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1. 发明申请

US20130075333A1 Apparatus and Process for Treatment of Water 审中-公开
标题翻译：水处理设备及工艺
公开(公告)号：US20130075333A1
公开(公告)日：2013-03-28
申请号：US13624830
申请日：2012-09-21
申请人： Randall B. Pruet , De Quang Vu , Prakhar Prakash
发明人： Randall B. Pruet , De Quang Vu , Prakhar Prakash
IPC分类号： C02F9/12 , C02F1/34 , C02F1/38 , B23P17/04 , C02F1/463 , C02F9/02 , B01D21/02 , C02F1/04 , C02F1/44
CPC分类号： B01D61/364 , B01D61/002 , B01D61/145 , B01D61/58 , B01D63/02 , B01D71/024 , C02F1/444 , C02F1/445 , C02F1/447 , C02F1/463 , C02F9/00 , C02F2209/06 , C02F2209/10 , C02F2209/20 , Y10T29/494
摘要： The invention relates to a system for use in the treatment of produced water, e.g., water treatment in connection with hydrocarbon production operations. Silica in produced water produces undesirable scaling in processing equipment, which causes excess energy usage and maintenance problems. Electrocoagulation (EC) at relatively high water temperature, followed by any of membrane distillation (MD) or forward osmosis (FO), may be combined with a process of ceramic ultra-filtration (UF filtration) to treat water. Water to be treated may be produced water that has been pumped from a subterranean reservoir. The treated water may be employed to generate steam. The system comprises a plurality of units (e.g., EC, forward osmosis, membrane distillation unit, UF filtration, etc) which can be configured as an on-site installation or a mobile unit for on-site or off-site water treatment.
摘要翻译：本发明涉及一种用于处理生产水的系统，例如与碳氢化合物生产操作有关的水处理。生产水中的二氧化硅在加工设备中产生不希望的结垢，导致能量消耗过多和维护问题。在相对较高的水温下进行电凝（EC），随后是膜蒸馏（MD）或正向渗透（FO）的任何一种，可以与陶瓷超滤（UF过滤）的方法结合来处理水。待处理的水可以产生已经从地下储层泵送的水。处理过的水可用于产生蒸汽。该系统包括可以配置为现场安装的多个单元（例如EC，正向渗透，膜蒸馏单元，UF过滤等），或用于现场或非现场水处理的移动单元。

2. 发明申请

US20130075335A1 Apparatus and Process For Treatment of Water 有权
标题翻译：水处理设备及工艺
公开(公告)号：US20130075335A1
公开(公告)日：2013-03-28
申请号：US13624846
申请日：2012-09-21
申请人： Prakhar Prakash , James Craig Pauley , Randall B. Pruet
发明人： Prakhar Prakash , James Craig Pauley , Randall B. Pruet
IPC分类号： C02F9/12
CPC分类号： B01D61/364 , B01D61/002 , B01D61/145 , B01D61/58 , B01D63/02 , B01D71/024 , C02F1/444 , C02F1/445 , C02F1/447 , C02F1/463 , C02F9/00 , C02F2209/06 , C02F2209/10 , C02F2209/20 , Y10T29/494
摘要： The invention relates to the treatment of water, including for example treatment in connection with hydrocarbon production operations. Silica in water produces undesirable scaling in processing equipment, which causes excess energy usage and maintenance problems. Electrocoagulation (EC) at relatively high water temperature followed by ultra-filtration (UF filtration) may be combined with forward osmosis (FO) to treat water. Water to be treated may be produced water that has been pumped from a subterranean reservoir. The treated water may be employed to generate steam. The treatment units (e.g., EC, forward osmosis, UF filtration, etc) can be configured into one system as an on-site installation or a mobile unit for on-site or off-site water treatment.
摘要翻译：本发明涉及水的处理，包括例如与碳氢化合物生产操作有关的处理。水中的二氧化硅在加工设备中产生不希望的结垢，这导致过多的能量消耗和维护问题。在相对较高的水温下进行电凝（EC），然后进行超滤（UF过滤）可与正向渗透（FO）组合以处理水。待处理的水可以产生已经从地下储层泵送的水。处理过的水可用于产生蒸汽。处理单元（例如EC，正向渗透，UF过滤等）可以被配置成一个系统作为现场安装或用于现场或非现场水处理的移动单元。

3. 发明授权

US09138688B2 Apparatus and process for treatment of water 有权
标题翻译：用于处理水的装置和方法
公开(公告)号：US09138688B2
公开(公告)日：2015-09-22
申请号：US13624846
申请日：2012-09-21
申请人： Prakhar Prakash , James Craig Pauley , Randall B. Pruet
发明人： Prakhar Prakash , James Craig Pauley , Randall B. Pruet
IPC分类号： B01D61/36 , B01D61/58 , C02F1/463 , C02F1/44 , C02F9/06 , B01D63/02 , C02F9/00 , B01D61/00 , B01D71/02 , B01D61/14
CPC分类号： B01D61/364 , B01D61/002 , B01D61/145 , B01D61/58 , B01D63/02 , B01D71/024 , C02F1/444 , C02F1/445 , C02F1/447 , C02F1/463 , C02F9/00 , C02F2209/06 , C02F2209/10 , C02F2209/20 , Y10T29/494
摘要： The invention relates to the treatment of water, including for example treatment in connection with hydrocarbon production operations. Silica in water produces undesirable scaling in processing equipment, which causes excess energy usage and maintenance problems. Electrocoagulation (EC) at relatively high water temperature followed by ultra-filtration (UF filtration) may be combined with forward osmosis (FO) to treat water. Water to be treated may be produced water that has been pumped from a subterranean reservoir. The treated water may be employed to generate steam. The treatment units (e.g., EC, forward osmosis, UF filtration, etc) can be configured into one system as an on-site installation or a mobile unit for on-site or off-site water treatment.
摘要翻译：本发明涉及水的处理，包括例如与碳氢化合物生产操作有关的处理。水中的二氧化硅在加工设备中产生不希望的结垢，这导致过多的能量消耗和维护问题。在相对较高的水温下进行电凝（EC），然后进行超滤（UF过滤）可与正向渗透（FO）组合以处理水。待处理的水可以产生已经从地下储层泵送的水。处理过的水可用于产生蒸汽。处理单元（例如EC，正向渗透，UF过滤等）可以被配置成一个系统作为现场安装或用于现场或非现场水处理的移动单元。

4. 发明申请

US20130075332A1 Apparatus and Process For Treatment of Water 有权
标题翻译：水处理设备及工艺
公开(公告)号：US20130075332A1
公开(公告)日：2013-03-28
申请号：US13624853
申请日：2012-09-21
申请人： Prakhar Prakash , James Craig Pauley , Randall B. Pruet
发明人： Prakhar Prakash , James Craig Pauley , Randall B. Pruet
IPC分类号： C02F9/12 , C02F1/66 , C02F1/463 , B01D61/36
CPC分类号： B01D61/364 , B01D61/002 , B01D61/145 , B01D61/58 , B01D63/02 , B01D71/024 , C02F1/444 , C02F1/445 , C02F1/447 , C02F1/463 , C02F9/00 , C02F2209/06 , C02F2209/10 , C02F2209/20 , Y10T29/494
摘要： The invention relates to the treatment of water, including for example treatment in connection with hydrocarbon production operations. Silica in water produces undesirable scaling in processing equipment, which causes excess energy usage and maintenance problems. Electrocoagulation (EC) at relatively high water temperature, followed by any of membrane distillation or forward osmosis (FO), may be combined with a subsequent process of ceramic ultra-filtration (UF filtration) employed to treat water. Water to be treated may be produced water that has been pumped from a subterranean reservoir. The treated water may be employed to generate steam. The treatment units (e.g., EC, forward osmosis, UF filtration, etc) can be configured into one system as an on-site installation or a mobile unit for on-site or off-site water treatment.
摘要翻译：本发明涉及水的处理，包括例如与碳氢化合物生产操作有关的处理。水中的二氧化硅在加工设备中产生不希望的结垢，这导致过多的能量消耗和维护问题。在较高的水温下进行电凝（EC），随后进行膜蒸馏或正向渗透（FO）的任何一种，可以与随后的用于处理水的陶瓷超滤（UF过滤）过程相结合。待处理的水可以产生已经从地下储层泵送的水。处理过的水可用于产生蒸汽。处理单元（例如EC，正向渗透，UF过滤等）可以被配置成一个系统作为现场安装或用于现场或非现场水处理的移动单元。

