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ฐานข้อมูล K-Factor ของฟิตติ้ง
สัมประสิทธิ์การสูญเสีย (K-factor) สำหรับฟิตติ้ง วาล์ว และอุปกรณ์ประกอบท่อ ใช้ในสมการการสูญเสียรอง: hm = K V2/2g
37 จาก 37 ฟิตติ้ง
| ประเภทฟิตติ้ง | รูปแบบ | K Factor | หมวดหมู่ | แหล่งอ้างอิง | หมายเหตุ |
|---|---|---|---|---|---|
| 90 deg Elbow | Standard radius (r/D = 1) | 0.90 (0.7-1.0) | elbow | Crane TP-410 | Screwed fitting. K = 30 f_T for standard radius. |
| 90 deg Elbow | Long radius (r/D = 1.5) | 0.60 (0.4-0.7) | elbow | Crane TP-410 | K = 20 f_T. Most common welded elbow in process piping. |
| 90 deg Elbow | Short radius (r/D = 0.5) | 1.50 (1.2-1.8) | elbow | Idelchik | Tight bend. Higher loss than standard. Avoid where possible. |
| 90 deg Elbow | Mitre (no vanes) | 1.10 (1.0-1.3) | elbow | Crane TP-410 | Sharp corner. Used where fabrication convenience outweighs losses. |
| 90 deg Elbow | Mitre (with vanes) | 0.20 (0.15-0.25) | elbow | Idelchik | Turning vanes dramatically reduce losses in rectangular duct bends. |
| 45 deg Elbow | Standard radius | 0.40 (0.3-0.5) | elbow | Crane TP-410 | K = 16 f_T. Approximately half the loss of a 90-degree elbow. |
| 45 deg Elbow | Long radius | 0.20 (0.15-0.25) | elbow | Crane TP-410 | Welded. Low loss fitting for direction changes. |
| 180 deg Return Bend | Standard | 2.20 (1.5-2.5) | elbow | Crane TP-410 | K = 50 f_T. High loss due to complete flow reversal. |
| Tee | Branch flow (diverging) | 1.80 (1.0-2.0) | tee | Crane TP-410 | K = 60 f_T. Flow splitting into branch. Higher loss than run-through. |
| Tee | Run-through (line flow) | 0.60 (0.3-0.9) | tee | Crane TP-410 | K = 20 f_T. Flow continuing straight through the tee. |
| Tee | Branch flow (converging) | 1.20 (0.8-1.5) | tee | Crane TP-410 | Flow merging from branch. Slightly less loss than diverging. |
| Cross | Branch flow | 2.00 (1.5-2.5) | tee | Idelchik | Four-way intersection. Rarely used in modern piping. |
| Reducer | Concentric (gradual contraction) | 0.15 (0.05-0.3) | reducer | Crane TP-410 | K depends on area ratio (d/D)^2 and cone angle. Values for 20-40 degree cone. |
| Reducer | Sudden contraction (d/D = 0.5) | 0.37 (0.3-0.5) | reducer | Idelchik | K = 0.5(1 - (d/D)^2). Based on smaller (downstream) velocity head. |
| Expansion | Gradual (diffuser, 7 deg cone) | 0.15 (0.1-0.25) | reducer | Miller | Optimal cone half-angle 3-4 degrees. K based on upstream velocity head. |
| Expansion | Sudden expansion (D/d = 2) | 0.56 (0.4-0.8) | reducer | Borda-Carnot | K = (1 - (d/D)^2)^2. Exact from momentum theory. Based on smaller (upstream) velocity. |
| Pipe Entrance | Sharp-edged (flush) | 0.50 | entrance | Crane TP-410 | Pipe flush with tank wall. Most common entrance condition. |
| Pipe Entrance | Re-entrant (projecting) | 0.78 (0.5-1.0) | entrance | Crane TP-410 | Pipe projecting into tank. Additional vena contracta effect. |
| Pipe Entrance | Well-rounded (r/D > 0.15) | 0.04 (0.03-0.1) | entrance | Idelchik | Bell-mouth entrance. Very low loss. Used in pump suction piping. |
| Pipe Entrance | Slightly rounded (r/D = 0.05) | 0.25 (0.1-0.3) | entrance | Idelchik | Small radius on entrance edge significantly reduces loss from sharp-edged. |
| Pipe Exit | Sharp-edged (into tank) | 1.00 | exit | Crane TP-410 | All kinetic energy is lost. K = 1.0 regardless of exit geometry. |
| Pipe Exit | Submerged discharge | 1.00 | exit | Fundamental | Velocity head is fully dissipated. Same as sharp-edged exit. |
| Gate Valve | Fully open | 0.17 (0.1-0.2) | valve | Crane TP-410 | K = 8 f_T. Very low loss when fully open. Primary isolation valve. |
| Gate Valve | 75% open | 0.90 | valve | Crane TP-410 | Loss increases rapidly as valve closes. Not suitable for throttling. |
| Gate Valve | 50% open | 4.50 | valve | Crane TP-410 | Very high loss. Avoid operating gate valves in partially open position. |
| Globe Valve | Fully open | 10.00 (6-15) | valve | Crane TP-410 | K = 340 f_T. High loss due to tortuous flow path. Good for throttling. |
| Ball Valve | Full bore, fully open | 0.05 (0.03-0.1) | valve | Crane TP-410 | Very low loss. Quarter-turn operation. Common replacement for gate valves. |
| Ball Valve | Reduced bore, fully open | 0.15 (0.1-0.5) | valve | Crane TP-410 | Port diameter smaller than pipe. K depends on area ratio. |
| Butterfly Valve | Fully open | 0.25 (0.2-0.5) | valve | Crane TP-410 | K = 45 f_T. Disc always in flow path. Good for large diameter throttling. |
| Check Valve | Swing type | 2.00 (1.0-2.5) | valve | Crane TP-410 | K = 100 f_T. Prevents backflow. Higher loss than other valve types. |
| Check Valve | Lift type | 10.00 (5-15) | valve | Crane TP-410 | K = 600 f_T. Globe-style body. Use only in horizontal pipe. |
| Check Valve | Wafer (dual plate) | 0.80 (0.5-1.5) | valve | Manufacturer | Low profile. Lower loss than swing check. Suitable for vertical installation. |
| Strainer | Y-type (clean) | 2.00 (1.5-3.0) | other | Manufacturer | Clean strainer. Loss increases as screen fouls. Monitor differential pressure. |
| Strainer | Basket type (clean) | 1.50 (1.0-2.5) | other | Manufacturer | Larger screen area than Y-type. Used in pump suction lines. |
| Flow Meter | Orifice plate (beta = 0.5) | 7.50 (5-30) | other | ISO 5167 | Permanent pressure loss depends on beta ratio (d/D). Higher beta = lower loss. |
| Flow Meter | Venturi (beta = 0.5) | 0.50 (0.3-1.0) | other | ISO 5167 | Much lower permanent loss than orifice. Recovers most of the differential pressure. |
| Coupling / Union | Threaded | 0.08 | other | Crane TP-410 | Negligible loss for welded or flanged joints (K ~ 0). |
หมายเหตุ
K factor คือสัมประสิทธิ์การสูญเสียแบบไร้มิติ ใช้ในสมการ: hm = K · V2 / 2g โดย V คือความเร็วเฉลี่ย และ g คือความเร่งเนื่องจากแรงโน้มถ่วง
ค่าที่แสดงเป็นค่าทั่วไปสำหรับการไหลแบบปั่นป่วนเต็มที่ (Re > 105) ที่ Reynolds number ต่ำกว่า ค่า K อาจสูงกว่านี้
วิธีการ Crane TP-410 แสดงค่า K เป็นผลคูณของสัมประสิทธิ์แรงเสียดทานแบบปั่นป่วนเต็มที่ fT(เช่น K = 30 fT สำหรับข้อศอก 90 องศามาตรฐาน) ทำให้ K ขึ้นกับขนาด ค่าที่แสดงที่นี่เป็นตัวแทนสำหรับขนาด DN50-DN150
แหล่งอ้างอิง: Crane TP-410 (2018), Idelchik Handbook of Hydraulic Resistance (ฉบับที่ 3), Miller Internal Flow Systems (1990), ISO 5167