CN205205059U - Plain processing continuous production line that adsorbs of short nature of urine - Google Patents
Plain processing continuous production line that adsorbs of short nature of urine Download PDFInfo
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- CN205205059U CN205205059U CN201520903682.7U CN201520903682U CN205205059U CN 205205059 U CN205205059 U CN 205205059U CN 201520903682 U CN201520903682 U CN 201520903682U CN 205205059 U CN205205059 U CN 205205059U
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Abstract
The utility model discloses a plain processing conitnuous production line that adsorbs of the short nature of urine belongs to chemical products processing technology field, its characterized in that: appear jar, a filter press, ultrafiltration buffer tank, milipore filter subassembly system, alcohol gunbarrel, the 2nd filter press and vacuum stoving case including absorption article elution jar, van -type pressure filter, foreign protein matter. By comparing with the prior art, the loader axle automatic supporting device has advantages of simple structure and reasonable design.
Description
Technical field
The utility model relates to a kind of Menotropins production unit, particularly kaolin absorbent articles processing continuous production line in a kind of Menotropins production process.
Background technology
At present, the main filtration equipment of Menotropins kaolin absorbent articles machining production line is whizzer, but separate unit whizzer filtration efficiency is low, filtration velocity is slow, and power consumption is many, want to improve production capacity, can only, by increasing whizzer quantity, equipment cost can be made like this to improve, the corresponding increasing of running cost, and filtration efficiency is low, the production cycle is long; This production line is after alcohol precipitation operation, during product separation, utilize Büchner funnel suction filtration product separation, but due to its limited filtering capacity, the lower sediment liquid after leaving standstill can only be separated, supernatant liquor can only fall in siphon, portioned product in supernatant liquor can lose, practice display, and efficiency is too low, and throughput is difficult to improve, the expansion of meeting limit production scale, needs in production process, repeatedly with acetone, ether dehydration, can increase cost like this, and acetone, ether are precursor chemicals, be not easy to management.So, be badly in need of one kaolin absorbent articles processing continuous production line in Menotropins production process.
Utility model content
Technical assignment of the present utility model is for above the deficiencies in the prior art, provides a kind of Menotropins to adsorb processing tinuous production.
The technical scheme in the invention for solving the technical problem is: a kind of Menotropins absorption processing tinuous production, is characterized in that: comprise absorbent articles wash-out tank, chamber-type press filter, heteroproteins precipitation tank, the first plate-and-frame filter press, ultrafiltration surge tank, hyperfiltration membrane assembly system, alcohol precipitation tank, the second plate-and-frame filter press and vacuum drying box, the outlet of described absorbent articles wash-out tank is connected with the first pneumatic pump and chamber-type press filter successively by pipeline, the outlet of described chamber-type press filter separates out tank with heteroproteins successively by pipeline, second pneumatic pump is connected with the first plate-and-frame filter press, the outlet of the first described plate-and-frame filter press by pipeline successively with ultrafiltration surge tank, 3rd pneumatic pump is connected with hyperfiltration membrane assembly system, the outlet of described hyperfiltration membrane assembly system by pipeline successively with alcohol precipitation tank, 4th pneumatic pump is connected with the second plate-and-frame filter press, the second described plate-and-frame filter press outlet is connected with dirty alcohol container, be provided with floating ball lever meter in described ultrafiltration surge tank, described floating ball lever meter is connected with the first magnetic valve by circuit, and the first magnetic valve is connected with the air inlet port of the second pneumatic pump.
Above-mentioned heteroproteins is separated out tank feeding mouth and is connected glacial acetic acid solution tank by the second magnetic valve, heteroproteins is separated out in tank and is provided with online pH meter, online pH meter is connected with the second electromagnetic valve circuit, and the second magnetic valve and compressed-air line and operated pneumatic valve are linked in sequence.
Above-mentioned hyperfiltration membrane assembly system is rolled membrane module.
Compared with prior art, the utility model has following outstanding beneficial effect:
1, utilize the utility model to produce, can greatly enhance productivity, reduce production energy consumption, shorten the production cycle, save artificial, reduce production cost;
2, utilize the utility model to produce, can reduce in process of production and use acetone, ether etc. to dewater, be convenient to manage acetone, ether precursor chemicals, decrease potential loss risk.
3, the utility model utilizes the first plate-and-frame filter press by complete for foreign protein lye disposable filtering, need not repeatedly can dismantle, and reduces evaporating, emitting, dripping or leaking of liquid or gas in production process.
4, the Menotropins kaolin absorbent articles of the utility model production is after alcohol precipitation, and by the second plate-and-frame filter press collecting by filtration product throw out, complete soln after alcohol precipitation can disposablely filter by the second plate-and-frame filter press, reduces product loss.
Accompanying drawing explanation
Fig. 1 is production line schema of the present utility model.
Embodiment
Below in conjunction with specification drawings and specific embodiments, the utility model is further illustrated.
As shown in Figure 1, the utility model comprises absorbent articles wash-out tank 1, chamber-type press filter 3, heteroproteins precipitation tank 4, first plate-and-frame filter press 6, ultrafiltration surge tank 7, hyperfiltration membrane assembly system 9, alcohol precipitation tank 10, second plate-and-frame filter press 12 and vacuum drying box 13.
The outlet of described absorbent articles wash-out tank 1 is connected with the first pneumatic pump 2 and chamber-type press filter 3 successively by pipeline, the outlet of described chamber-type press filter 3 separates out tank 4 with heteroproteins successively by pipeline, second pneumatic pump 5 is connected with the first plate-and-frame filter press 6, the outlet of the first described plate-and-frame filter press 6 by pipeline successively with ultrafiltration surge tank 7, 3rd pneumatic pump 8 is connected with hyperfiltration membrane assembly system 9, the outlet of described hyperfiltration membrane assembly system 9 by pipeline successively with alcohol precipitation tank 10, 4th pneumatic pump 11 is connected with the second plate-and-frame filter press 12, the second described plate-and-frame filter press 12 outlet is connected with dirty alcohol container, and vacuum drying box 13 is used for throw out in dry second plate-and-frame filter press 12 sheet frame, Menotropins kaolin absorbent articles is after alcohol precipitation, and by the second plate-and-frame filter press 12 collecting by filtration product throw out, complete soln after alcohol precipitation can disposablely filter by the second plate-and-frame filter press 12, reduces product loss.
In described ultrafiltration surge tank 7, floating ball lever meter 14 is installed, described floating ball lever meter 14 is connected with the first magnetic valve by circuit, first magnetic valve is connected with the air inlet port of the second pneumatic pump 5, the first described magnetic valve can control the second pneumatic pump 5 propulsion source pressurized air, thus control the second pneumatic pump 5, control the first plate-and-frame filter press 6 and filter filtrate, thus the first plate-and-frame filter press 6 can be controlled to ultrafiltration surge tank 7 feed, realize carrying out Automatic-feeding to ultrafiltration surge tank 7.
Fill basic solution in described absorbent articles wash-out tank 1, described basic solution by concentration be 25% ammonia soln and pure water configure form.Described heteroproteins is separated out tank 4 feeding mouth and is connected glacial acetic acid solution tank by the second magnetic valve, described glacial acetic acid solution by concentration be 50% glacial acetic acid solution and pure water configure and form.In prioritization scheme, described heteroproteins is separated out in tank 4 and is provided with online pH meter, described online pH meter is connected with the second electromagnetic valve circuit, second magnetic valve and compressed-air line and operated pneumatic valve are linked in sequence, second magnetic valve can control compressed-air line, operated pneumatic valve on compressed air pipe line traffic control glacial acetic acid solution tank, can automatically control to add Glacial acetic acid, thus the pH value of regulator solution, the structure of described online pH meter, install, parameter setting and data transmission are resolved and are prior art, model difference is bought according to market, its peripheral hardware connects different, again be not repeated.The alcohol that concentration is 95% is filled in described alcohol precipitation tank 10.
Hyperfiltration membrane assembly system 9 in the present embodiment is specially rolled membrane module.
Operating process is as follows: first poured into by the kaolin containing Menotropins in absorbent articles wash-out tank 1, then stir through opening, carry out ammoniacal liquor wash-out, then suck chamber-type press filter through the first pneumatic pump 2 to filter, filtrate is sent into heteroproteins precipitation tank 4 and carry out foreign protein precipitation process, then send into the first plate-and-frame filter press 6 through the second pneumatic pump 5 to filter, ultrafiltration surge tank 7 will be sucked by the 3rd pneumatic pump 8 and hyperfiltration membrane assembly system 9 carries out ultrafiltration removal of impurities from the filtrate in the first plate-and-frame filter press 6, then filtrate is sent into alcohol precipitation tank 10 and carry out alcohol precipitation, then filtered by the second plate-and-frame filter press 12, product is sent into vacuum drying box 13 vacuum-drying.
It should be noted that; particular of the present utility model has been described in detail the utility model; for a person skilled in the art, the various apparent change carried out it when not deviating from spirit and scope of the present utility model is all within protection domain of the present utility model.
Claims (3)
1. a Menotropins absorption processing tinuous production, is characterized in that: comprise absorbent articles wash-out tank, chamber-type press filter, heteroproteins precipitation tank, the first plate-and-frame filter press, ultrafiltration surge tank, hyperfiltration membrane assembly system, alcohol precipitation tank, the second plate-and-frame filter press and vacuum drying box, the outlet of described absorbent articles wash-out tank is connected with the first pneumatic pump and chamber-type press filter successively by pipeline, the outlet of described chamber-type press filter separates out tank with heteroproteins successively by pipeline, second pneumatic pump is connected with the first plate-and-frame filter press, the outlet of the first described plate-and-frame filter press by pipeline successively with ultrafiltration surge tank, 3rd pneumatic pump is connected with hyperfiltration membrane assembly system, the outlet of described hyperfiltration membrane assembly system by pipeline successively with alcohol precipitation tank, 4th pneumatic pump is connected with the second plate-and-frame filter press, the second described plate-and-frame filter press outlet is connected with dirty alcohol container, be provided with floating ball lever meter in described ultrafiltration surge tank, described floating ball lever meter is connected with the first magnetic valve by circuit, and the first magnetic valve is connected with the air inlet port of the second pneumatic pump.
2. a kind of Menotropins absorption processing tinuous production according to claim 1, it is characterized in that: described heteroproteins is separated out tank feeding mouth and connected glacial acetic acid solution tank by the second magnetic valve, described heteroproteins is separated out in tank and is provided with online pH meter, described online pH meter is connected with the second electromagnetic valve circuit, and the second magnetic valve and compressed-air line and operated pneumatic valve are linked in sequence.
3. a kind of Menotropins absorption processing tinuous production according to claim 1, is characterized in that: described hyperfiltration membrane assembly system is rolled membrane module.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520903682.7U CN205205059U (en) | 2015-11-13 | 2015-11-13 | Plain processing continuous production line that adsorbs of short nature of urine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520903682.7U CN205205059U (en) | 2015-11-13 | 2015-11-13 | Plain processing continuous production line that adsorbs of short nature of urine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205205059U true CN205205059U (en) | 2016-05-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520903682.7U Active CN205205059U (en) | 2015-11-13 | 2015-11-13 | Plain processing continuous production line that adsorbs of short nature of urine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205205059U (en) |
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2015
- 2015-11-13 CN CN201520903682.7U patent/CN205205059U/en active Active
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |