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Recovery of components ethylene oxide or alkyl glycols

An ethylene oxide, ethylene technology for recycled content in ethylene oxide that addresses unattractive, stranded cracking facilities, etc.

Pending Publication Date: 2022-07-08
EASTMAN CHEM CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] It is also desirable to continue the feedstock used to make ethylene oxide and alkyl glycols from olefins obtained from cracking facilities, which themselves may be put on hold as production from natural gas fields or oil becomes economically unattractive

Method used

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  • Recovery of components ethylene oxide or alkyl glycols
  • Recovery of components ethylene oxide or alkyl glycols
  • Recovery of components ethylene oxide or alkyl glycols

Examples

Experimental program
Comparison scheme
Effect test

example

[0832] r-pyrolysis oil example 1-4

[0833]Table 1 shows the composition of the r-pyrolysis oil samples by gas chromatographic analysis. The r-pyrolysis oil samples were prepared from waste high and low density polyethylene, polypropylene and polystyrene materials. Sample 4 was a laboratory distilled sample in which hydrocarbons greater than C21 were removed. The boiling point curves of these materials are shown in Figure 13-16 middle.

[0834] Table 1. Gas chromatographic analysis of r-pyrolysis oil examples

[0835]

[0836]

[0837]

[0838]

[0839] r-pyrolysis oil example-5-10

[0840] Six r-pyrolysis oil compositions were prepared by distilling r-pyrolysis oil samples. They were prepared by processing the material according to the procedure described below.

example 5

[0841] Example 5. r-Pyrolysis oil boils at least 90% at 350°C, 50% boils between 95°C and 200°C, and at least 10% boils at 60°C.

[0842] A 250 g sample of the 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 a reflux ratio of 1:1 at atmospheric pressure. Collect liquid fractions every 20mL, record overhead temperature and mass to build Figure 17 Boiling curve shown. The distillation was repeated until about 635 g of material had been collected.

example 6

[0843] Example 6. r-pyrolysis oil with at least 90% boiling at 150°C, 50% boiling between 80°C and 145°C, and at least 10% boiling at 60°C.

[0844] A 150 g sample of the 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 a reflux ratio of 1:1 at atmospheric pressure. Collect liquid fractions every 20mL, record overhead temperature and mass to build Figure 18 Boiling curve shown. The distillation was repeated until about 200 g of material had been collected.

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Abstract

The ethylene oxide composition having the recovery component value is obtained by reacting an ethylene stream comprising the recovery component ethylene to produce the recovery component ethylene oxide or by deducting the recovery component value applied to the ethylene oxide composition from the recovery stock. At least a portion of the recovered component value in the feedstock or in the partition obtained from the ethylene oxide manufacturer is derived from the recovered waste and / or the pyrolysis of the recovered waste and / or the hot steam cracking of the recovered component pyrolysis oil. Alkyl glycol compositions and / or alkyl glycol polyester compositions having a recovery component alkyl glycol or alkyl glycol polyester prepared by reacting recovery component feedstocks or by deducting from the recovery stock suitable for alkyl glycol compositions and / or alkyl glycol polyesters. At least a portion of the recovery component value in the feedstock or in the partition obtained from the alkyl glycol or alkyl glycol polyester manufacturer is derived from the recovery waste and / or the pyrolysis of the recovery waste and / or the hot steam cracking of the recovery component pyrolysis oil.

Description

technical field [0001] The present invention relates to recycled content of ethylene oxide, in particular to recycled content of ethylene oxide, wherein the recycled content is obtained directly or indirectly from sewage produced by pyrolysis of recycled waste. Background technique [0002] Ethylene oxide is an important product of organic synthesis. Most ethylene oxide is used as an intermediate in the production of numerous other chemicals such as alkanolamines, polyether polyols, most notably ethylene glycol, which is used to make polyesters such as polyethylene terephthalate Ethylene glycol and copolyesters containing CHDM, neopentyl glycol, propylene glycol or TMCD as modifiers containing ethylene terephthalate. Polyester polymers have many uses, including fibers for clothing, upholstery, carpets, upholstery and bedding, and pillows; for packaging films and bottles; as an ingredient in antifreeze; and in the manufacture of fiberglass, to make Jet skis, bathroom fences...

Claims

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Application Information

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IPC IPC(8): C07D301/00C07D303/04C07C29/88C08G63/16
CPCC07D303/04C07C29/106C08G63/16Y02P20/582C07C31/202C07D301/03
Inventor 大卫·尤金·斯莱文斯基达里尔·贝汀肯尼·伦道夫·帕克迈克尔·加里·波拉塞克威廉·刘易斯·特拉普武显春
Owner EASTMAN CHEM CO