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BenchCAT Catalog

INTRODUCTION

  • The BenchCAT is built for researchers who need to process larger catalyst volumes or require custom reactor configurations. Typically designed as floor-standing systems or specialized setups, BenchCAT units are ideal for advanced catalysis studies, pilot-scale testing, or any application that goes beyond standard fixed-bed reactor capabilities.
  • By comparison, the μBenchCAT series consists of pre-engineered, benchtop systems that sit easily on a lab table or workbench. These compact units are optimized for fixed-bed catalytic experiments, with configurable options for gas and liquid feeds, as well as a range of temperature and pressure conditions. The microBenchCAT offers a spaceefficient and cost-effective solution for routine testing and academic research.
  • Choose the BenchCAT when your research demands greater scale, flexibility, or custom design beyond what the microBenchCAT series offers. AMI will customize these instruments to meet your exact research needs today.

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  • BenchCAT Catalog

APPLICATIONS

  • 01 Petrochemical Industry
  • 02 Coal Chemical Industry
  • 03 Fine Chemicals
  • 04 Environmental Protection
  • 05 CO2 Adsorption & Capture
  • 06 Hydrogenation Catalysis Systems
  • 07 Adsorption Separation
  • 08 Multichannel Capability
  • 09 Flue Gas Denitrification Systems
  • 10 Fixed-Bed Reactors
  • 11 Fluidized-Bed Reactors
  • 12 Trickle-Bed Reactors
  • 13 Slurry-Phase (Autoclave) Reactors
  • 14 Catalyst Evaluation Systems
  • 15 Photocatalytic Reaction Systems
  • 16 Electrochemical Reaction Systems

Client Cases

  • Heavy Oil Hydrocracking Catalyst Evaluation Reactor
  • The reactor is used to evaluate the performance and effectiveness of hydrocracking catalysts for heavy petroleum fractions. In this device, heavy petroleum fractions typically come into contact with the catalyst and react under high temperature and pressure conditions to convert the heavy fractions into lighter products, such as fuel oil or paraffin. The system generally includes a gas supply system, liquid supply system, preheating reaction system, condensation separation system, and backpressure system. By evaluating the catalyst performance, the petroleum processing technology can be improved, enhancing product quality and yield.
  • Design Parameters:
  • Catalyst Loading 100 mL
    2 Inlet Gas Streams, 1 Inlet Liquid Stream
    Design Reaction Pressure 10.0 MPa
    Design Reaction Temperature 500°C
  • CO2Gas Adsorption and Capture Reactor
  • This reactor is specifically designed for studying and experimenting with the CO2adsorption process. It uses specific adsorbents (such as molecular sieves, activated carbon, etc.) to simulate the process of CO2being adsorbed from the gas phase onto solid adsorbents. The technical features include real-time monitoring of CO2concentration changes, control over the selectivity of the adsorbent, and the ability to perform multiple adsorption-desorption cycles to evaluate the regeneration performance of the adsorbent. It is primarily used in the research of carbon capture technologies, providing insights into CO2 adsorption behavior under various conditions, evaluating the performance of adsorbents, and offering scientific data to address climate change and mitigate greenhouse gas emissions.
  • CO2 Hydrogenation Catalyst Evaluation Device (Touchscreen)
  • The device features a touchscreen interface, allowing users to intuitively and conveniently control experimental conditions and monitor the reaction process. Technical Features: Full-component backpressure after the reaction. It ensures stable reaction pressure while enabling pressure control, allowing subsequent process steps to be operated at atmospheric pressure. This design not only saves costs but also accommodates different process modes.
  • Methanol - Carrying 2ml Multifunctional Catalyst Evaluation Reactor
  • SCR Desulfurization and Denitrification Reactor
  • Design Parameters:
  • Catalyst Loading 100 mL
    Catalyst loading 50 g~100 g
    N2 gas flow rate 0~ 2 L/min
    Air gas flow rate 0 ~4 L/min
    Reserved gas flow rate 0 ~2 L/min
    Liquid Feed Rate 5 ~ 250 g/h
    Design Pressure ≤ 6 MPa
    Design Reaction Temperature 850°C
    Design Preheating Temperature 350°C
  • 100g MTO Fixed Fluidized Bed
  • It is primarily used to evaluate the performance of catalysts in the MTO process, to improve MTO catalysts, and to enhance the selectivity and yield of olefins. The unit consists of a reactor, catalyst supply system, fluidized bed system, and product analysis module. Its technical features include controllable reaction temperature and pressure, an efficient fluidized bed system, and the capability for real-time monitoring and analysis of products.
  • Methanation High-Pressure Dual-Channel Parallel Reactor
  • The methanation reactions of CO and CO2 are volume-reducing reactions, and higher pressure promotes a more complete reaction.
  • Technical Features:
  • The high-pressure reactor and the dual-tube parallel reaction furnace are specially designed to ensure the matching of the reactor and parallel reaction furnace while maintaining parallel temperature conditions.
  • Fluidized - bed Reactor
  • Simulation of Fluidized - bed Catalytic Reaction:
  • It can simulate the common fluidized - bed catalytic reaction conditions in industry, where the granular bed material is in a fluidized state under the action of gas flow. This design brings the experiment closer to actual industrial applications.
  • Better Mass Transfer and Reaction Performance:
  • The special structure of the fluidized bed enables the granular bed material to be efficiently mixed in the flowing gas, improving the mass - transfer efficiency and enhancing the contact between the catalyst and the reactants.
  • Study on the Kinetics of Fluidized - bed Catalysts:
  • This involves studying the kinetic behavior of catalysts in a dynamic fluidized bed. It is of great significance for understanding the stability, durability of the catalyst in actual reactions, as well as its response to different gas components.
  • Experimental Results Closer to Practical Applications:
  • The catalyst evaluation device can provide a more realistic dynamic of gas flow in the bed layer, making the experimental results closer to actual industrial applications, thus better guiding the design and application of industrial catalysts.
  • Catalyst Loading 100 ~150 g
    NH3 Gas Flow Rate 0 ~ 3000 m1/min ±1% FS
    N2 Gas Flow Rate 0 ~ 1000 m1/min ±1% FS
    Liquid Feed Rate 0 ~ 5 m1/min ±1% FS
    Reaction Pressure micro positive pressure ±1°C
    Reaction Temperature 0 ~ 750°C ±1°C
    Preheating Temperature 0 ~ 350°C ±1°C
  • VOC Reactor
  • The VOC (Volatile Organic Compound) reaction device is used for the treatment of volatile organic pollutants, typically applied in air pollution control. These devices generally include a gas treatment unit where VOCs are oxidized, degraded, or converted into harmless substances. The technical features of the device enable the efficient removal of VOCs using high-performance catalysts or oxidants.
  • ·Design Parameters:
  • Catalyst Loading 0.1~1.0g
    VOC Gas Carrying Equipment The VOC raw material is delivered to the reactor in the form of saturated vapor pressure.
    VOC Carrying Capacity 5%~10%
    Inlet Gas-Liquid Phase The raw materials can be heated using an air bath, ensuring integrated full-pipeline insulation to prevent any "cold spots" in the stainless steel pipelines and valves.
    Post-Reaction Full-component insulated chromatographic detection is conducted.
  • Fischer-Tropsch Synthesis Reaction Product Online Gas Chromatography Analysis System
  • The Fischer-Tropsch synthesis reaction system uses synthesis gas (a mixture of carbon monoxide and hydrogen) as raw material, and through a catalyst and suitable conditions, synthesizes liquid hydrocarbons or hydrocarbon compounds. This process is a key component of gas liquefaction technology, and is typically used to produce synthetic lubricating oils and synthetic fuels from coal, natural gas, or biomass. Fischer- Tropsch synthesis has received intermittent attention as a source of low-sulfur diesel fuel, addressing issues related to the supply or cost of petroleum-based hydrocarbons.
  • Fixed Bed Hydrogenation Catalyst Evaluation Reactor
  • Catalyst Loading: 1～6ml
    High-Precision Constant Flow Pump Enhances the accuracy of liquid feed.
    Precision Pressure Gauges Installed at the reactor inlet and outlet, providing clear pressure differential before and after the reaction. Post-Reaction Secondary
    Cryogenic Separation Allows for the complete collection of light component products.
  • Gas Pressure Swing Adsorption and Desorption Reactor (Touchscreen)
  • Equipped with an advanced touchscreen interface, this device is designed to evaluate the adsorption and desorption behavior of gases under different pressure conditions. It simulates the performance of adsorbents in varying pressure environments for comprehensive adsorbent performance evaluation. The device also features high-precision data acquisition and real-time monitoring capabilities, providing researchers with a convenient and accurate experimental platform.
  • Three-Channel Catalyst Evaluation Reactor
  • The key design feature of the three-channel parallel evaluation device is that the three reaction tubes are heated within the same reaction furnace under high-pressure conditions, ensuring uniform catalyst temperature across all three tubes. This process is particularly suited for reactions that require strict temperature control and repetitive testing, greatly improving experimental efficiency.
  • Three-Channel Catalyst Evaluation Reactor
  • The key design feature of the three-channel parallel evaluation device is that the three reaction tubes are heated within the same reaction furnace under high-pressure conditions, ensuring uniform catalyst temperature across all three tubes. This process is particularly suited for reactions that require strict temperature control and repetitive testing, greatly improving experimental efficiency.
  • Syngas to Methanol Reactor
  • The reactor is used to convert syngas (a mixture of carbon monoxide and hydrogen) into methanol through a chemical reaction. The syngas-to-methanol process is an important chemical engineering technology, as methanol can be used as a solvent, fuel, or an intermediate for other chemicals. During the setup process, it is important to control reaction conditions such as temperature and pressure to improve yield and selectivity. A more efficient reactor design ensures the continuity and stability of the reaction.
  • 2000ml Trickle - bed Reactor
  • The purpose of choosing a trickle - bed reactor for a liquid - phase catalytic catalyst evaluation device is to closely approximate the actual application scenarios.
  • In a trickle - bed reactor, by controlling the droplet falling rate and uniformity, the efficient distribution of the catalyst can be achieved, thereby maximizing the reaction efficiency to the greatest extent. Its design advantage lies in its adaptability to catalysts with a high specific surface area, including particles or nanoparticles, to give full play to their active sites. This type of reactor enables fine control of individual droplets, covering parameters such as the falling rate, size, and interval, providing researchers with greater freedom in experimental design.
  • Moreover, the trickle - bed reactor is conducive to in - depth study of the kinetic behavior of liquid - phase catalytic reactions, including aspects such as adsorption, desorption, and reaction rates. Through the trickle - bed reactor, researchers can gain a deep understanding of the mechanism of liquid - phase catalytic reactions, providing strong support for the design and application of catalysts.
  • Catalyst Loading 800ml
    Air Gas Flow Rate 0 ~ 5 NL/min ±1% FS
    N2 Gas Flow Rate 0 ~ 5 NL/min ±1% FS
    Liquid Feed Rate 0 ~ 50 ml/min ±1% FS
    Reaction Pressure 1 ~ 2 MPa ±1% FS
    Reaction Temperature 80 ~ 100°C ±1°C
  • Methane Combustion Reactor
  • The methane combustion reaction apparatus is designed to simulate and study the combustion process of methane in the presence of oxygen. The system includes methane and oxygen supply systems, reaction systems, online detection systems, and control systems.
  • Design Parameters
  • Catalyst bed height 10 ~ 20 mm
    Operating pressure Atmospheric pressure
    Design pressure 0.1 MPa
    Operating temperature 1000°C Accuracy: ±0.1°C
    Design temperature 1000°C Accuracy: ±0.1°C
    Sampling temperature 100 ~ 200°C
    Reactor Independent temperature control
    Mixing type Static mixer SV Type
    Reactor Tubular Quartz material
    Condensate Tank Circulating Refrigeration Jacket cooling
    MS Sampling Methods Full Component Sampling Continuous control
    GC Sampling Methods Gas Phase Sampling Continuous control
    Equipment Framework Aluminum Alloy Vertical with pulley
    Control Method PLC+LabVIEW Security Protection
  • Methane Combustion Reactor
  • The methane combustion reaction apparatus is designed to simulate and study the combustion process of methane in the presence of oxygen. The system includes methane and oxygen supply systems, reaction systems, online detection systems, and control systems.
  • Design Parameters
  • Catalyst bed height 10 ~ 20 mm
    Operating pressure Atmospheric pressure
    Design pressure 0.1 MPa
    Operating temperature 1000°C Accuracy: ±0.1°C
    Design temperature 1000°C Accuracy: ±0.1°C
    Sampling temperature 100 ~ 200°C
    Reactor Independent temperature control
    Mixing type Static mixer SV Type
    Reactor Tubular Quartz material
    Condensate Tank Circulating Refrigeration Jacket cooling
    MS Sampling Methods Full Component Sampling Continuous control
    GC Sampling Methods Gas Phase Sampling Continuous control
    Equipment Framework Aluminum Alloy Vertical with pulley
    Control Method PLC+LabVIEW Security Protection

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