CN112221537B

CN112221537B - Using white carbon black and TiCl4Method for preparing high-activity propylene and hydrogen peroxide gas phase epoxidation catalyst by gas-solid phase reaction

Info

Publication number: CN112221537B
Application number: CN202011220178.9A
Authority: CN
Inventors: 郭洪臣; 刘宏伟; 祝全仁
Original assignee: Dalian University of Technology
Current assignee: Dalian University of Technology
Priority date: 2020-11-05
Filing date: 2020-11-05
Publication date: 2021-07-06
Anticipated expiration: 2040-11-05
Also published as: CN112221537A

Abstract

Using white carbon black and TiCl₄A method for preparing a high-activity propylene and hydrogen peroxide gas phase epoxidation catalyst by gas-solid phase reaction belongs to the technical field of petrochemical catalysts. The method firstly uses TiCl₄Grafting the titanium graft of silicon oxide on white carbon black through gas-solid phase reaction to obtain a titanium graft of silicon oxide, and then dispersing the titanium graft in tetrapropyl quaternary ammonium cation TPA⁺In the template agent aqueous solution, the dispersion does not form gel under the condition, and only a very small amount of tetrapropyl quaternary ammonium cation template agent needs to be added to obtain a TS-1 zeolite crystallization product. The invention is beneficial to reducing the synthesis cost of the TS-1 zeolite crystallization product, and the crystallization product has high crystallinity, more importantly, the catalytic activity of the crystallization product on the gas-phase epoxidation reaction of propylene and hydrogen peroxide is very high, thereby effectively suppressing the ineffective decomposition reaction of the hydrogen peroxide reaction raw material in the reaction competition and greatly improving the effective utilization rate of the hydrogen peroxide under the gas-phase epoxidation reaction condition.

Description

Using white carbon black and TiCl4Method for preparing high-activity propylene and hydrogen peroxide gas phase epoxidation catalyst by gas-solid phase reaction

Technical Field

The invention belongs to the technical field of petrochemical catalysts, and relates to a preparation method of a catalyst for a phase epoxidation reaction of propylene and hydrogen peroxide.

Background

The desired product of the hydrogen peroxide gas phase epoxidation reaction of propylene is Propylene Oxide (PO). PO is an important downstream product of propylene, mainly used for the production of polyether polyols, propylene glycol and propylene glycol ethers. The downstream PO industrial chain is developed, and the terminal application relates to many fields of chemical industry, household appliances, automobiles, buildings, aerospace, food, tobacco, medicines, cosmetics and the like.

At present, the industrial production process of PO comprises three technical routes, namely a chlorohydrin method, an oxidation method (including isobutane, ethylbenzene and cumene oxidation) and a liquid phase epoxidation method (HPPO process) of propylene and hydrogen peroxide. The chlorohydrin method is a traditional technology for producing PO, has simple process and low raw material price, but has serious corrosion to equipment, great pollution to environment and low atom utilization rate, and does not meet the requirement of green chemistry. The co-oxidation method can overcome the defects of the chlorohydrin method, but the yield of the co-product is overlarge, or the process technology is too complex, so that the industrial application is not favorable. In contrast, HPPO processes that have been industrially applied in recent years have received much attention because they overcome not only the problems of equipment corrosion, environmental pollution, and low atom utilization rate of the chlorohydrin process, but also the problems of co-products of the co-oxidation process.

The HPPO process employs a pressurized liquid phase reaction process. Due to the low reaction temperature (typically 30-60 ℃), the epoxidation reaction of hydrogen peroxide in HPPO processes is highly efficient (typically more than 90%) and has a low rate of inefficient decomposition (typically less than 10%). However, the HPPO process must use a large amount of solvent to ensure the liquid-liquid uniform mixing of propylene (oily) and aqueous hydrogen peroxide solution, thereby ensuring the epoxidation reaction of hydrogen peroxide and propylene and preventing the decomposition of hydrogen peroxide itself.

Methanol solvent is considered most suitable for the liquid phase epoxidation of propylene. In addition to being widely available, inexpensive and having a generally meaningful solvent role, methanol is also believed to be likely to participate in the activation process of hydrogen peroxide by forming a so-called five-membered ring "transition state with the hydrogen peroxide molecule and the backbone titanium active center. Therefore, methanol is considered to have an additional effect of promoting the activation of hydrogen peroxide and the epoxidation reaction, compared with other solvents. This is also the reason why the production units of the current HPPO process all use methanol as solvent.

However, the use of methanol solvents also creates significant complications for the HPPO process. Firstly, methanol is easy to generate solvolysis side reaction with a propylene oxide product to generate byproducts such as high-boiling-point substance propylene glycol monomethyl ether and the like. These by-products not only severely reduce the selectivity of propylene oxide, but also increase the difficulty of wastewater treatment. Secondly, the methanol solvent must be recycled and requires complex refining treatments (including hydrogenation, rectification and resin adsorption) before recycling, which not only leads to complications in the HPPO process flow, but also increases investment and energy consumption. In addition, the recycled methanol solvent after the complex refining treatment still has more than ten or even two or thirty trace impurities (including fusel, aldehyde, ether, ester and oxacyclic) which are difficult to remove. These trace impurities, which return to the reactor with the recycled methanol, accelerate the deactivation of the epoxidation catalyst and severely shorten the life cycle and life of the epoxidation catalyst. These problems arising from the use of solvents greatly diminish the competitive advantage of the HPPO process.

We have pursued research studies on the gas-phase epoxidation of propylene and hydrogen peroxide since 2002. The gas phase epoxidation reaction is carried out at normal pressure and at a temperature of more than 100 ℃. Under the condition, the reactants of propylene and hydrogen peroxide are directly mixed in the form of gas molecules, and the two reactants can pass through the bed layer of the TS-1 molecular sieve catalyst together to smoothly perform epoxidation reaction without any solvent. The gas-phase epoxidation reaction process of propylene and hydrogen peroxide does not use a solvent, so that the problems of the conventional HPPO process can be fundamentally overcome, and the process is expected to become a novel process for producing propylene oxide with higher industrial popularization value.

We have first developed a dielectric barrier discharge plasma technique capable of directly synthesizing gaseous hydrogen peroxide of high purity from a mixture of hydrogen and oxygen and are described in the following documents Chemical Communications,2005(12): 1631-1633; modern chemical, 2006,26(s2): 71-73; 3204-; new electrical and energy technology, Vol28,2009, No. 3P 73-76; chi.j.cat., 2010,31: 1195-; the chemical bulletin Vol63,2012, No.11, P3513-3518; journal of Catalysis 288(2012) 1-7; 8604-8607. ang. and Angewandte Chemie,2013, 125 (32); chinese patent application No. 200310105210.9, 200310105211.3, 200310105212.8. We have realized the in-situ continuous synthesis of hydrogen peroxide gas by using the plasma technology and completed the first stage of research work on propylene gas phase epoxidation in 2007 (Zhou Jun Cheng]Dalian university of Dalian graduate, 2007). In particular, the research work employed a specially designed two-stage integrated reactor. The first stage reactor is a Dielectric Barrier Discharge (DBD) plasma reactor and is used for providing continuity and stability for the epoxidation reaction stage by taking a mixed gas of hydrogen and oxygen as a raw material (the concentration of the oxygen in the hydrogen is less than 6v percent)Is fed with gaseous hydrogen peroxide. The second stage reactor is a gas phase epoxidation fixed bed reactor of propylene and hydrogen peroxide gas, and TS-1 molecular sieve particles are filled in the reactor. The results of the gas phase epoxidation reaction obtained in this study at 90 ℃, 1atm are: about 7% propylene conversion, 93% Propylene Oxide (PO) selectivity and 0.24kg PO kgTS-1^-1h^-1Propylene oxide yield. Later, we used the same system and non-classical (also called cheap) method of synthesis of micron large crystal TS-1 (unmodified) as the catalyst, have conducted more comprehensive research work. The results reported in the publication Chin.J.Catal.,2010,31: 1195-1199 show that the selectivity of propylene oxide can still reach about 95% at a reaction temperature of 110 ℃, and the yield of propylene oxide is maintained at 0.25kgPO kgTS-1^-1h^-1On the other hand, the catalyst activity was stable in the continuous 36-hour gas-phase epoxidation reaction. But the epoxidation selectivity, i.e. the effective utilization rate of hydrogen peroxide, is only about 36%.

In addition to our earlier work, we know from the literature ind. eng. chem. res.2008,47,2086-. They employed a special glass vaporizer or a microchannel falling film evaporator to vaporize a 50 wt% aqueous hydrogen peroxide solution to provide a gaseous hydrogen peroxide feed for the vapor phase epoxidation reaction. The gas phase epoxidation reactor is a microchannel reactor internally coated with a TS-1 molecular sieve. The reaction results obtained at 140 ℃ and 1atm are: propylene oxide selectivity>90% yield of propylene oxide>1kgPO kgTS-1^-1h^-1. But the effective utilization rate of the hydrogen peroxide is only about 25 percent.

The above research work on the phase epoxidation of propylene and hydrogen peroxide has shown that the epoxidation reaction can effectively occur on a TS-1 molecular sieve catalyst by directly contacting propylene and hydrogen peroxide gas without the participation of a methanol solvent, and a considerable yield of propylene oxide is achieved. Moreover, the selectivity of the propylene oxide reaches about 90 percent, which is close to the result of liquid-phase epoxidation. This shows that the gas phase epoxidation of propene with hydrogen peroxide process has important development value. However, since the gas phase epoxidation reaction of propylene and hydrogen peroxide needs to be carried out under normal pressure and at a relatively high reaction temperature (100-. This is the biggest challenge for industrial applications.

