Gas separation – Means within gas stream for conducting concentrate to collector
Reexamination Certificate
2001-09-20
2003-11-18
Hopkins, Robert A. (Department: 1724)
Gas separation
Means within gas stream for conducting concentrate to collector
C055S465000, C159S031000, C096S189000
Reexamination Certificate
active
06648938
ABSTRACT:
OBJECT OF THE INVENTION
These Specifications refer to an apparatus for cleaning a fluid in the form of steam from a circuit, whose utility lies in separating the chemical compounds in the water from industrial process tailings, particularly those generated by industries incorporating electrolysis processes.
The invention provides purified water in line with the terms of the current provisions on industry-generated waste water, its operation being based on the distillation of such waste water at low temperature in a controlled atmosphere.
In summary, the invention can be used not just to clean sewer and industrial waters but also to clean any industrial waste which may be mixed in the steam, operating downstream from the output of any steam jet to complete the steam treatment operation as such.
The invention also allows separation of chemical compounds in water from industrial process tailings, especially in industries using electrolysis, and in all types of industries whose normal operation creates waste water requiring treatment for subsequent disposal.
The invention provides treated water in line with the current regulations on industrial-origin waste water, and is based on the distillation of such waste water at low temperatures in a controlled atmosphere.
FIELD OF THE INVENTION
This invention is usable in industries manufacturing elements, devices and systems applicable to the treatment of waste water, specifically in that dedicated to the treatment of industrial-origin waste water: it may also be used to clean any industrial waste which may be incorporated or mixed in to the steam.
PRIOR ART
The applicant is familiar with many devices and systems which can be used to recycle industrial waters: the most widely-used are those which precipitate the elements dissolved in the medium by varying the conditions of acidity, redox potential, oxygen concentration, or temperature.
These systems require subsequent processing of the flows treated to eliminate traces of compounds which are hard to precipitate: it is sometimes virtually impossible to regenerate the flow of polluted water.
Procedures are also known for osmosis and reverse osmosis-based water treatments applicable to specific cases and, given such specificity, not widespread in industry.
The applicant is aware of treatment procedures based on the distillation of liquid wastes, fundamentally developed to desalinate sea-water to make it drinkable or to provide water for irrigation.
These distillation treatment procedures are based on heating the effluent, generally water, in closed volumes. Such effluent contains chemicals in dissolution whose steam pressure is greater than that of the water, which is thus evaporated and separated from the remaining chemical compounds.
Subsequent condensation of the steam from the separated water enables it to be restored to the liquid state, virtually free of traces of compounds in its composition, to the extent that it is common to add certain compounds to the water treated to render it drinkable.
The procedure described, fully familiar to any specialist in the field, uses large amounts of energy, needed to raise the temperature of the liquid beyond evaporation point, which is dependent on the pressure in the vessel where the procedure takes place.
The applicant is not aware of the existence of any procedure using distillation to treat waste water, and is specifically unaware of any device usable for these purposes on industrial waters from industrial electrolysis processes and whose characteristics are suitable for its application.
Nor is the applicant familiar with any current invention which can be used not just to clean sewer and industrial waste water but also any industrial waste which may be incorporated or mixed in to the steam.
DESCRIPTION OF THE INVENTION
The apparatus for cleaning fluid in the form of steam from a circuit, as proposed in the invention, constitutes an evident novelty in its field of application, providing a device able to treat industrial liquid effluent, principally that from industries incorporating electrolysis processes, by evaporating the water in closed volumes by heating at controlled atmospheric pressure.
In specific terms, the invention is based on an evaporation chamber where internal pressure and temperature conditions can be varied so as to reduce the water steam pressure to a point where it will evaporate at around 30° C., making use of the excess heat flows from the industrial processes generating the effluent and even of their exhaust temperatures to evaporate it.
It is vital that the liquid effluents should not contain dissolved compounds of less density than the water or, if they are present, they are not prohibited in treated water under the industrial waters legislation.
The evaporation chamber, fed from a suitable tank, provides a given flow of water vapour which leads to a separator, and a flow of dense, unevaporated compounds which are placed in a suitable separate vessel.
The separator is included to provide a second separation of compounds whose steam pressure is slightly higher than that of water vapour, and of any solid particles which may be dragged along with the flow.
The separator comprises a volume with two accesses on opposite sides where the water vapour enters and exits: it has a tabular element located below the vertical opposite the water vapour input, sloping downward and with a channel at the bottom, so that the water vapour impacts against said tabular element and the solid particles adhere and the temperature drops, liquefying the compounds whose steam pressure is slightly above that of the water, and which are collected in the lower channel and evacuated through the appropriate drains.
The water vapour flow, accelerated by suction fans, then runs to a cooler which liquefies the water vapour so that it can run into public channels or be fed back into the industrial processes from which it came.
Optionally, the water vapour can be freely expelled into the atmosphere, without the need for the cooler mentioned above.
The invention applies preferably to effluents from electrolysis plants whose characteristics are suitable for treatment by the apparatus to clean a fluid in the form of steam delivered from a circuit which is the subject of these Specifications: it should be installed close to such plants in order to make use of the heat generated during electrolysis and in the associated machinery.
The invention can also be used to clean any industrial waste which may be mixed in to the steam.
It must also be pointed out that the invention may optionally comprise an evaporation chamber where internal pressure and temperature conditions can be varied, to reduce the water vapour pressure to a point where it can evaporate at temperatures of about 30° C.: also as an option, surplus heat flows from the industrial processes generating these effluents can be used, as can their exhaust heat, to evaporate them.
It is of the greatest importance that the liquid effluents should not contain dissolved compounds of less density than the water or, if they do, such compounds are not prohibited in treated water under the industrial waters legislation.
The evaporation chamber, supplied from a suitable tank, provides a certain flow of water vapour, which runs to a separator, and a flow of dense unevaporated compounds which are deposited in a suitable separate vessel.
The separator is included to provide a second separation of compounds whose steam pressure is slightly higher than that of water vapour, and of any solid particles which may be dragged along with the flow.
The separator comprises a volume with two accesses on opposite sides where the water vapour enters and exits: it has a tabular element located below the vertical opposite the water vapour input, sloping downward and with a channel at the bottom, so that the water vapour impacts against said tabular element and the solid particles adhere and its temperature drops, liquefying the compounds whose steam pressure is slightly above that of the water, which are collected in the lower chann
Hopkins Robert A.
Kasper Horst
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