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    • 4. 发明申请
    • SOOT WATER CLEANING BY MEANS OF CONTINUOUS PRESSURE FILTRATION
    • RUSS净水器连续压滤
    • WO2012076305A2
    • 2012-06-14
    • PCT/EP2011070239
    • 2011-11-16
    • SIEMENS AGMEHLHOSE FRIEDEMANNTAFFELT PETERHANNEMANN FRANKFISCHER NORBERTPUTZ MIRKO
    • MEHLHOSE FRIEDEMANNTAFFELT PETERHANNEMANN FRANKFISCHER NORBERTPUTZ MIRKO
    • B01D29/52B01D35/16C10J3/485C10J3/78C10J3/84C10J2300/169Y02E20/18
    • In a pressure filtration system for cleaning residual quenching water of a gasifying device that gasifies carbon-containing fuels under elevated pressure, the soot water from the quencher is passed to a filter system (1), which has a number of pressure filter chambers operating alternately in filtering mode under gasifying pressure or in cleaning mode. The filtrate from the pressure filter chambers is passed to a quenching water reservoir, from which the quencher is fed with quenching water. This only entails small temperature and pressure losses with respect to the residual quenching water leaving, and only a small additional amount of energy has to be expended to overcome the remaining pressure difference to bring the filtrate that is to be returned back to the gasifying pressure. The invention, in which the residual quenching water is therefore cleaned substantially under gasifying pressure in a pressure filter, avoids flash evaporation of the residual quenching water into the vacuum area, with vapour cooling and a subsequent increase in pressure and reheating. In this way, the electrical energy requirement of the gasifying process itself can be reduced by orders of magnitude and the energy content and associated water content of the untreated gas can be set to the steam contents required for the CO shift reaction without additional amounts of heat being used up. This leads altogether to an improvement in the overall efficiency of IGCC and chemical synthesis processes. In an advantageous way, calcite precipitation is avoided in the soot water system, since no flash evaporation and preheating of the residual quenching water to be returned is required.
    • 在对升高的压力下净化Restquenchwasser一个含碳燃料的压力过滤系统气化的气化装置中,从淬灭剂(1)被提供过滤器系统的烟灰水,具有多个交替地在过滤器中的气化压力下操作,或在Abreinigungsbetrieb压力过滤室操作。 从压力过滤室将滤液供给至从该淬灭剂被馈送有骤冷水Quenchwasservorlagebehälter。 在这里,只有很小的温度和压力损失退出Restquenchwasser而且必须花费一些额外的能量来克服目前的压力差,使由于滤液回气化压力。 本发明,其中,所述R​​estquenchwasser因此基本上在压力过滤器净化气化压力下,避免了闪光灯膨胀Restquenchwassers的与蒸汽冷却和随后的加压和再加热的真空区域。 以这种方式,气化过程所需的电性质可以通过幅度和能量含量的顺序来减少和原料气体的有关水含量被调节到所需的无需额外热量消耗的CO变换反应蒸气内容。 这导致IGCC和化学合成过程的整体效率的全面提高。 有利地,方解石沉淀避免在炭黑水系统由于不需要再循环Restquenchwassers的松弛和预热。
    • 5. 发明申请
    • GAS AND STEAM TURBINE INSTALLATION
    • 燃气和蒸汽透平设备
    • WO0004285A3
    • 2000-03-30
    • PCT/DE9902058
    • 1999-07-02
    • SIEMENS AGSCHIFFERS ULRICHHANNEMANN FRANK
    • SCHIFFERS ULRICHHANNEMANN FRANK
    • F01K23/06F02C3/28
    • F01K23/068Y02E20/16Y02E20/18Y02P80/154
    • The invention relates to a gas and steam turbine installation (1) comprising a heat recovery steam generator (30) which is positioned downstream of the gas turbine (2) on the exhaust gas side and whose heating surfaces are mounted in the water-steam circuit (24) of the steam turbine (20). For the integrated gasification of a fossil fuel (B) a gasification device (132) is positioned upstream of the combustion chamber (6) of the gas turbine (2). Oxygen (O2) can be supplied to the gasification device (132) from an air separation unit (138) which on its input side can be subjected to a partial flow (T) of air compressed in an air compressor (4) assigned to the gas turbine (2). The aim of the invention is to ensure with the above type of gas and steam turbine installation (1) reliable cooling of the exhaust air during all operating conditions with an especially simple construction, independently of the integration concept on which the invention is based. To this end, for cooling the partial flow (T) of compressed air a heat exchanger (162) is positioned on the primary side inside an exhaust air duct (140) which links the air compressor (4) and the air separation unit (138). On the secondary side said heat exchanger is connected to a water-steam drum (164) to form an evaporation circuit (163) for a flow medium (S').
