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Comprehensive utilization method for waste residues and waste liquor generated in catalytic cracking catalyst production

A catalytic cracking and catalyst technology, which is applied in the direction of physical/chemical process catalysts, catalyst carriers, molecular sieve catalysts, etc., can solve the problem of less research on the overall reuse of waste residue and wastewater, cracking catalyst cracking activity, hydrothermal stability, dry gas and coke yield Low-level problems, to achieve the effect of reducing the difficulty of exchange, improving anti-wear performance, and controlling screening

Inactive Publication Date: 2016-07-06
QINGDAO HUICHENG PETROCHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] CN102896000B provides a method for utilizing catalyst production waste residue, which uses catalyst waste residue as a catalyst filler or carrier to prepare a cracking catalyst. The difference from CN1150301C is that this invention provides a method for using cracking catalyst waste residue to prepare a cracking catalyst active carrier A new method, the active carrier prepared by this method, ultra-stable Y-type molecular sieve, alumina binder and clay beating, spray drying to obtain a cracking catalyst with high cracking activity, good hydrothermal stability, and low yield of dry gas and coke
[0014] At present, in the existing technology, most of the waste residues generated in the catalyst preparation process are used to prepare molecular sieves or as catalyst supports, but there are few studies on the overall reuse of waste residues and wastewater generated in the entire system

Method used

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  • Comprehensive utilization method for waste residues and waste liquor generated in catalytic cracking catalyst production
  • Comprehensive utilization method for waste residues and waste liquor generated in catalytic cracking catalyst production
  • Comprehensive utilization method for waste residues and waste liquor generated in catalytic cracking catalyst production

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] The waste residue produced by molecular sieve exchange, filtration and washing and the waste residue produced by gelation, washing and filtration of catalytic cracking catalyst were pressed with a plate and frame filter press for 30 minutes to form a filter cake, which was analyzed and burned for later use;

Embodiment 2

[0046] (1) Take 1200g of pressed filter cake and 4800g of molecular sieve secondary exchange zero-grade filtrate, mix and beat for preliminary exchange, add hydrochloric acid with a concentration of 6.4% to adjust the pH value to about 3.7, react for 20min, and take 4800g of catalyst washing waste liquid for rinsing , Wash with 3840g deionized water, filter the obtained material into a ball mill, add 1500g deionized water to grind for 2h, analyze the solid content and wait for gelation.

[0047] (2) Weigh 2250g of the slurry modified by the above method, mix it with 1286g REUSY and 279g deionized water for beating for 3h, add 580g of pseudoboehmite and stir vigorously for 30min, add 15wt% hydrochloric acid to the colloid for acidification and peptization for 15min, and continue stirring The catalyst is prepared by spray drying after uniformity.

[0048] (3) 600 g of the obtained catalyst was calcined in a muffle furnace at 430° C. for 1.5 h, and after the end, the sample was t...

Embodiment 3

[0051] (1) Take 1200g of pressed filter cake and 5760g of molecular sieve secondary exchange zero-grade filtrate, mix and beat for preliminary exchange, add hydrochloric acid with a concentration of 6.4% to adjust the pH value to about 3.7, react for 20min, and take 4800g of catalyst washing waste liquid for rinsing , Wash with 3840g deionized water, filter the obtained material into a ball mill, add 1500g deionized water to grind for 2h, analyze the solid content and wait for gelation.

[0052] (2) Weigh 2344g of the slurry modified by the above method, mix it with 1286g REUSY and 300g deionized water for beating for 3h, add 464g of pseudo-boehmite and stir vigorously for 30min, add 15wt% hydrochloric acid to the colloid for acidification and peptization for 15min, and continue stirring The catalyst is prepared by spray drying after uniformity.

[0053] (3) 600 g of the obtained catalyst was calcined in a muffle furnace at 430° C. for 1.5 h, and after the end, the sample was ...

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PUM

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Abstract

A method for comprehensive utilization of catalytic cracking catalyst production waste residue / waste liquid, comprising: (1) pressing dry the waste residue produced by catalytic cracking catalyst production with a plate and frame filter press; (2) combining the filter residue obtained in step (1) with Molecular sieve exchange waste liquid beating, inorganic acid to adjust the pH value of the slurry for preliminary ion exchange; (3) filter the slurry in step (2) through a filter, and rinse the waste liquid with catalytic cracking catalyst; (4) beat (3), Grinding with a wet ball mill; (5) pulping the material obtained in (4), active components, and a binder, gelling, and spray drying to obtain a catalytic cracking catalyst. The obtained catalytic cracking catalyst has high cracking activity and can be used as an auxiliary agent.

Description

technical field [0001] The invention relates to a method for comprehensive utilization of waste residue / wastewater produced in catalytic cracking catalyst production. Background technique [0002] For a long time, catalytic cracking has been an important means of deep processing of heavy oil at home and abroad, and plays a pivotal role in the development of the national economy. As one of the technical cores of catalytic cracking catalysts, the demand for catalytic cracking catalysts is increasing day by day. According to statistics, the domestic demand for catalytic cracking catalysts in 2015 was 200,000-250,000 tons, so the environmental pollution caused by the preparation of catalytic cracking catalysts also caused received widespread attention at home and abroad. [0003] The production of catalytic cracking catalysts includes molecular sieve preparation (ion exchange, hydrothermal calcination, filtration, washing), molecular sieve, carrier, binder mixing into gel, spra...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/16B01J32/00
CPCB01J29/166B01J2229/18
Inventor 刘惠娟高明军叶红张新功张晓佳
Owner QINGDAO HUICHENG PETROCHEM TECH
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