CN207738679U - 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate is separated by solid-liquid separation and wash mill - Google Patents
2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate is separated by solid-liquid separation and wash mill Download PDFInfo
- Publication number
- CN207738679U CN207738679U CN201721811281.4U CN201721811281U CN207738679U CN 207738679 U CN207738679 U CN 207738679U CN 201721811281 U CN201721811281 U CN 201721811281U CN 207738679 U CN207738679 U CN 207738679U
- Authority
- CN
- China
- Prior art keywords
- washing machine
- liquid
- tank
- propen
- chloromethyl
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Polyesters Or Polycarbonates (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
The utility model belongs to pharmaceutical technology field, and in particular to a kind of separation of solid and liquid and wash mill of 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate.The separation of solid and liquid and wash mill of 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate described in the utility model, including filtration washing machine, salt-forming reaction tank, washing liquid tank, mother liquor tank and washing mother liquor holding tank；The discharge port of salt-forming reaction tank is connect with the feed inlet of filtration washing machine, the discharge port of washing liquid tank is connect with the feed inlet of filtration washing machine, the feed inlet of mother liquor tank is connected with the liquid outlet of filtration washing machine, and the feed inlet for washing mother liquor holding tank is connected with the liquid outlet of filtration washing machine.2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate described in the utility model is separated by solid-liquid separation and wash mill, it is scientific and reasonable, structure design is simple, by mother liquor press filtration it is complete after, then with cleaning solution 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate solid is washed, integrate filtering and washing, operating environment is improved, the process time is shortened, is improved work efficiency, reduce energy consumption, with good economic efficiency and social benefit.
Description
Technical field
The utility model is related to a kind of separation of solid and liquid of 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate and wash mills, belong to pharmaceutical equipment technology neck
Domain.
Background technology
2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate is a kind of polymer that will not be absorbed by the body, and is free of metal and calcium.It carries multiple amidos,
It is connect with polymer backbone by a carbon atom.These amidos can be protonated in enteron aisle inside points, and with ion exchange and hydrogen bond
It is combined with phosphoric acid molecules.2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate reduces its absorption, reaching reduces serium inorganic phosphorus concentration by combining the phosphorus in gastrointestinal tract
Effect.
It is domestic at present and in the world in 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate production, it is to carry out after the completion of 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate reaction mostly
It is centrifuged repeatedly, washs, complex process, the complex for operation step and time is longer, therefore in order to shorten the process time and improve environment
Friendliness simultaneously makes up the market vacancy, and it is very necessary to develop the process unit being simple to operate and friendly to environment.
Utility model content
According to the above-mentioned deficiencies of the prior art, the technical problems to be solved in the utility model is：A kind of carbonic acid department dimension is provided
The separation of solid and liquid and wash mill for drawing nurse can shorten the production cycle, improve working efficiency.
The separation of solid and liquid and wash mill of 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate described in the utility model, including filtration washing machine, at salt
Retort, washing liquid tank, mother liquor tank and washing mother liquor holding tank；The discharge port of salt-forming reaction tank is logical with the feed inlet of filtration washing machine
Feeding pipe connection is crossed, the discharge port of washing liquid tank is connect with the feed inlet of filtration washing machine by feeding pipe, mother liquor tank
Feed inlet is connected with the liquid outlet of filtration washing machine, and the feed inlet for washing mother liquor holding tank is connected with the liquid outlet of filtration washing machine.
The material that salt-forming reaction tank generates enters filtration washing machine by feeding pipe and is filtered, and the mother liquor filtered out is logical
The liquid outlet for crossing filtration washing machine enters mother liquor tank, and 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate solid then stays in filtration washing machine；Filtering is completed
Afterwards, cleaning solution enters filtration washing machine by feeding pipe and is washed to 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate solid；After washing, carbonic acid
Sevelamer is discharged from filtration washing machine.
The filtration washing machine is connected with pressure gas cylinder, and pressure gas cylinder can be adjusted in filtration washing machine
Mother liquor in filtration washing machine is pressed into mother liquor tank by gas pressure by liquid outlet.
The filtration washing machine is connected with drier, drier to the 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate solid after filtration washing into
Row drying.
