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1. 发明授权

US4671900A Preparation of light-colored, wash active .alpha.-sulfofatty acid 失效
标题翻译：制备浅色，洗涤活性α-磺基脂肪酸
公开(公告)号：US4671900A
公开(公告)日：1987-06-09
申请号：US288769
申请日：1981-07-31
申请人： Karl Schmid , Werner Stein , Horst Baumann
发明人： Karl Schmid , Werner Stein , Horst Baumann
IPC分类号： C07C67/00 , C07C301/00 , C07C303/06 , C07C303/42 , C07C303/44 , C07C309/09 , C07C309/17 , C07C309/58 , C07C309/62 , C11C3/00 , C11D1/28 , C07C143/90
CPC分类号： C07C303/42 , C11C3/00 , C11D1/28
摘要： This invention is directed to the preparation of .alpha.-sulfofatty acid esters. More particularly, this invention is directed to a process for the simplified preparation of light-colored, wash-active esters of .alpha.-sulfofatty acids with monovalent C.sub.1 to C.sub.8 alcohols or their salts from fats and oils of vegetable and/or animal origin comprising re-esterification with the monovalent alcohols or saponification and esterification with the monovalent alcohols, separation of the fatty acid ester formed, hydrogenation of the fatty acid ester, sulfonation, and bleaching, wherein a fatty acid ester fraction from which accompanying fatty acid glycerides have been removed to the extent of about 1 percent by weight or less, based upon the weight of the material to be sulfonated, is introduced into the sulfonation stage.
摘要翻译：本发明涉及α-磺基脂肪酸酯的制备。更具体地，本发明涉及一种简单制备α-磺基脂肪酸的浅色洗涤活性酯与一价C1至C8醇或其植物和/或动物来源的脂肪和油的盐的方法，其包括re 用单价醇进行酯化反应或用单价醇皂化和酯化，形成脂肪酸酯的分离，脂肪酸酯的氢化，磺化和漂白，其中伴随的脂肪酸甘油酯已被除去的脂肪酸酯部分基于待磺化材料的重量约1重量％或更少的程度引入磺化阶段。

2. 发明授权

US3988247A Sulfonated lubricating agents for leather and furs and process 失效
标题翻译：用于皮革和毛皮的磺化润滑剂和工艺
公开(公告)号：US3988247A
公开(公告)日：1976-10-26
申请号：US391201
申请日：1973-08-24
申请人： Gerhard Dieckelmann , Jurgen Plapper , Horst Baumann , Werner Stein
发明人： Gerhard Dieckelmann , Jurgen Plapper , Horst Baumann , Werner Stein
IPC分类号： C14C9/00 , C14C9/02
CPC分类号： C14C9/02 , C07C309/00
摘要： Process and agent for fatting or lubrication of leather and furs based on the salts of sulfonated chlorinated products of higher fatty acids or of esters of higher fatty acids, said fatty acids having from 8 to 24 carbon atoms, especially natural fats and oils or tallow fatty acid methyl ester, having a chlorine content of 20% to 45% by weight and essentially free of olefinic double bonds and having an SO.sub.3 content of from 40 to 150 mol percent based on the chlorinated product, which agent and the leather and furs so treated are extraordinarily resistant to the effect of light, to oxidation and to acids.
摘要翻译：基于高级脂肪酸的磺化氯化产物或高级脂肪酸的酯的脂肪酸，具有8至24个碳原子的脂肪酸，特别是天然脂肪和油或牛油脂肪的皮革和毛皮的脂肪化或润滑的方法和试剂酸性甲酯，其氯含量为20重量％至45重量％，基本上不含烯属双键，并且基于氯化产物，SO 3含量为40至150摩尔％，该试剂和皮革和毛皮如此处理对光，氧化和酸的作用非常有抵抗力。

3. 发明授权

US4080372A Continuous process for bleaching acid alpha-sulfo-fatty acid esters 失效
标题翻译：用于漂白酸性α-磺基脂肪酸酯的连续方法
公开(公告)号：US4080372A
公开(公告)日：1978-03-21
申请号：US748096
申请日：1976-12-06
申请人： Werner Stein , Horst Baumann , Hans Josef Rommerskirchen
发明人： Werner Stein , Horst Baumann , Hans Josef Rommerskirchen
IPC分类号： C07C309/30 , C07C20060101 , C07C67/00 , C07C301/00 , C07C303/42 , C07C303/44 , C07C309/17 , C07C309/58 , C11D1/28 , C07C143/90
CPC分类号： C07C303/42
摘要： A continuous process for the bleaching of acid .alpha.-sulfo-fatty acid esters of predominantly C.sub.16-24 fatty acids comprising continuously adding the hydrogen peroxide bleach in aqueous solution as well as from 2% to 50% by weight, based on the sulfonated esters, of a C.sub.6-18 alkylbenzene sulfonic acid, to said raw, acid .alpha.-sulfo-fatty acid esters at a temperature of 40.degree. to 65.degree. C, continuously passing said mixture through a confined zone of dimensions sufficient to give a proper bleach retention time and continuously recovering bleached .alpha.-sulfo-fatty acid esters.
摘要翻译：用于漂白主要为C 16-24脂肪酸的酸性α-磺基脂肪酸酯的连续方法包括基于磺化酯连续地加入过氧化氢漂白剂在水溶液中，以及2重量％至50重量％的C 6-18烷基苯磺酸，在40℃至65℃的温度下，将所述生的酸式α-磺基脂肪酸酯连续地通过所述混合物通过足够的适当的漂白保留时间的限定区域并连续回收漂白的α-磺基脂肪酸酯。

