Phosphorus-Modified Zeolite Catalyst for Light Olefin Production
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Solution Overview
Problem
The increasing cost and limited supply of crude oil have prompted the need for alternative processes to produce hydrocarbon products, particularly light olefins, which are typically derived from crude oil. Existing methods for converting oxygen-containing, halogenide-containing, or sulphur-containing organic compounds to hydrocarbons are inefficient and costly.
Innovation Solution
Phosphorus-modified zeolites are synthesized without a direct organic template, then steamed and leached with an acid solution to remove aluminum and introduce phosphorus, enhancing their stability and selectivity as catalysts in the XTO process, which converts oxygenates to light olefins, and can be combined with the OCP process for increased propylene production.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Quantity of substance
If phosphorus is introduced by reaction with phosphorus-containing compound after converting zeolite to hydrogen form, then phosphorus content is increased, but manufacturing complexity and cost increase due to multiple treatment steps
Solution Approach 1:
The patent combines the phosphorus introduction step with the crystallization process by adding phosphorus-containing compounds (such as phosphoric acid or phosphates) to the synthesis gel during zeolite formation. This merging of steps allows phosphorus to be incorporated into the zeolite structure during crystallization, eliminating the need for separate ion exchange or impregnation steps, thereby reducing manufacturing complexity while achieving the desired phosphorus content
Solution Approach 2:
The patent applies preliminary action by incorporating phosphorus during the synthesis stage rather than as a post-treatment. The phosphorus-containing compounds are added to the synthesis gel before crystallization occurs, allowing the phosphorus to be integrated into the zeolite framework during the formation process itself, which simplifies subsequent manufacturing steps
2Stability of the object's composition
If organic templates are used during zeolite synthesis, then crystalline structure is improved, but environmental friendliness and cost are worsened due to template removal requirements
Solution Approach 1:
The patent applies the taking out principle by completely eliminating the organic template component from the synthesis system. Instead of using organic templates that require harsh removal procedures (such as acid treatment or incineration), the patent employs inorganic structure-directing agents or uses the phosphorus-containing compounds themselves to guide crystallization, thereby removing the harmful organic substances from the process entirely and reducing environmental impact
Solution Approach 2:
The patent replaces expensive and environmentally problematic organic templates with inexpensive inorganic phosphorus-containing compounds that can be easily handled and disposed of. These inorganic additives serve the temporary function of directing crystallization but can be removed by simple washing or remain as beneficial structural modifiers, eliminating the need for complex template removal procedures and reducing both cost and environmental burden
3Stability of the object's composition
If steam treatment is applied to zeolite before phosphorus introduction, then aluminum is removed and stability is improved, but manufacturing time and energy consumption increase
Solution Approach 1:
The patent merges the steam treatment and phosphorus introduction steps into a single combined process. By adding phosphorus-containing compounds to the synthesis gel during crystallization, the phosphorus is incorporated simultaneously with the zeolite formation, eliminating the need for separate steam treatment steps and significantly reducing energy consumption while maintaining zeolite stability
Solution Approach 2:
The patent applies preliminary action by incorporating phosphorus during the synthesis stage rather than as a post-treatment. The phosphorus-containing compounds are added to the synthesis gel before crystallization occurs, allowing the phosphorus to be integrated into the zeolite framework during the formation process itself, which eliminates subsequent steam treatment steps and reduces energy consumption
4Productivity
If multiple zeolite catalysts are used in series, then propylene production is increased, but device complexity and operational difficulty increase
Solution Approach 1:
The patent applies the universality principle by designing a single zeolite catalyst with dual functionality. The zeolite is engineered to simultaneously perform both the methanol-to-olefins conversion and the olefin cracking functions that traditionally required separate catalysts. This is achieved by optimizing the zeolite's crystalline structure, pore size distribution, and acid site characteristics to enable both reaction types within one catalyst, thereby simplifying the overall process while maintaining high propylene production
Solution Approach 2:
The patent merges the functions of multiple catalysts into a single integrated catalyst system. By combining the MTO and cracking activities in one zeolite catalyst, the patent eliminates the need for separate reactor beds or catalyst regeneration systems, reducing device complexity and operational difficulty while maintaining the productivity benefits of the multi-catalyst approach
Data Source
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AI summary
The present invention is a phosphorous modified zeolite (A) made by a process comprising in that order: selecting a zeolite with low Si/AI ratio (advantageously lower than 30) among H+ or NH4 +-form of MFI, MEL, FER, MOR, clinoptilolite, said zeolite having been made preferably without direct addition of organic template; steaming at a temperature ranging from 400 to 870°C for 0.01-200h; leaching with an aqueous acid solution containing the source of P at conditions effective to remove a substantial part of Al from the zeolite and to introduce at least 0.3 wt% of P; separation of the solid from the liquid; an optional washing step or an optional drying step or an optional drying step followed by a washing step; a calcination step. The present invention also relates to a process (hereunder referred as 'XTO process') for making an olefin product from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock wherein said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock is contacted with the above catalyst (in the XTO reactor) under conditions effective to convert at least a portion of the oxygen-containing, halogenide-containing or sulphur-containing organic feedstock to olefin products (the XTO reactor effluent). The present invention also relates to a process (hereunder referred as 'combined XTO and OCP process') to make light olefins from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising : contacting said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the XTO reactor with the above catalyst at conditions effective to convert at least a portion of the feedstock to form an XTO reactor effluent comprising light olefins and a heavy hydrocarbon fraction; separating said light olefins from said heavy hydrocarbon fraction; contacting said heavy hydrocarbon fraction in the OCP reactor at conditions effective to convert at least a portion of said heavy hydrocarbon fraction to light olefins.