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Process for producing ethylene from an ethanol feedstock

A raw material, ethanol technology, which is applied in the field of ethylene production, can solve the problems of affecting catalyst performance and poor catalyst stability, and achieve the effects of reducing energy consumption, high ethylene selectivity, and reducing reaction temperature

Inactive Publication Date: 2019-04-09
FAR EASTERN NEW CENTURY COPRRATION
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because these catalysts are not supported by the carrier, the hydration reaction between silver ions and water in the catalyst may occur, resulting in poor catalyst stability and undesirably affecting the performance of the catalyst

Method used

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  • Process for producing ethylene from an ethanol feedstock
  • Process for producing ethylene from an ethanol feedstock
  • Process for producing ethylene from an ethanol feedstock

Examples

Experimental program
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Effect test

preparation example Construction

[0052] The preparation method of the supported heteropolyacid salt catalyst comprises the following steps: (1). Provide a supported heteropolyacid catalyst, wherein, the supported heteropolyacid catalyst contains a heteropolyacid and supports the heteropolyacid Carrier; (2). Provide a metal salt solution, wherein the type of metal is selected from the group consisting of copper, silver, gold, zinc, cadmium and mercury; and (3). Make the loaded heteropolyacid The catalyst is reacted with the metal salt solution to obtain a crude product, and the supported heteropolyacid salt catalyst is obtained after drying the crude product.

[0053] Preferably, the preparation method of the supported heteropolyacid catalyst is such as but not limited to incipient wetness impregnation (incipient wetness impregnation), and its specific steps are described in detail as follows: (1). Dissolving the heteropolyacid in water to obtain the heteropolyacid A polyacid solution; and (2). Mixing the hete...

Embodiment 1

[0073] 0.189 g of silver nitrate was dissolved in 3 ml of distilled water to obtain a silver nitrate solution. The silver nitrate solution was slowly dropped into a supported silicotungstic acid catalyst with a total weight of 12 g and stirred evenly to obtain a crude product. After the crude product is placed in an oven and dried at 130°C, a supported silver silicotungstate catalyst is obtained [silicotungstate silver salt compound is (AgH 3 )SiW 12 o 40 , The content of silver is 1wt%]. 3ml of the supported silver silicotungstate catalyst was placed in a fixed bed reactor. Use a liquid control pump to pump 95% (v / v) ethanol into a preheating tank to vaporize into ethanol gas, and use nitrogen as the carrier gas (humidity 5%) to carry the ethanol gas into the fixed bed reactor, at a space velocity of 1h -1 1. The dehydration reaction of ethanol was carried out under the condition that the reaction temperature was 220° C. and the reaction pressure was 0.1 MPa, and the gas...

Embodiment 2

[0075] 0.992 g of silver nitrate was dissolved in 3 ml of distilled water to obtain a silver nitrate solution. The silver nitrate solution was slowly dropped into a supported silicotungstic acid catalyst with a total weight of 12 g and stirred evenly to obtain a crude product. After the crude product is placed in an oven and dried at 130°C, a supported silver silicotungstate catalyst is obtained [silicotungstate silver salt compound is (AgH 3 )SiW 12 o 40 , The silver content is 5wt%]. 3ml of the supported silver silicotungstate catalyst was placed in a fixed bed reactor. Use a liquid quality control pump to pump 95% (v / v) ethanol into a preheating tank to vaporize into ethanol gas, and use nitrogen as a carrier gas (humidity 5%) to bring ethanol gas into the fixed In a bed reactor, at a space velocity of 1 h -1 1. The dehydration reaction of ethanol was carried out under the condition that the reaction temperature was 200° C. and the reaction pressure was 0.1 MPa, and th...

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Abstract

The invention provides a process for producing ethylene from an ethanol feedstock. The process comprises a step of subjecting the ethanol feedstock to a dehydration reaction in the presence of a supported heteropolyacid salt catalyst, wherein the supported heteropolyacid salt catalyst includes a support and a heteropolyacid salt compound which is carried on the support and which is represented bya formula selected from the group consisting of a chemical formula 1, a chemmical formula 2 and a chemical formula 3. The definition of each substituent in the chemical formula 1, the chemical formula2 and the chemical formula 3 are shown in a description and a claim. According to the process for producing ethylene from an ethanol feedstock of the disclosure, in which the dehydration reaction ofethanol is performed in the presence of the supported heteropolyacid salt catalyst, the dehydration reaction may be performed at a relatively low temperature to reduce energy consumption, and the ethanol conversion and ethylene selectivity thus obtained are superior.

Description

technical field [0001] The invention relates to a method for producing ethylene from ethanol raw materials, in particular to a method for producing ethylene by carrying out ethanol dehydration reaction using a supported heteropolysalt catalyst. Background technique [0002] Ethylene, the main component of plastics, can be produced by cracking petroleum hydrocarbons to form ethylene, or by dehydrating ethanol to form ethylene. With the reduction of petroleum resources, the cost of using petroleum to produce ethylene is becoming more and more expensive. However, compared with petroleum, ethanol can be used in the process of producing ethylene through the fermentation of glucose, starch, etc. Bioethanol, and compared with Cracking petroleum hydrocarbons to form ethylene, and using bio-ethanol for dehydration to produce bio-ethylene can greatly reduce greenhouse gas emissions, so now the production of ethylene from ethanol is the mainstream technology in the industry. [0003] ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C1/24C07C11/04
CPCC07C1/24C07C2523/888C07C2523/68C07C2527/188C07C11/04C07C2523/30C07C2523/50C07C2523/72C07C2521/08Y02P20/52C07C2527/19C07C2521/16C07C2521/04
Inventor 杨怡芬纪法成廖瑞芬郭俊毅
Owner FAR EASTERN NEW CENTURY COPRRATION