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Method for preparing m-pentadiene petroleum resin

A technology of petroleum resin and piperylene, which is applied in the field of preparation of piperylene petroleum resin, can solve the problems of complex post-treatment process and waste water generation, and achieve the effect of high selectivity, broad application prospect and simplified catalysis

Inactive Publication Date: 2012-02-15
CHANGCHUN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] According to public patents at home and abroad and relevant information reports, now, with the traditional AlCl 3 The process of synthesizing and polymerizing piperylene petroleum resin with a catalytic system is prone to emulsification when the catalyst is removed, and a large amount of waste water is generated, and the post-treatment process is more complicated (references: [1] Yu Tao, Ding Wei, Zhang Rongming. Preparation of light-colored C by complex catalyst 5 Petroleum Resin [J]. Progress in Chemical Industry, 2003, 22(5): 503~505. [2] Xiamei Hu. Application of Composite Catalytic System in the Synthesis of Piperylene Resin [J]. Jinshan Oil Chemical Fiber, 2002(2 ): 11~14. [3] WOJCIK R T.Cationic polymerization of piperylene using as the catalyst system an aluminum halide and an inorganic phosphoric acid: US, 4 098 982 [P]. 1978-07-04. [4] Zhang Chuntao , Xu Bokun. A production process of high-grade piperylene petroleum resin: CN, 101 134 797 [P]. 2008-03-05.)

Method used

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  • Method for preparing m-pentadiene petroleum resin
  • Method for preparing m-pentadiene petroleum resin
  • Method for preparing m-pentadiene petroleum resin

Examples

Experimental program
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Effect test

Embodiment 1

[0022] The invention provides a kind of preparation method of piperylene petroleum resin, and its steps and conditions are as follows:

[0023] (1) The present invention has used a kind of composite catalyst system for synthetic piperylene petroleum resin, and it is the SiO of pretreatment 2 As a carrier, AlCl 3 loading onto pretreated SiO 2 On the support, get AlCl 3 / SiO 2 Supported main catalyst, pretreated SiO 2 :AlCl 3 The mass ratio of the catalyst and AlCl is 2:1; 3 / SiO 2 The mass ratio of the supported main catalyst is 1.25:100, and the cocatalyst is the liquid acid CH 4 o 3 S or H 3 PO 4 ; Pretreated SiO 2 is at 200°C, the SiO 2 Roast for 24h, or put SiO 2 After soaking in hydrochloric acid solution for 8 hours, dry it in vacuum at 80°C for 72 hours, and then use 30% H 2 o 2 After treatment for 8 h, vacuum drying at 80 °C for 72 h, the obtained pretreated SiO 2 ; Pretreated SiO 2 The specific surface area is 319m 2 / g, the pore volume is 0.9mL / g.

...

Embodiment 2

[0030] The conditions prepared in Example 2 are shown in Table 1, and the rest are the same as in Example 1. The obtained piperylene petroleum resin had a softening point of 95.3°C, a Gardner color of 2, and a resin yield of 76.5%.

Embodiment 3

[0031] The conditions for the preparation of Example 3 are shown in Table 1, and the rest are the same as in Example 1. The obtained piperylene petroleum resin had a softening point of 98.3° C., a Gardner color of 4, and a resin yield of 81.7%.

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Abstract

The invention provides a method for preparing an m-pentadiene petroleum resin. Pre-treated SiO2 is taken as a carrier, and AlCl3 is loaded to the SiO2 carrier to form an AlCl3 / SiO2 supported main catalyst; and liquid acid CH4O3 or H3PO4 is taken as a cocatalyst, and high reactivity and high selectivity of a target product are showed in the reaction. In the method, the process of the removal of a catalyst is simplified; meanwhile, the catalyst can be recycled after being filtered and separated, the environmental pollution is reduced, the method has the advantages of environment friendliness and the like, and the continuous production can be realized. The production cost is reduced; the problems that a large amount of wastewater is generated when the catalyst is removed, the post-treatment process is more complicated and the quality of products is low in the conventional process are solved; and the softening point of the obtained m-pentadiene petroleum resin is 95.3 to 103.5 DEG C, the Gardner chroma is 2 to 5, and the yield of the resin is 76.5 to 83.8 percent.

Description

technical field [0001] The invention relates to a preparation method of piperylene petroleum resin. Background technique [0002] C 5 Distillate is a by-product with a large output in the ethylene industry, accounting for 8% to 16% of ethylene output. In 2010, the total amount of cracking in China was nearly 1.5 million tons, and by 2015 it is expected to exceed 2 million tons. [0003] cleavage C 5 After separation, piperylene with a mass fraction of about 65% can be obtained. The main use of piperylene is to make high-grade aliphatic petroleum resin. This kind of resin generally has an average relative molecular mass between 1000 and 3000, and usually has the characteristics of light color, low density and high saturation. It is different from alicyclic C 5 Petroleum resin and C 5 and C 9 fractions of copolymer resins compared to other aliphatic C 5 Petroleum resin has better tackiness, thermal stability and lighter color, and is widely used in adhesives, hot-melt r...

Claims

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Application Information

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IPC IPC(8): C08F240/00C08F4/18C08F4/14C08F4/02
CPCY02P20/584
Inventor 张龙高超胡江磊
Owner CHANGCHUN UNIV OF TECH
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