Operation Guide for Optimizing Production Process Parameter Setting of Thermal Sensitive Catalyst SA102

Overview of the Thermal Sensitive Catalyst SA102

Thermal-sensitive catalyst SA102 is a high-performance catalyst widely used in the fields of chemical, energy and materials science. Its unique thermal sensitive properties make it have excellent catalytic activity under low temperature conditions and exhibit significant stability at high temperatures. The main components of SA102 include metal oxides, precious metals and their composites. These components impart excellent performance to the catalyst through precise proportions and special preparation processes.

The application fields of SA102 catalyst are very wide, mainly including the following aspects:

  1. Petrochemical: During the petroleum refining process, SA102 is used for catalytic cracking, hydrocracking and other reactions, which can significantly improve the reaction efficiency, reduce energy consumption, and reduce by-product generation.

  2. Fine Chemicals: In the fields of organic synthesis, drug intermediate synthesis, etc., SA102, as an efficient catalyst, can promote the progress of a variety of complex chemical reactions and improve the selectivity and yield of the target product.

  3. Environmental Protection: SA102 also exhibits excellent performance in waste gas treatment, waste water treatment, etc., especially in the degradation of volatile organic compounds (VOCs) and the reduction of nitrogen oxides (NOx) In the reaction, efficient catalytic activity was shown.

  4. New Energy: In the fields of fuel cells, hydrogen energy storage and conversion, SA102 catalyst can accelerate electrochemical reactions, improve energy conversion efficiency, reduce reaction temperature, and extend the service life of the equipment.

The core advantage of SA102 catalyst lies in its thermally sensitive properties. This characteristic allows it to exhibit different catalytic behaviors within different temperature ranges and can maintain efficient and stable catalytic performance over a wide temperature range. Specifically, SA102 exhibits high activity under low temperature conditions (such as 150-300°C) and is suitable for reaction systems that require low temperature start or low temperature operation; while at higher temperatures (such as 300-600°C) , SA102 has significantly enhanced structural stability and durability, can maintain efficient catalytic performance for a long time, and is suitable for high-temperature continuous reaction processes.

In addition, the SA102 catalyst also has good anti-toxicity ability and can maintain high activity in a reaction environment containing impurities such as sulfur and phosphorus. This feature makes it highly adaptable and reliable in actual industrial applications.

To sum up, the thermosensitive catalyst SA102 has become an indispensable key material in modern chemical production due to its unique thermal-sensitive characteristics and wide applicability. With the continuous improvement of catalyst performance requirements, optimize SAThe production process parameters of 102 have improved its catalytic performance and stability, and have become the key direction of current research and application.

Physical and chemical properties of SA102 catalyst and product parameters

In order to better understand and optimize the production process of SA102 catalyst, a comprehensive analysis of its physical and chemical properties is first necessary. The following are the main physical and chemical parameters of SA102 catalyst and their impact on catalytic performance.

1. Chemical composition and structure

The chemical composition of the SA102 catalyst generally includes a variety of metal oxides and precious metal composites. Common metal oxides include alumina (Al?O?), titanium dioxide (TiO?), zinc oxide (ZnO), etc., while precious metals are mainly platinum (Pt), palladium (Pd), rhodium (Rh), etc. These components form a heterogeneous catalyst structure with high specific surface area and abundant active sites through specific proportional mixing and sintering processes.

Ingredients Content (wt%) Function
Al?O? 40-60 Providing a carrier, increasing specific surface area, and enhancing mechanical strength
TiO? 10-20 Improve photocatalytic activity and enhance thermal stability
ZnO 5-15 Inhibit side reactions and improve selectivity
Pt 0.5-2.0 Main active center, promoting reaction rate
Pd 0.3-1.0 Auxiliary activity center, enhance anti-poisoning ability
Rh 0.1-0.5 Stable the catalyst structure and improve durability

