CN2562869Y - Liquid catalytic machine - Google Patents
Liquid catalytic machine Download PDFInfo
- Publication number
- CN2562869Y CN2562869Y CN02274648U CN02274648U CN2562869Y CN 2562869 Y CN2562869 Y CN 2562869Y CN 02274648 U CN02274648 U CN 02274648U CN 02274648 U CN02274648 U CN 02274648U CN 2562869 Y CN2562869 Y CN 2562869Y
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- CN
- China
- Prior art keywords
- magnetic
- liquid
- catalytic
- ultrasonic wave
- liquid catalyst
- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/087—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/10—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing sonic or ultrasonic vibrations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J2219/0873—Materials to be treated
- B01J2219/0877—Liquid
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model provides a liquid catalytic machine belonging to the device of the physical catalytic technical field strengthening the physical property of liquid material and accelerating the perfect chemical reaction process. To ensure that the molecules of fluid material obtain more activation energy, the additive effects of intense ultrasonic wave and high magnetic energy intensification are adopted to ensure that the liquid material obtains a more sufficient and perfect catalytic treatment. The catalytic process of the machine is finished by special catalytic system device. The structure of the catalytic system device is mainly composed of a magnetism revolving injection part, a labyrinth magnetism intensify part and a intense ultrasonic wave part generated in a intense magnetic field. The utility model can be used for the combustion system of liquid material, the course of production and the deep processing process.
Description
1, technical field:
This liquid catalyst machine is a kind of equipment that belongs to liquid towards material strengthening physical performance and promote to improve the physics catalysis technical field of chemical reaction process.
2, background technology:
This liquid catalyst machine is to adopt magnetic to intensify with the magnetized superimposed effect of intense ultrasonic wave to conceive the special catalysis system device of design and realize the catalysis purpose.
The catalytic treatment of liquid towards material adopts the chemical catalyst mode to carry out mostly.Modes such as independent employing laser, microwave, ultrasonic wave, stirring, electric pulse, infrared ray, magnetization are also arranged in the liquid production process in recent years, and the liquid towards material carries out catalysis.Pass through numerous scientific and technical personnel's research and test the employing variety of way repeatedly aspect the catalytic treatment of liquid towards material, obtained a lot of achievements.The liquid towards material has been done a lot of discussions and research in the physics catalysis technical field.As Japanese East Asia fuel industry pearl formula commercial firm, in the patent of China's application---" ultrasonic wave gunite and nozzle " (CN85107669A) utilizes Superaudio impulse vibration " activation " liquid fuel molecule and spray burning." activation " that this nozzle provides fluid molecule can, be to utilize the supersonic frequency vibration generating arrangement of other electric pulse to drive the pulse field energy that a vibrating elements does reciprocal impact to realize.(application number: 87105894.4) its catalytic way and process are to make the contact area that increases solid-liquid to and for example domestic patent of invention " efficient aging technology of interface method drinks and equipment " in the application of fine jade sea, the interfacial area of the expansion solid-liquid of maximum possible, the exchange molecular amounts at interface is increased, quicken molecule " activation " and short its precocity, and then reached the purpose of catalysis.
The research of a lot of scientists to the physics catalysis technique is abroad also arranged in recent years, once reported as " world technology is translated newspaper " " ... and the conventional pressurization raising chemical reaction velocity of heating is completely different, the scientist at Britain Ha Weier chemical technology center is testing technology---the phonochemistry technology that a kind of high-frequency sound energy improves chemical reaction velocity.Ultrasonic wave (more than 16 kilo hertzs) is squeezed in the chemical reaction liquid, can be made reaction speed improve more than 100 times.Its main cause is the empty effect of hyperacoustic one-tenth---the formation and the disappearance of microvesicle in the reactant liquor.When microvesicle disappeared, the temperature and pressure of end point suddenly rose, and temperature can reach 6000K (sic, annotate in the school) pressure can reach 300 atmospheric pressure.The Another reason of ultrasonic wave catalytic action is super melange effect.As everyone knows, the speed of chemical reaction is directly proportional with the chemical agent contact area of participating in reaction usually.Here it is, and people's stirring method commonly used is accelerated the basic reason of chemical reaction velocity.The high strength supersonic wave energy plays equally or bigger effect.Mechanical agitation each second is the fastest has only hundreds of, and hyperacoustic stirring action is equivalent to each second about 20,000 times ... "
In the catalytic process of liquid towards material, no matter be to adopt chemical mode or physics mode, in fact all striving improving molecule " activation " energy, excited molecule " activation " is the process of " activation " again, and " activation " of molecule can then derive from certain extraneous energy.How to make molecule obtain more " activation " can, with raising with improve catalytic effect, people seek and explore unremitting in every way in every field.
3, summary of the invention:
The utility model provides a kind of liquid catalyst machine, and its purpose is to separate fluid product that must not add catalyst and the problem that can improve aspect existence such as its " activation " energy at the fluid molecule that can add catalyst better.
Technical scheme:
A kind of liquid catalyst machine, it is characterized in that: this liquid catalyst machine be by magnetic rotation penetrate part, labyrinth type magnetic intensifies part and intense ultrasonic wave magnetic intensifies part and constitutes, and magnetic rotation is penetrated part, labyrinth type magnetic and is intensified part and intense ultrasonic wave magnetic and intensify that the passage that is to be provided with by the centre interconnects.
The inside of penetrating part in magnetic rotation is provided with cyclone pipe and strong bar magnet, and the external process of cyclone pipe becomes helicla flute; Strong bar magnet is assemblied in the centre of cyclone pipe.
Labyrinth type magnetic is equipped with two relative magnetics in intensifying partly, has continuous rotating Baltimore groove on the contact-making surface of magnetic.
Intense ultrasonic wave magnetic is equipped with two relative magnetics in intensifying partly, is provided with the sheet ticker in the middle of two magnetics, and respectively there is a strong point both sides of sheet ticker.
Advantage of the present utility model and effect:
By the enforcement of this liquid catalyst machine, can greatly improve the reaction speed of liquid, reduce use equipment, improved production efficiency.
4, description of drawings:
Accompanying drawing 1 is a structural representation of the present utility model.
5, the specific embodiment:
This liquid catalyst machine is conceived design for pursuing above-mentioned purpose, and is to rely on a kind of special catalysis system device to realize.For catalysant provide catalysis can process, be by magnetic rotation penetrate the part, labyrinth type magnetic intensify the part and intense ultrasonic wave magnetic intensify part, three phases is finished.
Phase I liquid stream in A part is penetrated in magnetic rotation is made cutting magnetic line and is advanced and since molecular characterization extremely, make intermolecular electronics quicken mutual gain and loss process, and perfect course of reaction.
It partly is that liquid flows in continuous rotating Baltimore groove from high-intensity magnetic field two interpolars that second stage intensifies B at labyrinth type magnetic, doing labyrinth type advances, molecule is intensified by magnetic, making molecule obtain " activation " once more can, intermolecular attraction reduces, and viscosity descends, and the molecule reorientation is arranged, improve liquid phase state, quickened course of reaction.
Phase III is in intense ultrasonic wave magnetic intensifies the C part, liquid produces hyperfrequency vibration (more than 20,000 hertz) with the high-pressure spray state in high-intensity magnetic field, promptly this kind liquid passes through between hyperfrequency vibration body surface and strong magnetic pole, be from sound, magnetic field, to pass through, this moment, sound field and magnetic field produced a kind of integration type superposition potential energy each other, make molecule obtain bigger " activation " energy, just molecule has been subjected to for the third time " activation "." activation " mode of phase III be will catalysis liquid, under the spray regime of high-pressure spray, self produces intensification, it itself is exactly the product that intense ultrasonic wave takes place, and under the superposition effect in strong sound field and magnetic field and by catalysis, this catalytic way is superior to both at home and abroad and discharges hyperacoustic single practice with methods such as electric pulses in liquid.The catalytic way of phase III is the special distinctive feature of this machine just also.
Because the catalysis characteristics of this machine determines, in the production and processing technology process of liquid, can play " polymerization " (chemical combination) respectively, decompose effects such as (fractionation, hydrolysis), emulsification, mixing.Also can be applicable to the combustion system of flammable liquid, physical state at most is indirect affects chemical reaction process, and then acceleration and the perfect physical and chemical reaction process of liquid, has improved production technology in production practices, has improved product quality and performances.
Description of drawings: the catalysis system of this liquid catalyst machine mainly is made of three parts, A is that part is penetrated in magnetic rotation among the figure, its architectural feature is that highly pressurised liquid has helicla flute by the outer surface of cyclone pipe 1 from cyclone pipe 1, the center closely is fitted with strong bar magnet 2, and high-pressure fluid is done cutting magnetic line rotation propelling and entered the B stage from helicla flute.B intensifies part for labyrinth type magnetic among the figure, passes through the labyrinth passage 4 of liquid in the middle of high magnetic 3 and 5, and molecule is intensified, intermolecular attraction reduces, and viscosity reduces, and the molecule reorientation is arranged, improved the state of liquid phase, quickened course of reaction, highly pressurised liquid continues to push ahead the stage to C.C is the superposition section in sound field and magnetic field among the figure, and liquid molecule under the state of high pressure and intensification is subjected to fierce the collision, acquires bigger " activation " energy, and catalysis finishes to the end, and liquid is sent into the finished product jar from the exit or entered catalysis system next time again.
1, cyclone pipe, 2, strong bar magnet, 3, magnetic, 4, labyrinth passage, 5, magnetic, 6, magnetic, 7, the sheet ticker, 8, magnetic.
