US4105494A
(en)
*
|
1973-01-05 |
1978-08-08 |
Sunds Aktiebolag |
Process of gas-phase bleaching high consistency finely disintegrated pulp
|
US4177105A
(en)
*
|
1973-05-22 |
1979-12-04 |
Kamyr, Incorporated |
Apparatus for delignifying and bleaching cellulose pulp
|
US4062722A
(en)
*
|
1974-01-18 |
1977-12-13 |
Carlos Ibanez Ajuria |
Device for treating deformable particles with the counterflowing liquids
|
US4089737A
(en)
*
|
1974-02-18 |
1978-05-16 |
Toyo Pulp Company, Ltd. |
Delignification of cellulosic material with an alkaline aqueous medium containing oxygen dissolved therein
|
US3964962A
(en)
*
|
1974-02-25 |
1976-06-22 |
Ingersoll-Rand Company |
Gaseous reaction apparatus and processes including a peripheral gas receiving chamber and a gas recirculation conduit
|
SE431662B
(en)
*
|
1974-07-05 |
1984-02-20 |
Kamyr Ab |
KEEP ON CONTINUOUS COOKING OF FIBER MATERIAL
|
US3966542A
(en)
*
|
1974-09-20 |
1976-06-29 |
General Signal Corporation |
Multi-stage bleaching of pulp using successively lower power levels
|
US4058433A
(en)
*
|
1975-03-06 |
1977-11-15 |
Gulf States Paper Corporation |
Conversion of sulfur in blank liquor to eliminate odorous emissions and facilitate the collection of sulfate soaps
|
NO137651C
(en)
*
|
1975-10-31 |
1978-03-29 |
Myrens Verksted As |
PROCEDURE AND APPARATUS FOR CONTINUOUS TREATMENT OF FINDEL FIBER MATERIAL OR CELLULOSIZED MASS WITH GAS WITHOUT COVER.
|
US4338158A
(en)
*
|
1976-04-09 |
1982-07-06 |
Weyerhaeuser Company |
Pulping in the presence of a protector
|
US4161421A
(en)
*
|
1977-09-13 |
1979-07-17 |
Kamyr, Inc. |
Method and apparatus for continuous oxygen bleaching of cellulosic pulp
|
US4259150A
(en)
*
|
1978-12-18 |
1981-03-31 |
Kamyr Inc. |
Plural stage mixing and thickening oxygen bleaching process
|
US4451268A
(en)
*
|
1982-09-29 |
1984-05-29 |
Lerch John A |
Dry acetylene generator
|
US4744873A
(en)
*
|
1986-11-25 |
1988-05-17 |
The Dow Chemical Company |
Multiple compartment electrolytic cell
|
US5135968A
(en)
*
|
1990-10-10 |
1992-08-04 |
Stranco, Ltd. |
Methods and apparatus for treating wastewater
|
US5164429A
(en)
*
|
1987-08-25 |
1992-11-17 |
Stranco, Inc. |
Polymer activation apparatus
|
US5061456A
(en)
*
|
1987-08-25 |
1991-10-29 |
Stranco, Inc. |
Polymer activation apparatus
|
US5316031A
(en)
*
|
1987-08-25 |
1994-05-31 |
Brazelton Carl L |
Valve with independent control of discharge through plurality of orifices
|
US5252635A
(en)
*
|
1987-08-25 |
1993-10-12 |
Stranco, Inc. |
Polymer activation method using two separate mixing zones
|
US5525195A
(en)
*
|
1989-02-15 |
1996-06-11 |
Union Camp Patent Holding, Inc. |
Process for high consistency delignification using a low consistency alkali pretreatment
|
US5188708A
(en)
*
|
1989-02-15 |
1993-02-23 |
Union Camp Patent Holding, Inc. |
Process for high consistency oxygen delignification followed by ozone relignification
|
US5085734A
(en)
*
|
1989-02-15 |
1992-02-04 |
Union Camp Patent Holding, Inc. |
Methods of high consistency oxygen delignification using a low consistency alkali pretreatment
