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    • 2. 发明申请
    • SAFE STORAGE AND TRANSPORTATION OF SULFUR DIOXIDE
    • 硫化二氧化硫的安全储存和运输
    • WO98042618A1
    • 1998-10-01
    • PCT/CA1998/000237
    • 1998-03-16
    • B01D53/14C01B17/48C01B17/56C01B17/60B01D53/50
    • C01B17/48B01D53/1481C01B17/56C01B17/60Y02A50/2349
    • The invention relates to a method of confining sulfur dioxide for storage or transportation under safe conditions. The method of the invention comprises the steps of (a) contacting a sulfur dioxide-containing gas stream with an absorbing medium comprising water and a water-soluble amine absorbent having at least one amine group with a pKa value greater than about 7 and at least one other amine group with a pKa value less than about 6.5 so that the at least one amine group with a pKa value greater than about 7 irreversibly absorbs sulfur dioxide in salt form rendering the amine absorbent non-volatile and the at least one other amine group with a pKa value less than about 6.5 reversibly absorbs sulfur dioxide, to thereby saturate the absorbing medium with sulfur dioxide against a partial pressure of sulfur dioxide of no more than about 1 atmosphere at 25 DEG C; and (b) charging the absorbing medium saturated with sulfur dioxide obtained in step (a) into a container for storage or transportation.
    • 本发明涉及一种将二氧化硫限制在安全条件下储存或运输的方法。 本发明的方法包括以下步骤:(a)使含二氧化硫的气流与包含水的吸收介质和具有pKa值大于约7的至少一个胺基的水溶性胺吸收剂接触,并且至少 pKa值小于约6.5的另一个胺基,使得pKa值大于约7的至少一个胺基不可逆地吸收盐形式的二氧化硫,使得胺吸收剂不挥发和至少一种其它胺基 pKa值小于约6.5可逆地吸收二氧化硫,从而使二氧化硫的吸收介质在25℃下对二氧化硫分压不超过约1个大气饱和; 和(b)将步骤(a)中获得的二氧化硫饱和的吸收介质装入用于储存或运输的容器中。
    • 7. 发明申请
    • SELECTIVE REMOVAL AND RECOVERY OF SULFUR DIOXIDE FROM EFFLUENT GASES USING ORGANIC PHOSPHOROUS SOLVENTS
    • 使用有机磷溶液从有利气体中选择性去除和回收二氧化硫
    • WO1998009713A1
    • 1998-03-12
    • PCT/US1997014283
    • 1997-08-12
    • MONSANTO COMPANY
    • MONSANTO COMPANYBURMASTER, Brian, M.McALISTER, Donald, R.
    • B01D53/50
    • B01D53/1481C01B17/60C01B17/76Y02A50/2348Y02A50/2349
    • A process for the selective removal and recovery of sulfur dioxide from effluent gases is disclosed. The sulfur dioxide is recovered in a sulfur dioxide absorption/desorption cycle which utilizes a liquid solvent to selectively absorb sulfur dioxide from the effluent gas. The liquid solvent comprises an organic phosphorous compound selected from phosphate triesters, phosphonate diesters, phosphinate monoesters and mixtures thereof. Preferably, the liquid solvent comprises phosphonate diesters of formula (I) wherein R , R and R are independently aryl or C1 to C8 alkyl. The organic phosphonate diesters are substantially water immiscible, the solubility of water in the organic phosphonate diester being less than about 10 weight percent at 25 DEG C, and have a vapor pressure less than about 1 Pa at 50 DEG C. In accordance with a preferred embodiment, the liquid solvent comprises dibutyl butyl phosphonate. The absorbed sulfur dioxide is subsequently stripped to regenerate the organic phosphorous solvent and produce a gas enriched in sulfur dioxide content. The sulfur dioxide-enriched gas may be used as part of the feed gas to a contact sulfuric acid plant or a Claus plant for the preparation of elemental sulfur or be cooled to condense sulfur dioxide in the form of a liquid product. The present invention is particularly useful in producing a sulfur dioxide-enriched gas from gases relatively weak in sulfur dioxide content.
    • 公开了从废气中选择性地除去和回收二氧化硫的方法。 在二氧化硫吸收/解吸循环中回收二氧化硫,其利用液体溶剂从废气中选择性地吸收二氧化硫。 液体溶剂包括选自磷酸三酯,膦酸二酯,次膦酸酯单酯及其混合物的有机磷化合物。 优选地,液体溶剂包括式(I)的膦酸二酯,其中R 1,R 2和R 3独立地为芳基或C 1至C 8烷基。 有机膦酸酯二酯基本上是水不混溶的,水在有机膦酸酯二酯中的溶解度在25℃下小于约10重量%,并且在50℃下具有小于约1Pa的蒸气压。根据优选的 液体溶剂包括丁基丁基膦酸二丁酯。 随后汽提吸收的二氧化硫以再生有机磷溶剂并产生富含二氧化硫含量的气体。 富含二氧化硫的气体可以作为进料气体的一部分用于接触硫酸设备或用于制备元素硫的克劳斯设备,或被冷却以冷凝液体产物形式的二氧化硫。 本发明特别可用于从二氧化硫含量相对较弱的气体制备富含二氧化硫的气体。
    • 8. 发明申请
    • METHOD AND APPARATUS FOR DESULFURIZATION OF A GAS
    • 用于气体脱硫的方法和装置
    • WO1993014026A1
    • 1993-07-22
    • PCT/US1993000319
    • 1993-01-13
    • HASEBE, NobuyasuHASEBE, Nobukatsu
    • C01B17/00
    • C01B17/60B01D53/501B01D53/73
    • An alkaline earth bicarbonate is solubilized in water and contacted by a flue gas. The solubilized alkaline earth bicarbonate reacts with the SO2 in the flue gas to form an alkaline earth sulfite which readily precipitates from the water solution and is efficiently separated therefrom. In accordance with the invention, the slurry exiting the desulfurization step is subjected to a heating step which causes soluble alkaline earth bisulfite formed during the desulfurization step to convert to the insoluble sulfite. The solids are separated from the aqueous phase and subjected to thermal degradation to recover the alkaline earth oxide and SO2. The alkaline earth oxide can be recirculated and reused in the desulfurization process while the SO2, which has practical uses as a precursor in various chemical processes and therefore is of commercial value, is liquified. Thermal degradation of the solids from the desulfurization step is carried out in apparatus which includes a preheater zone, an ignition and heating chamber and a degradation zone. The thermal degradation is carried out in the presence of heated pellets which are themselves inert to the degradation reaction. Preferably, the pellets are heated in the ignition and heating chamber prior to contact with the solids from the desulfurization step.
    • 将碱土碳酸氢盐溶解在水中并与烟气接触。 溶解的碱土金属碳酸氢盐与烟道气中的SO 2反应,形成碱土金属亚硫酸盐,其易于从水溶液中沉淀并与其有效分离。 根据本发明,离开脱硫步骤的浆料经受加热步骤,其导致在脱硫步骤期间形成的可溶性碱土金属亚硫酸氢盐转化为不溶性亚硫酸盐。 将固体与水相分离并进行热降解以回收碱土金属氧化物和SO 2。 碱土金属氧化物可以在脱硫过程中再循环和重复使用,而具有实用用途的SO2在各种化学过程中作为前体,因此具有商业价值,被液化。 来自脱硫步骤的固体的热降解在包括预热器区域,点火和加热室以及降解区域的设备中进行。 热降解在本身对降解反应惰性的加热颗粒存在下进行。 优选地,在与脱硫步骤的固体接触之前,在点火和加热室中加热颗粒。