CN1445020A - Compound catalyst for many metals oxide and preparation method - Google Patents
Compound catalyst for many metals oxide and preparation method Download PDFInfo
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- CN1445020A CN1445020A CN 03121882 CN03121882A CN1445020A CN 1445020 A CN1445020 A CN 1445020A CN 03121882 CN03121882 CN 03121882 CN 03121882 A CN03121882 A CN 03121882A CN 1445020 A CN1445020 A CN 1445020A
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Abstract
A catalyst for preparing acylic acid by gas-phase selective oxidizing of acrylaldehyde has a formula MoaVbCucTedX1eX2fX3gX4hX5iOx, where X1 is chosen from W and Nb, X2 is chosen from Mg, Ca, Sr and Ba, X3 is chosen from Fe, Co and Ni, X4 is chosen from Si, Al and Ti, and X5 is chosen from Sb, Sn and Bi. Its advantages are high activity and high selectivity.
Description
Technical field
The gas that the present invention relates to a kind of gas that is used for containing unsaturated aldehyde and a kind of molecule-containing keto carries out the compound multi-metal-oxide catalyst of selective oxidation reaction in gas phase, particularly relates to acrylic acid compound multi-metal-oxide catalyst of a kind of propenal vapor phase catalytic oxidation system and preparation method.
Background technology
By the acid of propylene two-step method catalytic gas phase oxidation system acrylic or methacrylic is the general-purpose industrial production method, be propylene with after molecular oxygen precursor and water vapour mix, enter and be equipped with that to be suitable for PROPENE IN GAS PHASE OXIDATION be in first section reactor of propenal catalyzer, contain the propenal gas mixture from what first stage reactor was discharged, be suitable for to be in second section reactor of vinylformic acid catalyzer, to make propenal generate vinylformic acid the propenal gaseous oxidation without separating directly to enter to be equipped with.
Being used for the propenal gaseous oxidation is acrylic acid catalyzer, be poly-metal deoxide or composite oxide catalysts, Mo-Bi-Fe system, Mo-V-Cu system etc. are arranged, with complex metal oxidess such as molybdenum [Mo], vanadium [V], copper [Cu] and other metals is the basic comprising catalyzer, has good propenal activity of conversion and generates acrylic acid selectivity.As the catalyzer among the CN 1298861A be with at least a at least a in molybdenum, vanadium, copper and the alkaline-earth metal, silicon, aluminium, titanium, the zirconium be necessary composition, also can be furnished with metal oxides such as tungsten, alkaline-earth metal, phosphorus, boron, tellurium is component, wherein tellurium (Te) and phosphorus, cerium, lead, arsenic, zinc are as a class material, add with inessential composition, need were with a kind of compound that contains alkaline-earth metal and silicon, aluminium, titanium, zirconium simultaneously when this invention required preparation composite oxides; With Mo, V, Te is the O composite metallic oxide catalyst of neccessary composition preparation, is used as the reaction that conversion of olefines is corresponding unsaturated nitrile more, opens clear 49-117419 as the spy.Think among the CN1179359 and carry out the Mo-Bi-Fe series catalysts that olefin ammoxidation uses and add a spot of tellurium being used for gas-phase fluidized-bed reaction, between the reaction time limit, can prevent the loss of molybdenum component in the catalyzer.
As everyone knows: the free molybdic oxide at high temperature reacts with water vapour in the molybdernum-containing metallic oxide catalyst, produces evaporable MoO
2(OH) gas, easily the mode with distillation runs off.Produce in acrylic acid unsaturated aldehyde selective oxidation reaction process at acrolein oxidation, the main multi-metal-oxide catalyst that contains molybdenum that adopts, and be to carry out catalyzed reaction more than 200 ℃, because water vapour is the carrier gas of reactant, the water vapour thermal capacitance also is medium of removing reaction heat greatly, so the distillation loss of molybdenum is inevitable in the catalyzer.The loss of molybdenum has reduced activity of such catalysts, selectivity, intensity and work-ing life, and molybdenum blocks pipeline in the deposition in reactive system downstream, also can influence the long-term operation of system.As being used to produce acrylic acid Mo series catalysts, should under temperature of reaction, suppress the loss of main active component metal molybdenum [Mo], improve the catalyzer physical strength, avoid under reaction conditions catalyzer to run off because of efflorescence under mechanical vibration, airflow scouring and the thermal shocking, thereby make catalyzer have higher acrolein conversion rate and higher vinylformic acid optionally simultaneously, minimizing Mo and the loss of other catalyst activity component reach the variety of issue that causes in the deposition of reactive system upstream device pipeline, prolong the work-ing life of catalyzer.
