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1.发明申请METHOD FOR PRODUCING PULP AND AT LEAST ONE ORGANIC LIQUID OR LIQUEFIABLE VALUABLE MATERIAL WITH EXHAUST GAS RECYCLING 审中-公开用于生产纸浆和至少一种有机液体或可液化WERTSTOFF带有废气再循环
公开(公告)号：WO2011138355A3
公开(公告)日：2012-01-12
申请号：PCT/EP2011057098
申请日：2011-05-04
Applicant: BASF SE , PROCHAZKA ROMAN , BITTERLICH STEFAN , DEUERLEIN STEPHAN , MACHHAMMER OTTO , KLINGLER DIRK , PANTOUFLAS EMMANOUIL
Inventor： PROCHAZKA ROMAN , BITTERLICH STEFAN , DEUERLEIN STEPHAN , MACHHAMMER OTTO , KLINGLER DIRK , PANTOUFLAS EMMANOUIL
CPC classification number: D21C3/02 , C10G1/02 , C10G2300/1014 , C10G2300/4081 , D21C11/0007 , D21C11/125 , Y02P30/20
Abstract: The present invention relates to an integrated method for producing pulp and at least one organic liquid or liquefiable valuable material, in which a) a lignocellulosic starting material is prepared and subjected to disruption with an aqueous-alkaline treatment medium, b) from the disrupted material a cellulose-enriched fraction and a cellulose-depleted black liquor are isolated, c) the black liquor is subjected to a treatment with at least one organic liquid or liquefiable valuable material and at least one exhaust gas stream being obtained, d) at least one of the exhaust gas streams of step c) is recirculated to the method for producing pulp and utilized.
Abstract translation: 本发明涉及一种用于生产纸浆和至少一种有机液体或可液化的可回收材料制成的集成方法，其中a）一个木素纤维素，其包括起始材料并进行消化用含水碱性处理介质，b）从所述消化的纤维素材料富集 馏分和纤维素贫化的黑液分离，c）将黑液的处理，以获得至少一种有机液体或的值可液化材料，和至少一个废气流，D）从步骤c的方法中的废气流）用于生产纸浆的至少一个引回和利用 ，
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2.发明申请METHOD FOR PRODUCING 1,2-PROPANDIOL BY LOW-PRESSURE HYDROGENATION OF GLYCERINE 审中-公开工艺制备1,2-丙二醇通过甘油的低压加氢
公开(公告)号：WO2009027502A3
公开(公告)日：2009-04-30
申请号：PCT/EP2008061387
申请日：2008-08-29
Applicant: BASF SE , HENKELMANN JOCHEM , PROCHAZKA ROMAN , BEY OLIVER , MAURER STEPHAN , STEINER JOCHEN , URTEL HEIKO , THEIS GERHARD , WAHL PETER , BECKER MICHAEL
Inventor： HENKELMANN JOCHEM , PROCHAZKA ROMAN , BEY OLIVER , MAURER STEPHAN , STEINER JOCHEN , URTEL HEIKO , THEIS GERHARD , WAHL PETER , BECKER MICHAEL
Abstract: The invention relates to a method for producing 1,2-propandiol, wherein a flow containing glycerine, in particular a flow produced on an industrial scale during the production of biodiesel, is subjected to low-pressure hydrogenation.
Abstract translation: 本发明涉及一种方法，用于生产1,2-丙二醇的方法，其包括使含有甘油的料流，特别是生物柴油流，低压加氢的制造过程中工业化生产。
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3.发明申请METHOD FOR PRODUCING 1,2-PROPANDIOL BY HYDROGENATING GLYCERINE IN A TWO-STEP REACTOR CASCADE 审中-公开用于生产1,2-丙二醇通过氢化甘油的两阶段反应器级联
公开(公告)号：WO2009027500A3
公开(公告)日：2009-05-07
申请号：PCT/EP2008061385
申请日：2008-08-29
Applicant: BASF SE , HENKELMANN JOCHEM , PROCHAZKA ROMAN , BEY OLIVER , MAURER STEPHAN , STEINER JOCHEN , URTEL HEIKO , THEIS GERHARD , WAHL PETER , MAIER PETRA , MEHRL GEORG
Inventor： HENKELMANN JOCHEM , PROCHAZKA ROMAN , BEY OLIVER , MAURER STEPHAN , STEINER JOCHEN , URTEL HEIKO , THEIS GERHARD , WAHL PETER , MAIER PETRA , MEHRL GEORG
CPC classification number: B01J23/83 , B01J23/002 , B01J35/0006 , B01J37/0203 , B01J37/18 , B01J2523/00 , C07C29/60 , C07C67/03 , Y02E50/13 , C07C31/205 , C07C69/24 , C07C69/52 , B01J2523/17 , B01J2523/31 , B01J2523/3706
Abstract: The invention relates to a method for producing 1,2-propandiol, wherein a flow containing glycerine, in particular a flow produced on an industrial scale during the production of biodiesel, is subjected to hydrogenation in a two-step reactor cascade.
