API · ASME · DIN · EN 標準工業閥門
擴張式閘閥(expanding)
擴張式閘閥以機械方式密封:關閉時閘板組件向外擴張壓向兩側閥座,產生與管線壓力無關的雙向扭矩式密封,而組件在行程中於密封面之間自由移動以減少磨損、延長壽命——這是高溫高壓管線要求嚴密關斷時的選擇。產品範圍涵蓋 NPS 2" 至 12"(DN50 至 DN300),ASME Class 300 至 2500(PN40 至 PN420),閥體為碳鋼、不鏽鋼、合金鋼與雙相不鏽鋼,端接為 RF、BW 或 RTJ,操作為手動、氣動、電動或液動,設計依 API 6D。成就這些性能餘量的是設計細節:閥座環朝外,僅在端點位置接觸(凸輪固定的閘板段無摩擦移動,部分行程不磨損閥座)、密封僅靠閥桿推力壓緊——即使零壓差也雙向氣泡級密封,無需壓力助封——且全開通徑為連續通道,可通清管器且壓降如直管。關閉時同時密封兩側閥座,兩者之間的腔體可排放或排空,實現雙阻塞排放(DBB)隔斷。典型失效路徑為液體服務中的腔體熱超壓(應加裝腔體洩壓並保持針閥開啟)、調試雜物刮傷閥座嵌件(啟動前沖洗並清潔循環管線),以及填料過度緊固使本已偏高的楔式扭矩再加劇。在水平管線上直立安裝、手輪位於中心線上方,安裝前全開/全關活動閥門以發現閘板機構阻礙,並將兩個閥體中部注射口(保持在管線壓力以上約 300 psi 內)僅作緊急輔助密封,閥蓋排空口用於驗證關閉後腔體已洩壓。注意兩套 API 框架:API 6D 管線閥採 ISO 5208 洩漏等級(面距 API 6D/ASME B16.10、對焊端 B16.25、額定 B16.34),較小的井口閥則屬 API 6A——兩者不可互換。選型取決於尺寸段對管線、壓力等級對峰值壓力,以及閥座範圍對關斷任務的匹配。
屬於 閘閥 系列
最後更新: 2026-11
系列規格
| Nominal valve connection size | NPS 2"~12"(DN50~DN300) |
|---|---|
| Pressure class / nominal rating designation | ASME CLASS 300~2500(PN40~PN420) |
| Valve body material | Carbon steel, Stainless steel, Alloy steel, Duplex stainless steel |
| End connection types | RF, BW, RTJ |
| Operation / closure mode | Manual, Pneumatic, Electric, Hydraulic |
| Design standards | API 6D |
| selection seat ring life vs slab | Compared with a slab gate valve of the same size, an expanding gate design gives the full-bore pigging conduit together with longer seat-ring seal life, because the seat faces engage with the gate only near the end of travel rather than rubbing throughout the stroke. |
| selection torque tightened bidirectional seal | The two-segment gate is expanded against both seats by the stem/handwheel thrust, so the mechanical seal tightens as operating torque increases and does not depend on line pressure to energize it; this makes the shut-off bidirectional and relatively insensitive to pressure surges and vibration. |
| selection full bore pigging conduit | In the fully open position the gate segments retract into the body so the bore becomes a continuous cylindrical conduit, allowing pipeline pigs and scrapers to pass and keeping turbulence and pressure drop close to that of an equal length of pipe. |
| selection double block and bleed | In the closed position the expanded gate seals simultaneously against both the upstream and downstream seats, so the body cavity between the seats can be drained or vented, giving a double-block-and-bleed isolation function from a single valve. |
| selection seat faces shielded from flow | The seat rings are oriented to face outward so they contact the flow medium as little as possible and engage fully with the gate only at the end positions; this shielding of the sealing faces is a main reason expanding gates tolerate abrasive or debris-laden service better than wedge gates. |
| selection cam locks segments during travel | A cam/guide mechanism holds the two gate segments against expansion while the gate is mid-stroke: the assembly slides without seat friction during travel and expands only at the fully open or fully closed position, which protects the seats from wear during partial stroking. |
| selection stem thrust not pressure energized | Bubble-tight isolation is achieved upstream and downstream simultaneously purely through stem thrust on the wedge slopes; no line-pressure energizing of the seal is required, so sealing performance is maintained at low or zero differential pressure. |
| selection temperature envelope | Standard material trim covers roughly -29 C to 190 C service with low-temperature and extended-temperature options beyond that; published envelopes differ widely between makers, so the applicable temperature window must be confirmed against the specific body/seat materials rather than the generic design. |
| failure thermal cavity overpressure liquid service | With the gate expanded and both seats sealed, trapped liquid in the body cavity can build dangerous overpressure when the line warms up; valves for liquid service must therefore be fitted with a functioning thermal cavity relief system, and any needle valves in that circuit must be open before operation. |
| failure debris damages seat inserts | Scale, welding slag and other foreign material left in the pipeline are a leading cause of seat leakage at commissioning: debris packed between the gate segments and seat faces scratches the inserts. The line must be flushed and the valve cycled clean before it is put into service. |
