NZ243803A - Liquid fuel delivery system with controlled vapour recovery - Google Patents

Description

V I \j 243803 Priority Dato(s): No.: Date: Complete Specification Filed: Class: Publication Date:...QE.Q...!9?)5. P.O. Journal No: NEW ZEALAND PATENTS ACT, 1953 COMPLETE SPECIFICATION A LIQUID DELIVERY SYSTEM /ffwe. GILBARCO INC., 7300 West Friendly Avenue, Greensboro, North Carolina 27420, United States of America, a corporation of the State of Delaware, United States of America hereby declare the invention for which^i^7 we pray that a patent may be granted to rp^/us, and the method by which it is to be performed, , ! to be particularly described in and by the following statement:- / ■r-1 1 - 1 .. J'j* (followed by page la) ' P/8 628/GIL 243803 - ia- The present invention relates to liquid dispensers, and more particularly but not exclusively to fuel dispensers, including a vapour recovery system.

In US Patent No. 5,040,577 there is disclosed a vapour recovery system in which the speed of a vapour recovery pump is controlled by a microprocessor, so that its volumetric flow is equal to the volumetric flow of liquid into a tank. In one embodiment the volumetric flow of the vapour recovery pump is modified so as to maintain an expected pressure at its input. In another, the volumetric flow of the vapour recovery pump is modified so that it maintains an expected volumetric flow. t In a dispensing system for vapourisable liquid, the liquid flows to the tank being filled through a tube and vapour is sucked by a recovery pump from the tank via an adjacent or coaxial tube. If the temperature of the liquid and the temperature of the vapour in the tank are the same, the volumetric flow of the vapour recovery pump can be made equal to the volumetric flow of liquid. However, if the temperatures are different, a heat exchange takes place^y "~q ^ s .A* r,v .......... • ' & 243803 P/8628/GIL. between the liquid and the vapour in the vehicle tank so that the vapour expands or contracts in accordance with the universal gas law PV = mRT, where R = Gas constant P = Pressure V = Volume T = Absolute temperature m = Mass of vapour Therefore the volume of vapour displaced from the tank may not be equal to the volume of fuel dispensed- According to the present invention there is provided a liquid delivery system, comprising: a liquid delivery path adapted for engagement with a tank to He filled; means for delivering liquid to the tank along said liquid delivery path; means for providing a first electrical signal indicative of the volumetric flow of the liquid; a second path that is adjacent to said liquid delivery path; vapour recovery means responsive to said first electrical signal for sucking vapour from the tank along. t 24380 said second path with a volumetric flow substantially proportional to the volumetric flow of the liquid; means for deriving second and third signals related to the temperatures of liquid in said liquid delivery path and vapour in said tank respectively; and control means responsive to said second and third signals for controlling the volumetric flow provided by said vapour recovery means such as to reduce the difference in the volume of vapour emerging from the tank, to which liquid is being delivered, and the volume of the vapour passing through said vapour recovery means.

By employing a system in accordance with the present invention it is possible to compensate for expansion or contraction of the vapour in the tank, in order that more accurate evacuation can be made of the vapour that is displaced from the tank as the liquid enters, avoiding sucking in excess air.

Preferably the control means increases the volumetric flow of the vapour recovery means when the temperature of the liquid is greater than the temperature of vapour, and decreases the volumetric flow of the vapour recovery means when the temperature of the liquid is less than the temperature of the vapour in the RECEIVE-o , 4 - 243803 tank. Therefore if the temperature of the vapour in the tank being filled is colder than the liquid being pumped into it from an underground reservoir, as may well occur during winter, the vapour in the vehicle tank will be heated and will expand. This will be compensated for by the present system, as will the opposite effects which may take place during the summer.

Advantageously the system further comprises: means for determining from said second and third signals an indication of the required volumetric flow of vapour to remove the vapour displaced from the tank by delivery of the liquid thereto; means for providing an indication of the actual volumetric flow of vapour produced by said vapour recovery means; and means responsive to said indication of the ideal vapour flow and the indication of the actual vapour flow for modifying the volumetric flow produced by said vapour recovery means.

In one embodiment the control means is responsive to said first signal for causing the vapour recovery means to have an initial nominal volumetric flow 243803 corresponding to the volumetric flow of liquid in said liquid delivery path; and responsive to said second and third signals for modifying the initial nominal volumetric flow provided by said vapour recovery means such as to reduce the difference in the volume of vapour emerging from the tank to which the liquid is being delivered and the volume of the vapour passing through said vapour recovery means.