4. 发明授权

US3931271A Process for the production of secondary alcohol ether sulfates 失效
标题翻译：二醇醇硫酸盐生产工艺
公开(公告)号：US3931271A
公开(公告)日：1976-01-06
申请号：US118549
申请日：1971-02-24
申请人： Horst Baumann , Wilfried Umbach , Werner Stein
发明人： Horst Baumann , Wilfried Umbach , Werner Stein
IPC分类号： C07C309/65 , C07C29/52 , C07C303/24 , C07C303/28 , C11D1/29 , C07C139/00 , C07C139/10 , C07C141/00
CPC分类号： C07C29/52 , C07C303/24 , C11D1/29
摘要： A process for the production of secondary alcohol ether sulfates which consists essentially of reacting adducts of secondary alkanols having from 6 to 22 carbon atoms adducted with 1 to 10 mols of an alkylene oxide selected from the group consisting of ethylene oxide and propylene oxide, said adduct having at least 1 mol of oxypropylene per mol of alcohol, with at least a molecular equivalent of a sulfating agent stronger than concentrated sulfuric acid at temperatures of from 0.degree.C to 50.degree.C and recovering said secondary alcohol ether sulfate.THE PRIOR ARTAt present secondary alcohols can be prepared from inexpensive raw materials, such as by oxidation of paraffins, substantially simpler than the preparation of primary alcohols. However, up to now the practical use of secondary alcohols is limited to non-ionic products prepared from them. Surface-active sulfates derived from secondary alcohols are used only in small amounts since the preparation of such raw materials for washing agents is very difficult, because of the instability of the secondary alkylsulfates. Primary alcohols, on the contrary, can be converted simply and with good yields into surface-active sulfates. In the sulfation of secondary alcohols, the conversion rates are low. In order to obtain somewhat usable products, expensive procedures have to be introduced, such as working with solvents and adduct formers, use of special sulfating agents, such as, for example, amidosulfonic acid, etc., as well as the addition of ethylene oxide adducts of primary alcohols. On the other hand, there is the possibility that by reaction of secondary alcohols with ethylene oxide, adducts with primary hydroxyl groups can be prepared, the sulfation products of which could be expected to have greater stability.It is, however, very difficult to prepare ethoxylates of secondary alcohols with a high conversion rate and small amounts of by-products. A higher conversion rate of the secondary alcohols with ethylene oxide can only be attained by relatively cumbersome procedures, such as, for example, a two-step ethoxylation in which in the first step an acidic catalyst is used and, after distilling off the unreacted secondary alcohol, in the second step an alkaline catalyst is utilized. However, the ethoxylated secondary alcohols obtained by this expensive procedure are also unsatisfactorily sulfated and can only be sulfated by the application of special procedures. This is difficult to explain since by the ethoxylation of secondary alcohols, adducts with primary hydroxyl groups were formed.OBJECTS OF THE INVENTIONAn object of the present invention is the development of a simple process for the production of secondary alcohol ether sulfates utilizing conventional strong sulfating agents to give products with a high degree of sulfation.Another object of the invention is the development of a process for the production of secondary alcohol ether sulfates which consists essentially of reacting adducts of secondary alkanols having from 6 to 22 carbon atoms adducted with 1 to 10 mols of an alkylene oxide selected from the group consisting of ethylene oxide and propylene oxide, said adduct having at least 1 mol of oxypropylene per mol of alcohol, with at least a molecular equivalent of a sulfating agent stronger than concentrated sulfuric acid at temperatures of from 0.degree.C to 50.degree.C and recovering said secondary alcohol ether sulfate.These and other objects of the invention will become more apparent as the description thereof proceeds.DESCRIPTION OF THE INVENTIONIt has now been surprisingly found that alkylene oxide adducts of secondary alcohols which contain at least one propylene glycol ether group can be sulfated simply with a high conversion rate. This result was the more unexpected since, as is known, on the introduction of propylene glycol ether groups by propoxylation, adducts with predominately secondary hydroxyl groups are formed. Therefore, the same difficulties in the further reaction of these adducts, especially in sulfation, would be expected as in the sulfation of secondary alcohols themselves. With this expectation, the sulfation of secondary alcohol propoxylates would appear to the expert as having little prospect of good yields.The invention relates, therefore, to a process for the preparation of surface-active ether and polyether sulfates which is characterized in that adducts of secondary alkanols having 6 to 22 carbon atoms adducted with 1 to 10 mols of alkylene oxide, possessing in the average at least 1 mol of propylene oxide per mol of alcohol, are reacted in a known manner at temperatures between 0.degree.C and 50.degree.C, particularly from 10.degree.C and 30.degree.C, with strong sulfating agents in at least stoichiometric amounts.As starting materials those adducts may be used that were obtained (1) by ethoxylation of secondary alcohols in the first step and subsequent propoxylation of the reaction mixtures, or (2) by reaction of secondary alcohols with ethylene oxide/propylene oxide mixtures, or (3) by the ethoxylation of reaction