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Coking crude benzol hydrogen desulfurization process

A technology for hydrodesulfurization and coking of crude benzene is applied in the field of hydrodesulfurization of coking crude benzene, and can solve problems such as restrictions on the use of aromatic hydrocarbon products

Inactive Publication Date: 2017-01-11
锡山区绿春塑料制品厂
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the sulfur content of pure benzene obtained by the above-mentioned process is about 0.5ppm, which greatly restricts the use of aromatic products.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] The catalyst was prepared by impregnation method, and the carrier was doped Cu 2+ SAPO-5, Cu 2+ The doping amount in SAPO-5 is controlled at 0.65% of the carrier mass. The active component molybdenum nitride MO 2 N, tungsten nitride W 2 N, molybdenum carbide Mo 2 The total content of C and tungsten carbide WC is 10% of the mass of the carrier, and their molar ratio is 1:0.4:0.3:0.8.

[0042] The catalyst is loaded into a fixed bed reactor, the reaction tube of the reactor is made of stainless steel with an inner diameter of 50 mm, the catalyst bed temperature is measured with a UGU808 temperature control meter, and the raw material light oil is manufactured by Beijing Satellite Manufacturing Plant The double-plunger micropump continuously transports the hydrogen gas from a high-pressure cylinder and controls the flow rate with a Beijing Qixing Huachuang D07-11A / ZM gas mass flow meter. The catalyst loading is 2kg.

[0043] The mixture of coked crude benzene and hydr...

Embodiment 2

[0046] The catalyst was prepared by impregnation method, and the carrier was doped Cu 2+ SAPO-5, Cu 2+ The doping amount in SAPO-5 is controlled at 0.7% of the carrier mass. The active component molybdenum nitride MO 2 N, tungsten nitride W 2 N, molybdenum carbide Mo 2 The total content of C and tungsten carbide WC is 10% of the mass of the carrier, and the molar ratio is 1:0.6:0.45):1.2.

[0047] All the other conditions are the same as in Example 1.

[0048] The final product was tested and its total sulfur content was reduced to 0.06 ppm.

Embodiment 3

[0073] The catalyst contains catalyst promoter TiO 2 , CeO 2 , V 2 o 5 and NbOPO 4 , its content is respectively 1%, 1.5%, 1% and 3%, all the other are identical with embodiment 1.

[0074] The final product was tested, and after 3 months of use, the pressure drop of the catalyst bed did not change, which was 16% lower than the pressure drop of the catalyst bed in Example 1 for the same use time.

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PUM

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Abstract

The invention discloses a coking crude benzol hydrogen desulfurization process, wherein a mixture of coking crude benzol and hydrogen enters a pre-reactor from a tower top, the pre-reactor is filled with a NiMo catalyst, the reaction temperature is 220-230 DEG C, the hydrogenation pressure is 3.2-3.8MPa, pre-reacted products enter a fixed bed reactor, the fixed bed reactor is filled with a hydrogen desulfurization catalyst, and the catalyst comprises a carrier and an active component; the carrier is SAPO-5, and a heteroatom Cu2<+> is doped into a synthesis framework structure of the SAPO-5; the active component is a mixture of Mo2N, W2N, Mo2C and WC; the catalyst further comprises a catalytic additive, and the catalytic additive is a mixture of TiO2, CeO2, V2O5 and NbOPO4. The reaction conditions of the fixed bed reactor are as follows: the reaction temperature is 320-380 DEG C, the hydrogenation pressure is 3.0-3.6MPa, the hydrogen to oil volume ratio is 500-800, and the volume space velocity is 1.5-2h<1>. A product subjected to a fixed bed hydrogenation reaction enters an extractive distillation unit, and arene is obtained. The process reduces the total sulphur content of the coking crude benzol to be lower than 0.1ppm, and meets extensive applications.

Description

technical field [0001] The invention relates to a hydrodesulfurization process, in particular to a hydrodesulfurization process of coking crude benzene. Background technique [0002] Coking is one of the main methods of coal processing. It is also called high-temperature dry distillation of coal, that is, bituminous coal suitable for coking is properly treated and heated to 950-1050°C in a coke oven with air isolation. After drying, pyrolysis, The stages of burning, bonding, solidification and shrinkage finally make coke. Volatile substances precipitated during the coking process include chemical products such as gas, tar, ammonia and crude benzene. In addition, the coal tar obtained in the coking process also contains a certain amount of aromatics such as benzene. [0003] The refining of coking crude benzene uses coking crude benzene as raw material, and removes harmful substances such as sulfur and nitrogen in it through physical or chemical methods, so as to obtain hig...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G45/12C10G65/04B01J29/85
CPCC10G45/12C10G65/04B01J29/85B01J2229/186B01J2229/183B01J21/063B01J23/22B01J23/10B01J27/195C10G2300/1096C10G2300/202B01J35/19
Inventor 朱忠良
Owner 锡山区绿春塑料制品厂
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