C5 C6 fractions isomerization isomalk 2
Pentane-hexane fractions isomerization technology Isomalk-2 is a unique Russian development in the sphere of light naphtha isomerization. The technology efficiency is proved on 10 commercial units. The process was first implemented in 2003 on a converted reforming unit at JSC Ufaneftekhim. Designing and construction of Isomalk-2 units in Russia and other countries are in progress.
Specific feature of the technology is application of SI-2 catalyst, which ensures process behavior in low temperature area of 120-180°C, which is thermodynamically favorable for isomerization of paraffin hydrocarbons, and possesses increased tolerance to catalytic poisons — water, sulfur, nitrogen.
SI-2 catalyst restores its activity in short-term water skip-ups up to 100 ppm and sulfur up to 5 ppm.
SI-2 catalyst is manufactured according to TU (Technical Specifications) 2177-009-04706192-00 revision No. 8 at own production site in Nizhny Novgorod. The catalyst is supplied only by SIE Neftehim, LLC.
Concerning the basic specifications of SI-2 catalyst, Isomalk-2 technology involves pre-treatment of feed, but unlike chlorinated catalysts, it does not require special adsorptive treatment of hydrogenate to remove sulfur, nitrogen, and water impurities. Necessary requirements of impurities content are met by simple hydrotreatment and stripping of unstable hydrogenate. Reactor section of Isomalk-2 involves one or two reactors with cooling the reactor effluent in a heat exchanger. If one reactor is used, cool hydrogen gas quench is necessary at the second catalyst bed inlet.
Necessity of cooling the reactor effluent is not so much due to exothermic nature of isomerization reactions, but rather because of significant exothermicity of benzene saturation in feed. Therefore, unit process flow diagram depends on feed composition. Isomalk-2 technology allows processing pentane-hexane fractions, containing considerable amounts of benzene (up to 5-8%) and C7 hydrocarbons – up to 10%. However, specific process solutions are to be applied in such cases.
Specific features of isomerization catalyst SI-2 are the following:
- Isomerization activity of SI-2 catalyst is much higher than that of zeolite catalysts and is as good as that of chlorinated ones;
- SI-2 catalyst is tolerant to catalytic poisons, the catalyst restores its activity even after short-time water skip-ups up to 100 ppm and sulfur skip-ups up to 5 ppm;
- Supply of acid reactants is not required and thus there is no off gas alkalization block;
- High yield of commercial isomerate – 97-99%;
- SI-2 catalyst service life is 10-12 years.
Octane number of Isomalk-2 isocomponent product is mainly defined by selection of process scheme.
COMMERCIAL UNITS REVAMP EXPERIENCE FOR ISOMALK-2 TECHNOLOGY IMPLEMENTATION
JSC UFANEFTEKHIM, RUSSIA
L-35-5/300 reforming unit conversion to Isomalk-2 isomerization process
The unit at JSC Ufaneftekhim is the first commercial unit where Isomalk-2 technology for C5-C6 fractions isomerization process was introduced. The unit was commissioned in October, 2003.
Initially L-35-5 reforming unit was converted for isomerization process under “once-through" scheme with pre-hydrotreatment on the unit L-24/300-1. Due to high space velocity (3.5-4.0 h-1) this unit produced isomerate with 79-80 RON and has 300 KTA capacity.
Conversion included re-piping of isomerization feed furnace; “quench” line installation, inclusion of recycle hydrogen gas drying section with NaA adsorbent (consists of two drying adsorbers and furnace for adsorbent regeneration), SI-2 catalyst loading into 2 reactors.
In June, 2008 the unit was revamped to increase feed capacity and to convert to scheme with unreacted hexanes recycle.
In August, 2011 SI-2 catalyst was regenerated and additional quantity of fresh catalyst (6.5 tons) was loaded to reactor R-3.
In December, 2012 the unit was revamped, including additional equipping with deisopentanization section for separation of isopentane fraction (as an overhead product) and pentane fraction (as a side cut), and construction of new furnace F-1 with one pass heating before reactor R-1.
2012 revamp allowed increasing the unit product octane number up to 90-91 RON at space velocity of 2.4-2.8 h-1 and increasing the capacity up to 500 KTA.
JSC RYAZAN OIL REFINING COMPANY, RUSSIA
The unit conversion from SI-1 zeolite catalyst to SI-2 oxide catalyst
In 1999 JSC Ryazan Oil Refining Company commissioned the first isomerization unit under Russian technology called Isomalk-1. “Detol” isomerization unit was operated over SI-1 zeolite catalyst.
