CN103285904B - Hydrogenation catalyst, and preparation method and application thereof - Google Patents
Hydrogenation catalyst, and preparation method and application thereof Download PDFInfo
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Abstract
The invention discloses a hydrogenation catalyst, and a preparation method and application thereof. The hydrogenation catalyst comprises a supporter and a hydrogenation active component supported on the supporter, wherein the supporter is rod-like SBA-15, and the hydrogenation active component contains one or more of Ru, Rh and Pd. By using the rod-like SBA-15 as the supporter of the hydrogenation catalyst, the hydrogenation catalyst provided by the invention has higher activity and selectivity than the hydrogenation catalyst using silicon dioxide or the like as the supporter in the prior art.
Description
Technical field
The present invention relates to a kind of hydrogenation catalyst and its preparation method and application.
Background technology
Cyclohexene and be important Organic Chemicals by its derivative downstream product adipic acid, nylon 6, nylon66 fiber, polyamide, polyester, has important industrial use and wide market prospects.By the important source material cyclohexene adopting benzene selective hydrogenation can prepare other multiple fine chemicals of synthesis.
The method of traditional mode of production cyclohexene is generally divided into two classes.One class take benzene as the multi-step synthetic route of raw material, first makes cyclohexane or cyclohexane halide by benzene, then cyclohexane made cyclohexanol and dewater and form cyclohexene or cyclohexane halide dehydrohalogenation is formed cyclohexene.Another kind of is be the one-step synthesis method route of raw material with benzene, is namely that feedstock portions hydrogenation generates corresponding cyclohexene with benzene, and this synthetic route is paid close attention to widely due to technique simple and fast.
As the method by making partial hydrogenation of benzene produce cyclohexene, the general ruthenium metal that adopts is as catalyst, and hydrogenation reaction is carried out under hydrated metal salt exists.Have many requirements for this kind of ruthenium catalyst, such as metal Ru is originally as fine grained, and silica, aluminium oxide, barium sulfate or zirconium silicate can be used as metal Ru described in supported carrier.But, not the cyclohexene adopting the preparation method of this kind of routine to prepare selective not high, and catalyst activity is lower, catalyst life is not long.In addition, also need in reaction system, to add such as slaine, acid or alkali as additive to improve the selective of cyclohexene in the method for routine, this not only can the corrosion of accelerating reactor or damage, also can spent catalyst.Therefore, from industrial point of view, even if also need a kind ofly not add the hydrogenation catalyst that this kind of additive also can improve cyclohexene yield.
Summary of the invention
The object of the invention is to the hydrogenation reaction overcoming prior art, the activity particularly preparing the hydrogenation catalyst adopted in the hydrogenation reaction of cyclohexene for benzene selective hydrogenation is lower, selective lower problem, and provide a kind of activity higher, selective good hydrogenation catalyst, and, hydrogenation catalyst of the present invention is applied to can reduce Metal Salts when benzene selective hydrogenation prepares cyclohexene consumption even without the need to adding Metal Salts, just can improve the selective of cyclohexene, in addition, the corrosion of Metal Salts to equipment and the consumption to hydrogenation catalyst can also be reduced further.
To achieve these goals, the invention provides a kind of hydrogenation catalyst, this catalyst comprises carrier and load hydrogenation active component on this carrier, wherein, described carrier is bar-shaped SBA-15, described hydrogenation active component contain be selected from Ru, Rh and Pd one or more.
Present invention also offers the preparation method of hydrogenation catalyst, the method comprises the soluble salt solutions of hydrogenation active component and carrier contact, and the carrier after contact is carried out drying, roasting; Wherein, described carrier is bar-shaped SBA-15, described hydrogenation active component contain be selected from Ru, Rh and Pd one or more.
Present invention also offers the application of described hydrogenation catalyst in hydrogenation reaction.
