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Reactor

[fǎn yìng qì]
Equipment to realize reaction process
Reactor is a kind of equipment to realize reaction process, which is widely used in chemical industry oil refining metallurgy And other fields. The reactor is used to realize liquid-phase single-phase reaction process and liquid-liquid, gas-liquid, liquid-solid, gas-liquid solid, etc Heterogeneous reaction process
The application of reactors began in ancient times kiln It is an original reactor. There are various types of reactors in modern industry, such as blast furnace and converter in metallurgical industry; In bioengineering Fermentation tank And various burner , are all different types of reactors.
Chinese name
Reactor
Foreign name
reactor
Definition
Equipment to realize reaction process
Widely used in
Chemical industry oil refining metallurgy
Type
Pipe type, tower type, etc
Operation mode
Indirect continuity

brief introduction

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Reactor is a kind of equipment to realize reaction process, which is used to realize liquid-phase single-phase reaction process and liquid-liquid, gas-liquid, liquid-solid, gas-liquid solid, etc Heterogeneous reaction process Stirring is often set in the device( Mechanical mixing Air agitation Etc.). When the height diameter ratio is large, multi-layer mixing blades can be used. When the materials need to be heated or cooled during the reaction, the jacket can be set at the reactor wall, or the heat exchange surface can be set in the reactor External circulation Conduct heat exchange.

type

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The types of common reactors (see the table) are: ① Tubular reactor Empty pipes with large length diameter ratio or Filling tube Composition, which can be used to realize Gas phase reaction and Liquid phase reaction 。② Kettle reactor It is composed of cylindrical containers with small length diameter ratio, often equipped with Mechanical mixing or Air agitation Device for liquid phase Single-phase reaction process Equal to liquid-liquid phase, gas-liquid phase and gas-liquid solid phase Heterogeneous reaction process For gas-liquid phase reaction process Bubbling Stirring kettle (see Bubble reactor ); be used for Gas-liquid solid reaction process Is called stirred tank type Slurry reactor 。③ Reactor with solid particle bed. Gas or (and) liquid pass through fixed or moving solid particle bed to realize multiphase reaction process, including Fixed bed reactor Fluidized bed reactor Moving bed reactor trickle-bed reactor Etc. ④ Tower reactor Used to realize gas-liquid phase or Liquid-liquid reaction process Tower equipment, including Packed tower Plate tower Bubble column Etc. (see color picture). ⑤ Jet reactor. utilize ejector conduct blend , implement Gas phase Or equipment for liquid-phase single-phase reaction process and gas-liquid and liquid-liquid multiphase reaction process. ⑥ Other various atypical reactors. as Rotary kiln Aeration tank Etc.

Operation mode

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Reactors can be divided into:
① Intermittent Kettle reactor , or intermittent kettle.
Flexible operation, easy to adapt to different operating conditions and product varieties, suitable for small batch, multi variety, long reaction time product production. The disadvantage of batch kettle is that it needs auxiliary operations such as loading and unloading, and the product quality is not easy to be stable. But some reaction processes, such as some fermentation reactions and polymerization , implement continuous production There are still difficulties, and the intermittent kettle is still used up to now.
Intermittent operation The reactor system adds raw materials to the reactor at a certain ratio, and discharges the materials at a time after the reaction meets certain requirements. Continuous operation The reactor system continuously adds raw materials and continuously discharges reaction products. When the operation reaches Stationary state The composition, temperature and other state parameters of materials at any position in the reactor do not change with time. Semi continuous operation The reactor is also called semi batch operation reactor, which is between the above two. Usually, one reactant is added at one time, and then another reactant is added continuously. After the reaction meets certain requirements, stop the operation and unload the materials.
The advantage of batch reactor is that the equipment is simple, and the same equipment can be used to produce a variety of products, especially suitable for small batch and multi variety production in pharmaceutical, dye and other industrial sectors. In addition, Batch reactor No item exists in Backmixing , favorable for most reactions. The disadvantage is that auxiliary processes such as loading and unloading, cleaning, etc. are required, and the product quality is not easy to be stable.
② Continuous Kettle reactor , or continuous kettle
Kettle reactor
)。 The disadvantages of intermittent kettle can be avoided, but the stirring will cause the back mixing of fluid in the kettle. When stirring violently, liquid viscosity is low or Average residence time For longer occasions, materials in the kettle flow pattern Can be regarded as All mixed Stream, reaction kettle Accordingly, it is called full mixing kettle. On request Conversion rate In case of high or series side reaction Backmixing Phenomenon is an adverse factor. This can be used Multi reactor in series To reduce the adverse effect of back mixing, and the reaction conditions can be controlled in separate kettles.
Mass production should adopt Continuous reactor The advantages of continuous reactor are stable product quality and easy operation control. Its disadvantage is that there are different levels of back mixing in continuous reactors, which is an adverse factor for most reactions, and should be suppressed through rational reactor selection and structural design.
③ Semicontinuous Kettle reactor
It refers to the reactor in which one kind of raw material is added at one time and another kind of raw material is added continuously. Its characteristics are between the intermittent kettle and the continuous kettle.

Feeding mode

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For those with more than two kinds of raw materials Continuous reactor The material flow direction can be concurrent or counter current. For equipment composed of several reactors in cascade Crossflow Feeding, that is, one raw material passes through each reactor in turn, and the other raw material is added to each reactor separately. In addition to the flow outside, there are also raw materials added from one end (or both ends) of the reactor and added in sections. Staged feeding means that one raw material is added from one end, and the other raw material is added from different positions of the reactor in several sections. Cross flow can also be regarded as a staged feeding mode. The feeding method shall be determined according to the characteristics of the reaction process.

Heat exchange mode

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Most reactions have obvious thermal effects. In order to carry out the reaction under appropriate temperature conditions, it is often necessary to carry out heat transfer There are indirect heat exchange and direct heat exchange. Indirect heat transfer refers to reaction material and Heat carrier Direct heat transfer refers to the direct contact between reaction material and heat carrier for heat transfer. yes Exothermic reaction , which can be carried by reaction products reaction heat To heat the raw materials to reach the required reaction temperature, this reactor is called self heating reactor.
According to the heat exchange conditions in the reaction process, reactors can be divided into:
① Isothermal reactor: the reaction system temperature is equal everywhere Ideal reactor The reaction heat effect is very small, or the heat exchange between the reaction material and the heat carrier is sufficient, or the heat feedback in the reactor is very large (such as violently stirred Kettle reactor )This can be approximately regarded as an isothermal reactor.
②  heat insulation An ideal reactor with no heat exchange between the reaction zone of the reactor and the environment. The large industrial reactor without heat exchange device in the reaction zone can be approximately regarded as an adiabatic reactor when the heat exchange with the outside is negligible.
③ The non isothermal and non adiabatic reactor has heat exchange with the outside world, and there is also heat feedback in the reactor, but it can not reach the isothermal conditions, such as tubular reactor Fixed bed reactor
Heat exchange can be carried out in the reaction area, such as the stirred tank with jacket for heat exchange, or in the reaction area, such as the multi-stage reactor with interstage heat exchange. [1]

Operating conditions

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It mainly refers to the operating temperature and pressure of the reactor. Temperature is a sensitive factor affecting the reaction process, so it is necessary to select an appropriate operating temperature or temperature sequence so that the reaction process can be carried out under optimal conditions. For example, for reversible Exothermic reaction The temperature sequence from high to low shall be adopted to give consideration to reaction rate and Equilibrium conversion rate (See chemical equilibrium )。
The reactor can be operated under normal pressure, pressure or negative pressure (vacuum). The pressurized reactor is mainly used for the reaction process with gas participation. Increasing the operating pressure is conducive to acceleration Gas phase reaction , for total Number of moles Reduced gas phase Reversible reaction , it can improve the balance conversion rate, such as synthetic ammonia Synthetic methanol Etc. Increasing the operating pressure can also increase the solubility of gas in liquid, so many gas-liquidreaction process Gas-liquid solid reaction process Pressure operation is adopted to improve the reaction rate, such as Paraxylene Oxidation, etc.

model selection

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For a specific reaction process, the selection of reactor should comprehensively consider technical, economic and safety factors.
The basic characteristics of the reaction process determine the appropriate reactor form. for example gas-solid reaction process Basically Fixed bed reactor Fluidized bed reactor or Moving bed reactor However, the thermal effect of the reaction and the reaction Conversion rate and Selection rate Requirements, physical and chemical properties and deactivation of catalyst, and even different reactors conceptual design And can be determined only after technical and economic analysis.
In addition to the form of reactor, Reaction pot The operation mode and feeding mode of shall also be considered. For example, for processes with series or parallel side reactions, staged feeding may be better than single feeding. Temperature sequence is also an important factor for reactor selection. For example, for exothermic Reversible reaction The temperature sequence from high to low shall be adopted Heat exchange reactor The temperature sequence of the reactor can be rationalized. Reactor at Process industry It plays an important role in production. As far as the construction investment and operation cost of the whole process are concerned, the proportion of reactors may not be very large. However, its performance and operation have an important impact on the pre-treatment, output and quality of products, raw material consumption, energy consumption and product cost. Therefore, the research and development of reactors is of great significance for the development of various process industries.