Summary of the invention
The present invention seeks to improving catalyst activity and optionally on the basis, further improving the activity of such catalysts component,, improve the bonding strength each other of many composite oxide of metal to be suppressed at high temperature and to contain the loss of the molybdenum under the water vapour reaction medium.
Catalyzer of the present invention is formed and can be expressed as:
Mo
aV
bCu
cTe
dX
1 eX
2 fX
3 gX
4 hX
5 iO
xWherein Mo is a molybdenum, and V is a vanadium, and Cu is a copper, and Te is a tellurium, X
1Be a kind of element that is selected from tungsten and niobium at least, X
2Be a kind of element that is selected from magnesium, calcium, strontium and barium at least, X
3Be a kind of element of chosen from Fe, cobalt and nickel at least, X
4Be a kind of element that is selected from silicon, aluminium and titanium at least, X
5Be to be selected from antimony at least, a kind of element of tin and bismuth, O is an oxygen element, a, b, c, d, e, f, g, h, i and x represent that its atoms of elements compares number, when a=12 was benchmark, b was a number of 1 to 8, preferably a number of 3 to 5, c is a number of 0.1 to 4, a number of 0.5 to 3 preferably, d is a number of 0.05 to 1, preferably a number of 0.1 to 1, e is a number of 0 to 3, a number of 0 to 2 preferably, f is a number of 0 to 1, preferably is a number of 0 to 0.5, g is a number of 0 to 30, a number of 0 to 20 preferably, h is a number of 0 to 60, preferably a number of 0 to 30, i is a number of 0 to 60, a number of 0 to 30 preferably, x is by satisfying the required number of each metallic element combined oxidation attitude, catalyzer is made up of its each element oxide or composite oxides.
In the catalyzer of the present invention, molybdenum, vanadium, copper and tellurium are the necessary component of catalyzer.Though the tellurium add-on seldom, but the component of raising catalyst performance lasting stability is absolutely necessary to the two-phase three-dimensional structure of stablizing molybdenum, free molybdic oxide and a series of molybdic acid copper crystal formation.Tellurium makes the molybdic acid copper crystal structure in the catalyzer further form sosoloid and promotes the migration of lattice oxygen, strengthens its structural stability, and the distillation loss and the over reduction of molybdenum suppress to some extent, and can improve catalytic selectivity.Each source metal can be its precursor compound, oxide compound or can be converted into the compound of oxide compound under heating, and the mixture that contains above-mentioned source metal.For example the molybdenum source can be a molybdate, the vanadium source can be ammonium vanadate, ammonium meta-vanadate, the tungsten source can be a tungstate, the copper source can be cupric nitrate, copper carbonate, the tellurium source can be telluric acid and or tellurium oxide, preferably use 300 purpose tellurium oxides,, can influence activity of such catalysts less than the dispersed variation of 300 purpose tellurium oxides.
Can add in the catalyzer of the present invention nonessential tungsten and or niobium, alkaline-earth metal such as magnesium, calcium, strontium and barium make catalyzer have high activity and good selectivity.Each source metal can be its precursor compound, oxide compound or the compound that can be converted into oxide compound under heating, and the mixture of above-mentioned source metal, and therefore concrete can be its nitrate, carbonate, formate, acetate, oxyhydroxide.
Can also add nonessential iron, cobalt or nickel and silicon, aluminium or elements such as titanium and antimony, tin auxiliary agent in the catalyzer of the present invention as catalyzer, as antimony-nickel-silicon-oxygen composite oxide, in forming the heat treatment process of composite oxides owing to have the solid state reaction between the metal oxide and the change of solid-phase construction, it is become have the carrier that improves catalyst selectivity concurrently, though cause preparing the undercapacity of catalyzer, but mainly be the carrier function of the improvement pore structure of expanded hole radius in catalyzer, thereby made catalyzer have good selectivity.Each source metal can be its precursor compound, oxide compound or the compound that can be converted into oxide compound under heating, and the mixture of above-mentioned source metal.Therefore concrete can be its nitrate, carbonate, formate, acetate, oxide compound and oxyhydroxide.Antimony is the oxide compound of its trivalent, tetravalence or pentavalent not necessarily, can also be that metaantimmonic acid is (as metantimonic acid [HSbO
3], positive metaantimmonic acid [H
3SbO
4], pyroantimonic acid [H
4Sb
2O
7]), antimonous acid is (as meta-antimonous acid [HSbO
2], ortho-antimonous acid [H
3SbO
3], pyroantimonous acid [H
4Sb
2O
5]), antimonyl oxalate [(SbO)
2C
2O
4], also can be antimonous nickel; Silicon can be silica gel, silicon sol and diatomite, and aluminium can be aluminium glue, aluminium colloidal sol, and the titanium source is if titanium dioxide can be the titanium dioxide of brookite, anatase octahedrite or rutile-type.
