Sk Innovation Co., Ltd.

Sk Lubricants Co., Ltd.

Sk Energy Co., Ltd.

Korea Advanced Institute of Science and Technology

Yonsei University

Sk Enmove Co., Ltd.

Sk Innovation Co., Ltd. and Sk Enmove Co., Ltd.

Do Woan Kim

Seung Hoon Oh

Gyung Rok Kim

Seung Woo Lee

Sun Woong Choi

Tae Jin Kim

Kyung Seok Noh

Jae Wook Ryu

Sang Il Lee

Yoon Kyung Lee

Do Kyoung Kim

Sang Hun Oh

Seon Ju Lim

Hee Jung Jeon

Eun Kyoung Kim

Yong Seung Kim

Jae Suk Choi

Hong Chan Kim

Ju Hwan Im

Jin Hee Ok

Cheol Joong Kim

Jae Suk Koh

Min Kee Choi

Jae Hyuk Lee

Yo Han Kim

Sung Won Kim

Dae Hyun Choo

Ju Hyun Lee

Hyuck Lee

Young Moo Park

Chang Kuk Kim

Jong Hyung Lee

Chang Ha Lee

Joong Min Park

Sam Ryong Park

Jin Kyu Choi

Do Hyoun Kim

Il Yong Jeong

Young Wook Jeon

Byoung In Lee

Tae Hong Seok

Kyung Jong Oh

Sung Bum Park

Sin Young Kang

Jae Hyun Koh

Bum Suk Chun

Byung Won Yoon

Yoon Mang Hwang

Jee Sun Shin

Chang Woo Joo

Ha Na Song

Hong Seok Jung

Sang Heup Moon

Myoung Han Noh

Woo Kyung Kim

Sam Ryong Pakr

Cheol Woo Park

Kyung Soo Jun

Han Seung Pan

Tae Won Uhm

Sang Jun Ju

Seong Han Song

Young Hwan Chu

Woo Young Kim

A Ra Cho

Hyuck Jae Lee

Jong Hee Song

Proposed is a process of producing a high-quality lube base oil using a refined oil fraction obtained from waste lubricant as a feedstock. The process includes purifying waste lubricant to obtain a refined oil fraction, pretreating the refined oil fraction, and blending the pretreated refined oil fraction with unconverted oil (UCO), before or after vacuum distillation and catalytic dewaxing of the unconverted oil, or between the vacuum distillation and the catalytic dewaxing of the unconverted oil.

Process of producing high-quality lube base oil by using refined oil fraction of waste lubricant

A process for reducing haze in a heavy base oil includes: obtaining a first effluent oil by contacting a hydrocarbon feedstock with a first catalyst including a zeolite of the ZSM-12 family; and obtaining a second effluent oil by contacting the first effluent oil with a second catalyst including a zeolite of the ZSM-48 family. A hydroisomerization catalyst system having reduced haze includes: a first catalytic region having a first catalyst disposed therein, the first catalyst including a zeolite of the ZSM-12 family; and a second catalytic region having a second catalyst disposed therein, the second catalyst including a zeolite of the ZSM-48 family. The first catalytic region is disposed upstream of the second catalytic region.

Process for reducing haze in heavy base oil and hydroisomerization catalyst system having reduced haze

This invention relates to a hydrogen spillover-based catalyst and use thereof, wherein a hydrogen activation metal cluster is dispersed in the form of being encapsulated in a crystalline or amorphous aluminosilicate matrix which is partially or fully structurally collapsed zeolite, thereby exhibiting high hydroprocessing or dehydrogenation activity and suppressed C&#x2014;C hydrogenolysis activity.

Catalyst containing metal cluster in structurally collapsed zeolite, and use thereof

Disclosed herein is a catalyst for producing biodiesel, including a carrier having water resistance and an active component supported on the carrier and used in a hydrotreating reaction or a decarboxylation reaction. Since the catalyst for producing biodiesel includes a carrier having strong water resistance, the deactivation of the catalyst due to the water produced through a process of producing HBD can be prevented, thus remarkably improving the long term stability of a catalyst.

Catalyst for producing hydrogenated biodiesel and method of producing the same

Disclosed herein is a method of making activated EU-2 zeolite, including: pores having a diameter of 30 to 40 &#x212b; while maintaining the crystal structure of the EU-2 zeolite; and pores having a diameter of 40 to 200 &#x212b;, wherein the volume of the pores having a diameter of 30 to 40 &#x212b; is 0.01 to 0.06 cc/g, and the volume of the pores having a diameter of 40 to 200 &#x212b; is 0.07 to 0.4 cc/g.

