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
    • 54. 发明申请
    • OPTIMISING THE UTILISATION OF RENEWABLE ENERGY FROM BIOMASS RESOURCES IN THE PALM OIL INDUSTRY
    • 优化棕榈油生物质资源可再生能源的利用
    • WO2012108756A1
    • 2012-08-16
    • PCT/MY2012/000021
    • 2012-02-03
    • PALANISAMY, Krishna Moorthy
    • PALANISAMY, Krishna Moorthy
    • C11B1/16F01D17/14
    • C11B1/16F01K17/00Y02E20/14
    • The invention provides an arrangement for operating energy system of a crude palm oil extraction plant and method thereof. The arrangement for operating energy system of a crude palm oil extraction plant achieves the target of higher efficiency of energy utilisation by using heat source at a low temperature featuring in the design operation point of the energy system providing thermal energy to the palm oil extraction process. Accordingly, the present invention provides an arrangement for operating energy system of a crude palm oil extraction plant which includes at least one heat source and at least one means to communicate heat from the at least one heat source to a unit process requiring heat energy wherein the energy system is designed and configured to operate at a design operation point for the temperature of the at least one heat source and wherein the at least one heat source temperature is between 115 °C and 141 °C. Preferably, the temperature of the at least one heat source is between 115 °C and 138 °C and the temperature of the at least one heat source is between 115 °C and 130 °C is more preferred. Most preferred is where the temperature of the at least one heat source is between greater than 100 °C and less than 115 °C.
    • 本发明提供了一种用于操作粗棕榈油提取装置的能量系统的装置及其方法。 原棕油提炼厂的经营能源体系安排,通过在提供热能的能源系统设计作业点的低温下使用热源,实现了提高能源利用效率的目标。 因此,本发明提供了一种用于操作粗棕榈油提取设备的能量系统的装置,其包括至少一个热源和至少一个将来自至少一个热源的热量传递到需要热能的单元过程的装置,其中, 能量系统被设计和配置成在至少一个热源的温度的设计操作点处操作,并且其中所述至少一个热源温度在115℃和141℃之间。 优选地,所述至少一个热源的温度在115℃至138℃之间,并且所述至少一个热源的温度在115℃和130℃之间是更优选的。 最优选的是至少一个热源的温度在大于100℃且小于115℃之间。
    • 56. 发明申请
    • 蒸気タービンサイクル
    • 蒸汽涡轮循环
    • WO2007083478A1
    • 2007-07-26
    • PCT/JP2006/325524
    • 2006-12-21
    • 株式会社 東芝後藤 功一沖田 信雄
    • 後藤 功一沖田 信雄
    • F01K7/40F01K7/34F01K7/38
    • F01K7/40F01K7/22F01K7/38F01K17/00
    • A steam turbine cycle which comprises a high pressure turbine (1), a reheat turbine (24), a boiler (4), a heater (6) for heating supply water to the boiler (4) with extraction steam from the turbines (1, 24), a water supply pump (12), and a condenser (10), and which is a single-stage reheat cycle where the working fluid is water and Rankine cycle as a regenerative cycle. Steam temperature at the outlet of the boiler (4) is 590°C or above. The cycle is constituted such that the temperature rise ratio between supply water temperature rise at a first supply water heater (7) corresponding to extraction steam (high pressure turbine exhaust gas extraction steam) (22) from exhaust gas of the high pressure turbine (1) and an average of supply water temperature rises at a second supply water heater (8) where the pressure of supply water is lower than that of first supply water heater (7) falls within a range of 1.9-3.5.