The filtration washing machine includes driving motor, and driving motor is located at filtration washing machine top, for agitating shaft with stir
It mixes paddle and power is provided, driving motor is connect by agitating shaft with agitating paddle, and filtration washing machine is internally provided with filter plate, and filter plate setting exists
Filtration washing motor spindle, filter plate is as filter medium, and under the action of pressure difference, solid material is retained by filter plate, and mother liquor from
Filter plate passes through, to achieve the purpose that separation of solid and liquid.
Possessed advantageous effect is the utility model compared with prior art：
2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate described in the utility model is separated by solid-liquid separation and wash mill, and scientific and reasonable, structure design is simple,
By mother liquor press filtration it is complete after, then with cleaning solution 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate solid is washed, integrates filtering and washing, improve
Operating environment shortens the process time, improves work efficiency, and reduces energy consumption, with good economic efficiency and social effect
Benefit.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the structural schematic diagram of filtration washing machine.
In figure：1, filtration washing machine；2, salt-forming reaction tank；3, washing liquid tank；4, mother liquor tank；5, drier；6, high pressure gas
Body steel cylinder；7, mother liquor holding tank is washed；8, feeding pipe；9, filtration washing machine discharge port；10, liquid outlet；11, filter plate；12, it stirs
Paddle；13, agitating shaft；14, driving motor.
Specific implementation mode
The utility model is described further with reference to embodiment：
The separation of solid and liquid and wash mill of 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate described in the utility model, including filtration washing machine 1, at salt
Retort 2, washing liquid tank 3, mother liquor tank 4 and washing mother liquor holding tank 7；The discharge port of salt-forming reaction tank 2 passes through feeding pipe 8 and mistake
The feed inlet of filter washing machine 1 connects, and the discharge port of washing liquid tank 3 is connected by the feed inlet of feeding pipe 8 and filtration washing machine 1
It connects, the feed inlet of mother liquor tank 4 is connected with the liquid outlet 10 of filtration washing machine 1, washs the feed inlet and filtration washing of mother liquor holding tank 7
The liquid outlet 10 of machine 1 is connected.Filtration washing machine discharge port 9 is connected with drier 5, and filtration washing machine 1 is also associated with high pressure gas
Steel cylinder 6.Filtration washing machine 1 includes driving motor 14, and driving motor 14 is located at 1 top of filtration washing machine, by agitating shaft 13 and
Agitating paddle 12 connects, and filtration washing machine 1 is internally provided with filter plate 11.
The course of work or operation principle of the utility model：
By 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate indentation filtration washing machine 1 obtained by the reaction in salt-forming reaction tank 2, by filtration washing machine 1
Agitating paddle 12 rises to a high position, and it is 0.25MPa to open pressure gas cylinder 6 and adjust gas pressure in filtration washing machine 1, and mother liquor is led to
It crosses liquid outlet 10 and is pressed into mother liquor tank 4 until no liquid outflow, drops to surface of material by agitating paddle 12 and open, material is flattened
Afterwards, stop stirring, press filtration 0.5-1 hours.After the completion of filtering, pressure in filtration washing machine 1 is emptied, it will be in washing liquid tank 3
Cleaning solution is put into filtration washing machine 1, opens agitating paddle 12, and mashing washing forms washing mother liquor for 1 hour, after washing, incited somebody to action
The agitating paddle 12 of filter washing machine 1 rises to a high position, opens gas pressure in the adjusting filtration washing of pressure gas cylinder 6 machine 1 and is
Agitating paddle 12 is dropped to material table by 0.25MPa at this time by washing mother liquor indentation washing mother liquor holding tank 7 until no liquid flows out
Face is simultaneously opened, and after material is flattened, stops stirring, press filtration 0.5-1 hours.After washing, pressure in filtration washing machine 1 is arranged
Sky transfers the material into drying box 5, sets the temperature of drying box 5 as 60-70 DEG C, drying 24-30 hours obtains carbonic acid department
Wella nurse.
