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全啟式安全閥
全啟式安全閥在達到整定壓力時瞬間全開,釋放全部喉部面積,使鍋爐、儲氣罐與容器周圍可壓縮或兩相服務的積壓迅速下降。產品範圍涵蓋彈簧加載結構,閥體為鑄鐵、WCB、SS304 或 SS316,內件組——噴嘴、調節環、閥盤、導向套與閥桿——為 2Cr13、SS304 或 SS316,碳鋼閥蓋與罩帽、鋼彈簧與 2Cr13 調整螺栓。工作壓力涵蓋 PN1.6 至 PN4.0 與 Class 150 至 Class 300,端接 NPT、RF 或 RTJ。設計依 API 520/521/526/527 洩放系列與 ASME 25.3,面距依 ASME B16.10、EN 558-1 或 DIN 3202,法蘭依 ASME B16.5、DIN 2543/2545 或 EN 12627,測試依 API 598 / DIN 323。操作處於狹窄邊際:約 10% 超壓(按規範為 3%-21%)換取全開啟,啟閉壓差(blowdown)-4% 至 -20% 決定回座點,且操作壓力必須低於回座點以避免前洩(simmer)——即 90-95% 整定壓力附近開始的閥座與閥盤間可聞洩漏。顫振(chatter)是可達數百赫茲的閥座-閥盤快速振盪,成因為入口損失過大(不可恢復的累計入口損失在銘牌排量下必須保持在整定壓力的 3% 以內)或選型過大,表現為閥座損傷、彈簧疲勞與閥桿咬傷;API 527 將金屬閥座洩漏限制在 90% 整定壓力,API 526 的 D-T 字母孔口框架面積選擇。選型取決於整定壓力對工作壓力區間、閥座與噴嘴材料對介質,以及管線的螺紋或法蘭端接。
屬於 安全閥 系列
最後更新: 2026-11
系列規格
| Set-pressure range | 0.1-10 MPa (0.1-2 at class 150; 1.6-5 at class 300; 3.2-10 at class 600) |
|---|---|
| Nominal valve connection size | DN32–DN150 |
| Valve body material | Cast Iron, WCB, SS304, SS316 |
| Nozzle Materials | 2Cr13, SS304, SS316 |
| Disc Materials | 2Cr13, SS304, SS316 |
| End connection types | NPT, RF, RTJ |
| Service temperature range | ≤300°C |
| Design standards | ASME 25.3, API 520, API 521, API 526, API 527 |
| Inspection and pressure-test standards | API 598, DIN 323 |
| Face-to-face dimensional standard | ASME B16.10, EN558-1, DIN 3202 |
| adjusting ring materials | 2Cr13, SS304, SS316 |
| guide sleeve materials | 2Cr13, SS304, SS316 |
| Bonnet material | Carbon Steel |
| spring materials | Steel |
| Stem material | 2Cr13, SS304, SS316 |
| adjusting bolt materials | 2Cr13 |
| cap materials | Carbon Steel |
| Working pressure (source-defined) | PN1.6, PN2.5, PN4.0, Class 150 to Class 300 |
| Flange standards | ASME B16.5, DIN 2543, DIN 2545, EN 12627 |
| overpressure allowance 10pct full lift | ASME/API practice allows roughly 10% overpressure for valves on unfired systems so the pop-action valve can achieve full lift and rated capacity; the huddling chamber assists the lift effort |
| overpressure typical range leser | Overpressure is usually expressed as a percentage of set pressure; a typical value is 10%, ranging between 3% and 21% depending on the code and application |
| blowdown definition crosby | Blowdown is the difference between the set pressure and the closing-point (reseat) pressure, expressed as a percentage of set pressure; where the closing point sits is determined by the control-chamber design |
| blowdown typical values leser | Typical blowdown values defined in codes and standards are -7% and -10%, ranging from -4% to -20% depending on the code and service (steam, gas or liquid) |
| operating margin vs blowdown crosby m11 | Operating pressure must stay below the reseating pressure: set at 100 psig with 7% blowdown the valve closes at 93 psig, so operation must remain below 93 psig to prevent leakage or flow from a partially open valve |
| inlet loss 3pct rule crosby | Inlet piping rule: the cumulative total of all non-recoverable inlet losses shall not exceed 3% of the valve set pressure, evaluated at nameplate capacity corrected for the flowing fluid; upstream system flow characteristics govern |
| chatter definition and causes valfonta | Chatter is the rapid oscillation of the plug on the valve seat - not ordinary vibration - with the moving component repeatedly striking the metal seat at frequencies that can reach hundreds of hertz; main drivers are excessive inlet-pipe pressure loss, oversizing and too-narrow blowdown margin, with seat/plug deformation, spring fatigue and stem galling as the damage modes |
| chatter cause summary projectmaterials | Chatter is rapid opening and closing of the valve disc, caused by excessive inlet pressure drop (over 3% of set pressure) or an oversized valve; simmer on spring-loaded valves begins at approximately 90-95% of set pressure |
| simmer definition crosby | Simmer is the audible or visible escape of fluid between the seat and disc at an inlet static pressure below the popping pressure and at no measurable capacity; it applies to safety or safety relief valves on compressible-fluid service |
| api527 seat leakage and api526 orifice | API 527 seat-tightness testing applies 90% of set pressure and limits metal-seated gas valves to 40 SCFH air up to 1,000 psig, and 0.60 SCFH air per inch of orifice diameter above 1,000 psig, while soft-seated valves must show zero leakage; API 526 standardizes orifice sizes by letter designation D through T, selected as the next larger standard orifice after the API 520 Part I required area |
| adjusting ring | 2Cr13, SS304, SS316 |
| guide sleeve | 2Cr13, SS304, SS316 |
| adjusting bolt | 2Cr13 |
| end connection | NPT, RF, RTJ |
| end connection dimension | ASME B16.5, DIN 2543, DIN 2545, EN 12627 |
範圍與來源備註
| overpressure wording | Overpressure wording: Crosby handbook gives the general 10% allowance for valves on unfired systems, while LESER states the code range spans 3%-21% by code and application; the page should quote 10% as typical, not as a universal limit. |
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訂購與文件
文件
請在詢問時一併說明您需要的文件組合——此結構的常見項目(材質證明、按所列檢驗標準的測試報告、尺寸圖)將於報價時確認並隨附供應。
報價
可直接報價的詢問應說明:公稱口徑與壓力額定、閥體與閥座材質偏好、端部連接、操作方式,以及含溫度的使用介質。本頁的典型值為基準參考範圍;具有約束力的數值於報價時確認。
樣品與供應
供應條件、訂購數量與交期按訂單議定——請在詢問時說明目的地國家與所需時程。
儲存與運輸
閥門儲存時應保護閥座與密封件免受紫外線、臭氧與變形影響,安裝前保留端面保護蓋;彈性體或 PTFE 閥座結構應避免長期戶外存放——閥座材料在陽光直射與冰凍條件下老化最快。
常見問題
全啟式安全閥的報價詢問應包含哪些內容?
執行標準與壓力等級、公稱口徑、閥體與閥座材質、介質及溫度、目的地——缺失的資訊會在報價過程中確認。
全啟式安全閥提供哪些口徑與壓力等級?
本頁面尚未公布該閥門經驗證的口徑與壓力等級範圍——適用於您工況的口徑與壓力等級會在報價過程中提出並確認。請在詢問時附上工況條件,選型結果會在報價中說明。
全啟式安全閥提供哪些閥體材質?
本頁面尚未公布該閥門經驗證的閥體材質範圍——適用於您工況的閥體材質會在報價過程中提出並確認。請在詢問時附上工況條件,選型結果會在報價中說明。
請求全啟式安全閥報價
在此提交需求——可直接報價的詢問應說明適用標準與等級、口徑、材質、介質、溫度與目的地.
您的資料如何處理,詳見我們的隱私權公告。
準備提出較大量或非標準需求? 全啟式安全閥詢價指南 說明應包含的內容、標準範圍與客製選項,以及應附上的文件。