mixtures of secondary alcohols with propylene oxide, or (4) by pure propoxylation of secondary alcohols. The preferred starting materials are the adducts of propylene oxide to secondary alcohols or secondary alkanol propoxylates having 6 to 22 carbon atoms in the alkanol and 1 to 10 oxypropylene units.The mixed alkoxylates to be used contain preferably 1 to 4, particularly 2 to 3, oxyethylene groups. Of particular advantage among the pure propylene oxide adducts are those substance mixtures which were obtained by reaction of 1.5 to 5 mols of propylene oxide with 1 mol of secondary alcohol.The starting materials can be obtained by conventional alkoxylation methods. The alkoxylation can be carried out both anionically, in the presence of alkaline alkoxylation catalysts, such as alkali metal hydroxides or alkali metal alcoholates, particularly sodium, potassium and lithium lower alkanolates, and cationically in the presence of acidic catalysts, such as BF.sub.3, or in the presence of the tertiary oxonium salts described as alkoxylation catalysts in Belgian Pat. No. 715,048.If mixed adducts are used which have been obtained by propoxylation of ethylene oxide adducts of secondary alcohols as starting materials, such mixed adducts are preferred in which the alkoxylation in the first step was carried out by a cationic catalyst and in the second step with an anionic catalyst.Among the mixed adducts which are obtained by simultaneous addition of ethylene oxide and propylene oxide, or by propoxylation in the first step and ethoxylation in the second step, as well as in the pure propoxylation products, these are preferably prepared by reaction with an anionic catalyst.The secondary alcohols utilized to prepare the alkoxylation mixtures can be either compounds of uniform chain length or mixtures of homologs. Of particular economic advantage are those alcohol mixtures which have been obtained by the oxidation of paraffins in the presence of boron compounds, such as, for example, boric acid, boron trioxide, borates, boric acid esters, as well as other known reagents for the formation of secondary alcohols, such as arsenic acid, arsenic acid esters, arsenic trioxide, and others.The alkoxylation mixtures utilizable for the subsequent sulfation can be used as crude products, that is, without intervening purification or processing operations. This is of essential importance for the technical execution of the process. These crude alkoxylation mixtures contain, therefore, in addition to the desired alkylene oxide adducts of secondary alcohols, as secondary constituents, the corresponding alkylene and/or polyalkylene glycols as well as, possibly, non-reacted secondary alcohol. The sulfation of the alkoxylate mixture is preferably carried out in the temperature range of from 10.degree.C to 30.degree.C.By "strong sulfating agents" are meant those which are stronger than concentrated sulfuric acid, for example, SO.sub.3 or SO.sub.3 /air mixtures, oleum, chlorosulfonic acid, and the like. The addition of adduct formers for the sulfating agent or the presence of solvents are not required in the process. The preferred sulfating agent is chlorosulfonic acid. The mol ratio between the alkoxylate and the sulfating agent is advantageously chosen in the range of from 1:1.0 to 1:1.2, particularly in the range of from 1:1.02 to 1:1.1.The sulfation reaction can be carried out continuously or discontinuously. The reaction times lie between fractions of seconds to about 20 minutes, depending upon the sulfating agent and/or sulfating apparatus used. Particularly short reaction times are attained if the reaction is carried out with very strong sulfating agents, such as SO.sub.3 /air mixtures, in modern short-time sulfation reactors which operate by the split-ring or falling film principle.The products of the process have a substantially higher degree of sulfation than the products obtained by the sulfation of technical ethylene oxide adducts of secondary alcohols. They have, without further processing, very good surface-active properties and are superior, particularly in regard to their wetting action, to the known commercial sulfated adducts of ethylene oxide to primary alcohols.The advantages attainable with the invention consist primarily in that as a raw material source for surface-active, water-soluble sulfates, secondary alcohols have been made available. Particularly those secondary alcohols which are easily obtainable by paraffin oxidation in the presence of the above-named oxidation catalysts to produce secondary alcohols with statistically distributed hydroxyl groups. These alcohols are converted by alkoxylation to the substances suitable for sulfation. Thus, these petrochemical raw materials can form the basis for the desired surface-active substances. Anionic active derivatives of secondary alcohols were up to now technically not producible by a simple way although secondary alcohols have been produced for some time on a large scale. The use of secondary alcohols was, therefore, until now limited to the production of non-ionic substances.A further advantage of the process according to the invention can be seen in that the necessary alkoxylation may be carried out without a large expense in regard to catalysts and/or equipment.The following examples are illustrative of the invention without being deemed limitative in any respect.
摘要翻译：一种生产仲醇醚硫酸盐的方法，其主要包括与6至22个碳原子的仲烷醇的加合物加成1至10摩尔选自环氧乙烷和环氧丙烷的环氧烷烃，所述加合物每摩尔醇具有至少1摩尔氧化丙烯，至少在0℃至50℃的温度下至少分子当量的硫酸化剂比浓硫酸更强，并回收所述仲醇醚硫酸盐。

