会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 2. 发明专利
    • CARBON DIOXIDE CLATHRATE PRODUCTION MEASURING APPARATUS
    • JPH0658896A
    • 1994-03-04
    • JP21272092
    • 1992-08-10
    • CHUBU ELECTRIC POWERMITSUBISHI HEAVY IND LTD
    • SAKAI MATSUSHIGESAJI AKIRANODA HIDETOMOTANII TADAAKINEGORO MASAAKIMINEMOTO MASAKIKITAMURA HIKARIKAMATA TOSHIHIRO
    • C01B32/50G01N27/06C01B31/20
    • PURPOSE:To determine production of carbon dioxide clathrate quantitatively by previously separating solid state clathrate mixed in a solution contained in a reaction vessel through a filter and then measuring electric conductivity of solution subjected to pretreatment. CONSTITUTION:Sample water 12 containing chlorine ions is injected through a sample liquid injection pump 13 into a reaction vessel 11 while furthermore carbon dioxide 14 is injected through an injection pump 15. The vessel 11 is placed in a cooling water tank 16. Carbon dioxide clathrate reaction is then promoted while stirring water and carbon dioxide by means of a stirrer 18 coupled with a motor 17. Reaction temperature and reaction pressure are measured, respectively, through a thermometer 19 and a pressure gauge 20 and recorded on a recorder 21. At that time, a solution discharge valve 22 for measuring electric conductivity in the reaction vessel is opened to produce pressure difference with respect to the atmospheric pressure thus separating solid state carbon dioxide clathrate through a filter 24 disposed in front of a vessel 23 for measuring electric conductivity in the reaction vessel. Solution mixed with no carbon dioxide clathrate is then filled in the vessel 23 and electric conductivity thereof is measured by means of an electric conductivity meter 26 associated with a sensor 25 for measuring electric conductivity. Measurement of electric conductivity is then converted through a data analyzer 27 into a production quantity of carbon dioxide clathrate.
    • 5. 发明专利
    • INK DRYING DEVICE
    • JPH08118602A
    • 1996-05-14
    • JP25343994
    • 1994-10-19
    • MITSUBISHI HEAVY IND LTD
    • HATANO SHIGEKAZUNAGANO HAYAMIMINEMOTO MASAKIWATANABE ICHIRO
    • B41F23/04F26B13/02
    • PURPOSE: To provide an ink drying device which can minimize exhaust gas amount to the outside and attain reduction in size and running cost. CONSTITUTION: Printing paper 5 is moved to going and returning passages in a dryer 6 continuously. High density heating gas on the going passage side of the dryer 6 is circulated in the order of a high density side circulating gas suction port 14, a gas circulating blower 15, a circulating gas heater 17, a high density side circulating gas blowing-off port 13 and the high density side circulating gas suction port 14. On the other hand, low density heating gas on the returning passage side of the dryer 6 is circulated in the order of a low density side circulating gas suction port 8, a gas circulating blower 9, a circulating gas heater 11, a low density side circulating gas blowing-off port 7 and the low density side circulating gas suction port 8. Therefore, high density heating gas on the going passage side and low density heating gas on the returning passage side are sprayed against the printing paper 5 from the respective gas blowing-off ports 13, 7.
    • 9. 发明专利
    • TREATMENT OF LIQUID USING ADSORPTION TOWER
    • JPH0557107A
    • 1993-03-09
    • JP21856691
    • 1991-08-29
    • MITSUBISHI HEAVY IND LTDDAINIPPON PRINTING CO LTD
    • MINEMOTO MASAKIKITA YOSHIHIROEITO TORU
    • B01D15/00C02F1/28
    • PURPOSE:To enhance the recovery of the component adsorbed lay on an adsorbent and to reduce the desorbing solution for desorbing the adsorbed component from the adsorbent by using the solution flowing out of an adsorption tower in the latter half of a liquid substituting period as a part of the desorbing solution. CONSTITUTION:The substitution of a rinse solution is performed on and after the first cycle using the rinse solution stored in a rinse solution tank 3 in place of a desorbing solution in the first half of liquid substitution. By this method, the solution flowing out of an adsorption tower 1 to flow to a passage 9 is stored in a third recovery tank 7. In the latter half of liquid substitution, the substitution of the desorbing solution is performed using the desorbing solution in a desorbing solution tank 2. At this time, the solution flowing out of the adsorption tower 1 to flow to the passage is stored in the rinse solution tank 3 to prepare for the substitution of the rinse solution of the next cycle. By this constitution, the amount of the desorbing solution supplied from the desorbing solution tank 2 to the adsorption tower 1 can be reduced. The high concn. outflow time of an adsorbed component at the time of the recovery of the desorbing solution is extended and the recovery of the adsorbed component is enhanced.