    • 一种蒸汽轮机循环,其包括高压涡轮机(1),再热涡轮机(24),锅炉(4),用于利用来自涡轮机(1)的提取蒸汽向锅炉(4)供应水的加热器 ,24),供水泵(12)和冷凝器(10),其是工作流体是水和朗肯循环作为再生循环的单级再热循环。 锅炉(4)出口的蒸汽温度为590℃以上。 该循环构成为使得从与高压汽轮机(1)的废气对应的抽取蒸汽(高压汽轮机废气抽取蒸汽)22的第一供水热水器7的供水温度升高之间的升温比 ),供给水的供给水低于第一供水热水器(7)的供给水的第二供水热水器(8)的平均供水温度上升,在1.9-3.5的范围内。
    • 57. 发明专利
    • System and method for recovering carbon dioxide
    • 回收二氧化碳的系统和方法
    • JP2012217903A
    • 2012-11-12
    • JP2011084929
    • 2011-04-06
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • IIJIMA MASAKI
    • B01D53/62B01D53/14C01B32/50F01K17/02
    • F01K7/22B01D53/1412B01D53/1425B01D53/1475B01D2252/204B01D2257/504B01D2258/0283F01K7/025F01K13/00F01K17/00F01K17/04F01K17/06Y02A50/2342Y02C10/04Y02C10/06Y02C10/08Y02E20/16Y02E20/185Y02E20/326
    • PROBLEM TO BE SOLVED: To provide a system and a method for recovering carbon dioxide by which reproduction of carbon dioxide absorption liquid can be surely performed without applying load onto boiler facilities.SOLUTION: The system for recovering carbon dioxide is provided with: a high pressure turbine 11, a medium pressure turbine 12, and a low pressure turbine 13; a main boiler 15 for producing steam 14 for driving the turbines; a carbon dioxide recovering apparatus 24 which comprises a carbon dioxide absorption tower 21 for absorbing and removing carbon dioxide in flue gas (exhaust gas) G discharged from the main boiler 15 by the carbon dioxide absorption liquid, and an absorbent reproducing tower 23 for reproducing the carbon dioxide absorbent, in which carbon dioxide is absorbed, by a reproduction superheater 22 to obtain reproduced carbon dioxide absorbent; an auxiliary boiler 30 for producing saturated steam 31 to be supplied to the reproduction superheater 22 of the absorbent reproducing tower 23; and a steam turbine 32 driven by the steam from the auxiliary boiler 30.
    • 要解决的问题:提供一种用于回收二氧化碳的系统和方法,其中可以可靠地执行二氧化碳吸收液体的再生,而不对锅炉设施施加负荷。 解决方案:用于回收二氧化碳的系统设置有:高压涡轮机11,中压涡轮机12和低压涡轮机13; 用于产生用于驱动涡轮机的蒸汽14的主锅炉15; 二氧化碳回收装置24,其包括二氧化碳吸收塔21,其用于吸收和除去由二氧化碳吸收液体从主锅炉15排出的烟道气(废气)G中的二氧化碳;以及吸收再生塔23, 通过再生过热器22吸收二氧化碳的二氧化碳吸收剂,以获得再生的二氧化碳吸收剂; 用于生产饱和蒸汽31的辅助锅炉30,供应给吸收再生塔23的再生过热器22; 以及由来自辅助锅炉30的蒸汽驱动的蒸汽轮机32.(C)2013,JPO&INPIT
    • 59. 发明授权
    • Mixing assembly and method for combining at least two working fluids
    • 混合组合和组合至少两种工作流体的方法
    • US09303533B2
    • 2016-04-05
    • US14138903
    • 2013-12-23
    • HARRIS CORPORATION
    • William R. Palmer
    • F01K25/06F01K7/34F01K19/02F01K17/00F01K7/02F01K7/16F01K21/04F01K25/08
    • F01K19/02F01K7/02F01K7/16F01K17/00F01K21/04F01K25/06F01K25/08
    • A method for producing work from heat including mixing a first working fluid F1 vapor with a second working fluid F2 vapor to form a third working fluid F3; atomizing and/or vaporizing a liquid into the third working fluid F3 to define a saturated working fluid; and expanding the saturated working fluid to perform useful work. A high pressure F1(2) portion of the first working fluid F1 may be expanded prior to the mixing step while the F2 vapor is compressed prior to the mixing step. The steps of compressing the F2 vapor and expanding the high pressure F1(2) portion of the first working fluid F1 may be carried out by an integral compressor and expander assembly (204/209). The integral compressor and expander assembly (204/209) may be positioned within a combined mixer assembly (300) with an internal mixing chamber (206) and outlets (375, 351) of both the compressor (204) and expander (209) are directed toward the mixing chamber 206.
    • 一种用于从热量产生工件的方法,包括将第一工作流体F1蒸气与第二工作流体F2蒸气混合以形成第三工作流体F3; 将液体雾化和/或蒸发到第三工作流体F3中以限定饱和工作流体; 并扩大饱和工作液进行有用的工作。 第一工作流体F1的高压F1(2)部分可以在混合步骤之前膨胀,同时在混合步骤之前压缩F2蒸气。 压缩F2蒸气并膨胀第一工作流体F1的高压F1(2)部分的步骤可以通过一体的压缩机和膨胀机组件(204/209)来实现。 整体式压缩机和膨胀器组件(204/209)可以位于组合式混合器组件(300)内,其中压缩机(204)和膨胀机(209)的内部混合室(206)和出口(375,351)均为 指向混合室206。