5. 发明授权

US4275048A Process for the preparation of fine droplet-reacted aluminosilicates of the smallest particle size 失效
标题翻译：制备最小粒径的微滴反应铝硅酸盐的方法
公开(公告)号：US4275048A
公开(公告)日：1981-06-23
申请号：US105255
申请日：1979-12-19
申请人： Werner Stein , Peter Christophliemk
发明人： Werner Stein , Peter Christophliemk
IPC分类号： C01B33/26 , C01B33/46 , C01B39/02 , C01B39/16 , C01B39/22 , C11D3/12 , C01B33/28
CPC分类号： C11D3/128 , C01B33/26 , C01B33/2823 , C01B39/02 , Y02P20/129
摘要： A process for the preparation of fine droplet-reacted sodium aluminosilicates with the smallest particle sizes, containing less than 0.1% by weight of granules exceeding 25 .mu.m in size, said aluminosilicates being insoluble in water and containing some bound water, of the general formulaxNa.sub.2 O.Al.sub.2 O.sub.3.y SiO.sub.2in which x is a number from 0.2 to 1.5 and y is a number from 1.5 to 10, prepared by reacting aqueous sodium aluminate with aqueous sodium silicate in the presence of an excess of aqueous sodium hydroxide and subsequent filtration, comprising the step of separately passing a solution of sodium aluminate with a composition corresponding to the molar ratios:1 Al.sub.2 O.sub.3 :1 to 10 Na.sub.2 O:20 to 200 H.sub.2 Oand a solution of sodium silicate with a composition corresponding to the molar ratios:Na.sub.2 O:SiO.sub.2 from 0.1 to 10 andH.sub.2 O:SiO.sub.2 from 5 to 200to a spray head, spraying the two solutions into intimate contact, at a ratio by weight corresponding the desired total composition within the molar ratios of:1.5 to 15 Na.sub.2 O:1 Al.sub.2 O.sub.3 :1 to 15 SiO.sub.2 :50 to 400 H.sub.2 Oat a temperature of between 0.degree. and 103.degree. C., employing a spray system with at least one spray head with at least two liquid channels, each terminating in a jet spray nozzle, one for each solution, in such a manner that the two solutions meet only after leaving the spray head at a velocity sufficient to form a fine mist of droplets, whereby the two reactants undergo reaction while still in the fine mist of droplets stage, with the formation of an X-ray-amorphous sodium aluminosilicate gel, allowing the droplets to settle and recovering an aqueous suspension of said X-ray-amorphous sodium aluminosilicate in a form adapted for crystallization.
摘要翻译：制备具有最小粒径的微小液滴反应的硅铝酸钠的方法，其含有小于0.1重量％的超过25μm的颗粒，所述铝硅酸盐不溶于水并含有一些结合水，通式 xNa2O.Al2O3.y SiO2，其中x为0.2至1.5的数，y为1.5至10的数，通过在过量的氢氧化钠水溶液存在下反应，使铝酸钠与硅酸钠水溶液反应制备，随后过滤，包括分别通过铝酸钠溶液，其组成对应于摩尔比：Al 2 O 3：1至10Na 2 O：20至200H 2 O和具有对应于Na 2 O:SiO 2摩尔比的组成的硅酸钠溶液将0.1至10和H 2 O:SiO 2从5至200喷雾至喷雾头，将两种溶液以相对于所需总组成的重量比例紧密接触，以摩尔比o f：1.5至15 Na 2 O：1 Al 2 O 3：1至15SiO 2：50至400H 2 O，温度为0至103℃，采用具有至少一个具有至少两个液体通道的喷头的喷雾系统终止于每个溶液中的一个喷射喷嘴，使得两个溶液仅在以足以形成细小雾滴的速度离开喷头之后才会聚，由此两种反应物在仍处于细微状态下进行反应形成液滴阶段，形成X射线无定形硅铝酸钠凝胶，允许液滴以适于结晶的形式沉淀并回收所述X射线无定形硅铝酸钠的水性悬浮液。

