CN1433335A - 用于处理亲油流体的工艺 - Google Patents
用于处理亲油流体的工艺 Download PDFInfo
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- CN1433335A CN1433335A CN01810710A CN01810710A CN1433335A CN 1433335 A CN1433335 A CN 1433335A CN 01810710 A CN01810710 A CN 01810710A CN 01810710 A CN01810710 A CN 01810710A CN 1433335 A CN1433335 A CN 1433335A
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- lipophilic fluid
- emulsion
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- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
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- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
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- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
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- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
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- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
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Abstract
本发明涉及一种用于处理包含在水和所述亲油流体的乳液中的亲油流体的工艺。该工艺包括,预处理乳液,从乳液中回收亲油流体,和纯化所述亲油流体以去除至少一部分在使用该乳液过程中收集的杂质。为前述每个步骤提供了方法选项。
Description
相关申请的交叉参考
本申请在美国法典35 U.S.C.119(e)第35条的名义下要求临时申请系列号60/209,250;60/209,468;60/209,443;和60/209,444(都递交于2000年6月5日);60/241,174(递交于2000年10月17日);和60/280,074(递交于2001年3月30日)。
本发明的领域
本发明涉及一种用于处理包含在水和亲油流体的乳液中的亲油流体的工艺。该工艺包括,预处理该乳液,从乳液中去除亲油流体,然后纯化该亲油流体以去除至少一部分在使用该乳液过程中所收集的杂质。为前述每个步骤提供了方法选项。
本发明的背景
长期以来,常用于清洁和处理织物制品如衣服的洗衣技术包括传统的水基洗涤和一项通常称作“干洗”的技术。传统水基洗涤技术包括,将织物制品浸渍在水和洗涤剂或皂产品的溶液中,随后漂洗和干燥。但这些常规浸渍清洁技术已证实对许多不适合水浸渍的织物制品不令人满意,这些制品因织物含量,结构等而需要特殊的处理和/或清洁方法。
因此已经开发了″干洗″洗衣方法的应用。干洗通常包括,使用非水,亲油流体作为用于清洁的溶剂或溶液。这样可以清洁和处理与水浸渍不相容的织物,而不会产生由水带来的可能严重的副作用。
尽管可得到各种非水亲油流体,但许多需要存在低含量的乳液或微乳液形式的水,这样可尽量发挥清洁效率而不会通过干洗损害要求″安全″的织物。另外,最后再利用和/或纯化非水,亲油流体以降低由干洗带来的与其水基等同洗涤相比明显较高的操作成本。如果水,污渍,和体污在使用之后也存在于乳液中,亲油流体的再利用就面临特殊的挑战。但再利用尤其在存在设备空间,成本,和安全问题时产生特殊问题。因此,需要一种成本有效的,有效率的,和安全的方式以处理或纯化在其使用之后的亲油流体,尤其在使用水和助剂如乳化剂时。
用于干洗溶剂/水乳液和/或混合物的传统分离技术通常包括,蒸馏所有的含溶剂的流体,包括不需要蒸馏的那些。关于此,蒸馏不仅用于从使用之后的干洗溶剂中去除杂质如体污,而且用于从水中分离溶剂-一种能够以其它方式进行的功能。蒸馏通常包括为实现分离所需的能量和设备形式的高操作成本,并因此在许多情况下,尤其在该设备在消费者家内时不理想。最后可以看出,蒸馏不是所有来自干洗的含溶剂的流体所需要的。例如,蒸发的溶剂-水混合物不必需要蒸馏,因为它们基本上″无杂质″且仅需要水-溶剂分离操作。
因此,仍需要一种成本有效的,有效率的,和安全的方法以处理使用之后的亲油流体,尤其当存在水和乳化剂时。
发明内容
本发明的综述
本发明提供了以成本有效的,有效率的,和安全的方式处理使用之后的亲油流体的方法。
在第一实施方案中,本发明提供了一种用于处理包含在水和至少一种亲油流体的乳液中的亲油流体的工艺。该工艺具有三个主要步骤。这些步骤是预处理乳液,从乳液中回收亲油流体,和纯化该亲油流体。
在第二实施方案中,本发明提供了一种用于纯化亲油流体和亲油流体蒸气的工艺。该工艺包括,收集亲油流体蒸气和具有水和亲油流体的第一乳液,冷凝该亲油流体蒸气,将冷凝的亲油流体蒸气和第一乳液合并以形成第二乳液,预处理第二乳液,从第二乳液中回收亲油流体,和纯化该亲油流体。
本领域普通技术人员根据以下的详细描述和所附权利要求可显然得出这些和其它的方面,特点,和优点。除非另有所指,本文的所有的百分数,比率和比例都是重量计的。除非另有所指,所有的温度是摄氏度(℃)。除非另有所指,所有的测量值是SI单位。所有的引用文件在此作为参考以相关部分引入本发明,从而作为本发明的一部分。
本发明的详细描述
定义
本文所用的术语″亲油流体″是指包括例如由下述试验限定的能够去除皮脂的任何非水流体或蒸气。