The present invention is by using bar-shaped SBA-15 as the carrier of hydrogenation catalyst, hydrogenation catalyst of the present invention is made to have higher activity and selectivity compared to employing silica of prior art etc. as the hydrogenation catalyst of carrier, supposition is: because described bar-shaped SBA-15 carrier is a kind of mesopore molecular sieve, on the one hand, bar-shaped SBA-15 has larger specific area and relatively large aperture, and its special microstructure makes it to be better combined with hydrogenation active component, and hydrogenation active component can disperse more even, on the other hand, the mesopore orbit of bar-shaped SBA-15 carrier has carrier and reactor dual-use function, therefore, it is possible to improve the activity and selectivity of hydrogenation catalyst further.
Other features and advantages of the present invention are described in detail in detailed description of the invention part subsequently.
Detailed description of the invention
Below the specific embodiment of the present invention is described in detail.Should be understood that, detailed description of the invention described herein, only for instruction and explanation of the present invention, is not limited to the present invention.
According to the present invention, described hydrogenation catalyst comprises carrier and load hydrogenation active component on this carrier, and wherein, described carrier is bar-shaped SBA-15, described hydrogenation active component contain be selected from Ru, Rh and Pd one or more.
The present invention is by using bar-shaped SBA-15 as the carrier of hydrogenation catalyst, hydrogenation catalyst of the present invention is made to have higher activity and selectivity compared to employing silica of prior art etc. as the hydrogenation catalyst of carrier, supposition is: because described bar-shaped SBA-15 carrier is a kind of mesopore molecular sieve, on the one hand, bar-shaped SBA-15 has larger specific area and relatively large aperture, and its special microstructure makes it to be better combined with hydrogenation active component, and hydrogenation active component can disperse more even, on the other hand, the mesopore orbit of bar-shaped SBA-15 carrier has carrier and reactor dual-use function, therefore, it is possible to improve the activity and selectivity of hydrogenation catalyst further.
In the present invention, described bar-shaped SBA-15 can be the formed body of bar-shaped SBA-15, also can for being directly bar-shaped SBA-15 (being generally Powdered), the present invention to this without particular/special requirement.
In the present invention, as long as ensure that described carrier is that bar-shaped SBA-15 can realize object of the present invention, the hole dimension as the bar-shaped SBA-15 of described carrier can be the known hole dimension of technical staff in Zeolite synthesis field.For the present invention, in order to improve the activity and selectivity of described hydrogenation catalyst of the present invention further, the present inventor finds in research process, be 6-10 nanometer at the most probable pore size of bar-shaped SBA-15 carrier, pore volume is 0.5-1.5 ml/g, when BET specific surface area is 600-700 meters squared per gram, described catalyst can be made to have higher catalytic activity.More preferably, the most probable pore size of SBA-15 is 6-6.5 nanometer, and pore volume is 0.8-1.2 ml/g, and BET specific surface area is 600-660 meters squared per gram.Further, the length of the rod of described bar-shaped SBA-15 carrier can be selected and change in wider scope, such as, can be 30-100 micron usually.
The SBA-15 meeting above-mentioned condition can be commercially available.Such as: be purchased the SBA-15 from high-tech limited company of Changchun Jilin University.
In the present invention, as long as ensure that described carrier is that bar-shaped SBA-15 can realize object of the present invention, therefore, the present invention is to the kind of described hydrogenation active component and consumption without particular/special requirement, and its range of choices is wider.For the present invention, under preferable case, described hydrogenation active component contain be selected from Ru, Rh and Pd one or more.More preferably in situation, in order to improve the activity of described hydrogenation catalyst further, described hydrogenation active component also containing be selected from Zn, Fe, Co, Ni and Mn one or more, and the gross weight of Ru, Rh and Pd is 0.01-100: 1 with the gross weight ratio of Zn, Fe, Co, Ni and Mn, more preferably 0.05-50: 1, be especially preferably 0.5-30: 1.
The range of choices of the hydrogenation active component in hydrogenation catalyst provided by the invention and the content of carrier is wider, and can select with reference to prior art, for the present invention, under preferable case, in described hydrogenation catalyst, hydrogenation active component is with the content of oxide basis for 0.1-50 % by weight, and the content of carrier is 50-99.9 % by weight; More preferably, in situation, in described hydrogenation catalyst, hydrogenation active component is with the content of oxide basis for 1-20 % by weight, and the content of carrier is 80-99 % by weight.
