KR930004155B1 - Process for treating crude oil - Google Patents

Process for treating crude oil Download PDF

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KR930004155B1
KR930004155B1 KR1019850004542A KR850004542A KR930004155B1 KR 930004155 B1 KR930004155 B1 KR 930004155B1 KR 1019850004542 A KR1019850004542 A KR 1019850004542A KR 850004542 A KR850004542 A KR 850004542A KR 930004155 B1 KR930004155 B1 KR 930004155B1
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crude oil
oil
distillation column
atmospheric distillation
crude
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KR1019850004542A
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Korean (ko)
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KR860001176A (en
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마사야 구노
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마사야 구노
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G7/00—Distillation of hydrocarbon oils
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1048—Middle distillates
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • C10G2300/202—Heteroatoms content, i.e. S, N, O, P

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

내용 없음.No content.

Description

원유(原油)의 신(新)처리방법New treatment method of crude oil

도면은 본 발명에 관한 1실시예의 플로우 차아트.Figure 1 is a flow chart of one embodiment according to the present invention.

* 도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings

1,4 : 원료탱크 2 : 수소하 분리탈황장치(HSP)1,4: Raw material tank 2: Separation desulfurization unit under hydrogen (HSP)

3 : 상압(常壓) 증류탑(topper)3: atmospheric distillation column (topper)

본 발명은 원유를 수소화(化)분리·탈황하는 방법 즉, HSP(Hydrostripping Process)의 개량방법에 관한 것과 동시에 보통의 상압 증류탑의 효율적인 이용방법에 관한 것이다.The present invention relates to a method for hydrocracking and desulfurizing crude oil, that is, a method for improving the HSP (Hydrostripping Process) and at the same time an efficient method for using a normal atmospheric distillation column.

현재에 있어서, 원유는 탈염시킨 후 상압증류탑에 도입되어 분리·정제되어 있으나, 원유는 반드시 전부, 상압증류탑에 있어서 최종제품으로는 되고있지 않을 뿐만아니라 원유의 종류에 따라서 변환운전을 하고, 그때문에 상압증류탑의 가동률을 떨어뜨리고 있었다. 이것은 원유의 종류에 따라 상압증류탑에 있어서 그대로 제품으로되는 것, 안되는 것이 존재하기 때문이며, 최종제품으로 하기 위하여 각종의 수소화처리가 행해지고 있는 것이 실태이다. 특히 경질·양질원유는 그대로 제품으로되는 것이 많은 반면, 중질·고유황 원유등은 이후의 처리를 필요로하기 때문에, 상압 증류탑에서의 상기한 종류의 원유의 동시운전에 의한 정제는 비경제이기 대문에 변환운전을 행하고 있었다.At present, crude oil is desalted and introduced into an atmospheric distillation column to be separated and refined. However, not all crude oil is necessarily the final product in the atmospheric distillation column, and the conversion operation is performed according to the type of crude oil. The operation rate of the atmospheric distillation tower was falling. This is because in the atmospheric distillation column depending on the type of crude oil, there are some products which are or cannot be used as they are, and in fact, various hydrogenation treatments are carried out in order to obtain a final product. In particular, since light and high quality crude oils are often produced as they are, heavy and high sulfur crude oils require further processing, and thus, refinement by simultaneous operation of the above-described types of crude oil in an atmospheric distillation column is not economical. The conversion operation was performed.

본 발명은 이들의 문제를 해결하고, 동시에 상압증류탑에서의 최종제품을 증가시킴과 아울러 상압증류탑의 가동률을 향상시키는 방법을 제공하는 데에있다. 즉 중질원유, 고유황 원유, 고파라피닉 원유등 수소화처리 유분(留分)이 많은 원유는 사전에 수소하 분리 탈황장치를 통하여 중간유분(Middle Distillate)+라이터(Lighter Fraction)를 탈황처리하고, 그 제품의 증류탑으로서 상압증류탑을 이용하여 분리정제한다.The present invention is to solve these problems, and at the same time to provide a method for increasing the final product in the atmospheric distillation column and at the same time improve the operation rate of the atmospheric distillation column. In other words, heavy crude oil such as heavy crude oil, high sulfur crude oil, high paraffinic crude oil, and the like, the crude oil having a large amount of hydrogenated oil is desulfurized by the middle distillate + lighter fraction through a hydrogen-separated desulfurization device. The product is separated and purified using an atmospheric distillation column as a distillation column of the product.