In August, 2005 the unit was converted to Isomalk-2 technology over SI-2 oxide catalyst. The revamp involved replacement of zeolite catalyst by low-temperature oxide SI-2 catalyst, implementation of scheme with make-up hydrogen gas supply through dryer, “quench” line installation, re-piping of the dryer from compressors discharge to suction, and construction of new hydrotreatment section for feed pre-hydrotreating.
First catalyst regeneration was made in 2009. Current service cycle is 4 years. The unit produces 400 KTA of isomerate.
The conversion of isomerization unit to SI-2 catalyst allowed decreasing the process temperature up to 130-140 °С and achieving isomerate octane number up to 83 RON that is 6 numbers higher than zeolite catalyst performances.
KINEF LTD., RUSSIA
Conversion of L-35-11/300 reforming unit to Isomalk-2 technology under “once-through” scheme
In 2005 L-35 -11/300 reforming unit, operated earlier over isoselectoforming technology, was converted to “once-through” low-temperature isomerization process using SI-2 oxide catalyst. Unit revamp included F-1 furnace and reactors re-piping; additional equipping of operating F-1 furnace sections with pilot burners, having flame alarms; hydrogen gas supply line installation to reactors inlet; additional cooler installation on hydrogen gas supply line to reactors; stripper reflux drum replacement, and re-piping of drying adsorbers.
In 2008 the unit revamp was performed that involved regeneration of KGM-70 hydrotreating catalyst and equipment replacement in hydrotreatment section because of physical depreciation.
In 2012 the unit turnaround was performed without SI-2 catalyst regeneration.
The conversion of isomerization unit to SI-2 catalyst allowed increasing the isomerate octane number by 7-8 numbers that significantly enhanced operating efficiency of KINEF, LTD.
From the time of the unit start-up in October, 2005 until the present time SI-2 catalyst has not been regenerated, and RON of produced isomerate keeps the level of 82-83 (at the start of run RON is 83-84), the capacity is 500 KTA.
S.C. PETROTEL-LUKOIL S.A., ROMANIA
Unit conversion from LPI-100 catalyst to SI-2 catalyst
In December, 2006 pentane-hexane fractions isomerization unit, operating before under Parisom technology over LPI-100 catalyst, was reloaded to SI-2 catalyst without revamp. The catalyst was replaced in two reactors; space velocity in reactor section was 2 h-1.
The unit operates under Isomalk-2 technology with feed deisopentanization and low-branched hexanes recycle. The unit capacity is 180 KTA. RON of isopenatane fraction is 93, RON of isomerate is 86-87.
In February, 2013 the unit was shut down for turnaround with isomerization reactors replacement, therefore the catalyst was regenerated. 6 years and 2 months had passed since the time of the start-up until the first regeneration.
The unit conversion to Isomalk-2 technology allowed increasing the octane number of isocomponents mixed fraction by 3-4 numbers and proved high activity of SI-2 catalyst in comparison with analogue oxide catalysts.
JSC NOVOIL, RUSSIA
Isomerization unit conversion from zeolite catalyst to SI-2 catalyst
Isomerization unit at Novo-Ufimsky Refinery is represented by section 300 of L-35-11-1000 unit, converted to isomerization process in 1997.
Initially the unit was commissioned under “once-through” scheme, and isomerization process was performed over zeolite catalyst. Hydrotreatment was performed at section 100 (feed treatment section of L-35-11-1000 unit).
At the first stage the revamp came down to re-piping and reloading the reactor section. Subsequently the unit has been equipped with deisohexanization column.
In February, 2009 the isomerization unit was converted to Isomalk-2 with low-branched hexanes recycle (DIH).
The revamp included replacement of zeolite catalyst by low-temperature oxide catalyst SI-2, inclusion H2 gas recycle drying section into the scheme, installation of reactor section emergency blow-down scheme, and replacement of isomerization reactors internals.
In November, 2012 revamp was performed, that involved internals replacement in hydrotreating section stripper and isomerization and reforming feed treatment column, as well as deisopentanization (DIP) section installation at absorbing gas fractionating unit AGFU-1.
The unit conversion to SI-2 catalyst allowed producing the isomerate octane number of 87-88 RON which is 7-8 numbers higher than that of zeolite catalyst.
