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    • 3. 发明授权
    • Cooling process and system for dry cooling power plants
    • US09927178B1
    • 2018-03-27
    • US15149152
    • 2016-05-08
    • TDA Research, Inc.
    • Girish SrinivasSteven Charles GebhardRobert James CopelandDavid P. Eisenberg
    • F28C1/04F02C6/18F01K9/00
    • F28C1/04F01K9/003F02C6/18F05D2220/31F05D2220/32F05D2260/213
    • A seasonal process that captures stores and uses water in an ambient temperature-dependent manner to improve the efficiency of a natural gas power plant, comprising: (a) providing a natural gas power plant, the natural gas power plant having a flue gas stream, a cooling tower, and a gas turbine; (b) providing a water collection system; (c) providing a water storage facility; wherein the flue gas stream comprises uncondensed water vapor; wherein the water collection system is operably connected to the flue gas stream and the flue gas stream is directed to flow, at least in part, into the water collection system; wherein the water collection system is operably connected to the water storage facility; wherein the water storage facility is operably connected to the cooling tower and the water storage facility is operably connected to the gas turbine; wherein the process comprises the following steps of condensing flue gas water or using water that has been condensed from the flue gas stream based on outdoor ambient dry bulb temperature: (I) Only condensing water from the flue gas stream to produce a condensed water stream if outdoor ambient dry bulb temperature is less than 85° F.; (II) Only using condensed water to spray cool the cooling tower if outdoor ambient dry bulb temperature is at least 85° F.; (III) Only using condensed water to fog cool the gas turbine if outdoor ambient dry bulb temperature is at least 55° F.; wherein condensed water that is not immediately used to cool the cooling tower or to fog cool the gas turbine is stored in the water storage facility; and wherein the process uses a total amount of water on an annual basis to cool the cooling tower and to fog cool the gas turbine that does not exceed the annual amount of water condensed from the flue gas stream. Optionally, the process has a cooling tower that is a dry cooling tower and condensed water is used to spray cool the dry cooling tower, or the cooling tower is a wet cooling tower, or the cooling tower is a hybrid wet-dry cooling tower. The process may further comprise a water collection system having a three stage desiccant cycle and a calcium chloride desiccant that recovers at least about 60 wt % of the water from the flue gas, operates at or above ambient pressure or comprises plastic piping or plastic vessels. Or the process may further comprise using a water collection system having at least one direct contact condensing column that recovers at least about 60 wt % of the water from the flue gas, operates at or above ambient pressure or comprises plastic piping or plastic vessels. Or the process may further comprise using a water collection system having at least one direct contact condenser and a rotating wheel heat exchanger that recovers at least about 60 wt % of the water from the flue gas, operates at or above ambient pressure, or further comprises plastic piping or plastic vessels. The coefficient of performance for the cooling process is optionally at least 2.0.
    • 5. 发明授权
    • Method of encapsulating waste
    • 封装废物的方法
    • US09044796B1
    • 2015-06-02
    • US14206811
    • 2014-03-12
    • TDA Research, Inc.
    • Christopher Brian France
    • B09B1/00B09B3/00A62D101/02
    • B09B3/0033A62D2101/02
    • A method of encapsulating and safely transporting hazardous waste is disclosed. The method comprises the steps of: first, providing a waste object at a first location; second, covering the waste object with a closed cell polymer foam; third, allowing a sufficient time for the closed cell polymer foam to cure; and fourth, transporting the covered waste object to a second location. In another embodiment the method comprises the steps of: first, providing a waste object at a first location; second, treating the waste object to decontaminate or neutralize the hazardous waste; third, covering the waste object with a closed cell polymer foam; fourth, allowing a sufficient time for the closed cell polymer foam to cure; and fifth, transporting the covered waste object to a second location.
    • 公开了一种封装和安全运输危险废物的方法。 该方法包括以下步骤:首先在第一位置提供废物; 第二,用闭孔聚合物泡沫覆盖废物; 第三,允许足够的时间使闭孔聚合物泡沫固化; 第四,将被覆盖废物运送到第二位置。 在另一个实施例中,该方法包括以下步骤:首先,在第一位置处提供废物; 二是处理废物对废物进行净化或中和; 第三,用闭孔聚合物泡沫覆盖废物; 第四,允许足够的时间使闭孔聚合物泡沫固化; 第五,将被覆盖废物运送到第二位置。
    • 6. 发明申请
    • MERCURY REMOVAL SORBENTS
    • MERCURY移除SORBENTS
    • US20140274667A1
    • 2014-09-18
    • US13834266
    • 2013-03-15
    • TDA Research, Inc.
    • Gokhan Alptekin
    • B01J27/138B01J27/06
    • B01J37/04B01J20/0222B01J20/0237B01J20/041B01J20/046B01J20/08B01J20/103B01J20/12B01J20/28004B01J20/28057B01J27/08B01J27/10B01J27/128B01J27/132B01J35/002B01J35/1014B01J35/1019B01J37/22B01J37/24
    • Sorbents and methods of using them for removing mercury from flue gases over a wide range of temperatures are disclosed. Sorbent materials of this invention comprise oxy- or hydroxyl-halogen (chlorides and bromides) of manganese, copper and calcium as the active phase for Hg0 oxidation, and are dispersed on a high surface porous supports. In addition to the powder activated carbons (PACs), this support material can be comprised of commercial ceramic supports such as silica (SiO2), alumina (Al2O3), zeolites and clays. The support material may also comprise of oxides of various metals such as iron, manganese, and calcium. The non-carbon sorbents of the invention can be easily injected into the flue gas and recovered in the Particulate Control Device (PCD) along with the fly ash without altering the properties of the by-product fly ash enabling its use as a cement additive. Sorbent materials of this invention effectively remove both elemental and oxidized forms of mercury from flue gases and can be used at elevated temperatures. The sorbent combines an oxidation catalyst and a sorbent in the same particle to both oxidize the mercury and then immobilize it.