상기한 수소하에서 분리탈황처리한 유분을 그 상압증류탑에 직접통하고 있는 경질·양질원유와의 유뷴과 혼합증류시키는 것에 의하여 최종제품을 증가시키는 것이다. 여기서 말하는 수소하 분리탈황장치로부터의 중간유분+라이터는 탈황처리되어 있기 때문에 경질·양질 원유로부터의 중간유분+라이터보다 양질내지는 손색이 없는 것이며, 따라서 전체적으로 보아 상압증류탑에서의 최종제품은 중량하여서 그 가동률의 향상에 관련되는 것으로 된다. 여기에서 수소하 분리탈황장치에 대하여 설명하면, 본 장치는 HSP라고도 불리우며, 국내외적으로 이미 알려진 것이나, 원유에 수소를 첨가하여 고온·고압하에서 분리하여 경질유분을 첨가수소와 함께 탈황하는 공정이며, 본 방법은 수소화처리를 필요로 하는 유분이 많은 원유의 분리(중간유분+라이터와 증질유분으로 분리)탈황에 이용하는데에 적합한 방법이다. 분리된 중질유분은 다른 적당한 장치로 보내어지게 된다. 즉 본 발명에 의한 원유의 신처리방법이라함은 위치에서 설명한 수소하 분리탈황방법과 기존의 상압증류탑을 경유하는 방법을 종합적으로 결합시킨 것으로서, 이 방법에 의하여The final product is increased by mixing and distilling the oil separated and desulfurized under the above-mentioned hydrogen with the oil and light oil which are directly passed through the atmospheric distillation column. Since the intermediate oil + lighter from the hydrogen-separated desulfurization unit here is desulfurized, it is inferior to the middle oil + lighter from light and high quality crude oil. It will be related to the improvement of the utilization rate. Herein, a description will be given of a separation desulfurization apparatus under hydrogen, which is also known as HSP, and is known at home and abroad, but is a process of desulfurizing light oil with additional hydrogen by adding hydrogen to crude oil and separating it under high temperature and high pressure. This method is suitable for use in the desulfurization of oily crude oil (medium oil + lighter and steam oil) requiring hydrogenation. The separated heavy oil is sent to another suitable device. In other words, the new treatment method of crude oil according to the present invention is a combination of the hydrogen separation and desulfurization method described in the above section and a conventional method of passing through an atmospheric distillation column.

(1) 기존의 상압증류탑의 가동률향상(1) Improvement of operation rate of existing atmospheric distillation tower

(2) 기존의 상압증류탑에서의 최종제품의 중량(2) Weight of final product in existing atmospheric distillation column

(3) 양질 원유 잔사유(殘渣油)와 거칠고 나쁜 원유 잔사유의 분리(3) Separation of good crude oil residues from coarse crude oil residues

(4) 각종 원유를 사용하였을때의 일괄적인 연속운전의 확보등을 달성할수가 있다.(4) It is possible to achieve the continuous continuous operation when various crude oils are used.

도면에 표시한 것은 본 발명의 1실시예인바, 원료탱크(1)에서의 중질·고유황 원유(HS 원유)는 수소하 분리탈황장치(2)로 통한 후 경질중간부분+라이터는 상압증류탑(3)으로 통해지고, 원료탱크(4)에서 공급된 경질원유에서의 유분과 그 상압증류탑내에서 혼합증류분리 정제되어 최정제품으로 된다.Shown in the drawings is an embodiment of the present invention, the heavy and high sulfur crude oil (HS crude oil) in the raw material tank (1) through the separation and desulfurization apparatus under hydrogen (2), the light intermediate portion + lighter is an atmospheric distillation tower ( 3), the oil from light crude oil supplied from the raw material tank 4 and the mixed distillation and purification in the atmospheric distillation column are refined to become the best products.

