{"id":53032,"date":"2025-10-21T14:27:12","date_gmt":"2025-10-21T12:27:12","guid":{"rendered":"https:\/\/ins.lukasiewicz.gov.pl\/?page_id=53032"},"modified":"2026-06-30T11:19:48","modified_gmt":"2026-06-30T09:19:48","slug":"catalyst-research-group","status":"publish","type":"page","link":"https:\/\/ins.lukasiewicz.gov.pl\/en\/about-us\/research-groups\/catalyst-research-group\/","title":{"rendered":"Catalyst Research Group"},"content":{"rendered":"\t\t<div data-elementor-type=\"wp-page\" data-elementor-id=\"53032\" class=\"elementor elementor-53032 elementor-47366\" data-elementor-post-type=\"page\">\n\t\t\t\t<div class=\"elementor-element elementor-element-eb6344c e-flex e-con-boxed e-con e-parent\" data-id=\"eb6344c\" data-element_type=\"container\" data-e-type=\"container\">\n\t\t\t\t\t<div class=\"e-con-inner\">\n\t\t\t\t<div class=\"elementor-element elementor-element-f195863 elementor-widget elementor-widget-text-editor\" data-id=\"f195863\" data-element_type=\"widget\" data-e-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<h2>Business Profile<\/h2>\n<ul>\n  <li aria-level=\"1\">Catalysts and sorbents for processes to obtain synthesis gases:\n    <ul>\n      <li aria-level=\"1\">Purification of raw materials (HDS catalysts, selective sorbents for sulfur and chlorine compounds),<\/li>\n      <li aria-level=\"1\">Steam reforming of hydrocarbons, steam conversion of CO, methanation of <sub>COx<\/sub>,<\/li>\n      <li aria-level=\"1\">Processing of coal and biomass gasification products.<\/li>\n    <\/ul>\n  <\/li>\n  <li>Catalysts for the synthesis of ammonia and methanol.<\/li>\n  <li>Catalysts for benzene and fat hydrogenation.<\/li>\n  <li>Catalysts for environmental processes, e.g. <sub>N2O<\/sub>decomposition, selective <sub>NOx<\/sub> reduction.<\/li>\n  <li>Media and inert materials.<\/li>\n  <li>Active aluminum and zinc oxides.<\/li>\n  <li>Zeolite materials.<\/li>\n  <li>Designing formulas and recipes for catalytic materials based on recycled raw materials from various industries, with particular emphasis on metallurgical waste, metallic waste from batteries and batteries, and spent catalysts and industrial sorbents.<\/li>\n<\/ul>\n\n<h2>Apparatus<\/h2>\n<strong>Preparation and formation of catalysts:<\/strong>\n<ul>\n  <li>Laboratory kits for obtaining catalytic materials by impregnation and co-precipitation methods with control of process parameters (HWS reactors).<\/li>\n  <li>Laboratory kit for filtration of catalytic materials (HWS).<\/li>\n  <li>Laboratory kit for controlled hydrothermal synthesis of catalytic materials (Buchi reactors).<\/li>\n  <li>A kit for controlled application of active phase precursors by spray impregnation on carriers.<\/li>\n  <li>Apparatus for thermal processing of catalytic materials (high-temperature furnaces).<\/li>\n  <li>Apparatus for the formation of catalytic materials: laboratory extruders and tableting machines.<\/li>\n  <li>A kit for forming materials using the disc granulation method.<\/li>\n  <li>Retsch AS 200 vibrating screen.<\/li>\n<\/ul>\n\n<strong>Evaluation of physical and chemical properties of materials:<\/strong>\n<ul>\n  <li>Panalytical Empyrean X-ray diffractometer with HTK-16N high-temperature camera.<\/li>\n  <li>Micromeritics Autopore IV 9510 mercury porosimeter.<\/li>\n  <li>Micromeritics ASAP 2050 Extended Pressure sorption analyzer.<\/li>\n  <li>Kit for catalyst characterization by temperature-programmed methods (TPR, TPD, TPO)\/MS Micromeritics AutoChem 2950 HP.<\/li>\n  <li>Netzsch STA 449 F3 Jupiter TG-DTA\/MS thermal analysis kit.<\/li>\n  <li>Apparatus for determining mechanical strength: Tinius Olsen H10K-S.<\/li>\n  <li>Erweka TAR material brittleness and abrasion testing apparatus.<\/li>\n<\/ul>\n\n<strong>Composition studies of gaseous and liquid samples:<\/strong>\n<ul>\n  <li>Agilent GC-FID\/FPD\/MS, Shimadzu GC-FID\/MS, Shimadzu GC dualFID chromatographs.