In the earlier invention, a method for modifying by using an alkali metal hydroxide solution to adjust the microenvironment of titanium of a titanium-silicon molecular sieve TS-1 framework titanium so as to improve the effective utilization rate of hydrogen peroxide in propylene gas-phase epoxidation reaction is provided. The Chinese invention patent (application number) 201910515504.X provides an alkali metal ion modified titanium silicalite molecular sieve capable of selectively promoting the hydrogen peroxide gas phase epoxidation reaction of propylene without participation of a solvent and a preparation method thereof. The preparation method is that alkali metal hydroxide solution is used for carrying out hydrothermal treatment on the titanium silicalite TS-1 with controlled degree, alkali metal cations must be retained on the titanium silicalite after the hydrothermal treatment, and at least a part of the alkali metal cations are in a balanced cation form and are positioned on silicon hydroxyl groups near framework titanium to modify the microenvironment of the framework titanium. The controlled hydrothermal treatment is realized by adjusting the concentration of the alkali metal hydroxide solution, the hydrothermal treatment temperature, the time, the liquid-solid ratio and other factors. According to the invention, as described in example 1, when a 0.1mol/L NaOH solution is used, at 170 ℃ and a liquid-solid ratio of 10 ml/g molecular sieve, for a large-grained TS-1 molecular sieve (the grain size is 1X 2X 6 μm, the total Si/Ti molar ratio is about 39.8, the sodium-titanium molar ratio is 0.003. index value I of framework titanium content_960cm-1/I_550cm-1About 0.51, relative crystallinity of about 100%) for 18 hours, and washing, drying and roasting the hydrothermally treated large-grain TS-1 molecular sieve, the obtained modified TS-1 molecular sieve can obtain the reaction results of 15.5% propylene conversion rate, 97.0% PO selectivity and 77.5% hydrogen peroxide effective utilization rate in gas phase epoxidation reaction. In contrast, the unmodified large-grain TS-1 molecular sieve matrix has the propylene conversion rate of only 4.5%, the PO selectivity of only 56.2% and the effective utilization rate of hydrogen peroxide of only 22.5% under the same reaction conditions. Chinese invention patent (application number) 201910515501.6 by using a catalyst containing a small amount of tetrapropyl quaternary ammonium cation (TPA)⁺) The alkali metal hydroxide solution carries out hydrothermal treatment on the titanium silicalite TS-1 in a controlled degree, alkali metal cations must be retained on the titanium silicalite after the hydrothermal treatment, and at least a part of the alkali metal cations are in a balanced cation form and are positioned on silicon hydroxyl groups near the framework titanium to modify the microenvironment of the framework titanium. In this invention, a small amount of tetrapropyl quaternary ammonium cation (TPA)⁺) The introduction of the alkali metal hydroxide enables the alkali metal hydroxide to adjust the titanium microenvironment of the TS-1 framework of the titanium silicalite molecular sieve, and the alkali metal hydroxide is suitable for large-grain TS-1 molecular sieves and nano TS-1 molecular sieves. According to the invention, when using a TPA containing 0.15mol/L⁺The 0.1mol/L NaOH solution is used for carrying out hydrothermal treatment on a nano TS-1 molecular sieve (with the grain size of 200-300 nanometers) for 16 hours at the temperature of 170 ℃ and under the condition that the liquid-solid ratio is 10 milliliters per gram of molecular sieve, and washing, drying and roasting the TS-1 molecular sieve after the hydrothermal treatment, so that the obtained modified nano TS-1 molecular sieve can obtain 14.8% of propylene conversion rate, 94.3% of PO selectivity and 74.0% of effective utilization rate of hydrogen peroxide in gas-phase epoxidation reaction. In contrast, the unmodified nano TS-1 molecular sieve matrix has the propylene conversion rate of only 4.3%, the PO selectivity of only 58.1% and the effective utilization rate of hydrogen peroxide of only 21.5% under the same reaction conditions.

It is noted that the catalyst modification and preparation method provided in the previous invention uses a titanium silicalite TS-1 precursor hydrothermally synthesized by a sol-gel method. Titanium silicalite is a silicate zeolite with a titanium heteroatom in the crystal framework. TS-1 is an extremely important member of the titanium silicalite family, and has excellent catalytic performance for the epoxidation reaction of propylene and hydrogen peroxide. The synthesis of TS-1 was first reported in patents GB2071071A and US4410501, Marcotaramasso et al. Like the common silicon-aluminum molecular sieve ZSM-5, TS-1 also has an MFI topological structure and a ten-membered ring cross channel system. A great deal of basic research shows that the titanium heteroatom exists in an isolated four-coordination form on a TS-1 framework, and the titanium heteroatom belongs to oxygen ligand to titanium central atom electricity in the vicinity of 210nm of ultraviolet visible diffuse reflection spectrumCharacteristic absorption of the sub-transition at 1120cm in the UV Raman spectrum^-1Characteristic resonance absorption occurs nearby. In addition, the skeleton titanium also has a mid-infrared region of 960cm in the infrared spectrum^-1Characteristic absorption belonging to Si-O-Ti antisymmetric stretching vibration (or Si-O bond stretching vibration disturbed by framework titanium) occurs.

In principle, there are two approaches to hydrothermally synthesizing titanium silicalite TS-1 by a sol-gel method: one route is the hydrothermal synthesis, i.e., the classical method, reported by Taramasso et al (USP4410501.1983) and Thangaraj et al (J Chem Soc Chem Commun, 1992: 123). As is well known, the raw material characteristic of the TS-1 molecular sieve synthesis technology by the classical method is that tetrapropylammonium hydroxide is taken as a template agent, and silicon ester and titanium ester are taken as a silicon source and a titanium source respectively. The product is observed on an electron microscope, the morphology features of the product are irregular aggregate morphology, the particle size of the aggregate is usually 200-300 nanometers, and the grain size of the primary crystals forming the aggregate is usually in a range of less than 100 nanometers. Although the later people do a lot of improvement work on the basis of Taramasso et al and Thangaraj et al, the above basic characteristics of the classical method for synthesizing TS-1 are not changed and are easy to judge.

The classical hydrothermal synthesis method has the advantage that the so-called nano TS-1 with the particle size of the aggregate of 200-300 nm can be obtained. The nanometer TS-1 has small grain size and short pore passage, and is favorable for reducing the diffusion resistance of the ten-membered ring microporous pore passage to reactant and product molecules. In addition, the nano TS-1 molecular sieve synthesized by the classical method has less non-framework titanium, and is beneficial to reducing the decomposition of the non-framework titanium on hydrogen peroxide. However, those skilled in the art will appreciate that the classical synthesis of TS-1 molecular sieves requires the use of a high purity template, TPAOH, and a source of silicon and titanium esters. Therefore, the cost of the classical method for hydrothermal synthesis of TS-1 is high.

The other way of hydrothermally synthesizing TS-1 is a cheap method. The hydrothermal synthesis methods of TS-1, which are referred to in the following documents, are all inexpensive methods: zeolite and Related microporus Materials State of the Art 1994, students in Surface Science and Catalysis, Vol.84; zeolite 16: 108-; zeolite 19: 246-; applied Catalysis A, General 185(1999) 11-18; catalysis Today 74(2002) 65-75; ind, eng, chem, res, 2011,50, 8485-; microporous and Mesoporous Materials 162(2012) 105-114; chinese patent application No. 201110295555.x and 201110295596.9. The raw material of cheap synthesis technique is characterized by that it uses tetrapropyl ammonium bromide as template agent and uses ammonia water or organic amines of methylamine, ethylamine, ethylenediamine, diethylamine, n-butylamine and hexanediamine as alkali source. The silicon source and the titanium source are commonly used as silica sol and titanium tetrachloride, and sometimes titanium ester is used as the titanium source. The morphology of the product observed on an electron microscope is characterized by monodisperse crystals with regular crystal edge crystal faces, including large-grain thin plate crystals reaching several microns or coffin-like small-grain crystals of 300-600 nanometers.

Although the raw material cost of the cheap hydrothermal synthesis technology is relatively low compared with the classical method, compared with the hydrothermal synthesis of industrial zeolites such as X, Y, M and ZSM-5, the hydrothermal synthesis of the TS-1 molecular sieve at least needs to use high-purity silica sol as a silicon source, in particular tetrapropylammonium quaternary ammonium cation (TPA) which acts as a template agent⁺) The dosage of the molecular sieve is large, so the cost of the TS-1 molecular sieve is still high. This situation is very unfavorable for industrial application of TS-1 molecular sieves.

White carbon black is a general name for white powdery X-ray amorphous silicic acid and silicate products, and mainly comprises precipitated silica (usually produced by reacting sodium silicate with a sulfuric acid solution), fumed silica (produced by using SiCl4 as a raw material in a gas phase in a high-temperature combustion reaction of hydrogen and oxygen), ultrafine silica dry gel and silica aerogel.

White carbon black and/or titanium tetrachloride have been used as cheap raw materials for the hydrothermal synthesis of titanium silicalite TS-1. For example, chinese patent applications 201510165516.6, 201610150083.1 and 201710789098.7 all disclose a hydrothermal synthesis method of TS-1 using silica white as a silicon source. A method for hydrothermally synthesizing TS-1 by using titanium tetrachloride as a titanium source is reported in published literature fuel chemistry, Vol.28, No.6, P550-554. The common characteristics of the reported methods are two, namely, when the white carbon black and/or the titanium tetrachloride are used for synthesizing the titanium silicalite TS-1, the white carbon black and/or the titanium tetrachloride are firstly formed into conventional titanium silicalite gel together with other raw materials, and then the gel is placed in a hydrothermal synthesis kettle for hydrothermal crystallization. Secondly, in order to fully crystallize the titanium-silicon gel, a large amount of tetrapropyl quaternary ammonium cation template agent (usually added in the form of tetrapropyl ammonium hydroxide, tetrapropyl ammonium bromide, ammonium chloride and the like) needs to be consumed. The amount of tetrapropyl quaternary ammonium cationic templating agent added is generally expressed in terms of the mode/silicon ratio, which is typically as high as 0.2 or more. Indeed, the methods reported in the literature are inexpensive synthesis methods for the aforementioned titanium silicalites. These approaches still require the consumption of large amounts of quaternary ammonium templating agent and therefore are not effective in reducing the cost of titanium silicalite molecular sieves.

