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Recovery of component (c4) alkanoic acids

A technology of alkanoic acid and heat recovery, applied in plastic recycling, chemical recycling, recycling technology, etc., can solve the problem of difficulty in separating and distributing the special part of gas

Pending Publication Date: 2022-03-18
EASTMAN CHEM CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In some cases, it may be difficult to dedicate a product with recycled content to a specific customer or downstream synthesis process for use in making derivatives of the product, especially if the recycled content product is gaseous or difficult to separate
Because gas infrastructure is continuous flow and often mixes gas streams from various sources, it can be difficult to segregate and distribute dedicated portions of gas made exclusively from recycled component feedstock

Method used

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  • Recovery of component (c4) alkanoic acids
  • Recovery of component (c4) alkanoic acids
  • Recovery of component (c4) alkanoic acids

Examples

Experimental program
Comparison scheme
Effect test

example

[0717] r-pyrolysis oil example 1-4

[0718] Table 1 shows the composition of r-pyrolysis oil samples by gas chromatography analysis. r-pyrolysis oil samples were prepared from waste high- and low-density polyethylene, polypropylene, and polystyrene materials. Sample 4 is a laboratory distilled sample where hydrocarbons larger than C21 were removed. The boiling point curves for these materials are shown in Figure 13-16 middle.

[0719] Table 1. Gas chromatographic analysis of r-pyrolysis oil examples

[0720]

[0721]

[0722]

[0723]

[0724] r-pyrolysis oil example-5-10

[0725] Six r-pyrolysis oil compositions were prepared by distillation of r-pyrolysis oil samples. They were prepared by processing the material according to the procedure described below.

example 5

[0726] Example 5. The r-pyrolysis oil is at least 90% boiling at 350°C, 50% boiling between 95°C and 200°C, and at least 10% boiling at 60°C.

[0727] A 250 g sample of r-pyrolysis oil from Example 3 was distilled through a 30-tray glass Oldershaw column equipped with a glycol-cooled condenser, a thermowell containing a thermometer, and a magnet-operated reflux regulated by an electronic timer. controller. Batch distillation was performed at atmospheric pressure with a reflux ratio of 1:1. Liquid fractions were collected every 20 mL, and the overhead temperature and mass were recorded to construct Figure 17 Boiling curve shown. The distillation was repeated until approximately 635 g of material was collected.

example 6

[0728] Example 6. r-pyrolysis oil boiling at least 90% at 150°C, 50% boiling between 80°C and 145°C, and at least 10% boiling at 60°C.

[0729] A 150 g sample of r-pyrolysis oil from Example 3 was distilled through a 30-tray glass Oldershaw column equipped with a glycol-cooled condenser, a thermowell containing a thermometer, and a magnet-operated reflux regulated by an electronic timer. controller. Batch distillation was carried out at atmospheric pressure with a reflux ratio of 1:1. Liquid fractions were collected every 20 mL, and the overhead temperature and mass were recorded to construct Figure 18 Boiling curve shown. The distillation was repeated until approximately 200 g of material was collected.

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Abstract

A process is provided for preparing a recovered component (C4) alkanoic acid (i.e. Butyric acid and / or isobutyric acid) and recovered (C4) alkanal derived from a recovered propylene composition.

Description

Background technique [0001] Waste materials, especially non-biodegradable waste materials, can negatively impact the environment when disposed of in landfill after a single use. Therefore, from an environmental point of view, it is desirable to recycle as much waste as possible. However, recycling waste can be challenging from an economic standpoint. [0002] To maximize recycling efficiency, it is desirable for large-scale production facilities to be able to process feedstock with recycled content derived from various waste materials. [0003] Some recycling operations involve complex and detailed separation of waste streams, which results in increased costs for obtaining the fractional streams of recycled waste. It is desirable to establish a recycled content that does not require it to be sorted into a single type of plastic or waste, or that can tolerate a variety of impurities in the waste stream. [0004] In some cases, it may be difficult to dedicate a product with r...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C51/235C07C51/14C07C45/50C10G1/00C10G1/10C10G3/00C10B49/16C10B49/22C10B53/02C10B57/06
CPCC07C51/235C07C51/14C07C45/50C10G1/10C10B53/02C10B57/06C10G3/40C10B49/16C10G1/002C10B49/22C07C47/02C07C53/124Y02P30/20Y02P20/582Y02E50/10C07C51/353
Inventor 大卫·尤金·斯莱文斯基肯尼·伦道夫·帕克威廉·刘易斯·特拉普达里尔·贝汀迈克尔·加里·波拉塞克武显春
Owner EASTMAN CHEM CO