CN206980702U - A kind of metering-type totally-enclosed solid-liquid reaction device - Google Patents
A kind of metering-type totally-enclosed solid-liquid reaction device Download PDFInfo
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- CN206980702U CN206980702U CN201720327737.3U CN201720327737U CN206980702U CN 206980702 U CN206980702 U CN 206980702U CN 201720327737 U CN201720327737 U CN 201720327737U CN 206980702 U CN206980702 U CN 206980702U
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- fluid reservoir
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- blending tank
- pump
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Abstract
The utility model discloses a kind of metering-type totally-enclosed solid-liquid reaction device, including operating platform, blending tank, settling tank, fluid reservoir, liquid level gauge, centrifugal pump, electricity case；Blending tank, settling tank and the fluid reservoir and staircase, lifting platform configured in prismatic is respectively equipped with the operating platform, the blending tank is provided with manhole, liquid-entering hole, reductor, agitator and liquid level gauge, the mixing pot bottom is connected by pipeline with outlet valve, mortar pump, hand-operated valve, and is connected respectively with the top of two settling tanks；Two settling tanks are merged by pipette, hand-operated valve is transported to supernatant liquid in fluid reservoir；The settling tank lower sediment delivers to membrane pump and filter press via outlet valve, and filter liquor is recycled into fluid reservoir；This is new using blending tank, settling tank, fluid reservoir prismatic lay-out, configures auxiliary pump and liquid level gauge confined reaction and separates, simplify operation circulation and utilize liquid, improve material service efficiency, green economy is environmentally friendly, production efficiency height.
Description
Technical field
Solid-liquid reaction technical equipment field is the utility model is related to, more particularly to a kind of metering-type totally-enclosed solid-liquid reaction dress
Put, the device that the solution that is particularly suitable for use in recycles.
Background technology
In chemical field and pharmaceutical field, solid-liquid reaction can usually occur, typically carry out in a kettle, foundationization
The type difference of reaction is learned, solid material and liquid material can simultaneously be added, can also sequentially added.And the solid in reacting
Need to carry out next step operation or deep processing, the liquid in reaction to need to reclaim, and to liquid again degree of thickening and denseness after, then
Secondary re-using.
In the prior art, in solid-liquid reaction under operating mode, the reuse of liquid is needed by weighing, metering, circulation and recovery work
Sequence；Its defect is to complete this series of operation device most separate configuration, step by step completion, is respectively completed by plurality of devices, no
But material waste is caused, the degree of accuracy of metering is low, and causes operator's workload to increase, and has a strong impact on production efficiency.
Utility model content
In order to solve the above technical problems, the utility model provides a kind of metering-type totally-enclosed solid-liquid reaction device, in order to
Overcome above problems, using double-decked platform formula structure, blending tank, settling tank, fluid reservoir prismatic lay-out, configuration membrane pump,
Filter press, centrifugal pump, liquid level gauge carry out the closed solid-liquid reaction of metering-type and separation, not only enormously simplify at operation but also liquid
Recycled in air-tight state, greatly improve the service efficiency of material.
To reach above-mentioned purpose, the technical solution of the utility model is as follows：A kind of metering-type totally-enclosed solid-liquid reaction device,
Including basic unit, operating platform, guardrail, support column, staircase, lifting platform, tank bracket, blending tank, settling tank, fluid reservoir, reductor,
Mortar pump, agitator, liquid level gauge, outlet valve, manhole, peep hole, pipeline, liquid inlet, centrifugal pump, pipette, hand-operated valve, electricity system
Case, it is characterised in that：
In the basic unit rectangle, operating platform with guardrail, the operation are fixedly installed by more support columns
A blending tank, two settling tanks and a fluid reservoir are fixedly installed respectively by multiple tank brackets on platform；The mixing
Tank, settling tank and fluid reservoir configure in prismatic；Staircase and lifting platform, the mixing are provided between the operating platform and basic unit
The manhole for launching solid and the liquid-entering hole for quantitatively adding liquid are provided with tank；It is provided with and subtracts at the top of the blending tank
Fast machine, and agitator is provided with by reductor driving；The blending tank side is equipped with by the liquid of PU transparent pipes sign scale
Position meter, the mixing pot bottom are connected by pipeline with outlet valve, mortar pump, hand-operated valve, and respectively with two settling tanks tops
Connection；The pipette with pipeline pump is provided with two settling tanks, manually valve merges upper strata two groups of pipette
Liquid is transported in centrifugal pump, and liquid is pumped into storage at the top of fluid reservoir by fixed centrifugal pump on the operational platform
In flow container；Lower sediment in the settling tank via the outlet valve of bottom delivers to membrane pump and filter press handle to obtain solid-state it is residual
Slag, and filter liquor is periodically recycled to fluid reservoir；Liquid in the fluid reservoir via bottom outlet valve and pipeline, centrifugal pump
Connection, and liquid is transmitted back in blending tank and recycled；Electric cabinet is provided with the operating platform, the electric cabinet is with subtracting
Fast machine, lift, centrifugal pump, mortar pump, membrane pump, the connection of filter press electric signal.
