Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
159 words
A method for the recovery of petrol from a mixture of petrol vapour and air, in which the petrol vapour is absorbed in an absorption means by direct contact with a cooled petroleum distillate supplied from a storage tank, and then the petrol dissolved in the petroleum distillate is stripped so that the petroleum distillate circulates in a substantially closed circuit, characterized in that the absorbing medium is a petroleum distillate having a higher boiling point range than petrol, and that the petroleum distillate in sequence is at least: (1) cooled by heat exchange with a cold reservoir, (2) brought into direct contact with the petrol/air mixture to absorb petrol, (3) transferred to a buffer tank and (4) transferred from the buffer tank to a stripping means, the amount of cooled petroleum distillate caused to contact the petrol/air mixture being controlled so that the concentration of petrol in the petroleum distillate transferred to the buffer tank is substantially constant.
Claim 2
Independent Claim
159 words
A method for the recovery of petrol from a mixture of petrol vapour and air, in which the petrol vapour is absorbed in an absorption means by direct contact with a cooled petroleum distillate supplied from a storage tank, and then the petrol dissolved in the petroleum distillate is stripped so that the petroleum distillate circulates in a substantially closed circuit, characterized in that the absorbing medium is a petroleum distillate having a higher boiling point range than petrol, and that the petroleum distillate in sequence is at least: (1) cooled by heat exchange with a cold reservoir, (2) brought into direct contact with the petrol/air mixture to absorb petrol, (3) transferred to a buffer tank and (4) transferred from the buffer tank to a stripping means, the amount of cooled petroleum distillate caused to contact the petrol/air mixture being controlled so that the concentration of petrol in the petroleum distillate transferred to the buffer tank is substantially constant.
Claim 3
Dependent Claim
42 words
A method according to claim 1, wherein the petroleum distillate conducted from the buffer tank to the stripping means is caused to be in heat exchanging relationship with the petroleum distillate which is passed from the stripping means to the cold reservoir.
Claim 4
Dependent Claim
35 words
A method according to claim 1, wherein the air, stripped of petrol and cooled after contact with the cooled petroleum distillate, is caused to be in indirect heat exchanging relationship with the incoming petrol/air mixture.
Claim 5
Dependent Claim
38 words
A method according to claim 3, wherein the heat exchanging relationship is provided through a flowing cooling medium, and that the flow amount per unit of time is controlled in dependence upon the temperature of the petrol/air mixture.
Claim 6
Dependent Claim
29 words
A method according to claim 3, wherein any water condensed by such heat exchanging relationship is separated before the petrol/air mixture is brought into contact with cooled petroleum distillate.
Claim 7
Dependent Claim
40 words
A method according to claim 1, wherein the amount of cooled petroleum distillate brought into contact with the petrol/air mixture is controlled in dependence upon the temperature in a mixing zone for the petrol/air mixture and the petroleum distillate, respectively.
Claim 8
Dependent Claim
33 words
A method according to claim 6, in which the petrol/air mixture is absorbed in the petroleum distillate in a washing tower, the petroleum distillate being introduced at several levels in the washing tower.
Claim 9
Dependent Claim
34 words
A method according to claim 7, wherein the amounts of petroleum distillate passed to the respective levels in the washing tower are mutually regulated to obtain a predetermined, vertical temperature distribution in the tower.
Claim 10
Dependent Claim
14 words
A method according to claim 1, wherein the stripping means is a distillation column.
Claim 11
Independent Claim
112 words
A system for the recovery of petrol from a mixture of petrol vapour and air, comprising an absorption means to absorb petrol from a received petrol/air mixture by means of a cooled petroleum distillate, said absorption means being connected to a stripping means to strip petrol dissolved in the petroleum distillate and a storage tank for petroleum distillate, respectively, characterized in that a buffer tank (3) is mounted between the absorption means (2) and the stripping means (5), and that flow regulating means (15, 16), which are dependent upon the temperature in a mixing zone in the absorption means (2), are interposed between the storage tank (7) and the absorption means (2).
Claim 12
Independent Claim
112 words
A system for the recovery of petrol from a mixture of petrol vapour and air, comprising an absorption means to absorb petrol from a received petrol/air mixture by means of a cooled petroleum distillate, said absorption means being connected to a stripping means to strip petrol dissolved in the petroleum distillate and a storage tank for petroleum distillate, respectively, characterized in that a buffer tank (3) is mounted between the absorption means (2) and the stripping means (5), and that flow regulating means (15, 16), which are dependent upon the temperature in a mixing zone in the absorption means (2), are interposed between the storage tank (7) and the absorption means (2).
Claim 13
Dependent Claim
64 words
A system according to claim 10, including a heat exchanger assembly (1) comprising one heat exchanger coil (25) placed in the received petrol/air mixture and a second heat exchanger coil (28) placed in the cold, petrol-stripped exhaust air from the absorption means (2), said heat exchanger coils being interconnected to form a closed circuit for a heat transferring medium having a controllable flow rate.
Claim 14
Dependent Claim
32 words
A system according to claim 10, including a heat exchanger (4) through which a substantially constant amount of petroleum distillate per unit of time flows to and from the stripping means (5).
Claim 15
Dependent Claim
85 words
A system according to claim 10, in which the absorption means is a washing tower, the washing tower (2) having a plurality of injection nozzles (20, 21) at different heights, and the flow regulating means comprising a valve (15) which is dependent upon the temperature at a predetermined height (at 16) and is adapted to regulate the total amount of petroleum distillate supplied to the tower so that the concentration of petrol in the petroleum distillate supplied to the buffer tank (3) is substantially constant.
Claim 16
Dependent Claim
21 words
A system according to claim 10, wherein the absorption means (2) is mounted directly on top of the buffer tank (3).