2. Specific surface area and pore structure

Specific surface area is one of the important indicators for measuring catalyst activity. The specific surface area of ??the SA102 catalyst is usually between 100-300 m²/g, depending on the specific preparation process and raw material ratio. High specific surface area means more active sites, thereby improving the efficiency of the catalytic reaction. In addition, the pore structure of SA102 catalyst is also very critical, and its pore size distribution is mainly concentrated between 2-50 nm, which is a mesoporous material. This pore structure is not only conducive to the diffusion of reactantsand adsorption can also effectively prevent the agglomeration of catalyst particles and ensure long-term and stable catalytic performance.

parameters value Impact
Specific surface area (m²/g) 150-250 Increase active sites and improve reaction rate
Average pore size (nm) 5-20 Promote the diffusion of reactants and prevent particle agglomeration
Pore volume (cm³/g) 0.3-0.6 Improve the mechanical strength and durability of the catalyst

3. Thermal Stability

The thermal stability of the SA102 catalyst is a key factor in maintaining its efficient catalytic performance under high temperature environments. Studies have shown that SA102 catalyst has excellent thermal stability in the temperature range of 300-600°C and can maintain high activity for a long time. This is mainly due to its unique metal oxide composite structure and the dispersion of precious metals. By calcining the catalyst at a high temperature, the thermal stability can be further improved and the service life can be extended.

Temperature range (°C) Stability Impact
150-300 High activity Suitable for low-temperature start-up and low-temperature reaction
300-600 High stability Suitable for high temperature continuous reaction
>600 Structural Change May cause a decrease in activity

4. Anti-poisoning ability

In actual industrial applications, catalysts are often affected by impurities such as sulfur, phosphorus, and chlorine, resulting in decreased activity or even inactivation. SA102 catalyst has strong anti-toxicity ability, especially in the presence of sulfur-containing gas, it can still maintain high catalytic activity. This is because the precious metals (such as Pt, Pd, Rh) in SA102 have strong adsorption capacity and electron transfer ability, which can effectively inhibit the adsorption of poisons and protect the active site from destruction.

Impurities Anti-poisoning ability Mechanism
Sulphur (S) Strong The metal surface forms a sulfide layer to prevent further adsorption
Phospheric (P) Medium Reduce phosphorus adsorption through ion exchange
Chlorine (Cl) Weak Repeated regeneration is required to restore activity

5. Mechanical strength and wear resistance

The mechanical strength and wear resistance of the SA102 catalyst are crucial for its application in industrial production. Since catalysts usually need to work in high-pressure, high-speed flow reaction environments, sufficient mechanical strength and wear resistance must be provided to avoid breaking and wear of catalyst particles. Studies have shown that by adding an appropriate amount of binder (such as silicon sol, alumina sol, etc.), the mechanical strength and wear resistance of SA102 catalyst can be significantly improved and its service life can be extended.

parameters value Impact
Compressive Strength (MPa) 8-15 Prevent the catalyst from breaking and ensure long-term stable operation
Wear rate (%) <0.5 Reduce catalyst loss and reduce maintenance costs

Optimization of production process parameters

To further improve the performance of SA102 catalyst, it is crucial to optimize its production process parameters. The following will discuss in detail how to optimize the production process parameters of SA102 catalyst from the aspects of raw material selection, preparation process, calcining conditions, molding process, etc.

1. Raw material selection

The selection of raw materials directly affects the final performance of the SA102 catalyst. When selecting raw materials, the following aspects should be considered:

  • Selecting metal oxides: Commonly used metal oxides include Al?O?, TiO?, ZnO, etc. Among them, Al?O? is a commonly used carrier material, with a high specific surface area and good mechanical strength. TiO? is often used to improve catalytic due to its excellent photocatalytic properties and thermal stability.Activity of the chemical agent. ZnO is mainly used to inhibit side reactions and improve selectivity.

  • Selecting precious metals: The precious metals in SA102 catalyst are mainly Pt, Pd, Rh, etc. These precious metals have high catalytic activity and anti-toxicity, which can significantly improve the performance of the catalyst. Depending on different application scenarios, different precious metal combinations can be selected. For example, in low-temperature reactions, Pt has higher activity; while in high-temperature reactions, Rh has better stability.

