公开(公告)号：WO2013174985A2

公开(公告)日：2013-11-28

申请号：PCT/EP2013/060754

申请日：2013-05-24

Applicant: FMC KONGSBERG SUBSEA AS

Inventor： TUVNES, Henrik, Johan ,  MIKKELSEN, René ,  ELLINGSEN, Haakon

CPC classification number: B01D19/0052 ,  B01D17/00 ,  B01D17/0214 ,  B01D17/0217 ,  B01D17/044 ,  B01D19/0063 ,  B01D19/0068 ,  B01D45/16 ,  E21B43/34 ,  E21B43/36

Abstract: The present invention concerns a gas-liquid separation system and a method for operating gas-liquid separation the system.

Abstract translation: 本发明涉及气液分离系统和操作气液分离系统的方法。

公开(公告)号：WO2010126717A1

公开(公告)日：2010-11-04

申请号：PCT/US2010/031215

申请日：2010-04-15

Applicant: NATIONAL TANK COMPANY ,  SAMS, Gary W.

Inventor： SAMS, Gary W.

IPC: C10G33/00

CPC classification number: B01D17/042 ,  B01D17/044 ,  B01D17/06 ,  C10G33/04

Abstract: A method for treating an interface rag includes the steps of removing a volume of rag at a controlled rate from an upstream rag source and passing the rag through a high pressure pump and a heater. The heater heats the rag to a temperature of at least 350°F to thermally decomposing any chemicals that had been added to the interface rag to promote separation. Diluent is then mixed with the heated rag to cool the rag to a temperature less than 300°F and produce a 30 API rag. The cooled diluted rag is then treated in an electrostatic treater or sent directly to a hydrocyclone cluster. The electrostatic treater is preferably a vertical electrostatic treater with a conical-shaped lower portion and a means for agitating the solid-laden water within the treater to prevent the solids from settling on the bottom of the treater.

Abstract translation: 用于处理界面抹布的方法包括以下步骤：从上游抹布源以可控速率去除一批抹布，并将抹布通过高压泵和加热器。 加热器将抹布加热到至少350°F的温度，以热分解添加到界面抹布中的任何化学物质以促进分离。 然后将稀释剂与加热的抹布混合以将破布冷却至低于300°F的温度并产生30个API抹布。 然后将冷却的稀释的抹布在静电处理器中处理或直接发送到水力旋流器簇。 静电处理器优选是具有锥形下部的垂直静电处理器和用于搅拌处理器内的固体含水的装置，以防止固体沉淀在处理器的底部。

公开(公告)号：WO2010088127A2

公开(公告)日：2010-08-05

申请号：PCT/US2010/021613

申请日：2010-01-21

Applicant: TRISTAR PRODUCTS AG ,  DAVIS, John, Henry

Inventor： DAVIS, John, Henry

IPC: C11B1/10

CPC classification number: C11B3/006 ,  B01D17/042 ,  B01D17/044 ,  B01D17/047 ,  C11B1/10

Abstract: An apparatus and method for extracting oils and fats from oil-bearing substances without using degrading temperatures. The apparatus may comprise an extraction chamber containing an oil-bearing substance, an oil-collecting chamber, a recovery pump, a first jacket adjacent at least a portion of the extraction chamber, and a second jacket adjacent at least a portion of the oil-collecting chamber. The method involves heating a solvent and reducing pressure to facilitate a low-temperature vacuum boil, delivering the heated solvent into the extraction chamber configured to facilitate the low-temperature vacuum boil of the solvent within the extraction chamber, pumping the solvent in vapor form out of the extraction chamber with the recovery pump, delivering the oil and fat extracted in the extraction chamber to the oil-collecting chamber, pumping solvent in vapor form out of the oil-collecting chamber with the recovery pump, and delivering the solvent received by the recovery pump to the first and second jackets to provide heat to the chambers.

Abstract translation: 用于在不使用降解温度的情况下从含油物质提取油和脂肪的装置和方法。 该设备可以包括含有含油物质的萃取室，采油室，回收泵，与萃取室的至少一部分相邻的第一外壳和邻近至少一部分含油物质的第二外壳， 收集室。 该方法包括加热溶剂并降低压力以促进低温真空煮沸，将加热后的溶剂输送到提取室中，该提取室被配置为便于提取室内的溶剂的低温真空煮沸，将蒸汽形式的溶剂泵出 将萃取室中萃取的油脂输送到油收集室，用回收泵将蒸汽形式的溶剂从油收集室抽出，并将由该萃取室接收的溶剂 回收泵送到第一和第二夹套，为腔室提供热量。

公开(公告)号：WO2008107696A3

公开(公告)日：2008-11-06

申请号：PCT/GB2008000815

申请日：2008-03-07

Applicant: PETROLEO BRASILEIRO SA ,  BENSON JOHN EVERETT ,  COUTINHO RAQUEL CAMPOS ,  HEREDIA MONTSERRAT FORTUNY ,  DE SOUZA MARCIO NELE ,  SANTOS ALEXANDRE FERREIRA

Inventor： COUTINHO RAQUEL CAMPOS ,  HEREDIA MONTSERRAT FORTUNY ,  DE SOUZA MARCIO NELE ,  SANTOS ALEXANDRE FERREIRA

IPC: B01D17/02 ,  B01D17/04 ,  B01J19/10 ,  C10G32/02 ,  C10G33/00 ,  C10G33/02 ,  C10G33/08

CPC classification number: C10G32/02 ,  B01D17/04 ,  B01D17/042 ,  B01D17/044 ,  C10G33/02

Abstract: A method is described for the microwave emulsion treatment of water-in-oil (W/O) emulsions, said method comprising the steps of a) in the laboratory, determining, for an W/O emulsion (604), (705), (713), (805), (812) the optimum conditions of the variables: water content, salt content, pH value of the aqueous phase, initial temperature, microwave application power, final temperature and drop size distribution to be adjusted in the industrial plant, as a function of the features of the tested crude oil such as viscosity, density, asphaltene content, total acidity, such conditions being those required for obtaining at least 90% separation efficiency of said emulsion in the presence of microwave radiation: b) utilizing such information for the initial adjustment of application conditions of the said method to phase separation units in refineries and production units; c) perform on line tests of the variables of step a) of the process response in the streams effluent from separation units, being said response the water content and salt content tests, so as to feedback the information to the best adjustment of the process conditions for microwave application; and d) additionally, utilizing the on line or laboratory tests of the effect of the method as a tool for the monitoring of the efficiency of the breaking of the W/O emulsion.

Abstract translation: 描述了用于微波乳液处理油包水（W / O）乳液的方法，所述方法包括以下步骤：a）在实验室中，对于W / O乳液（604），（705）， （713），（805），（812）所述变量的最佳条件：水含量，盐含量，水相的pH值，初始温度，微波应用功率，最终温度和液滴尺寸分布 作为受试原油的特征如粘度，密度，沥青质含量，总酸度的函数，这些条件是在微波辐射存在下获得所述乳液的至少90％分离效率所需的条件：b） 利用这些信息将所述方法的应用条件初始调整到炼油厂和生产单元中的相分离装置; c）对来自分离单元的流出物中的过程响应的步骤a）的变量进行在线测试，被称为响应含水量和盐含量测试，以便反馈信息以最佳调节过程条件 用于微波应用; 和d）另外，利用该方法的效果的在线或实验室测试作为监测W / O乳液破坏效率的工具。

公开(公告)号：WO2006088826A3

公开(公告)日：2007-01-25

申请号：PCT/US2006005098

申请日：2006-02-13

Applicant: TOTAL SEPARATION SOLUTIONS LLC

Inventor： SMITH KEVIN W

IPC: E21B21/06 ,  B01D17/02 ,  B01D17/04 ,  E21B43/40

CPC classification number: E21B21/063 ,  B01D17/044 ,  B01D17/047

Abstract: A cavitation device is used to heat, concentrate and recycle or otherwise reuse dilute and other oil well fluids, brines and muds, and solution mining fluids, all of which commonly contain ingredients worthy of conservation. The cavitation device is powered by a Diesel engine whose exhaust may be used to heat the incoming fluid, and the product of the cavitation device is directed to a flash tank.

