafiltration column, the ultrafiltration column includes cylindrical housing closed at both ends, the inlet tube is arranged in sheath top plate, several branched pipes are equipped in inlet tube lower end, permeable hole is densely covered on branched pipe, ultrafiltration membrane is equipped in branched pipe, branched pipe is placed in shell, the bottom edge of the shell is equipped with outlet tube, outlet tube is connected to shell inner cavity, a water inlet pipe is worn in the middle part of shell bottom plate, water inlet pipe is connected by a horizontal distributive pipe with each branch's pipe end, water inlet pipe one end is connected with peristaltic pump two, a regulation pipe is also connected in the part that water inlet pipe is placed in shell exterior, a matched piston is equipped in regulation pipe.The device is high for the separative efficiency of latex beads, and same time can separate more latex beads, and then production cost of the latex enhancing than turbid reagent is effectively reduced.
Description
Technical field
The utility model relates to latex intensifieds than turbid reagent production field, and in particular to a kind of latex intensified is more raw than turbid reagent
Produce device.
Background technique
Currently, latex enhancing immune has centrifuge or ultrafiltration system than the important device of turbid reagent production process.For
Lesser latex microsphere needs high revolving speed if separated using centrifugal method, and latex aggregation is blocking in centrifugal process,
Again dispersion is more troublesome, and centrifuge capacity is limited, can not amplify production on a large scale；Hyperfiltration technique condition is more mild,
The fairly large Linear Amplifer production of energy, but complete ultrafiltration system in the market is expensive.
Utility model content
In order to solve the above-mentioned technical problem, the utility model discloses a kind of latex intensified than turbid reagent process units, the dress
The separative efficiency height for latex beads is set, same time can separate more latex beads, and then latex increasing is effectively reduced
By force than the production cost of turbid reagent.
The utility model is achieved through the following technical solutions:
A kind of latex intensified than turbid reagent process units, including ultrafiltration column and peristaltic pump one, peristaltic pump one by conduit with
The inlet tube of ultrafiltration column is connected, and the ultrafiltration column includes cylindrical housing closed at both ends, and the inlet tube is arranged on shell top
On plate, several branched pipes are equipped in inlet tube lower end, permeable hole is densely covered on branched pipe, ultrafiltration membrane is equipped in branched pipe, point
Branch pipe is placed in shell, and the bottom edge of the shell is equipped with outlet tube, and outlet tube is connected to shell inner cavity, in shell bottom plate
Portion wears a water inlet pipe, and water inlet pipe is connected by a horizontal distributive pipe with each branch's pipe end, water inlet pipe one end
It is connected with peristaltic pump two, a regulation pipe is also connected in the part that water inlet pipe is placed in shell exterior, is equipped with one in regulation pipe
Matched piston, the piston other end are connected with a fluid pressure drive device.
In the utility model, peristaltic pump one is used for latex intensified than the inlet tube in turbid reagent raw liquor pump excess of imports filter column
Interior, liquid is entered in several branched pipes by inlet tube, is the liquid pressing in branched pipe using peristaltic pump one, is made in pressure
Under, liquid is discharged through permeable hole from branched pipe after ultrafiltration membrance filter, and the latex beads solution of discharge enters shell inner cavity
And finally enter latex intensified than in turbid reagent collection device through outlet tube, ultrafiltration column in use for some time, due to dense
Poor polarization, the intracorporal impurity of liquid can gradually be gathered in ultrafiltration membrane surface, the filter efficiency of ultrafiltration membrane caused to be remarkably decreased, this
Utility model is connected with water inlet pipe by horizontal tube in branch's pipe end, and water inlet pipe is connected with peristaltic pump two, therefore in branched pipe
After ultrafiltration for a period of time, say that branch's liquid in pipe is drawn back using peristaltic pump one, starting peristaltic pump two injects pure water into branched pipe,
And the flushing that pure water flow velocity carries out branched pipe is adjusted using peristaltic pump two, keep the impurity for being attached to ultrafiltration membrane surface cleaned dry
Only, it cleans the liquid finished to extract out through peristaltic pump two, then proceeds by ultra-filtration process, due to periodically being carried out to ultrafiltration membrane surface
Cleaning, avoids impurity from depositing, substantially increases the ultrafiltration efficiency of ultrafiltration membrane, and then life of the latex enhancing than turbid reagent is effectively reduced
Produce cost.
In the utility model, the cleaning of ultrafiltration membrane need to only utilize peristaltic pump two and water inlet pipe, without specially by branch
Pipe taking-up processing, cleaning efficiency are high.
The adjusting pipe end is equipped with opening.Two other end of peristaltic pump is connected with a water tank.The water inlet pipe leans on
One end of nearly distributive pipe is equipped with a solenoid valve.
