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工业减压阀调节器调节方法(常规工况篇)

工业减压阀调节器调节方法(常规工况篇)

工业减压阀调节器调节方法(常规工况篇)

详细介绍

工业减压阀调节器调节方法(常规工况篇)
在工业生产体系中,减压阀调节器是流体输送系统的核心压力控制部件,广泛应用于石油化工、电力冶金、生物医药等领域,其核心功能是将上游管道或容器内的高压流体(压力范围通常为1.6-10MPa)稳定减压至下游设备所需的工作压力(0.1-1MPa不等),同时抵御流量波动、介质温度变化等干扰因素,保障生产工艺的连续性与安全性。与家用燃气减压阀相比,工业级减压阀结构更复杂,常见类型包括活塞式、波纹管式及先导式等,调节精度要求更高(压力误差需控制在±5%以内),因此必须建立标准化的调节流程,结合工况参数与设备特性科学操作。
调节前的系统性准备是规避操作风险的基础,核心在于“参数核对、状态排查、工具到位”。首先需明确工艺文件中的压力要求,上游输入压力、下游工作压力及最大允许波动值需精准记录,同时确认减压阀的型号规格(如公称直径、压力等级、介质兼容性)与工况匹配——例如输送腐蚀性介质时需使用衬氟材质减压阀,高温工况则需选用耐高温密封件。其次进行设备状态检查:关闭减压阀前后的截止阀,打开旁通阀平衡压力,拆卸过滤器端盖清理杂质,防止阀芯卡阻;检查压力表、压力变送器等附属仪表的校准状态(校准有效期需在3个月内),用氮气对管道进行吹扫,确保无残留介质或杂物。最后准备专用工具,包括扭矩扳手、压力校验仪、密封脂及备用密封垫,同时在操作区域设置警示标识,配备便携式可燃气体检测仪(针对易燃易爆介质)或有毒气体检测仪,操作人员需穿戴防静电工作服、防护手套及护目镜。
分步调节流程需遵循“缓慢升压、精准微调、稳定观测”的原则,避免压力骤变对下游设备造成冲击。第一步是开启上游截止阀,采用“间歇式开启”方式,将阀门开度控制在1/4圈,待上游压力稳定后(通过压力表观测,波动值≤0.05MPa),关闭旁通阀。第二步是初调减压阀,对于活塞式减压阀,顺时针旋转调节螺杆压缩弹簧,推动活塞下移缩小阀口开度,降低出口压力;波纹管式减压阀则通过调节螺母改变波纹管的伸缩量,间接控制阀瓣开度。初调阶段需将出口压力调至低于目标压力10%-15%,例如目标压力为0.5MPa时,初调至0.42-0.45MPa。第三步是精调与状态观测,缓慢开启下游截止阀至1/3开度,让流体缓慢通过减压阀,此时通过压力校验仪实时监测出口压力,顺时针微调调节部件提升压力,逆时针旋转降低压力,每次调节幅度控制在调节螺杆1/8圈以内,避免超调。当压力稳定在目标值后,将下游截止阀完全打开,持续观测30分钟,记录压力波动情况,确保波动值符合工艺要求。
精度校验与安全防控是调节工作的收尾关键。精度校验可采用“双仪表比对法”,将便携式压力校验仪与管道压力表同时接入出口端,对比两者读数,若误差超过±5%,需重新微调并检查仪表接线或传感元件。对于先导式减压阀,还需校验先导阀的响应灵敏度,通过瞬时增大下游流量(如开启备用支路),观察主阀压力恢复时间,正常情况下应≤3秒。安全防控方面,调节完成后需关闭上下游截止阀,对减压阀法兰连接处进行气密性测试,采用肥皂水涂抹密封面,无气泡产生即为合格;同时整理调节记录,标注调节时间、操作人员、压力参数及设备状态,建立设备档案。若调节过程中出现压力骤升或阀芯卡涩,应立即关闭上游截止阀,打开泄放阀降压,排查故障后重新进行调节操作,严禁在压力异常状态下强行调节。

#关键词 工业使用

Adjustment Method of Industrial Pressure Reducing Valve Regulator (Conventional Operating Conditions)

In industrial production systems, pressure reducing valve regulators are the core pressure control components of fluid transport systems, widely used in fields such as petrochemicals, power metallurgy, and biomedicine. Their core function is to stabilize and reduce the pressure of high-pressure fluids (usually ranging from 1.6-10MPa) in upstream pipelines or containers to the working pressure required by downstream equipment (ranging from 0.1-1MPa), while resisting interference factors such as flow fluctuations and medium temperature changes, ensuring the continuity and safety of production processes. Compared with household gas pressure reducing valves, industrial grade pressure reducing valves have a more complex structure, with common types including piston type, bellows type, and pilot type. They require higher regulation accuracy (pressure error must be controlled within ± 5%), so it is necessary to establish a standardized regulation process and operate scientifically based on operating parameters and equipment characteristics.

