CN103357436A - Alkali treatment modification method of alumina carrier as well as preparation method and application of silver catalyst supported by alumina carrier - Google Patents
Alkali treatment modification method of alumina carrier as well as preparation method and application of silver catalyst supported by alumina carrier Download PDFInfo
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Abstract
The invention relates to an alkali treatment modification method for forming an alpha-alumina carrier of a silver catalyst used for producing ethylene oxide through ethylene oxidation. The method has the beneficial effect of increasing the pore canal of the carrier by treating the formed alpha-alumina carrier with an alkaline solution at a certain concentration under the heating and stirring conditions. The silver catalyst prepared from and supported by the alpha-alumina carrier prepared by the method is beneficial to diffusion of reaction products. The modified alpha-alumina carrier shows good selectivity when applied to the reaction process of producing ethylene oxide through ethylene oxidation.
Description
Technical field
The present invention relates to catalyst and catalyst carrier technical field, specifically, relate to a kind of preparation and application of silver catalyst of alkali treatment modifying, its load of alpha-alumina supports, more particularly, relate to a kind of preparation method of the silver catalyst that adopts method of modifying that alkaline solution processes alpha-alumina supports and this modification alpha-alumina supports load and in the application of being produced by ethylene in the oxirane.
Background technology
Ethylene mainly generates oxirane (EO) under the silver catalyst effect, side reaction occurs simultaneously generate carbon dioxide and water etc., and wherein active, selective and stability is the main performance index of silver catalyst.Required reaction temperature when so-called activity refers to that process for ethylene oxide production reaches certain reaction load, reaction temperature is lower, and the activity of catalyst is higher.So-called selectively refer to react in conversion of ethylene become the ratio of the overall reaction molal quantity of the molal quantity of oxirane and ethene.So-called stability then is expressed as the fall off rate of activity and selectivity, and the fall off rate more stability of small catalyst is better.
The silver catalyst that uses high activity, high selectivity and have good stability in the process of ethylene production oxirane can be increased economic efficiency greatly, and the silver catalyst of therefore making high activity, high selectivity and good stability is the main direction of silver catalyst research.
The preparation method of silver catalyst mainly comprise the preparation of porous carrier (such as aluminium oxide) and active component and auxiliary agent loaded to as described in this two processes on the carrier.Therefore, the performance of silver catalyst has the important relationship except composition and the preparation method with catalyst, and performance and the preparation method of the carrier that also uses with catalyst have important relationship.What silver catalyst carrier was generally selected is the less Alpha-alumina of specific area.
Carrier need to provide certain surface to come load active component, and with the active component Uniform Dispersion in the above, this has just proposed very high requirement to the pore structure of carrier.The hole of alumina support can be divided three classes: 1) primary particle intercrystalline hole mainly is the dewatering hole of alumina raw material crystal grain, is slit between the parallel-plate face of 1～2nm size substantially; 2) hole between the alumina raw material offspring, effusion and crystalline phase variation with moisture in calcining change, and are the hole more than the tens nanometer; And 3) defective hole and the macropore that produce when pore creating material and carrier moulding.
Suitable carrier not only should have higher intensity, and suitable specific surface and pore structure also should be able to be provided.By Manufactured carrier is processed, can be to the carrier surface modification, improve the dispersion situation of catalytic active component silver, the Acidity of Aikalinity of change carrier surface, the suction of modulation metal silver surface electronics situation and reaction species, desorption situation, thereby the catalytic performance of raising silver catalyst.The more existing research work reports of this respect.
Chinese patent CN1044416 has reported a kind of method by dipping, be coated with the unformed silica that is covered with 0.03～20%wt on surface, carrier duct, afterwards drying and 700～1500 ℃ of silicon oxide surface modified supports that high-temperature roasting obtains, it is said behind this carrier loaded active component silver and the auxiliary agent, again 400～950 ℃ of heat treatments under inert atmosphere, gained catalyst have higher selective, active and lasting service life.
US Patent No. 4786743 has also been described a kind of silver catalyst of being made through the carrier acid-treated, that contain step-like structure of pKa≤3 by the surface, and the gained catalyst has preferably heat endurance, activity and selective.But high selectivity also only about 80%.
German patent DE 2933950 has been reported a kind of method of silver catalyst carrier being carried out purifying.This patent is thought should use pure α-Al
2O
3As carrier material, if can't buy the α-Al of this purity
2O
3, can be commercially common α-Al
2O
3Beginning to carry out purifying, is that the NaOH solution of 1wt% boils 30min with the concentration of about equivalent, then is finished the water washing completely without salt, until moistening α-Al
2O
3The pH value be lower than 8.This patent thinks and also can adopt additive method to obtain described carrier, as to adopt the concentration of about equivalent be that the hydrofluoric acid solution of 1wt% boils carrier 10min, then washes with water, until the pH value is not less than 5.It is said, adopt the method gained carrier to make active and obviously improvement in service life (stability) after the silver catalyst of alkali metal containing auxiliary agent, but selectively also only about 81.7%, and complex disposal process.
Japan Patent JP2002136868 has reported a kind of alumina support.It is at first with the support material forming, becoming main component in 500～2000 ℃ of lower roastings again is the support precursor of aluminium oxide, then adopt concentration 0.1～15% hydrofluoric acid solution to process the gained presoma, 1000～2000 ℃ of lower roasting a few hours, finally make the carrier finished product afterwards.It is said that the rhenium-containing silver catalyst that is made by this carrier has excellent catalytic activity, selective and service life.But this preparation process is higher to equipment requirement, and production cost is high, is unfavorable for implementing.
Chinese patent CN1467022A discloses a kind of preparation method of silver catalyst for ethylene oxide carrier, and the method solves the high not enough defective of silver catalyst activity that conventional art makes by alpha-alumina supports is carried out alkali treatment with alkaline matter.The alkali treatment of this invention comprises solution or gas dual mode, the alkaline matter consumption counts 0.01～500% with vehicle weight percentage, 30～800 ℃ for the treatment of temperatures, processing time 1～30h, carrier after the alkali treatment is washed with water to efflux for neutral, dry, make silver catalyst carrier, load silver and be selected from auxiliary agent at least a in sulphur, rhenium, molybdenum, tungsten, nickel, alkali metal or the alkaline-earth metal on this carrier, the load capacity of silver is counted 5～40% of catalyst weight with silver, and auxiliary agent is take the load capacity of element wt as 0.001～1% of catalyst weight.The silver catalyst of this inventive method preparation has advantages of that for the production of oxirane reaction temperature is low, reactivity is high.
Chinese patent CN101850243A has reported a kind of alpha-alumina supports through fluorine-containing acid solution-treated and carried silver catalyst thereof.Described carrier adopts industrial hydrated alumina to be prefabricated into the semi-finished product alpha-alumina supports particle of the alkaline including earth metal of definite shape, adopts afterwards certain density this semi-finished product carrier of fluorine-containing acid solution-treated, obtains after roasting again.After the gained carrier was made silver catalyst, it had higher activity, stability and service life.
Foregoing invention all mainly is activity, the stability that has improved silver catalyst, but to optionally the raising effect is little.Therefore, need at present a kind of optionally treatment technology of preformed catalyst carrier of silver catalyst that improves of exploitation, and by its silver catalyst of making and application process thereof.
Summary of the invention
Technical problem to be solved by this invention is the alkali treatment modifying method that a kind of alpha-alumina supports is provided for above-mentioned the deficiencies in the prior art, the method adopts certain density alkaline solution under heating and stirring condition the moulding alpha-alumina supports to be processed, and has increased the duct of carrier.Make the silver catalyst of its load with the modification alpha-alumina supports that the method makes, be conducive to the diffusion of product.Therefore, this modification alpha-alumina supports is applied to ethylene produces the reacting ethylene oxide process, its selective obviously raising.
For this reason, the invention provides a kind of alkali treatment modifying method of alpha-alumina supports, comprise alpha-alumina supports carried out alkali treatment after, the process of wash again, drying being produced the modification alpha-alumina supports; Wherein, described alkali treatment process is for heating the process of stir process with alkaline solution, and the concentration of described alkaline solution is 0.2～4mol/l, and reaction temperature is 20～200 ℃.The concentration of preferred described alkaline solution is 0.5～1.5mol/l, and reaction temperature is 40～100 ℃.
In an embodiment of the inventive method, the solid-liquid mass ratio of the alpha-alumina supports of described alkali treatment process and alkaline solution is 1: 1～1: 150, and the reaction time is 0.2～3h.
In a preferred embodiment of the inventive method, the solid-liquid mass ratio of the alpha-alumina supports of described alkali treatment process and alkaline solution is 1: 20～1: 60, and the reaction time is 0.5～1.5h.
According to the inventive method, described alkali is inorganic base and/or alkaline, inorganic salts, and it is selected from potassium hydroxide, a hydration ammonia, barium hydroxide, NaOH, calcium hydroxide, magnesium hydroxide or the sodium carbonate any one, or the mixture more than two kinds wherein.In preferred potassium hydroxide, NaOH, the sodium carbonate any one, or the mixture of two kinds or three kinds wherein.