|
US5211811A
(en)
*
|
1989-02-15 |
1993-05-18 |
Union Camp Patent Holding, Inc. |
Process for high consistency oxygen delignification of alkaline treated pulp followed by ozone delignification
|
US5181989A
(en)
*
|
1990-10-26 |
1993-01-26 |
Union Camp Patent Holdings, Inc. |
Reactor for bleaching high consistency pulp with ozone
|
US5409570A
(en)
*
|
1989-02-15 |
1995-04-25 |
Union Camp Patent Holding, Inc. |
Process for ozone bleaching of oxygen delignified pulp while conveying the pulp through a reaction zone
|
US5173153A
(en)
*
|
1991-01-03 |
1992-12-22 |
Union Camp Patent Holding, Inc. |
Process for enhanced oxygen delignification using high consistency and a split alkali addition
|
US5217574A
(en)
*
|
1989-02-15 |
1993-06-08 |
Union Camp Patent Holdings Inc. |
Process for oxygen delignifying high consistency pulp by removing and recycling pressate from alkaline pulp
|
US5472572A
(en)
*
|
1990-10-26 |
1995-12-05 |
Union Camp Patent Holding, Inc. |
Reactor for bleaching high consistency pulp with ozone
|
US5441603A
(en)
*
|
1990-05-17 |
1995-08-15 |
Union Camp Patent Holding, Inc. |
Method for chelation of pulp prior to ozone delignification
|
US5164043A
(en)
*
|
1990-05-17 |
1992-11-17 |
Union Camp Patent Holding, Inc. |
Environmentally improved process for bleaching lignocellulosic materials with ozone
|
US5164044A
(en)
*
|
1990-05-17 |
1992-11-17 |
Union Camp Patent Holding, Inc. |
Environmentally improved process for bleaching lignocellulosic materials with ozone
|
US5520783A
(en)
*
|
1990-10-26 |
1996-05-28 |
Union Camp Patent Holding, Inc. |
Apparatus for bleaching high consistency pulp with ozone
|
US5174861A
(en)
*
|
1990-10-26 |
1992-12-29 |
Union Camp Patent Holdings, Inc. |
Method of bleaching high consistency pulp with ozone
|
CA2068981C
(en)
*
|
1991-05-24 |
1996-08-27 |
Michael A. Pikulin |
Two stage pulp bleaching reactor
|
US5372679A
(en)
*
|
1992-06-08 |
1994-12-13 |
Air Products And Chemicals, Inc. |
Reactor system for treating cellulosic pulp at a constant upward flow velocity
|
US5338779A
(en)
*
|
1992-09-18 |
1994-08-16 |
Stranco, Inc |
Dry polymer activation apparatus and method
|
US5554259A
(en)
*
|
1993-10-01 |
1996-09-10 |
Union Camp Patent Holdings, Inc. |
Reduction of salt scale precipitation by control of process stream Ph and salt concentration
|
US6174409B1
(en)
|
1997-09-19 |
2001-01-16 |
American Air Liquide Inc. |
Method to improve final bleached pulp strength properties by adjusting the CI02:03 ration within a single (D/Z) stage of the bleaching process
|
US6409926B1
(en)
|
1999-03-02 |
2002-06-25 |
United States Filter Corporation |
Air and water purification using continuous breakpoint halogenation and peroxygenation
|
US6143184A
(en)
|
1999-03-02 |
2000-11-07 |
United States Filter Corporation |
Air and water purification using continuous breakpoint halogenation
|
MXPA02012886A
(en)
|
2000-06-22 |
2003-05-14 |
United States Filter Corp |
Corrosion control utilizing a hydrogen peroxide donor.
|
US6419817B1
(en)
|
2000-06-22 |
2002-07-16 |
United States Filter Corporation |
Dynamic optimization of chemical additives in a water treatment system
|
US6716359B1
(en)
|
2000-08-29 |
2004-04-06 |
United States Filter Corporation |
Enhanced time-based proportional control
|
US20020129911A1
(en)
*
|
2000-10-16 |
2002-09-19 |
Marcoccia Bruno S. |
Process and configuration for providing external upflow/internal downflow in a continuous digester
|
US6620315B2
(en)
|
2001-02-09 |
2003-09-16 |
United States Filter Corporation |
System for optimized control of multiple oxidizer feedstreams
|
US6776926B2
(en)
*
|
2001-08-09 |
2004-08-17 |
United States Filter Corporation |
Calcium hypochlorite of reduced reactivity
|
US7108781B2
(en)
*
|
2002-02-26 |
2006-09-19 |
Usfilter Corporation |
Enhanced air and water purification using continuous breakpoint halogenation with free oxygen radicals
|
US6991735B2
(en)
*
|
2002-02-26 |
2006-01-31 |
Usfilter Corporation |
Free radical generator and method
|
US10343939B2
(en)
|
2006-06-06 |
2019-07-09 |
Evoqua Water Technologies Llc |
Ultraviolet light activated oxidation process for the reduction of organic carbon in semiconductor process water
|
US8652336B2
(en)
*
|
2006-06-06 |
2014-02-18 |
Siemens Water Technologies Llc |
Ultraviolet light activated oxidation process for the reduction of organic carbon in semiconductor process water
|
US12103874B2
(en)
|
2006-06-06 |
2024-10-01 |
Evoqua Water Technologies Llc |
Ultraviolet light activated oxidation process for the reduction of organic carbon in semiconductor process water
|
US9365436B2
(en)
*
|
2007-04-03 |
2016-06-14 |
Evoqua Water Technologies Llc |
Method of irradiating a liquid
|
US8741155B2
(en)
*
|
2007-04-03 |
2014-06-03 |
Evoqua Water Technologies Llc |
Method and system for providing ultrapure water
|
US20080245737A1
(en)
*
|
2007-04-03 |
2008-10-09 |
Siemens Water Technologies Corp. |
Method and system for providing ultrapure water
|
US8961798B2
(en)
*
|
2007-04-03 |
2015-02-24 |
Evoqua Water Technologies Llc |
Method for measuring a concentration of a compound in a liquid stream
|
US8753522B2
(en)
*
|
2007-04-03 |
2014-06-17 |
Evoqua Water Technologies Llc |
System for controlling introduction of a reducing agent to a liquid stream
|
US9365435B2
(en)
*
|
2007-04-03 |
2016-06-14 |
Evoqua Water Technologies Llc |
Actinic radiation reactor
|
US9725343B2
(en)
|
2007-04-03 |
2017-08-08 |
Evoqua Water Technologies Llc |
System and method for measuring and treating a liquid stream
|
US8591730B2
(en)
*
|
2009-07-30 |
2013-11-26 |
Siemens Pte. Ltd. |
Baffle plates for an ultraviolet reactor
|
CN103370401A
(en)
|
2010-08-17 |
2013-10-23 |
安德里兹技术资产管理有限公司 |
Method and system for the torrefaction of lignocellulosic material
|
EP2527301B1
(en)
|
2011-05-26 |
2016-04-27 |
Evoqua Water Technologies GmbH |
Method and arrangement for a water treatment
|
WO2013003599A2
(en)
*
|
2011-06-28 |
2013-01-03 |
Andritz Inc. |
Method for the torrefaction of lignocellulosic material
|
US20130098751A1
(en)
*
|
2011-06-28 |
2013-04-25 |
Andritz Inc. |
Method for the torrefaction of lignocellulosic material
|
WO2013003615A2
(en)
|
2011-06-28 |
2013-01-03 |
Andritz Inc. |
System for the torrefaction of lignocellulosic material
|
JP2014532096A
(en)
*
|
2011-09-21 |
2014-12-04 |
アンドリッツ インコーポレーテッド |
Method and system for roasting lignocellulosic material
|
FR2982273B1
(en)
*
|
2011-11-09 |
2014-03-14 |
Commissariat Energie Atomique |
DRYING AND TORREFACTION REACTOR OF BIOMASS, PREFERABLY LIGNO-CELLULOSIC
|
US11161762B2
(en)
|
2015-01-21 |
2021-11-02 |
Evoqua Water Technologies Llc |
Advanced oxidation process for ex-situ groundwater remediation
|
CA2918564C
(en)
|
2015-01-21 |
2023-09-19 |
Evoqua Water Technologies Llc |
Advanced oxidation process for ex-situ groundwater remediation
|
CN107020041A
(en)
*
|
2016-01-29 |
2017-08-08 |
上海戴沃机械科技有限公司 |
A kind of new mine product stirs barrel
|
US12083526B1
(en)
*
|
2023-03-13 |
2024-09-10 |
Namon A. Nassef |
Waste stream homogenizing apparatus and method
|