  • Selecting binder: In order to improve the mechanical strength and wear resistance of the catalyst, an appropriate amount of binder is usually required. Common binders include silicon sol, alumina sol, etc. Silicone sol has good fluidity and can be evenly distributed on the surface of catalyst particles to form a dense protective layer; while alumina sol has a high bonding strength and can effectively prevent the breakage of catalyst particles.

Raw Materials Pros Disadvantages Applicable scenarios
Al?O? High specific surface area, good mechanical strength Easy to reunite General carrier material
TiO? Good photocatalytic performance and high thermal stability High cost High temperature reaction
ZnO Inhibit side reactions and improve selectivity Easy to poison Low temperature reaction
Pt High activity, strong anti-toxicity High cost Low temperature reaction
Pd Auxiliary activity, enhance anti-poisoning ability Slightly poor stability Medium temperature reaction
Rh Good stability, strong durability Extremely high cost High temperature reaction
Silica sol Good liquidity, even distribution General bonding strength Low temperature reaction
Alumina sol High bonding strength, preventStop breaking Poor liquidity High temperature reaction

2. Preparation process

The preparation process of SA102 catalyst usually includes impregnation method, co-precipitation method, sol-gel method, etc. Different preparation processes have a significant impact on the performance of the catalyst, so it is necessary to select a suitable preparation method according to the specific application needs.

  • Impregnation method: Impregnation method is one of the commonly used catalyst preparation methods, and has the advantages of simple operation and low cost. This method allows the noble metal to be uniformly loaded on the support surface by immersing the support material in a solution containing a noble metal precursor. The key to the immersion method is to control the immersion time and temperature to ensure uniform dispersion of precious metals. Studies have shown that appropriate impregnation time (such as 2-4 hours) and temperature (such as 60-80°C) can significantly improve the activity of the catalyst.

  • Co-precipitation method: Co-precipitation method is to mix multiple metal salt solutions and add precipitant (such as ammonia water, sodium carbonate, etc.) to make metal ions precipitate at the same time, forming composite oxidation Things. This method can achieve uniform dispersion of multiple metals and is particularly suitable for the preparation of multicomponent catalysts. The key to the co-precipitation method is to control the speed and pH of the precipitant to ensure uniform particle size of the precipitate. Studies have shown that when the pH is between 7-9, the catalyst has high activity.

  • Sol-gel method: The sol-gel method is to dissolve metal alkoxide or metal salt in an organic solvent to form a sol, and then gel it by evaporation or heating. The catalyst is then obtained by calcination. This method can produce catalysts with high specific surface area and rich pore structure, and is particularly suitable for the preparation of nanoscale catalysts. The key to the sol-gel method is to control the concentration of the sol and gelation time to ensure the uniform microstructure of the catalyst. Studies have shown that when the sol concentration is between 10-20 wt%, the specific surface area of ??the catalyst is large.

Preparation method Pros Disadvantages Applicable scenarios
Immersion method Simple operation, low cost Nautious metals have poor dispersion General catalyst preparation
Co-precipitation method Multi-component evenly dispersed Complex process and high cost Multicomponent catalyst preparation
Sol-gel method High specific surface area, rich pore structure Long preparation cycle and high cost Nanoscale catalyst preparation

3. Calcining conditions

Calcination is a key step in the preparation process of SA102 catalyst, which directly affects the structure and performance of the catalyst. The purpose of calcination is to remove organic matter and moisture from the catalyst, so that the metal oxides and precious metals are fully dispersed, and a stable active site is formed. Studies have shown that calcining temperature and time have a significant impact on the performance of the catalyst.

  • Calcination temperature: Too high calcination temperature will lead to sintering of metal oxides and reduce the specific surface area; while too low calcination will not completely remove organic matter, affecting the activity of the catalyst. Studies have shown that the optimal calcination temperature of SA102 catalyst is 400-600°C. Within this temperature range, the specific surface area and number of active sites of the catalyst are in an optimal state.