<\/li>\n<\/ul>\n\n<strong>Non-pressure and pressure plants for kinetic studies (steam reforming, steam CO conversion, <sub>COx<\/sub> methanation, methanol and ammonia synthesis, benzene hydrogenation,<sub>H2S<\/sub>sorption):<\/strong>\n<ul>\n  <li>Non-gradient reactors with stirring (400-800\u00b0C &#8211; depending on the process).<\/li>\n  <li>Tiomkin-type pressure reactors (10-100 bar, 150-500\u00b0C &#8211; depending on the process).<\/li>\n  <li>Differential reactor for ammonia synthesis with pre-contacting for testing at pressures up to 150 bar and temperatures up to 520\u00b0C.<\/li>\n  <li>Pressure autoclave for liquid-phase process research.<\/li>\n<\/ul>\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\t\t<\/div>\n\t\t<div class=\"elementor-element elementor-element-0c2680b e-flex e-con-boxed e-con e-parent\" data-id=\"0c2680b\" data-element_type=\"container\" data-e-type=\"container\">\n\t\t\t\t\t<div class=\"e-con-inner\">\n\t\t\t\t<div class=\"elementor-element elementor-element-e9709ca elementor-widget elementor-widget-heading\" data-id=\"e9709ca\" data-element_type=\"widget\" data-e-type=\"widget\" data-widget_type=\"heading.default\">\n\t\t\t\t<div class=\"elementor-widget-container\">\n\t\t\t\t\t<h2 class=\"elementor-heading-title elementor-size-default\">Manager<\/h2>\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t<div class=\"elementor-element elementor-element-c0ca7e6 e-con-full e-flex e-con e-child\" data-id=\"c0ca7e6\" data-element_type=\"container\" data-e-type=\"container\">\n\t\t<div class=\"elementor-element elementor-element-01036ae e-con-full e-flex e-con e-child\" data-id=\"01036ae\" data-element_type=\"container\" data-e-type=\"container\">\n\t\t\t\t<div class=\"elementor-element elementor-element-058c84a elementor-view-default elementor-widget elementor-widget-icon\" data-id=\"058c84a\" data-element_type=\"widget\" data-e-type=\"widget\" data-widget_type=\"icon.default\">\n\t\t\t\t<div class=\"elementor-widget-container\">\n\t\t\t\t\t\t\t<div class=\"elementor-icon-wrapper\">\n\t\t\t<div class=\"elementor-icon\">\n\t\t\t<i aria-hidden=\"true\" class=\"far fa-user\"><\/i>\t\t\t<\/div>\n\t\t<\/div>\n\t\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t<div class=\"elementor-element elementor-element-7f2157d elementor-widget elementor-widget-text-editor\" data-id=\"7f2157d\" data-element_type=\"widget\" data-e-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><strong>Dr. Katarzyna Antoniak-Jurak<\/strong><\/p>\t\t\t\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t<div class=\"elementor-element elementor-element-20a95de e-con-full e-flex e-con e-child\" data-id=\"20a95de\" data-element_type=\"container\" data-e-type=\"container\">\n\t\t\t\t<div class=\"elementor-element elementor-element-793cae0 elementor-view-default elementor-widget elementor-widget-icon\" data-id=\"793cae0\" data-element_type=\"widget\" data-e-type=\"widget\" data-widget_type=\"icon.default\">\n\t\t\t\t<div class=\"elementor-widget-container\">\n\t\t\t\t\t\t\t<div class=\"elementor-icon-wrapper\">\n\t\t\t<div class=\"elementor-icon\">\n\t\t\t<i aria-hidden=\"true\" class=\"far fa-envelope\"><\/i>\t\t\t<\/div>\n\t\t<\/div>\n\t\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t<div class=\"elementor-element elementor-element-84b9b8e elementor-widget elementor-widget-text-editor\" data-id=\"84b9b8e\" data-element_type=\"widget\" data-e-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><a href=\"mailto:Katarzyna.Antoniak-Jurak@ins.lukasiewicz.gov.pl\">Katarzyna.Antoniak-Jurak@ins.lukasiewicz.gov.pl<\/a><\/p>\t\t\t\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t<div class=\"elementor-element elementor-element-0e202a8 e-con-full e-flex e-con e-child\" data-id=\"0e202a8\" data-element_type=\"container\" data-e-type=\"container\">\n\t\t\t\t<div class=\"elementor-element elementor-element-fb96b3c elementor-view-default elementor-widget elementor-widget-icon\" data-id=\"fb96b3c\" data-element_type=\"widget\" data-e-type=\"widget\" data-widget_type=\"icon.default\">\n\t\t\t\t<div class=\"elementor-widget-container\">\n\t\t\t\t\t\t\t<div class=\"elementor-icon-wrapper\">\n\t\t\t<div class=\"elementor-icon\">\n\t\t\t<i aria-hidden=\"true\" class=\"fas fa-phone-alt\"><\/i>\t\t\t<\/div>\n\t\t<\/div>\n\t\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t<div class=\"elementor-element elementor-element-ac5b5b5 elementor-widget elementor-widget-text-editor\" data-id=\"ac5b5b5\" data-element_type=\"widget\" data-e-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><a href=\"tel:(81) 473 17 54\">(81) 473 17 54<\/a><\/p>\t\t\t\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t\t\t<\/div>\n\t\t","protected":false},"excerpt":{"rendered":"<p>Business Profile Catalysts and sorbents for processes to obtain synthesis gases: Purification of raw materials (HDS catalysts, selective sorbents for sulfur and chlorine compounds), Steam reforming of hydrocarbons, steam conversion of CO, methanation of COx, Processing of coal and biomass gasification products. Catalysts for the synthesis of ammonia and methanol. Catalysts for benzene and fat [&hellip;]<\/p>\n","protected":false},"author":230,"featured_media":47551,"parent":53028,"menu_order":0,"comment_status":"closed","ping_status":"closed","template":"","meta":{"_acf_changed":false,"_seopress_titles_title":"","_seopress_titles_desc":"","_seopress_robots_index":"","_seopress_robots_follow":"","_seopress_robots_imageindex":"","_seopress_robots_snippet":"","_seopress_robots_primary_cat":"","_seopress_robots_breadcrumbs":"","_seopress_robots_freeze_modified_date":"","_seopress_robots_custom_modified_date":"","_seopress_robots_canonical":"","_seopress_social_fb_title":"","_seopress_social_fb_desc":"","_seopress_social_fb_img":"","_seopress_social_fb_img_attachment_id":0,"_seopress_social_fb_img_width":0,"_seopress_social_fb_img_height":0,"_seopress_social_twitter_title":"","_seopress_social_twitter_desc":"","_seopress_social_twitter_img":"","_seopress_social_twitter_img_attachment_id":0,"_seopress_social_twitter_img_width":0,"_seopress_social_twitter_img_height":0,"_seopress_redirections_value":"","_seopress_redirections_enabled":"","_seopress_redirections_enabled_regex":"","_seopress_redirections_logged_status":"","_seopress_redirections_param":"","_seopress_redirections_type":0,"_seopress_analysis_target_kw":"","inline_featured_image":false,"footnotes":""},"class_list":["post-53032","page","type-page","status-publish","has-post-thumbnail","hentry"],"acf":{"page_icon":null},"publishpress_future_action":{"enabled":false,"date":"2026-07-09 23:03:10","action":"change-status","newStatus":"draft","terms":[],"taxonomy":"translation_priority","extraData":[]},"publishpress_future_workflow_manual_trigger":{"enabledWorkflows":[]},"_links":{"self":[{"href":"https:\/\/ins.lukasiewicz.gov.pl\/en\/wp-json\/wp\/v2\/pages\/53032","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/ins.lukasiewicz.gov.pl\/en\/wp-json\/wp\/v2\/pages"}],"about":[{"href":"https:\/\/ins.lukasiewicz.gov.pl\/en\/wp-json\/wp\/v2\/types\/page"}],"author":[{"embeddable":true,"href":"https:\/\/ins.lukasiewicz.gov.pl\/en\/wp-json\/wp\/v2\/users\/230"}],"replies":[{"embeddable":true,"href":"https:\/\/ins.lukasiewicz.gov.pl\/en\/wp-json\/wp\/v2\/comments?post=53032"}],"version-history":[{"count":1,"href":"https:\/\/ins.lukasiewicz.gov.pl\/en\/wp-json\/wp\/v2\/pages\/53032\/revisions"}],"predecessor-version":[{"id":53033,"href":"https:\/\/ins.lukasiewicz.gov.pl\/en\/wp-json\/wp\/v2\/pages\/53032\/revisions\/53033"}],"up":[{"embeddable":true,"href":"https:\/\/ins.lukasiewicz.gov.pl\/en\/wp-json\/wp\/v2\/pages\/53028"}],"wp:featuredmedia":[{"embeddable":true,"href":"https:\/\/ins.lukasiewicz.gov.pl\/en\/wp-json\/wp\/v2\/media\/47551"}],"wp:attachment":[{"href":"https:\/\/ins.lukasiewicz.gov.pl\/en\/wp-json\/wp\/v2\/media?parent=53032"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}