| failure pre install cycle check for obstruction | Before installation the valve should be fully opened and closed once; if any abnormal resistance is felt, operation must stop and the stem and bore inspected for obstructions, since debris jammed in the gate-segment mechanism is easier to remove on the bench than in-line. |
| failure gland overtightening raises torque | Over-compressing the stem packing shortens packing life and noticeably raises operating torque, which matters for an expanding gate where the handwheel already works against wedge friction; the gland should be tightened only enough to stop leakage. |
| installation upright orientation recommended | The standard mounting is on a horizontal line with the stem vertical and the handwheel above the valve centerline, which keeps the gate-segment assembly aligned and supported; some makers qualify other orientations, and horizontal-stem or vertical-line installations require special design or tooling. |
| installation secondary sealant injection ports | Two sealant/lubricant injection ports in the body mid-section allow an approved sealant to be injected to the seat-gate interface as an emergency secondary seal if the sealing surfaces are damaged and leaking; injection pressure is kept within about 300 psi above line pressure. |
| installation cavity bleed via bonnet vent | With the valve fully closed, body-cavity pressure can be vented through the bonnet vent fitting (operator standing clear of the vent), and bottom drain plugs allow flushed-out debris to be removed; this gives a routine way to prove cavity depressurization after double-block-and-bleed closure. |
| standards api 6d vs api 6a envelopes | Expanding gate valves are made to two distinct API frames: pipeline valves to API 6D (roughly NPS 2-36, ASME Class 300-2500) and wellhead valves to API 6A (smaller bores at 2000-15000 psi working pressures); a 6D valve is not interchangeable with a 6A valve of similar size. |
| standards leakage testing iso 5208 api6d | Acceptance leakage testing for API 6D expanding gate valves is specified against ISO 5208 leakage-rate classes (with API 6D setting the class requirements per service), in addition to the standard hydrostatic shell and seat tests. |
| standards design codes b16 34 face to face | Pressure-boundary dimensions follow ASME B16.34 for pressure-temperature ratings, with face-to-face to API 6D/ASME B16.10, butt-weld ends to ASME B16.25, and welded-end/adapting-flange dimensions to ASME B16.34/MSS SP-44. |
| special features | Bi-directional torque based mechanical seal, Gate assembly travels freely between the seal surfaces which reduces the wear risk and prolongs the valve service life |
| applications | High temperature and high pressure pipelines |
範圍與來源備註
| temperature envelope disagreement | Temperature envelope disagreement: one OEM states -29 to 190 C standard (low-temp option to -46 C) while another claims -196 to +649 C working temperature; the wide claim likely reflects special trims and must not be used as the generic envelope. |
|---|---|
| orientation guidance differs | Orientation guidance differs: one OEM IOM recommends upright installation (handwheel above centerline), another states vertical as designed but horizontal acceptable, and a third offers special horizontal-stem/vertical-line designs; present as upright preferred with other orientations per manufacturer qualification. |
| torque comparison tension | Torque comparison tension: one OEM claims lower operating torque than an equivalent slab gate while the expanding design also deliberately uses higher seating torque to mechanically expand the gate - the statements refer to different points in the stroke and must not be merged into a single torque claim. |
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
擴張式閘閥(expanding)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。
擴張式閘閥(expanding)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。
擴張式閘閥(expanding)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。
請求擴張式閘閥(expanding)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? 擴張式閘閥(expanding)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。