US4202736A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process and apparatus for the thorough purification of water and the highly purified water obtained thereby
Assignee: Institut Pasteur
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Filing: 1977-06-13
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Granted: 1980-05-13
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Expires: 1997-06-13
Abstract
Abstract The water is heated to convert it into steam; the steam is passed from a container into a superheating zone and then condensed in the form of purified water. The superheating zone contains at least in part, a packing of a material inert with respect to steam and impurities possibly present in the latter. The steam is superheated in said zone by means of supplementary heating to a temperature exceeding 300 DEG C., and reaching notably from 400 DEG to 700 DEG C., preferably from 500 DEG to 700 DEG C. Highly purified apyrogenic water freed from undesired organic substances, useful in research in physical chemistry, physics, biochemistry or molecular biology or in the medical field is, produced by this process.
Inventors
- 👤 Herbert S. Marcovich
- 👤 Remi D. Perrin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 03:32
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/02; B; B01; B01D; B01D1/00; B01D1/0011; B01D1/0017; C02F1/04; C02F1/72; Y; Y10; Y10S; Y10S203/00; Y10S203/11
Claims Analysis
Total Claims: 33
Claim 1
Independent Claim
103 words
A distillation process for producing apyrogenic water which comprises the following steps: (a) introducing water into a heating zone, (b) heating the water in the heating zone to convert it into steam, (c) superheating the steam to a temperature within a range exceeding 300° C. and up to 700° C., (d) concurrently with step (c), passing the steam over and between packing material inert at the temperature with respect to said steam and to any impurities therein and thus maintaining the steam at said temperature for a dwell time sufficient to produce apyrogenic water, and (e) condensing the superheated steam into apyrogenic water.
Claim 2
Dependent Claim
103 words
A distillation process for producing apyrogenic water which comprises the following steps: (a) introducing water into a heating zone, (b) heating the water in the heating zone to convert it into steam, (c) superheating the steam to a temperature within a range exceeding 300° C. and up to 700° C., (d) concurrently with step (c), passing the steam over and between packing material inert at the temperature with respect to said steam and to any impurities therein and thus maintaining the steam at said temperature for a dwell time sufficient to produce apyrogenic water, and (e) condensing the superheated steam into apyrogenic water.
Claim 3
Dependent Claim
17 words
A process according to claim 1 which consists essentially of steps (a), (b), (c), (d) and (e).
Claim 4
Dependent Claim
19 words
A process according to claim 1 wherein the temperature range for step (c) is from 400° to 700° C.
Claim 5
Dependent Claim
16 words
A process according to claim 1 wherein said temperature range is from 500° to 700° C.
Claim 6
Dependent Claim
31 words
A process according to claim 1 which comprises contacting the water of step (b) with an agent for oxidising any undesired organic substance in said water during steps (c) and (d).
Claim 7
Dependent Claim
12 words
A process according to claim 5 wherein the oxidising agent is oxygen.
Claim 8
Dependent Claim
29 words
A process according to claim 1 wherein step (c) comprises superheating the steam in contact with a catalyst for facilitating destruction of any organic substance entrained in said steam.
Claim 9
Dependent Claim
12 words
A process according to claim 7 wherein the catalyst comprises platinum sponge.
Claim 10
Dependent Claim
11 words
A process according to claim 7 wherein the catalyst comprises alumina.
Claim 11
Dependent Claim
99 words
A process according to claim 1 wherein step (a) comprises introducing the water at a flow rate and the purified water condensed in step (e) is collected at a flow rate, which process further comprises adjusting the flow rate of introducing the water in step (a), adjusting the flow rate of collecting purified water from step (e), adjusting the temperature for superheating the steam in step (c) and maintaining the steam at that temperature for a dwell time which, at the adjusted flow rates and temperature, is sufficient to obtain water having desired apyrogeneity and a minimum organic-substance content.
Claim 12
Dependent Claim
31 words
A process according to claim 34 wherein the dwell time is in the order of from 0.05 to 0.2 minute at a temperature of from about 400° to about 700° C.
Claim 13
Dependent Claim
7 words
A single-distillation process according to claim 1.