Different from the method, the key point of the invention is based on white carbon black and TiCl₄To prepare a catalyst for the gas-solid phase epoxidation of propylene with hydrogen peroxide. Moreover, as will be seen from the technical solutions provided later, the catalyst for the vapor phase epoxidation of propylene with hydrogen peroxide according to the present invention is actually TiCl using white carbon black₄The graft is cheap raw material, and is prepared from very small amount of template agent TPA⁺There is a titanium silicalite molecular sieve TS-1 which is synthesized hydrothermally. As will be seen from the examples which follow, TiCl with this white carbon black₄The graft is cheap raw material, and has very small amount of template agent TPA⁺The TS-1 molecular sieve synthesized by hydrothermal reaction has low cost, high catalytic activity for epoxidation reaction of propylene and hydrogen peroxide at high temperature, and can obviously inhibit decomposition reaction of the hydrogen peroxide, so that the effective utilization rate of the hydrogen peroxide is obviously improved.

We note that the publications R.A.Sheldon, J.K.Kochi, Metal-catalyst oxides of Organic Compounds, Academic Press, Amsterdam,1981, Langmuir 1987,3, 111-11, Langmuir 1993,9, 3497-371, ChemUSChem 2009,2, 508-₄Preparation of TiCl by direct reaction with silicon oxide in the gas phase or in the liquid phase₄The method of grafting the silicon oxide catalyst shows that the catalyst is effective to the epoxidation reaction of ethylbenzene peroxide and propylene in the process of producing propylene oxide and styrene by an ethylbenzene-propylene co-oxidation method (PO/SM). However, in these documents, the grafting catalyst concerned is an amorphous catalyst and this amorphous catalyst is used for the liquid phase epoxidation of propene with ethylbenzene hydroperoxide, an organic hydroperoxide. In which propylene and H are not involved₂O₂More specifically propylene and H₂O₂The gas phase epoxidation reaction of (1).

According to the report of the publication chem.Eur.J.2013,19, 9849-9858, TiCl is mentioned above₄A typical preparation process of the grafted silica catalyst mainly comprises the following steps: firstly, soaking silicon oxide powder in water, and then drying overnight at 120 ℃; and secondly, heating the silicon oxide carrier for pretreatment. A suitable heat treatment temperature is 700 ℃. The purpose of the high-temperature heat treatment is to remove hydrogen bond silicon hydroxyl of the silicon oxide carrier and only keep independent silicon hydroxyl (the infrared vibration frequency is 3740 cm)^-1) (ii) a Thirdly, TiCl treatment is carried out on the pretreated silicon oxide carrier under the conditions of room temperature and vacuum₄Gas phase grafting; fourthly, the single-foot SiO-TiCl generated by grafting on the silicon oxide carrier is subjected to thermal post-treatment₃Species reconstitution as tripodia (. ident.SiO-)₃TiCl species, improving the stability of Ti active sites; and finally, removing residual chlorine on the catalyst through alcoholysis reaction of tert-butyl alcohol, and improving the activity and selectivity of the catalyst.

We also note that the following patents and publications are also relevant:

U.S. patent application 2016/0237051A1 discloses a process for preparing a silica-containing coating by reacting silica with TiCl₄A method for preparing an epoxidation titanium silicon catalyst by reaction. However, it is technically characterized in that oxygen is first introduced into a quartz tube with nitrogen gasDrying the silica support (200 ℃ C. for 2 hours), adding the silicone ester to the dried support at room temperature to effect silylation, and adding TiCl to the support at room temperature₄Such as a toluene solution, to perform a titanium deposition reaction. And finally, carrying out temperature programming treatment on the reactant in nitrogen to obtain the target catalyst. The method for temperature programming comprises the following steps: 10min at 60 ℃ → 15min at 200 ℃ → 60min at 600 ℃ → 30min at 700 ℃ → 30min at 800 ℃. The obtained catalyst was used for the liquid phase epoxidation of 1-octene with tert-butyl hydroperoxide (TBHP).

Chinese patent application 201610021367.0 discloses a method for preparing an olefin epoxidation catalyst. But its technical characteristics do: the preparation process of the catalyst comprises TiCl₄Vapor deposition reaction → silanization treatment → hydrolysis treatment → molybdenum modification treatment → hydrolysis treatment → silanization treatment. Wherein, in the vapor deposition reaction step, the fumed silica, the hydroxyl-rich silica gel and the chromatographic silica gel are used as carriers. And the vapor phase deposition reaction is carried out at the temperature of 100-280 ℃, preferably 150-200 ℃; in the molybdenum modification treatment step, molybdenum oxydichloride or/and molybdenum pentachloride is directionally reacted with hydroxyl on titanium, and the modification reaction is carried out in organic solvents such as p-dichlorobenzene, o-dichlorobenzene, diphenyl ether and N-methylpyrrolidone (preferably p-dichlorobenzene) and at the temperature of 170-230 ℃ (preferably 180-200 ℃). In the hydrolysis treatment step, the hydrolysis temperature is 300-380 ℃, preferably 320-350 ℃; in the step of silylation treatment, hexamethyldisilazane and trimethylsilylimidazole are used as silylation reagents, and the silylation reaction is carried out at 100-250 ℃, preferably at 150-220 ℃. The epoxidation of olefins is carried out in the liquid phase with tert-butyl hydroperoxide as the oxidant.

Chinese patent application 201710295868.2 discloses a method for vapor deposition of TiCl on all-silicon molecular sieves₄A method for preparing a titanium silicalite molecular sieve catalyst. The technological feature is that the all-silicon molecular sieve is heated in reaction tube for dewatering, and TiCl is introduced into the reaction tube at 850 deg.C₄The gas is used for carrying titanium. After the end of the loading operation, the unreacted TiCl was purged with nitrogen at 400 deg.C₄And roasting the titanium-loaded molecular sieve at the temperature of 500-600 ℃ in the air atmosphere to obtain the target catalyst. The catalyst is used for liquid phase epoxidation reaction of propylene and cumene hydroperoxide.

It is clear that the methods disclosed in these patent documents are not relevant to the present invention.

Furthermore, we have noted that TiCl is also implicated in some publications₄A method for preparing a titanium silicon catalyst by directly reacting with silicon oxide. For example:

the temperature of dehydration pretreatment (200-800 ℃) for silica gel and TiCl is reported in the Journal of Molecular Catalysis,33(1985)275-287₄The effect of the reaction. The silica gel and TiCl₄The reaction is sometimes carried out in an n-heptane solvent (liquid phase reaction) at room temperature. After the reaction, the liquid was removed by pipette and the solid sample was incubated at 60 ℃ and-10 ℃^-2Carrying out decompression treatment for 24 hours at mbar; the silica gel and TiCl₄The reaction is sometimes carried out in the gas phase, at a reaction temperature of 170 ℃ and TiCl₄The gas is generated by bubbling Ar gas. The research shows that when the dehydration temperature of the pretreatment is not less than 600 ℃, the silica gel and the TiCl₄The Cl/Ti molar ratio of the reaction product is close to 3, which indicates that Ti only forms a single bond with the surface of the silicon oxide; when the dehydration temperature of the pretreatment is 400 ℃, silica gel and TiCl₄The Cl/Ti mol of the reaction product is about 2.8, which shows that most Ti forms only single bond with the silicon oxide surface at the moment, but a few Ti forms multiple bonds with the silicon oxide surface; when the dehydration temperature of the pretreatment is 200 ℃, a large amount of Ti forms multiple bonds with the surface of the silicon oxide. The text does not refer to silica gels and TiCl₄Catalytic study of reaction products.

Disclosure of Catalysis Letters 13(1992)229-238 on TiCl₄Catalyst p-phenol and H formed by deposition on crystalline or amorphous silicon oxide₂O₂The performance of the hydroxylation reaction was investigated. Wherein the crystalline silica is a defect type all-silica zeolite Silicalite-1, the amorphous silica is chromatographic silica, and the specific surface area is 450m²/g。TiCl₄The deposition method comprises the following steps: sample deposition on TiCl₄A pretreatment for dehydration with nitrogen (at least 6 hours) was previously carried out at 450 ℃. TiCl (titanium dioxide)₄The deposition reaction is carried out in the gas phase. TiCl (titanium dioxide)₄Gas bubbling with Nitrogen (room temperature), TiCl₄The deposition was carried out at 450 ℃ for 2 hours. TiCl (titanium dioxide)₄Immediately after the end of the deposition, a nitrogen purge was carried out at the reaction temperature for 2 hours in order to remove the unreacted TiCl from the catalyst bed₄The purpose of (1). Cooling and collecting the obtained catalyst for phenol and H₂O₂Hydroxylation reaction. The results show that TiCl is deposited on amorphous silica₄The prepared catalyst has poor catalytic performance on phenol hydroxylation reaction.