Preferably this system comprises a housing having a vapour barrier mounted therein dividing it into non-hazardous and hazardous zones, said hazardous zone comprising: the means for delivering liquid in the form of a liquid delivery pump for withdrawing liquid from a reservoir and forcing it along said delivery path; the means for providing said first electrical signal in the form of a meter; said delivery path; said means for deriving said second signal; said vapour recovery means; and said second path, said non-hazardous zone comprising: said control means; and driving means for said vapour recovery means, the housing further comprising: 243803 means for coupling said second signal from a first transducer means to said controller through said vapour barrier; and mechanical means extending through said vapour barrier for coupling said driving means to said vapour recovery means.

Advantageously the system further comprises: a flow meter coupled to said second path for providing a fourth signal indicative of the volumetric flow of vapour through said second path; and means for coupling said fourth signal through said vapour barrier to said control means; and said control means being programmed to provide a signal to said driving means so as to further modify the volumetric flow of said vapour recovery means such that it is proportional to the amount theoretically required to compensate for the difference in the volume of vapour emerging from the tank to which liquid is being delivered and the volume of the vapour passing through the vapour recovery means.

This fourth signal enables any difference between the actual volumetric flow and ideal volumetric flow, that can be caused by pump wear and differences between pumps due to variations within tolerance limits, to be compensated for. n.z. pr P/8628/GIL -t-U Preferably the means for deriving said third signal comprises an atmospheric temperature sensor. This is advantageous because atmospheric temperature can easily be measured, and usually approximates to the the temperature of the vapour in the tank being filled.

The invention is particularly applicable to a fuel dispensing system.

One embodiment of the invention will now be described, by way of example only, with reference to the accompanying drawings, of which: Fig. 1 is a schematic illustration of a fuel dispenser, in accordance with the invention; and * Fig. 2 is a flow chart used in explaining the operation of the fuel dispenser shown in Fig. 1.

In the embodiment of the invention shown in Fig. 1, liquid is pumped from a reservoir 2 by a pump 4 with a volumetric flow VL that is determined by the position of a trigger 6 of a nozzle 8. A spout 9 of nozzle 8 is inserted into the fill pipe 10 of the tank 12 that is to be filled P/8628/GIL 243803 with liquid 13. The liquid flows to the nozzle from the pump 4 via a tube 14, a temperature transducer 16, a flow meter 18, and a tube 20. As vapour 15 is forced from a tank 12, it is drawn by a recovery pump 24 through holes 11 in the spout and associated tube 22 and forced through a flow meter 26 and a tube 28 to the reservoir 2.

As described below, means are provided for initially driving the recovery pump 24 at such speed that its volumetric flow, Vv, equals the volumetric flow, VL, of the liquid produced by the pump 4. Signals from the flow meter 18 are applied via a lead 31 to a microprocessor 30 that is programmed to supply a control signal to a drive pulse source 32 that supplies drive pulses to a stepping motor 34. The stepping motor 34 is mechanically coupled via a rod 36 to drive the recovery pump 24. The frequency of the drive pulses supplied by the source 32 is such that the motor 34 drives the recovery pump 24 at such a speed as to cause Vv = V The volumetric flow of the recovery pump 24 may be modified as follows to accommodate the change in volume of the vapour emanating from the tank 12. The signal provided by the temperature transducer 16 representing the temperature, TL, of the liquid flowing to the tank 12 is 2^3803 conducted to the microprocessor 30 via a lead 38. A temperature transducer 40 supplies a signal representing the atmospheric or ambient temperature TA to the microprocessor 30 via a lead 42. The microprocessor 30 modifies the control signal supplied in the drive pulse source 32 in a manner described in Fig. 2 so as to change the nominal volumetric flow Vv of the recovery pump 24 to the required value VR.

Reference is now made to the flow chart of Fig. 2. At the start of the program, the microprocessor 30 reads the signal VL on the led 31 as indicated by a block 44. A determination is made as to whether any liquid is flowing by comparing VL with zero, block 46. If V L = 0, the processes return to the block 44, via line 48.

