GB569710A - Improvements in or relating to the drying of grain and apparatus therefore - Google Patents

Improvements in or relating to the drying of grain and apparatus therefore

Info

Publication number
GB569710A
GB569710A GB1499343A GB1499343A GB569710A GB 569710 A GB569710 A GB 569710A GB 1499343 A GB1499343 A GB 1499343A GB 1499343 A GB1499343 A GB 1499343A GB 569710 A GB569710 A GB 569710A
Authority
GB
United Kingdom
Prior art keywords
grain
sieve
adsorbent material
regenerator
fed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB1499343A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to GB1499343A priority Critical patent/GB569710A/en
Publication of GB569710A publication Critical patent/GB569710A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00Drying solid materials or objects by processes not involving the application of heat
    • F26B5/16Drying solid materials or objects by processes not involving the application of heat by contact with sorbent bodies, e.g. absorbent mould; by admixture with sorbent materials

Landscapes

  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Molecular Biology (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Fats And Perfumes (AREA)

Abstract

569,710. Drying systems. MORAN, T., and JONES, C. R. Sept. 13, 1943, No. 14993. [Class 34 (ii)] [Also in Group I] A process for drying grain consists in mixing therewith relatively small quantities ' of adsorbent materials such as silica gel or activated alumina, the adsorbent being '-removed from the grain after a relatively short time, then regenerated and again added to the grain, and so on in succession. The expression relatively small quantity" means a quantity which is small in comparison with that required to reduce the moisture content of the grain to any predetermined value in a given time, and " a relatively short time " means a period of time which is short in comparison with that required to reduce the moisture of a given quantity of the grain to any predetermined value. In one construction, shown diagrammatically in Fig 1, a grain drying plant comprises three bins a<1>, a2, a3, to which grain is fed by bucket or screw elevators b<1>, b<2>, b3, and to which adsorbent material is fed at d from a regenerator e. The contents of each bin passes over a series of sieves c<1>, c<2>, c<3>, which permit the adsorbent material to pass through them, such material being conveyed to the regenerator. The grain passes over the sieves to be fed to the next bin, the last sieve c<3> discharging into a bag h or like receptacle. The grain, before reaching the first bin a<1>,passes over a further sieve c which effects a preliminary cleaning. In a modification, Figs. 3 and 4, the grain is fed at t to a rotating drum u fitted with scoops v which carry the grain and adsorbent material up to drop them on to an inclined sieve w. The adsorbent material passes into the drum from regenerator 13 at 14 and is distributed over the grain by a screw conveyor x working in an apertured trough y. Sieve w permits the passage therethrough of the adsorbent mixture which is conveyed back to the regenerator by a screw conveyor 11. The grain falls back into the drum and eventually discharging into a bag 15. In a further modification, Fig. 2 (not shown), the grain and adsorbent material are fed to an inclined vibrating sieve arranged over a hopper, the latter serving to receive the adsorbent material which passes through the sieve and to deliver it to the regenerator. The grain passes down the sieve and is eventually discharged into bags or like receptacle. In the above processes any fine dust caused by the break-up of the adsorbent material, and which may adhere to the grain prior to its cleaning before milling, acts as an inhibitor to insect nests.
GB1499343A 1943-09-13 1943-09-13 Improvements in or relating to the drying of grain and apparatus therefore Expired GB569710A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1499343A GB569710A (en) 1943-09-13 1943-09-13 Improvements in or relating to the drying of grain and apparatus therefore

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1499343A GB569710A (en) 1943-09-13 1943-09-13 Improvements in or relating to the drying of grain and apparatus therefore

Publications (1)

Publication Number Publication Date
GB569710A true GB569710A (en) 1945-06-05

Family

ID=10051181

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1499343A Expired GB569710A (en) 1943-09-13 1943-09-13 Improvements in or relating to the drying of grain and apparatus therefore

Country Status (1)

Country Link
GB (1) GB569710A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2600367A (en) * 1948-04-30 1952-06-10 American Cyanamid Co Capsule drying and burnishing method
US2730814A (en) * 1953-03-25 1956-01-17 Commercial Solvents Corp Process for drying materials of high moisture diffusion resistance
DE1604992B1 (en) * 1963-04-02 1970-04-09 Mizusawa Industrial Chem Process for the continuous drying of water-containing gel bodies
WO2001090669A1 (en) * 2000-05-25 2001-11-29 Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno Method for drying finely divided substances

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2600367A (en) * 1948-04-30 1952-06-10 American Cyanamid Co Capsule drying and burnishing method
US2730814A (en) * 1953-03-25 1956-01-17 Commercial Solvents Corp Process for drying materials of high moisture diffusion resistance
DE1604992B1 (en) * 1963-04-02 1970-04-09 Mizusawa Industrial Chem Process for the continuous drying of water-containing gel bodies
WO2001090669A1 (en) * 2000-05-25 2001-11-29 Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno Method for drying finely divided substances
NL1016895C2 (en) * 2000-05-25 2001-11-30 Tno Method for drying finely divided substances.
US6986213B2 (en) 2000-05-25 2006-01-17 Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno Method for drying finely divided substances

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