Process plant

Refrigeration – Storage of solidified or liquified gas – Liquified gas transferred as liquid

Reexamination Certificate

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Details

C062S050400, C062S606000, C137S455000, C196S133000, C208S179000

Reexamination Certificate

active

06729145

ABSTRACT:

The present invention relates to a process plant for handling combustible fluids, for example an oil production plant in which gaseous hydrocarbons are separated from oil and in which surplus gases or residual gases from uncontrolled build-ups of gas pressure in the process escape through process or safety valves in the process plant and are conducted to a collection line.
It should be stressed that the expression process plant means not only plants for oil production in which hydrocarbon gases are separated from oil, but also refining plants and all types of equipment or plant in which combustible fluids are formed which must be handled optimally in terms of safety, finance and the environment.
In a process plant, for example a plant for the production of oil, there will normally be a large number of separators, compressors and/or other process equipment which are connected, in the process pipe line system, with valves, pressure regulators, temperature regulators and other components which, in given situations, may fail and lead to leaks, uncontrolled build-up of pressure, etc. The plant therefore has integral safety systems in the form of pressure control valves, safety valves and blow down valves which are connected to and will conduct surplus or residual fluids to a collection line for further transport to a flare for burning or emission into the atmosphere. In connection with flare burning, a combustion gas is usually added to the collection line continuously to ensure that a minimum flame is maintained in the flare. In connection with emission into the atmosphere without burning, an inert gas is usually added to prevent explosion.
British patent application no. 2.066.936 describes a refining plant for oil in which surplus gases in the form of hydrocarbons are recovered. The surplus gases are diverted from a flare line system and condensed in one or more stages by compression and cooling. The condensate is returned to the process. The residual gas, however, is conducted to a flare tower and burned.
East German patent specification no. 266.006 mentions a plant for combining combustible gases from several sources with different compositions in two main streams. The gases are combined using a computer which regulates the mixture on the basis of measurements of the calorific value of the gases. The gases are burned in a flare tower.
Moreover, Norwegian patent no. 177161 describes a solution for recovering surplus gas from an oil/gas treatment plant in which the surplus gas is collected in a collection line and recovered while gas which escapes in an emergency situation in connection with an abnormal increase in pressure (blow out) is conducted to a branch line for burning in a flare tower.
For all of the above known solutions, flares are used to burn all or part of the surplus gases or residual gases from the process plant. However, the use of a flare entails several disadvantages:
The construction of the flare (flare tower) in itself is very expensive and will account for a not inconsiderable part of the overall costs of a process plant.
Burning or emitting the surplus gases represents an environmental problem as CO, and hydrocarbon gases will, among other things, contribute to the greenhouse effect.
The surplus gases or fluids are valuable in themselves and represent a direct financial loss when burned or emitted into the environment.
The present invention describes a device in connection with a process plant in which the stated disadvantages have been eliminated, i.e. in which the flare has been removed and all surplus gases and residual gases are dealt with and recycled.
The present invention is characterised in that the surplus or residual gases are conducted via a collection line to one or more low-pressure stores and that a connection line or return line is arranged from the store's gas area to the process or another treatment unit for the processing of the gas.
Claims 2-3 define advantageous features of the invention.


REFERENCES:
patent: 1918100 (1933-07-01), Harnsberger
patent: 3714790 (1973-02-01), Battey
patent: 3733838 (1973-05-01), Delahunty
patent: 3844262 (1974-10-01), Dieges
patent: 3877240 (1975-04-01), Kniel et al.
patent: 3903708 (1975-09-01), Mair
patent: 4637440 (1987-01-01), Potter
patent: 5030339 (1991-07-01), Czarnecki
patent: 6045659 (2000-04-01), Bjoerkhaug et al.
patent: 94-25541 (1994-11-01), None

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