CN102078778A - Steam bubbling type PASP (polyaspartic acid) solution mixing tank - Google Patents
Steam bubbling type PASP (polyaspartic acid) solution mixing tank Download PDFInfo
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- CN102078778A CN102078778A CN2009102521290A CN200910252129A CN102078778A CN 102078778 A CN102078778 A CN 102078778A CN 2009102521290 A CN2009102521290 A CN 2009102521290A CN 200910252129 A CN200910252129 A CN 200910252129A CN 102078778 A CN102078778 A CN 102078778A
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- mixing tank
- solution mixing
- steam
- pasp
- liquid level
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Abstract
The invention discloses a steam bubbling type PASP (polyaspartic acid) solution mixing tank which comprises a dissolving tank body, a porous steam loop and a liquid level and temperature automatic control device; and 0.4Mpa steam bubbling stirring is adopted for replacing mechanical stirring. By utilizing the steam bubbling type PASP solution mixing tank, electrical energy can be saved, raw materials can be completely dissolved and uniformly mixed, and the liquid level and temperature can be controlled automatically.
Description
Technical field the present invention relates to chemical machinery, directly relates to the PASP solution mixing tank.
The present China of background technology is because the excessive common urea of using, nutrient is single, lack trace element, cause that clay fertilizer runs off, effect of increasing production is poor, destroy ecological environment, our company has researched and developed a kind of novel high-efficiency environment friendly urea, incorporates poly-aspartic-acid and various trace elements before the common urea granulation in the urine.The poly-aspartic acid solution needs even mixed dissolution various trace elements, has designed a kind of steam bubble formula mixing channel.
Summary of the invention purpose of the present invention just provides a kind of steam bubble formula PASP solution mixing tank, improves dissolution velocity, mixes saves energy.
The object of the present invention is achieved like this: steam bubble formula PASP solution mixing tank, form by fluid bowl body, porous steam loop, liquid level and automatic temperature control.
As further scheme of the present invention, described fluid bowl body has feeding-in solid body mouth, liquid-inlet, thermometer boss, interface of the level gauge.
As further again scheme of the present invention, described porous steam loop annular diameter 1000mm, 20 of Ф 2mm fumaroles are bored on endless tube top.
As further again scheme of the present invention, liquid level and automatic temperature control thermometer boss connect thermal resistance, and operating desk is put auto-controlling apparatus, and liquid level gauge band float valve is connected with pump motor, realizes control automatically.Because the present invention replaces mechanical agitation with the form of steam bubble, so improved dissolution velocity, mixes, and has saved electric energy.
Appended drawings is a structural principle schematic diagram of the present invention, and the invention will be further described below in conjunction with accompanying drawing.
Specific embodiment accompanying drawing shows the structure of PASP solution mixing tank of the present invention, is made up of fluid bowl body 1, porous steam loop 2, liquid level and automatic temperature control 3; Described fluid bowl body 1 has feeding-in solid body mouth, liquid-inlet, thermometer boss, interface of the level gauge; Described porous steam loop 2 annular diameter 1000mm, 20 of Ф 2mm fumaroles are bored on endless tube top.Liquid level and automatic temperature control 3 thermometer bosses connect thermal resistance, and operating desk is put auto-controlling apparatus, and liquid level gauge band float valve is connected with pump motor, realize control automatically.
The course of work of the present invention: PASP liquid is entered in the groove by liquid-inlet 2, and the solid trace element is packed into by feeding-in solid body mouth 3 in the groove.Steam feeds steam ring pipe 5 by steam inlet pipe 4, and the aperture of 0.4Mpa steam above endless tube sprays, and the bubbling agitated liquid improves the purpose that dissolving mixes.Post-decompression steam is discharged from drain 9.The liquid that mixes is discharged by the lower end mixture export, and temperature and liquid level realize automatic control by automaton.
Claims (4)
1. a steam bubble formula PASP solution mixing tank is characterized in that: be made up of fluid bowl body (1), porous steam loop (2), liquid level and automatic temperature control (3).
2. steam bubble formula PASP solution mixing tank according to claim 1, it is characterized in that: described fluid bowl body (1) has feeding-in solid body mouth, liquid-inlet, thermometer boss, interface of the level gauge.
3. steam bubble formula PASP solution mixing tank according to claim 1 is characterized in that: described porous steam loop (2) annular diameter 1000mm, 20 of Ф 2mm fumaroles are bored on endless tube top.
4. steam bubble formula PASP solution mixing tank according to claim 1 is characterized in that: liquid level and automatic temperature control (3) thermometer boss connects thermal resistance, and operating desk is put auto-controlling apparatus, and liquid level gauge band float valve is connected with pump motor, realizes control automatically.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009102521290A CN102078778A (en) | 2009-12-01 | 2009-12-01 | Steam bubbling type PASP (polyaspartic acid) solution mixing tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009102521290A CN102078778A (en) | 2009-12-01 | 2009-12-01 | Steam bubbling type PASP (polyaspartic acid) solution mixing tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102078778A true CN102078778A (en) | 2011-06-01 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009102521290A Pending CN102078778A (en) | 2009-12-01 | 2009-12-01 | Steam bubbling type PASP (polyaspartic acid) solution mixing tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102078778A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102755852A (en) * | 2012-07-30 | 2012-10-31 | 济南大学 | Gas explosion-preventive spiral spray pipe bubbling stirring apparatus |
| CN105413550A (en) * | 2015-12-02 | 2016-03-23 | 马鞍山钢铁股份有限公司 | Sludge blending heating device |
-
2009
- 2009-12-01 CN CN2009102521290A patent/CN102078778A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102755852A (en) * | 2012-07-30 | 2012-10-31 | 济南大学 | Gas explosion-preventive spiral spray pipe bubbling stirring apparatus |
| CN102755852B (en) * | 2012-07-30 | 2014-04-09 | 济南大学 | Gas explosion-preventive spiral spray pipe bubbling stirring apparatus |
| CN105413550A (en) * | 2015-12-02 | 2016-03-23 | 马鞍山钢铁股份有限公司 | Sludge blending heating device |
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Legal Events
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|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20110601 |