Abstract translation: 本发明涉及一种方法，用于生产1,2-丙二醇的方法，其包括使含有甘油的料流，特别是在制造生物柴油料流的加氢在两阶段反应器级联中工业生产。
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4.发明申请METHOD FOR PRODUCING CYCLOHEXANE BY USING STARTING MATERIALS ORIGINATING FROM A STEAM CRACKING PROCESS 审中-公开用蒸汽裂解过程得到的提取物制备环己烷的方法
公开(公告)号：WO2014060460A3
公开(公告)日：2014-06-26
申请号：PCT/EP2013071601
申请日：2013-10-16
Applicant: BASF SE
Inventor： TSCHIRSCHWITZ STEFFEN , WISSEL-STOLL KATHRIN , BÜRKLE JOCHEN , KOSTOVA ALBENA , SCHMITT MARKUS , WLOKA VERONIKA , DEUERLEIN STEPHAN , BOSCH MARCO , OEHLENSCHLÄGER STEFFEN , SCHREIBER MICHAEL , AVERLANT GAUTHIER LUC MAURICE , JONI JONI , PROCHAZKA ROMAN , BOCK MARTIN , KINDLER ALOIS , MALKOWSKY DANIELA , SPUHL KATHARINA , BITTERLICH STEFAN , PFEIFFER DANIEL
CPC classification number: C07C5/10 , C07C5/29 , C07C2523/755 , C07C2527/125 , C07C2601/14 , C07C13/18
Abstract: The invention relates to a method for producing cyclohexane by isomerizing a hydrocarbon mixture (KG1) containing methylcyclopentane (MCP) in the presence of a catalyst. The catalyst is preferably an acidic ionic liquid. A flow (S1) originating from a steam cracking process is used as a starting material. The hydrocarbon mixture (KG1) is obtained from said stream (S1) in a device for removing aromatics. The hydrocarbon mixture has a reduced aromatic content in comparison with the flow (S1). (KG1) can also be (nearly) free of aromatics. In dependence on the type and amount of the aromatics remaining in the hydrocarbon mixture (KG1), in particular if benzene is present, a hydrogenation of (KG1) additionally can be performed before the isomerization. Furthermore, additional purification steps can optionally be performed before or after the isomerization or hydrogenation in dependence on the presence of other components of (KG1). Preferably high-purity cyclohexane (in accordance with specifications) is isolated from the hydrocarbon mixture (KG2) arising during the isomerization, wherein the specifications are given, for example, by the use of the cyclohexane for the production of caprolactam known to the person skilled in the art.