    • 背景技术在燃气和蒸汽涡轮设备(1)具有其加热表面被连接到蒸汽涡轮机(20)的水 - 蒸汽循环(24)的燃气涡轮机中的一个(2)的废气侧的下游热回收蒸汽发生器(30),化石燃料的整体煤气化 燃气涡轮机的气化装置(132)的上游(2)的燃烧室(6)的(B)。 气化装置(132)是从空气分离装置(138),相关联的部分,在输入侧与所述燃气涡轮机(2)的空气压缩机(4)的压缩空气可被作用中的一个的部分流(T)供给的氧(O2)。 在这样的燃气和蒸汽涡轮机(1)的目的是确保泄放空气的可靠的冷却在所有操作条件下特别简单的设计,无论集成的基本概念的。 为了这个目的,根据本发明是冷却压缩空气在空气压缩机(4)与所述空气分离装置(138),其连接在连接在热交换器(162)的初级侧的泄放空气管道(140)的部分流(T),二次侧以形成用于流动介质的蒸发器循环(163) (S“)是连接到水蒸汽鼓(164)。
    • 9. 发明申请
    • CALIBRATION OF DUST LOAD FLOW MEASURING SYSTEMS
    • 粉尘计量系统的标定
    • WO2009037009A3
    • 2009-05-28
    • PCT/EP2008058059
    • 2008-06-25
    • SIEMENS AGTIETZE GUENTERFISCHER NORBERTHANNEMANN FRANK
    • TIETZE GUENTERFISCHER NORBERTHANNEMANN FRANK
    • G01F1/76G01F25/00
    • G01F25/0007G01F1/76G01F25/0046
    • The invention relates to a method for calibrating a dust load flow measuring system, wherein the dust delivery line (5) leading from a metering vessel (1) to the gasification reactor (4) can be connected in the delivery direction downstream of the installed dust load flow measuring device (3) instead of to the gasification reactor with a calibration line (6) leading to the input sluice (2). The input sluice is provided with a weighing unit (WG) such that the weight of the content of the input sluice can be determined. A settable differential pressure (PIC) is controlled between the metering vessel and the input sluice (10). From the set differential pressure and the change of the weight in the input sluice, the dust load flow can be determined in a time interval. The advantages are that necessary functional tests and calibration experiments in dust input systems of gasification units can be carried out with only minor additional effort under on-site delivery conditions and with sufficiently long experiment durations.
    • 它提出了一种方法,用于校准灰尘质量流量测量系统,其特征在于,从一个计量容器(1)到气化反应器(4),导致尘埃传送管道(5)在所安装的尘埃块后面的输送方向流量测量装置(3)代替与所述气化反应器与 到输入闸龙头(2)校准线(6)可连接到设置有称重装置(WG),输入水闸使得输入水闸的含量的质量可以被确定,一个可调节的压力差(PIC)的配料容器和入口闸门之间的受控(10 )是根据设定的压差和粉尘流量时间间隔内入口锁定的质量变化确定的。 优点是必要的功能测试和校准测试气化厂的灰尘进入系统可以用少的额外工作实际生产条件下,用足够长的测试期间进行。
    • 10. 发明申请
    • GAS AND STEAM TURBINE INSTALLATION
    • 燃气和蒸汽透平设备
    • WO0004279A3
    • 2000-03-30
    • PCT/DE9902106
    • 1999-07-08
    • SIEMENS AGSCHIFFERS ULRICHHANNEMANN FRANK
    • SCHIFFERS ULRICHHANNEMANN FRANK
    • F01K23/06F02C3/28F02C6/18
    • F01K23/068F02C3/28F02C6/18Y02E20/16Y02E20/18Y02P80/154Y02T10/16
    • The invention relates to a gas and steam turbine installation (1) comprising a waste heat steam generator (30) mounted downstream from the gas turbine (2) on the flue-gas side. The heating surfaces of the waste heat steam generator are connected to the water-steam circuit (24) of the steam turbine (20). A gasification device (132) for fuel (B) is arranged upstream from the combustion chamber (6) of the gas turbine (3) for integrated gasification of a fossil fuel (B) via a fuel line (130). In order to obtain a highly effective installation, a heat exchanger (159) is mounted on the primary side in the fuel line (130) between the gasification device and a saturator, in addition to a device (146) for mixing nitrogen (N2). Said heat exchanger is also mounted on the secondary side in the fuel line (130) between the saturator (150) and the combustion chamber (6).
    • 背景技术在燃气和蒸汽涡轮设备(1)具有其加热表面被连接到蒸汽涡轮机(20)的水 - 蒸汽循环(24)的燃气涡轮机中的一个(2)的废气侧的下游热回收蒸汽发生器(30),化石燃料的整体煤气化 经由燃料管线(130)中的气化装置(132),用于燃料(B)上游的燃气涡轮机(2)的燃烧室(6)的(B)。 对于本发明中的特别高的效率水平是在用于混合氮气(N 2),换热器(159)之间,次级侧连接在气化装置(132)和除了一个混合装置(146)的饱和器(150)之间的初级侧上的燃料管线(130) 饱和器(150)和所述燃烧室(6)同样在燃料管线(130)连接。