Hydrogenation catalyst of the present invention can be prepared with reference to the various methods of prior art, such as can adopt conventional infusion process preparation, can select according to the concrete form of bar-shaped SBA-15 carrier, if such as carrier is the formed body of bar-shaped SBA-15, such as dry impregnation method (i.e. equi-volume impregnating) then can be selected to be prepared, if carrier directly adopts bar-shaped SBA-15 (Powdered), then such as incipient wetness can be selected to carry out dipping preparation.In the present invention, the bar-shaped SBA-15 of preferred employing powder prepares hydrogenation catalyst, when adopting the bar-shaped SBA-15 of powder to prepare hydrogenation catalyst, incipient wetness can be selected to prepare catalyst of the present invention, described incipient wetness such as can be carried out as follows: by the soluble salt solutions of hydrogenation active component and bar-shaped SBA-15 carrier contact, and the carrier after contact is carried out drying, roasting.Wherein, when hydrogenation active component is multiple element, the method for the soluble salt solutions of hydrogenation active component and bar-shaped SBA-15 carrier contact can be undertaken by the following two kinds method: (1) soluble-salt of various active component can be made after a kind of mixed solution again with described carrier contact; (2) also the soluble-salt of different active components can be made into the aqueous solution separately, then carrier be contacted with the soluble salt solutions of various active component (order contacted with the soluble salt solutions of various active component can be selected arbitrarily) successively.
According to the present invention, as Ru, Rh and Pd of described main active component, the range of choices of the kind of their soluble-salt is wider, and conventional soluble-salt all can be used for the present invention, such as, can be its respective chloride, nitrate etc., preferably chloride.In addition, the soluble-salt of other active components preferably contained, such as, one or more in Zn, Fe, Co, Ni and Mn.The range of choices of the kind of their soluble-salt is wider, and conventional soluble-salt all can be used for the present invention, such as, can be one or more in halide, acetate, sulfate and nitrate, is preferably nitrate.
According to the preparation method of hydrogenation catalyst of the present invention, the character of described bar-shaped SBA-15 aforementioned to the description of hydrogenation catalyst in be described in detail, do not repeat them here.
According to the preparation method of hydrogenation catalyst of the present invention, the selection of the kind of described hydrogenation active component aforementioned to the description of hydrogenation catalyst in be described in detail, do not repeat them here.
According to the preparation method of hydrogenation catalyst of the present invention, the range of choices of the consumption of the soluble-salt of described active component is wider, can select according to prior art, for the present invention, the consumption of the soluble-salt of preferred described active component makes in the hydrogenation catalyst prepared, hydrogenation active component with the content of oxide basis for 0.1-50 % by weight, the content of carrier is 50-99.9 % by weight, more preferably the consumption of the soluble-salt of described active component makes in the hydrogenation catalyst prepared, hydrogenation active component with the content of oxide basis for 1-20 % by weight, the content of carrier is 80-99 % by weight.
In the present invention, the range of choices of the solution type of described soluble salt solutions is wider, is generally the aqueous solution, depending on the circumstances or the needs of the situation, solvent for the formation of solution can also be the organic solvents such as alcohol, ketone, oxolane, hexane and toluene, or is the mixed solution of described organic solvent and water.
According to the preparation method of hydrogenation catalyst of the present invention, the range of choices of the condition of described drying, roasting is wider, the drying of prior art, the condition of roasting all can realize object of the present invention, and the temperature of such as described drying is generally 100-200 DEG C, and the time is 0.5-10 hour.And the present inventor finds unexpectedly in research process, adopt bar-shaped SBA-15 of the present invention as carrier material, the activity and selectivity of hydrogenation catalyst of the present invention can be improved by the temperature reasonably controlling roasting further.Therefore, the temperature for the preferred described roasting of the present invention is 300-500 DEG C, and be more preferably 350-450 DEG C, the time is 0.5-12 hour, is more preferably 1-8 hour.