本文所用的术语″织物″和″纺织品″是指任何通常在水基洗衣工艺中或在溶剂基干洗工艺中清洁的制品。因此该术语包括本体织物和纤维,以及布,亚麻,布料,和衣物附件的成品。该术语也包括整体或部分由制品制成的其它的物品,如搬运袋,家具罩,帆布和类似物。
本文所用的术语″吸收性材料″或″吸收性聚合物″是指例如要详细描述的任何能够选择性吸收或吸附水和/或含水液体而不会吸收亲油流体的材料。在本领域中,它们也称作″响应凝胶,″″凝胶,″和″聚合物凝胶″。关于相变凝胶的列举,参见教科书
响应凝胶,体积转变II(Responsive Gels,VolumeTransitions II),Ed K.Dusek,Springer Verlag Berlin,1993(在此作为参考引入)。另外参见,
热响应凝胶(Thermo-responsive Gels),Radiat.Phys.Chem.,46卷,No.2,pp.185-190,Elsevier Science Ltd.Great Britain,1995(在此作为参考引入)。也适用于本发明的超吸收性聚合物是具有吸收容量5克/克或更高的聚合物材料。另外参见,
超吸收性聚合物科学和技术(Superabsorbent Polymers Science and Technology),由Fredric L.Buchholz和NicholasA.Peppas编辑,American Chemical Society,Washington DC,1994(尤其是Tadao Shimomura和Takashi Namba的题为″高性能超吸收性聚合物的制备和应用″的第9章),在此作为参考引入。
本文所用的术语″吸收性基质渗透性助剂″或″垫片材料″或″垫片″是指不溶于水的任何纤维或颗粒材料。
本文所用的术语″吸收性基质″是指任何形式的能够吸收或吸附水的基质。它最少包括一种吸收性材料。它可视需要包括垫片材料和/或高表面积材料。
亲油流体
一般来说,亲油流体可在环境温度和压力下完全为液体,可以是容易熔化的固体,如,在温度范围约0℃-约60℃下变成液体的固体,或可在环境温度和压力,如在25℃和1atm.压力下包含液体和蒸气相的混合物。因此,本质上的亲油流体不是一种可压缩的气体如二氧化碳。优选的是,本文的亲油流体是不可燃的或具有较高的闪点和/或低VOC特性,等于或,优选,超过已知的常规干洗流体的特性,其中这些术语具有用于干洗工业的常规含义。
本文的合适的亲油流体容易流动且为非粘稠的。一般来说,本文的亲油流体要求是能够至少部分溶解在以下试验中定义的皮脂(如体污)的流体。亲油流体的混合物也是合适的,但要满足试验要求,亲油流体可包括干洗溶剂,尤其包括非氟化溶剂,或全氟化胺的较新类型的任何级分。尽管不适用作亲油流体,一些全氟化胺如全氟三丁基胺可作为存在于亲油流体的许多可能的附加物之一存在。其它的合适的亲油流体包括二醇溶剂体系如,高级二醇如C6-或C8-或更高级的二醇;有机硅氧烷溶剂,包括环状和无环类型,和类似物;及其混合物。
适合作为亲油流体的主要组分加入的优选的非含水液体包括低挥发性非氟化有机物,硅氧烷,尤其非氨基-官能硅氧烷的那些,及其混合物。低挥发性非氟化有机物包括例如OLEAN和其它的多元醇酯,或某些相对非挥发性可生物降解的中链支化石油级分。适用作主要组分,如,50%以上的亲油流体的硅氧烷包括有时称作″D5″,的环五硅氧烷,或视需要补充有其它的相容的硅氧烷的具有约类似挥发性的线性类似物。合适的硅氧烷在文献中是熟知的,参见例如Kirk Othmer的化学技术百科全书(Encyclopedia ofChemical Technology),并可从许多商业途径得到,包括GeneralElectric,Toshiba Silicone,Bayer,和Dow Corning。其它的合适的流体可得自Procter & Gamble或Dow Chemical和其它的供应商。例如,一种合适的硅氧烷是SF-1528(得自GE)硅氧烷流体。尤其是,SF-1528流体是90%环五硅氧烷(D5)。
能够满足对干洗流体的已知要求(如,闪点等)并如下述试验方法所示能够至少部分溶解皮脂的任何非水流体都适用作本文的亲油流体。特定材料去除皮脂的能力可通过任何已知的技术测定。一般准则是,全氟丁基胺(Fluorinert FC-43)自身(有或没有附加物)是一种参考材料,根据定义它不适用作本文的亲油流体(它基本上是一种非溶剂),而D5则溶解皮脂。
以下是用于研究和限定用作亲油流体的其它的材料,如,其它的低-粘度,自由流动硅氧烷的方法。该方法使用市售Criscocanola油,油酸(95%纯度,得自Sigma Aldrich Co.)和角鲨烯(99%纯,得自J.T.Baker)作为皮脂的典型污垢。试验材料在评估过程中应该基本上无水且没有任何添加的附加物,或其它的材料。
准备三个小瓶。将1.0g canola油放在第一个;在第二小瓶中放入1.0g油酸(95%),并在第三和最后的小瓶中放入1.0g角鲨烯(99.9%)。向每个小瓶中加入1g要测试亲油性的流体。在室温和室压下将包含亲油污垢和所要测试的流体的每个小瓶在标准旋涡混合器上在最大设定值下单独混合20秒。将小瓶放在台上并在室温和室压下沉降15分钟。如果在放置时在任何包含亲油污垢的小瓶中形成单相,那么该流体就确定为适用作本发明的″亲油流体″。但如果在所有的三个小瓶中形成单独的两层或多层,那么溶解在试验流体中的流体的量需要在否决或接受该流体为合格之前进一步确定。
在这种情况下,使用注射器从每个小瓶中的每层小心提取200微升样品。将注射器提取的层样品放在GC自动取样器小瓶中并在确定三个典型污垢中的每个和正在测试的流体的校正样品的保留时间之后进行常规GC分析。如果发现超过1%,优选更多的GC试验流体存在于由油酸,canola油或角鲨烯层组成的任何一层,那么该试验流体也合格地用作亲油流体。如果需要,该方法可进一步使用二十七氟三丁基胺(heptacosafluorotributylamine),即,Fluorinert FC-43(不合格)和环五硅氧烷(合格)校正。
合适的GC是配有裂口/无裂口注射器和FID的Hewlett Packard气体色谱HP5890 II系列。适用于确定亲油流体存在量的柱是J & W Scientific毛细管柱DB-1HT,30米,0.25mm id,0.1um膜厚度cat#1221131。GC合适地在以下条件下操作:
载体气体:氢
柱头压力:9psi