6. 发明授权

US3956351A Process for separating fatty mixtures 失效
标题翻译：分离脂肪混合物的方法
公开(公告)号：US3956351A
公开(公告)日：1976-05-11
申请号：US465528
申请日：1974-04-30
申请人： Werner Stein , Richard Schuh
发明人： Werner Stein , Richard Schuh
IPC分类号： B01F17/02 , B01F17/00 , C11B7/00 , C09F5/10 , C11B3/00 , C11C1/08
CPC分类号： C11B7/0091
摘要： A method for separating mixtures of fatty substances into components with different melting points in which a fatty substance suspension separated from a liquid fat portion is transformed by heating to temperatures between the melting point of the solid portions and about 85.degree. C by means of the usual separating devices at ordinary or increased gravity into a three-phase system which consists of molten solid particles as the lightest phase, of an intermediate aqueous phase of medium specific gravity rich in wetting agents, and of a heavy aqueous phase which is low in wetting agents, and the solid portions are then separated.
摘要翻译：将脂肪物质的混合物分离成具有不同熔点的成分的方法，其中从液体脂肪部分分离的脂肪物质悬浮液通过加热至固体部分的熔点和约85℃之间的温度而被转化将平均或增加重力的分离装置分离成由熔融固体颗粒作为最轻的阶段组成的三相体系，比较浓的介质的中间水相富含润湿剂，以及湿润剂低的重水相然后分离固体部分。

7. 发明授权

US5343984A Rotating drive for an adjusting spindle of a disk brake for motor vehicles 失效
标题翻译：用于机动车辆的盘式制动器的调节主轴的旋转驱动器
公开(公告)号：US5343984A
公开(公告)日：1994-09-06
申请号：US18241
申请日：1993-02-16
申请人： Dieter Bieker , Johann Iraschko , Werner Stein
发明人： Dieter Bieker , Johann Iraschko , Werner Stein
IPC分类号： F16D65/16 , F16D65/14 , F16D65/52 , F16D65/56 , F16D65/40
CPC分类号： F16D65/183 , F16D65/568 , F16D2121/14 , F16D2125/32 , F16D2125/48 , F16D2125/52 , F16D2125/64
摘要： A rotating drive for an adjusting spindle of a disk brake for motor vehicles, in particular street vehicles, has a cam lever (4), which can be rotated around an axis (19) parallel to the brake disk, comprising one cantilever (23) on each side of said lever comprising angular offset radial boreholes (24, 24') which receive radial pins (17, 17'). The pins (17, 17') reach into the double forked end of a drive lever (15), which can be rotated around an axis (20), crossing at right angles at a distance from the axis (19). The rotational movements of the drive lever (15) are transferred to a reset drive, which belongs to an adjusting spindle extending at right angles to the plane of the brake disk.
摘要翻译：用于机动车辆，特别是街道车辆的盘式制动器的调节主轴的旋转驱动器具有可围绕平行于制动盘的轴线（19）旋转的凸轮杆（4），包括一个悬臂（23）在所述杠杆的每一侧包括接收径向销（17,17'）的角偏移径向钻孔（24,24'）。销（17,17'）到达驱动杆（15）的双叉形端部，驱动杆（15）可以围绕轴线（20）旋转，与轴线（19）成一定距离成直角交叉。驱动杆（15）的旋转运动被传送到复位驱动器，该复位驱动器属于与制动盘的平面成直角延伸的调节主轴。

8. 发明授权

US4618582A Process for producing Xanthomonas biopolymers 失效
标题翻译：产生黄单胞菌属生物聚合物的方法
公开(公告)号：US4618582A
公开(公告)日：1986-10-21
申请号：US346591
申请日：1982-02-08
申请人： Konrad Engelskirchen , Werner Stein , Michael Bahn , Ludwig Schieferstein , Joachim Schindler , Rolf Schmid
发明人： Konrad Engelskirchen , Werner Stein , Michael Bahn , Ludwig Schieferstein , Joachim Schindler , Rolf Schmid
IPC分类号： C12P19/06 , C12R1/64 , C12N1/20 , C12N1/26
CPC分类号： C12P19/06 , Y10S435/91
摘要： In the aerobic culture of microorganisms of the Xanthomonas genus in fermentation media, the use of water-in-oil emulsions in the media minimizes viscosity problems and enhances yields of Xanthomonas biopolymers. Preferably, the emulsion is formed with a surfactant and the microorganism is Xanthomonas campestris.
摘要翻译：在发酵培养基中黄单胞菌属微生物的需氧培养中，在培养基中使用油包水乳剂使粘度问题最小化并提高黄单胞菌属生物聚合物的产量。优选地，乳液由表面活性剂形成，微生物是野油菜黄单胞菌（Xanthomonas campestris）。