한편 중질·고유황 원유의 중질유분(H Residue)은 다른 적당한 장치로 보내어져서 처리되고, 경질·양질원유의 중질유분(L Residue)도 다른 적당한 장치로 보내어져서 처리된다. 또한 HSP로부터의 중간유분+라이터의 상압증류탑에의 통하는 방법은 상압증류탑본체, 사이드 스트리피(stripper), 안정장치, 배관등으로 적당하게 나누어서 통하게하는 것도 가능하다.On the other hand, the heavy oil (H Residue) of heavy and high sulfur crude oil is sent to another suitable apparatus for processing, and the heavy oil (L Residue) of light and good crude oil is also sent to another suitable apparatus for processing. The medium distillation + lighter from the HSP to the atmospheric distillation column can be appropriately divided into an atmospheric distillation column main body, a side stripper, a stabilizer, and a piping.

Claims (1)

수소화 처리를 필요로하는 유분이 많은 중질원유·고유황원유의 거칠고 나쁜 원유를 사전에 수소화분리 탈황장치(2)를 통하여 중간유분+라이터를 탈황백유화(白油化)하고, 그 제품의 정제에 경질원유·양질원유를 처리하고 있는 상압 증류탑(3)을 이용하는 것에 의하여, 그 상압증류탑의 가동률을 향상시켜서 그 상압증류탑에 있어서의 최종제품을 중량시키는 원유의 신처리방법.Desulfurization and whitening of the intermediate oil + lighter is carried out in advance through the hydrocracking desulfurization apparatus (2) to coarse and bad crude oils with heavy oil and high sulfur crude oil that require hydrogenation. The new crude oil processing method of using the atmospheric distillation column (3) which processes light crude oil and high quality crude oil to improve the operation rate of the atmospheric distillation column, and to weigh the final product in the atmospheric distillation column.
KR1019850004542A 1984-07-12 1985-06-26 Process for treating crude oil KR930004155B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP59-143358 1984-07-12
JP59143358A JPS6123690A (en) 1984-07-12 1984-07-12 Novel method for treating crude oil

Publications (2)

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KR860001176A KR860001176A (en) 1986-02-24
KR930004155B1 true KR930004155B1 (en) 1993-05-21

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JP (1) JPS6123690A (en)
KR (1) KR930004155B1 (en)
CN (1) CN85105314A (en)
AU (1) AU576254B2 (en)
BR (1) BR8503130A (en)
NO (1) NO166413C (en)

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JPH04183195A (en) * 1990-11-19 1992-06-30 Fujitsu Ltd Amplifier circuit
CN101684414B (en) * 2008-09-27 2013-04-24 中国石油化工股份有限公司 Hydrotreating method of high-acid and high-calcium crude oil
JP5421794B2 (en) * 2010-01-12 2014-02-19 日揮株式会社 Crude oil processing system
JP5421793B2 (en) * 2010-01-12 2014-02-19 日揮株式会社 Crude oil processing system

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JPS5372013A (en) * 1976-12-09 1978-06-27 Lion Corp Process for dispersing coal in oil
JPS55157216A (en) * 1979-05-28 1980-12-06 Hitachi Maxell Ltd Manufacture of magnetic powder for magnetic recording

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CN85105314A (en) 1987-01-14
NO166413C (en) 1991-07-17
KR860001176A (en) 1986-02-24
NO166413B (en) 1991-04-08
AU4483385A (en) 1986-01-16
NO852636L (en) 1986-01-13
JPS6123690A (en) 1986-02-01
AU576254B2 (en) 1988-08-18
BR8503130A (en) 1986-03-18

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