流量:柱流量@约1.5ml/min。
裂口排气@约250-500ml/min。
隔膜清洗@1ml/min。
注射:HP 7673自动取样器,10ul注射器,1ul注射量
注射器温度:350℃
检测器温度:380℃
炉温度程序:起始60℃,保持1min。
升温速率25℃/min。
最终380℃,保持30min。
适用于本文的优选的亲油流体可进一步在具有优异的衣服护理分布(garment care profile)的基础上评价是否合格。衣服护理分布试验是本领域熟知的且包括,使用各种衣服或织物制品组件,包括织物,用于缝合的线和松紧带,等,和各种钮扣测试所要认证的流体。用于本文的优选的亲油流体具有优异的衣服护理分布,例如它们具有良好的收缩分布或织物起皱分布且不会明显损害塑料钮扣。
为了衣服护理试验或其它的条件,如,可燃性,亲油流体可以大致为与织物制品接触的最终亲油流体所用的比率存在于,如与水的混合物中。去除皮脂并以不同方式适用作亲油流体的某些物质,例如,乳酸乙酯可因为其溶解钮扣的倾向而十分令人讨厌。如果这种材料用于亲油流体,它要与水和/或其它的溶剂配制使得总的混合物基本上不损害钮扣。其它的亲油流体,例如D5很好地满足衣服护理要求。一些合适的亲油流体可在授权的U.S.专利Nos.5,865,852;5,942,007;6,042,617;6,042,618;6,056,789;6,059,845;和6,063,135中找到。
亲油溶剂可包括线性和环状聚硅氧烷,烃和氯化烃。更优选的是线性和环状聚硅氧烷和二醇醚,乙酸酯,乳酸酯类的烃。优选的亲油溶剂包括在760mm Hg.下沸点低于约250℃的环状硅氧烷。具体地,优选用于本发明的环状硅氧烷是八甲基环四硅氧烷,十甲基环五硅氧烷,和十二甲基环六硅氧烷。优选,环状硅氧烷包括十甲基环五硅氧烷(D5,五聚体)且基本上没有八甲基环四硅氧烷(四聚体)和十二甲基环六硅氧烷(六聚体)。
但应该理解,除了优选的环状硅氧烷,有用的环状硅氧烷混合物可包含少量的其它的环状硅氧烷,包括八甲基环四硅氧烷和六甲基环三硅氧烷或更高级的环状化合物如十四甲基环七硅氧烷。一般,这些其它的环状硅氧烷在有用的环状硅氧烷混合物中的量低于基于混合物总重的约10%。环状硅氧烷混合物的工业标准是,这些混合物包含低于混合物的约1%重量的八甲基环四硅氧烷。
因此,本发明的亲油流体优选包含超过占亲油流体总重量约50%,更优选超过约75%,甚至更优选至少约90%,最优选至少约95%重量的十甲基环五硅氧烷。另外,亲油流体可包含硅氧烷,它是环状硅氧烷的一种混合物,具有超过该混合物的约50%,优选超过约75%,更优选至少约90%,最优选至少约95%最高约100%重量的十甲基环五硅氧烷和低于该混合物的约10%,优选低于约5%,更优选低于约2%,甚至更优选低于约1%,最优选低于约0.5%-约0%重量的八甲基环四硅氧烷和/或十二甲基环六硅氧烷。
辅助成分
辅助材料可广泛使用且可以较宽的量使用。例如,都可用于洗衣和清洁成品的洗涤酶如蛋白酶,淀粉酶,纤维素酶,脂肪酶和类似物以及漂白剂催化剂(包括具有锰或类似过渡金属的大环类型)在本文中可以典型或非典型量使用。催化性的辅助材料,例如酶可以″正向″或″反向″模式使用,这是独立于本发明的一个有用的发现。例如,脂肪酶或其它的水解酶可视需要在醇作为附加物的存在下用于将脂肪酸转化成酯,这样增加它们在亲油流体中的溶解度。这是一种″反向″操作,不同于该水解酶通常在水中用于将水溶性不太好的脂肪酯转化成水溶性更好的物质。在任何情况下,任何辅助成分必须适合与亲油流体结合使用。
组合物可包含乳化剂。乳化剂是化学领域所熟知的。本质上,乳化剂用于将两个或多个不可溶或半可溶相结合到一起以产生稳定的或半稳定的乳液。优选在本发明中,乳化剂用作双重目的,其中它能够不仅用作乳化剂而且用作处理性能促进剂。例如,乳化剂也可用作表面活性剂以促进清洁性能。普通乳化剂和乳化剂/表面活性剂都有市售。
一些合适的清洁添加剂包括,但是不限于,助洗剂,表面活性剂,酶,漂白剂活化剂,漂白剂催化剂,漂白剂助剂,漂白剂,碱性源,抗细菌剂,着色剂,香料,前香料,整理助剂,石灰皂分散剂,组合物臭味控制剂,气味中和剂,聚合物染料转移抑制剂,晶体生长抑制剂,光漂白剂,重金属离子螯合剂,抗锈蚀剂,抗微生物剂,抗氧化剂,抗再沉积剂,电解质,pH改性剂,增稠剂,研磨剂,二价或三价离子,金属离子盐,酶稳定剂,腐蚀抑制剂,二胺或多元胺和/或其烷氧基化物(alkoxylates),泡沫稳定化聚合物,溶剂,加工助剂,织物软化剂,荧光增白剂,水溶助剂,泡沫或水沫抑制剂,泡沫或水沫促进剂,织物软化剂,抗静电剂,染料固定剂,染料磨损抑制剂,抗脱色剂,减皱剂,抗皱剂,去污聚合物,排污剂,防晒剂,抗褪色剂,及其混合物。
术语″表面活性剂″通常是指在水,亲油流体,或两者的混合物中表面活性的物质。一些说明性的表面活性剂包括例如用于常规含水洗涤剂体系的非离子,阳离子和硅氧烷表面活性剂。合适的非离子表面活性剂包括,但是不限于:
a)如US 4685930 Kasprzak中的壬基苯酚和肉豆寇基醇的聚氧化乙烯缩合物;和
b)脂肪醇乙氧基化物,R-(OCH2CH2)aOH,a=1-100,通常12-40,R=具有8-20个C原子的烃残基,通常线性烷基。例子包括聚氧基亚乙基月桂基醚,具有4或23个氧基亚乙基基团;聚氧基亚乙基鲸蜡基醚,具有2,10或20个氧基亚乙基基团;聚氧基亚乙基硬脂基醚,具有2,10,20,21或100个氧基亚乙基基团;聚氧基亚乙基(2),(10)油基醚,具有2或10个氧基亚乙基基团。市售实施例包括,但是不限于:ALFONIC,BRIJ,GENAPOL,NEODOL,SURFONIC,TRYCOL。另外参见US 6013683(Hill等人)。
合适的阳离子表面活性剂包括,但是不限于,具有下式的二烷基二甲基铵盐:
R′R″N+(CH3)2-X-
其中每个R′R″独立地选自由12-30个C原子组成的基团或衍生自牛油,椰子油或大,X=Cl或Br,实例包括:二(十二烷基)二甲基溴化铵(DDAB),二(十六烷基)二甲基氯化铵,二(十六烷基)二甲基溴化铵,二(十八烷基)二甲基氯化铵,二(二十烷基)二甲基氯化铵,二(二十二烷基)二甲基氯化铵,二椰子二甲基氯化铵,二牛油二甲基溴化铵(DTAB)。市售实施例包括,但是不限于:ADOGEN,ARQUAD,TOMAH,VARIQUAT。另外参见US6013683(Hill等人)。
