System and method for preparing durene by utilization of toluene and methanol

A technology for the preparation of durene and methanol, which is applied in chemical instruments and methods, condensation between hydrocarbons and non-hydrocarbons, purification/separation of hydrocarbons, etc., which can solve the problem of limited raw material sources, high raw material costs, and low yields and other problems to achieve the effect of solving the low purity and improving the purity

Pending Publication Date: 2017-07-07
潍坊弘润新材料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The process of crystallization and separation of carbon ten components is complicated, the yield of durene is low, and the source of raw materials for heavy aromatics rich in durene is limited, which cannot meet the market demand of downstream homoanhydride or polyimide; The process of producing durene also has the defects of limited source of raw materials, catalyst deactivation, and insufficient stability; the method of methylation of methylbenzene with methanol and the method of chloromethylation of methylbenzene have high raw material costs, limited sources, and the use of Catalyst activity, selectivity and stability are unsatisfactory, corrosion is serious, and the environment is polluted; the reaction conditions of the gas-phase isomerization and disproportionation of p-trimethylbenzene are harsh, and industrialization has not yet been realized; the research on the alkylation reaction of benzene / toluene with methanol as raw material is in the domestic market. It mainly produces p-xylene, and there are few related studies on the production of durene; the method of producing durene from methanol or synthesis gas has many by-products, the degree of alkylation is difficult to control, and the catalyst is easily deactivated.
[0004] Although the relevant technology has disclosed the use of methanol and toluene as raw materials to prepare trimethylbenzene and tetramethylbenzene, in this method, it has shown that durene has good selectivity, but the yield of durene is between Below 10%, the yield of durene is low, the utilization rate of raw materials is low, the preparation cost of durene is high, and it is difficult to realize industrial production
[0005] Therefore, the raw materials for the preparation of durene mainly come from naphtha cracking or catalytic reforming of aromatics. With the increasing shortage of petroleum resources, the raw materials for the preparation of durene are subject to more and more restrictions.
[0006] To sum up, there is still a lack of effective solutions for problems such as limited sources of raw materials, high cost of raw materials, low yield of durene, and low purity of durene in the prior art.

Method used

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  • System and method for preparing durene by utilization of toluene and methanol

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] Toluene and methanol reach 350°C after being preheated by preheater 1, and then the preheated toluene and methanol are transported into alkylation reactor 2 for reaction. The mass flow rate of raw material gas toluene and methanol is 4234kg / h, and the reaction temperature is 390°C, reaction pressure 5.0MPa, mass space velocity 3h -1 , the reaction catalyst is HZSM-5 molecular sieve catalyst, and the reaction residence time is 3s; the reaction liquid is separated from oil and water to remove water and dry gas, and the separated waste liquid is sent to the waste water treatment station for treatment, and the separated dry gas is passed into the heating furnace for combustion, which is The heat is provided by the alkylation reactor, and the separated oil phase enters the first rectification tower 4, the temperature at the top of the tower is 100°C, rectification under normal pressure, the top components are recovered to the preheater 1, after heating Enter the alkylation r...

Embodiment 2

[0042] Toluene and methanol reach 330°C after being preheated by preheater 1, and then the preheated toluene and methanol are transported into alkylation reactor 2 for reaction. The mass flow rate of raw material gas toluene and methanol is 7465kg / h, and the reaction temperature is 360°C, reaction pressure 4.0MPa, mass space velocity 4h -1 , the reaction catalyst is HZSM-5 molecular sieve catalyst, and the reaction residence time is 4s; the reaction liquid is separated from oil and water to remove water and dry gas, and the separated waste liquid is sent to the waste water treatment station for treatment, and the separated dry gas is passed into the heating furnace for combustion. The heat is provided by the alkylation reactor, and the separated oil phase enters the first rectification tower 4, the temperature at the top of the tower is 100°C, rectification under normal pressure, the top components are recovered to the preheater 1, after heating Enter the alkylation reactor 2 ...

Embodiment 3

[0044] Toluene and methanol are preheated by preheater 1 to reach 340°C, and then the preheated toluene and methanol are transported into alkylation reactor 2 for reaction, the mass flow rate of raw material gas toluene and methanol is 3578kg / h, and the reaction temperature is 380 ℃, the reaction pressure is 3.0MPa, and the mass space velocity is 2h -1 , the reaction catalyst is HZSM-5 molecular sieve catalyst, and the reaction time is 5s; the reaction liquid is separated from oil and water to remove water and dry gas, and the separated waste liquid is sent to the waste water treatment station for treatment, and the separated dry gas is passed into the heating furnace for combustion to produce alkane The basement reactor provides heat, and the separated oil phase enters the first rectification tower 4, the temperature at the top of the tower is 100°C, rectification under normal pressure, and the top components are recovered to the preheater 1, and then enter the The reaction i...

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Abstract

The invention discloses a system and a method for preparing durene by the utilization of toluene and methanol. The problems such as limited sources of raw materials, high cost of raw materials, low yield of durene, low purity of durene and the like existing in the durene preparation technologies in the prior art are solved. The prepared durene has high yield and high purity. The technical scheme comprises the following steps: preheating toluene and methanol and introducing the preheated toluene and methanol into an alkylation reactor, and reacting at the reaction temperature of 350-400 DEG C at the reaction pressure of 2.0-5.0 MPa at the mass space velocity of 1-5 h<-1> for the reaction retention time of 1-5 s by using an HZSM-5 molecular sieve catalyst as a reaction catalyst; removing moisture and dry gas by oil-water separation of the reaction liquid, removing toluene, mixed xylenes and mixed trimethylbenzenes by rectifying the oil phase, and cooling for crystallization so as to obtain pure durene.

Description

technical field [0001] The invention belongs to the field of petrochemical synthesis, and in particular relates to a system and method for preparing durene by using toluene and methanol. Background technique [0002] Durene, that is, 1,2,4,5-tetramethylbenzene, is an important fine chemical raw material, and is an important raw material for medicine, powder coating matting agent, dye, pesticide, and surfactant. The most important use is to produce pyromellitic dianhydride and further produce polyimide. Polyimide has the advantages of thermal oxidation stability and good insulation, and is widely used in aerospace, electrical insulation, atomic energy industry, satellite, nuclear submarine, microelectronics and other precision machinery. [0003] At present, the production process of durene mainly includes: C10 component crystallization separation method, trimylene isomerization method, trimylene chloromethylation method, trimylene gas phase isomerization disproportionation ...

Claims

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Application Information

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IPC IPC(8): C07C2/86C07C7/04C07C7/14C07C15/02
CPCC07C2/864C07C7/005C07C7/04C07C7/14C07C2529/40C07C15/02Y02P20/52
Inventor 马延春张范安良海赵汝臣朱文聪
Owner 潍坊弘润新材料有限公司
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