    • 公开了一种吸附剂和使用它们在宽范围的温度下从烟道气中去除汞的方法。 本发明的吸附剂材料包含锰,铜和钙的氧化或羟基 - 卤素(氯化物和溴化物)作为HgO氧化的活性相,并且分散在高表面多孔载体上。 除了粉末活性炭(PAC)之外,该载体材料可以由市售的陶瓷载体如二氧化硅(SiO 2),氧化铝(Al 2 O 3),沸石和粘土组成。 载体材料还可以包含各种金属如铁,锰和钙的氧化物。 本发明的非碳吸附剂可以容易地注入烟气中并与粉煤灰一起回收到颗粒控制装置(PCD)中,而不改变副产物飞灰的性质,使其能够用作水泥添加剂。 本发明的吸附剂材料有效地从烟道气中除去元素和氧化形式的汞,并且可以在高温下使用。 吸附剂将氧化催化剂和吸附剂结合在相同的颗粒中,以使氧化汞,然后固定。
    • 7. 发明授权
    • Method of making alkyl esters
    • 制备烷基酯的方法
    • US07795460B2
    • 2010-09-14
    • US11381924
    • 2006-05-05
    • Brian Elliott
    • Brian Elliott
    • C11B1/00
    • C07C67/08C11C3/003Y02E50/13C07C69/52C07C69/24
    • Methods of making alkyl esters are described herein. The methods are capable of using raw, unprocessed, low-cost feedstocks and waste grease. Generally, the method involves converting a glyceride source to a fatty acid composition and esterifying the fatty acid composition to make alkyl esters. In an embodiment, a method of making alkyl esters comprises providing a glyceride source. The method further comprises converting the glyceride source to a fatty acid composition comprising free fatty acids and less than about 1% glyceride by mass. Moreover, the method comprises esterifying the fatty acid composition in the presence of a solid acid catalyst at a temperature ranging firm about 70° C. to about 120° C. to produce alkyl esters, such that at least 85% of the free fatty acids are converted to alkyl esters. The method also incorporates the use of packed bed reactors for glyceride conversion and/or fatty acid esterification to make alkyl esters.
    • 本文描述了制备烷基酯的方法。 这些方法能够使用原始的,未加工的,低成本的原料和废油脂。 通常,该方法包括将甘油酯源转化为脂肪酸组合物并酯化脂肪酸组合物以制备烷基酯。 在一个实施方案中,制备烷基酯的方法包括提供甘油酯源。 该方法还包括将甘油酯源转化成包含游离脂肪酸和小于约1%甘油酯的脂肪酸组合物。 此外,该方法包括在固体酸催化剂存在下,在约70℃至约120℃的温度范围内酯化脂肪酸组合物以产生烷基酯,使得至少85%的游离脂肪酸 被转化为烷基酯。 该方法还包括使用填充床反应器进行甘油酯转化和/或脂肪酸酯化以制备烷基酯。
    • 10. 发明授权
    • Poly(heteroaromatic) block copolymers with electrical conductivity
    • 具有导电性的聚(杂芳族)嵌段共聚物
    • US07279534B2
    • 2007-10-09
    • US10234968
    • 2002-09-03
    • Silvia DeVito LuebbenBrian ElliottCarolina Wilson
    • Silvia DeVito LuebbenBrian ElliottCarolina Wilson
    • C08F26/06C08F234/04
    • C08G61/126C08F293/00C08F293/005C08F295/00C08F297/00C08F297/04C08G61/123C08G61/124C08L53/00C08L53/02C08L2666/24
    • The present invention provides block copolymers containing at least one block of a poly(heteroaromatic) polymer and at least two blocks of a non-conjugated polymer. The chemically different blocks of the copolymer are covalently bonded to each other in an alternating fashion through an appropriate linkage group. The poly(heteroaromatic) block may exist in its neutral or oxidized form, and when in the oxidized form, it associates with organic or inorganic counter-anions to balance the charge. The poly(heteroaromatic) polymer is an intrinsically conducting polymer (ICP), and when in the oxidized form it is electrically conducting. When the ICP block or blocks of the block copolymer are in the doped form, the block copolymer is electrically conducting. Preferably the conducting block copolymers have conductivities in the range 10−6-103 S/cm. Block copolymers of this invention are soluble or dispersible in water, one or more organic solvents, or in a mixture thereof at a level of at least about 0.1 g/liter.
    • 本发明提供含有至少一个聚(杂芳族)聚合物嵌段和至少两个非共轭聚合物嵌段的嵌段共聚物。 共聚物的化学上不同的嵌段通过适当的连接基团以交替的方式彼此共价键合。 聚(杂芳族)嵌段可以其中性或氧化形式存在,并且当以氧化形式时,其与有机或无机反阴离子相结合以平衡电荷。 聚(杂芳族)聚合物是本征导电聚合物(ICP),当处于氧化形式时,它是导电的。 当嵌段共聚物的ICP嵌段或嵌段是掺杂形式时,嵌段共聚物是导电的。 优选地,导电嵌段共聚物的导电率在10 -6 -3 3 / S / cm的范围内。 本发明的嵌段共聚物以至少约0.1g /升的水平可溶或分散于水,一种或多种有机溶剂或其混合物中。