Open literature oil and gas chemical industry volume 28 first phase, p1-3 on TiCl₄Titanium silicalite catalyst prepared by gas-solid isomorphous substitution of ZSM-5 zeolite for styrene/H₂O₂The catalytic performance of the liquid phase oxidation reaction of (1) is reported. The preparation process of the titanium silicalite catalyst is as follows: first, a hydrogen type ZSM-5 zeolite (Si/Al. gtoreq.280) was dealuminated with 1mol/L HCl. The dealuminated zeolite is shaped, dried at 500 deg.C for 4 hr by introducing nitrogen, and then carried with TiCl by dry nitrogen₄The dried zeolite is isomorphously substituted with steam at a temperature close to 700 ℃. The reaction result shows that the catalyst prepared by the isomorphous substitution method has a catalytic effect on the liquid-phase epoxidation reaction of styrene (the main product is styrene oxide).

The published application Catalysis A, General 194-195(2000)507-514 reports the preparation of Si/Ti/SiO by chemical grafting₂The catalyst has catalytic action on the epoxidation reaction of styrene. TiCl for the catalyst₄Tetraethoxysilane (TEOS) and SiO₂And (3) preparing a carrier. The preparation process comprises the following steps: first, amorphous SiO₂(specific surface area 480 m)²Per gram) sufficient dry pretreatment (typically using 773K temperature) was obtained by calcination in an oxygen atmosphere and nitrogen purging. Then, carry TiCl with nitrogen₄For SiO under gas phase conditions₂Performing titanium grafting treatment, and blowing dry nitrogen to remove excessive TiCl at the end of titanium grafting₄Thereby obtaining Ti/SiO₂(773K) In that respect Next, the Ti/SiO is reacted in an isopropanol solution containing ethyl orthosilicate₂(773K) Carrying out room temperature liquid phase silanization treatment, and carrying out operations such as hydrolysis, filtration, drying, roasting and the like on the treated sample to obtain the target Si/Ti/SiO₂A catalyst.

Published Journal of Molecular Catalysis A Chemical 172(2001)219-225 reports cyclohexene on TiCl₄Ti/SiO prepared by chemical grafting method₂Reaction performance of liquid phase epoxidation on catalyst. In the work therein, dry deboronized silica gel was used as TiCl₄And (3) carrying out grafting reaction. Wherein, the boron-containing silicon dry glue is H₃BO₃And tetraethoxysilane prepared by a sol-gel method. The boron-removed silicon dry gel is obtained by treating boron-containing silica gel with HCl solution. Ti/SiO₂Catalyst preparation by reaction with TiCl₄Grafting dehydrated pretreated boron-removed silicon dry glue (pretreated under 773K) at room temperature to obtain the boron-removed silicon dry glue.

The use of TiCl 4034 is reported in the publications Ind.Eng.chem.Res.2002,41,4028-₄Ti/SiO prepared by Chemical Vapor Deposition (CVD)₂The catalytic performance of the catalyst on propylene liquid phase epoxidation reaction. The chemical vapor deposition is carried out on a silica gel carrier, and the adopted temperature range is 400-1100 ℃. The liquid phase epoxidation reaction of the propylene takes tert-butyl hydroperoxide as an oxidant. The results show that TiCl₄Chemical vapor deposition temperature on silica gel vs. Ti/SiO₂The Ti content and the catalytic activity of the catalyst have little influence, but have great influence on the liquid phase epoxidation selectivity of the propylene. As the temperature of chemical vapor deposition is increased, the selectivity of the propylene oxide product is rapidly increased, and the temperature of Ti/SiO is increased at 900 DEG C₂The Ti content of the catalyst is 0.89-1.07 wt.%, and the selectivity reaches the maximum value. The characterization by XPS shows that the catalyst is Ti/SiO₂Si-OTiCl on a surface₃Is the active center of the epoxidation reaction, and the silicon hydroxyl (Si-OH) groups on the catalyst are acidic and are detrimental to the epoxidation reaction. The increase in the temperature of the chemical vapor deposition, which can increase the selectivity of the catalyst, is believed to be associated with the removal of the silicon hydroxyl groups from the surface of the catalyst at high temperatures. However, the study suggests that the catalyst Ti/SiO₂Si-OTiCl on a surface₃Is an epoxidation active center in view of the aforementioned tripodal titanium species (. ident.Si-O)₃The view that TiCl is a catalytically active center (chem. Eur. J.2013,19, 9849-9858) is different.

Journal of Nanoscience and Nanotechnology Vol.11, 8152-8157,2011 reports the use of TiCl in a fluidized bed reactor₄Silica gel (400 m) at high ratio²/g) chemical vapor deposition of TiO₂The method of (1). The chemical vapor deposition is carried out under vacuum (1mbar-1000mbar) provided by a vacuum pump connected to the reaction system. TiCl (titanium dioxide)₄The gas was generated using a glass saturator placed in an oven, high purity helium was used as the carrier gas, synthetic air (20.5% O in nitrogen)₂) Used as reaction gas. Before the chemical vapor deposition reaction begins, silica gel microspheres are filled into a tubular reactor, so that the silica gel and the whole reaction system (including a glass saturator) are fully dried in helium flow, the temperature of the reactor is controlled to be 200 ℃, and the temperature of the saturator is controlled to be 110 ℃. After drying was complete, the reactor temperature was raised to 400 ℃, the reaction gas (synthesis air) was passed through the reactor, and helium was passed through the saturator. Then a metered quantity of TiCl is added to the saturator₄The reaction temperature is controlled to 75 ℃ by an oven, and a vacuum system is started to maintain the pressure of the reactor in a vacuum state (such as 400mbar) to enter a chemical vapor deposition reaction state. After the deposition reaction is finished, the reactor is recovered to the normal pressure state, and the product is calcined for two hours by introducing air at 400 ℃ to obtain TiO₂-SiO₂And (c) a complex. Research shows that TiO is easy to be formed on the surface of silica gel by the chemical vapor deposition method₂Film (anatase structure). The catalytic use of the composite is not reported herein.

It is clear that in the above publications, the grafting catalysts involved are essentially amorphous catalysts and that propylene and H are not involved therein₂O₂More specifically propylene and H₂O₂The gas phase epoxidation reaction of (1). Therefore, the methods reported in these documents are not relevant to the present invention.

In the presence of organic hydrogen peroxide as oxygenIn the case of the agent, although TiCl is grafted onto the silicon oxide₄Prepared Ti/SiO₂The catalyst has good catalytic activity and selectivity for liquid phase epoxidation of olefin, but the catalyst is easily deactivated under reaction conditions. How to slow down the deactivation speed of the catalyst and thus prolong the service life of the catalyst is a long-standing task. According to the report of the publication chem.eur.j.2013,19,9849-9858, in addition to that some by-products generated during the olefin epoxidation reaction can cause the catalyst to be poisoned and deactivated, the tripodal surface titanium active centers grafted on the silicon oxide are easy to migrate, aggregate and lose under the conditions of liquid phase epoxidation, which results in Ti/SiO₂The more major cause of catalyst deactivation. If mixing Ti/SiO₂Catalysts for the conversion of H₂O₂In the case of an olefin liquid phase epoxidation reaction system as an oxidizing agent, the presence of a large amount of water will cause Ti/SiO₂The catalyst rapidly fails.

Thus, the publication J.Phys.chem.C 2007,111,5083-5089 explicitly states that TiCl is₄Ti/SiO prepared by grafting method₂H cannot be used as a catalyst for the liquid phase epoxidation of olefins₂O₂An oxidizing agent. The reference relates to Ti/SiO₂Is prepared by dichlorocyclopentadienyl titanium (TiCp)₂Cl₂) Grafted on silicon oxide carriers with different shapes. The silicon oxide carriers with different morphologies refer to ordered mesoporous silicon oxide MCM-41, unordered porous silicon oxide and gas phase SiO₂(one of white carbon black). The grafting process features that the carrier is soaked in chloroform solution of dichlorocyclopentadienyl titanium, the silicon hydroxyl is activated with triethylamine to graft Ti (IV) onto the silicon hydroxyl, and the grafted matter is roasted at 550 deg.c in oxygen atmosphere to produce Ti (IV) active center on the carrier. The prepared catalyst is also used for liquid-phase epoxidation reaction of limonene, tert-butyl hydroperoxide and hydrogen peroxide. The article clearly indicates that with H₂O₂The oxidizing agent can lead the titanium-silicon catalyst prepared by the grafting method to be quickly and irreversibly inactivated. When H is used, the compound₂O₂In the case of the oxidizing agent, the epoxide product of limonene is not obtained.

In addition to this, the present invention is,the publications Applied Catalysis A: General 301(2006) 59-65 indicate that, from the viewpoint of the effective utilization of the oxidizing agent, the oxidizing agent is efficiently utilized by TiCl₄Ti/SiO prepared by grafting silicon oxide₂The catalyst cannot use hydrophilic H in liquid-phase oxidation reaction₂O₂As the oxidizing agent, only hydrophobic and oleophilic organic hydrogen peroxide can be used. In this document, the grafting process is carried out using a chemical vapor deposition reaction at 900 ℃. Before this, the silica gel powder carrier was subjected to a drying pretreatment (with nitrogen as a carrier gas) at 400 ℃. The prepared Ti/SiO₂The catalyst is used for liquid phase epoxidation of propylene and 1-octene. In the epoxidation reaction, cumene hydroperoxide and tert-butyl hydroperoxide are respectively used as oxidants. The results show that the effective utilization rate of the oxidizing agent is along with that of Ti/SiO₂The Ti content of the catalyst increases rapidly. However, when cumene hydroperoxide is used as the oxidizing agent, a higher effective oxidizing agent utilization rate can be obtained as compared with t-butyl hydroperoxide. This is because Ti/SiO₂The silicon hydroxyl groups on the catalyst have protonic acidity and can accelerate the decomposition of the oxidant. However, the rates of epoxidation of olefins with different oxidants are roughly equivalent, but the decomposition rates on the silicon hydroxyl groups are different. In Ti/SiO rich in silicon hydroxyl₂On the catalyst, because the silicon hydroxyl group has hydrophilicity, the tert-butyl hydroperoxide oxidant with relatively strong hydrophilicity is easy to interact with the silicon hydroxyl group, so that more side reactions of oxidant decomposition are caused. In contrast, cumene hydroperoxide oxidizing agent, which is less hydrophilic and more lipophilic, readily reacts with Ti/SiO₂The active centers (Si-O-Ti) of the catalyst interact, resulting in more epoxidation and less decomposition side reactions. It is apparent that H is comparable to the organic hydroperoxide oxidizing agent described above₂O₂Most hydrophilic and most prone to binding with the silicon hydroxyl groups resulting in a large number of inefficient decomposition, and from this perspective researchers have used organic hydroperoxides as oxidizing agents in liquid phase epoxidation reactions instead of H₂O₂The reason for this is also very well understood.

In summary, up to nowTiCl-passed₄Ti/SiO prepared by grafting on silicon oxide₂The catalyst is mainly used in a liquid phase reaction process which takes organic hydrogen peroxide as an oxidant. In the liquid phase epoxidation reaction mode, Ti/SiO₂The catalyst can not get rid of the problems of the migration, aggregation and loss of the active center of the catalyst caused by liquid phase water. This is because the use of organic hydrogen peroxide can avoid the use of H₂O₂The influence of a large amount of water by the aqueous solution is unavoidable by the influence of a small amount of water generated by the decomposition of the organic hydrogen peroxide. Therefore, even when organic oxidants such as t-butyl hydroperoxide, ethylbenzene hydroperoxide and cumene hydroperoxide are used, TiCl is grafted with silica as indicated in the publications chem. Eur. J.2013,19, 9849-9858₄The obtained Ti/SiO₂The catalyst still faces the problem of rapid deactivation in the liquid phase epoxidation of olefins. How to slow down the deactivation rate of the catalyst and thus prolong the service life of the catalyst is an arbitrary and long-distance work.

Publications chem.Commun. (1998)325, chem.Commun. (1998)2211, Lang-muir 21(2005) 9576, J.am.chem.Soc.129(2007)1122, Langmuir 27(2011)6295, etc. have attempted to provide Ti/SiO₂Grafting hydrophobic silane or siloxane blocking agent onto the catalyst. Such blocking agents do have a positive effect, but the effect is not satisfactory. According to the recently published report on Molecular Catalysis 477(2019)110509, polymethylhydrosiloxane (TMS- (O-Si (CH)) with better hydrophobicity is prepared by dehydrogenation reaction with silicon hydroxyl₃)(H))_n) Grafting of OTMS to Ti/SiO₂The catalyst surface shows better modification effect than that of a common end capping agent in improving the stability of the catalyst. Unfortunately, even if polymethylhydrosiloxane having a low degree of polymerization is used as the modifier, the diffusion performance of the catalyst in the liquid phase reaction is affected due to the bulky size of the polymer, thereby reducing the catalytic activity of the catalyst. Moreover, this increasingly complex post-modification treatment significantly reduces the reliability of the catalyst.

As can be seen from the above reports, even for the liquid-phase epoxidation reactionSay, by mixing TiCl₄Amorphous Ti/SiO prepared by grafting on silicon oxide₂The catalyst is also subject to a great limitation.

Disclosure of Invention

The invention provides a catalyst based on white carbon black and TiCl₄To prepare a catalyst for the gas-solid phase epoxidation of propylene with hydrogen peroxide.

Specifically, the invention provides a preparation method of a propylene and hydrogen peroxide gas phase epoxidation catalyst, which is to use TiCl of white carbon black₄The graft is cheap material, and is prepared with very small amount of tetrapropyl quaternary ammonium cation template agent (TPA)⁺) The hydrothermal synthesis of titanium silicalite molecular sieve TS-1 exists. We have found through extensive studies that if white carbon black (cheap silicon source) and TiCl are mixed₄If two raw materials (cheap titanium source) are directly used for hydrothermal synthesis, the TS-1 zeolite crystallization product is difficult to obtain. The direct application in hydrothermal synthesis refers to the reaction of white carbon black and TiCl₄Co-dispersed in tetrapropyl quaternary ammonium cation (TPA)⁺) Forming titanium silicagel in the hydroxide aqueous solution, and then carrying out hydrothermal treatment on the titanium silicagel in a closed crystallization kettle, thereby obtaining the TS-1 zeolite crystallization product. By doing so, unless a large amount of TPA is used⁺The crystallinity of the TS-1 zeolite in the template, otherwise hydrothermally synthesized solids, is low. The hydrothermal synthesis product with very low crystallinity has very low catalytic activity for the gas phase epoxidation of propylene and hydrogen peroxide, and the hydrogen peroxide raw material for epoxidation is mainly converted by ineffective decomposition. Surprisingly, if TiCl is first introduced₄Grafting the titanium oxide graft (Ti-SiO) on white carbon black through gas-solid phase reaction to obtain the titanium graft of silicon oxide₂) Then the titanium graft (Ti-SiO)₂) Dispersed in tetrapropyl quaternary ammonium cation (TPA)⁺) In an aqueous hydroxide solution (in which case the dispersion does not gel), only very small amounts of tetrapropyl quaternary ammonium cation (TPA) need to be added⁺) The template agent can obtain the crystallized product of the TS-1 zeolite. The method is not only beneficial to reducing the synthesis cost of the TS-1 zeolite crystallization product, but also has high crystallization degree of the crystallization product, and more importantly, the method is used for gas phase ring of propylene and hydrogen peroxideThe catalytic activity of the oxidation reaction is very high, so that the ineffective decomposition reaction of the hydrogen peroxide reaction raw material is effectively suppressed in reaction competition, and the effective utilization rate of the hydrogen peroxide under the condition of gas-phase epoxidation reaction is greatly improved.

The implementation of the invention can be carried out according to the following technical scheme:

firstly, drying and roasting pretreatment is carried out on a white carbon black raw material.

Various commercially available fumed and precipitated silicas (silicon dioxide, SiO)₂) Are suitable for use in the present invention. The fumed silica is white amorphous powder produced by high-temperature hydrolysis reaction of silicon chloride (such as silicon tetrachloride) in mixed gas flow generated by combustion of air and hydrogen. Commercially available products of this type are also hydrophilic and hydrophobic, and also high-to-low ratio tables. Precipitated silica refers to silica produced by neutralization of a silicate (e.g., sodium silicate) with an inorganic acid (e.g., sulfuric acid), and precipitation, washing, and drying (usually spray drying) processes. The preferred white carbon black raw material of the invention is fumed silica because the fumed silica has large specific surface area and high chemical purity.

The white carbon black raw material can be obtained from commercial sources, and can also be prepared by engineers familiar with the field according to conventional methods or methods reported in patents and research papers. For example, chinese patent CN200910227646.2 relates to a method for preparing fumed silica.

In order to achieve the effect of the present invention, TiCl must be grafted₄Before the gas-solid reaction, the white carbon black raw material is dried and roasted for pretreatment, so that the moisture and other adsorbed impurities on the surface of the white carbon black raw material are thoroughly removed. The drying can be carried out at a temperature in the range of 30 to 200 ℃. Preferably in the temperature range of 80-120 ℃. Drying can be carried out in still, dry air or in a flowing atmosphere. The flowing atmosphere is most conveniently dry air or nitrogen. The advantage of adopting flowing atmosphere is favorable to taking away the steam that releases in the white carbon black drying process in time, reaches better drying effect. Thus, in principle all that is done is not possible with this purposeOther safe and economical atmospheres which react with the white carbon black or hinder the grafting reaction can be used. In addition to the drying temperature, atmosphere, drying time is a parameter that needs attention. However, since the present invention does not limit the production process, specification and drying equipment of the raw material of the white carbon black, and the drying is followed by the calcination to ensure the pretreatment effect, the drying time parameter can be selected by the engineer familiar with the art in principle. The recommended drying time ranges from 0.5 hours to 100 hours, preferably from 3 hours to 12 hours.

It is emphasized that the dried white carbon black raw material should be well preserved before calcination to avoid adsorbing moisture and other impurities in the air. In order to avoid process complication, the white carbon black and TiCl are preferred₄The gas-solid phase grafting reaction is carried out in-situ and continuously by drying and roasting pretreatment in a reactor. In this case, the drying operation is as described above. And after the drying operation is finished, the material is heated to the roasting temperature by a program for roasting treatment. The roasting treatment is carried out at 200-800 ℃, preferably at 250-700 ℃, and more preferably at 300-500 ℃. The time of the calcination treatment may be selected from 0.5 to 10 hours, preferably 1 to 3 hours, and 2 to 3 hours. The atmosphere for the calcination treatment may be conveniently the same as that for the drying.

The surface moisture content and other adsorbed impurities of the white carbon black subjected to the drying and roasting pretreatment are extremely low, and the white carbon black completely meets TiCl₄Carrying out gas-solid phase grafting reaction. Under convenient conditions, the pretreated white carbon black can be sampled and analyzed theoretically so as to determine the content of moisture and other adsorbed impurities in the pretreated white carbon black. However, in practice, it is difficult to ensure that the sample is not exposed to the atmosphere, and therefore, it is difficult to ensure the reliability of the analysis result, and thus it is not recommended to perform such sampling analysis.

Secondly, grafting TiCl on the pretreated white carbon black through gas-solid phase reaction₄。

The grafting reaction is carried out at a suitable temperature. To make TiCl₄The purpose of fully grafting on the surface of the white carbon black is achievedThe grafting reaction should be continued for a sufficient time. The grafting reaction may be carried out by a gas-solid phase fixed bed reaction method or a gas-solid phase fluidized bed reaction method.

