CN1122144C - Producing method of high-speed vaporized boiling point-free organic matter flow without decomposition - Google Patents
Producing method of high-speed vaporized boiling point-free organic matter flow without decomposition Download PDFInfo
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- CN1122144C CN1122144C CN98110753A CN98110753A CN1122144C CN 1122144 C CN1122144 C CN 1122144C CN 98110753 A CN98110753 A CN 98110753A CN 98110753 A CN98110753 A CN 98110753A CN 1122144 C CN1122144 C CN 1122144C
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- boiling point
- material flow
- high speed
- organic substance
- decomposition
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- Processes Of Treating Macromolecular Substances (AREA)
Abstract
The present invention relates to a method for a boiling point-free organic substance to produce high-speed vaporized material flow in a molecule state or a highly dispersive state under the condition of no decomposition. The method has five kinds of different specific ways; the method is mainly implemented in the way that a boiling point-free organic substance is heated and sprayed at the temperature which is below the heat decomposition point of the organic substance and over the boiling point of a solvent by tens of degrees.
Description
No boiling point organic substance produces the method for high speed carburetion (molecular state or high degree of dispersion attitude) material flow under no decomposition condition.It is that gas phase is received a kind of implementation methods of micron technology, in order to improve the organic usability of former no boiling point.Nanometer technology history is also very short, and nobody was engaged in the gas phase nano Study on Technology, so there is not documents.
The organic substance of (under the normal pressure) no boiling point will obtain high speed carburetion (molecular state or high degree of dispersion attitude) material flow, does not allow former material that thermolysis is arranged again, and is essential with special method:
1, will not have the boiling point organic substance and be dissolved in low-pressure liquefied vapour as compression natural gas or natural oil vapour, and utilize columniform simple and easy injection moulding cigarette lighter type device, the device size is decided by application target, after packing into, one opens, and just can obtain not having the high speed carburetion material flow of decomposition, and mixing certainly has solvent molecule.
2, the initial temperature of the organic thermolysis of (under the normal pressure) no boiling point, normal～250 ℃ approximately (if be lower than 250 ℃ then can corresponding adjustment this method the heat supply source temperature).Select preferably insoluble or be slightly soluble in liquefied petroleum gas, the flash-point above solvent of tens degree that is above the boiling point, and no boiling point organic substance solubility is preferably in more than 1/3, with the reinject liquefied petroleum gas of 1-15% of solution injection injection moulding earlier cigarette lighter type device.The device bag as dried mud base tube, the tube etc. of making pottery, and leaves the air adiabatic layer with heat insulation layer; Make the steam flow fairlead stretch out base portion 1-1.5cm, put the profiled metal paillon foil to strengthen the absorption or the transmission of heat, then flow of solution is after the fairlead that is heated in advance more than the solvent boiling point, certainly also be decided by the fairlead bore, one opens, just can obtain not having the high speed carburetion material flow of decomposition, mixing certainly has solvent and natural gas molecule.For obtaining the bigger vaporization material flow of total amount, device can be used the steam flow fairlead more than 2.
But 3, in 2, introduce even add earlier the means of melting missible oil of the water of 1/3-1/2, also can obtain diameter less than 0.1 micron the no decomposing organic matter material flow of high speed gasification.
4, in 2, introduce even add colloidal powder and the colloidal suspending agent means of water 1/3-1/2, also can obtain the no decomposing organic matter material flow of high speed gasification of diameter 0.1-1 micron.
5, in 2, introduce even add earlier the means of the water and milk voltinism missible oil of 1/3-1/2, the also feasible no boiling point organic substance material flow of high speed gasification to diameter 0.1-1 micron.
2,3,4,5, all taked heater means, just as not heating the no decomposing organic matter material flow that can only obtain the rough segmentation divergence, both have principle distinction at performance.
Claims (5)
1, a kind ofly produces the method that the organic nothing of no boiling point under the normal pressure is decomposed high speed carburetion molecular state or high degree of dispersion attitude material flow, it is characterized in that: will not have the boiling point organic substance and be dissolved in low-pressure liquefied vapour as compression natural gas or natural oil vapour, utilize simple and easy injection moulding cigarette lighter type device, the device size is decided by application target, after packing into, one opens, and just can obtain not having the high speed carburetion molecular state material flow of decomposition, and mixing certainly has solvent molecule.
2, a kind ofly produce the method that the organic nothing of no boiling point under the normal pressure is decomposed high speed carburetion molecular state or high degree of dispersion attitude material flow, it is characterized in that: select preferably insoluble or be slightly soluble in liquefied petroleum gas, the flash-point above solvent of tens degree that is above the boiling point, and no boiling point organic substance solubility is preferably in more than 1/3; Solution is injected injection moulding cigarette lighter type device, the liquefied petroleum gas of the 1-15% that reinjects earlier; The device bag is with heat insulation layer; Make the steam flow fairlead stretch out base portion 1-1.5cm, put the profiled metal paillon foil to strengthen the absorption of heat, then flow of solution after preheat earlier more than the solvent boiling point can be more than one fairlead the time, one opens, just can obtain not having the high speed carburetion material flow of decomposition, certainly assorted have solvent and natural gas molecule, this method to be adapted to～organic substance of 250 ℃ of initial thermolysiss; If initial heat decomposition temperature is lower than 250 ℃, then should the corresponding temperature of turning down heat supply source.
3, method according to claim 2 is characterized in that: but introduce even add earlier the means of melting missible oil of the water of 1/3-1/2, and can obtain diameter does not have the no boiling point organic substance material flow that decomposes less than 0.1 micron high speed gasification yet.
4, method according to claim 2 is characterized in that: introduce even add the hydrocolloid agent of 1/3-1/2 and the means of colloidal suspending agent earlier, can obtain diameter does not have the no boiling point organic substance material flow that decomposes less than 0.1 micron high speed gasification yet.
5, method according to claim 2 is characterized in that: introduce emulsibility missible oil even add the means of 1/3-1/2 water earlier, the high speed gasification that yet can obtain 0.1 micron of diameter does not have the no boiling point organic substance material flow that decomposes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98110753A CN1122144C (en) | 1998-03-30 | 1998-03-30 | Producing method of high-speed vaporized boiling point-free organic matter flow without decomposition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98110753A CN1122144C (en) | 1998-03-30 | 1998-03-30 | Producing method of high-speed vaporized boiling point-free organic matter flow without decomposition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1230652A CN1230652A (en) | 1999-10-06 |
| CN1122144C true CN1122144C (en) | 2003-09-24 |
Family
ID=5220776
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98110753A Expired - Fee Related CN1122144C (en) | 1998-03-30 | 1998-03-30 | Producing method of high-speed vaporized boiling point-free organic matter flow without decomposition |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1122144C (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1090915A (en) * | 1992-12-29 | 1994-08-17 | 普拉塞尔技术有限公司 | Cryogenic fluid vaporizer system and method |
-
1998
- 1998-03-30 CN CN98110753A patent/CN1122144C/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1090915A (en) * | 1992-12-29 | 1994-08-17 | 普拉塞尔技术有限公司 | Cryogenic fluid vaporizer system and method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1230652A (en) | 1999-10-06 |
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