Abstract translation: 空化装置用于加热，浓缩和再循环或以其他方式重新利用稀释的其他油井液，盐水和泥浆以及溶液采矿液，所有这些通常都含有值得保护的成分。 空化装置由柴油发动机驱动，其排气可用于加热进入的流体，并且空化装置的产物被引导到闪蒸罐。

公开(公告)号：WO2002066137A1

公开(公告)日：2002-08-29

申请号：PCT/NO2002/000077

申请日：2002-02-22

Applicant: STATOIL ASA ,  SJØBLOM, Johan ,  KALLEVIK, Harald ,  WESTVIK, Arild ,  AUFLEM, Inge, Harald

Inventor： SJØBLOM, Johan ,  KALLEVIK, Harald ,  WESTVIK, Arild ,  AUFLEM, Inge, Harald

IPC: B01D17/04

CPC classification number: B01D19/0036 ,  B01D17/0205 ,  B01D17/0208 ,  B01D17/044 ,  B01D17/047 ,  B01D19/0005

Abstract: Process for separation of oil, water and gas in a separator by breaking of water-in-oil emulsions in a composition comprising a water, oil and optionally a gaseous phase, including the following steps: a) dissolving a gas comprising one or more components into said composition prior to said operator, wherein the amount of said water phase is at least about 1 weight-% based on total composition, b) introducing said composition into said separator, wherein pressure in said separator is of at least about 2 bar, and c) reducing the pressure in said separator in order to facilitate the separation of oil, water and the optional gaseous phase.

Abstract translation: 通过在包含水，油和任选的气相的组合物中破坏油包水乳液来分离分离器中的油，水和气体的方法，包括以下步骤：a）将包含一种或多种组分 在所述操作者之前加入所述组合物，其中基于总组合物，所述水相的量为至少约1重量％，b）将所述组合物引入所述分离器中，其中所述分离器中的压力为至少约2巴， 和c）降低所述分离器中的压力以便于油，水和任选的气相的分离。

公开(公告)号：WO9854441A3

公开(公告)日：1999-03-18

申请号：PCT/GB9801556

申请日：1998-05-28

Applicant: KVAERNER PROCESS SYSTEMS AS ,  HAYS LANCE GREGORY ,  DAVIES SIMON ROGER HENDERSON

Inventor： HAYS LANCE GREGORY ,  DAVIES SIMON ROGER HENDERSON

IPC: B01D17/00 ,  B01D19/00 ,  E21B43/34 ,  B01D17/02 ,  B01D17/04 ,  E21B43/40

CPC classification number: E21B43/34 ,  B01D17/00 ,  B01D17/0217 ,  B01D17/044 ,  B01D17/047 ,  B01D17/12 ,  B01D19/0052 ,  B01D19/0068

Abstract: A process and apparatus for separating fluids of different density, primarily gas, oil and water from an oil well production flow (12), including a rotary separation turbine (11) separating at least the gas phase, but preferably also the liquid phases, and preferably returning water (16) to the separation step to increase the water cut of the mixture being separated.

公开(公告)号：WO99000352A1

公开(公告)日：1999-01-07

申请号：PCT/US1998/012202

申请日：1998-06-12

IPC: C12P7/54 ,  B01D11/04 ,  B01D17/00 ,  B01D17/04 ,  C07C51/48 ,  C07C53/08 ,  C07C55/10 ,  C07C59/08 ,  C12P7/40

CPC classification number: B01D17/042 ,  B01D11/0457 ,  B01D17/00 ,  B01D17/0211 ,  B01D17/0214 ,  B01D17/041 ,  B01D17/044 ,  B01D17/045 ,  B01D17/047 ,  B01D17/048 ,  C07C51/48 ,  C07C53/08

Abstract: Dilute solutions of fermentation sales may be concentrated by extracting water using low-miscibility, low-molecular-weight secondary and tertiary amines, e.g. triethylamine (TEA), diisopropyl amine (DIA), N,N-diethylmethylamine (DEMA), and mixtures thereof. At 30 DEG C-55 DEG C, which coresponds to typical fermentation temperatures, these low-molecular-weight amines or their mixtures, can extract large amounts of water from dilute aqueous solutions containing fermentation salts. Thus, dilute fermentation salt solutions can be concentrated by selectively removing water. At these low temperatures, the amine phase contains 20-35 % water and a much reduced quantity of fermentation salt. When the temperature is raised, water phases out of the amine, allowing the amine to be recycled and reused to extract additional water. Using this approach, about 82,5 % of water can be removed from a 3 % dilute solution using conventional multistage, countercurrent extraction, thus providing a 15 % concentrated fermentation salt solution.

Abstract translation: 发酵销售的稀释溶液可以通过使用低混溶性，低分子量仲胺和叔胺例如水， 三乙胺（TEA），二异丙胺（DIA），N，N-二乙基甲胺（DEMA）及其混合物。 这些低分子量胺或其混合物在30℃-55℃下对应于典型的发酵温度，可以从含有发酵盐的稀释水溶液中提取大量的水。 因此，可以通过选择性除去水来浓缩稀释的发酵盐溶液。 在这些低温下，胺相含有20-35％的水和大量减少的发酵盐。 当温度升高时，水从胺中脱出，允许胺再循环并重新使用以提取额外的水。 使用这种方法，可以使用常规的多级逆流萃取，从3％稀释溶液中除去约82.5％的水，从而提供15％浓缩的发酵盐溶液。

公开(公告)号：WO98054441A2

公开(公告)日：1998-12-03

申请号：PCT/GB1998/001556

申请日：1998-05-28

IPC: B01D17/00 ,  B01D19/00 ,  E21B43/34 ,  E21B43/40 ,  B01D17/02 ,  B01D17/04

CPC classification number: E21B43/34 ,  B01D17/00 ,  B01D17/0217 ,  B01D17/044 ,  B01D17/047 ,  B01D17/12 ,  B01D19/0052 ,  B01D19/0068

Abstract: A process and apparatus for separating fluids of different density, primarily gas, oil and water from an oil well production flow (12), including a rotary separation turbine (11) separating at least the gas phase, but preferably also the liquid phases, and preferably returning water (16) to the separation step to increase the water cut of the mixture being separated.

Abstract translation: 一种用于从油井生产流（12）中分离不同密度的流体（主要是气体，油和水）的方法和装置，包括至少分离气相，但优选液相的旋转分离涡轮机（11），以及 优选将水（16）返回到分离步骤以增加待分离的混合物的水分。

公开(公告)号：WO1998019764A1

公开(公告)日：1998-05-14

申请号：PCT/US1997020117

申请日：1997-11-05

Applicant: SEPARATHERM, INC.

Inventor： SEPARATHERM, INC. ,  BRYANT, William, H. ,  FRAZIER, Jerry, W.

IPC: B01D17/00

CPC classification number: B01D21/2488 ,  B01D17/00 ,  B01D17/0211 ,  B01D17/0214 ,  B01D17/042 ,  B01D17/044 ,  B01D17/047 ,  B01D17/12 ,  B01D21/00 ,  B01D21/0006 ,  B01D21/0039 ,  B01D21/009 ,  B01D21/16 ,  B01D21/2427 ,  B01D21/245 ,  B01D21/34

Abstract: A method and apparatus for processing contaminated material are provided. The apparatus is intended to process many types of contaminated material, all of which consist of: one or more hydrocarbons, and water and/or one or more inert solids. The objective of the invention is to reduce waste disposal costs by separating the ingredients of the contaminated material (i.e., hydrocarbons, and water and/or inert solids) and directing the separated ingredients to distinct containers. The apparatus broadly comprises a coalescer unit, an organics recovery unit, and a solids separation unit. The contaminated material is first heated and blended into a coalescent slurry by the coalescer unit. The coalesced slurry is then processed by the organics recovery unit which separates the hydrocarbons, solids and water from one another based upon their respective specific gravities. The hydrocarbons are discharged from the organics recovery unit into a hydrocarbon recovery container. The solids and water are discharged to the solids separation unit. The solids are discharged from the solids separation unit into a solids recovery container. The water is pumped from the solids separation unit to a water recovery container.

Abstract translation: 提供了一种处理污染物质的方法和装置。 该装置旨在处理许多类型的受污染的材料，其全部由以下组成：一种或多种烃，以及水和/或一种或多种惰性固体。 本发明的目的是通过分离被污染物质的成分（即烃，水和/或惰性固体）并将分离的成分引导到不同的容器来减少废物处理成本。 该设备广泛地包括聚结器单元，有机物回收单元和固体分离单元。 被污染的材料首先被加热并通过聚结器单元共混成聚结浆料。 合并后的浆料然后由有机物回收单元处理，该单元基于它们各自的比重将烃，固体和水彼此分离。 烃从有机物回收装置排出到烃回收容器中。 固体和水被排出到固体分离单元。 固体从固体分离单元排出到固体回收容器中。 水从固体分离单元泵送到水回收容器。