合适的硅氧烷表面活性剂包括,但是不限于具有二甲基聚硅氧烷憎水部分和一个或多个亲水聚亚烷基侧链并具有以下通式的聚氧化烯聚硅氧烷:
R1-(CH3)2SiO-[(CH3)2SiO]a-[(CH3)(R1)SiO]b-Si(CH3)2-R1
其中a+b是约1-约50,优选约3-约30,更优选约10-约25,且每个R′是相同的或不同的且选自甲基、和具有以下通式的聚(氧化乙烯/氧化丙烯)共聚物:
-(CH2)nO(C2H4O)c(C3H6O)dR2至少一个R′是聚(氧化乙烯/氧化丙烯)共聚物基团,和其中n是3或4,优选3;总c(对于所有的聚亚烷基氧基侧基)具有值1-约100,优选约6-约100;总d是0-约14,优选0-约3;和更优选d是0;c+d的总和具有值约5-约150,优选约9-约100且每个R2是相同的或不同的并选自氢、具有1-4个碳原子的烷基、和乙酰基基团,优选氢和甲基基团。这些表面活性剂的例子可在U.S.专利No.′s5,705,562和5,707,613(两者都授予Hill)中找到。
这种表面活性剂的例子是Silwet表面活性剂,得自CK Witco,OSi分部,Danbury,Connecticut。代表性的Silwet表面活性剂如下。
名称 平均MW 平均a+b 平均总c
L-7608 600 1 9
L-7607 1,000 2 17
L-77 600 1 9
L-7605 6,000 20 99
L-7604 4,000 21 53
L-7600 4,000 11 68
L-7657 5,000 20 76
L-7602 3,000 20 29
聚亚烷基氧基基团(R1)的分子量低于或等于约10,000。优选,聚亚烷基氧基基团的分子量低于或等于约8,000,和最优选为约300-约5,000。因此,c和d的值可以是提供在这些范围内的分子量的那些数。但亚乙基氧基单元(-C2H4O)在聚醚链(R1)中的数目必须足以使聚氧化烯聚硅氧烷水可分散或水溶性的。如果亚丙基氧基基团存在于聚亚烷基氧基链,它们可无规分布在链中或作为嵌段存在。优选的Silwet表面活性剂是L-7600,L-7602,L-7604,L-7605,L-7657,及其混合物。除了表面活性,聚氧化烯聚硅氧烷表面活性剂也可提供其它的益处,如抗静电作用,和对织物的软化。
聚氧化烯聚硅氧烷的制备是本领域熟知的。本发明的聚氧化烯聚硅氧烷可根据U.S.Pat.No.3,299,112所提出的工艺制备。其它的合适的硅氧烷表面活性剂是SF-1488,它可购自GE silicone fluids。
适合作为附加物与亲油流体结合使用的这些和其它的表面活性剂是本领域熟知的,更详细描述于Kirk Othmer的化学技术百科全书(Encyclopediaof Chemical Technology,3rd Ed.,Vol.22,pp.360-379,″表面活性剂和洗涤剂体系″。进一步合适的非离子洗涤剂表面活性剂一般公开于U.S.专利3,929,678(Laughlin等人,1975年12月30日授权)第13栏第14行至第16栏第6行。
附加物也可以是抗静电剂。任何适用于洗衣和干洗领域的熟知的抗静电剂都适用于本发明的方法和组合物。尤其合适的抗静电剂是已知能提供抗静电作用的织物软化剂子类。例如,这些织物软化剂具有碘值超过20的脂肪酰基基团,如N,N-二(牛酰基-氧基-乙基)-N,N-二甲基甲基硫酸铵。但可以理解,术语″抗静电剂″不仅局限于该子类的织物软化剂,而且包括所有的抗静电剂。
尽管详细描述了用于本发明的方法和/或组合物,应该理解且本领域熟练技术人员可以认识到,能够实现本发明的任何组合物,工艺,和/或装置都可使用。
吸收性材料
形成水凝胶的吸收性聚合物
本发明的吸收性聚合物优选包含至少一种形成水凝胶的吸收性聚合物(也称作形成水凝胶的聚合物)。
可用于本发明的形成水凝胶的聚合物包括各种能够吸收含水液体的水不可溶,但水可溶胀的聚合物。这些形成水凝胶的聚合物是本领域熟知的且任何这些聚合物都可用于本发明。
可用于本发明的形成水凝胶的吸收性聚合物可具有在宽范围内的尺寸,形状和/或形态。这些聚合物可以是最大尺寸与最小尺寸的比率不大的颗粒(如,粒剂,粉末,颗粒间聚集体,颗粒间交联聚集体,和类似物)的形式且可以是纤维,片材,膜,泡沫材料,片和类似物的形式。形成水凝胶的吸收性聚合物也可包含具有低含量的一种或多种添加剂,例如粉状硅石,沸石,活性炭,分子筛,表面活性剂,胶,粘结剂,和类似物的混合物。该混合物中的组分可以物理和/或化学方式连接,使得形成水凝胶的聚合物组分和非形成水凝胶的聚合物添加剂不容易物理分离。形成水凝胶的吸收性聚合物可以是基本上非多孔(即,没有内孔隙率)或具有显著的内孔隙率。
其它的胶凝聚合物
基于丙烯酰胺的凝胶也适用于本发明。具体地,合适的是丙烯酰胺,2-(丙烯酰基氧基)乙基酸磷酸盐,2-丙烯酰氨基2-甲基丙烷磺酸,丙烯酸2-二甲基氨基乙酯,2,2′-二(丙烯酰氨基)乙酸,3-(甲基丙烯酰氨基)丙基三甲基氯化铵,丙烯酰氨基甲基丙烷二甲基氯化铵,丙烯酸酯,丙烯腈,丙烯酸,二烯丙基二甲基氯化铵,二烯丙基氯化铵,丙烯酸二甲基氨基乙酯,甲基丙烯酸二甲基氨基乙酯,乙二醇,二甲基丙烯酸酯,乙二醇单甲基丙烯酸酯,甲基丙烯酰胺,甲基丙烯酰氨基丙基三甲基氯化铵,N,N-二甲基丙烯酰胺,N[2[[5-(二甲基氨基)-1-萘基]磺酰基]氨基[乙基]-2-丙烯酰胺,N-[3-二甲基氨基)丙基]丙烯酰胺盐酸盐,N-[3-(二甲基氨基)丙基)甲基丙烯酰胺盐酸盐,聚(二烯丙基二甲基氯化铵),甲基丙烯酸2-(2-羧基苯甲酰基氧基)乙酯钠,丙烯酸钠,烯丙基乙酸钠,甲基丙烯酸钠,苯乙烯磺酸钠,乙烯基乙酸钠,三烯丙基胺,三甲基(N-丙烯酰基-3-氨基丙基)氯化铵,三苯基甲烷-无色衍生物,乙烯基-封端的聚甲基硅氧烷,N-(2-乙氧基乙基)丙烯酰胺,N-3-(甲氧基丙基)丙烯酰胺,N-(3-乙氧基丙基)丙烯酰胺,N-环丙基丙烯酰胺,N-n-丙基丙烯酰胺,和N-(四氢糠基)丙烯酰胺。
另外合适的是基于N-异丙基丙烯酰胺的凝胶。这些可包括N-异丙基丙烯酰胺,甲基丙烯酸2-(二乙基氨基)乙酯,甲基丙烯酸2-(二甲基氨基)乙酯,2-丙烯酰氨基-2-甲基-1-丙烷磺基丙烯酸酯,丙烯酸,丙烯酰胺甲基丙烯酸烷基酯,二(4-二甲基氨基)苯基)(4-乙烯基苯基)甲基无色氰化物,刀豆球蛋白A(卵磷脂),甲基丙烯酸己基酯,甲基丙烯酸月桂基酯,甲基丙烯酸,甲基丙烯酰氨基丙基三甲基氯化铵,甲基丙烯酸正丁基酯,聚(四氟乙烯),聚四亚甲基醚二醇,丙烯酸钠,甲基丙烯酸钠,乙烯基磺酸钠,和乙烯基-封端的聚甲基硅氧烷。