Two peep holes are symmetrically arranged with the blending tank, for observing the reactiveness in blending tank；The mixing
Tank, settling tank, be provided with manhole at the top of fluid reservoir, people's centerline hole and blending tank, settling tank, fluid reservoir center line it
Between angle be 30 degree.
The mortar pump, membrane pump, filter press are fixedly installed on basic unit.
The liquid from blending tank to fluid reservoir, from settling tank to fluid reservoir and from fluid reservoir to blending tank, configure
There is the mortar pump with polyethylene-lined.
The thickness that the blending tank, settling tank, the inner tank wall pressure of fluid reservoir serve as a contrast PU is no less than 3mm；On the agitator
Agitating paddle winding polytetrafluoroethylene (PTFE) thickness be no less than 3mm；The agitating shaft of the agitator and it is other contacted with material zero
The thickness of part spraying polytetrafluoroethylene (PTFE) is no less than 1mm；The blowing uses PPR material pipe fittings with pipeline.
The staircase is used for above and below personnel, and the lifting platform is used for the conveying of solid material；The blending tank is used for solid
With the hybrid reaction of liquid, the settling tank is used for the precipitated and separated of solid-liquid mixed reactant, and the fluid reservoir is used to store back
The reaction liquid of receipts, and liquid is back to by blending tank by centrifugal pump and mortar pump.
Operation principle of the present utility model is：Blending tank, the settling tank stood, fluid reservoir, filter press are passed through into inner tube
Road, centrifugal pump, mortar pump, flow meter realize continuous feed and discharging, while solution returns into a closed assembly
Receive, next batch production and application is carried out after adjusting concentration；Specifically, material carries out solid-liquid in the blending tank with agitator
After mixing, it is pumped in the settling tank of standing, is reacted by mortar, then the precipitation for bottom being sunken in the settling tank of standing
Thing pump into filter press, the filtrate in settling tank in supernatant and filter press by centrifugal pumping into fluid reservoir, next time
Before production, in solution constant displacement pump to blending tank, according to solution concentration in fluid reservoir, electricity will be added into blending tank in fluid reservoir
Xie Zhi, concentration is adjusted, then produced, reach closed quantity-produced purpose.
Pass through above-mentioned technical proposal, the beneficial effect of technical solutions of the utility model are：Using double-decked platform formula structure, mix
Tank, settling tank, fluid reservoir prismatic lay-out are closed, configuration membrane pump, filter press, centrifugal pump, liquid level gauge carry out the closed solid-liquid of metering-type
Reaction and separation, not only enormously simplify operation but also liquid recycles in air-tight state, greatly improve the use of material
Efficiency；Large-scale continuous production can be realized, while whole process is in air-tight state, realizes separation of solid and liquid and utilization and recycle, green
Economic and environment-friendly, production efficiency is high.
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 required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, drawings in the following description are only
It is some embodiments of the 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 a kind of metering-type totally-enclosed solid-liquid reaction device front view schematic diagram disclosed in the utility model embodiment；
Fig. 2 is a kind of metering-type totally-enclosed solid-liquid reaction device front view schematic diagram disclosed in the utility model embodiment.