Claims (4)
1, a kind of liquid catalyst machine, it is characterized in that: this liquid catalyst machine be by magnetic rotation penetrate (A) partly, labyrinth type magnetic intensifies (B) part and intense ultrasonic wave magnetic and intensifies (C) part and constitute, and magnetic rotation penetrate (A) partly, labyrinth type magnetic intensifies (B) part and intense ultrasonic wave magnetic to intensify (C) partly is that passage by the centre setting interconnects.
2, a kind of liquid catalyst machine according to claim 1 is characterized in that: the inside of penetrating (A) part in magnetic rotation is provided with cyclone pipe (1) and strong bar magnet (2), and the external process of cyclone pipe (1) becomes helicla flute; Strong bar magnet (2) is assemblied in the centre of cyclone pipe (1).
3, a kind of liquid catalyst machine according to claim 1 is characterized in that: labyrinth type magnetic intensify (B) part in two relative magnetics (3) and (5) are housed, on the contact-making surface of magnetic (3) and (5), have continuous rotating Baltimore groove.
4, a kind of liquid catalyst machine according to claim 1, it is characterized in that: intense ultrasonic wave magnetic intensify (C) part in two relative magnetics (6) and (8) are housed, be provided with sheet ticker (7) in the middle of two magnetics (6) and (8), respectively there is a strong point both sides of sheet ticker (7).
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN02274648U CN2562869Y (en) | 2002-08-09 | 2002-08-09 | Liquid catalytic machine |
AU2003257785A AU2003257785A1 (en) | 2002-08-09 | 2003-08-08 | Liquid activator |
PCT/CN2003/000650 WO2004014544A1 (en) | 2002-08-09 | 2003-08-08 | Liquid activator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN02274648U CN2562869Y (en) | 2002-08-09 | 2002-08-09 | Liquid catalytic machine |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2562869Y true CN2562869Y (en) | 2003-07-30 |
Family
ID=27633249
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN02274648U Expired - Fee Related CN2562869Y (en) | 2002-08-09 | 2002-08-09 | Liquid catalytic machine |
Country Status (3)
Country | Link |
---|---|
CN (1) | CN2562869Y (en) |
AU (1) | AU2003257785A1 (en) |
WO (1) | WO2004014544A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102914175A (en) * | 2012-11-18 | 2013-02-06 | 昆山市大金机械设备厂 | Molten metal stirring method |
CN103105074A (en) * | 2012-11-15 | 2013-05-15 | 昆山市大金机械设备厂 | Molten metal rabbling furnace |
CN108675580A (en) * | 2018-07-03 | 2018-10-19 | 成都诺德源环保科技有限公司 | A kind of sludge treatment equipment and trash-removal device |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU514632A1 (en) * | 1974-05-24 | 1976-05-25 | The method of thickening the liquid dispersed system | |
JPS61259780A (en) * | 1985-05-13 | 1986-11-18 | Toa Nenryo Kogyo Kk | Vibrator for ultrasonic atomization |
DE3626356C2 (en) * | 1986-08-04 | 1994-02-03 | Guenter J Britz | Method and device for optimizing the generation of energy from and removal of pollutants during reactions in incineration plants with continuous combustion |
JPH0611095Y2 (en) * | 1989-10-16 | 1994-03-23 | 東湘電機株式会社 | Magnet type stirring device capable of generating ultrasonic waves |
US5897826A (en) * | 1996-06-14 | 1999-04-27 | Materials Innovation, Inc. | Pulsed pressurized powder feed system and method for uniform particulate material delivery |
GB9822958D0 (en) * | 1998-10-20 | 1998-12-16 | Adept Technologies As | Reactor for treating liquids |
US6186228B1 (en) * | 1998-12-01 | 2001-02-13 | Phillips Petroleum Company | Methods and apparatus for enhancing well production using sonic energy |
-
2002
- 2002-08-09 CN CN02274648U patent/CN2562869Y/en not_active Expired - Fee Related
-
2003
- 2003-08-08 AU AU2003257785A patent/AU2003257785A1/en not_active Abandoned
- 2003-08-08 WO PCT/CN2003/000650 patent/WO2004014544A1/en not_active Application Discontinuation
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103105074A (en) * | 2012-11-15 | 2013-05-15 | 昆山市大金机械设备厂 | Molten metal rabbling furnace |
CN102914175A (en) * | 2012-11-18 | 2013-02-06 | 昆山市大金机械设备厂 | Molten metal stirring method |
CN108675580A (en) * | 2018-07-03 | 2018-10-19 | 成都诺德源环保科技有限公司 | A kind of sludge treatment equipment and trash-removal device |
Also Published As
Publication number | Publication date |
---|---|
WO2004014544A1 (en) | 2004-02-19 |
AU2003257785A1 (en) | 2004-02-25 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |