{"id":10593,"date":"2026-07-06T05:15:11","date_gmt":"2026-07-06T05:15:11","guid":{"rendered":"https:\/\/ntgdvalve.com\/?p=10593"},"modified":"2026-07-06T05:56:47","modified_gmt":"2026-07-06T05:56:47","slug":"check-valve-pressure-drop-cv","status":"publish","type":"post","link":"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/","title":{"rendered":"\u041f\u0435\u0440\u0435\u043f\u0430\u0434 \u0434\u0430\u0432\u043b\u0435\u043d\u0438\u044f \u0432 \u043e\u0431\u0440\u0430\u0442\u043d\u043e\u043c \u043a\u043b\u0430\u043f\u0430\u043d\u0435 \u0438 \u043a\u043e\u044d\u0444\u0444\u0438\u0446\u0438\u0435\u043d\u0442 Cv: \u043a\u0430\u043a \u0441\u043e\u043f\u0440\u043e\u0442\u0438\u0432\u043b\u0435\u043d\u0438\u0435 \u043f\u043e\u0442\u043e\u043a\u0443 \u0432\u043b\u0438\u044f\u0435\u0442 \u043d\u0430 \u0432\u044b\u0431\u043e\u0440"},"content":{"rendered":"<p><strong>Author Name:<\/strong> Bruce Zheng<\/p>\n<p><strong>Author Role:<\/strong> Co-Founder and Valve Engineer at NTGD Valve<\/p>\n<p><strong>Author Bio:<\/strong> Bruce Zheng is Co-Founder and Valve Engineer at NTGD Valve, focusing on industrial valve selection, application, and technical content for global B2B buyers.<\/p>\n<p><strong>Last Updated:<\/strong> July 5, 2026<\/p>\n<p>Check valve pressure drop is the pressure difference or energy loss created when fluid passes through a check valve. It is not determined by line size alone. It depends on flow rate, valve design, internal flow path, disc or plate position, medium properties, Cv value, and whether the valve is fully open under real operating conditions.<\/p>\n<p>For industrial piping systems, pressure drop is not only a calculation item. It affects pump head, energy use, stable valve opening, water hammer risk, and final check valve selection. A valve with low catalog pressure drop can still perform poorly in service if the operating flow is too low to hold the valve open, if the cracking pressure is not suitable, or if the valve is installed in disturbed flow.<\/p>\n<p>The practical selection point is simple: pressure drop should be low enough for the system, but the valve must also open stably, close reliably, and match the real operating condition. Final sizing should be checked against the manufacturer\u2019s pressure drop curve, Cv table, head loss chart, or project-specific datasheet.<\/p>\n<p>The article below explains how to separate pressure drop, Cv, head loss, cracking pressure, and type-specific check valve behavior before sending an RFQ or approving a valve for service.<\/p>\n<figure id=\"attachment_10602\" aria-describedby=\"caption-attachment-10602\" style=\"width: 1672px\" class=\"wp-caption aligncenter\"><img fetchpriority=\"high\" decoding=\"async\" class=\"size-full wp-image-10602\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-cv-hero-diagram.png\" alt=\"Check valve pressure drop and Cv hero diagram with flow arrows and \u0394P label\" width=\"1672\" height=\"941\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-cv-hero-diagram.png 1672w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-cv-hero-diagram-768x432.png 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-cv-hero-diagram-1536x864.png 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-cv-hero-diagram-18x10.png 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-cv-hero-diagram-600x338.png 600w\" sizes=\"(max-width: 1672px) 100vw, 1672px\" \/><figcaption id=\"caption-attachment-10602\" class=\"wp-caption-text\">Check valve pressure drop should be reviewed with Cv, head loss, valve type, and stable opening.<\/figcaption><\/figure>\n<div id=\"ez-toc-container\" class=\"ez-toc-v2_0_85 counter-hierarchy ez-toc-counter ez-toc-grey ez-toc-container-direction\">\n<div class=\"ez-toc-title-container\">\n<p class=\"ez-toc-title\" style=\"cursor:inherit\">Table of Contents<\/p>\n<span class=\"ez-toc-title-toggle\"><a href=\"#\" class=\"ez-toc-pull-right ez-toc-btn ez-toc-btn-xs ez-toc-btn-default ez-toc-toggle\" aria-label=\"Toggle Table of Content\"><span class=\"ez-toc-js-icon-con\"><span class=\"\"><span class=\"eztoc-hide\" style=\"display:none;\">Toggle<\/span><span class=\"ez-toc-icon-toggle-span\"><svg style=\"fill: #0a0a0a;color:#0a0a0a\" xmlns=\"http:\/\/www.w3.org\/2000\/svg\" class=\"list-377408\" width=\"20px\" height=\"20px\" viewBox=\"0 0 24 24\" fill=\"none\"><path d=\"M6 6H4v2h2V6zm14 0H8v2h12V6zM4 11h2v2H4v-2zm16 0H8v2h12v-2zM4 16h2v2H4v-2zm16 0H8v2h12v-2z\" fill=\"currentColor\"><\/path><\/svg><svg style=\"fill: #0a0a0a;color:#0a0a0a\" class=\"arrow-unsorted-368013\" xmlns=\"http:\/\/www.w3.org\/2000\/svg\" width=\"10px\" height=\"10px\" viewBox=\"0 0 24 24\" version=\"1.2\" baseProfile=\"tiny\"><path d=\"M18.2 9.3l-6.2-6.3-6.2 6.3c-.2.2-.3.4-.3.7s.1.5.3.7c.2.2.4.3.7.3h11c.3 0 .5-.1.7-.3.2-.2.3-.5.3-.7s-.1-.5-.3-.7zM5.8 14.7l6.2 6.3 6.2-6.3c.2-.2.3-.5.3-.7s-.1-.5-.3-.7c-.2-.2-.4-.3-.7-.3h-11c-.3 0-.5.1-.7.3-.2.2-.3.5-.3.7s.1.5.3.7z\"\/><\/svg><\/span><\/span><\/span><\/a><\/span><\/div>\n<nav><ul class='ez-toc-list ez-toc-list-level-1 ' ><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-1\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#What_Is_Check_Valve_Pressure_Drop\" >What Is Check Valve Pressure Drop?<\/a><ul class='ez-toc-list-level-3' ><li class='ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-2\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Quick_definition_for_industrial_piping_systems\" >Quick definition for industrial piping systems<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-3\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Why_pressure_drop_matters_in_pump_and_process_lines\" >Why pressure drop matters in pump and process lines<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-4\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Why_check_valves_are_different_from_simple_open-bore_valves\" >Why check valves are different from simple open-bore valves<\/a><\/li><\/ul><\/li><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-5\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Pressure_Drop_Pressure_Loss_Head_Loss_and_Cv_Terms_to_Separate_First\" >Pressure Drop, Pressure Loss, Head Loss and Cv: Terms to Separate First<\/a><ul class='ez-toc-list-level-3' ><li class='ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-6\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Pressure_drop_vs_pressure_loss\" >Pressure drop vs pressure loss<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-7\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Head_loss_in_feet_of_water_or_meters_of_head\" >Head loss in feet of water or meters of head<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-8\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Cv_flow_coefficient_as_a_capacity_indicator\" >Cv \/ flow coefficient as a capacity indicator<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-9\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Cracking_pressure_is_not_the_same_as_operating_pressure_drop\" >Cracking pressure is not the same as operating pressure drop<\/a><\/li><\/ul><\/li><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-10\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#What_Determines_Pressure_Drop_Across_a_Check_Valve\" >What Determines Pressure Drop Across a Check Valve?<\/a><ul class='ez-toc-list-level-3' ><li class='ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-11\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Flow_rate_and_velocity\" >Flow rate and velocity<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-12\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Specific_gravity_viscosity_and_fluid_condition\" >Specific gravity, viscosity and fluid condition<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-13\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Internal_flow_path_disc_position_and_body_design\" >Internal flow path, disc position and body design<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-14\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Whether_the_valve_is_fully_open_or_only_partly_open\" >Whether the valve is fully open or only partly open<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-15\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Installation_disturbance_and_upstream_flow_stability\" >Installation disturbance and upstream flow stability<\/a><\/li><\/ul><\/li><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-16\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#How_Cv_Relates_to_Check_Valve_Pressure_Drop\" >How Cv Relates to Check Valve Pressure Drop<\/a><ul class='ez-toc-list-level-3' ><li class='ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-17\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#What_does_Cv_mean_for_a_check_valve\" >What does Cv mean for a check valve?<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-18\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Basic_relationship_between_flow_rate_specific_gravity_and_%CE%94P\" >Basic relationship between flow rate, specific gravity and \u0394P<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-19\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Why_check_valve_Cv_values_must_come_from_manufacturer_data\" >Why check valve Cv values must come from manufacturer data<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-20\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Why_%E2%80%9Chigher_Cv%E2%80%9D_does_not_automatically_mean_better_selection\" >Why \u201chigher Cv\u201d does not automatically mean better selection<\/a><\/li><\/ul><\/li><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-21\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#How_to_Read_a_Check_Valve_Pressure_Drop_Cv_or_Head_Loss_Chart\" >How to Read a Check Valve Pressure Drop, Cv or Head Loss Chart<\/a><ul class='ez-toc-list-level-3' ><li class='ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-22\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Start_with_the_correct_valve_type_and_size\" >Start with the correct valve type and size<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-23\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Match_flow_rate_and_operating_condition\" >Match flow rate and operating condition<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-24\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Read_pressure_drop_head_loss_or_Cv_consistently\" >Read pressure drop, head loss or Cv consistently<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-25\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Check_velocity_range_and_minimum_flow_assumptions\" >Check velocity range and minimum flow assumptions<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-26\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Avoid_using_another_manufacturers_chart_as_a_universal_value\" >Avoid using another manufacturer\u2019s chart as a universal value<\/a><\/li><\/ul><\/li><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-27\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#How_Check_Valve_Type_Changes_Pressure_Drop_and_Head_Loss\" >How Check Valve Type Changes Pressure Drop and Head Loss<\/a><ul class='ez-toc-list-level-3' ><li class='ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-28\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Swing_check_valves\" >Swing check valves<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-29\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Spring-loaded_lift_and_piston_check_valves\" >Spring-loaded, lift and piston check valves<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-30\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Dual_plate_and_wafer_check_valves\" >Dual plate and wafer check valves<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-31\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Silent_nozzle_and_non-slam_check_valves\" >Silent, nozzle and non-slam check valves<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-32\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Ball_Y-pattern_and_special_check_valve_designs\" >Ball, Y-pattern and special check valve designs<\/a><\/li><\/ul><\/li><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-33\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Why_Low_Pressure_Drop_Is_Not_the_Only_Selection_Target\" >Why Low Pressure Drop Is Not the Only Selection Target<\/a><ul class='ez-toc-list-level-3' ><li class='ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-34\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Oversized_valves_and_unstable_opening\" >Oversized valves and unstable opening<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-35\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Undersized_valves_and_excessive_pressure_loss\" >Undersized valves and excessive pressure loss<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-36\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Minimum_flow_chatter_and_wear_risk\" >Minimum flow, chatter and wear risk<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-37\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Low_pressure_drop_vs_low_cracking_pressure\" >Low pressure drop vs low cracking pressure<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-38\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#When_a_low_pressure_drop_check_valve_should_be_requested\" >When a low pressure drop check valve should be requested<\/a><\/li><\/ul><\/li><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-39\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#RFQ_Data_Checklist_for_Check_Valve_Pressure_Drop_Review\" >RFQ Data Checklist for Check Valve Pressure Drop Review<\/a><ul class='ez-toc-list-level-3' ><li class='ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-40\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Flow_data_and_allowable_pressure_drop\" >Flow data and allowable pressure drop<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-41\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Medium_specific_gravity_viscosity_and_temperature\" >Medium, specific gravity, viscosity and temperature<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-42\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Line_size_valve_type_and_installation_orientation\" >Line size, valve type and installation orientation<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-43\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Cracking_pressure_minimum_flow_and_closure_requirement\" >Cracking pressure, minimum flow and closure requirement<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-44\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Required_datasheet_drawing_or_pressure_drop_curve\" >Required datasheet, drawing or pressure drop curve<\/a><\/li><\/ul><\/li><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-45\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#FAQ_Check_Valve_Pressure_Drop_Cv_and_Head_Loss\" >FAQ: Check Valve Pressure Drop, Cv and Head Loss<\/a><ul class='ez-toc-list-level-3' ><li class='ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-46\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Is_cracking_pressure_the_same_as_pressure_drop\" >Is cracking pressure the same as pressure drop?<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-47\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#What_does_Cv_mean_for_a_check_valve-2\" >What does Cv mean for a check valve?<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-48\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Is_check_valve_head_loss_the_same_as_pressure_drop\" >Is check valve head loss the same as pressure drop?<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-49\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#How_do_you_calculate_pressure_drop_across_a_check_valve\" >How do you calculate pressure drop across a check valve?<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-50\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Does_a_check_valve_reduce_pressure\" >Does a check valve reduce pressure?<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-51\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Is_a_higher_Cv_always_better_for_a_check_valve\" >Is a higher Cv always better for a check valve?<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-52\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#When_should_a_low_pressure_drop_check_valve_be_selected\" >When should a low pressure drop check valve be selected?<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-3'><a class=\"ez-toc-link ez-toc-heading-53\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Do_swing_check_valves_have_lower_pressure_drop_than_spring-loaded_check_valves\" >Do swing check valves have lower pressure drop than spring-loaded check valves?<\/a><\/li><\/ul><\/li><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-54\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Conclusion_Match_Pressure_Drop_Data_to_Real_Operating_Conditions\" >Conclusion: Match Pressure Drop Data to Real Operating Conditions<\/a><\/li><li class='ez-toc-page-1 ez-toc-heading-level-2'><a class=\"ez-toc-link ez-toc-heading-55\" href=\"https:\/\/ntgdvalve.com\/ru\/check-valve-pressure-drop-cv\/#Application_Specification_Support\" >Application \/ Specification Support<\/a><\/li><\/ul><\/nav><\/div>\n<h2><span class=\"ez-toc-section\" id=\"What_Is_Check_Valve_Pressure_Drop\"><\/span>What Is Check Valve Pressure Drop?<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<h3><span class=\"ez-toc-section\" id=\"Quick_definition_for_industrial_piping_systems\"><\/span>Quick definition for industrial piping systems<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Check valve pressure drop is the pressure reduction measured across a check valve while fluid is flowing through it. In simple terms, the valve creates resistance. That resistance converts part of the fluid energy into turbulence, velocity change, friction loss, and local losses around the internal closing element.<\/p>\n<p>For a check valve, this resistance is not fixed. It changes with:<\/p>\n<ul>\n<li>flow rate;<\/li>\n<li>fluid density and viscosity;<\/li>\n<li>valve size;<\/li>\n<li>valve type;<\/li>\n<li>internal body geometry;<\/li>\n<li>disc, plate, ball, piston, or spring position;<\/li>\n<li>installation orientation;<\/li>\n<li>upstream and downstream flow conditions.<\/li>\n<\/ul>\n<p>This is why two check valves with the same nominal size can create different pressure drops in the same pipeline.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Why_pressure_drop_matters_in_pump_and_process_lines\"><\/span>Why pressure drop matters in pump and process lines<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>In pump discharge lines, cooling water circuits, fire water systems, industrial water lines, chemical process systems, and other piping networks, check valve pressure loss becomes part of the total system loss. If it is underestimated, the system may not deliver the required flow. If it is overestimated, the project may oversize the pump, pipe, or valve unnecessarily.<\/p>\n<p>A high pressure drop may lead to:<\/p>\n<ul>\n<li>higher pump head requirement;<\/li>\n<li>reduced flow at downstream equipment;<\/li>\n<li>unnecessary energy consumption;<\/li>\n<li>noise or vibration;<\/li>\n<li>excessive velocity through the valve;<\/li>\n<li>unstable check valve behavior.<\/li>\n<\/ul>\n<p>A very strict low pressure drop requirement can also create a selection trap. It may push the project toward a larger or more open-flow valve, but if that valve cannot reach a stable full-open position at normal or minimum flow, the result may be chatter, accelerated wear, and unstable pressure loss.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Why_check_valves_are_different_from_simple_open-bore_valves\"><\/span>Why check valves are different from simple open-bore valves<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Some isolation valves, such as full-port ball valves or gate valves in the fully open position, can have a relatively open flow path. A check valve is different because it contains a moving closure element that must respond to flow direction.<\/p>\n<p>Depending on the design, this element may be a swinging disc, dual plates, a guided piston, a spring-loaded disc, a ball, or a nozzle-style non-slam element. Even when the valve is open, part of the internal mechanism remains in or near the flow path.<\/p>\n<p>Because of this internal moving element, treating check valve pressure drop as a generic minor fitting loss without manufacturer verification can lead to undersized pump margin, unstable valve opening, or unexpected system loss.<\/p>\n<p>To connect this pressure-drop discussion with basic valve operation, review how forward flow opens and reverse flow closes the valve in our <a href=\"https:\/\/ntgdvalve.com\/how-does-a-check-valve-work\/\">check valve working principle guide<\/a>.<\/p>\n<h2><span class=\"ez-toc-section\" id=\"Pressure_Drop_Pressure_Loss_Head_Loss_and_Cv_Terms_to_Separate_First\"><\/span>Pressure Drop, Pressure Loss, Head Loss and Cv: Terms to Separate First<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<p>Before reviewing a check valve Cv value or a head loss chart, it is useful to separate several terms that are often mixed together.<\/p>\n<table>\n<thead>\n<tr>\n<th>Term<\/th>\n<th>Meaning in this article<\/th>\n<th>Why it matters<\/th>\n<th>Do not confuse it with<\/th>\n<\/tr>\n<\/thead>\n<tbody>\n<tr>\n<td>Pressure drop<\/td>\n<td>Pressure difference across the check valve during flow<\/td>\n<td>Used to understand system loss and pump head impact<\/td>\n<td>Pressure rating<\/td>\n<\/tr>\n<tr>\n<td>Pressure loss<\/td>\n<td>General term for pressure reduction caused by resistance<\/td>\n<td>Often used similarly to pressure drop in piping discussions<\/td>\n<td>Permanent valve damage<\/td>\n<\/tr>\n<tr>\n<td>Head loss<\/td>\n<td>Energy loss expressed as height of fluid column, often feet or meters of head<\/td>\n<td>Common in water, pump, and hydraulic calculations<\/td>\n<td>Physical elevation only<\/td>\n<\/tr>\n<tr>\n<td>Cv \/ flow coefficient<\/td>\n<td>A valve capacity value that relates flow rate and pressure drop under defined conditions<\/td>\n<td>Helps compare flow capacity between valve designs<\/td>\n<td>Product model \u201cCV\u201d or control valve-only sizing<\/td>\n<\/tr>\n<tr>\n<td>Cracking pressure<\/td>\n<td>Differential pressure required to start opening a check valve<\/td>\n<td>Important for low-flow or low-differential-pressure service<\/td>\n<td>Full-open operating pressure drop<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<h3><span class=\"ez-toc-section\" id=\"Pressure_drop_vs_pressure_loss\"><\/span>Pressure drop vs pressure loss<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>In many industrial discussions, pressure drop and pressure loss are used almost interchangeably. Both describe pressure reduction caused by resistance in the valve or piping system. In this article, pressure drop is used when discussing the value across the check valve, while pressure loss is used more broadly for the system effect.<\/p>\n<p>For selection, the key question is not only whether pressure is lost. The important question is whether the loss is acceptable for the required flow rate, pump head, and operating margin.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Head_loss_in_feet_of_water_or_meters_of_head\"><\/span>Head loss in feet of water or meters of head<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Head loss expresses the same energy-loss concept in a hydraulic format. Instead of saying a valve creates a certain pressure drop, a water system may describe the same loss as feet of water or meters of head. This is common in pump calculations and water-system documents.<\/p>\n<p>When comparing data, do not mix units without conversion. A manufacturer may present one chart in pressure drop, another in head loss, and another in Cv. The engineer or buyer must confirm that the chart unit, flow unit, and fluid basis match the project.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Cv_flow_coefficient_as_a_capacity_indicator\"><\/span>Cv \/ flow coefficient as a capacity indicator<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Cv is the flow coefficient of a valve. In check valve selection, the check valve flow coefficient is the main capacity term used to relate flow rate, fluid specific gravity, and pressure drop under defined conditions.<\/p>\n<p>A higher Cv generally means the valve can pass more flow at a given pressure drop. However, for check valves, Cv should not be read as the only selection answer. The valve must also open stably, avoid chatter, close correctly, and meet the project\u2019s pressure, temperature, material, and installation requirements.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Cracking_pressure_is_not_the_same_as_operating_pressure_drop\"><\/span>Cracking pressure is not the same as operating pressure drop<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Cracking pressure is the differential pressure at which a check valve begins to open or shows the first indication of flow. It does not mean the valve is fully open. It also does not equal the operating pressure drop at normal flow.<\/p>\n<p>This distinction is critical for check valves. A valve may crack open at a low pressure, but still require sufficient flow to reach a stable open position. If the valve operates partly open for long periods, it may chatter, vibrate, wear the seat or disc, and create more pressure loss than expected.<\/p>\n<p>In low differential pressure service, engineers should verify both cracking pressure and the full-open flow condition. Operating pressure drop alone does not confirm that the valve will open stably or reseat correctly.<\/p>\n<figure id=\"attachment_10596\" aria-describedby=\"caption-attachment-10596\" style=\"width: 1672px\" class=\"wp-caption aligncenter\"><img decoding=\"async\" class=\"size-full wp-image-10596\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cracking-pressure-vs-pressure-drop-diagram.png\" alt=\"Cracking pressure versus operating pressure drop diagram for a check valve\" width=\"1672\" height=\"941\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cracking-pressure-vs-pressure-drop-diagram.png 1672w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cracking-pressure-vs-pressure-drop-diagram-768x432.png 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cracking-pressure-vs-pressure-drop-diagram-1536x864.png 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cracking-pressure-vs-pressure-drop-diagram-18x10.png 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cracking-pressure-vs-pressure-drop-diagram-600x338.png 600w\" sizes=\"(max-width: 1672px) 100vw, 1672px\" \/><figcaption id=\"caption-attachment-10596\" class=\"wp-caption-text\">Cracking pressure describes initial opening, while operating pressure drop applies when flow passes through the open valve.<\/figcaption><\/figure>\n<h2><span class=\"ez-toc-section\" id=\"What_Determines_Pressure_Drop_Across_a_Check_Valve\"><\/span>What Determines Pressure Drop Across a Check Valve?<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<p>Check valve pressure drop is driven by both fluid conditions and valve design. A chart or Cv value is useful only when the operating condition behind it is understood.<\/p>\n<table>\n<thead>\n<tr>\n<th>Factor<\/th>\n<th>How it affects pressure drop<\/th>\n<th>Selection note<\/th>\n<\/tr>\n<\/thead>\n<tbody>\n<tr>\n<td>Flow rate<\/td>\n<td>Higher flow usually increases pressure drop<\/td>\n<td>Use normal, minimum, and maximum flow, not only design flow<\/td>\n<\/tr>\n<tr>\n<td>Velocity<\/td>\n<td>High velocity increases dynamic loss and may cause noise or wear<\/td>\n<td>Check the recommended velocity range for the valve type<\/td>\n<\/tr>\n<tr>\n<td>Specific gravity<\/td>\n<td>Denser liquids generally require more pressure drop for the same flow and Cv<\/td>\n<td>Confirm the actual medium, not only \u201cwater equivalent\u201d<\/td>\n<\/tr>\n<tr>\n<td>Viscosity<\/td>\n<td>Higher viscosity can increase resistance and affect opening behavior<\/td>\n<td>Important for oils, slurries, viscous chemicals, and low-flow systems<\/td>\n<\/tr>\n<tr>\n<td>Valve type<\/td>\n<td>Internal flow path and closure element change resistance<\/td>\n<td>Compare swing, lift, dual plate, silent, piston, and other designs<\/td>\n<\/tr>\n<tr>\n<td>Opening position<\/td>\n<td>A partly open check valve can create higher loss and unstable operation<\/td>\n<td>Verify minimum flow required for stable opening<\/td>\n<\/tr>\n<tr>\n<td>Installation condition<\/td>\n<td>Elbows, pumps, reducers, and disturbed flow can affect valve behavior<\/td>\n<td>Review upstream \/ downstream piping before final selection<\/td>\n<\/tr>\n<tr>\n<td>Manufacturer design<\/td>\n<td>Same nominal type can vary between brands and models<\/td>\n<td>Use manufacturer data, not generic values<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<figure id=\"attachment_10603\" aria-describedby=\"caption-attachment-10603\" style=\"width: 1672px\" class=\"wp-caption aligncenter\"><img decoding=\"async\" class=\"size-full wp-image-10603\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-flow-path-cutaway.png\" alt=\"Check valve cutaway diagram showing flow path, disc plate, seat area, and pressure drop\" width=\"1672\" height=\"941\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-flow-path-cutaway.png 1672w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-flow-path-cutaway-768x432.png 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-flow-path-cutaway-1536x864.png 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-flow-path-cutaway-18x10.png 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-flow-path-cutaway-600x338.png 600w\" sizes=\"(max-width: 1672px) 100vw, 1672px\" \/><figcaption id=\"caption-attachment-10603\" class=\"wp-caption-text\">The internal flow path, disc position, and seat area can change the actual pressure drop across a check valve.<\/figcaption><\/figure>\n<p>These factors work together. Two check valves with the same nominal size may produce different actual \u0394P because their flow path, closure element, spring load, opening angle, and manufacturer design are different. When the flow range, medium, valve type, or opening condition is uncertain, the pressure drop review should be manufacturer-specific.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Flow_rate_and_velocity\"><\/span>Flow rate and velocity<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Flow rate is the first input for pressure drop review. As flow increases, velocity through the valve also increases, and the pressure drop normally rises. This rise is not always linear. Small increases in flow can create larger increases in pressure loss, especially through compact or internally restricted valve designs.<\/p>\n<p>Velocity also affects valve behavior. Check valves rely on flow to move and hold the closure element open. If velocity is too low, the valve may not open fully. If velocity is too high, the valve may suffer from noise, vibration, erosion, or excessive head loss.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Specific_gravity_viscosity_and_fluid_condition\"><\/span>Specific gravity, viscosity and fluid condition<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>A check valve pressure drop chart is often based on water or a defined test medium. Real industrial fluids may be different. Higher specific gravity, viscosity, suspended solids, gas content, or two-phase conditions can change the actual pressure loss and valve behavior.<\/p>\n<p>For clean water service, chart reading may be relatively direct. For viscous liquids, slurry, corrosive media, or mixed-phase flow, the project should avoid relying only on a generic Cv value. The supplier should review the actual medium and operating range.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Internal_flow_path_disc_position_and_body_design\"><\/span>Internal flow path, disc position and body design<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>The body shape and closure element create the local loss inside the valve. A swing check valve may offer a different flow path from a spring-loaded lift check valve. A dual plate wafer check valve may be compact but still has plates and springs in the flow path. A silent or nozzle check valve may control closing behavior but can create a different pressure drop profile.<\/p>\n<p>The name of the check valve type is not enough. The actual body design, seat geometry, guide structure, spring force, and disc travel can change pressure drop.<\/p>\n<p>For a component-level view of how the body, disc, seat, spring and hinge affect movement and sealing, use the <a href=\"https:\/\/ntgdvalve.com\/check-valve-parts-components\/\">check valve parts and components guide<\/a>.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Whether_the_valve_is_fully_open_or_only_partly_open\"><\/span>Whether the valve is fully open or only partly open<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>A major check valve selection mistake is assuming the valve is always fully open during operation. In reality, if flow is too low, the disc or plate may float in a partly open position. This can increase pressure loss, create noise, and cause wear.<\/p>\n<p>A check valve should be selected for the operating flow range, not only the line size. The normal flow should be high enough to hold the valve open in a stable condition, while the maximum flow should not create excessive pressure drop or velocity.<\/p>\n<p>One of the first questions to ask the manufacturer is: what minimum flow is required for this valve to reach a stable, fully open position in this line size and orientation?<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Installation_disturbance_and_upstream_flow_stability\"><\/span>Installation disturbance and upstream flow stability<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>A check valve installed immediately after a pump, elbow, reducer, tee, or control element may see uneven flow. This can affect disc movement, pressure drop, noise, and closing behavior.<\/p>\n<p>This article does not replace a check valve installation guide, but pressure drop review should include installation conditions. Adequate upstream and downstream piping helps stabilize the flow entering the valve. Detailed installation distance, orientation, and support requirements should be checked against the project installation guide or the manufacturer\u2019s IOM.<\/p>\n<p>For detailed orientation, pump discharge spacing, pipe support and startup checks, refer to the <a href=\"https:\/\/ntgdvalve.com\/check-valve-installation\/\">check valve installation guide<\/a>.<\/p>\n<h2><span class=\"ez-toc-section\" id=\"How_Cv_Relates_to_Check_Valve_Pressure_Drop\"><\/span>How Cv Relates to Check Valve Pressure Drop<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<h3><span class=\"ez-toc-section\" id=\"What_does_Cv_mean_for_a_check_valve\"><\/span>What does Cv mean for a check valve?<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Cv is the flow coefficient of the check valve. In check valve selection, it helps estimate how much flow can pass through the valve at a given pressure drop. It is also useful for comparing flow capacity between valve designs of the same nominal size.<\/p>\n<p>However, a check valve Cv value should always be tied to the actual valve design and opening condition. A Cv value from one manufacturer, one valve type, or one size cannot be assumed to apply to another valve.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Basic_relationship_between_flow_rate_specific_gravity_and_%CE%94P\"><\/span>Basic relationship between flow rate, specific gravity and \u0394P<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>For liquid service, a simplified Cv relationship is useful for preliminary screening. For a given flow rate and fluid specific gravity, an engineer can use the relationship to check whether a valve\u2019s Cv range is likely to meet the allowable pressure drop before requesting the full manufacturer curve.<\/p>\n<p>A common simplified relationship is:<\/p>\n<p><strong>\u0394P \u2248 SG \u00d7 (Q \/ Cv)\u00b2<\/strong><\/p>\n<table>\n<thead>\n<tr>\n<th>Variable<\/th>\n<th>Meaning<\/th>\n<th>Needed from<\/th>\n<th>Caution<\/th>\n<\/tr>\n<\/thead>\n<tbody>\n<tr>\n<td>\u0394P<\/td>\n<td>Pressure drop across the valve<\/td>\n<td>Calculation or manufacturer data<\/td>\n<td>Usually expressed in psi or bar, depending on the chart<\/td>\n<\/tr>\n<tr>\n<td>SG<\/td>\n<td>Specific gravity of the fluid<\/td>\n<td>Process data<\/td>\n<td>Water is commonly used as a reference, but real fluids may differ<\/td>\n<\/tr>\n<tr>\n<td>Q<\/td>\n<td>Flow rate<\/td>\n<td>Project operating data<\/td>\n<td>Use normal, minimum, and maximum flow where possible<\/td>\n<\/tr>\n<tr>\n<td>Cv<\/td>\n<td>Valve flow coefficient<\/td>\n<td>Manufacturer datasheet or curve<\/td>\n<td>Must match valve type, size, and design<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<figure id=\"attachment_10599\" aria-describedby=\"caption-attachment-10599\" style=\"width: 1672px\" class=\"wp-caption aligncenter\"><img loading=\"lazy\" decoding=\"async\" class=\"size-full wp-image-10599\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cv-pressure-drop-formula-diagram.png\" alt=\"Check valve Cv and pressure drop formula diagram with flow rate and specific gravity\" width=\"1672\" height=\"941\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cv-pressure-drop-formula-diagram.png 1672w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cv-pressure-drop-formula-diagram-768x432.png 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cv-pressure-drop-formula-diagram-1536x864.png 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cv-pressure-drop-formula-diagram-18x10.png 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-cv-pressure-drop-formula-diagram-600x338.png 600w\" sizes=\"(max-width: 1672px) 100vw, 1672px\" \/><figcaption id=\"caption-attachment-10599\" class=\"wp-caption-text\">This diagram explains how flow rate, specific gravity, Cv, and \u0394P are connected for preliminary pressure drop review.<\/figcaption><\/figure>\n<p>A general <a href=\"https:\/\/www.engineeringtoolbox.com\/flow-coefficients-d_277.html\" target=\"_blank\" rel=\"noopener\">Cv flow coefficient reference<\/a> explains the liquid-service relationship between flow rate, specific gravity and pressure drop; in this article, it is used only as a preliminary check before manufacturer-specific check valve data.<\/p>\n<p>This formula should be treated as a conceptual estimate for clean liquid service under defined conditions, normally assuming a stable, fully open valve. It should not be used as the final sizing basis for gas, steam, high-viscosity liquids, slurry, two-phase flow, or a check valve that may operate partly open or unstably.<\/p>\n<p>Final selection must be checked against the manufacturer\u2019s pressure drop curve, Cv table, datasheet, or test basis for the actual valve design.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Why_check_valve_Cv_values_must_come_from_manufacturer_data\"><\/span>Why check valve Cv values must come from manufacturer data<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Check valve Cv values are manufacturer-specific. They depend on the internal geometry, travel of the closure element, seat design, spring load, and test basis. Even if two valves are both called \u201cswing check valves,\u201d their Cv values may not be the same.<\/p>\n<p>For RFQ or technical approval, the buyer should request one or more of the following:<\/p>\n<ul>\n<li>Cv value;<\/li>\n<li>pressure drop curve;<\/li>\n<li>head loss chart;<\/li>\n<li>datasheet with flow capacity;<\/li>\n<li>recommended flow range;<\/li>\n<li>minimum flow for stable opening;<\/li>\n<li>cracking pressure, if relevant to the service.<\/li>\n<\/ul>\n<h3><span class=\"ez-toc-section\" id=\"Why_%E2%80%9Chigher_Cv%E2%80%9D_does_not_automatically_mean_better_selection\"><\/span>Why \u201chigher Cv\u201d does not automatically mean better selection<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>A higher Cv may lower calculated \u0394P, but it does not automatically improve check valve selection. If normal flow is below the valve\u2019s minimum stable opening range, the closure element may not stay fully open.<\/p>\n<p>That condition can create chatter, seat or disc wear, unstable pressure loss, and higher long-term maintenance cost. Selection should balance allowable pressure drop with stable opening, closing behavior, flow range, and installation condition.<\/p>\n<h2><span class=\"ez-toc-section\" id=\"How_to_Read_a_Check_Valve_Pressure_Drop_Cv_or_Head_Loss_Chart\"><\/span>How to Read a Check Valve Pressure Drop, Cv or Head Loss Chart<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<p>Many search results for check valve pressure drop lead to PDFs, head loss charts, Cv tables, or product data curves. These documents can be useful, but they must be read carefully.<\/p>\n<table>\n<thead>\n<tr>\n<th>Step<\/th>\n<th>Data to check<\/th>\n<th>Common mistake<\/th>\n<\/tr>\n<\/thead>\n<tbody>\n<tr>\n<td>1<\/td>\n<td>Valve type and exact model<\/td>\n<td>Using a chart from a different check valve design, leading to inaccurate \u0394P estimation<\/td>\n<\/tr>\n<tr>\n<td>2<\/td>\n<td>Valve size and end connection<\/td>\n<td>Assuming line size equals correct valve size, which may cause sizing error<\/td>\n<\/tr>\n<tr>\n<td>3<\/td>\n<td>Flow rate range<\/td>\n<td>Checking only maximum flow and ignoring normal or minimum flow<\/td>\n<\/tr>\n<tr>\n<td>4<\/td>\n<td>Fluid basis<\/td>\n<td>Using water-based data for a different fluid without review<\/td>\n<\/tr>\n<tr>\n<td>5<\/td>\n<td>Unit system<\/td>\n<td>Mixing psi, bar, feet of head, meters of head, gpm, or m\u00b3\/h<\/td>\n<\/tr>\n<tr>\n<td>6<\/td>\n<td>Velocity range<\/td>\n<td>Ignoring recommended velocity range, which may lead to chatter, noise, or high loss<\/td>\n<\/tr>\n<tr>\n<td>7<\/td>\n<td>Opening condition<\/td>\n<td>Assuming full-open behavior at all flows<\/td>\n<\/tr>\n<tr>\n<td>8<\/td>\n<td>Manufacturer source<\/td>\n<td>Treating another manufacturer\u2019s chart as universal<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<figure id=\"attachment_10598\" aria-describedby=\"caption-attachment-10598\" style=\"width: 1672px\" class=\"wp-caption aligncenter\"><img loading=\"lazy\" decoding=\"async\" class=\"size-full wp-image-10598\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-chart-reading-guide.png\" alt=\"Check valve pressure drop chart reading guide with flow rate curve and operating point\" width=\"1672\" height=\"941\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-chart-reading-guide.png 1672w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-chart-reading-guide-768x432.png 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-chart-reading-guide-1536x864.png 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-chart-reading-guide-18x10.png 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-chart-reading-guide-600x338.png 600w\" sizes=\"(max-width: 1672px) 100vw, 1672px\" \/><figcaption id=\"caption-attachment-10598\" class=\"wp-caption-text\">A pressure drop chart should be read using the correct valve type, actual flow range, fluid basis, and manufacturer curve.<\/figcaption><\/figure>\n<h3><span class=\"ez-toc-section\" id=\"Start_with_the_correct_valve_type_and_size\"><\/span>Start with the correct valve type and size<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>A pressure drop chart is only useful when it matches the valve type and size being considered. A swing check valve chart should not be used for a spring-loaded lift check valve. A wafer check valve curve should not be used for a nozzle check valve. A pressure drop chart from one manufacturer should not be treated as a universal value for all valves.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Match_flow_rate_and_operating_condition\"><\/span>Match flow rate and operating condition<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Pressure drop should be checked at the actual operating flow rate. In many projects, one design flow is not enough. The check valve may see a minimum flow, normal flow, peak flow, startup flow, or pump trip condition. Each can affect valve opening and pressure loss.<\/p>\n<p>For pump discharge service, minimum flow is especially important. A check valve that looks acceptable at maximum flow may chatter at low flow.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Read_pressure_drop_head_loss_or_Cv_consistently\"><\/span>Read pressure drop, head loss or Cv consistently<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Some charts show pressure drop directly. Others show head loss. Some provide Cv tables instead of curves. The engineer should confirm which value is being used and how it relates to the project calculation.<\/p>\n<p>When reading a check valve head loss chart, pay attention to whether the chart is based on feet of water or meters of head. A head loss chart expresses energy loss in pumping terms, which can be convenient for pump selection. It represents the same physical behavior as a pressure drop curve, but the unit and reading method are different.<\/p>\n<p>For head-loss terminology, the Hydraulic Institute\u2019s <a href=\"https:\/\/datatool.pumps.org\/fluid-flow-iii\/fr-loss-water\" target=\"_blank\" rel=\"noopener\">valves and fittings minor-loss reference<\/a> explains how valve and fitting losses are treated as part of system friction loss.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Check_velocity_range_and_minimum_flow_assumptions\"><\/span>Check velocity range and minimum flow assumptions<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Some check valve designs require a minimum velocity or minimum flow to open fully and remain stable. If the chart assumes a stable open position but the actual system operates below that range, the real pressure loss and wear risk may be different.<\/p>\n<p>This is one of the reasons check valve pressure drop review should include both hydraulic data and operating behavior.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Avoid_using_another_manufacturers_chart_as_a_universal_value\"><\/span>Avoid using another manufacturer\u2019s chart as a universal value<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>A generic chart can help early-stage comparison, but final selection should rely on the manufacturer\u2019s own data for the selected valve. The final RFQ should ask for pressure drop, Cv, head loss, or flow curve information that matches the exact valve design being supplied.<\/p>\n<p>Ignoring installation condition, valve model, flow range, or chart basis can make the chart reading look correct on paper while the actual system performance differs from expectation.<\/p>\n<h2><span class=\"ez-toc-section\" id=\"How_Check_Valve_Type_Changes_Pressure_Drop_and_Head_Loss\"><\/span>How Check Valve Type Changes Pressure Drop and Head Loss<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<p>Different check valve types create different flow resistance. The table below is a selection-support comparison, not a universal ranking. Actual pressure drop must still be verified from manufacturer data.<\/p>\n<table>\n<thead>\n<tr>\n<th>Check valve type<\/th>\n<th>Typical flow path \/ internal feature<\/th>\n<th>Pressure drop tendency<\/th>\n<th>Selection note<\/th>\n<\/tr>\n<\/thead>\n<tbody>\n<tr>\n<td>Swing check valve<\/td>\n<td>Hinged disc swings away from the seat<\/td>\n<td>Generally lower resistance potential when fully open compared with spring-loaded lift designs, but highly dependent on body design and disc stability<\/td>\n<td>Often considered for higher-flow water or process lines, but verify stable opening at normal and minimum flow<\/td>\n<\/tr>\n<tr>\n<td>Spring-loaded check valve<\/td>\n<td>Spring force helps close the disc<\/td>\n<td>Spring load can add opening resistance and affect full-open behavior<\/td>\n<td>Useful where faster closing is required; confirm cracking pressure, Cv, and minimum flow<\/td>\n<\/tr>\n<tr>\n<td>Lift check valve<\/td>\n<td>Guided disc or piston lifts from the seat<\/td>\n<td>Often higher resistance than a simple swing design because the flow path is more restricted<\/td>\n<td>Review carefully where allowable \u0394P is tight or flow range varies<\/td>\n<\/tr>\n<tr>\n<td>Piston check valve<\/td>\n<td>Guided piston movement<\/td>\n<td>Can provide controlled movement but may add resistance through the guided path<\/td>\n<td>Suitable for certain pressure \/ process conditions; verify Cv and full-open behavior<\/td>\n<\/tr>\n<tr>\n<td>Dual plate \/ wafer check valve<\/td>\n<td>Two spring-assisted plates in compact body<\/td>\n<td>Compact design, but plates and springs influence head loss<\/td>\n<td>Useful where face-to-face space is limited; confirm pressure drop curve for the exact model<\/td>\n<\/tr>\n<tr>\n<td>Silent \/ nozzle check valve<\/td>\n<td>Designed for non-slam or controlled closing<\/td>\n<td>Pressure drop depends on spring, body profile, and non-slam design<\/td>\n<td>Consider where water hammer or reverse-flow control is critical, not only where lowest \u0394P is requested<\/td>\n<\/tr>\n<tr>\n<td>Ball check valve<\/td>\n<td>Ball moves away from seat under flow<\/td>\n<td>Pressure drop depends strongly on body and ball travel<\/td>\n<td>Common in some slurry or wastewater services; verify flow path and solids handling<\/td>\n<\/tr>\n<tr>\n<td>Y-pattern or special check valve<\/td>\n<td>Angled or special internal path<\/td>\n<td>Design-specific<\/td>\n<td>Use exact manufacturer data and application review<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<figure id=\"attachment_10601\" aria-describedby=\"caption-attachment-10601\" style=\"width: 1672px\" class=\"wp-caption aligncenter\"><img loading=\"lazy\" decoding=\"async\" class=\"size-full wp-image-10601\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-type-pressure-drop-comparison-matrix.png\" alt=\"Check valve type comparison matrix for pressure drop and head loss review\" width=\"1672\" height=\"941\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-type-pressure-drop-comparison-matrix.png 1672w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-type-pressure-drop-comparison-matrix-768x432.png 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-type-pressure-drop-comparison-matrix-1536x864.png 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-type-pressure-drop-comparison-matrix-18x10.png 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-type-pressure-drop-comparison-matrix-600x338.png 600w\" sizes=\"(max-width: 1672px) 100vw, 1672px\" \/><figcaption id=\"caption-attachment-10601\" class=\"wp-caption-text\">Different check valve designs create different flow paths, so type selection must be checked against pressure drop data.<\/figcaption><\/figure>\n<h3><span class=\"ez-toc-section\" id=\"Swing_check_valves\"><\/span>Swing check valves<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>A swing check valve can offer a relatively open flow path when the disc is fully open. This is why swing check valve pressure drop and head loss are often reviewed for water, wastewater, and pump discharge lines.<\/p>\n<p>However, a swing check valve is not automatically low-loss in every condition. If the flow is too low to hold the disc fully open, the disc may flutter or remain partly open. In that condition, pressure loss and wear can increase.<\/p>\n<figure id=\"attachment_10606\" aria-describedby=\"caption-attachment-10606\" style=\"width: 2560px\" class=\"wp-caption aligncenter\"><img loading=\"lazy\" decoding=\"async\" class=\"size-full wp-image-10606\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/swing-check-valve-24-inch-900lb-ca15-workshop-photo-scaled.jpg\" alt=\"Real 24 inch 900LB CA15 swing check valve in workshop\" width=\"2560\" height=\"1706\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/swing-check-valve-24-inch-900lb-ca15-workshop-photo-scaled.jpg 2560w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/swing-check-valve-24-inch-900lb-ca15-workshop-photo-768x512.jpg 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/swing-check-valve-24-inch-900lb-ca15-workshop-photo-1536x1024.jpg 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/swing-check-valve-24-inch-900lb-ca15-workshop-photo-2048x1365.jpg 2048w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/swing-check-valve-24-inch-900lb-ca15-workshop-photo-18x12.jpg 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/swing-check-valve-24-inch-900lb-ca15-workshop-photo-600x400.jpg 600w\" sizes=\"(max-width: 2560px) 100vw, 2560px\" \/><figcaption id=\"caption-attachment-10606\" class=\"wp-caption-text\">A swing check valve can offer an open flow path when fully open, but stable disc movement still needs verification.<\/figcaption><\/figure>\n<div style=\"position: relative; width: 100%; max-width: 100%; padding-bottom: 56.25%; height: 0; overflow: hidden; margin: 24px 0;\"><iframe style=\"position: absolute; top: 0; left: 0; width: 100%; height: 100%; border: 0;\" title=\"NTGD Swing Check Valve\" src=\"https:\/\/www.youtube.com\/embed\/1ewvEqwuRbs\" allowfullscreen=\"allowfullscreen\"><br \/>\n<\/iframe><\/div>\n<h3><span class=\"ez-toc-section\" id=\"Spring-loaded_lift_and_piston_check_valves\"><\/span>Spring-loaded, lift and piston check valves<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Spring-loaded, lift, and piston check valves may provide more controlled closing behavior, but the spring or guided element can increase flow resistance. These designs should be reviewed with Cv data, pressure drop curves, and minimum flow conditions.<\/p>\n<p>For these valves, cracking pressure and full-open pressure drop should be separated. Cracking pressure tells you when the valve starts opening; it does not confirm the valve is fully open at the operating flow.<\/p>\n<p>For a closer look at spring-assisted closure and non-slam selection boundaries, see the <a href=\"https:\/\/ntgdvalve.com\/spring-loaded-check-valve\/\">spring loaded check valve selection guide<\/a>.