US4314877A
Expired / Lapsed
US
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Method and apparatus for drying radioactive waste water concentrates from evaporators
Assignee: Kraftwerk Union AG
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Filing: 1980-10-28
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Granted: 1982-02-09
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Expires: 2000-10-28
Abstract
Abstract Drying radioactive waste water concentrates from evaporators to produce a dried product of low residual moisture by (a) preheating a waste water concentrate with a solids content of at most 20% by weight to a temperature of 50°-70° C., (b) passing the preheated concentrate with a solids content of at most 20% by weight into a two-cylinder drier at the rate of 10 to 20 liters per square meter of usable cylinder surface per hour, (c) maintaining the cylinder temperature between about 160° to 210° C., (d) retaining the concentrate in the drier for a residence time of 7 to 18 seconds on the cylinder to produce a dried product of low residual moisture on the cylinder surface, and (e) discharging the dried product of low residual moisture from the cylinder surface.
Inventors
- 👤 Horst Queiser
- 👤 Othmar Meichsner
- 👤 Dietmark Erbse
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 20:34
CPC Classifications
G; G21; G21F; G21F9/00; G21F9/04; G21F9/06; G21F9/08; Y; Y10; Y10S; Y10S159/00; Y10S159/12
Claims Analysis
Total Claims: 22
Claim 1
Independent Claim
126 words
Method for drying radioactive waste water concentrates from evaporators which comprises (a) preheating a waste water concentrate with a solids content of at most 20% by weight to a temperature of 50°-70° C., (b) passing the preheated concentrate with a solids content of at most 20% by weight into a two-cylinder drier at the rate of 10 to 20 liters per square meter of usable cylinder surface per hour, (c) maintaining the cylinder temperature between about 160° to 210° C., (d) retaining the concentrate in the drier for a residence time of 7 to 18 seconds on the cylinder to produce a dried product of low residual moisture on the cylinder surface, and (e) discharging the dried product of low residual moisture from the cylinder surface.
Claim 2
Dependent Claim
126 words
Method for drying radioactive waste water concentrates from evaporators which comprises (a) preheating a waste water concentrate with a solids content of at most 20% by weight to a temperature of 50°-70° C., (b) passing the preheated concentrate with a solids content of at most 20% by weight into a two-cylinder drier at the rate of 10 to 20 liters per square meter of usable cylinder surface per hour, (c) maintaining the cylinder temperature between about 160° to 210° C., (d) retaining the concentrate in the drier for a residence time of 7 to 18 seconds on the cylinder to produce a dried product of low residual moisture on the cylinder surface, and (e) discharging the dried product of low residual moisture from the cylinder surface.
Claim 3
Dependent Claim
25 words
Method according to claim 1, wherein the preheated concentrate passed into the drier has a content of filterable solids of at most 5% by weight.
Claim 4
Dependent Claim
18 words
Method according to claim 1, wherein the drying takes place under reduced pressure of 0.8 to 0.1 bar.
Claim 5
Dependent Claim
22 words
Method according to claim 1, wherein the waste water concentrate prior to drying is adjusted to a pH-value of 3 to 8.
Claim 6
Dependent Claim
24 words
Method according to claim 1, wherein the waste water concentrate contains boron salts and wherein the cylinder temperature is between 180° to 210° C.
Claim 7
Dependent Claim
21 words
Method according to claim 5, wherein the concentrate is adjusted to a sodium metaborate content of at most 10% by weight.
Claim 8
Dependent Claim
16 words
Method according to claim 6, wherein the sodium metaborate content is adjusted by adding calcium chloride.
Claim 9
Dependent Claim
24 words
Method according to claim 4, wherein the waste water concentrate contains boron salts and wherein the cylinder temperature is between 180° and 210°0 C.
Claim 10
Dependent Claim
21 words
Method according to claim 8, wherein the concentrate is adjusted to a sodium metaborate content of at most 10% by weight.