According to the hydrogenation catalyst that method of the present invention prepares, usually need before use first to carry out reducing and active component Ru, Rh and Pd being activated.Described reduction reducing agent used can be conventional various reducing agents, such as, and hydrogen, carbon monoxide, alcohol steam, hydrazine, formaldehyde and sodium borohydride etc.Be preferably hydrogen.The temperature that the condition of described activation generally includes activation is 80-500 DEG C, is preferably 100-450 DEG C.
In addition, by described hydrogenation catalyst is contacted with the aqueous solution of slaine the effect also can playing activating catalyst.Such as, described slaine can be the aqueous solution contact of carbonate, the salt of weak acid of acetate or the strong acid salt of hydrochloride, sulfate or nitrate of periodic table of elements I A major element and/or IIA major element and/or manganese, iron, cobalt, zinc etc.Be specifically as follows: the 0.1-100 described hydrogenation catalyst being immersed in hydrogenation catalyst weight doubly, is preferably in 0.1-10 described aqueous metal salt doubly and carries out activation process.The concentration of described aqueous metal salt can be 0.01-20 % by weight usually.Described contact conditions carries out usually under inert atmosphere or hydrogen atmosphere, and dry.The activity of further increase catalyst, preferably after the drying, carries out reduction treatment in hydrogen atmosphere.
Present invention also offers the application of described hydrogenation catalyst in hydrogenation reaction.Be specially adapted to benzene selective hydrogenation and prepare cyclohexene.Hydrogenation catalyst of the present invention, by adopting bar-shaped SBA-15 as carrier material, makes hydrogenation catalyst of the present invention for hydrogenation reaction, and particularly benzene selective hydrogenation is prepared in the method for cyclohexene and had higher activity and selectivity.Except adopting hydrogenation catalyst of the present invention, the condition that described benzene selective hydrogenation prepares cyclohexene can be carried out with reference to prior art well-known to those skilled in the art.
More than describe the preferred embodiment of the present invention in detail; but the present invention is not limited to the detail in above-mentioned embodiment, within the scope of technical conceive of the present invention; can carry out multiple simple variant to technical scheme of the present invention, these simple variant all belong to protection scope of the present invention.
It should be noted that in addition, each concrete technical characteristic described in above-mentioned detailed description of the invention, in reconcilable situation, can be combined by any suitable mode, in order to avoid unnecessary repetition, the present invention illustrates no longer separately to various possible combination.
In addition, also can be combined between various different embodiment of the present invention, as long as it is without prejudice to thought of the present invention, it should be considered as content disclosed in this invention equally.
Below will be described the present invention by embodiment.
In following preparation example and embodiment, described bar-shaped SBA-15 carrier is purchased from high-tech limited company of Changchun Jilin University, and specific nature is in table 1.
Table 1
In the present invention, gas chromatograph is adopted (to be purchased from Shanghai Precision Scientific Apparatus Co., Ltd, model is GC128) to analysis formed each in oil-phase product, undertaken quantitatively by correcting normalization method, all can refer to prior art to carry out, calculate the evaluation index such as the conversion ratio of benzene, the selective of cyclohexene on this basis.
Cyclohexene selective (%)=(molal quantity of the benzene consumed in the molal quantity/reaction of the cyclohexene of generation) × 100%,
The conversion ratio (%) of benzene=(molal quantity of the molal quantity of the benzene consumed in reaction/the be provided to benzene feedstock in reaction) × 100%.
Embodiment 1-6
The present embodiment is for illustration of the preparation of hydrogenation catalyst provided by the invention.
Under nitrogen protection, aforesaid for the present invention bar-shaped SBA-15 is calcined 10 hours at 400 DEG C, with eliminating hydroxide and Residual water, thus obtain the bar-shaped SBA-15 carrier through thermal activation, and prepare hydrogenation catalyst C1-C6 according to incipient wetness.Adopt incipient wetness to prepare hydrogenation catalyst and comprise the aqueous solution using ruthenic chloride respectively; The aqueous solution of ruthenic chloride and zinc chloride; The aqueous solution of ruthenic chloride, zinc chloride and nickel nitrate; The aqueous solution of radium chloride; The aqueous solution of radium chloride and cobaltous sulfate; The aqueous solution of palladium bichloride floods.Regulate the concentration of salt in the aqueous solution of aforementioned soluble-salt, prepare the hydrogenation catalyst C1-C6 containing different activities component composition, by the slaking 4 hours under room temperature (25 DEG C) of the solid that obtains after dipping, 120 DEG C of dryings 6 hours.Finally, calcine 2 hours in the air of dried solid at 450 DEG C, the feature of the catalyst prepared according to preceding method is listed in table 2.