<\/p>\n<figure id=\"attachment_10605\" aria-describedby=\"caption-attachment-10605\" style=\"width: 2560px\" class=\"wp-caption aligncenter\"><img loading=\"lazy\" decoding=\"async\" class=\"size-full wp-image-10605\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/lift-piston-check-valve-dn100-1500lb-a105-high-pressure-scaled.jpg\" alt=\"Real DN100 1500LB A105 lift piston check valve for high pressure service\" width=\"2560\" height=\"1706\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/lift-piston-check-valve-dn100-1500lb-a105-high-pressure-scaled.jpg 2560w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/lift-piston-check-valve-dn100-1500lb-a105-high-pressure-768x512.jpg 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/lift-piston-check-valve-dn100-1500lb-a105-high-pressure-1536x1024.jpg 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/lift-piston-check-valve-dn100-1500lb-a105-high-pressure-2048x1365.jpg 2048w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/lift-piston-check-valve-dn100-1500lb-a105-high-pressure-18x12.jpg 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/lift-piston-check-valve-dn100-1500lb-a105-high-pressure-600x400.jpg 600w\" sizes=\"(max-width: 2560px) 100vw, 2560px\" \/><figcaption id=\"caption-attachment-10605\" class=\"wp-caption-text\">A real lift piston check valve shows why guided movement, Cv data, and pressure drop curves should be checked together.<\/figcaption><\/figure>\n<h3><span class=\"ez-toc-section\" id=\"Dual_plate_and_wafer_check_valves\"><\/span>Dual plate and wafer check valves<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Dual plate and wafer check valves are compact and widely used in industrial piping. They can be useful where face-to-face length is limited. However, the plates, springs, hinge pins, and body profile create a design-specific flow path.<\/p>\n<p>For these valves, chart reading is especially important. The same nominal size can have different pressure drop behavior depending on plate angle, spring design, and body geometry.<\/p>\n<figure id=\"attachment_10604\" aria-describedby=\"caption-attachment-10604\" style=\"width: 2560px\" class=\"wp-caption aligncenter\"><img loading=\"lazy\" decoding=\"async\" class=\"size-full wp-image-10604\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/dual-plate-check-valve-dn500-pn6-5a-workshop-photo-scaled.jpg\" alt=\"Real DN500 PN6 dual plate check valve bodies in workshop\" width=\"2560\" height=\"1707\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/dual-plate-check-valve-dn500-pn6-5a-workshop-photo-scaled.jpg 2560w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/dual-plate-check-valve-dn500-pn6-5a-workshop-photo-768x512.jpg 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/dual-plate-check-valve-dn500-pn6-5a-workshop-photo-1536x1024.jpg 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/dual-plate-check-valve-dn500-pn6-5a-workshop-photo-2048x1365.jpg 2048w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/dual-plate-check-valve-dn500-pn6-5a-workshop-photo-18x12.jpg 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/dual-plate-check-valve-dn500-pn6-5a-workshop-photo-600x400.jpg 600w\" sizes=\"(max-width: 2560px) 100vw, 2560px\" \/><figcaption id=\"caption-attachment-10604\" class=\"wp-caption-text\">Dual plate check valves are compact, but their plates and body geometry still affect pressure drop and head loss.<\/figcaption><\/figure>\n<h3><span class=\"ez-toc-section\" id=\"Silent_nozzle_and_non-slam_check_valves\"><\/span>Silent, nozzle and non-slam check valves<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Silent or nozzle check valves are often selected to reduce slam or improve closure behavior. Their pressure drop must be evaluated together with closing speed, flow stability, and water hammer risk.<\/p>\n<p>A non-slam design may be the better engineering choice even if another valve type appears to have lower pressure drop on a simplified chart. The final decision should consider system behavior, not only one pressure loss value.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Ball_Y-pattern_and_special_check_valve_designs\"><\/span>Ball, Y-pattern and special check valve designs<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Ball check valves, Y-pattern check valves, and other special designs should be reviewed by application. The pressure drop depends heavily on internal passage, ball or disc movement, seat design, and orientation.<\/p>\n<p>These designs should not be selected from a generic type name alone. They require product-specific data.<\/p>\n<h2><span class=\"ez-toc-section\" id=\"Why_Low_Pressure_Drop_Is_Not_the_Only_Selection_Target\"><\/span>Why Low Pressure Drop Is Not the Only Selection Target<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<p>Low pressure drop is usually desirable, but it should not be the only selection target. A check valve must also open, stay open, close, and reseat correctly.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Oversized_valves_and_unstable_opening\"><\/span>Oversized valves and unstable opening<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Oversizing can reduce calculated pressure drop, but it may create unstable operation. If the valve is too large for the actual flow, the closure element may not reach a stable full-open position. This can cause chattering, vibration, noise, and accelerated wear.<\/p>\n<table>\n<thead>\n<tr>\n<th>Sizing issue<\/th>\n<th>Pressure drop symptom<\/th>\n<th>Operating risk<\/th>\n<th>What to verify<\/th>\n<\/tr>\n<\/thead>\n<tbody>\n<tr>\n<td>Oversized valve<\/td>\n<td>Low calculated \u0394P at design flow, but unstable at normal flow<\/td>\n<td>Chatter and accelerated seat \/ disc wear, leading to premature leakage and shortened maintenance cycle<\/td>\n<td>Minimum flow for stable opening<\/td>\n<\/tr>\n<tr>\n<td>Undersized valve<\/td>\n<td>Excessive pressure drop<\/td>\n<td>Pump energy penalty, reduced downstream flow, high velocity, erosion, and possible system bottleneck<\/td>\n<td>Allowable \u0394P and velocity<\/td>\n<\/tr>\n<tr>\n<td>Wrong valve type<\/td>\n<td>Chart does not match actual service<\/td>\n<td>Misleading selection, unstable operation, or unexpected head loss<\/td>\n<td>Exact type and manufacturer curve<\/td>\n<\/tr>\n<tr>\n<td>Wrong cracking pressure<\/td>\n<td>Valve starts opening too late or too easily<\/td>\n<td>Unstable opening, poor reseal, leakage risk, or premature wear<\/td>\n<td>Cracking pressure and closure requirement<\/td>\n<\/tr>\n<tr>\n<td>Wrong installation condition<\/td>\n<td>Real flow is disturbed<\/td>\n<td>Noise, vibration, inaccurate chart behavior, or shortened component life<\/td>\n<td>Upstream \/ downstream piping condition<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<figure id=\"attachment_10600\" aria-describedby=\"caption-attachment-10600\" style=\"width: 1672px\" class=\"wp-caption aligncenter\"><img loading=\"lazy\" decoding=\"async\" class=\"size-full wp-image-10600\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-sizing-risk-board.png\" alt=\"Check valve pressure drop sizing risk board comparing oversized and undersized valves\" width=\"1672\" height=\"941\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-sizing-risk-board.png 1672w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-sizing-risk-board-768x432.png 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-sizing-risk-board-1536x864.png 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-sizing-risk-board-18x10.png 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-sizing-risk-board-600x338.png 600w\" sizes=\"(max-width: 1672px) 100vw, 1672px\" \/><figcaption id=\"caption-attachment-10600\" class=\"wp-caption-text\">Oversizing may reduce calculated \u0394P, while undersizing can create high velocity and system bottlenecks.<\/figcaption><\/figure>\n<h3><span class=\"ez-toc-section\" id=\"Undersized_valves_and_excessive_pressure_loss\"><\/span>Undersized valves and excessive pressure loss<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>An undersized check valve may create high pressure drop and high velocity. This can reduce downstream flow, increase pump load, and create erosion or noise. In severe cases, it can become a bottleneck in the system.<\/p>\n<p>The correct valve size should be based on system flow, allowable pressure drop, line size, velocity, and valve behavior, not only on the nominal pipe size.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Minimum_flow_chatter_and_wear_risk\"><\/span>Minimum flow, chatter and wear risk<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Check valve chatter is often linked to unstable opening. If the flow is not strong enough to hold the disc, plate, piston, or ball in a stable position, the element may move repeatedly. This can damage the seat, hinge, spring, guide, or sealing surface.<\/p>\n<p>A valve with a very low calculated pressure drop may still be a poor selection if the normal flow is below the stable operating range.<\/p>\n<p>An industry discussion in <a href=\"https:\/\/valvemagazine.com\/articles\/the-misunderstood-check-valve\/\" target=\"_blank\" rel=\"noopener\">Valve Magazine on check valve sizing and chatter<\/a> also warns that check valves should be sized for the application, not only line size or the largest Cv value.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Low_pressure_drop_vs_low_cracking_pressure\"><\/span>Low pressure drop vs low cracking pressure<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Low pressure drop and low cracking pressure are related to flow behavior, but they are not the same.<\/p>\n<ul>\n<li>Low pressure drop describes lower resistance during flow.<\/li>\n<li>Low cracking pressure describes a lower differential pressure required to start opening the valve.<\/li>\n<\/ul>\n<p>A low cracking pressure check valve may be useful in low-differential-pressure service, but it still must close reliably and remain stable in operation. The project should not assume that low cracking pressure automatically means low operating pressure loss or better service life.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"When_a_low_pressure_drop_check_valve_should_be_requested\"><\/span>When a low pressure drop check valve should be requested<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>A low pressure drop check valve may be appropriate when:<\/p>\n<ul>\n<li>pump head margin is limited;<\/li>\n<li>system energy loss must be minimized;<\/li>\n<li>the service has high flow rate;<\/li>\n<li>the allowable \u0394P across the valve is strict;<\/li>\n<li>the valve is installed in a long pipeline where cumulative losses matter;<\/li>\n<li>the process cannot tolerate excessive pressure loss.<\/li>\n<\/ul>\n<p>In projects with limited pump head margin, a low pressure drop design may be a valid candidate. But it must still meet minimum flow, stable opening, closure, installation, material, pressure, and temperature requirements. Otherwise, the operating risk can be greater than the pressure drop benefit.<\/p>\n<p>Even when these conditions point toward a low pressure drop check valve, the selection should be validated against the manufacturer\u2019s pressure drop curve for the specific model, size, and operating flow range, not just a catalog description.<\/p>\n<h2><span class=\"ez-toc-section\" id=\"RFQ_Data_Checklist_for_Check_Valve_Pressure_Drop_Review\"><\/span>RFQ Data Checklist for Check Valve Pressure Drop Review<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<p>Pressure drop cannot be reviewed from nominal size alone. A useful RFQ should give the supplier enough operating data to check the valve against real flow behavior, not only against a catalog name.<\/p>\n<table>\n<thead>\n<tr>\n<th>RFQ data item<\/th>\n<th>Why it is needed<\/th>\n<th>What the supplier should confirm<\/th>\n<\/tr>\n<\/thead>\n<tbody>\n<tr>\n<td>Flow rate<\/td>\n<td>Main input for pressure drop and Cv review<\/td>\n<td>Normal, minimum, and maximum flow<\/td>\n<\/tr>\n<tr>\n<td>Medium<\/td>\n<td>Affects density, viscosity, corrosion, and sealing<\/td>\n<td>Compatibility and flow behavior<\/td>\n<\/tr>\n<tr>\n<td>Specific gravity<\/td>\n<td>Required for Cv \/ \u0394P review<\/td>\n<td>Whether water-based data needs correction<\/td>\n<\/tr>\n<tr>\n<td>Viscosity<\/td>\n<td>Can affect pressure loss and opening behavior<\/td>\n<td>Whether standard data is still valid<\/td>\n<\/tr>\n<tr>\n<td>Line size<\/td>\n<td>Affects velocity and fit<\/td>\n<td>Valve size and end connection<\/td>\n<\/tr>\n<tr>\n<td>Valve type<\/td>\n<td>Different designs have different pressure drop<\/td>\n<td>Swing, lift, piston, dual plate, silent, nozzle, etc.<\/td>\n<\/tr>\n<tr>\n<td>Allowable pressure drop<\/td>\n<td>Defines the hydraulic limit<\/td>\n<td>Pressure drop at operating flow<\/td>\n<\/tr>\n<tr>\n<td>Head loss requirement<\/td>\n<td>Important for pump \/ water system design<\/td>\n<td>Head loss chart or equivalent data<\/td>\n<\/tr>\n<tr>\n<td>Operating pressure and temperature<\/td>\n<td>Defines pressure class and material boundary<\/td>\n<td>Suitable rating and material<\/td>\n<\/tr>\n<tr>\n<td>Cracking pressure<\/td>\n<td>Important for low-flow or low-differential systems<\/td>\n<td>Opening differential, if applicable<\/td>\n<\/tr>\n<tr>\n<td>Orientation<\/td>\n<td>Affects opening, closing, and reseating behavior<\/td>\n<td>Horizontal, vertical up, vertical down, or special condition<\/td>\n<\/tr>\n<tr>\n<td>Installation condition<\/td>\n<td>Disturbed flow can affect stability<\/td>\n<td>Pump discharge, elbows, reducers, straight run<\/td>\n<\/tr>\n<tr>\n<td>Required documents<\/td>\n<td>Needed for approval<\/td>\n<td>Datasheet, drawing, pressure drop curve, test document if required<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<figure id=\"attachment_10597\" aria-describedby=\"caption-attachment-10597\" style=\"width: 1672px\" class=\"wp-caption aligncenter\"><img loading=\"lazy\" decoding=\"async\" class=\"size-full wp-image-10597\" src=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-rfq-checklist.png\" alt=\"RFQ checklist for check valve pressure drop and Cv review\" width=\"1672\" height=\"941\" srcset=\"https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-rfq-checklist.png 1672w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-rfq-checklist-768x432.png 768w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-rfq-checklist-1536x864.png 1536w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-rfq-checklist-18x10.png 18w, https:\/\/ntgdvalve.com\/wp-content\/uploads\/2026\/07\/check-valve-pressure-drop-rfq-checklist-600x338.png 600w\" sizes=\"(max-width: 1672px) 100vw, 1672px\" \/><figcaption id=\"caption-attachment-10597\" class=\"wp-caption-text\">Pressure drop review needs flow rate, medium, specific gravity, viscosity, valve type, allowable \u0394P, cracking pressure, and orientation.<\/figcaption><\/figure>\n<p>Providing these data allows the supplier or valve engineer to return pressure drop and Cv advice matched to the actual operating condition, not a generic catalog selection.<\/p>\n<p>After the pressure drop, Cv and operating-flow limits are clear, the broader <a href=\"https:\/\/ntgdvalve.com\/check-valve-selection-guide\/\">check valve selection guide<\/a> can help compare valve type, orientation, water hammer risk and RFQ fit.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Flow_data_and_allowable_pressure_drop\"><\/span>Flow data and allowable pressure drop<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>The most useful RFQ input is a real flow range, not only one design point. Minimum flow helps check stable opening. Normal flow helps check everyday pressure loss. Maximum flow helps check velocity and hydraulic limit.<\/p>\n<p>Allowable pressure drop should be stated if the project has a strict limit. If the allowable value is not known, the supplier can still provide pressure drop data for engineering review.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Medium_specific_gravity_viscosity_and_temperature\"><\/span>Medium, specific gravity, viscosity and temperature<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>The pressure drop chart may be based on water or a standard test condition. If the project fluid is oil, slurry, chemical, condensate, seawater, gas, steam, or mixed-phase flow, the supplier should know before selection.<\/p>\n<p>Temperature also matters because it can affect viscosity, material selection, seat design, and pressure rating.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Line_size_valve_type_and_installation_orientation\"><\/span>Line size, valve type and installation orientation<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Line size alone is not enough. The RFQ should also identify preferred valve type, end connection, pressure class, installation orientation, and whether the valve is installed after a pump, elbow, reducer, or other disturbance.<\/p>\n<p>If the valve must be installed vertically or in a low-flow condition, cracking pressure and reseating behavior may need extra review.<\/p>\n<p>If the installation direction or body arrow is still under review, confirm it with the <a href=\"https:\/\/ntgdvalve.com\/check-valve-flow-direction\/\">check valve flow direction guide<\/a> before final RFQ approval.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Cracking_pressure_minimum_flow_and_closure_requirement\"><\/span>Cracking pressure, minimum flow and closure requirement<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>For check valves, pressure drop review should not ignore opening and closing behavior. A valve must start opening at the correct differential pressure, reach stable opening at normal flow, and close before reverse flow creates damage.<\/p>\n<p>If the system has low differential pressure or intermittent flow, ask the supplier to confirm cracking pressure, minimum flow, and closure performance.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Required_datasheet_drawing_or_pressure_drop_curve\"><\/span>Required datasheet, drawing or pressure drop curve<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>For technical approval, the buyer may need more than a catalog description. Useful documents include:<\/p>\n<ul>\n<li>datasheet;<\/li>\n<li>general arrangement drawing;<\/li>\n<li>Cv value or Cv table;<\/li>\n<li>pressure drop curve;<\/li>\n<li>head loss chart;<\/li>\n<li>material list;<\/li>\n<li>test requirement;<\/li>\n<li>installation note;<\/li>\n<li>IOM document, if available.<\/li>\n<\/ul>\n<p>These documents help connect the selected check valve to real operating conditions, not only nominal size and pressure class.<\/p>\n<h2><span class=\"ez-toc-section\" id=\"FAQ_Check_Valve_Pressure_Drop_Cv_and_Head_Loss\"><\/span>FAQ: Check Valve Pressure Drop, Cv and Head Loss<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<h3><span class=\"ez-toc-section\" id=\"Is_cracking_pressure_the_same_as_pressure_drop\"><\/span>Is cracking pressure the same as pressure drop?<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>No. Cracking pressure is the differential pressure required to start opening a check valve. Pressure drop is the pressure loss across the valve during flow. A check valve may crack open before it is fully open, so cracking pressure should not be used as a substitute for operating pressure drop.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"What_does_Cv_mean_for_a_check_valve-2\"><\/span>What does Cv mean for a check valve?<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Cv is the flow coefficient of the check valve. It indicates the valve\u2019s flow capacity under defined conditions. A higher Cv generally means lower pressure drop at the same flow rate, but the valve must still open stably and suit the service conditions.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Is_check_valve_head_loss_the_same_as_pressure_drop\"><\/span>Is check valve head loss the same as pressure drop?<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>They describe the same energy-loss concept in different forms. Pressure drop is usually expressed as pressure difference, while head loss is expressed as height of fluid column, such as feet or meters of head. Always check the units before comparing data.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"How_do_you_calculate_pressure_drop_across_a_check_valve\"><\/span>How do you calculate pressure drop across a check valve?<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>For an initial liquid-service estimate, engineers may use the Cv relationship with flow rate, specific gravity, and valve Cv. The basic inputs are Q, SG, Cv, valve type, and fluid condition. Final validation should use the manufacturer\u2019s pressure drop curve or Cv table for the specific valve model, size, and operating flow range.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Does_a_check_valve_reduce_pressure\"><\/span>Does a check valve reduce pressure?<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Yes. Every check valve creates some flow resistance and therefore some pressure loss during flow. In a well-designed system, this reduction is allowed for in the hydraulic calculation. In a poorly selected valve, it can become a noticeable system bottleneck.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Is_a_higher_Cv_always_better_for_a_check_valve\"><\/span>Is a higher Cv always better for a check valve?<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Not always. A higher Cv can reduce calculated \u0394P, but it may not improve the selection if the valve is oversized or cannot stay fully open at normal flow. Minimum flow, stable opening, closure behavior, and system dynamics must be checked together.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"When_should_a_low_pressure_drop_check_valve_be_selected\"><\/span>When should a low pressure drop check valve be selected?<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>A low pressure drop check valve may be considered when pump head margin is limited, energy loss is critical, flow rate is high, or the allowable \u0394P is strict. It should still be validated against the manufacturer\u2019s curve for the actual model, size, operating flow range, and installation condition.<\/p>\n<h3><span class=\"ez-toc-section\" id=\"Do_swing_check_valves_have_lower_pressure_drop_than_spring-loaded_check_valves\"><\/span>Do swing check valves have lower pressure drop than spring-loaded check valves?<span class=\"ez-toc-section-end\"><\/span><\/h3>\n<p>Often, but only when the swing check valve is fully open and stable. A swing check valve can have a more open flow path than some spring-loaded or lift designs, but actual pressure drop depends on manufacturer design, valve size, flow rate, disc stability, and installation condition.<\/p>\n<p><script type=\"application\/ld+json\"> { \"@context\": \"https:\/\/schema.org\", \"@type\": \"FAQPage\", \"mainEntity\": [ { \"@type\": \"Question\", \"name\": \"Is cracking pressure the same as pressure drop?\", \"acceptedAnswer\": { \"@type\": \"Answer\", \"text\": \"No. Cracking pressure is the differential pressure required to start opening a check valve. Pressure drop is the pressure loss across the valve during flow. A check valve may crack open before it is fully open, so cracking pressure should not be used as a substitute for operating pressure drop.\" } }, { \"@type\": \"Question\", \"name\": \"What does Cv mean for a check valve?\", \"acceptedAnswer\": { \"@type\": \"Answer\", \"text\": \"Cv is the flow coefficient of the check valve. It indicates the valve\u2019s flow capacity under defined conditions. A higher Cv generally means lower pressure drop at the same flow rate, but the valve must still open stably and suit the service conditions.\" } }, { \"@type\": \"Question\", \"name\": \"Is check valve head loss the same as pressure drop?\", \"acceptedAnswer\": { \"@type\": \"Answer\", \"text\": \"They describe the same energy-loss concept in different forms. Pressure drop is usually expressed as pressure difference, while head loss is expressed as height of fluid column, such as feet or meters of head. Always check the units before comparing data.\" } }, { \"@type\": \"Question\", \"name\": \"How do you calculate pressure drop across a check valve?\", \"acceptedAnswer\": { \"@type\": \"Answer\", \"text\": \"For an initial liquid-service estimate, engineers may use the Cv relationship with flow rate, specific gravity and valve Cv. The basic inputs are Q, SG, Cv, valve type and fluid condition. Final validation should use the manufacturer\u2019s pressure drop curve or Cv table for the specific valve model, size and operating flow range.\" } }, { \"@type\": \"Question\", \"name\": \"Does a check valve reduce pressure?\", \"acceptedAnswer\": { \"@type\": \"Answer\", \"text\": \"Yes. Every check valve creates some flow resistance and therefore some pressure loss during flow. In a well-designed system, this reduction is allowed for in the hydraulic calculation. In a poorly selected valve, it can become a noticeable system bottleneck.\" } }, { \"@type\": \"Question\", \"name\": \"Is a higher Cv always better for a check valve?\", \"acceptedAnswer\": { \"@type\": \"Answer\", \"text\": \"Not always. A higher Cv can reduce calculated \u0394P, but it may not improve the selection if the valve is oversized or cannot stay fully open at normal flow. Minimum flow, stable opening, closure behavior and system dynamics must be checked together.\" } }, { \"@type\": \"Question\", \"name\": \"When should a low pressure drop check valve be selected?\", \"acceptedAnswer\": { \"@type\": \"Answer\", \"text\": \"A low pressure drop check valve may be considered when pump head margin is limited, energy loss is critical, flow rate is high or the allowable \u0394P is strict. It should still be validated against the manufacturer\u2019s curve for the actual model, size, operating flow range and installation condition.\" } }, { \"@type\": \"Question\", \"name\": \"Do swing check valves have lower pressure drop than spring-loaded check valves?\", \"acceptedAnswer\": { \"@type\": \"Answer\", \"text\": \"Often, but only when the swing check valve is fully open and stable. A swing check valve can have a more open flow path than some spring-loaded or lift designs, but actual pressure drop depends on manufacturer design, valve size, flow rate, disc stability and installation condition.\" } } ] } <\/script><\/p>\n<h2><span class=\"ez-toc-section\" id=\"Conclusion_Match_Pressure_Drop_Data_to_Real_Operating_Conditions\"><\/span>Conclusion: Match Pressure Drop Data to Real Operating Conditions<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<p>Check valve pressure drop is not a single catalog value that can be applied to every system. It is affected by flow rate, Cv, head loss expression, valve type, internal design, medium properties, opening behavior, and installation condition.<\/p>\n<p>For early selection, Cv values, pressure drop charts, and head loss curves can help compare valve options. For final selection, the project should confirm the actual operating flow range, allowable \u0394P, medium, valve type, minimum flow, cracking pressure, and manufacturer-specific data.<\/p>\n<p>The best check valve is not simply the one with the lowest pressure drop. It is the valve that meets the hydraulic requirement while opening stably, closing reliably, and fitting the project\u2019s real operating conditions. That is the difference between a catalog match and a reliable engineering selection.<\/p>\n<div class=\"ntgd-cta-box\">\n<h2><span class=\"ez-toc-section\" id=\"Application_Specification_Support\"><\/span>Application \/ Specification Support<span class=\"ez-toc-section-end\"><\/span><\/h2>\n<p>If a misapplied check valve could lead to unstable operation, unexpected energy loss, pump margin issues, or premature wear, NTGD can review the pressure drop, Cv, and operating data before final selection.<\/p>\n<p>Prepare the operating flow range, medium details, specific gravity, viscosity, allowable \u0394P or head loss limit, preferred valve type, orientation, and any required datasheet or drawing format. This allows the valve engineer to check whether the selected check valve matches the real piping system instead of relying only on nominal size or a generic chart.<\/p>\n<\/div>\n","protected":false},"excerpt":{"rendered":"<p>\u041f\u043e\u0439\u043c\u0438\u0442\u0435, \u043a\u0430\u043a \u043f\u0435\u0440\u0435\u043f\u0430\u0434 \u0434\u0430\u0432\u043b\u0435\u043d\u0438\u044f \u0432 \u043e\u0431\u0440\u0430\u0442\u043d\u043e\u043c \u043a\u043b\u0430\u043f\u0430\u043d\u0435, \u043a\u043e\u044d\u0444\u0444\u0438\u0446\u0438\u0435\u043d\u0442 Cv \u0438 \u043f\u043e\u0442\u0435\u0440\u0438 \u0434\u0430\u0432\u043b\u0435\u043d\u0438\u044f \u0432\u043b\u0438\u044f\u044e\u0442 \u043d\u0430 \u0432\u044b\u0431\u043e\u0440 \u043a\u043b\u0430\u043f\u0430\u043d\u0430, \u0447\u0442\u0435\u043d\u0438\u0435 \u0434\u0438\u0430\u0433\u0440\u0430\u043c\u043c \u0438 \u0430\u043d\u0430\u043b\u0438\u0437 \u0437\u0430\u043f\u0440\u043e\u0441\u043e\u0432 \u043d\u0430 \u043f\u0440\u0435\u0434\u043b\u043e\u0436\u0435\u043d\u0438\u0435. \u0412 \u0434\u0430\u043d\u043d\u043e\u043c \u0440\u0443\u043a\u043e\u0432\u043e\u0434\u0441\u0442\u0432\u0435 \u043e\u0431\u044a\u044f\u0441\u043d\u044f\u044e\u0442\u0441\u044f \u043f\u0440\u0435\u0434\u0435\u043b\u044b \u0440\u0430\u0441\u0447\u0451\u0442\u0430, \u0440\u0430\u0437\u043b\u0438\u0447\u0438\u044f \u043c\u0435\u0436\u0434\u0443 \u0442\u0438\u043f\u0430\u043c\u0438 \u043a\u043b\u0430\u043f\u0430\u043d\u043e\u0432 \u0438 \u0440\u0438\u0441\u043a\u0438, \u0441\u0432\u044f\u0437\u0430\u043d\u043d\u044b\u0435 \u0441\u043e \u0441\u0442\u0430\u0431\u0438\u043b\u044c\u043d\u044b\u043c \u043e\u0442\u043a\u0440\u044b\u0442\u0438\u0435\u043c.<\/p>","protected":false},"author":1,"featured_media":10602,"comment_status":"open","ping_status":"open","sticky":false,"template":"","format":"standard","meta":{"_acf_changed":false,"_eb_attr":"","site-sidebar-layout":"default","site-content-layout":"","ast-site-content-layout":"default","site-content-style":"default","site-sidebar-style":"default","ast-global-header-display":"","ast-banner-title-visibility":"","ast-main-header-display":"","ast-hfb-above-header-display":"","ast-hfb-below-header-display":"","ast-hfb-mobile-header-display":"","site-post-title":"","ast-breadcrumbs-content":"","ast-featured-img":"","footer-sml-layout":"","theme-transparent-header-meta":"default","adv-header-id-meta":"","stick-header-meta":"","header-above-stick-meta":"","header-main-stick-meta":"","header-below-stick-meta":"","astra-migrate-meta-layouts":"set","ast-page-background-enabled":"default","ast-page-background-meta":{"desktop":{"background-color":"var(--ast-global-color-4)","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-opacity":"","overlay-gradient":""},"tablet":{"background-color":"","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-opacity":"","overlay-gradient":""},"mobile":{"background-color":"","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-opacity":"","overlay-gradient":""}},"ast-content-background-meta":{"desktop":{"background-color":"var(--ast-global-color-5)","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-opacity":"","overlay-gradient":""},"tablet":{"background-color":"var(--ast-global-color-5)","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-opacity":"","overlay-gradient":""},"mobile":{"background-color":"var(--ast-global-color-5)","background-image":"","background-repeat":"repeat","background-position":"center center","background-size":"auto","background-attachment":"scroll","background-type":"","background-media":"","overlay-type":"","overlay-color":"","overlay-opacity":"","overlay-gradient":""}},"footnotes":""},"categories":[45],"tags":[],"class_list":["post-10593","post","type-post","status-publish","format-standard","has-post-thumbnail","hentry","category-blog"],"acf":[],"_links":{"self":[{"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/posts\/10593","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/posts"}],"about":[{"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/types\/post"}],"author":[{"embeddable":true,"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/users\/1"}],"replies":[{"embeddable":true,"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/comments?post=10593"}],"version-history":[{"count":4,"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/posts\/10593\/revisions"}],"predecessor-version":[{"id":10609,"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/posts\/10593\/revisions\/10609"}],"wp:featuredmedia":[{"embeddable":true,"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/media\/10602"}],"wp:attachment":[{"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/media?parent=10593"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/categories?post=10593"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/ntgdvalve.com\/ru\/wp-json\/wp\/v2\/tags?post=10593"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}