CN1714925A - Quick reactor and its method - Google Patents
Quick reactor and its method Download PDFInfo
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- CN1714925A CN1714925A CNA2005100210570A CN200510021057A CN1714925A CN 1714925 A CN1714925 A CN 1714925A CN A2005100210570 A CNA2005100210570 A CN A2005100210570A CN 200510021057 A CN200510021057 A CN 200510021057A CN 1714925 A CN1714925 A CN 1714925A
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Abstract
The present invention relates to technological method for reacting matter to react fast in flow and the reactor therewith. The reactants are made to pass successively through the Venturi mixing reactor, fast supersonic Venturi reactor, spiral reactor and product collector constituting the fast reactor to realize fast reaction. Specifically, the main reactant and the supplementary reactant entering through different inlets are first reacted in the Venturi mixing reactor to produce intermediate A; the intermediate A enters the fast supersonic Venturi reactor and produce intermediate B under the ultrasonic radiating action; the intermediate B is jetted to the spiral reactor for fast reaction to obtain intermediate C; the intermediate C is jetted to the product collector for reaction and separation; and the gas is led out from the top for collection or treatment and the product is collected or pumped to the Venturi mixing reactor for further reaction.
Description
One, technical field
The present invention relates to the reactor that a kind of reactive material the rapid-action technical method takes place and utilize this technical method to make in flowing.Belong to chemical reactor and biochemical reactor field.
Two, background technology.
Be that chemical reaction or biochemical reaction all carry out in reactor, current people have an unprecedently grand occasion to the research of substance reaction, have obtained many great achievements, and very few to the research of reactor.Present widely used reactor, no matter be plug flow reactor, piston flow reactor or fixed bed reactors, nearly all be that container adds the mechanical stirring device formation, efficient is low, energy consumption is high, the reaction is not thorough but all exist, and produces the many deficiencies of polluting waste.
In order to improve stirring efficiency, further improve heat and mass effect between reactant, people have developed a large amount of various jet reactor and fluidized-bed reactor again, increase reaction efficiency by improving stirring efficiency, but still can not fundamentally address the above problem, its course of reaction control is complicated, and reaction efficiency is still undesirable, differs bigger with the theoretical value of expecting.
In order to improve reaction speed, people have been put into a large amount of energy in the research and utilization of the reaction temperature, pressure and the use catalyst that how to pass through the change reactor.Improve molecular motion speed, strengthen intermolecular collision by improving temperature and pressure, accelerate heat and mass transfer process between the reactive material, to reach the purpose that promotes reaction speed.But, directly the cost of the temperature and pressure of augmenting response device is: increased investment and energy consumption, increased course of reaction, control is complicated, also increased the waste discharge value volume and range of product that environment is had pollution, simultaneously some unsafe hazards increase, blast that causes as HTHP and leakage etc.
Three, Fa Ming content
The objective of the invention is to overcome the deficiencies in the prior art, utilize the development of the power chemistry harmony principles of chemistry a kind of under the normal temperature and pressure condition that need not to heat, pressurize, reactive material is realized rapid-action technical method and the reactor that utilizes this technical method to make thereof.
The present invention is achieved by the following technical solutions:
A kind of under the normal temperature and pressure condition that need not to heat, pressurize, reactant is realized the rapid-action technical method, it is characterized in that: do not increasing under the normal temperature and pressure condition of temperature and pressure, reactant passes through successively by the venturi mixing reactor, venturi ultrasonic wave flashing reactor, the flashing reactor that helical reactors and product gatherer constitute is realized fast reaction.
Further the specific implementation process is as follows:
The venturi mixing reactor is entered the mouth by major ingredient, nozzle, and the auxiliary material inlet constitutes.The reactant major ingredient sprays into the venturi mixing reactor that has the auxiliary material inlet from the major ingredient inlet through nozzle, auxiliary material is pressed control ratio to suck, the reactant each component is made intense impact in the venturi mixing reactor, quick oscillation and contraction wait motion with expansion, consequent powerful impact, mechanical force such as shear and flexible and not only finish the abundant mixing of each component rapidly, and break the boundary of different component substance fast, phase transfer takes place, the molecule generation intermediate A that reacts immediately under high velocity impact, intermediate A enters the preceding contraction section of the venturi flashing reactor that is attached thereto through venturi mixing reactor end.