In one embodiment of the invention, described alpha-alumina supports is the alpha-alumina supports of moulding, and its raw material is a kind of mixture, comprising:
Three water α-Al
2O
3, its content is 50～90wt%, particle diameter is 200 orders～500 orders;
A false water Al
2O
3, its content is 5～50wt%, particle diameter is 200 orders～400 orders;
Heavy alkaline earth metal compound, its content is 0～1.5wt%;
Fluoride-mineralization agent, its content are 0.1～3.0wt%;
Binding agent, its content are 15～60wt%;
Water, an amount of.
In another embodiment of the present invention, the alpha-alumina supports of described moulding is the common form in this area, comprises annular, sphere, cylindricality or porous column shape, or other shape.
According to the inventive method, described water-washing process is with the α-Al after alkali treatment with deionized water
2O
3Carrier is washed till filtrate and is neutral.The baking temperature of described dry run is 60～180 ℃, and preferred baking temperature is 80～120 ℃.
The present invention also provides a kind of preparation method of silver catalyst of the modification alpha-alumina supports load that makes with method of the present invention, comprising:
Steps A is with silver catalyst maceration extract dipping modification alpha-alumina supports;
Step B, leaching silver catalyst maceration extract;
Step C has the modification alpha-alumina supports activation of silver catalyst maceration extract to make the silver catalyst of modification alpha-alumina supports load load;
Wherein, the specific area of the alpha-alumina supports of modification described in the steps A is 0.2～2.0m
2/ g, pore volume are 0.35～0.85ml/g, water absorption rate 〉=30%, and crushing strength is 20～140N/ grain.
In one embodiment of the invention, the maceration extract of silver catalyst described in the steps A comprises:
Silver compound, its consumption are 1～40wt%;
Alkali metal promoter, its consumption are 5～2000wt ppm;
Base earth metal promoter, its consumption are 0～10000wt ppm;
Rhenium auxiliary agent, its consumption are 10～2000wt ppm;
Organic amine, its consumption are 1～24wt%.
According to the present invention, in the described silver catalyst maceration extract, described silver compound is major catalyst, and described alkali metal promoter, base earth metal promoter, rhenium auxiliary agent etc. are catalyst promoter.
In a preferred embodiment of the present invention, the maceration extract of silver catalyst described in the steps A comprises:
Silver compound, its consumption are 5～25wt%;
Alkali metal promoter, its consumption are 5～1500wt ppm;
Base earth metal promoter, its consumption are 0～8000wt ppm;
Rhenium auxiliary agent, its consumption are 100～1000wt ppm.
According to the inventive method, described silver compound comprises silver oxide, silver nitrate and/or silver oxalate; Described alkali metal promoter is to be selected from the compound of lithium, sodium, potassium, rubidium or caesium one or more, and comprising cesium sulfate, cesium nitrate, lithium nitrate and/or potassium hydroxide, the preferred as alkali auxiliary agent is cesium sulfate; Described base earth metal promoter is to be selected from the compound of magnesium, calcium, strontium or barium one or more, comprising in oxide, oxalates, sulfate, acetate and the nitrate of magnesium, calcium, strontium and barium one or more; Described rhenium auxiliary agent is selected from one or more in oxide, perrhenic acid, perrhenic acid caesium or the ammonium perrhenate of rhenium, and preferred described rhenium auxiliary agent is ammonium perrhenate; Described organic amine is pyridine, butylamine, ethylenediamine, 1, and 3-propane diamine, monoethanolamine or its mixture, preferred described organic amine are the mixture of ethylenediamine and monoethanolamine.
In a preferred embodiment according to the present invention, the maceration extract of silver catalyst described in the steps A also comprises the coassist agent of rhenium auxiliary agent, with the activity of further improvement gained silver catalyst, selective and stable.The coassist agent of described rhenium auxiliary agent can be the compound of arbitrary transition metal in the periodic table of elements, or the mixture of several transistion metal compounds, oxyacid and the salt thereof of preferred group vib and VIIB family element, such as wolframic acid, sodium tungstate, potassium tungstate, ammonium tungstate, wolframic acid caesium, molybdic acid, ammonium molybdate, ammonium metatungstate etc., its consumption is 0～1000wt ppm, and preferably its consumption is 0～500wt ppm.
According to the inventive method, described dipping process is to carry out being lower than under the atmospheric pressure, preferably carries out under less than the condition of 10mmHg in vacuum, and dip time is 10～60min.