When cleaning, under the action of peristaltic pump two, the pure water of higher flow rate is entered in branched pipe, closes peristaltic pump at this time
Two, starting fluid pressure drive device pushes the piston in regulation pipe back and forth, and under piston driving, the pure water in branched pipe is back and forth
Flow at high speed further increases pure water to the scouring effect of ultrafiltration membrane surface, keeps cleaning more thorough.
A peristaltic pump one and latex intensified is connected than turbid reagent stoste storage bin, the outlet tube and a glue
Cream enhancing is connected than turbid reagent collection device.
The peristaltic pump one, peristaltic pump two and fluid pressure drive device pass through a controller plc operation.
Ultrafiltration membrane is equipped in the horizontal tube.Valve is respectively provided on the water inlet pipe of two side of the inlet tube and peristaltic pump.
The inlet tube is equipped with a tracheae with valve.
The utility model compared with prior art, has the following advantages and benefits:
A kind of latex intensified of the utility model is used for latex intensified than turbid reagent process units, peristaltic pump one than turbid reagent
In inlet tube in raw liquor pump excess of imports filter column, liquid is entered in several branched pipes by inlet tube, is point using peristaltic pump one
Liquid pressing in branch pipe, under pressure, liquid are discharged through permeable hole from branched pipe after ultrafiltration membrance filter, the cream of discharge
Glue microspheres solution enters shell inner cavity and finally enters latex intensified than in turbid reagent collection device through outlet tube, ultrafiltration column
In use for some time, since concentration polarization acts on, the intracorporal impurity of liquid can gradually be gathered in ultrafiltration membrane surface, lead to ultrafiltration
The filter efficiency of film is remarkably decreased, and the utility model is connected with water inlet pipe, water inlet pipe connection by horizontal tube in branch's pipe end
There is peristaltic pump two, therefore after branched pipe ultrafiltration for a period of time, say that branch's liquid in pipe is drawn back using peristaltic pump one, starting is wriggled
Pump two injects pure water into branched pipe, and adjusts the flushing that pure water flow velocity carries out branched pipe using peristaltic pump two, makes to be attached to super
The impurity of filter membrane surface is cleaned, and is cleaned the liquid finished and is extracted out through peristaltic pump two, then proceeds by ultra-filtration process, by
Ultrafiltration membrane surface is cleared up in periodically, impurity is avoided to deposit, substantially increases the ultrafiltration efficiency of ultrafiltration membrane, and then effectively drop
Production cost of the low latex enhancing than turbid reagent.
Detailed description of the invention
Attached drawing described herein is used to provide to further understand the utility model embodiment, constitutes the one of the application
Part does not constitute the restriction to the utility model embodiment.In the accompanying drawings:
FIG. 1 is a schematic structural view of the utility model.
Label and corresponding parts title in attached drawing:
1- ultrafiltration column, 11- inlet tube, 12- shell, 13- outlet tube, 2- peristaltic pump one, 21- conduit, 3- branched pipe, 4- into
Water pipe, 41- distributive pipe, 42- solenoid valve, 5- peristaltic pump two, 6- regulation pipe, 61- piston, 62- solenoid valve two, 7- hydraulic-driven dress
It sets.
Specific embodiment
For the purpose of this utility model, technical solution and advantage is more clearly understood, below with reference to embodiment and attached drawing,
The utility model is described in further detail, and the exemplary embodiment and its explanation of the utility model are only used for explaining this
Utility model is not intended to limit the scope of the present invention.
Embodiment 1
As shown in Figure 1, a kind of latex intensified of the utility model is than turbid reagent process units, including ultrafiltration column 1 and peristaltic pump
One 2, peristaltic pump 1 is connected by conduit 21 with the inlet tube 11 of ultrafiltration column 1, and the ultrafiltration column 1 includes cylinder closed at both ends
Shape shell 12, the inlet tube 11 are arranged on 12 top plate of shell, are equipped with several branched pipes 3, branched pipe 3 in 11 lower end of inlet tube
On be densely covered with permeable hole, ultrafiltration membrane is equipped in branched pipe 3, branched pipe 3 is placed in shell 12, the bottom edge of the shell 12
Equipped with outlet tube 13, outlet tube 13 is connected to 12 inner cavity of shell, and a water inlet pipe 4, water inlet pipe 4 are worn in the middle part of 12 bottom plate of shell
Be connected by a horizontal distributive pipe 41 with each 3 end of branched pipe, 4 one end of water inlet pipe is connected with peristaltic pump 25, into
The part that water pipe is placed in shell exterior is also connected with a regulation pipe 6, is equipped with a matched piston 61, piston in regulation pipe 6
61 other ends are connected with a fluid pressure drive device 7.
6 end of regulation pipe is equipped with opening.25 other end of peristaltic pump is connected with a water tank.The water inlet pipe 4
A solenoid valve 42 is equipped with close to one end of distributive pipe.
