Patent classifications
B01D5/0081
OLEFIN POLYMERIZATION PROCESS
The present invention relates to an olefin polymerization process comprising polymerization of at least one olefin monomer in one or more polymerization reactors. In addition, the present invention relates to a system for vapor phase polymerization of at least one polymerizable monomer.
ELECTRIC MOTOR-OPERATED FOOD PROCESSOR
An electric motor-operated food processor has a base unit having an electric motor and a preparation vessel that can be arranged on the base unit. A heater and agitator are allocated to the preparation vessel. The food processor can have a distillation apparatus that can be connected with the preparation vessel. The distillation apparatus has a steam receptacle, a condenser and a liquid dispenser. The preparation vessel and steam receptacle are connected in terms of flow when the preparation vessel and distillation apparatus are in a connected state.
WATER DISTILLATION DEVICE
Water distillation device, comprising: a body having a lateral wall and defining a cavity suitable for allowing the distillation of an amount of water to distill, wherein in said cavity are defined a distillation chamber and a condensation chamber, wherein the condensation chamber comprises a collection portion designed to collect at least temporarily distilled water, a heater, configured to heat the amount of water to distill present, in use, in the distillation chamber, a cooler, configured to cause a condensation of a distillation steam deriving from the heating of the water to distill through the heater, wherein the cooler is a refrigerator evaporator, the heater is a refrigerator condenser and wherein the water distillation device comprises a refrigerator compressor connected to the refrigerator evaporator and to the refrigerator condenser, said refrigerator compressor being configured to compress a gas directed within said refrigerator condenser determining, in use, a heating of the latter sufficient to cause a boiling of the water to distill, said refrigerator evaporator being configured to allow an expansion of the gas previously compressed by the refrigerator compressor determining, in use, a cooling of the distillation steam sufficient to cause a condensation of the distillation steam in the collection portion, the water distillation device comprising an intermediate duct connected in correspondence of an its own ending with the refrigerator condenser and in correspondence of an its own second ending with the refrigerator evaporator, said intermediate duct being configured and specifically designed to transport a fluid and/or gas outflowing from the refrigerator condenser toward the refrigerator evaporator, the water distillation device comprising a pre-cooling system for the gases outflowing from the refrigerator condenser, configured to cool at least a part of the intermediate duct, said pre-cooling system comprising an active cooler configured to subtract heat from said at least a part of the intermediate duct.
WATER DISTILLATION DEVICE
Water distillation device, comprising: a body defining a cavity suitable for allowing the distillation of an amount of water to distill, wherein in said cavity are defined a distillation chamber and a condensation chamber, and wherein the condensation chamber comprises a collection portion designed to collect at least temporarily distilled water, a heater, configured to heat the amount of water to distill present, in use, in the distillation chamber, a cooler, configured to cause a condensation of a distillation steam deriving from the heating of the water to distill through the heater,
wherein the body comprises a head portion and a main portion, said distillation chamber being realized in substantial correspondence of the main portion,
the water distillation device comprising a junction portion angularly joining the head portion with said main portion,
the head portion comprising a three ways element in turn comprising a first way, a second way and a third way, wherein said first way faces on said junction portion, and wherein said third way houses said cooler and substantially defines the condensation chamber and a collection portion for the distilled water.
METHOD AND DEVICE FOR FILTERING THE RECYCLED ATMOSPHERE OF A PRINT HEAD
A device for recovery of an atmosphere containing solvent vapours from at least one ink recovery reservoir of a print machine comprising: n (n>1) filter(s) arranged downstream from the at least one ink recovery reservoir, each filter: comprising an inlet face, an outlet face and a filter body between these two faces, and each of the filter being upstream from a condenser or other solvent extraction structure, an atmosphere output from the at least one ink recovery reservoir passing through a separator and through the inlet face, and then through the filter body and through the outlet face before being sent to the solvent extraction structure, the device further comprising at least one second reservoir to recover liquid from the separator.
PRESSURE-CONTROLLED OIL REFINING DEVICE
The present invention relates to a pressure-controlled oil refining device for refining oil from liquid-state oil waste. The purpose of the present invention is to provide a pressure-controlled oil refining device wherein: liquid-state oil waste is introduced and then heated such that, as the pressure rises, the vaporized fluid (oil+impurities) is transferred in the upward direction; a pressure valve is opened/closed such that the oil and impurities can be separated from the fluid and then discharged; the oil is condensed by a cooler such that the same can be liquefied again and stored; and the oil can be refined from the oil waste and reused.
Method for Preventing Fouling of Cryogenic Injection Systems
A method for preventing blockage of a cryogenic injection system is disclosed. The cryogenic injection system is provided comprising a gas feed line attached to a gas distributor. A gas is fed through the gas feed line and the gas distributor into a cryogenic liquid. A portion of the gas feed line passes through the cryogenic liquid. An insulative layer is provided for the portion of the gas feed line that passes through the cryogenic liquid. Heat transfer through the insulative layer between the portion of the gas feed line and the cryogenic liquid is countered sufficiently to prevent blockage of the gas feed line by a component or components of the gas. In this manner, blockage of the cryogenic injection system is prevented.
Solar still system and related solar driven irrigation apparatus
The present invention is related to a solar driven irrigation apparatus for converting contaminated water contained in a contaminated water body into distilled water and using said distilled water for irrigating the vegetation grown on the said irrigation apparatus, the solar driven irrigation apparatus comprising a cover in the form of a geometrical projection comprising a wall, an opening, a semi-permeable mesh, a soil layer and a chamber. The present invention also related to a process for irrigating natural vegetation using the solar driven irrigation apparatus.
Apparatus and method for solvent recovery from drying process
Method and apparatus for condensing a majority of the solvent in a process gas stream at low temperatures, e.g., below the freezing point of water, ca. ?5? C. The gas stream exiting the condenser step may be further processed in one or more emission control devices, such as a single or multi-step series of concentrator devices, such as zeolite concentrator devices. One or more emission control operations can be carried out downstream of the single or multi-step concentrators. The aforementioned condensing process enables the one or more concentrators to operate in a favorable temperature range for removal of 99% or more of VOC, thereby meeting or exceeding strict environmental regulations.
Urea Manufacturing Method And Urea Manufacturing Apparatus
Provided are urea manufacturing method and apparatus, which can increase the conversion ratio into urea and to reduce the consumption of steam. The temperature of the reactor is increased by introducing the entire amount of raw material ammonia and introducing a portion of the decomposed gas from the stripper into the reactor. The raw material ammonia is preferably heated using the steam condensate generated in the purification step, and/or the steam generated by the heat of condensation of the decomposed gas and the unreacted substances in the condensation step. The heating temperature is preferably between 70 and 140 C.