CN100486952C - Preparing process and apparatus for nano aromatic copper salt - Google Patents
Preparing process and apparatus for nano aromatic copper salt Download PDFInfo
- Publication number
- CN100486952C CN100486952C CNB2006101021072A CN200610102107A CN100486952C CN 100486952 C CN100486952 C CN 100486952C CN B2006101021072 A CNB2006101021072 A CN B2006101021072A CN 200610102107 A CN200610102107 A CN 200610102107A CN 100486952 C CN100486952 C CN 100486952C
- Authority
- CN
- China
- Prior art keywords
- nanometer
- copper salt
- packing layer
- aromatic
- reaction
- 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
Images
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
The present invention relates to process and apparatus for preparing nanometer aromatic copper salt. Aromatic acid saponifying liquid and soluble copper salt as materials are compounded into solutions, the solutions are pumped into a bumping flow contactor to bump mutually at high speed to form bumped fog surface and produce depositing crystallization reaction, and the reacted liquid is further mixed in a rotary stuffing layer for secondary reaction to obtain yellowish gel. The gel is maintained to mature, filtered, washed and dried to obtain the nanometer aromatic copper salt. The process of preparing aromatic copper salt with carboxylic acid with benzene ring has molecular level mixing, fast formation of supersaturation and formation of fine crystal nucleus. The prepared nanometer aromatic copper salt has controllable crystal grain, homogeneous size and high dispersivity, and is suitable for use as thermosensitive record material, paper dying material, antiseptic material, etc.
Description
Technical field
The present invention relates to a kind of continuous method for preparing nano aromatic copper salt, comprise nano aromatic copper salt preparation method and device.
Background technology
Aromatic copper salt has extremely important purposes in the chemical industry chain, aromatic copper salt has unique optical activity, catalytic performance, biological activity and magnetic, is widely used in thermal recording medium, paper coloring, impregnating material and antiphlogistic drug etc.Aromatic copper salt is as combustioncatalysts, and catalyst grain size is littler, and its catalytic effect is stronger, and catalyzer is refine to submicron order or nano level from micron order, and combustionvelocity is greatly improved.
At present, relevant nano level aromatic copper salt preparation method seldom reports both at home and abroad, and suitability for industrialized production adopts continuous-stirring reactor (STR), and the prepared aromatic copper salt granularity that gets is more than more than ten microns.Many researchists are optimized existing STR structure of reactor and operational condition, and expectation directly obtains nano level aromatic copper salt, but the result is undesirable.According to the reactive crystallization theory, the precondition that obtains fine particle be exactly in reactor moment form high degree of supersaturation, make crystal grain outburst nucleation.Aromatic copper salt has organic groups such as phenyl ring and carboxylic acid, the viscosity of this reaction solution is relatively large, require reactant to reach the mixing and the reaction of molecular level at short notice, the common response device is the requirement that impossible reach such, and this also is to adopt STR can't obtain nano level aromatic copper salt basic reason as reactor.
Summary of the invention
The present invention seeks to prepare aromatic copper salt viscosity height at the carboxylic acid that has phenyl ring, in common response device STR, can not reach the mixing of molecular level, can not form high degree of supersaturation in short period of time, can not form tiny nucleus during the reaction nucleation, be that reaction precipitation method prepares nanoparticle " bottleneck ".
The present invention adopts following technical scheme to realize: the preparation method of nano aromatic copper salt, saponification liquor and soluble copper salt with aromatic acid are raw material, be mixed with certain density solution, place basin respectively, two kinds of stock liquids are rotated in the packing layer intermediary percussion flow contactor by the pump input, two strands of liquid phases form cloudy surface to high-speed impact, enter the rotation packing layer subsequently, reaction crystallization process occurs in the bump cloudy surface and rotates in the packing layer, reaction solution compiles by rotating in the packing layer, flow into basin, resultant of reaction is through overcuring, filter, washing and spraying drying obtain nano aromatic copper salt.Aromatic acid saponification liquor concentration is 0.2-2mol/L, and the concentration of copper salt solution is 0.2-2mol/L; Resultant of reaction is light yellow gel, and it is scattered in 50-80 ℃ the hot water again, and insulation slaking 1-10 hour obtains growing complete fragrant mantoquita crystal.Aromatic acid is a phenylformic acid, phthalic acid, resorcylic acid.Soluble copper salt is a cupric sulfate pentahydrate, cupric chloride, cupric nitrate.
For implementing the used device of preparation method of nano aromatic copper salt, comprise basin, basin rotates the packing layer two ends with hollow form and is communicated with, the rotation packing layer is fixed in the right cylinder by the ring-type silk screen and constitutes, the bottom has liquid exit, and right cylinder is connected through belt with motor, and rotating speed is adjustable in 100-3000rpm, the vacancy is provided with the percussion flow contactor in the ring-type silk screen, between rotation packing layer and the basin flow is set and takes into account pump.The ring-type silk screen is Stainless Steel Cloth or plastic silk screen.During the stroke speed of percussion flow contactor＜10m/s, rotate the packing layer rotating speed〉1000rpm.The stroke speed of percussion flow contactor〉during 15m/s, rotate packing layer rotating speed＜1000rpm.
Reaction precipitation of the present invention does not have special requirement to temperature of reaction, but better when being reflected at 70-80 ℃.When lower stroke speed (being lower than 10m/s), require (greater than 1000rpm) reaction under higher rotation speed.When higher stroke speed (being lower than), also can than (greater than 1000rpm) under the slow speed of revolution greater than 15m/s.
(to call β-Cu) in the following text is example, the following reaction that whole process relates to prepare nano level resorcin acid copper.
The reactant viscosity of aromatic copper salt is big, in the common response device, can not reach the mixing of molecular level under the agitation condition, thereby can not form high degree of supersaturation at short notice, and can not form tiny nucleus during the reaction nucleation, be that reaction precipitation method prepares nanoparticle " bottleneck ".The present invention has broken through traditional feed way of common response device and the conventional thought that mixes, adopt high pressure bump feeding manner, having good microcosmic on the impact surface mixes, the place that forms high saturation is provided for reaction precipitation, make reactant reach the mixing of molecular level, for nanoparticle forms the condition of having created.May cause the reactant can not abundant catalytic probability owing to splash in order to eliminate the bump edge, will clash into atomizing nozzle and place and rotate filler, the filler of high speed rotating also provides highly microcosmic hybird environment, helps unreacted portion to react at packing layer.Because liquid is extremely short to the packing layer required time from the bump edge, guarantees that all reactants react simultaneously, also can avoid the nanoparticle that generates long and grow at reactor residence time, reach the purpose of continuous preparation nano aromatic salt.
The present invention adopts high pressure bump feeding manner, has good microcosmic on the impact surface and mixes, and for reaction precipitation provides the place that forms high saturation, makes reactant reach the mixing of molecular level, for nanoparticle forms the condition of having created.May cause the reactant can not abundant catalytic probability owing to splash in order to eliminate the bump edge, to clash into atomizing nozzle and place the rotation packing layer, the filler of high speed rotating also provides height microcosmic hybird environment, helps unreacted portion to react at packing layer.Because liquid is extremely short to the packing layer required time from the bump edge, guarantees that all reactants react simultaneously, also can avoid the nanoparticle that generates long and grow at reactor residence time.
Thermolysis catalytic performance of the present invention trial sheet is as follows:
Take by weighing GAP and nanometer organic copper sample by different homogenous quantities ratios, place stirring tank, fully mix, centrifugal expelling water carries out the thermal decomposition performance experiment.By the visible nanosized copper of following table the gentle initial peak temperature in the peak that makes the GAP decomposition peak is shifted to an earlier date respectively, peak width (AT) reduces, and the combustion speed of propelling agent is increased.This is because organic copper and liquid GAP molecule form complex compound, reduced the activation energy that GAP decomposes, the decomposition reaction temperature of GAP is shifted to an earlier date, minimizing along with nano-cu content, the decomposition peak-to-peak temperature of GAP/ nanometer organic copper, starting temperature are moved after all, Δ T increases gradually, and speed of reaction then reduces gradually, but the addition of nanometer organic copper is not linear to the influence of GAP thermolysis peak temperature.
The nanometer organic copper influences the GAP pyrolysated
| Sequence number | Sample | Summit temperature/℃ | The starting temperature at peak/℃ | ΔT/ |
| 1 | GAP：Cures | 253.7 | 184.4 | 69.3 |
| 2 | GAP：Cures (1.5:1) | 221.5 | 163.1 | 58.4 |
| 3 | GAP：Cures (5:1) | 222.9 | 164.3 | 58.6 |
| 4 | GAP：Cures (15:1) | 233.1 | 164.8 | 68.3 |
| 5 | GAP：Cures (20:1) | 236.7 | 166.2 | 70.5 |
Annotate: Δ T is the poor of summit temperature and initial peak temperature, and GAP:Cures is a weight ratio.
Description of drawings
Fig. 1 is a nano aromatic copper salt preparation facilities synoptic diagram of the present invention
Fig. 2 is embodiment 1 an aromatic acid shot copper footpath distribution plan
Fig. 3 is embodiment 2 an aromatic acid shot coppers footpath distribution plan
Among the figure: 1-percussion flow contactor, 2-rotates packing layer, 3-motor, 4-basin, 5-basin, 6-pump, 7-pump, 8-under meter, 9-under meter, 10-liquid exit, 11-silk screen, 12-right cylinder, 13-belt
Embodiment
The present invention is a kind of nano level aromatic copper salt preparation method.Mainly by going on foot at percussion flow-rotation packing layer reaction precipitation and maturation process two, concrete steps are:
A: reaction solution is prepared: in the sodium hydroxide solution of (generally greater than 50 ℃) of heat, under agitation condition, add aromatic acid, regulator solution pH value is 7-10, and gained solution is the aromatic acid saponification liquor.Under the agitation condition, copper sulfate is dissolved in an amount of hot water, obtains copper-bath, and clarification is standby naturally.
B: reaction precipitation: after respectively aromatic acid saponification liquor and copper-bath being preheated to 50-80 ℃, two kinds of liquid are sent into simultaneously the percussion flow contactor that rotates the bed of packings inner chamber respectively through high-pressure pump, two strands of liquid phases are to high-speed impact, form impact surface, the chemical reaction precipitation takes place in reactant on knockout process and impact surface.Impact surface edge liquid enters and rotates in the packing layer, the further hybrid reaction of reaction solution under powerful centrifugal action, and reaction solution compiles and obtains lurid gel.
C: with lurid gel detergent, remove sulfate ion and sodium ion after, be scattered in again in 50-80 ℃ the hot water, insulation slaking a few hours, the aromatic copper salt crystal development is complete, more after filtration, washing and drying obtain nano level aromatic copper salt.
Resorcin acid saponification liquor and the 0.5mol/l copper-bath of preparation 0.5mol/l, under 70 ℃ the temperature, two kinds of liquid are sent into simultaneously the percussion flow contactor that rotates the bed of packings inner chamber respectively through high-pressure pump, two strands of liquid phases are to the 20m/s high-speed impact, form impact surface, the chemical reaction precipitation takes place in reactant on knockout process and impact surface.Impact surface edge liquid enters and rotates in the packing layer, and rotating the packing layer rotating speed is 1000rpm, the further hybrid reaction of reaction solution under powerful centrifugal action, and reaction solution compiles and obtains lurid gel.Behind the lurid gel detergent that obtains, be scattered in again in 50 ℃ the hot water, insulation slaking 10 hours, more after filtration, after washing and the drying, obtain organic copper powder mean diameter 20-100nm.
Resorcin acid saponification liquor and the 1.0mol/l copper-bath of preparation 1.0mol/l, under 70 ℃ the temperature, two kinds of liquid are sent into simultaneously the percussion flow contactor that rotates the bed of packings inner chamber respectively through high-pressure pump, two strands of liquid phases are to the 30m/s high-speed impact, form impact surface, the chemical reaction precipitation takes place in reactant on knockout process and impact surface.Impact surface edge liquid enters and rotates in the packing layer, and rotating the packing layer rotating speed is 1000rpm, the further hybrid reaction of reaction solution under powerful centrifugal action, and reaction solution compiles and obtains lurid gel.Behind the lurid gel detergent that obtains, be scattered in again in 50 ℃ the hot water, insulation slaking 10 hours, more after filtration, after washing and the drying, obtain organic copper powder mean diameter 20-100nm.
Resorcin acid saponification liquor and the 1.0mol/l copper-bath of preparation 1.0mol/l, under 50 ℃ the temperature, two kinds of liquid are sent into simultaneously the percussion flow contactor that rotates the bed of packings inner chamber respectively through high-pressure pump, two strands of liquid phases are to the 30m/s high-speed impact, form impact surface, the chemical reaction precipitation takes place in reactant on knockout process and impact surface.Impact surface edge liquid enters and rotates in the packing layer, and rotating the packing layer rotating speed is 500rpm, the further hybrid reaction of reaction solution under powerful centrifugal action, and reaction solution compiles and obtains lurid gel.Behind the lurid gel detergent that obtains, be scattered in again in 50 ℃ the hot water, insulation slaking 10 hours, more after filtration, after washing and the drying, obtain organic copper powder mean diameter 20-100nm.
The saponification liquor and the 1.0mol/l copper nitrate solution of the phthalic acid of preparation 1.0mol/l, under 50 ℃ the temperature, two kinds of liquid are sent into simultaneously the percussion flow contactor that rotates the bed of packings inner chamber respectively through high-pressure pump, two strands of liquid phases are to the 30m/s high-speed impact, form impact surface, the chemical reaction precipitation takes place in reactant on knockout process and impact surface.Impact surface edge liquid enters and rotates in the packing layer, and rotating the packing layer rotating speed is 500rpm, the further hybrid reaction of reaction solution under powerful centrifugal action, and reaction solution compiles and obtains lurid gel.Behind the lurid gel detergent that obtains, be scattered in again in 50 ℃ the hot water, insulation slaking 10 hours, more after filtration, after washing and the drying, obtain organic copper powder mean diameter 20-100nm.
Claims (7)
1. device for preparing nanometer resorcin acid mantoquita, comprise basin, it is characterized in that basin (4), (5) are communicated with hollow form rotation packing layer (2) two ends, rotate packing layer (2) and be fixed in formation in the right cylinder (12) by ring-type silk screen (11), the bottom has liquid exit (10), right cylinder (12) is connected through belt (13) with motor (3), the vacancy is provided with percussion flow contactor (1) in the ring-type silk screen (11), rotates between packing layer (2) and basin (4), (5) under meter (8), (9) and pump (6), (7) are set respectively.
2. the device of preparation nanometer resorcin acid mantoquita according to claim 1 is characterized in that ring-type silk screen (11) is a Stainless Steel Cloth.
3. the device of preparation nanometer resorcin acid mantoquita according to claim 1 is characterized in that ring-type silk screen (11) is a plastic silk screen.
4. the preparation method of nanometer resorcin acid mantoquita, described method is finished in claim 1 or 2 or 3 described devices, the steps include: that saponification liquor and soluble copper salt with resorcin acid are raw material, be mixed with certain density solution, place basin (4) respectively, (5) in, two kinds of stock liquids are rotated in packing layer (2) the intermediary percussion flow contactor (1) by the pump input, two strands of liquid phases form cloudy surface to bump, enter subsequently and rotate packing layer (2), reaction crystallization process occurs in the bump cloudy surface and rotates in the packing layer (2), reaction solution compiles in rotating packing layer (2), flow into basin, resultant of reaction is through overcuring, filter, washing and spraying drying obtain nanometer resorcin acid mantoquita.
5. the preparation method of nanometer resorcin acid mantoquita according to claim 4 is characterized in that resorcin acid saponification liquor concentration is 0.2-2mol/L, and the concentration of copper salt solution is 0.2-2mol/L; Resultant of reaction is light yellow gel, and it is scattered in 50-80 ℃ the hot water again, and insulation slaking 1-10 hour obtains growing complete nanometer resorcin acid mantoquita crystal.
6. the preparation method of nanometer resorcin acid mantoquita according to claim 4 is characterized in that soluble copper salt is a cupric sulfate pentahydrate, cupric chloride, cupric nitrate.
7. the preparation method of nanometer resorcin acid mantoquita according to claim 4, it is characterized in that: during the stroke speed of percussion flow contactor (1)＜10m/s, rotate packing layer (2) rotating speed〉1000rpm, the stroke speed of percussion flow contactor (1)〉during 15m/s, rotate packing layer (2) rotating speed＜1000rpm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101021072A CN100486952C (en) | 2006-10-28 | 2006-10-28 | Preparing process and apparatus for nano aromatic copper salt |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101021072A CN100486952C (en) | 2006-10-28 | 2006-10-28 | Preparing process and apparatus for nano aromatic copper salt |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1986514A CN1986514A (en) | 2007-06-27 |
| CN100486952C true CN100486952C (en) | 2009-05-13 |
Family
ID=38183471
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006101021072A Expired - Fee Related CN100486952C (en) | 2006-10-28 | 2006-10-28 | Preparing process and apparatus for nano aromatic copper salt |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100486952C (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103043689A (en) * | 2012-12-22 | 2013-04-17 | 中北大学 | Method and device for synthesizing superfine magnesium hydrate fire retardant |
| CN104610042A (en) * | 2015-01-08 | 2015-05-13 | 南京理工大学 | Preparation method of nano 2,4-copper resorcylic |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102059142B (en) * | 2010-11-27 | 2012-07-25 | 中北大学 | Method for preparing copper plumbum chelate/mesoporous carbon composite material |
| CN110026146B (en) * | 2019-03-14 | 2021-05-18 | 中北大学 | Device and method for preparing benzaldehyde by impinging stream rotating packed bed |
-
2006
- 2006-10-28 CN CNB2006101021072A patent/CN100486952C/en not_active Expired - Fee Related
Non-Patent Citations (2)
| Title |
|---|
| 络合物[Cu(pic)(His)(OH2)]2H2O的合成和结构特征. 刘英等.聊城大学学报，第18卷第2期. 2005 |
| 络合物[Cu(pic)(His)(OH2)]2H2O的合成和结构特征. 刘英等.聊城大学学报，第18卷第2期. 2005 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103043689A (en) * | 2012-12-22 | 2013-04-17 | 中北大学 | Method and device for synthesizing superfine magnesium hydrate fire retardant |
| CN103043689B (en) * | 2012-12-22 | 2014-12-10 | 中北大学 | Method and device for synthesizing superfine magnesium hydrate fire retardant |
| CN104610042A (en) * | 2015-01-08 | 2015-05-13 | 南京理工大学 | Preparation method of nano 2,4-copper resorcylic |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1986514A (en) | 2007-06-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102923749B (en) | Carbonization method for preparing nano calcium carbonate | |
| CN100486952C (en) | Preparing process and apparatus for nano aromatic copper salt | |
| CN106564908B (en) | A kind of method that Impinging Stream-Rotating Packed Bed strengthens microwave synthesis ZSM-5 molecular sieve | |
| CN100450932C (en) | Nm-class calcium carbonate carbonization process | |
| CN101774623A (en) | Industrial preparation method of rice-shaped ultra-fine activated calcium carbonate | |
| CN105601652B (en) | A kind of method for preparing metal-organic framework materials | |
| FI83426B (en) | FOERFARANDE FOER KONTINUERLIG FRAMSTAELLNING AV MICROCRYSTALLINE KITOSAN. | |
| CN103896284B (en) | A kind of monodisperse silica nano particle and preparation method thereof | |
| CN115716918A (en) | Method for preparing metal-organic framework material by ball milling-solution blending | |
| CN112275295B (en) | Nano copper-manganese catalyst, preparation method thereof and method for preparing 4-dimethylaminopyridine | |
| CN102249257A (en) | Method for recycling crystallization mother liquor from SUZ-4 molecular sieve production for producing SUZ-4 molecular sieve | |
| CN116947795B (en) | Continuous synthesis method of S-hydroxypropyl tetrahydropyran triol | |
| CN104891545A (en) | Carbonization reaction device and method for nano calcium carbonate production | |
| CN202953834U (en) | Nanometer calcium carbonate carbonation reaction still | |
| CN100379492C (en) | Super alkali composite catalyst for preparing superfine KF/Al2O3 using Sol-gel method | |
| CN114408958B (en) | Device and method for preparing hollow spherical calcium carbonate and hollow spherical calcium carbonate prepared by using device | |
| CN1119333C (en) | Process for hydrorefining caprolactam | |
| CN1280198C (en) | Nano-class silver oxide and preparation method thereof | |
| CN1869017A (en) | Production technology and device of paranminophenyl-beta-hydroxyethyl sulfone sulfate | |
| CN1429657A (en) | Method of forming essence microcapsule using interface polymerization reaction | |
| CN112316863A (en) | Preparation method of nano-grade microcapsule | |
| CN103381485B (en) | A kind of method preparing 3-mercaptopropionic acid parcel silver nano-grain | |
| CN106632394A (en) | Method for preparing rifampicin by utilizing cascade reaction of kettle type reaction device and microchannel reaction device | |
| CN100537605C (en) | Industrial preparing method and device for methyl hydroxy alkyl cellulose | |
| CN219356247U (en) | Reaction device for preparing nano-scale barium sulfate |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| 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: 20090513 Termination date: 20111028 |