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ÇöÀç Á¦°¡ ´ã´çÇÏ°í ÀÖ´Â Unit Àº HMB Case °¡ 4°¡ÁöÀÔ´Ï´Ù. µû¶ó¼, Pump design case ¼±Á¤ ½Ã Max Volumetric flowrate case ·Î Pump design case ¸¦ ¼±Á¤Çߴµ¥ ÀÌ¿Í °°ÀÌ ¼±Á¤ÇÑ ¸íÈ®ÇÑ ÀÌÀ¯°¡ ÀÖ´ÂÁö ¾Ë°í ½Í½À´Ï´Ù.
Á¦°¡ ¾Ë±â·Î´Â »ó´ëÀûÀ¸·Î ÀûÀº case ·Î design case ¸¦ ¼±ÅÃÇϸé Pump performance curve »ó Max allowable shut off head °¡ Áõ°¡ÇÏ¿©, Pump discharge line ÀÇ design pressure °¡ ÀÌÀ¯ ¾øÀÌ ³ô¾Æ Áú ¼ö Àֱ⠶§¹®À¸·Î ¾Ë°í ÀÖ½À´Ï´Ù.(ÀÌ°Í ¶ÇÇÑ ¸íÈ®ÇÏÁö ¾Ê½À´Ï´Ù.) µû¶ó¼ ¾Æ·¡¿Í °°ÀÌ Áú¹® µå¸³´Ï´Ù.
Q1. HMB Case °¡ ¿©·¯ °³ ÀÏ ¶§ Pump design case ¼±Á¤ ½Ã Maximum volumetric flowrate case ·Î ¼±ÅÃÇØ¾ß ÇÏ´Â ÀÌÀ¯¿¡ ´ëÇØ ¼³¸í ºÎŹ µå¸³´Ï´Ù. ȤÀº ´Ù¸¥ ±âÁØÀÌ ÀÖ´Ù¸é ¼³¸í ºÎŹµå¸³´Ï´Ù.
Q2. ¸¸¾à HMB case°¡ A¿Í B case °¡ ÀÖÀ» ¶§, A case °¡ max volumetric flowrate case ÀÌ°í, B case ´Â A case ¿Í À¯·® Â÷ÀÌ°¡ °ÅÀÇ ¾ø´Â »óȲ + B case ¿¡¼ÀÇ density °¡ A case º¸´Ù À۾Ƽ suction line pressure drop ÀÌ ¸¹ÀÌ ¹ß»ýÇÏ¿© B case ¿¡¼ÀÇ NPSHa °¡ A case ¿¡¼ÀÇ NPSHa º¸´Ù ÀÛÀ» ¶§
Áï, B case NPSHa < A case NPSHa ÀÏ ¶§ Pump Vendor ÀÔÀå¿¡¼´Â NPSHa NPSHr °£ ÃæºÐÇÑ margin À» µÖ¾ßÇϱ⠶§¹®¿¡ Vendor ¿¡°Ô´Â B csae °¡ ´õ severeÇÑ case ¶ó°í »ý°¢Çϴµ¥ ÀÌ·² ¶§¿¡ µµ maximum volumetric flowrate ±âÁØÀ¸·Î¸¸ design case ¸¦ ¼³Á¤ÇÏ´Â°Ô ¸Â´ÂÁö ±Ã±ÝÇÕ´Ï´Ù.
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