Method of preparing an activated EU-2 zeolite

Disclosed herein is an activated EU-2 zeolite, including: pores having a diameter of 30 to 40 &#x212b; while maintaining the crystal structure of the EU-2 zeolite; and pores having a diameter of 40 to 200 &#x212b;, wherein the volume of the pores having a diameter of 30 to 40 &#x212b; is 0.01 to 0.06 cc/g, and the volume of the pores having a diameter of 40 to 200 &#x212b; is 0.07 to 0.4 cc/g.

Activated EU-2 zeolite and use thereof

Specific embodiments of the present invention provide a hydrocracking process for converting low value-added heavy hydrocarbon distillates into high value-added hydrocarbon distillates using a supercritical solvent as a medium.

Hydrocracking process of heavy hydrocarbon distillates using supercritical solvent

This invention relates to a hydrocracking catalyst for preparing valuable light aromatic hydrocarbons from polycyclic aromatic hydrocarbons derived from oil, which includes (i) beta-zeolite, (ii) pseudo-boehmite, and (iii) one or more metals selected from among metals of Groups VIII and VIB, and which further includes a cocatalyst component, thereby producing a maximum amount of BTX (Benzene, Toluene, Xylene) from LCO (Light Cycle Oil).

Hydrocracking catalyst for preparing valuable light aromatic hydrocarbons from polycyclic aromatic hydrocarbons

Provided is a method for reducing the amount of organic acids in a hydrocarbon oil fraction by hydrogenating the organic acids in the hydrocarbon oil fraction under mild conditions. Provided is a new method able to overcome the problem of organic-acid-induced corrosion during the process of distillation, by using hydrogen or a hydrogen-containing mixed gas and a hydrogenation catalyst to subject the organic acids in the hydrocarbon oil fraction to hydrogenation at an appropriate temperature and pressure, thereby converting the same to hydrocarbons and so reducing the amount of organic acids in the hydrocarbon oil fraction.

Method for reducing the amount of organic acids in a hydrocarbon oil fraction

Disclosed herein is a method of simultaneously removing sulfur and mercury from a hydrocarbon material, including: hydrotreating the hydrocarbon material containing sulfur and mercury in the presence of a catalyst including a metal supported with a carrier to convert sulfur into hydrogen sulfide, and adsorb mercury on a metal active site or a carrier of the catalyst in the form of mercury sulfide.

Method of simultaneously removing sulfur and mercury from hydrocarbon material using catalyst by means of hydrotreating reaction

This invention relates to a method of producing aromatics and light paraffins from hydrocarbonaceous oils derived from oil, coal or wood, including partially saturating and hydrocracking the oils derived from oil in a hydrogenation and reaction area, separating them depending on the number of carbons, recirculating heavy oils having 11 or more carbons to the hydrogenation and reaction area, feeding oils suitable for producing BTX to an aromatic separation process and a transalkylation process to recover aromatics, and feeding hydrocarbonaceous components having 5 or fewer carbons to a light separation process, thus obtaining light paraffins.

Method for producing valuable aromatics and light paraffins from hydrocarbonaceous oils derived from oil, coal or wood

The present invention relates to a method of producing aromatic products (benzene/toluene/xylene) and olefin products from petroleum fractions obtained by fluid catalytic cracking, and, more particularly, to a method of producing products comprising high-concentration aromatic products and high value-added light olefin products from light cycle oil obtained by fluid catalytic cracking.

Method for producing high value aromatics and olefin from light cycle oil produced by a fluidized catalytic cracking process

Disclosed is a method of simultaneously manufacturing high quality naphthenic base oil and heavy base oil using a single catalyst system, by subjecting an oil fraction (slurry oil or light cycle oil) produced by fluid catalytic cracking and an oil fraction (deasphalted oil) produced by solvent deasphalting to hydrotreating, catalytic dewaxing and hydrofinishing of the single catalyst system, thereby obtaining not only products having low viscosity but also heavy base oil products (150BS) having high viscosity which was impossible to obtain using a conventional catalytic reaction process, and also thereby producing base oil products having different properties using the single catalyst system, thus generating economic benefits and exhibiting superior efficiency.

Method of simultaneously manufacturing high quality naphthenic base oil and heavy base oil

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Daejeon, South Korea

Do Woan Kim