When block 46 indicates that VL > 0, a block 50 indicates that the microprocessor 30 reads the signals on the leads 38 and 42 respectively representing the temperature, TL, of the liquid and the temperature, T A, of the atmosphere. In block 52, the signal supplied to the pulse drive source 32 is changed if required to a value as shown below: VR = VL ^ f (VG) TA 24 3 8 0 3 This equation is obtained as follows: From Boyle's and Charles laws R = Gas constant P = Pressure V = Volume T = Absolute temperature m = Mass of vapour If one assumes that Px = P2 = atmospheric pressure, this ignores the pressure drop due to vapour flow through the fill pipe, for a system that uses a "bootless" nozzle, i.e. a nozzle that does not have a "ring" or "boot" on the end of the spout that seals off the end of a fill pipe to the tank, then the mass of vapour does not change. Therefore mx = m2, PV = mRT (1 ) Where: thus: EiYiHh = P?V?m: Ti T2 (2) P/8628/GIL. 243803 and equation (2) reduces to equation (3) below: Y, = V2 (3) T1 T2 Assuming that ' the vapour exiting the tank is either ■warmed or cooled, from its initial temperature (Tv) within the tank, by heat transfer to the temperature of the liquid (Tl) entering the tank, then: T1 = Tv = Initial absolute temperature of the vapours in the tank T2 = Tl = Absolute temperature of the liquid being delivered ♦ V, = VL = Volume of vapours being displaced at T, by the liquid being dispensed into the tank V2 = VR = Volume of vapours that need to be recovered by substitution into equation 3, equations (4) and (5) are obtained as shown below: 4 3 8 0 3 Yr (4) or VR = VL T; (5) substituting TA for Tv gives: VR = VL Alternatively, the signal supplied to the drive pulse source 32 may have to be modified such that: VR = VL I"Tt + a (Tv - Tt)1 [f(VG)] Tv The reason for this substitution is as follows: If a temperature difference exists between the fuel entering the tank and the vapour exiting the tank, then because the heat transfer from the fuel entering the tank to the vapour leaving the tank may not be complete or total, i 2 5 SEP 1995 jj 243803 13 (i.e. 100%), then the assumption that T2 = TL may be incorrect. In this case a correction factor "a" is added to the formula to compensate for this inefficiency in heat transfer such that: where "a" is a correction factor multiplied by the temperature difference between TL and Tv, the product of which is subtracted from the temperature TL to give a more accurate value for T2. This correction factor "a" is empirically derived through experimentation.

Substituting the compensated value of T2 given in equation (6), into equations (3) and (4) gives The above equations 1 to 7 have been derived assuming the vapour behaves as an ideal gas. However this is only an approximation and a modifier f (VG) has to be added giving equation 8 below: T2 = TL - a (Tl - Tv) (6) Vr = VL rTT + a (T„ - Tr)1 (7) VR = VL ITi^: a LTv-^i TlUL [f (VG) ] Tv (8) 2 5 SEP 19S5 received j 243803 The value of the f (VG) modifier may be effected by the blend of the fuel, additives condensation, fluid dynamics or compressibility and the like.

Other modifications to the formula may have to be made on a trial and error basis, depending on the application. The formulas hereinbefore set out are only a guide to the general laws of thermodynamics which have to be addressed by the control algorithms, and it will be appreciated that the control algorithm could equally well be derived empirically.

Thus far, it has been assumed that the actual volumetric flow VA of the recovery pump 26 corresponds precisely to the ideal value VR, but, as indicated previously, this may not always be the case because of differences between different pumps and wear occurring in the pumps. If desired, the ideal value of VR can be attained by the microprocessor reading the signal on the lead 27 representing actual vapour flow, Vfl, as indicated by block 54, comparing it with the ideal value VR, which it has computed from TL, TA and if need be by block 56, and changing the signal supplied to the drive pulse source 32 to a value such that VA = VR, as indicated by a block 58. The process then returns to the start at the block 44.

P N-Z. r-AKi-T office 2 5 SEP 1995 ?4 3803 P/8628/GIL Note that in the embodiment of the invention shown in Fig. 1, the electrical apparatus is enclosed in a non-hazardous zone 33 above a vapour barrier 35. The fluid handling mechanical apparatus are enclosed below vapour barrier 35 in a hazardous zone 37.

If correction for deviation of the actual volumetric flow, VA, from the ideal volumetric flow is not desired, the procedure can be returned to its start after the block 52 as indicated by the dashed line 62. In either case, the process is repeated rapidly enough to follow changes in the volumetric flow of liquid VL as well as changes in other parameters such as TL and TA. 24J80J

Claims (14)

WHAT WE CLAIM IS:

1. A liquid delivery system, comprising: a liquid delivery path adapted for engagement with a tank to be filled; means for delivering liquid to the tank along said liquid delivery path; means for providing a first electrical signal indicative of the volumetric flow of the liquid; a second path that is adjacent to said liquid delivery path; vapour recovery means responsive to said first electrical signal for sucking vapour from the tank along said second path with a volumetric flow substantially proportional to the volumetric flow of the liquid; means for deriving second and third signals related to the temperatures of liquid in said liquid delivery path and vapour in said tank respectively; and control means responsive to said second and third signals for controlling the volumetric flow provided by said vapour recovery means such as to reduce the difference in the volume of vapour emerging from the tank to which liquid is being delivered and the volume of the vapour passing through said vapour recovery means. N.Z. rvVf' t 5 BK? F.:c. ; •• 243803 17-

2. A system as claimed in claim 1 , wherein the control means increases the volumetric flow of the vapour recovery means when the temperature of the liquid is greater than the temperature of vapour, and decreases the volumetric flow of the vapour recovery means when the temperature of the liquid is less than the temperature of the vapour in the tank.

