| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 161 | Heating corn syrup solids with acids to produce a dry powder | US3657010D | 1970-01-26 | US3657010A | 1972-04-18 | MITCHELL WILLIAM A; SEIDEL WILLIAM C |
| Hydrolyzed starch materials such as corn syrups are heated in the presence of acid to a temperature of about 300* F. to 370* F. The resultant product is allowed to cool and solidify; it may then be ground to a dry powder. The powder so produced can be stored in paper envelopes under rather severe temperature humidity conditions and will remain dry and will not clump.
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| 162 | Method of producing granular dextrose | US3650829D | 1969-08-06 | US3650829A | 1972-03-21 | WALON RAOUL GUILLAUME PHILIPPE |
| A process for producing a granular dextrose product having a high content of beta dextrose by seeding a starch hydrolyzate solution containing at least about 90% by weight dry substance, and having a dextrose equivalent of at least 90, to obtain a crystallized mass, breaking the mass up into particles, and recovering a granular dextrose product. Also, the use of the product for lozenges and bakery products.
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| 163 | Dextrose crystallization process | US3592688D | 1969-09-10 | US3592688A | 1971-07-13 | DEAN GEORGE RHOADES; PYLE RONALD EMMETT |
| RELATIVELY LARGE CRYSTALS OF DEXTROSE HYDRATE CAN BE CONSISTENTLY PRODUCED BY A PROCESS WHICH COMPRISES CONTACTING A SUPERSATURATED SOLUTION OF DEXTROSE WITH DEXTROSE HYDRATE SEED CRYSTALS AT A TEMPERATURE BELOW ABOUT 90*F. DURING DEXTROSE CRYSTALLIZATION TO FORM A MASSECUITE AND RECOVERING CRYSTALS OF DEXTROSE HYDRATE FROM SUCH MASSECUITE.
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| 164 | Isothermal crystallization of dextrose | US3547696D | 1967-11-06 | US3547696A | 1970-12-15 | MUELLER HELMUT |
| 165 | Process for preparing a dry free-flowing glucose product from a solution thereof | US3477874D | 1965-04-15 | US3477874A | 1969-11-11 | REPSDORPH INGER; KROYER KARL KRISTIAN KOBS; DAMGARD-IVERSEN JORGEN |
| 166 | Process for crystallizing dextrose | US45309965 | 1965-05-04 | US3406046A | 1968-10-15 | TITTELBOOM MARCEL L E VAN |
| 167 | Process for producing dextrose | US30808463 | 1963-09-11 | US3265533A | 1966-08-09 | HARRY MEISEL |
| 168 | Process for producing dextrose | US35906964 | 1964-04-13 | US3239378A | 1966-03-08 | OPILA ROBERT L |
| Substantially anhydrous dextrose (containing at least 40% anhydrous b -dextrose, dissolving readily in water and being stable against loss of b -dextrose content) is prepared by spraying a dextrose liquor (containing at least 90% dextrose and 88-98% dry substance) maintained at 105-150 DEG C., on to a seed bed (consisting essentially of dextrose) maintained at 10-40 DEG C., continuously mixing the liquor and seed bed until substantially complete crystallization of the dextrose in the liquor occurs, discharging the resultant crystallized material from the mixing zone at 30-60 DEG C. into a stream of air, maintained at 5-35 DEG C. and having a relative humidity below 60%, and simultaneously cooling the crystallized product to 10-40 DEG C. and evaporating the residual moisture therefrom by means of the heat of crystallization of the dextrose and sensible heat of said liquor. Sensible heat is defined as the heat evolved as the liquor cools. It is preferred to use a seed bed composed of anhydrous dextrose crystals. Total hydrolysate liquors resulting from enzymatic hydrolysis of starch may provide the dextrose liquor. The process is illustrated by reference to flow sheets and drawings of apparatus (not shown). Reference has been directed by the Comptroller to Specification 843,787. | ||||||
| 169 | Process for producing sugars from starch | US20840962 | 1962-07-09 | US3236687A | 1966-02-22 | SMITH NORMAN B; PETZOLD EDGAR N |
| Glucose is produced by hydrolysing starch to convert it to glucose, clarifying the hydrolysate, evaporating the hydrolysate to a solids content above 88% by weight, mixing the concentrated hydrolysate with a gas and subjecting the concentrated hydrolysate to a shearing stress whereby solidification of crystalline glucose is achieved, and recovering the solidified glucose. The gas used is any gas which is inert to the concentrated hydrolysate, e.g. air, nitrogen and oxygen. The starch is hydrolysed by means of a mineral acid or microbiological enzymes. Before concentration the hydrolysate may be purified by treatment with ion exchange resins. The shearing stress is preferably applied by means of gear type pumps in which the concentrated hydrolysate is subjected to a shearing action by the meshing gears. | ||||||
| 170 | Spray drying of liquids | US28999363 | 1963-06-24 | US3236285A | 1966-02-22 | MEE ANTONY J; ABEL SMITH THOMAS |
| 171 | Method of producing dried starch conversion product | US20422262 | 1962-06-21 | US3197338A | 1965-07-27 | HURST THOMAS L; GAUDLITZ ROBERT T |
| 172 | Manufacture of dextrose controlling particle size | US45268654 | 1954-08-27 | US2901382A | 1959-08-25 | ROHWER ROBERT G; CADOTTE JOHN E; HAROLD RETER |
| 173 | Stabilized dextrose composition | US60310756 | 1956-08-09 | US2854359A | 1958-09-30 | WILSON ALEXANDER L; IRWIN FRANKEL |
| 174 | Method of recovering sugar crystals from solution | US31943240 | 1940-02-17 | US2213710A | 1940-09-03 | AUGUST LUDWIG; SWIHART CALVIN L |
| 175 | Nonhygroscopic starch conversion product and method of manufacture | US19742338 | 1938-03-22 | US2192952A | 1940-03-12 | OTTOMAR WOLFF |
| 176 | Production of high purity crystalline dextrose | US7917736 | 1936-05-11 | US2152874A | 1939-04-04 | COPLAND CHARLES J |
| 177 | Dried corn sirup product and method of producing the same | US5940836 | 1936-01-16 | US2149517A | 1939-03-07 | FLEMING RAPHAEL S; PARKER FREDERICK D; GERE HAWLEY WILLIAM |
| 178 | Method of controllably retarding the crystallization of dextrose | US2706535 | 1935-06-17 | US2145662A | 1939-01-31 | MINER CARL S; ALVA THOMPSON |
| 179 | Production of dextrose | US4356235 | 1935-10-04 | US2100433A | 1937-11-30 | DALE JULIAN K |
| 180 | Manufacture of dextrose | US70947934 | 1934-02-02 | US2065724A | 1936-12-29 | NEWKIRK WILLIAM B |
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