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    • 1. 发明申请
    • METHOD FOR REMOVAL OF AMMONIA FROM A GAS MIXTURE
    • 从气体混合物中去除氨的方法
    • WO1990008736A1
    • 1990-08-09
    • PCT/NO1990000028
    • 1990-02-02
    • NORSK HYDRO A.SEIMER, Dag, ArneOI, Lars, Erik
    • NORSK HYDRO A.S
    • C01C01/12
    • C01C1/0464Y02P20/52
    • The present invention relates to a method of catalytic production of ammonia, where a gas mixture consisting mainly of unconverted synthesis gas, some ammonia, inert gases and possibly also water is recirculated to the synthesis reactor being first freed from the main part of the ammonia and possibly also water by absorption. The gas mixture is brought in contact with a hygroscopic absorption agent having two or more OH-groups for absorption of ammonia and possibly also water. The absorption is carried out at a pressure being substantially the same as the ammonia synthesis pressure, and ammonia being desorbed from the absorption agent at a lower pressure and higher temperature than at the absorption. At least part of the possibly present water is removed from the absorption agent before it is supplied to the absorption column. Preferably it is applied ethylene glycol, diethylene glycol or triethylene glycol alone or in mixture as absorption agent. Possible water can be removed from the absorption agent by inert stripping gas before it is returned to the absorption column.
    • 本发明涉及一种催化生产氨的方法,其中主要由未转化的合成气,一些氨,惰性气体和可能的水组成的气体混合物再循环到合成反应器中,首先从氨的主要部分中脱除, 也可能通过吸收水。 使气体混合物与具有两个或更多个OH基团的吸湿剂接触以吸收氨以及可能的水。 吸收在与氨合成压力基本相同的压力下进行,氨在比吸收更低的压力和更高的温度下从吸收剂中解吸。 至少部分可能存在的水在被提供给吸收塔之前从吸收剂中除去。 优选单独使用乙二醇,二甘醇或三甘醇或作为吸收剂的混合物。 可能的水可以在惰性汽提气体返回到吸收塔之前从吸收剂中除去。
    • 3. 发明申请
    • PRE-TREATMENT OF NATURAL GAS TO BE CONDENSED TO LIQUEFIED NATURAL GAS (LNG)
    • 预处理天然气被用于液化天然气(LNG)
    • WO1994011090A1
    • 1994-05-26
    • PCT/NO1993000166
    • 1993-11-11
    • NORSK HYDRO A.SEIMER, Dag, Arne
    • NORSK HYDRO A.S
    • B01D53/14
    • B01D53/1493B01D53/14B01D53/1475B01D53/263C10G2300/1025Y02C10/06
    • The present invention relates to pre-treatment of natural gas for removal of CO2 and water by means of absorption down to LNG specification regarding CO2 and H2O content. The natural gas is brought in contact with a two-component absorption solution comprising one component acting as a solvent, which can be a mixture of solvents, having high affinity for water and being compatible with the other components having the ability to react reversibly with CO2. Used absorption solution is regenerated by stripping with large amounts of inert gas, preferably natural gas, containing substantially no CO2 or H2O. Both the absorption and desorption can be performed in two stages. The two-component absorption solution comprises ethylene glycols, glycol ethers or normal methyl pyrrolidone and alkanolamines.
    • 本发明涉及通过根据关于CO 2和H 2 O含量的LNG规范的吸收来除去天然气以除去二氧化碳和水。 使天然气与双组分吸收溶液接触,该双组分吸收溶液包含作为溶剂的一种组分,其可以是溶剂的混合物,对水具有高亲和力并且与具有与CO 2可逆反应的能力的其它组分相容 。 使用大量不含CO 2或H 2 O的惰性气体,优选天然气进行汽提再生二氧化碳吸收溶液。 吸收和解吸都可以分两个阶段进行。 双组分吸收溶液包括乙二醇,二醇醚或正甲基吡咯烷酮和链烷醇胺。
    • 4. 发明申请
    • PURIFICATION OF NATURAL GAS
    • 天然气净化
    • WO1995017948A1
    • 1995-07-06
    • PCT/NO1994000213
    • 1994-12-23
    • NORSK HYDRO A.SEIMER, Dag, ArneANDERSSON, Gry
    • NORSK HYDRO A.S
    • B01D53/14
    • B01D53/263B01D53/14B01D53/1425B01D53/1468B01D53/1493B01D53/507C10L3/10
    • The present invention relates to a process for the purification of natural gas to make it comply with gas or pipeline specifications comprising that the gas has a dew point between 0 DEG C and -18 DEG C and a H2S content below 4 ppm by volume. H2S and water are removed simultaneously from the natural gas in an absorption column where the gas is contacted with an amine-glycol solution. The glycol solution is then heated, flashed and then brought in contact with a stripping gas to be freed of the water and H2S, whereupon the stripping gas containing removed H2S and water is combusted with air whereby the H2S is converted to SO2 which subsequently is absorbed in a contact unit to which sea water is supplied and brought in contact with the exhaust gas from the combustion unit. The absorption solution is preferably a mixture of a primary and/or secondary alkanolamine in mono-, di-, and/or triethylene glycol.