Compound multi-metal-oxide catalyst of the present invention also has good activity even without the carrier support, can certainly use carrier, for example: silica, aluminum oxide, silica-alumina, titanium dioxide or its mixture.
The preparation method of compound multi-metal-oxide catalyst of the present invention is not limited, but proposes a kind of special preparation method at this, and the catalyzer that uses this kind method to obtain can make the catalytic activity of many composite oxide of metal as far as possible ideally show.
This catalyzer is to obtain by following manner:
(1) preparation contain molybdenum, vanadium or and the aqueous solution of nonessential tungsten or niobium metal element,
With contain copper or and the aqueous solution of nonessential alkaline-earth metal form slurry,
Dry through evaporating, dry, pulverizing, formation contains molybdenum, vanadium, tungsten or niobium, copper and alkali
The composite I of earth metals, perhaps with above-mentioned mixture again through thermal treatment,
Resolve into composite oxides I ' under 200-400 ℃.
(2) add the change of iron content, cobalt or nickel and silicon, aluminium or titanium and antimony or tin if necessary again
Compound then mixes above-mentioned metallic compound or its oxide compound, at 120-900 ℃
The composite oxides II that is sintered into.
This blending means can be that metallic compound or the employing of its oxide compound are solvent-free
Or the dry mixed of water existence, as grinding or pulverize, mixing, also can be metal
The wet-mixed that compound or its oxide compound exist at solvent or water, as be mixed with molten
Liquid, slurry or be kneaded into base mud after drying, calcining, or its dry method and wet
The combination of method.
(3) to composite I or composite oxides I ' or and composite oxides II in add
Necessary tellurium (as telluric acid or tellurium oxide) or and niobium metal element solvable of containing
Property compound, insolubility oxide compound or its mixture, dry state or hygrometric state preferably
Mix or kneading, last extrusion molding 200-400 ℃ of following activation heat treatment is
Catalyzer.
Among the present invention, grind or pulverize and be meant the material processing by 350-20 mesh standard sieve net, evaporation is dry to be carried out under lasting intensively stirred 60-120 ℃ temperature, and drying is carried out under 80-120 ℃ of temperature, decomposes, activates or calcine and carry out under 120-900 ℃ of temperature.
Catalyzer of the present invention is to adopt hygrometric state or dry state extrusion molding.Preferably adopt the hygrometric state moulding, particularly solution, slurry or the water-soluble salt with part metals carries out shaping of catalyst, guarantees that catalyzer more has higher intensity.Catalyzer can be shaped to ball-type, sheet or cylinder shape, circular ring type or other abnormal shape.
The catalyzer that is made of compound poly-metal deoxide of the present invention can be used for containing the gas of unsaturated aldehyde and a kind of gas of molecule-containing keto carries out selective oxidation reaction in gas phase, and the gas that specifically contains propenal, molecular oxygen and water vapour is being to carry out the acrylic acid process of gas phase selective catalytic oxidation system.
Catalyst performance evaluation of the present invention is carried out in tubular reactor, loading catalyst in the pipe, outer heating agent such as thermal oil or the dissolved salt maintenance temperature of reaction that adopts steady temperature of pipe, feeding contains the gas of unsaturated aldehyde and a kind of gas of molecule-containing keto carries out catalyzed reaction, because the oxidizing reaction of carrying out the strong heat release of hydro carbons, formation temperature distributes in beds, and therefore can adopt the temperature (hot(test)-spot temperature) of control catalyst bed temperature distribution top temperature point is that a steady temperature is carried out catalyst performance evaluation as benchmark.
The catalyst performance index definition is as follows:
Catalyzer of the present invention makes the gas that contains unsaturated aldehyde and a kind of gas of molecule-containing keto carry out the catalytic selectivity oxidizing reaction in gas phase, and have the characteristics of high reactivity and highly selective, be specially adapted to carry out the acrylic acid reaction of propenal vapor phase catalytic oxidation system.
Embodiment
Embodiment 1
Preparation of Catalyst:
In a stainless steel vessel, add 500 ml deionized water, under violent stirring, add 162.9 gram ammonium molybdate [(NH successively
4)
6Mo
7O
244H
2O], 38.4 gram ammonium meta-vanadate [NH
4VO
3] heating make it the dissolving, this mixed-salt aqueous solution is A.In second stainless steel vessel, add 50 ml deionized water, under violent stirring, add 33.5 gram cupric nitrate [Cu (NO
3)
2], heating makes it abundant dissolving, and this mixed-salt aqueous solution is B.Two kinds of solution are mixed, form the co-precipitation slurry, dry up into solid continuing under heating and the violent stirring evaporation, pulverize it then, form the powder C that passes through 60 eye mesh screens.It is even that 45 gram powder C and 300 orders 2.2 gram tellurium oxides [TeO] are added in the mixing tanks thorough mixing, moves on in the kneader, continues to spray into 20 milliliters deionized water, is kneaded into base mud, is shaped to the granules of catalyst of φ 4 * 4mm on extrusion-dicing machine.380 ℃ were decomposed activation in lasting 5 hours down in retort furnace, formed final catalyzer.It consists of:
Mo
12V
4.2Cu
1.8Te
0.2O
x
Evaluating catalyst:
In the internal diameter φ 20mm stainless steel tube reactor, load 35 milliliters of catalyzer, feed reaction mixture gas with standard gaseous air speed 1800h-1, reaction mixture gas consists of:
Propenal Vol.% 8
Oxygen Vol.% 12
Nitrogen Vol.% 62
Water vapor Vol.% 18
The control hot(test)-spot temperature is 295 ℃, and evaluation result is as shown in table 1.
Embodiment 2
In a stainless steel vessel, add 500 ml deionized water, under heating and violent stirring, add 162.9 gram ammonium molybdate [(NH successively
4)
6Mo
7O
244H
2O], 38.4 gram ammonium meta-vanadate [NH
4VO
3], 20.7 gram ammonium paratungstate [(NH
4)
6W
7O
246H
2O] make it dissolving, this mixed-salt aqueous solution is A.In second stainless steel vessel, add 50 ml deionized water, under violent stirring, add 4.8 gram strontium nitrate [Sr (NO successively
3)
2] and 33.5 gram cupric nitrate [Cu (NO
3)
2], heating makes it abundant dissolving, and this mixed-salt aqueous solution is B.Two kinds of solution are mixed, form the co-precipitation slurry, dry up into solid continuing under heating and the violent stirring evaporation, pulverize it then, form the powder C that passes through 60 eye mesh screens.It is even that 53 gram powder C and 300 orders 2.2 gram tellurium oxides [TeO] are added in the mixing tanks thorough mixing, is shaped to the granules of catalyst of φ 4 * 4mm.380 ℃ were decomposed activation in lasting 5 hours down in retort furnace, formed final catalyzer.It consists of:
Mo
12V
4.2W
1.0Sr
0.3Cu
1.8Te
0.2O
x
Adopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Embodiment 3
In a stainless steel vessel, add 500 ml deionized water, under violent stirring, add 162.9 gram ammonium molybdate [(NH successively
4)
6Mo
7O
244H
2O], 38.4 gram ammonium meta-vanadate [NH
4VO
3], 20.7 gram ammonium paratungstate [(NH
4)
6W
7O
246H
2O] heating make it the dissolving, this mixed-salt aqueous solution is A.In second stainless steel vessel, add 50 ml deionized water, under violent stirring, add 4.8 gram strontium nitrate [Sr (NO successively
3)
2] and 33.5 gram cupric nitrate [Cu (NO
3)
2], heating makes it abundant dissolving, and this mixed-salt aqueous solution is B.Two kinds of solution are mixed, form the co-precipitation slurry, dry up into solid continuing under heating and the violent stirring evaporation, pulverize it then, form the powder C that passes through 60 eye mesh screens.In the 3rd stainless steel vessel, add 100 ml deionized water, add 105.0 gram nickelous nitrate [Ni (NO
3)
2], 55.0 gram basic nickel carbonate [NiCO
32Ni (OH)
24H
2O], after making it to dissolve, add 125.5 grams, 300 purpose antimonous oxide [Sb
2O
3] powder and 44.4 grams, 300 purpose silicon powder [SiO
2], evaporation is dried up under lasting heating and violent stirring, calcines 3 hours down at 800 ℃ then, pulverizes it, forms the powder D by 60 eye mesh screens.It is even that 53 gram powder C, 55 gram powder D and 300 orders, 2.2 gram tellurium oxides [TeO] are added in the mixing tanks thorough mixing, is shaped to the granules of catalyst of φ 4 * 4mm.380 ℃ were decomposed activation in lasting 5 hours down in retort furnace, formed final catalyzer.It consists of:
Mo
12V
4.2W
1.0Sr
0.3Cu
1.8Ni
10.4Sb
11.2Si
9.6Te
0.2O
x
Adopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Embodiment 4
Powder C among the embodiment 1 is continued down to decompose in 3 hours at 300 ℃, be ground into by 60 eye mesh screens, get 55 among 45 gram powder C and the embodiment 3 and restrain powder D and mix, step is identical with embodiment 1 thereafter.Its catalyzer consists of:
Mo
12V
4.2Cu
1.8Ni
10.4Sb
11.2Si
9.6Te
0.2O
x
Adopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Embodiment 5
In a stainless steel vessel, add 500 ml deionized water, under heating and violent stirring, add 123.6 gram ammonium molybdates and 4.6 gram molybdic oxide [MoO successively
3], 38.4 gram ammonium meta-vanadate [NH
4VO
3], 20.7 gram ammonium paratungstate [(NH
4)
6W
7O
246H
2O] make it dissolving, this mixed-salt aqueous solution is A, all the other processes are identical with embodiment 2.Getting the catalyzer that 41 gram powder C make consists of:
Mo
12V
4.2W
1.0Sr
0.3Cu
1.8Te
0.2O
x
Adopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Embodiment 6
With the powder C45 gram of embodiment 1 preparation and the powder D55 gram and the 3.5 gram telluric acid [H of embodiment 3 preparations
6TeO
6] mix, other is identical with embodiment 1.Its catalyzer consists of:
Mo
12V
4.2Cu
1.8Ni
10.4Sb
11.2Si
9.6Te
0.2O
x
Adopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Embodiment 7
Adopt embodiment 2 identical methods to prepare catalyzer, just when obtain solution A, adopt 18.1 gram nitric acid niobium [NbNO
3] replace ammonium paratungstate, adopt 4.1 gram nitrate of baryta [Ba (NO during obtain solution B
3)
2] replace strontium nitrate, make powder C, to get 60 order C48 gram and mix with 300 orders, 2.2 gram tellurium oxides, other is identical with embodiment 2.Its catalyzer consists of:
Mo
12V
4.2Nb
1.6Ba
0.3Cu
1.8Te
0.2O
x
Adopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Embodiment 8
Adopt the method identical to prepare powder C, in the 3rd stainless steel vessel, add 100 ml deionized water, add 105.0 and restrain nickelous nitrate [Ni (NO with embodiment 3
3)
2], 596 gram Xiao Suangu [Co (NO
3)
26H
2O], after making it to dissolve, add 190.8 gram antimonyl oxalates [(SbO)
2C
2O
4] and 44.4 grams, 300 purpose silicon powder [SiO
2], evaporation is dried up under lasting heating and violent stirring, calcines 3 hours down at 800 ℃ then, pulverizes it, forms the powder D by 60 eye mesh screens.It is even that 53 gram powder C, 55 gram powder D and 300 orders, 2.2 gram tellurium oxides [TeO] are added in the mixing tanks thorough mixing, is shaped to the granules of catalyst of φ 4 * 4mm.380 ℃ were decomposed activation in lasting 5 hours down in retort furnace, formed final catalyzer.Its catalyzer consists of:
Mo
12V
4.2W
1.0Sr
0.3Cu
1.8Co
5.6Ni
4.7Sb
11.2Si
9.6Te
0.2O
x
Adopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Embodiment 9
Adopt the method for embodiment 3 to prepare catalyzer, just when preparation powder D, adopt 34.5 grams, 300 purpose aluminium sesquioxide [Al
2O
3] and 300 purposes, 4.9 gram titanium dioxide [TiO
2] replace silicon powder, mix with the powder D of 50 grams with 53 gram powder C, other is identical with embodiment 3.Its catalyzer consists of:
Mo
12V
4.2W
1.0Sr
0.3Cu
1.8Ni
10.4Sb
11.2Al
8.8Ti
0.8Te
0.2O
x
Adopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Embodiment 10
116 gram nickelous nitrates are dispersed in 300 milliliters 80 ℃ the soft water, and 21.7 gram silicon powders, 88.8 gram antimonous oxides and 3.3 gram telluric acids add in the said mixtures and fully and stir.With slurry heating, concentrated and dry.Then the gained solid is placed High Temperature Furnaces Heating Apparatus, calcined 3 hours down at 600-800 ℃.Calcinate is ground, make particle promptly obtain composite powder A by 80 mesh sieves.
500 milliliters of soft water are heated to about 70 ℃, add 19.5 gram ammonium paratungstates, 100 gram ammonium molybdates, 63.9 gram ammonium meta-vanadates and 29.9 gram cupric nitrates in succession and make it abundant dissolving.Then the A powder is added in this solution, violent stirring is mixed.Slurry concentrates down and drying at 100 ℃.Dried product is ground and makes it by 40 mesh sieves.Mediate then, extrusion, pelletizing obtain φ 4 * 4mm particle.The particle 380 ℃ of following roastings in High Temperature Furnaces Heating Apparatus that obtain were made catalyzer in 5 hours.