Claims (4)
1. the separation of solid and liquid and wash mill of a kind of 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate, it is characterised in that：Including filtration washing machine (1), at salt
Retort (2), washing liquid tank (3), mother liquor tank (4) and washing mother liquor holding tank (7)；The discharge port of salt-forming reaction tank (2) and filtering
The feed inlet of rinsing maching (1) connects, and the discharge port of washing liquid tank (3) is connect with the feed inlet of filtration washing machine (1), mother liquor tank
(4) feed inlet is connected with the liquid outlet (10) of filtration washing machine (1), the feed inlet and filtration washing of washing mother liquor holding tank (7)
The liquid outlet (10) of machine (1) is connected.
2. the separation of solid and liquid and wash mill of 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate according to claim 1, it is characterised in that：The mistake
Filter washing machine (1) is connected with pressure gas cylinder (6).
3. the separation of solid and liquid and wash mill of 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate according to claim 1, it is characterised in that：The mistake
Filter washing machine (1) is connected with drier (5).
4. the separation of solid and liquid and wash mill of 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate according to claim 1, it is characterised in that：The mistake
Filter washing machine (1) includes driving motor (14), and driving motor (14) is connect by agitating shaft (13) with agitating paddle (12), crosses diafiltration
It washs machine (1) and is internally provided with filter plate (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721811281.4U CN207738679U (en) | 2017-12-21 | 2017-12-21 | 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate is separated by solid-liquid separation and wash mill |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721811281.4U CN207738679U (en) | 2017-12-21 | 2017-12-21 | 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate is separated by solid-liquid separation and wash mill |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207738679U true CN207738679U (en) | 2018-08-17 |
Family
ID=63119198
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721811281.4U Active CN207738679U (en) | 2017-12-21 | 2017-12-21 | 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate is separated by solid-liquid separation and wash mill |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207738679U (en) |
-
2017
- 2017-12-21 CN CN201721811281.4U patent/CN207738679U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102583453B (en) | Industrial method for producing battery-grade lithium carbonate or high-purity lithium carbonate | |
| CN101735372B (en) | Chelate resin and production method and application thereof | |
| CN107055577B (en) | A kind of method and device for extracting superpurity lithium carbonate from industrial level lithium carbonate | |
| CN103626836A (en) | Extraction process for polypeptide from waste liquid obtained in production of crude heparin sodium product | |
| CN105129852B (en) | The system that a kind of high-efficiency self-circulation wet method continuously prepares sodium dichromate | |
| WO2016145977A1 (en) | Enzymatic gelatin preparation process | |
| CN102626646B (en) | Device and method for recycling cobalt-manganese catalyst in oxidation section | |
| CN103466713B (en) | Low-grade manganese high-pressure process primary crystallization prepares Manganous sulfate monohydrate | |
| CN208617686U (en) | A kind of sludge resource, which crushes to be dried, utilizes device | |
| CN105152174B (en) | A kind of preparation method of high-purity white carbon | |
| CN207738679U (en) | 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate is separated by solid-liquid separation and wash mill | |
| CN218872211U (en) | Continuous production device for anti-dripping agent | |
| CN208512543U (en) | A kind of reaction kettle with cleaning function | |
| CN208097541U (en) | A kind of filtration washing drying device being separated by solid-liquid separation for peptizer DBD | |
| CN203625062U (en) | Titanium concentrate acidolysis residue recycling system | |
| CN107936160A (en) | 2-Propen-1-amine polymer with(chloromethyl)oxirane carbonate separation of solid and liquid and wash mill and method | |
| CN216172212U (en) | High-purity glycocyamine production system | |
| CN105565354A (en) | Preparation method of supported calcium hydroxide activated clay | |
| CN1155388A (en) | Method of extracting somatic protein from zymotic liquid or zymotic waste liquid | |
| CN108383142A (en) | A kind of method of secondary aluminium aluminium cinder resource metaplasia production aluminium oxide | |
| CN104151859B (en) | A kind of device of indigo Product recycling mixed base | |
| CN107099660A (en) | A kind of leaching of Rare Earth Production, alkali turn, excellent molten, removal of impurities and precipitation technique | |
| CN205398130U (en) | Carbide slag preparation industry naoh reaction unit | |
| CN101492543B (en) | Process for preparing granule chitosan | |
| CN205023875U (en) | System for sodium dichromate is prepared in succession to high -efficient self -loopa wet process |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |