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    PETROLEUM DISTILLATION METHOD AND SYSTEM
    101.
    发明申请
    PETROLEUM DISTILLATION METHOD AND SYSTEM 审中-公开
    石油蒸馏方法和系统

    公开(公告)号：WO0151588A8

    公开(公告)日：2001-11-01

    申请号：PCT/US0101049

    申请日：2001-01-12

    Applicant: FOXBORO CO ,  KARG RANDAL W ,  CLINKSCALES THOMAS A

    Inventor： KARG RANDAL W ,  CLINKSCALES THOMAS A

    IPC: B01J19/00 ,  C10G7/12

    CPC classification number: B01J19/0006 ,  B01J19/0033 ,  B01J2219/00168 ,  B01J2219/00186 ,  C10G7/12 ,  G01N24/08 ,  G01N24/085 ,  G01R33/4625

    Abstract: In a distillation control system, a nuclear magnetic resonance (NMR) sensor identifies the composition of petroleum distillates from a distillation tower, and preferably also identifies the composition of the input feed method. This information is processed to obtain estimates of values of selected properties of the distillates and the feed. These values are provided to a multivariate controller, together with a setpoint of desired quality factors selected on the basis of competitive market forces, environmental regulations and economic factors including feed and product prices and operating cost. On the basis of the NMR measured values of selected quality properties, the multivariate controller generates values of manipulated operating variables that, when applied to the distillation system, adjust the distillation operation to reduce differences between the controlled variables and their respective setpoints. The ultimate values of the operating variables are determined, preferably in conjunction with an optimizer so that product qualities are maintained and the tower is operated in an economically optimum manner subject to specific characteristics of the refinery.

    Abstract translation: 在蒸馏控制系统中，核磁共振（NMR）传感器识别来自蒸馏塔的石油馏分的组成，并且优选还识别输入进料方法的组成。 处理这些信息以获得馏出物和原料选定性质的估计值。 这些值被提供给一个多变量控制器，以及根据竞争市场力量，环境法规和经济因素（包括饲料和产品价格以及运营成本）选择的理想质量因素的设定值。 根据选定质量特性的NMR测量值，多变量控制器生成操作操作变量的值，当操作变量应用于蒸馏系统时，调整蒸馏操作以减小控制变量与其相应设定值之间的差异。 确定操作变量的最终值，优选与优化器一起确定，从而保持产品质量，并且根据精炼厂的特定特性以经济优化的方式操作塔。

    METHOD AND SYSTEM FOR CONTROLLING A FLUID CATALYTIC CRACKER
    102.
    发明申请
    METHOD AND SYSTEM FOR CONTROLLING A FLUID CATALYTIC CRACKER 审中-公开
    用于控制流体催化裂化器的方法和系统

    公开(公告)号：WO01051589A1

    公开(公告)日：2001-07-19

    申请号：PCT/US2001/001068

    申请日：2001-01-12

    IPC: B01J19/00 ,  C10G7/12 ,  C10G11/18 ,  B01J8/00

    CPC classification number: B01J19/0006 ,  B01J19/0033 ,  B01J2219/00168 ,  B01J2219/00186 ,  C10G7/12 ,  G01N24/08 ,  G01N24/085 ,  G01R33/4625

    Abstract: A method for controlling the output of a distillation tower fed by a fluid catalytic cracker uses one or more NMR sensors to obtain on-line measurements of values of selected properties of feedstock and/or of distillation tower outputs. The measured values are provided to a multivariate controller. On the basis of the measured values and setpoint information provided by an optimizer, the multivariate controller determines values of manipulated variables for controlling the catalytic cracker to produce products of desired qualities and maximize unit economic return.

    Abstract translation: 用于控制由流化催化裂化器供给的蒸馏塔的输出的方法使用一个或多个NMR传感器来获得原料和/或蒸馏塔输出的选定性质的值的在线测量。 将测量值提供给多变量控制器。 基于由优化器提供的测量值和设定点信息，多变量控制器确定用于控制催化裂化器的操作变量的值以产生期望质量的产物并且最大化单位经济回报。

    TEMPERATURE CONTROLLED REACTION VESSEL
    104.
    发明申请
    TEMPERATURE CONTROLLED REACTION VESSEL 审中-公开
    温度控制反应器

    公开(公告)号：WO9857741A8

    公开(公告)日：1999-07-15

    申请号：PCT/US9812102

    申请日：1998-06-15

    Applicant: ARENCIBIA ASSOCIATES INC

    Inventor： ARENCIBIA JOSE P JR

    IPC: B01J19/00 ,  F28D1/06

    CPC classification number: B01J19/0013 ,  B01J19/0006 ,  B01J2219/00078 ,  B01J2219/0009 ,  B01J2219/00094 ,  B01J2219/00155 ,  F28D1/06

    Abstract: A novel reaction vessel apparatus (110) is provided. The reaction vessel (110) includes internally placed temperature controlling thermal probes (400) in which liquid is boiled. The energy of vaporization is supplied by the reaction vessel contents. The vapor produced by the boiling may be directed to channel coils (100) which surround the outside of the reaction vessel wall (120). The channel coils (100) contact the outside wall (120) of the reaction vessel (110) perpendicularly, and provide mechanical support for the reaction vessel. The mechanical support from the channel coils (100) allows for a decrease in the thickness of the reaction vessel wall (120) and corresponding increased heat transfer efficiency between the channel coil contents and the reaction vessel contents. The entire above described apparatus is enclosed within an evacuated shell (300) which provides additional insulation.

    Abstract translation: 提供了一种新的反应容器装置（110）。 反应容器（110）包括内部放置的温度控制热探针（400），其中液体被煮沸。 蒸发能量由反应容器内容物提供。 通过沸腾产生的蒸气可以被引导到围绕反应容器壁（120）外部的通道线圈（100）。 通道线圈（100）垂直地与反应容器（110）的外壁（120）接触，并为反应容器提供机械支撑。 来自通道线圈（100）的机械支撑件允许反应容器壁（120）的厚度减小，并且相应地增加了通道线圈内容物和反应容器内容物之间的传热效率。 整个上述装置被封装在提供额外绝缘的真空壳（300）内。

    METHOD AND APPARATUS FOR MEASUREMENT OF CVD EXHAUST DEPOSITS
    106.
    发明申请
    METHOD AND APPARATUS FOR MEASUREMENT OF CVD EXHAUST DEPOSITS 审中-公开
    CVD排除沉积物的测量方法和装置

    公开(公告)号：WO98055667A1

    公开(公告)日：1998-12-10

    申请号：PCT/US1998/010572

    申请日：1998-05-21

    IPC: B01J15/00 ,  B01J19/00 ,  C23C16/44 ,  B01J3/02

    CPC classification number: C23C16/4412 ,  B01J15/00 ,  B01J19/0006

    Abstract: A method and system for quantifying the amount of byproduct buildup in the reaction chamber and support systems used to fabricate semiconductor device layers is disclosed. One embodiment of the present invention places a film thickness measuring device in an exhaust pipe (150) of a reactor (100). The film thickness measuring device is positioned such that the operating parameters, for example temperature, of that particular device are optimized. The thickness of the exhaust byproduct buildup is then measured using the film thickness measuring device. Once the amount of byproduct buildup is quantified at the location of the film thickness measuring device then the byproduct buildup at other locations in the system be determined.

    Abstract translation: 公开了一种用于量化用于制造半导体器件层的反应室和支撑系统中的副产物积累量的方法和系统。 本发明的一个实施例将膜厚测量装置放置在反应器（100）的排气管（150）中。 膜厚测量装置被定位成使得该特定装置的操作参数，例如温度被优化。 然后使用膜厚测量装置测量排气副产物积累的厚度。 一旦在膜厚测量装置的位置量化了副产物积累的量，则确定系统中其他位置处的副产物积累。

    GAS GENERATING SYSTEM AND METHOD
    107.
    发明申请
    GAS GENERATING SYSTEM AND METHOD 审中-公开
    气体发生系统和方法

    公开(公告)号：WO98046346A1

    公开(公告)日：1998-10-22

    申请号：PCT/US1998/007738

    申请日：1998-04-14

    IPC: C01B3/38 ,  B01J8/00 ,  B01J19/00 ,  C01B3/32 ,  H01M8/06

    CPC classification number: C01B3/32 ,  B01J8/001 ,  B01J19/0006 ,  H01M8/0612

    Abstract: A system (10) for generating a desired output gas (S) from an input fuel (F) for use in a downstream process (12) is disclosed. The system includes a plurality of fuel processing units (14) to generate the desired output gas (5), wherein each of the plurality of fuel processing units (14) includes a reformer which uses waste gas output (G) from the downstream process (12) to facilitate the processing of the fuel. Each of the fuel processing units is operational over a range up to full capacity, wherein the plurality of fuel processing units are interconnected in a collective operating scheme to process the fuel. A control system (16) is provided for controlling the plurality of fuel processing units (14) in response to requirements of a dynamic load demand (LS) from the downstream operation (12). The control system (16) is operative to adjust the operational level of each of the plurality of fuel processing units (14) to produce individual responses from each of the fuel processing units. The individual responses are combined to produce a collective response for meeting the requirements of the dynamic load demand. A method for generating a desired output gas from an input fuel for use in a downstream process is also provided.

    Abstract translation: 公开了一种用于从用于下游过程（12）的输入燃料（F）产生期望输出气体（S）的系统（10）。 该系统包括多个燃料处理单元（14）以产生所需的输出气体（5），其中多个燃料处理单元（14）中的每一个包括使用来自下游过程的废气输出（G）的重整器 12）以便于燃料的加工。 每个燃料处理单元在一直到满容量的范围内操作，其中多个燃料处理单元以集体操作方案相互连接以处理燃料。 提供控制系统（16），用于响应来自下游操作（12）的动态负载需求（LS）的要求来控制多个燃料处理单元（14）。 控制系统（16）可操作以调节多个燃料处理单元（14）中的每个燃料处理单元（14）的操作水平，以产生来自每个燃料处理单元的各个响应。 将各个响应组合起来以产生满足动态负载需求要求的集体响应。 还提供了用于从下游处理中使用的输入燃料产生期望输出气体的方法。

    HEAT EXCHANGER ADAPTED FOR THE PRODUCTION OF CARBON BLACK
    108.
    发明申请
    HEAT EXCHANGER ADAPTED FOR THE PRODUCTION OF CARBON BLACK 审中-公开
    热交换器适用于生产炭黑

    公开(公告)号：WO1997021065A1

    公开(公告)日：1997-06-12

    申请号：PCT/SE1996001575

    申请日：1996-11-29

    Applicant: EDMESTON AB

    Inventor： EDMESTON AB ,  BERGLUND, Göran ,  ERIKSSON, Ulf

    IPC: F28F09/00

    CPC classification number: C09C1/50 ,  B01J19/0006 ,  F28D7/16 ,  F28F9/00 ,  F28F2265/26

    Abstract: A tube heat exchanger intended to be used for the production of carbon black, comprises a cylindrical chamber (16) which is enclosed by a cylindrically shaped outer shell wall (14') and two end walls (17, 18), and a plurality of tubes (13') which extend through the entire cylindrically shaped chamber (16), from one end wall to the other. To the heat exchanger are provided an inlet (1') and an outlet (25) for gas intended to flow on the outside of the tubes (13'). Moreover, the heat exchanger comprises a further shell wall (23), which is cylindrical and placed inside and concentrically with the outer shell wall (14'), so that a cylindrically shaped gap space (29), which is open at both ends, is formed between the two shell walls. The gas entering through the inlet (1') passes this gap space (29) before it comes into contact with the tubes (13'). The advantage of this is that the outer shell wall is cooled and that the amount of carbon precipitations within the tubes diminishes.

    Abstract translation: 用于生产炭黑的管式热交换器包括由圆柱形外壳壁（14'）和两个端壁（17,18）包围的圆柱形腔室（16），以及多个 从整个圆柱形腔室（16）延伸的管（13'），从一个端壁到另一个端壁。 为热交换器设置有用于在管（13'）的外侧流动的气体的入口（1'）和出口（25）。 此外，热交换器包括另外的壳壁（23），该壳壁是圆柱形的并且放置在外壳壁（14'）的内部并同心地设置，使得在两端敞开的圆柱形间隙空间（29） 形成在两个壳壁之间。 通过入口（1'）进入的气体在与管（13'）接触之前通过该间隙空间（29）。 其优点是外壳壁被冷却，并且管内的碳沉淀量减少。

    METHOD FOR CONTROLLING CHEMICAL SYNTHESIS PROCESSES
    110.
    发明申请
    METHOD FOR CONTROLLING CHEMICAL SYNTHESIS PROCESSES 审中-公开
    用于控制化学合成方法的方法

    公开(公告)号：WO1996041822A1

    公开(公告)日：1996-12-27

    申请号：PCT/EP1996002408

    申请日：1996-06-01

    Applicant: SOLVAY (SOCIETE ANONYME) ,  DE SELLIERS, Jacques

    Inventor： SOLVAY (SOCIETE ANONYME)

    IPC: C08F10/00

    CPC classification number: G05B13/048 ,  B01J19/0006 ,  C08F10/00 ,  C08F2400/02 ,  G05B11/32 ,  Y02P20/582 ,  C08F2/00

    Abstract: A method for controlling a process for synthesising at least one chemical in a plant including at least one reactor (R) that may be considered as a perfectly mixed reactor, wherein control variables (GC) enable the process to be controlled so that a number of variables known as controlled variables (GR) and related to the properties of the product and/or the operation of the process match corresponding set values (CGR). Said method comprises the steps of (a) inputting set values for the controlled variables (CGR); (b) using a prediction unit (OP) to calculate predictions of the controlled variables (PGR) on the basis of measurements of the process control variables (MGC); (c) using a control unit (OC) to calculate set values for the process control variables (CGC) on the basis of the set values (CGR) and predictions (PGR) of the controlled variables; and (d) transmitting set values for the process control variables (CGC) to process control actuators. The prediction unit (OP) is based on a mathematical process model known as a direct model (M), and designed in such a way that the mass MXR of at least one component (X) in the reactor (R) is predicted by means of the equation MXR = LAG (FXRin . tau X, tau X), wherein FXRin is the mass flow rate of component X at the inlet of the reactor R, tau X is the dwell time of x in the reactor, and the function y = LAG (u, tau ) is the solution of the differential equation tau . dy/dt + y, calculated with the instantaneous value of u and tau as well as with the last calculated value of y.

    Abstract translation: 一种用于控制合成工厂中至少一种化学物质的方法，该方法包括可被认为是完全混合的反应器的至少一个反应器（R），其中控制变量（GC）使得该过程能够被控制，使得多个 被称为受控变量（GR）的变量与产品属性和/或过程的操作相关的变量与相应的设定值（CGR）相匹配。 所述方法包括以下步骤：（a）输入控制变量（CGR）的设定值; （b）使用预测单元（OP）基于过程控制变量（MGC）的测量来计算受控变量（PGR）的预测; （c）使用控制单元（OC）根据控制变量的设定值（CGR）和预测（PGR）来计算过程控制变量（CGC）的设定值; 和（d）将过程控制变量（CGC）的设定值发送到过程控制执行器。 预测单元（OP）基于称为直接模型（M）的数学过程模型，并且被设计成使得反应器（R）中的至少一个组分（X）的质量MXR通过手段预测 方程式MXR = LAG（FXRin.TX X，τX），其中FXRin是反应器R入口处的组分X的质量流率，τX是反应器中x的停留时间，函数y = LAG（u，τ）是微分方程tau的解。 dy / dt + y，用u和tau的瞬时值以及最后计算的y计算。

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