Corresponding component title of the numeral represented by with letter in figure：
1. the support column of basic unit's 2. operating platform, 3. guardrail 4.
5. the blending tank of 6. lifting platform of staircase, 7. tank bracket 8.
9. the mortar pump of 10. fluid reservoir of settling tank, 11. reductor 12.
13. the manhole of 14. liquid level gauge of agitator, 15. outlet valve 16.
17. the centrifugal pump of 18. pipeline of peep hole, 19. liquid inlet 20.
21. the electricity case of 22. hand-operated valve of pipette 23.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belong to the scope of the utility model protection.
According to Fig. 1 and Fig. 2, the utility model provides a kind of metering-type totally-enclosed solid-liquid reaction device, including basic unit 1,
Operating platform 2, guardrail 3, support column 4, staircase 5, lifting platform 6, tank bracket 7, blending tank 8, settling tank 9, fluid reservoir 10, reductor
11st, mortar pump 12, agitator 13, liquid level gauge 14, outlet valve 15, manhole 16, peep hole 17, pipeline 18, liquid inlet 19, centrifugal pump
20th, pipette 21, hand-operated valve 22, electricity case 23.
Rectangle, operating platform 2 with guardrail 3 are fixedly installed by more support columns 4 in the basic unit 1, it is described
8, two settling tanks 9 of a blending tank and a fluid reservoir are fixedly installed respectively by multiple tank brackets 7 on operating platform 2
10；The blending tank 8, settling tank 9 and fluid reservoir 10 configure in prismatic；Staircase is provided between the operating platform 2 and basic unit 1
5 and lifting platform 6, the manhole 16 for launching solid and the liquid-entering hole for quantitatively adding liquid are provided with the blending tank 8
19；The top of blending tank 8 is provided with reductor 11, and the driving of reductor 11 is provided with agitator 13；The blending tank 8
Side is equipped with by the liquid level gauge 14 of PU transparent pipes sign scale, and the bottom of blending tank 8 passes through pipeline 18 and outlet valve 15, sand
Stock pump 12, hand-operated valve 22 connect, and are connected respectively with two tops of settling tank 9；It is provided with two settling tanks 9 with pipe
The pipette 21 of road pump, manually valve 22 merges supernatant liquid is transported in centrifugal pump 20 two groups of pipette 21, and passes through
Liquid is pumped into fluid reservoir 10 by the centrifugal pump 20 being fixed on operating platform 2 from the top of fluid reservoir 10；The settling tank 9
Interior lower sediment delivers to membrane pump via the outlet valve 15 of bottom and filter press handles to obtain solid residue, and filter liquor is determined
Phase is recycled to fluid reservoir 10；Liquid in the fluid reservoir 10 is connected via the outlet valve 15 of bottom with pipeline 18, centrifugal pump 20,
And liquid is transmitted back in blending tank 8 and recycled；Be provided with electric cabinet 23 on the operating platform 2, the electric cabinet 23 with
Reductor 11, lift, centrifugal pump 20, mortar pump 12, membrane pump, the connection of filter press electric signal.
Two peep holes 17 are symmetrically arranged with the blending tank 8, for observing the reactiveness in blending tank 8；It is described
Blending tank 8, settling tank 9, the top of fluid reservoir 10 are provided with manhole 16, the center line of manhole 16 and blending tank 8, settling tank 9,
Angle between the center line of fluid reservoir 10 is 30 degree.
The mortar pump 12, membrane pump, filter press are fixedly installed on basic unit 1.
The liquid from blending tank 8 to fluid reservoir 10, from settling tank 9 to fluid reservoir 10 and from fluid reservoir 10 to blending tank
8, it is each equipped with the mortar pump 12 with polyethylene-lined.