另外合适的是的基于N,N′-二乙基丙烯酰胺的凝胶。这些可包括N,N′-二乙基内烯酰胺,甲基丙烯酰氨基丙基三甲基氯化铵,N-丙烯酰氧基琥珀酰亚胺酯,N-叔-丁基丙烯酰胺,和甲基丙烯酸钠。
基于丙烯酸酯的凝胶也是合适的。这些可包括丙烯酸2-二甲基氨基乙酯,2-丙烯酰氨基-2-甲基丙烷磺酸,丙烯酰胺,三烯丙基胺,丙烯酸酯,丙烯酰胺,甲基丙烯酸甲酯,二乙烯基苯,甲基丙烯酸N,N-二甲基氨基乙酯,聚(氧基四亚甲基二甲基丙烯酸酯),聚(甲基丙烯酸2-羟基乙酯),聚(甲基丙烯酸2-羟基丙酯),和聚乙二醇甲基丙烯酸酯。
另外合适的是基于各种单体的凝胶。这些可包括丙烯酸,甲基丙烯酰氨基丙基三甲基氯化铵,胶原,二棕榈酰磷脂酰乙醇胺(dipalmitoylphosphatidylethanolamine),聚[4-6-十二烯-1,10-二醇二(n-丁氧基羰基甲基氨基甲酸乙酯)],聚[二[氨基乙氧基)乙氧基]磷腈(phosphazene)],聚[二[(丁氧基乙氧基)乙氧基]磷腈],聚[二[乙氧基乙氧基)乙氧基]磷腈],聚[二[甲氧基乙氧基)乙氧基]磷腈],聚[二[甲氧基乙氧基)磷腈],聚二甲基硅氧烷,聚氧化乙烯,聚(亚乙基-二甲基硅氧烷-氧化乙烯),聚(N-丙烯酰吡咯烷),聚[n,n-二甲基-N-[(甲基丙烯酰基氧基乙基]-N-(3-磺基丙基)铵甜菜碱],聚甲基丙烯酸,聚甲基丙烯酰基二肽,聚乙烯基醇,聚乙烯基醇-乙酸乙烯基酯,聚乙烯基甲基醚,呋喃改性的聚(n-乙酰基亚乙基亚胺),和马来酰亚胺改性的聚(n-乙酰基亚乙基亚胺)。
另外合适的是公开于U.S.专利Nos.4,555,344、4,828,710,和欧洲申请EP648,521 A2(都在此作为参考引入)的凝胶。
高表面积材料
除了渗透性吸收剂(例如,形成水凝胶的吸收性聚合物),本发明可包含高表面积材料。正是这种高表面积材料本身或与形成水凝胶的吸收性聚合物结合提供具有高毛细管吸附吸收容量的分离装置或容器。
高表面积材料可以是纤维(以下称作″高表面积纤维″)性质的,这样在与形成水凝胶的吸收性聚合物或其它的渗透性吸收剂结合时提供纤维网或纤维基质。另外,高表面积材料可以是开孔的亲水聚合物泡沫材料(以下称作″高表面积聚合物泡沫材料″或更多一般地称作″聚合物泡沫材料″)。
除了这些纤维,熟练技术人员可以认识到,吸收领域中熟知的其它的纤维可通过改性以提供用于本文的高表面积纤维。可改性以获得本发明所需高表面积的纤维的例子公开于以上的U.S.专利No.5,599,335(尤其参见21-24栏),在此作为参考引入。
垫片
适用于本发明的垫片材料包括任何不溶于水的纤维或颗粒材料。垫片可分散在整个的吸收性材料基质中,这样将其渗透性提高至仅由吸收性材料组成的基质之上;或,垫片可用于即使在吸收性材料在暴露于水时溶胀和/或胶凝之后也保持渗透性。因此,垫片有助于在载水流体经过基质时降低跨越吸收性材料基质的压降。另外,如果吸收性材料倾向在暴露于水之后凝结并随后塌陷,该垫片可帮助降低或防止塌陷时的凝胶凝结。
合适的水不可溶垫片材料的非限定性例子包括沙,硅石,硅铝酸盐,玻璃微球,粘土,层化硅酸盐,木材,天然纺织品材料,合成纺织品材料,矾土,氧化铝,硅酸铝,氧化钛,氧化锌,分子筛,沸石,活性炭,硅藻土,水合硅石,云母,微结晶纤维素,蒙脱石,桃坑粉末,美洲山核桃壳粉末,滑石,氧化锡,二氧化钛,胡桃壳粉末,和不同的金属或金属合金的颗粒。另外有用的是由混合聚合物(如,共聚物,三元聚合物,等),如聚乙烯/聚丙烯共聚物,聚乙烯/丙烯/异丁烯共聚物,聚乙烯/苯乙烯共聚物,和类似物制成的颗粒。
吸收性基质
为了增加″干″吸收性基质渗透性或保持吸收性基质在湿润时的渗透性,重要的是向垫片提供足够的吸收性材料,和,视需要,高表面积材料比率。由于可能的垫片的重量可根据吸收性材料的重量而变化极大,该比例必须在″干″体积基础上确定。″净基质体积″是吸收性材料,垫片,和,视需要,任何高表面积材料的体积,不包括材料本身可包含的任何内体积或任何归因于内材料空隙空间的体积。″内材料空隙体积″是当颗粒和/或纤维占据给定空间时在材料颗粒和/或纤维之间通常且自然出现的累积空隙体积。″干本体基质体积″等于净基质体积与内材料空隙体积在于基上的总和。对于本发明,优选的是,吸收性材料是干本体基质体积的50-100%,更优选75-95%。优选的是,垫片是干本体基质体积的1-50%,更优选5-25%。优选的是,可有可无的高表面积材料是干本体基质体积的1-50%,更优选5-25%。
凝胶材料,垫片,和,视需要,高表面积材料可成型为片材或膜或薄膜并以不同方式成型。片材构型取决于用途且一般包括四种一般的构型,即,管,中空纤维,板和框架单元,和螺旋缠绕的组件,所有这些都在本发明的范围内。
方法选项
本发明可视需要与几种熟知的工艺结合以纯化流体。这些工艺可用于帮助水-亲油流体分离操作和/或在已使用亲油流体之后用于从中去除杂质。
蒸馏工艺通过在容器中加热液体而生产蒸气,随后冷凝该蒸气并将它们收集在其它的容器。可用的蒸馏工艺的种类是简单的,分馏,蒸汽,不混溶性溶剂,共沸,萃取,真空,分子,共沸剂(entrainer)升华,和冷冻干燥。
萃取是将一种或多种化合物从一种液体选择性地转移至其它的不混溶性液体或由固体转移至液体。前者工艺称作液体-液体萃取且是一种间接的分离技术,因为两种组分不是直接分离。加入一种外来物质(不混溶性液体)以提供第二相。
″倾析″和″密度分级″是重力型分离方法。″倾析器″定义为一种利用重力将物流连续分离成两个液相的容器。使用Stokes定律,可用推导出液滴在连续相中的沉降速率并因此设计倾析器。
离子交换是化合物中的一种离子交换为相同种类的不同离子的一个过程:阳离子交换为其它的阳离子且阴离子交换为其它的阴离子。离子交换树脂常用于进行交换。所用的离子交换树脂都可视为固体溶液,无论它是阳离子或阴离子交换剂,强或弱离子化的,凝胶或大孔的,球形或粒状的。实际上,所观察到的每个离子交换行为可归结为组分在两个溶液相之间的分布,其中之一限定为固体相。组分转移发生在相之间的界面上,该界面是珠粒或粒剂的表面。离子交换树脂的内相包含四种必要的组分。这些组分包括:三维聚合物网状结构,永久连接到网状结构上的离子官能团,抗衡离子,和溶剂。在某些条件下,可以在树脂内有其它的组分如第二溶剂,共离子,和非离子溶液。