    • 本发明涉及一种天然气净化方法,使其符合气体或管道规格,包括气体的露点在0℃至-18℃之间,H2S含量低于4ppm(体积)。 在气体与胺 - 乙二醇溶液接触的吸收塔中,同时从天然气中除去H 2 S和水。 然后将乙二醇溶液加热,闪蒸,然后与汽提气接触以除去水和H 2 S,随后将含有除去的H 2 S和水的汽提气体与空气一起燃烧,由此将H 2 S转化成SO 2,随后被吸收 在供给海水并与来自燃烧单元的废气接触的接触单元中。 吸收溶液优选是单 - ,二 - 和/或三甘醇中的伯和/或仲烷醇胺的混合物。
    • 5. 发明申请
    • HEAT-INSULATED COMPOSITE PROFILED SECTION
    • 隔热复合型材构件
    • WO1997009504A1
    • 1997-03-13
    • PCT/DE1996001652
    • 1996-09-05
    • NORSK HYDRO A.SSCHULZ, Harald
    • NORSK HYDRO A.S
    • E06B03/263
    • E06B3/26303E06B2003/26332E06B2003/26352
    • The invention concerns a heat-insulated composite profiled section comprising an insulation weg (6) having two substantially parallel delimiting walls (6.1, 6.2) which form a cavity therebetween. The delimiting walls (6.1, 6.2) can be interconnected by at least one transverse web (10). From an initial wall thickness s = 0.5 mm and a heat conductivity lambda = 0.35 W/mK of the delimiting walls (6.1, 6.2), the width (D) of the insulation web is set at 20 mm in oder to achieve thermal insulance of the insulation web in the range of from 0.15 m K/W to 0.30 m K/W, 30 mm for thermal insulance in the range of from 0.25 m K/W to 0.50 m K/W, 40 mm for thermal insulance in the range of from 0.35 m K/W to 0.65 m K/W, and 50 mm for thermal insulance in the range of from 0.40 m K/W to 0.80 m K/W. Therefore, the width (d) of the cavity or hollow chamber is less than or equal to the width (D) of the insulation web and greater than or equal to one third of the width (D) of the insulation web, provided the height of the cavity or hollow chamber (11) is less than or equal to 5 mm. If the height of the cavity or hollow chamber is between 5 mm and 20 mm and at least one transverse web (10) is present, the ratio of height (h) to width (d) is greater than or equal to 0.2 and less than or equal to 5. For a variation in the wall thickness (s) of between 0.25 mm and 1.0 mm, a dependency of the thermal insulance on the wall thickness (s) according to the relation: R(s)=R(s=0.25 mm) + (s - 0.25)/0.25 * DELTA R, with the value of DELTA R ranging from 0.025 to 0.05, has to be taken into account. Increasing the heat conductivity of the delimiting walls (6.1, 6.2) by 10 % in the range of from 0.15 W/mK to 0.40 W/mK reduces the thermal insulance by between 2 and 4 %, which is to be taken into account accordingly for the dimensions initially selected.
    • 绝缘带(6)具有两个基本上平行的边界壁(6.1,6.2)在它们之间形成空腔。 边界壁(6.1,6.2)可通过至少一个横向腹板(10)被连接到彼此。 从壁厚s =0.5毫米启动和热导率的λ= 0.35 W /边界壁的MK(6.1,6.2),以达到绝缘腹板的热阻范围0.15米<2> K / W的宽度之间( 绝缘带至20mm,在该范围的D)0.25米<2> K / W和0.50米之间<2> K / W的绝缘带的宽度(D)至30毫米,在范围0.35米之间 <2> K / W和0.65米<2> K / W的绝缘带的宽度(D)为40mm,在范围0.40米<2> K / W和0.80米<2> K的 / W在规定的50mm左右的绝缘带的宽度(D)。 空腔或中空室的宽度(d)的选择为小于或等于所述绝缘纤维网的宽度(D)且大于或等于所述绝缘纤维网的宽度(D)的第三个,只要空腔或中空室的高度(11) 小于或等于5毫米。 在腔或以上5毫米到20毫米,至少一个现有的横向腹板(10)的高度(h)的比率的宽度的范围内的中空室的高度被选择为大于或等于0.2且小于或等于5(d)中 , 如果壁厚(多个)在0.25mm至1.0mm之间的范围内,根据等式R(S)= R(S)而变化,作为壁的厚度(S)的热阻的依赖= R(S = 0 考虑到0.25)/ 0.25 *增量R,并与值范围R的增量0.025至0.05 - 25mm)的+(S。 增加边界壁的10%的热导率(6.1,6.2)范围为0.15 W / mK以下,且0.40 W之间/ mK的导致由2〜4%的降低热阻的,对应于当最初选择的输出变量 被考虑在内。
    • 8. 发明申请
    • PIPE JOINT
    • 管接头
    • WO1996004502A1
    • 1996-02-15
    • PCT/NO1995000132
    • 1995-07-21
    • NORSK HYDRO A.SBOE, EinarCARLSEN, Hans-PaulHOLGERSEN, StigHAUGERUD, Olav, Sveinung
    • NORSK HYDRO A.S
    • F16L39/00
    • F16L15/001F16L39/00
    • Pipe joint for joining two pipe end sections (1, 1'), the pipes support in their walls one or more bores (7) and/or lines or conduits (8) for hydraulic or electrical energy transfer. The pipe joint comprises a pipe union (3) with internal threads (13, 13'), one section thereof is threaded to the right, and another to the left. These threads correspond respectively with similar external threads (6, 6') at the pipe ends. A joining part (2) is arranged between the two pipe ends, and serves to mutually centre and lock the pipe end sections. In the joining part (2) there is arranged joining sleeves (4) for each bore (7) or line (8), to obtain a tight joint between these.
    • 用于连接两个管端部分(1,1')的管接头,管道在其壁上支撑用于液压或电能传递的一个或多个孔(7)和/或管线(8)。 管接头包括具有内螺纹(13,13')的管接头(3),其一部分向右螺纹,另一部分向左螺纹连接。 这些螺纹分别与管端相似的外螺纹(6,6')相对应。 连接部分(2)设置在两个管端之间,用于相互中心并锁定管端部。 在连接部分(2)中,为每个孔(7)或管线(8)布置有连接套筒(4),以在它们之间获得紧密接合。