The available following atomic ratio of the composition of the catalyzer that makes is thus represented:
Mo
12V
3.2W
0.5Cu
2.6Te
0.3Ni
8.4Sb
12.2Si
7.6O
X
Evaluating catalyst adopts embodiment 1, and evaluation result sees Table 1.
Embodiment 11
In 500 milliliters 80 ℃ deionized water, adding 3.3 gram telluric acids, 100 gram ammonium molybdates, 19.2 gram ammonium meta-vanadates and 19.5 gram ammonium paratungstates and violent stirring successively fully dissolves, other adds in 40 ml deionized water and incorporates formation co-precipitation solution in the said mixture into after 23.0 gram cupric nitrates dissolve, and concentrate drying and pulverizing obtain powders A by 40 eye mesh screens under lasting heating and the violent stirring.
Adding 55 gram basic nickel carbonates, 22.8 gram silicon powders and 78.4 gram antimonous oxides in 180 milliliters of 50 ℃ of deionized waters in succession fully stirs.With slurry heating, concentrated and dry.Then resulting solid was calcined 3 hours under 600-800 ℃ in High Temperature Furnaces Heating Apparatus.Calcined material is carried out abrasive grains obtain powder B by 60 molybdenums sieve.
40 gram A and 60 gram B are mixed the deionized water that adds 20 milliliters is shaped to φ 4 * 4mm through kneading, extrusion, pelletizing particle.380 ℃ were decomposed activation in following 5 hours in muffle furnace, formed catalyzer.It consists of:
Mo
12V
3.2W
1.5Cu
2.0Te
0.3Ni
9.2Sb
11.3Si
8.0O
X
Embodiment 12
500 ml deionized water are heated to 80 ℃, add 16.2 gram ammonium paratungstates, 127.8 gram ammonium molybdates, 23.2 gram ammonium meta-vanadates and 15.6 gram copper carbonates successively and make it dissolving.With solution heating, concentrated and dry, solid obtained powders A through pulverizing 40 mesh sieves then.
B powder and A powder mixes with among 3.3 gram tellurium oxides, the embodiment 11 add 20 ml deionized water obtain φ 4 * 4mm through kneading, extrusion and pelletizing particle.380 ℃ of roastings in following 5 hours form final catalyst in muffle furnace.It consists of:
Mo
12V
3.3W
0.9Cu
1.8Te
0.3Ni
9.2Sb
11.3Si
8.0O
X
The evaluation of this catalyzer is with embodiment 1.Evaluation result sees Table 1.
Comparative Examples 1
Except the non-oxidation tellurium, other is identical with embodiment 1, and its catalyzer consists of:
Mo
12V
4.2Cu
1.8O
x
Adopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Comparative Examples 2
Except no telluric acid, other is identical with embodiment 6, and its catalyzer consists of:
Mo
12V
4.2Cu
1.8Ni
10.4Sb
11.2Si
9.6O
x
Adopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Comparative Examples 3
Except no cupric nitrate, other is identical with embodiment 3, and its catalyzer consists of:
Mo
12V
4.2W
1.0Sr
0.3Ni
10.4Sb
11.2Si
9.6Te
0.2O
xAdopt the method identical with embodiment 1 to carry out evaluating catalyst, evaluation result is as shown in table 1.
Table 1
| Project | Acrolein conversion rate | Generate the vinylformic acid selectivity | |
| Embodiment | ????1 | ????99.1 | ????95.6 |
| ????2 | ????99.2 | ????97.4 | |
| ????3 | ????99.5 | ????98.7 | |
| ????4 | ????98.3 | ????97.1 | |
| ????5 | ????98.9 | ????96.9 | |
| ????6 | ????97.8 | ????96.3 | |
| ????7 | ????97.7 | ????95.1 | |
| ????8 | ????97.6 | ????94.4 | |
| ????9 | ????98.3 | ????94.8 | |
| ????10 | ????96.8 | ????95.3 | |
| ????11 | ????97.2 | ????95.6 | |
| ????12 | ????98.5 | ????97.6 | |
| Comparative Examples 1 | ????97.5 | ????92.5 | |
| Comparative Examples 2 | ????96.1 | ????92.7 | |
| Comparative Examples 3 | ????94.2 | ????90.3 | |
Claims (11)
1. the compound multi-metal-oxide catalyst of unsaturated aldehyde selective oxidation is made of requisite molybdenum, vanadium, copper and tellurium composite oxides, and its catalyzer consists of:
Mo
aV
bCu
cTe
dX
1 eX
2 fX
3 gX
4 hX
5 iO
xWherein Mo is a molybdenum, and V is a vanadium, and Cu is a copper, and Te is a tellurium, X
1Be a kind of element that is selected from tungsten and niobium at least, X
2Be a kind of element that is selected from magnesium, calcium, strontium and barium at least, X
3Be a kind of element of chosen from Fe, cobalt and nickel at least, X
4Be a kind of element that is selected from silicon, aluminium and titanium at least, X
5Be a kind of element that is selected from antimony, tin and bismuth at least, O is an oxygen, and a, b, c, d, e, f, g, h, i and x represent that its atoms of elements compares number, when a=12 is benchmark, b is a number of 1 to 8, and c is a number of 0.1 to 4, and d is a number of 0.05 to 1, e is a number of 0 to 3, f is a number of 0 to 1, and g is a number of 0 to 30, and h is a number of 0 to 60, i is a number of 0 to 60, and x is by satisfying the required number of each metallic element combined oxidation attitude.