LUKOIL-VOLGOGRADNEFTEPERERABOTKA Ltd., RUSSIA
Reforming unit revamp
In December, 2011 JSC SIE Neftehim developed Design Basis (Process Design Regulations) for conversion of L-35-11/300/400-95N catalytic reforming unit at Lukoil-Volgogradneftepererabotka Ltd. to light naphtha isomerization process. It is under design now.
The isomerization unit will include feed pre-hydroteatment section, and Isomalk-2 isomerization section with low-branched hexanes recycle.
In the process of unit revamp the maximal using of existing equipment is provided.
The isomerization section feed will be IBP-75°С fraction with C7+ hydrocarbons content up to 3.0 wt. % and benzene up to 1.5 wt. %. This fraction is produced at gasoline re-distillation unit No.7 and Crude Desaulter/CDU-1 (after construction completing).
After revamp guaranteed isocomponent octane number will be 86-88 RON at space velocity of 2.5 h-1 and with yield of not less than 96 wt. %. The unit capacity is 300 KTA.
ISOMALK-2 NEW COMPLEXES
JSC GAZPROMNEFT–OMSK REFINERY, RUSSIA
New isomerization unit under scheme with feed deisopentanization, pentanes and low-branched hexanes recycle has been designed under license of JSC SIE Neftehim. It is the largest isomerization unit under Isomalk-2 technology. It is the first national unit that was designed and constructed according to the Russian technology from start to finish.
JSC SIE Neftehim provided Engineering Design Basis for the unit in 2007.
Designing and engineering documentation was elaborated by JSC Neftechimproekt, Saint-Petersburg, under the supervision of JSC SIE Neftehim.
General design contractor is JSC OMSKNEFTECHIMPROEKT.
The unit engineering and construction were performed in a uniquely short period - 3 years. This became possible because engineering documentation elaboration and procurement of long-lead equipment were carried out as early as during designing stage. Moreover, design engineering was not suspended even under complex economical circumstances in the country.
800 KTA capacity unit start-up took place in November, 2010.
Isomalk-2 unit at Omsk Refinery allows producing isopentane fraction with octane number of 92-93 numbers and light isohexane fraction with octane number up to 92.5 RON.
JSC SLAVNEFT–YANOS, RUSSIA
The new isomerization unit with throughput of 720 KTA besides isomerization section includes feed pretreatment and pentane-hexane fraction prehydrotreatment sections. Naphtha isomerization is performed under feed deisopentanization and low-branched hexanes recycle process scheme.
The unit was designed by JSC Neftechimproekt, Russia, Saint- Petersburg.
Design Basis was provided by JSC SIE Neftehim in 2007.
The fist construction stage had been finished by 2009.
Author supervision was carried out, FEED and Detailed Engineering Documentation for equipment, as well as process regulations were approved. Equipment procurement and the unit construction had been completed by August, 2011.
The long terms of the unit construction were conditioned with construction suspension due to complex economic situation.
Start-up was performed in October, 2011.
The unit produces hexane isocomponent with octane number of 89-89.5 and isopentane fraction with 92-93 RON.
JSC SARATOV REFINERY, RUSSIA
In view of the necessity to bring commercial motor gasolines quality into compliance with Euro-4 the refinery management made a decision to introduce isomerization process. Feed of the isomerization unit hydrotreatment section is straight-run fraction IBP-70°С from gasoline re-destillation section at Crude Desalter-CDU.
Design Basis was developed by JSC SIE Neftehim in March, 2008.
In 2008 JSC NEFTECHIMPROEKT carried out FEED stage.
The whole engineering process was carried out under strict control of the Licensor.
Start-up of the unit was conducted in March, 2013.
Feed unit capacity is 300 KTA. Isomerization process proceeds under the scheme with feed deisopentanization, n-pentane and low-branched hexanes recycle. The unit produces isocomponent with octane number of 91.5-92.5.
BUSINESS UNIT KOGALYMNEFTEGAZ REFINERY, RUSSIA
In September 2016, a small-scale isomerization unit Isomalk-2 was started-up.
The design works were carried out by Lukoil-Nizhegorodnefteorgsintez Ltd.
The unit was designed and constructed with the participation of SIE Neftehim, LLC. The unit composition includes a hydrotreating section and a fractionation section. Hydrotreated fraction (IBP-70 °C) is isomerized according to the scheme with low-branched hexanes recycle to obtain isomerate having no less than 88 RON.
The unit feed (straight-run naphtha mixture) capacity is 15 KTA.