The gas-solid phase reaction recommended by the invention is carried out at a suitable temperature of 100-700 ℃, preferably at a temperature of 200-500 ℃, and more preferably at a temperature of 300-500 ℃. The duration of the grafting reaction recommended by the invention is suitably in the range of 0.5 to 100 hours, preferably in the range of 1 to 48 hours, and more preferably in the range of 1 to 24 hours.

In order to carry out the gas-solid phase grafting reaction, TiCl may be added₄Heating and then using the TiCl produced₄And carrying out gas-solid phase grafting reaction on the gas and the white carbon black. TiCl can also be carried by nitrogen bubbling₄Contacting with white carbon black to carry out gas-solid phase grafting reaction. Alternatively, combining the two i.e. TiCl₄Heating to a suitable temperature to increase its volatility while carrying TiCl with a nitrogen carrier gas₄And carrying out gas-solid phase grafting reaction on the gas and the white carbon black.

TiCl proposed by the invention₄The feeding method is to mix TiCl₄Heating the raw material to a proper temperature and carrying TiCl with nitrogen₄And the gas enters a reactor to carry out gas-solid phase grafting reaction with the white carbon black. Wherein, TiCl₄The heating temperature and the nitrogen carrying capacity of the raw materials can be selected by engineers familiar with the field according to the grafting purpose (titanium carrying capacity on the white carbon black) to be achieved under the condition of considering the grafting reaction conditions. In fact, engineers familiar with the art can flexibly mix TiCl₄The heating temperature of the raw materials, the nitrogen gas carrying capacity and the temperature and duration of the grafting reaction are combined, so that the expected purpose of the grafting reaction, namely the titanium carrying capacity on the white carbon black, is achieved under the specific white carbon black treatment capacity, the reactor scale and the structural form.

However, considering TiCl₄The boiling point of the starting material is about 136 ℃ and therefore TiCl control is convenient₄The feeding speed of raw materials is increased to improve TiCl₄Utilization of raw materials, prevention of TiCl entering the reactor₄The raw material is too high in concentration and too high in flow rateThe TiCl proposed by the present invention is not ready to react and causes waste₄The heating temperature of the raw material should be as low as possible than TiCl₄The boiling point of the feedstock (136 ℃) and the nitrogen loading should also be low as appropriate.

Engineers skilled in the art can determine suitable TiCl on the basis of tests according to the expected purpose of grafting reaction, i.e. titanium loading on the white carbon black, and the prerequisites of specific gas-solid reaction mode (fixed bed, fluidized bed) and reactor scale₄The heating temperature of the raw materials and the nitrogen carrying capacity.

TiCl is finished on the pretreated white carbon black₄After the gas-solid phase grafting reaction, the graft needs to be subjected to nitrogen purging post-treatment so as to carry the unreacted TiCl entrained therein₄All are removed. The nitrogen purging can be carried out at a constant temperature at the reaction temperature, and can also be carried out in the process of cooling the reactor. If desired, the nitrogen purge can also be carried out at a temperature above the grafting reaction temperature. The nitrogen purging is carried out at the temperature higher than the grafting reaction temperature, so that the titanium loss of the grafting material can not be obviously caused, but the bonding degree of part of surface titanium and white carbon black (such as the generation of tripodal titanium) can be changed, and the proportion of chlorine atoms and titanium atoms is reduced. In addition, after the white carbon black graft subjected to nitrogen purging is cooled, the white carbon black graft can be subjected to water washing treatment outside the reactor. Similar to the nitrogen purge treatment at high temperature, the post-water wash treatment does not result in a significant reduction in the titanium content of the graft, but reduces the ratio of chlorine atoms to titanium atoms. However, these changes do not greatly affect the vapor phase epoxidation catalyst of propylene to be produced in the present invention.

Thirdly, using TiCl of white carbon black₄The graft is cheap material and has very small amount of tetrapropyl quaternary ammonium cation (TPA)⁺) Hydrothermal synthesis of titanium silicalite TS-1 in the presence of template agent

The hydrothermal synthesis method refers to that the white carbon black TiCl is subjected to TiCl synthesis₄The grafts are dispersed in tetrapropyl quaternary ammonium cation (TPA)⁺) And (3) putting the mixture into a template agent solution, and then putting the mixture into a crystallization kettle for proper hydrothermal crystallization treatment. The synthesis method is combined with conventional hydrothermal synthesisTiCl with the biggest difference being white carbon black₄Grafting onto tetrapropyl Quaternary ammonium cation (TPA)⁺) The templating agent solution does not form a gel but exists as a solid precipitate.

The conditions of the hydrothermal synthesis are as follows:

modulus of silicon ratio (TPA)⁺/SiO₂): the suitable range is 0.01-0.10, preferably 0.02-0.08;

water to silicon ratio (H)₂O/SiO₂): the suitable range is 0.3-100, preferably 2.0-40

Hydrothermal crystallization temperature range: 80 to 180 ℃, preferably 100 to 170 DEG C

Hydrothermal crystallization time range: from 2 hours to 240 hours, preferably from 4 hours to 120 hours, of tetrapropyl Quaternary ammonium cation (TPA)⁺) The template solution is preferably tetrapropylammonium hydroxide solution. Of course, a combination of a halide salt of a tetrapropyl quaternary ammonium cation and an organic amine such as ethylamine, n-propylamine, n-butylamine, and the like may be used as a template in place of the tetrapropyl ammonium hydroxide solution. Tetrapropylammonium chloride and ammonium bromide are preferred when a combination of a halide salt of a tetrapropylquaternary ammonium cation and an organic amine is used as a template, in view of the problem of negative ion contamination of tetrapropylammonium fluoride and the problem of iodine in tetrapropylammonium iodide. The composition can be determined by the skilled engineer based on published or patent literature reports. In addition, seed crystals may be used to promote the crystallization of the graft in the hydrothermal synthesis of the present invention. The seed crystals are most conveniently titanium silicalite TS-1. The TS-1 zeolite as the seed crystal may be a commercially available product or a hydrothermal synthesis product obtained by the present invention.

When tetrapropylammonium hydroxide solution is used as a template solution, the typical steps of hydrothermal synthesis are as follows: first, according to a predetermined mode silicon ratio (TPA)⁺/SiO₂) Water to silicon ratio (H)₂O/SiO₂) Measuring tetrapropylammonium hydroxide solution with certain concentration, then weighing TiCl with white carbon black added into the template solution₄Grafting, simply stirring, adding the mixture into a hydrothermal crystallization kettle, and performing hydrothermal treatment at a predetermined temperatureAnd (5) crystallizing for a proper time. And separating and recovering the solid crystal from the crystallization kettle according to a conventional method after the hydrothermal crystallization treatment reaches the preset time. Then, after conventional post-treatment operations such as washing, drying and roasting, the TS-1 titanium silicalite crystal is obtained.

The invention has the beneficial effects that: first, TiCl₄The product of the gas-solid phase reaction with the white carbon black, namely the graft, is relatively cheap, and the raw material for synthesizing the titanium silicalite has low cost, high purity and less impurities; secondly, with TiCl₄The titanium silicalite synthesized by the grafting material which is the product of gas-solid phase reaction with the white carbon black is not only easy to obtain the titanium silicalite with high crystallinity, but also can greatly reduce the dosage of the tetrapropylammonium hydroxide template agent; in addition, the titanium silicalite prepared by the method has the obvious characteristic of high activity for the gas-phase epoxidation reaction of propylene and hydrogen peroxide, and is very favorable for inhibiting the self-decomposition side reaction of the hydrogen peroxide at high temperature, so that the effective utilization rate of the hydrogen peroxide is obviously improved.

Drawings

FIG. 1 is a schematic view of a reaction apparatus of the present invention.

FIG. 2 is a graph showing the results of XRD characterization of the TS-1 catalyst.

FIG. 3 is a graph showing the results of SEM characterization of the TS-1 catalyst.

FIG. 4 is a graph showing the results of characterization of the TS-1 catalyst by UV-Vis.

FIG. 5 is a graph showing the results of characterization of the TS-1 catalyst by framework vibrational FT-IR spectroscopy.

Fig. 6 is a XRD analysis result pattern of comparative example 1.

Fig. 7 is a XRD analysis result pattern of comparative example 2.

Detailed Description

The present invention will be further illustrated by the following examples, but the present invention is not limited to these examples.

The effect of the present invention can be evaluated by the following method:

(1) x-ray fluorescence spectroscopy compositional analysis

TiCl of white carbon black₄Titanium content in graft, and TiCl using white carbon black₄The Si/Ti ratio of TS-1 zeolite sample obtained by hydrothermal crystallization of graft can be determined by conventional X-ray fluorescence spectrometry (XRF)

(2) X-ray diffraction of polycrystalline powder

TiCl of white carbon black₄The hydrothermal crystallization of the graft can be characterized by conventional X-ray polycrystalline powder diffraction (XRD) technique. The scanning range is 5-50 degrees. The relative crystallinity of the samples was calculated according to the following formula:

(3) scanning electron microscope

TiCl with white carbon black₄The crystal morphology of the TS-1 zeolite sample obtained by performing hydrothermal crystallization on the graft can be characterized by using a conventional field emission Scanning Electron Microscope (SEM) technology.

(4) Ultraviolet visible diffuse reflectance spectrum (UV-Vis)

When the method is used, BaSO4 can be used as a reference substance. The method can provide information on four-coordination framework titanium, six-coordination amorphous non-framework titanium and anatase titanium oxide.

