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
    • 17. 发明专利
    • Modification of coal
    • 煤的修改
    • JPS61126200A
    • 1986-06-13
    • JP24451184
    • 1984-11-21
    • Mitsubishi Heavy Ind Ltd
    • UEDA TAKASHIKAJIMOTO HIKOKUSUSERA TOSHIKUNI
    • C10G1/06B01J23/00B01J23/88C10L9/04
    • PURPOSE: To modify coal and to obtain modified coal of a high calorific value in a high liquid yield, by thermally treating the coal with addition of water and a hydrogen donor in the presence of CO and a Co.Mo-base catalyst.
      CONSTITUTION: To 1pt.wt., on a dry ashless base, (low-grade) coal 4 are added 1pt.wt or more water 5 and 0.5pt.wt. or more hydrogen donor solvent 6 such as hydrogenated anthracene oil and the resulting mixture is sent to a reactor 1, where it is thermally treated at 300W500°C under a CO pressure of 1W200kg/ cm
      2 G for 1W3hr, with addition of CO 7 and a Co.Mo-base catalyst 8 comprising about 5% CoO and about 15% MoO
      3 supported on a heat-resistant porous substrate suchas Al
      2 O
      3 nd presulfurized with H
      2 S for a predetermined time. The reaction product 9 is sent to a high-temp. gas/liquid separator 2 and separated from oil-cong. modified coal 13, while gas-contg. light oil 10 is separated into gas 11 and high oil 12 by a low-temp. gas/liquid separator 3.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:通过在CO和CO基催化剂的存在下,通过添加水和氢供体来对煤进行热处理,以改善煤和获得高产量的高热值的改性煤。 构成:在1重量份的干燥无灰基础上,(低级)煤4加入1pt.wt以上的水5和0.5pt.wt。 或更多的氢供体溶剂6,例如氢化蒽油,并将所得混合物送入反应器1,在其中在300-500℃下在1-200kg / cm 2 G的CO压力下热处理1 -3小时,加入CO 7和包含负载在耐热多孔基材上的约5%CoO和约15%MoO 3的Co.Mo基催化剂8,如Al2O3并用H 2 S预硫预定时间。 将反应产物9送至高温。 气/液分离器2并与油 - 分离。 改性煤13,同时加气。 轻油10通过低温分离成气体11和高油12。 气/液分离器3。
    • 18. 发明专利
    • Preparation of calcined titanium oxide and catalyst
    • 计算氧化钛和催化剂的制备
    • JPS5935025A
    • 1984-02-25
    • JP14366482
    • 1982-08-19
    • Mitsubishi Heavy Ind LtdSakai Chem Ind Co Ltd
    • SERA TOSHIKUNIMITSUOKA SHIGEAKIMORII ATSUSHISUYAMA KOUHEIABE KAZUMITSUNAKATSUJI TADAOBABA TOSHIKATSUMATSUDA TOSHIAKI
    • B01D53/94B01J21/06B01J23/10B01J23/12B01J23/22B01J23/24B01J23/28B01J23/30B01J23/34B01J23/70C01G23/00C04B35/46
    • PURPOSE: To prepare a calcined titanium oxide, having a large surface area, improved strength and heat resistance, and suitable for a catalyst or catalytic carrier, by adding a fine particulate silicic acid to titanium sulfate, hydrolyzing the titanium sulfate heating, and drying and calcining the hydrolysis product.
      CONSTITUTION: A fine particulate silicic acid is added to hydrolyze titanium sulfate under heating, and the resultant hydrolysis product is then dried and calcined to prepare calcined titanium oxide. In the method, the titanium sulfate is hydrolyzed under heating preferably in the presence of a fine particulate silicic acid to produce metatitanic acid, which is then converted into a sol. The resultant sol is filtered, dried and calcined. The presence of the fine particulate silicic acid suppresses the crystal growth of the titanium oxide in calcination, and the ungrown anatase type crystals remain. Thus, the aimed calcined titanium oxide having a large surface area and improved mechanical strength and heat resistance is obtained. The resultant product is suitably used as a catalytic carier or directly as a catalyst.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:为了制备具有大表面积,改善的强度和耐热性并且适用于催化剂或催化载体的煅烧二氧化钛,通过将细颗粒硅酸加入到硫酸钛中,水解硫酸钛加热和干燥, 煅烧水解产物。 构成:在加热下加入细粒状硅酸水解硫酸钛,然后将所得水解产物干燥并煅烧以制备煅烧氧化钛。 在该方法中,硫酸钛在加热下优选在细粒状硅酸的存在下水解,生成偏钛酸,然后将其转化为溶胶。 将所得溶胶过滤,干燥并煅烧。 细粒状硅酸的存在抑制了煅烧时的氧化钛的晶体生长,残留有未生长的锐钛矿型晶体。 因此,获得具有大表面积和改善的机械强度和耐热性的目标煅烧氧化钛。 所得产物适合用作催化剂或直接作为催化剂使用。
    • 20. 发明专利
    • Waste gas treating catalyst
    • 废气处理催化剂
    • JPS5727135A
    • 1982-02-13
    • JP10132280
    • 1980-07-25
    • Mitsubishi Heavy Ind Ltd
    • YOKOYAMA SHIGEOSERA TOSHIKUNIMITSUOKA SHIGEAKIOBAYASHI YOSHIAKI
    • B01D53/94B01J27/02B01J27/053C01B17/79
    • PURPOSE: To obtain a catalyst which can effectively accelerate denitration reaction and oxidation reaction of SO
      2 simultaneously for treating waste gas, by allowing Fe
      2 (SO
      4 )
      3 to be carried on a V
      2 O
      5 -TiO
      2 catalyst.
      CONSTITUTION: This catalyst is composed of 3W10wt% V
      2 O
      5 , 0.5W5% Fe
      2 (SO
      4 )
      3 , and the rest of TiO
      2 . This catalyst is obtained by impregnating and carrying aqueous FeSO
      4 .7H
      2 O solution to a catalyst which is formed by adding V
      2 O
      5 to a TiO
      2 carrier manufactured from titanium hydroxide and by heating and drying the product. The Fe
      2 (SO
      4 )
      3 contained in the above-mentioned amount accelerates SO
      2 → SO
      3 conversion reaction without reducing the denitration reaction so much. In this way, Nox contained in waste gases of boilers can be removed and, at the same time, dust, such as fly ash, etc., can also be removed efficiently. Moreover, when Fe(III) is used from the first time for allowing to contain Fe
      2 (SO
      4 )
      3 , the denitrating capacity is remarkably retarded.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:通过使Fe2(SO4)3载带在V2O5-TiO2催化剂上,获得可以有效加速SO2脱硝反应和氧化反应的催化剂,用于处理废气。 构成:该催化剂由3-10wt%V2O5,0.5-5%Fe2(SO4)3和其余TiO2组成。 该催化剂通过将FeSO 4·7H 2 O水溶液浸渍并携载到通过将V 2 O 5加入到由氢氧化钛制造的TiO 2载体中并通过加热和干燥产物而形成的催化剂而获得。 上述量中所含的Fe 2(SO 4)3加剧了SO 2 SO 3转化反应,而不会使脱硝反应减少。 以这种方式,可以除去锅炉废气中所含的Nox,同时可以有效地除去粉尘,如飞灰等。 此外,当第一次使用Fe(III)以允许含有Fe 2(SO 4)3时,脱硝能力显着延迟。