Abstract translation: 本发明涉及一种通过在催化剂存在下使含有甲基环戊烷（MCP）的烃混合物（KG1）异构化来制备环己烷的方法。 该催化剂优选为酸性离子液体。 使用的原料是来源于蒸汽裂化过程的物流（S1）。 从此流（S1），在一种用于具有降低的芳族含量相对于所述功率（S1），任选的（KG1）可以（几乎）是不含芳烃的芳烃分离而获得的烃类混合物（KG1）。 取决于残留在烃混合物（KG1）中的芳族化合物的性质和量，特别是在苯的存在下，（KG1）的氢化可以另外在异构化之前进行。 另外，取决于（KG1）的其它组分的存在，进一步的纯化步骤可以任选地在异构化或氢化之前或之后进行。 从异构化期间获得的烃混合物（KG2）优选是分离的高纯度（规格）环己烷，规格例如通过使用环己烷来制备己内酰胺以生产技术人员已知的。
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5.发明申请METHOD FOR PRODUCING 1,2-PROPANDIOL BY HYDROGENATING GLYCERINE IN AT LEAST THREE SUCCESSIVE REACTORS 审中-公开在至少三个反应器中氢化甘油制备1,2-丙二醇的方法
公开(公告)号：WO2009027501A2
公开(公告)日：2009-03-05
申请号：PCT/EP2008061386
申请日：2008-08-29
Applicant: BASF SE , HENKELMANN JOCHEM , PROCHAZKA ROMAN , BEY OLIVER , MAURER STEPHAN , STEINER JOCHEN , URTEL HEIKO , THEIS GERHARD , WAHL PETER
Inventor： HENKELMANN JOCHEM , PROCHAZKA ROMAN , BEY OLIVER , MAURER STEPHAN , STEINER JOCHEN , URTEL HEIKO , THEIS GERHARD , WAHL PETER
Abstract: The invention relates to a method for producing 1,2-propandiol, wherein a flow containing glycerine, in particular a flow produced on an industrial scale during the production of biodiesel, is subjected to hydrogenation in an at least three-step reactor cascade.
Abstract translation: 本发明涉及一种方法，用于生产1,2-丙二醇的方法，其包括使含有甘油的料流，特别是在制造生物柴油料流进行氢化以至少三阶段的反应器级联中工业生产。
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Patent Agency Ranking6.发明申请HYDROCARBON CONVERSION METHOD IN THE PRESENCE OF AN ACIDIC IONIC LIQUID WITH PRIOR HYDROGENATION 审中-公开烃转化方法在酸的离子液体与上游加氢PRESENCE
公开(公告)号：WO2014060462A3
公开(公告)日：2014-06-26
申请号：PCT/EP2013071604
申请日：2013-10-16
Applicant: BASF SE
Inventor： PROCHAZKA ROMAN , BOCK MARTIN , TSCHIRSCHWITZ STEFFEN , AVERLANT GAUTHIER LUC MAURICE , JONI JONI , SCHMITT MARKUS , SPUHL KATHARINA , BÜRKLE JOCHEN , KINDLER ALOIS , MALKOWSKY DANIELA , BITTERLICH STEFAN , HÜBNER MICHAEL
IPC: C07C5/00
CPC classification number: C07C5/29 , C07C5/10 , C07C2521/04 , C07C2523/46 , C07C2523/755 , C07C2527/125 , C07C2601/14 , C07C13/18
Abstract: The invention relates to a method for hydrocarbon conversion in the presence of an acidic ionic liquid. The hydrocarbon conversion is preferably an isomerization, in particular an isomerization of methylcyclopentane (MCP) to form cyclohexane. Before the hydrocarbon conversion, a hydrogenation is performed. Preferably, benzene is hydrogenated to form cyclohexane. The cyclohexane arising in the hydrogenation and/or isomerization is preferably isolated from the method. In a preferred embodiment of the invention, low boilers, in particular C5-C6 alkanes such as cyclopentane or isohexanes, are removed by distillation from the hydrocarbon mixture used for the hydrocarbon conversion after the hydrogenation and before the hydrocarbon conversion.
Abstract translation: 本发明涉及在酸性离子液体存在下进行烃转化的方法。 烃转化优选为异构化，特别是甲基环戊烷（MCP）异构化为环己烷。 在烃转化之前，进行氢化，优选将苯氢化成环己烷。 产生的氢化和/或异构化环己烷优选从该方法中分离出来。 在本发明的一个优选的实施方案中，氢化之后和之前的烃转化，尤其是之前的异构化，低沸点，且特别C5-C6烷烃，例如环戊烷或异己烷，从用于通过蒸馏的烃转化烃混合物中分离出来。
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7.发明申请
公开(公告)号：WO2011069933A3
公开(公告)日：2011-10-13
申请号：PCT/EP2010068911
申请日：2010-12-06
Applicant: BASF SE , MIRK DANIELA , SCHAPPERT CHRISTOPH , STABEL UWE , GAFFRON EBERHARDT , PROCHAZKA ROMAN
Inventor： MIRK DANIELA , SCHAPPERT CHRISTOPH , STABEL UWE , GAFFRON EBERHARDT , PROCHAZKA ROMAN
CPC classification number: B01J23/96 , B01J23/462 , B01J35/008 , B01J35/1019 , B01J35/1061 , B01J35/1066 , B01J35/1071 , B01J35/1076 , B01J35/109 , B01J38/06 , C07C5/10 , C07C2521/04 , C07C2521/08 , C07C2523/46 , C07C2601/14 , Y02P20/125 , Y02P20/52 , Y02P20/584 , C07C13/18
Abstract: The invention relates to a method for regenerating a supported hydrogenation catalyst containing ruthenium, wherein the catalyst is treated with steam and subsequently dried. The invention further relates to an integrated method for hydrogenating benzene to form cyclohexane in the presence of a supported catalyst containing ruthenium, comprising the catalyst regeneration steps in addition to the hydrogenation step.
Abstract translation: 一种负载型含钌氢化催化剂的再生方法，其中催化剂用蒸汽处理，然后干燥。 在含有钌的负载型催化剂存在下将苯氢化成环己烷的综合方法，除氢化步骤外还包括催化剂再生步骤。
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8.发明申请METHOD FOR HYDROGENATING GLYCERIN INTO 1,2-PROPANEDIOL HYDROGENATING DESULFURIZATION IN A SACRIFICIAL BED 审中-公开过程作为甘油与1,2-丙二醇加氢 - 加氢脱硫床上受害者
公开(公告)号：WO2010146117A2
公开(公告)日：2010-12-23
申请号：PCT/EP2010058543
申请日：2010-06-17
Applicant: BASF SE , PROCHAZKA ROMAN , MAURER STEPHAN , BEY OLIVER , STEINER JOCHEN , HENKELMANN JOCHEM , THEIS GERHARD , WAHL PETER
Inventor： PROCHAZKA ROMAN , MAURER STEPHAN , BEY OLIVER , STEINER JOCHEN , HENKELMANN JOCHEM , THEIS GERHARD , WAHL PETER
IPC: C07C29/60
CPC classification number: C07C29/60 , C07C29/90 , C07C31/205 , C07C31/225
Abstract: The present invention relates to a method for producing 1,2-propanediol from glycerin, comprising at least the steps of: (A) providing a glycerin flow G1, (B) desulfurization of the glycerin flow G1 from step (A) by hydrogenating with hydrogen at a pressure of 50 300 bar in the presence of a catalyst in order to obtain a glycerin flow G2, and (C) hydrogenating the glycerin flow G2 from step (B) with hydrogen in the presence of a catalyst, in order to obtain 1,2-propanediol.
Abstract translation: 本发明涉及一种用于生产由甘油1,2-丙二醇的方法，包括至少如下步骤：（A）提供一种甘油流G1，在压力从步骤（A）通过用氢气氢化的甘油流G1的（B）脱硫 50 - 300巴，以获得在催化剂的存在下，以获得甘油流G2与从步骤（B）的甘油流G2的（C）氢化与氢气在催化剂的存在下，以产生1,2-丙二醇。
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公开(公告)号：BRPI0815971A2
公开(公告)日：2015-02-18
申请号：BRPI0815971
申请日：2008-08-29
Applicant: BASF SE
Inventor： HENKELMANN JOCHEM , PROCHAZKA ROMAN , BEY OLIVER , MAURER STEPHAN , STEINER JOCHEN , URTEL HEIKO , THEIS GERHARD , WAHL PETER , MAIER PETRA , MEHRL GEORG
Abstract: The present invention relates to a process for preparing 1,2-propanediol, in which a glycerol-containing stream, especially a stream obtained on the industrial scale in the production of biodiesel, is subjected to a hydrogenation in a two-stage reactor cascade.
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10.发明专利
公开(公告)号：PL2200958T3
公开(公告)日：2016-04-29
申请号：PL08803383
申请日：2008-08-29
Applicant: BASF SE
Inventor： HENKELMANN JOCHEM , PROCHAZKA ROMAN , BEY OLIVER , MAURER STEPHAN , STEINER JOCHEN , URTEL HEIKO , THEIS GERHARD , WAHL PETER , MAIER PETRA , MEHRL GEORG
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