(5) Zeolite framework vibration Fourier transform infrared spectroscopy (FT-IR)

The method adopts KBr tabletting technology to prepare samples. Before the experiment, a proper amount of sample and spectrally pure KBr are respectively taken and dried for 4 hours at 110 ℃. The dried KBr and zeolite samples were then mixed at a ratio of 200:1 and ground to a powder and pressed into flakes at a pressure of 6 MPa. The method mainly provides the information of the titanium of the four-coordination framework of the TS-1 zeolite. Generally speaking, TS-1 zeolite four-coordinate framework titanium can vibrate in the framework to 960cm of Fourier transform infrared spectrum^-1Characteristic absorption bands appear.

(6) Experiments on the gas-phase epoxidation of propene and hydrogen peroxide

The experimental apparatus is described in detail in the references Ind.Eng.chem.Res.2020,59,7, 2828-2838. The experimental method is as follows: the fluidized reactor was filled with 0.5g of catalyst, and a hydrogen peroxide feed solution (50 wt%) was fed by a peristaltic pump (H)₂O₂The solution at 2.2g/h) was vaporized in an electrothermal Teflon tube to produce hydrogen peroxide vapor (100 ℃). By H₂As a carrier gas to carry the hydrogen peroxide vapor into the reactor to join the propylene. H₂And the propylene flow rates were 160ml/min and 45ml/min, respectively. The space velocity of propylene to the catalyst is WHSV about 10h^-1Propylene and H₂O₂Is approximately equal to 4. The gas phase epoxidation reaction was carried out at 140 ℃ and 0.1 MPa. The epoxidation product was analyzed using an on-line GC-2014C shimzu with dual detectors. The organic products were analyzed by FID detector and DB-Wax (30m 0.32mm) column, and CO by TCD detector and GDX (3m 3mm) column₂。

Example 1:

The embodiment adopts a commercial fumed silica as a raw material, and the main specification characteristic is that the specific surface area is 380m²(ii) in terms of/g. In order to conveniently carry out drying and roasting pretreatment in a flowing atmosphere in a laboratory, the white carbon black is firstly tabletted and sieved, and white carbon black with the granularity of 20-40 meshes is selected as an experimental sample. The drying and roasting pretreatment of the experimental sample are carried out in situ on a gas-solid phase grafting reaction device. The reaction apparatus is schematically shown in FIG. 1.

6g of white carbon black with the granularity of 20-60 meshes is added into a reaction tube of a reaction device. The white carbon black was then subjected to a drying pretreatment in a nitrogen stream (60ml/min) at a drying temperature of 110 ℃ for a drying time of 6 hours.

After the completion of the drying, the temperature of the reaction tube was raised to 400 ℃ at a temperature rising rate of 10 ℃/min while keeping the nitrogen flow constant, and then the white carbon black was subjected to a calcination pretreatment for 2 hours while maintaining the temperature and the nitrogen flow.

The grafting reaction is carried out at 400 ℃. To make TiCl₄The purpose of full grafting is achieved on the surface of the white carbon black, and the grafting reaction lasts for 5 hours. The grafting reaction is carried out according to a gas-solid fixed bed reaction mode.

TiCl₄The feeding method is that TiCl is added₄Heating the raw materials to 40 ℃ by a circulating water jacket, introducing purging nitrogen into TiCl₄In a pot, carry TiCl by bubbling₄And the obtained product enters a reactor to carry out gas-solid phase grafting reaction with white carbon black, wherein the nitrogen flow is 60 ml/min.

TiCl is finished on the pretreated white carbon black₄After the gas-solid phase grafting reaction, carrying TiCl₄The nitrogen flow of (2) was changed to nitrogen purging, and the grafts were continuously purged with nitrogen flow of 60ml/min at the grafting temperature for 1 hour. Then, the temperature of the reaction tube is reduced to room temperature under the condition of nitrogen purging, and the TiCl of the white carbon black is collected₄The color of the graft is light blue. Analysis of the graft by XRF revealed a silicon to titanium ratio (Si/Ti) of about 36.

The conditions of the hydrothermal synthesis are as follows: modulus of silicon ratio (TPA)⁺/SiO₂) 0.06, water to silicon ratio (H)₂O/SiO₂)32 deg.C, hydrothermal crystallizing temperature of 170 deg.C, hydrothermal crystallizing time of 48 hr, tetrapropyl quaternary ammonium cation (TPA)⁺) The templating agent solution was provided as a tetrapropylammonium hydroxide solution. The hydrothermal synthesis steps are as follows: first, according to a predetermined mode silicon ratio (TPA)⁺/SiO₂) Water to silicon ratio (H)₂O/SiO₂)50 ml of 0.1mol/L tetrapropylammonium hydroxide solution is weighed, and 5g of white carbon black TiCl is added into the template solution₄And (3) simply stirring the graft, adding the mixture into a hydrothermal crystallization kettle, and performing hydrothermal crystallization treatment in an electric oven at the temperature of 170 ℃ for 48 hours. And (3) taking the synthesis kettle out of the oven after the hydrothermal crystallization treatment reaches the preset time, chilling the synthesis kettle to room temperature by using water, then opening the synthesis kettle, performing suction filtration on the mixture to obtain a solid product, drying the solid product at 110 ℃, and finally roasting the solid product at 540 ℃ to remove the template agent in the pore channel (for 6 hours) to obtain the TS-1 titanium silicalite crystal. The crystallized product can be directly used for gas-phase epoxidation reaction of propylene and hydrogen peroxide. By XThe results of the RD, SEM, UV-Vis and framework vibration FT-IR spectrum techniques on the characterization of the TS-1 catalyst are shown in the attached figures 2,3, 4 and 5. Wherein XRD analysis shows that the white carbon black has TiCl₄The grafts had been fully crystallized to TS-1 zeolite with no heterocrystals. SEM photograph shows that the synthesized TS-1 zeolite has uniform grain size and belongs to large grains. The UV-Vis and framework vibration FT-IR spectrograms show that the TS-1 catalyst has both four-coordination framework titanium and six-coordination amorphous titanium species and anatase titanium oxide phase. XRF analysis showed that the TS-1 catalyst had a silicon to titanium ratio (Si/Ti) of 56.

The TS-1 zeolite is used as a catalyst for gas-phase epoxidation of propylene and hydrogen peroxide, and the conversion rate of the propylene and the effective utilization rate of the hydrogen peroxide are respectively about 16.7 percent and 70.0 percent, and the gas-phase epoxidation of the propylene mainly generates three products of propylene oxide (28 percent), acetaldehyde (21 percent) and propionaldehyde (42 percent).

The above reaction results show that TiCl using white carbon black₄The graft is cheap material and has very small amount of tetrapropyl quaternary ammonium cation (TPA)⁺) The titanium silicalite TS-1 synthesized by hydrothermal reaction in the presence of the template agent has very high catalytic activity and effective utilization rate of hydrogen peroxide for propylene epoxidation reaction under the condition of gas phase reaction.

Comparative example 1:

this example illustrates that if white carbon black and TiCl are used₄Instead of first forming TiCl of white carbon black by gas-solid reaction as in example 1₄Grafting the material, hydrothermal synthesizing TS-1 in the presence of small amount of template agent, adding the two into template agent solution of the same dosage to prepare gel, and hydrothermal crystallizing to obtain high activity gas phase epoxidized TS-1 zeolite catalyst.

The implementation method of the embodiment is as follows: according to the modulus of silicon ratio (TPA)⁺/SiO₂) 0.06, water to silicon ratio (H)₂O/SiO₂) The specific surface area of 5g is 380m for a compounding ratio of 32²Per g fumed silica and 2.71g TiCl₄And then the mixture is added into 50ml of tetrapropylammonium hydroxide solution with the concentration of 0.1mol/L to prepare uniform titanium silicagel. Then, the gel was put into a water heaterSealing the crystallization kettle, and carrying out hydrothermal crystallization treatment in an electric heating oven. The crystallization temperature is 170 ℃, and the crystallization time is 48 hours. And (3) taking the synthesis kettle out of the oven after the hydrothermal crystallization treatment reaches the preset time, chilling the synthesis kettle to room temperature by using water, then opening the synthesis kettle, performing suction filtration on the mixture to obtain a solid product, drying the solid product at 110 ℃, and finally roasting the solid product at 540 ℃ to remove the template agent in the pore channel (for 6 hours) to obtain the TS-1 titanium silicalite crystal. XRD analysis results show (figure 6), the relative crystallinity of TS-1 zeolite in the hydrothermal crystallization product obtained in the example is extremely low (-0%), when the hydrothermal synthesis product is used as a catalyst for the gas-phase epoxidation reaction of propylene and hydrogen peroxide, the reaction activity is very low, most of hydrogen peroxide is converted through self-decomposition reaction, so that the propylene conversion rate is only 3.4%, and the effective utilization rate of the hydrogen peroxide is only 16.9%.

Comparative example 2:

comparative example 1 was repeated, but the water-to-silicon ratio (H) was determined by changing the concentration of the tetrapropylammonium hydroxide solution to 0.42mol/L₂O/SiO₂) Constant, but modulus of silicon ratio (TPA)⁺/SiO₂) The hydrothermal crystallization time was increased to 0.25 and simultaneously to 120 hours. XRD analysis results show (figure 7), the relative crystallinity of TS-1 zeolite in the hydrothermal crystallization product obtained in the embodiment is close to 100%, when the hydrothermal synthesis product is used as a catalyst for the gas-phase epoxidation reaction of propylene and hydrogen peroxide, the reaction activity is high, and the effective utilization rate of hydrogen peroxide is high and reaches 16.5% and 70.4% respectively.

