US4132260A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for hardening of foundry cores
Assignee: Individual
•
Filing: 1977-10-11
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Granted: 1979-01-02
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Expires: 1997-10-11
Abstract
Abstract It is known to harden foundry cores by admixing a polymerizable material therewith and then curing by addition of a catalyst. Means are provided for injecting gaseous catalysts and compressed air, sequentially, into the die which contains the admixture of polymerizable material and foundry core material. In accordance with the invention, the gaseous catalyst and compressed air respectively, are injected into the die containing the mixture of foundry material in measured desired amounts and very rapidly.
Inventors
- 👤 Werner Luber
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 09:51
CPC Classifications
B; B22; B22C; B22C9/00; B22C9/12; B22C9/123; H; H01; H01H; H01H35/00; H01H35/14; H01H35/141; H01H35/142
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
378 words
Method of hardening foundry core means made of a mixture which includes sand and curable compounds in which, to harden the core means, the core means is exposed in a core-forming apparatus to a mixture of a gaseous catalyst and a carrier gas, and to compressed air wherein, in order to accurately predetermine the volume, pressure and temperature of the gaseous catalyst-carrier gas mixture being applied to the core means, and of the compressed air being applied to the core means, the method comprises the providing a source (4, 5, 6) of gaseous catalyst-carrier gas mixture; providing a source (12, 13) of compressed air; providing a first temporary storage vessel (8) for gaseous catalyst-carrier gas mixture; supplying said catalyst-carrier gas mixture from said mixture source to said first temporary storage vessel (8); segregating and temporarily storing a predetermined quantity, which corresponds to the desired amount to cure the core means in the core forming apparatus, of the mixture of gaseous catalyst and carrier gas in the first temporary storage vessel (8); providing a second temporary storage vessel (11) of substantially greater volume capacity than said first temporary storage vessel (8); supplying compressed air from said compressed air source to said second temporary storage vessel; segregating and temporarily storing a predetermined quantity, which corresponds to the desired amount to flush the core means in the core forming apparatus, of compressed air in the second temporary storage vessel (11); controlling pressure, and the temperature of the compressed air in said second temporary storage vessel to be higher than the pressure and temperature of the gaseous catalyst-carrier gas mixture in said first temporary storage vessel to thereby segregate a controlled larger quantity of compressed air therein; suddenly and abruptly and rapidly injecting such stored mixture of gaseous catalyst-carrier gas from said first temporary storage vessel into the core means in the core forming apparatus by admitting the segregated, desired quantity of said stored mixture into the core forming apparatus; and then suddenly and abruptly and rapidly injecting said compressed air from said second temporary storage vessel at said elevated temperature and with said higher pressure into the core means in the core forming apparatus by admitting the segregated desired larger quantity of said stored compressed air into the core forming apparatus.
Claim 2
Dependent Claim
378 words
Method of hardening foundry core means made of a mixture which includes sand and curable compounds in which, to harden the core means, the core means is exposed in a core-forming apparatus to a mixture of a gaseous catalyst and a carrier gas, and to compressed air wherein, in order to accurately predetermine the volume, pressure and temperature of the gaseous catalyst-carrier gas mixture being applied to the core means, and of the compressed air being applied to the core means, the method comprises the providing a source (4, 5, 6) of gaseous catalyst-carrier gas mixture; providing a source (12, 13) of compressed air; providing a first temporary storage vessel (8) for gaseous catalyst-carrier gas mixture; supplying said catalyst-carrier gas mixture from said mixture source to said first temporary storage vessel (8); segregating and temporarily storing a predetermined quantity, which corresponds to the desired amount to cure the core means in the core forming apparatus, of the mixture of gaseous catalyst and carrier gas in the first temporary storage vessel (8); providing a second temporary storage vessel (11) of substantially greater volume capacity than said first temporary storage vessel (8); supplying compressed air from said compressed air source to said second temporary storage vessel; segregating and temporarily storing a predetermined quantity, which corresponds to the desired amount to flush the core means in the core forming apparatus, of compressed air in the second temporary storage vessel (11); controlling pressure, and the temperature of the compressed air in said second temporary storage vessel to be higher than the pressure and temperature of the gaseous catalyst-carrier gas mixture in said first temporary storage vessel to thereby segregate a controlled larger quantity of compressed air therein; suddenly and abruptly and rapidly injecting such stored mixture of gaseous catalyst-carrier gas from said first temporary storage vessel into the core means in the core forming apparatus by admitting the segregated, desired quantity of said stored mixture into the core forming apparatus; and then suddenly and abruptly and rapidly injecting said compressed air from said second temporary storage vessel at said elevated temperature and with said higher pressure into the core means in the core forming apparatus by admitting the segregated desired larger quantity of said stored compressed air into the core forming apparatus.
Claim 3
Dependent Claim
30 words
Method according to claim 1, wherein the temperature of the catalyst-carrier gas mixture is about 30°-50° C., and the temperature of the compressed air is about 100° to 115° C.
Claim 4
Dependent Claim
28 words
Method according to claim 1, wherein the volume of gaseous catalyst-carrier gas mixture is about 1 liter; and the volume of heated, compressed air is about 10 liters.
Claim 5
Dependent Claim
81 words
Method according to claim 1, wherein the step of segregating and temporarily storing the mixture gaseous catalyst and carrier gas, comprises segregating a quantity of about 1 liter and storing said quantity, temporarily, at a temperature of about 30° C. in said first vessel (8), and the step of segregating and temporarily storing the compressed air comprises segregating and storing a quantity of about 10 liters of compressed air at a temperature of about 100°-115° C. in said second vessel (11).
Claim 6
Dependent Claim
64 words
Method according to claim 1, wherein the step of segregating and temporarily storing the compressed air comprises storing compressed air at a temperature of about 100°-115° C. and at the pressure of 4 to 8, atm gauge and having a volume of about 10 times the volume of the gaseous catalyst-carrier gas mixture at a pressure of said mixture of about 2 atm gauge.
Claim 7
Dependent Claim
21 words
A method according to claim 1 wherein, prior to any curing steps, foundry core material is injected into a core-forming apparatus.
References Cited (Backward Citations)
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-01-01 | 1982-07-03 | 1983-01-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-01-01 | 1986-07-03 | 1987-01-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-01-01 | 1990-07-03 | 1991-01-02 | $7700.00 | Window Closed / Lapsed |