Claim 14
Dependent Claim
43 words
A distillation process according to claim 1 for obtaining water having at most 0.1 mg/l of organic substance, as determined after freeze drying, and wherein the dwell time of step (d) is sufficient to produce water of such purity at the dwell temperature.
Claim 15
Dependent Claim
7 words
A single-distillation process according to claim 13.
Claim 16
Dependent Claim
24 words
A single-distillation process according to claim 1 wherein the dwell time of step (d) is for a period of from 0.05 to 0.2 minute.
Claim 17
Dependent Claim
124 words
Distillation apparatus for purifying water to a high degree which comprises: (a) container means for containing water being vaporized into steam, (b) charging means for introducing water into the container means, (c) condensing means to condense steam into purified water, (d) conduit means to provide a flow path for conducting steam to the condensing means for the container means, (e) heating means for superheating steam in the conduit means to a temperature in the range of from above 300° up to 700° C., and (f) packing means in the conduit means to increase the flow path of steam superheated by heating means (e) and to maintain steam in the conduit means at the temperature and for a dwell time sufficient to yield apyrogenic water.
Claim 18
Dependent Claim
124 words
Distillation apparatus for purifying water to a high degree which comprises: (a) container means for containing water being vaporized into steam, (b) charging means for introducing water into the container means, (c) condensing means to condense steam into purified water, (d) conduit means to provide a flow path for conducting steam to the condensing means for the container means, (e) heating means for superheating steam in the conduit means to a temperature in the range of from above 300° up to 700° C., and (f) packing means in the conduit means to increase the flow path of steam superheated by heating means (e) and to maintain steam in the conduit means at the temperature and for a dwell time sufficient to yield apyrogenic water.
Claim 19
Dependent Claim
28 words
Apparatus according to claim 16 wherein the condensing means is a reflux condenser, and the packing means is inert with respect to steam and to any impurities therein.
Claim 20
Dependent Claim
18 words
Apparatus according to claim 16 which further comprises means to recover purified water condensed in the condensing means.
Claim 21
Dependent Claim
30 words
Apparatus according to claim 16 wherein the heating means is means to maintain steam in the conduit means at a temperature within the range of from 400° to 700° C.
Claim 22
Dependent Claim
14 words
Apparatus according to claim 16 wherein the heating means is within the conduit means.
Claim 23
Dependent Claim
13 words
Apparatus according to claim 50 wherein said heating means is a radiating device.
Claim 24
Dependent Claim
44 words
Apparatus according to claim 21 wherein the conduit means is a column having an axis, the radiating device comprises a tungsten filament located in the axis of the column and surrounded by a jacket of packing means which are inert with respect to steam.
Claim 25
Dependent Claim
12 words
Apparatus according to claim 22 wherein the packing means are of silica.
Claim 26
Dependent Claim
18 words
Apparatus according to claim 20 wherein the heating means comprises a platinum resistance traversed by an electrical current.
Claim 27
Dependent Claim
48 words
Apparatus according to claim 16 wherein the packing means is of a material which is inert with respect to steam and substances entrained therein, the material being characterised by emission of photons corresponding to a black body at the temperature to which the heating means brings superheated steam.
Claim 28
Dependent Claim
12 words
Apparatus according to claim 25 wherein the material is transparent fused silica.
Claim 29
Dependent Claim
13 words
Apparatus according to claim 25 wherein the material is an opaque inert substance.
Claim 30
Dependent Claim
24 words
Apparatus according to claim 25 wherein the packing means has a low coefficient of expansion, excellent thermal conductivity and very high transparency to photons.
Claim 31
Dependent Claim
13 words
Apparatus according to claim 16 comprising thermal insulating means for the conduit means.
Claim 32
Dependent Claim
29 words
Apparatus according to claim 29 wherein the conduit means is a column coated externally with means to provide good thermal insulation and the heating means is within the column.
Claim 33
Dependent Claim
20 words
Apparatus according to claim 30 wherein the means to provide good thermal insulation is a coating layer of gold plating.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-05-13 | 1983-11-12 | 1984-05-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-05-13 | 1987-11-12 | 1988-05-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-05-13 | 1991-11-12 | 1992-05-13 | $7700.00 | Window Closed / Lapsed |