This example illustrates that if white carbon black and TiCl are used₄Instead of first forming TiCl of white carbon black by gas-solid reaction as in example 1₄Grafting the materials, hydrothermal synthesizing TS-1 in the presence of small amount of template agent, directly adding the grafting materials and the template agent solution to prepare gel, and then dehydrating and thermally crystallizing, so that the high-activity propylene gas-phase epoxidation TS-1 zeolite catalyst can be obtained only under the condition of high template agent dosage, but the cost of the TS-1 zeolite catalyst is increased by doing so.

Comparative example 3:

example 1 was repeated, but the time of the graft reaction was changed to 1 hour, 3 hours and 7 hours in order in the second step, while the preparation was repeated for 5 hours of the graft reaction sample. All grafts are not subjected to hydrothermal crystallization treatment and are directly used for measuring the grafting amount of titanium and propylene gas phase epoxidation reaction. The XRF measurements gave samples with silicon to titanium ratios (Si/Ti) of 48, 42, 36 and 38, corresponding to graft reaction times of 1 hour, 3 hours, 5 hours and 7 hours, respectively. In the epoxidation reaction, the propylene conversion of the above samples was 1.4%, 2.3%, 2.6% and 2.5% in this order, and the hydrogen peroxide effective utilization was 6.5%, 10.3%, 11.8% and 9.6% in this order.

This example illustrates that the grafting reaction time is TiCl affecting white carbon black₄Important factor of titanium content on grafts. The titanium content of the graft can be increased by prolonging the grafting time. On the other hand, although the amorphous graft without hydrothermal crystallization has a certain catalytic capacity (propylene conversion rate) for the gas-phase epoxidation reaction of propylene and hydrogen peroxide, and the catalytic capacity obviously has a positive corresponding relation with the titanium content of the graft, the graft without hydrothermal crystallization has undesirable activity for the gas-phase epoxidation reaction of propylene and hydrogen peroxide.

Comparative example 4:

example 1 was repeated, but in the second step the temperature of the grafting reaction was changed to 200 deg.C, 300 deg.C, and 500 deg.C in this order. All grafts are not subjected to hydrothermal crystallization treatment, and the propylene gas phase epoxidation reaction results of samples corresponding to grafting reaction temperatures of 200 ℃, 300 ℃ and 500 ℃ respectively are as follows: the conversion rate of propylene is 2.4%, 1.8% and 2.3% in sequence, and the effective utilization rate of hydrogen peroxide is 10.8%, 8.2% and 10.4% in sequence.

This example illustrates the grafting reaction temperature on TiCl of white carbon black₄The graft preparation effect is weak. On the other hand, it can be seen from the combination of example 2 that the amorphous graft without hydrothermal crystallization has a catalytic activity (propylene conversion) for the vapor phase epoxidation of propylene and hydrogen peroxide, and the activity is relatively low, and further hydrothermal crystallization is necessary.

Example 2:

example 1 was repeated, but the amount of tetrapropylammonium hydroxide, i.e. the modulus to silica ratio (TPA), was adjusted in the hydrothermal crystallization treatment stage of the third step⁺/SiO₂) The concentration of the template agent solution is changed to 0.03, 0.039 and 0.048 respectively, the water-silicon ratio is kept unchanged, and the hydrothermal crystallization time is prolonged to 72 hours. Corresponds to the mode silicon ratio (TPA)⁺/SiO₂) 0.03, 0.039 and 0.048 in this order, the results of the gas phase epoxidation of propylene of the samples were: the propylene conversion rates were 6.3%, 11.8% and 15.2% in this order, and the hydrogen peroxide effective utilization rates were 27.6%, 50.7% and 67.8% in this order.

This example illustrates the silicon on silicon ratio (TPA)⁺/SiO₂) Influence on white carbon black TiCl₄The important factor of the hydrothermal crystallization result of the grafting material. However, the catalyst preparation method provided by the invention is adopted to prepare the catalyst with extremely low modulus of silicon (TPA)⁺/SiO₂) The high-activity titanium silicalite TS-1 catalyst can be prepared. The benefits of the present invention can be clearly seen in comparison with comparative examples 1 and 2.

Claims

1. Using white carbon black and TiCl₄The method for preparing the high-activity propylene and hydrogen peroxide gas phase epoxidation catalyst by gas-solid phase reaction is characterized by comprising the following steps:

firstly, drying and roasting pretreatment is carried out on the raw material of the white carbon black

Drying the white carbon black raw material at the temperature of 30-200 ℃ for 0.5-100 hours, roasting the dried white carbon black raw material at the temperature of 200-800 ℃ for 0.5-10 hours, and ensuring that water and other adsorbed impurities on the surface of the white carbon black raw material are thoroughly removed;

secondly, grafting TiCl on the pretreated white carbon black through gas-solid phase reaction₄

The temperature of the gas-solid phase grafting reaction is 100-700 ℃, and the duration time of the gas-solid phase grafting reaction is 0.5-100 hours; grafting TiCl on pretreated white carbon black through gas-solid phase reaction₄Thereafter, the graft was aftertreated with a nitrogen purge to ensure that the unreacted TiCl entrained therein was retained₄All are removed;

thirdly, using TiCl of white carbon black₄Grafting material is prepared by adding very small amount of tetrapropyl quaternary ammonium cation TPA⁺Hydrothermal synthesis of titanium silicalite TS-1 in the presence of template agent

The hydrothermal synthesis refers to the preparation of white carbon black TiCl₄The graft is dispersed in tetrapropyl quaternary ammonium cation TPA⁺Putting the mixture into a template agent solution, and then putting the mixture into a crystallization kettle for hydrothermal crystallization treatment; TiCl of white carbon black₄Grafting on tetrapropyl Quaternary ammonium cation TPA⁺The template agent solution does not form gel after being dispersed, but exists in the form of solid precipitate;

the conditions of the hydrothermal synthesis are as follows: mode silicon ratio TPA⁺/SiO₂The range is 0.01-0.10; water to silicon ratio H₂O/SiO₂The range is 0.3-100; the hydrothermal crystallization temperature range is 80-180 ℃; the hydrothermal crystallization time range is 2 hours to 240 hours.

2. The process of claim 1 using white carbon black and TiCl₄A method for preparing a high-activity propylene and hydrogen peroxide gas phase epoxidation catalyst by gas-solid phase reaction is characterized in that in the first step:

the drying temperature is 80-120 ℃, and the drying time is 3-12 hours;

the roasting treatment temperature is 250-700 ℃, and the roasting treatment time is 1-3 hours;

the white carbon black is gas phase white carbon black or precipitation white carbon black;

the drying process is carried out in static, dry air, or in a flowing atmosphere, when in a flowing atmosphere, a flowing atmosphere is dry air or nitrogen;

in order to prevent the dried and roasted white carbon black from adsorbing water vapor and impurities in the air again in the transfer process, the white carbon black and TiCl are pretreated by drying and roasting₄The gas-solid phase grafting reaction is carried out in situ and continuously in a reactor.

3. The process of claim 2 using white carbon black and TiCl₄The method for preparing the high-activity propylene and hydrogen peroxide gas phase epoxidation catalyst through gas-solid phase reaction is characterized in that in the first step, the roasting treatment temperature is 300-500 ℃, and the roasting treatment time is 2-3 hours.

4. The process according to claim 1,2 or 3 using white carbon black and TiCl₄The method for preparing the high-activity propylene and hydrogen peroxide gas phase epoxidation catalyst by gas-solid phase reaction is characterized in that in the second step:

the temperature of the gas-solid phase grafting reaction is 200-500 ℃, and the duration time of the gas-solid phase grafting reaction is 1-48 hours;

the gas-solid phase grafting reaction is carried out according to a gas-solid phase fixed bed reaction mode or a gas-solid phase fluidized bed reaction mode;

the gas-solid phase reaction grafting method is carried out by selecting one of the following three modes:

method one, TiCl is treated₄Heating, using the generated TiCl₄Carrying out gas-solid phase grafting reaction on the gas and the white carbon black;

carrying TiCl by nitrogen bubbling₄Contacting with white carbon black to carry out gas-solid phase grafting reaction;

in the third way, TiCl is reacted₄Heating to a suitable temperature to increase its volatility while carrying TiCl with a nitrogen carrier gas₄Carrying out gas-solid phase grafting reaction on the gas and the white carbon black;

TiCl₄the heating temperature of the raw material is lower than TiCl₄The boiling point of the starting material is 136 ℃ and care is taken to mix TiCl₄The heating temperature and the nitrogen carrying capacity of the raw materials are matched with the temperature and the duration of the grafting reaction.

5. The process of claim 4 using white carbon black and TiCl₄The method for preparing the high-activity propylene and hydrogen peroxide gas phase epoxidation catalyst through gas-solid phase reaction is characterized in that in the second step, the temperature of gas-solid phase grafting reaction is 300-500 ℃, and the duration time of the gas-solid phase grafting reaction is 1-24 hours.

6. The use of white carbon black and TiCl as claimed in claim 1,2, 3 or 5₄The method for preparing the high-activity propylene and hydrogen peroxide gas phase epoxidation catalyst by gas-solid phase reaction is characterized in that in the third step:

the conditions of the hydrothermal synthesis are as follows: mode silicon ratio TPA⁺/SiO₂The range is 0.02-0.08; water to silicon ratio H₂O/SiO₂The range is 2.0-40; the hydrothermal crystallization temperature range is 100-170 ℃; the hydrothermal crystallization time range is 4-120 hours;

tetrapropyl quaternary ammonium cation TPA⁺The template solution is tetrapropylammonium hydroxide solution.

7. The process of claim 4 using white carbon black and TiCl₄The method for preparing the high-activity propylene and hydrogen peroxide gas phase epoxidation catalyst by gas-solid phase reaction is characterized in that in the third step: