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Method for continuous production of hanging type tetrahydrochysene dicyclopentadiene

A technology of hanging tetrahydrodicyclopentadiene and palladium dichloride, applied in the field of preparation of hanging tetrahydrodicyclopentadiene, achieving the effects of increased yield, simple preparation process and low equipment requirements

Active Publication Date: 2010-07-07
XIAN MODERN CHEM RES INST +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The technical problem to be solved by the present invention is to overcome the shortcoming of the above-mentioned method for preparing hanging-type tetrahydrodicyclopentadiene, and provide a kind of dicyclopentadiene with high conversion rate, high selectivity of hanging-type tetrahydrodicyclopentadiene, simple operation, A method for continuous production of hanging tetrahydrodicyclopentadiene with low environmental pollution, low energy consumption, long service life of catalyst, low product cost and high yield

Method used

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  • Method for continuous production of hanging type tetrahydrochysene dicyclopentadiene
  • Method for continuous production of hanging type tetrahydrochysene dicyclopentadiene
  • Method for continuous production of hanging type tetrahydrochysene dicyclopentadiene

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Effect test

Embodiment 1

[0033] Take the used raw material dicyclopentadiene 13.2g (0.1 mole) of preparing hanging tetrahydrodicyclopentadiene as example, other raw materials used and preparation method are as follows:

[0034] 1. Preparation of metal salt solution

[0035] Palladium dichloride is formulated into the palladium dichloride aqueous solution that weight concentration is 10% by conventional method, and chloroplatinic acid is formulated into the chloroplatinic acid aqueous solution that weight concentration is 10%, and nickel nitrate is formulated into the nickel nitrate that weight concentration is 30%. aqueous solution.

[0036] 2. Preparation of supported catalyst

[0037] Each 3 g of Hβ molecular sieve and silicon dioxide with a silicon-aluminum ratio of 20 are packed into different flasks, and 1.11 g of chloroplatinic acid aqueous solution with a weight concentration of 10% is added per gram of support in each flask, and the addition amount of each gram of support is as follows: The ...

Embodiment 2

[0049] Take the used raw material dicyclopentadiene 13.2g (0.1 mole) of preparing hanging tetrahydrodicyclopentadiene as example, other raw materials used and preparation method are as follows:

[0050] In step 2 of the process for preparing the supported catalyst, 3 g of Hβ molecular sieve and silicon dioxide with a silicon-aluminum ratio of 80 are loaded into different flasks, and chloroplatinic acid with a weight concentration of 10% is added per gram of molecular sieve in each flask Aqueous solution 0.21g, stir 4 hours, use rotary evaporator, temperature is 75 ℃, vacuum degree is 0.09MPa rotary evaporation, takes out and puts into crucible, puts crucible into muffle furnace, roasts in 600 ℃ air atmosphere for 3 hours, naturally After cooling, it is taken out, pressed into tablets, granulated, and passed through a 40-60 mesh sieve to prepare a molecular sieve supported catalyst loaded with 1% platinum and a supported catalyst loaded with 1% platinum loaded on silicon dioxide...

Embodiment 3

[0055] Take the used raw material dicyclopentadiene 13.2g (0.1 mole) of preparing hanging tetrahydrodicyclopentadiene as example, other raw materials used and preparation method are as follows:

[0056] In step 2 of the process for preparing the supported catalyst, 3 g of Hβ molecular sieve and silicon dioxide with a silicon-aluminum ratio of 50 are loaded into different flasks, and 10% chloroplatinic acid with a weight concentration of 10% is added to each flask by per gram of carrier Aqueous solution 0.65g, stir 4 hours, use rotary evaporator, temperature is 75 ℃, vacuum degree is 0.09MPa rotary evaporation, takes out and puts into crucible, puts crucible into muffle furnace, roasts 5 hours in 400 ℃ of air atmosphere, naturally After cooling, it is taken out, pressed into tablets, granulated, and passed through a 40-60 mesh sieve to prepare a molecular sieve supported catalyst supporting 3% platinum and a supported catalyst supporting 3% platinum on silicon dioxide. The weig...

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Abstract

The invention relates to a method for continuously producing hanging-typed tetrahydro-dicyclopentadiene which comprises the steps: metal salt solution preparation, supported catalyst preparation, catalyst activation, catalytic reaction and separation and purification. Compared with the method for preparing the hanging-typed tetrahydro-dicyclopentadiene, the method for continuously producing the hanging-typed tetrahydro-dicyclopentadiene adds two different types of catalyst respectively into two fixed bed reactors of catalyst test apparatus, and prepares the hanging-typed tetrahydro-dicyclopentadiene by the catalytic reaction of dicyclopentadiene and hydrogen in one step. The used catalyst with simple preparation technique has no corrosive property and low requirement to equipment; the temperature of catalytic reaction can be adjusted; the yield rate is improved, and the production cost of products is reduced. The method for continuously producing the hanging-typed tetrahydro-dicyclopentadiene has the advantages of simple operation, good repeatability, small environment pollution and low energy consumption, etc. The identification result of the prepared hanging-typed tetrahydro-dicyclopentadiene after substance identification by a GC-MS and a superconducting Fourier digital nuclear magnetic resonance instrument is consistent with a standard diagram.

Description

technical field [0001] The invention belongs to the technical field of liquid fuels, and in particular relates to a preparation method of hanging tetrahydrodicyclopentadiene. Background technique [0002] High density hydrocarbon fuel refers to the density greater than 0.8g / cm 3 Its form can be liquid or solid, and its composition can be a pure component or a mixture of various hydrocarbons. According to the source and density of the fuel, it can be divided into high-density kerosene and synthetic polycyclic hydrocarbon fuels. , high-tension cage fuel and colloidal fuel with nanoscale additives, the densities range from 0.8 to 0.9 g / cm 3 , 0.9~1.0g / cm 3 and greater than 1.0g / cm 3 . The molecular formula of hanging tetrahydrodicyclopentadiene is C 10 h 16 , the molecular weight is 132.2, and the chemical structural formula is: [0003] [0004] Hanging tetrahydrodicyclopentadiene is a fuel with high density, high stability, and high heat of combustion. It is an idea...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C13/61C07C5/13B01J29/10B01J29/72B01J23/89
Inventor 刘昭铁吕剑王伟杜咏梅刘忠文郝青青李春迎杨建明张呈平亢建平
Owner XIAN MODERN CHEM RES INST