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US5174901A Expired / Lapsed US ⏱️ 0.0 years remaining

Liquid purifying system

Assignee: Individual
•
Filing: 1991-06-10
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Granted: 1992-12-29
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Expires: 2011-06-10
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Abstract

Abstract In a system for purifying liquid, a method is provided wherein the liquid is pretreated by passing it through a sand filter water softener and carbon filter for removal of hardness and particulate matter. The liquid is then pumped through a reverse osmosis membrane for removal of organic compounds and ionized and biological impurities. The liquid passes from the reverse osmosis membrane through a strong acid cation exchange resin for removal of the cations present in the reverse osmosis effluent. The acidified liquid is neutralized hy passing it through calcium carbonate, thus adding calcium salt and carbonic acid to the liquid for a better tasting, calcium-enriched product.

Inventors

  • 👤 Verity C. Smith

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 16:43
CPC Classifications
B; B01; B01D; B01D61/00; B01D61/02; B01D61/04; B01D61/025; B01D61/08; C; C02; C02F; C02F9/00; C02F9/20; B01D2311/00; B01D2311/04; B01D2311/06; C02F1/00; C02F1/001; C02F1/28; C02F1/283; C02F1/30; C02F1/32; C02F1/44; C02F1/441; C02F1/66; C02F1/42; C02F2001/425

Claims Analysis

Total Claims: 26
Claim 1
Independent Claim 119 words
A method for purifying liquid in a system comprising a portable liquid purification unit, said method comprising: a) passing a liquid through a sand filter; b) passing the effluent from a) through a carbon filter; c) passing the effluent from b) through a water softener; d) collecting the effluent from c) in a storage tank, from where said effluent is pumped into and through a reverse osmosis membrane; e) passing the effluent from d) through a strong acid cation exchange resin in the hydrogen form for acidifying the effluent; f) directly thereafter passing the effluent from e) through a bed of calcium carbonate for neutralizing the effluent; and g) collecting the effluent from f) in a second storage tank.
Claim 2
Independent Claim 119 words
A method for purifying liquid in a system comprising a portable liquid purification unit, said method comprising: a) passing a liquid through a sand filter; b) passing the effluent from a) through a carbon filter; c) passing the effluent from b) through a water softener; d) collecting the effluent from c) in a storage tank, from where said effluent is pumped into and through a reverse osmosis membrane; e) passing the effluent from d) through a strong acid cation exchange resin in the hydrogen form for acidifying the effluent; f) directly thereafter passing the effluent from e) through a bed of calcium carbonate for neutralizing the effluent; and g) collecting the effluent from f) in a second storage tank.
Claim 3
Dependent Claim 21 words
The method of claim 1 further comprising: h) recovering the effluent from g) and circulating said effluent to the delivery taps.
Claim 4
Dependent Claim 21 words
The method of claim 2 wherein the effluent from h) is purified by passing it through a 0.22-1 micro meter filter.
Claim 5
Dependent Claim 23 words
The method of claim 2 wherein said effluent is dispensed through said delivery taps, said delivery taps being controlled by a timing means.
Claim 6
Dependent Claim 24 words
The method of claim 4 wherein said timing means comprises the opening and closing of a solenoid valve for a fixed period of time.
Claim 7
Dependent Claim 22 words
The method of claim 1 further comprising: i) recovering the effluent from g) and returning said effluent to said second storage tank.
Claim 8
Dependent Claim 20 words
The method of claim 1 wherein the reverse osmosis membrane of d) leaves a residual of 1-150 parts per million.
Claim 9
Dependent Claim 21 words
The method of claim 1 wherein the effluent from f) is purified by running it through a 1-5 micro meter filter.
Claim 10
Dependent Claim 20 words
The method of claim 1 wherein the purified liquid is dispensed via a sterilizing ultraviolet light protected tube or faucet.
Claim 11
Dependent Claim 12 words
The method of claim 9 wherein the ultraviolet light is 254 nanometers.
Claim 12
Dependent Claim 25 words
The method of claim 1 wherein the purified liquid not dispensed is returned to said second storage tank via a sterlizing ultraviolet light protected tube.
Claim 13
Dependent Claim 15 words
The method of claim 11 wherein the ultraviolet light is between 180 and 260 nanometers.
Claim 14
Independent Claim 114 words
A system for purifying liquid comprising: a) means for passing a liquid through a series of filters, such as a sand filter, carbon filter or water softener; b) a storage tank into which the effluent from a) is collected and stored; c) a reverse osmosis membrane through which the effluent from b) is pumped; d) means for first acidifying effluent and then directly thereafter neutralizing effluent including, an acid cation exchange resin in the hydrogen form through which the effluent from c) is passed; and a bed of calcium carbonate through which the effluent from d) is passed; and e) a second storage tank into which the effluent from e) is collected and stored.
Claim 15
Independent Claim 114 words
A system for purifying liquid comprising: a) means for passing a liquid through a series of filters, such as a sand filter, carbon filter or water softener; b) a storage tank into which the effluent from a) is collected and stored; c) a reverse osmosis membrane through which the effluent from b) is pumped; d) means for first acidifying effluent and then directly thereafter neutralizing effluent including, an acid cation exchange resin in the hydrogen form through which the effluent from c) is passed; and a bed of calcium carbonate through which the effluent from d) is passed; and e) a second storage tank into which the effluent from e) is collected and stored.
Claim 16
Dependent Claim 17 words
The system of claim 13 further comprising delivery taps to which the effluent from f) is circulated.
Claim 17
Dependent Claim 27 words
The system of claim 14 wherein the effluent from f) is purified by passing it through a 0.22-1 micro meter filter prior to reaching the delivery taps.
Claim 18
Dependent Claim 23 words
The system of claim 14 wherein the delivery taps are controlled by a timing means, which means allows said effluent to be dispensed.
Claim 19
Dependent Claim 21 words
The system of claim 16 wherein the timing means open and close a solenoid valve for a fixed period of time.
Claim 20
Dependent Claim 20 words
The system of claim 13 wherein the reverse osmosis membrane of c) leaves a residual of 1-150 parts per million.
Claim 21
Dependent Claim 22 words
The system of claim 13 further comprising a 1-5 micro meter filter through which the effluent from e) is passed and purified.
Claim 22
Dependent Claim 26 words
The system of claim 13 further comprising a sterilizing ultraviolet light protected tube or faucet for dispensing the purified liquid, said ultraviolet light being 254 nanometers.
Claim 23
Dependent Claim 33 words
The system of claim 13 further comprising a sterilizing inline ultraviolet light protected tube for returning the purified liquid to the second storage tank, said ultraviolet light being between 180 and 260 nanometers.
Claim 24
Dependent Claim 18 words
The system of claim 13 wherein the functioning of the purifying system is monitored and/or operated by computer.
Claim 25
Independent Claim 46 words
A method of producing a purified drinking water enriched with calcium comprising: a) passing the water through a cation exchange resin in the hydrogen form for acidifying the water; and b) directly thereafter passing the effluent from a) through a bed of calcium carbonate for neutralizing.
Claim 26
Independent Claim 46 words
A method of producing a purified drinking water enriched with calcium comprising: a) passing the water through a cation exchange resin in the hydrogen form for acidifying the water; and b) directly thereafter passing the effluent from a) through a bed of calcium carbonate for neutralizing.

References Cited (Backward Citations)

US4659463A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1995-12-29 1996-06-29 1996-12-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-12-29 2000-06-29 2000-12-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-12-29 2004-06-29 2004-12-29 $7700.00 Window Closed / Lapsed

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