Solid phosphoric acid catalyst and methods of olefin dimerization reaction with the same
一种烯烃二聚反应、磷酸催化剂的技术,应用在化学仪器和方法、有机化学方法、物理/化学过程催化剂等方向,达到制备简单、催化剂寿命长、活性和二聚物选择性高的效果
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
preparation example Construction
[0025] The preparation of the catalyst, that is, the loading of phosphoric acid on the carrier can be carried out by immersing the carrier in an aqueous phosphoric acid solution and then removing the remaining aqueous phosphoric acid solution. The apparatus used for the preparation of the catalyst is not particularly limited, and a general batch tank can be used. If a reactor for dimerization of olefins is used, the catalyst can be filled simultaneously with the preparation of the catalyst. The concentration of the phosphoric acid aqueous solution used for immersion is not particularly limited, and it is preferable to reduce the amount of heat reduction to a predetermined value in the state of immersion in the case of 92% by mass or less. When the concentration is higher than this, only It is not preferable to adjust the amount of reduction in heating by immersion since it is necessary to add water and make separate adjustments. The concentration of the commonly used phosphori...
Embodiment 1
[0037] 20.0 g of 0.8 to 1.7 mmφ synthetic silica granules (Cariact Q-50 manufactured by Fuji Silicone Chemicals) were immersed in 100 ml of a 42% by mass phosphoric acid aqueous solution put into a 200 ml beaker. After immersion for 1 hour, the aqueous solution was removed on a mesh filter to prepare a solid phosphoric acid catalyst A. Under the conditions of 250°C and 20 minutes, 28 mg of the obtained catalyst was subjected to thermogravimetric analysis, and as a result, the heating loss (moisture) was 12.6 mg (45.0 mass %), and the carrier and P in the catalyst 2 o 5 The proportion of the total amount was 55.0% by mass. Then, 2.00 g of the catalyst was sufficiently washed with water, dried, and the mass was measured. As a result, it was 0.71 g, and the amount of the carrier in the catalyst was 35.5% by mass. Therefore, P in the catalyst 2 o 5 The proportion of 19.5% by mass, the amount of heating reduction relative to P 2 o 5 The ratio of 230.8% by mass.
[0038] Fill...
Embodiment 2
[0040] Fill 2g solid phosphoric acid catalyst A in the tubular stainless steel reactor (inner diameter 8mm), from the top of reactor with 21.3g / h (WHSV=30h -1 ) feed feed contains the normal hexane of 50ppm water, a part of the reaction liquid that will be taken out from the lower part is combined in the feed in the form of recirculation (recirculation ratio R / F=4), pressure and temperature are adjusted to reaction initiation condition (1.0 MPa, 80°C). About 1 hour after the start of the feed, the pressure and temperature were stable under the reaction initiation conditions, so the feed was switched to an olefin-containing feedstock (30 mass % isobutene, 5 mass % n-butene, 65 mass % n-hexane, 250 mass ppm water ), the dimerization reaction was carried out continuously for 30 days. The reaction results are shown in Table 1.
PUM
Property | Measurement | Unit |
---|---|---|
particle diameter | aaaaa | aaaaa |
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