Hydrogenation method for producing high grade diesel oil and high grade reforming raw material
A diesel and raw material technology, applied in the field of hydrogenation for the production of high-quality diesel and high-quality reforming raw materials, can solve the problems of low naphtha yield, increased cost, and reduced operational flexibility, and achieve simple process flow and moderate process conditions , The effect of strong adaptability of raw materials
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0050] In this embodiment, a kind of catalytic diesel is used as raw material oil A, and the main properties of the raw material are shown in Table 1. As can be seen from Table 1, the cetane number of this raw material is only 31.
[0051] After the raw material oil A is mixed with hydrogen, it is sequentially contacted with a hydrofinishing catalyst and a hydrocracking catalyst to react without intermediate separation. The reaction product is cooled and separated to obtain a hydrogen-rich gas and a liquid phase stream, and the obtained liquid phase stream is obtained by fractional distillation. The loading volume ratio of light naphtha fraction, heavy naphtha fraction and diesel fraction, hydrotreating catalyst and hydrocracking catalyst is 60:40. The reaction conditions are shown in Table 2, and the yield and properties of the main products obtained are shown in Table 3.
[0052] As can be seen from Table 3, the obtained heavy naphtha fraction sulfur and nitrogen content are...
Embodiment 2
[0060] After the raw material oil A is mixed with hydrogen, it is sequentially contacted with a hydrofinishing catalyst and a hydrocracking catalyst to react without intermediate separation. The reaction product is cooled and separated to obtain a hydrogen-rich gas and a liquid phase stream, and the obtained liquid phase stream is obtained by fractional distillation. Light naphtha fractions, heavy naphtha fractions, kerosene fractions, diesel fractions and tail oil fractions, among which the kerosene fractions with a distillation range of 175-230°C are all recycled back to the inlet of the hydrotreating reactor. In terms of weight, the recycled kerosene fraction It accounts for 15% of raw oil A. The loading volume ratio of the hydrorefining catalyst and the hydrocracking catalyst is 60:40. The reaction conditions are shown in Table 4, and the yield and properties of the main products obtained are shown in Table 5. As can be seen from Table 5, the obtained heavy naphtha fracti...
Embodiment 3
[0066] With a kind of light wax oil as raw material oil B, with a kind of catalytic diesel oil as raw material oil C, another kind of catalytic diesel oil as raw material oil D, raw material oil B, raw material oil C and raw material oil D are in weight ratio 41:41: 18 After mixing, the mixed raw material oil E was obtained. The main properties of these raw material oils are shown in Table 6.
[0067] After the raw material oil E is mixed with hydrogen, it is sequentially contacted with a hydrofinishing catalyst and a hydrocracking catalyst without intermediate separation, and the reaction product is cooled and separated to obtain a hydrogen-rich gas and a liquid phase stream, and the obtained liquid phase stream is obtained by fractional distillation The reaction conditions of light naphtha fraction, heavy naphtha fraction, diesel oil fraction and tail oil fraction are shown in Table 7, and the yield and properties of the main products obtained are shown in Table 8. The loadi...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com