Apparatus using solid perm-selective membranes in multiple groups for simultaneous recovery of specified products from a fluid mixture
OwnerCraig W. Colling, George A. Huff JR.inventors
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Abstract
Apparatus is disclosed for economical separation of fluid mixtures. Broadly, apparatus of the invention comprises modules using solid perm-selective membranes. More particularly, the invention relates to a plurality of membrane modules disposed in a first product group, a second product group, and optionally one or more intermediate group. Apparatus of the invention with the membrane modules in multiple groups is beneficially useful for simultaneous recovery of a very pure permeate product and a desired non-permeate product from a mixture containing organic compounds.
Claims20
Apparatus using perm-selective membranes in multiple groups for simultaneous recovery of a very pure permeate product and a desired non-permeate product from a fluid mixture of compounds, which apparatus comprises
- (1-A) a plurality of membrane modules disposed in a first product group, one or more intermediate group, and a second product group, each module comprising a solid perm-selective membrane which under a suitable differential of a driving force exhibits a permeability of at least 0.1 Barrer, a channel having at least one inlet and one outlet for flow of fluid in contact with one side of a membrane, and contiguous with the opposite side thereof a permeate chamber having at least one outlet for flow of permeate,
- (1-B) means for distribution of a fluid feedstock into the channel inlets of at least a portion of the intermediate group of modules,
- (1-C) means for collection of permeate effluent from the chamber outlets of at least a portion of the intermediate group of modules and distribution of this intermediate permeate into the channel inlets of the first product group modules,
- (1-D) means for collection of a permeate product effluent from the chamber outlets of the first product group of modules,
- (1-E) means for collection of non-permeate effluent from the channel outlets of the first product modules and distribution thereof into the channel inlets of at least a portion of the intermediate group of modules,
- (1-F) means for collection of non-permeate from the channel outlets of the intermediate group of modules and distribution of this intermediate non-permeate into the channel inlets of the second product group modules, and
- (1-G) means for collection of a non-permeate product effluent from the channel outlets of the second product group of modules.
Apparatus using perm-selective membranes in multiple groups for simultaneous recovery of a very pure permeate product and a desired non-permeate product from a fluid mixture of compounds, which apparatus comprises
- (2-A) a plurality of membrane modules disposed in a first product group, one or more intermediate group, and a second product group, each module comprising a solid perm-selective membrane which under a suitable differential of a driving force exhibits a permeability of at least 0.1 Barrer, a channel having at least one inlet and one outlet for flow of fluid in contact with one side of a membrane, and contiguous with the opposite side thereof a permeate chamber having at least one outlet for flow of permeate,
- (2-B) means for distribution of a fluid feedstock into the channel inlets of at least a portion of the intermediate group of modules,
- (2-C) means for collection of permeate effluent from the chamber outlets of at least a portion of the intermediate group of modules and distribution of this intermediate permeate into the channel inlets of the first product group modules,
- (2-D) means for collection of a permeate product effluent from the chamber outlets of the first product group of modules,
- (2-E) means for collection of non-permeate effluent from the channel outlets of the first product modules and distribution thereof into the channel inlets of at least a portion of the intermediate group of modules,
- (2-F) means for collection of non-permeate from the channel outlets of the intermediate group of modules and distribution of this intermediate non-permeate into the channel inlets of the second product group modules,
- (2-G) means for collection of a non-permeate product effluent from the channel outlets of the second product group of modules, and
- (2-H) means for collection of permeate effluent from the chamber outlets of the second product modules and distribution thereof into the channel inlets of the first product of modules.
Apparatus using perm-selective membranes in multiple groups for simultaneous recovery of a very pure permeate product and a desired non-permeate product from a fluid mixture of compounds, which apparatus comprises
- (11-A) a plurality of membrane modules disposed in a first product group, one or more intermediate group, and a second product group, each module comprising a solid perm-selective membrane which under a suitable differential of a driving force exhibits a permeability of at least 0.1 Barrer, a channel having at least one inlet and one outlet for flow of fluid in contact with one side of a membrane, and contiguous with the opposite side thereof a permeate chamber having at least one outlet for flow of permeate,
- (11-B) means for distribution of a first fluid feedstock into the channel inlets of at least a portion of the intermediate group of modules,
- (11-C) means for collection of permeate effluent from the chamber outlets of at least a portion of the intermediate group of modules and distribution of this intermediate permeate into the channel inlets of the first product group modules,
- (11-D) means for distribution of a second fluid feedstock into the channel inlets of the first product group of modules,
- (11-E) means for collection of a permeate product effluent from the chamber outlets of the first product group of modules,
- (11-F) means for collection of non-permeate effluent from the channel outlets of the first product modules and distribution thereof into the channel inlets of at least a portion of the intermediate group of modules,
- (11-G) means for collection of non-permeate from the channel outlets of the intermediate group of modules and distribution of the non-permeate into the channel inlets of the second product group modules,
- (11-H) means for collection of a non-permeate product effluent from the channel outlets of the second product group of modules, and
- (11-I) means for collection of permeate effluent from the chamber outlets of the second product modules and distribution thereof into at least a portion of the channel inlets of the intermediate group of modules.
Dependencies are inferred from the claim text.