According to the inventive method, the described activation of step C is to carry out in air or oxygen content are not more than the nitrogen oxygen atmosphere of 21v%.Its activation temperature is 180～700 ℃, and soak time is 1～120min; Preferred described activation temperature is 200～500 ℃, and soak time is 2～60min.
The present invention also provides a kind of application of silver catalyst in ethylene production oxirane process of modification alpha-alumina supports load of method preparation of the present invention.Wherein, described ethylene oxidation reactions is carried out under oxygen and silver catalyst existence condition, and described silver catalyst is the silver catalyst of the modification alpha-alumina supports load that makes by alkali treatment modifying.Described reaction temperature is 200～275 ℃.
In the present invention, the specific area of carrier adopts nitrogen physisorption BET method to measure according to international testing standard ISO-9277.For example, can use the U.S. NOVA2000e of Kang Ta company type nitrogen physisorption instrument to measure the specific area of carrier.
The pore volume of carrier adopts mercury injection method to measure.For example, can use the AutoPore9510 of U.S. Merck ﹠ Co., Inc type mercury injection apparatus to measure the pore volume of carrier.
The amount of alkaline earth metal compound can obtain by calculating or measure (as adopting x-ray fluorescence analysis) in the carrier.
The side pressure strength of carrier for example, can adopt Dalian Chemical Research ﹠. Design Inst. to produce DL II type intelligence detector for strength of particles, chooses at random 30 support samples, and measuring radially averages after the crushing strength obtains.
Used term " water absorption rate " refers to the volume of the carrier saturated adsorption water of unit mass among the present invention, and unit is ml/g.Assay method is as follows, at first takes by weighing a certain amount of carrier and (supposes that its quality is m
1), in boiling water, to boil behind the 1h carrier taken out and be erected at the moderate wet gauze of water content and remove the unnecessary moisture of carrier surface, the quality of the carrier after the last weighing adsorbed water (is assumed to m
2), calculate as follows the water absorption rate of carrier.
Water absorption rate=(m
2-m
1)/m
1/ ρ
Water
ρ wherein
WaterThe density of measuring water under temperature, the atmospheric pressure.
According to the inventive method alpha-alumina supports is carried out modification, the more horn of plenty of the unmodified carrier of orifice throat ratio of the modification alpha-alumina supports that obtains, the silver catalyst of being made by this modification alpha-alumina supports demonstrates good selective in ethylene is produced the process of oxirane.The present invention all is easy to obtain to the raw material that alumina support carries out modification, and preparation method's step is simple.
Description of drawings
Come the present invention is described in further detail below in conjunction with accompanying drawing:
Fig. 1 is the scanning electron microscope (SEM) photograph of the unmodified alpha-alumina supports of embodiment 1 preparation.
Fig. 2 is the scanning electron microscope (SEM) photograph of the modification alpha-alumina supports of embodiment 6 preparations.
The specific embodiment
Describe the present invention in detail below in conjunction with embodiment and accompanying drawing, these embodiment and accompanying drawing only play the illustrative effect, are not limited to range of application of the present invention.
Embodiment 1 preparation α-Al
2O
3Carrier, and as the Comparative Examples of embodiment 2～7; α-Al that embodiment 2～7 makes embodiment 1 under different reaction conditions respectively
2O
3Carrier carries out alkali treatment, makes modified alpha-Al
2O
3Carrier; α-Al that embodiment 8 adopts embodiment 1 to make
2O
3Carrier prepares silver catalyst, and as the Comparative Examples of embodiment 9～14; Modified alpha-Al that embodiment 9～14 adopts respectively embodiment 2～7 to make
2O
3Carrier prepares silver catalyst.The mensuration of catalyst performance
The various silver catalysts that relate among the present invention are tested its initial activity and selective with laboratory microreactor (hereinafter to be referred as " little anti-") evaluating apparatus.The reactor that the micro anti-evaluation device uses is the stainless steel tube of internal diameter 4mm, and reactor places heating jacket.The admission space of catalyst is 1ml, and inert filler is arranged at the bottom, makes beds be positioned at the flat-temperature zone of heating jacket.
The condition determination of the catalyst activity and selectivity that the present invention uses is as follows:
Reacting gas forms (mol%)
When stable reach above-mentioned reaction condition after the METHOD FOR CONTINUOUS DETERMINATION reactor enter, exit gas forms.Measurement result carries out calculating as follows after volume contraction is proofreaied and correct selective S:
Wherein Δ EO be work off one's feeling vent one's spleen poor with the inlet gas ethylene oxide concentration, Δ CO
2Be to work off one's feeling vent one's spleen poorly with the inlet gas gas concentration lwevel, get the result of the test of the average of 10 groups of above test datas as the same day.
Embodiment
Embodiment 1: preparation α-Al
2O
3Carrier
With 200～500 purposes, three water α-Al
2O
3403g, the false water Al of 200～400 purposes
2O
381g, NH
4F3g and BaSO
4Mix 0.5g put into blender, then change in the kneader, add rare nitric acid (nitric acid: water=1: 3, weight ratio) 90ml, but be kneaded into the paste of extrusion molding.Extrusion molding is the five hole columns of external diameter 8.0mm, long 6.0mm, internal diameter 1.0mm, at 80～120 ℃ of lower dry 10h, free water content is reduced to below the 10wt%, makes moulding alpha-alumina supports green compact.Then these green compact are put into electric furnace, be elevated to 1400 ℃ through 30h from room temperature, constant temperature 2h is with prepared white α-Al
2O
3Carrier called after Z-1, and measure its crushing strength and water absorption rate, the results are shown in Table 1, the stereoscan photograph of this carrier is seen Fig. 1.
Embodiment 2: preparation modified alpha-Al
2O
3Carrier
Press the Ba (OH) of solid-liquid mass ratio preparation in 1: 1 20g 0.2mol/l
2Solution, and with Ba (OH)
2Solution temperature constant temperature to 20 ℃ takes by weighing 20g Z-1 carrier and puts into Ba (OH)
2Solution, stir 0.2h after, carrier is taken out, use washed with de-ionized water, to filtrate pH value be about 7.Then carrier is put into baking oven in 100 ℃ of dry 10h, with prepared modification alpha-alumina supports called after Z-2, and measure its crushing strength and water absorption rate, the results are shown in Table 1.
Embodiment 3: preparation modified alpha-Al
2O
3Carrier
Press the Ca (OH) of solid-liquid mass ratio preparation in 1: 150 3000g 4.0mol/l
2Solution, and with Ca (OH)
2Solution is heated to 200 ℃, takes by weighing 20g Z-1 carrier and puts into Ca (OH)
2Solution, stir 3.0h after, carrier is taken out, use washed with de-ionized water, to filtrate pH value be about 7.Then carrier is put into baking oven in 100 ℃ of dry 10h, with prepared modification alpha-alumina supports called after Z-3, and measure its crushing strength and water absorption rate, the results are shown in Table 1.
Embodiment 4: preparation modified alpha-Al
2O
3Carrier
Press the Mg (OH) of solid-liquid mass ratio preparation in 1: 20 400g 0.5mol/l
2Solution, and with Mg (OH)
2Solution is heated to 40 ℃, takes by weighing 20g Z-1 carrier and puts into Mg (OH)
2Solution, stir 0.5h after, carrier is taken out, use washed with de-ionized water, to filtrate pH value be about 7.Then carrier is put into baking oven in 100 ℃ of dry 10h, with prepared modification alpha-alumina supports called after Z-4, and measure its crushing strength and water absorption rate, the results are shown in Table 1.
Embodiment 5: preparation modified alpha-Al
2O
3Carrier
Press the KOH solution of solid-liquid mass ratio 1: 30 preparation 600g 0.8mol/l, and KOH solution be heated to 60 ℃, take by weighing 20g Z-1 carrier and put into KOH solution, stir 0.8h after, carrier is taken out, use washed with de-ionized water, to filtrate pH value be about 7.Then carrier is put into baking oven in 100 ℃ of dry 10h, with prepared modification alpha-alumina supports called after Z-5, and measure its crushing strength and water absorption rate, the results are shown in Table 1.
Embodiment 6: preparation modified alpha-Al
2O
3Carrier
Press the NaOH solution of solid-liquid mass ratio 1: 40 preparation 800g 1.2mol/l, and NaOH solution be heated to 80 ℃, take by weighing 20g Z-1 carrier and put into NaOH solution, stir 1.1h after, carrier is taken out, use washed with de-ionized water, to filtrate pH value be about 7.Then carrier is put into baking oven in 100 ℃ of dry 10h, with prepared modification alpha-alumina supports called after Z-6, and measure its crushing strength and water absorption rate, the results are shown in Table 1, the stereoscan photograph of this carrier is seen Fig. 2.
Embodiment 7: preparation modified alpha-Al
2O
3Carrier
Press the Na of solid-liquid mass ratio preparation in 1: 60 1200g 1.5mol/l
2CO
3Solution, and with Na
2CO
3Solution is heated to 100 ℃, takes by weighing 20g Z-1 carrier and puts into Na
2CO
3Solution, stir 1.5h after, carrier is taken out, use washed with de-ionized water, to filtrate pH value be about 7.Then carrier is put into baking oven in 100 ℃ of dry 10h, with prepared modification alpha-alumina supports called after Z-7, and measure its crushing strength and water absorption rate, the results are shown in Table 1.
Table 1
| Embodiment | 1 | 2 | 3 | 4 | 5 | 6 | 7 |
| Support samples | Z-1 | Z-2 | Z-3 | Z-4 | Z-5 | Z-6 | Z-7 |
| Crushing strength (N/ grain) | 126 | 127 | 110 | 127 | 129 | 131 | 129 |
| Water absorption rate (%) | 50.54 | 50.56 | 53.2 | 50.82 | 51.06 | 51.20 | 51.03 |
| Specific area (m 2/g) | 1.438 | 1.419 | 1.412 | 1.420 | 1.396 | 1.313 | 1.399 |
Embodiment 8: the preparation silver catalyst
The 700g silver nitrate is dissolved in the 750ml deionized water makes liquor argenti nitratis ophthalmicus; The 325g ammonium oxalate is dissolved in the deionized water of 50 ℃ of 250ml and makes ammonium oxalate solution; Liquor argenti nitratis ophthalmicus evenly mixes with ammonium oxalate solution under vigorous stirring, generates white silver oxalate precipitation; Behind the aging 1h of silver oxalate precipitation, filter, and with the deionized water washing leaching cake until in the filtrate without nitrate ion, make paste silver oxalate filter cake, the silver-colored approximately 60wt% of containing metal in the filter cake that obtains, moisture approximately 15wt%.
With the 300g ethylenediamine, 110g monoethanolamine and 375g deionized water add glass flask, stir, after mixing, in prepared mixed solution, slowly add the paste silver oxalate while stirring, temperature remains between-5 ℃ to 10 ℃, silver oxalate is all dissolved, then add 2.2g cesium sulfate and 1.4g strontium acetate, add again deionized water and make the solution gross mass reach 2000g, make the silver catalyst maceration extract, the silver content of the silver compound maceration extract that obtains is 22wt%.
Get the support samples Z-1 that 15g embodiment 1 makes and put into the container that can vacuumize.Vacuum is evacuated to and is lower than 10mmHg, adds the silver catalyst maceration extract, and the submergence carrier keeps 30min.Then unnecessary silver catalyst maceration extract is removed in leaching.Carrier behind the dipping is heated 5min in 350 ℃ air stream, cooling, with obtained silver catalyst called after CZ-1, content (wherein content is all in metal) to the silver in the obtained silver catalyst and auxiliary agent is analyzed, and use the microreactor evaluating apparatus to measure its activity and selectivity, the results are shown in Table 2.
Embodiment 9: the preparation silver catalyst
Embodiment 9 changes carrier Z-1 as different from Example 8 and makes carrier Z-2, with obtained silver catalyst called after CZ-2, content (wherein content is all in metal) to the silver in the obtained silver catalyst and auxiliary agent is analyzed, and use the microreactor evaluating apparatus to measure its activity and selectivity, the results are shown in Table 2.
Embodiment 10: the preparation silver catalyst
Embodiment 10 changes carrier Z-1 as different from Example 8 and makes carrier Z-3, with obtained silver catalyst called after CZ-3, content (wherein content is all in metal) to the silver in the obtained silver catalyst and auxiliary agent is analyzed, and use the microreactor evaluating apparatus to measure its activity and selectivity, the results are shown in Table 2.
Embodiment 11: the preparation silver catalyst
Embodiment 11 changes carrier Z-1 as different from Example 8 and makes carrier Z-4, with obtained silver catalyst called after CZ-4, content (wherein content is all in metal) to the silver in the obtained silver catalyst and auxiliary agent is analyzed, and use the microreactor evaluating apparatus to measure its activity and selectivity, the results are shown in Table 2.
Embodiment 12: the preparation silver catalyst
Embodiment 12 changes carrier Z-1 as different from Example 8 and makes carrier Z-5, with obtained silver catalyst called after CZ-5, content (wherein content is all in metal) to the silver in the obtained silver catalyst and auxiliary agent is analyzed, and use the microreactor evaluating apparatus to measure its activity and selectivity, the results are shown in Table 2.