3. A system as set forth in claim 1 or 2 further comprising: means for determining from said second and third signals an indication of the required volumetric flow of vapour to remove the vapour displaced from the tank by delivery of the liquid thereto; means for providing an indication of the actual volumetric flow of vapour produced by said vapour recovery means; and means responsive to said indication of the required volumetric flow of vapour and the indication of the actual vapour flow for modifying the volumetric flow produced by said vapour recovery means.

4. A liquid delivery system as claimed in any 2 5 SEP 1995 - 18 - M 3 8 0 3 preceding claim wherein the control means is responsive to said first signal for causing the vapour recovery means to have an initial nominal volumetric flow corresponding to the volumetric flow of liquid in the liquid delivery path; and responsive to said second and third signals for modifying the initial nominal volumetric flow provided by said vapour recovery means such as to reduce the difference in the volume of vapour emerging from the tank to which the liquid is being delivered and the volume of the vapour passing through said vapour recovery means.

5. A system as claimed in any preceding claim, further comprising a housing having a vapour barrier mounted therein dividing it into non-hazardous and hazardous zones, said hazardous zone comprising: the means for delivering liquid in the form of a liquid delivery pump for withdrawing liquid from a reservoir and forcing it along said delivery path; the means for providing said first electrical signal in the form of a meter; said delivery path; said means for deriving said second signal; said vapour recovery means; and said second path, said non-hazardous zone comprising: said control means and 2 5 SEP 199! ^4380 - 19 - driving means for said vapour recovery means, the housing further comprising: means for coupling said second signal from a first transducer means to said controller through said vapour barrier; and mechanical means extending through said vapour barrier for coupling said driving means to said vapour recovery means.

6. A system as set forth in claim 5, further comprising: a flow meter coupled to said second path for providing a fourth signal indicative of the volumetric flow of vapour through said second path; and means for coupling said fourth signal through said vapour barrier to said control means; and said control means being programmed to provide a signal to said driving means so as to further modify the volumetric flow of said vapour recovery means such that it is proportional to the amount theoretically required to compensate for the difference in the volume of vapour emerging from the tank to which liquid is being delivered and the volume of the vapour passing through the vapour recovery means.

7. A system as claimed in any preceding claim wherein N.Z. PATFNT OFTIO ICE 2 5 SEP K 243803 - 20 - said liquid is a fuel.

8. A system as claimed in any preceding claim wherein the liquid delivered has a variable volumetric flow.

9. A system as claimed in any preceding claim wherein the means for deriving said third signal comprises an atmospheric temperature sensor.

10. A system as claimed in any preceding claim further comprising: a nozzle coupled to said delivery path and said second path, wherein said nozzle having manually controllable means for varying the volumetric flow of said fuel delivery pump.

11. A method of dispensing fuel comprising: delivering fuel to a tank along a first path with a variable volumetric flow; producing an electrical signal indicative of said volumetric flow; sucking vapour from the tank in response to the electrical signal, along a second path that is adjacent to the first path with a nominal volumetric flow corresponding to said volumetric flow; ?4^803 P/8628/GIL - 21 - producing second and third signals respectively representing the absolute temperatures of fuel in the first path and vapour in the tank; and increasing the volumetric flow of the vapour being sucked, in response to said second and third signals, if the temperature of the fuel is greater than the temperature of vapour and decreasing the volumetric flow of the vapour being sucked, in response to said second and third signals, if the temperature of the fuel is less than the temperature of vapour.

12. The method of Claim 11, further comprising the steps of: calculating from said second and third signals an indication of the ideal volumetric flow of vapour required to remove the vapour displaced from the tank by delivery of the fuel'thereto; producing an indication of the actual volumetric flow of vapour produced by sucking back vapour at a given time; and adjusting the volumetric vapour flow in response to said indication of the ideal vapour flow and the indication of the actual vapour flow for equating the rates of actual- • vapour flow and ideal vapour flow. V t, . v-t1 •> cf-

13. A liquid delivery system substantially as hereinbefore ^ r , described with reference to the accompanying drawings.

14. A method of dispensing fuel substantially as hereinbefore j DATED THIS <^DAY OF described with reference to the accompanying drawings. ^ J p^RK & SON PER AGENTS FO^^ETA^ICXNT*