用如活性炭的吸附是一个用于分离液体的重要单元操作并利用发生在吸附剂材料表面上的表面现象。当与固体表面有关的能量将分子或离子物质从液体吸引到固体时,发生吸附。被吸附的材料可在表面上形成一至几个分子深的层。表面的量和性能以及在表面上的环境条件控制吸附。许多高度多孔固体在接触湿溶剂混合物时优先吸附水并可将水去除至非常低的浓度。尽管它们可单程(on a once-through basis)使用,它们能够通过加热而再生。通常使用分子筛;但离子交换树脂型有机吸附剂是具有吸引力的选择。
色谱是一种多步分离技术,基于化合物之间在吸附到表面上或溶解于液体薄膜中的差异。更常见的色谱类型是纸,薄层,高效,气体,和凝胶渗透。色谱分离过程中的两种主要的工作机理是置换和分割。
渗析是溶质因溶质浓度的跨膜梯度而穿过膜的转移作用。它伴随渗透,即溶剂因溶剂浓度的跨膜梯度而穿过膜的一种转移作用。在透析时,溶质转移的方向与渗透中的溶剂转移方向相反。在浓度梯度的驱动下经低分子量溶质分子或离子的通道通过半渗透膜,从而经过渗析可有效地从溶液中去除低分子量溶质分子或离子。
电渗析是电解质在电驱动力下转移通过溶液和膜的体系的一个过程。目前所用的术语电渗析是指具有离子交换膜的多腔电渗析。电渗析有四种变型:电解质,浓度稀释,离子取代,和反转。
渗滤(diafiltration)与常规渗析的区别在于,微物质去除的速率不取决于浓度而简单地是超滤速率(膜面积)相对所要交换或透析的体积的函数。通过重复或连续加入新鲜溶剂,可有效地并迅速地冲洗或交换盐和其它的微物质。
固体可设计成吸附水同时排斥溶剂。同样,膜可设计成通过水并保留溶剂或或反之亦然。用于从溶剂-水混合物中去除水的渗透蒸发的应用包括使用亲水膜。从水中去除溶剂是相同的,只是使用排斥水但亲油的膜。
结晶是由蒸气,熔体,或溶液产生晶体的一个过程且与沉淀的区别在于,后者通常具有特别高的超饱和水平,主要成核作用,和低溶解度比率。
离心是一项根据密度差异分离材料的技术,分离的速率通过施加不断增加的旋转力而增强。该力称作离心力且提供该旋转力的装置称作离心机。
过滤主要用于从液体中去除固体。具体地,将包含低固体物质的液体过滤使得它们变成光学透明的溶液。滤筒的结构是圆柱状,具有打褶或未打褶的,可处理的或可清洁的过滤介质。过滤介质通常整体粘结到塑料或金属硬件上。
沉积是通过重力沉降而从液体中分离悬浮的固体颗粒。沉降也可根据沉降速率的不同而用于分离固体颗粒。
汽提是可将许多有机溶剂从废水中去除至可排放水的水平的一种方法。该方法特别适用于具有低水溶解度或相当于水高挥发性的溶剂。
干燥剂干燥包括,将水湿溶剂与一种适合取出水并形成第二相的固体,通常电解质接触。水可随后从该第二相中通过其它的方式(如倾析)去除。
化学品加入包括,加入化学品以改变液体的至少一个物理-化学性能如pH,离子强度,等等。这些化学品的例子包括盐,酸,碱,凝结剂,和絮凝剂。
酶,微生物,或细菌加入包括,将酶,微生物,或细菌加入废物流以从该物流中去除有机污染物。
温度改变可增强二元混合物的分离作用并可包括混合物的冷却和/或加热两者。增加混合物的温度有助于凝聚(coalescence),而冷却有助于结晶或冷冻一种组分。
静电凝聚包括,将包含两个相互不溶的相(例如亲油流体和水)的乳液,其中一相是连续相且另一相是不连续相,暴露于电场以将不连续相凝聚成尺寸足够大的液滴,这样滴液因为两相的密度差异而从乳液中下沉。为了实现该方法,两相必须在介电恒定和密度方面具有至少较小的差异。电凝聚是熟知的工艺且描述于US.专利号3,207,686(Jarvis等人);3,342,720(Turner);3,772,180(Prestridge);3,939,395(Prestridge);4,056,451(Hodgson);4,126,537(Prestridge);4,308,127(Prestridge);和5,861,089(Gatti等人)。
吸收包括,将乳液暴露于一种能够从乳液中″吸收″至少一种组分的材料。吸收性材料通常经历体积改变(膨胀或收缩率),不同于主要是表面变化的吸附作用。在一个例子中可以采用吸收性聚合物从溶剂-水乳液中去除水。
工艺
本发明涉及一种处理包含在至少由水和亲油流体组成的乳液中的亲油流体的工艺。该工艺包括,预处理乳液,从乳液中回收亲油流体,和纯化亲油流体。该工艺可进一步包括,首先将织物暴露于亲油流体和水并随后收集乳液形式的亲油流体和水。该工艺可视需要包括一个混合步骤,其中将至少一部分亲油流体和至少一部分水混合形成乳液,然后暴露于织物。乳化剂也可在混合步骤过程中加入。
如果它确实包含乳化剂,乳液可包含最高约10%重量的乳化剂。亲油流体和水乳液优选具有水/亲油流体/乳化剂比率约1/98.9/0.1-约40/55/5(乳液重量)。最后,如″辅助成分″章节所讨论,乳化剂可同时用作表面活性剂。
优选的是,亲油流体包括线性硅氧烷,环状硅氧烷,和这些硅氧烷的混合物。更优选的是,这些硅氧烷选自八甲基环四硅氧烷,十甲基环五硅氧烷,十二甲基环六硅氧烷,和这些硅氧烷的混合物。甚至更优选的是,亲油流体包含十甲基环五硅氧烷。最后,最优选的是,亲油流体包含十甲基环五硅氧烷且基本上没有八甲基环四硅氧烷。
本发明的″收集″步骤可以几种方式进行。将包括亲油流体和水的织物加料(fabric load)旋转是常规洗衣应用中所熟知的。拧或扭转或挤压受处理的织物也是熟知的用于从织物和织物制品中去除流体的机械方式。蒸发也可用于收集亲油流体和水和/或-干燥织物加料。加热织物加料,亲油流体和水或其它的用于蒸发的熟知方式可实现该作用。旋转和/或翻滚可与加热结合以有助于蒸发和蒸发均匀性。如果采用该方法,它需要随后的亲油流体和水的冷凝,然后是回收和纯化步骤。
″预处理″步骤可以许多常规方式进行。预处理方法的非限定性例子包括沉积,离心,旋流作用暴露,倾析,过滤,化学品加入,和温度改变。预处理形式也包括前述方法的组合。
如果进行过滤,最好将亲油流体和水乳液经过一个颗粒物质过滤器,使得去除约25微米或更大的颗粒和颗粒聚集体,优选使得去除约15微米或更大的颗粒和颗粒聚集体,更优选使得去除约10微米或更大的颗粒和颗粒聚集体,甚至更优选使得去除约5微米或更大的颗粒和颗粒聚集体,甚至更优选使得去除约1微米或更大的颗粒和颗粒聚集体。还可以将亲油流体和水乳液暴露于活性炭以进一步预处理。
