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. 发明授权
    • Hydroxylammonium nitrate free of ammonium nitrate
    • 硝酸铵不含硝酸铵
    • US5651951A
    • 1997-07-29
    • US445480
    • 1995-05-22
    • David W. CawlfieldRonald L. DotsonHarry J. LoftisSanders H. MooreRobert T. BrookerJay S. Stirrat
    • David W. CawlfieldRonald L. DotsonHarry J. LoftisSanders H. MooreRobert T. BrookerJay S. Stirrat
    • C01B21/14C01B21/20
    • C01B21/1454
    • The present invention relates to a multi-step process for producing HAN that is free of ammonium nitrate. The process comprises the steps of: (a) stripping ammonia from an ammonia-containing, aqueous hydroxylamine solution having a hydroxylamine concentration of at least 10% by weight based upon the weight of the hydroxylamine solution, by contacting the ammonia-containing hydroxylamine solution with a stripping agent selected from the group consisting of inert gases and steam to provide an ammonia-free, aqueous hydroxylamine solution, and (b) reacting the ammonia-free, aqueous hydroxylamine solution with aqueous nitric acid having an acid concentration of at least about 0.1%, preferably at least about 20%, based upon the weight of the aqueous nitric acid, to produce ammonium nitrate-free HAN. In another process embodiment of the invention, the above-described ammonia stripping step is not required, and the hydroxylamine concentration is at least about 0.5%, based upon the weight of the reaction mixture employed. Also disclosed is the ammonium nitrate-free HAN product produced by the process of this invention.
    • 本发明涉及一种不含硝酸铵的生产HAN的多步法。 该方法包括以下步骤:(a)通过使含氨的羟胺溶液与含羟胺的羟胺溶液接触,从基于羟胺溶液重量的羟胺浓度至少为10重量%的含氨基羟胺溶液中除去氨 选自惰性气体和蒸汽的汽提剂,以提供无氨的羟胺水溶液,和(b)使无氨水羟胺溶液与酸浓度为至少约0.1的硝酸水溶液反应 %,优选至少约20%,基于硝酸水溶液的重量,以产生不含硝酸铵的HAN。 在本发明的另一方法实施方案中,不需要上述氨汽提步骤,并且基于所用反应混合物的重量,羟胺浓度为至少约0.5%。 还公开了通过本发明的方法生产的不含硝酸铵的HAN产物。
    • 3. 发明授权
    • Hydroxylammonium nitrate free of ammonium nitrate
    • 硝酸铵不含硝酸铵
    • US5510097A
    • 1996-04-23
    • US245928
    • 1994-05-19
    • David W. CawlfieldRonald L. DotsonHarry J. LoftisSanders H. MooreRobert T. BrookerJay S. Stirrat
    • David W. CawlfieldRonald L. DotsonHarry J. LoftisSanders H. MooreRobert T. BrookerJay S. Stirrat
    • C01B21/14C01B21/20
    • C01B21/1454
    • The present invention relates to a multi-step process for producing HAN that is free of ammonium nitrate. The process comprises the steps of: (a) stripping ammonia from an ammonia-containing, aqueous hydroxylamine solution having a hydroxylamine concentration of at least 10% by weight based upon the weight of the hydroxylamine solution, by contacting the ammonia-containing hydroxylamine solution with a stripping agent selected from the group consisting of inert gases and steam to provide an ammonia-free, aqueous hydroxylamine solution, and (b) reacting the ammonia-free, aqueous hydroxylamine solution with aqueous nitric acid having an acid concentration of at least about 0.1%, preferably at least about 20%, based upon the weight of the aqueous nitric acid, to produce ammonium nitrate-free HAN. In another process embodiment of the invention, the above-described ammonia stripping step is not required, and the hydroxylamine concentration is at least about 0.5%, based upon the weight of the reaction mixture employed. Also disclosed is the ammonium nitrate-free HAN product produced by the process of this invention.
