Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Modification method of biomass pyrolysis oil

一种生物质热解油、改性的技术,应用在生物燃料、生物原料、分离方法等方向,能够解决生物质热解油粘度变大、有机共沸物损耗、反应器堵塞等问题,达到反应时间极短、设备低廉、进料容易的效果

Active Publication Date: 2013-07-24
WUHAN KAIDI ENG TECH RES INST CO LTD
View PDF6 Cites 10 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In these processes, it is very easy to make the biomass pyrolysis oil become more viscous or even agglomerate and deteriorate during heating and rectification
At the same time, because biomass pyrolysis oil contains more low boiling point components, the rectification process will cause the loss of these low boiling point components and some organic azeotropes
However, the equipment for catalytic hydrogenation is generally complex and costly, and reactor blockage and catalyst deactivation are prone to occur during the production process.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Modification method of biomass pyrolysis oil
  • Modification method of biomass pyrolysis oil
  • Modification method of biomass pyrolysis oil

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Take 1000g of biomass pyrolysis oil and place it in a 1500ml three-necked flask, and slowly add 0.5g of sodium chloride and 0.25g of polyoxypropylene ether during stirring. Continue to stir for 5 minutes. After the biomass pyrolysis oil is fully mixed with the added demulsifier, transfer the mixed solution into a separating funnel and let it stand for 20 minutes. At this time, the lower aqueous solution becomes clear and the water-oil interface is clear, and the upper biomass pyrolysis oil I and the lower aqueous solution are separated.

[0032] Put the molded high-silicon REUSY / clay catalyst into 80°C, 1mol / L NH 4 NO 3 Soaked in the solution for 6 hours, the soaked catalyst was dried and calcined at 150°C for 3 hours. The calcined catalyst was aged at 600°C and 100% steam for 3 hours. Take by weighing 200g this catalyst and pack in the fixed fluidized bed, at mass space velocity 6h -1 The catalyst-oil ratio is 8, the reaction temperature is 450°C, and the reaction ...

Embodiment 2

[0036] Take 1000g of biomass pyrolysis oil and place it in a 1500ml three-necked flask, and slowly add 1g of sodium sulfate and 1g of propylene glycol during stirring. Continue to stir for 5 minutes. After the biomass pyrolysis oil is fully mixed with the added demulsifier, transfer the mixed solution into a separating funnel and let it stand for 20 minutes. At this time, the lower aqueous solution becomes clear and the water-oil interface is clear, and the upper biomass pyrolysis oil II and the lower aqueous solution are separated.

[0037] Put the molded REY / clay catalyst into 80℃, 1mol / L NH 4 NO 3 Soaked in the solution for 6 hours, the soaked catalyst was dried and calcined at 300°C for 4 hours. The calcined catalyst was aged at 800°C and 100% steam for 5 hours. Take by weighing 200g this catalyst and pack in the fixed fluidized bed, with mass space velocity 10h -1 The catalyst-oil ratio is 8, the reaction temperature is 550°C, and the reaction pressure is 0.3Mpa, and ...

Embodiment 3

[0041] Take 1000g of biomass pyrolysis oil and place it in a 1500ml three-neck flask, and slowly add 0.6g of sodium chloride and 0.3g of polyoxypropylene ether during stirring. Continue to stir for 5 minutes. After the biomass pyrolysis oil is fully mixed with the added demulsifier, transfer the mixed solution into a separating funnel and let it stand for 20 minutes. At this time, the lower layer aqueous solution becomes clear and the water-oil interface is clear, and the upper layer biomass pyrolysis oil III and the lower layer aqueous solution are separated.

[0042] Put the molded high-silicon REUSY / clay catalyst into 80°C, 1mol / L NH 4 NO 3 Soaked in the solution for 6 hours, the soaked catalyst was dried and calcined at 150°C for 3 hours. The calcined catalyst was aged at 600°C and 100% steam for 3 hours. Take by weighing 200g this catalyst and pack in the fixed fluidized bed, at mass space velocity 6h -1 The catalyst-oil ratio is 8, the reaction temperature is 450°C, ...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention provides a modification method of biomass pyrolysis oil. The modification method of the biomass pyrolysis oil specifically comprises the following steps of: I, demulsification layering dehydration: adding an inorganic salt iron and an organic demulsifier into the biomass pyrolysis oil, wherein the mass ratio of the inorganic salt to the biomass pyrolysis oil is (1:2000)-(1:800), the mass ratio of the organic demulsifier to the biomass pyrolysis oil is (1:4000)-(1:1000), mixing completely, standing and taking an upper-layer biomass pyrolysis oil; II, carrying out catalytic cracking modification on the biomass pyrolysis oil: using a modified catalyst: (1) modified catalyst: carrying out ageing treatment on a zeolite molecular sieve load carclazyte catalyst for 2-8 hours with 100% water vapor at 500-800 DEG C; placing the aged catalyst in a reactor, injecting the biomass pyrolysis oil in a reactor with the catalyst, wherein the agent-oil ratio is 1:(3-16), and carrying out biomass pyrolysis oil catalytic cracking modification at the mass airspeed of 6-15h<1>, the reaction temperature of 380-700 DEG C and the reaction pressure of 0.1Mpa-0.8Mpa.

Description

technical field [0001] The invention provides a method for modifying biomass pyrolysis oil. Specifically, it is the technology of direct catalytic cracking of biomass pyrolysis oil to produce fuel oil after dehydration. Background technique [0002] Fossil energy such as petroleum, coal, and natural gas is increasingly exhausted. Biomass energy is the fourth largest energy after petroleum, coal, and natural gas. It has the advantages of extensive sources, safety, renewable cycle, and zero carbon dioxide emissions. Biomass sources mainly include crops, trees, other plants and straw, etc. Biomass can produce different types of energy fuels through a series of conversion technologies, such as biomass carbonization can produce high-quality solid fuels, and biomass gasification can produce gaseous fuels , Biomass liquefaction can obtain liquid fuel, etc. Biomass directly converted to liquid fuel technology can convert low-quality, low-calorific-value biomass energy into high-q...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): C10G55/06
CPCB01D17/047B01J29/088B01J29/405B01J2229/186B01J2229/36B01J2229/42C10B53/02C10G3/49C10G11/18C10G33/04C10G2300/1011C10L1/02Y02E50/10Y02P30/20
Inventor 汪大闪宋德臣刘倩倩郑申棵詹晓东金家琪张岩丰
Owner WUHAN KAIDI ENG TECH RES INST CO LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products