Comparative example 1
This comparative example is for illustration of the preparation of the hydrogenation catalyst of prior art.
Hydrogenation catalyst is prepared according to the method for embodiment 1, unlike, with silica supports, (average grain diameter is 50 microns, and BET specific surface area is 70m
2/ g, aperture be the pore volume of 250-1500 dust account for that aperture is all well volume of 75-150000 dust 95%, aperture be the aperture of 350-1500 dust account for that aperture is all well volume of 75-150000 dust 85%) replace bar-shaped SBA-15 carrier, obtain reference catalyst CB1, the feature of described reference catalyst is listed in table 2.
Table 2
The total content (comprising the weight ratio between various active component) of hydrogenation active component in the hydrogenation catalyst of bar-shaped SBA-15 supported on carriers hydrogenation active component is determined at respectively by elementary analysis ICP, and the content of described carrier.
EXPERIMENTAL EXAMPLE 1-6
This EXPERIMENTAL EXAMPLE prepares cyclohexene for illustration of hydrogenation catalyst of the present invention is used for benzene selective hydrogenation.
The catalyst prepared by embodiment 1-6 respectively reduces 3 hours in the hydrogen gas stream at 200 DEG C, with activating catalyst.Gained catalyst EPMA (X-ray microanalyzer) analyzes, and confirmation active component Ru, Rh, Pd are dispersed on carrier.Analyze for EMPA, as measurement device, the accelerating potential of electron gun is set to 20KV to use JXA-8600M (Nippon Denshi K.K.), and probe current is 2.0 × 10
-8a.
120 ml waters are added in the stainless steel autoclave sweeping the 0.5L blown in advance with nitrogen completely, 6 grams of hydrogenation catalysts (adding the hydrogenation catalyst through overactivation that embodiment 1-6 prepares respectively) and 80 milliliters of benzene, and introduce hydrogen, react by stirring (1000 revs/min) at Hydrogen Vapor Pressure is 5.0MPa and reaction temperature is 150 DEG C, after having reacted, cooling autoclave, takes out oil phase, use chromatographic product, result is as shown in table 3.
EXPERIMENTAL EXAMPLE 7
This EXPERIMENTAL EXAMPLE prepares cyclohexene for illustration of hydrogenation catalyst of the present invention is used for benzene selective hydrogenation.
According to the method for EXPERIMENTAL EXAMPLE 1-6, hydrogenation catalyst C1 is activated, and carry out benzene selective hydrogenation according to the method for EXPERIMENTAL EXAMPLE 1 and prepare cyclohexene, unlike, 20 milliliters of hexylene glycols are added in autoclave together with 80 milliliters of benzene with phenmethylol (hexylene glycol is 0.8: 1 with the volume ratio of benzene).Use chromatographic product, result is as shown in table 3.
EXPERIMENTAL EXAMPLE 8
This EXPERIMENTAL EXAMPLE prepares cyclohexene for illustration of hydrogenation catalyst of the present invention is used for benzene selective hydrogenation.
According to the method for EXPERIMENTAL EXAMPLE 1-6, hydrogenation catalyst C1 is activated, and carry out benzene selective hydrogenation according to the method for EXPERIMENTAL EXAMPLE 1 and prepare cyclohexene, unlike, 20 milliliters of hexylene glycols are added in autoclave together with 80 milliliters of benzene.Use chromatographic product, result is as shown in table 3.
Comparative example 2
This comparative example prepares cyclohexene for illustration of reference hydrogenation catalyst is used for benzene selective hydrogenation.