″回收″步骤同样可以许多熟知的方式进行。回收方法的非限定性例子包括机械凝聚,电凝聚,化学品加入,膜过滤,温度改变,汽提,微生物加入,吸收性材料暴露,离心,蒸馏,吸附,吸收,结晶,沉淀,温度改性,渗滤,电解,提取,pH改变,和离子强度改变。
许多用于进行吸附的可能方式是将乳液暴露于活性炭。回收形式也可包括前述方法的组合。
″纯化″步骤可以许多方式进行。非限定性实施例包括膜过滤,蒸馏,提取,汽提,酶加入,离子交换,干燥剂干燥,色谱,和吸附。纯化形式也可包括前述方法的组合。
本发明还涉及用于纯化亲油流体和亲油流体蒸气的工艺。该工艺包括收集亲油流体蒸气和包含水和亲油流体的第一乳液的步骤。然后,将亲油流体蒸气冷凝形成冷凝的亲油流体蒸气。将冷凝的亲油流体蒸气与第一乳液合并形成第二乳液。第二乳液可随后按照上述进行预处理。在预处理之后,亲油流体和冷凝的亲油流体蒸气可用上述的相同方法从第二乳液中回收。在从乳液中回收之后,亲油流体和冷凝的亲油流体蒸气按照上述方法进行纯化。如同第一实施方案,该工艺也可视需要包括,首先将织物暴露于亲油流体和水并随后收集第一乳液形式的亲油流体和水。该工艺可视需要包括混合步骤,其中将至少一部分亲油流体和至少一部分水混合形成第一乳液,然后暴露于织物。乳化剂也可在混合步骤过程中加入。
以上讨论的任何组合物或乳液还可包含附加物,选自以上″辅助成分″章节的成分,包括,但不限于,酶,漂白剂,表面活性剂,织物软化剂,香料,抗细菌剂,抗静电剂,增白剂,染料固定剂,染料磨损抑制剂,抗脱色剂,减皱剂,抗皱剂,去污聚合物,排污剂,防晒剂,抗褪色剂,助洗剂,起泡剂,组合物臭味控制剂,组合物着色剂,pH缓冲剂,防水剂,污垢排斥剂,和这些附加物的混合物。
本发明的方法和体系可用于服务,如干洗服务,尿布服务,均匀清洁服务,或商业,如作为旅馆,餐馆,会议中心,机场,游船,港口设施,娱乐场一部分的自助洗衣店,干洗机,亚麻服务,或可以是用于家庭。
本发明的方法可在对现有装置的改进且更新的装置中进行,该装置使得在常规工艺,如水洗之外进行本发明的工艺。
本发明的方法也可在这样的装置中进行,该装置不是对现有装置的改进但特定地构造使得进行本发明或可作为亲油流体处理体系的一部分加入其它装置。它包括所有的相连管线,如与化学品和水供给的连接,和废洗涤流体的排水设备。
本发明的体系可在这样的装置中进行,该装置不是对现有装置的改进但特定地构造使得进行本发明和,可能地,常规工艺,如水洗。
本发明的方法也可在能够具有″双重模式″功能的装置中进行。″双重模式″装置能够在同一转筒中洗涤和干燥织物。这些装置尤其在欧洲可广泛得到。
用于进行本发明的装置通常包含一些种类的控制体系。这些包括电体系,如,所谓的聪明控制体系(smart control system),以及更传统的电机械体系。控制体系使得使用者能够选择所要清洁的织物负荷的尺寸,污染的种类,污染的程度,清洁周期的时间。另外,使用者可使用预定的清洁和/或复新周期,或该装置可根据许多可确定的参数控制周期长度。这在电控制体系时尤其如此。例如,如果亲油流体的收集速率达到一个稳定速率,该装置可在固定时间之后自己关掉,或启动另一亲油流体的工艺。
在电控制体系的情况下,一种选择是使控制设备成为所谓的″聪明设备″。这意味着包括,但不限于,自诊断体系,负荷类型和周期选择,将机器连接到因特网上并使消费者能够远程启动该装置,当该已清洁织物制品时告知,或在该装置故障时让供应商远程诊断问题。另外,如果本发明体系仅为清洁体系的一部分,所谓的″聪明体系″可与用于完成其余清洁工艺的其它的清洁设备,如洗衣机,和干燥器连接。
Claims (13)
1.一种用于处理包含在乳液中的亲油流体的工艺,所述乳液的特征在于水和所述亲油流体,所述工艺特征在于步骤:
a.预处理所述乳液;
b.从所述乳液中回收所述亲油流体;和
c.纯化所述亲油流体。
2.根据权利要求1的工艺,进一步特征在于步骤:
a.将织物暴露于所述亲油流体和所述水;和
b.收集所述乳液形式的所述亲油流体和所述水。
3.根据权利要求2的工艺,其中所述工艺还特征在于一个混合步骤,其特征在于将至少一部分所述亲油流体和至少一部分所述水和任选的乳化剂混合形成所述乳液,然后将所述织物暴露于所述亲油流体和所述水。
4.根据权利要求2-3中任一项的工艺,其中所述收集步骤特征在于,旋转所述织物或扭所述织物使得所述亲油流体和所述水从所述织物中去除或从所述织物中蒸发所述亲油流体和所述水并冷凝所述蒸发的亲油流体和水或其组合。
5.根据权利要求1-4中任一项的工艺,其中所述预处理步骤特征在于沉积,或离心处理,或旋流作用暴露,或倾析,或过滤,或温度改变,或化学品加入,或其组合。
6.根据权利要求1-5中任一项的工艺,其中所述预处理步骤特征在于将所述乳液经过一个过滤器以去除1微米或更大的颗粒和颗粒聚集体。
7.根据权利要求1-6中任一项的工艺,其中所述回收步骤特征在于机械凝聚,或电凝聚,或化学品加入,或膜过滤,或温度改变,或汽提,或微生物加入,或吸收性材料暴露,或离心,或蒸馏,或吸附,或优选被活性炭吸收,或结晶,或沉淀,或温度改变,或渗滤,电解,或提取,或pH改变,或离子强度改变,或其组合。
8.根据权利要求1-7中任一项的工艺,其中所述纯化步骤特征在于膜过滤,或蒸馏,或提取,或汽提,或酶加入,或离子交换,或干燥剂干燥,或吸附,或其组合。
9.根据权利要求1-8中任一项的工艺,其中所述乳液特征在于水/结合的亲油流体和,以所述乳液重量计,1/98.9/0.1到40/55/5的冷凝的亲油流体蒸气/乳化剂比率。
10.根据权利要求1-9中任一项的工艺,其中所述亲油流体特征在于线性硅氧烷,环状硅氧烷,或其混合物。
11.根据权利要求1-10中任一项的工艺,其中所述亲油流体特征在于十甲基环五硅氧烷。
12.根据权利要求1-11中任一项的工艺,其中所述乳液还特征在于选自酶,漂白剂,表面活性剂,织物软化剂,香料,抗细菌剂,抗静电剂,增白剂,染料固定剂,染料磨损抑制剂,抗脱色剂,减皱剂,抗皱剂,去污聚合物,防晒剂,抗褪色剂,助洗剂,起泡剂,组合物臭味控制剂,组合物着色剂,pH缓冲剂,防水剂,污垢排斥剂,及其混合物的辅助成分。
13.用于纯化亲油流体和亲油流体蒸气的根据权利要求1-12中任一项的工艺,所述工艺特征在于如下步骤:
a.收集所述亲油流体蒸气和特征在于水和所述亲油流体的第一乳液;
b.将所述亲油流体蒸气冷凝形成冷凝的亲油流体蒸气;
c.将所述冷凝的亲油流体蒸气和所述第一乳液合并形成第二乳液;
d.预处理所述第二乳液;
e.从所述第二乳液中回收所述亲油流体和所述缩合亲油流体蒸气;和
f.纯化所述亲油流体和所述冷凝的亲油流体蒸气。
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US09/849,842 US6828292B2 (en) | 2000-06-05 | 2001-05-04 | Domestic fabric article refreshment in integrated cleaning and treatment processes |
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CN104944533A (zh) * | 2014-03-26 | 2015-09-30 | 北京师范大学 | 一种全氟化合物的浓缩分离去除方法 |
CN110662863A (zh) * | 2017-05-31 | 2020-01-07 | 拉费尔有限公司 | 用于去除流体的装置和包括所述装置的洗涤设备 |
CN113583038A (zh) * | 2021-07-27 | 2021-11-02 | 合盛硅业(鄯善)有限公司 | 八甲基环四硅氧烷提纯方法 |
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CZ20033404A3 (cs) * | 2001-06-22 | 2004-05-12 | Theáprocterá@Ágambleácompany | Přípravky pro péči o tkaniny vužívající lipofilní kapalné systémy |
US7276162B2 (en) | 2001-09-10 | 2007-10-02 | The Procter & Gamble Co. | Removal of contaminants from a lipophilic fluid |
US6955761B2 (en) | 2001-09-10 | 2005-10-18 | Procter & Gamble Company | Multifunctional filter |
AR036777A1 (es) | 2001-09-10 | 2004-10-06 | Procter & Gamble | Filtro para remover agua y/o surfactantes de un fluido lipofilo |
JP4302519B2 (ja) * | 2001-09-10 | 2009-07-29 | ザ プロクター アンド ギャンブル カンパニー | 親油性流体処理方法 |
CA2457353C (en) | 2001-09-10 | 2008-08-26 | The Procter & Gamble Company | Method for processing a lipophilic fluid |
US7300594B2 (en) * | 2003-06-27 | 2007-11-27 | The Procter & Gamble Company | Process for purifying a lipophilic fluid by modifying the contaminants |
US7297277B2 (en) * | 2003-06-27 | 2007-11-20 | The Procter & Gamble Company | Method for purifying a dry cleaning solvent |
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Cited By (4)
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CN104944533A (zh) * | 2014-03-26 | 2015-09-30 | 北京师范大学 | 一种全氟化合物的浓缩分离去除方法 |
CN104944533B (zh) * | 2014-03-26 | 2017-08-25 | 北京师范大学 | 一种全氟化合物的浓缩分离去除方法 |
CN110662863A (zh) * | 2017-05-31 | 2020-01-07 | 拉费尔有限公司 | 用于去除流体的装置和包括所述装置的洗涤设备 |
CN113583038A (zh) * | 2021-07-27 | 2021-11-02 | 合盛硅业(鄯善)有限公司 | 八甲基环四硅氧烷提纯方法 |
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KR20030025234A (ko) | 2003-03-28 |
CA2409127A1 (en) | 2001-12-13 |
EP1292731A2 (en) | 2003-03-19 |
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JP2003535991A (ja) | 2003-12-02 |
JP5160012B2 (ja) | 2013-03-13 |
EP1292731B1 (en) | 2010-09-08 |
WO2001094679A2 (en) | 2001-12-13 |
MXPA02011959A (es) | 2003-04-22 |
CA2409127C (en) | 2007-08-28 |
KR100498528B1 (ko) | 2005-07-01 |
WO2001094679A3 (en) | 2002-08-22 |
AU2001268200B2 (en) | 2005-02-17 |
CZ20023984A3 (cs) | 2003-04-16 |
ATE480660T1 (de) | 2010-09-15 |
WO2001094679A8 (en) | 2003-10-23 |
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