Ideal Fluids, Inc.

United States of America

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IPC Class
A62D 3/34 - Dehalogenation using reactive chemical agents able to degrade 1
B01D 3/00 - Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping 1
B01D 3/14 - Fractional distillation 1
B01D 3/36 - Azeotropic distillation 1
B01D 3/40 - Extractive distillation 1
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Found results for  patents

1.

PROCESS AND APPARATUS FOR THE PYROLYTIC CONVERSION OF ORGANIC HALIDES TO HYDROGEN HALIDES

      
Application Number US2010023726
Publication Number 2010/129078
Status In Force
Filing Date 2010-02-10
Publication Date 2010-11-11
Owner IDEAL FLUIDS, INC. (USA)
Inventor Tarancon, Gregorio, Iii

Abstract

A process for the conversion of organic halide compounds, including refrigerant fluids, is provided. The process includes contacting the organic halide compound with an additive hydrogen donor (methane, ethane, propane, alkanes, etc.) at a reaction temperature, to produce a product stream that includes a hydrogen halide and carbon oxide.

IPC Classes  ?

2.

APPARATUS AND PROCESS FOR THE SEPARATION AND PURIFICATION OF IDEAL AND NON-IDEAL REFRIGERANT MIXTURES

      
Application Number US2010023334
Publication Number 2010/098965
Status In Force
Filing Date 2010-02-05
Publication Date 2010-09-02
Owner IDEAL FLUIDS, INC. (USA)
Inventor Tarancon, Gregorio, Iii

Abstract

An apparatus for separating and purifying a refrigerant mixture comprising: a first distillation column (302), a first condenser (330), a first reboiler (310), wherein the first distillation column (302), the first condenser (330), the first reboiler (310) are fluidly connected; and a sorter vessel (320) comprising a sorter agent, wherein said sorter vessel is fluidly connected to the first distillation column (302), a second distillation column (502), a second condenser (530), a second reboiler (510), wherein the second distillation column (502), the second condenser (530), the second reboiler (510) are fluidly connected; and a heat exchanger (402); wherein the heat exchanger (402) is fluidly connected to the first and second distillation columns (302, 502), such that the heat exchanger is positioned to receive condensate from first and second condenser and to transfer the condensate from the first condenser (302) to the second distillation column (502), and to transfer the condensate from the second condenser (530) to the first ditillation column (302).

IPC Classes  ?

  • B01D 3/36 - Azeotropic distillation
  • B01D 3/14 - Fractional distillation
  • B01D 3/40 - Extractive distillation
  • B01D 3/00 - Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping