進口調節閥,進口球閥,進口截止閥,進口減壓閥,進口蝶閥,進口閘閥,進口高壓小型球閥,進口小型高壓球閥,進口…

進口調節閥如何選型

選擇進口調節閥時，首先要收集完整的工藝流體的物理特性參數與調節閥的工作條件，主要流體的成份、溫度、密度、粘度、正常流量、最大流量、最小流量、最大流量與最小流量下的進出口壓力、最大壓差等。而在技術方面主要掌握和確定調節閥本身的結構、流量特性、額定流量系數Kv值、口徑大小、工藝允許壓差計算及執行機構的選擇、材料和安裝等方面的內容。

選擇進口調節閥時一般應遵循的原則有如下幾點。一、首先從動力源來選擇，美國威盾VTON根據方便和反應速度的要求來選擇用什麼驅動方式的調節閥，主要有進口電動調節閥，進口氣動調節閥，進口自力式調節閥。二 調節閥的結構型式︰應能滿足介質溫度、壓力、流動性、流向、調節範圍以及嚴密性的要求。按結構分類主要有進口單座調節閥，進口雙座調節閥，進口套筒調節閥。三、 調節閥的流量特性︰應能滿足系統特性進行合理的補償。調節閥的流量特性是指介質流過閥的相對流量與閥桿相對位移間的關系，數學表達式如下︰Q/Qmax=f(l/L)，式中Q/Qmax為相對流量，為調節閥在某一開度時流量Q與全開流量Qmax之比；l/L為相對位移，調節閥在某一開度時閥芯位移l與全開位移L之比。選擇的總體原則是調節閥的流量特性應與調節對象特性及調節器特性相反，這樣可使調節系統的綜合特性接近于線性。選擇流量特性通常在工藝系統要求下進行，但是還要考慮下述實際情況。1、直線性流量特性適用範圍︰ヾ差壓變化小，幾乎恆定；ゝ工藝流程的主要參數的變化呈線性；ゞ系統壓力損失大部分分配在調節閥上(改變開度，閥上差壓變化相對較小)；々外部干擾小，給定值變化小，可調範圍要求小。2、等百分比特性適用範圍︰ヾ實際可調範圍大；ゝ開度變化，閥上差壓變化相對較大；ゞ管道系統壓力損失大；々工藝系統負荷大幅度波動；ぁ調節閥經常在小開度下運行。3、除了以上兩種常用的流量特性之外，還有拋物線特性和快開特性等其他流量特性的調節閥。四 調節閥的口徑︰應能滿足工藝上對流量的要求。有進口大口徑調節閥，進口小口徑調節閥。根據已知的流體條件，計算出必要的Kv值，選取合適的調節閥口徑。

Control valve selection and common sense Select the control valve, the first complete collection of the physical characteristics of the process fluid control valve parameters and operating conditions, the main fluid composition, temperature, density, viscosity, normal flow, maximum flow, minimum flow, maximum flow and minimum flow rate import and export pressure, maximum pressure and so on. In the technical aspects of the main control valve itself and determine the structure, flow characteristics, the rated flow coefficient Kv value, aperture size, technology allows the calculation of pressure and actuator selection, materials and installation aspects. Select the control valve when the general principles to be followed are the following. A valve structure type: should be able to meet the medium temperature, pressure, flow, flow, adjust the scope and rigor of the requirements. Two valve flow characteristics: the system should be able to meet the characteristics of reasonable compensation. Control valve flow characteristics is the medium flow through the valve stem relative to flow and the relationship between the relative displacement, mathematical expressions are as follows: Q / Qmax = f (l / L), where Q / Qmax for the relative flow rate, as adjusted When opening the valve at a flow rate Q and the ratio of full-flow Qmax; l / L for the relative displacement of the valve when the valve opening in a displacement l and the ratio of full-shift L. The overall principle is the selection control valve regulating the flow characteristics should be the object characteristics and regulator features the contrary, it will give a comprehensive control system features close to linear. Select the flow characteristics in the process is usually carried out under the system requirements, but also consider the following facts. 1, the linear flow characteristics of the scope of application: ヾ pressure change is small, almost constant; ゝ The main process parameter changes linearly; ゞ loss of most of the distribution system pressure control valve on the (change in opening the valve on the pressure change is relatively small); 々 external interference, given the value of small changes, small adjustable range of requirements. 2, the percentage of properties such as the scope of application: ヾ actual adjustable range; ゝ opening change, relatively large changes in differential pressure valve; ゞ large piping system pressure loss; 々 process system load fluctuations; ぁ valve often in small opening run. 3, in addition to the above two common flow characteristics, there are parabolic features and other features quick opening flow characteristics of control valve. Three valve diameter: should be able to meet the technical requirements on the traffic. According to the known fluid conditions, necessary to calculate the Kv value, select the appropriate valve diameter.