The venturi flashing reactor is made of the supersonic generator and the after-contraction section of preceding contraction section, expansion chambers, band display unit.Intermediate A enters the preceding contraction section of venturi flashing reactor from venturi mixing reactor end, inject expansion chambers, compressed, expansion, impact and vibration, mechanical force actings in conjunction such as producing powerful impact once more, shear and stretch is in intermediate A, meanwhile intermediate A is subjected to the ultrasonic radiation effect that supersonic generator sends again, produces a large amount of cavitation bubbles.React not increasing under the normal temperature and pressure condition of temperature and pressure although be, the ultrasonic cavitation bubble but collapses in extremely short time nanosecond, and produce high temperature and hundreds of atmospheric pressure of thousands of degree in minimum space, form special high energy microcell environment, the molecular link distortion of intermediate A, fracture, cause molecular ionization, produce free radical, open more chemical reaction passage and cause series of chemical, corresponding minimizing reactions steps and process, ultrasonic radiation simultaneously also will produce light,, physical effect such as shock wave and microjet, cause intermediate A in high energy microcell environment, to be reacted with high heat transfer and high mass transfer rate, reaction speed obtains high gradient and increases suddenly, and reaction efficiency significantly improves.Moreover, the former reaction that should under high temperature or high pressure or HTHP, just can carry out, under the normal temperature and pressure condition of pressurization of not heating, be able to carry out smoothly fast like this, produce a large amount of products and a small amount of composite intermediate B of reactant, intermediate B is directly injected through the contraction section of venturi flashing reactor end and is continued reaction in the helical reactors that is attached thereto.Chemical Physics effect principle that ultrasonic wave produces and concrete engineering example see " Chemical Engineer's technology pandect " P886-898 page or leaf related Sections that the Kuang Shenglu chief editor is published by Chemical Industry Press in March, 2002 for details.
Helical reactors is made of spiral pipe, intermediate B is directly injected in the helical reactors through the contraction section of venturi flashing reactor end, flowing in spiral pipe must be the turbulent flow attitude, to guarantee intermediate B except that along conduit axis moves, also producing violent radial motion, to form strong shearing force, for this reason, the pipeline Reynolds number must reach setting value 〉=2300, intermediate B is made circular motion along spiral pipe simultaneously, the centripetal force that its centripetal acceleration produces will produce and add large impact and shearing force, so just guaranteed to react to remain under the acting in conjunction of mechanical forces such as strong shearing and impact and continued to carry out fast, obtain directly injecting the product gatherer that is attached thereto with the horizontal line direction from the helix tube end by most products and the composite intermediate C of micro-reaction thing.
The product gatherer is that a tapering at the bottom cone is provided with the product outlet, the top cylinder is provided with gas vent, in the separator of pretending, outer turbination container around spiral reaction tube, return duct is with reflux pump, the major ingredient inlet and the product outlet of venturi mixing reactor are communicated with, intermediate C is injected on the cylinder inwall of gatherer from helical reactors reaction tube terminal horizontal, under effect of inertia, do around the wall circular motion, because of cylinder diameter very greater than the spiral reaction tube diameter, intermediate C penetrates and promptly obtains extremely expansion, the same reaction that guarantees that the micro-reaction thing is carried out in the time of staying at gatherer remains is shearing, expansion, impact under the acting in conjunction that reaches mechanical forces such as stretching and carry out, micro-reaction is carried through to the end in the time of staying at gatherer.Generate if any gas, liquid or solid material in the product, can realize separating through phase-separating device: gas is derived from the top gas outlet and is collected or otherwise processed, all the other products are collected from the product outlet, or under the reflux pump effect, send into the venturi mixing reactor through return duct, continue the participation system reaction.So far, entire reaction period finishes, and its reaction effect will approach or reach the theoretical value of reaction.
Advantage of the present invention is: ingenious utilization simple ripe device be built into can the realizable force chemical effect and the sonochemical effect mutual association coordinate the flashing reactor of having an effect, minimizing reactions steps and process have been realized, fast reaction speed, reaction is carried out thoroughly, and investment and energy consumption are all very low, range of application is very extensive again, as long as chemical reaction that reactant can flow in pipeline smoothly and biochemical reaction all are suitable for, and course of reaction circulates in the enclosed path and carries out, contamination-free is discharged, be to realize rapid-action advanced technology method under the normal temperature and pressure condition, the flashing reactor of making of the present technique method is not only the important tool that reaction that difficulty carries out or the slow reaction of reaction speed are carried out fast smoothly, also be under normal temperature and pressure, finish should the reaction that just can finish be carried out smoothly under the condition of pressurization of heating or pressurize or heat important tool, realize the important tool of advanced forward position reaction theory achievement especially, really realized the reaction efficient low-consume, the course of reaction cleaning is beneficial to environmental protection.At chemical industry that relates to chemical reaction and biochemical reaction and environmental protection field great actual application value and vast market prospect are arranged.
