U105 Nozzle Boot

U105 Nozzle Boot

Materials:

Body: Body: Aluminum (Spray-Painted)

Package:

Product ID Net Weight Cross Weight Dimension

U105-A 1.5kg/case of1 1.6kg/case of1 8.9×7.7×41cm/case of1

U105-B 1.7kg/case of1 1.8kg/case of1 8.9×7.7×41cm/case of1

U105-C 1.1kg/case of1 1.2kg/case of1 8.9×7.7×41cm/case of1

U105-D 1.3kg/case of1 1.4kg/case of1 8.9×7.7×41cm/case of1

U105-E 1.5kg/case of1 1.6kg/case of1 8.9×7.7×41cm/case of1

U105-F 1.7kg/case of1 1.8kg/case of1 8.9×7.7×41cm/case of1

U105-G 1.7kg/case of1 1.8kg/case of1 8.9×7.7×41cm/case of1

on quickly increase in recent year, consumption of finished oil increase al well, the vapor pollution and resource wa fuel dispenser ste in forecourt become more important safety factor in considerable filing station, safety distance and vapor density in particular. At present, vapor separator device is installed and obtain content effect in most of large and middle cities reference to foreign improving measures. Its recovery principle is divided as two phases: first phase refers to closed discharge from tank vehicle; second phase refers to vapor recovery as refueling oil. Phase I vapor-recovery system The first phase system aims at to rebuild the delivery pipe and vapor recovery pipe between vehicle tank and tank. (Diagram 4-1) The volume of vapor will be increased as flowing into tank because of waves and shock. Therefore, the inlet pipe should be deeply stretched under oil level so as to reduce oil waves. As for a tank exceeding 945L of volume, inlet pipe is needed stretching into oil no higher 15cm than bottom of tank. Oil flows into t fuel dispenser ank from under level, vapor flow back into vehicle tank under pressure. In principle, the volume of oil and vapor is corrective. In order to make as little as vapor volatize during delivery, the structure of traditional ventilating pipe should be improved, making system in sealed state under normal pressure range. Reclaimed vapor is dealt with through condensation, adsorption and burn after taking back. Its operation principle is similar to the vapor system of balanced nozzle. Diagram 4-1: Phase I Vapor Recovery System The pipeline installation is illustrating in Diagram 4-2. The height of air pipe at least 4m. The length of back air is shorter than air pipe, diameter larger than that of air pipe. It is prohibited to appear overflow phenomenon as vehicle tank discharge, shut off switch of air pipe. The jointer between air back and discharge pipe should adopt speed jointer. Phase II vapor-recovery system Phase II refers to the progress in which vapor in vehicle tank is fuel dispenser

If any abort of the operation is necessary it must be implemented within the EPS　　 fuel dispenser application. This request was not consistent with the rules of managing request one at a　　 time and it introduces complexity.　　 RepeatLastMessage Request to repeat the last message because the response was never received correctly.　　 This solution enables avoiding AckNak in the message transport. It can be used only　　 once the Timeout for the response is elapsed.　　 TotalAmount no.　　 SalesItems: no.　　 Loyalty: no.　　 OriginalTransaction: no.　　attributes Name Type fuel dispenser Use Annotation　　 RequestType CardRequestType Required Gives type of request see above detail.　　 ApplicationSende ApplicationType Optional Identifies the application sending the request. Used only for information　　 r logging purpose. (Unlikely more than one POS is present at one cash　　 desk!)　　 WorkstationID WorkstationIDType Required Identifies the logical workstation (associated to the socket) sending　　 the request: it can be only one at a time sending only one request at a　　 time.　　 Usually the POS (more than fuel dispenser

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