Systematic preparation before adjustment is the foundation for avoiding operational risks, with the core being "parameter verification, status investigation, and tool deployment". Firstly, it is necessary to clarify the pressure requirements in the process documents. The upstream input pressure, downstream working pressure, and maximum allowable fluctuation value should be accurately recorded. At the same time, the model and specifications of the pressure reducing valve (such as nominal diameter, pressure rating, medium compatibility) should be confirmed to match the working conditions - for example, fluorine lined pressure reducing valves should be used when transporting corrosive media, and high-temperature sealing components should be selected for high-temperature working conditions. Next, perform equipment status check: close the shut-off valves before and after the pressure reducing valve, open the bypass valve to balance the pressure, remove the filter end cover to clean impurities, and prevent valve core blockage; Check the calibration status of auxiliary instruments such as pressure gauges and pressure transmitters (calibration validity period should be within 3 months), blow the pipeline with nitrogen to ensure that there is no residual medium or debris. Finally, prepare specialized tools including torque wrenches, pressure calibrators, sealing grease, and spare sealing gaskets. At the same time, set up warning signs in the operating area, equip with portable combustible gas detectors (for flammable and explosive media) or toxic gas detectors, and operators need to wear anti-static work clothes, protective gloves, and goggles.

The step-by-step adjustment process should follow the principle of "slow pressure rise, precise adjustment, and stable observation" to avoid the impact of sudden pressure changes on downstream equipment. The first step is to open the upstream shut-off valve using an "intermittent opening" method, controlling the valve opening at 1/4 turn. After the upstream pressure stabilizes (with a fluctuation value of ≤ 0.05MPa observed through a pressure gauge), close the bypass valve. The second step is to initially adjust the pressure reducing valve. For piston type pressure reducing valves, rotate the adjusting screw compression spring clockwise to push the piston downwards to reduce the valve opening and lower the outlet pressure; The bellows type pressure reducing valve indirectly controls the valve disc opening by adjusting the nut to change the expansion and contraction of the bellows. In the initial adjustment stage, the outlet pressure needs to be adjusted to 10% -15% lower than the target pressure. For example, when the target pressure is 0.5MPa, it should be initially adjusted to 0.42-0.45MPa. The third step is fine tuning and status observation. Slowly open the downstream shut-off valve to 1/3 opening, allowing the fluid to slowly pass through the pressure reducing valve. At this time, monitor the outlet pressure in real time through a pressure calibrator. Adjust the adjusting component clockwise to increase the pressure, and counterclockwise to decrease the pressure. The adjustment amplitude should be controlled within 1/8 turn of the adjusting screw each time to avoid overshoot. After the pressure stabilizes at the target value, fully open the downstream shut-off valve, observe continuously for 30 minutes, record the pressure fluctuation, and ensure that the fluctuation value meets the process requirements.

Accuracy verification and safety prevention and control are the key to the completion of regulation work. Accuracy verification can be carried out using the "dual instrument comparison method". The portable pressure calibrator and pipeline pressure gauge can be connected to the outlet end at the same time, and the readings of the two instruments can be compared. If the error exceeds ± 5%, the instrument wiring or sensing components need to be re adjusted and checked. For pilot operated pressure reducing valves, it is also necessary to verify the response sensitivity of the pilot valve. By instantaneously increasing the downstream flow (such as opening the backup branch), observe the pressure recovery time of the main valve. Under normal circumstances, it should be ≤ 3 seconds. In terms of safety prevention and control, after the adjustment is completed, the upstream and downstream shut-off valves should be closed, and the flange connection of the pressure reducing valve should be tested for airtightness. The sealing surface should be coated with soapy water, and if no bubbles are generated, it is considered qualified; At the same time, organize adjustment records, label adjustment time, operators, pressure parameters, and equipment status, and establish equipment files. If there is a sudden increase in pressure or a stuck valve core during the adjustment process, the upstream shut-off valve should be immediately closed, the relief valve should be opened to reduce pressure, and the fault should be investigated before resuming the adjustment operation. It is strictly prohibited to forcibly adjust under abnormal pressure conditions.




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