Great advantage of the present invention is: being reflected at need not to heat also need not to pressurize more need not heat and carries out under the condition of normal temperature and pressure of pressurization, slow reaction of reaction speed and the difficult reaction of carrying out are carried out smoothly fast, and can be finished the former reaction that should under the condition of pressurization of heating or pressurize or heat, just can carry out fast.Can be widely used in each field that relates to chemical reaction and biochemical reaction, and will produce huge economic benefit, environmental benefit and social benefit.
Four, accompanying drawing and explanation
Accompanying drawing is the assembling schematic diagram that is exclusively used in flashing reactor of the present invention.
Among the figure: 1-major ingredient inlet, 2-nozzle, 3-auxiliary material inlet, 4-venturi mixing reactor, 5-venturi ultrasonic wave flashing reactor, the supersonic generator of 6-band display unit, 7-helical reactors, 8-product gatherer, the 9-phase-separating device, 10-gas vent, the outlet of 11-product, the 12-reflux pump, the 13-return duct.
Five, implementation
Below the present invention is made detailed description.
The present invention is achieved by the following technical solutions:
A kind of under the normal temperature and pressure condition that need not to heat, pressurize, reactant is realized the rapid-action technical method, it is characterized in that: do not increasing under the normal temperature and pressure condition of temperature and pressure, reactant passes through successively by the venturi mixing reactor, venturi ultrasonic wave flashing reactor, the flashing reactor that helical reactors and product gatherer constitute is realized fast reaction.
Further the specific implementation process is as follows:
Venturi mixing reactor 4 enters the mouth 1 by major ingredient, nozzle 2, and auxiliary material inlet 3 constitutes.The reactant major ingredient sprays into the venturi mixing reactor 4 that has auxiliary material inlet 3 from major ingredient inlet 1 through nozzle 2, auxiliary material press control ratio suck from auxiliary material inlet 3, fully mixes and fast reaction generation intermediate A.
Venturi flashing reactor 5 is made of the supersonic generator 6 and the after-contraction section of preceding contraction section, expansion chambers, band display unit.Intermediate A enters the preceding contraction section of venturi flashing reactor 5 from venturi mixing reactor 4 ends, injects expansion chambers, is subjected to the ultrasonic radiation effect that supersonic generator 6 sends, and generates intermediate B.
Helical reactors 7 is made of spiral pipe.Intermediate B is injected in the helical reactors 7 through the contraction section of venturi flashing reactor 5 ends, and reaction obtains intermediate C under the acting in conjunction of mechanical forces such as strong shearing and impact.
Product gatherer 8 is that a tapering at the bottom cone is provided with product outlet 11, the top cylinder is provided with gas vent 10, in the separator 9 of pretending, around the turbination container of spiral reaction tube, return duct 13 is communicated with the major ingredient inlet 1 of product outlet 11, reflux pump 12, venturi mixing reactor 4 outward.
Intermediate C is injected on the cylinder inwall of gatherer 8 from helical reactors 7 reaction tube terminal horizontal, reaction is carried through to the end in 8 time of staying at gatherer, gas is derived from top gas outlet 10 and is collected or otherwise processed, all the other products are collected from product outlet 11, or send into venturi mixing reactor 4 through return duct 13 and continue the participation system reaction under reflux pump 12 effects.
Claims (8)
1, a kind of under the normal temperature and pressure condition that need not to heat, pressurize, reactant is realized the rapid-action technical method, it is characterized in that: do not increasing under the normal temperature and pressure condition of temperature and pressure, reactant passes through successively by the venturi mixing reactor, venturi ultrasonic wave flashing reactor, the flashing reactor that helical reactors and product gatherer constitute is realized fast reaction, that is:
Venturi mixing reactor 4 is made of reactant major ingredient inlet 1, nozzle 2, auxiliary material inlet 3, the reactant major ingredient from major ingredient inlet 1 through nozzle 2 inject venturi mixing reactor 4 expansion chambers, auxiliary material is sucked from auxiliary material inlet 3 by control ratio, generate intermediate A;
Venturi flashing reactor 5 is made of the supersonic generator 6 and the after-contraction section of preceding contraction section, expansion chambers, band display unit, intermediate A enters the preceding contraction section of venturi flashing reactor 5 from venturi mixing reactor 4 ends, inject expansion chambers, ultrasonic radiation effect through supersonic generator 6 sends generates intermediate B;
Helical reactors 7 is made of spiral pipe, and intermediate B is injected in the helical reactors 7 through the contraction section of venturi flashing reactor 5 ends, strong shear and the acting in conjunction of mechanical forces such as impact under reaction obtain intermediate C;
Product gatherer 8 is that a tapering at the bottom cone is provided with product outlet 11, the top cylinder is provided with gas vent 10, in the separator 9 of pretending, outer turbination container around spiral reaction tube, return duct 13 is with product outlet 11, reflux pump 12, the major ingredient inlet 1 of venturi mixing reactor 4 is communicated with, intermediate C is injected on the cylinder inwall of gatherer 8 from helical reactors 7 reaction tube terminal horizontal, reaction is carried through to the end in 8 time of staying at gatherer, gas is derived from top gas outlet 10 and is collected or otherwise processed, all the other products are collected from product outlet 11, or send into venturi mixing reactor 4 through return duct 13 and continue the participation system reaction under reflux pump 12 effects.