    • 本发明涉及一种不含硝酸铵的生产HAN的多步法。 该方法包括以下步骤:(a)通过使含氨的羟胺溶液与含羟胺的羟胺溶液接触,从基于羟胺溶液重量的羟胺浓度至少为10重量%的含氨基羟胺溶液中除去氨 选自惰性气体和蒸汽的汽提剂,以提供无氨的羟胺水溶液,和(b)使无氨水羟胺溶液与酸浓度为至少约0.1的硝酸水溶液反应 %,优选至少约20%,基于硝酸水溶液的重量,以产生不含硝酸铵的HAN。 在本发明的另一方法实施方案中,不需要上述氨汽提步骤,并且基于所用反应混合物的重量,羟胺浓度为至少约0.5%。 还公开了通过本发明的方法生产的不含硝酸铵的HAN产物。
    • 5. 发明授权
    • Integrated process of using chloric acid to separate zinc oxide and
manganese oxide
    • 使用氯酸分离氧化锌和氧化锰的综合过程
    • US5411643A
    • 1995-05-02
    • US228631
    • 1994-04-18
    • David W. CawlfieldLeslie R. Ward
    • David W. CawlfieldLeslie R. Ward
    • C01G9/02C01G45/02C25C1/16H01M6/52
    • C22B19/22C01G45/02C01G9/02H01M6/52C01P2002/80C01P2004/80Y02P10/234Y02P20/125Y02W30/84
    • A process for producing manganese dioxide and zinc metal comprising the steps of:(1) reacting a mixture of zinc oxide and manganese oxide with an aqueous chloric acid solution wherein the chloric acid is in molar excess of the manganese oxide in a reaction zone to form a reaction mixture in the zone comprising chlorine gas, a solid phase containing manganese dioxide, and a liquid phase containing zinc oxide, chloric acid and water; the concentration of chloric acid in the liquid phase is greater than about 1% by weight of the liquid phase upon leaving the reaction zone;(2) separating the chlorine gas from the solid phase and the liquid phase;(3) separating the solid phase containing manganese dioxide from the liquid phase containing zinc ions, chlorate ions, chloric acid, and water thereby forming a separated solid phase and a separated liquid phase;(4) subjecting the separated liquid phase to electrolysis in an electrochemical cell, thereby producing zinc metal at the cathode and oxygen at the anode;(5) removing water from said separated liquid phase to concentrate the chloric acid in the separated liquid phase thereby forming a separated solid phase and a separated liquid phase;(6) returning the separated and concentrated liquid phase back to the reaction zone; and(7) recovering the zinc metal from the electrolytic cell.
    • 一种生产二氧化锰和锌金属的方法,包括以下步骤:(1)使氧化锌和氧化锰的混合物与氯酸水溶液反应,其中氯酸在反应区中与氧化锰摩尔过量以形成 在包含氯气的区域中的反应混合物,含有二氧化锰的固相和含有氧化锌,氯酸和水的液相; 在离开反应区时,液相中氯酸的浓度大于液相重量的约1%; (2)从固相和液相中分离出氯气; (3)从含有锌离子,氯酸根离子,氯酸和水的液相中分离含有二氧化锰的固相,由此形成分离的固相和分离的液相; (4)在电化学电池中对分离的液相进行电解,从而在阴极处产生锌金属和在阳极处产生氧; (5)从分离的液相中除去水分,将氯酸浓缩在分离的液相中,从而形成分离的固相和分离的液相; (6)使分离浓缩的液相返回到反应区; 和(7)从电解槽回收锌金属。
    • 6. 发明授权
    • Process for producing solid manganese dioxide
    • 生产固体二氧化锰的方法
    • US5401477A
    • 1995-03-28
    • US180838
    • 1994-01-12
    • David W. CawlfieldLeslie R. Ward
    • David W. CawlfieldLeslie R. Ward
    • B01D11/02B01D11/04C01G9/02C01G45/02H01M6/52
    • C01G9/02C01G45/02C22B19/22H01M6/52C01P2002/80C01P2004/80Y02P10/234Y02W30/84
    • A process for producing manganese dioxide comprising the steps of:(1) reacting manganese oxide with a molar excess of an aqueous chloric acid solution in a reaction zone to form a reaction mixture in said zone comprising chlorine gas, a solid phase containing manganese dioxide, and a liquid phase containing chloric acid and water; the concentration of chloric acid in said liquid phase is greater than about 5% by weight of said liquid phase upon leaving the reaction zone;(2) separating said chlorine gas from said solid phase and said liquid phase;(3) separating said solid phase containing manganese dioxide from liquid phase containing chloric acid and water;(4) removing water from said separated liquid phase to concentrate said chloric acid in said separated liquid phase; and(5) returning said separated and concentrated liquid phase back to said reaction zone for further reaction with manganese oxide.
    • 一种制备二氧化锰的方法,包括以下步骤:(1)在反应区中使氧化锰与摩尔过量的氯酸水溶液反应,以在所述的包含氯气的区域中形成反应混合物,含有二氧化锰的固相, 和含有氯酸和水的液相; 所述液相中氯酸的浓度在离开反应区时大于所述液相的约5重量%; (2)从所述固相和所述液相中分离出所述氯气; (3)从包含氯酸和水的液相中分离含有二氧化锰的固相; (4)从所述分离的液相中除去水以将所述氯酸浓缩在所述分离的液相中; 和(5)将所述分离和浓缩的液相返回到所述反应区,以进一步与氧化锰反应。