Preparation method of high-selectivity hydroisomerization catalyst

A hydroisomerization, high-selectivity technology, applied in catalyst activation/preparation, molecular sieve catalysts, chemical instruments and methods, etc. The effect of avoiding the accumulation of reaction heat, stable activity and low cost

Inactive Publication Date: 2018-06-08
洛阳金达石化有限责任公司
View PDF7 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] At present, most of the hydrogenation isomerization catalysts used in China are Pt and Pb noble metal catalysts, which have good hydrogenation reaction characteristics, but the hydrogenation reaction is accompanied by the occurrence of cracking side reactions, which reduces the yield of the target product, and the cracking reaction When it is severe, it will have a great impact on the properties of the product, making the controllability of the hydroisomerization reaction worse

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
  • Preparation method of high-selectivity hydroisomerization catalyst
  • Preparation method of high-selectivity hydroisomerization catalyst

Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0028] Step a, the preparation steps of catalyst carrier are as follows:

[0029] 1. Prepare SAPO-II molecular sieve and inorganic binder according to the mass ratio of 40-80%: 20-60% to make the main powder, and add 0.1-5% of the total weight of the powder into the mixer for dry mixing 10-60 minutes, take out the powder and pass through a 20-60 mesh screen to remove coarse particles;

[0030] 2. Put the sieved powder into the mud making machine, then add water of 60-150% of the weight of the powder, and knead for 20-90 minutes to make the powder into mud;

[0031]3. Put the mud material in step 2 into the mud refining machine, and knead the mud material into a dense mud section for subsequent molding;

[0032] 4. The mud section in step 3 is shaped into a cylindrical, three-lobe or four-lobe mud base by an extruder and a mold;

[0033] 5. The mud in step 4 is dried at room temperature to 200°C until the moisture content is lower than 15%;

[0034] 6. Then send the green bo...

Embodiment 1

[0038] A preparation method of highly selective hydroisomerization catalyst, which comprises the following steps:

[0039] Catalyst carrier: Put 1.0kg of silica sol, 1kg of SAPO-II molecular sieve, 0.2kg of hydroxypropyl cellulose and 0.3kg of squash gum into the conical mixer, take it out after 15 minutes of mixing and put it into the mud making machine Make the mud for 10 minutes, take it out, extrude it into a strip-shaped clover-shaped green body through an extruder with a clover mold, dry it in an oven at 70°C until the water content of the green body is 6.3%, and bake it in a muffle furnace at 570°C for 7 hours;

[0040] Impregnation: Put the catalyst carrier into the vacuum impregnation machine (there is no solution in the vacuum impregnation machine at this time), heat to 120°C, start the vacuum pump, and vacuum it for 60 minutes, the vacuum degree is -0.093Mpa, and the input lanthanum content is 0.1g / L of lanthanum nitrate solution, keep the vacuum state, after immer...

Embodiment 2

[0043] Catalyst carrier: put 0.418kg aluminum sol, 0.582kg SAPO-II molecular sieve, 0.2kg hydroxypropyl cellulose and 0.3kg safflower gum into the conical mixer, take it out after 15 minutes of mixing and put it into the mud making machine Inner: make mud for 10 minutes, take it out, extrude it into a strip-shaped clover-shaped green body through an extruder with a clover mold, dry in an oven at 70°C until the water content of the green body is 5.3%, and bake in a muffle furnace at 570°C for 6 hours;

[0044] Impregnation: Put the catalyst carrier into the vacuum impregnation machine, heat it to 120°C, start the vacuum pump, and evacuate it for 60 minutes. After immersion for 30 minutes, turn off the vacuum pump, open the pressure relief valve, wait until the vacuum gauge returns to zero, open the drain valve, discharge the lanthanum nitrate solution out of the impregnation machine, start the dehydration device, remove the floating water of the green body, and place the removed...

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 discloses a preparation method of a high-selectivity hydroisomerization catalyst. The method comprises the following steps: preparing main powder by using a SAPO-II molecular sieve and an inorganic binder, adding an organic binder, carrying out dry mixing, and sieving the mixed powder; adding water into the sieved powder, and kneading the powder to a mud material; extruding the mud material into a mud blank with an outline structure through a die; drying the mud blank and sending the dried mud blank to a kiln for roasting to obtain a catalyst carrier; supporting active componentsinto the catalyst carrier through a solution impregnation method, and finally carrying out drying, roasting and activating, and vulcanizing to obtain the high-selectivity hydroisomerization catalyst.The catalyst prepared by the method provided by the invention has the characteristics of low cost, high liquid yield, high hydrogenation activity and high selectivity, is suitable for the hydroisomerization process of high-pour-point white oil, and is particularly suitable for the hydroisomerization reaction for producing low-pour-point white oil from high-pour-point white oil with high aromatichydrocarbon content.

Description

technical field [0001] The invention belongs to the technical field of catalyst preparation, and in particular relates to a preparation method of a highly selective hydrogenation isomerization catalyst. Background technique [0002] With the increasing application of high-performance engines in industrial production, the demand for high-grade lubricating oils with low viscosity, low freezing point and high viscosity index is increasing day by day. Although the long-chain n-alkanes (i.e. waxes) in the lubricating oil fraction have a high viscosity index (VI), their low-temperature fluidity is poor and the octane number is low, so part or all of the waxes should be removed to obtain Lubricating oil with good fluidity at low temperature. The commonly used dewaxing processes are solvent dewaxing, catalytic dewaxing and isomerization dewaxing. Traditional solvent dewaxing technology, such as ketone-benzene dewaxing process, has been gradually eliminated due to factors such as c...

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
Patent Type & AuthorityApplications(China)
IPC IPC(8): B01J29/85B01J37/02C10G45/64
CPCB01J29/85B01J37/0205B01J37/0207C10G45/64C10G2400/14
Inventor赵华韩明徐翠翠牛同治王进才姚光纯
Owner洛阳金达石化有限责任公司