2, reactive material generation rapid-action method according to claim 1, it is characterized in that: venturi mixing reactor 4 terminal preceding contraction section inlets with venturi flashing reactor 5 are connected as a single entity, the after-contraction section outlet of venturi flashing reactor 5 is connected as a single entity with the inlet of helical reactors 7, the inlet of the outlet of helical reactors 7 and product gatherer 8 is connected as a single entity, the product outlet 11 of product gatherer 8 is communicated with by the major ingredient inlet 1 of return duct 13 with reflux pump 12, venturi mixing reactor 4, forms flashing reactor.
3, reactive material generation rapid-action method according to claim 1 is characterized in that: the supersonic generator 6 of venturi flashing reactor 5 built-in band display unit.
4, reactive material generation rapid-action method according to claim 1 is characterized in that: pipeline Reynolds number 〉=2300 of helical reactors 7.
5, reactive material generation rapid-action method according to claim 1 is characterized in that: be provided with return duct 13 and be communicated with the major ingredient inlet 1 of venturi mixing reactor 4 in product outlet 11, reflux pump 12 is housed on return duct 13.
6, reactive material generation rapid-action method according to claim 1, it is characterized in that: product gatherer 8 is one and is provided with product outlet 11 at the bottom cone, the top cylinder is provided with gas vent 10, in the separator 9 of pretending, outward around the turbination container of spiral reaction tube.
7, reactive material generation rapid-action device according to claim 6 is characterized in that: the upper cylinder diameter of product gatherer 8 is very greater than the reaction tube diameter of helical reactors 7.
8, reactive material generation rapid-action device according to claim 6 is characterized in that: according to product kind and shape, and can built-in phase-separating device 9.
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| Application Number | Priority Date | Filing Date | Title |
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| CNB2005100210570A CN100357018C (en) | 2005-06-07 | 2005-06-07 | Quick reactor and its method |
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| CNB2005100210570A CN100357018C (en) | 2005-06-07 | 2005-06-07 | Quick reactor and its method |
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| CN1714925A true CN1714925A (en) | 2006-01-04 |
| CN100357018C CN100357018C (en) | 2007-12-26 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108993370A (en) * | 2018-10-18 | 2018-12-14 | 辽宁石油化工大学 | A kind of spiral coil isothermal reactor and its application method |
| CN111760517A (en) * | 2020-07-01 | 2020-10-13 | 西安交通大学 | Supercritical hydrothermal synthesis system and method capable of switching multi-material mixing mode and sequence |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US5123433A (en) * | 1989-05-24 | 1992-06-23 | Westinghouse Electric Corp. | Ultrasonic flow nozzle cleaning apparatus |
| CN2256882Y (en) * | 1996-07-05 | 1997-06-25 | 佟燕 | Machine for emulsifying light diesel oil |
| NL1013135C2 (en) * | 1999-09-24 | 2001-03-30 | Kema Nv | Method and device for removing solid particles from a gas. |
| CN1166448C (en) * | 2001-07-27 | 2004-09-15 | 鞍山钢铁学院 | Liquid phase nano powder body and preparation method of nano particle agglutinative structure material |
| CN2499118Y (en) * | 2001-08-31 | 2002-07-10 | 江寿良 | Venturi fast reactor |
| CN2626605Y (en) * | 2003-07-15 | 2004-07-21 | 上海焦化有限公司 | Jet type internal circulation reacting device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108993370A (en) * | 2018-10-18 | 2018-12-14 | 辽宁石油化工大学 | A kind of spiral coil isothermal reactor and its application method |
| CN111760517A (en) * | 2020-07-01 | 2020-10-13 | 西安交通大学 | Supercritical hydrothermal synthesis system and method capable of switching multi-material mixing mode and sequence |
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Application publication date: 20060104 Assignee: SICHUAN ANLIN OIL AND GAS ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. Assignor: Jiang Suian Contract record no.: 2014510000008 Denomination of invention: Quick reactor and its method Granted publication date: 20071226 License type: Common License Record date: 20140226 |
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