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    • 3. 发明授权
    • Stuffing box sealing arrangement
    • 填料箱密封布置
    • US4765631A
    • 1988-08-23
    • US829698
    • 1986-02-13
    • Klaus KohnenAdolf LinkeHans Niermann
    • Klaus KohnenAdolf LinkeHans Niermann
    • F16J15/24F16J15/16F16J15/18F16J15/40
    • F16J15/183F16J15/162
    • A stuffing box sealing arrangement for sealing a rotary shaft which extends into a pressure space includes two separate consecutive pressure chambers arranged at axially spaced locations along the shaft and an intervening space sealed with respect to the exterior of the arrangement and the pressure space and arranged between the pressure chambers. A plurality of stuffing sealing rings is accommodated in each of the pressure chambers and two glands are provided each being arranged around the shaft at one of the locations in registry with the respective associated plurality of stuffing sealing rings. Each of the glands is independently pressed against the respective associated plurality of stuffing sealing rings, and lubrication water is supplied into the intervening space to continuously lubricate both pluralities of stuffing sealing rings.
    • 用于密封延伸到压力空间中的旋转轴的填料函密封装置包括沿着轴的轴向间隔开的位置布置的两个单独的连续的压力室和相对于该装置的外部和压力空间密封的中间空间,并且布置在 压力室。 多个填充密封环被容纳在每个压力室中,并且两个密封件被设置成各自围绕轴设置在与相应的相关联的多个填充密封环对准的位置之一处。 每个密封件独立地压靠在相应的多个填充密封环上,并且润滑水被供应到中间空间中以连续润滑两个填充密封环。
    • 5. 发明授权
    • Method and arrangement for gasifying finely divided fluidized solid
combustible material
    • 气化精细分散的流化固体可燃材料的方法和装置
    • US4017269A
    • 1977-04-12
    • US579816
    • 1975-05-22
    • Karl-Heinz DutzAdolf Linke
    • Karl-Heinz DutzAdolf Linke
    • C10J3/30G05D16/20C10J3/50
    • G05D16/2046C10J3/30C10J3/506C10J3/723C10J3/78C10J2200/154C10J2300/093C10J2300/0956C10J2300/0959Y10S48/04
    • The arrangement includes a source of finely divided solid combustible material fluidized in an inert gas, and also a source of combustion-supporting gas, such as oxygen, air, or oxygen-enriched air. A gasifier is provided for gasifying finely divided solid combustible material by reacting the same with combustion-supporting gas, and the gasifier has one or more inlets. A first conduit connects the source of combustible material to an inlet of the gasifier. A second conduit connects the source of combustion-supporting gas to an inlet of the gasifier. A pressure-regulating unit is automatically operative for maintaining the pressure of fluidized combustible material entering the gasifier higher than the pressure of combustion-supporting gas entering the gasifier and higher than the pressure of gases in the gasifier, to prevent the combustion-supporting gas and also the gases in the gasifier from passing out of the gasifier into the first conduit and becoming mixed with fluidized combustible material before such combustible material can enter the gasifier.
    • 该装置包括在惰性气体中流化的精细分散的固体可燃物质源,以及燃烧负载气体源,例如氧气,空气或富氧空气。 提供气化器用于通过使其与燃烧负载气体反应来使细分散的固体可燃材料气化,并且气化器具有一个或多个入口。 第一导管将可燃材料源连接到气化器的入口。 第二导管将燃烧支持气体源连接到气化器的入口。 压力调节单元自动工作,以保持进入气化器的流化可燃材料的压力高于进入气化器的燃烧气体的压力高于气化器中气体的压力,以防止燃烧气体和 气化器中的气体也从气化器中排出到第一导管中,并在这种可燃材料进入气化器之前与流化的可燃材料混合。
    • 9. 发明授权
    • Process for working up municipal plastic waste materials by gasification
    • 通过气化处理市政塑料废料的工艺
    • US5470361A
    • 1995-11-28
    • US331364
    • 1994-10-27
    • Adolf LinkeWerner PohlKarl SchmidRolf Wetzel
    • Adolf LinkeWerner PohlKarl SchmidRolf Wetzel
    • C10J3/46C10J3/66C10J3/06C10K1/02C10K1/06
    • C10J3/00C10J3/66C10J3/721C10K1/003C10K1/004C10K1/02C10K1/101C10K1/143C10J2300/0906C10J2300/0946C10J2300/0959C10J2300/169C10J2300/1884Y02E50/32
    • In the process for gasification of municipal waste plastic waste material pieces of about a 20 mm piece size are compressed and heated at a pressure of from 40 to 80 bar until at a temperature of from 230.degree. to 300.degree. C. to produce an HCl-containing gas and a plastic waste material containing less than 3000 mg of HCl per kg and the HCl-containing gas produced is washed with water to produce a hydrochloric acid solution. The plastic waste material is then heated further until at a temperature of from 400.degree. to 500.degree. C. to form a plastic melt having a viscosity of less than 300 cSt, advantageously less than 50 cSt. This plastic melt is gasified at a pressure of 4 bar with oxygen in a flame reaction to form a crude gas containing a preponderant proportion of CO in relation to CO.sub.2 in a gasification chamber having a central temperature of about 1600.degree. C. The crude gas is withdrawn from the gasification reactor at a temperature of 1300.degree. to 1600.degree. C., quenched with a water spray to cool it until at a temperature of 700.degree. to 900.degree. C. and then further cooled by indirect heat transfer in a heat exchanger producing steam until at a temperature of from 220.degree. to 300.degree. C. The cooled crude gas is dedusted until a dust content of less than 20 mg/Nm.sup.3 of crude gas is reached and the dedusted gas is washed and desulfurized to form the product gas.
    • 在城市废塑料废气的气化过程中,将大约20毫米片尺寸的废料在40至80巴的压力下压缩和加热至230℃至300℃的温度,以产生HCl- 含有气体和每千克含有少于3000毫克HCl的塑料废料,所生成的含HCl气体用水洗涤以产生盐酸溶液。 然后将塑料废料进一步加热至400℃至500℃的温度,以形成粘度小于300cSt,有利地小于50cSt的塑料熔体。 该塑料熔体在4巴的压力下与氧气在火焰反应中气化,形成一种粗气体,其在中心温度为约1600℃的气化室中含有相对于CO 2的CO优选比例。粗气体为 在1300℃至1600℃的温度下从气化反应器中取出,用水喷雾骤冷至700℃至900℃的温度,然后通过间接传热在热交换器中进一步冷却,产生 蒸汽直至温度为220〜300℃。将冷却的粗气除尘至达到小于20mg / Nm3的原油的粉尘含量,并将除尘气体洗涤并脱硫形成产物气体。