The utility model concrete operation step is：As shown in fig. 1, solid material adds blending tank 8, in stirring condition
Under, after being well mixed with liquid, by the pump of mortar pump 12 into settling tank 9, solidliquid mixture reacts layering in settling tank 9,
Upper strata is solution, and the pipeline by the pipette 21 of the upper end of settling tank 9 is pumped to fluid reservoir 10；Lower floor is sediment, by heavy
Outlet valve 15, the pipeline pump to filter press of the lower port of shallow lake tank 9；After press filtration, solid residue is obtained, filtrate is by filter press
Plastic tank stores, regular pump to fluid reservoir 10；When producing again, by solution pump in fluid reservoir 10 to first blending tank 8, flow
Meter can read the volume being pumped into, while read the concentration of solution in fluid reservoir 10 in the wall of fluid reservoir 10, calculate maintenance accordingly
The quality of solute is added needed for stoste bulk concentration again.
Relevant configured parameter is as follows：
1. the volume V=11000L of blending tank 8, actual load 8500L；
2. two settling tanks 9 and a fluid reservoir 10, each volume are V=11000L, each actual load 8500L；
3. the motor power P=18.5kw of reductor 11；
4. agitating paddle frequency control, the range of speeds is 0-29rpm；
5. the tank body of blending tank 8 is rolled using the Q235A materials of 12mm thickness, settling tank 9 and fluid reservoir 10 use 8mm thickness
Q235A materials roll；
6. inner tank wall pressure lining PU5mm is thick, agitating paddle winding polytetrafluoroethylene (PTFE) 4mm is thick, agitating shaft and other connect with material
Tactile parts spraying polytetrafluoroethylene (PTFE) 1mm；
7. blowing uses the pipe fitting of PPR materials；
8. the model UHB-ZK80/50-20 polyethylene-lineds of mortar pump 12, every motor power 11kw.
By above-mentioned specific embodiment, the beneficial effects of the utility model are：Using double-decked platform formula structure, blending tank,
Settling tank, fluid reservoir prismatic lay-out, configuration membrane pump, filter press, centrifugal pump, liquid level gauge carry out the closed solid-liquid reaction of metering-type and
Separation, not only enormously simplify operation but also liquid recycles in air-tight state, greatly improve the service efficiency of material；Can
To realize large-scale continuous production, while whole process is in air-tight state, realizes separation of solid and liquid and utilization and recycle, green economy ring
Protect, production efficiency is high.
The foregoing description of the disclosed embodiments, professional and technical personnel in the field are enable to realize or new using this practicality
Type.A variety of modifications to these embodiments will be apparent for those skilled in the art, determine herein
The General Principle of justice can be realized in other embodiments in the case where not departing from spirit or scope of the present utility model.Cause
This, the utility model is not intended to be limited to the embodiments shown herein, and is to fit to and principles disclosed herein
The most wide scope consistent with features of novelty.
Claims (5)
- A kind of 1. metering-type totally-enclosed solid-liquid reaction device, it is characterised in that including basic unit, operating platform, guardrail, support column, Staircase, lifting platform, tank bracket, blending tank, settling tank, fluid reservoir, reductor, mortar pump, agitator, liquid level gauge, outlet valve, people Hole, peep hole, pipeline, liquid inlet, centrifugal pump, pipette, hand-operated valve, electricity case；Consolidated in the basic unit by more support columns Surely rectangle, operating platform with guardrail are provided with, is fixedly installed respectively by multiple tank brackets on the operating platform One blending tank, two settling tanks and a fluid reservoir；The blending tank, settling tank and fluid reservoir configure in prismatic；The behaviour Make to be provided with staircase and lifting platform between platform and basic unit, the manhole for launching solid is provided with the blending tank and is used for Quantitatively add the liquid-entering hole of liquid；Reductor is provided with the top of the blending tank, and agitator is provided with by reductor driving； The blending tank side is equipped with passes through pipeline and discharging by the liquid level gauge of PU transparent pipes sign scale, the mixing pot bottom Valve, mortar pump, hand-operated valve connection, and connected respectively with the top of two settling tanks；It is provided with two settling tanks with pipe The pipette of road pump, manually supernatant liquid is transported in centrifugal pump two groups of pipette by valve merging, and by being fixed on behaviour Liquid is pumped into fluid reservoir by the centrifugal pump made on platform at the top of fluid reservoir；Lower sediment in the settling tank via The outlet valve of bottom delivers to membrane pump and filter press handles to obtain solid residue, and filter liquor is periodically recycled into fluid reservoir；Institute The liquid stated in fluid reservoir is connected via the outlet valve of bottom with pipeline, centrifugal pump, and liquid is transmitted back in blending tank and circulated Use；Electric cabinet, the electric cabinet and reductor, lift, centrifugal pump, mortar pump, barrier film are provided with the operating platform Pump, the connection of filter press electric signal.
