CN201701900U - Liquid mixing machine used in chemical industry production - Google Patents
Liquid mixing machine used in chemical industry production Download PDFInfo
- Publication number
- CN201701900U CN201701900U CN2010201619162U CN201020161916U CN201701900U CN 201701900 U CN201701900 U CN 201701900U CN 2010201619162 U CN2010201619162 U CN 2010201619162U CN 201020161916 U CN201020161916 U CN 201020161916U CN 201701900 U CN201701900 U CN 201701900U
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- CN
- China
- Prior art keywords
- shaft
- liquid
- chemical industry
- industry production
- machine used
- 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.)
- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 25
- 239000000126 substance Substances 0.000 title claims abstract description 12
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 9
- 238000003756 stirring Methods 0.000 claims description 12
- 230000033001 locomotion Effects 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 29
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 8
- 239000001301 oxygen Substances 0.000 abstract description 8
- 229910052760 oxygen Inorganic materials 0.000 abstract description 8
- 239000007789 gas Substances 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 abstract 1
- 229910001873 dinitrogen Inorganic materials 0.000 abstract 1
- 229910001882 dioxygen Inorganic materials 0.000 abstract 1
- 229910052757 nitrogen Inorganic materials 0.000 description 14
- LRWZZZWJMFNZIK-UHFFFAOYSA-N 2-chloro-3-methyloxirane Chemical compound CC1OC1Cl LRWZZZWJMFNZIK-UHFFFAOYSA-N 0.000 description 3
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000006392 deoxygenation reaction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229930185605 Bisphenol Natural products 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
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- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model discloses a liquid mixing machine used in the chemical industry production, which comprises a mixing shaft capable of being supplied with a gas and a power device. During the operation process, the mixing shaft is supplied with nitrogen gas to remove oxygen gas from the liquid, thereby solving the technical problem of incomplete oxygen removal during the chemical industry production.
Description
Technical field
The utility model relates to a kind of liquid stirrers, especially for the liquid stirrers in the Chemical Manufacture.
Background technology
In Chemical Manufacture, it is addings of not wishing to have air that a lot of chemical reactions are arranged, because airborne oxygen can react with some chemical composition, thereby reduced the quality of finished product after the reaction, therefore, we need be toward supplying nitrogen in the liquid in the reactive tank, drive away the oxygen of the inside, in the process of supplying nitrogen, reactive tank is stirred, the one, can remove oxygen more fully, the 2nd, can allow compound fully react.For example, in the process of producing epoxy resin, need be miscible ECH (epoxychloropropane) and BPA (bis-phenol base propane), in this process, need remove the oxygen of the inside toward supplying nitrogen in BPA and the ECH mixture.Generally speaking, employing be with a wireway, be passed into mixed liquor bottom, supplying nitrogen.But so normally can cause removal oxygen insufficient.
The utility model content
The liquid stirrers that the utility model provides a kind of chemical industry to use can solve and remove the inadequate technical problem of oxygen.
A kind of liquid stirrers that is used for Chemical Manufacture, the power set that comprise shaft and stirring vane and can drive the shaft motion, stirring vane is positioned at an end of shaft, and shaft is for can at one end feeding the hollow tubular object that the other end of gas is discharged.
Power set link to each other with shaft, the motion of driving shaft, stirring vane is positioned at an end of shaft, and be in below the liquid level, feed nitrogen at the shaft other end, nitrogen just can be discharged from a liquid level end once, and shaft is stirring liquid in addition, the nitrogen that enters liquid will be stirred, thereby can improve the efficient of deoxygenation gas and can remove oxygen in the liquid more fully.
Description of drawings
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail.
