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

A kind of residual oil catalyst and its preparation method and application

A catalyst and residual oil technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of increasing reactor load, reducing catalyst activity, and product separation. Difficulties and other problems, to achieve the effect of reducing solid content, reducing wear, and high cracking activity

Active Publication Date: 2017-03-29
CHINA PETROLEUM & CHEM CORP +1
View PDF2 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Solid powder catalyst is a kind of residual oil slurry bed hydrocracking catalyst that is widely used. For example, in the prior art of residual oil slurry bed hydrocracking, ferrous sulfate, ore powder or coal powder are used as additives. These solid powder catalysts It has good coke loading performance, but it has the disadvantages of large amount of addition, poor dispersion in raw materials, and serious wear and tear on equipment
[0005] CN1020112C proposed the hydrocracking of heavy oil in the presence of ultra-fine ferric sulfate, requiring that ferric sulfate or iron ore etc. be mixed with oil and ground to a particle size of less than 45 microns in a stirring ball mill, preferably at least 50% of the particles The particle size is less than 5 microns. Although the use of this catalyst is beneficial to reduce coke formation and improve asphalt conversion, it is easy to operate in the laboratory to grind the solid to several microns, but the industrial implementation has higher requirements for the grinding machine, and the loss is large. Difficult to achieve
[0006] CN1255407A and USP5866501 disclose a kind of dispersive fine-grained, anion-modified and phosphorus-promoted iron oxide slurry catalyst, which has a large specific surface area and a particle size less than 50 angstroms, which is used in the form of wet cake gel , but the wet cake contains at least 60% water, the introduction of this part of water will not only increase the load on the reactor, but also bring difficulties to the separation of subsequent products. After drying, it is added as a dry powder. Due to the aggregation between particles, the catalyst activity Lower, more heavy fractions

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
  • A kind of residual oil catalyst and its preparation method and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039]Dissolve 58.0g of ferrous sulfate heptahydrate and 0.20g of EDTA in 400g of deionized water, add 200.0g of C1 and stir evenly, take another 25.0g of ammonia water and drop into the above solution while stirring, and continue to stir for 40min, then perform suction filtration and washing to obtain The filter cake was dried at 110°C for 2 hours to obtain solid particles. Another 20 mL of acetic acid solution with a pH value of 2.8 was sprayed onto the above powder and stirred for 20 min, then dried at 110°C for 3 hours, and the residual oil catalyst obtained by grinding was denoted as B1, and the iron content in B1 was analyzed to be 5.1% by weight , the water content is 2.0% by weight.

Embodiment 2

[0041] Weigh 58g of ferrous sulfate heptahydrate and put it into a beaker, add 200g of deionized water and stir continuously to dissolve, add 150.0g of C2 and stir to mix evenly, add 25g of ammonia water drop by drop while stirring, continue to stir for 60min, then suction filter, After washing, the obtained filter cake was dried at 105° C. for 2 hours to obtain solid particles. Another 30 mL of sulfuric acid solution with a pH value of 1.45 was sprayed onto the above powder and stirred for 20 min, then dried at 110°C for 3 hours, and the residual oil catalyst obtained by grinding was denoted as B2, and the iron content in B2 was analyzed to be 6.5% by weight , the water content is 1.8% by weight.

Embodiment 3

[0043] Weigh 80g of ferric chloride and 0.55g of diammonium hydrogen phosphate into a beaker, add 100g of deionized water and stir to dissolve continuously, weigh 80.0g of C3 and stir to mix evenly, add 30g of ammonia water drop by drop while stirring. Inject air and continue to stir for 60 minutes, then suction filter and wash to obtain a filter cake and dry it at 105°C for 5 hours to obtain solid particles. Another 15 mL of sulfuric acid solution with a pH value of 1.9 was sprayed onto the above powder and stirred for 30 min, then dried at 110°C for 3 hours, and the residual oil catalyst obtained by grinding was designated as B3. The iron content in the B3 catalyst was 20.0% by weight, and the water content was 1.5% by weight.

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

PropertyMeasurementUnit
particle sizeaaaaaaaaaa
specific surface areaaaaaaaaaaa
particle sizeaaaaaaaaaa
Login to View More

Abstract

The invention relates to a residual oil catalyst and a preparation method and application of the residual oil catalyst. The catalyst consists of active components including a Fe-containing compound modified by B-acid and a carbon-based material. When the catalyst is used for residual oil thermal hydrocracking reaction, the addition quantity of the catalyst is 0.1%-2.0% of a heavy hydrocarbon raw material by weight according to Fe. The catalyst provided by the invention is suitable for the hydrocracking process of super-thick oil and poor-quality residual oil with high content of asphaltene and metal, has the functions of cracking activity, hydrogenation activity and coking inhibition, adopts a simple preparation method, does not contain metal, and is low in cost.

Description

technical field [0001] The invention relates to a residual oil hydrocracking catalyst, a preparation method of the catalyst, and a residual hydrothermal cracking method using the catalyst. Background technique [0002] The problem of increasingly heavy and inferior oil resources in the world and the contradiction between the rapid economic growth and the increasing demand for petroleum products have made refineries pay more and more attention to the technology of lightening heavy oil. Among them, hydrocracking of slurry bed residue The process has strong competitiveness and good development prospects because it can handle low-quality raw materials with high carbon residue and high metal content. Catalyst is one of the core technologies of residual oil hydrocracking process. It plays a very important role in reducing reaction severity, improving reaction efficiency, increasing oil yield and reducing coke yield, thereby reducing residual oil processing cost and improving its e...

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 & Authority Patents(China)
IPC IPC(8): B01J23/745C10G47/12
Inventor 王卫平吴治国王蕴王鹏飞任杰王子军申海平
Owner CHINA PETROLEUM & CHEM CORP
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