20xx年cvm公司太平镁厂管理制度规程汇编(编辑修改稿)

20xx年cvm公司太平镁厂管理制度规程汇编(编辑修改稿)内容摘要：

en facing OUTWARDS to reduce obstruction footprint in an event of evacuation. o The PersonInCharge shall monitor all personnel in the facilities constantly:  Only authorized personnel shall be allowed to operate any equipment such as valves, regulators, gauges, etc.  All personnel entering to the facility shall only perform their designated task in their designated zones and shall not be permitted to wander around the facility.  The PersonInCharge shall control and limit the number of persons entering the facility. There shall be no more than 5 persons present in the facility at any given time. Observers, visitors or person not directly involve in the duties carried out in the facility shall only be allowed into the facility no longer than thirty (30) minutes.  In the event where more than 5 personnel is required for the designated duties in the facility, the PersonInCharge shall be responsible to seek for approval from both the Section Head of Engineering Department and the Safety and Health Officer on duty. Each PersonInCharge shall be monitoring not more than 5 working personnel at any one time. II. EXIT FROM AND ISOLATION OF THE FACILITY o All personnel exiting the facility before the pletion of designated task/duties shall report to the PersonInCharge.  The PersonInCharge shall be responsible to ensure that any inplete task/duties is properly sealed and is leakfree before discharging the personnel. o All personnel shall assemble outside of the facility in the designated assembly point and a head count shall be carried out. o The PersonInCharge shall ensure that all personnel are accounted for. Should there be personnel missing, a search party of two (2) persons shall be anized to locate and escort the said person out. o Upon all persons accounted for, the PersonInCharge shall shut and lock all access / exit gates. Description This safety rules and guidelines describe the necessity action and precautions for all personnel preparing and later putting the fuel gas piping system into operation. Objective The objective of this document is to ensure that all authorized personnel preparing and putting the fuel gas piping system into operation is done in a safe manner. This involves the operation of the correct ponents in the system to provide flow to whichever portion required. Important preparations I. Quantify and verify the operating parameters – pressure, temperature and volume for the ining portion and the actual piping system meant to be put into operation. II. Identify and rectify ponents that had been operated for isolating the piping system, specifically: o Isolation valves shall be returned to closed position. o Spectacle or paddle blinds shall be engaged to OPEN position. o Removable spool pieces shall be installed back in position. o Flanges that been disengaged shall be installed back in position. III. Identify bleed or vent points in the section. These shall be in SHUT position and ONLY operate when REQUIRED. Instructions I. Crack open the equalizing valve at the most upstream portion of the piping system to start flow. o In the absence of equalizing valve, crack open the most upstream main line isolation valve. II. Leaving the valve in cracked open position, the line pressure shall be allowed to stabilize. o While introducing the medium into the pipe work, ensure that NO SOURCE OF IGNITION is present within 3 meters from the pipe work and exit point of the fluid. NOTE: Cracking open a valve involves opening the valve as slowly and as little as practicable until an indication of slow is detected. There will be a hissing noise as the gas starts to exit the valve orifice. This will stop once the line pressure is stabilized. o Source of ignition include, but are not limited to naked flames, embers, hot surface (150oc or 25oc lower than the autoignition temperature, whichever is lower) and nonintrinsically safe electrical connections. o Depending on the position of the fluid in the pipe work prior to putting it into operation, the vent or bleed valve may be operated to allow the displaced initial fluid to escape. During this venting/bleeding/purging process, PersonInCharge is to make sure that everyone within the 30m radius is made known. NO SOURCE OF IGNITION mentioned should be present within 15m radius during this purging. III. When the piping system have been filled and stabilized: o The main line isolation valve shall be operated to the intended operating position. o The vent or bleed valve shall be returned to SHUT position. o Valve Lock Out and Tag Out (LOTO) procedures shall be applied, if applicable. IV. Monitoring After Commencing Operation o PersonInCharge is required to periodically inspect the portion of pipe work that had been put into operation to verify its integrity. Instructions Scope And safetyrelated responsibilities for LPG station Access and movement of LPG container carrier trucks within the industrial pound 1. Container carrier trucks must have a entry card issued by the CVM Magnesium security force in order to access the factory area 2. The vehicle will be subjected to a search and full inspection in case of any leakage or damage on containers before access to the factory. 3. The driver of the container carrier truck must maintain the vehicle speed require when moving within the factory area. 4. The security must ensure that the vehicle plies with all of the stipulations in the abovementioned instructions, vehicle condition and movement instructions. Safety instructions for handling operations in stations 1. Before any filling or transferring of LPG operation begin the container carrying vehicle, must ensure that:  The trucks is immobilised using brakes.  Container c。