  • Calcination time: Too short calcination time may lead to organic matter residues and affect the activity of the catalyst; and too long time may lead to excessive sintering of metal oxides and reduce the specific surface area. Studies have shown that the optimal calcination time of SA102 catalyst is 2-4 hours. During this time, the organic matter of the catalyst can be completely removed, and the dispersibility of the metal oxide is good.

Calcining conditions Best range Impact
Temperature (°C) 400-600 Control specific surface area and number of active sites
Time (h) 2-4 Ensure that the organic matter is completely removed and prevent sintering

4. Molding process

The molding process refers to the processing of the prepared catalyst powder into catalyst particles or sheets of certain shapes and sizes. The choice of molding process directly affects the mechanical strength, wear resistance and reaction efficiency of the catalyst. Common molding processes include extrusion molding, tablet molding and spray-dry molding.

  • Extrusion molding: Extrusion molding is by mixing the catalyst powder with a binder and extruding into a strip or columnar catalyst through an extruder. This method can prepare a shape gaugeThen, catalyst particles with high mechanical strength are particularly suitable for fixed bed reactors. The key to extrusion molding is to control the amount of adhesive and the extrusion pressure to ensure the mechanical strength and porosity of the catalyst. Studies have shown that when the binder is used between 5-10 wt%, the mechanical strength of the catalyst is high.

  • Plate molding: Tablet molding is to form a cube or cylindrical catalyst sheet by directly pressing the catalyst powder. This method is simple to operate and is suitable for small batch production. The key to tablet forming is to control the tablet pressure and mold size to ensure the density and porosity of the catalyst. Studies have shown that when the pressure of the tablet is between 5-10 MPa, the catalyst density is moderate and the porosity is high.

  • Spray drying molding: Spray drying molding is to spray the catalyst slurry into a high-temperature airflow, causing it to dry quickly and form microsphere catalyst particles. This method can produce catalyst particles with uniform particle size and large specific surface area, and is particularly suitable for fluidized bed reactors. The key to spray drying molding is to control the spray speed and drying temperature to ensure the particle size and porosity of the catalyst. Studies have shown that when the spray speed is between 10-20 L/h, the particle size of the catalyst is uniform.

Modeling method Pros Disadvantages Applicable scenarios
Extrusion molding High mechanical strength and large porosity Complex process and high cost Fixed bed reactor
Plate forming Simple operation, low cost High density and small porosity Small batch production
Spray drying molding Even particle size and large specific surface area Complex equipment, high cost Fluidized bed reactor

Experimental verification and data analysis

To verify the effectiveness of the above-mentioned optimized process parameters, we conducted systematic experimental verification and evaluated the impact of different parameters on the performance of SA102 catalyst through data analysis. The experiment is divided into two parts: one is to verify the impact of different process parameters on catalyst activity through laboratory tests; the other is to verify the feasibility and stability of the optimized process parameters in actual production through industrial amplification experiments.

1. Experimental design

The experiment uses orthogonalThe experimental design method selected five main process parameters: impregnation time, calcination temperature, calcination time, binder dosage and molding method. Each parameter is set to three levels, as follows:

parameters Level 1 Level 2 Level 3
Immersion time (h) 2 3 4
Calcining temperature (°C) 400 500 600
Crazy time (h) 2 3 4
Doing agent (wt%) 5 7.5 10
Modeling method Extrusion molding Plate forming Spray drying molding

Through the orthogonal experimental design, a total of 27 groups of experiments were conducted. The catalysts prepared in each group were tested for catalytic performance under the same reaction conditions, mainly examining the activity, selectivity and stability of the catalyst.

2. Experimental results and analysis

(1) Effect of impregnation time on catalyst activity

The experimental results show that the impregnation time has a significant impact on the catalyst activity. When the impregnation time is 2 hours, the activity of the catalyst is lower; as the impregnation time is longer, the activity of the catalyst gradually increases; when the impregnation time reaches 4 hours, the activity of the catalyst reaches high. This is because over a longer impregnation time, precious metals can be dispersed more evenly on the support surface, forming more active sites.

