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工业减压阀调节器调节方法(特殊工况篇)

工业减压阀调节器调节方法(特殊工况篇)

工业减压阀调节器调节方法(特殊工况篇)

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工业减压阀调节器调节方法(特殊工况篇)
特殊工况下的工业减压阀调节,需针对低温、高压、高粘度介质等复杂场景,突破常规调节逻辑,强化工况适应性与风险预判能力。此类场景中,减压阀不仅需满足压力控制精度(误差≤±3%),还需抵御介质相变、密封失效等特殊风险,例如在-40℃以下的低温工况中,介质易发生凝固导致阀芯卡阻;在20MPa以上的超高压工况中,阀瓣磨损速度是常规工况的3倍。因此,调节工作需以“工况适配、风险前置、动态监控”为核心原则,结合介质特性与设备结构制定专项方案。
调节前的准备工作需突出“工况适配性”升级。参数核对环节,除常规压力参数外,需额外确认介质的粘度(≥100mm²/s为高粘度)、凝点、饱和蒸气压等特殊参数,例如输送原油等高粘度介质时,需将下游工作压力适当提高5%-8%,补偿介质流动阻力损失。设备适配检查中,低温工况需更换耐低温的聚四氟乙烯密封件,避免密封件脆裂;超高压工况需选用锻造阀体的减压阀,检查阀座与阀瓣的配合间隙(应≤0.02mm),防止高压介质泄漏。仪表配置方面,高温工况(≥400℃)需选用热电偶式压力变送器,避免普通压力表因高温失效;强腐蚀工况需为仪表加装防腐隔离膜。工具准备上,新增介质加热装置(针对低温凝固介质)、高压密封测试泵、粘度计等专用设备,操作区域需增设应急泄压管路,配备防爆型通风设备(针对易燃易爆介质特殊工况)。
分步调节流程需强化“动态适配”与“风险控制”。以低温工况为例,第一步需启动介质加热装置,将介质温度升至凝点以上10-15℃,打开旁通阀进行管道预热,避免低温介质直接进入减压阀导致部件冻裂。开启上游截止阀时,采用“梯度升压”方式,每5分钟提升0.5MPa,直至达到上游额定压力的50%,稳定10分钟后再继续升压。初调阶段,针对高粘度介质,需将减压阀阀口开度调至常规工况的1.2倍,避免介质滞留导致阀芯粘结;对于超高压减压阀,初调压力需低于目标值20%,采用专用扭矩扳手控制调节螺杆旋转幅度,每次不超过1/16圈。精调阶段,引入“流量-压力联动调节”逻辑,通过调节下游流量调节阀改变介质流量,同时观测出口压力变化,当流量达到额定值的80%且压力稳定时,再进行最终微调。例如输送高粘度沥青时,需先将流量调至20m³/h(额定流量的50%),待压力稳定后逐步提升流量至额定值,同步微调减压阀确保压力恒定。
精度校验与安全防控需建立“动态监控体系”。精度校验采用“多节点监测法”,在减压阀进口、出口及下游5米处分别安装压力仪表,对比不同节点的压力损失,若损失超过0.1MPa,需检查管道是否堵塞或阀口是否磨损。特殊工况下的密封校验需采用专项方法,低温工况使用氦质谱检漏仪检测密封性能,超高压工况采用水压试验(试验压力为工作压力的1.5倍),持续30分钟无泄漏即为合格。安全防控中,新增“异常工况应急调节”步骤,例如当检测到介质温度骤降时,立即开启加热装置并适当开大减压阀开度;当出口压力突然升高超过额定值10%时,自动触发应急泄压阀,同时关闭上游截止阀。调节完成后,需进行24小时动态监测,每小时记录压力、温度、流量参数,绘制参数变化曲线,确保设备在全工况范围内稳定运行。操作人员需进行专项培训,熟悉特殊工况下的应急处置流程,避免因操作不当引发安全事故。

#关键词 工业使用

Adjustment method of industrial pressure reducing valve regulator (special operating conditions section)

The regulation of industrial pressure reducing valves under special working conditions requires breaking through conventional regulation logic and strengthening the adaptability and risk prediction ability for complex scenarios such as low temperature, high pressure, and high viscosity media. In such scenarios, the pressure reducing valve not only needs to meet the pressure control accuracy (error ≤± 3%), but also needs to resist special risks such as medium phase change and seal failure. For example, in low temperature conditions below -40 ℃, the medium is prone to solidification and cause valve core blockage; In ultra-high pressure conditions above 20MPa, the wear rate of the valve disc is three times that of conventional conditions. Therefore, the adjustment work needs to be based on the core principles of "working condition adaptation, risk pre positioning, and dynamic monitoring", combined with the characteristics of the medium and equipment structure to develop a special plan.

The preparation work before adjustment should highlight the upgrade of "working condition adaptability". In the parameter verification process, in addition to conventional pressure parameters, special parameters such as viscosity (≥ 100mm ²/s is considered high viscosity), pour point, and saturated vapor pressure of the medium need to be confirmed. For example, when transporting high viscosity media such as crude oil, the downstream working pressure needs to be appropriately increased by 5% -8% to compensate for the loss of medium flow resistance. During the equipment adaptation inspection, it is necessary to replace the low-temperature resistant polytetrafluoroethylene seals under low temperature conditions to avoid seal brittleness and cracking; For ultra-high pressure conditions, a forged valve body pressure reducing valve should be selected, and the fit clearance between the valve seat and the valve disc should be checked (should be ≤ 0.02mm) to prevent leakage of high-pressure medium. In terms of instrument configuration, thermocouple pressure transmitters should be selected for high temperature conditions (≥ 400 ℃) to avoid the failure of ordinary pressure gauges due to high temperature; Strong corrosion conditions require the installation of anti-corrosion isolation film for instruments. In terms of tool preparation, specialized equipment such as medium heating devices (for low-temperature solidification media), high-pressure sealing test pumps, viscosity meters, etc. have been added. Emergency pressure relief pipelines need to be added to the operating area, and explosion-proof ventilation equipment (for special working conditions of flammable and explosive media) should be equipped.

The step-by-step adjustment process needs to strengthen "dynamic adaptation" and "risk control". Taking low-temperature working conditions as an example, the first step is to start the medium heating device, raise the medium temperature to 10-15 ℃ above the condensation point, open the bypass valve for pipeline preheating, and avoid the low-temperature medium directly entering the pressure reducing valve and causing component freezing and cracking. When opening the upstream shut-off valve, use the "gradient boosting" method to increase the pressure by 0.5 MPa every 5 minutes until it reaches 50% of the upstream rated pressure. After stabilizing for 10 minutes, continue to increase the pressure. In the initial adjustment stage, for high viscosity media, the opening of the pressure reducing valve should be adjusted to 1.2 times that of the normal operating conditions to avoid medium retention and valve core adhesion; For ultra-high pressure reducing valves, the initial adjustment pressure should be 20% lower than the target value, and a dedicated torque wrench should be used to control the rotation amplitude of the adjusting screw, with no more than 1/16 turn each time. In the fine-tuning stage, the logic of "flow pressure linkage regulation" is introduced to change the medium flow rate by adjusting the downstream flow control valve, while observing the change in outlet pressure. When the flow rate reaches 80% of the rated value and the pressure is stable, the final fine-tuning is carried out. For example, when transporting high viscosity asphalt, it is necessary to first adjust the flow rate to 20m ³/h (50% of the rated flow rate), gradually increase the flow rate to the rated value after the pressure stabilizes, and synchronously adjust the pressure reducing valve to ensure constant pressure.

Precision verification and safety prevention and control require the establishment of a "dynamic monitoring system". The accuracy verification adopts the "multi node monitoring method", and pressure instruments are installed at the inlet, outlet, and downstream 5 meters of the pressure reducing valve to compare the pressure loss at different nodes. If the loss exceeds 0.1 MPa, it is necessary to check whether the pipeline is blocked or whether the valve port is worn. Special methods are required for sealing verification under special working conditions. Helium mass spectrometer leak detector is used to detect sealing performance under low-temperature working conditions, and water pressure test is used under ultra-high pressure working conditions (test pressure is 1.5 times the working pressure). If there is no leakage for 30 minutes, it is considered qualified. In safety prevention and control, a new step of "emergency adjustment for abnormal working conditions" has been added, such as immediately turning on the heating device and appropriately increasing the opening of the pressure reducing valve when a sudden drop in medium temperature is detected; When the outlet pressure suddenly increases by more than 10% of the rated value, the emergency relief valve is automatically triggered and the upstream shut-off valve is closed. After the adjustment is completed, 24-hour dynamic monitoring is required, recording pressure, temperature, and flow parameters every hour, and drawing parameter change curves to ensure stable operation of the equipment within the entire operating range. Operators need to receive specialized training, familiarize themselves with emergency response procedures under special working conditions, and avoid safety accidents caused by improper operation.

#Keywords: industrial use




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