2. multi-metal-oxide catalyst according to claim 1 is made of requisite molybdenum, vanadium, copper and tellurium composite oxides, and its catalyzer consists of: Mo
aV
bCu
cTe
dX
1 eX
2 fX
3 gX
4 hX
5 iO
x, wherein Mo is a molybdenum, and V is a vanadium, and Cu is a copper, and Te is a tellurium, X
1Be a kind of element that is selected from tungsten and niobium at least, X
2Be a kind of element that is selected from magnesium, calcium, strontium and barium at least, X
3Be a kind of element of chosen from Fe, cobalt and nickel at least, X
4Be a kind of element that is selected from silicon, aluminium and titanium at least, X
5Be a kind of element that is selected from antimony, tin and bismuth at least, O is an oxygen, and a, b, c, d, e, f, g, h, i and x represent that its atoms of elements compares number, when wherein being benchmark with a=12, b is a number of 3 to 5, and c is a number of 0.5 to 3, and d is a number of 0.1 to 1, e is a number of 0 to 2, f is a number of 0 to 0.5, and g is a number of 0 to 20, and h is a number of 0 to 30, i is a number of 0 to 30, and x is by satisfying the required number of each metallic element combined oxidation attitude.
3. multi-metal-oxide catalyst according to claim 1 and 2 is characterized in that catalyzer is by requisite molybdenum, vanadium, copper and tellurium composite oxides combination X
1And/or X
2The composite oxides mixture, its catalyzer consists of: Mo
aV
bCu
cTe
dX
1 eX
2 fO
x, X
1Be W elements, X
2It is strontium element, a, b, c, d, e, f and x represent that its atoms of elements compares number, when wherein being benchmark with a=12, b is a number of 3 to 5, and c is a number of 0.5 to 3, and d is a number of 0.1 to 1, e is a number of 0 to 2, f is a number of 0 to 0.5, and e and f are not 0 simultaneously, and x is by satisfying the required number of each metallic element combined oxidation attitude.
4. multi-metal-oxide catalyst according to claim 1 and 2 is characterized in that catalyzer is by requisite molybdenum, vanadium, copper and tellurium composite oxides combination X
3, X
4, X
5The mixture of complex metal oxides, its catalyzer consists of: Mo
aV
bCu
cTe
dX
3 gX
4 hX
5 iO
x, X wherein
3Be nickel element, X
4Be a kind of element of silicon, aluminium and titanium, X
5Be to be selected from antimony element; A, b, c, d, g, h, i and x represent that its atoms of elements compares number, when wherein being benchmark with a=12, b is a number of 3 to 5, c is a number of 0.5 to 3, d is a number of 0.1 to 1, and g is a number of 3 to 20, and h is a number of 2 to 30, i is a number of 5 to 30, and x is by satisfying the required number of each metallic element combined oxidation attitude.
5. multi-metal-oxide catalyst according to claim 1 and 2 is characterized in that catalyzer is by requisite molybdenum, vanadium, copper and tellurium composite oxides combination X
1And/or X
2And combination X
3, X
4, X
5The mixture of complex metal oxides, its catalyzer consists of: Mo
aV
bCu
cTe
dX
1 eX
2 fX
3 gX
4 hX
5 iO
x, X wherein
1Be W elements, X
2Be strontium element, X
3Be nickel element, X
4Be a kind of element of silicon, aluminium and titanium, X
5Be to be selected from antimony element; A, b, c, d, e, f, g, h, i and x represent that its atoms of elements compares number, when wherein being benchmark with a=12, b is a number of 3 to 5, and c is a number of 0.5 to 3, d is a number of 0.1 to 1, e is a number of 0 to 2, and f is a number of 0 to 0.5, and e and f are not 0 simultaneously, g is a number of 8 to 20, h is a number of 2 to 30, and i is a number of 5 to 30, and x is by satisfying the required number of each metallic element combined oxidation attitude.