Embodiment 13: the preparation silver catalyst
Embodiment 13 changes carrier Z-1 as different from Example 8 and makes carrier Z-6, with obtained silver catalyst called after CZ-6, content (wherein content is all in metal) to the silver in the obtained silver catalyst and auxiliary agent is analyzed, and use the microreactor evaluating apparatus to measure its activity and selectivity, the results are shown in Table 2.
Embodiment 14: the preparation silver catalyst
Embodiment 14 changes carrier Z-1 as different from Example 8 and makes carrier Z-7, with obtained silver catalyst called after CZ-7, content (wherein content is all in metal) to the silver in the obtained silver catalyst and auxiliary agent is analyzed, and use the microreactor evaluating apparatus to measure its activity and selectivity, the results are shown in Table 2.
Table 2 (in the table listed reaction temperature and selectively be the data of reaction when proceeding to the 20th day)
Respectively with above-described embodiment 2～7 and embodiment 1, and embodiment 9～14 compares and can find out with embodiment 8, and alpha-alumina supports is carried out the duct that alkali treatment has increased carrier.Make the silver catalyst of its load with the modification alpha-alumina supports that the method makes, be conducive to the diffusion of reaction product; This modification alpha-alumina supports is applied to ethylene produces the reacting ethylene oxide process, the selective of catalyst obviously improves.
The above only is preferred embodiment of the present invention; but protection domain of the present invention is not limited to this; any those skilled in the art can easily change or change in technical scope disclosed by the invention, and this change or variation all should be encompassed within protection scope of the present invention.Therefore, protection scope of the present invention should be as the criterion with the protection domain of claims.
Claims (10)
1. the alkali treatment modifying method of an alpha-alumina supports, comprise alpha-alumina supports carried out alkali treatment after, the process of wash again, drying being produced the modification alpha-alumina supports; Wherein, described alkali treatment process is for heating the process of stir process with alkaline solution, and the concentration of described alkaline solution is 0.2～4mol/l, and reaction temperature is 20～200 ℃.
2. method according to claim 1, it is characterized in that: the concentration of described alkaline solution is 0.5～1.5mol/l, reaction temperature is 40～100 ℃.
3. method according to claim 1 and 2, it is characterized in that: the solid-liquid mass ratio of the alpha-alumina supports of described alkali treatment process and alkaline solution is 1: 1～1: 150, the reaction time is 0.2～3h.
4. method according to claim 3, it is characterized in that: the solid-liquid mass ratio of the alpha-alumina supports of described alkali treatment process and alkaline solution is 1: 20～1: 60, the reaction time is 0.5～1.5h.
5. method according to claim 1, it is characterized in that: described alkali is inorganic base and/or alkaline, inorganic salts, it is selected from potassium hydroxide, a hydration ammonia, barium hydroxide, NaOH, calcium hydroxide, magnesium hydroxide or the sodium carbonate any one, or the mixture more than two kinds wherein; In preferred potassium hydroxide, NaOH, the sodium carbonate any one, or the mixture of two kinds or three kinds wherein.
One kind according to claim 1～5 in the preparation method of silver catalyst of the modification alpha-alumina supports load that makes of the described method of any one, comprising:
Steps A is with silver catalyst maceration extract dipping modification alpha-alumina supports;
Step B, leaching silver catalyst maceration extract;
Step C has the modification alpha-alumina supports activation of silver catalyst maceration extract to make the silver catalyst of alpha-alumina supports load load;
It is characterized in that: the specific area of the alpha-alumina supports of modification described in the steps A is 0.2～2.0m
2/ g, pore volume are 0.35～0.85ml/g, water absorption rate 〉=30%, and crushing strength is 20～140N/ grain.
7. method according to claim 6, it is characterized in that: the maceration extract of silver catalyst described in the steps A comprises:
Silver compound, its consumption are 1～40wt%;
Alkali metal promoter, its consumption are 5～2000wt ppm;
Base earth metal promoter, its consumption are 0～10000wt ppm;
Rhenium auxiliary agent, its consumption are 10～2000wt ppm;
Organic amine, its consumption are 1～24wt%.
8. method according to claim 7, it is characterized in that: described silver catalyst maceration extract comprises:
Silver compound, its consumption are 5～25wt%;
Alkali metal promoter, its consumption are 5～1500wt ppm;
Base earth metal promoter, its consumption are 0～8000wt ppm;
Rhenium auxiliary agent, its consumption are 100～1000wt ppm.
9. method according to claim 6 is characterized in that: the described activation of step C is to carry out in air or oxygen content are not more than the nitrogen oxygen atmosphere of 21v%.
One kind according to claim 6～9 in the silver catalyst of modification alpha-alumina supports load of the described method of any one preparation produce application in the oxirane process at ethylene.