According to the method for EXPERIMENTAL EXAMPLE 1-6, reference hydrogenation catalyst CB1 is activated, and carry out benzene selective hydrogenation according to the method employing of EXPERIMENTAL EXAMPLE 1 through the hydrogenation catalyst CB1 of overactivation and prepare cyclohexene, and in reaction system, add 14.5 grams of white vitriols.Use chromatographic product, result is as shown in table 3.
Table 3
| Numbering | Reaction time (minute) | Benzene conversion ratio (%) | Cyclohexene selective (%) |
| EXPERIMENTAL EXAMPLE 1 | 60 | 55.1 | 70.5 |
| EXPERIMENTAL EXAMPLE 2 | 60 | 54.7 | 71.5 |
| EXPERIMENTAL EXAMPLE 3 | 60 | 54.5 | 72.6 |
| EXPERIMENTAL EXAMPLE 4 | 60 | 51.4 | 73.1 |
| EXPERIMENTAL EXAMPLE 5 | 60 | 52.5 | 74.3 |
| EXPERIMENTAL EXAMPLE 6 | 60 | 57.4 | 67.3 |
| EXPERIMENTAL EXAMPLE 7 | 60 | 55.4 | 71.5 |
| Test example 8 | 60 | 55.1 | 71.1 |
| Comparative example 2 | 60 | 51.5 | 62.6 |
From the result of upper table 3, hydrogenation catalyst of the present invention is used for benzene selective hydrogenation and prepares the conversion ratio that cyclohexene can significantly improve the selective of cyclohexene and benzene in the short period of time.In addition, experimentally embodiment 1 can be found out with the results contrast of comparative example 2, under the prerequisite adopting hydrogenation catalyst provided by the invention, even if do not add Metal Salts in reaction system, cyclohexene selective still higher, and do not add metallic addition and also can reduce the corrosion of equipment and the consumption to hydrogenation catalyst.In addition, experimentally embodiment 1 can be found out with the results contrast of EXPERIMENTAL EXAMPLE 7 and 8, and the reaction of preparing cyclohexene of described benzene selective hydrogenation is carried out can improving the selective of cyclohexene further under the existence of alcohol (particularly the hexylene glycol of special ratios and phenmethylol).
Claims (13)
1. a hydrogenation catalyst, this catalyst comprises carrier and load hydrogenation active component on this carrier, it is characterized in that, described carrier is bar-shaped SBA-15, described hydrogenation active component contain be selected from Ru, Rh and Pd one or more; The length of the rod of described bar-shaped SBA-15 is 30-100 micron, and the most probable pore size of described bar-shaped SBA-15 is 6-10 nanometer, and pore volume is 0.5-1.5 ml/g, and BET specific surface area is 600-700 meters squared per gram; Described hydrogenation active component is also containing one or more in Zn, Fe, Co, Ni and Mn, and the gross weight of Ru, Rh and Pd is 0.01-100:1 with the gross weight ratio of Zn, Fe, Co, Ni and Mn.
2. hydrogenation catalyst according to claim 1, wherein, the gross weight of described Ru, Rh and Pd and the gross weight of Zn, Fe, Co, Ni and Mn are than being 0.05-50:1.
3. hydrogenation catalyst according to claim 2, wherein, the gross weight of described Ru, Rh and Pd and the gross weight of Zn, Fe, Co, Ni and Mn are than being 0.5-30:1.
4. hydrogenation catalyst according to claim 1, wherein, in described hydrogenation catalyst, hydrogenation active component is with the content of oxide basis for 0.1-50 % by weight, and the content of carrier is 50-99.9 % by weight.
5. hydrogenation catalyst according to claim 4, wherein, described hydrogenation active component is with the content of oxide basis for 1-20 % by weight, and the content of carrier is 80-99 % by weight.
