KR890017209A - Oxidation of hydrocarbons using the distribution of oxidizing gases - Google Patents

Oxidation of hydrocarbons using the distribution of oxidizing gases Download PDF

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Publication number
KR890017209A
KR890017209A KR1019890007062A KR890007062A KR890017209A KR 890017209 A KR890017209 A KR 890017209A KR 1019890007062 A KR1019890007062 A KR 1019890007062A KR 890007062 A KR890007062 A KR 890007062A KR 890017209 A KR890017209 A KR 890017209A
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South Korea
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oxygen
hydrocarbon
recycled
water
aqueous
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KR1019890007062A
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Korean (ko)
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KR970002035B1 (en
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카레튼 헨드릭스 데이비드
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배르너 퀘스터스
바스프 코포레이션
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Priority claimed from US07/199,844 external-priority patent/US5068464A/en
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07BGENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B33/00Oxidation in general

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

내용 없음No content

Description

산화기체의 분배를 이용하는 탄화수소의 산화방법Oxidation of hydrocarbons using the distribution of oxidizing gases

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

제1도는 산소수용액으로부터 액체탄화수소로의 산소의 이동을 도시한 실험장치, 제2도는 탄화수소의 대규모 산화를 위한 공정 흐름도.1 is an experimental apparatus showing the movement of oxygen from an aqueous oxygen solution to a liquid hydrocarbon, and FIG. 2 is a process flow diagram for large-scale oxidation of hydrocarbons.

Claims (19)

산소분자를 산화제로 사용하며 산화된 탄화수소 생성물을 함유하는 산화물로 탄화수소를 부분 산화하는 방법에 있어서 , a) 분리된 용기에서 산소수용액을 제조하고; b) 실제량의 산소가 수용액상으로부터 탄화수소상으로 이동하도록 산소수용액을 산화될 액체 탄화수소와 접촉시키고; 그리고 c) 상승된 온도에서 상기의 산소함유 탄화수소를 산화하는 단계로 구성됨을 특징으로 하는 탄화수소의 산화방법.A method of partially oxidizing a hydrocarbon with an oxide containing an oxidized hydrocarbon product using an oxygen molecule as an oxidant, comprising: a) preparing an oxygen aqueous solution in a separate vessel; b) contacting the aqueous oxygen solution with the liquid hydrocarbon to be oxidized such that the actual amount of oxygen is transferred from the aqueous phase to the hydrocarbon phase; And c) oxidizing the oxygen-containing hydrocarbon at an elevated temperature. 제1항에 있어서, 액체수용액은 약 5바 내지 200바의 압력에서 물에 산소를 용해함으로써 제조됨을 특징으로 하는 방법.The method of claim 1, wherein the aqueous liquid solution is prepared by dissolving oxygen in water at a pressure of about 5 bar to 200 bar. 제1항에 있어서, 산소의 이동이 역류흐름의 조건하에서 관 안에서 일어남을 특징으로 하는 방법.The method of claim 1 wherein the movement of oxygen occurs in the tube under conditions of backflow. 제2항에 있어서, 산소의 이동이 역류흐름의 조건하에서 관 안에서 일어남을 특징으로 하는 방법.3. The method of claim 2 wherein the movement of oxygen occurs in the tube under conditions of backflow. 제1항에 있어서, 단계(b)동안 형성된 산소가 없는 물이 단계(a)에서 재순환됨을 특징으로 하는 방법.The method of claim 1 wherein the oxygen free water formed during step (b) is recycled in step (a). 제2항에 있어서, 단계(b)동안에 형성된 산소없는 물이 단계(a)에서 재순환됨을 특징으로 하는 방법.The method of claim 2 wherein the oxygen free water formed during step (b) is recycled in step (a). 제3항에 있어서, 단계(b)동안에 형성된 산소가 없는 물이 단계(a)에서 재순환됨을 특징으로 하는 방법.4. The method of claim 3 wherein the oxygen free water formed during step (b) is recycled in step (a). 제4항에 있어서, 단계(b)동안에 형성된 산소가 없는 물이 단계(a)에서 재순환됨을 특징으로 하는 방법.5. The method of claim 4, wherein the oxygen free water formed during step (b) is recycled in step (a). 제1항에 있어서, 단계(b)가 주변온도에서 일어남을 특징으로 하는 방법.The method of claim 1 wherein step (b) occurs at ambient temperature. 제4항에 있어서, 단계(b)가 주변온도에서 일어남을 특징으로 하는 방법.5. The method of claim 4 wherein step (b) occurs at ambient temperature. 제1항에 있어서, 단계(b)가 단계(a)보다 더 높은 온도에서 일어남을 특징으로 하는 방법.The method of claim 1 wherein step (b) occurs at a higher temperature than step (a). 산소 분자를 산화제로 사용하며, 산화된 탄화수소 생성물을 함유하는 산화물로 탄화수소를 부분 산화하는방법에 있어서, a) 분리된 용기에서 산소수용액을 제조하고; b) 실제량의 산소를 수용액상으로부터 탄화수소상으로 이동하도록 산소수용액을 산화될 액체 탄화수소와 접촉시키고; 그리고 c) 상승된 온도에서 상기의 산소를 함유하는 탄화수소를 산화시키고; 그리고 d) 언급된 생성물과 물 간에 산소를 분배하여 단계(c)의 생성물로부터 비반응된 모든 산소를 역류방식으로 제거하는 단계들로 구성됨을 특징으로 하는 탄화수소의 산화방법.A method of partially oxidizing a hydrocarbon with an oxide containing an oxidized hydrocarbon product, using oxygen molecules as an oxidant, the method comprising: a) preparing an aqueous oxygen solution in a separate vessel; b) contacting the aqueous oxygen solution with the liquid hydrocarbon to be oxidized to transfer the actual amount of oxygen from the aqueous phase to the hydrocarbon phase; And c) oxidizing the oxygen containing hydrocarbon at elevated temperature; And d) partitioning oxygen between the mentioned product and water to remove all unreacted oxygen from the product of step (c) in a countercurrent manner. 제12항에 있어서, 단계(d)에서 언급된 물은 신선한 물임을 특징으로 하는 방법.13. The method of claim 12, wherein the water mentioned in step (d) is fresh water. 제12항에 있어서, 단계(d)에서 언급된 물은 산소가 제거된 공정용수임을 특징으로 하는 방법.13. The process according to claim 12, wherein the water mentioned in step (d) is process water deoxygenated. 제12항에 있어서, 단계(d)에서 생성된 산소-부화된 물은 단계(a)에서 재순환됨을 특징으로 하는 방법.13. The process of claim 12 wherein the oxygen-enriched water produced in step (d) is recycled in step (a). 제13항에 있어서, 단계(d)에서 생성된 산소-부화된 물은 단계(a)에서 재순환됨을 특징으로 하는 방법.The process of claim 13, wherein the oxygen-enriched water produced in step (d) is recycled in step (a). 제14항에 있어서, 단계(d)에서 생성된 산소-부화된 물은 단계(a)에서 재순환됨을 특징으로 하는 방법.The method of claim 14, wherein the oxygen-enriched water produced in step (d) is recycled in step (a). 제12항에 있어서, 단계(c)의 생성물에 함유된 과산화물 및 히드로 과산화물들이 단계(d)의 비반응된 산소를 제거하기 전에 분해됨을 특징으로 하는 방법.13. The process of claim 12 wherein the peroxide and hydroperoxides contained in the product of step (c) are decomposed before removing the unreacted oxygen of step (d). 제12항에 있어서, 단계(c)의 생성물에 함유된 과산화물 및 히드로 과산화물들이 분해되고, 결과되는 혼합물이 단계(d)에 따라 처리된 탄화수소 부분만을 갖는 탄화수소 및 탄화수소 산화물 부분들로 분리되는 것을 특징으로 하는 방법.13. The peroxide and hydroperoxides contained in the product of step (c) are decomposed and the resulting mixture is separated into hydrocarbon and hydrocarbon oxide parts having only the hydrocarbon part treated according to step (d). How to. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019890007062A 1988-05-26 1989-05-26 Process for oxidation of hydrocarbon utilizing partitioning oxidizing gas KR970002035B1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US199844 1988-05-26
US07/199,844 US5068464A (en) 1988-05-26 1988-05-26 Process for the oxidation of hydrocarbons utilizing partitioning of oxidizing gas
US199,844 1988-05-26

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KR890017209A true KR890017209A (en) 1989-12-15
KR970002035B1 KR970002035B1 (en) 1997-02-21

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CN (1) CN1038086A (en)
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CN1038086A (en) 1989-12-20
KR970002035B1 (en) 1997-02-21

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