Claim 11
Dependent Claim
16 words
Method according to claim 9, wherein the sodium metaborate content is adjusted by adding calcium chloride.
Claim 12
Dependent Claim
160 words
Apparatus for drying radioactive waste water concentrates from evaporators comprising (a) a feed tank equipped with a stirrer and with a jacket for the passage of a heating medium to heat the tank, (b) an inlet opening in the tank for the introduction of waste water concentrates from evaporators, (c) a discharge opening near the bottom of the tank and a return opening near the top of the tank together with connecting conducts and an interposed pump to form a circulatory loop for circulating waste water concentrates from and to the tank, (d) a bleeder line having one end connected to the circulatory loop for bleeding waste water concentrates, and having a line length shorter than the loop, (e) a pump connected to the bleeder line to regulate the flow of concentrates therethrough, (f) said bleeder line having its other end connected to a two-cylinder drier with a scraper associated with the cylinders to remove dry material from the cylinders.
Claim 13
Dependent Claim
160 words
Apparatus for drying radioactive waste water concentrates from evaporators comprising (a) a feed tank equipped with a stirrer and with a jacket for the passage of a heating medium to heat the tank, (b) an inlet opening in the tank for the introduction of waste water concentrates from evaporators, (c) a discharge opening near the bottom of the tank and a return opening near the top of the tank together with connecting conducts and an interposed pump to form a circulatory loop for circulating waste water concentrates from and to the tank, (d) a bleeder line having one end connected to the circulatory loop for bleeding waste water concentrates, and having a line length shorter than the loop, (e) a pump connected to the bleeder line to regulate the flow of concentrates therethrough, (f) said bleeder line having its other end connected to a two-cylinder drier with a scraper associated with the cylinders to remove dry material from the cylinders.
Claim 14
Dependent Claim
36 words
Apparatus according to claim 11, wherein said pump connected to the bleeder line is a readjustable eccentric worm pump, which feeds into an oscillating tube which can be moved in the longitudinal direction of the cylinders.
Claim 15
Dependent Claim
39 words
Apparatus according to claim 12, wherein the oscillating tube is connected to the bleeder line by means of a flexible hose and the end of the oscillating tube facing the cylinders ends 1 to 20 cm above the cylinders.
Claim 16
Dependent Claim
22 words
Apparatus according to claim 13, wherein said scrapers associated with the cylinders are pressed-on and readjusted by means of a compressed-air cylinder.
Claim 17
Dependent Claim
41 words
Apparatus according to claim 14, wherein beneath said scraper into which the dry material sequentially passes are a discharge funnel, a filling line, a hood and lifting station for tanks for receiving the dry material, which are provided with heating devices.
Claim 18
Dependent Claim
23 words
Apparatus according to claim 15, wherein the discharge funnel, the filling line and the lifting station are each equipped with a vibration device.
Claim 19
Dependent Claim
23 words
Apparatus according to claim 11, wherein said two-cylinder drier is connected to a vapor outlet line which is connected to a washing tank.
Claim 20
Dependent Claim
56 words
Apparatus according to claim 17, wherein a pump for maintaining reduced pressure in the two-cylinder drier is interposed in said vapor outlet line following said washing tank, and wherein the vapor outlet line from said pump leads through a water tank having a vapor release line in which is disposed a separator for removal of droplets.
Claim 21
Dependent Claim
53 words
Apparatus according to claim 11, wherein said two-cylinder drier has at its upper end a rinsing-water line and a connection for adding chemicals, such as cleaning agents and the like, to pump water entering through the rinsing line with the chemicals dissolved therein in circulation through the drier for the purpose of decontamination.
Claim 22
Dependent Claim
22 words
Apparatus according to claim 11, wherein the cylinder surfaces and the surfaces in the area of the vapors consist of corrosion-resistant steel.
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) | 1985-02-08 | 1985-08-10 | 1986-02-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-02-08 | 1989-08-10 | 1990-02-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-02-08 | 1993-08-10 | 1994-02-09 | $7700.00 | Window Closed / Lapsed |