9. 发明授权

US4178408A Flame-proof epoxy fibrous structure and laminates thereof 失效
标题翻译：防火环氧纤维结构及其层压板
公开(公告)号：US4178408A
公开(公告)日：1979-12-11
申请号：US874966
申请日：1978-02-03
申请人： Arnold Franz , Werner Stein
发明人： Arnold Franz , Werner Stein
IPC分类号： C08L69/00 , B32B27/18 , C08G59/00 , C08J5/24 , C08K5/00 , C08K5/06 , C08L63/00 , C08L67/00 , C08L77/00 , H05K1/03 , D04H1/58 , B32B17/04
CPC分类号： C08J5/24 , C08K5/06 , H05K1/0373 , C08J2363/00 , H05K2201/012 , H05K2203/122 , Y10T442/3415
摘要： A formed epoxy resin composition comprising a condensed epoxy resin and pentabromodiphenylether; the use of pentabromodiphenylether alone or with other brominated diphenyl ethers as a flame-retardant agent for compositions containing epoxide resins especially fibrous substrates of glass and/or cellulose fibers containing epoxide resins therein.
摘要翻译：一种形成的环氧树脂组合物，其包含缩合环氧树脂和五溴二苯醚; 单独使用五溴二苯醚或其他溴化二苯醚作为阻燃剂，用于含有环氧树脂的组合物，特别是含有环氧树脂的玻璃和/或纤维素纤维的纤维基质。

10. 发明授权

US4074013A Corrodible iron-containing surfaces carrying corrosion-inhibiting coating 失效
标题翻译：可腐蚀的含铁表面带有腐蚀抑制涂层
公开(公告)号：US4074013A
公开(公告)日：1978-02-14
申请号：US683516
申请日：1976-05-05
申请人： Karlheinz Koch , Gerhard Kolaczinski , Wolfgang Rupilius , Werner Stein
发明人： Karlheinz Koch , Gerhard Kolaczinski , Wolfgang Rupilius , Werner Stein
IPC分类号： C09D5/08 , C07C67/00 , C07C213/00 , C07C213/04 , C07C215/08 , C09K15/20 , C10M133/08 , C23F11/14 , C23F11/00 , B32B15/04
CPC分类号： C10M133/08 , C23F11/142 , C10M2215/042 , C10N2230/12 , Y10T428/31678
摘要： Corrodible iron-containing metals (including steel) possess decreased tendency to corrode when contacted with aqueous media (including dilute strong mineral acids) when they carry a surface coating of mixtures of aminoalkanols of the formula: ##STR1## wherein R.sub.1 and R.sub.2 each represent a C.sub.1-21 alkyl; and wherein the sum of the carbon atoms in R.sub.1 and R.sub.2 is 6 to 22. The vicinal ##STR2## substituents are non-terminal and are preferably uniformly distributed along the chain. The aminoalkanols are useful both in free base and in salt form.
摘要翻译：可腐蚀的含铁金属（包括钢）当与水性介质（包括稀释无机酸）接触时具有降低的腐蚀倾向，当它们具有下式的氨基链烷醇的混合物的表面涂层时：其中R1和R2各自表示 C1-21烷基; 并且其中R 1和R 2中的碳原子的总和为6至22个。邻位的取代基是非末端的，并且优选地沿着链均匀分布。氨基链烷醇在游离碱和盐形式中都是有用的。

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