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    • 62. 发明专利
    • COOKING OF LIGNOCELLOSIC MATERIAL
    • JP2000336587A
    • 2000-12-05
    • JP15078299
    • 1999-05-28
    • JUJO PAPER CO LTDKAWASAKI KASEI CHEMICALSASAHI GLASS CO LTD
    • SHIMIZU MASAHIROWATABE KEIGOANDO TATSUYANAKAO MAKOTO
    • D21C3/00D21C3/02D21C3/22D21C3/24D21C7/00
    • PROBLEM TO BE SOLVED: To reduce the Kappa number at the same effective alkali addition ratio and improve the pulp yield at the same Kappa number in a method for cooking a lignocellulosic material. SOLUTION: This method comprises using hardwood or coniferous chips, adding an alkaline cooking liquor containing a polysulfide sulfur at 3-20 g/L concentration expressed in terms of sulfur content and further the sulfur content in an amount of 45-100 wt.% and an effective alkali in an amount of 45-79 wt.% based on the respective total amounts contained in the alkaline cooking liquor introduced into the cooking system to the top of a permeating vessel and further feeding an alkaline cooking liquor containing a quinone compound in a specific amount based on the bone-dry chips to the permeating vessel or the bottom of an upper cooking zone in the continuous cooking method using two vessel digesting devices comprising the permeating vessel installed in front of a digester and a column top zone, the upper cooking zone and a lower cooking zone installed from the top to the bottom in the interior of the digester, a strainer arranged in each zone bottom and capable of discharging a cooking black liquor extracted from at least the one strainer of the respective strainers to the outside of the cooking system.
    • 63. 发明专利
    • HUMIDIFYING METHOD
    • JPH02293551A
    • 1990-12-04
    • JP11406389
    • 1989-05-09
    • ASAHI GLASS CO LTD
    • NAKAO MAKOTOHORIE HIROFUMIYAMADA YOSHIKAZUSUGAYA YOSHIO
    • F24F6/04B01D53/22B01D53/26B01D71/82C08J5/20
    • PURPOSE:To obtain a humidifying method having large water, steam permeating speed by controlling stationary ion concentration of an ion exchanger film, water absorption rate, ion exchange volume in specific ranges by a humidifying film. CONSTITUTION:Gas to be humidified is brought into contact with one side face of a humidifying film, and water is brought into contact with the other side face to humidify the gas. The film is formed of an ion exchange layer having 40-150vol.% of water absorption rate, 0.5-6N of stationary ion concentration, 0.6-2.5meq./g of resin of ion exchange volume, 0.1-300mum of thickness, and steam permeating speed is 100Nm /m .hr.atm or more. If the ion concentration exceeds 6N, the steam permeating speed is remarkably reduced, while if it is 0.5N or less, the speed is decreased, and impurities sucdh as calcium contained in water are permeated through the film. If the water absorption rate is 40vol.% or less, the steam permeating speed is reduced, while if it exceeds 150vol.%, film state retention capacity is lost. It is desirable for the ion exchange volume to be 0.6-2.5meq/g of resin so that a film having excellent steam permeating speed and high film strength may be obtained.
    • 68. 发明专利
    • TREATMENT OF ELECTRODE
    • JPS6267187A
    • 1987-03-26
    • JP20655985
    • 1985-09-20
    • ASAHI GLASS CO LTD
    • NAKAO MAKOTOKISHINO HIDEJI
    • C25B11/06
    • PURPOSE:To adequately regenerate an electrode having debased activity by immersing the electrode stuck with a porous nickel layer on a base body surface into an aq. inorg. acid soln. so that only the porous nickel layer is eliminated and dissolved. CONSTITUTION:The porous nickel layer contg. Raney-nickel alloy particles, etc. is stuck to the electrode for electrolysis. The electrode is immersed in the aq. soln. of >=1 kinds selected from a hydrochloric acid, sulfuric acid and nitric acid at a relatively low temp. of about 0-60 deg.C when the electrode activity of said electrode is debased. The Raney-nickel particles which are lost in the electrode activity react easily with the inorg. acid and are dissolved in the form of a nickel salt. The iron and nickel hydroxide sticking to the electrode are dissolved in the liquid in the above-mentioned process. On the other hand, the electrode base body hardly dissolves; therefore, only the porous nickel layer is selectively removed. The acid used for the dissolution is reused for electroplating after impurities such as iron are removed therefrom.