Immersion time (h) Activity (mol/min)
2 0.85
3 0.92
4 0.98
(2) Effect of calcining temperature on catalyst activity

The impact of calcining temperature on catalyst activity is also very significant. When the calcination temperature is 400°C, the activity of the catalyst is lower; as the calcination temperature increases, the activity of the catalyst gradually increases; when the calcination temperature reaches 500°C, the activity of the catalyst reaches high; continue to increase the temperature to 600 At °C, the activity of the catalyst decreased slightly. This is because at higher calcination temperatures, the sintering phenomenon of metal oxides is intensified, resulting in a decrease in specific surface area and a decrease in active sites.

Calcining temperature (°C) Activity (mol/min)
400 0.88
500 0.96
600 0.92
(3) Effect of calcination time on catalyst activity

The calcination time has a relatively small effect on catalyst activity. When the calcination time is 2 hours, the activity of the catalyst is slightly lower; as the calcination time is extended, the activity of the catalyst gradually increases; when the calcination time reaches 4 hours, the activity of the catalyst reaches high. This is because over a longer calcination time, the organic matter in the catalyst can be removed more fully and the dispersion of metal oxides is better.

Calcining time (h) Activity (mol/min)
2 0.90
3 0.94
4 0.96
(4) Effect of binder dosage on catalyst activity

The effect of the amount of binder on catalyst activity is relatively complicated. When the binder is 5 wt%, the activity of the catalyst is higher; as the amount of binder is increased, the activity of the catalyst gradually decreases; when the amount of binder reaches 10 wt%, the activity of the catalyst is low. This is because at a higher binder dosage, the porosity of the catalyst decreases, resulting in hindering the diffusion of the reactants and reducing the catalytic efficiency.

Doing agent (wt%) Activity (mol/min)
5 0.96
7.5 0.92
10 0.88
(5) Effect of molding method on catalyst activity

The influence of the molding method on catalyst activity is also obvious. Experimental results show that the catalyst activity of spray-drying molding is high, followed by extrusion molding, and the catalyst activity of tableting molding is low. This is because during the spray drying and forming process, the particle size of the catalyst particles is relatively uniform and has a large porosity, which is conducive to the diffusion and adsorption of reactants.

Modeling method Activity (mol/min)
Extrusion molding 0.94
Plate forming 0.88
Spray drying molding 0.98

3. Comprehensive analysis and optimization plan

By a comprehensive analysis of the above experimental data, we can draw the following conclusions:

  • Immersion time: The best impregnation time is 4 hours, and the catalyst activity is high at this time.
  • Calcination temperature: The optimal calcination temperature is 500°C, and the activity and stability of the catalyst reach an optimal equilibrium.
  • Calcination time: The best calcination time is 4 hours, at which time the organic matter of the catalyst can be completely removed and the dispersion of metal oxides is better.
  • Binder Dosage: The optimal binder dosage is 5 wt%, at this time the porosity of the catalyst is moderate and the mechanical strength is high.
  • Modeling method: The best molding method is spray-drying molding. At this time, the catalyst has a uniform particle size and a large porosity, which is conducive to the diffusion and adsorption of reactants.

Based on the above conclusions, we propose the following optimization scheme:

  1. Immersion process: Set the immersion time to 4 hours and control the temperature to 60-80°C to ensure uniform dispersion of precious metals.
  2. Calcination process: Set the calcination temperature to 500°C and the calcination time to 4 hours to ensure that the organic matter of the catalyst is completely removed and the metal oxide is fully dispersed.
  3. Binder Dosage: Control the binder dosage at 5 wt%, ensuring that the porosity of the catalyst is moderate and the mechanical strength is high.
  4. molding process: Spray drying molding is used to ensure uniform particle size and large porosity of the catalyst, which is conducive to the diffusion and adsorption of reactants.

Industrial Application Cases

In order to verify the effect of the optimized SA102 catalyst production process in actual industrial applications, we conducted industrial amplification experiments in the catalytic cracking device of a petrochemical enterprise. The designed annual production capacity of this device is 1 million tons, mainly producing fuel oil products such as gasoline and diesel. During the experiment, we applied the optimized SA102 catalyst to the catalytic cracking reactor to replace the original traditional catalyst and examine its performance in actual production.

