Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Esterification catalyst, esterification catalysis system and method for preparation of esterification catalyst and esterification catalyst reaction

An esterification catalytic system and esterification catalyst technology are applied in the directions of physical/chemical process catalysts, catalyst carriers, chemical instruments and methods, etc., which can solve the problems of high price, pollute the environment, and the owners cannot afford it, and reduce production costs. , the effect of solving environmental pollution

Pending Publication Date: 2018-03-27
广西锟德能源科技有限公司
View PDF6 Cites 2 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] For the esterification of acidic animal and vegetable oils, most of the traditional processes use homogeneous liquid catalysts, and most of them use concentrated sulfuric acid as the esterification catalyst. However, concentrated sulfuric acid has three disadvantages as the esterification catalyst: first, the product needs to be washed with water, resulting in a large amount of Wastewater pollutes the environment; second, the catalyst cannot be separated from the product, and the sulfur content of the product far exceeds the standard; third, it corrodes equipment
However, the use of heterogeneous solid acid catalysts is expensive, and the cost is very high when used in the manufacture of biodiesel, and the owner cannot afford it.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Esterification catalyst, esterification catalysis system and method for preparation of esterification catalyst and esterification catalyst reaction

Examples

Experimental program
Comparison scheme
Effect test

Embodiment

[0015] The present invention adopts the following technical solutions: an esterification catalyst, including silica gel and iron, zirconium, titanium, tin, scandium, and sulfuric acid adsorbed on the silica gel; the iron, zirconium, titanium, tin, scandium, and sulfuric acid account for the mass of the silica gel The percentages are: iron 9%-30%, zirconium 0.009%-0.015%, titanium 9%-30%, tin 0.3%-3%, scandium 0.003%-0.009%, sulfuric acid 59%. The silica gel is C-type macroporous silica gel, with an average pore diameter of 8.0-10.0 nm and a specific surface area of ​​300-400 square meters per gram.

[0016] Such as figure 1 As shown, the esterification catalytic system for preparing esterification catalyst includes raw liquid pool 1, chemical filter tank 2, adsorption zone 3, drying and dehydration zone 4, roasting furnace 5, esterification reaction tank 6, deacidification oil tank 7, silica gel 8; The raw liquid pool 1, chemical filter 2, adsorption area 3, drying and dehydr...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention provides an esterification catalyst, an esterification catalysis system and a method for preparation of the esterification catalyst and esterification catalyst reaction. The esterification catalyst is prepared from silica gel, and iron, zirconium, titanium, tin, scandium and sulfuric acid which are adsorbed on the silica gel; the mass percent of the iron, the zirconium, the titanium,the tin, the scandium and the sulfuric acid in the silica gel is respectively as follows: 9-30% of the iron, 0.009-0.015% of the zirconium, 9-30% of the titanium, 0.3-3% of the tin, 0.003-0.009% of the scandium and 59% of the sulfuric acid. The esterification catalysis system comprises a stock solution pool, a chemical filter pool, an adsorption area, a drying dehydration area, a roasting furnace, an esterification reaction pool, a deacidification oil tank and C-shaped macropore silica gel; the stock solution pool, the chemical filter pool, the adsorption area, the drying dehydration area, the roasting furnace, the esterification reaction pool and the deacidification oil tank are successively connected, and the C-shaped macropore silica gel is connected with the adsorption area. Accordingto the esterification catalyst, the esterification catalysis system and the method for the preparation of the esterification catalyst and the esterification catalyst reaction, the production cost ofbiodiesel is reduced, the sulfur content and acid value of a product achieve the purpose of meeting GB (V) diesel oil standard, the defect that traditional process causes environmental pollution easily is solved, and the esterification catalyst, the esterification catalysis system and the method for the preparation of the esterification catalyst and the esterification catalyst reaction make contributions to production of biodiesel, energy conservation, emission reduction and environmental protection.

Description

technical field [0001] The invention relates to an esterification catalyst, an esterification catalytic system and a method for preparing the esterification catalyst and performing esterification catalytic reaction. Background technique [0002] For the esterification of acidic animal and vegetable oils, most of the traditional processes use homogeneous liquid catalysts, and most of them use concentrated sulfuric acid as the esterification catalyst. However, concentrated sulfuric acid has three disadvantages as the esterification catalyst: first, the product needs to be washed with water, resulting in a large amount of Wastewater pollutes the environment; second, the catalyst cannot be separated from the product, and the sulfur content of the product far exceeds the standard; third, it corrodes the equipment. However, the use of heterogeneous solid acid catalysts is expensive, and the cost is very high when used in the manufacture of biodiesel, which is beyond the affordabil...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
IPC IPC(8): B01J27/053B01J21/08B01J32/00B01J35/10C11C3/04
CPCC11C3/04B01J21/08B01J27/053B01J35/615B01J35/647Y02E50/10
Inventor 欧卓木欧鹏卓寿镛陈军黄俭
Owner 广西锟德能源科技有限公司
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products