{"id":5735,"date":"2024-08-26T13:25:35","date_gmt":"2024-08-26T13:25:35","guid":{"rendered":"https:\/\/karabau.kz\/?page_id=5735"},"modified":"2024-08-26T13:31:04","modified_gmt":"2024-08-26T13:31:04","slug":"%d1%88%d0%b8%d0%ba%d1%96-%d0%bc%d2%b1%d0%bd%d0%b0%d0%b9%d0%b4%d1%8b-%d1%82%d0%b5%d1%80%d0%b5%d2%a3-%d3%a9%d2%a3%d0%b4%d0%b5%d1%83%d0%b4%d1%96-%d0%bf%d0%b0%d0%b9%d0%b4%d0%b0%d0%bb%d0%b0%d0%bd%d1%83-od","status":"publish","type":"page","link":"https:\/\/karabau.kz\/en\/%d1%88%d0%b8%d0%ba%d1%96-%d0%bc%d2%b1%d0%bd%d0%b0%d0%b9%d0%b4%d1%8b-%d1%82%d0%b5%d1%80%d0%b5%d2%a3-%d3%a9%d2%a3%d0%b4%d0%b5%d1%83%d0%b4%d1%96-%d0%bf%d0%b0%d0%b9%d0%b4%d0%b0%d0%bb%d0%b0%d0%bd%d1%83-od\/","title":{"rendered":"Operation of Deep Crude Oil Processing (ODCOP)"},"content":{"rendered":"<div data-elementor-type=\"wp-page\" data-elementor-id=\"5735\" class=\"elementor elementor-5735\">\n\t\t\t\t\t\t<section class=\"has_ma_el_bg_slider elementor-section elementor-top-section elementor-element elementor-element-ecdd23b elementor-section-boxed elementor-section-height-default elementor-section-height-default jltma-glass-effect-no\" data-id=\"ecdd23b\" data-element_type=\"section\">\n\t\t\t\t\t\t<div class=\"elementor-container elementor-column-gap-default\">\n\t\t\t\t\t<div class=\"has_ma_el_bg_slider elementor-column elementor-col-100 elementor-top-column elementor-element elementor-element-e5e6b6e jltma-glass-effect-no\" data-id=\"e5e6b6e\" data-element_type=\"column\">\n\t\t\t<div class=\"elementor-widget-wrap elementor-element-populated\">\n\t\t\t\t\t\t<div class=\"elementor-element elementor-element-a73d29f jltma-glass-effect-no elementor-widget elementor-widget-text-editor\" data-id=\"a73d29f\" data-element_type=\"widget\" data-widget_type=\"text-editor.default\">\n\t\t\t\t<div class=\"elementor-widget-container\">\n\t\t\t\t\t\t\t\t\t<p><span style=\"font-weight: 400;\">The complex of deep crude oil processing KT-1 starts secondary processes of oil distillation at the refinery. The designed capacity of the complex for vacuum distillation of oil residue is 2,0 million t\/year.<\/span><\/p><p><span style=\"font-weight: 400;\">ODCOP allows producing additional valuable oil products from oil residue: high-octane component of gasolines of grades AI-92-K4, AI-95-K4, and component of hydrotreated diesel fuel, propane-propylene and butane-butylene fraction (feedstock for petroleum chemistry).<\/span><\/p><p><span style=\"font-weight: 400;\">The complex KT-1 is unique in terms of set of process unit:<\/span><\/p><ul><li><span style=\"font-weight: 400;\">\u2022 Vacuum distillation of oil residue, capacity 2,0 million t\/year; \u2022 vacuum gasoil hydrotreating unit, capacity 2,4 million t\/year; \u2022 catalytic cracking unit, capacity 1,868 million t\/year; \u2022 absorption and gas fractionation unit, capacity 1,25 million t\/year; \u2022 fuel gas waste-heat recovery unit; \u2022 hydrogen production unit.<\/span><\/li><\/ul><p><span style=\"font-weight: 400;\">In 20 century, taking into account gathered experience of KT-1 system operation there has been started an extensive modernization of the complex with involving research institutes and design companies in order to extend recovery of light oil products, and to make greater variety of output oil products as well as to enhance environmental situation. As a result of this reconstruction in KT-1 complex the parameter of oil processing depth has been brought up to 84 %, production of high-octane gasoline of grade AI-92 has been launched.<\/span><\/p><p><span style=\"font-weight: 400;\">Within 2020-2022 in \u041a\u0422-1 complex there were significant works performed in terms of replacement of process equipment and improvement of technologies which has allowed increasing output of target products by more than 4,0 %. The overall volume of gasoline is produced with octane number not lower than 92,0 points by research method. Catalytic cracking \u2013 capacity has been increased from 1250 thousand t\/year up to 1868 thousand t\/year; increased output of diesel fraction has been achieved. High quality of oil products is the main parameter of KT-1 performance.<\/span><\/p><p><span style=\"font-weight: 400;\">Characteristic of KT-1 sections<\/span><\/p><p><span style=\"font-weight: 400;\">SECTION 001<\/span><\/p><p><span style=\"font-weight: 400;\">Section 001 the unit of vacuum distillation of oil residue, which is designed for processing mazut by the vacuum distillation method in order to produce:<\/span><\/p><ul><li><span style=\"font-weight: 400;\">\u2022 vacuum distillate \u2013 feed of vacuum gasoil hydrotreating; \u2022 dark product \u2013 component of fuel oil; \u2022 oil tar \u2013 feed of delayed coking unit and bitumen production unit.<\/span><\/li><\/ul><p><span style=\"font-weight: 400;\">SECTION 100<\/span><\/p><p><span style=\"font-weight: 400;\">Section 100 is a vacuum distillate hydrotreating unit, intended for preliminary hydrogenation tempering of feedstock of catalytic cracking for decrease in sulphurous, nitrogenous, oxigenous, metallorganic compounds and polycyclic aromatics with simultaneous decrease in its coking capacity, and also gas treating with monoethanolamine fr om hydrogen sulphide.<\/span><\/p><p><span style=\"font-weight: 400;\">Hydrotreating process of feedstock of catalytic cracking is carried out by traditional production procedure and consists of:<\/span><\/p><ul><li><span style=\"font-weight: 400;\">\u2022 the furnace block, including furnaces for heating of gas mixture before its going into reactors and for unstable hydrogenated feed before its rectification in the atmospheric distillation column; \u2022 the reaction block, where hydrotreating process is carried out and the hydrogenated feed is separated from circulating hydrogeneous and hydrocarbonic gases; \u2022 rectification (stabilisation) section of hydrogenated feed, wh ere hydrogenated feed is cut into gasoline, diesel fuel and the hydrotreated vacuum distillate; \u2022 the block of monoethanolamine treating of gases, where circulating hydrogenous gas, residue gas of catalytic cracking, unstripped gas of visbreaking, propane-propylene fraction and hydrocarbon gas of Section 100 are exposed to purification fr om hydrogen sulphide; \u2022 the alkalizing block of butane-butylene fraction, where at the idle reaction block the stripping column of hydrocarbon gas of visbreaking is used in the clearing circuit of butane-butylene fraction by alkali.<\/span><\/li><\/ul><p><span style=\"font-weight: 400;\">Output products:<\/span><\/p><ul><li><span style=\"font-weight: 400;\">\u2022 hydrotreated vacuum gasoil; \u2022 component of diesel fuel \u2013 feedstock for diesel fuel hydrotreating unit of LK-6U<\/span><\/li><\/ul><p><span style=\"font-weight: 400;\">SECTION 200<\/span><\/p><p><span style=\"font-weight: 400;\">Section 200, included in the combined unit of KT-1, is designed for processing hydrotreated vacuum gasoil into more valuable oil products: high-octane component of motor gasoline, feed for producing liquefied hydrocarbon gas, component of diesel fuel, components of commercial fuel oil, also it includes the reaction block of catalytic cracking, the block of rectification and process condensate treatment, air compressor station.<\/span><\/p><p><span style=\"font-weight: 400;\">For the reaction block the flow diagram of catalytic cracking is accepted as at the unit type G-43-107ML with a direct-flow riser and fluid catalyst of microspherical shape.<\/span><\/p><p><span style=\"font-weight: 400;\">The catalytic cracking of the hydrotreated feed is target-oriented in the set of processes of complex \u041a\u0422-1 and provides for yield of the following products:<\/span><\/p><ul><li><span style=\"font-weight: 400;\">\u2022 unstripped gas and unstable gasoline, used as a feed in the section of absorption and gas fractionation for producing propane-propylene, butane-butylene fractions, dry hydrocarbon gas, high-octane component of motor gasoline (fraction IBP \u2013 205 \u00b0\u0421);<\/span><\/li><\/ul><ul><li><span style=\"font-weight: 400;\">\u2022 light gasoil (fraction 195-340 \u00b0\u0421), used as a component of diesel fuel;<\/span><\/li><\/ul><ul><li><span style=\"font-weight: 400;\">\u2022 fraction above 340 \u00b0\u0421, used as a component of fuel oil.<\/span><\/li><\/ul><p><span style=\"font-weight: 400;\">Rectification of the given cracking products is carried out under the traditional process diagram for all models of catalytic cracking in the rectifying column \u041a-201.<\/span><\/p><p><span style=\"font-weight: 400;\">The reconstructed block of process condensate treatment (as a part of this section) allows upgrading the qualitative composition of condensate up to the standard level before its dumping to treatment facilities of the refinery.<\/span><\/p><p><span style=\"font-weight: 400;\">SECTION 300<\/span><\/p><p><span style=\"font-weight: 400;\">The section of absorption and gasfractionating is intended for absorption, stabilization and fractionation of unstripped gas and unstable gasoline from the catalytic cracking section.<\/span><\/p><p><span style=\"font-weight: 400;\">The section of absorption and gasfractionating consists of the following blocks:<\/span><\/p><ul><li><span style=\"font-weight: 400;\">\u2022 the absorption block, where deethanization and absorption of unstriped gas and unstable gasoline are carried out; absorption process is conducted at the low temperatures with application of water and air cooling that provides for extraction of fraction C3 and above by not less than 80 per cent from potential;<\/span><\/li><\/ul><ul><li><span style=\"font-weight: 400;\">\u2022 the stabilization and fractionation block of top fraction, where stabilization of unstable gasoline is carried out - the saturated absorbent of the block of absorption with separation into stable gasoline and top fraction, which is separated into propane-propylene and butane-butylene fractions.<\/span><\/li><\/ul><p><span style=\"font-weight: 400;\">Output products:<\/span><\/p><ul><li><span style=\"font-weight: 400;\">\u2022 propane-propylene fraction;<\/span><\/li><li><span style=\"font-weight: 400;\"> \u2022 butane-butylene fraction;<\/span><\/li><li><span style=\"font-weight: 400;\"> \u2022 stable gasoline of catalytic cracking \u2013 component of K4 gasoline<\/span><\/li><\/ul><p><span style=\"font-weight: 400;\">.SECTION 400<\/span><\/p><p><span style=\"font-weight: 400;\">Waste Heat Recovery Section is included in Operation of DCOP and it is intended for using heat of secondary energy resources available in the unit in a form of hot flue gases with temperature from 440\u00b0\u0421 up to 600\u00b0\u0421. While normal operation of section there is a steam 12 kgf\/cm2 produced which goes then for process needs of ODCOP.<\/span><\/p><p><br \/><br \/><br \/><br \/><\/p>\t\t\t\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t\t<\/div>\n\t\t<\/div>\n\t\t\t\t\t<\/div>\n\t\t<\/section>\n\t\t\t\t<\/div>","protected":false},"excerpt":{"rendered":"<p>The complex of deep crude oil processing KT-1 starts secondary processes of oil distillation at the refinery. The designed capacity of the complex for vacuum distillation of oil residue is 2,0 million t\/year.<span class=\"more-dots\">&#8230;<\/span> <span class=\"more-tag\"><a class=\"more-link\" href=\"https:\/\/karabau.kz\/en\/%d1%88%d0%b8%d0%ba%d1%96-%d0%bc%d2%b1%d0%bd%d0%b0%d0%b9%d0%b4%d1%8b-%d1%82%d0%b5%d1%80%d0%b5%d2%a3-%d3%a9%d2%a3%d0%b4%d0%b5%d1%83%d0%b4%d1%96-%d0%bf%d0%b0%d0%b9%d0%b4%d0%b0%d0%bb%d0%b0%d0%bd%d1%83-od\/\">Reade More<span class=\"screen-reader-text\"> \"\u0428\u0438\u043a\u0456 \u043c\u04b1\u043d\u0430\u0439\u0434\u044b \u0442\u0435\u0440\u0435\u04a3 \u04e9\u04a3\u0434\u0435\u0443\u0434\u0456 \u043f\u0430\u0439\u0434\u0430\u043b\u0430\u043d\u0443 (ODCOP)\"<\/span><\/a><\/span><!-- .more-tag --><\/p>","protected":false},"author":1,"featured_media":0,"parent":0,"menu_order":0,"comment_status":"closed","ping_status":"closed","template":"","meta":{"footnotes":""},"class_list":["post-5735","page","type-page","status-publish","hentry"],"yoast_head":"<!-- This site is optimized with the Yoast SEO plugin v23.3 - 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