6. according to the multi-metal-oxide catalyst of claim 1 or 2, it is characterized in that the nickel source is be selected from basic nickel carbonate, nickelous acetate, nickelous nitrate, nickelous oxalate, nickel oxide at least a kind of.
7. according to the multi-metal-oxide catalyst of claim 1 or 2, it is characterized in that silicon and aluminium source are be selected from oxide compound or its colloidal sol at least a kind of.
8. according to the multi-metal-oxide catalyst of claim 1 or 2, it is characterized in that the antimony source is be selected from metaantimmonic acid, antimonyl oxalate, weisspiessglanz at least a kind of.
9. the preparation method of the described multi-metal-oxide catalyst of claim 1 is characterized in that the catalyzer that obtains in the following ways:
(1) preparation contain molybdenum, vanadium or and the aqueous solution of nonessential tungsten or niobium metal element, and contain
Copper or and the aqueous solution of nonessential alkaline-earth metal form slurry, dry through evaporating,
Dry, pulverizing form the composite I that contains molybdenum, vanadium, tungsten or niobium, copper and alkaline-earth metal,
Perhaps with above-mentioned mixture again through thermal treatment, under 200-400 ℃, resolve into composite oxides
I′。
(2) with metallic compound or its oxide compound of iron content, cobalt or nickel and silicon, aluminium or titanium and antimony or tin
Mix, at 120-900 ℃ of composite oxides II that is sintered into.
(3) to composite I or composite oxides I ' or and composite oxides II in add necessary
Contain tellurium or and the soluble compound of niobium metal element, insolubility oxide compound or its mix
Compound, dry state or hygrometric state mix or mediate, and last extrusion molding is lived down at 200-400 ℃
Heat-transmission is treated to catalyzer.
10. Preparation of catalysts method according to claim 9 is characterized in that when preparation composite oxides II the mixing of many metallic compounds or its oxide compound can be that metallic compound or its oxide compound adopt the method for grinding or pulverizing to mix.
11. Preparation of catalysts method according to claim 9, it is characterized in that when preparation composite oxides II, the mixing of many metallic compounds or its oxide compound be with the part metals compound make in the presence of solvent or the water solution, again add insoluble oxide compound in heating and under stirring evaporation dry, calcining, the method for pulverizing are mixed.
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|---|---|---|---|
| CNB031218822A CN1169619C (en) | 2003-04-17 | 2003-04-17 | Compound catalyst for many metals oxide and preparation method |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100453175C (en) * | 2004-09-30 | 2009-01-21 | 友联有机合成化学有限公司 | Catalyst and its preparation method and use of the said catalyst in 5h-dibenzanthracene-(b,f)-aza |
| CN101511472B (en) * | 2006-09-11 | 2013-03-27 | 赢创德固赛有限责任公司 | Catalyst containing Mo, preparation method thereof and method for preparing methyl hydrosulfide |
| CN105934315A (en) * | 2014-02-05 | 2016-09-07 | 三菱丽阳株式会社 | Method for manufacturing extrusion molding |
| CN111659408A (en) * | 2020-04-23 | 2020-09-15 | 宜兴市申生催化剂有限公司 | Preparation method of catalyst for preparing acrylic acid by acrolein oxidation |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| US9140728B2 (en) | 2007-11-02 | 2015-09-22 | Emerson Climate Technologies, Inc. | Compressor sensor module |
| US8964338B2 (en) | 2012-01-11 | 2015-02-24 | Emerson Climate Technologies, Inc. | System and method for compressor motor protection |
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- 2003-04-17 CN CNB031218822A patent/CN1169619C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100453175C (en) * | 2004-09-30 | 2009-01-21 | 友联有机合成化学有限公司 | Catalyst and its preparation method and use of the said catalyst in 5h-dibenzanthracene-(b,f)-aza |
| CN101511472B (en) * | 2006-09-11 | 2013-03-27 | 赢创德固赛有限责任公司 | Catalyst containing Mo, preparation method thereof and method for preparing methyl hydrosulfide |
| CN105934315A (en) * | 2014-02-05 | 2016-09-07 | 三菱丽阳株式会社 | Method for manufacturing extrusion molding |
| CN111659408A (en) * | 2020-04-23 | 2020-09-15 | 宜兴市申生催化剂有限公司 | Preparation method of catalyst for preparing acrylic acid by acrolein oxidation |
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| Publication number | Publication date |
|---|---|
| CN1169619C (en) | 2004-10-06 |
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