Embodiment 2
As shown in Figure 1, a kind of latex intensified of the utility model is than turbid reagent process units, including ultrafiltration column 1 and peristaltic pump
One 2, peristaltic pump 1 is connected by conduit 21 with the inlet tube 11 of ultrafiltration column 1, and the ultrafiltration column 1 includes cylinder closed at both ends
Shape shell 12, the inlet tube 11 are arranged on 12 top plate of shell, are equipped with several branched pipes 3, branched pipe 3 in 11 lower end of inlet tube
On be densely covered with permeable hole, ultrafiltration membrane is equipped in branched pipe 3, branched pipe 3 is placed in shell 12, the bottom edge of the shell 12
Equipped with outlet tube 13, outlet tube 13 is connected to 12 inner cavity of shell, and a water inlet pipe 4, water inlet pipe 4 are worn in the middle part of 12 bottom plate of shell
Be connected by a horizontal distributive pipe 41 with each 3 end of branched pipe, 4 one end of water inlet pipe is connected with peristaltic pump 25, into
The part that water pipe is placed in shell exterior is also connected with a regulation pipe 6, is equipped with a matched piston 61, piston in regulation pipe 6
61 other ends are connected with a fluid pressure drive device 7.
6 end of regulation pipe is equipped with opening.25 other end of peristaltic pump is connected with a water tank.The water inlet pipe 4
A solenoid valve 42 is equipped with close to one end of distributive pipe.
The peristaltic pump 1 is connected with a latex intensified than turbid reagent stoste storage bin, the outlet tube 13 and one
A latex intensified is connected than turbid reagent collection device.
The peristaltic pump 1, peristaltic pump 25 and fluid pressure drive device 7 pass through a controller plc operation.
The regulation pipe 6 is equipped with solenoid valve 2 62.
Above-described specific embodiment, to the purpose of this utility model, technical scheme and beneficial effects carried out into
One step is described in detail, it should be understood that being not used to limit the foregoing is merely specific embodiment of the present utility model
Determine the protection scope of the utility model, within the spirit and principle of the utility model, any modification for being made equally is replaced
It changes, improve, should be included within the scope of protection of this utility model.
Claims (6)
1. a kind of latex intensified is than turbid reagent process units, including ultrafiltration column and peristaltic pump one, peristaltic pump one is by conduit and surpasses
The inlet tube of filter column is connected, which is characterized in that the ultrafiltration column includes cylindrical housing closed at both ends, the inlet tube setting
In sheath top plate, several branched pipes are equipped in inlet tube lower end, permeable hole is densely covered on branched pipe, is equipped in branched pipe super
Filter membrane, branched pipe are placed in shell, and the bottom edge of the shell is equipped with outlet tube, and outlet tube is connected to shell inner cavity, outside
A water inlet pipe is worn in the middle part of shell bottom plate, water inlet pipe is connected by a horizontal distributive pipe with each branch's pipe end, into
Water pipe one end is connected with peristaltic pump two, a regulation pipe is also connected in the part that water inlet pipe is placed in shell exterior, in regulation pipe
Equipped with a matched piston, the piston other end is connected with a fluid pressure drive device.
2. a kind of latex intensified according to claim 1 is than turbid reagent process units, which is characterized in that the regulation pipe end
End is equipped with opening.
3. a kind of latex intensified according to claim 1 is than turbid reagent process units, which is characterized in that the peristaltic pump two
The other end is connected with a water tank.
4. a kind of latex intensified according to claim 1 is than turbid reagent process units, which is characterized in that the water inlet pipe leans on
One end of nearly distributive pipe is equipped with a solenoid valve.
5. a kind of latex intensified according to claim 1 is than turbid reagent process units, which is characterized in that the peristaltic pump one
It is connected with a latex intensified than turbid reagent stoste storage bin, the outlet tube and a latex intensified are collected than turbid reagent and filled
It sets connected.
6. a kind of latex intensified according to claim 1 is than turbid reagent process units, which is characterized in that the peristaltic pump
One, peristaltic pump two and fluid pressure drive device pass through a controller plc operation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821359635.0U CN208799971U (en) | 2018-08-22 | 2018-08-22 | A kind of latex intensified is than turbid reagent process units |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821359635.0U CN208799971U (en) | 2018-08-22 | 2018-08-22 | A kind of latex intensified is than turbid reagent process units |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208799971U true CN208799971U (en) | 2019-04-30 |
Family
ID=66236303
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821359635.0U Active CN208799971U (en) | 2018-08-22 | 2018-08-22 | A kind of latex intensified is than turbid reagent process units |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208799971U (en) |
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2018
- 2018-08-22 CN CN201821359635.0U patent/CN208799971U/en active Active
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