6. a preparation method for hydrogenation catalyst, the method comprises: by the soluble salt solutions of hydrogenation active component and carrier contact, and the carrier after contact is carried out drying, roasting; It is characterized in that, described carrier is bar-shaped SBA-15, described hydrogenation active component contain be selected from Ru, Rh and Pd one or more; The length of the rod of described bar-shaped SBA-15 is 30-100 micron, and the most probable pore size of described bar-shaped SBA-15 is 6-10 nanometer, and pore volume is 0.5-1.5 ml/g, and BET specific surface area is 600-700 meters squared per gram; Described hydrogenation active component is also containing one or more in Zn, Fe, Co, Ni and Mn, and the gross weight of Ru, Rh and Pd is 0.01-100:1 with the gross weight ratio of Zn, Fe, Co, Ni and Mn.
7. method according to claim 6, wherein, the gross weight of described Ru, Rh and Pd and the gross weight of Zn, Fe, Co, Ni and Mn are than being 0.05-50:1; The soluble-salt of described hydrogenation active component is one or more in chloride, acetate, sulfate and nitrate.
8. method according to claim 7, wherein, the gross weight of described Ru, Rh and Pd and the gross weight of Zn, Fe, Co, Ni and Mn are than being 0.5-30:1.
9. method according to claim 6, wherein, the temperature of described roasting is 300-500 DEG C, and the time of roasting is 0.5-12 hour; The temperature of described drying is 100-200 DEG C, and the time is 0.5-10 hour.
10. method according to claim 9, wherein, the temperature of described roasting is 350-450 DEG C, and the time of roasting is 1-8 hour.
11. methods according to claim 6, wherein, the consumption of described soluble-salt makes in the hydrogenation catalyst prepared, and hydrogenation active component is with the content of oxide basis for 0.1-50 % by weight, and the content of carrier is 50-99.9 % by weight.
12. methods according to claim 6, wherein, the consumption of described soluble-salt makes in the hydrogenation catalyst prepared, and hydrogenation active component is with the content of oxide basis for 1-20 % by weight, and the content of carrier is 80-99 % by weight.
The application of hydrogenation catalyst in hydrogenation reaction that the preparation method of the hydrogenation catalyst in the hydrogenation catalyst in 13. 1 kinds of claim 1-5 described in any one or claim 6-12 described in any one prepares.
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| CN103566930B (en) * | 2013-11-01 | 2016-01-13 | 山东新和成药业有限公司 | A kind of Pd/SiO 2catalysts and its preparation method and application |
| CN105694956B (en) * | 2014-11-27 | 2017-07-11 | 中国海洋石油总公司 | A kind of method of inferior feedstock oil hydrogenation desulfurization and denitrogenation |
| CN105689009B (en) * | 2014-11-27 | 2018-04-20 | 中国海洋石油集团有限公司 | Inferior feedstock oil hydrogenation desulfurization and denitrogenation carriers for catalysts and its preparation method and application |
| CN105689008B (en) * | 2014-11-27 | 2018-05-01 | 中国海洋石油集团有限公司 | A kind of inferior feedstock oil hydrogenation desulfurization and denitrogenation catalyst and its application |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101514001A (en) * | 2009-03-10 | 2009-08-26 | 中国科学院上海硅酸盐研究所 | Bar-shaped ordered mesopore silicon dioxide nano material and preparation method thereof |
| CN101602507A (en) * | 2009-06-29 | 2009-12-16 | 上海应用技术学院 | A kind of one-dimensional rod-like mesoporous material and its production and application |
-
2012
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Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101514001A (en) * | 2009-03-10 | 2009-08-26 | 中国科学院上海硅酸盐研究所 | Bar-shaped ordered mesopore silicon dioxide nano material and preparation method thereof |
| CN101602507A (en) * | 2009-06-29 | 2009-12-16 | 上海应用技术学院 | A kind of one-dimensional rod-like mesoporous material and its production and application |
Non-Patent Citations (2)
| Title |
|---|
| Nanometric palladium confined in mesoporous silica as efficient catalysts for toluene oxidation at low temperature;Chi He et al;《Applied Catalysis B: Environmental》;20110922;第111-112卷;46-57 * |
| 硅基载钯催化剂的形貌对肉桂醛加氢反应性能的影响;王婧;《中国优秀硕士学位论文全文数据库 工程科技I辑》;20101015(第10期);36-39 * |
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