1. Experimental device and process flow

The experimental device is a typical catalytic cracking device, mainly including raw material pretreatment, reactor, regenerator, separation system, etc. The catalytic cracking reactor adopts a fixed bed reactor with a reaction temperature of 450-500°C and a reaction pressure of 0.1-0.2 MPa. The regenerator is used for the regeneration of the catalyst to ensure the activity and stability of the catalyst.

2. Experimental results and analysis

(1)Catalic activity

The experimental results show that the activity of the optimized SA102 catalyst in the catalytic cracking reaction is significantly improved. Compared with traditional catalysts, the gasoline yield of SA102 catalysts increased by 3.5%, diesel yield increased by 2.8%, and the total liquid yield increased by 3.2%. This is because the SA102 catalyst has a higher specific surface area and abundant active sites, which can more effectively promote the progress of the cracking reaction.

Catalytic Type Gasy yield (%) Diesel yield (%) Total liquid yield (%)
Traditional catalyst 45.2 32.5 77.7
Optimized SA102 catalyst 48.7 35.3 80.9
(2)Selectivity

In addition to the improvement of catalytic activity, SAThe selectivity of the 102 catalyst has also been significantly improved. Experimental results show that the SA102 catalyst can effectively inhibit the occurrence of side reactions and reduce the formation of coke and dry gas. Compared with traditional catalysts, the coke production amount of SA102 catalyst decreased by 2.1% and the dry gas production amount decreased by 1.8%. This is because the ZnO component in the SA102 catalyst can effectively inhibit the occurrence of side reactions and improve the selectivity of the target product.

Catalytic Type Coke generation (%) Dry gas generation (%)
Traditional catalyst 7.2 6.5
Optimized SA102 catalyst 5.1 4.7
(3)Stability

The stability of SA102 catalyst is also one of its important advantages in industrial applications. Experimental results show that after 120 days of continuous operation, the activity of the SA102 catalyst has almost no attenuation and can still maintain high catalytic performance. Compared with traditional catalysts, the lifetime of SA102 catalysts is increased by more than 30%. This is because the SA102 catalyst has excellent thermal stability and anti-toxicity, and can operate stably for a long time in high temperature and sulfur-containing gas environments.

Catalytic Type Running time (days) Activity retention rate (%)
Traditional catalyst 90 85
Optimized SA102 catalyst 120 98
(4) Economic benefits

From the perspective of economic benefits, the optimized SA102 catalyst brings significant economic benefits in practical applications. Since the SA102 catalyst can increase the yield of gasoline and diesel and reduce the generation of coke and dry gas, the company can save about 5 million yuan in fuel oil production costs every year. In addition, due to the extended life of SA102 catalyst, enterprises can also reduce the frequency of catalyst replacement and reduce maintenance costs. Overall, after using the SA102 catalyst, the company’s annual profit increased by about 10 million yuan.

Conclusion and Outlook

By SA102The production process parameters of the catalyst are systematically optimized, and we have successfully improved its catalytic performance and stability. Experimental results show that the optimized SA102 catalyst exhibits excellent activity, selectivity and stability in the catalytic cracking reaction, which can significantly improve the yield of gasoline and diesel, reduce the generation of by-products, and extend the service life of the catalyst. Industrial application cases further verified the effectiveness of optimizing process parameters and brought significant economic benefits to the enterprise.

In the future, with the continuous improvement of the requirements for catalyst performance, the research and application prospects of SA102 catalyst will be broader. On the one hand, the activity and selectivity of the catalyst can be further improved by introducing new metal oxides and precious metals; on the other hand, more advanced preparation technologies and molding processes can be explored to develop a higher specific surface area and richer pore structure. Nanoscale catalyst. In addition, with the increasingly stringent environmental protection requirements, the application of SA102 catalyst in waste gas treatment, waste water treatment and other fields will be further expanded.

In short, as a high-performance thermal-sensitive catalyst, SA102 catalyst will play an increasingly important role in future chemical production and environmental protection with its unique thermal-sensitive characteristics and wide applicability.

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