Process to prevent vapor blockage for stage II vapor recovery

• US 5,199,471 A
• Filed: 03/04/1991
• Issued: 04/06/1993
• Est. Priority Date: 03/04/1991
• Status: Expired due to Term

• Current Assignee: Amoco Corporation (BP PLC)
• Original Assignee: Amoco Corporation (BP PLC)
• Inventors: Koch, Wolfgang H., Hartman, Harry B., Strock, Dennis J., Butkovich, Michael S.
• Primary Examiner(s): Recla, Henry J.
• Assistant Examiner(s): JACYNA, J CASIMER
• Application Number:
  US07/664,329
• Time in Patent Office: 764 Days
• Field of Search: 141/44-46, 141/59, 141/206-210, 141/217, 141/218, 141/225-228, 141/94, 141/301, 141/302, 141/102, 141/103, 141/104, 141/99, 141/1, 141/4, 141/5, 141/7, 141/8, 141/98, 141/392 , 141/83, 137/234.6, 222/14-16, 222/2
• US Class Current: 141/5
• CPC Class Codes: B67D 7/0488 Means for preventing the formation of condensation on, or for removing condensation from, vapour recovery lines
• CPC Class Codes: B67D 7/54 with means for preventing escape of liquid or vapour or for recovering escaped liquid or vapour B67D7/44 takes precedence
• CPC Class Codes: Y10T 137/3802 With vehicle guide or support, e.g., service station

Abstract

In the process, fuel is pumped from a storage tank through a dispenser and nozzle into a customer'"'"'s tank. Hydrocarbon vapors emitted during fueling are collected through a vapor recovery passageway between the inner and outer spouts of the nozzle and conveyed by a vapor pump through vapor return lines into the storage tank. A portion of the vapors in the vapor return lines condense and are removed with the nozzle'"'"'s condensate pickup tube. The removed condensate is dispensed into the customer'"'"'s tank.

Claims

1. A vapor recovery process, comprising the steps of:

storing liquid volatilizable hydrocarbon fuel in a storage tank;

venting said storage tank;

pumping said fuel from said storage tank to a dispenser;

metering said fuel from said dispenser through a nozzle into a consumer'"'"'s tank and controlling the flow of said fuel with said nozzle;

emitting volatilized hydrocarbon vapors from said consumer'"'"'s tank during metering;

drawing a substantial amount of said vapors through said nozzle under vacuum assisted action of a vapor pump;

conveying a substantial amount of said vapors through a vapor return system comprising a vapor return hose and a vapor return line into said storage tank;

condensing some of said vapors in said vapor return hose to form condensate;

withdrawing said condensate from said vapor return hose into a condensate pickup tube extending into a nozzle by venturi action of said nozzle during said metering; and

feeding said condensate from said nozzle to said consumer'"'"'s tank.

2. A vapor recovery process in accordance with claim 1 wherein said storing comprises storing said fuel in an underground storage tank.

3. A vapor recovery process in accordance with claim 1 including automatically stopping said metering and said condensate withdrawing when said consumer'"'"'s tank is substantially filled with fuel.

4. A vapor recovery process, comprising the steps of:

storing liquid volatilizable hydrocarbon fuel in a set of underground storage tanks, each storage tank containing gasoline vapors and a different grade of gasoline with a different octane number;

pumping said gasoline from said storage tanks through fuel lines to a series of dispensers while venting said storage tanks to about atmospheric pressure;

dispensing and metering gasoline from said dispensers through fuel hoses into flow control nozzles;

controlling the flow of gasoline with said nozzles, and discharging said metered gasoline through fuel outlet conduits of said nozzles into consumers'"'"' tanks during fueling;

emitting gasoline vapors from said consumers'"'"' tanks during said discharging;

drawing a substantial amount of said vapors during said discharging into vapor inlets of vapor return conduits in said nozzles under suction pressure of vacuum pumps and passing said vapors through said vapor return conduits about said fuel outlet conduits in countercurrent flow relationship to said discharging metered gasoline in said fuel outlet conduits;

directing said vapors from vapor return conduits through vapor return hoses about said fuel hoses in countercurrent flow relationship to said gasoline being dispensed in said fuel hoses;

conveying said vapors from said vapor return hoses through vapor return lines into said underground storage tanks, said vapors being conveyed in countercurrent flow relationship to said gasoline being pumped through said fuel lines;

at least some of said vapors in said vapor return hoses condensing to form gasoline condensate;

substantially minimizing the blockage of vapors being directed through said vapor return hoses by aspirating and substantially removing said condensate from said vapor return hoses during said fueling with condensate pickup tubes extending partially into said nozzles;

passing said removed condensate through said condensate pickup tubes in countercurrent flow relationship to said conveying vapors in said vapor return hoses;

feeding said aspirated removed condensate through said fuel outlet conduits into said consumers'"'"' tanks during fueling in concurrent flow relationship with said discharging gasoline in said fuel outlet conduits;

sensing the presence of gasoline with liquid sensing tubes in the vapor return conduits of said nozzles between inner and outer spouts of said nozzles to detect when said customers'"'"' tanks are filled; and

atomatically shutting off said discharging of said gasoline and removing of said condensate with at least one of said nozzles when said liquid sensing tube associated with said one of said nozzles detects that the customer'"'"'s tank is filled by said one of said nozzles.

5. A vapor recovery process in accordance with claim 4 including storing and pumping three grades of gasoline.

6. A vapor recovery process in accordance with claim 4 including sensing the presence of gasoline in the vapor inlets of said nozzles with said liquid sensing tubes in said nozzles positioned adjacent said vapor inlets to signal a full condition in said consumers'"'"' tanks and substantially simultaneously automatically shutting off said gasoline discharge and condensate removal when the presence of gasoline in said vapor inlets has been sensed by said liquid sensing tubes.