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289650A (en) * | 2015-10-09 | 2016-02-03 | 江苏常青树新材料科技有限公司 | Preparation method of catalyst used for carrying out catalytic combustion on volatile organic compound containing low-concentration methane |
| CN105618080A (en) * | 2016-01-30 | 2016-06-01 | 凯姆德（北京）能源环境科技有限公司 | Ozone catalytic oxidation catalyst for treating reverse osmosis concentrated water and preparation method of catalyst |
| CN106031865A (en) * | 2015-03-09 | 2016-10-19 | 中国石油天然气股份有限公司 | Preparation method of alumina carrier and silver-loaded catalyst, and catalyst |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5801259A (en) * | 1996-04-30 | 1998-09-01 | Shell Oil Company | Ethylene oxide catalyst and process |
| CN1467028A (en) * | 2002-07-10 | 2004-01-14 | 中国石油化工股份有限公司 | Method for preparing vinyl epoxide argentum catalyst |
| CN1634652A (en) * | 2003-12-31 | 2005-07-06 | 中国石油化工股份有限公司北京燕山分公司研究院 | Silver catalyst carrier for epoxyethane production, preparation method and application thereof |
| CN101007287A (en) * | 2006-01-28 | 2007-08-01 | 中国石油化工股份有限公司 | Carrier of ethylene oxide silver catalyst, and its preparation method and application |
| CN102133544A (en) * | 2010-01-25 | 2011-07-27 | 中国石油化工股份有限公司 | Alkaline-earth metal fluoride modified alumina supporter, preparation method thereof, and silver catalyst made from alumina supporter and application of silver catalyst in ethylene epoxide (EO) production |
-
2012
- 2012-03-28 CN CN201210086813.8A patent/CN103357436B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5801259A (en) * | 1996-04-30 | 1998-09-01 | Shell Oil Company | Ethylene oxide catalyst and process |
| CN1467028A (en) * | 2002-07-10 | 2004-01-14 | 中国石油化工股份有限公司 | Method for preparing vinyl epoxide argentum catalyst |
| CN1634652A (en) * | 2003-12-31 | 2005-07-06 | 中国石油化工股份有限公司北京燕山分公司研究院 | Silver catalyst carrier for epoxyethane production, preparation method and application thereof |
| CN101007287A (en) * | 2006-01-28 | 2007-08-01 | 中国石油化工股份有限公司 | Carrier of ethylene oxide silver catalyst, and its preparation method and application |
| CN102133544A (en) * | 2010-01-25 | 2011-07-27 | 中国石油化工股份有限公司 | Alkaline-earth metal fluoride modified alumina supporter, preparation method thereof, and silver catalyst made from alumina supporter and application of silver catalyst in ethylene epoxide (EO) production |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
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| CN106031865B (en) * | 2015-03-09 | 2018-10-16 | 中国石油天然气股份有限公司 | Preparation method of alumina carrier and silver-loaded catalyst, and catalyst |
| CN105289650A (en) * | 2015-10-09 | 2016-02-03 | 江苏常青树新材料科技有限公司 | Preparation method of catalyst used for carrying out catalytic combustion on volatile organic compound containing low-concentration methane |
| CN105618080A (en) * | 2016-01-30 | 2016-06-01 | 凯姆德（北京）能源环境科技有限公司 | Ozone catalytic oxidation catalyst for treating reverse osmosis concentrated water and preparation method of catalyst |
| CN108097200A (en) * | 2016-11-25 | 2018-06-01 | 中国石油化工股份有限公司 | A kind of method for preparing modified aluminas |
| CN108097201A (en) * | 2016-11-25 | 2018-06-01 | 中国石油化工股份有限公司 | A kind of modified aluminas and preparation method thereof |
| CN108097201B (en) * | 2016-11-25 | 2020-08-07 | 中国石油化工股份有限公司 | Modified alumina and preparation method thereof |
| CN108097200B (en) * | 2016-11-25 | 2020-08-11 | 中国石油化工股份有限公司 | Method for preparing modified alumina |
| CN111905732A (en) * | 2019-05-09 | 2020-11-10 | 中国石油化工股份有限公司 | Silver catalyst and activation method and application thereof |
| CN111151256A (en) * | 2020-01-20 | 2020-05-15 | 山东玉皇化工有限公司 | Catalyst for synthesizing hexamethylene diamine |
| CN111151256B (en) * | 2020-01-20 | 2023-03-24 | 山东玉皇化工有限公司 | Catalyst for synthesizing hexamethylene diamine |
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