5. 发明授权

US06531515B2 Hydrocarbon recovery in a fischer-tropsch process 有权
公开(公告)号：US06531515B2
公开(公告)日：2003-03-11
申请号：US09788792
申请日：2001-02-20
申请人： Richard O. Moore, Jr. , Roger D. Van Gelder , Grant C. Hilton , Clive Jones , Randall B. Pruet
发明人： Richard O. Moore, Jr. , Roger D. Van Gelder , Grant C. Hilton , Clive Jones , Randall B. Pruet
IPC分类号： C07C2700
CPC分类号： C10G2/32
摘要： An integrated process for improved hydrocarbon recovery from a natural gas resource is disclosed. A methane-rich stream, an LPG stream and optionally a C5+ stream are isolated from a natural gas source in a first separation zone and desulfurized. The methane-rich stream is converted to syngas and subjected to hydrocarbon synthesis, for example, Fischer-Tropsch synthesis. The products from the hydrocarbon synthesis typically include a C4− fraction, a C5-C20 fraction, and a C20+ wax fraction. These fractions are isolated in a second separation zone. The C4− fraction is recycled through the first separation zone to provide methane for conversion to synthesis gas and an additional LPG fraction. The C4− fraction can be treated, for example, with hydrotreating or hydroisomerization catalysts and conditions before or after the separation. The C5-C20 fraction and the C20+ wax and heavy fraction are subjected to additional process steps, for example, hydro treatment, hydroisomerization, and/or hydrocracking. The products are sent to a third separation zone, and yield an additional C4− fraction, as well as higher molecular weight products. The additional C4− fraction can also be sent to the first separation zone and treated in an analogous fashion to the C4− fraction from the hydrocarbon synthesis. Any sulfur-containing compounds resulting from the additional processing of the hydrocarbon synthesis products (i.e., hydroconversion reactions) can be treated along with the sulfur-containing compounds in the natural gas, eliminating the need for a second sulfur-treatment plant.

6. 发明授权

US06887908B1 Treatment of reaction water from a Fischer-Tropsch reactor 有权
标题翻译：处理费 - 托反应器的反应水
公开(公告)号：US06887908B1
公开(公告)日：2005-05-03
申请号：US10879474
申请日：2004-06-28
申请人： Randall B. Pruet
发明人： Randall B. Pruet
IPC分类号： C02F1/02 , C02F1/68 , C02F1/72 , C07C27/00 , C10G2/00
CPC分类号： C02F1/025 , C02F1/72 , C02F2101/32 , C02F2103/365
摘要： An integrated Fischer-Tropsch process provides methods for recovering reaction water from a Fischer-Tropsch reactor with minimal adverse environmental effects and with reduced costs compared to traditional methods. Reaction water, preferably separated from an overhead stream from a Fischer-Tropsch reactor, is vaporized and contaminants are thermally oxidized while in the vapor state. The thermal oxidation also produces flue gases, which flue gases may be condensed to recover water.
摘要翻译：集成的费 - 托方法提供了从费 - 托反应器回收反应水的方法，其具有最小的不利环境影响并且与传统方法相比降低了成本。反应水优选与费 - 托反应器的塔顶物流分离，蒸发，污染物在蒸汽状态下被热氧化。热氧化还产生烟道气，烟道气可以被冷凝以回收水。

7. 发明授权

US07276105B2 Separation of water from Fischer-Tropsch product 有权
标题翻译：从费 - 托产品中分离水
公开(公告)号：US07276105B2
公开(公告)日：2007-10-02
申请号：US10880336
申请日：2004-06-28
申请人： Randall B. Pruet
发明人： Randall B. Pruet
IPC分类号： B01D53/22
CPC分类号： C10G2/32 , B01D53/268 , B01D2257/108 , C01B3/50 , C01B2203/04 , C01B2203/0465 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/0495 , C01B2203/062 , C10G31/11 , C10G33/06 , Y02P20/126
摘要： A method for separating water from a Fischer-Tropsch reactor product stream in a cost effective and energy efficient manner which comprises feeding a Fischer-Tropsch product stream to a separation membrane, preferably a ceramic membrane, and recovering water vapor from the downstream permeate side of the membrane.
摘要翻译：一种以费用有效和能量有效的方式从费 - 托反应器产物流中分离水的方法，其包括将费 - 托产物流进料到分离膜，优选陶瓷膜，并从下游渗透侧回收水蒸气膜。

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