Abstract:
IN CATALYST IN A REACTION TANK HAVING A MATERIAL FEED PIPE AT THE LOWER PORTION THEREOF AND A PRODUCT-TAKINGOUT-PIPE AT THE UPPER PORTION THEREOF, A DISCHARGE NOZZLE AND A SUCTION NOZZLE ARE PROVIDED, THE DISCHARGE NOZZLE BEING CONNECTED TO THE DISCHARGE SIDE OF A PUMP PROVIDED OUTSIDE THE REACTION TANK AND THE SUCTION NOZZLE BEING CONNECTED TO THE SUCTION SIDE OF THE PUMP, RESPECTIVELY. WHEN THE PUMP OPERATES, A REACTION LIQUID IS DISCHARGED FROM THE DISCHARGED NOZZLE AND THEN SUCKED INTO THE SUCTION NOZZLE ALONG WITH CATALYST. THUS, CATALYST IS RECOVERED IN A CATALYST RECOVERY TANK PROVIDED BETWEEN THE SUCTION NOZZLE AND THE PUMP, AND THE REACTION LIQUID IS CIRCULATED FROM THE PUMP TO THE SUCTION NOZZLE THROUGH THE DISCHARGE NOZZLE. EITHER THE DISCHARGE NOZZLE OR THE SUCTION NOZZLE
IS, AS OCCASION DEMANDS, SLID SO AS TO MAKE CONTACT WITH THE OTHER. THUS, THE INNER SURFACE OF THE SUCTION NOZZLE IS RINSED BY CIRCULATING A REACTION LIQUID, AND THEREBY CATALYST ADHERING TO THE INNER SURFACE OF THE SAID SUCTION NOZZLE IS REMOVED.
Abstract:
WHEN A-GLACTOSIDASE IS FORMED IN THE MYCELIUM OF MORTIERELLA VINACEA VAR, RAFFINOSEUTILIZER (ATCC NO. 20034), IT IS SUBSTANTIALLY FREE FROM INVERTASE. MYCELLIAL MATTER TAKEN FROM THIS MOLD AND PREPARATION CONTAINING THE ENZYME MAY THUS BE ADDED TO SUGAR BEET JUICE OR BEET MOLASSES FOR REDUCING THE RAFFINOSE CONTENT OF THE SAME, THEREBY GREATELY INCREASING THE RECOVERY OF SUCROSE CONTENT.
Abstract:
A METHOD OF MANUFACTURING POLYETHYLENE DIFFRACTION GRATING IN WHICH A HIGH OR MEDIUM DENSITY POLYETHYLENE FILM HELD BETWEEN CELLOPHANE FILMS OR POLYIMIDE FILMS IS PASSED AT A CONSTANT VELOCITY OVER AND MAINTAINED IN CLOSE CONTACT WITH HEATING ZONE AND COOLING ZONE WHICH ARE MAINTAINED AT PREDETERMINED TEMPERATURES.
Abstract:
WOOD OR OTHER VEGETABLE MATERIAL HAVING A NON-UNIFORM SHAPE SUCH AS SHAPELESS PARTICLE POWDER, FLAKY POWDER, CHIP AND THE OTHERS IS CARBONIZED IN AN ACIDIC ATMOSPHERE CONTAINING VAPOR OR GAS OF HYDROCHLORIC OR HYDROBROMIC ACID OR ITS ANHYDRIDE FOR 10 MINUTES TO 10 HOURS AT A TEMPERATURE OF 80-1200* C. TO OBTAIN ACTIVATED CARBON OF SUPERIOR ADSORPTION ACTIVITY IN VERY HIGH YIELDS. IF DESIRED, THE ACTIVATED CARBON SO OBTAINED IS HEATED FURTHER IN AN ATMOSPHERE CONTAINING AN OXIDIZING GAS SUCH AS STEAM, CARBON DIOXIDE GAS OR AIR, OR IN AN INERT ATMOSPHERE TO IMPROVE THE ADSORPTION ACTIVITY OF SAID CARBON.