Fig. 1 is the schematic diagram of the liquid stirrers used of a kind of chemical industry
The specific embodiment
Shown in Figure 1,5 is reactive tank, power set 1 link to each other with shaft 2 by transmission device 3, and drive shaft 2 motions, the liquid level that stirring vane 6 is positioned at an end of shaft 2 and is positioned at reactive tank 5 is below 4, shaft 2 is a hollow structure, can discharge from the end feeding nitrogen of shaft 2 and from the other end that is positioned in addition below the liquid level.
When in running order, power set 1 drive shaft 2 and stirring vane 6 stirs below liquid level, simultaneously shaft 2 are fed nitrogen, and nitrogen will be emerged with next end from the liquid level of shaft, the nitrogen of emerging can form bubble below liquid level, and can rise.The nitrogen bubble that rises can be stirred blade and smash, and forms very tiny bubble, and enters in the liquid uniformly along with stirring the liquid stream that forms, thereby has reached than using wireway directly toward sending nitrogen better effect below the liquid level.
The utility model can also be holed shaft 2 on the tube wall of the end that stirring vane 6 is arranged, make the nitrogen that feeds to discharge from these holes, has further increased the efficient of deoxygenation gas.
Claims (2)
1. liquid stirrers that is used for Chemical Manufacture, the power set that comprise shaft and stirring vane and can drive the shaft motion, stirring vane is positioned at an end of shaft, it is characterized in that described shaft is for can at one end feeding the hollow tubular object that the other end of gas is discharged.
2. the liquid stirrers that is used for Chemical Manufacture according to claim 1 is characterized in that, described shaft has the hole of can supplied gas discharging on the tube wall of the end that stirring vane is housed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201619162U CN201701900U (en) | 2010-04-16 | 2010-04-16 | Liquid mixing machine used in chemical industry production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201619162U CN201701900U (en) | 2010-04-16 | 2010-04-16 | Liquid mixing machine used in chemical industry production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201701900U true CN201701900U (en) | 2011-01-12 |
Family
ID=43439046
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201619162U Expired - Fee Related CN201701900U (en) | 2010-04-16 | 2010-04-16 | Liquid mixing machine used in chemical industry production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201701900U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102218279A (en) * | 2010-04-16 | 2011-10-19 | 南亚环氧树脂(昆山)有限公司 | Liquid stirrer for chemical production |
| CN102443350A (en) * | 2011-10-17 | 2012-05-09 | 西北农林科技大学 | Ventilated raw lacquer stirrer and operating method |
| CN103341336A (en) * | 2013-06-17 | 2013-10-09 | 济南卡博唐生物科技有限公司 | Stirrer of stirred tank |
| CN104828415A (en) * | 2015-04-29 | 2015-08-12 | 中煤科工集团武汉设计研究院有限公司 | Jet mixing coal slurry tank |
| CN106390841A (en) * | 2016-11-21 | 2017-02-15 | 郑州天舜电子技术有限公司 | Nutrient solution raw material anti-pollution mixing equipment used for biological medicine |
-
2010
- 2010-04-16 CN CN2010201619162U patent/CN201701900U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102218279A (en) * | 2010-04-16 | 2011-10-19 | 南亚环氧树脂(昆山)有限公司 | Liquid stirrer for chemical production |
| CN102443350A (en) * | 2011-10-17 | 2012-05-09 | 西北农林科技大学 | Ventilated raw lacquer stirrer and operating method |
| CN102443350B (en) * | 2011-10-17 | 2013-10-09 | 西北农林科技大学 | A ventilated lacquer mixer |
| CN103341336A (en) * | 2013-06-17 | 2013-10-09 | 济南卡博唐生物科技有限公司 | Stirrer of stirred tank |
| CN104828415A (en) * | 2015-04-29 | 2015-08-12 | 中煤科工集团武汉设计研究院有限公司 | Jet mixing coal slurry tank |
| CN106390841A (en) * | 2016-11-21 | 2017-02-15 | 郑州天舜电子技术有限公司 | Nutrient solution raw material anti-pollution mixing equipment used for biological medicine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110112 Termination date: 20130416 |