- 2. a kind of metering-type totally-enclosed solid-liquid reaction device according to claim 1, it is characterised in that on the blending tank Two peep holes are symmetrically arranged with, for observing the reactiveness in blending tank；The blending tank, settling tank, fluid reservoir top Manhole is provided with, the angle between people's centerline hole and blending tank, settling tank, fluid reservoir center line is 30 degree.
- A kind of 3. metering-type totally-enclosed solid-liquid reaction device according to claim 1, it is characterised in that the mortar pump, Membrane pump, filter press are fixedly installed on basic unit.
- 4. a kind of metering-type totally-enclosed solid-liquid reaction device according to claim 1, it is characterised in that the liquid is from mixed Close tank to fluid reservoir, from settling tank to fluid reservoir and from fluid reservoir to blending tank, be each equipped with carry polyethylene-lined sand Stock pump.
- A kind of 5. metering-type totally-enclosed solid-liquid reaction device according to claim 1, it is characterised in that the blending tank, The thickness that settling tank, the inner tank wall pressure of fluid reservoir serve as a contrast PU is no less than 3mm；Agitating paddle winding polytetrafluoroethyl-ne on the agitator The thickness of alkene is no less than 3mm；The agitating shaft of the agitator and other parts contacted with material spray polytetrafluoroethylene (PTFE) Thickness is no less than 1mm；The pipeline uses PPR material pipe fittings.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720327737.3U CN206980702U (en) | 2017-03-30 | 2017-03-30 | A kind of metering-type totally-enclosed solid-liquid reaction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720327737.3U CN206980702U (en) | 2017-03-30 | 2017-03-30 | A kind of metering-type totally-enclosed solid-liquid reaction device |
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| Publication Number | Publication Date |
|---|---|
| CN206980702U true CN206980702U (en) | 2018-02-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720327737.3U Expired - Fee Related CN206980702U (en) | 2017-03-30 | 2017-03-30 | A kind of metering-type totally-enclosed solid-liquid reaction device |
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| CN (1) | CN206980702U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116553410A (en) * | 2023-07-11 | 2023-08-08 | 涉县津东经贸有限责任公司 | High-pressure reaction kettle assembly system |
-
2017
- 2017-03-30 CN CN201720327737.3U patent/CN206980702U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116553410A (en) * | 2023-07-11 | 2023-08-08 | 涉县津东经贸有限责任公司 | High-pressure reaction kettle assembly system |
| CN116553410B (en) * | 2023-07-11 | 2023-09-05 | 涉县津东经贸有限责任公司 | High-pressure reaction kettle assembly system |
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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: 20180202 Address after: 518052 Guangdong city of Shenzhen province Qianhai Shenzhen Hong Kong cooperation zone before Bay Road No. 1 building 201 room A (located in Shenzhen Qianhai business secretary Co. Ltd.) Patentee after: Shenzhen Fuwei new energy Co. Ltd. Address before: No. 2, No. 2, Jianye Road, high and New Technology Industrial Park, Changshu economic and Technological Development Zone, Changshu, Jiangsu Patentee before: Jiangsu strong Amperex Technology Limited |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180518 Address after: 215000 1 Building 2, Jianye Road, high tech Industrial Park, Changshu economic and Technological Development Zone, Suzhou, Jiangsu Patentee after: Jiangsu strong Amperex Technology Limited Address before: 518052 Room 201, building A, No. 1, Qian Wan Road, Qianhai Shenzhen Hong Kong cooperation zone, Shenzhen, Guangdong (Shenzhen Qianhai business secretary Co., Ltd.) Patentee before: Shenzhen Fuwei new energy Co. Ltd. |
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| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180209 Termination date: 20210330 |
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| CF01 | Termination of patent right due to non-payment of annual fee |